NOVELTY - Nitrobacter sp. H2S1 strain having excellent organic matter decomposition function and growth capacity, is new.    USE - The microbial agent is useful for improving physio-chemical property of effluent in livestock manure treatment system (claimed). The strain is useful for removing high concentration nitrogen and sludge generated in livestock manure wastewater.    ADVANTAGE - The strain added to highly efficient nitrification tank and livestock wastewater treatment system.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a microbial agent comprising cells or a culture medium of Nitrobacter sp. H2S1.
NOVELTY - Modified Cyanobacterium comprising an exogenous polynucleotide encoding a diacylglycerol acyltransferase (DGAT) and at least one exogenous polynucleotide encoding at least one lipid packaging protein, is new. The modified Cyanobacterium has an increased growth rate and/or produces or accumulates an increased amount of neutral lipids as compared to a wild-type Cyanobacterium expressing only an exogenous DGAT.    USE - (I) is useful for producing neutral lipid (claimed) such as triglyceride, fatty acid ester, wax ester, and carotenoid, which is useful for producing biofuels and/or various specialty chemicals such as glycerin.    ADVANTAGE - (I) increase the size and/or number of the neutral lipids, and improves the production efficiency of the neutral lipids.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of (I).
NOVELTY - Isolated fungus having imperfect stage of Nodulisporium, is new.    USE - The isolated fungus including Nodulisporium, Hypoxylon, Annulohypoxylon, Daldinia, and Xylaria is useful for: producing at least one compound, including 1,8-cineole and 1-methyl-1,4-cyclohexadiene; alcohol including ethanol (all claimed); and volatile organic compounds including hydrocarbons, which are useful in the production of biofuels, plastics, plasticizers, antibiotics, rubber, fuel additives, and/or adhesives.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) a method for producing at least one compound including 1,8-cineole and 1-methyl-1,4-cyclohexadiene, comprising culturing a microorganism on or within a culturing media in a container under conditions sufficient for producing the compound; and (2) a method for producing an alcohol, comprising culturing a fungus having the imperfect stage of Nodulisporium on or within a culturing media in a container under conditions sufficient for producing the alcohol.
NOVELTY - Invention relates to a method of producing hydrogen, a hydrogen-methane mixture, synthesis gas, primarily containing H2 and CO, for producing hydrogen, alcohol, ammonia, dimethyl ether, ethylene, for Fischer-Tropsch processes and can be used in chemical industry for processing hydrocarbon gases, and in technologies using a hydrogen-methane mixture. In the method, the raw material source used is at least two parallel streams containing lower alkanes. Before feeding for partial oxidation, the first stream is mixed with steam and an oxygen-containing gas. A catalytic partial oxidation reaction is then carried out, products of which are mixed with the second stream and catalytic adiabatic conversion is the carried out to obtain a hydrogen-containing gas. The second stream is heated in a heating heat-exchanger by removing heat from products of partial oxidation of the first stream. The oxygen-containing gas used is compressed air or exhaust gas from a high-pressure gas turbine.    USE - Chemistry.    ADVANTAGE - Low capital costs and low content of ballast gases in the production gas.12 cl, 1 dwg, 4 tbl, 1 ex
NOVELTY - Pulverized solid fuel comprises algae mass having oil content of 60-80%, where the algae mass is in form of micronized powder having particles of size 0.04-0.5 mm.    USE - The pulverized solid fuel is useful as fertilizer raw material (claimed) and alternative energy, and in boiler for automatically generating power.    ADVANTAGE - The pulverized solid fuel is environmentally-friendly, and controls amount of heat generated during combustion when compared to existing fossil fuels.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) fertilizer raw material comprising burnt pulverized solid fuel and remaining burnt ash; and    (2) method for preparing the above-mentioned pulverized solid fuel, involves extracting oil from the algae mass, drying the algae mass, hot extruding the dried mass to pellets, and crushing the extruded pellets to the above-mentioned particle size.
NOVELTY - Solid fuel comprises 5-50 wt.% of algae biomass, and 50-95 wt.% of fuel additive.    USE - The solid fuel is useful in a fertilizer (claimed).    ADVANTAGE - The eco-friendly solid fuel can be rapidly prepared with excellent calorific value.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the solid fuel, comprising drying algae biomass, crushing the fuel additive by a crusher, and sterilizing the dried algae biomass and crushed fuel additive and then mixing.
NOVELTY - For production of plant bio-enhancers containing Bacillus, Pseudomonas and trichoderma, a very low cost natural bio-degradable medium having 35% cow dung, 6% cow urine, 10% jaggery, 10% gypsum, 4% potato extract (for trichoderma) and water (balance), is used.    USE - For production of plant bio-enhancers containing Bacillus, Pseudomonas, and trichoderma, which is also useful as salt tolerant growth enhancers (claimed).    ADVANTAGE - The bio-degradable medium provides rapid multiplication rate; is highly economical; and has low cost of production (i.e. approximately 15-20 rupees/kg only) of 1 kg formulation. The formulation has multiple roles i.e. apart from enhanced nutrient uptake, growth enhancer and protection against soil borne as well as foliar diseases. The ingredients of growth medium are widely available; and are natural carbon source/ biodegradable. The medium can be easily adapted by farmers, take care most of the problems and cover from seed treatment, soil application and foliar spray. Since theses isolates are from distressed barren sodic environment (pH 9.65-10.4), they are behaving differently as deprived isolates and, thus providing much better activity in both sodic as well as in normal soils. The count has crossed 107 and even after formulation it has live count of more than 106 which remains same even after 6 months. The medium increases the productivity of vegetables, flowers (gladiolus) and fruits (banana) to 20% higher than the conventional methods. Commercial crops like banana and gladiolus can be cultivated in sodic soils of pH 9-9.3 with higher productivity. The medium significantly reduces use of chemical pesticides and fungicides, and thus very suitable for organic production system and protecting the environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of salt tolerant growth enhancers in liquid form.
NOVELTY - Manufacture of 1,4-benzoquinone (II), involves oxidizing phenol derivative (I) with hydrogen peroxide in presence of copper halide and hydroxylamine compound.    USE - Manufacture of 1,4-benzoquinone. Uses include but are not limited to hydrogen acceptor, oxidizing agent, dehydrogenation agent, polymerization inhibitor, synthetic intermediate of pharmaceutical and agrochemical field and manufacturing intermediate of tocopherol.    ADVANTAGE - The method enables safe and environmentally-friendly manufacture of 1,4-benzoquinone.    DETAILED DESCRIPTION - Manufacture of 1,4-benzoquinone of formula (II), involves oxidizing phenol derivative of formula (I) with hydrogen peroxide in presence of copper halide and hydroxylamine compound.    X=H or hydroxy;and    R1, R2, R3, R4=H or substituent chosen from alkyl, alkoxy, alkylsulfonyl, aryl, aryloxy, arylsulfonyl, aralkyl, hydroxy and halo.
NOVELTY - Producing methane gas and compost comprises fermenting food waste and poultry waste having a moisture content of less than 20%.    USE - The method is useful for producing methane gas and compost (claimed).    ADVANTAGE - The method is capable of simply producing the methane gas and compost, with high quality and without using separate control agent to control the moisture, in an environmentally friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an apparatus for producing methane gas and compost comprising a storage tank for storing pulverized poultry waste, a food waste storage tank, a mixer for mixing the pulverized poultry waste and food waste, a conveyor for transferring the resulting mixture, a fermentation tank for fermenting the mixture, a gas storage tank for collecting methane gas from the fermentation tank, and a generator.
NOVELTY - Production of compost and methane gas using pig manure and poultry manure involves fermenting pig manure and poultry manure, such that moisture content becomes 20% or less.    USE - Production of compost and methane gas (claimed).    ADVANTAGE - Compost and methane gas are produced using simple apparatus by environmentally-friendly method.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for compost-and-methane-gas-producing apparatus.
NOVELTY - Producing ethanol comprises dissolving solid alkali metal ethylcarbonate in water to obtain ethanol and alkali metal bicarbonate.    USE - The method is useful for producing ethanol, which is useful as a fuel alcohol (claimed) for thermal power plant, petrochemistry and cement industries.    ADVANTAGE - The method is capable of easily and economically producing the eco-friendly ethanol with less energy consumption.
NOVELTY - The generator (1) has a dehumidification unit (20) that dehumidifies the hydrogen gas emitted in water electrolysis cell. The dehumidification unit is provided with distribution channel which distributes hydrogen gas. A heating portion is provided to reproduce the adsorption agent by heating. The adsorption agent is provided to dehumidify distributed hydrogen gas in distribution channel, so that the heating regeneration of adsorption agent is carried out by heating portion, and water is supplied to distribution channel of dehumidification unit.    USE - Hydrogen oxygen generator.    ADVANTAGE - The water is supplied in the apparatus, when emergency shut down of the driving is carried out, so that the inside of the apparatus is cooled fully.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an operation method of hydrogen oxygen generator.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen oxygen generator. (Drawing includes non-English language text)    Hydrogen oxygen generator (1)    Water-electrolysis module (10)    Hydrogen gas transfer pipe (11)    Gas-liquid separator for hydrogen gas (12)    Hydrogen gas storage tank (13)
NOVELTY - The method involves determining operation of a batch of dehumidifiers (31) after shutdown. The regeneration of adsorption agent is performed. The dehumidifier is transferred from dehumidification mode to regeneration mode and operation of batch is started. The accumulated time of regeneration is computed with respect to predetermined count of shutdown. The specific accumulated time and accumulation time for dehumidification are added. The dry gas obtained by dehumidification mode or the product gas obtained before shutdown is used for regenerating gas in batch of dehumidifiers.    USE - Method for obtaining hydrogen and oxygen gases.    ADVANTAGE - The discharge of to-be-processed gas from the dehumidifier is suppressed, even when dehumidifying performance is insufficient in the middle of operation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen and oxygen generation apparatus.    Water electrolysis apparatus (1)    Dehumidifying apparatus (3)    Control mechanism (6)    Dehumidifiers (31,32)    Hydrogen and oxygen generation apparatus (100)
NOVELTY - The apparatus (1) has a combustor (10) to heat modifier (9). A feeding device (13) feeds air to combustor. A heater (30) heats hydro-desulfurization device (3). A detector detects temperature of hydro-desulfurization device. A flow path (24) through which portion of air fed from feeding device to combustor is passed, is provided. A controller (29) is provided to adjust flow rate of air to level higher than the level set when detected temperature is not higher than first temperature threshold, when detected temperature exceeds first temperature threshold set previously.    USE - Hydrogen generating apparatus for fuel cell system (claimed).    ADVANTAGE - The temperature of hydride-sulfurization device is maintained to an appropriate temperature, and the performance decrement of the hydrodesulfurization device is suppressed effectively.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) an operating method of hydrogen generating apparatus; and    (2) an operating method of fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the hydrogen generating apparatus. (Drawing includes non-English language text)    Hydrogen generating apparatus (1)    Hydrodesulfurization device (3)    Modifier (9)    Combustor (10)    Air supply device (13)    Cooling flow path (24)    Controller (29)
NOVELTY - Synthesizing acylglycerol oligomers comprises reacting (a) a precursor including cyclic carboxylic esters of a/a' acylglycerol oligomers, (b) a metallic catalyst consisting of metal cation salts, organometallic compounds and metallic oxides and (c) an organic primer including hydroxyl organic compounds at a reaction temperature of less than 220?oC.    USE - The method is useful for synthesizing acylglycerol oligomers (claimed), which are useful for treating plants and/or as vectorizing adjuvant.    ADVANTAGE - The method is capable of easily and economically synthesizing the acylglycerol oligomers without the need for purification or extraction process in an environmentally friendly manner.    DETAILED DESCRIPTION - Synthesizing acylglycerol oligomers comprises reacting (a) a precursor including cyclic carboxylic esters of a/a' acylglycerol oligomers of formula (I), (b) a metallic catalyst consisting of metal cation salts, organometallic compounds and metallic oxides and (c) an organic primer including hydroxyl organic compounds at a temperature of less than 220?oC.    R1 = organic moiety formed from at least two atoms of C, H, O and N linked by covalent bonds.
NOVELTY - The aerator (1) has water tank (100) that is provided in reservoir water space (101). The respective rotary shaft (200) is rotatably arranged inside the water tank. The drive unit (300) is provided for rotating the rotary shaft. The water tank is feeding with the liquefied fertilizer and air by feeding unit (400) through the fluid paths (210,220). The stirring unit is installed at the rotary shaft for mixing the liquefied fertilizer received inside the water tank.    USE - Aerator used in livestock application.    ADVANTAGE - The air is distributed evenly within the water tank accommodating the excrements and effluent. The fermentation time is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the aerator.    Aerator (1)    Water tank (100)    Reservoir water space (101)    Rotary shaft (200)    Fluid path (210,220)    Drive unit (300)    Feeding unit (400)
NOVELTY - Making triols and diols, comprises performing an hydrodeoxygenation reaction on a feedstock comprising a biomass-derived reactant and hydrogen by contacting the feedstock with a heterogeneous metal-comprising bifunctional catalyst or a combination of two or more heterogeneous metal comprising catalysts that catalyze cleavage of C-C and C-O bonds for a temperature, pressure and weight hourly space velocity to yield a product mix comprising triols and/or diols.    USE - The method is useful for making triols and diols from biomass-derived feedstocks (claimed) including petroleum derived feedstocks, where the diols include 1,3-propanediol 1,4-butanediol, 1,5-pentanediol and 1,6-hexanediol.    ADVANTAGE - The method is capable of economically making triols and diols from petroleum derived feedstocks with high yield and sustainability.
NOVELTY - Aerosolized composition comprises: a cyclic oligosaccharide; a fragrance; a volatile solvent; a propellant; and a non-volatile solvent, where the weight ratio of the non-volatile solvent to the cyclic oligosaccharide is less than 1:1.    USE - The composition is useful: for delivering an improved moisture-triggered fragrance release system (claimed); for applying to an article, such as a fabric or any absorbent article including feminine hygiene articles, diapers, and adult incontinence articles; and as a body spray, feminine spray, adult incontinence spray and baby spray.    ADVANTAGE - The composition is free of an antiperspirant active and non-volatile solvent, and thus provides improved moisture-triggered fragrance, with long lasting fragrance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for delivering an improved moisture-triggered fragrance release system comprising contacting a substrate with the aerosolized composition.
NOVELTY - Method (M1) of producing biological product in a plant, involves expressing in the plant, a bacterial gene of glycolate catabolic cycle and a plant gene chosen from farnesyl diphosphate synthase (FPS) and squalene synthase (SQS).    USE - The method (M1) is useful for producing biological product in plant. The biological product is chosen from biofuel, biofuel intermediate, therapeutic compound, bioplastic, terpene, nutraceutical compound, terpenoid-derived compound, and carbon containing compound (all claimed). The method is also useful for modifying photorespiration in plants and in synergistic production of bioproducts.    ADVANTAGE - The method increases production and yield of biological product.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method (M2) of producing a biological product from a plant or an alga, involves coupling a carbon-concentrating process and a bioproduct synthesis pathway;    (2) plant (P1) produced by the method (M1);    (3) part of a plant (P1); and    (4) composition produced from the plant (P1).
NOVELTY - An isolated nucleic acid encoding a protein having acyl-acyl carrier protein (ACP) thioesterase activity, is new.    USE - The nucleic acid is useful for producing an oil or oil-derived product (claimed) and producing foods, fuels and chemicals (including plastics, foams, films, etc).    DETAILED DESCRIPTION - An isolated nucleic acid having at least 80% sequence identity to any of the 51 defined nucleotide sequences comprising 1074-1284 bp (SEQ ID NOS. 2, 3, 5, 6, 8, 9, 11, 12, 14, 15, 17, 18, 20, 21, 23, 24, 26, 27, 29, 30, 32, 33, 35, 36, 38, 39, 41, 42, 44, 45, 47, 48, 50, 51, 53, 54, 56, 57, 59, 60, 62, 63, 65, 66, 68, 69, 71, 72, 74, 76, or 78) or any equivalent sequences by virtue of the degeneracy of the genetic code, or an isolated nucleic acid sequence encoding a protein having at least 80% sequence identity to any of the 27 defined sequences comprising 357-427 amino acids (SEQ ID NOS. 1, 4, 7, 10, 13, 16, 19, 22, 25, 28, 31, 34, 37, 40, 43, 46, 49, 52, 55, 58, 61, 64, 67, 70, 73, 75, or 77), or its fragment having acyl-acyl carrier protein (ACP) thioesterase activity, is new. The sequences are given in the specification. INDEPENDENT CLAIMS are:    (1) a method of producing a recombinant cell that produces an altered fatty acid profile by transforming the cell with a nucleic acid above;    (2) a host cell produced by the method of (1);    (3) a method for producing an oil or oil-derived product by cultivating a host cell of (2), and extracting oil produced thus, optionally where the cultivation is heterotrophic growth on sugar; and    (4) an oil produced by the method of (3), optionally having a fatty acid profile comprising at least 20% C8, C10, C12, C14 or C16 fatty acids, or an oil-derived product produced by the method of (3).
NOVELTY - Producing diethyl ether comprises dehydrating ethanol in the vapor phase at a pressure and a temperature in the presence of a catalyst. The catalyst comprises (A) tin impregnated on a solid catalyst material comprising titania, zeolite, phosphotungstate or hydrotalcite.    USE - The process is useful for preparing diethyl ether, which is useful in a fuel additive (all claimed), and as anesthesia, and fuel including gasoline, diesel and biofuel for compression ignition engines (e.g. diesel engines) No biological data given.    ADVANTAGE - The process is capable of preparing diethyl ether with good handling and storage properties and without the risk of explosion in an environmentally-friendly manner. The diethyl ether improves fuel properties and performance of the engine.    DETAILED DESCRIPTION - Producing diethyl ether comprises dehydrating ethanol in the vapor phase at a pressure and a temperature in the presence of a catalyst. The catalyst comprises: (A) tin impregnated on a solid catalyst material comprising titania, zeolite, phosphotungstate or hydrotalcite; (B) germanium impregnated on a solid catalyst material comprising zeolite or alumina, (B1) a group IA metal comprising lithium, sodium, cesium or potassium impregnated on a silica support, (B3) a group IA metal comprising lithium, sodium or potassium impregnated on a magnesium oxide solid catalyst material, or (B3) copper impregnated on a hydroxyapatite solid catalyst material; or (C) an alumina solid catalyst material, and a metal impregnated on the alumina solid catalyst material. The metal is tin, copper, platinum and/or palladium.
NOVELTY - Stabilized biodiesel fluid composition comprises: a methyl ester based fluid consisting of vegetable oil, algae oil, animal fat and/or tall oil; optionally, a petrodiesel fluid; and at least one component consisting of 2,4,6-tris(di-1-6C-alkylaminomethyl)phenol (TAP) and a salt of at least one mono 12-30C carboxylic fatty acid and TAP having a molar ratio of up to 3 moles of mono 12-30C carboxylic fatty acid per mole of TAP. The stabilized biodiesel fluid composition has an oxidative stability index (OSI) of greater than 10 hours at 110 degrees C as measured by AOCS 12b-92.    USE - The composition is useful as dielectric fluid, lubricant and biodiesel.    ADVANTAGE - The composition exhibits improved oxidative stability and/or hydrolytic stability at elevated use temperatures.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for stabilizing a biodiesel fluid composition, comprising mixing together at or above ambient temperature the methyl ester based fluid, optionally, the petrodiesel fluid, and the component consisting of TAP or a salt mixture comprising mono 12-30C carboxylic fatty acid and the TAP.
NOVELTY - Treating (M1) a pyrolysis oil involves: contacting pyrolysis oil with at least one alpha -hydroxysulfonic acid under conditions effective to phase separate pyrolysis oil into water soluble phase containing sugars, organic acids, and carbonyl compounds and water insoluble phase containing lignin and phenolic species; separating water insoluble phase from water soluble phase; and removing alpha -hydroxysulfonic acid in its component form from water soluble phase by heating and/or reducing pressure to produce acid-removed water soluble phase free of alpha -hydroxysulfonic acid.    USE - For treating pyrolysis oil (claimed).    ADVANTAGE - The separation of lignin derived compounds (lignin and phenolic fractions) from bio oil by use of reversible alpha -hydroxysulfonic acid remarkably increase the extraction efficiency.    DETAILED DESCRIPTION - Treating (M1) a pyrolysis oil involves: providing a pyrolysis oil; contacting the pyrolysis oil with at least one alpha -hydroxysulfonic acid under conditions effective to phase separate the pyrolysis oil into a water soluble phase containing sugars, organic acids, and carbonyl compounds and a water insoluble phase containing lignin and phenolic species; separating the water insoluble phase from the water soluble phase; optionally removing water from the water soluble phase and removing the alpha -hydroxysulfonic acid in its component form from the water soluble phase or water removed-soluble phase by heating and/or reducing pressure to produce an acid-removed water soluble phase substantially free of the alpha -hydroxysulfonic acid.
NOVELTY - Reducing a pressure drop across a hydroprocessing reactor having a reactor feed, where the reactor feed comprises a bio-oil feed and a hydrocarbon diluent (110), comprises either stopping or substantially reducing the bio-oil feed supplied to the hydroprocessing reactor and supplying the hydrocarbon diluent to the reactor to generate a mass flux of at least 1000 lb/hour/ft2.    USE - The method is useful for reducing a pressure drop across a hydroprocessing reactor having a reactor feed and producing a hydroprocessing product (claimed).    ADVANTAGE - The method rapidly reduces the reactor pressure drop to 80%.    DETAILED DESCRIPTION - Reducing a pressure drop across a hydroprocessing reactor having a reactor feed and producing a hydroprocessing product, where the reactor feed comprises a bio-oil feed and a hydrocarbon diluent (110), comprises either stopping or substantially reducing the bio-oil feed supplied to the hydroprocessing reactor and supplying the hydrocarbon diluent to the reactor to generate a mass flux of at least 1000 lb/hour/ft2, or at least combining a bio-oil feed with a boiling point of 100-350 degrees F at 550-750 degrees C to produce the reactor feed, recycling the hydroprocessing product at 550-800 degrees F, substantially reducing the bio-oil feed, supplying recycled hydroprocessing product to generate a mass flux of at least 2000 lb/hour/ft2 and reducing the pressure drop after the theoretical void fraction drops below 26%.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a hydroprocessing system with two fixed bed reactors.    Hydrogen-rich gas (104)    Hydrocarbon diluent (110)    Bio-oil first stream (112)    First reactor (116)    Second reactor. (126)
NOVELTY - Refrigerant composition exhibiting a nominal composition, comprises: 57-59 wt.% pentafluoroethane; 38-41 wt.% 1,1,1,2-tetrafluoroethane; and 2.5-3 wt.% isobutane.    USE - The refrigerant composition is useful as replacement for R22 refrigerant for upgrading existing R22 refrigeration unit (claimed) and in air conditioning and refrigeration equipments.    ADVANTAGE - The refrigerant composition exhibits: cooling capacity relative to R22 refrigerant that is at least 90% at conventional operating conditions for an R22 refrigeration system; and performance factor relative to R22 refrigerant that is more than 1 and less than 1.2 (preferably less than 1.12) at conventional operating conditions for an R22 refrigeration system.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for upgrading an existing chlorodifluoromethane (R22) refrigeration unit using a mineral oil lubricant to eliminate the R22 refrigerant, comprising replacing the R22 refrigerant from the refrigeration unit with the refrigerant formulation.
NOVELTY - Preparing a product from a precursor material, comprises: mixing a particulate material and a binder to form a precursor material; and irradiating the precursor material with microwave radiation to activate the binder and form the product.    USE - The method is useful for preparing a product such as a fuel product from precursor material (claimed) including wood, paper, plastic, coal fines, biomass, low moisture bituminous coal fines, high moisture bituminous coal fines, sub-bituminous coal fines, lignite, anthracite coal fines, wheat straw, corn stover, switch grass, Miscanthus, hemp, willow, Sorghum, sugar cane, bamboo, poplar, oak, wood chips, saw dust, municipal solid waste, yard clippings, or leaves, where the fuel includes coal and biomass.    ADVANTAGE - The method is capable of economically preparing the fuel product from precursor material.
NOVELTY - The integrated power generation and chemical production method involves introducing an anode fuel stream (105) including reformable fuel into anode inlet of anode (127) of MCFC then introducing cathode inlet stream (119) including carbon dioxide and oxygen into a cathode inlet of cathode (129) of MCFC. The MCFC is operated to generate electricity at predetermined thermal ratio while generating anode exhaust (125) from an anode outlet. A hydrogen-containing stream, a synthesis gas-containing stream, or a combination, are separated from anode exhaust.    USE - Integrated power generation and chemical production method.    ADVANTAGE - Reduces or minimizes losses due to loss of heat energy by operating a MCFC to reform excess fuel and allow for production of increased synthesis gas and/or increased hydrogen while minimizing the system complexity for heat exchange and reforming. The additional synthesis gas and/or additional hydrogen can then be used in a variety of applications, including chemical synthesis processes and/or collection/repurposing of hydrogen for use as a clean fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the reaction system.    Fuel stream (105)    Cathode inlet stream (119)    Anode exhaust (125)    Anode (127)    Cathode (129)
NOVELTY - The hydrogen generation method involves operating MCFC to generate electricity while generating anode exhaust including hydrogen and carbon dioxide. A separation on the anode exhaust is performed to form a carbon dioxide-rich gas stream, and a carbon dioxide-depleted gas stream. The carbon dioxide-depleted gas stream is delivered to subsequent refinery processes. The further separation is performed to carbon-depleted gas stream to produce hydrogen-rich stream.    USE - Hydrogen generation method used in refinery.    ADVANTAGE - Utilizes MCFC to generate electricity and provide hydrogen to various refinery processes, including providing hydrogen in place of using a carbon-based fuel for various combustion reactions. The carbon dioxide-containing streams generated by refinery processes can also be used as input streams to the MCFC. Enables stream to be transported easily and efficiently over long distances at relatively low cost and effectively distributed over a wide area.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the operation of an MCFC for generation of electrical power.
NOVELTY - Producing electricity, comprises: introducing recycled anode exhaust fuel stream, low energy content fuel stream, and oxygen-containing stream into combustion zone; performing combustion reaction in combustion zone to generate combustion exhaust; introducing anode fuel stream comprising reformable fuel into anode; introducing cathode inlet stream comprising carbon dioxide and oxygen into cathode; generating electricity within molten carbonate fuel cell; generating anode exhaust comprising hydrogen; and separating at least portion of anode exhaust to form recycled anode exhaust fuel stream.    USE - The method is useful for producing electricity.    ADVANTAGE - The method: utilizes fuel cells which are operated to have reduced anode fuel utilization; and generates electricity with reduced greenhouse gas emissions.    DETAILED DESCRIPTION - Producing electricity, comprises: introducing a recycled anode exhaust fuel stream, a low energy content fuel stream, and an oxygen-containing stream into a combustion zone, where the recycled anode exhaust fuel stream comprises hydrogen, and the low energy content fuel stream comprises at least 30 vol.% of at least one inert gas; performing a combustion reaction in the combustion zone to generate a combustion exhaust; introducing an anode fuel stream comprising a reformable fuel into an anode of a molten carbonate fuel cell, and/or an internal reforming element associated with the anode of the molten carbonate fuel cell; introducing a cathode inlet stream comprising carbon dioxide and oxygen into a cathode of the molten carbonate fuel cell; generating electricity within the molten carbonate fuel cell; generating an anode exhaust comprising hydrogen from an anode outlet of the molten carbonate fuel cell; and separating at least a portion of the anode exhaust to form the recycled anode exhaust fuel stream.
NOVELTY - Synthesizing hydrocarbonaceous compounds comprises: introducing a fuel stream comprising a reformable fuel into an anode of a molten carbonate fuel cell and/or an internal reforming element associated with the anode; introducing a cathode inlet stream comprising carbon dioxide and oxygen into a cathode of the cell; generating electricity within the cell; generating an anode exhaust comprising hydrogen (H2), carbon monoxide (CO) and carbon dioxide (CO2); reacting a portion of the anode exhaust under effective Fischer-Tropsch conditions in presence of a shifting Fischer-Tropsch catalyst.    USE - The method is useful for synthesizing hydrocarbonaceous compounds (claimed) using Fischer-Tropsch synthesis.    ADVANTAGE - The method is capable of efficiently synthesizing the hydrocarbonaceous compounds with high quality.    DETAILED DESCRIPTION - Synthesizing hydrocarbonaceous compounds comprises: introducing a fuel stream comprising a reformable fuel into an anode of a molten carbonate fuel cell and/or an internal reforming element associated with the anode; introducing a cathode inlet stream comprising carbon dioxide and oxygen into a cathode of the molten carbonate fuel cell; generating electricity within the molten carbonate fuel cell; generating an anode exhaust comprising hydrogen (H2), carbon monoxide (CO) and 20 vol.% of carbon dioxide (CO2); reacting a portion of the anode exhaust under effective Fischer-Tropsch conditions in the presence of a shifting Fischer-Tropsch catalyst to produce a gaseous product and a non-gaseous product, where a CO2 concentration in a portion of the anode exhaust is 80% of a CO2 concentration in the anode exhaust; and recycling a portion of the gaseous product to the cathode inlet.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic view of a molten carbonate fuel cell.    Fuel stream (105)    Fuel cell (120)    Anode exhaust (125)    Second water-gas shift reactor (131)    Carbon dioxide output stream. (143)
NOVELTY - Method of producing fermentable sugars from cellulosic biomass, involves providing in a reaction vessel at starting time, a reaction mixture comprising 40-70 wt.% cellulosic biomass and 4-24 wt.% ammonia, increasing the liquid content of the reaction mixture over time to a final time tn, where the solid concentration decreases by 20-30% and producing a pretreated biomass, and contacting the pretreated biomass with a saccharification enzyme consortium under suitable conditions to produce fermentable sugars.    USE - The method is useful for producing fermentable sugars which are contacted with a biocatalyst for the production of a target compound chosen from ethanol, methanol, propanol, butanol, 1,3-propanediol, glycerol, xylitol, mannitol, lactic acid, acetic acid, formic acid, succinic acid, glutamic acid, 3-hydroxypropionic acid, fumaric acid, maleic acid and butyric acid (all claimed).    ADVANTAGE - The fermentable sugars are produced in at least 3% greater yield than yield from a process with constant biomass solid concentration.
NOVELTY - Processing a stream of cellulosic fines containing inorganic particles having an affinity for polysaccharide degradative enzymes, comprises: adding at least one surfactant to the stream to bind to surfaces of the inorganic particles to reduce interaction with the enzymes without inactivating the enzymes in solution; adding at least one polysaccharide degradative enzyme to the solution; and maintaining the solution with the cellulosic fines, the surfactant and the enzyme for a sufficient period of time to degrade at least a portion of the cellulosic fines into fermentable sugars.    USE - The method is useful for processing stream of cellulosic fines (claimed) to produce high value fermentable sugars, which are used to produce bioethanol, biodiesel, alkoxy ester, and bioplastics e.g. polyhydroxyalkanoates.    ADVANTAGE - The method: avoids the use of membranes and separation tanks to separate inhibitors, thus lowering the cost; and enables both the organic and inorganic components to be separated and made available for downstream use, thus substantially reducing the amount of burden on landfill.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) enzymatically hydrolyzing a mixed stream of cellulosic fines and inorganic particles having a competitive binding affinity for hydrolytic enzymes, comprising adding at least one surfactant to the stream to reduce an affinity of the hydrolytic enzymes for the inorganic particles, adding at least one hydrolytic enzyme to the solution, and hydrolyzing the cellulosic fines with the hydrolytic enzyme; and    (2) a system for enzymatically hydrolyzing the mixed stream of cellulosic fines and inorganic particles, comprising a feed for adding the surfactant to the stream, a feed for adding the hydrolytic enzyme to the solution, and an incubator for hydrolyzing the cellulosic fines with the hydrolytic enzyme.
NOVELTY - Deactivating organisms used in fermenting a biomass to produce one or more bioproducts, comprises conveying the organisms from a fermentation chamber to a distillation unit, and then effecting a positive six-log kill of the organisms in the distillation unit.    USE - The method is useful for deactivating organisms used in fermenting a biomass to produce one or more bioproducts (claimed).    ADVANTAGE - The method can be efficiently used in deactivating organisms (e.g., naturally occurring organisms, genetically modified organisms, etc.) used to ferment biomass in connection with bioproduct production processes.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a system for producing one or more bioproducts, comprising: a chamber comprising genetically modified organisms operable to ferment a biomass to a desired bioproduct; a distillation unit configured to receive the fermented biomass, including the genetically modified organisms, from the chamber, the distillation unit operable to separate the desired bioproduct from the fermented biomass, the distillation unit also operable to effect a positive six-log kill of the genetically modified organisms in the distillation unit.
NOVELTY - Controlling bacterial contamination in ethanol fermentation, comprises: (a) introducing a fermentation mixture comprising yeast Saccharomyces cerevisiae into a vessel used during ethanol production; (b) introducing either (b1) a recombinant bacteriophage lytic endolysin as an active agent, (b2) a recombinant yeast host cell comprising genes that encode the recombinant bacteriophage lytic endolysin or (b3) a recombinant yeast extract from the host cell to the vessel; and (c) fermenting the fermentation mixture by the yeast to produce ethanol.    USE - The method is useful for controlling bacterial contamination comprising lactic acid bacterial contamination in ethanol fermentation (claimed).    ADVANTAGE - The method utilizes the endolysin constructs, which are highly exolytic against a variety of lactobacilli in fermentation systems.    DETAILED DESCRIPTION - Controlling bacterial contamination in ethanol fermentation, comprises: (a) introducing a fermentation mixture comprising yeast Saccharomyces cerevisiae into a vessel used during ethanol production; (b) introducing either (b1) a recombinant bacteriophage lytic endolysin as an active agent, (b2) a recombinant yeast host cell comprising genes that encode the recombinant bacteriophage lytic endolysin or (b3) a recombinant yeast extract from the host cell to the vessel; and (c) fermenting the fermentation mixture by the yeast to produce ethanol. The recombinant endolysin is an antimicrobial agent having exolytic activity for at least one of targeted Gram positive lactic acid bacterial species to at least reduce the levels of growth of and colonization by the targeted lactic acid bacterial species present in the vessel during ethanol production without inhibiting the growth of the fermenting yeast or recombinant yeast host cells in the vessel, thus resulting in increased ethanol production from the fermentation mixture.
NOVELTY - Synthesizing hydrocarbonaceous compounds, comprises e.g.: introducing a fuel stream comprising a reformable fuel into an anode of a molten carbonate fuel cell and/or an internal reforming element associated with the anode; introducing a cathode inlet stream comprising carbon dioxide and oxygen into a cathode of the fuel cell; generating electricity within the molten carbonate fuel cell; generating an anode exhaust comprising hydrogen, carbon monoxide, and carbon di oxide; and separating carbon di oxide from at least a portion of the anode exhaust to produce an anode effluent gas stream.    USE - The method is useful for synthesizing hydrocarbonaceous compounds.    ADVANTAGE - The method provides increased power production on-site which: is efficient due to reducing or minimizing transmission losses; and reduces or potentially eliminates the need for inverters and/or other power electronics that can further lower electrical efficiency.    DETAILED DESCRIPTION - Synthesizing hydrocarbonaceous compounds, comprises: introducing a fuel stream comprising a reformable fuel into an anode of a molten carbonate fuel cell and/or an internal reforming element associated with the anode; introducing a cathode inlet stream comprising carbon di oxide and oxygen into a cathode of the fuel cell; generating electricity within the molten carbonate fuel cell; generating an anode exhaust comprising hydrogen, carbon monoxide, and carbon di oxide; separating carbon di oxide from at least a portion of the anode exhaust to produce an anode effluent gas stream; reacting at least a portion of the anode effluent gas stream in the presence of a methanol synthesis catalyst under conditions for forming methanol to produce at least one methanol-containing stream and at least one stream comprising gaseous or liquid products; and recycling at least a portion of the streams comprising gaseous or liquid products to form at least a portion of a cathode inlet stream.
NOVELTY - Producing hydrolyzate from cellulosic material comprises: adding hydrothermally treated stillage and/or a fraction to cellulosic material; treating the mixture of hydrothermally treated stillage and cellulosic material with at least one hydrolyzing enzyme; and hydrolyzing complex carbohydrates in the cellulosic material.    USE - The method is useful for: producing hydrolyzate from cellulosic material including dried distillers grains, corn kernel fiber, wheat straw, grasses, corn stover, corn cobs, silage, bagasse, wood chips, forest trimmings, starch and sugars consisting of sugar beets, cane sugar and sweet sorghum; increasing sugar production rate and yield of sugars from cellulosic material; producing ethanol, organic acids and organism metabolites; and producing biomass including algae, fungi, yeast and/or bacteria (all claimed), where the ethanol is useful as an oxygenate, octane booster and extender in gasoline.    ADVANTAGE - The cost effective method economically and efficiently produces the hydrolyzate in high yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the hydrolyzate produced by the above method.
NOVELTY - Method for producing plant biomass involves growing plant having plant cells carrying an exogenous gene that promotes double-stranded DNA breakage, where the biomass of the plant is increased.    USE - The method involves producing plant biomass (claimed).    ADVANTAGE - The method enables to produce plant biomass with increased yield and reduced emission of green house gases from plants.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) plant production method involves introducing an exogenous gene that promotes double-stranded DNA breakage into plant cells and obtaining transformed plant cells, and obtaining plant which has acquired biomass increasing ability from the transformed plant cells;    (2) transformed plant having plant cells carrying the exogenous gene that promotes double-stranded DNA breakage, and having increased ploidy;    (3) plant acquired by hybridization using as parent plant transformed plant having plant cells carrying exogenous gene that promotes double-stranded DNA breakage, and having increased ploidy;    (4) seed of the plant;    (5) method for producing plant having biomass increasing ability, involves hybridizing the first plant with second plant;    (6) method for producing useful substance, involves fermenting the biomass of the plant as raw material; and    (7) plant biomass increasing agent, comprising DNA coding for protein having double-stranded DNA breakage activity.
NOVELTY - Synthesizing low nitrogen concentration organic product from biomass comprises: a first hydrothermal treatment comprising treating together an aqueous suspension of a biomass and a first organic solvent (120), which is immiscible with water at room temperature, under a first subcritical hydrothermal condition comprising a first treatment temperature of 150-350 degrees C and pressure of 500-3000 psi to produce a first multi-phasic mixture including an organic phase and an aqueous phase; and separating the organic phase from the aqueous phase (130).    USE - The method is useful for synthesizing low nitrogen concentration organic product from biomass comprising algae consist essentially of microalgae (all claimed). The product is suitable for refining into hydrocarbons (transportation fuels).    ADVANTAGE - The subcritical hydrothermal treatment can be performed at a generally low temperature and followed by a second hydrothermal treatment at high temperature.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a product consisting of organic phase produced by the process.    DESCRIPTION OF DRAWING(S) - The figure shows a flowchart representing the method of synthesizing low nitrogen concentration organic product from biomass.    Obtaining biomass (110)    Subjecting the biomass together with solvent into a subcritical hydrothermal treatment (120)    Separating the organic phase from aqueous phase (130)    Refining organic phase (140)    Optionally processing the aqueous phase (160)
NOVELTY - A wood plastic composite (C1) comprises thermoplastic resin; cellulosic filler; lubricant, and optionally coupling agent. The lubricant comprises oleaginous microbial biomass.    USE - As wood plastic composite used in article such as flooring material, outdoor decking, wood paneling, window framing material, interior trim material, railing, fencing, and automotive part (claimed).    ADVANTAGE - The composite is free from metal stearates (preferably zinc stearate) not derived from oleaginous microbe. The composite improves bulk properties (such as density, impact resistance, flexural strength, flexural modulus, and water absorptivity) when an oleaginous biomass is used to as lubricant replacement in wood plastic composite.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing wood plastic composite (C1) involving mixing oleaginous microbial biomass with thermoplastic resin, cellulosic filler, and optionally coupling agent to form mixture; extruding, injection molding, or calendaring the mixture to form composite (C1).
NOVELTY - Hydroisomerization of a paraffinic hydrocarbon feedstream involves contacting the hydrocarbon feedstream with hydrogen, and a catalyst comprising a crystalline metal silicate molecular sieve having iron in the crystalline framework; and yielding a product having an increase in branched hydrocarbons relative to the feedstream.    USE - For the hydroisomerization of a paraffinic hydrocarbon feedstream to obtain a product (i.e. diesel fuel and biojet fuel) having an increase in branched hydrocarbons (claimed).    ADVANTAGE - The method produces product having a cloud point of 0 to -65 degrees C, particularly the product is a diesel fuel having a cloud point of -10 to -50 degrees C, and is a biojet fuel having a cloud point of -25 to -65 degrees C; and utilizes modified zeolite catalyst to obtain product in high yield.
NOVELTY - Stabilized aminophenolic composition comprises: a 2,4,6-tris(di-1-6 carbons containing-alkyl aminomethyl)phenol (TDAP); and at least one component comprising an ester based fluid comprising esters of mono-, di-, tri- or poly-hydroxy alcohols, or at least one mono 12-30C carboxylic fatty acid in a molar ratio of up to 3 moles of mono 12-30C carboxylic fatty acid per mole of TDAP so that a salt is formed from the mono 12-30C carboxylic fatty acid and the TDAP.    USE - The stabilized aminophenolic composition is useful as dielectric fluids, lubricant fluids and biodiesel fluids.    ADVANTAGE - The stabilized aminophenolic composition: has an oxidative stability index of greater than 20 hours at 130 degrees C as measured by AOCS 12b-92; has an improved stability relative to the TDAP alone, where the improved stability is demonstrated by at least one of the performance metrics including an extrapolated onset of thermal decomposition of the TDAP in the stabilized aminophenolic composition occurs at a higher temperature than the extrapolated onset of thermal decomposition of the substantially pure TDAP as measured by thermogravimetric analysis, ASTM E2402-11, preferably the extrapolated onset of thermal decomposition of the TDAP in the stabilized aminophenolic composition occurs at a temperature greater than 153 degrees C as measured by thermogravimetric analysis, ASTM E2402-1 (all claimed); exhibits hydrolytic stability at higher use temperatures; utilizes additives to enhance the stability of the vegetable oils which are more cost effective than chemically modifying the oils; and utilizes the salts which have higher thermal stability, greater solubility in oils, and are safer and less hazardous.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for stabilizing an aminophenolic composition comprising mixing the components (a) and (b) together at or above ambient temperature, through which the stabilized aminophenolic composition is obtained.
NOVELTY - Mixed solvent fermentation process (P1) comprises: (a) culturing lignocellulosic biomass with wood-rot fungi of the phylum Basidiomycota in an appropriate bioreactor and under appropriate aerobic conditions for an appropriate amount of time to establish growth; and (b) converting the bioreactor to anaerobic conditions to produce a vapor phase containing volatile solvents.    USE - The process is useful for mixed solvent fermentation (claimed) which is useful for producing biofuels including petroleum-derived diesel or jet fuel.    ADVANTAGE - The process efficiently generates sulfur-free fuels from low-cost raw materials, and thus is cost effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a mixed solvent fermentation process (P2) comprising: step (a) as above per se; and introducing into the bioreactor an appropriate amount of a metabolic inhibitor to produce a vapor phase containing volatile solvents.
NOVELTY - The method comprises: injecting 9,10-anthraquinone into a water system; injecting a nitrate or nitrite into the water system; injecting nitrogen reducing bacteria into the water system; and injecting a molybdate or molybdate salt into the water system. The 9,10-anthraquinone is continuously applied or periodically applied at a pre-set frequency. The nitrate or nitrite is continuously applied in an amount to achieve a concentration of less than 500 ppm by weight in the water solution. The bacteria is present in an amount to achieve a concentration of 10-108 bacteria count/ml in water system.    USE - The method is useful for controlling sulfides in water systems (claimed) for controlling souring and microbiologically influenced corrosion in oil and gas production.    ADVANTAGE - The method is capable of effectively controlling the sulfides in the water systems in an environmentally friendly manner using non toxic biocides including nitrogen reducing bacteria.    DETAILED DESCRIPTION - The method comprises: injecting 9,10-anthraquinone into a water system; injecting a nitrate or nitrite into the water system; injecting nitrogen reducing bacteria into the water system; and injecting a molybdate or molybdate salt into the water system. The 9,10-anthraquinone is continuously applied or periodically applied at a pre-set frequency. The nitrate or nitrite is continuously applied in an amount to achieve a concentration of less than 500 ppm by weight in the water solution. The nitrogen reducing bacteria is present in an amount to achieve a concentration of 10-108 bacteria count/ml in the water system. An amount of molybdate or molybdate salt added is sufficient to achieve 5-100 ppm by weight in the water system. The 9,10-anthraquinone is added in quantities sufficient to achieve a concentration of 5-1000 ppm by weight in the water system.
NOVELTY - Improved artificial fireplace log (10) comprises an elongated combustible body defined by a solid core and formed from compacted recycled wood fibers and bio waxes derived from organic materials, where the log contains a luxurious scented material that produces a luxurious scent when the log is burned.    USE - The artificial fireplace log is useful in indoor and outdoor of house.    ADVANTAGE - The improved artificial fireplace log has enhanced fragrances, and high standard quality, convenience, reliability, and environmental sustainability, and can be wrapped in paper without requiring kindling or starting material.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of an artificial fireplace log.    Artificial fireplace log (10)    Container (11)    Inlet (12)    Log sections (14, 15)    Multiple fragrant pellet. (16)
NOVELTY - Refinery system (10A) comprises: a feedstock supply line (11A); a first endothermic chamber that receives feedstock from the feedstock supply line and processes the feedstock under elevated heat during a first time period; a second endothermic chamber that receives feedstock from the feedstock supply line under elevated heat during a second time period; and a refining processor downstream and in communication with each of the first chamber and the second chamber.    USE - The refinery system is useful for processing syncrude and syngas for generating an oil byproduct including biodiesel.    ADVANTAGE - The refinery system: maintains a continuous supply of syngas, syncrude, and carbon char from processed feedstock, and thus eliminates inefficiencies associated with starting and stopping a pyrolysis system, increases production uptime and yields higher efficiency in recycling feedstocks; and has single downstream processing equipment and thus is cost effective.    DESCRIPTION OF DRAWING(S) - The figure illustrates a system diagram of a portion of a processing system.    Refinery system (10A)    Feedstock supply (11A)    Endothermic chamber (12A)    Catalytic chamber (14A)    Compressor (20)
NOVELTY - System, comprises: a water supply; a hydrogen production cell, where water is cleaved into hydrogen and oxygen atoms by electrolysis and orthohydrogen is converted into parahydrogen; a water trap and filter, where trace water is separated from parahydrogen; a magnetic reactor, where parahydrogen is converted into atomic hydrogen; and a mix tank, where atomic hydrogen is mixed with a combustible gas.    USE - The system is useful for converting orthohydrogen into parahydrogen, converting parahydrogen into atomic hydrogen, and mixing converted atomic hydrogen with a combustible gas (claimed).    ADVANTAGE - The system: minimizes unburned hydrocarbon and carbon dioxide emissions; and provides a carbon-free combustible fuel which can be easily ignited under conditions of low oxygen.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for converting orthohydrogen into parahydrogen, converting parahydrogen into atomic hydrogen, and for mixing converted atomic hydrogen with a combustible gas, comprising: feeding water from a water supply into a hydrogen production cell, where the hydrogen production cell comprises at least one microcell connected in series; pulsing electric current into the microcells to enable electrolysis in the hydrogen production cell, where water molecules are broken down into molecular hydrogen and molecular oxygen, and the molecular hydrogen is part orthohydrogen and part parahydrogen; passing the molecular hydrogen through a first set of coils positioned at the hydrogen output of each microcell, where a vibrational frequency is applied inside of the coils to convert orthohydrogen into parahydrogen; passing the parahydrogen through a magnetic reactor containing at least one magnet to convert the parahydrogen into atomic hydrogen, where a second set of coils wrap around the magnetic reactor; and mixing the atomic hydrogen with a combustible gas to create a mixed gas fuel.
NOVELTY - Treating a reforming catalyst, comprises heating a catalyst metal used for reforming hydrocarbon in a reducing gas mixture environment, where the reducing gas mixture comprises hydrogen and at least one sulfur-containing compound. The sulfur containing compound includes one or more of hydrogen sulfide, carbonyl sulfide, carbonyl disulfide and organic sulfur containing compounds such as thiophenes and thiophanes.    USE - The method is useful for treating a catalyst, which is useful for reforming hydrocarbon to produce hydrogen that is useful in a solid oxide fuel cell stack (all claimed).    ADVANTAGE - The method is capable of rapidly treating the catalyst with improved durability and without suppressing catalyst activity thus improving service life and efficiency the fuel cell stack.    DETAILED DESCRIPTION - Treating a reforming catalyst, comprises heating a catalyst metal used for reforming hydrocarbon in a reducing gas mixture environment, where the reducing gas mixture comprises hydrogen and at least one sulfur-containing compound. The sulfur containing compound includes one or more of hydrogen sulfide, carbonyl sulfide, carbonyl disulfide and organic sulfur containing compounds such as thiophenes, thiophanes, sulfide compounds of formula (RSH), disulfide compounds of formula (RS2R1), tri-sulfide compounds of formula (RS3R1) and mercaptan compounds of formula (RSR1). N.B.: R and R1 are not defined. An INDEPENDENT CLAIM is included for an article for reforming hydrocarbons, comprising the catalyst metal, where the catalyst metal is treated by heating in reducing gas mixture environment.
NOVELTY - Preparing tricalcium phosphate nanogranule, comprises (a) preparing a reaction solution containing clarified nitrate ion, phosphate ion and calcium ion, and (b) exciting the nitrate with water and high temperature initiator by a microwave reaction process to produce tricalcium phosphate nanogranule.    USE - The method is useful for preparing tricalcium phosphate nanogranule, which is useful in a genetic infection, a drug delivery, a fluorescent dyeing, a composite biological material and a bracket and for promoting biomedical bone tissue regeneration (all claimed).    ADVANTAGE - The method is capable of preparing the tricalcium phosphate nanogranule with good chemical properties and less energy consumption in an economical manner.
NOVELTY - A water treatment system comprises greater than or equal to 1 carrier platforms in which carrier platform comprises sedimentation tank (2), filter carrier (3), drainage cavity (4), and water outlet (5) formed on building structure (1).    USE - A water treatment system for river water source wetland drainage ditch sewage (claimed).    ADVANTAGE - Water treatment system is simple, low-cost, and easy to maintain, saves energy and cost, and has fast effect, high water purification efficiency, simple construction, and no pollution, and improves water source wetland water purification capacity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for purification of wastewater which involves naturally flowing sewage into sedimentation tank, performing preliminary sedimentation clarification, filtering sewage through rear wall into drainage cavity, filtering overflow downward through surface of filter carrier into drainage cavity, and flowing filtered water from drainage cavity through water outlet to next carrier platform or downstream.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of water treatment system.    Building structure (1)    Sedimentation tank (2)    Filter carrier (3)    Drainage cavity (4)    Water outlet (5)
NOVELTY - Treating kitchen garbage, comprises separating solid and liquid wastes from the garbage, subjecting the separated solid waste to biological treatment to form an organic fertilizer mother material and then decomposing to form an organic fertilizer, and sieving the organic fertilizer.    USE - The method is useful for treating kitchen garbage into an organic fertilizer (claimed).    ADVANTAGE - The method ensures safe treatment of the kitchen garbage into the organic fertilizer, thus reducing waste circulation, transportation cost of garbage landfill, incineration cost and peculiar smell of the garbage.
NOVELTY - The aerobic composting device comprises a dehydrator, a stirrer with which the dehydrator is connected, a compost bin with which the stirrer is connected, a fermentation bin with which the compost bin is connected, a suction unit, and an oxygen aeration unit.    USE - Aerobic composting device.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an aerobic composting method.
NOVELTY - Microbial inoculum comprises 20-30 wt.% of Trichoderma, 20-30 wt.% of Azotobacter, 20-30 wt.% of phosphate solubilizing bacteria, 20-30 wt.% of silicate bacteria, 20-30 wt.% of photosynthetic bacteria, 20-30 wt.% of Bacillus, 20-30 wt.% of yeast, 20-30 wt.% of actinomycete and 20-30 wt.% of lactic acid bacterium.    USE - The microbial inoculum is useful for fermenting organic solid waste material (claimed).
NOVELTY - Compost fermenting tower comprises compost tower (1), spray tower (2), gas absorption tower (3), cover (4), screw pole (5), gas pipe (6), gas supply pipe (7), support frame (8), bolt (10), discharge port (101), feeding port (102), first cover (103), pressing plate (501) and rotating handle (502).    USE - Compost fermenting tower.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of compost fermenting tower.    Compost tower (1)    Spray tower (2)    Gas absorption tower (3)    Cover (4)    Screw pole (5)    Gas pipe (6)    Gas supply pipe (7)    Support frame (8)    Bolt (10)    Discharge port (101)    Feeding port (102)    First cover (103)    Pressing plate (501)    Rotating handle (502)
NOVELTY - Organic fertilizer comprises 20-25 pts. wt. fermented chicken manure, 20-25 pts. wt. fermented cow dung, 40-50 pts. wt. inorganic nutrients comprising nitrogen, phosphorus and potassium, and 2-4 pts. wt. granulated binder.    USE - Organic fertilizer.    ADVANTAGE - The organic fertilizer has a quick and prolonged fertilizing effect.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for preparing the organic fertilizer comprising either mixing 50-60% of fresh chicken manure, 10-15% of bean cake, 5-10% of corn powder and 3-6% of sodium humate, inoculating microorganism corrosion solution agent, regulating water content to 60%, introducing the raw material into a solid fermenting device, where the fermentation is carried out at high temperature for more than 35 days, or at 50 degrees C for less than or equal to 12 days, drying and grinding, or fermenting dairy manure fermentation product including grass peat, fly ash and a fresh cow dung, by two secondary fermentation processes, adding proper amount of auxiliary material, and stacking to achieve a moisture content of 50-60%, adjusting ratio between carbon and nitrogen to 25-30:1, mixing 0.3% of fermenting cow manure, and fermenting at 60 degrees C for 48 hours to 20 days, mixing solid nitrogen, phosphorus and potassium at 45-50 degrees C for 15 days, drying and grinding.
NOVELTY - Preparing microorganism soil repairing agent, comprises: (a) culturing Bacillus licheniformis CGMCC1.7461 in a seed culture medium containing carbon source, nitrogen source and a growth factor; (b) fermenting the culture medium to obtain an organic phosphorus pesticide having an ability to degrade Bacillus licheniformis; and (c) mixing the pesticide with liquid microbial phosphorus and potassium fertilizer and a liquid concentrate of potassium humate in a ratio of 10-50:10-50:1-10.    USE - The process is useful for preparing microbial soil repairing agent (claimed).    ADVANTAGE - The process produces the microbial soil repairing agent in high yield and purity without polluting environment.    DETAILED DESCRIPTION - Preparing microbial soil repairing agent, comprises: (a) culturing Bacillus licheniformis CGMCC1.7461 in a seed culture medium containing carbon source, nitrogen source and a growth factor; (b) fermenting the culture medium to obtain an organic phosphorus pesticide having an ability to degrade Bacillus licheniformis; and (c) mixing the pesticide with liquid microbial phosphorus, potassium fertilizer and a liquid concentrate of potassium humate in a ratio of 10-50:10-50:1-10. The liquid microbial phosphorus potassium compound fertilizer is GB20287-2006 having an effective microbial bacteria content of greater than or equal to 200 million/ml of a commercial product.
NOVELTY - Organic fertilizer comprises 30-50 wt.% of animal manure, 30-50 wt.% of industrial and agricultural wastes, 5-20 wt.% of humic acid, 3-20 wt.% of activated powder, 1-5 wt.% of biological soil pesticide, 5-20 wt.% of sawdust or corn waste, and 5-15 wt.% of magnetized water. The fertilizer is prepared by: mixing animal manure, industrial and agricultural wastes, wooden meal or corn waste and humic acid according to the proportion and then crushing into 20-80 meshes; and adding activate powder and biological soil pesticide to the crushed mixture and then adding the magnetized water.    USE - Organic fertilizer.    ADVANTAGE - The fertilizer: is rich in organic substance and easy to decompose; maintains soil fertility; and has increased the utilization ratio.    DETAILED DESCRIPTION - Organic fertilizer comprises 30-50 wt.% of animal manure, 30-50 wt.% of industrial and agricultural wastes, 5-20 wt.% of humic acid, 3-20 wt.% of activated powder, 1-5 wt.% of biological soil pesticide, 5-20 wt.% of sawdust or corn waste, and 5-15 wt.% of magnetized water. The fertilizer is prepared by: mixing animal manure, industrial and agricultural wastes, wooden meal or corn waste and humic acid and then crushing into 20-80 meshes; adding activate powder and biological soil pesticide to the crushed mixture and then adding the magnetized water, and uniformly stirring the mixture; and drying the stirred mixture and then fermenting for 20-30 days.
NOVELTY - Organic fertilizer comprises 30-70 pts. wt. tea saponin, 20-50 pts. wt. bagasse, 15-30 pts. wt. straw, 0.01-0.5 pts. wt. effective microorganism (EM)-inoculum, 0.01-3 pts. wt. strain regulator, 5-20 pts. wt. balancing agent, and 0.01-3 pts. wt. seaweed.    USE - The organic fertilizer is useful for rice (claimed) and providing resistance to rice against insects and bacteria.    ADVANTAGE - The organic fertilizer can improve the soil structure and effectively reduce the heavy metal content in soil and rice paddy fields.    DETAILED DESCRIPTION - Organic fertilizer comprises 30-70 pts. wt. tea saponin, 20-50 pts. wt. bagasse, 15-30 pts. wt. straw, 0.01-0.5 pts. wt. effective microorganism (EM)-inoculum, 0.01-3 pts. wt. strain regulator, 5-20 pts. wt. balancing agent, and 0.01-3 pts. wt. seaweed. The organic fertilizer is prepared by mixing fermentation material of the rice, bagasse and straw in a fermentation tank, adjusting water content to 50-70%, adding EM inoculum and fermenting until the fertilizer is decomposed, then adding the strain regulator and balancing agent and uniformly stirring, enzymolyzing the fermented fertilizer and then naturally drying, crushing the material using 50-100 mesh sieve, and adding alginate material and then uniformly mixing, granulating and packaging.
NOVELTY - Composite microbial fertilizer comprises an organic fertilizer component, an inorganic fertilizer component, bentonite, a composite microbial component, 10-15 wt.% of nitrogen, 4-8 wt.% of phosphorus, 6-10 wt.% of potassium, and 25 wt.% of organic matter. The microorganism number content in the composite microbial component is 2-18 hundred million colony forming unit/g.    USE - The composite microbial fertilizer is useful for rice (claimed) and for preventing and treating a rice disease, preferably bacterial and fungal diseases.    ADVANTAGE - The composite microbial fertilizer improves rice yield and quality and soil environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the fertilizer, comprising mixing the organic fertilizer component, the inorganic fertilizer component and bentonite according to a ratio of 33.3:35.1-62.4:0.3-27.6, pelleting the mixture into granule with grain diameter of 4 mm, then adding nitrogen, phosphorus, potassium, and organic matter to obtain a semi finished product having a water content of 12%, adding the composite microbial component into the semi finished product according to a weight ratio of 96:4, and uniformly mixing at 30 degrees C to obtain a finished product having a water content of 15% .
NOVELTY - Preparing an organic substance comprises mixing 40-42 pts. wt. chicken manure, 30-36 pts. wt. mushroom residue, 25-30 pts. wt. cotton seed hull, 40-50 pts. wt. rice corn, 12-18 pts. wt. tobacco stalk, 10-12 pts. wt. grass peat, 6-8 pts. wt. perlite and 3-5 pts. wt. ceramic compound in a fermenting tank, adding 1-3% of organic matter in the mixture and then sealing in a plastic film, adding water in the sealed mixture and then adjusting the water content of the mixture to 55-70%, and fermenting the mixture at 60-70 degrees C for 3 days.    USE - The method is useful for preparing an organic substance, which is useful for cultivating cherry tomato (claimed).    ADVANTAGE - The method is capable of preparing the organic substance with improved quality and disease resistance ability.    DETAILED DESCRIPTION - Preparing an organic substance comprises mixing 40-42 pts. wt. chicken manure, 30-36 pts. wt. mushroom residue, 25-30 pts. wt. cotton seed hull, 40-50 pts. wt. rice corn, 12-18 pts. wt. tobacco stalk, 10-12 pts. wt. grass peat and 6-8 pts. wt. perlite in a fermenting tank, adding 1-3% of organic matter in the mixture and then sealing in a plastic film, adding water in the sealed mixture and then adjusting the water content of the mixture to 55-70%, fermenting the mixture at 60-70 degrees C for 3 days, adjusting pH value of the fermented mixture to 6.8-7.2 and a control value of the mixture to 0.90-1.1 mS/cm, drying the mixture until water content becomes 5-8%, screening, cleaning and air separating the dried mixture, separating the mixture having a grain diameter of less than 6 mm, and adding 1-4% of Bacillus subtilis and Bacillus licheniformis in the mixture and then packaging.
NOVELTY - Special fertilizer for Eucommia seedling comprises 10-30 pts. wt. urea as nitrogen source, 5-15 pts. wt. diammonium phosphate as phosphate source, 20-30 pts. wt. shrimp shell powder, 5-20 pts. wt. chicken manure, 5-20 pts. wt. soybean meal, and 5-15 pts. wt. seaweed powder.    USE - As special fertilizer for Eucommia seedling.    ADVANTAGE - The special fertilizer is environmentally-friendly, cost-effective, convenient to use, and simple to prepare, and promotes rapid growth of Eucommia seedling.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the special fertilizer, which involves mixing the chicken manure, soybean meal, and seaweed powder, fermenting mixture for 15-18 days, uniformly mixing fermented mixture with shrimp shell powder, urea, and diammonium phosphate, granulating the mixture using polyvinyl formaldehyde solution, continuously rolling granulated mixture to obtain rolled product with diameter of 2-4 mm, and drying, sieving, and cooling rolled product.
NOVELTY - Organic fertilizer comprises 6-8 wt.% of compost material consisting of dried lake sludge and dried rice straw, a chemical fertilizer, 0.6-1.2 wt.% of plant growth regulator, 1-2 wt.% of compost agent, 1-2 wt.% of molasses or brown sugar, and 50-60 wt.% of water. The organic fertilizer is prepared by crushing dried lake sludge and dried lake sludge, then adding the compost agent, the molasses or brown sugar, water, the chemical fertilizer and plant growth regulator, and fermenting the mixture at 50-60 degrees C for 42 days to obtain the organic fertilizer.    USE - The organic fertilizer is useful for promoting vegetation restoration (claimed), where the vegetation includes camphor trees, oak trees, Osmanthus shrubs, and Pittosporum tobira.    ADVANTAGE - The organic fertilizer increases a soybean nodulation and chlorophyll concentration (SPAD) value to 11.4-15.6% and leaf area to 13.6-40.7%.    DETAILED DESCRIPTION - Organic fertilizer comprises 6-8 wt.% of compost material consisting of dried lake sludge having a water content of less than 10% and dry weight ratio of 1.2-1.8 and dried rice straw having a dry weight ratio of 0.8-1.2, a chemical fertilizer, 0.6-1.2 wt.% of plant growth regulator, 1-2 wt.% of compost agent, 1-2 wt.% of molasses or brown sugar, and 50-60 wt.% of water. The chemical fertilizer is urea. The compost agent is VT-1000. The plant growth regulator is algae. The organic fertilizer is prepared by crushing dried lake sludge and dried lake sludge, then adding the compost agent, the molasses or brown sugar, water, the chemical fertilizer and plant growth regulator, fermenting the mixture at 50-60 degrees C for 42 days to obtain the organic fertilizer having an organic matter content of 35-45% and nitrogen content of 0.7-1%. An INDEPENDENT CLAIM is included for preparing the organic fertilizer.
NOVELTY - Acidic paddy soil conditioner comprises a component A prepared by mixing 25-70 pts. wt. plant ash, 20-35 pts. wt. biological carbon, 20-35 pts. wt. lime paste, and 1-15 pts. wt. plant source organic fertilizer, and then extrusion molding the mixed material. The mixed material has a pH value of 8-12, organic matter content of more than 10 wt.%, calcium carbonate content of greater than 20 wt.%, 4-8 wt.% of potassium oxide, and less than 28 wt.% of water content.    USE - Acidic paddy soil conditioner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for application method of acidic paddy soil conditioner, comprising uniformly applying 80-160 kg/667 m2 of the component A in the soil before planting crops.
NOVELTY - Extraction distillation separation of cyclohexane and ethyl acetate mixture is carried out by sending mixture to an extraction distillation tower having 40-80 theoretical plates, and extracting using mixture of dimethyl sulfoxide and N,N-dimethylformamide as extracting agent; collecting cyclohexane at distillation tower top and collecting extracting agent and ethyl acetate at tower bottom; and circulating extracting agent.    USE - Method for extraction distillation separation of cyclohexane and ethyl acetate mixture (claimed).    ADVANTAGE - The method has low energy consumption, high yield and safe and simple operation, is environment-friendly, and can realize clean production.
NOVELTY - Preparation of pharmaceutical-grade anhydrous ethanol involves preparing composite absorbent agent, filling obtained composite absorbent in absorber, passing mixture of ethanol and water into absorber, maintaining absorber temperature at 85 degrees C under pressure of 1.2-1.5 atm, condensing ethanol in condensation tower, drying anhydrous ethanol in upper end of the absorber through condensing column, and maintaining the condensing column temperature at 15 degrees C.    USE - Preparation of pharmaceutical-grade anhydrous ethanol (claimed).    ADVANTAGE - The method efficiently provides high-quality pharmaceutical-grade anhydrous ethanol with high yield and productivity, by simple method with reduced consumption of energy without affecting the environment.
NOVELTY - Method of purifying long-chain dicarboxylic acid involves mixing crude long-chain dicarboxylic acid with paraffin, heating, dissolving, separating alkane solution, and carrying out cooling-crystallization or precipitation.    USE - Method of purifying long-chain dicarboxylic acid (claimed).    ADVANTAGE - The method efficiently provides purified long-chain dicarboxylic acid with high yield, with low energy consumption.
NOVELTY - Oxiracetam is refined by dissolving oxiracetam crude product in 1.5-10 times water, adding anion exchange resin at 25-60 degrees C, absorbing for 0.5-5 hours in which weight ratio anion exchange resin:oxiracetam crude product is 1/5-1, filtering resin particles, collecting filtered liquid, adding cation exchange resin as acid-binding agent in filtered liquid, regulating solution pH at 5-6, filtering resin, collecting filtered liquid, concentrating water part, taking resulting concentrated liquid residual solution with weight of 1.5-3 times oxiracetam crude product feeding amount, and cooling.    USE - Refinement of oxiracetam used for preparing medical-grade oxiracetam.    ADVANTAGE - Refinement process is low in cost, environment-friendly, simple, and controllable, has mild reaction conditions, effectively removes oxiracetam crude product impurities, and produces high purity and stable quality product.    DETAILED DESCRIPTION - Oxiracetam is refined by dissolving oxiracetam crude product in 1.5-10 times water, adding anion exchange resin at 25-60 degrees C, absorbing for 0.5-5 hours in which weight ratio anion exchange resin:oxiracetam crude product is 1/5-1, filtering resin particles, collecting filtered liquid, adding cation exchange resin as acid-binding agent in filtered liquid, regulating solution pH at 5-6, filtering resin, collecting filtered liquid, concentrating water part, taking resulting concentrated liquid residual solution with weight of 1.5-3 times oxiracetam crude product feeding amount, and cooling.
NOVELTY - 3-(2-Hydroxyethyl)-2-oxazolidinone preparation involves treating 1-(2-hydroxyethyl)ethyleneimine in presence of nitrogen-containing compound as a catalyst in a carbon dioxide atmosphere to perform cyclization reaction to give the target compound.    USE - Method for preparing 3-(2-hydroxyethyl)-2-oxazolidinone (claimed).    ADVANTAGE - The method prepares 3-(2-hydroxyethyl)-2-oxazolidinone in a simple, cost-effective and eco-friendly manner without using metal catalyst.    DETAILED DESCRIPTION - 3-(2-Hydroxyethyl)-2-oxazolidinone preparation involves treating 1-(2-hydroxyethyl)ethyleneimine in presence of nitrogen-containing compound as a catalyst in a carbon dioxide atmosphere to perform cyclization reaction to give the target compound. The nitrogen-containing compound is selected from methylcyanide, pyridine, aminopyridine, 2-methylpyridine, 2-(pyridine-2-yl)-6-(pyridine-3-yl)pyridine, triethylamine, tributylamine, (2-(dimethylamino)ethyl)dimethylamine, 2H,3H,4H,5H,6H,7H,8H,9H,10H-pyrimido(1,2-a)azepine, bicycle(2,2-a)octane, aniline, N-methylamine, dodecanamide, benzamide, N,N-dimethylbenzamide, N,N-dimethylaniline, pentafluorobenzamide, 4,6-dimethylpyrimidin-2-amine or benzonitrile.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic magnetic hydrogen spectrum of the prepared 3-(2-hydroxyethyl)-2-oxazolidinone.
NOVELTY - 2-((4-(Methoxy propoxy)-3-methyl pyridine-2-yl)methylthio)-1-H benzimidazole intermediate synthesis involves dissolving 2-chloromethyl-4-(3-methoxy-propoxy)-3-methyl-pyridine hydrochloride as raw material in water, and then neutralizing with an alkali solution to form combined organic phase. The formed organic phase is extracted by using organic solvent at 20-50 degrees C for 3-10 hour. The reaction mixture is poured into an ice-water bath, in which mercaptobenzimidazole is added dropwise at room temperature for 2-5 hours, and then allowed to stand form organic phase.    USE - Method for synthesizing 2-((4-(methoxy propoxy)-3-methyl pyridine-2-yl)methylthio)-1-H benzimidazole intermediate (claimed).    ADVANTAGE - The method synthesizes 2-((4-(methoxy propoxy)-3-methyl pyridine-2-yl)methylthio)-1-H benzimidazole intermediate in a simple and cost-effective manner with high product yield and high purity on industrial scale.    DETAILED DESCRIPTION - 2-((4-(Methoxy propoxy)-3-methyl pyridine-2-yl)methylthio)-1-H benzimidazole intermediate synthesis involves dissolving 2-chloromethyl-4-(3-methoxy-propoxy)-3-methyl-pyridine hydrochloride as raw material in water, and then neutralizing with an alkali solution to form combined organic phase. The formed organic phase is extracted by using organic solvent at 20-50 degrees C for 3-10 hour. The reaction mixture is poured into an ice-water bath, in which mercaptobenzimidazole is added dropwise at room temperature for 2-5 hours, and then allowed to stand form organic phase. The formed organic phase is placed at -20-10 degrees C in an ice bath, in which an organic oxidant is added dropwise. The reaction mixture is placed in an alkali solution at 5-25 degrees C in an ice water bath with stirring, and then allowed to stand to form aqueous phase. The formed aqueous phase is washed with acid (10-50%). The organic solvent and the combined organic phase are concentrated to obtain the finished intermediate.
NOVELTY - Producing sodium copper chlorophyllin by supercritical purification comprises (i) adding alcohol or ketone solvent in the pasty chlorophyll and dissolving, then adding liquid alkali, thermal insulating and carrying out saponification, (ii) subjecting the saponified chlorophyll for extraction washing with non-polar solvent, (iii) adding copper salt in washed chlorophyll, thermal insulating and coppering, (iv) using supercritical carbon dioxide for purifying copper chlorophyll, and (v) adding sodium hydroxide after purifying, and reacting to obtain the product.    USE - The method is useful for producing sodium copper chlorophyllin by supercritical purification (claimed).    ADVANTAGE - The method overcomes the particularity of molecular structure of chlorophyll derivative, can greatly increase the yield of copper-based chlorophyll, and is environmentally friendly.
NOVELTY - Synthesizing bivalirudin comprises coupling, deprotecting and washing using 3 ml/g of ethyl acetate for 1-9 times.    USE - The method is useful for synthesizing bivalirudin (claimed).    ADVANTAGE - The method synthesizes bivalirudin with high yield and quality in a cost-effective and environmentally-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for bivalirudin obtained by the method.
NOVELTY - A biomass biofuel pyrolysis method involves utilizing zinc chloride or inorganic salt and molten salt with melting point of more than 360 degrees C as a carrier.    USE - Method for pyrolysis of biomass biofuel.    ADVANTAGE - The method enables pyrolysis of biomass biofuel with high quality and high yield.
NOVELTY - An anti-coking additive for biomass fuel comprises 20-30 wt.% aluminium oxide, 15-30 wt.% magnesium carbonate, 40-65 wt.% calcium oxide and 2-8 wt.% biomass feedstock.    USE - As anti-coking additive in the biomass fuel preparation process (claimed).    ADVANTAGE - The anti-coking additive can increase pole straw biomass fuel ash fusion point which solves the biomass solid fuel combustion process coking problem and also can increase fuel efficiency, combustion efficiency and the utilization rate of straw fuel.
NOVELTY - The system has a conveying device, a straw crusher and a methane tank. The straw crusher is comprised with cylindrical movable blade (8), and fixed blade is positioned tangent to rotating mechanism. A conveying device is comprised with conveying cylinder, conveying tube and fan. The marsh gas tank is comprised with tank portion, tank cover, connecting tube and pneuma tank. A marsh gas tank pressure control mechanism is configured for controlling the inner pressure of marsh gas tank, and a temperature regulating mechanism is configured for regulating temperature of marsh gas tank.    USE - Marsh gas generating system.    ADVANTAGE - High efficiency, improved safety and energy-saving effect is achieved using the simple structured marsh gas generating system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the marsh gas generating system.    Movable cutter cylinder (7)    Movable blade (8)    Motor (9)    Shaft joint (10)    Rotating shaft (11)
NOVELTY - Producing biogas from cassava residue through fermentation involves taking wet cassava residue, which is then dried. The lumps of dried cassava residue is then crushed using mortar, and then placed in an oven at 60 degrees C for 8 hours to obtain dried and crushed cassava residue of constant weight.    USE - Method for producing biogas from cassava residue through fermentation and for preparing starch from generated cassava residue (claimed).    ADVANTAGE - The method enables to produce biogas by pre-processing agricultural waste to extract cellulose and lignin from cassava residue through fermentation technology. The produced biogas are generated in large amount, and is also prepared in simple and cost-effective manner.    DETAILED DESCRIPTION - Producing biogas from cassava residue through fermentation involves taking wet cassava residue, which is then dried. The lumps of dried cassava residue is then crushed using mortar, and then placed in an oven at 60 degrees C for 8 hours to obtain dried and crushed cassava residue of constant weight. The resulting product is then stored in a refrigerator at 4 degrees C, and then placed at room temperature. The refrigerated cassava product is then soaked in sodium hydroxide solution for 3 hours, taken out and then washed with distilled water to obtain neutralized cassava product. The neutralized cassava product is then dried at 60 degrees C, and then fermented, where pH value of the fermentation mixture is adjusted to 7.0 using hydrochloric acid and sodium hydroxide solution. The obtained product is then inoculated with sewage sludge in a sewage treatment tank at 35 plus minus 2 degrees C for 40 days to complete the production process of biogas. The generated cassava residue is then utilized for preparing starch.
NOVELTY - Anaerobic digestion of waste oil involves (a) adding sludge and fat-degrading bacteria in basal medium, where mass ratio of sludge, fat-degrading bacteria and basal medium is 100-300:1-2:1000, (b) adding inorganic medium to anaerobic fermentation bacteria before anaerobic digestion, in mass ratio of 1-12:100, and (c) sequentially adding 100 %mass anaerobic fermentation bacteria, 1-2 %mass waste oil and 0.1-0.15 %mass additive to the reactor, mixing uniformly, and producing biogas by anaerobic fermentation process.    USE - The method is useful for anaerobic digestion of waste oil which is useful for producing biogas (claimed).    ADVANTAGE - The method increases fat degradation activity of microorganism, increases the contact area of microorganism with oil, as inorganic media is added, and converts waste oil into biogas.
NOVELTY - Processing cellulose-containing biomass material comprises: (a) placing cellulose-containing biomass material into storage container; (b) closing the storage container, and introducing carbon dioxide until the pressure value within storage container is 10 kPa to 7MPa; (c) introducing hydrolysate into the storage container, where the storage pressure value is 45-450 MPa, and (d) waiting for a set time after draining pressure.    USE - The method is useful for processing cellulose-containing biomass material (claimed).    ADVANTAGE - The method can reduce device cost and energy consumption.
NOVELTY - The system has a laser light source unit i.e. broadband light source, connected with an optical intensity modulator to modulate amplitude. An optical fiber circulator carries laser to a sensing head to sense a reflected optical signal through the optical fiber circulator. A photoelectric detector is connected with a processing unit. The optical fiber circulator, the sensing head and the photoelectric detector are connected with two dense wavelength multiplexers that are provided with corresponding light paths. An adjustable optical fiber delay line is connected with each light path.    USE - Multi-point monitoring type wave multiplexing optical fiber hydrogen sensing system.    ADVANTAGE - The system realizes the multi-point monitoring process so as to monitor large number of to-be-detected points of to be detected objects or to be detected areas.    DESCRIPTION OF DRAWING(S) - The drawing shows a circuit block diagram of a multi-point monitoring type wave multiplexing optical fiber hydrogen sensing system.
NOVELTY - Solid-state hydrogen generating apparatus comprises hydrogen storage device (2), hydrogen supply device and power generation device (3), where the hydrogen storage device comprises hydrogen storing bottle (1) containing hydrogen storing granules with average diameter of 20-200 mu m, where the granule has a interior cavity surrounded by a porous wall, the bottle is provided with a hydrogen-absorbing pores (12) at one end which are disposed within a filter (13), and shell of the hydrogen storage bottle has copper-based alloy liner and carbon fiber reinforced layers.    USE - As solid-state hydrogen generating apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of solid-state hydrogen generating apparatus.    Hydrogen storing bottle (1)    Hydrogen storage device (2)    Power generation device (3)    Hydrogen-absorbing pores (12)    Filter (13)
NOVELTY - A solid hydrogen generating apparatus has a hydrogen storage device, a hydrogen supply unit and power generation unit. The hydrogen storage device has hydrogen storage bottles containing hydrogen storage granules having average particle diameter of 20-200 microns. The bottle has interior cavity surrounded by porous wall and hydrogen-absorbing pores at one end, and is made of aluminum alloy. The power generating unit has a porous cell hydrogen fuel electrode, air electrode and a polymer electrolyte membrane containing fluoropolymer.    USE - Solid hydrogen generating apparatus (claimed).    DETAILED DESCRIPTION - A solid hydrogen generating apparatus has a hydrogen storage device, a hydrogen supply unit and power generation unit. The hydrogen storage device has hydrogen storage bottles containing hydrogen storage granules having average particle diameter of 20-200 microns. The bottle has interior cavity surrounded by porous wall and hydrogen-absorbing pores at one end, and is made of aluminum alloy containing 3.5-5.6 %mass magnesium, 0-3 %mass mixture of tantalum and niobium, 0.1-0.5 %mass rhenium, 0.3 %mass or less zirconium, 0.4 %mass or less silicon, 0.4 %mass or less zinc, 0.4 %mass or less copper, 0.4 %mass or less chromium, 0.8 %mass or less manganese, 0.8 %mass or less iron and remainder of aluminum. The power generating unit has a porous cell hydrogen fuel electrode, air electrode and a polymer electrolyte membrane containing fluoropolymer.
NOVELTY - A solid-state hydrogen generating apparatus has hydrogen storage unit and power generation cell unit. The hydrogen storage unit has hydrogen storage bottle containing hydrogen storage granules having average particle diameter of 20-200 microns, and filter. The bottle has interior cavity surrounded by a porous wall, and one end of the bottle is provided with a hydrogen-absorbing pores. The bottle is made of iron-based porous metal material.    USE - Solid-state hydrogen generating apparatus (claimed).
NOVELTY - The device has a hydrogen storage device body provided with a storage bottle shell. Average diameter of granule is about 20-200 microns. The hydrogen storage device body is fixed with a porous wall that is formed with a hollow cavity. The hollow cavity is matched with a pneumatic hole. An end of the storage bottle shell is matched with the pneumatic hole. An air electrode is covered with a polymer electrolyte film that is made of polymer material. The hydrogen storage device body is made of nanometer carbon tube, nano glass ball, nano ceramic, zeolite and nano-fiber materials.    USE - Hydrogen generating device.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a hydrogen generating device.
NOVELTY - A solid-state hydrogen-generating apparatus consists of hydrogen storage unit, hydrogen supply unit and power generation cell unit. The hydrogen storage unit has hydrogen storage bottles containing hydrogen storage granules and filter. The bottle has interior cavity surrounded by a porous wall. The bottle is made of silver-cadmium oxide material. The silver-cadmium oxide material contains silver, cadmium, nickel, tin and lanthanum and/or cerium. The power generation cell unit has porous cell hydrogen fuel electrode, air electrode and polymer electrolyte membrane containing fluoropolymer.    USE - Solid-state hydrogen-generating apparatus (claimed).    DETAILED DESCRIPTION - A solid-state hydrogen-generating apparatus consists of hydrogen storage unit, hydrogen supply unit and power generation cell unit. The hydrogen storage unit has hydrogen storage bottles containing hydrogen storage granules having average particle diameter of 20-200 microns, and filter. The bottle has interior cavity surrounded by a porous wall, and one end of the bottle is provided with a hydrogen-absorbing pores. The bottle is made of silver-cadmium oxide material. The silver-cadmium oxide material contains 85-97 wt.% silver, 2-15 wt.% cadmium, 0.01-0.5 wt.% nickel, 0.01-1 wt.% tin, and 0.01-0.5 wt.% lanthanum and/or cerium. The power generation cell unit has porous cell hydrogen fuel electrode, air electrode and polymer electrolyte membrane containing fluoropolymer.
NOVELTY - A solid hydrogen generating device comprises hydrogen supply device, power generation device (3), copper-based storage bottle (1), porous wall, hollow cavity, gas hole (12), and metal palladium filter (13). Copper-based alloy comprises 45-50 pts. wt. copper, 35-40 pts. wt. zinc, 10-15 pts. wt. nickel, 3-6 pts. wt. manganese, and 0-5 pts. wt. lead.    USE - Solid hydrogen generating device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of solid hydrogen generating device.    Storage bottle (1)    Power generation device (3)    Gas hole (12)    Filter (13)    Output port (31)
NOVELTY - A solid hydrogen generating device comprises hydrogen storage unit, hydrogen supply unit and power generation unit. The hydrogen storage unit comprises storage bottle containing hydrogen-absorbing particles having average diameter of 20-200 microns, hollow cavity and porous wall. One end of the bottle is provided with hydrogen-absorbing pores in which a filter is arranged. The bottle is formed using hydrogen storage alloy.    USE - Solid hydrogen generating device (claimed).
NOVELTY - The device has a hydrogen storage device provided with a storage bottle. Hydrogen is stored in an inner part of the storage bottle. Average diameter of a granule is 20-200 microns. A porous wall is formed with a hollow cavity. An end of the storage bottle is formed with a pneuma hole. An inner hole is formed with a filter. The storage bottle is made of iron based alloy. The hydrogen storage device is linked with a nano meter carbon tube that is made of nano glass ball, nano ceramic, zeolite, nano-fiber or mixture of the material. The filter is provided with a stainless steel micro net.    USE - Iron-based alloy solid hydrogen power generating device.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of an iron-based alloy solid hydrogen power generating device.
NOVELTY - The device has a hydrogen storage device including a storing bottle for storing hydrogen. An end of the storage bottle is formed with a pneuma hole. An inner part of the pneuma hole is provided with a filter. The storage bottle is provided with a shell that comprises an aluminum alloy inner container and a non-metal material enhance layer. A power generating device is provided with a porous hydrogen fuel electrode and an air electrode and overlapped with a polymer electrolyte film. The polymer electrolyte film is made of polymer material i.e. PTFE. The filter is made of metal palladium.    USE - Solid hydrogen power generating device.    DETAILED DESCRIPTION - The hydrogen storage device is made from one of a nanometer carbon tube, nano glass ball, nano ceramic, zeolite, nano-fiber or mixture material. The non-metallic material enhance layer is made of carbon fiber.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a solid hydrogen power generating device.
NOVELTY - The device has a hydrogen storage device provided with a storage bottle. Hydrogen is stored in an inner part of the storage bottle. Average diameter of a granule is 20 microns to 200 microns. A porous wall is formed with a hollow cavity. An end of the storage bottle is formed with a pneuma hole. An inner hole is formed with a filter. The storage bottle is made of iron based alloy. A porous hydrogen fuel electrode, an air electrode and a polymer electrolyte film are overlapped together. The polymer electrolyte film is provided with a polymer. A fluoro polymer is expanded as PTFE.    USE - Polymer electrolyte membrane solid hydrogen power generating device.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a polymer electrolyte membrane solid hydrogen power generating device.
NOVELTY - A solid hydrogen generating device comprises hydrogen storage unit, hydrogen supply unit and power generation unit. The hydrogen storage unit comprises storage bottle containing hydrogen-absorbing particles having average diameter of 20-200 microns, hollow cavity and porous wall. One end of the bottle is provided with hydrogen-absorbing pores in which a filter is arranged. The bottle is formed using copper-based alloy. The power generation unit comprises hydrogen fuel electrode, air electrode and polymer electrolyte film. The polymer electrolyte film comprises fluoropolymer.    USE - Solid hydrogen generating device (claimed).
NOVELTY - The device has a hydrogen storage bottle provided with a storage hydrogen granule. A hollow cavity is matched with a pneuma hole. An end of the hydrogen storage bottle is formed with the pneuma hole. The hydrogen storage bottle is formed as a nano meter carbon tube, nano glass ball, nano ceramic, zeolite, nano-fiber materials. A filter is matched with the pneuma hole by a stainless steel micro net and a metal powder sintering molding part.    USE - Iron based alloy hydrogen storing device.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of an iron based alloy hydrogen storing device.
NOVELTY - The device has a hydrogen storage device body provided with a storage bottle shell. Average diameter of granule is about 20-200 microns. The hydrogen storage device body is fixed with a porous wall that is formed with a hollow cavity. The hollow cavity is matched with a pneumatic hole that is formed at an end of the storage bottle shell. An air electrode is covered with a polymer electrolyte film that is made of polymer material. The hydrogen storage device body is made of nanometer carbon tube, nano glass ball, nano ceramic, zeolite and nano-fiber materials.    USE - Hydrogen generating device.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a hydrogen generating device.
NOVELTY - The device has a hydrogen storage device unit provided with a storing bottle. An inner part of the storing bottle is filled with hydrogen. The hydrogen storage device unit is formed with a porous wall that is formed with a hollow cavity. The cavity is formed with a pneumatic hole that is matched with an end of the storing bottle. An inner part of the pneumatic hole is matched with a filter. A storage bottle shell is provided with a titanium-nickel alloy inner bag and a carbon fiber enhance layer. A polymer electrolyte film is formed with a fluoropolymer layer that is formed by PTFE material.    USE - Solid-state hydrogen energy generating device.    DETAILED DESCRIPTION - The hydrogen storage device unit is formed by nanometer carbon tube, nano glass ball, nano ceramic, zeolite, nano-fiber or mixture material. The filter is fixed with a stainless steel micro net.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a solid-state hydrogen energy generating device.
NOVELTY - Preparation of catalyst (C1), involves: (1) heating a mixture of metal salt, hydrotalcite, binder and pore-forming agent at 50-110 degrees C, where the metal salt is a mixture of nickel salt and rare earth element salt, or mixture of nickel salt and cobalt salt; (2) according to heating rate of 0.1-10 degrees C/minute, raising the temperature to 300-450 degrees C for first time ablation, cooling to 10-30 degrees C, molding, according to heating rate of 0.1-10 degrees C/minute raising the temperature to 500-800 degrees C for a second time ablation.    USE - For preparation of catalyst useful for synthesis of methane (claimed).    ADVANTAGE - The catalyst prepared by this method is high temperature resistant; and is not easy to sintering. The method for synthesis of methane effectively solves the problem of violent exothermic reaction and provides synthesis of high methane conversion rate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for synthesis of methane, by using fresh synthesis gas feed and the catalyst (C1), and carrying out reaction in a reactor comprising a first and a second reactor system, which are in communication, involving following any one method: method (1): returning as recycling material, the material of the first or second outlet of the reactor to the inlet of the first reactor and mixing with the fresh synthesis gas feed; and method (2): carrying out bypass shunt of the fresh material as a raw material to the second reactor inlet.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic flow diagram of the method for preparation of the catalyst. (Drawing includes non-English language text).
NOVELTY - Wastewater heat preservation device comprises sewage inlet water valve (1), bacteria tank (2), clean water outlet water valve (3) and top insulating film (4).    USE - Wastewater heat preservation device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of wastewater heat preservation device.    Sewage inlet water valve (1)    Bacteria tank (2)    Clean water outlet water valve (3)    Top insulating film (4)
NOVELTY - Organic fertilizer comprises 40-60 pts. wt. human and animal excreta, 30-50 pts. wt. saw wood or rice husk powder, 5-15 pts. wt. dried vegetables or tea leaves, 2-4 pts. wt. bog soil, and 10-20 pts. wt. potassium sulfate.    USE - The organic fertilizer is useful for promoting growth of flowers, nursery plants and roots.    ADVANTAGE - The organic fertilizer is environmentally-friendly, suitable for loose soil and nontoxic, increases yield of plants to 7-15% and nitrogen utilization rate to 5-7%, and improves disease resistance ability of the plants.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the above-mentioned organic fertilizer, which involves (a) mixing the above-mentioned components except bog soil and potassium sulfate, adding obtained mixture to fermentation agent, piling up at 25-30 degrees C for 30-45 days, and (b) mixing obtained product with the bog soil and potassium sulfate, and granulating mixture.
NOVELTY - Microbial fertilizer comprises 300-350 pts. wt. sawdust, 130-160 pts. wt. monoammonium phosphate, 150-165 pts. wt. potassium sulfate, 60-70 pts. wt. ammonium sulfate, 270-285 pts. wt. urea, 55-60 pts. wt. bentonite, 50-60 pts. wt. biological agent, and 5-8 pts. wt. trace elements (suitable quantity).    USE - As microbial fertilizer.    ADVANTAGE - The microbial fertilizer exhibits excellent synergistic effect.    DETAILED DESCRIPTION - Microbial fertilizer comprises 300-350 pts. wt. sawdust, 130-160 pts. wt. monoammonium phosphate, 150-165 pts. wt. potassium sulfate, 60-70 pts. wt. ammonium sulfate, 270-285 pts. wt. urea, 55-60 pts. wt. bentonite, 50-60 pts. wt. biological agent, and 5-8 pts. wt. trace elements. The trace element comprises 3-5 pts. wt. zinc sulfate, 2-3 pts. wt. borax, 0.13-0.15 pts. wt. manganese sulfate, 0.2-0.25 pts. wt. copper sulfate, 0.03-0.04 pts. wt. magnesium sulfate, 0.06-0.07 pts. wt. ferrous sulfate, 0.35-0.4 pts. wt. titanium dioxide, 0.04-0.06 pts. wt. potassium iodide, 0.03-0.05 pts. wt. sodium sulfate, 2-3 pts. wt. potassium sulfate, and 2-3 pts. wt. silicon powder. The biological agent includes photosynthetic bacteria, lactic acid bacteria, yeast, actinomycetes, and Bacillus subtilis. The fertilizer is prepared by uniformly mixing trace elements with saw dust, and adding biological agent except B.subtilis, adding urea to mixture, sealing the mixture, performing fermentation at 25-30 degrees C for 3-5 days, and adding raw materials (remainder) and B.subtilis, and granulating, drying, cooling, coating, and packing obtained product.
NOVELTY - A biodiesel refining method by alkali catalytic synthesis involves subjecting crude biodiesel to lower vacuum evaporation at 50-80 degrees C to remove residual ethanol, and preprocessing the product. The preprocessed product is added to 8% bentonite absorbent and preheated at 40-80 degrees C for 10-60 minutes, followed by stirring the product for 10-60 minutes, and separating the product from the bentonite absorbent to obtain refined biodiesel oil.    USE - Method for refining biodiesel.    ADVANTAGE - The method enables refining biodiesel with increased efficiency and yield up to 1-5% and no discharge of wastewater, in simple and cost-effective manner.
NOVELTY - An oxygen-enriched fuel comprises oxygen-containing organic substance which does not contain active hydrogen, and an additive. Oxygen-containing organic substance includes ketone compound, ether compound, ester compound and acetal compound. The content of ester compound is 0-99.99%, the content of other compounds is 0-100%, and the content of additive is 0-10%. The oxygen-enriched fuel is used alone, or mixed with 1-100% mixture of fossil fuel.    USE - Oxygen-enriched fuel is used in engine.    ADVANTAGE - The oxygen-enriched fuel is economical and environmentally-friendly.
NOVELTY - A methanol gasoline additive compound contains 0.1-0.5 %mass demulsifier, 1-5 %mass water repellent, 0.1-0.3 %mass anticorrosive metal, 0.5-0.8 %mass rubber anti-swelling agent, 0.01-0.05 %mass calorific value agent, 0.1-0.5 %mass antifreezing agent, 70-90 %mass solubilizing agent, 0.1-0.3 %mass stabilizer, and 0.05-0.1 %mass n-octane.    USE - Methanol gasoline additive compound for vehicles.    ADVANTAGE - The methanol gasoline additive compound has excellent corrosion resistance, high combustion efficiency and stable property, and is economical and environmentally-friendly.
NOVELTY - A high property methanol gasoline production additive comprises 20-30 vol.% isobutyl alcohol, 25-40 vol.% isoamyl alcohol, 8-16 vol.% dioctyl phthalate, 3-10 vol.% dioctyl alcohol, 0.05-0.1 vol.% methylcyclopentadienyl manganese tricarbonyl, 0.5-1.5 vol.% triacetin, 0.1-2.5 vol.% 2,4-di-tert-4-cresol, 0.5-3 vol.% aldehyde condensate mixture and 1-3 vol.% dicyclohexylamine nitrite.    USE - High property methanol gasoline production additive.    ADVANTAGE - The additive enables methanol and gasoline stable solubility, protects car's rubber and metal parts, and enhances power.
NOVELTY - Method for performing enzymatic synthesis of DL-serine, involves using formaldehyde and glycine as substrate, and catalyst having serine hydroxymethyltransferase activity and D-threonine aldolase activity, configuring molecule of formaldehyde and glycine into a single serine molecule in the presence of coenzyme and performing racemization using catalyst having an amino acid racemase activity to obtain product.    USE - The method is useful for performing enzymatic synthesis of DL-serine (claimed).    ADVANTAGE - The method is performed simply, has synthesizes cost-effectively and rapidly, provides high yield, is environmentally-friendly, and is suitable for large scale industrial production.
NOVELTY - One a kind of sewage disposing system, comprising biological reaction area and separating area sediment, drop drive provided with biological membrane treatment device at upper part biological reaction zone, the drop drive biological membrane process and device, upper rotate shaft equipped with multiple pulp-sheet number, the board for sewage pipe and below also provided with one multi-biological film bearing disk on rotating shaft, wherein biological membrane bearing plate of one part is immersed in liquid face below. One sewage treatment system of this utility new model supply and, using sewage entering into pool and the energy, and drop water way of driving wheel of pulp, rotate drive shaft rotate, to make biological film bearing disc, at the same time make sewage for one time. When sewage from pulp of overflow too further increase contact face and the air, thus further. Processing the circulation process through the water inlet time and automatically controlling sewage, using biological reaction pool for Anaerobic, anoxic and aerobic in different period equal, to reach good sewage treatment effect.
NOVELTY - This utility new type relates to a sewage treatment of one microorganism carrier, especially one used for a biochemical degradation device of purifying water filler composite biochemical ball. This utility new type circular net-shaped outer shell through the rock slurry rock wrapped into a round sphere, used for a special filling material of composite in a biochemical method. A microorganism carrier effect of biological filler, does not participate in the biological and chemical reaction in the sewage environment, is easy to gather pollutant, increase oxygen utilization ratio and unit water treatment composite ball of biochemical quantity.
NOVELTY - This utility new type relates to a one chamber a storage fermentation-type pig manure treatment system, inner is set with a bunker several manure storing fermenting tank, front and back wall body set with a manure storing fermenting tank of the excrement and the excrement opening port, side set with feeding platform and a material groove channel of seal type pig manure storehouse, marsh gas tank and the pipeline is connected with a sewage collecting pipeline. Because the manure storing pool set. the sealed fermentation warehouse inner pig manure, pig manure to ensure complete seal, with the external isolation of a lower, inner rated fully fermented, the fermentation process in a sewage collecting to produce marsh gas tank is used, a rear pig manure ferment into high fertilizer efficiency of organic fertilizer. Can be valid torsion in pig manure aspect a process for the living environment pollution of local soil and the surrounding residents and changes waste into valuable, create income for. A structure is simple, set cost and use cost are low, which can obviously improve the behind management condition and whole pig farm increase economic benefit of pig farm waste management facility is one great innovation of environmental protection product, it has a strong practicability.
NOVELTY - A up this utility new type relates to a movable one , wherein it comprise one fermentation tank (1), the fermentation tank (1) at the bottom by a bracket (9), bearing (10) and silk screen (2) is composed of a bracket strip (9) is multi-root, the one end fixed on the fermentation tank (1) of tank body lower end, and the other end fixed on a bearing (10), a silk screen (2) on the mounting bracket (9) and bearing (10) of bottom of the said fermentation tank (1) in a fixed set with one rotating shaft (3), the rotating shaft (3) connecting with a continuous spiral blade (4). This utility new type has simple structure, is convenient to use, applied to the earthworm compost technology, earthworm movable range is in the middle layer, which not only maintain the upper continuous adding mixing organic garbage raw material of sludge, the lower layer is a continuous output earthworm manure and decomposed.
NOVELTY - One a municipal domestic garbage vertical carbonization furnace, it is one of the main device of dry distillation workshop of municipal domestic garbage dry distillation plant, municipal domestic garbage by preprocessing plant, removing metal and a stone, separating the light a dry substance, the drying temperature to 100-110 degrees, working dry interface of temperature of the furnace reaches 900-1300 degrees centigrade, scattering of the biomass and other combustible garbage in pyrolysis is combustible gas generating workshop for use. Wherein the device is comprise of one or multi-a a garbage feeder (1) vertical dry distiller (2) heater (3) discharge cabinet (4) is a carbon (5) a remote control system (6). The garbage feeder (1) is connected with the garbage vertical dry distiller (2) of feeding opening is connected with garbage vertical dry distiller (2) lower end with one material shifting rod with the heater (3) is connected with discharge cabinet (4) and vertical dry distiller (2) heater (3) is connected with a remote control system (6) is connected with the garbage feeder (1) vertical dry distiller (2) heater (3) discharge cabinet (4) is a carbon (5). The device a per dry domestic garbage for 1-50 tons. The furnace of dry interface of working temperature according to a different product and adjusting.
NOVELTY - This utility new type belonging to the biomass energy utilization technology field, specific relates to a one vertical roller type biomass pyrolysis reactor. The reactor comprise feeding port, driving system, seal reaction room, high temperature heat exchange coil, a multi-stage gear transfer a pressure roller, a multi-stage smooth transfer a pressure roller, a gas phase product exit and solid-phase product exit. Rear biomass raw material entering into vertical roller type biomass pyrolysis reactor, falling to the roller gap one level two gear-type transfer a pressure roller of the action of gravity, the lower roller pressure transmission effect and high temperature roller surface contact, a forced crushing and pyrolysis, and then residue through the action of gravity and pressure roller transmission, in turn through multi-stage gear-type transfer pressure roller and a smooth transfer a pressure roller to finish the complete pyrolysis reaction and obtain a coke product of powder shape. Gear-type transfer pressure roller and a smooth transfer pressure roller are provided with a high temperature heat tube for heating roller surface, so as to provide the biomass pyrolysis of heat.
NOVELTY - A one hot moisture type straw gasification furnace, comprise a furnace body, a furnace body set with feeding port, one side middle part set with water tank and storage tank, the lower part one side set with opening, and the other side set with water pump, and the water tank and the water pump, set with a roller, the bottom of said furnace body is set with a cone, a conical hopper and the feeding port is connected with a lower opening of a gas room, a gas room is connected with lower oxidation room, lower room is connected with a combustion chamber, a combustion chamber lower opening set with vane rotate, rotate the wind ring set with air room, air room set with fan opening, a combustion room set with outer liner, liner is set with a water inlet tube and a steam outlet tube, the inner liner is set with water level controller, a water inlet tube and water pump, the steam outlet tube and storage tank. This utility new type design is reasonable, convenient to use, utilize a produce biomass gas, steam, clean and sanitary, environment pollution is small, multiple functions, low cost, a high utilization rate.
NOVELTY - Flue gas of a one microwave pyrolyzing biomass a pumping port, lower part by straight, curved and the upper flange, the lower part is straight restrain waveguide section of one box body, restrain the bottom of waveguide section connected microwave heating cavity, the top of one side of the opening mounting flange, the other side of the top part opening connected the upper curve, the upper curve is one upper small lower big inclined three-way component, a skew tee member of the mounting flange, and the top is connected with an external gas pumping pipeline. This utility new type reverse by microwave transmission characteristic, restrain waveguide section, a large-calibre, large smoke channel feeding and discharging port of the special structure design, the industrial and continuous production practice use microwave energy for pyrolyzing biomass of in, the microwave safety and reliable shielding inner heating furnace cavity of the microwave, but also solves the problem that the tar blocking valid small hole and elongated, attachment cannot be a cleaning, it does not need to stop in time, convenient for the deposition of tar collecting and using, production efficiency is greatly increase.
NOVELTY - This utility new type claims a one biomass gasification furnace, producing pneuma can comprise, pneuma tank inner wall set with one layer inner liner, pneuma tank is set with seal cover, seal cover set with a feeding port, the bottom set with air inlet, further comprise one vibrator, a vibrator by motor, a connecting rod, a pressure plate, a connecting rod passes through the seal cover center extends to producing pneuma tank inner, the connecting rod extends out one end making pneuma tank of eccentric wheel through a motor transmission shaft to up, connecting to one end extends into the artificial pneuma tank of inner connecting pole of platen. This utility new type through set with one vibrator may be making a biomass pressing inner pneuma tank add material and use process in time, which avoids the process use in biomass burning space overhead of the biomass in producing pneuma inner tank completely is produce of a combustion gas multi-combustion time is long, and it is convenient to operation, no need uncovering seal cover pressing process in, there is no smoke pneuma, energy-saving and environment-friendly.
NOVELTY - This utility new type relates to one used for a sludge straw pelleting drying machine of spiral shaft rotate shaft, a rotate shaft is divided into a feeding part and stir part, a feeding part set with spiral fixing mounting a feeding spiral blade, stir part fix set with stir blade, a feeding spiral blade is strip-shaped spiral blade, and through rigid with the rotate shaft fixing a suspension loop, a stir blade is spiral fixed mounting upper the stir part of rotate shaft of spiral blade, a stir blade of the outer edge distance set with stir. This utility new type design, the feeding and stir integrated on one of rotate shaft a, a and a mixing and supply of a base and the stir effect is very good.
NOVELTY - This utility new type claims a carrier one fast prepare biology diesel oil heat exchanging device comprise circulation lifting device, a heater, a mix tank, a crude oil tank, catalyste tank, methanol tank, a distilling tower, a depositing tank, separator, circulation lifting device shell exit a heater exit through valve I and the mix tank exit and the entrance, a folding oil tank tube, catalyste tank and methanol tank through valve II, a valve III and valve IV is connected to together mix tank of entrance, entrance of separator exit of a folding tube, one a separator exit a circulation device of the lower part entrance, and the other a one exit a depositing tank entrance, a distillation tower entrance connected with exit depositing tank, a depositing tank exit is connected with methanol tank, circulation lifting device and a motor, the device using circulation lifting device so that a carrier can be sand circulation use, the heating of sand and reactant directly contact, it can realize ultra-short reactant contact inner time raise temperature to the needed reaction temperature, accelerate the ester exchange reaction, shortens the reaction time, increase the efficiency.
NOVELTY - This new type utility claims one a pipeline-type continuous preparation biology diesel oil device, the is a pipeline one preparation device, pipeline include methanol cavity catalyste cavity, mix pre-heating cavity, main reaction cavity, separate cavity, cavity, water cavity, the pipeline most left clapboard I and methanol chamber separated by separating plate I and plate II catalyste chamber separated by separating plate II and III clapboard mix pre-heating chamber, separated by insulating plate III and IV clapboard main reaction cavity, separated by insulating plate IV and V separated clapboard separate cavity, separated cavity sulphuric acid, insulating plate by pipeline VI and most insulating water outlet cavity by the right insulating plate and V plate VI, the device the reaction raw material tank, mix preheating, main reaction and separate process set in one of pipeline, a, good continuity, high efficiency, and realize the continuous biological diesel oil production, and is suitable for industrial production application.
NOVELTY - This utility new type provide the one a wine without oxygen supplying system for garbage fermentation device, belonging to the beverage processing device technology field. It solves the problem that the existing technology is easy to cause aerobic fermentation of technology. It comprise fermentation mechanism and gas conveying mechanism, said mechanism comprise barrel-shaped fermentation of fermentation tank, a fermentation tank body inner with the fermentation tank body set with a detachable connecting a filter network, the top part of the fermentation tank with the fermentation tank body seal connecting a cover body, the cover body set with exhaust valve, a gas conveying mechanism comprise nitrogen storage tank, a nitrogen storage tank through a first control valve connected fermentation tank, further include oxygen-free water production mechanism. This utility new type can prevent aerobic fermentation, increase the quality of wine and so on.
NOVELTY - This utility new type provide the one from a stirring type wine without oxygen supplying system for garbage fermentation device, belonging to the beverage processing device technology field. It solves the problem that the existing technology is easy to cause aerobic fermentation of technology. It comprise fermentation mechanism and gas conveying mechanism, said mechanism comprise barrel-shaped fermentation of fermentation tank, a fermentation tank body inner with the fermentation tank body set with a detachable connecting a filter network, the top part of the fermentation tank with the fermentation tank body seal connecting a cover body, the cover body set with exhaust valve, a gas conveying mechanism comprise nitrogen storage tank, a nitrogen storage tank through a valve connected fermentation tank. This utility new type using nitrogen as power of stir, the whole stir process a low state in the absence of oxygen, would not caused by aerobic fermentation, which not only plays the role of stir, but also prevents the aerobic fermentation, increase the quality of wine.
NOVELTY - This utility new type provide a one life garbage fermentation system. This utility new type comprise: fermenting house for stacking to ferment of solid waste material, heat source, through hot air pipeline and a fermenting house a; percolate processing device, through percolate collecting pipeline and a fermenting house a. biological a spray device, through spraying pipeline and a fermenting house connecting the marsh gas collecting device, marsh gas through a pipeline and a fermenting house and a percolate processing device a connect. In marsh gas and percolate, and fermentation process through implementation of this utility new type technology for solution of the invention can obtain following technology effects: a for garbage in anaerobic fermentation process and a biological fermentation, a rear collecting garbage fermentation produce a valid use green energy and reduce a damage for the environment.
NOVELTY - This utility new type claims a integral organic household garbage dry anaerobic fermentation device comprise the 1 reaction area, the 2 reaction area, circulation reflux tube and vertical to liquid discharge tube, the 1 reaction area and the second reaction area through 2 with separating different reaction area of gas exit the acidolysis process a. This utility new type can be a different reaction area between the fermentation gas of a collection, promotes hydrolysis liquid and separate a solid phase material, through set with biogas slurry circulation reflux device, the acid liquid through liquid circulation tube and distributed water taking inner circulation device form a return rolling, avoids the sedimentation accumulation of biological sludge. This utility new type not only realize a phase anaerobic fermentation, solid-liquid three phase separate pneuma, at the same time, maintain higher concentration and active micro organism of solid state fermentation, the whole fermentation system is more stable, more. The whole system has compact structure, small floor area, a divided area.
NOVELTY - This utility new type claims a stir one pneuma biogas tank body, comprise a tank body and a feeding pipeline, a feeding pipeline comprise main pipeline and one group branch pipeline, a main channel vertical to the bottom of the tank body, one group branch pipeline and a main pipeline lower end connected, the branch pipeline and the bottom of the tank body is parallel to or set with the included angle between the opening of branch pipeline close to the bottom of the tank body. This utility new type overcomes the pneuma biogas tank body on a stirrer stir, a large, high cost, bad effect of stir, one provide a consumption energy is small, the cost is low, the effect of stir stir pneuma biogas tank body.
NOVELTY - A kind of one integrated double phase Anaerobic straw marsh gas ferment device, it includes fermentation tank and storage tank, wherein fermentation tank inner cavity of upper separate plate is divided into the following two independent of the space, as on a filtering bed as produced acid phase, as follows for fixed bed as produced methane phase, provided with a filter bed liquid inlet in a filter bed top, and a filtering bed liquid inlet port connect the shower nozzle and an air outlet, a filter bed and side face upper part set with a feeding port, a filter bed side is set with the lower part has discharge port and a filter bed liquid outlet port, is set with fixing bed liquid inlet bottom in fixed bed, is set with sieve plate at lower part of fixing bed and the fixed bed is set with liquid outlet mouth at upper part of fixed bed and fixed bed outlet, is set with filler and in fixed bed, upper storage tank has storage tank is set with liquid storage tank and storage tank liquid inlet mouth, also set with air outlet of storage tank in a storage tank, a filter bed liquid outlet port and fixed bed liquid inlet connected with the fixed bed liquid outlet liquid storage tank enter into and out of storage, a storage tank liquid outlet port and a filter bed liquid inlet port connect.
NOVELTY - This new utility model claims of a kind of one vertical baffle composite Anaerobic digestion device, comprising outside cylinder, and the internal cylinder centre position is set with outside with center relux cylinder, the bottom of the center relux cylinder is cone structure, the outside wall of the centre relux cylinder and inner wall of outside cylinder between the space forming sludge bed area; the bottom of outside cylinder is set with pipe hole type material distributing device, said tube hole type material distributing device and bottom part of pipe connected with feedstock, the feedstock tube and one bi-directional regulate and control mechanism connected with, the regulate and control mechanism of bi-direction controlling end is connected with controller, the outside of the cylinder and upper part set with three phase separator, the three phase separator (containing filler area) upper part set with the overflow groove, the overflow groove is set with upper part set with air chamber, upper end of the air chamber is set with set with marsh gas pipe, one end the overflow groove is set with a discharging port, the discharging port through the overflow pipe and outside of U-type pipe is set with water seal structure connected with.
NOVELTY - Cultivation of Pleurotus ostreatus comprises crushing sugarcane straw to 4-8 cm strips as raw material; preparing culture medium comprising sugarcane straw fiber, calcium superphosphate, gypsum powder, sucrose, calcium carbonate, magnesium sulfate, and potassium hydrogen phosphate; mixing with water and heap fermenting; enzymolyzing, placing in presterilized shed, paving culture medium at 26-32 cm thickness, sowing or planting strain, and covering with soil when mycelium grows; and controlling mushroom shed temperature at 12-15 degrees C at 80-90% air humidity, and spraying with water.    USE - Method for cultivating Pleurotus ostreatus (claimed).    ADVANTAGE - The method has low cost and high yield, promotes good quality mushroom, and has short growing period in greenhouse or sun-shading area.    DETAILED DESCRIPTION - Cultivation of Pleurotus ostreatus comprises crushing sugarcane straw to 4-8 cm strips as raw material; preparing culture medium comprising 85.5-95.8 wt.% sugarcane straw fiber, 2-9 wt.% calcium superphosphate, 3 wt.% gypsum powder, 1 wt.% sucrose, 1 wt.% calcium carbonate, 0.1 wt.% magnesium sulfate, and 0.1 wt.% potassium hydrogen phosphate, where pH value is 6-7.5; mixing with water and heap fermenting; enzymolyzing, placing in presterilized shed, paving culture medium at 26-32 cm thickness, sowing or planting strain, and covering with soil when mycelium grows; and controlling mushroom shed temperature at 12-15 degrees C at 80-90% air humidity, and spraying with water.
NOVELTY - Culturing Coprinus comatus using fibrous sugarcane straw comprises (a) mechanically crushing sugarcane straw into 3-6 cm sugarcane straw fiber; (b) providing culture materials of sugarcane straw fiber, rice bran, lime, corn flour, magnesium sulfate; (c) mixing the culture materials with water, pre-wetting, and carrying out heap fermentation; (d) adding the fermented culture material into pre-sterilized shed, rear paving the mixed material or planting strain, and covering the soil; and (e) controlling the fruiting period temperature to 12-15 degrees C, and timely spraying of heavy water.    USE - The method is useful for culturing Coprinus comatus using fibrous sugarcane straw (claimed).    ADVANTAGE - The method is economical, produces high yield and good quality Coprinus comatus, has short growing period.    DETAILED DESCRIPTION - Culturing Coprinus comatus using fibrous sugarcane straw comprises (a) mechanically crushing sugarcane straw into 3-6 cm sugarcane straw fiber, and using it as a main raw material for mushroom cultivation medium; (b) providing culture materials of 65-73% sugarcane straw fiber, 18-26% rice bran, 3.5% lime, 5% corn flour, 0.5% magnesium sulfate, and pH of 5.4-6.0; (c) mixing the culture materials with water, pre-wetting, and carrying out heap fermentation; (d) adding the fermented culture material into pre-sterilized shed, paving on the upper bed surface to thickness of 26-32 cm, rear paving the mixed material or planting strain, and covering the soil; and (e) controlling the fruiting period temperature to 12-15 degrees C, air humidity to 80-90%, and timely spraying of heavy water.
NOVELTY - Culturing yellow silk algae comprises selecting yellow silk algae strain and BG11 seed liquid culture medium, inoculating a yellow silk algae seed liquid into a nutrient limitation expanded culture device, culturing by illumination in a light illumination intensity and concentrated carbon dioxide for 5-25 days.    USE - The yellow silk algae is useful for preparing biological oil including biological diesel oil or aviation biological fuel oil, and in feed, bait, food or food additive (all claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biologically preparing yellow silk algae oil, comprising selecting yellow silk culture and a yellow silk algal biomass, and extracting and/or pressing the culture.
NOVELTY - Herbicidal composition comprises chlortoluron, pretilachlor and halosulfuron methyl as active component according to the mass ratio of 15-120:10-50:0.5-10.    USE - The composition is used in preventing and treating grassy weed, wheat broadleaf weed and large cornfield weed (claimed).    ADVANTAGE - The composition exhibits obvious synergistic effect, reduces the dosage of agricultural chemical, reduces the administration times, reduces the cost, reduces bad influence on ecological environment, enlarges weeding spectrum, solves the single-time use defect and limitation, prolongs use life, exhibits quick effect, and can be used for long period.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) agro chemical preparation comprisinig herbicidal composition and auxiliary material, prepared into any dosage form;    (2) use of herbicidal composition in preventing and treating grassy weed, wheat broadleaf weed and large cornfield weed; and    (3) use method of composition, comprising applying before sowing or after two-leaf stage, or applying before sowing or after three-leaf stage stage.
NOVELTY - Liquid formulation comprises 2-10 wt.% of emamectin benzoate, 2-10 wt.% of thiacloprid, 3-15 wt.% of surface active agent, 2-6 wt.% of glacial acetic acid and 59-90 wt.% of alcohol solvent.    USE - The liquid formulation is useful for controlling pest on trees in forest, municipal garden and park, scenic area and street.    ADVANTAGE - The liquid formulation has low cost, high pest control effect on a target tree, wide application range, high work efficiency, and can be prepared in a simple, convenient and eco-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the liquid formulation comprising dissolving the thiacloprid using the glacial acetic acid to obtain first mixed liquid, dissolving the emamectin benzoate using the alcohol solvent to obtain second mixed liquid, mixing the first mixed liquid and second mixed liquid, then adding the surface active agent, stirring and uniformly mixing.
NOVELTY - Disinfectant comprises bentonite, precipitating agent, divalent copper antibacterial agent and oxidizing agent in a mass ratio of 100:2-20:0.1-3:0.01-3.    USE - The disinfectant is useful in the form of powder, suspension or liquid for deodorizing garbage (claimed), preferably domestic garbage.    ADVANTAGE - The disinfectant is inexpensive and prepared by simple process, and solves environmental odor.
NOVELTY - Preparation comprises 10-15 pts. wt. bismerthiazol, 27% 10-14 pts. wt. noble copper suspending agent, 72% 4-8 pts. wt. streptomycin sulfate, 3-6 pts. wt. copper acetate, 3-7 pts. wt. Polygonum, 2-4 pts. wt. wormwood, 4-6 pts. wt. oriental wormwood, 13-15 pts. wt. thunder god vine aqueous extract solution, 4-8 pts. wt. hypericin, 4-8 pts. wt. matrine, 5-8 pts. wt. salt and 100-115 pts. wt. water.    USE - The preparation is used for preventing and treating Anthurium bacterial leaf spot (claimed).    ADVANTAGE - The preparation is prepared by simple technique, is easy to use, and reduces the pesticidal use and environmental pollution, which is good for ecological balance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for the use method of preparation, comprising (a) providing bismerthiazol, noble copper suspending agent, streptomycin sulfate, copper acetate, Polygonum, wormwood, oriental wormwood, thunder god vine aqueous extract solution, hypericin, matrine, salt, and water, then mixing, stirring uniformly, to obtain preparation, and (b) using 1000-1100 times of preparation, spraying on damaged plant for 4 weeks for 2-4 times, where each dosing interval is 5-8 days.
NOVELTY - Fermentation production of microalgae grease involves taking microalgae grease slag in a fermentation tank, adding water, mixing, using temperature control device to control inner temperature of fermentation tank, fermenting, placing the material after fermentation in a drying device and drying, to the fermentation tank containing microalgae grease slag, adding plant protein raw material and fermentation strain, after drying the material, crushing in a crusher, and to the finished product after crushing, adding conventional feed to form microalgae grease mixed fermented feed.    USE - For fermentation production of microalgae grease (claimed) rich in unsaturated fatty acids such as linoleic acid, linolenic acid, arachidonic acid, EPA and DHA and so on and used in health food and medicine for promoting and improving growth of animal, enhancing immunity, increasing cultivation survival rate and product quality; and in aquatic product and animal feed industry.    ADVANTAGE - The method uses high-quality feed raw material, has wide application prospect in aquatic product and animal feed industry, improves shortage of feed protein source, allows efficient use of microalgae grease slag and reduces environmental pollution.
NOVELTY - Preparing probiotics comprises crushing kitchen garbage and then wet heating at 100 degrees C for 30 minutes, reducing the temperature to 28-37 degrees C, regulating the pH value to 6-7, adding lipase, yeast and lactic acid microbial agent, fully mixing, performing aerobic fermenting at 28 degrees C for 24-48 hours, anaerobic fermenting at 37 degrees C for 24-48 hours and fermenting at 40-60 degrees C for 48-92 hours, and drying obtained product.    USE - The method is useful for preparing probiotics (claimed).    ADVANTAGE - The method is capable of efficiently preparing the probiotics with good synergistic effect and high activity.
NOVELTY - A burning biomass of one heat-conducting oil boiler, by biomass feeding device, a disk oil tube, a boiler main body and a coal economizer. The boiler main body comprise fire grate, furnace arch and by furnace arch is formed by a furnace wall, a furnace arch by front furnace arch and rear furnace arch is composed of the front and back furnace arch upwards extending form the smoke exit pneuma and surrounded by furnace wall, fire grate arranged on the furnace arch lower part, furnace inner wall furnace arch of the biomass feeding device arranged on the boiler main body front end, furnace wall form of arch of the outer wall surface, a disk oil tube is arranged on the boiler body inner, coal economizer sequential inner arranged on the tail flue of boiler. This utility new type is to biomass as fuel, is a carrier of heat supply device, a wide application in petrochemical industry, light industry, textile, building material and so on. Has a simple structure, a low cost economical.
NOVELTY - A method based on microwave plasma device for removing nitrogen oxides, includes microwave plasma generator comprising a chemical reactor, the flue gas containing nitrogen oxides are ionized in the plasma chemical reactor in a reduction reaction by a reducing agent, the removal of nitrogen oxides in the flue gas. The reducing agent is formed by hydrogen, carbon monoxide, methane and ammonia or carbon.    USE - Flue gas denitration based microwave plasma nitrogen oxide removing device.    ADVANTAGE - The device has better strengthening effect, and increases chemical reactor operating rate when reducing agent gas ionization is in a plasma state. The device can form a plasma torch that contains positive ion and negative ion to ensure removing rate of nitrogen microwave plasma to reach more than 90%, and reduces flue gas forming difficulties. The device increases positive ion and negative ion reaction collision rate, reaction speed and reaction conversion rate so as to reduce reducing agent utilization rate.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a flue gas denitration based microwave plasma nitrogen oxide removing device.'(Drawing includes non-English language text)'
NOVELTY - A hydrophobic cavity and hydrophilic surface hollow submicrosphere comprises organic-inorganic composite structure comprising silicon-containing polymer.    USE - Hydrophobic cavity and hydrophilic surface hollow submicrosphere used for hydrophobic encapsulation, oil water separation, hydrophobic drug delivery, catalyst protection and microreactor (all claimed).    ADVANTAGE - The method has simple process, good repeatability and less environment pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of hydrophobic cavity and hydrophilic surface hollow submicrosphere comprising dispersing silane coupling agent, silicon dioxide colloid particle and isoamyl acetate into water, heating at 60 degrees C, adding persulfate, polymerizing, and drying.
NOVELTY - The device has main portion (5) that is set on upper portion of ground. A lower half unit is set on the ground lower unit. The top of the main portion is connected with the ground through the slope (8) which is connected with the main portion. The main portion is set with upper portion of opening of a waste reservoir unit (3). The inner wall of the waste reservoir unit is set with a waterproof layer (4).    USE - Device for storing livestock waste.    ADVANTAGE - The penetration of the dirt into a waste reservoir unit is prevented and is used conveniently to save force operation. The farm waste storage device prevents the fertilizer effect, while preventing the entry of mosquito. The waterproof layer prevents waste leakage pollution and reduces the waste smell easily. The careless falling of human into the waste is prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the device for storing livestock waste.    Clap board (2)    Waste reservoir unit (3)    Waterproof layer (4)    Main portion (5)    Slope (8)
NOVELTY - A biofuel from vegetable-based biomaterial is manufactured by making biomaterial finer in greater than or equal to 1 stage by defibration and is dried with the heat from heat-releasing process and finalizing the drying after the finer making stage.    USE - Manufacture of biofuel from vegetable-based biomaterial used for replacing fossil fuels (claimed).    ADVANTAGE - High dry material is obtained in short time and refining and drying are performed in efficient manner. Dust explosion and operating disturbances are prevented. Carbon dioxide emissions are reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a utilization of manufactured biofuel which involves burning biofuel in the same combustion plant, from which heat brought to drying was obtained, or is transported to a separate combustion plant to be burned, manufacturing pellets from biofuel that has been made finer and dried or manufacturing refined, and liquid biofuel from biofuel that has been made finer and dried biofuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the defribator and dryer.    Disk refiner (1)    Drying apparatus (10)    Drying units (11, 12)    Separator (13)    Channel (14)
NOVELTY - Producing biodiesel, comprises: (a) combining animal or vegetable oil with a salt to create a first composition; (b) combining a short chain alcohol with a strong base to create a second composition; and (c) combining the first and second compositions together.    USE - The process is useful for producing biodiesel, such as fatty acid methyl ester biodiesel (all claimed) and glycerol byproduct.    ADVANTAGE - The process ensures effective production of biodiesel in an industrial scale commercially viable and less time consuming manner, and decreases the amount of time for the glycerol byproduct to settle out.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a method of reacting a natural oil with a short chain alcohol in the presence of an alkaline catalyst, comprising (i) providing a natural oil, (ii) providing a salt, (iii) providing a short chain alcohol, (iv) providing an alkaline catalyst, (v) combining the natural oil with the sodium chloride into the first composition, (vi) combining the short chain alcohol with the alkaline catalyst into the second composition and (vii) combining the first and second composition;    (2) the biodiesel produced by the above process; and    (3) a reaction product comprising fatty acid methyl ester produced by the above method.
NOVELTY - Production of propylene and 4C hydrocarbon involves feeding methanol-containing feedstock into a fluidized bed reactor, reacting under the action of catalyst to generate reaction product flow containing 1C hydrocarbon, 2C hydrocarbon, propylene, by-product, 4C hydrocarbon, 5C hydrocarbon, and 6C hydrocarbon, passing reaction product flow into separation system, and extracting 1C, 2C and 5C hydrocarbon and propylene.    USE - Production of propylene and 4C hydrocarbon (claimed).
NOVELTY - A compacted torrefied biomass from pre-processed biomass (101) is produced by drying pre-processed biomass in a dryer (104) having pre-dryer (102) and main dryer with heater exhaust gas from heater (108), torrefying dried biomass in torrefaction processor which consists of torrefaction reactor (112) and cooling compactor (122), with heat generated by heater, and combusting syngas from torrefaction processor with support fuel in the heater, yielding heat for the dryer and torrefaction reactor.    USE - Production of compacted torrefied biomass from pre-processed biomass for biofuels and fuel feedstock used for power plant.    ADVANTAGE - Torrefied biomass is cooled and compacted to ease handling and reduce dust content.    DESCRIPTION OF DRAWING(S) - The drawing shows a simplified flow chart of the process to torrefy pre-processed biomass.    Pre-processed biomass (101)    Pre-dryer (102)    Dryer (104)    Heater (108)    Torrefaction reactor (112)    Cooling compactor (122)
NOVELTY - Waste transformer and pressure tank for converting the organic material or food residues (waste) into gas energy, supporting technology component and other suitable article in every shape and size, comprise hard metal or any suitable construction material. The waste transformer is a transformer for converting the organic material or food residues (waste) into gas energy. The pressure tank has a container for liquid- or gaseous fuel.    USE - The waste transformer is useful for converting the organic material or food residues (waste) into gas energy (claimed).    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the waste transformer.    Container (1)    Control or switching system (2)    Cover (3)    Back entrance (4)    Gas tank (8)
NOVELTY - Preparing carboxylic acid amide compounds (I), comprises: (a) providing carboxylic acid ester compounds (II) and ammonia; (b) mixing (II) and ammonia; and (c) reacting (II) and ammonia to (I) and alcohol compounds (III), where the ammonia is fed in liquid form or in supercritical form.    USE - The process is useful for producing carboxylic acid amides (I) such as trichloroacetic acid amide and/or trifluoroacetic acid amide (claimed). (I) are useful as important precursors to produce agrochemical active agents.    ADVANTAGE - The environmentally friendly process produces (I) in high yield, selectivity and high conversion rate and improved space-time yield.    DETAILED DESCRIPTION - Preparing carboxylic acid amides compounds of formula (RC(O)NH2) (I), comprises: (a) providing carboxylic acid ester compounds of formula (RC(O)OR1a) (II) and ammonia; (b) mixing (II) and ammonia; and (c) reacting (II) and ammonia to obtain (I) and alcohol compounds of formula (R1a-OH) (III), where the ammonia is fed in liquid form or in supercritical form.    R = optionally branched, optionally substituted 1-6C-alkyl (preferably methyl, ethyl, n-propyl, n-butyl, isopropyl, sec-butyl, isobutyl, tert-butyl, n-pentyl or n-hexyl), substituted phenyl, naphthyl or 5-6 membered heterocyclic rings comprising 1-3 heteroatoms of N, S or O; and    R1a = optionally branched, optionally substituted 1-6C-alkyl, preferably methyl, ethyl, n-propyl, n-butyl, isopropyl, sec-butyl, iso-butyl, tert-butyl, n-pentyl or n-hexyl.    An INDEPENDENT CLAIM is included for a plant for preparing (I), comprising a feed tank (1) for ammonia, a storage tank (2) for (II), a cascade mixer (3), a dweller (4) and a phase separator (5).    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a plant for preparing carboxylic acid amides compounds.    Feed tank for ammonia (1)    Storage tank (2)    Cascade mixer (3)    Dweller (4)    Phase separator. (5)
NOVELTY - The gasification reactor system (100') has a gasification reactor (20') for producing a combustible gas mixture, and a feed unit (10) for conveying a starting material of wood or biomass, where the feed unit opens with a conveyor (11) above or laterally in the head region of a gasification reactor. A sealed locking element (14) is arranged in a conveying path and in front of the conveyor.    USE - Gasification reactor system for producing a combustible gas mixture.    ADVANTAGE - The gasification reactor system has a gasification reactor for producing a combustible gas mixture, and a feed unit for conveying a starting material of wood or biomass, where the feed unit opens with a conveyor above or laterally in the head region of a gasification reactor, and thus ensures simple and efficient performance of the gasification reactor system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a gasification reactor system.    Feed unit (10)    Conveyor (11)    Locking element (14)    Gasification reactor (20')    Gasification reactor system (100')
NOVELTY - A composite catalyst for microwave reaction zone is manufactured by adjusting pH of mixture of carbon structure which has porous structure suitable for substance transport and absorbs microwave, sulfuric acid, and/or fuming sulfuric acid to less than or equal to 5 and heating mixture at 20-200 degrees C.    USE - Manufacture of composite catalyst for microwave reaction zone used for manufacture of ester compound used in biodiesel fuel.    ADVANTAGE - Composite catalyst can be efficiently manufactured over a short period of time, and ester compound can be mass-produced.
NOVELTY - Disclosed is a catalytic conversion device for generation of hydrogen, and particularly a catalytic conversion device that is mounted in an exhaust pipe to absorb waste heat of an engine to activate generation of hydrogen, which comprises a preheating body, a catalyst bed, a heating tube, and a plurality of heating catalysts arranged in the heating tube. The heating tube is externally sleeved on the preheating body and a catalyst bed. Each heating catalyst is filled between the heating tube and the preheating body and the catalyst bed. The heating tube has two ends that are set in a closed form, and one of the ends is communicated via a tube with a fuel gas tank in order to deliver oxygen-containing fuel gas into the heating tube for temperature rise of the heating catalyst to heat the catalyst bed and the preheating body to a working temperature of the catalyst for generation of hydrogen, whereby upon starting the engine, an operation of adding hydrogen to the engine can be started up immediately to achieve the purpose of pollution reduction and fuel saving for the entire process.
NOVELTY - Preparing solid fuel comprises: crushing rice hulls into a powder having a predetermined size using a mill; crushing a wet food waste; mixing 45-49 wt.% of crushed rice hull with 50-54 wt.% of crushed food waste and 1 wt.% of additive and then stirring using an internal agitator; maturing the stirred mixture for a specific period of time; mixing 70 wt.% of hard coal powder with 30 wt.% of the aged mixture; and injecting the mixture into a dry flask, and shaping the mixture into a solid fuel product in a certain shape.    USE - The method is useful for preparing solid fuel from waste including food waste and rice hulls (claimed).    ADVANTAGE - The method is capable of preparing the solid fuel in a simple and effective manner with high content of the fixed carbon, and reducing the smell of the food waste.
NOVELTY - Genetically modified microorganism is new.    USE - The genetically modified microorganism is useful for: converting one carbon compound including methane, methanol and formaldehyde to acetyl-coenzyme A (CoA) and two or more carbon products; and making a product including acetate, ethanol, ethylene, n-alcohols, alcohols, alkenes, fatty acids, fatty acid methyl-esters, alkanes and isoprene from acetyl-CoA, methane, methanol or formaldehyde (all claimed).    ADVANTAGE - The genetically modified microorganism converts the carbon compounds to acetyl-CoA and two or more carbon product at molar yields greater than 0.35 moles, preferably greater than 0.49 moles of acetyl-CoA per mole of a one carbon compound in a cost effective manner.
NOVELTY - Anaerobic degradation of cyanide, involves: (a) providing a solution comprising cyanide and fermentable organic matter having a chemical oxygen demand (COD) of 1500-32000 mg/1; and (b) treating the solution in an anaerobic digestion reactor.    USE - The method is useful for anaerobic degradation of cyanide (claimed).    ADVANTAGE - The method can be effectively used in the anaerobic biological treatment of cyanide and production of biogas from cyanide using a mixture of cyanide contaminated industrial wastes and organic matter rich industrial wastes as inflow for the treatment in typical anaerobic biogas production reactors.
NOVELTY - A cellulase cel5-KG71 gene derived from rumen microorganism of Capra hircus aegagrus and comprising a 1467 base pair sequence (SEQ ID NO: 1) fully defined in the specification, is new.    USE - The cellulase cel5-KG71 gene encoding cellulase protein is useful in feed additive for promoting cellulolytic activity and detergent composition, and for producing biofuel (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) cellulase protein of cellulase superfamily, comprising a 488 amino acid sequence (SEQ ID NO: 2) fully defined in the specification, where the cellulase protein is encoded by the gene;    (2) recombinant vector comprising the gene;    (3) host cell in which recombinant vector is transformed;    (4) feed additive for promoting cellulolytic activity comprising the cellulase protein;    (5) detergent composition comprising the cellulase protein; and    (6) method for producing biofuel involves adding the cellulase protein to biomass and hydrolyzing mixture.
NOVELTY - Biogas generation system (1) comprises a fermentable-chamber (10), a device for supplying fermentable material to fermentable-chamber, apparatus for discharging fermented material from the fermentable-chamber, and device to conduct the biogas out from the fermentable-chamber and supplying to a consumer. The fermentable-chamber is formed as a film tube (12), which is closed at both ends by end pieces.    USE - The biogas generation system is useful for the fermentation of fermentable material to produce biogas (claimed).    ADVANTAGE - The biogas generation system: is cost efficient; has simple components, which are easily procurable; contains a kit which can be transported by simple means, constructed simply and quickly, and is easy to use and safely operable.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an assembly kit for building a biogas generation system, comprising two end pieces to build a film tube, device to build the end pieces of a fermentable-chamber from the film tube, device for supplying fermentable material to fermentable-chamber, device to build apparatus for discharging fermented material from the fermentable-chamber, device to conduct the biogas out from the fermentable-chamber, optional device to build a storage unit and optionally device for conducting biogas from storage unit and supplying to a consumer.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic sectional side view of biogas production system.    Biogas generation system (1)    Fermentable-chamber (10)    Film tube (12)    First end piece (20)    Pipe section (21)
NOVELTY - Catalyst composition comprises carbon monoxide methanation catalytically active component and transition metal capable of forming polyanion, and has a structure formed by presence of the transition metal in a non-crystalline state.    USE - The catalyst composition is useful in methanation process (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for methanation catalyst, which comprises above-mentioned composition.
NOVELTY - Preparing olanzapine, comprises condensing 4-amino-2-methyl-10H-thieno(2,3-b)(1,5)benzodiazepine or its salt with N-methylpiperazine in the presence of a mixed solvent containing a first solvent of N-methyl-2-pyrrolidone or dimethylsulfoxide and a second solvent of ethanol or 1-propanol.    USE - The process is useful for preparing olanzapine or its crystalline form-II (claimed), which is useful for treating mental disorders such as schizophrenia, schizophreniform disorder and acute mania, and mild anxiety disorders. No biological data given.    ADVANTAGE - The process is capable of simply and rapidly preparing olanzapine with ultra high purity and high yield in an economical and environmental-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a process-I for preparing olanzapine crystalline form-II, comprising crystallizing the olanzapine with 1-4C alcohol and water to give a crystalline product.
NOVELTY - Manufacturing fuel using livestock and sewage sludge and food waste, comprises: (S1) performing raw material crushing step by supplying rice hulls and waste wood into a grinder and crushing into power of size 6-14 mm; (S2) performing compression drying step by supplying 50-70 pts. wt. unprocessed livestock and sewage sludge or food waste into a compressor, primarily dehydrating, and then supplying into a drier, adding 15-35 pts. wt. rice hulls and 15-35 pts. wt. waste wood, and drying by heating; and (S3) molding the dried fuel into a length of 18-22 cm and a diameter of 4-5 mm.    USE - The method is useful for manufacturing fuel using livestock and sewage sludge and food waste (claimed).    ADVANTAGE - The method molds into uniform shape without adding separate additive mixture, reduces manufacturing cost, and provides excellent storage and delivery of fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic process flow for manufacturing fuel using livestock and sewage sludge and food waste (Drawing includes non-English language text).    Raw material crushing step (S1)    Compression drying step (S2)    Molding step (S3)
NOVELTY - Method for producing hydrogen, involves heat-treating sludge and waste comprising high protein content in anaerobic digester to prepare mixed waste solution, and performing anaerobic fermentation of the mixed waste solution by culturing microbes under dark condition.    USE - The method is useful for producing hydrogen (claimed).
NOVELTY - Producing refuse derived fuel using sewage sludge, comprises (a) mixing heat medium oil and sewage sludge, heating and drying, (b) injecting the oil mixed sewage sludge in a drying tank and re-drying to dry water by heating under vacuum condition, (c) centrifuging the dried sewage sludge to separate oil, (d) mixing carbon additive in the sewage sludge powder and kneading by adding water, (e) injecting the kneaded product in an extrusion molding machine, screw compressing, discharging by conveying and forming solid fuel by cutting, and (f) drying the solid fuel to obtain thermal coal.    USE - The refuse derived fuel is useful for generating electricity.    ADVANTAGE - The method prevents environment pollution by treating sewage sludge.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic flow chart of the method for manufacturing thermal coal using refuse derived fuel (Drawing includes non-English language text).
NOVELTY - Fuel pellet comprises a mixture including 75-95 wt.% of palm bark powder and 5-25 wt.% of palm berries powder. The mixture is pressed by compression molding at 1200 degrees C. A moisture content of the raw materials is less than or equal to 10%.    USE - The fuel pellet is useful for a pulverized coal-fired boiler (claimed).    ADVANTAGE - The highly efficient fuel pellet can be prepared in a cost-effective and eco-friendly manner without the need of separate binder.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing fuel pellet, comprising: preparing the mixture by mixing the palm bark powder and the palm berries powder; and compressing the mixture to obtain the fuel pellet.
NOVELTY - A biological treatment system (100) for water purification comprises chamber (110) having an inlet (112) and an outlet (128), filler layer (120) disposed in a room that allows the deposition of microorganisms and growth of the film, and device for supplying air (114) into the room during the treatment to be mixed with water and air supply to the microorganisms.    USE - As biological treatment system for water purification (claimed).    ADVANTAGE - The biological treatment systems for water purification, solves the problem such as no water flow in plant and biological rubbish dirt layer on layer of packaging in layered flow that causes difficulty formation of biofilms that are no longer present in biological treatment systems water purification. The performance of the filler layer of biofilm on contact with microorganisms and water in very well and at the end of the treated water out of the system that has the concentration of organic matter is very low.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for assembling a biological treatment system for water purification involving providing support layer into a space that has an inlet and an outlet, provision of a number of air ducts, air ducts each having a number of air nozzles can be arranged vertically in the same distance to allow compressed air to be distributed evenly in the room through the regulation of anti-gravity flow, filling the room with a layer of filler to allow the deposition of microorganisms and the growth of a film, and the relationship of the inlet chamber to a source of water waste.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of biological treatment systems.    Biological treatment system (100)    Chamber (110)    Inlet (112)    Air (114)    Filler layer (120)    Air compressor (124)    Gate valve (126)    Outlet (130) Support layer (128)
NOVELTY - Use of a thermophilic nuclease for degrading nucleic acids in vivo and/or in situ, where the thermophilic nuclease is heterologous to the host cell, is claimed.    USE - The thermophilic nuclease is useful for degrading nucleic acids in vivo and/or in situ and producing biomass product which is free of active nucleic acid (all claimed).    ADVANTAGE - The thermophilic nuclease ensures controllable nucleic acids degradation without impeding desired end product, in an industrial production scalable and economical manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a genetically modified cell comprising a heterologous nucleic acid sequence encoding a thermophilic nuclease gene, where the thermophilic nuclease produced using the thermophilic nuclease gene, is latent at the temperature at which the cell has normal growth, the genetically modified cell produces one or more end products, and the end products are not the thermophilic nuclease;    (2) a method for degrading nucleic acids in vivo and/or in situ, comprising (a) introducing the thermophilic nuclease gene into a host cell, (b) growing the host cell at a temperature at which the thermophilic nuclease is latent, and (c) degrading the nucleic acids of the host cell by changing the temperature in step (b) to a temperature at which the thermophilic nuclease is active; and    (3) a process for the production of a biomass product which is free of active nucleic acid molecules, comprising (A) introducing the thermophilic nuclease gene into a host cell, where the host cell produces the biomass product, (B) fermenting the host cell at a temperature at which the thermophilic nuclease is latent, (C) degrading the nucleic acids of the cell by changing the temperature in step (B) to a temperature at which the thermophilic nuclease is active, and (D) recovering the biomass product, where the order for performing steps (C) and step (D) may be exchanged.
NOVELTY - Production of biofuel (24) involves pretreating coal (10) and providing solubilized coal, bio-reacting solubilized coal with one or more types of coal-utilizing bacteria (9), generating biomass (18) and lipids (19) from the solubilized coal, and converting lipids into biofuel.    USE - Production of biofuel used as jet fuel, fuel replacement, salable chemical, lipid slurry, fuel blending agent, and direct fuel replacement (all claimed) for transportation and power plant.    ADVANTAGE - The method enables production of biofuel from coal with efficient recycling of byproducts, by simple and economical process, and is environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for coal-to-biofuel production system.    DESCRIPTION OF DRAWING(S) - The drawing shows the process flow diagram explaining production of biofuel from coal.    Coal-utilizing bacteria (9)    Coal (10)    Acid (11)    Biomass (18)    Lipid (19)    Anaerobic digester (20)    Methane (21)    Methanol (23)    Biofuel (24)
NOVELTY - Preparation of solid fuel involves uniformly mixing 90 wt.% rice hull, 2.4 wt.% black oak sawdust, 2 wt.% cornstalk, 1.2 wt.% straw, 1.1 wt.% peanut hull and 1.1 wt.% coconut shell in a reactor, pressurizing to pressure of 90-100 ton using compressor, heating at 400-600 degrees C for 20 hours, adding 300-400 kg silica, 200-300 kg sodium chloride, 10-15 g starch and water, mixing uniformly, pressurizing to pressure of 90-100 ton using the compressor, heating, and curing at room temperature.    USE - Preparation of solid fuel (claimed).    ADVANTAGE - The method provides solid fuel by an environmentally-friendly process.
NOVELTY - The system (100) has gasification furnace (140) that transduces the flow medium heated by combustion furnace (110), for gasifying the gasification raw material with the heat provided in flow medium, so that the gasifying gas is generated. A cooling mechanism (160) cools the flow medium circulated between gasification furnace and combustion furnaces. The residuals of and gasification raw material and flow medium are introduced into the combustion furnace from the gasification furnace, so that the residuals are burned in furnace for heating the flow medium.    USE - Gasification-gas production system for gasifying gasification raw material such as coal, biomass and tire tip and for generating gasifying gas used for electric power generation system, manufacture of hydrogen, manufacture of synthetic fuel and manufacture of chemicals such as chemical fertilizer.    ADVANTAGE - The overheating of combustion furnace is prevented, without reducing the production amount of gasifying gas. Since the flow medium is heated only with a residue to the temperature required by the gasification furnace, the need of introducing the supplementary fuel into the combustion furnace is avoided.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram illustrating the specific structure of gasification gas production system. (Drawing includes non-English language text)    Gasification-gas production system (100)    Combustion furnace (110)    Gasification furnace (140)    Cooling mechanism (160)    Circulation pipe (162)
NOVELTY - The system (1) has anaerobic-treatment tank (12) which generates biogas by carrying out the anaerobic treatment of the organic waste water. A former stage process tank (11) processes the organic waste water in the former stage of the anaerobic-treatment tank. A gas return unit returns a portion of the biogas emitted in the anaerobic-treatment tank to former stage from the anaerobic-treatment tank. A reduction tank is provided in the former stage of former stage process tank for reduction-processing the organic waste water.    USE - Anaerobic-treatment system.    ADVANTAGE - The raise of the oxidation-reduction potential of the organic waste water in anaerobic-treatment tank is suppressed. The anaerobic treatment is performed by anaerobic-treatment system suitably.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for anaerobic-treatment method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the anaerobic-treatment system.    Anaerobic-treatment system (1)    Former stage process tank (11)    Anaerobic-treatment tank (12)    Baffle plate (20)    Treated-water discharge unit (23)
NOVELTY - A phosphoric-acid phosphorus concentration meter (141) detects the amount of phosphorus in to-be-processed water which flows into primary sedimentation basin (1) from outside system. An initial sediment-anaerobic tank bypass inflow pump (11) outputs a signal which makes the amount of inflow to-be-processed water to anaerobic tank (4) to a predetermined value, according to output value of amount detection unit. A primary sedimentation basin inflow pump (14) adjusts the amount of inflow to-be-processed water to the basin, according to output value of output unit.    USE - Control apparatus of biological water treatment apparatus for removing nitrogen and phosphorus contained in sewage flowing into lakes, marshes, etc.    ADVANTAGE - The denitrification and phosphorus discharge are efficiently performed by adjusting suitably the flow volume of sewage which flows in into an anaerobic tank, other than operating quantities such as amount of activated sludge stored in biological reactor and flow volume of activated sludge returned to biological reactor. Hence the control apparatus ensures a favorable water quality.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the control apparatus of biological water treatment apparatus.    Primary sedimentation basin (1)    Anaerobic tank (4)    Initial sediment-anaerobic tank bypass inflow pump (11)    Primary sedimentation basin inflow pump (14)    Phosphoric-acid phosphorus concentration meter (141)
NOVELTY - Sulfonated dehydro-abietic acid is prepared by mixing rosin or disproportionated rosin with 1-10 carbon-containing aliphatic alkane, petroleum ether, or acetone, refluxing, centrifuging, drying to obtain rosin acid dehydrogenase, pre-cooling, reacting with strong inorganic acid, dropping crushed ice until all ice dissolves, centrifuging, washing filter cake with cold water, adding filter cake to boiling water, completely dissolving, adding activated carbon and diatomaceous earth, refluxing, filtering to remove diatomite and activated carbon, collecting filtrate, and cooling.    USE - Preparation of sulfonated dehydro-abietic acid for detergent and treating gastrointestinal ulcer, acute and chronic gastritis, and erosive gastritis (all claimed).    ADVANTAGE - Process reduces generation of by-product, reduces energy consumption, improves yield, and has high purity.    DETAILED DESCRIPTION - Sulfonated dehydro-abietic acid is prepared by mixing rosin or disproportionated rosin with 1-10 carbon-containing aliphatic alkane, petroleum ether, or acetone, refluxing, centrifuging, drying to obtain rosin acid dehydrogenase, pre-cooling, reacting with strong inorganic acid, dropping crushed ice until all ice dissolves, centrifuging, washing filter cake with cold water, adding filter cake to boiling water, completely dissolving, adding activated carbon and diatomaceous earth, refluxing, filtering to remove diatomite and activated carbon, collecting filtrate, cooling to obtain precipitate large amount of solid, filtering, blast drying filter cake to obtain crude sulfonated rosin acid dehydrogenase, adding organic solvent, refluxing, completely dissolving, filtering while hot, cooling filtrate to crystallize, centrifuging, leaching with organic solvent, and vacuum drying filter cake.
NOVELTY - The three-stage gasifier has a first reactor (130) that gasifies air applied from the solid material. The prior pyrolysis tunnel (120) disassembles solid material transferred from the silo (110) to tar and char. The silo stores the solid material passes through and generated in the first reactor in which the carbon absorbent is used. A spreader plate (150) made of nickel reduces the tar content within the producer gas generated in the first reactor and filled in second reactor (140). The nitrogen is injected into prior pyrolysis tunnel.    USE - Three-stage gasifier for production of low-tar producer gas from sewage sludge.    ADVANTAGE - The catalyst is not used in the producer gas production and the generation of tar is suppressed while achieving the productivity improvement and cost reduction efficiently. The steam and catalyst are not used and the content of hydrogen is maximized.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the three-stage gasifier for production of low-tar producer gas. (Drawing includes non-English language text)    Silo (110)    Prior pyrolysis tunnel (120)    Reactors (130,140)    Spreader plate (150)    Refining section (160)
NOVELTY - The fire log has molded, compacted log unit that is produced from one of dry ingredients of woodchip, wood pulp, sawdust, straw or combination of these in varying proportions. The dry ingredients are used in varying proportions of total volume of final log. The binding agent is provided to retain the compacted log unit in defined shape. The binding agent is used in varying proportions of total volume of final log.    USE - Robust moisture resistant fire log for use in solid fuel burning units or open fires.    ADVANTAGE - The moisture resistant fire log can be lit directly with a naked flame without the necessity to use additional combustible materials. The handling of robust product is easy. The desired burn time is increased or decreased by increasing or decreasing the amount of wax binder in the composition of fire log. The manufacturing cost of the robust moisture resistant fire log is reduced.    DETAILED DESCRIPTION - The binding agent is provided with paraffin wax, animal wax, vegetable wax and petroleum wax. The binding agent is coated to finished log product to offer moisture resistance. An INDEPENDENT CLAIM is included for a method for producing robust moisture resistant fire log, involves feeding dry ingredients are feed into wood grinder/shredder to achieve the required consistency and size. The binding agent is heated to liquefying temperature. The dry ingredients and binding agent are mixed thoroughly to ensure complete coating of dry ingredients to produce final mixture.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of fire log.
NOVELTY - A high selectivity oxidation method of (2-methoxy-5-methylphenyl)methanol derivative (I) to (2-methoxyphenyl)methanol derivative (II) comprises using Dess-Martin periodinane and 2-iodoxybenzoic acid as oxidizing agent at 1:1-10 molar ratio.    USE - Oxidation method of (2-methoxy-5-methylphenyl)methanol derivative to (2-methoxyphenyl)methanol derivative (claimed).    ADVANTAGE - The method has high product yield and environment-friendly.    DETAILED DESCRIPTION - A high selectivity oxidation method of (2-Methoxy-5-methylphenyl)methanol derivative of formula (I) to (2-Methoxyphenyl)methanol derivative of formula (II) comprises using Dess-Martin periodinane and 2-iodoxybenzoic acid as oxidizing agent at 1:1-10 molar ratio.    R=hydroxy protecting group comprising trimethyl silicon base, tertiary butyl dimethyl silicon base, cyclopentyl or benzyl.
NOVELTY - A photochemical reaction solution is obtained by mixing pseudosaponin diacetate, hematoporphyrin photosensitizer, triethylamine and acetic anhydride in organic solvent. The solution is supplied into photochemical immersion reactor bubbling vessel, and air or oxygen is bubbled. Blue light-emitting diode lamps are installed, and subjected to photosensitized oxidation reaction. The product is distilled, and supplied into acetic acid reflux elimination reaction. The product is dissolved in petroleum ether, and recrystallized, to obtain dehydrogenated 16-diketene acetate ester.    USE - Preparation of dehydrogenated 16-diketene acetate ester useful for producing steroidal drugs.    ADVANTAGE - The method economically and environmentally-friendly enables preparation of dehydrogenated 16-diketene acetate ester with yield of 82.6%.    DETAILED DESCRIPTION - A photochemical reaction solution is obtained by mixing pseudosaponin diacetate, hematoporphyrin photosensitizer, triethylamine and acetic anhydride in organic solvent at room temperature. The reaction solution is supplied into photochemical immersion reactor bubbling vessel, and air or oxygen is bubbled to the bottom of reactor. Cooling water valve is opened, blue light-emitting diode lamps are installed for performing photosensitive oxidation reaction, and subjected to photosensitized oxidation reaction at room temperature. The photosensitized oxidation reaction product is distilled under reduced pressure for removing organic solvent, and supplied into acetic acid reflux elimination reaction. The obtained product is rotated in acetic acid elimination reactor, dissolved in petroleum ether at 60-90 degrees C, washed to neutral, petroleum ether is distilled off under reduced pressure, and resulted crude product is recrystallized using methanol, to obtain dehydrogenated 16-diketene acetate ester.
NOVELTY - 2-(3-cyano-4-isobutylphenyl)-4-methylthiazole-5-formic acid crystal is prepared by mixing 2-(3-cyano-4-isobutylphenyl)-4-methylthiazole-5-formic acid with first solvent e.g. ethanol, 1-propanol, 2-propanol, 1-butanol, 2-butanol, acetone or ethyl acetate and second solvent e.g. n-propyl acetate, isopropyl acetate, n-butyl acetate, titanium dioxide or methyl tert.-butyl ether in which ratio 2-(3-cyano-4-isobutylphenyl)-4-methylthiazole-5-formic acid:first solvent:second solvent is 1 g:0.1-10 ml:3-40 ml, heating and crystallizing at low temperature.    USE - Preparation of 2-(3-cyano-4-isobutylphenyl)-4-methylthiazole-5-formic acid crystal (claimed).    ADVANTAGE - The preparation method is nontoxic, environment-friendly, and uses highly-selective solvent system.
NOVELTY - The method involves making sodium hydroxide solution contact (S2) the cellulose filter sludge of the radioactive slurry, then adding (S4) cellulose degradation enzyme. The cellulose contained in the cellulose filter sludge is saccharified (S5). Glycolytic yeast is added (S6) to the solution containing the generated saccharide, and the saccharide is decomposed (S7) into alcohol. The alcohol contained in the solution is evaporated by heating, and separated (S8).    USE - Reduction treatment method of radioactive waste containing a filter sludge, e.g., produced in purification of primary system cooling water of nuclear power plant.    ADVANTAGE - The time required for volume reduction of a cellulose filter sludge can be shortened.    DESCRIPTION OF DRAWING(S) - The drawing is a flowchart illustrating the reduction treatment method of radioactive waste containing a filter sludge. (Drawing includes non-English language text).    Sodium hydroxide solution/cellulose filter sludge contacting step (S2)    Cellulose degradation enzyme adding step (S4)    Cellulose saccharifying step (S5)    Glycolytic yeast adding step (S6)    Saccharide decomposing step (S7)    Alcohol evaporating and separating step (S8)
NOVELTY - Preparing acetic acid (S)-1-(acetylamino-methyl)-2-chloro-ethyl ester (I) comprises mixing S-epoxy chloropropane, benzaldehyde and ammonium hydroxide in an organic solvent in the condensation reaction and esterification.    USE - Used for preparing acetic acid (S)-1-(acetylamino-methyl)-2-chloro-ethyl ester (claimed).    ADVANTAGE - The method does not need high temperature and high pressure condition lower reaction, and the reagent is low-toxic solvent, and it has safety, is environment friendly, and economical.
NOVELTY - This new type utility claims one a high COD, high ammonia nitrogen industrial sewage anaerobic biological processing device. The device comprise UASB reaction and Anammox reaction tank, tank UASB reaction tank comprise the first three phase separator set on the top part and set with a first water distributor on the bottom of the first water distributor through pipeline and the sewage pipeline connecting valve, the top part of UASB reaction tank is set with overflow port, the overflow port through valve and pipeline connecting with water storage tank, the Anammox reaction can comprise the second set of top part three phase separator and the second water distributor set at the bottom of the second water distributor with the impounding reservoir of a connecting, second water distributor through a bottom valve water tank connect with the water, a water storage tank set with a liquid level sensor. The high COD, high ammonia nitrogen industrial sewage anaerobic biological treatment device investment cost is low, the processing efficiency is high, the floor space is small, operation cost is low, does not produce second pollution.
NOVELTY - This utility new type is a rotate one biological rotor component, used for fresh domestic sewage treatment device, the sewage treatment device comprise box body, a denitrification pool, an inclined tube sedimentation tank, a sludge pump, rotate the rotor component through pipeline connected biological denitrification pool and the inclined tube sedimentation tank, biological rotate rotor component is arranged in the box body and comprise inner shell is opened with an air through hole and a power machine driving by a multi-synchronous rotate a series of biological rotor rotate, each rotate biological rotor using a multi-stage biological turntable, a each plate set with a radial slice of biological belt. This utility new type domestic sewage treatment device for lifting a utilization rate of energy, oxygen conversion rate of the microorganism biochemical degradation of capacity so that the sewage can realize for removal of organic matter, mounting is convenient to lower the lower energy consumption condition, simple operation, use life is long, low noise, no peculiar smell, the sludge amount is small.
NOVELTY - This utility new type is a biological one turntable integral domestic sewage treatment device, the sewage treatment device comprise box body, a denitrification pool, biological treatment unit, an inclined tube sedimentation tank, a sludge pump, mud pool, denitrification pool, used for sewage and reflux of sewage mix, the bottom of the mud storage area, the inner part has a mounting table area ratio of filler, a multi-microorganism growth surface of filler, biological treatment unit connected denitrification pool, and comprise a shell of air through hole and electric machine drive by a multi-synchronous rotate a series of biological rotor rotate, each rotate biological rotor using a multi-stage biological turntable, a each plate set with a radial sheet of biology. This utility new type lifting a utilization rate of energy, oxygen conversion rate of the microorganism biochemical degradation of capacity so that the sewage can realize for removal of organic matter, mounting is convenient to lower the lower energy consumption condition, simple operation, use life is long, low noise, no peculiar smell, the sludge amount is small.
NOVELTY - This utility new type a a solution of silicon-potassium fertilizer of molding, a molding of fertilizer is through machinery pressure molding of the shape of elliptical geometrical shape. The main advantages are as follows: 1. The traditional fertilizer as raw material of a machinery process in a secondary molding processing is elliptic through machinery processing rear, density of product, table area, dissolve speed is obviously reduced, so as to reduce the leaching loss of fertilizer, prolongs the period of validity, and it has obvious slow release effect. 2. Easy processing into good controllability control applying fertilizer, preparation is elliptic, in the transportation process is not easy to be extrusion crushing, further strength is large, can be stored for a long time storing and is not easy to deform. 3. Can be divided according to annular indentation of fertilizer molding surface, the molding a fertilizer broken into four parts, is convenient to control fertilizing dosage to avoid the multi-fertilizing of the environmental pollution.
NOVELTY - A one circulation fluidized bed biomass gasification device, include fluidized bed gasification furnace, circulation separator, a dust separator, a fluidized bed gasification furnace with the circulation separator composed of biomass circulation fluidized bed, fluidized bed gasification furnace of side wall mounting with a packing auger feeder, feeder through start-shaped seal and a connecting feeder, a fluidized bed gasification furnace lower part set with combustion room, a combustion chamber set with air distribution plate and the top, inner combustion room arranged light oil burner, combustion room through blast pipe and blower connect, output end of circulation separator the bottom of the fluidized bed gasification furnace lower returning input port connecting the smoke output end of circulation separator is connected with the inlet of dust-removing separator connect. This utility new type using star seal feeding a seal uniform feeding, through, parameter adjusting draught fan, the feeding position of a close to zero pressure, reduces the feeding process in the exist pressure difference caused by the seal is difficult to realize the raw material uniform, solves the problem that the seal feeding of raw material.
NOVELTY - Capsule comprises loratadine as active component, and auxiliary component including 6 wt.% of desloratadine, 30-50 wt.% of microcrystalline cellulose, 20-40 wt.% of calcium hydrophosphate, 10-30 wt.% of pregelatinized starch and 1-5 wt.% of talcum powder.    USE - The capsule is useful for treating perennial allergic rhinitis.    ADVANTAGE - The capsule can be prepared in a simple and eco-friendly manner with good stability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing capsule, comprising dissolving pregelatinized starch in water to obtain pregelatinized starch aqueous solution, regulating pH value to 7-8 using sodium bicarbonate solution, crushing the desloratadine into fine powder, placing desloratadine in boiling granulating drier, and then spraying the pregelatinized starch, covering the pregelatinized starch in the loratadine fine powder to obtain pregelatinized starch, wrapping pregelatinized starch on the desloratadine drug, mixing desloratadine and pregelatinized starch, and adding microcrystalline cellulose and calcium hydrophosphate, performing wet granulating process to obtain product, slowly stirring the mixture into 30% of ethanol aqueous solution as wetting agent, preparing soft material, then granulating using 24 meshes sieve to obtain wet granule, placing obtained wet granule in a boiling drying granulator at 500 plus minus 5 degrees C for 40-60 minutes and then drying to obtain dry granule, and adding obtained dry granule and talcum powder and into a three-dimensional mixer at rotating speed of 30 revolutions per minute for 40 minutes.
NOVELTY - This utility new type relates to one a cottonseed mix oil refining by-product increase utilization rate of desolventizing device, is the device time prepare acetate solution to the cottonseed oil refining by-product mix is use of raw material, include a desolvation and solvent recovery device, the material is stainless steel. Using the device, solvent of gossypol in the cotton seed mix of gossypol in sodium oil refining by-product by acidification, a rear impurity removing of fully removing diethyl ether and a futher. The a cottonseed oil refining by-product mix a comprehensive utilization and high economic value a greatly increase.
NOVELTY - Preparing micro methanol reformer combustion chamber catalyst comprises taking the reformer combustion chamber with a flow field as the anode, placing in an electrolyte, applying direct current (DC) or alternating current (AC) voltage on flow field for processing, so as to form a porous oxide ceramic membrane layer on the flow field surface, taking it as a carrier and loading platinum on it.    USE - The method is useful for preparing micro methanol reformer combustion chamber catalyst (claimed).    ADVANTAGE - The catalyst solves the problem of poor adhesion of the catalyst in the existing methanol reformer combustion chamber, small contacting area of reaction gas with the catalyst, and low catalyst utilization.
NOVELTY - This utility new type claims a glycerol one purifying device, belonging to the field of chemical technology field, the device comprise a valve I, exchange column I, a valve II, a valve III, a valve IV, a valve V, a valve VI, a valve VII, a valve VIII, a valve IX, a valve X, exchange column II, column III, exchange exchange column IV, column V exchange, exchange column I of lower end exchange column II and a lower connecting end, upper end and upper end column III of exchange of exchange column II connect, lower end and lower end of exchange column IV of exchange column III connect, upper end and upper end of exchange column V of exchange column IV connect, this utility new type a. make glycerin purification process flow is simple and pollution-free, and the efficiency is high.
NOVELTY - An ammonia-oxidizing bacteria sandwich-type multilayer immobilized bioactive filler comprises embedded body loaded with ammonia-oxidizing bacteria and nonwoven carrier in which non-woven carrier and embedded body have alternating arrangement. Ammonia-oxidizing bacteria sandwich-type multilayer immobilized bioactive filler is prepared by cutting solidified filler to form ammonia-oxidizing bacteria particulate bioactive filler, and fixedly bonding nonwoven carrier fiber filament with embedded body.    USE - An ammonia-oxidizing bacteria sandwich-type multilayer immobilized bioactive filler for water treatment (claimed).    ADVANTAGE - Ammonia-oxidizing bacteria sandwich-type multilayer immobilized bioactive filler saves energy and embedded liquid, reduces processing cost and formation of dense film, has shortened start-up time, good fluidized state, high processing efficiency, and long service life, and maintains high bacteria concentration.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of ammonia-oxidizing bacteria sandwich-type multilayer immobilized bioactive filler which involves using secondary clarifier sludge from municipal wastewater treatment plant as bacteria source, screening, enrichment culturing, centrifugally enriching ammonia-oxidizing bacteria to obtain ammonia-oxidizing bacteria solution with concentration of 108-1010 cells/ml, heating polyvinyl alcohol to 90 degrees C, dissolving in water to obtain polyvinyl alcohol solution, cooling to 30 degrees C, mixing with ammonia-oxidizing bacteria solution to obtain embedded solution with polyvinyl alcohol concentration of 70-140 g/L, evenly coating on polyvinyl alcohol nonwoven fabric carrier, stacking coated nonwoven fabric, crosslinking with saturated boric acid for 1.5 hours, taking out, adjusting boric acid solution pH to 8-10, performing 2nd crosslinking for 5 hours, rinsing with clean water, and cutting.
NOVELTY - The device has a water inlet tube (14) which is fixed on a bottom inner box portion (1), and arranged with an uniform water hole. A reverse flushing water inlet valve (13) is connected with a water inlet pipe through a reverse flushing inlet pipe. An air inlet valve (15) is connected with an air inlet distribution tube through an air inlet pipe. A loop tube (16) is fixed with uniform holes.    USE - Sewage water processing device for removing nitrogen and phosphorus.    ADVANTAGE - The stable operation of the processing device is ensured.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the sewage water processing device.    Bottom inner box portion (1)    Reverse flushing water inlet valve (13)    Water inlet tube (14)    Air inlet valve (15)    Loop tube (16)
NOVELTY - Method for treating, disposing and recycling livestock manure, involves producing livestock manure precipitate by placing the manure in precipitation wells, separating the precipitate to solid portion and liquid portion, purifying the obtained solid portion and liquid portion, obtaining biogas slurry, liquid biogas and biogas, and purifying the biogas slurry which is useful for planting.    USE - The method is useful for treating and disposing livestock manure and recycling livestock manure into biogas slurry used as organic fertilizer for planting, biogas which used in photovoltaic greenhouse for growing duckweed and algae, and as fuel, liquid biogas, and water used for pasture and crop cultivation. The duckweed is used as livestock feed ingredient (all claimed).    ADVANTAGE - The method is harmless as it achieves zero emissions.
NOVELTY - Preparing biological carbon from organic waste, comprises mixing organic waste by a conveyor and then heating and sterilizing, placing sterilized organic waste in a cyclone dust collector and then processing, fully mixing the processed organic waste in a mix hopper and then heating, drying and sterilizing, placing the sterilized organic waste in a carbonization machine and then carbonizing, placing the carbonized organic waste in a pre-heater and then pre-heating, cooling and drying, and placing the dried organic waste in a burner and then heating and cooling by a cooling machine.    USE - The method is useful for preparing biological carbon from organic waste (claimed).    ADVANTAGE - The method is capable of preparing the biological carbon from organic waste with high utilization rate, less energy consumption, and high carbonizing efficiency and good stability in an eco-friendly manner.    DETAILED DESCRIPTION - Preparing biological carbon from organic waste, comprises (a) mixing organic waste by a conveyor and then heating at 400-600 degrees C and sterilizing, placing the sterilized organic waste in a cyclone dust collector and then processing, and exhausting flue gas, (b) fully mixing the processed organic waste in a mix hopper and then heating by a microwave generator at temperature of 200-300 degrees C, drying and sterilizing, (c) placing the sterilized organic waste in a carbonization machine and then carbonizing at temperature of 400-600 degrees C, placing the carbonized organic waste in a pre-heater and then pre-heating at 200-300 degrees C, cooling and drying, and (d) placing the dried organic waste in a burner and then heating at 300-400 degrees C and cooling by a cooling machine.
NOVELTY - Fertilizer composition comprises potassium dihydrogen phosphate, nitrogen, peat, golden cypress, dried tea leaves, soybean meal, amino acid, zinc sulfate, copper sulfate, ferrous sulfate, borax, sodium 5-nitroguaiacolate, soil modifier, yeast, sodium alpha -naphthaleneacetic acid, vitamin B, vitamin C, and citric acid.    USE - The fertilizer composition is useful for promoting growth of plant, thick leaves, root and thick stem.    ADVANTAGE - The fertilizer improves disease and insect resistance in plants, and is rich in nutrition, nontoxic and environmentally-friendly.    DETAILED DESCRIPTION - Fertilizer composition comprises 10-15 pts. wt. potassium dihydrogen phosphate, 6-10 pts. wt. nitrogen, 10-15 pts. wt. peat, 8-10 pts. wt. golden cypress, 16-20 pts. wt. dried tea leaves, 8-10 pts. wt. soybean meal, 5-10 pts. wt. amino acid, 0.5-1 pt. wt. zinc sulfate, 0.2-0.5 pt. wt. copper sulfate, 0.5-1 pt. wt. ferrous sulfate, 0.5-1 pt. wt. borax, 0.02-0.1 pt. wt. sodium 5-nitroguaiacolate, 5-35 pts. wt. soil modifier, 0.4-1 pt. wt. yeast, 0.02-0.1 pt. wt. sodium alpha -naphthaleneacetic acid, 0.025-0.15 pt. wt. vitamin B, 0.025-0.15 pt. wt. vitamin C, and 0.03-0.1 pt. wt. citric acid. An INDEPENDENT CLAIM is included for method for preparing the fertilizer composition, which involves uniformly mixing peat, soybean meal and dried tea leaves, mixing obtained mixture with yeast and water, piling mixture, performing aerobic fermentation of piled product to obtain first mixture, mixing the first mixture, potassium dihydrogen phosphate, nitrogen, amino acid, zinc sulfate, copper sulfate, ferrous sulfate, borax, sodium 5-nitroguaiacolate, soil modifier, vitamin B and vitamin C to obtain second mixture, periodically turning second mixture, uniformly mixing second mixture, sodium alpha -naphthaleneacetic acid and citric acid to obtain fertilizer, granulating the fertilizer, drying granules, and packing and storing dried granules.
NOVELTY - Straw composting agent comprises decomposing material, bran, flax residue, soybean, potato residue, microbial strain, fermented molasses and basidiomycetes.    USE - Straw composting agent.    ADVANTAGE - The straw composting agent prevents soil pollution, and is prepared in simple and cost-effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing straw composting agent, which involves fermenting raw materials at pH of 4.4-4.6 for 15-25 days at 25-36 degrees C, where fermented material is dried to obtain desired product.
NOVELTY - Mushroom culture medium comprises 45-55 wt.% sunflower straw, 15-20 wt.% apple tree sawdust, 15-25 wt.% pear tree sawdust, 4-7 wt.% bran, 1-3 wt.% gypsum powder and 1-3 wt.% calcium superphosphate.    USE - Used as a mushroom culture medium.    ADVANTAGE - The culture medium has high nutritional value, contains thiamine, riboflavin and niacin required for microorganism growth, further contains alpha -amylase, beta -amylase, oxidase and peroxidase required for microorganism; includes gypsum powder so as to make up the sulfur and calcium deficiency; and can decompose the organic matter in the culture compound.
NOVELTY - A vehicle methanol gasoline contains 70-80 pts. wt. methanol, 10-20 pts. wt. gasoline, 0.2-0.3 pt. wt. ethane, 0.2-0.3 n-hexane, 0.35-0.8 pt. wt. ethanol, 0.2-0.3 pt. wt. peroxide, 0.02-0.05 pt. wt. corrosion inhibitor (102TB), 0.02-0.05 pt. wt. anti-swelling agent (107PT), 0.02-0.05 pt. wt. methyl tert.-butyl ether, 0.2-0.5 pt. wt. eicosapentaenoic acid, and 0.2-0.5 pt. wt. oleic acid.    USE - Vehicle methanol gasoline (claimed).    ADVANTAGE - The gasoline is clean, environment-friendly, convenient to use, and energy-saving, has low cost, wide and easy to buy raw materials, enhanced stability, and reduced tail gas, and saves fuel cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of vehicle methanol gasoline fully mixing ethane, n-hexane, ethanol, corrosion inhibitor (102TB), and eicosapentaenoic acid, stirring at normal temperature for 30 minutes, standing, stirring for 60 minutes, adding anti-swelling agent (107PT) and methyl tert.-butyl ether, uniformly mixing to obtain 1st material, mixing peroxide and methanol, heating to 40-50 degrees C, standing and stirring for 40 minutes to cool, stirring in pressure tank at 0.8 MPa for 20 minutes, standing for 30 minutes to obtain semi-finished product, filtering in 106-mesh filter screen to obtain 2nd material, adding gasoline and 2nd material in reaction container, stirring, adding 1st material, uniformly stirring, and standing for 45 minutes.
NOVELTY - Removing hydrogen sulfide from biogas comprises (i) washing and absorbing biogas using mixture of sodium carbonate and/or potassium carbonate as desulfurization absorption liquid; (ii) performing substitution reaction of desulfurization rich liquid with solid particles containing 1-30 mm of iron element or iron oxide to obtain regenerated sodium carbonate or potassium carbonate; and (iii) recovering sulfur from desulfurization poor liquid obtained in the (ii) and recycling.    USE - The method is useful for removing hydrogen sulfide from biogas (claimed).    ADVANTAGE - The method avoids sulfur deposition and blockage at the absorption tower, is simple and economical; and utilizes a simple device.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for removing hydrogen sulfide from biogas, comprising an absorption tower, a regeneration tower and a precipitation-separation device, where the absorption tower outlet is connected with the regeneration tower inlet, the regeneration tower outlet is connected with the precipitation-separation device inlet, and the precipitation-separation device outlet is connected with the absorption tower inlet.
NOVELTY - Quick batch targeted screening of microalgae in bio-diesel comprises collecting algae containing acidic wastewater sample; enrichment culturing; diluting enriched water sample, adding diluted enriched water sample into BG11 solid culture medium plate, plate culturing; picking single microalgae grown on solid culture medium plates, placing on slide to prepare microalgae cell temporary slide, dyeing with sudan black B lipophilic dye, and comparing oil containing reference microalgae, where if cell black oil droplets area is greater than reference cell lines, considering it as target microalgae.    USE - The method is useful in biomass energy field and biodiesel oil production production filed (all claimed).    ADVANTAGE - The method is fast and efficient in screening the target strain.    DETAILED DESCRIPTION - Quick batch targeted screening of microalgae in bio-diesel comprises (i) collecting algae containing acidic wastewater sample; (ii) enrichment culturing the collected wastewater sample, to obtain enriched water sample, where the enrichment culturing conditions include temperature of 10-40 degrees C, light intensity of 2500-20000 lux, illumination time of 8-24 hours/day, aeration rate of 0.1-1 vvm, where the carbon dioxide volume fraction is 0.03-50%, and the enrichment culture period is 8-20 days; (iii) diluting the enriched water sample, adding diluted enriched water sample into BG11 solid culture medium plate, plate culturing at 10-40 degrees C under light intensity of 2500-20000 lux, illumination time of 8-24 hours/day, and then incubating the plates for 8-15 days; (iv) picking single microalgae grown on solid culture medium plates, placing on a slide to prepare microalgae cell temporary slide, dyeing with sudan black B lipophilic dye, under an optical microscope, comparing the oil containing reference microalgae, where if the cell black oil droplets area is greater than the reference cell lines, considering it as the target microalgae.
NOVELTY - This utility new type claims a one aerobic compost reactor oxygen concentration in real time monitoring system. Oxygen concentration in real time monitoring system include vent tube, an oxygen concentration sensor, a micro-negative pressure device and a real-time display and store a; air tube of one end with the micro-negative pressure device are connected, along the opening end of air tube to the direction of the connecting end of micro-negative pressure device a, in turn set with pre-filter and oxygen concentration sensor through inner tube, pre-filter and said oxygen concentration sensor are through out of inner tube of air tube, and the oxygen concentration sensor set on the measuring pneuma hole inner of oxygen concentration sensor and a converter connecting, a converter converts the oxygen concentration sensor of a simulate electric signal into a digital signal, a real time display and the terminal comprise a computer, computer is connected with the signal converter connecting. This utility new type aerobic compost reactor oxygen concentration in real time monitoring system, a rear two level filter can be valid to prevent high humidity gas for damage of oxygen concentration sensor, valid life and increase the precision of sensor.
NOVELTY - This new type utility claims one prepare biology diesel oil of a device, belonging to the field of chemical technology field, the device include feeding tube I, a heat exchanger, a feeding tube II, a tubular reactor, a distilling tower, a separate tower, a branch tube, a fuel inlet, high pressure boiler, set with a fuel inlet in the lower high pressure boiler part distributed with multi-ring feeding tube I in a high pressure boiler hearth wall, a feed tube exit of I and the branch tube is connected with each branch pipeline and a tube type reactor of the branch tube is connected with the feeding tube II through heat exchanger and one end tube-type reactor, the other end of tubular reactor of distillation tower is connected with the upper end of distillation tower is set with a tube, a tube through heat exchanger and feeding tube I is connected with distillation tower through pipeline and the separate tower, this utility new type using a tubular reactor a continuous preparation a biological diesel oil, at the same time considering also a methanol raw material oil pre-heating time a, the characteristics are that supercritical methanol prepare biology diesel oil of production is continuous, efficient and energy-saving.
NOVELTY - A low pressure gas system of open Low-temperature pneuma biogas tank, it has one upper end open marsh gas pool, two side opening of marsh gas tank set with a feeding port, a discharging port, a marsh gas tank upper end by flexible film cover is sealed, one end outer inner one section the pneuma tube into the tank from the upper end of the biogas tank, gas-guide tube the pneuma of marsh gas is connected with a gas pipeline the mounting with a gas pump, one shunt tube with the gas tube connected, shunt tube extends to one pressure control device in the pressure control device is one tank body, upper part of the tank body is provided with one discharge port in lower part is opened with one overflow port, the tank body is equipped with water dividing tube extends to water in. When the marsh gas tank gas is gradually increased in a low, a flexible thin film a gradually a is to avoid too high a pressure increase, when the pressure reach the time, through pressure control device, a pressure of a gas inner marsh gas pool, time pressure of marsh gas when the marsh gas tank, inner gas pump through a marsh gas output to a gas user to ensure the marsh gas can be a use.
NOVELTY - This utility new type provide a one household garbage landfill processing system, said system comprise: in turn in a preprocessing stage aeration, a., garbage stationary, rear aeration process four a period of reactor, and connecting liquid connecting pipeline and gas connecting pipeline of the reactor a, reactor of aeration preprocessing period for the inner of garbage process the upper layer aeration preprocessing, producing a filtered liquid collecting port at the bottom of reactor of a. period with the top of a filtered liquid entering into; reactor at the bottom of aeration preprocessing period a filtered liquid collecting port and the reactor top seepage filtered liquid entrance of garbage stabilization period, stable period of reactor of garbage seepage filtered liquid collecting port and the aeration preprocessing stage of reactor of the top of a filtered liquid entrance connected with the rear aeration rear reactor of a period for the inner of garbage process aeration process. This utility new type for filling garbage through taking the upper layer aeration preprocessing, the accumulated a organic acid and waste acid stage is shortened, the degradation speed is increase.
NOVELTY - This new utility model relates to a kind of quantification for one discharge grid-type marsh gas production device, comprises marsh gas pool, a feed box, a lifting device, a feeding port, a discharging port and sealing fixed with header setting in the liquid relux device in marsh gas pool, the marsh gas pool top, upper header set with one air outlet, a marsh gas pool one end of top part equipped with feedstock wherein, marsh gas pool the other end top part is provided with a discharging port, and feedstock port and discharging port on lower bottom corresponding to the marsh gas pool set with guide rail, the bottom of the box and equipped with guide rail matching the each roller box bottom through box lifting device from feedstock wherein enter into marsh gas pool and guide rail and rolling connected with the shell body of the case provided with grid is uniformly distributed, the marsh gas pool in guide rail and two side periphery respectively provided with attached to membrane strain, strain film attached to the periphery side set with two heating machine, the utility model is new type equipment is simple, suitable operation, high efficiency and can ferment raw material to carry out quantitative control, outlet, feedstock is suitable for quantitative discharging grid-type marsh gas production device.
NOVELTY - The integrated organic agricultural waste spiral slag from the marsh gas fermenting device, comprise the box, the material tube, the fermentation cylinder outer cylinder, spiral lamina, fermentation cylinder inner cylinder, air blower, an overflow slag tube, waste residue collecting tank, a fine sieve, circulation gas tube, circulation pump, circulation liquid tube and gas exit, the said box through the material tube and the tube of the outer fermentation cylinder connected, said fermentation cylinder outer cylinder and inner cylinder fermentation cylinder inner mounting with a spiral lamina, said fermentation cylinder outer cylinder mounting with air blower, the air outlet of said air blower with spiral plate welding, a fermentation cylinder in the outer cylinder upper part mounting an overflow slag tube, a waste residue collecting tank middle part mounting with a fine sieve, a waste residue collecting tank through upper circulation tube and the marsh gas fermentation cylinder outer cylinder upper part connected, a waste residue collecting tank lower part connected with a circulation pump, a circulation pump of exit and the material box upper part connected, this utility new type has simple structure, is convenient to use, the organic agricultural waste processing to marsh gas, and the slag can be automatic.
NOVELTY - This utility new type claims a one for refuse derived fuel molding machine of hot air, a refuse derived fuel molding machine comprise connecting a material supply cabin in turn, molding machine between the main body and the scraper, a material feeding and scraper through one air conveying device connected, a discharge port feeding port is connected with a molding machine main body of a scraper conveyor through a chute connected between the three is seal structure. This utility new type garbage derived fuel molding machine produce in production of heat in the process of drying raw material, reduce the material water content part, to solve the problem of high water content due to a difficult molding of refuse derived fuel, but also has the function of saving energy source.
NOVELTY - The system has a pigsty system, a solid-liquid separate system and a solid-liquid treatment system. The top portion of the main portion is set with a steel frame structure, an energy-saving and environment-protecting layer and a temperature control system. The bottom portion of the main portion is mounted with a fecal leakage plate. The solid-liquid treatment system is connected with concentrate tank and marsh gas tank that is composed of a stirrer, a fermentation groove, a turning device, a pressing device, a push-pull device and a packaging machine.    USE - Energy-saving and environment-friendly type disposable sewage treatment system.    ADVANTAGE - The marsh gas and fertilizer are manufactured from pigsty excrement. The hygien level of the farm and the pig environment are improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for treatment method of disposable sewage through ecological circulation.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating the disposable sewage treatment process. (Drawing includes non-English language text)
NOVELTY - Extracting beta -carotene from salt tolerant algae, comprises mixing the algae with distilled water in mass ratio of 1:5 and then stirring to adjust pH value of 5-6.5 using hydrochloric acid, mixing protease with salt liquid in mass ratio of 1:33.3-54.5 to dissolve and then heat preserving at 55-65 degrees C for 1-1.5 hours and passivating at 85-95 degrees C for 8-12 minutes, centrifuging extracted liquid at speed of 2500-3500 revolutions per minute for 8-12 minutes, and mixing the precipitate with plant oil in a ratio of 1:5 and then heating at 70-85 degrees C for 20-35 minutes, cooling and filtering.    USE - The method is useful for extracting beta -carotene from salt tolerant algae (claimed).    ADVANTAGE - The method is capable of simply and economically extracting the beta -carotene from algae with less energy consumption in an eco-friendly manner.
NOVELTY - Preparing fertilizer involves fermenting mixture of molasses, corn and water using bacteria for 40-56 hours to obtain fermentation liquid. Pig manure, superphosphate, fermentation liquid and carbon source substance are mixed and then fermented to obtain fermentation material. Carbon source substance is selected from rice hull, wooden flour, straw powder, bran or corn powder. Fermentation material is fermented at 30-35 degrees C for 72-96 hours and then continuously fermented at 60-70 degrees C for 36-48 hours to obtain fermentation product.    USE - Method for preparing fertilizer (claimed).    DETAILED DESCRIPTION - Preparing fertilizer involves fermenting mixture of molasses, corn and water using bacteria for 40-56 hours to obtain fermentation liquid. Pig manure, superphosphate, fermentation liquid and carbon source substance are mixed and then fermented to obtain fermentation material. Carbon source substance is selected from rice hull, wooden flour, straw powder, bran or corn powder. Fermentation material is fermented at 30-35 degrees C for 72-96 hours and then continuously fermented at 60-70 degrees C for 36-48 hours to obtain fermentation product. Fermentation product is fermented at 40-50 degrees C for 36-48 hours to obtain the finished product.
NOVELTY - Organic fertilizer comprises 79-81% mushroom cultivation and crop wastes, 17-18% chicken manure and 1-4% rice bran    USE - As organic fertilizer (claimed).    ADVANTAGE - The organic fertilizer not only can a by using agricultural production in produce a waste according to a bran, chicken manure, rice hull, rice, the product avoids the excessive use fertilizer soil caused by pollution of at the same time, and reduces the use of pesticide, provides good quality and safety of agricultural products, and environmental protection also makes a great contribution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing organic fertilizer involving mixing food waste with bacteria cultivation, crop waste, manure and rice bran to get the starting material, adding raspberry bacteria, other agents and selenium mixture to the broth in the starting materials used in the fermentation of the mixture in a vacuum state, fermenting the mixture to obtain fermentation product, and dehydrating fermentation product to obtain organic fertilizer.
NOVELTY - Pig waste organic fertilizer comprises 15-25 pts. wt. Bacillus licheniformis, 20-32 pts. wt. lees, 24-40 pts. wt. yeast powder, 10-18 pts. wt. rice bran, 20-28 pts. wt. brown sugar, 100-150 pts. wt. honey, 50-75 pts. wt. pig manure, 300-400 pts. wt. pig urine, 10-15 pts. wt. pig bone, 5-8 pts. wt. pig hair, 1-3 pts. wt. pig blood, 7-12 pts. wt. horse dung, 20-25 pts. wt. rice straw, 70-90 pts. wt. wheat straw, 10-15 pts. wt. Sorghum, 5-10 pts. wt. peanut, 5-10 pts. wt. green vitriol, 6-7 pts. wt. copper and 1 pt. wt. magnesium sulfate.    USE - As pig waste organic fertilizer.    ADVANTAGE - The organic fertilizer is prepared using pig waste thus the pig waste is recycled and the environmental pollution problem is solved, and replaces chemical fertilizers that affect the soil, thus can be used for long term.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the above-cited pig waste organic fertilizer, which involves (a) mixing B.licheniformis, lees, yeast powder, rice bran, brown sugar and honey, and storing the mixture in dark condition at 20-30 degrees C for 3-8 days, (b) adding pig manure, pig urine, pig bone, pig hair, pig blood, horse dung, rice straw, wheat straw, Sorghum, peanut, green vitriol, copper and magnesium sulfate into the obtained mixture, and stacking up to a height of 1.5-2 m at a humidity of 45-50%, (c) performing anaerobic fermentation at 20-30 degrees C for 10-15 days in summer and 15-20 days in winter, crushing the fermented product, granulating the crushed material and drying the granules.
NOVELTY - This utility new type claims a petrochemical one biological film reactor, wherein include biochemical reaction tank, a biochemical reaction tank connected with a sedimentation tank and a metering pump, and the other end metering pump connected with a sewage pool, a biochemical reaction tank connecting with a temperature control device, a biochemical reaction tank comprise reaction tank body and connected aeration device of reaction tank body, inner said reaction tank body set with a biological reaction, and the reaction tank body inner set on the sewage of suspension biological filler mix. This utility new type is a membrane biological method lower the relative simple technology, application of advanced, combine a conventional activated sludge process sewage, a maximum limit has degradation ability of efficient strain, low energy consumption, a high efficiency, use the new type packing material, which greatly saves cost.
NOVELTY - This new type utility claims one a powdery high water-containing fertilizer production storage hopper, wherein storage hopper comprise cone, driving device, and device, upper, lower end of said bin bodies set with material entrance and a material exit, a drive device set on the upper part of said storage bin cone, a stirring device set on said storage bin inner cone, said driving device connecting a stirring device and a stirring device driving the stirring operation in the storage hopper cone, said inner lining plate is set on the inner wall of storage hopper of a vertebral body. This utility new type can overcome the high water material for bonding a storage bin wall and would not cause bridge, so as to ensure the smooth process operation, lining not only solves the hanging problem of, at the same time, can solve the problem that the organic substance for corrosion of steel cone, increase use life.
NOVELTY - This utility new type relates to a one fertilizer production device, specifically to a composite fertilizer one a heat using device. Comprise tower body and the tower body upper end set with a ventilation hole, the ventilation hole is inserted in pipe, and the other end a ventilation tube of connected water storage tank, the ventilation tube outer side a detachably sleeved heat collecting sleeve, a lower end opening of the heat collecting pipe, and the opening end of heat pipe is inserted to the water tank in, a water storage tank and the heat collecting pipe connecting set with one-way valve. The device a vent-pipe through the hot air into the water tank in a heat exchange, at the same time, in order to prevent the hot air caused by heat loss in the pipeline on the outer side of pipeline set with heat collecting sleeve, a the heat, which avoids resource waste, and it will not cause air pollution.
NOVELTY - One a biomass hot gas cooling system, include gas-heat exchanger, soot, hot oil flow regulating device, ,-condensed water heat exchanger, water pump, gas-heat exchanger with the conduction oil between the condensed water heat exchanger through the hot oil flow regulating device, and a heat conducting oil circulation pipeline, a condensed water exit of water tank with the conduction oil-condensed water heat exchanger of water inlet connecting,-water exit condensed water heat exchanger through a condensed water pump with the condensed water inlet of water tank connect, exchange pitch of gas-heat exchanger 35-65 mm, the heat exchange tube are arranged in parallel mounting a soot-blowing device connected with a blower gas-inner heat exchanger, the heat exchange blower nearest pitch is 150-300 mm, the most distal is 1-1.5 m. This utility new type efficient by using a hot gas display heat, at the same time, efficient quenching of a soot layer, but also ensures the heat exchange tube is not .
NOVELTY - This utility new type provide a biomass gasification one high temperature ash cooling conveying system, comprise soot blowing device and in turn in series connecting a cold, first airlock, a manual door, second lock, middle storage hopper, a cabin pump, concentrated tank, a cold ash machine comprise at least two section arranged in series and vertical to the heat exchange tube set with a blower, a heat exchange interval of adjacent tube is between 25-40 mm, the soot blower interval nearest the heat exchange tube 150-300 mm, and a distal most is 1-1.5 m, a middle storage bin connected with the atmosphere, middle storage hopper in a dust storage cabin pump through using positive pressure conveying system to the central ash storage tank. This utility new type ash can ensure smoothly through biomass ash does not bypass the heat exchanger block, at the same time, ensures the heat exchange effect to reduce heat exchanger cost; it also avoids a conveying a high pressure air entering into negative pressure operation high temperature gasification gas area to prevent the gas explosion.
NOVELTY - The utility model claims a new one for a damaged slope vegetation recovery of strip type planting device, comprise inner bag planting, planting the outer bag and covering layer, the outer bag is slightly smaller than inner planting vegetation bag, length is the same, the outer bag, planting two bag bottom and with the thread sewed inner bag planting of the other side, the sewing side 5 cm of area set with planting hole, planting hole lengthways pitch is 6 to 10 cm, the transverse pitch 5 to 8cm; planting outer bag outer side set with coated layer, and binding silk ring with a fixed, binding silk interval 50 to 80cm; planting inner bag filled with planting material, planting the outer bag filled with a base, mounting time, with the anchor device fixed on the side slope damage cleaning of the upper. The device a pocket attached efficient planting base material, solves the problem that the valid fixing and anti-scour base material a, fertilizer effect is good, the operation is convenient, a green carbon, construction process is energy-saving and environment-friendly, application prospect is good.
NOVELTY - This utility new type claims a sheepcot one, relating to the sheep industry field, the structure include sheepcot main body and the periphery of the sheepcot sheepcot peripheral include a peripheral railing and set with a outer door on the upper peripheral railing, a sheepcot main body comprise two side wall, rear wall, roof, inner rail, and fermenting bed set on the inner rail of a, one surface of said rear wall, wall, inner rail and door set on the inner rail of a form of breeding sheep, said inner enclosure wall surrounded and the other side of walking, the problem set with groove of 50 cm depth, forming fermenting bed, a fermenting bed side wall of four sides of paving 5 cm of cement plate, a fermenting bed air grid plate top surface frame, a fermenting bed pad material is paved, this utility new type solves the problem that the traditional sheepcot exist excrement processing convenient ventilation is not good and sanitary difficult of the breeding of a sheep.
NOVELTY - The method involves preparing synthetic zeolite. The preprocessing fly ash and sodium hydroxide solution are mixed and the resulting solution is cooled to room temperature to obtain second precipitate. The second precipitate is dried and grinded to obtain the synthetic zeolite. The water plant sludge is dried, grinded and filtered, to obtain peat. The foaming agent is dissolved in the de-ionized water to obtain the foaming agent solution. The foaming agent solution is added to the raw material and mixed uniformly so as to obtain the nitrogen phosphorus removal material.    USE - Method for preparing nitrogen-phosphorus removal material using zeolite synthesized from coal ash to remove nitrogen and phosphorus in domestic sewage.    ADVANTAGE - The raw material source is wide. The nitrogen-phosphorus removal material preparation cost is reduced. The synthetic zeolite has higher porosity. The material is processed using the foaming agent, such that the resulting material for removing nitrogen and phosphorus in water has large porosity. The blocking of absorbing hole is prevented effectively, such that the nitrogen-phosphorus removal process is performed smoothly. The nitrogen phosphorus removing effect is improved.    DETAILED DESCRIPTION - The fly ash and the hydrochloric acid solution are mixed and mixing solution is cooled at room temperature to obtain the first precipitate. The obtained first precipitate is rinsed with de-ionized water and is dried to obtain the preprocessing fly ash. An INDEPENDENT CLAIM is included for the regeneration method of nitrogen-phosphorus removal material.    DESCRIPTION OF DRAWING(S) - The drawing shows a photographic view of the synthetic zeolite.
NOVELTY - Plant-based carbon material, is claimed. The material is obtained by carbonizing sunflower disc after extracting pectin, then activating using distilled water and concentrated aqueous ammonium.    USE - Used as plant-based carbon material.    ADVANTAGE - The material is simple and economical to prepare, and has good adsorption ability for copper ions.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing plant-based carbon material, comprising: (i) washing sunflower disc after extracting pectin, drying and crushing; (ii) adding the crushed material into a carbonization furnace and carbonizing under nitrogen gas protection from room temperature to 400 degrees C at a rate of 3 degrees C/minute, then heating from 400 degrees C to 600-800 degrees C at a rate of 1 degrees C/minute to obtain carbonized material; and (iii) activating the carbonized material at 600-800 degrees C for 120 minutes and cooling to 60 degrees C under nitrogen gas protection.
NOVELTY - An adsorbent composition comprises 65-80 %mass activated carbon (a) prepared from biogas residue, 4-7 %mass activating agent (b), 10-15 %mass dispersing agent (c), 4-8 %mass swelling agent (d) and 2-5 %mass adsorbent (e).    USE - Composition is used for adsorbing sulfur dioxide and nitrogen gas from pyrite ore roasting furnace (claimed).    ADVANTAGE - The adsorbent composition is economical and environmentally-friendly, and can be prepared by simple process. Activated carbon is prepared by simple process using biogas having excellent recyclability.
NOVELTY - One of mixed waste treatment centre, comprising multiple processing part for pre-processing part and removing smell and mixed waste, its outlet is connected with the pre-processing part and sorting system, and respectively is connected with the sorting system and outlet. This new utility model and garbage composed of part are all effective recycling use, burning the material needed at least, burning without harmful substance production, environmental protection effect is good; the garbage recycling using efficiency is high, the processing speed is fast.
NOVELTY - The method comprises providing a carrier made of polyurethane foam polymer materials, nitrifying the carrier with a nitrifying bacteria concentrate liquid and then centrifuging to obtain a suspension, concentrating the suspension with 108-109 cells/ml of nitrifying bacteria to obtain a concentrate, mixing the nitrifying bacteria and the concentrate with a polyvinyl alcohol solution, adding calcium into the mixture, stirring the mixture and polyurethane foam with saturated boric acid solution for 1-3 hours, and adjusting pH value of the mixture to 8-10 and then crosslinking for 3-24 hours.    USE - The method is useful for preparing an immobilized bioactive filler, which is useful for preparing a polyurethane-based carrier for treating sewage (all claimed).    ADVANTAGE - The method is capable of rapidly preparing the immobilized bioactive filler with high processing capacity.    DETAILED DESCRIPTION - The method comprises providing a carrier made of polyurethane foam polymer materials, nitrifying the carrier with a nitrifying bacteria concentrate liquid and then centrifuging to obtain a suspension, concentrating the suspension with 108-109 cells/ml of nitrifying bacteria to obtain a concentrate, mixing the nitrifying bacteria and the concentrate with a polyvinyl alcohol solution, adding calcium into the mixture, stirring the mixture and polyurethane foam with saturated boric acid solution for 1-3 hours, adjusting pH value of the mixture to 8-10 and then crosslinking for 3-24 hours and taking out, and washing a surface residual material of the mixture and then slicing. The sliced mixture has a length of 3-5 mm, a breadth of 3-5 mm and a diameter of 3-5 mm, and has rectangle or cube shape.
NOVELTY - A denitrifying bacteria immobilized biologically active filler comprises granular biologically active filler obtained by performing pressing adsorption on polyurethane foam block to adsorb embedded solution containing denitrifying bacteria, curing, and cutting.    USE - A denitrifying bacteria immobilized biologically active filler for water treatment (claimed).    ADVANTAGE - Denitrifying bacteria immobilized biologically active filler is stable, improves denitrification reactor capacity, shortens starting time, has high denitrification efficiency and utilization rate and large specific surface area, and saves raw material.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of denitrifying bacteria immobilized biologically active filler which involves using polyurethane foam high-molecular material as embedded carrier, using residual sludge from secondary settling tank of municipal wastewater treatment plant as bacteria source, screening, enrichment culturing to obtain denitrifying bacteria bacterial suspension, centrifugally enriching to obtain denitrifying bacteria concentrated liquid with concentration of 108-109 cells/ml, performing polyvinyl alcohol-boric acid secondary crosslinking method, mixing denitrifying bacteria concentrated liquid with polyvinyl alcohol solution, adding calcium carbonate to obtain embedded solution with polyvinyl alcohol concentration of 30-50 g/L and calcium carbonate concentration of 10 g/L, pouring into polyurethane foam, repeatedly pressing polyurethane foam to let embedded solution enter polyurethane foam, placing in saturated boric acid solution for 1-3 hours, adjusting pH to 8-10, crosslinking for 3-24 hours, taking out, washing residual substance from surface, and cutting.
NOVELTY - Oily sludge treatment system comprises sludge tank (1), sludge conveying pump (2), stabilizing tank (3) provided with stirrer, first measuring pump (4), destabilization tank (5) provided with stirrer, connecting tube (6), first flocculation tank (7) provided with stirrer, second metering pump (8), second flocculation tank (9), outlet tube (10), belt-type filtering device (11), screw conveying pump (12), water collector (13), water tank (14), mixed coal device (15) for producing coal cluster, coal powder conveying device (16) and bottom sledge.    USE - Oily sludge treatment system.    ADVANTAGE - The system has simple structure, reliability, and easy operation and is convenient to move.    DETAILED DESCRIPTION - Oily sludge treatment system comprises sludge tank (1), sludge conveying pump (2), stabilizing tank (3) provided with stirrer, first measuring pump (4), destabilization tank (5) provided with stirrer, connecting tube (6), first flocculation tank (7) provided with stirrer, second metering pump (8), second flocculation tank (9), outlet tube (10), belt-type filtering device (11), screw conveying pump (12), water collector (13), water tank (14), mixed coal device (15) for producing coal cluster, coal powder conveying device (16) and bottom sledge. The sludge conveying pump is connected with sludge tank and destabilization tank.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of oily sludge treatment system.    Sludge tank (1)    Sludge conveying pump (2)    Stabilizing tank (3)    First measuring pump (4)    Destabilization tank (5)    Connecting tube (6)    First flocculation tank (7)    Second metering pump (8)    Second flocculation tank (9)    Outlet tube (10)    Belt-type filtering device (11)    Screw conveying pump (12)    Water collector (13)    Water tank (14)    Mixed coal device (15)    Coal powder conveying device (16)
NOVELTY - Fermenting animal manure involves mixing animal manure, fermenting enzymes, deodorizing agent, rice hull powder, corn straw powder or sawdust and water to obtain a solution. The solution is sprayed on bed of animal manure for fermentation.    USE - Method for fermenting animal manure (claimed).    ADVANTAGE - The method enables to ferment animal manure that removes fecal odor and decomposes waste matter.
NOVELTY - Processing organic waste involves placing garbage bins on automatic lifting feeding machine device using touch screen controlled parameters to control input and start program, where trash is raised by starting feeding motors. Garbage bin is opened in disposal machine fermentation tank by inlet hydraulic rod. Sensor sends stop signal to controller, trash and garbage for stopping feed input into the fermentation tank. Trash is returned to original position by sending stop signal. Agitator is started to rotate waste matter, where temperature of fermentation is controlled by temperature sensor.    USE - Method for processing organic waste (claimed).    ADVANTAGE - The method enables to process organic waste in a simple, efficient, rapid and controlled manner.
NOVELTY - Liquid fertilizer comprises (in wt.%): biogass slurry (90), microbial strain (5), red sugar and molasses (5), fermenting agent and stabilizer (0.125) and compounds containing nitrogen, phosphorus, potassium, sulfur, calcium, magnesium, iron, zinc, copper or other microelements (1-2).    USE - Liquid fertilizer used for regulating plant nutrition.    ADVANTAGE - The liquid fertilizer improves soil condition.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing liquid fertilizer, which involves fermenting raw material in a sealed fermenter at 25-36 degrees C, where fermented material is sampled, tested and then packed.
NOVELTY - Fertilizer composition comprises (in pts.wt.): urea (35-40), wheat bran (20-30), shrimp shell powder (20-25), Sarcandra glabra (10-12), ferrous sulfate (3-4), zinc sulfate (2-3), ammonium sulfate (1-3), borax (4-5), vanadium (3-4), carboxymethyl cellulose (1-2), spherical nano-ferroferric oxide magnetic powder (2-4), modified maize straw (5-7), chlorothalonil (2-4) and copper sulfate (1-3).    USE - Fertilizer composition used for growing crop and increasing disease-resistant ability and reducing plant diseases caused by insect pests in root of Rehmannia.    ADVANTAGE - The fertilizer composition is prepared in a cost-effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fertilizer composition, which involves:    (A) mixing shrimp shell meal, wheat bran and Sarcandra glabra, and then grinding and crushing to obtain powder;    (B) adding sucrose (2.5-3.0 wt.%) and ray fungus (0.5-1.0 wt.%) with the powder and fermenting for 10-15 days to obtain a fermentation product; and    (C) mixing the fermentation product with remaining raw material, and then drying and granulating to obtain the desired product.
NOVELTY - Preparing culture medium involves mixing putrescine (0.01-0.05 wt.%) with distilled water (60-62 wt.%) to obtain aqueous putrescine solution (10 mg/ml). Bran, cottonseed hull, rice bran and water are mixed and stirred with aqueous putrescine uniformly to obtain a mixture. The mixture is treated into a sealed cultivation bottle at 100 plus minus 5 for 1.5-2.0 hours, and then cooled to room temperature to obtain the desired product.    USE - Method for preparing culture medium used for promoting golden needle mushroom (claimed).    ADVANTAGE - The method enables to prepare culture medium in an eco-friendly and cost-effective manner, ensures quick growth of the golden needle mushroom, and has shorten production cycle. The culture medium enhances proliferation of cell division of the golden needle mushroom.
NOVELTY - Organic fertilizer comprises (in pts.wt.): aconite (10-20), Ligularia ( 5-10), Pedicularis (4-8), Euphorbia (10-15), Oxytropis (20-30), Lagochilus inebrians (2-3), Chinese Pulsatilla (5-10), Artemisia chrysanthemum stem, leaf and seed (3-8), mushroom residue (50-60), Phellodendron (10-20) and cotton seed hull (5-10). Biological active bacteria is added to the raw material. Biological active bacteria comprises Bacillus mucilaginosus, Bacillus megaterium and Bacillus subtilis.    USE - Organic fertilizer used as insect repellent (claimed).    DETAILED DESCRIPTION - Organic fertilizer comprises (in pts.wt.): aconite (10-20), Ligularia ( 5-10), Pedicularis (4-8), Euphorbia (10-15), Oxytropis (20-30), Lagochilus inebrians (2-3), Chinese Pulsatilla (5-10), Artemisia chrysanthemum stem, leaf and seed (3-8), mushroom residue (50-60), Phellodendron (10-20) and cotton seed hull (5-10). Biological active bacteria is added to the raw material. Biological active bacteria comprises Bacillus mucilaginosus, Bacillus megaterium, Bacillus subtilis, Glomus mosseae and Glomus versiforme in mass ratio of 2:2:3:1.5:2, respectively. An INDEPENDENT CLAIM is included for a method for preparing organic fertilizer, which involves:    (A) mixing aconite, Ligularia, Pedicularis, Euphorbia, Lagochilus inebrians, root of Chinese Pulsatilla, Artemisia chrysanthemum stem, leaf, seed, mushroom residue, cotton seed and rice;    (B) crushing the obtained material using a crusher;    (C) adding tap water to the crushed material;    (D) mixing the obtained material in a microwave at 120-140 degrees C for 30-60 minutes, where the frequency of electromagnetic wave is 300 megahertz -300 gigahertz;    (E) adding biological active bacteria composition to the obtained material;    (F) fermenting the obtained material;    (G) cooling the obtained material;    (H) sieving the obtained material; and    (I) granulating the obtained material to obtain the desired product.
NOVELTY - Soil repairing agent comprises (in pts.wt.): Louis Pasteur Bacillus spore powder (0.01-3), phosphor gypsum powder (5-50), organic compost (10-60), grass carbon powder (5-50), potassium humate powder (1.5-5), powder carrier (0.2-0.5) and glycerol (0.15-1), where powder carrier is zeolite powder, white carbon black, diatomite or their mixtures.    USE - Soil repairing agent used for accelerating passivation of heavy metal and stimulating the growth of crops (claimed).    ADVANTAGE - The soil repairing agent enhances immunity of crop.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing soil repairing agent, which involves:    (A) weighing raw material;    (B) mixing phosphor-gypsum powder, organic compost, grass carbon powder and yellow potassium humate powder uniformly in a disc granulator or drum pelletizer;    (C) adding water to the obtained material to obtain granule;    (D) drying the obtained granule;    (E) cooling and sieving the obtained granule;    (F) spraying glycerol to the obtained granule;    (G) mixing Louis Pasteur Bacillus spore powder and powder carrier uniformly in a mixer;    (H) coating the obtained granule; and    (I) packing the obtained granule to obtain the desired product.
NOVELTY - Preparation of fenofibrate involves using 4-hydroxy-4'-chloro-benzophenone, acetone and sodium hydroxide as inorganic alkali.    USE - Preparation of fenofibrate (claimed).    ADVANTAGE - The method enables economical and environmentally-friendly preparation of fenofibrate, with reduced generation of waste.
NOVELTY - Extraction of catalpol involves processing fresh Rehmannia with water, adding methanol, stirring, filtering, extracting with methanol, concentrating, adding ethanol, stirring, decanting, concentrating in absence of alcohol, filtering, extracting with n-butanol, distilling under reduced pressure, and recrystallizing.    USE - Extraction of catalpol (claimed).    ADVANTAGE - The catalpol is economically and environmentally-friendly manufactured.
NOVELTY - Maduramicin (I) is new.    USE - New maduramicin is useful for preparing drug for preventing coccidiosis in livestock and poultry animals e.g. chicken, duck, quail, pig, cattle, sheep, horse and other livestock and poultry animals.    ADVANTAGE - Maduramicin does not cause excessive livestock and poultry poisoning.    DETAILED DESCRIPTION - Maduramicin of formula (I), is new. An INDEPENDENT CLAIM is included for preparation of high-purity maduramicin (I), which involves mixing 50 g maduramicin with 80 ml glacial acetic acid at room temperature, then adding 10 ml acetic anhydride and reacting at 5 plus minus 1 degrees C, then adding catalyst-containing glacial acetic acid solution, heating at 60-65 degrees C for 50-80 minutes, adding deionized water, filtering, and washing filter cake.
NOVELTY - The method involves performing isobutane circulation process in an isobutyl tower return tank. The isobutyl tower return tank is connected with a heat exchanger. A sulphuric acid settling tank is connected with a reactor, a compressor entrance separating tank and a refrigerating compressor. Liquid acid circulation flow is established in a refrigerant circulation pump. Ratio of pentane to hexene is about 1.1-1.5: 1. Pressure of modified reactor reaction is about 0.4-0.5 MPa. Acid circulation concentration is about 90-97 %.    USE - Sulfuric acid alkylation unit operating time shortening method for a petroleum refining technology field.    ADVANTAGE - The method enables eliminating large different butane circulation process, shortening sulfuric acid alkylated device operation time, saving a large amount of isobutane, reducing operation cost and increasing economic benefit.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a sulfuric acid alkylation unit operating time shortening method.'(Drawing includes non-English language text)'
NOVELTY - A methanol-fuel additive comprises 9900-10200 pts. wt. ethanol, 198-202 pts. wt. ethylene glycol monobutyl ether, 198-202 pts. wt. ammonium acetate, 495-505 pts. wt. linoleic acid, 247.5-252.5 pts. wt. ethylene glycol, 495-505 pts. wt. polysorbate-80, 2970-3030 pts. wt. seaweed powder, and 2970-3030 pts. wt. cinnamon tree powder.    USE - Methanol-fuel additive is used for vehicle.    ADVANTAGE - The vehicle containing the methanol-fuel additive has excellent performance characteristics, does not cause wear, reduces power and fuel consumption, and prevents damage of oil pump in vehicles.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of methanol-fuel additive, which involves mixing ethanol and polysorbate-80, reacting, adding ethylene glycol monobutyl ether, ammonium acetate, linoleic acid, ethylene glycol, seaweed powder and cinnamon tree powder, and stirring.
NOVELTY - A vehicle methanol gasoline composite additive contains 1-15 mass% sulfur corrosion inhibitor, 4-10 mass% fuel oxidation product-preventing corrosion inhibitor, 5-30 mass% fuel improver, 0.5-5 mass% dispersing agent, and 70-85 mass% latent solvent.    USE - Vehicle methanol gasoline composite additive for oil tank, oil pump, oil table, and oil pipe corrosion.    ADVANTAGE - The additive reduces combustion system abrasion, enhances anti-water layering ability of methanol gasoline, ensures reliable operation of engine and tail gas processing system, and does not produce residue.
NOVELTY - A coal-based synthetic natural gas is produced by feeding coal-based synthetic gas in sulfur-containing methanation reactor, reacting by methanation using sulfur, cooling exit gas from methanation reactor, feeding gas in fine desulfurization reactor, reacting until sulfur content of gas is less than or equal to 20 ppb, feeding exit gas from desulfurization reactor to depth methanation reactor, reacting until carbon monoxide volume content is 10 ppm to obtain methane-rich gas, decarburizing methane-rich gas to obtain liquefied natural gas, and removing carbon and carbon dioxide in coal-based synthetic natural gas.    USE - Production process of coal-based synthetic natural gas (claimed).    ADVANTAGE - The process maximizes methanation and conversion reaction and has simple operation, low investment, and high resource application rate.    DETAILED DESCRIPTION - A coal-based synthetic natural gas is produced by feeding coal-based synthetic gas in sulfur-containing methanation reactor, reacting by methanation using sulfur in which volume ratio hydrogen of coal-based synthetic gas:carbon monoxide is 0.2-1.6, cooling exit gas from methanation reactor, feeding gas in fine desulfurization reactor, reacting until sulfur content of gas is less than or equal to 20 ppb, feeding exit gas from desulfurization reactor to depth methanation reactor, reacting until carbon monoxide volume content is 10 ppm to obtain methane-rich gas, decarburizing methane-rich gas to obtain liquefied natural gas, and removing carbon and carbon dioxide in coal-based synthetic natural gas produced during methanation.    DESCRIPTION OF DRAWING(S) - The drawing shows a process flow diagram of production process of coal-based synthetic natural gas. (Drawing includes non-English language text).
NOVELTY - The device has an air inlet tube whose one end is connected with marsh gas tank and other end is installed on machine. A valve is installed on air inlet tube. One end of air outlet tube is connected with desulfurizer and other end is connected with dehydration purifying device (9). A marsh gas channel control probe (6) is located between dehydration purifying device and air outlet tube.    USE - Biogas purification device used in manufacture of glass handicraft article.    ADVANTAGE - The biogas purification device has high safety and reliability.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biogas purification device.    Automatic control center (1)    Digester (3)    Intake manifold (4)    Marsh gas channel control probe (6)    Dehydration purifying device (9)
NOVELTY - Preparation of clean environmentally-friendly straw coal involves mixing wheat straw grains having length of 1-3 mm and corn stalk grains having length of 1-3 mm in ratio of 3:5, pressing mixture into blocks, uniformly mixing straw block, slime and fine washed coal, gangue, additive, binder and water in ratio of 20:30:25:22:1:2, controlling moisture content to 18-20%, maintaining for 5-8 days, stirring at room temperature, molding, forming multilayered molded product, drying for 1.5-2 hours and refining.    USE - Preparation of clean environmentally-friendly straw coal (claimed).    ADVANTAGE - The clean straw coal is efficiently prepared with improved thermal efficiency and combustibility, without affecting the environment.    DETAILED DESCRIPTION - Preparation of clean environmentally-friendly straw coal involves mixing wheat straw grains having length of 1-3 mm and corn stalk grains having length of 1-3 mm in ratio of 3:5, pressing mixture into blocks, uniformly mixing straw block, slime and fine washed coal containing 80% or more particles with size of less than 3 mm, gangue, additive, binder and water in ratio of 20:30:25:22:1:2, controlling moisture content to 18-20%, maintaining for 5-8 days, stirring at room temperature, molding, forming multilayered molded product, drying for 1.5-2 hours and refining into industrial-type straw coal and civil-type straw coal with respective dimensions of 10 cmx 7 cmx 5 cm and 8 cmx 5 cmx 3 cm.
NOVELTY - Heynigia riparia SX01 strain that has preservation number CCTCC M2013610, and is new.    USE - Heynigia riparia SX01 strain used in biomass energy field and production of biological diesel oil.    ADVANTAGE - The Heynigia riparia SX01 strain is cost-effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing Heynigia riparia SX01 strain, which involves:    (A) culturing Heynigia riparia in a blue green 11 liquid culture medium;    (B) fermenting the mixture at 10-45 degrees C;    (C) adding glucose (40g/l) in the fermented mixture; and    (D) culturing the mixture for 5-15 days to obtain desired product.
NOVELTY - A Chlorella sorokiniana strain (GS03) (CCTCCM2013607) is new.    USE - As Chlorella sorokiniana strain used in biomass energy field; for conversion of carbon dioxide and production of bio-diesel (claimed).    ADVANTAGE - Compared with the reported microalgae, the algae strain has higher tolerance to carbon dioxide, high conversion efficiency for carbon dioxide, high biological yield rate and oil yield. So microalgae oil can greatly reduce the production cost of bio-diesel, and has great application prospects in the field of biological energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fermentation of Chlorella sorokiniana strain (GS03) and carbon dioxide (CO2) fixation method involving: 1) preparation of seed solution: under sterile conditions, culturing Chlorella sorokiniana GS03 single microalgae in a sterilized bG-11 broth culture medium under logarithmic growth phase, to obtain a micro-algae seed liquid; and 2) biological fermentation: inoculating the microalgae seed solution into sterilized BG11 culture medium under logarithmic growth phase, where the culture temperature is 10-45 degrees C, pH value of the culture medium is 4-11, the illumination intensity is 2500-150001 ux, light-dark ratio is 8-24: 16-0, culture processing in the sterile air, ventilation quantity is 0.2-1 vvm, CO2 content is 0.03-30 vol./vol.%, culturing for 10-14 days, and after culture, obtaining Chlorella sorokiniana GS03 fermentation liquid.
NOVELTY - Desmodesmus communes (GS05), comprising a preservation number CCTCC M2013609, is new.    USE - The Desmodesmus communes strain is useful for biomass energy production, preferably biodiesel oil and sewage treatment (claimed) and combined deep industrial flue gas emissions and municipal waste water purification.    ADVANTAGE - The strain is capable of fixing 0.03-30% carbon dioxide with carbon dioxide fixation efficiency of 90-370 mg/l/day, biomass (dry weight) concentration of 700-3800 mg/l, oil content of 20-43%, and oil fatty acid composition, preferably C16 and C18 short chain fatty acids; and has wastewater nitrogen and phosphorus removal rate of more than 95%.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for: (1) fermenting and fixing Desmodesmus communes (GS05), comprising (a) preparation of seed liquid by picking single colony of Desmodesmus communes under sterile conditions, inoculating into sterilized blue-green (BG)-11 liquid culture medium, culturing to logarithm growth period to obtain microalgae seed liquid, (b) inoculating the log phase culture of microalgae seed liquid into sterilized BG-11 liquid culture medium of pH 4-11, culturing at 10-45 degrees C at an illumination intensity of 2500-15000 lux, light-dark ratio of 8-24:16-0, culturing under sterile air with ventilation quantity of 0.2-1 vvm, where carbon dioxide content is 0.03-30 vol./vol.%, culturing for 10-14 days, and harvesting Desmodesmus communes fermentation broth; and (2) fermentative synthesis of biodiesel oil using Desmodesmus communes, comprising (i) preparing fermentation broth as aforementioned, (ii) carrying out solid-liquid separation, collecting microalgae to obtain algae slurry, (iii) drying the sludge to obtain algae powder, and (iv) taking algae powder to prepare fatty acid methyl ester using boron trifluoride catalysis.
NOVELTY - Sludge fermentation process by using redox mediator involves adding sewage to the sewage treatment plant, and then dehydrating the obtained residual sludge. The obtained material is transferred to the anaerobic fermenting tank. Redox mediator is added in alkaline water solution, where pH of alkaline water solution is 10-12. The residual sludge is stirred for 1-6 hours, and then redox mediator solution is added to the obtained material. The obtained material is performed for anaerobic fermentation with at 15-35 degrees C.    USE - Method for sludge fermentation process (claimed).    ADVANTAGE - The method enables to perform sludge fermentation process in fast and efficient manner.    DETAILED DESCRIPTION - Sludge fermentation process by using redox mediator involves adding sewage to the sewage treatment plant, and then dehydrating the obtained residual sludge. The obtained material is transferred to the anaerobic fermenting tank. Redox mediator is added in alkaline water solution, where pH of alkaline water solution is 10-12. The residual sludge is stirred for 1-6 hours, and then redox mediator solution is added to the obtained material. The obtained material is performed for anaerobic fermentation with at 15-35 degrees C. Phosphate buffering liquid, sodium bicarbonate buffering liquid or alkaline solution is added to the obtained material for regulating pH value to 6.0-12.
NOVELTY - Catalyst comprises amorphous nickel-boron with atomic ratio of 1-5.    USE - The catalyst is used for electrically decomposing water for hydrogen (claimed).    ADVANTAGE - The catalyst has low electric potential, high catalytic efficiency, stable property, and low cost; is prepared by simple process, and replaces the noble metal platinum catalyst.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing catalyst, comprising loading the amorphous nickel-boron on the carrier surface using chemical plating method, and feeding chemical plating liquid containing nickel-boron with atomic ratio of 3-10.
NOVELTY - This utility new type of a one in a waste water recovery device of garlicin, comprise inner tank body, reaction of reaction cavity inner cavity with a water solution and organic solvent, a tank body set with a liquid inlet tube and a liquid outlet tube, wherein the bottom of tank body set with an air inlet tube, an air inlet tube for introducing in the reaction cavity liquid fully mix of gas, the top part of tank body set with a discharge tube, the top part of tank body set with a pumping device, pumping device comprise pump, a turbine, a worm and a turbine motor, a worm into organic solvent in a reaction chamber in the inner of worm is the liquid chamber, an inlet through a drainage tube with the liquid cavity connected. This utility new type of device, the tank body of the top part and lower part set with a liquid inlet tube and a liquid outlet tube, reaction cavity of tank body in a organic solvent, making liquid inlet tube by entering into a production waste water of allicin in a effectively in the organic solvent, a removing processing enterprise wastewater in garlic allicin and a secondary.
NOVELTY - This utility new type claims a taking water sample and one of aritificial wetland. Include a bed, bed body inside in turn set with the water gathering ground water, sewage treatment area, a water outlet water gathering ground. Inlet water gathering ground by water, a water inlet baffle plate is composed of a sewage treatment area by , filling layer, water taking tube, a liquid plate, the right side is the water outlet baffle water gathering ground. Working time, sewage flows into the water inlet water gathering ground, after , and then is left by the water baffle plate lower end of gap entering into sewage treatment area, in the sewage treatment area, the sewage , filling layer, water taking tube, plant root processing, a guide plate, a water taking tube distribute uniformity with a small time taking water so that the cross section of a uniformity of sewage flows out from the water taking tube, it can obtain a surface water, light filler layer water, filling deep water layer, water layer, at last, sewage by outlet baffle. This utility new type water taking is convenient, collect a water sample has representativeness, scientific research aritificial wetland technology provide a great convenience.
NOVELTY - This utility new type relates to a one aeration biological filter tank, filter tank comprise main body, a water inlet tube, a water tube and the aeration tube, lower part of the filter pool main body extending downwards form a support cavity, the water inlet tube and the aeration tube are set on the cavity inner support, and a lower part of a support cavity is further set with a biological film exit, in addition, the inner filter tank body is also set with the multi-layer filter material, the said of the water tube is set on the upper part of filter tank main body one end. This utility new type using lower upwards by a water inlet, such that processing of sewage can be valid contact with the filter material, the treatment effect, and the flushing water tube a, a is a valid change for biological film of flushing, enhance organic matter removing effect, and it can realize valid dephosphorization and the purpose of nitrogen, and the multilayer filter material of set, then realize the layer growth but for different biological flora of the layer material, which is good for microorganism of value-added, metabolism, it is helpful to the degradation and removal of organic pollutant.
NOVELTY - Biological organic fertilizer fermenting tank. The current of the fermentation tank is simple structure, naturally or by the sunshine for a long, uniform heating, reduces the biological organic fertilizer of production speed and production capacity, which seriously influences the development of the enterprise. A one biological organic fertilizer fermenting tank, the comprise of the leg (1) is provided with a heat insulating shell, the insulating shell connecting heat preservation, heat insulating feeder connecting the heat preservation cover, the heat preservation connecting shell (2), the inner heat preservation shell is equipped with heating device, the heat preservation shell inner connecting a device, the heat preservation shell connecting one group turning stir device. This utility new type used for biological organic fertilizer fermenting.
NOVELTY - This utility new type claims a one continuous fowl dejecta fermentation box comprise box body and tile, said box body is divided into a plurality of fermentation chamber, a feeding car through the live stock excrement conveying slide way to the top layer of fermentation chamber, further set with a rotating plate of the said each upper clapboard a, the fermentation tank is divided into a multi-fermentation chamber, a continuously to ferment, a rear excrement fermentation and to a lower layer to continue the fermentation and shortens fermentation period, increase the fermentation efficiency, device structure is simple and practical, and the cost is low.
NOVELTY - This utility new type relates to a sludge compost one experiment device, include fermentation groove, peripheral side wall of ferment groove using foam heated board as side plate, inner fermentation groove of a floor along the lengthways is uniformly distributed with multiple cloth pneuma, fermentation groove an inner space is divided into several gas distribution, each inner grid partition has a pneuma channel of the same number, each distributing a middle is equipped with partition for pneuma branch tube, a gas supplying branch tube and a cloth pneuma channel at the intersection set with four pipeline, an air supply branch tube comprise cloth pneuma cross tube and gas distribution, several inner partition of the pneuma distributing branch tube along the fermentation groove two side pool wall out fermentation groove, a is connected with the ferment groove two side of the pneuma, the pneuma header pipe is connected with the fermentation groove side of several centrifugal air blower. This utility new type in complete fermentation groove oxygen charging cloth pneuma of arrangement the distributing area, the whole aerobic fermentation stack charging uniformity.
NOVELTY - This utility new type bottom relates to biomass fuel gasification field, especially relates to a biomass fuel gasification production line one with gasification furnace, comprise a furnace body, a furnace body upper end and lower end a closeness set with furnace cover and furnace, a furnace upper cover set with a feeding port, a furnace body set on the inner edge of the inner wall of said furnace body is a match , a cavity from the inner part of said furnace body is a fuel cavity and is located on the upper part of lower part of ash, ash corresponding to a body of a side wall set with a first air outlet. The use time, the biomass fuel is placed in furnace body of the gasification furnace inner, the barrier, the fuel of inner cavity is not to completely combust the fuel produce a combustion gas, the combustible gas from the first air outlet.
NOVELTY - This utility new type belongs to machinery technology field, relating to a biological fuel a one machine, in particular a one collector collecting raw material and processing as a whole biological fuel of a machine. A molding mechanism include one discharge bucket, one turntable and a multi-inner pressure roller, a feeding channel and the discharging bucket connected, a discharge bucket a uniform is provided with a multi-hole molding, said turntable is in the inner bucket, the discharging plate and the discharging bucket wall is the same as the diameter of said turntable is in the discharging bucket bottom of the inner pressing roller fixed on a turntable, a multi-inner pressure roller along rotating-disk circle uniform set, a multi-inner pressure roller edge are connected with the material bucket inner wall. Especially through a feeding mechanism and feeding mechanism feeding raw material. This utility new type has simple operation, it is suitable for production, of a different working intensity is low, the safety coefficient high time in operation.
NOVELTY - This utility new type claims a one photo-thermal constant-temperature methane producing pneuma device, comprise the marsh gas tank, bottle, water, light gathering heat collector, an oil tank, a PLC controller, wherein the marsh gas tank set with an annular tube, oil tank exit tube is equipped with a light gathering heat collector, the heat collector of light oil tank exit tube by valve I a and access in a marsh gas tank upper annular tube entrance, oil tank of the other one strip exit tube through valve II is connected with the annular tube entrance in a marsh gas tank connect, a ring tube exit and the pond in connecting marsh gas tank, marsh gas tank and connecting bottle, a bottle set with valve opening, lower part is connected with water collecting bottle, a position higher than the water bottle, valve I and valve II a connect with the PLC controller, the device makes full use of solar energy constant temperature marsh gas pool, the structure is simple, the use is convenient, energy-saving and environment-friendly.
NOVELTY - A briquetting one combustion gasification heating furnace, the furnace body lower end one side set with water inlet, and the water inlet of relative one side upper end set with water outlet, the furnace body lower end set with grate, grate is combustion room, combustion chamber left and right two side set with a lower air inlet channel, the combustion room is set with gasification room, a gasification room and set on one side of the pneuma valve is connected, the air inlet valve mounting inlet; the top of the furnace body set with flame heating area, the upper part, a gasification room and flame heating area flame heating area located on the gasification room of through air inlet hole connected with the flame heating area and the water outlet and set with exhaust port. This utility new type can increase utilization rate of straw combustion, at the same time, increase heat value of flame, enhance heating efficiency of heating furnace, and reduces the discharge of the harmful substance content in gas, protect the environment and save energy.
NOVELTY - The device has gasification furnace portion (1) whose top surface is set with material inlet, and bottom is set with slag outlet. The slag outlet is connected with feeding mechanism (5), and material inlet is connected with lifting reducing cabin door control mechanism (4) set on feeding mechanism. A linkage material level meter (3) is set on top surface of gasification furnace portion. A rotary grate portion (2) is set at bottom of gasification furnace portion. A dust-removing system is connected with coke gasification furnace.    USE - Biomass fuel gas formation device.    ADVANTAGE - The design of the biomass fuel gas formation device is smart and rational, and the device is realized easily. The manufacturing cost of the device is reduced. The structure of the device is reasonable. Since the fuel is fully burned, the gasification efficiency of the device is increased. Hence the energy utilization rate of the device is greatly increased, and the resource is saved. The working stability of the device is good. The adaptability of the device is good. The popularization and application of the device are good.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the biomass fuel gas formation device.    Gasification furnace portion (1)    Rotary grate portion (2)    Linkage material level meter (3)    Lifting reducing cabin door control mechanism (4)    Feeding mechanism (5)
NOVELTY - Waste crop straw resource type integrated environmentally friendly carbon production process comprises e.g. collecting waste straw type resource in agricultural production, corn straw, wheat straw, cotton straw or bean straw, crushing, adding bonding agent, adding saw dust and bamboo, placing in a stirring device, heating, stirring, analyzing water content, adding water content qualified straw powder into a bar molding extruder, carrying out extrusion molding process, ensuring the heating temperature of rod, obtaining carbon rods of standard size, and naturally cooling.    USE - The method is useful for waste crop straw resource type integrated environmentally friendly carbon production process (claimed).    DETAILED DESCRIPTION - Waste crop straw resource type integrated environmentally friendly carbon production process, comprises (i) collecting waste straw type resource in agricultural production as main material, corn straw, wheat straw, cotton straw or bean straw, crushing the straw into 80-100 meshes, (ii) adding bonding agent in the straw, at the same time, adding part of saw dust, and bamboo, then placing in a stirring device and stirring, (iii) heating in a stirring device in the stirring process, stirring while heating, so that the powder can mix together, controlling the heating temperature at 50-60 degrees C, heating at 30-60 degrees C, (iv) analyzing water content after mixing material, where the water content of material is 15-20%, drying high water content material, adding water in low water content material, then mixing, (v) adding the water content qualified straw powder into a bar molding extruder and carrying out extrusion molding process, ensuring the heating temperature of rod inside the molding press to not less than 200 degrees C, obtaining carbon rods of standard size, and (vi) naturally cooling the obtained carbon rod to normal temperature to obtain the product.
NOVELTY - A dense biomass fuel comprises 50-80 pts. wt. wheat straw, 35-45 pts. wt. corn cob, 20-30 pts. wt. pine needle, 10-15 pts. wt. sawdust, 5-10 pts. wt. traditional Chinese medicine slag, 8-14 pts. wt. fish powder, 12-18 pts. wt. palm shell, 5-10 pts. wt. tea seed cake, 7-14 pts. wt. soybean oil, 6-12 pts. wt. bone powder, 10-15 pts. wt. coconut husk, and 15-20 pts. wt. peanut shell.    USE - A dense biomass fuel.    ADVANTAGE - The fuel has an increased heating value, is smokeless and environment-friendly, has a combustion rate of more than 98%, and is inexpensive.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the dense biomass fuel, comprising uniformly mixing wheat straw, corn cob, pine needle, sawdust, traditional Chinese medicine slag, fish powder, palm shell, tea seed cake, soybean oil, bone powder, coconut husk, and peanut shell; naturally drying at room temperature until the moisture content is 5-10%; compression molding; naturally cooling to room temperature; and packing.
NOVELTY - Water washing treatment of chloride furnace slag is performed by washing chloride furnace slag with water to dissolve chloride ions in water and removing.    USE - Water washing treatment of chloride furnace slag for preparing chlorine, hydrogen, caustic soda (all claimed), and titanium tetrachloride (TiCl4).    ADVANTAGE - Water washing treatment of chloride furnace slag is low-cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for use of chlorinated slag treatment liquid which involves precipitating calcium ion (Ca2+), magnesium ion (Mg2+), sulfate ion (SO42-), iron(III) ion (Fe3+), and other heavy metal ions in chloride-ion-containing water, filtering to remove precipitates and insoluble impurities to obtain electrolyte solution, and performing electrolysis to produce chlorine gas, hydrogen gas, and caustic soda solution.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart for the water washing treatment of chloride furnace slag. (Drawing includes non-English language text).
NOVELTY - In oil wellhead a liquid gas concentration on-line detection device, include gas sense detection unit, gas sense detecting unit through a communication with the metering station monitoring module connecting the gas sense detecting unit set in a normal oil opening of a well for a liquid containing oxygen and natural gas by a gas concentration process in real time monitoring, communication module through the gas concentration information conveying to metering station monitoring module in. This utility new type can real time online detection in oil extraction well a liquid a containing oxygen and natural gas of gas concentration, and the data process, the a to b to each of a standard signal through wired or wireless transmission device to a monitoring module in a report form, at the same time, sending alarm signal, is of safety and data management in a process oil supply the technology based on a furthest ensures safety production of oil extraction process.
NOVELTY - Mushroom cultivation method comprises alternate drying pear branches, wheat bran or rice bran without plant diseases and insect pests with special fertilizer, where the diameter of the branch is 0.8-1 cm. The special fertilizer is nitrogen-containing special edible fertilizer.    USE - Mushroom cultivation method (claimed).
NOVELTY - Cow cultivation method includes padding in the fermented cattle shed using a fermentation padding to the manufacturing process of a cushion material, padding and stirring; piling into trapezoid, sprinkling and continuously stirring the water holding padding cloth insulating sack, fermenting, stacking and covering; and fermenting, laying a paving on the inner column, mixing rice husk and sawdust, covering upper surface, leveling, waiting, and mixing the cattle excrement in a pad layer.    USE - Cow cultivation method (claimed).    ADVANTAGE - The method has real zero exhaust and zero pollution.    DETAILED DESCRIPTION - Cow cultivation method comprises:    (A) padding in the fermented cattle shed using a fermentation padding to the manufacturing process of a cushion material, where the fermentation padding comprises 20 pts. wt. chaff, 55 pts. wt. sawdust, 4 pts. wt. rice bran, corn straw or peanut peel powder, 20 pts. wt. microbial inoculum, and 0.5-1 pts. wt. paving cushion, padding and stirring;    (B) piling into trapezoid, sprinkling in the stacking and continuously stirring the water holding padding cloth insulating sack, 45-50% fermenting, stacking and covering; and    (C) fermenting for 4-10 days, using fermented pad, laying a paving on the inner column, mixing 10 pts wt. rice husk and 10 pts. wt. sawdust, covering upper surface, leveling to a thickness of 10 cm, waiting for 24 hours at inlet, automatic adjusting the humidity and temperature of fermented material of cattle shedding, and mixing the cattle excrement in a pad layer.
NOVELTY - Complex microorganism phosphate-solubilizing microbial inoculum comprises Pseudomonas veronii, Rahnella aquatilis and Bacillus megaterium, respectively having a preservation number CGMCC NO.8741, CGMCC NO.8739 and CGMCC NO.8737.    USE - The microbial inoculum is useful in increasing crop yield after being mixed with nitrogenous fertilizer, phosphate fertilizer and/or potash fertilizer (claimed), preferably increasing yield of wheat and rape.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the inoculum, comprising (a) inoculating Pseudomonas veronii and Rahnella aquatilis into inorganic phosphorus liquid culture medium, culturing at 28-30 degrees C at a rotating speed of 180 revolutions/minute for 48 hours, (b) inoculating Bacillus megaterium into organic phosphorus liquid culture medium, culturing at 28-30 degrees C at a rotating speed of 180 revolutions/minute for 96 hours, and (c) mixing the resulting fermented microbial inoculum with an additive, mixing uniformly, drying and packaging to obtain the finished product.
NOVELTY - A Lysinibacillus fusiformis strain (CGMCC NO: 8835), is new.    USE - The L.fusiformis strain is useful in preparation of phosphate fertilizer (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) microbial inoculum comprising bacteria and culture medium, where the bacteria are L.fusiformis; and (2) use of L.fusiformis, in preparation of microbial fertilizers.
NOVELTY - A layered molecular sieve adsorbent contains 30-90 pts. wt. Mobil Crystalline Material (MCM)-49 molecular sieve and/or MCM-22 molecular sieve and balance oxide binder.    USE - Layered molecular sieve adsorbent for low-pressure methane adsorption (claimed).    ADVANTAGE - Layered molecular sieve adsorbent has excellent molecular diffusion performance, high adsorption rate, and good adsorption-desorption performance. Preparation process is simple and has low production cost.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparation of layered molecular sieve adsorbent which involves mixing Mobil Crystalline Material (MCM)-49 molecular sieve and/or MCM-22 molecular sieve and oxide binder, adding polymer compound porogen, mixing, adding diluted nitric acid, mixing, performing extrusion molding, and calcining at 400-600 degrees C; and    (2) layered molecular sieve adsorbent used for low-pressure methane adsorption.
NOVELTY - High storage density methane adsorbed metal organic framework material comprises 50-80 pts. wt. naphthalene carboxylic acid organic ligand and 20-50 pts. wt. trivalent metal cation.    USE - High storage density methane adsorbed metal organic framework material.    ADVANTAGE - The material has pore size of 1-2 nm, specific surface area of not less than 2000 m2/g, methane adsorption of 190-210 V/V at 3.5 MPa and 25 degrees C.
NOVELTY - A molten iron catalyst comprises ferroferric oxide, where ratio of ferrous ion to ferric ion is 0.45-0.60.    USE - Molten iron catalyst used for synthesizing industrial ammonia (claimed).    ADVANTAGE - The method improves resource utilization, reduces gas mud (ash) waste, and reduces environmental pollution problems. The molten iron catalyst meets industry standards, in line with China's recycling economy, energy conservation, and economic development policies.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of molten iron catalyst comprising using steel industry waste gas mud (ash) as raw material and adding accelerator and promoter, where promoter is alumina and potassium hydroxide.
NOVELTY - Converter mud molten iron catalyst comprises ferroso ferric oxide. The bivalent iron and trivalent iron specific value of the catalyst is 0.45-0.60.    USE - The converter mud molten iron catalyst is useful for synthesizing industrial ammonia (claimed).    ADVANTAGE - The method reduces the sintering production cost, and improves the production environment for the enterprise to create good economic benefit and environmental benefit.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM also included for preparing the catalyst, comprising taking converter sludge as raw materials, and adding accelerant, where the accelerant is alumina and potassium hydroxide.
NOVELTY - Catalyst comprising ferrous oxide and ferric oxide with a ratio of 0.45-0.60, is new.    USE - The catalyst is useful for preparing industrial synthesis of ammonia (claimed).    ADVANTAGE - The catalyst is capable of preparing ammonia with less energy consumption and without emission in an economical manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of the catalyst.
NOVELTY - A molten iron catalyst comprises ferric oxide as main chemical component, where ratio of ferrous ion to ferric ion is 0.45-0.60.    USE - Molten iron catalyst used for synthesizing industrial ammonia (claimed).    ADVANTAGE - The method improves recovery efficiency and reduces blast furnace dust ash. The molten iron catalyst meets industry standards, in line with China's recycling economy, energy conservation policy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of molten iron catalyst comprising using blast furnace dust ash waste from iron and steel industry as raw material and adding accelerator and promoter, where promoter is cobalt oxide, alumina and potassium hydroxide.
NOVELTY - Fused iron catalyst with iron sludge comprises ferrous ferric oxide as main chemical component, where R is divalent iron (Fe2+)/trivalent iron (Fe3+) is 0.45-0.60.    USE - The fused iron catalyst is useful for industrial preparation of synthetic ammonia (claimed).    ADVANTAGE - The catalyst: improves the recovery efficiency; reduces recovery cost; opens up the quantization reduction of iron sludge. The method: eliminates the problems of environmental pollution; achieves the industrial standards; saves energy; and reduces emission.
NOVELTY - A high temperature methanation catalyst preparation comprises magnesium oxide-alumina (MgO-Al2O3) spinel catalyst carrier or MgO-Al2O3 spinel catalyst carrier and titanium oxide (TiO2) composite inorganic oxide carrier, active component of nickel in the form of nickel oxide, and additive of lanthanum oxide and/or cerium(IV) oxide (La2O3 and/or CeO2).    USE - High temperature methanation catalyst used for reacting carbon monoxide and carbon hydroxide with hydrogen gas to produce methane (claimed).    ADVANTAGE - The catalyst is stable at high temperature and has high catalytic activity at low temperature and low energy consumption and cost.    DETAILED DESCRIPTION - A high temperature methanation catalyst comprises magnesium oxide-alumina (MgO-Al2O3) spinel catalyst carrier or MgO-Al2O3 spinel catalyst carrier and titanium oxide (TiO2) composite inorganic oxide carrier, active component of nickel in the form of nickel oxide, and additive of lanthanum oxide and/or cerium(IV) oxide. The catalyst is prepared by:    (A) mixing magnesium oxide or magnesium hydroxide and alumina hydrate (2Al2O3-nH2O) or magnesium or aluminum and mixing as first dry powder material MgO-Al2O3 spinel or mixing MgO-Al2O3 spinel and TiO2 or metatitanic acid and mixing as second dry powder material MgO-Al2O3 and TiO2 spinel inorganic oxide composite carrier; and adding first or second dry powder material to lanthanum and/or cerium in aqueous soluble salt solution, peptizer, and 45-65% water, mixing, drying at 480-600 degrees C, calcining, and crushing;    (B) adding soluble nickel salt and powder, mixing, drying, roasting, grinding, adding additive, peptizer, and 30-36 wt.% water, kneading, molding, drying, and roasting;    (C) adding soluble nickel stable solution and soaking; and    (D) drying and calcining, where mass ratio of nickel in second step to nickel in third step is 1:5-5:1.
NOVELTY - An excess hydrogen microbubble preparation device comprises water container (1) equipped with water inlet (5), water outlet (6), cathode electrode (2), anode electrode (3), and water-permeable film (4) between electrodes. The area at the side of water-permeable film containing the anode electrode and cathode electrode is smaller than the opposite side of water-permeable film containing the electrodes. Water-permeable film has thickness less than or equal to 5 mm.    USE - An excess hydrogen microbubble preparation device (claimed).    ADVANTAGE - The device generates a large amount of ultrafine hydrogen microbubbles simultaneously with oxygen production.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of an excess hydrogen microbubble preparation device.    Water container (1)    Cathode electrode (2)    Anode electrode (3)    Water-permeable film (4)    Water inlet (5)    Water outlet (6)
NOVELTY - A cement grinding aid comprises 3-8 wt.% lignosulfonate.    USE - Cement grinding aid.    ADVANTAGE - The cement grinding aid can be prepared with convenient processing operation without causing secondary pollution to the environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the cement grinding aid using papermaking waste acidic red liquid, comprising:    (A) depositing papermaking waste liquid sludge;    (B) entering liquid into an anaerobic fermentor for fermentation process;    (C) filtering the fermentation liquid to obtain lignin salt solid and filtrate comprising lignin salt;    (D) drying the lignin salt to obtain the finished product; and    (E) heating the filtrate to 60-65 degrees C and stirring to obtain the finished product.
NOVELTY - This utility new type belongs to environmental protection technology field, claims an organic sewage biological integrated processing device, comprise in turn pipeline connecting a lattice well, a sedimentation tank, a first filter tank, a microorganism reaction tank and second filter tank, the bottom of the sedimentation tank filling material is river sand of 50 cm thickness, the under-fill of first filter tank is divided into three layer, by lower to upper in turn is concavo-convex rod soil layer, diatomaceous earth layer and between the upper active carbon layer, a sedimentation tank and filter tank of first pipeline set with valve, between the first filter pool and microorganism reaction tank set with a pH value detecting a, upper end of said dust reaction tank is set with a feeding port, a second filter pool of the under-fill by lower to upper in turn is amide and macro-porous resin layer inner layer positive ion polymer middle set with water exit pipeline, a pipeline set with a plate frame filter, used for collecting microorganism and fermentation product to prepare a fertilizer.
NOVELTY - This utility new type belongs to the sewage treatment system technology field, specific relates to a sewage processing system one. This utility new type solves the problem that the existing integrated module exist planting cultivation animal produce of waste water and waste residue difficult to treat and reasonable use of technology. This utility new type number include a marsh gas tank, the marsh gas tank through the pipeline set with a lower tank body connected part, a pipeline set with pressure valve, the top part of each marsh gas tank set with a biogas pneuma chamber, one side biogas pneuma chamber set with a discharge tube at the bottom of the last one marsh gas tank set with a biogas liquid discharge port, discharge hole is connected with a biogas liquid discharge tube is set left side connect the marsh gas tank, lower end sewage feeding tube of the right side of the bottom of a first set with marsh gas pool feeding port, a sewage feeding hole and sewage connecting marsh gas tank, a sewage feeding tube upper end is connected with the one end excrement of connecting channel, waste channel is set at the back of the animal breeding area. This utility new type has a cultivation animal produce rational utilization of waste water, waste residue and the advantages of a continuously a produce marsh gas.
NOVELTY - This new type utility claims one a granulating system, include fertilizer pelleting machine, the inlet end of said fertilizer pelleting machine in turn set with semi-wet material crusher, horizontal type stirring mill and sieving machine, rear fermentation of material rear in turn by crusher, a stirrer and a machine system entering into a granulator and granulating. This utility new type system a screen front the granulation to make the material size uniformity, increase the efficiency of granulation, and the structure design of machine, it can process multi-different diameter of granule of a screening, operation is simple and convenient.
NOVELTY - This utility new type provide a one humic acid fertilizer fermenting device, comprise the cabinet body and the cabinet body set with inner horizontal direction of multiple material storage disk, a feeding unit, temperature control unit, discharge unit, a feeding unit set on the cabinet body upper end, the upper part set with the collecting material hopper, lower part set with a crusher, raw material through rear into a crusher to crush the material disk. Temperature control unit cabinet body, wherein set with heating element, adjust temperature of inner cabinet body. Discharge unit set on the cabinet body upper end face a, connecting pneuma waste collecting device or container, a storage disk a from the cabinet body inner, the bottom thereof is uniformly distributed with water leakage hole. This utility new type has the advantages of the waste cotton seed small volume, the utility model is new type crushing device in the fermentation device, reduces the device volume. It also reduces the extra cost of a purchasing device, use the transport link maintenance are obvious. More important, the utility model is a new type production efficiency is high, it can produce high economic value.
NOVELTY - A one kitchen garbage biological treatment device, it relates to garbage treatment technology field. A the first conveyor (1), a high speed centrifuge (2), a second conveyor (3), a stirrer (4) and third conveyor (5), the first conveyor (1) is arranged below the tail of set with high speed centrifuge (2), high speed centrifuge (2) one side of the lower part set with a second conveyor (3), the second conveyor (3) is arranged below the tail of set with a stirrer (4), a stirrer (4) one side of the lower part set with a spiral conveying machine (6), one side of spiral conveying machine (6) is set with a third conveyor (5). Its device, use of the space is small, the processing process is simple and has no pollution, a little energy consumption efficiency is high, a short time and the economic benefit is high, a rear product, large market demand, and use high temperature resistant bacteria in the waste treatment process, it can completely kill harmful bacteria, it is more safety.
NOVELTY - This utility new type relates to straw cracking, device technology field of purification, a gas generating device of straw cracking, purification, include cracking cavity and purifier, crack chamber on the purifier and pipeline connecting with the cracking chamber is provided with a feeding port, a feeding port having an upper cover, a cracking chamber under the air inlet tube and a slag outlet, a cracking chamber in air inlet tube with a blowing nozzle, wherein the cavity of the cracking chamber is a reversed cavity, the air inlet tube is further connected one section dreg and the other discharging tube of end cover, the blowing nozzle is upward, with amplification of opening, there is a gap between the cavity inner blowing opening and a crack chamber on the lower part, it has better effect of cracking, but also can clean residues in a discharging tube, would not block tube of slag, reduce the maintenance frequency of the cracking cabin outside and with a movable cover.
NOVELTY - This utility new type relates to clean energy, specifically to multi-plasma torch producing the oil and natural gas device, comprise: CO2 tank (1), a screw rod sense the coal (2), a O2 storage tank (15), a steam storage tank (16), a H2 storage tank (4), a CO2 deaerator (14), a multi-plasma torch the hydrogen generator (3), multi-plasma torch the oil synthesizer (6), impurity purification separator (7), a H2 microwave fractionator (8), multi-plasma torch producing a generator (18), a level CH4 a (19), the third level CH4 a (20), CH4 a cooler (21), a CH4 storage tank (23), gasoline tank (9), a diesel oil tank (10). This utility new type of beneficial effects as follows: 1, a high utilization rate, reduce a malfunction caused by a capacity reducing, can large scale production oil and natural gas, 2, production cost is reduced, device investment, saves land area, 3, can be a multi-a raw material for a refining process.
NOVELTY - This utility new type claims a biomass double-section type one pneuma, include a furnace body and a furnace body installed on the inner of the furnace inner liner, furnace inner liner in from upper to lower in turn. storage bin, a cracking room first, second cracking room) and dust hopper, a cracking room upper part and the first lower part connecting storage hopper, the lower part with the second cracking room upper end connecting the second cracking room upper part and lower first cracking room connecting part, lower part and the ash is connected upper part side edge is provided with a fuel gas exit. The utility model is new type of biomass double-section type pneuma, lower collecting suction type fixed bed and a suction type fixed bed as a whole, the advantages of each, which overcomes the disadvantages of each, which is a full-new one of fixed bed furnace.
NOVELTY - This utility new type relates to biomass fuel gasification field, especially relates to one vaporizing burner of biomass fuel production line with a secondary furnace, a furnace body, a furnace body comprise the first air outlet is covered a gasification furnace of, a first air outlet located on lower half part of said furnace body, said furnace body side wall of upper end set with a second air outlet, a second air outlet through gas pipeline and a cooling dust-removing device. Set the first side air gasification furnace, a gas from the lower end to upper end side flow, and then gas pipeline of the furnace body upper end in entering into cooling dust-removing device, the gas is a down flow of the secondary inner furnace, flow time, mix the gas in a dust impurity sedimentation inner part on the secondary furnace so as to reduce the content of dust impurity in the fuel gas.
NOVELTY - This utility new type relates to biomass fuel gasification field, especially relates to a biomass fuel gasification production line one with vacuum pump, comprise pump body, an air inlet tube and the pneuma tube, a gas inlet tube and a filter through gas pipeline, the pneuma tube with a filter device through gas pipeline, a pump body lower end set with a drain outlet, a air inlet tube set with a water inlet tube, a water inlet tube and a gas inlet tube, a water inlet tube upper end set with hopper. Because the inner gas containing tar and water steam, time when the vacuum pump is long time working, inner pump body would accumulate and tar, the tar has a viscosity, and easy to make the blade inner pump body of the adhesion and reduces the working efficiency of vacuum pump, and the time when the tar and water by multi-even would block the air inlet tube and the pneuma tube to make the vacuum pump cannot be normal working, the outlet set on the pump body lower end, inner the pump body accumulation of tar and water can be discharged, the vacuum pump can be normal working.
NOVELTY - This utility new type relates to biomass fuel gasification field, especially relates to a biomass fuel gasification production line one with cooling and dedusting device, comprise first drainage cylinder, lower end of said first drain barrel set with a drain valve, a first upper drainage barrel is vertically set with a washing tube, a washing cylinder upper end sealed and lower end and a first drain barrel, lower end side wall of said washing barrel set with a first air inlet, a first air inlet and the second air outlet side upper of the gas pipeline through connecting, a washing cylinder upper end set with a third air outlet, a third outlet is connected with filter through gas pipeline connect. Inner gas through first air inlet entering into washing cylinder, a gas flow upwards from the third air outlet entering into filter in, the gas upwards flow time, impurity in the fuel gas from a fuel gas falls in first drain barrel, through first drain barrel, reduces the content of impurity in the fuel gas.
NOVELTY - This utility new type bottom relates to biomass fuel gasification field, especially relates to a biomass fuel gasification production line, one include connecting in turn through gas pipeline of the gasification furnace, a cooling dust-removing device, filter, vacuum pump, a fine filter device and pneuma storage cabinet, a gasification furnace include furnace body, a furnace body upper end and lower end sealed set with a furnace cover and a furnace, a furnace cover set with a feeding port, a furnace body in a set with the inner wall of said furnace body is a match , the said separated internal cavity of said furnace body is a fuel cavity and is located on the upper part of lower part of ash, ash corresponding to a body of a side wall set with a first air outlet, a first air outlet through the said fuel gas pipeline and a cooling dust-removing device connect. Gas is vacuum pump pumping inner entering into gas storage cabinet, then conveying to a farmer in a each, so that user can open gas cooker can use so as to greatly convenient for the use of user.
NOVELTY - This utility new type relates to biomass fuel gasification field, especially relates to a biomass fuel gasification furnace one production line using, comprise third drain cylinder, a third upper drainage barrel are set with water , pneuma liquid separate cylinder and fine filter cylinder, a third drain barrel inner set with a second partition, a second partition the said third drainage barrel with a water corresponding to a right a drainage barrel and the pneuma liquid separate cylinder and a fine filter cartridge corresponding to a left drain cylinder, a right inner drainage barrel is equipped with cooling water. Inner gas through gas pipeline entering into right drain barrel, the gas pipeline extends into the inner cooling water, the gas entering into the over flow cooling water through water bath rear cooling water, flow channel through water bath rear gas, then entering into pneuma liquid separate cylinder, pneuma liquid separate cylinder separate fuel gas in a water gas, comprising gas entering into fine filter cylinder and a filter of pure gas, and then gas through fine filter inner rear cylinder by the gas pipeline entering into gas storage cabinet.
NOVELTY - This utility new type provide a high purity one biogas purifying device. Said high purity biogas purifying device can comprise following unit in turn fluid connected of the raw material biogas storage unit, marsh gas pressurizing unit, unit, drying unit, a decarbonising unit, natural gas pressurizing unit, unit, fixed storage unit. A filling unit can include a sequence of disk in turn fluid connected and the pneuma. A decarbonising unit include pressure swing adsorption column group, a pressure swing adsorption column group comprise first and second adsorption column adsorption column, a first adsorption column and a second adsorption column in absorbing raw material marsh gas high pressure in a low carbon dioxide, de-absorbing the carbon dioxide, so as to said carbon dioxide from said raw material gas in removing low at normal pressure.
NOVELTY - This utility new type claims a one integrated a biomass fuel molding machine, include raw material conveying device, a rotary drying furnace, a hot air drying furnace, stir mixer and machine frame, wherein the raw material conveying device connecting the rotary drying furnace, a hot air drying furnace produced by high purification air by the end of rotary drying furnace set with a heat transfer pipeline is sent to the rotary drying furnace in, stir mixer comprise stir cylinder, a feeding port, a mixture exit and stirrer, stir opening of cylinder upper part is feeding port, middle of cylinder set with stirrer stir, stir cylinder of lower part opening is mixture exit, the lower part of mixture exit set with the hopper, an exit of a mounting is connected with exit of feeding room, a feeding room of the feeding auger is connected with granulating, granulating chamber lower part set with a discharging port, and the power connecting mechanism. This utility new type constructed of a raw material biomass in a mix more uniform, this utility new type structure is simple, use is convenient, a production of a biomass as a fuel use.
NOVELTY - This utility new type relates to biomass energy production technology field, especially relates to a dewaxing device one. Include the leaching tank (2), at least part of the set with a leaching tank (2) in a pushing device (6), a leaching tank (2) one end set with a discharging port (5) and solvent entrance (11), and the other end is set with feeding port (4) and extracting liquid exit (12), wherein a solvent entrance (11) and said leaching liquid exit (12) for removing a two cerate flows through a passage of the said pushing device (6) used for the said feeding port (4) is sent to a leaching tank (2) of the material by a discharge hole (5), and it further comprise first heat exchanger for said removing cerate for heating a process (13). The dewaxing device can remove the valid of waxy material surface.
NOVELTY - This utility new type surface layer refers to a one in four seasons type solar energy marsh gas dry-type anaerobic fermentation system, seal fermenting tank set with polyurethane insulating layer, and the inner winding set with the radiating tube, rear solar energy hot water device with the marsh gas boiler complementary heating device in series connecting a radiating tube so that the inner tank a temperature of 20 to 40 degrees between the inner range, increase the fermentation efficiency to make the outside weather temperature can uniform a biogas in four seasons. Seal fermentation tank inner layer upper end set with seal opening, feeding from the top, a tank inner surface fresh, preventing the crusting layer. Biogas residue pumping machine and seal fermenting tank bottom connecting the bottom precipitate is discharged from precipitate produce. Biogas residue pumping machine tail end set with solid-liquid separate machine, solid-liquid separate machine lower end set with biogas, biogas storage tank and stir mix machine connect. Solid-liquid separate the biogas residue and biogas slurry separate machine, and the stored in the liquid storage tank, circulation in stir mix machine inner and reduces the operation cost.
NOVELTY - A one electric field induction type electrolysis hydrogen device, it is container by a two bottom connected with one group of high voltage electrode, one group and low voltage electrode, high voltage electrode set in the container of the outer wall, a low voltage electrode set on the inner wall of container. A container is made of insulation material, the inner container storage of electrolytic liquid. The outer wall of two end of high voltage electrode is the strong electric field in the. The lower induction effect of strong electric field, produce electrolytic liquid of positive ion and negative ion of a of a corresponding area fast moving, form the positive ion collecting area and negative ion concentration area. The device greatly increase the electric pulse moving speed of iron to ensure the low-voltage electrode of a valid exchange, so that electrolytic speed greatly increase, and because a exchange a large electric current of a low voltage so that the electrolysis of efficiency increase, a greatly increase.
NOVELTY - Preparation of water hyacinth biological carbon involves washing stems of water hyacinth, cutting, performing primary dehydration, freeze-drying, processing in tube furnace, blowing nitrogen, and heating at high temperature in anaerobic condition.    USE - Preparation of water hyacinth biological carbon (claimed).    ADVANTAGE - Water hyacinth biological carbon having excellent quality is stably prepared.
NOVELTY - Fluidized bed reactor comprises reactor main body (1), air or gas inlet (2), reaction product exit (4), urea solution entrance (3), and heating resistance silks (5).    USE - Fluidized bed reactor used for flue gas denitration of urea solution (claimed).    ADVANTAGE - The method ensures low cost and simple control, and does not produce second pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of fluidized bed reactor (Drawing includes non-English language text).    Reactor main body (1)    Air or gas inlet (2)    Urea solution entrance (3)    Reaction product exit (4)    Heating resistance silks (5)
NOVELTY - Completely autotrophic nitrogen-removal over nitrite involves adjusting suspended solid value of inoculated sewage treatment plant activated sludge, performing aeration, adjusting alkalinity, precipitating and simultaneously discharging water, performing nitrification process, removing ammonia, controlling dissolved oxygen content and alkalinity, performing aeration, precipitating and simultaneously discharging water, measuring nitrogen content of water sample from discharged water, removing nitrogen, performing aeration process, adjusting alkalinity and removing nitrogen load.    USE - Completely autotrophic nitrogen-removal over nitrite (claimed).    ADVANTAGE - The method enables completely autotrophic nitrogen-removal over nitrite with total nitrogen removal load of 0.41 kgN/m3/day.    DETAILED DESCRIPTION - Completely autotrophic nitrogen-removal over nitrite involves adjusting mixed liquor suspended solid value and mixed liquor volatile suspended solid value of inoculated sewage treatment plant activated sludge to 12.5-13.5 g/L and 10-11 g/L, respectively, controlling dissolved oxygen content to 0.25-0.35 mg/L, performing aeration for 4.5-7.5 hours, stirring, adjusting alkalinity to 1500-1700 mg/L, precipitating and simultaneously discharging water by pumping, measuring ammonia and nitrate/nitrite nitrogen concentration in water sample of separated water, performing nitrification process at nitrous accumulation rate of 50%, removing ammonia for 5 consecutive days, controlling dissolved oxygen content and alkalinity at 0.15-0.24 mg/L, performing aeration for 8.5-9.5 hours, precipitating and simultaneously discharging water though suction outlet, measuring nitrogen content of water sample from discharged water, removing nitrogen for 5 consecutive days, controlling dissolved oxygen content at 0.15-0.24 mg/L, performing aeration process for 10-11 hours, adjusting alkalinity to 1900-2100 mg and removing nitrogen load for 5 consecutive days.
NOVELTY - In situ method for ecological restoration of acid mine drainage and polluted water bodies such as lakes and reservoirs, comprises adding a remaining sewage directly from bottom of the polluted water bodies to built an anaerobic buffered area, and carrying out a AMD ecological restoration process in the anaerobic buffered area using an ecological restoration system, floating bed plants and anaerobic microorganisms. The plant provides organic nutrients to the microorganisms, and absorbs harmful heavy metals.    USE - The in situ method is useful for ecological restoration of acid mine drainage and polluted water bodies such as lakes and reservoirs (claimed).
NOVELTY - Cassava ethanol wastewater treatment involves processing cassava ethanol wastewater with the anaerobic biogas, and entering the processed cassava ethanol wastewater into an anoxic fluidized bed reactor. The anoxic fluidized bed reactor is equipped with a middle tank of a biological reactor. A nano-filtration device is provided, which is equipped with a water outlet.    USE - Method for treating cassava ethanol wastewater (claimed).    ADVANTAGE - The method enables to treat cassava ethanol wastewater in an eco-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a system for treating cassava ethanol wastewater, which comprises integration film box and a box bottom that is set in water inlet area.
NOVELTY - Preparing biosolid involves drying municipal sewage sludge and then grinding it to obtain granules. The obtained granules are put into polytetrafluoroethylene lined stainless steel hydrothermal reaction kettle. Water and catalyst solution are added into the reaction kettle and then heated at 150-200 degrees C for 5-10 hours, and then cooled to obtain mixture. The obtained mixture is filtered in vacuum and then dried to obtain the finished product, where mass ratio of sludge and water is 1:4-1:10, and mass ratio of sludge and catalyst solution is 1:3-1:80.    USE - Method for preparing biosolid used as fuel (claimed).
NOVELTY - Fermenting sludge involves keeping phosphorus-containing chemical-biological sludge into a reactor and mixing for 24 hours. Supernatant is discharged, and then concentrated. Chemical dephosphorization of the obtained material is performed. Chemical and biological sludge mixture is mixed with disodium ethylenediaminetetraacetic acid and pH value is set to 6.5-7.5 in the sealed reactor at 30-50 degrees C. Anaerobic fermentation is carried out for 5-10 days. Anaerobic fermentation of residual mud phosphorus is prevented to increase release rate of phosphor mix sludge.    USE - Method for fermenting sludge (claimed).    DETAILED DESCRIPTION - Fermenting sludge involves keeping phosphorus-containing chemical-biological sludge into a reactor and mixing for 24 hours. Supernatant is discharged, and then concentrated. Chemical dephosphorization of the obtained material is performed. Chemical and biological sludge mixture is mixed with disodium ethylenediaminetetraacetic acid and pH value is set to 6.5-7.5 in the sealed reactor at 30-50 degrees C. Anaerobic fermentation is carried out for 5-10 days. Anaerobic fermentation of residual mud phosphorus is prevented to increase release rate of phosphor mix sludge. Aluminum salt or iron salt are added to the phosphorus-containing chemical biological mixture.
NOVELTY - Organic waste disposal high speed fermentation machine comprises feeding frame (1), outer guide rail (3), main machine front end (4), lifting screw (18), feeding frame roller (20), lifting frame (21), nut (28), lifting rod (29), chain wheel (30), inner guide rail (31), lower connecting column (32), inner shaft (34), transmission shaft (35) and transmission device (45).    USE - Organic waste disposal high speed fermentation machine.    ADVANTAGE - The simple, convenient, nonpolluting and low noise machine occupies small floor area and reduces labor.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of organic waste disposal high speed fermentation machine.    Feeding frame (1)    Outer guide rail (3)    Main machine front end (4)    Lifting screw (18)    Feeding frame roller (20)    Lifting frame (21)    Nut (28)    Lifting rod (29)    Chain wheel (30)    Inner guide rail (31)    Lower connecting column (32)    Inner shaft (34)    Transmission shaft (35)    Transmission device (45)
NOVELTY - Organic fertilizer comprises 65-70 wt.% cattle and sheep excrement, 16-20 wt.% wheat bran, 8-12 wt.% conditioning agent, 1-2 wt.% pH regulator, 3-5 pts. wt. deodorant and 0.1-0.2 wt.% microbial inoculum. The conditioning agent comprises bean powder, sawdust, wheat husk and mushroom. The pH regulator is natural gypsum, dilute hydrochloric acid, sulfuric acid or superphosphate.    USE - The organic fertilizer is nutrition-rich and has simple preparation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of organic fertilizer comprising mixing raw materials, performing enzymolysis for 5-7 days at 70 degrees C using microbial inoculum, mixing, cooling and evaporating water.
NOVELTY - Industrial aerobic compost three-dimensional real-time acquisition system comprises real-time display (1), data wire (2), data collect module (3), air inlet (4), gas-guide soft pipe (5), control handle (6), filter network (7), temperature sensor (8), transmission line (9), card groove (10), signal converter (11), universal serial bus interface (12).    USE - Industrial aerobic compost three-dimensional real-time acquisition system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of industrial aerobic compost three-dimensional real-time acquisition system.    Real-time display (1)    Data wire (2)    Data collect module (3)    Air inlet (4)    Gas-guide soft pipe (5)    Control handle (6)    Filter network (7)    Temperature sensor (8)    Transmission line (9)    Card groove (10)    Signal converter (11)    Universal serial bus interface (12)
NOVELTY - A microbial composite fertilizer comprises greater than or equal to 30 wt.% organic matter, greater than or equal to 4 wt.% nitrogen, greater than or equal to 4 wt.% phosphorus, greater than or equal to 4 wt.% potassium, 150000000-250000000 cells/g phosphorus-solubilizing bacteria, 150000000-250000000 cells/g potassium-solubilizing bacteria, 150000000-250000000 cells/g nitrogen-fixing bacteria, 150000000-250000000 cells/g alkaliphilic bacteria, 150000000-250000000 cells/g halophilic bacteria, 200000000-300000000 cells/g thermophilic bacteria and 200000000-300000000 cells/g thermophilic Actinomycetes.    USE - Microbial composite fertilizer for improving soil structure, increasing soil organic matter content, hastening decomposition, increasing soil fertility, and improving soil pH.    ADVANTAGE - The fertilizer promotes decomposition of straw, improves survival in alkaline and saline environments, and can be applied to both normal and saline soils.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of microbial composite fertilizer comprising crushing organic matter base material, adding microbes, nitrogen fertilizer, phosphate fertilizer and potash fertilizer, mixing at 20-28 degrees C, adding water to water content of 30-45%, stirring, fermenting naturally at 45-60 degrees C, crushing, sieving, adding trace elements, granulating, and packing.
NOVELTY - Forest felling residue substrate comprises forest felling residue fermentation product and special composite fertilizer. The felling residue fermentation product comprises forest felling residue, animal manure, and water. The special composite fertilizer comprises nitrogen, phosphorus, potassium and microelement.    USE - Forest felling residue substrate used for growing seedling (claimed) i.e. fast-growing tree species.    ADVANTAGE - The substrate is environment-friendly, reduces environment pollution and facilitates low carbon environmental protection.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of substrate comprising crushing forest felling residue, mixing with pig and/or cow dung, and water, fermenting, drying, washing, drying; and mixing with special composite fertilizer.
NOVELTY - Microbial organic fertilizer comprises water (20-40%), nitrogen, phosphorus and potassium ( greater than or equal to 8.11%), total valid viable count of cells ( greater than or equal to 0.2 hundred million/g), amino nitrogen (77.1858 mg/g), amino acid ( greater than or equal to 14%), iron, zinc and molybdenum (1-1.5%), and arsenic, mercury and other heavy metal elements (0%).    USE - Microbial organic fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing microbial organic fertilizer, which involves:    (A) preparing green Trichoderma viride strain seed liquid;    (B) inoculating seed liquid to Jatropha curcas fruit oil;    (C) stirring the obtained material uniformly; and    (D) keeping the obtained material to obtain the finished product.
NOVELTY - Micro-nano organic selenium-enriched foliar fertilizer preparation involves cleaning and removing impurity from protein raw material, and then the obtained material is dried. The obtained raw material is mixed with water, and then the obtained material is processed in constant temperature ultra-micro crushing system. Animal protein hydrolytic enzyme is added the obtained material for enzymolysis. The obtained material is centrifuged, and then the obtained material is separated. The obtained supernatant liquid is dried by using spray dryer to obtain amino acid.    USE - Method for preparing micro-nano organic selenium-enriched foliar fertilizer (claimed).    ADVANTAGE - The method enables to prepare micro-nano organic selenium-enriched foliar fertilizer is eco-friendly in nature, has less toxic property, and has industrial application.    DETAILED DESCRIPTION - Micro-nano organic selenium-enriched foliar fertilizer preparation involves cleaning and removing impurity from protein raw material, and then the obtained material is dried. The obtained raw material is mixed with water, and then the obtained material is processed in constant temperature ultra-micro crushing system. Animal protein hydrolytic enzyme is added the obtained material for enzymolysis. The obtained material is centrifuged, and then the obtained material is separated. The obtained supernatant liquid is dried by using spray dryer to obtain amino acid. The obtained amino acid is processed in constant temperature super-micro-crushing system. Mineral source micro-nanoselenium (10-30 pts.), biological glue (1-5 pts.) and water (400-550) are mixed with obtained amino acid to obtain micro-nano organic selenium-enriched foliar fertilizer.
NOVELTY - Biological fertilizer composition comprises (in pts.wt.): Broussonetia papyrifera leaves (60-70), soybean (7-15), green manure (10-15), slurry (4-8), biological fertilizer (5-10) and complex biological agents (6-12).    USE - Biological fertilizer composition.    ADVANTAGE - The biological fertilizer composition shows improved organic matter in soil, ecological environment, and is eco-friendly in nature.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing biological fertilizer composition, which involves:    (A) drying Broussonetia papyrifera leaves for 5-8 hours in a dryer, and then crushing the dried product;    (B) drying soybean, green manure and slurry in sunlight, and then crushing the dried material;    (C) mixing the obtained material with crushed Broussonetia papyrifera uniformly, and then adding water to the obtained mixture with stirring    (D) adding complex biological agents and coating agent with stirring to the obtained material with stirring, and then fermenting them, where fermenting temperature is 25-30 degrees C, fermentation time is 7-10 days;    (E) turning the fermented material in each 2-3 days; and    (F) drying the obtained fermented material, and then granulating the dried material to obtain the finished product.
NOVELTY - Recovering acetic acid plant exhaust gas useful components, comprises conveying tail gas from the reaction process and tail gas from the distillation process into tail gas absorption column, contacting with the methanol absorbent, conveying the tail gas absorption column stream into the torch system, recycling the stream from tower bottom to the reaction process, where the temperature of methanol is more than 0-12 degrees C.    USE - The method is useful for recovering acetic acid plant exhaust gas useful components (claimed).    ADVANTAGE - The method is suitable for industrial production methanol low pressure carbonyl-based synthesized acetic acid gas recovery.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of acetic acid plant exhaust gas useful components recovering system
NOVELTY - An energy-saving multi-system methanol production is carried out by connecting a same product reaction system in series, entering all raw material gas into a first reaction system, and entering exhaust gas from the first reaction system into next reaction system to be used as raw material gas.    USE - Method for energy-saving multi-system methanol production (claimed).    ADVANTAGE - The method can reduce consumption of synthesis gas and device investment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an energy-saving multi-system methanol production device comprising a same product reaction device provided with a circulation machine, a heat exchanger, a reactor, a cooler and a separator connected in series.
NOVELTY - Solvent, p-methoxytoluene and catalyst (c1) are added to oxidation reactor, oxygen is bubbled, and oxidized to obtain organic phase (p1) and aqueous phase (a1). Base is added to organic phase (p1), and distilled to obtain organic phase (p2). Distilled water is added to resultant product, pH is adjusted, and filtered, to obtain p-methoxybenzoic acid. The organic phase (p2) is distilled, to obtain p-methoxybenzaldehyde and methoxybenzyl acetate. Acetate is subjected to alkali hydrolysis, to obtain crude methoxybenzyl alcohol. Alcohol is distilled, to obtain pure methoxybenzyl alcohol.    USE - Oxidation of p-methoxytoluene used in medicine and food.    ADVANTAGE - The method enables oxidation of p-methoxytoluene under mild reaction conditions. The method is economical and environmentally-friendly.    DETAILED DESCRIPTION - Solvent, p-methoxytoluene and catalyst (c1) are added to oxidation reactor, oxygen is bubbled at specified temperature for specified time, oxidized, solvent is recovered, and catalyst (c1) is washed using water to obtain organic phase (p1) and aqueous phase (a1). Then, base is added to organic phase (p1), and distilled under reduced pressure to obtain organic phase (p2). Distilled water is added to the resultant product, pH is adjusted using acid, and filtered to obtain p-methoxybenzoic acid. To the obtained aqueous phase (a1) distilled water is added, evaporated, and catalyst (c1) and solvent are recovered. The organic phase (p2) is distilled, to obtain p-methoxybenzaldehyde and methoxybenzyl acetate. Methoxybenzyl acetate is subjected to alkali hydrolysis, to obtain crude methoxybenzyl alcohol. The alcohol is distilled, to obtain pure methoxybenzyl alcohol.
NOVELTY - Production of L-carnitine and inorganic salt comprises adjusting pH to 3-8 of carnitine and inorganic salt-containing carnitine crude product, and separating L-carnitine and inorganic salt through chromatographic separation.    USE - Method for production of L-carnitine and inorganic salt (claimed).    ADVANTAGE - The method is environment-friendly, obtains high-purity L-carnitine, does not need regeneration of chromatographic resin, and it has low cost.
NOVELTY - A tiopronin intermediate alpha -chloropropionylglycine is prepared by mixing glycine with sodium hydroxide aqueous solution, cooling and dropping alpha -chloropropionyl chloride and sodium hydroxide aqueous solution, controlling concentration of sodium hydroxide aqueous solution to 8-25 wt.%, cooling, and directly separating crystal.    USE - Preparation of tiopronin intermediate alpha -chloropropionylglycine (claimed).    ADVANTAGE - Preparation process has high product yield, reduces cost and reaction device, and is environment-friendly.
NOVELTY - Preparation of chlorocarbonyl(4-(trifluoromethoxy)phenyl)carbamate involves mixing (trifluoromethoxy)aniline, sodium hydroxide and toluene, cooling the resultant product to -10 degrees C to 10 degrees C, dripping methyl chloroformate, heating the resultant product, washing, adding alkali, dissolving triphosgene in toluene, dripping the reaction mixture, washing the resultant product with water, drying, distilling the resultant product, adding petroleum ether, precipitating the resultant product and filtering.    USE - Preparation of chlorocarbonyl(4-(trifluoromethoxy)phenyl)carbamate which is used for preparing agricultural pesticide indoxacarb.    ADVANTAGE - The method enables environmentally-friendly preparation of chlorocarbonyl(4-(trifluoromethoxy)phenyl)carbamate with high yield and high purity.    DETAILED DESCRIPTION - Preparation of chlorocarbonyl(4-(trifluoromethoxy)phenyl)carbamate involves mixing (trifluoromethoxy)aniline, sodium hydroxide and toluene, cooling the resultant product to -10 degrees C to 10 degrees C, dripping methyl chloroformate, heating the resultant product at 30-40 degrees C for 1.5-5 hours, washing the resultant product, then adding alkali to the resultant product, heating the resultant product at 106-110 degrees C for 2.5-5 hours to obtain reaction mixture, dissolving triphosgene in toluene at 0-10 degrees C, then dripping the reaction mixture at 0-15 degrees C, carrying out thermal reaction for 1-2 hours, washing the resultant product with water, drying, distilling the resultant product, adding petroleum ether, precipitating the resultant product and filtering.
NOVELTY - An orange ketone is prepared by adding haloepoxy chalcone, ligand, and alkaline substance in organic solvent, and reacting 80-140 degrees C for 2.5-5 hours under action of copper catalyst.    USE - Preparation of orange ketone (claimed).    ADVANTAGE - The product has high regioselectivity and stereoselectivity, method is simple, does not produce pollution, has mild reaction conditions, and high yield, raw materials are readily available, and catalyst is low cost.    DETAILED DESCRIPTION - An orange ketone of formula (II) is prepared by adding haloepoxy chalcone of formula (I), ligand, and alkaline substance in organic solvent, reacting 80-140 degrees C for 2.5-5 hours under action of copper catalyst.    R1, R2=halo, 1-20C alkyl, OMe, NO2, or aryl; and X=Cl, Br, or I.
NOVELTY - Escitalopram impurity J is synthesized by taking escitalopram oxalate as raw material, reacting with solvent in the presence of hydrogen peroxide, adding acid binding agent, and hydrolyzing.    USE - Synthesis of escitalopram impurity J (claimed).    ADVANTAGE - The method is low cost, fast, simple, environment-friendly, has mild reaction conditions, and high yield, and material has high purity.    DETAILED DESCRIPTION - Escitalopram impurity J of formula (II) is synthesized by taking escitalopram oxalate of formula (I) as raw material, reacting with solvent in the presence of hydrogen peroxide, adding acid binding agent, and hydrolyzing..
NOVELTY - Dehydrated vinblastine preparation involves reacting a compound (II) with peroxide and solid acid catalyst in an alkali reaction medium to perform oxidation reaction to obtain compound (III). The obtained compound (III) is treated with a compound (IV) and reducing agent to obtain S-R type dehydration optical isomers of vinblastine.    USE - Method for preparing dehydrated vinblastine (claimed).    ADVANTAGE - The method prepares dehydrated vinblastine having high optical purity in a simple and cost-effective and eco-friendly manner under mild reaction conditions on industrial scale.    DETAILED DESCRIPTION - Dehydrated vinblastine preparation involves reacting chloro carboxylic compound of formula (I) with peroxide and solid acid catalyst in an alkali reaction medium to perform oxidation reaction to obtain carboxylic compound of formula (II). The obtained carboxylic compound of formula (II) is treated with a dicarboxylic compound of formula (III) and reducing agent to obtain S-R type dehydration optical isomers of vinblastine.
NOVELTY - Production of soluble humic acid involves adding humic acid-containing raw materials with humic acid content of 60% or more, extracting agent and water to a reactor in a solid-liquid weight ratio of 1:0.5-1, heating at 140-160 degrees C, pressurizing under 1-2 Kg pressure for 20-120 minutes, heat-preserving, aging at 60-80 degrees C for 48-168 hours, and low-temperature drying.    USE - Production of soluble humic acid used in agricultural applications.    ADVANTAGE - The method enables energy-saving and environmentally-friendly production of high-quality soluble humic acid by a simple process.
NOVELTY - A mixed refrigerant is obtained by mixing specific amount of ethylene (R1150), propane (R290) and/or 1,1,1,2-tetrafluoroethane (R134a), at room temperature, and has use temperature of -50 degrees C to -90 degrees C.    USE - Mixed refrigerant (claimed).    ADVANTAGE - The mixed refrigerant has zero ozone-depletion potential, reduced global warming potential and excellent thermo physical property.
NOVELTY - A mixed refrigerant is chosen from carbon dioxide/propane mixed refrigerant, carbon dioxide/cyclopropane mixed refrigerant, carbon dioxide/propyne mixed refrigerant, carbon dioxide/butane mixed refrigerant, carbon dioxide/isobutane mixed refrigerant, carbon dioxide/maleic anhydride mixed refrigerant, carbon dioxide/trans-butene mixed refrigerant and carbon dioxide/cyclopentane mixed refrigerant.    USE - Mixed refrigerant is used in system for power circulation (all claimed).    ADVANTAGE - The mixed refrigerant has low flammability, excellent circulating efficiency, and better temperature match with fluid heat source exchanger, and is thus an excellent coolant for condensation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for power circulation method.
NOVELTY - The biomass pyrolysis device comprises a pyrolysis furnace, a feeding device, an air supply unit equipped with an inlet channel, a discharging unit, a fixed plate, a movable plate, a thrust plate, a lever, reciprocating carts, a plenum chamber, an insulation layer, a regulation screw, and a gas control channel. The pyrolysis furnace is provided with a transfer mechanism, and comprises an air chamber and a pyrolysis chamber. The transfer mechanism is disposed between the air chamber and the pyrolysis chamber. The thrust plate is connected with a beam pipe and right side and left side panels.    USE - Biomass pyrolysis device.    DETAILED DESCRIPTION - The biomass pyrolysis device comprises a pyrolysis furnace, a feeding device, an air supply unit equipped with an inlet channel, a discharging unit, a fixed plate, a movable plate, a thrust plate, a lever, reciprocating carts, a plenum chamber, an insulation layer, a regulation screw, and a gas control channel. The pyrolysis furnace is provided with a transfer mechanism, and comprises an air chamber and a pyrolysis chamber. The transfer mechanism is disposed between the air chamber and the pyrolysis chamber. The thrust plate is connected with a beam pipe, a right side panel and a left side panel. The beam pipe is disposed between the pyrolysis furnace and plates. The reciprocating carts are provided with rollers. The plenum chamber is fixed in the pyrolysis furnace. The pyrolysis furnace has a rear baffle wall or a pyrolysis gas barrier. A top end of the pyrolysis chamber is provided with a pyrolysis gas outlet, and a bottom end of the pyrolysis chamber is provided with a cleaning hopper. The hopper is provided with a window.
NOVELTY - A straw decomposition and conversion comprehensive utilization device comprises straw crusher (1), cracking furnace (2), cyclone separator (3), condenser (4), gas purification device (5), fractionating tower (6), conveying pipeline, carbon outlet, air inlet and air outlet. Gas purification device comprises purification box, 2 clapboards, 3 chambers, atomizing nozzle, air inlet, vent tube, vent hole, feeding port, baffle plate, air outlet, liquid discharging port and connecting pipeline. Connecting pipeline comprises main pipeline, branch pipeline, regulating valve and circulation pump.    USE - Straw decomposition and conversion comprehensive utilization device for producing biomass fuel gas, charcoal and tar.    ADVANTAGE - The device has complete product recovery, high conversion efficiency, high purification degree, no secondary pollution generation, and no serious energy waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of straw decomposition and conversion comprehensive utilization device.    Straw crusher (1)    Cracking furnace (2)    Cyclone separator (3)    Condenser (4)    Gas purification device (5)    Fractionating tower (6)
NOVELTY - A biomass pyrolysis device comprises: tube, rotating cone, support device, driving device, coaxial tube, front seal cover, material flowing tube, air outlet tube and carrier flow tube; where the tube is divided into two parts, where the front part is set with rotating cone and coaxial tube, and the inner wall of back part is set with a staggered arrangement; where the front seal cover is set with a material flowing tube, an air outlet tube and a carrier flow tube, where the material flowing tube and a carrier flow tube extending to the cone.    USE - For pyrolysis of biomass (claimed).    ADVANTAGE - The biomass pyrolysis device greatly increases circulation of0 the heat efficiency, avoids the carrier, and reduces the energy consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for pyrolysis of biomass involves: entering the material through the material flowing tube into bottom tube, entering a carrier on the rotating cone through the carrier flow tube, stirring the reaction mixture, and discharging gas through the air outlet tube.
NOVELTY - The method involves utilizing nitrogen in a reaction system during raw material drying process. Rear filter raw material oil is flown into a raw material oil buffering tank and mixed with vulcanizing agent and pre-processing agent. A feeding pump is connected to a heat exchanger for mixing the hydrogen raw material oil and hydrogen. A rear air cooler is connected to a high pressure separator. Hydrogenation reactors and the buffering tank are arranged together in a turn manner. A heat preservation and energy-saving unit is covered with insulating layers.    USE - Biomass oil hydrogenation refining heterogeneous prepare low pour point diesel oil component condensing method.    DETAILED DESCRIPTION - The vulcanizing agent is carbon disulfide or thiophene. The pre-processing agent is zinc oxide, iron oxide, manganese oxide, calcium oxide, magnesium oxide or metal oxide.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a biomass oil hydrogenation refining heterogeneous prepare low pour point diesel oil component condensing method.'(Drawing includes non-English language text)'
NOVELTY - A coal and biomass liquefied product analyzing method, involves placing liquefied coal or biomass in bottom of a vessel, extracting mixture with tetrahydrofuran derivative. Solvent is added to bottom of inner vessel for distilling the extract. Distilled extract is subjected to solid-liquid separation to obtain primary raffinate extract. Primary raffinate extract is dried at 40-250 degrees C to obtain asphalt substances. Asphalt weight and asphalt weight after drying is weighed accurately to obtain product conversion rate and yield of asphalt and heavy oil yield.    USE - Method for analyzing coal and biomass liquefied product.    ADVANTAGE - The method enables analyzing coal and biomass liquefied product simply and conveniently and with increased calculation accuracy of residue quantity.    DETAILED DESCRIPTION - A coal and biomass liquefied product analyzing method, involves placing liquefied coal or biomass in bottom of a vessel, extracting mixture with tetrahydrofuran derivative or 35-50 wt.% extraction agent using Soxhlet extraction, and obtaining solid extract through extraction tube and drying the extract at 40-250 degrees C for 0.01-100 hours. Solid residue containing the vessel total weight is not changed. Solvent is added to bottom of inner vessel for distilling the extract. Distilled extract is subjected to solid-liquid separation to obtain primary raffinate extract. Primary raffinate extract is dried at 40-250 degrees C to obtain asphalt substances. Asphalt weight and asphalt weight after drying is weighed accurately to obtain product conversion rate and yield of asphalt and heavy oil yield. Product conversion rate is calculated using dry solid residue mass and total mass of raw material. Asphalt yield is calculated using mass of the asphalt and total mass of the dried asphalt.
NOVELTY - The method involves passing raw material oil e.g. plant oil and animal oil, into a rear stripping tower bottom heat exchanger. Nitrogen gas is utilized to exhaust air and realize drying treatment. Mixed vulcanizing agent e.g. carbon disulfide and thiophene, is output from a raw material oil buffering tank. A rear high pressure separator is cooled by an air cooler. Hydrogenation reaction process is performed by a hydrogenation reactor. Gas is separated from liquid by using the rear high pressure separator. Light component oil is separated from a top part of a separate stripping tower.    USE - Biomass oil catalytic hydrogenation high cetane diesel engine component preparation method.    ADVANTAGE - The method enables reducing energy consumption, avoiding environment pollution and improving quality of a biomass oil catalytic hydrogenation high cetane diesel engine component.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a biomass oil catalytic hydrogenation high cetane diesel engine component preparation method.'(Drawing includes non-English language text)'
NOVELTY - The device has a fan (1) connected with an air inlet pipeline (3) that is connected with an oxygen supply room (6). A gas-making system is provided with a gas reaction room (9) and an ash ignition port (7). A pneuma hole plate is fixed with the gas reaction room and the oxygen supply room. A packing auger shaft is fixed with a feeding tube (16) that is connected with the gas reaction room through a feeding port (12). A circuit integrated control system i.e. integrated circuit control box (18), is connected with the fan and a feed electrical machine (17).    USE - Biomass gasification integrated device.    ADVANTAGE - The device is simple in structure and simple to operate. The device has wide application range, and reduces tar and smoke and avoids formation of residue.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a biomass gasification integrated device.    Fan (1)    Air inlet pipeline (3)    Oxygen supply room (6)    Ash ignition port (7)    Gas reaction room (9)    Feeding port (12)    Feeding tube (16)    Feed electrical machine (17)    Integrated circuit control box (18)
NOVELTY - A nano-alcohol-based fuel comprises 30-60 wt.% methanol, 30-60 wt.% plant alcohol, 9-9.9 wt.% stabilizer, and 0.1-1 wt.% nano-synergistic agent.    USE - A nano-alcohol-based fuel (claimed).    ADVANTAGE - Fuel has high thermal value, is clean and environment-friendly, and replaces coal, diesel oil, liquefied gas, and supplemental natural gas fuel.
NOVELTY - A biomass particle fuel contains uniformly mixed and press-molded 50-60 mass% biomass carbon powder, 30-40 mass% crushed municipal organic solid waste powder, 1-10 mass% coal powder, 1-2 mass% coal tar, 0.2-0.5 mass% sulfur fixing agent, and 0.1-0.3 mass% ferrous sulfate in which biomass particle fuel outer surface is covered with 1 layer of biomass polyester, and biomass carbon powder is prepared by drying 60-70 mass% wood material and 30-40 mass% crop straw, crushing, press-molding, performing pyrolysis and gasification reactions, cooling, and crushing.    USE - A biomass particle fuel (claimed).    ADVANTAGE - Biomass particle fuel is environment-friendly, non-breakable, and convenient to transport and store, has good adhesion and high combustion value, and does not produce sulfur dioxide and fly ash.    DETAILED DESCRIPTION - A biomass particle fuel contains uniformly mixed and press-molded 50-60 mass% biomass carbon powder, 30-40 mass% crushed municipal organic solid waste powder, 1-10 mass% coal powder, 1-2 mass% coal tar, 0.2-0.5 mass% sulfur fixing agent, and 0.1-0.3 mass% ferrous sulfate in which biomass particle fuel outer surface is covered with 1 layer of biomass polyester, biomass carbon powder is prepared by drying 60-70 mass% wood material and 30-40 mass% crop straw, crushing, press-molding, performing pyrolysis and gasification reactions, cooling, and crushing, crushed municipal organic solid waste powder is prepared by performing municipal solid waste classification, selecting recyclable municipal organic solid waste, drying, and crushing, sulfur fixing agent is quicklime and/or calcium carbonate, and biomass polyester is prepared by mixing 3.2 g malic acid and 1.5 g glycerin, adding 20 ml anhydrous ethanol and 0.5 ml 20% sulfuric acid, heating to dissolve, cooling, pouring on metal surface, putting in vacuum oven, and heating at 90 degrees C or 100 degrees C for 11 hours to obtain light yellow film.
NOVELTY - Production of biomass fuel particles involves screening raw material, drying and storing after cyclone separation, stirring the stored material, granulating using sub-feed granulator, and screening.    USE - Production of biomass fuel particles (claimed).    ADVANTAGE - The method enables production of biomass fuel particles with high quality and high efficiency.
NOVELTY - Coal is biologically desulfurized by crushing coal using crusher into less than or equal to 150 mesh particles, selecting 3 bacterial strains i.e. Thiobacillus thiooxidans, Thiobacillus thermophilus, and Pseudomonas stutzeri, and carrying out desulfurization while stirring by performing organic sulfur removal for 5-30 days using Pseudomonas stutzeri, and carrying out inorganic sulfur removal for 5-25 days using Thiobacillus thiooxidans and Thiobacillus thermophilus mixed bacterial liquid in which bacteria concentration is 2x 104-2x 109 cells/ml.    USE - Biological desulfurization of coal (claimed).    ADVANTAGE - Biological desulfurization process is simple, highly efficient, and low in cost, has high sulfur removal rate and mild reaction conditions, and retains active component in coal.    DETAILED DESCRIPTION - Coal is biologically desulfurized by crushing coal using crusher into less than or equal to 150 mesh particles, selecting 3 bacterial strains i.e. Thiobacillus thiooxidans, Thiobacillus thermophilus, and Pseudomonas stutzeri, carrying out desulfurization while stirring by performing organic sulfur removal for 5-30 days using Pseudomonas stutzeri, and carrying out inorganic sulfur removal for 5-25 days using Thiobacillus thiooxidans and Thiobacillus thermophilus mixed bacterial liquid in which bacteria concentration is 2x 104-2x 109 cells/ml, coal slurry concentration is 5-40%, and reaction temperature is 10-40 degrees C, washing desulfurized coal using water, filtering and drying, putting in oven, and drying at 70-150 degrees C for 0.5-3 hours.
NOVELTY - Method for creating healthy agricultural system by comprehensive utilization of resources is claimed.    USE - The method is useful for creating healthy agricultural system for producing Chlorella sp. cultivation liquid which is used as functional feed, fertilizer and insecticide (all claimed).
NOVELTY - Composite biological agent for livestock and poultry cultivation sewage treatment, comprises Bacillus amyloliquefaciens IAE deposited under CCTCC NO: M 2013086, Trichoderma asperellum 12 deposited under CCTCC NO: M2013213, and Bacillus thuringiensis.    USE - The composite biological agent is useful for livestock and poultry cultivation sewage treatment (claimed).    ADVANTAGE - The composite biological agent can reduce odor emissions in aquaculture effluent, can significantly chemical oxygen demand (COD) after treatment of sewage, and can reduce pollution of soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for preparing composite biological agent for livestock and poultry cultivation sewage treatment, comprising: (a) inoculating Bacillus amyloliquefaciens IAE deposited under CCTCC NO: M 2013086 to seed liquid culture medium; (b) inoculating Trichoderma asperellum 12 deposited under CCTCC NO: M2013213 in potato-dextrose-agar (PDA) liquid culture medium; (c) inoculating Bacillus thuringiensis to liquid seed culture medium; and (d) performing microbial fermentation.
NOVELTY - Dried sludge is utilized to prepare a dilute microbial solution, which comprises mixing Pseudomonas stutzeri with Trichoderma reese and Streptomyces strains in a volume fraction ratio of 1:1:1.    USE - Dried sludge used for promoting growth of Festuca arundinacea in saline soil, and for measuring biomass, enzyme activity, malondialdehyde and proline content (claimed).    ADVANTAGE - The dried sludge effectively screen microorganisms that find immense potential in promoting the growth of plant by enabling plants to grow in saline soil and other adverse conditions.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for cultivating drought resistance Festuca arundinacea plant, which involves:    (A) culturing sludge microbial agent, which involves isolating and purifying microbes such as Pseudomonas stutzeri, Trichoderma reese, and Streptomyces strains from the sludge, and then growing bacterial microorganisms into a flask containing liquid medium;    (B) incubating the culture medium flask at certain conditions, and then calculating optical density of the obtained bacterial suspension at 600 nanometer;    (C) performing experiment, where Festuca arundinacea seeds are sown in the normal soil, and then inoculating Festuca arundinacea seeds into a culture medium to obtain tillering stage of plant;    (D) adding sludge microbial inoculum into the Festuca arundinacea seeds culture medium, and growing the drought resistance plants under controlled environmental growth under white fluorescent light, and then observing the results after35 days; and    (E) washing the roots and shoots of Festuca arundinacea, and then drying it in an oven-dried to determine its dry biomass.
NOVELTY - An A2B-type hydrogen storage electrode alloy comprises magnesium-yttrium-titanium-nickel-manganese-containing compound.    USE - A hydrogen storage electrode alloy (claimed).    ADVANTAGE - Hydrogen storage electrode alloy has nanocrystalline-amorphous structure which reversibly absorbs and releases hydrogen through electrochemical process, high discharge capacity, excellent electrochemical circulation stability, improved surface activity, and good electrochemical hydrogen storage property.    DETAILED DESCRIPTION - An A2B-type hydrogen storage electrode alloy comprises magnesium-yttrium-titanium-nickel-manganese-containing compound of formula (Mg20-x-yYxTiyNi10-zMnz) in which x, y, and z are atomic ratio.    x=1-4;    y=0.2-1; and    z=1-4.    An INDEPENDENT CLAIM is included for preparation of A2B-type hydrogen storage electrode alloy which involves vacuumizing metal raw material in vacuum induction furnace at pressure of 5x 10-5-1x 10-2 Pa, filling inert gas which is pure helium gas or argon gas with pressure of 0.01-0.1 MPa in which volume ratio of pure helium gas or argon gas is 1:1, heating at 1500-1700 degrees C to obtain molten mother alloy liquid, holding for 5 minutes, directly injecting in copper casting mold to obtain mother alloy ingot, placing in quartz tube with slit at bottom, melting by induction heating, injecting liquid alloy in rotating water-cooled copper roller surface under pressure of protective gas and line speed of 10-40 m/s to obtain quenched alloy sheet, mechanically crushing and sieving through 200 meshes sieve, placing into stainless steel ball milling pot in which ratio of grinding media and material is 40:1, vacuumizing by filling highly pure argon gas, and ball milling at rotating speed of 350 rpm in omni-directional planetary ball mill.    DESCRIPTION OF DRAWING(S) - The drawing shows a photograph of microstructure and electron diffraction ring of ball milled-alloy powder. (Drawing includes non-English language text).
NOVELTY - Extracting ethane from natural gas involves pre-cooling the natural gas by refrigerant to -37 degrees C and then separating the gas using former low temperature separator. The separated gas is cooled to -61 degrees C and then the cooled gas is separated using later low temperature separator. The separated gas is pressurized by a compressor to 6 megapascal and then the pressurized gas is entered into heat exchanger at 75 degrees C for condensation. The condensed gas is depressurized to 3.5 megapascal after super cooling. The super cooled natural gas is entered into demethanizer column to obtain the liquid phase.    USE - Method for extracting ethane from natural gas (claimed).    ADVANTAGE - The method enables to extract ethane from natural gas in simple and cost-effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device, which comprises heat exchanger, a compressor, an expander, former low temperature separator, later low temperature separator, demethanizer, the heat exchanger is provided with the former low temperature separator, the expander and compressor, the compressor is connected with the heat exchanger, the demethanizer, liquid phase exit of former and later low temperature separator, and the former low temperature separator is connected with the demethanizer.
NOVELTY - Method for determining biodegradability and stability of sewage residue, involves (a) adding sewage residue to an Erlenmeyer flask comprising recombinant bacteria inoculants; (b) removing air remaining in the flask, performing shaking culture , and (c) determining biodegradability and stability of sewage residue by performing biochemical methane potential (BMP) test.    USE - The method is useful for determining biodegradability and stability of sewage residue chosen from primary sewage residue, dewatered sewage residue and digested sewage residue (claimed).    DETAILED DESCRIPTION - Method for determining biodegradability and stability of sewage residue, involves (a) adding sewage residue to an Erlenmeyer flask comprising recombinant bacteria inoculants in a ratio of 1:5-5:1, adjusting pH of resulting sewage residue mixed with inoculants to 9-11 by adding alkali and maintaining resulting mixed residue at 53-57 degrees C; (b) removing air remaining in the flask for several minutes by treating the flask with nitrogen, performing shaking culture periodically for 5-8 days, where the volatile fatty acid (VFA) concentration in the mixed residue is converted to carbon, and (c) determining biodegradability and stability of sewage residue by performing biochemical methane potential (BMP) test, where the sewage residue is stable at a coefficient value of 1-3.
NOVELTY - The converter has a high frequency transformer (T) comprising two winding groups (n1, n2). One of the two winding groups is connected with an excitation inductor (Lm). An end of a resonance inductor (Lr) is respectively connected with the first winding group and a first switching transistor (S1). A source electrode of a second switching transistor (S3) is connected with a second winding group that is connected with an anode of a first rectifying diode (D01). An unequal end of the other winding group is connected with an anode of a second rectifying diode (D03).    USE - LLC resonant three-port DC-DC converter. Uses include but are not limited to renewable energy generation, electric vehicle, fuel cell vehicle and energy storage applications.    ADVANTAGE - The converter can connect a non-isolate type bi-directional buck-boost converter with an isolation type full-bridge LLC resonance converter that is effectively connected with a raw edge switching multiplexing transistor to reduce requirement of number of switching transistors so as reduce processing cost and increase power density and reliability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for controlling an LLC resonant three-port DC-DC converter.    DESCRIPTION OF DRAWING(S) - The drawing shows a circuit diagram of an LLC resonant three-port DC-DC converter.'(Drawing includes non-English language text)'    Rectifying diodes (D01, D03)    Excitation inductors (Lm)    Resonance inductance (Lr)    Switching transistors (S1, S3)    High frequency transformer (T)    Winding groups (n1, n2)
NOVELTY - This utility new type provide the one electric heating of a biological diesel oil distillation tower, the tower kettle comprise from up to down in turn and connecting a heat exchange device, a device, distillation device and circulation heating device, a circulation heating device using a heating electric heater, said electric heater by the electric heater, the left electric heater, circulation pump, electric heater, film film heater and right circulation pump is composed of a film and the left falling-film electric heater electric heater through a left circulation pump a material circulation heating, said film heater and right film heater and a right circulation pump through a material circulation heating. This utility new type using electric heating way, which not only reduces the device cost, and there is no pollution, and is beneficial to environment protection, speed cooling of distillation tower heating, material retained a short, it is not easy to produce coking phenomenon of material, increase the production efficiency, a recovery by in excess of a heat, a the inner tower saving energy and reducing consumption.
NOVELTY - This utility new type provide the one a biological diesel esterification reaction tower, include: material outlet, methanol inlet, thermometer, pressure gauge, a liquid level meter, a valve, methanol exit, material inlet and tower body, a material inlet and a methanol exit set at the top end of said tower body, a methanol inlet and a material outlet set with set a layer of multi-hole plate, a discharge valve set on each layer hole plate side to maintain the material with liquid level height at the bottom of the tower body, a tower body in interval, a liquid level meter set on the each layer hole plate side is used for liquid level height of material layer a observation tower body each layer hole plate, a thermometer and a pressure measuring meter set on the each layer hole plate side to observe temperature and pressure of each layer hole plate. This utility new type has simple structure, it is not easy to coke, and convenient to clean and high pressure resistance property is strong, not need catalyste is added in the esterification reaction process, a of the methanol tower inner the subcritical, reaction speed is fast, reaction more thoroughly.
NOVELTY - This utility new type provide a one garbage treatment device, the aerobic fermentation tank and anaerobic fermentation tank are set with an air inlet and discharge port are set with a stir blade inner aerobic fermentation tank and anaerobic fermentation tank. Stir blade by first stir blade, stir blade second, third stir blade, stir efficiency, good evenness. This utility new type organic waste for discharge of organic waste can be used for the industry, in agriculture, livestock, food processing and so on of the same flow developed industry, at the same time, for garbage treatment of local government can be made.
NOVELTY - Cultivating pear seedlings, involves (a) selecting deep soil with excellent organic content and water conditions, (b) plowing soil and fertilizing soil using e.g. manganese sulfate, (c) soaking cuttage in 0.3-0.4% indolebutyric acid (IBA) and 0.2-0.5% ethanol solution for 4-5 hours and removing cuttage, (d) inserting the cuttage in the soil, watering soil, maintaining temperature of the soil at 25-30 degrees C, weeding soil, fertilizing soil, and topdressing 1.2 kg urea on the soil for 2-3 times, and (e) harvesting seedlings, when seedlings grow up to 45-50 cm.    USE - The method is useful for cultivating pear seedlings (claimed).    ADVANTAGE - The method cultivates pear seedlings at high yield, and is cost-effective and environmentally-friendly. The pear seedlings cultivated by the method have high survival rate.    DETAILED DESCRIPTION - Method for cultivating pear seedlings, involves (a) selecting deep soil with excellent organic content and water conditions, (b) plowing soil to 25-30 cm, fertilizing soil using 200-250 kg farmyard manure, 80-90 kg rice bran, 3-4 kg manganese sulfate, 100-150 kg rock based magnesium phosphate fertilizer, 20-30 kg chicken feathers, and 100-120 kg modified crop straw, (c) soaking cuttage in 0.3-0.4% indolebutyric acid (IBA) and 0.2-0.5% ethanol solution for 4-5 hours and removing cuttage, (d) inserting the cuttage in the soil, watering soil, maintaining temperature of the soil at 25-30 degrees C, weeding soil, fertilizing soil, and topdressing 1.2 kg urea on the soil for 2-3 times, and (e) harvesting seedlings, when seedlings grow up to 45-50 cm.
NOVELTY - Cultivation method of Phellinus igniarius involves: a) binding or bundling the wooden material and paving culture medium on it to obtain the material bag; and b) cooling the material bag, sterilizing and then inoculating the Phellinus igniarius culture, where the culture medium is kudzu root.    USE - As cultivation method of Phellinus igniarius (claimed).    ADVANTAGE - The present cultivation method can reduce the invasion and infection; can reduce the pollution rate by 11.7% to 17.9%; and can increase yield of Phellinus igniarius by more than 15%.
NOVELTY - Pig manure is processed using Hermetia illucens larvae by defining pigsty (1), placing fecal leakage plate (2), connecting to manure collecting groove (3), placing padding, allowing access of probiotic bacteria, forming bed (4), laying nylon yarn network (5), feeding H. illucens larva, discharging pig urine, collecting manure, digesting to convert into insect protein, allowing pig urine to permeate, maturing larvae, removing nylon yarn network, changing, and adding new larvae.    USE - Method for processing pig manure using H. illucens larvae (claimed).    ADVANTAGE - The treatment process is a clean, low-cost, safe and non-polluting recycling process suitable for intensive pig farming.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of pig manure processing system.    Pigsty (1)    Fecal leakage plate (2)    Manure collecting groove (3)    Bed (4)    Nylon yarn network (5)
NOVELTY - A catalyst comprises redox active component which is supported on a carrier. The carrier is capable of providing mechanical support and transmitting oxygen atom or ion.    USE - Catalyst is used for gasifying garbage.    ADVANTAGE - The catalyst has excellent catalytic activity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of catalyst, which involves preparing carrier by hydrothermal, impregnation, sol-gel or co-precipitation process, introducing rare-earth metal oxide into the carrier by immersion method or deposition-precipitation method, introducing carbon dioxide active component into the obtained carrier by immersion method or deposition-precipitation, and introducing carbon-based active component into the resultant carrier by immersion method.
NOVELTY - Nylon biological carrier comprises active carbon and adhesive that is uniformly adhered to the surface of nylon felt material, and is embedded in the bonding hole structure of nylon material felt. The nylon material felt has net-shaped porous structure.    USE - Nylon biological carrier used as microbial support for treatment of sewage (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing a nylon biological carrier, which involves:    (A) processing the nylon felt material;    (B) processing the active carbon; and    (C) dipping adhesive in the nylon felt material.
NOVELTY - Fertilizer preparation involves fermenting animal manure with aerobic compost into a fermentation tank at 55 degrees C for 72 hours. The obtained aerobic compost is placed into a feeder. Soil microbial composite is sprayed on the surface of aerobic compost, and then stirred uniformly. Nitrogenous fertilizer, phosphate fertilizer, potash fertilizer and trace element fertilizer are added to the obtained compost material, and then stirred. Water retention agent is added to the obtained material, and then stirred uniformly into a squeezing granulator.    USE - Method for preparing fertilizer (claimed).    ADVANTAGE - The method enables to produce fertilizer that increases productivity of hill sloping field and dissolves nutrition substance from dust.    DETAILED DESCRIPTION - Fertilizer preparation involves fermenting animal manure with aerobic compost into a fermentation tank at 55 degrees C for 72 hours. The obtained aerobic compost is placed into a feeder. Soil microbial composite is sprayed on the surface of aerobic compost, and then stirred uniformly. Nitrogenous fertilizer, phosphate fertilizer, potash fertilizer and trace element fertilizer are added to the obtained compost material, and then stirred. Water retention agent is added to the obtained material, and then stirred uniformly into a squeezing granulator. The obtained material is extruded into bar-shaped intermediate, and then polished to obtain spherical granule, where diameter of the spherical granule is 3-5 mm. An INDEPENDENT CLAIM is included for a method for preparing microbial organic fertilizer, which involves mixing aerobic compost, soil composite dust, water retention agent, ammonium sulfate, calcium superphosphate, potassium sulfate and trace element fertilizer to obtain fertilizer.
NOVELTY - Bioorganic fertilizer composition comprises (in wt.%): fermented chicken manure (85-88), bentonite (8-10) and humic acid (2-7).    USE - Bioorganic fertilizer composition.    ADVANTAGE - The bioorganic fertilizer composition is rich in multi-trace elements, and improves yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing, which involves:    (A) mixing fermented chicken manure, bentonite and humic acid uniformly;    (B) fermenting the obtained mixture at 50-70 degrees C for 7 days, and then fermenting at 35-50 degrees C for 18 days;    (C) performing secondary fermentation of the obtained fermented material at 40-50 degrees C for 7-10 days;    (D) mixing uniformly the obtained fermented material; and    (E) granulating the obtained material, and then drying them to obtain granular organic biological fertilizer.
NOVELTY - Production of straw-based carbon involves compression-molding straw, leaves, fruit and rice, forming molded product, providing the molded product into circulation-type carbonization furnace, and carbonizing at optimum temperature.    USE - Production of straw-based carbon (claimed).    ADVANTAGE - The method enables economical production of straw-based carbon having high calorific value and carbon density, and low defect rate.
NOVELTY - The composite biomass liquid fuel comprises fine methanol of 99.9% purity as main raw material, and 5-8% of an additive including methanol, n-butyl alcohol, excessive potassium, toluene, tung oil, camphor, acetone, hydrogen peroxide or ferrocene.    USE - Composite biomass liquid fuel.    ADVANTAGE - The composite biomass liquid fuel facilitates convenient transportation and strong hydrophilicity.
NOVELTY - The clean fuel comprises 50-65 wt.% of methanol, 3-6 wt.% of isobutyl alcohol, 1-3 wt.% of ferrocene, 0.5-2 wt.% of camphor, 1-3.5 wt.% of hydrogen peroxide solution, and 25-40 wt.% of water.    USE - Clean fuel.    ADVANTAGE - The clean fuel has good combustion value and high heat productivity, and can be prepared in a simple, cost-effective and eco-friendly manner without producing carbon, sulfur oxide, nitrogen oxide and other toxic gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing clean fuel, which involves:    (A) pouring methanol, isobutanol, ferrocene, camphor and water into a non-metallic container to form a mixed solution;    (B) stirring the formed mixture by using a non-metal stirrer for 3-5 minutes; and    (C) adding hydrogen peroxide solution in the formed mixture with stirring for 3-5 minutes for forming clean fuel.
NOVELTY - The methanol fuel additive comprises 10-15% of ethanol, 3-5% of isobutyl alcohol, 10-15% of methylal, 2-4% of dicyclopentadienyl iron, 2-4% of magnesium nitrate, 2-4% of ammonium sulfate, and 60-70% of distilled water.    USE - Methanol fuel additive used for preparing methanol water fuel oil field (claimed).    ADVANTAGE - The methanol fuel additive has high heating hydrogen conversion rate up to 25200 kilojoules per kilogram, low oil consumption, and reduces harmful smoke.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing methanol fuel additive, which involves:    (A) adding10-15% of ethanol, 3-5% of isobutyl alcohol, 10-15% of methylal, 2-4% of a dicyclopentadienyl iron, 2-4% of magnesium nitrate, and 2-4% of ammonium sulfate in 60-70% of distillation water;    (B) stirring the reaction mixture in a high speed mixer at high speed for 10 minutes; and    (C) continuously stirring the formed mixture for 15 minutes to obtain the methanol fuel additive.
NOVELTY - The nano-formulated fuel technology comprises a waste water well (1), a water pump (2), a grid (3), a regulating tank (4), a biochemical tank (5), a metering pump (14), a static mixer (6), a precipitation tank (7), and a precise filter (8). A high speed shearing machine (16), an oil pump (9), a methanol tank (10), an additive tank (17), an oil filter (11), and a finished product tank (12) are also included in the nano-formulated fuel technology.    USE - Nano-formulated fuel technology.    ADVANTAGE - The nano-formulated fuel technology reduces serious pollution problem by using garbage penetrating liquid.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing nano-formulated fuel, which involves:    (A) placing waste water of garbage penetrating liquid through pipeline and water pump into regulating tank;    (B) homogenizing the collected water;    (C) placing the homogenized water into biochemical tank for performing anaerobic acidification treatment;    (D) adding additive in additive tank with stirring through a pipeline to form a product; and    (E) filtering the formed product into a finished product tank.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the nano-formulated fuel technology.    Waste water well (1)    Water pump (2)    Grid (3)    Regulating tank (4)    Biochemical tank (5)    Static mixer (6)    Precipitation tank (7)    Precise filter (8)    Oil pump (9)    Methanol tank (10)    Oil filter (11)    Finished product tank (12)    Metering pump (14)    High speed shearing machine (16)    Additive tank (17)
NOVELTY - This utility new type relates to biomass fuel gasification field, especially relates to a biomass fuel gasification production line one with filter, comprise second drainage barrel, a second drain barrel set with a filter bucket, a second drain barrel lower end set with a drain valve, a filter bucket set with a second air inlet and a fourth outlet, a second air inlet and the third air outlet cooling dust-removing device through a gas pipeline, a fourth outlet is connected with vacuum pump through gas connecting pipeline, a filter bucket lower end and a second drain barrel, lower end of said filter bucket set with fifth grid of clapboard, a filter bucket inner space a fifth clapboard inner set with a filter core. Time when the gas passes through filter core, a dust impurity, water vapour and tar in fuel gas is filter core absorbing and reduces the gas in the dust impurity, gas and water content of tar.
NOVELTY - A novel chitosan composite hemostatic powder preparing method involves dissolving chitosan and calcium salt in acid condition using co-precipitation technology to obtain a co-precipitate under alkaline condition, followed by centrifuging, washing, dehydrating, drying, sieving and sterilizing the obtained co-precipitate to obtain a finished product.    USE - Method for preparing novel chitosan composite hemostatic powder.    ADVANTAGE - The method enables preparing novel chitosan composite hemostatic powder with better hemostatic effect, high yield and better stability in a simple, rapid, cost-effective and eco-friendly manner.
NOVELTY - A polyvinyl acetate and polyether-b-polyamide blend film comprises film material containing 0.01-99 %mass polyvinyl acetate and remainder of Pebax (RTM: polyether-b-polyamide).    USE - Polyvinyl acetate and polyether-b-polyamide blend film is used as gas-separating film for separating mixture of different gas components into permeable gas comprising carbon dioxide, hydrogen sulfide or sulfur dioxide, and non-permeable gas containing nitrogen, oxygen and 1-4C hydrocarbon gas (all claimed).    ADVANTAGE - The blend film has high gas separation efficiency.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (i) preparation of polyvinyl acetate and polyether-b-polyamide blend film, which involves dissolving Pebax (RTM: polyether-b-polyamide) in solvent at 70-110 degrees C to obtain Pebax (RTM: polyether-b-polyamide) solution having mass concentration of 0.1-20%, adding polyvinyl acetate solution to prepare homogeneous casting film liquid, coating the liquid on glass plate or PTFE plate, and removing residual solvent from obtained film; and (ii) usage of polyvinyl acetate and polyether-b-polyamide blend film as gas-separating film for separating gas mixture of different gas components.
NOVELTY - Recovery of ammonia from ethanolamine-ammonia reaction product involves dividing ethanolamine-ammonia reaction product into three portions, providing primary portion of reaction product into flash tank, providing the vapor from tank into condenser, mixing resultant condensate with liquid ammonia, providing resultant product into reactor in which one portion of the liquid is fed to heat exchanger, providing secondary portion of the reaction product into heat exchanger, providing the resultant product into flash tank and providing vapor from tank to condenser.    USE - Recovery of ammonia from ethanolamine-ammonia reaction product (claimed).    ADVANTAGE - Ammonia is recovered from ethanolamine-ammonia reaction product with high recovery rate by environmentally-friendly method.    DETAILED DESCRIPTION - Recovery of ammonia from ethanolamine-ammonia reaction product involves dividing ethanolamine-ammonia reaction product into three portions, providing primary portion of reaction product into flash tank in which pressure is reduced to 1.6-2.2 MPa, providing the vapor from the flash tank into condenser, mixing resultant condensate with liquid ammonia through circulation pump, providing the resultant product into a reactor in which one portion of the liquid is fed to heat exchanger, then providing secondary portion of the reaction product into heat exchanger at 60-80 degrees C, providing the resultant product into flash tank at 85-100 degrees C, then again providing the vapor from the tank to condenser, then mixing the condensate with liquid ammonia through the circulation pump, providing the resultant product into kettle reactor at 150-200 degrees C under 1.5-3 MPa, reducing the temperature of heat exchanger to 50-60 degrees C, then providing the resultant product into cooler at 30-50 degrees C, then directly circulating the tertiary portion of the reaction product into the reactor, and adjusting the reactor temperature to 60 degrees C or more.
NOVELTY - Preparing bethanechol chloride comprises adding chloroform in a kettle, then adding methyl choline chloride, stirring, then adding solid phosgene, adding catalyst and stirring to stop the reaction, reducing temperature of the reaction liquid, adding aqueous ammonia into the reaction liquid, decompressing and concentrating, adding methyl choline chloride into anhydrous ethanol, centrifugally filtering, adding ammonium chloride with methyl choline of crude product into anhydrous ethanol, then adding activated carbon for decoloring, cooling, extracting, and then filtering to obtain filter cake.    USE - The method is useful for preparing bethanechol chloride (claimed).    ADVANTAGE - The method is capable of simply preparing the bethanechol chloride with high yield in a cost-effective and eco-friendly manner.    DETAILED DESCRIPTION - Preparing bethanechol chloride comprises adding chloroform in a reaction kettle, then adding methyl choline chloride at a temperature of 40 degrees C, edge stirring, then adding solid phosgene, where the ratio of methyl choline chloride to solid phosgene is 1:2-2.9, adding catalyst and stirring for 5-10 minutes, raising temperature to 50-80 degrees C for 3-8 hours, where the catalyst is dimethyl formamide, pyridine or triethylamine, and the dosage of the catalyst is 1-5 wt.% of methyl choline, stopping the reaction, reducing temperature of the reaction liquid to 15-25 degrees C, adding 20-30 wt.% of aqueous ammonia into the reaction liquid to regulate pH value to 8-10, decompressing and concentrating until it is dry, adding methyl chloride choline into 3-5 times of anhydrous ethanol, centrifugally filtering to obtain ammonia of methyl choline, adding ammonium chloride with methyl choline of crude product into 1-5 times of anhydrous ethanol, then adding 2-4 wt.% of active carbon for decoloring, cooling, extracting, and then filtering to obtain filter cake.
NOVELTY - Preparing guanidotaurine (I), comprises (i) mixing taurine (II) and water in a weight ratio of 1:2-1:4, adding sodium hydroxide solution to adjust pH to 10-12, and reacting to obtain sodium taurate (III), (ii) heating the obtained reaction product (III) to 60 degrees C, adding cyanamide and reacting in presence of a phase transfer catalyst to obtain crude product of (I), and (iii) adjusting pH of the obtained product to neutral, cooled to 10 degrees C, and carrying out solid-liquid separation to obtain solid high-purity product of (I).    USE - The method is useful for preparing guanidotaurine (claimed).    ADVANTAGE - The method: has short process route; does not generate waste gas and solid residue, recycles mother liquor and reduces production cost; has mild reaction conditions, safe and simple operation, and high product yield and purity; and is environment-friendly, and suitable for large-scale production.    DETAILED DESCRIPTION - Preparing guanidotaurine of formula (I), comprises (i) mixing taurine of formula (II) and water in a weight ratio of 1:2-1:4, adding sodium hydroxide solution to adjust pH to 10-12, and reacting to obtain sodium taurate of formula (III), (ii) heating the obtained reaction product (III) to 60 degrees C, adding cyanamide and reacting in presence of a phase transfer catalyst to obtain crude product of (I), and (iii) adjusting pH of the obtained product to neutral, cooled to 10 degrees C, and carrying out solid-liquid separation to obtain solid high-purity product of (I).
NOVELTY - Preparation of phthalylglycine-L-glutamine comprises adding inorganic alkali and L-glutamine in water, cooling to - 5 to - 12 degrees C to prepare water solution, where inorganic alkali is caustic soda and/or sodium carbonate, fast dropping phthalylglycyl chloride into water solution, where dropping speed is controlled at 2.5-3 g/s, reacting at 8-12 degrees C, adding concentrated acid solution, regulating pH at 3-4, precipitating white crystals, adding dilute acid solution, regulating the pH at 1.5-2, precipitating white crystals, filtering the white crystals and drying to obtain the product.    USE - Preparation of phthalylglycine-L-glutamine (claimed).    ADVANTAGE - The method uses easily obtained raw materials, has simple operation, high product yield and high product purity, avoids the use of toxic and harmful organic solvent and reduces the generation of industrial wastewater, waste gas emissions, pollution to the environment, and phthalylglycine-L-glutamine side effect.
NOVELTY - Preparing phthaloyl-L-alanyl glutamine involves reacting inorganic alkali and L-glutamine; cooling to 0 degrees C in water, forming solution, selecting inorganic alkali from inorganic strong alkali, adding phthaloyl L in the solution of alanyl chloride, at reaction temperature of 8-12 degrees C, finishing reaction, adding concentrated hydrochloric acid in the solution, regulating pH value to 4-5, separating out white crystal, adding diluted acid solution in solution, regulating pH value to 1.5-2, separating out white crystal, crystalizing and drying filter product.    USE - For preparing phthaloyl-L-alanyl glutamine (claimed).    ADVANTAGE - The preparation has simple operation, has high purity and high product yield, and avoids the use of toxic, harmful organic solvents, reduces production of industrial waste water, waste water, emissions, and reduce pollution to the environment. The method effectively reduces the side effects of alanylglutamine preparations in clinical.    DETAILED DESCRIPTION - Preparing phthaloyl-L-alanyl glutamine involves reacting inorganic alkali and L-glutamine; cooling to 0 degrees C in water, forming solution, selecting inorganic alkali from inorganic strong alkali, caustic soda, adding phthaloyl L alpha -alanyl chloride, dropping speed at 2.5-3 g per second, and a reaction temperature of 8-12 degrees C, finishing reaction, adding concentrated hydrochloric acid in the solution, regulating pH value to 4-5, separating out white crystal, adding diluted acid solution in the solution, regulating the pH value to 1.5-2, separating out white crystal further; separating out white crystal filter, drying to obtain phthaloyl-L-alanyl glutamine.
NOVELTY - Differential pressure type feeding and discharging device of two phase liquid organic waste anaerobic fermentation system comprises an acidifying tank and a fermentation tank, which are connected together via a connector. The base of the acidification tank and the fermentation tank are set at a specific height difference, where the material delivery is based on liquid level pressure difference.    USE - Used as differential pressure type feeding and discharging device of two phase liquid organic waste anaerobic fermentation system.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the differential pressure type feeding and discharging device of two phase liquid organic waste anaerobic fermentation system.
NOVELTY - Bacillus safensis Shafu strain (I) preserved under a number of CGMCC No.8843, is new.    USE - (I) is useful in the preparation of microorganism fertilizer (claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a microbial inoculum comprising (I) and culture medium; and    (2) use of (I) in the preparation of microorganism fertilizer.
NOVELTY - A hydrogen-producing catalyst comprises core part (10) which has inorganic substance and compressive strength that is higher than sintered body of perovskite type oxide, and coating part (20) which coats the surface of core part and perovskite type oxide (22) which carries active metal (24).    USE - A hydrogen-producing catalyst for manufacturing reformed gas (claimed).    ADVANTAGE - Reaction efficiency of catalytic reaction is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a manufacture of hydrogen producing catalyst which involves preparing core part (10) containing inorganic substance in which compressive strength is higher than sintered body of perovskite type oxide (22), making the perovskite type oxide which carries active metal, and organic binder and inorganic binder (26) adhere to surface of core part by rolling granulation process and forming a coating part (20) which coats surface of core part including active metal (24).    DESCRIPTION OF DRAWING(S) - The drawing shows an expanded schematic view of the hydrogen-producing catalyst.    Core part (10)    Coating part (20)    Perovskite type oxide (22)    Active metal (24)    Inorganic binder (26)
NOVELTY - An electrode comprises base (311) with surface and protrusion part (312) which protrudes from surface of base. Protrusion parts are positioned away from each other on surface of base. Material of surface of protrusion part is material whose hydrogen overvoltage is lower than that of material of surface of base. Electrode generates hydrogen gas from electrolyte solution. Electrode is provided on gas production apparatus which produces hydrogen gas and oxygen gas using photocatalyst from electrolyte solution containing water.    USE - An electrode for gas production apparatus (claimed).    ADVANTAGE - Production of bubbles of generated hydrogen gas on surface of electrode is suppressed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for gas production apparatus comprising 1st electrode, 1st chamber which accommodates 1st electrode, 2nd electrode containing photocatalyst which produces oxygen gas from electrolyte solution, and 2nd chamber which accommodates 2nd electrode.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the 1st electrode.    Base (311)    Protrusion part (312)    Bus bar (313)    Terminal (314)    1st surface (s1)
NOVELTY - Synthetic vilanterol intermediate (I) preparation involves reacting 2,2-dimethyl-6-(oxiran-2-yl)-2,4-dihydro-1,3-benzodioxine and amine chiral auxiliary agent (II). The amine chiral auxiliary agent is S-benzene ethyl amine chiral auxiliary agent or S-naphthalene ethylamine chiral auxiliary agent.    USE - Method for preparing synthetic vilanterol intermediate used as catalyst (claimed).    ADVANTAGE - The method prepares synthetic vilanterol intermediate in a simple, cost-effective and eco-friendly manner.    DETAILED DESCRIPTION - Synthetic vilanterol intermediate of formula (I) preparation involves reacting 2,2-dimethyl-6-(oxiran-2-yl)-2,4-dihydro-1,3-benzodioxine and amine chiral auxiliary agent of formula (II). The amine chiral auxiliary agent is S-benzene ethyl amine chiral auxiliary agent or S-naphthalene ethylamine chiral auxiliary agent. An INDEPENDENT CLAIM is included for a method for preparing synthetic vilanterol intermediate.
NOVELTY - The present invention employs the ferrous phosphate powder (vivianite, Fe.sub.3(PO.sub.4).sub.2-8H.sub.2O). A platinum catalyst is reduced on the powder to form a catalyst (Pt/vivianite), and a Pt/vivianite/C catalyst is formed after mixing Nafion with carbon black. With electrochemical performance testing, the electrochemical activity area (EAS) can be enhanced by taking vivianite powder as the platinum catalyst carrier, and platinum poisoned by carbon monoxide can also be improved. Accordingly, the overall catalyst conversion performance can be increased, and the usage of platinum catalyst can be reduced as well.
NOVELTY - Product based on a dried material of manure of animal of equine type, comprises residues of wood amalgamated with dried material of animal manure.    USE - The product is useful as a fuel (claimed) and insulating slabs.    ADVANTAGE - The product can be simply, eco-friendly and economically produced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing the product, comprising crushing the soiled wood residues and the dried material of animal manure, dehydrating the mixture, processing the mixture to obtain the product ready to use.
NOVELTY - The microchannel array (10) has a first lamina (14a) that is provided with several flanges extending along a perimeter of the first lamina. Several elongated bosses (31) are provided with the first flow paths. The first lamina is provided with an opening. A second lamina (14b) is provided with second flow paths and an opening. The second lamina is formed above the first lamina such that the second lamina is configured to enclose the first flow paths of the first lamina and the opening of the first lamina is coaxial with the opening of the second lamina.    USE - Microchannel array for recuperative heat exchanger in solid oxide fuel cell and chemical reactor for fuel reforming and nanomaterial synthesis.    ADVANTAGE - Since the flanges, the inlet bosses, and the outlet bosses are formed into the first lamina quickly and with less labor and materials, the cost of production of the microchannel array is reduced. The fabrication of the microchannel array is performed by bonding one lamina at a time rather than attempting to bond all laminae at once, thus the defects in the welds are corrected and the production yield and the reliability of micro channel are improved. Since the welds performed on the first and second laminae do not overlap one another, the weld crowning is reduced and/or eliminated.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of making a microchannel array.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the microchannel array.    Microchannel array (10)    Laminae (14a,14b)    Boss (31)    Flow insert (38)    High-pressure inlet and outlet headers (80,81)
NOVELTY - Mitigating the effects of slagging, fouling and/or corrosion caused by biomass ash in a biomass combustion system, comprises: (a) injecting biomass into a combustion region of the biomass combustion system and combusting the biomass, where the biomass ash is created; and (b) injecting a mitigant into the combustion region of the biomass combustion system to capture at least some of the biomass ash.    USE - The methods are useful for mitigating the effects of slagging, fouling and/or corrosion caused by biomass ash in a biomass combustion system, improving the combustion efficiency of the biomass combustion system and manufacturing biomass fuel for combustion in the biomass combustion system (all claimed).    ADVANTAGE - The method easily and rapidly reduces the slagging, fouling and corrosion caused by the biomass ash to acceptable operational levels thus improving the efficiency of the heat transfer and operation of the biomass combustion system.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) the biomass combustion system comprising a furnace having the combustion region, a gas pass, and an unit for injecting biomass and the mitigant into the combustion region, where combustion of the biomass generates biomass ash and the mitigant comprises particles for capturing biomass ash;    (2) a biomass fuel for combustion in the biomass combustion system, comprising biomass and the mitigant for capturing biomass ash, where the mitigant comprises particles to which the biomass ash is adhere; and    (3) a method-1 of manufacturing the biomass fuel, comprising mixing the biomass and the mitigant for capturing biomass ash.
NOVELTY - The method involves using the gases exiting from a membrane module (1) for heating the entered fresh air (L). More than 50 percent of heat energy contained in an exhaust gas (A) is used for preheating the fresh air. The heating on the required temperature level of 800 to 900 degree centigrade takes place by direct injection of fuel- or synthetic gas (S) from the biomass gasification in a combustion chamber of the membrane module.    USE - Method for energy-efficient oxygen generation in the biomass gasification using a membrane module (Claimed) with mixed-conducting, oxygen-permeable membranes for the production of high purity oxygen.    ADVANTAGE - The method involves using the gases exiting from a membrane module for heating the entered fresh air, and thus ensures simple and efficient generation of the oxygen.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a membrane module with a housing.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a membrane module.    Membrane module (1)    Heat exchangers (3,4)    Exhaust gas (A)    Fresh air (L)    Fuel- or synthetic gas (S)
NOVELTY - The system (100) has a driver (102) that provides a drive shaft (104) with a rotational energy. A compressor (110) has a rotary shaft (112) that is coupled to a drive shaft such that rotational energy is transmitted to rotary shaft. A primary sidestream (150) is formed from conduits (146,152) and is configured to flow through streams. The primary sidestream is arranged at a first distance of three times the first conduit diameter upstream of compressor, such that streams are mixed to form a first combined process fluid stream to be fed into and pressurized into a compressor.    USE - System for mixing and pressurizing process fluid stream e.g. liquefied natural gas (LNG) and ethylene, used in refinery.    ADVANTAGE - The portion of a process fluid stream is fed through a coupled conduits at a first junction that is arranged upstream of a compressor a distance of three times the first conduit diameter, thus removing a portion of a process fluid stream from the process fluid stream. The sidestreams are mixed efficiently with the process fluid streams at the junction, thus the pressure and temperature stratification to disturb the impeller inlet flow is eliminated.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a method for mixing and pressurizing a plurality of process fluid streams;    (2) a system for removing at least a portion of a process fluid stream; and    (3) a method for removing a portion of a process fluid stream.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a system for mixing and pressurizing the process fluid streams.    Sidestream mixing system (100)    Driver (102)    Drive shaft (104)    Compressor (110)    Rotary shaft (112)    Conduits (146,152)    Primary sidestream (150)
NOVELTY - Preparing (P1) rivaroxaban (I) involves a) contacting 4-(4-((5S)-5-(amino methyl)-2-oxo-1,3-oxazolidin-3-yl)phenyl)morpholin-3-one (II) or its salt with an oxidizing agent to form a first reaction mixture; b) then contacting the first reaction mixture with 5-chloro thiophene-2-carboxaldehyde (VIII) to form a second reaction mixture; and c) isolating compound (I) from the second reaction mixture.    USE - For preventing and treating various thromboembolic disease, in particular deep vein thrombosis (DVT), pulmonary embolism (PE), myocardial infract, angina pectoris, reocclusions and restenoses after angioplasty or aortocoronary bypass, cerebral stroke, transitory ischemic attacks, and peripheral arterial occlusive diseases.    ADVANTAGE - The rivaroxaban (I) is free of 4-(4-((R)-5-(((1-(5-Chloro-thiophen-2-yl)-meth-(E)-ylidene)-amino)-methyl)-2-oxo-oxazolidin-3-yl)-phenyl)-morpholin-3-one. The process avoids the formation of isomeric and other process-related impurities, while affording the desired rivaroxaban product with high yield and purity. The process is simple, eco-friendly, inexpensive, reproducible, robust and well suited on industrial scale.    DETAILED DESCRIPTION - Preparing rivaroxaban of formula (I) involves a) contacting 4-(4-((5S)-5-(amino methyl)-2-oxo-1,3-oxazolidin-3-yl)phenyl)morpholin-3-one of formula (II) or its salt with an oxidizing agent to form a first reaction mixture; b) then contacting the first reaction mixture with 5-chloro thiophene-2-carboxaldehyde of formula (VIII) to form a second reaction mixture; and c) isolating compound (I) from the second reaction mixture. (Structure I, II, VIII, WO2014155259A2-001) An INDEPENDENT CLAIM is included for purifying (P2) rivaroxaban (I) involving: a) providing a solution of rivaroxaban in a mixture of alcohol solvent and halogenated hydrocarbon solvent or their aqueous mixtures; b) precipitating the solid from the solution; and c) isolating the pure rivaroxaban (I).
NOVELTY - A working fluid composition comprises 3C or 4C hydrocarbon refrigerant, and a refrigerator oil including a mixed ester obtained by mixing complex ester (A), which is synthesized from polyalcohol, 6-12C polybasic acid, and 4-18C monohydric alcohol or 4-18C monobasic fatty acid, with polyol ester (B), which is synthesized from polyalcohol and 4-18C monobasic fatty acid, in mass ratio of 5/95-95/5 as a base oil. The viscosity of the refrigerant at 80 degrees C and absolute pressure of 1.5 MPa is 1 mm2/second or more.    USE - Working fluid composition is used for refrigerator. Can also be used for air conditioner of motor vehicle e.g. car, room and industries, dehumidifier, refrigerated warehouse, automatic vending machine, showcase, chemical processing plant, and heat pump used for hot water supply.    ADVANTAGE - The working fluid composition has high storage stability. The device using the composition has high abrasion resistance and usability for long period of time.
NOVELTY - Ethanol is manufactured from biomass saccharified liquid under low temperature by using the fungi which belong to the Mrakia genus.    USE - Manufacture of ethanol from biomass saccharified liquid under low temperature for manufacture of alcoholic drink.    ADVANTAGE - Ethanol fermentation and simultaneous saccharification fermentation from biomass are possible in a low-temperature environment, and manufacturing method is low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of high concentration ethanol from sugar liquid under low temperature using the fungi which belong to the Mrakia genus.
NOVELTY - Solid fuel is manufactured by mixing and stirring organic sludge with high water content and foodstuff waste material, adding less than or equal to 5 mm dry granulated material, and mixing and stirring. Moisture content of dry granulated material becomes less than or equal to 20% after drying. Production of solid fuel is possible even in natural drying.    USE - Manufacture of solid fuel for boiler (claimed).    ADVANTAGE - The need to transport organic sludge with high water content can be eliminated, organic sludge with high water content can be easily handled, solid fuel can be easily produced, and environmental impact of waste can be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for recycling system which uses manufacturing method of solid fuel.
NOVELTY - Glycerol is provided as raw material, and subjected to hydrothermal reaction under alkaline conditions in presence of catalyst containing active element chosen from iron group element, precious metal element, platinum group element and base metal element, to obtain lactic acid.    USE - Manufacture of lactic acid used as biodiesel fuel.    ADVANTAGE - The method economically enables manufacture of lactic acid having reduced amount of impurities such as formic acid, acetic acid, methanol, ethanol, ethylene glycol and propylene glycol by reducing energetic burden in purification process, at reduced temperature and pressure with yield of 30% or more.
NOVELTY - A biomass is gasified using supercritical water by suspending slurry component of hydrous biomass or biomass into nonmetallic-type catalyst, in gasification reactor (60) provided with double-pipe heat exchanger (40). The generated gas generated from reactor (60), ash and nonmetallic-type catalyst are suspended in water. The double-pipe heat exchanger pre-heats the suspension, during operation of biomass gasification system (100). The gasification reactor is cleaned by replacing suspension with fresh water. Thus, operation of biomass gasification system is enabled.    USE - Operation of biomass gasification system (claimed).    ADVANTAGE - The method enables operation of biomass gasification system with reduced clogging of interior pipe by tar.    DETAILED DESCRIPTION - A biomass is gasified using supercritical water by suspending slurry component of hydrous biomass or biomass into a nonmetallic-type catalyst, in a gasification reactor provided with double-pipe heat exchanger. The generated gas generated from the gasification reactor, ash and nonmetallic-type catalyst are suspended in water. The heat of mixture discharged from gasification reactor is utilized. The double-pipe heat exchanger pre-heats the suspension, during operation of biomass gasification system. The gasification reactor is cleaned by replacing the suspension with fresh water and supplying fresh water to gasification reactor through the double-pipe heat exchanger, and piping in the double-pipe heat exchanger. Thus, operation of biomass gasification system is enabled. An INDEPENDENT CLAIM is included for biomass gasification system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view (Drawing includes non-English language text)    Adjustment tank (10)    Crusher (20)    Double-pipe heat exchanger (40)    Gasification reactor (60)    Biomass gasification system (100)
NOVELTY - The method involves measuring vibration produced by oscillation detection sensor in multiple location of an outer peripheral surface of piping (10). The measured vibration value is compared with the vibration value measured when adhesion of the deposit to the wall surface of clogging or a pipe interior had in a pipe interior. The change of a vibration is analyzed. The chemical solution is poured from the upstream of an oscillation detection sensor (30). The change of the vibration is detected when the change of a vibration is detected by analyzing the change of a vibration.    USE - Method for detecting adhesion of the deposit for clogging pipe interior or the wall surface of the pipe interior.    ADVANTAGE - The method involves measuring vibration produced by oscillation detection sensor in multiple location of an outer peripheral surface of piping, and thus rapidly detect the position of the clogging or adhesion, and rapidly remove the clogging of a pipe interior or the wall surface of the pipe interior.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a piping system; and    (2) a biomass gasification system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a piping system.    Outer tube (1)    Inner tube (2)    Piping (10)    Oscillation detection sensor (30)    Vibration measurement device (40)
NOVELTY - The method involves grinding biomass feedstock during crushing process, where radioactive cesium is adhered to the biomass feedstock. Fast-pyrolysis process is performed on the grinded biomass feedstock such that the cesium prevents the feedstock from vaporizing. A liquid containing raw material is collected and a solid containing silicone-Oxygen-Cesium group is collected during the fast-pyrolysis process. The feedstock is heated in oxygen-free atmosphere in the fast-pyrolysis process. Silica is added during the crushing process and the fast-pyrolysis process.    USE - Method for performing decontamination processing on radioactive cesium adhered biomass to collect bio oil.    ADVANTAGE - The silica is added during the crushing process and the fast-pyrolysis process, so that bio-oil can be recovered from the biomass in an efficient manner, the radioactive cesium can be removed in an efficient manner in a chemically stabilized state and bio-gas can be recycled.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram explaining a method for performing decontamination processing on radioactive cesium adhered biomass.'(Drawing includes non-English language text)'
NOVELTY - The arrangement (1) has a fuel cell section (110) that includes a water inlet, a hydrogen outlet (112), and an oxygen outlet (113). A catalyst section (200) includes a hydrogen inlet (212), carbon oxide inlet (214) and a methane outlet (216). The hydrogen outlet of fuel cell section couples to the hydrogen inlet of catalyst section. The catalyst section converts the hydrogen and carbon oxide into methane. The control unit is adapted to control the controllable valve so as to obtain an optimum converting process to convert the hydrogen and carbon oxide into methane.    USE - Fuel cell arrangement.    ADVANTAGE - The efficiency of the fuel cell is significantly increased, when controlling the carbon oxide feeding to the catalyst section. The catalyst section is provided with a wall section being coated with a catalyst agent. Thus, an easy construction of a catalyst is provided. The wall section is pleated or formed in a surface-increasing manner so that the active surface of the catalyst agent is high. Thus, the methanation process is improved with respect to efficiency. The high current gradient is quickly reacted with a controlling process so as to avoid damages of the fuel cell arrangement, when detecting a high current gradient.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for improving efficiency of fuel cell arrangement.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fuel cell arrangement.    Fuel cell arrangement (1)    Fuel cell section (110)    Hydrogen outlet (112)    Oxygen outlet (113)    Catalyst section (200)    Hydrogen inlet (212)    Oxide inlet (214)    Methane outlet (216)
NOVELTY - Manufacture of hydrogen involves performing hydrogenation process by hydrogenating a gas containing hydrogen and hydrocarbon in the presence of hydrogenation catalyst and hydrocarbon oil containing aliphatic unsaturated hydrocarbon or aromatic hydrocarbon, carrying out separation process by separating hydrogenation-processed material obtained by the hydrogenation process into hydrocarbon gas containing 10 volume% or less hydrogen and hydrocarbon oil, and carrying out steam reforming reaction using separated hydrocarbon gas as raw material and manufacturing hydrogen.    USE - Manufacture of hydrogen used as fuel for boiler and heating furnace.    ADVANTAGE - The method enables efficient manufacture of hydrogen with high yield and reduced energy, and selective removal of hydrogen from source gas containing hydrocarbon and hydrogen, by simple process.    DETAILED DESCRIPTION - Manufacture of hydrogen involves performing hydrogenation process by hydrogenating a gas containing hydrogen and hydrocarbon having liquid space velocity of 0.5-5 (hour)-1 at 0.1-0.6 MPa and 250 degrees C in the presence of hydrogenation catalyst and hydrocarbon oil containing aliphatic unsaturated hydrocarbon or aromatic hydrocarbon, carrying out separation process by separating hydrogenation-processed material obtained by the hydrogenation process into hydrocarbon gas containing 10 volume% or less hydrogen and hydrocarbon oil, and performing hydrogen production process by carrying out steam reforming reaction using separated hydrocarbon gas as raw material and manufacturing hydrogen.
NOVELTY - The device (100) has a drain opening (118) including a dripping-off edge (120). A dripping-off shaft (122) is arranged below the dripping-off edge. A dissipation container (124) for quench liquid is arranged below the dripping-off shaft. The dripping-off shaft is partially heated. The dripping-off shaft surrounds an annular gap filled with inert gas. An outer cylinder defining the annular gap is made of an insulated material. A section (123) of the dripping-off shaft is adjustable with respect to power and temperature.    USE - Device for separation and discharge of slag from a gasification system for carbonaceous feedstock e.g. charcoal, biomass or refinery residues.    ADVANTAGE - The dissipation container for quench liquid is arranged below the dripping-off shaft, which is partially heated, thus ensuring outflow of the slag in a simple and reliable manner, minimizing the heating power, and ensuring easier operation of separation and removal of slag from the gasification plant.    DETAILED DESCRIPTION - The device allows a heating element (130) that is provided for realization of the heatableness of the dripping-off shaft. The heating element is made of molybdenum silicide.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a device for separation and removal of slag from a gasification system for carbonaceous feedstock.    Device for separation and removal of slag from a gasification system (100)    Drain opening (118)    Dripping-off edge (120)    Dripping-off shaft (122)    Section of dripping-off shaft (123)    Dissipation container (124)    Heating element (130)
NOVELTY - Usage method of organic sludge fuel involves forming molded product using organic sludge fuel and slag making material. The content of slag making material with respect to sum total of organic sludge fuel and slag making material is 10-70 %mass.    USE - Usage method of organic sludge fuel for forming molded product for manufacture of steel (all claimed) and fertilizer.    ADVANTAGE - The organic sludge fuel has excellent handleability. The steel is manufactured molded product containing organic sludge fuel with high productivity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of steel, which involves injecting molded product into a steel furnace;    (2) molded product; and    (3) manufacture of molded product, which involves mixing organic sludge fuel and slag making material, molding, and obtaining molded product.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view explaining manufacture of steel.    Hopper (10)    Cutting-out apparatus (14,16)    Mixing hopper (18)    Molding machine (20)    Conveyor (24)
NOVELTY - The apparatus (100) has a modifier which reforms the source gas discharged from the siloxane removal apparatus (2), and generates a hydrogen-containing gas. A combustor (5) burns the gas and combustion air which are emitted from the modifier. A flame rod (7) detects the combustion state of the combustor. A controller (8) determines that the siloxane removal apparatus is abnormal, or reports abnormality, when the output from the combustion detector is more than predetermined time and falls below predetermined output on predetermined running condition.    USE - Hydrogen generating apparatus for fuel cell system (claimed).    ADVANTAGE - The replacement time of the siloxane removal apparatus for purifying a sewage gas is easily and appropriately detectable. The deterioration of siloxane removal apparatus at the stage is detected more appropriately.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the hydrogen generating apparatus. (Drawing includes non-English language text)    Siloxane removal apparatus (2)    Combustor (5)    Flame rod (7)    Controller (8)    Hydrogen generating apparatus (100)
NOVELTY - The reformer has a control apparatus having fuel suppression mode which controls the amount of hydrogen generation by changing the fuel supply amount to modification catalyst while maintaining input electrical power to catalyst to preset maximum value. An electric power suppression mode which controls the amount of hydrogen generation is switched according to the state of vehicle by changing both the input electrical power and fuel supply amount to modification catalyst. The input electrical power is changed within a range smaller than maximum value in power suppression mode.    USE - Fuel reformer for vehicle.    ADVANTAGE - Since the quantity of fuel supplied to modification catalyst is minimized, the advancing of caulking is suppressed as much as possible. Since the amount of hydrogen generation is controlled, the input electrical power is suppressed by second control when there are no allowances in the residual amount of electrical storage apparatus, so that the burden of generator is reduced and the deterioration of fuel consumption is suppressed by extension.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating the process of controlling amount of hydrogen generation in modification catalyst. (Drawing includes non-English language text)    Step for setting amount of target hydrogen generation corresponded at target of production amount of hydrogen (S1)    Step for computing SOC of battery (S2)    Step for determining whether battery SOC is larger than predetermined value (S3)    Step for setting input electrical power to permissible maximum value (S4)    Step for setting fuel supply amount between minimum amount and limiting amount (S5)
NOVELTY - The wood-coal fluidized bed dryer (10) has a heat exchanger tube that is arranged in interior furnace (12). A butt strap (13) that blows fluidization gas and forms fluidized-bed into inclined surface. A heat exchanger tube (31) is equipped with furnace inner bottom face by-pass group (30L) which is arranged in space in which the maximum particle size of wood-coal raw material is passed. The dense space is formed in upper tube group of furnace which and is arranged from furnace inner bottom face by-pass group.    USE - Wood-coal fluidized bed dryer.    ADVANTAGE - The moisture in wood-coal is dried effectively by flow of fine grain by using characteristic of fluidized-bed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for drying method of wood-coal.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the moisture fuel flow mobile layer drying apparatus. (Drawing includes non-English language text)    Wood-coal fluidized bed dryer (10)    Interior furnace (12)    Butt strap (13)    Furnace inner bottom face by-pass group (30L)    Heat exchanger tube (31)
NOVELTY - The system (100) has a water containment vessel (110) having an enclosed housing forming a chamber with one or more openings for exhaust and/or pressure relief. One or more hydrogen and/or oxyhydrogen production devices are positioned within the chamber and submersed under water placed in the chamber. One or more bubblers (130), prime movers (140) and power collection devices (150) are also positioned within the chamber and submersed under water. A chemical reformation cell is comprised of opening for introduction of chemical elements from outside the chamber.    USE - Water submersed oxyhydrogen power generation system.    ADVANTAGE - The water-filled containment vessel reduces the risk of ignition since any leaked oxyhydrogen gas is likely to be neutralized by the containment water, and absorbs and contains the energy of any explosions that result from accidental ignition. The environmental noise pollution is reduced and the integrity and lifespan of adjacent infrastructure are prolonged, as the mass and volume of the containment water and vessel structure serve to contain and mitigate the spread of noise and vibrations produced by the prime movers and other components of the system. Temperature control is provided for the contained apparatus by the containment water. The utilization of inert gas for prime mover assists in controlling the volumetric flow rates and temperature of the fluid moving through the prime mover, permitting optimal control of the prime mover operations and maximizing energy conversion efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of producing energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the water submersed oxyhydrogen power generation system.    Water submersed oxyhydrogen power generation system (100)    Water containment vessel (110)    Bubbler (130)    Prime mover (140)    Power collection device (150)
NOVELTY - The sensor is provided to detect detection target gas based on resistance value of gas detection layer (14) heated by heater layer (12). The relationship between resistance value of gas detection layer measured in initial state and the gas concentration of detection target gas is defined by preset expression. A rectangular coordinate system is set with the resistance value and the gas concentration which uses two measuring points consisting of resistance value in an area which is 4000 ppm or more, when coefficient of preset equation and gradient coefficient are computed.    USE - Thin film type gas sensor for detecting target gas such as carbon monoxide, methane gas, propane gas, nitrogen and methanol vapor in atmosphere.    ADVANTAGE - The detecting ability of gas to be examined is maintainable over a long period of time. The thin film type gas sensor is selected over a long period of time in a product initial stage according to the inspection of the thin film type gas sensor.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an inspection method of the thin film type gas sensor.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the sensor device used with the thin film type gas sensor. (Drawing includes non-English language text)    Sensor device (2)    Silicon substrate (10)    Support layer (11)    Heater layer (12)    Gas detection layer (14)
NOVELTY - Method for preparing flatfish liquid fertilizer, involves collecting flatfish from market, crushing collected flatfish, adding crushed mixture into storage tank, adding molasses, lactic acid bacteria and yeast to the mixture, stirring the mixture, fermenting the stirred mixture, supplying air, and performing secondary fermentation of the mixture at room temperature for 4-7 months.    USE - The method is useful for preparing flatfish liquid fertilizer (claimed).    ADVANTAGE - The method prepares flatfish liquid fertilizer cost-effectively with high quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for flatfish liquid fertilizer, which is prepared by the method.
NOVELTY - A one circulating anaerobic fermentation marsh gas storage system, comprise controllable container fermentation room, desulfurization device, a gas storage device, a discharge tank and heating device, controllable fermentation room container set with a gas exit, exit and liquid reflux inlet, exit and a discharging tank through first liquid inlet connecting tube. The utility model is new type has reasonable design, simple structure, good sealing property, to prevent gas leakage, gas for power generation, heating and so on, for a sewage waste in anaerobic fermentation process stir uniform, which helps to increase efficiency and anaerobic fermentation marsh gas yield, and of the rear biogas anaerobic fermentation again by circulation, strong practicability and easy popularization and application.
NOVELTY - Circulating marsh gas anaerobic fermentation system, include excrement sewage tank, fermenting preprocessing tank, solar energy water heater, a controllable container fermentation room, a discharging tank and heater, excrement sewage pool inlet of exit of preprocessing tank connecting with the fermentation, fermenting the inlet of exit is connected with the controllable container room of preprocessing fermentation tank connecting water outlet of solar energy water heater and the fermentation preprocessing pool and a controllable container fermentation room of a water inlet connecting, controllable fermentation room container set with a gas exit, exit and liquid reflux inlet, exit and a discharging pool through third liquid inlet connecting tube, the utility model is new type has reasonable design, simple structure, good sealing property, a for excrement sewage in anaerobic fermentation process stir uniform, which helps to increase efficiency and anaerobic fermentation marsh gas yield, and rear anaerobic fermentation of the biogas slurry again by circulation, strong practicability and easy popularization and application.
NOVELTY - Circulating marsh gas anaerobic fermentation device, include a controllable container fermentation room, a discharging tank and a heater, a controllable container fermentation room set with marsh gas exit, exit and liquid reflux inlet, exit and a discharging tank through first liquid inlet connecting tube, a heater comprise a water tank, the bottom of hot water tank is set with methane combustion furnace, hot water tank is set with a water adding port and air vent, a water tank inner pipe, the inlet of heat exchange coil tube through second liquid tube is connected with the liquid outlet of the discharging tank connect, a second liquid tube set with second sewage pump, exit of coiled tube through liquid return port of third liquid tube is connected with the controllable container fermentation room connect. This utility new type has reasonable design, simple structure, good sealing property, a for excrement sewage in anaerobic fermentation process uniform stir, rear is helpful to increase efficiency and anaerobic fermentation marsh gas yield, and the anaerobic fermentation of biogas slurry again by circulation, strong practicability and easy popularization and application
NOVELTY - The present invention is directed to an improved one pot green catalytic process for the synthesis of 2, 3 ,6-trisubstituted pyridines by multi component reaction (3-MCR) of (E)-3-(dimethylamino)-1-aryl/heteroaryl/alkyl prop-2-en-1-one alkylacetoacetate ammonium acetate in the presence of catalytic amount of solid supported protic acid or metal Lewis acid as an catalyst .
NOVELTY - A primary reactant chosen from methyl (2E)-2-(2-((6-chloropyrimidin-4-yl)oxy)phenyl)-3-methoxyprop-2-enoate (II) and methyl 2-(2-((6-chloropyrimidin-4-yl)oxy)phenyl)-3,3-dimethoxyprop-2-enoate (III) and 2-cyanophenol or its salt as secondary reactant are reacted in presence of N-methyl pyrrolidinone solvent, to obtain methyl (E)-2-(2-(6-(2-cyanophenoxy)pyrimidin-4-yl-oxy)phenyl)-3-methoxyacrylate (I).    USE - Manufacture of methyl-2-(2-(6-(2-cyanophenoxy)pyrimidin-4-yl-oxy)phenyl)-3-methoxyacrylate (claimed).    ADVANTAGE - The method economically and environmentally-friendly provides methyl-2-(2-(6-(2-cyanophenoxy)pyrimidin-4-yl-oxy)phenyl)-3-methoxyacrylate having high recovery rate with high yield, without using catalyst.    DETAILED DESCRIPTION - A primary reactant chosen from methyl (2E)-2-(2-((6-chloropyrimidin-4-yl)oxy)phenyl)-3-methoxyprop-2-enoate of formula (II) and methyl 2-(2-((6-chloropyrimidin-4-yl)oxy)phenyl)-3,3-dimethoxyprop-2-enoate of formula (III) and 2-cyanophenol or its salt as secondary reactant are reacted in presence of N-methyl pyrrolidinone solvent, to obtain methyl-(E)-2-(2-(6-(2-cyanophenoxy)pyrimidin-4-yl-oxy)phenyl)-3-methoxyacrylate of formula (I).    Y'= -C(CO2CH3)=CHOCH3 or -CH(CO2CH3)CH(OCH3)2.
NOVELTY - Preparing dioscin involves crushing rhizoma Dioscoreae nipponicae, performing percolating extraction, and concentrating the ethanol extracting solution using macro-porous adsorption resin chromatography, collecting and concentrating the eluant, performing elution process using 25-35% aqueous methanol solution in C18 column, collecting the eluant, concentrating and drying the eluant, freezing and drying the obtained product.    USE - The method is useful for preparing dioscin used as a chemical reference substance (claimed).    ADVANTAGE - The method enables to prepare product cost-effectively, and simply, and which does not cause toxic effects.    DETAILED DESCRIPTION - Preparation of dioscin comprises crushing rhizoma Dioscoreae nipponicae, performing percolating extraction using 40-80% aqueous ethanol solution, combining the ethanol extracting solution, and concentrating the ethanol extracting solution, until there is no alcohol taste using macro-porous adsorption resin chromatography and 15-25%, or 40-60% methanol water solution, collecting the obtained eluant, and concentrating the eluant until there is no alcohol taste, adding acetone to the concentrated product, and separating precipitate, performing elution process using 25-35% aqueous methanol solution in C18 column, collecting the eluant, concentrating and drying the eluant, freezing and drying the obtained dioscin with purity of more than 98%.
NOVELTY - Hydrolyzing pleuromutilin comprises adding sulphuric acid solution to butyl acetate extraction liquid of pleuromutilin, heating to 80-90 degrees C, reacting for 5-6 hours, standing and layering, concentrating the butyl acetate phase upper layer in a vacuum at 60-70 degrees C, washing the concentrate with hot water 2-3 times, adding drying agent for dehydration, filtering, slowly cooling the filtrate to 0-5 degrees centigrade, separating the product, filtering and drying to obtain pleuromutilin hydrolyzate    USE - Method for hydrolysis of pleuromutilin (claimed).    ADVANTAGE - The method is suitable for industrial production, avoids using alkali which reduces operational risks, uses direct concentration and crystallization steps which reduces use of organic solvent, and has short production cycle, simple operation, high product yield, and less pollution.
NOVELTY - 6-Methoxy-7-hydroxy-quinazolin-4-one is prepared using 2-iodo(bromo)-4-methoxy-5-hydroxybenzonitrile and amidine hydrochloride as raw materials. 4-(3-Bromo-propyl)morpholine is introduced as alkyl side chain to obtain 7-methoxy-6-(3-(4-morpholinyl)propoxy)quinazolin-4-one. The obtained compound is reacted with a chlorinating agent to obtain 4-chloro-7-methoxy-6(3-(4-morpholinyl)propoxy)quinazoline. The obtained compound is reacted with 3-chloro-4-fluoroaniline, to obtain gefitinib.    USE - Microwave synthesis of gefitinib (claimed).    ADVANTAGE - The method enables simple, environmentally-friendly, safe, economical and convenient industrial microwave synthesis of gefitinib with high yield.
NOVELTY - Preparing valsartan involves mixing amide methyl ester sodium azide and the reaction solvent and then adding catalyst to the mixed material. The obtained material is preserved at room temperature and then the obtained material is reacted with tetrazole to obtain valsartan methyl ester as a white solid. The obtained material is distilled to remove solvent and then the distilled material is recrystallized to obtain raw material amide methyl ester. The valsartan methyl ester is subjected to alkali hydrolysis, acidification and extraction to obtain the desired product.    USE - Method for preparing valsartan (claimed).    ADVANTAGE - The method enables to prepare valsartan without producing toxic waste.
NOVELTY - An anacetrapib intermediate is synthesized by using 3,5-bis(trifluoromethyl)bromobenzene as raw materials, performing Grignard reaction with Weinrib amide to obtain tert.-butoxy carbamate (Boc)-protected ketone, performing ruthenium(II)-catalyzed asymmetric reduction with enantiomeric excess of greater than or equal to 99% to obtain (1R,2S)-1-(3,5-bis(trifluoromethyl)phenyl)-2-Boc-aminopropanol, and performing ring-closing reaction under alkaline conditions to obtain 5-(3,5-bis(trifluoromethyl)phenyl) methyl-1,3-oxazolidin-2-one.    USE - Synthesis of anacetrapib intermediate (claimed).    ADVANTAGE - Synthesis process has low cost and mild reaction conditions and is environment-friendly. Product has high selectivity and increased drug purity.    DETAILED DESCRIPTION - An anacetrapib intermediate is synthesized by using 3,5-bis(trifluoromethyl)bromobenzene of formula (1) as raw materials, performing Grignard reaction with Weinrib amide of formula (2) to obtain tert.-butoxy carbamate (Boc)-protected ketone of formula (3), performing ruthenium(II)-catalyzed asymmetric reduction with enantiomeric excess of greater than or equal to 99% to obtain (1R,2S)-1-(3,5-bis(trifluoromethyl)phenyl)-2-Boc-aminopropanol of formula (4), and performing ring-closing reaction under alkaline conditions to obtain 5-(3,5-bis(trifluoromethyl)phenyl) methyl-1,3-oxazolidin-2-one of formula (A)..
NOVELTY - 2-ethoxy-3-((4-(2-(1H-tetrazol-5-yl)phenyl)phenyl)methyl)-3H-benzimidazole-4-carboxylic acid (candesartan cilexetil C8) is prepared by mixing ethyl-2-ethoxy-1-(((2-cyanobiphenyl-4-yl)methyl)benzimidazole)-7-carboxylate (candesartan cilexetil C6), sodium azide, and solvent, adding inorganic ammonium salt, reacting less than or equal to 50% tetrazolium, cooling, filtering to obtain white solid 1H-benzimidazole-7-carboxylic acid,1-((2'-cyano(1,1'-biphenyl)-4-yl)methyl)-2-ethoxy-ethyl ester (candesartan cilexetil C7), distilling mother liquor to remove solvent, and adding lower carbon alcohol.    USE - Preparation of 2-ethoxy-3-((4-(2-(1H-tetrazol-5-yl)phenyl)phenyl)methyl)-3H- benzimidazole-4-carboxylic acid for antihypertensive drug.    ADVANTAGE - Process is environment-friendly, does not generate highly toxic wastewater, and has low production cost.    DETAILED DESCRIPTION - Candesartan cilexetil C8 is prepared by mixing candesartan cilexetil C6, sodium azide, and solvent, adding inorganic ammonium salt, reacting less than or equal to 50% tetrazolium, cooling, filtering to obtain white solid candesartan cilexetil C7, distilling mother liquor to remove solvent, adding lower carbon alcohol or lower carbon carboxylic acid ester, cooling, filtering, recovering unreacted candesartan cilexetil C6, hydrolyzing candesartan cilexetil C7 in sodium hydroxide aqueous solution, and acidifying.
NOVELTY - Methoxybenzyl 7-phenylacetamido-3-chloromethy-3-cephem-4-carboxylatee preparation involves mixing sodium iodide, triphenylphosphine, and formaldehyde solution with methylene chloride, acetone and water, where methylene chloride is added to dissolve the obtained precipitate. Acetone is recovered from the organic layer to obtain desired product.    USE - Method for preparing methoxybenzyl 7-phenylacetamido-3-chloromethy-3-cephem-4-carboxylate (claimed).    ADVANTAGE - The method enables to prepare methoxybenzyl 7-phenylacetamido-3-chloromethy-3-cephem-4-carboxylate in an eco-friendly, cost-effective, and convenient manner.
NOVELTY - An amino-containing crosslinked polyarylethersulfone (I), is new.    USE - New amino-containing crosslinked polyarylethersulfone is used for preparing amino-containing crosslinked polyarylethersulfone film/thermally-crosslinked film, and amino-containing crosslinked polyarylethersulfone/carbon nanotube gas separation membrane or thermally-crosslinked gas separation membrane (all claimed).    ADVANTAGE - The gas separation membrane formed using the amino-containing crosslinked polyarylethersulfone has excellent gas permeability and selectivity.    DETAILED DESCRIPTION - An amino-containing crosslinked polyarylethersulfone of formula (I), is new.    n=more than 0 and 0.3 or less;    A=group of formula (i);and    m=0.6 or more and less than 0.9.    INDEPENDENT CLAIMS are included for the following:    (1) preparation of amino-containing crosslinked polyarylethersulfone (I);    (2) usage of amino-containing crosslinked polyarylethersulfone (I) for preparing amino-containing crosslinked polyarylethersulfone film or amino-containing crosslinked polyarylethersulfone thermally-crosslinked film; and    (3) usage of amino-containing crosslinked polyarylethersulfone (I) for preparing amino-containing crosslinked polyarylethersulfone/carbon nanotube gas separation membrane or amino-containing crosslinked polyarylethersulfone/carbon nanotube thermally-crosslinked gas separation membrane, which involves using amino-containing crosslinked polyarylethersulfone (I) as substrate and carboxylic acid-modified carbon nanotubes as filler.
NOVELTY - Device comprises raw material inlet (1), raw material cutting device (2), material conveyer belt (3), filter net (4), rain cover (5), silo (6), horizontal grate furnace microwave pyrolysis device (7), feeding sealing device (8), discharging sealing device (9), porous metal filter (10), condensing device (11), gas cylinders (12), oil storage tank (13), pump (14), spray shower (15), rotary steam condenser (16), motor (17), activated carbon storage box (18), gas-solid heat exchanger (19), fans (20), horizontal grate cover microwave pyrolysis unit (21) and inside cover of microwave generator (23).    USE - Device used for preparing bio-oil, activated carbon and combustible gas from biomass (claimed).    DESCRIPTION OF DRAWING(S) - The drawing shows a structure schematic diagram of device.    Raw material inlet (1)    Raw material cutting device (2)    Material conveyer belt (3)    Filter net (4)    Rain cover (5)    Silo (6)    Horizontal grate furnace microwave pyrolysis device (7)    Feeding sealing device (8)    Discharging sealing device (9)    Porous metal filter (10)    Condensing device (11)    Gas cylinders (12)    Oil storage tank (13)    Pump (14)    Spray shower (15)    Rotary steam condenser (16)    Motor (17)    Activated carbon storage box (18)    Gas-solid heat exchanger (19)    Fans (20)    Horizontal grate cover microwave pyrolysis unit (21)    Inside cover of microwave generator (22)
NOVELTY - Active sludge treatment involves discarding the supernate by rotating the active sludge at 5000 rotations per minute. The obtained product is ultrasonically treated with hydrochloric acid. The obtained product is extracted by adding dichloromethane and methanol solvent. The obtained mixture is esterified by adding sulfuric acid. The obtained esterified mixture is extracted by adding normal hexane solvent to obtain desired product.    USE - Method for treating active sludge used for preparing biological diesel oil (claimed).    ADVANTAGE - The method enables to treat active sludge in a cost-effective manner.
NOVELTY - A co-solvent for extraction of oil sand at normal temperature comprises 30-60 mass% carbon disulfide, 15-50 mass% , methyl tertiary-butyl ether, 5-10 mass% toluene, 2-16 mass% petroleum ether, 2-3 mass% n-heptane, 1-3 mass% n-pentane and 1-2 mass% cyclohexane. Carbon sulfide and , methyl tertiary-butyl ether are added to reaction tank, and stirred. Toluene, petroleum, n-heptane, n-pentane and cyclohexane are added to mixture and stirred uniformly to obtain co-solvent.    USE - Co-solvent used for extracting oil sand at normal temperature (claimed).    ADVANTAGE - The co-solvent is easy to control, and has good dissolubility, and enables simple, inexpensive and effective extraction of asphalt oil under normal conditions with high recovery rate of asphalt.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for extracting oil sand at normal temperature, which involves crushing oil sand using 40 mesh sieve to obtain granules, selecting oil sand granules, adding the co-solvent and oil sand granules in mass ratio of 0.6-1to extracting tank, stirring the mixture at normal temperature for 30-50 minutes, separating the mixture to solid and liquid with centrifuge, distilling obtained supernatant with distillation tower to obtain asphalt oil, drying the obtained solid at 100 degrees C to obtain clean sand, and determining content of clean sand and asphalt oil.
NOVELTY - A centralized gas supply device for pyrolysis and biomass gasification which fully utilizes rural straw waste, dead wood, and other plant resources comprises preprocessing part, gas generation part, and gas transmission and distribution part.    USE - A centralized gas supply device for pyrolysis and biomass gasification (claimed).    ADVANTAGE - Gasification efficiency is increased, pipeline blockage is reduced which avoids secondary pollution, and purification rate is high.
NOVELTY - The device has a pyrolysis reactor (1) fixed on a combustion reactor (2) and provided with a feeding port (1A) and a pyrolysis pneuma exit (1B). The combustion reactor is provided with an air-circulation bed material inlet (2A) and a secondary air inlet (2B). A gasification reactor (3) is provided with a coke inlet (3A) and a steam inlet (3B). A circulation bed material exit part (2C) is connected with a cyclone separator (4). The air-circulation bed material inlet is connected with a gas cooler (6). A waste heat boiler (7) is connected with the gasification reactor via a pipeline.    USE - Biomass gasification-type enriched gas such as hydrogen, carbon dioxide and carbon monoxide producing device.    ADVANTAGE - The device ensures pyrolysis and coke gasification process and realizes full utilization rate of fixed carbon so as to effectively obtain hydrogen-rich gas. The device obtains hydrogen-enriched gas product from normal gasification mixed low carbon hydrocarbon gas and tar so as to improve subsequent purification efficiency with simple and convenient operation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biomass gasification-type enriched gas such as hydrogen, carbon dioxide and carbon monoxide producing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a biomass gasification-type enriched gas producing device. '(Drawing includes non-English language text)'    Pyrolysis reactor (1)    Feeding port (1A)    Pyrolysis pneuma exit (1B)    Combustion reactor (2)    Air-circulation bed material inlet (2A)    Secondary air inlet (2B)    Circulation bed material exit part (2C)    Gasification reactor (3)    Coke inlet (3A)    Steam inlet (3B)    Cyclone separator (4)    Gas cooler (6)    Waste heat boiler (7)
NOVELTY - An alcohol-based fuel comprises 85-95 pts. wt. methanol, 2-8 pts. wt. ethanol, 2-5 pts. wt. tertiary butyl alcohol, 1-2 pts. wt. paraffin oil, 0.2-0.5 pt. wt. ferric chloride, 0.2-0.5 pt. wt. methyl tertiary butyl ether and 0.05-0.1 pt. wt. ethyl acetate.    USE - Alcohol-based fuel.    ADVANTAGE - The fuel is energy efficient.
NOVELTY - An environment-friendly bio-oil comprises 65-70 wt.% No.97 gasoline, 5-10 wt.% methanol, 0.2-0.5 wt.% ethanol, 3-15 wt.% combustion improver, 0.1-0.5 wt.% antioxidant, 0.003-0.1 wt.% fast burning agent, 7-10 wt.% bio-oil and 1 wt.% antiexplosion liquid.    USE - Environment-friendly bio-oil.    ADVANTAGE - The oil is low-cost and energy efficient.
NOVELTY - Refined biodiesel oil is prepared by pretreating waste oil, adding acidic catalyst and emulsifying agent into pretreated waste oil, regulating temperature at 60-130 degrees C, passing into volatile organic compound (VOC) of paint exhaust gas and gas phase methanol, performing esterification reaction for 5-10 hours, standing to obtain crude biodiesel oil, adding liquid methanol and solid alkaline catalyst into obtained crude biodiesel oil with mass ratio of 70-80:5-25:1-5, regulating reaction temperature at 50-65 degrees C, and stirring for 0.5-2 hours under atmospheric pressure.    USE - Preparation of refined biodiesel oil for free fatty acid and high moisture content oil, such as cooking oil.    ADVANTAGE - Process has high production yield, and product has improved calorific value.    DETAILED DESCRIPTION - Refined biodiesel oil is prepared by pretreating waste oil, adding acidic catalyst and emulsifying agent into pretreated waste oil, regulating temperature at 60-130 degrees C, passing into VOC of paint exhaust gas and gas phase methanol, performing esterification reaction for 5-10 hours, standing to obtain crude biodiesel oil, adding liquid methanol and solid alkaline catalyst into obtained crude biodiesel oil with mass ratio of 70-80:5-25:1-5, regulating reaction temperature at 50-65 degrees C, stirring for 0.5-2 hours under atmospheric pressure, completing transesterification reaction, centrifuging or standing reaction product, collecting upper layer, distilling, and collecting vapor at 250-330 degrees C in which mass ratio acidic catalyst:methanol:VOC of paint exhaust gas:emulsifying agent is 100:0.2-5:10-20:10-20:0.5-2.
NOVELTY - Shaking type biogas digester has a box shaped waste slurry holding tank (3) attached with a hand stirrer (5), and an air outlet tube (7), where the tank, stirrer and tube are made of plastic material.    USE - Shaking type biogas digester (claimed).    ADVANTAGE - The biogas digester has high durability as the components are made of plastic material that does not rust even when immersed in water or septic tanks for long period. Damage of the box and stirrer while shaking process and leakage of biogas are prevented with the use of screw cap. The digester is energy-saving and environmentally-friendly, and enables to completely release methane by digesting the waste.    DESCRIPTION OF DRAWING(S) - The drawing shows shaking type biogas digester.    Box shaped waste slurry holding tank (3)    Thread type plastic screw cap (4)    Hand stirrer (5)    Air outlet tube (7)
NOVELTY - The system has a marsh gas fermentation tank, an overflow tube (1), a overflow device (2), and pipe supports. Overflow tube of the port is inclined downwards at one end, and connects with the marsh gas fermentation tank. The other end of the overflow tube is connected with the overflow device. The overflow device is set with biogas tube a (5) and biogas tube b (6), liquid inlet of biogas tube a is lower than the liquid inlet of biogas tube b, and biogas tube a is mounted with a sluice valve (7) and electric valve (8).    USE - Double pipe-type methane fermentation tank overflow system.    ADVANTAGE - Prevents pipeline blockage, and increases fermentation efficiency by the activated sludge inner tank.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram double pipe-type methane fermentation tank overflow system.    Overflow tube (1)    Overflow device (2)    Biogas tube a (5)    Biogas tube b (6)    Sluice valve (7)    Electric valve (8)
NOVELTY - Device comprises a main body (1), an upper cover (2), a circulation pump (3), a water pipe (4) and a valve (7). The main body is provided with a pump and a water pipe, where the waste water is collected in the water tank. The main body is set with a solid-phase reaction area (11) and a liquid phase reaction area (12). The liquid phase reaction area comprises lower screen stencil (12-1) and a filler screen (12-2).    USE - Device used for treating kitchen garbage.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a device.    Main body (1)    Upper cover (2)    Circulation pump (3)    Water pipe (4)    Valve (7)    Solid-phase reaction area (11)    Liquid phase reaction area (12)    Lower screen stencil (12-1)    Filler screen (12-2)
NOVELTY - Multi-level balance biogas tank comprises tank body, arc-shaped top tank (1) and collecting tube. The tank top (1) as main tube is at least two set pneuma room of clapboard. The gas collecting tube comprise outer of the marsh gas tank, the branch tube corresponding to a set pneuma room number. The branch tube one end connected main tube on the arc-shaped tank top (1) inner set with a certain number of, in the other end is inserted in tank body through the arcshaped top part is connected to the corresponding set of pneuma room.    USE - As multi-level balance biogas tank (claimed).    ADVANTAGE - The multi-level balance biogas tank produces circular arc smooth transition which reduces a stress, use long life, can be joint without stopping maintenance, balances gas, not taking up the ground, the tank top is a multipneuma room, multi-set air outlet tube, if a certain pneuma room air, would not influence working of other pneuma room, increase continuity of penjiao mechanism for flushing in a marsh gas tank, the crust to increase.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic diagram of multi-level balance biogas tank.    Arc-shaped top tank (1)    Pneuma hole (3)    Tank body (4) (4)    Discharge hole (5)    Heating tube (6)
NOVELTY - Method for ultrasonic/acid pretreatment-enhanced anaerobic fermentation of kitchen garbage, involves (a) processing and crushing kitchen garbage, adding water to the kitchen garbage to adjust total solid content of the crushed kitchen garbage to 25-35 g/l, and obtaining mixed liquid of kitchen garbage, (b) placing the mixed liquid of kitchen garbage in reaction container, performing ultrasonic pretreatment and acid treatment, and obtaining solution of kitchen garbage, and (c) performing anaerobic fermentation, and inoculating sludge during fermentation.    USE - The method is useful for ultrasonic/acid pretreatment-enhanced anaerobic fermentation of kitchen garbage (claimed).    ADVANTAGE - The method, releases largest extent of solid phase organic matter to liquid phase under optimum control conditions, and produces volatile fatty acid with 70% or more conversion ratio.    DETAILED DESCRIPTION - Method for ultrasonic/acid pretreatment-enhanced anaerobic fermentation of kitchen garbage, involves (a) collecting kitchen garbage, removing oil of kitchen garbage, crushing the kitchen garbage using electric stirrer, adding water to the crushed kitchen garbage to adjust total solid (TS) content of the crushed kitchen garbage to 25-35 g/l, and obtaining mixed liquid of kitchen garbage, (b) placing the mixed liquid of kitchen garbage in reaction container, regulating ultrasonic energy at a density of 0.25-1.25 W/ml, performing ultrasonic pretreatment for 5-30 minutes, then adding acid solution to adjust pH of the pretreated kitchen garbage to 1-5, performing acid treatment for 10-24 hours, and obtaining solution of kitchen garbage, and (c) adding the solution of kitchen garbage in bottle, performing anaerobic fermentation, and inoculating sludge during fermentation to obtain product.
NOVELTY - Preparing L-lactic acid involves mixing sludge and organic waste to obtain mixture, where organic waste comprises carbohydrate fermented organic waste. The obtain mixture is concentrated and then water is added to obtain another mixture. Anaerobic fermentation is performed in alkaline condition to obtain supernatant.    USE - Method for preparing L-lactic acid (claimed).
NOVELTY - Biological diesel oil preparation involves using lipase gene, recombinant vector and expression host, where lipase gene is provided as starting material. The obtained gene is cultured in situ and then added with exogenous grease. The reaction substrate is processed catalytically to obtain desired product.    USE - Method for preparing biological diesel oil (claimed).    ADVANTAGE - The method enables to prepare biological diesel oil in a simple, eco-friendly and cost-effective manner.
NOVELTY - Method of using dissimilatory metal reducing bacteria to promote methanogen for producing methane involves taking anaerobic digestion sludge, bottom sediments, and/or sewage as inoculum, screening methanogen in anaerobic digestion sludge and/or bottom sediments, centrifuging dissimilatory metal reducing bacteria having 1x 1010 cells/ml concentration, and mixing with methanogen and anaerobic digestion sludge in volume ratio of 3:3:4, in an anaerobic fermentation tank.    USE - The method is useful for producing methane using dissimilatory metal reducing bacteria to promote methanogen (claimed).    DETAILED DESCRIPTION - Method of using dissimilatory metal reducing bacteria to promote methanogen for producing methane involves taking anaerobic digestion sludge, bottom sediments, and/or sewage as inoculum, screening methanogen in anaerobic digestion sludge and/or bottom sediments, centrifuging dissimilatory metal reducing bacteria having 1x 1010 cells/ml concentration, and mixing with methanogen and anaerobic digestion sludge in volume ratio of 3:3:4, in an anaerobic fermentation tank. The dissimilatory metal reducing bacteria are one or more of Geobacter sp., Shewanella sp. and Rhodoferax ferrireducens.
NOVELTY - This utility new type claims a one of combustion device of biomass fuel hot air furnace, comprise combustion room, combustion room set with feeding port and waste exit, a combustion room outer side is surrounded with air distribution room, air distribution room and burning room and set with air inlet, a combustion chamber is further set with air outlet, air outlet cover set with an upper cover plate, a cover plate is provided with an air outlet aperture is less than the aperture of the through hole, the through hole is the air outlet, futher of combustion chamber is columnar structure set, one end of room is set with opening, and the other end the combustion room of sealing set, wind room towards a combustion chamber sealing end surface set with a fan mechanism, set at the opening. This utility new type reasonable structure, the hot air, and a valid by using heat, reducing a heat loss.
NOVELTY - This new type utility claims one a biomass granule drying device, aiming to provide a one biomass raw material a water evaporation and drying uniformity of biomass granule drying device. The biomass drying device comprise a set in turn from front to rear of a biomass combustion machine (1), a rotate device (2), exhaust fan (3), a separate device and flue gas (4) and a raw material input device (5), a device (6), a biomass granule burner (1) of smoke pneuma exit through conveying pipeline (7) and a rotate device a (2) is connected, a raw material input device (5) is located in said conveying pipeline (7), a feeding port, a rotate said device (2) of rear end and said exhaust fan (3) of entrance is connected with a exhaust fan (3) of the said granule with the flue gas exit separate device (4), a material output device (6) is located in said a and flue gas separate device (4) of the material outlet.
NOVELTY - Methane synthesis involves feeding gas purification operation, refrigerant compression operation, liquefaction operation, and liquefied natural gas storage operation, where feeding gas purification operation involves conveying the feeding gas to drying chamber for drying and filtration process. The obtain gas is free from water molecules and conveyed to refrigerant compression chamber, which is provided with nitrogen gas for cooling operation. The refrigerant compression chamber is provided with a compressor, a cooler and a buffer tank.    USE - Method for synthesizing liquefied natural gas (claimed).    ADVANTAGE - The method enables to synthesize liquefied natural gas in an energy-saving manner.    DETAILED DESCRIPTION - Methane synthesis involves feeding gas purification operation, refrigerant compression operation, liquefaction operation, and liquefied natural gas storage operation, where feeding gas purification operation involves conveying the feeding gas to drying chamber for drying and filtration process. The obtain gas is free from water molecules and conveyed to refrigerant compression chamber, which is provided with nitrogen gas for cooling operation. The refrigerant compression chamber is provided with a compressor, a cooler and a buffer tank. The nitrogen gas enters into the buffer tank for enhancing the buffering operation. The obtain gas is conveyed to liquefaction operation for purification process. The purified gas subjected to cryogenics process in a cryogenic chamber, which is provided with a heat exchanger, gas-liquid separation tank, and distillation column. The obtain gas is cooled and conveyed to gas-liquid separation tank and then conveyed to distillation column where hydrogen and nitrogen gases are separated from the bottom of the distillation column. The obtained distilled gas is conveyed to storage chamber. The storage chamber is provided with controlling chamber and distributed control system.
NOVELTY - This utility new type claims a one burning method gas thermal measuring device of distribution pneuma.. The system comprises gas storage pneuma small ball inflation pipeline and combustion distribution pneuma pipeline. Pneuma storage small ball inflation time firstly using vacuum pump ball and the pipeline inside. The inflation ball and the pipeline off rear mass balance with a ball and a charging gas of total quality, the consumption of gas mass a mass difference through a combustion and inflation ball obtain. Combustion time measuring, firstly using argon pneuma flushing gas pipeline, according to the opening of the combustion heat in a heat medium temperature control pipeline total electromagnetic valve, ending stage prior to the crossover valve closing fuel gas electromagnetic valve, a flame pipe total valve closing the rear, the pneuma storage small ball of gas possible from the participant. This utility new type a gas quality measure, a fuel gas-oxygen-argon pneuma and flow rate regulating ratio, realize the test process according to fast open and cut off fuel-oxygen-argon mix pneuma of pneuma.
NOVELTY - Preparation of high-performance biomass activated carbon fiber involves immersing cylinder sponge loofah in sodium hydroxide aqueous solution, washing until washing liquid becomes neutral, drying, mixing alkali-treated dry sponge and water-soluble phenolic resin, fully impregnating, dip-drying, pre-oxidizing obtained modified loofah, carbonizing obtained loofah to obtain biomass activated carbon fiber, processing the biomass activated carbon fiber with diluted acid to remove ash product, washing using water until washing liquid becomes neutral, and drying.    USE - Preparation of high-performance biomass activated carbon fiber used as filter material and electrode.    ADVANTAGE - The high-performance biomass activated carbon fiber having high compressive strength is economically prepared by environmentally-friendly method.    DETAILED DESCRIPTION - Preparation of high-performance biomass activated carbon fiber involves immersing cylinder sponge loofah in sodium hydroxide aqueous solution, washing until washing liquid becomes neutral, drying to obtain alkali-treated dry sponge, mixing the alkali-treated dry sponge and water-soluble phenolic resin, fully impregnating for 24-48 hours, dip-drying, pre-oxidizing obtained modified loofah for 2 hours under protection of inert gas, carbonizing obtained loofah, to obtain biomass activated carbon fiber, processing the biomass activated carbon fiber with diluted acid to remove ash product, washing using water until washing liquid becomes neutral, and drying.
NOVELTY - Solid alkali catalyst composition comprises 0.4-2.2% calcium, 53-59% magnesium, and 40-45% oxide.    USE - The composition is used in preparing biodiesel oil (claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) preparing solid alkali catalyst composition comprising dissolving calcium salt and magnesium salt in deionized water and preparing solution, then adding dispersant, adding precipitator to adjust pH to 10-11, under water bath environment, stirring, carrying out ultrasonic treatment, allowing it to stand and aging, filtering and washing the suspension until filtered liquid is neutral, drying the white precipitate, grinding and sieving, and calcining to obtain calcium-magnesium complex oxide, i.e. complex solid alkali catalyst;    (2) use of solid alkali catalyst composition in preparing biodiesel oil; and    (3) preparing biodiesel oil, comprising adding oil, methanol and solid alkali complex catalyst in the reaction kettle, reacting at nitrogen atmosphere, heating, stirring, filtering, allowing it to stand and layering, taking the upper layer crude diesel oil and carrying out vacuum distillation to obtain the biodiesel oil.
NOVELTY - Fertilizer comprises 40-50 pts. wt. humic acid, 10-20 pts. wt. urea, 5-8 pts. wt. ferrous sulfate, 6-10 pts. wt. potassium sulfate, 3-6 pts. wt. zinc sulfate, 3-6 pts. wt. magnesium sulfate, 3-6 pts. wt. borax, 20-30 pts. wt. acidified bone cement, 10-15 pts. wt. fermented pine needle powder, 0.01-0.03 pt. wt. molasses, 1-3 pts. wt. plant growth inducing agent, and 0.03-0.07 pt. wt. fermentation bacteria.    USE - The fertilizer is useful for improving soil quality, stimulating growth of crops, and increasing product quality.    ADVANTAGE - The fertilizer improves growth rate of vegetables by 9.5-10.5%, and apple and peach by more than 8.3%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves mixing urea, potassium sulfate, zinc sulfate, magnesium sulfate and borax to obtain mixture, sifting the mixture using a sieve to obtain product having particle size of 80 mesh, adding humic acid, acidified bone cement, fermented pine needle powder, plant growth inducing agent to the product, uniformly stirring added materials to obtain fertilizer, and packing obtained solid fertilizer.
NOVELTY - Fertilizer comprises 10-30 wt.% animal excrement, 10-30 wt.% corn stalks, 10-30 wt.% common mineral soil, 5-15 wt.% potato powder, 5-15 wt.% wheat bran, 1-5 wt.% chitosan, 1-3 wt.% magnesium sulfate, 1-3 wt.% salt, 1-3 wt.% enzyme, and 1-3 wt.% organic fertilizer fermenting agent.    USE - As fertilizer.    ADVANTAGE - The fertilizer is green and rich in amino acids.
NOVELTY - Use of Phytolacca acinosa, a manganese hyperaccumulator plant is claimed in preparation of organic fertilizer. The preparation method involves (a) harvesting P.acinosa; (b) adding suitable amount of dextrin and spraying with resveratrol; (c) adding white rot fungi culture liquid to the processed P.acinosa; (d) adding rapeseed cake powder to culture material; (e) adding suitable amount of complex microbial strains; (f) composting the mixture; and (g) mixing with granulating agent and formulating mixture to obtain product.    USE - The P.acinosa is useful for preparing organic fertilizer for restoring manganese in plants (claimed).    DETAILED DESCRIPTION - Use of manganese hyperaccumulator plant, preferably Phytolacca acinosa is claimed in preparation of organic fertilizer. The preparation method involves (a) harvesting P.acinosa during late flowering phase, drying and crushing to obtain 10-20 mm size fragments and piling the crushed fragments; (b) adding suitable amount of dextrin to the piled material and spraying with resveratrol; (c) adding white rot fungi culture liquid to the processed P.acinosa, and culturing for 15 days, where the lignin and cellulose in the plant is pretreated; (d) adding rapeseed cake powder to the obtained culture material and homogenizing obtained mixture; (e) adding suitable amount of complex microbial strains to the obtained culture material and performing turning of culture material with adequate ventilation; (f) composting the mixture to obtain decomposed organic fertilizer; and (g) mixing the decomposed organic fertilizer with suitable amount of granulating agent and formulating mixture to obtain product.
NOVELTY - Base is added to methanol solution of hydroxylamine salt at 45 degrees C or less under stirring, organic carboxylic acid methyl ester (I) or (II) is added, and reacted at 30-70 degrees C for 2-6 hours. The reaction solution is distilled and methanol is recovered, to obtain hydroxamate (III) or (IV). The reaction solution is cooled to less than 30 degrees C, sulfuric acid is added and distilled to recover methanol, to obtain hydroxamic acid (V) or (VI).    USE - Preparation of hydroxamic acid or isohydroxamate (claimed).    ADVANTAGE - The method enables preparation of hydroxamic acid or isohydroxamate with high yield under mild reaction conditions. Generation of wastewater is suppressed during preparation of hydroxamic acid or isohydroxamate.    DETAILED DESCRIPTION - Base is added to methanol solution of hydroxylamine salt at 45 degrees C or less under stirring, organic carboxylic acid methyl ester of formula (I) or (II) is added, and reacted at 30-70 degrees C for 2-6 hours. The reaction solution is distilled and methanol is recovered, to obtain hydroxamate of formula (III) or (IV). The reaction solution is cooled to less than 30 degrees C, sulfuric acid is added and distilled to recover methanol, to obtain hydroxamic acid of formula (V) or (VI).    M=alkali metal atom;    R=5-21C alkyl;and    X=H or hydroxy.
NOVELTY - Method for preparing fungicide using bran and rice hull, involves uniformly mixing bran and rice hull, sugar to water and yeast spore, yeast and Acetobacter xylinum, fermenting sugar solution and bacteria, adding above-cited components in layer by layer to fermenting tank and fermenting mixture, and filtering fermented product.    USE - wheat grain blight, cucumber downy mildew, rice sheath blight, apple anthracnose, downy mildew, phytophthora early blight, tobacco brown spot disease (all claimed).    ADVANTAGE - The method is simple, suitable for mass production and environment-friendly, and has no pesticide residue.    DETAILED DESCRIPTION - Method for preparing fungicide using bran and rice hull, involves uniformly mixing the bran and rice hull in ratio of 5-8:1, then mixing sugar to water in ratio of 1:10-20 to form sugar solution, then mixing the yeast spore, yeast and Acetobacter xylinum in ratio of 0-5:0-5:0-5, fermenting sugar solution and bacteria mix in ratio of 80-100:1, adding above-cited components in layer by layer to fermenting tank and fermenting for 26-30 degrees C for 15-20 days, adding sodium hydroxide to fermented liquid for regulating pH value to 6-8, and filtering to obtain flavonoids containing apigenin, 5-alkyl resorcinols, 5-pentadecyl resorcinol, heneicosanoic acid, resorcinol, pentosan sugars, chitosan, oligosaccharin, amino oligosaccharins, lentinan, and mixture of glucose sugar.
NOVELTY - Bactericide is prepared using bran by dissolving sugar in water to form sugar water, mixing Barley yeast, yeast and Acetobacter xylinum in broth, mixing sugar water and mixed bacterial solution to obtain mixture, paving bran layer in fermentation tank, uniformly spraying mixture on each layer, fermenting, filtering to obtain fermentation liquid and solid slag, adjusting pH of fermentation liquid, filtering to obtain e.g. flavonoids, alkylresorcinol, pentosan polysaccharide, chitosan, and oligosaccharin mixture, and preparing plant-based agricultural bactericide using mixture.    USE - Preparation of bactericide using bran for wheat sheath blight, cucumber downy mildew, rice sheath blight, apple anthracnose, pepper blight, tomato early blight, and tobacco brown spot disease (all claimed).    ADVANTAGE - Process is environment-friendly, simple, and yields agriculturally safe product without pesticide residues.    DETAILED DESCRIPTION - Bactericide is prepared using bran by dissolving sugar in water with ratio of 1:10-20 to form sugar water, mixing Barley yeast, yeast and A. xylinum in broth with ratio of 0-5:0-5:0-5, mixing sugar water and mixed bacterial solution with ratio of 80-100:1 to obtain mixture, paving bran layer in fermentation tank, uniformly spraying mixture on each layer, fermenting at constant temperature of 26-30 degrees C for 15-20 days, filtering to obtain fermentation liquid and solid slag, adjusting pH of fermentation liquid to 6-8 using sodium hydroxide, filtering to obtain flavonoids such as apigenin, alkylresorcinol, such as 5-nonadecyl resorcinol, 5-heneicosanyl resorcinol, 5-tricosanyl resorcinol, pentosan polysaccharide, chitosan, oligosaccharin, amino oligosaccharin, lentinan, and polyallyl glucose mixture, and preparing plant-based agricultural bactericide using mixture.
NOVELTY - Producing insect protein powder and bio-organic fertilizer comprises crushing plant fiber auxiliary material, mixing gibberellins fermentation residue and plant fiber auxiliary material powder in a fermenting tank, inoculating active dry yeast into the fermenting tank, then carrying out anaerobic fermentation to obtain maggot culture material, cultivating by inoculating housefly eggs into the maggot culture material and then separating living maggots and fermentation residue, drying and then crushing maggots to obtain insect protein powder, and drying the fermentation residue.    USE - The method is useful for producing bio-organic fertilizer, and insect protein powder (claimed). The insect protein powder is useful in feed additive for poultry or fish.    ADVANTAGE - The method is capable of producing high quality bio-organic fertilizer without any pesticide residue, harmful substances and peculiar smell, and insect protein powder with 50-60% of protein content.    DETAILED DESCRIPTION - Producing insect protein powder and bio-organic fertilizer comprises crushing plant fiber auxiliary material of 4 cm in length with a crusher into powder having diameter of less than 0.6 mm, uniformly mixing 10-60 wt.% of gibberellins fermentation residue having moisture content of 60-70% and plant fiber auxiliary material powder in a fermenting tank, inoculating 0.1-1 wt.% of active dry yeast into the fermenting tank and then sealing the tank with a plastic film, then carrying out anaerobic fermentation to obtain maggot culture material, inoculating 1-5 g of housefly eggs into the maggot culture material, then cultivating at 20-35 degrees C for 3-6 days and then separating living maggots and fermentation residue, drying the maggots at 80 degrees C and then crushing to obtain insect protein powder, and drying the fermentation residue until the water content is 12-15% to obtain organic fertilizer.
NOVELTY - A selenium-enriched walnut fertilizing method comprises adding 5-10 kG organic selenium-enriched fertilizer to walnut tree 4 times; applying once from October to November, following year in March, next in May to June and finally August to September.    USE - Selenium-enriched walnut fertilizing method (claimed).    ADVANTAGE - The method is low-cost and environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of selenium-enriched fertilizer comprising taking 3-6 pts. wt. walnut green husk, 1-3 pts. wt. peach branch, 1-2 pts. wt. walnut, 2-4 pts. wt. corn stalks and 8-15 pts. wt. selenium material, crushing, stirring, taking 1-2 pts. wt. bran, 2-4 pts. wt. grass powder and 0.5-1.5 pts. wt. calcium carbonate, adding crushed powder mixture, stirring, adding water and lime, regulating pH to 6.5-7.5, adding 0.01-0.04 pt. wt. Trichoderma and 0.01-0.04 pt. wt. Aspergillus oryzae, stirring, covering in plastic thin film, fermenting for 7-15 days, turning once in morning and afternoon, adding 0.005-0.01 pt. wt. Bacillus subtilis and 0.002-0.005 pt. wt. yeast, stirring, covering in plastic thin film, fermenting for 3-5 days, and turning once in morning and afternoon.
NOVELTY - This utility new type relates to a one organic waste pneuma of integrated processing device, said device comprise air washing unit and a bioreactor, a washing air recovery unit comprise liquid connected by a tube connecting the bottom of washing tower, an air-floating tower and washing tower and air floatation tower via the circulation pump together forming a closed loop of cooler and air washing tower top of the rectifying tower are set with an air outlet, said air outlet by pipeline through the converging rear connecting to the bioreactor. This utility new type a device structure is simple, a force can recovery, the part organic matter, a a for organic waste pneuma, valid to process.
NOVELTY - The absorption method comprises: performing pre-treatment on biogas, controlling the pressure of the raw material gas to 0.6-1 MPa and then decarburizing at 80-85 degrees C, absorbing the carbon dioxide using a absorption tower, and discharging the biogas from the tower to obtain an absorbent solution; and placing the absorbent solution in a regeneration tower and then decarburizing at 80-85 degrees C to remove the carbon dioxide in the decarburization solution and then separating, recycling and circulating, and discharging the biogas to the regeneration tower and then heating in an electric heater.    USE - The absorption method is useful for removing carbon dioxide from biogas during purification of biogas (claimed).    ADVANTAGE - The absorption method is capable of removing the carbon dioxide from the biogas at constant temperature in an economical manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an absorption device for removing carbon dioxide form biogas.
NOVELTY - The device has box portion (1) whose bottom opening is set with solid discharging port (11) and aeration device (12). The clapboard (5) is provided for dividing the box portion into solid processing area (6) and liquid processing area (7) into which solid-liquid domestic waste is introduced. The inner liquid processing area is set with filling material (8) which is used for microbial growth. The organic liquid degraded using organic matter is discharged through liquid outlet (10) and generated waste is discharged through solid discharging port.    USE - Device for processing rural household garbage used for producing crop fertilizer.    ADVANTAGE - The garbage in the rural area is treated effectively, and the environment pollution is suppressed.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the device for processing rural household garbage.    Box portion (1)    Clapboard (5)    Solid processing area (6)    Liquid processing area (7)    Filling material (8)    Liquid outlet (10)    Solid discharging port (11)    Aeration device (12)
NOVELTY - Anaerobic tank comprises anaerobic tank (14), main body (20), inlet (21), outlet (22), two bulkhead plates (23,24), intermediate tube (25), delivery tube (26) and cleaning port (27).    USE - Anaerobic tank used for fermenting sewage (claimed).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of anaerobic tank.    Anaerobic tank (14)    Main body (20)    Inlet (21)    Outlet (22)    Bulkhead plates (23,24)    Intermediate tube (25)    Delivery tube (26)    Cleaning port (27)
NOVELTY - An enhanced denitrification and biological deodorization device comprises anoxic area (A1), aerobic area (OI, OII), sludge port (9) and displaced ball (10).    USE - Enhanced denitrification and biological deodorization device.    ADVANTAGE - The device strengthens denitrification effect and reinforcing effect, has reflux ratio of 200%, controls temperature and has certain short effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of enhanced denitrification and biological deodorization device.    Sludge port (9)    Displaced ball (10)    Anoxic area (A1)    Aerobic area (OI, OII)
NOVELTY - An ammonia nitrogen high manganese sewage biological purification filter layer is quickly recovered by starting filter pool reverse flushing pipeline valve, closing, opening filter tank outlet water pipeline valve, closing, stopping water, starting filter pool inlet water valve, closing filter pool water outlet pipeline valve, closing inlet water valve, recovering water manganese ammonia concentration, filtering to concentration of less than 0.05-0.1 mg/l, continuous filtering for 3 days, and increasing filtration speed.    USE - Method for fast recovering ammonia nitrogen high manganese sewage biological purification filter layer (claimed).    ADVANTAGE - The method recovers and removes ammonia nitrogen manganese at short period of time.
NOVELTY - Method for deodorizing sewage, involves setting a middle layer of transverse holes in culture tank compartment divided into two layers in the culture tank, setting a material of horizontal clapboard in the upper layer, taking culture medium, sterilizing with high pressure and temperature, spraying the medium uniformly in a filter material, providing Bacillus and ensuring normal growth of the Bacillus, and adding the microbial culture into activated sewage sludge.    USE - The method is useful for deodorizing sewage (claimed).    ADVANTAGE - The method eliminates or reduces the odor of the sewage.
NOVELTY - Electrically mediated method for promoting anaerobic microbial sludge digestion, involves (a) pre-treating sludge by adding sodium hydroxide solution to sludge, ultrasonically treating the sludge and refrigerating the pre-treated material, (b) performing microbial electrolysis cell anaerobic reaction, continuously introducing pure oxygen to remove residual nitrogen and processing the material, and (c) performing electric reaction using microbial electrode as anode and carbon coated with molybdenum as cathode, adding fresh sludge inoculum and fermenting the mixture.    USE - The electrically mediated method is useful for promoting anaerobic microbial sludge digestion (claimed).    ADVANTAGE - The electrically mediated method rapidly promotes anaerobic microbial sludge digestion, improves sludge organic material utilization rate and sludge recovery rate, eliminates acid accumulation, and promotes yield.    DETAILED DESCRIPTION - Electrically mediated method for promoting anaerobic microbial sludge digestion, involves (a) pre-treating sludge by adding sodium hydroxide solution to sludge to regulate the pH to 10, ultrasonically treating the sludge for 10 minutes and refrigerating the pre-treated material, (b) performing microbial electrolysis cell (MEC) anaerobic reaction at 0.6-0.9 V and 30 degrees C for 24 hours, continuously introducing 99.998% pure oxygen for 20 minutes to remove residual nitrogen, and processing the material, and (c) performing electric reaction using microbial electrode as anode and carbon coated with molybdenum as cathode, adding 10% fresh sludge inoculum, and fermenting the mixture at 35-38 degrees C and 100 revolutions per minutes for 5-20 days.
NOVELTY - Bioconversion method involves (a) adding earthworm, fermenting organic waste, and using biological activity of earthworm for treating the organic waste, and (b) (i) processing earthworm in an automatic reactor, monitoring earthworm living environment automatically, and making earthworm to adapt to live in various environmental parameters, and (ii) obtaining optimal conditions for growth and reproduction of earthworm through experiments such as temperature, humidity, and pH value parameter.    USE - The bioconversion method is useful for treating organic waste using earthworm (claimed).
NOVELTY - Use of filter mud (by-product of sugar refining) and bagasse are claimed, for preparing biological humic acid, where the biological humic acid comprises 45-48 wt.% total humic acid, 22.2-24.4 wt.% fulvic acid, 18.3-20 wt.% brown humic acid and 3.5-5 wt.% black humic acid.    USE - The filter mud and bagasse are useful for preparing biological humic acid (claimed), which is useful for preparing agricultural fertilizer used for increasing soil organic matter content and fertility.    ADVANTAGE - The filter mud and bagasse enable preparation of the biological humic acid that rapidly increases crop yield and quality.
NOVELTY - The turn throwing mechanism has support frame (6) whose lower end is set with lower power transmission shaft (8) and upper end is set with upper power transmission shaft (1). The power transmission shafts are set with chain wheels (2,9) respectively. A chain plate is set with support material supporting plate. L-type hanging plate (5) is uniformly fixed on belt (4) and chain plate.    USE - Turn throwing mechanism of turner for organic fertilizer production device.    ADVANTAGE - Since power transmission shafts are set with chain wheels respectively, durability of the belt is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the turn throwing mechanism of turner.    Upper power transmission shaft (1)    Chain wheels (2,9)    Belt (4)    Support frame (6)    Lower power transmission shaft (8)
NOVELTY - The method involves decomposing a crop straw using biomass slow speed pyrolysis technology. The straw carbon is processed into active carbon and organic sewage is filtered using a filter (4). The organic sewage is absorbed in filter core bag (5). The carbon base of waste slag is absorbed in the core bag. The carbon base sewage residue is filtered and dewatered and dried. The carbon base waste slag, sheep manure and coconut casing powder are mixed and biological microbial inoculum is added through fermentation of fifteen days to prepare organic fertilizer.    USE - Method of manufacturing environment-friendly carbon-based organic fertilizer.    ADVANTAGE - The environment pollution due to sewage is reduced and agricultural production is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating process of manufacturing environment-friendly carbon-based organic fertilizer.    Water inlet (1)    Steel pipe (2)    Valve (3)    Filter core bag (5)    Water outlet (6)
NOVELTY - Method for preparing edible mushroom cultivation substrate, involves (a) processing walnut shell, and immersing crushed walnut shell in water containing plant ash and performing leaching process, (b) roasting mulberry branches, processing roasted mulberry branches, flue-cured tobacco and pine wood chips, and performing degreasing treatment, and (c) mixing 30-60 pts. wt. processed walnut shell, 10-20 pts. wt. processed mulberry branches, 10-20 pts. wt. pine wood chips, 10-20 pts. wt. wheat bran or rice, adding glucose and gypsum, and mixing obtained product.    USE - The method is useful for preparing edible mushroom cultivation substrate (claimed).    ADVANTAGE - The method prepares substrate in an environmentally-friendly manner using cost-effective raw materials.    DETAILED DESCRIPTION - Method for preparing edible mushroom cultivation substrate, involves (a) processing walnut shell by crushing walnut shell to obtain particles with diameter of 10 mm or less, and immersing crushed walnut shell in water containing plant ash and performing leaching process for 24-48 hours, where the amount of water containing plant ash is 2-6 times with respect to the amount of crushed walnut shell, (b) obtaining and roasting mulberry branches, pulverizing the pine wood chips into particles of 10 mm or less, processing mulberry branches, flue-cured tobacco and pine wood chips, and performing degreasing treatment, where the flue-cured tobacco is crushed to obtain powder with particle diameter of 15 mm or less, and (c) mixing 30-60 pts. wt. processed walnut shell, 10-20 pts. wt. processed mulberry branches, 10-20 pts. wt. pine wood chips, 10-20 pts. wt. wheat bran or rice, then adding 0.5-1 pts. wt. glucose and 1 pts. wt. gypsum, and mixing obtained product.
NOVELTY - Method of preparing organic fertilizer involves (a) subjecting distillers grains to fermentation using bacterial strain; (b) weighing 35-40 pts. wt. earthworm manure, 25-35 pts. wt. dairy manure, 15-25 pts. wt. pig manure, 1-3 pts. wt. quicklime and 0.5-2 pts. wt. distillers grains to obtain mixture having moisture content of 60%; and (c) fermenting the mixture obtained in step (b) for 5-8 months by turning the fermented mixture for 2-3 times every month to obtain product.    USE - The method is useful for preparing organic fertilizer (claimed).    ADVANTAGE - The method ensures to prepare fertilizer having high nutrition content.
NOVELTY - Organic fertilizer comprises 20% or more organic matter and 1% or more biochar, where the water content of the organic fertilizer is 7-14%. The organic fertilizer is prepared by leaching biochar using pyroligneous acid solution for 0.5 hour or more, adding deodorant and then water to composting raw materials comprising 10-90 %mass leaves or straw and livestock manure (remainder), mixing the raw materials uniformly, composting obtained mixture, and drying and granulating obtained compost to obtain odorless organic fertilizer containing biochar.    USE - Organic fertilizer (claimed).    ADVANTAGE - The fertilizer increases organic matter content of soil, and improves soil structure, moisture and nutrient holding capacity, is rich in biochar, and promotes growth of beneficial microorganisms. The biochar promotes absorption of ammonia and sulfurated hydrogen and reduces loss of nitrogen and sulfur during composting process.    DETAILED DESCRIPTION - Organic fertilizer comprises 20% or more organic matter and 1% or more biochar, where the water content of the organic fertilizer is 7-14%. The organic fertilizer is prepared by leaching biochar using pyroligneous acid solution for 0.5 hour or more, adding deodorant to composting raw material, adding water (suitable quantity) to composting raw materials, where the composting raw materials comprise 10-90 %mass leaves or straw and livestock manure (remainder), completely mixing the raw materials, composting obtained mixture, and drying and granulating obtained compost to obtain odorless organic fertilizer containing biochar.
NOVELTY - Preparation of fingolimod hydrochloride (I) involves dissolving aromatic compound (II) in a solvent, hydrolyzing the resultant product in presence of alkali to obtain hydroxy compound (III), reacting the resultant product with chlorinating agent to obtain chlorine-containing compound (IV) as intermediate compound, reacting the resultant product with N-acetyl diethyl malonate to obtain intermediate compound (V), reducing the resultant product to obtain hydroxy compound (VI), adding acetyl protecting agent to obtain amino compound (VII), and carrying out hydrogenation reaction.    USE - Preparation of fingolimod hydrochloride (claimed).    ADVANTAGE - The method environmentally-friendly provides fingolimod hydrochloride with high yield by simple process.    DETAILED DESCRIPTION - Preparation of fingolimod hydrochloride of formula (I) involves dissolving aromatic compound of formula (II) in a solvent (A), hydrolyzing the resultant product in presence of alkali and a solvent (B) to obtain hydroxy compound of formula (III), reacting the resultant product with chlorinating agent to obtain chlorine-containing compound of formula (IV) as intermediate compound, reacting the resultant product with N-acetylmalonate to obtain intermediate compound of formula (V), reducing the resultant product to obtain hydroxy compound of formula (VI), adding acetyl protecting agent to obtain amino compound of formula (VII), and carrying out hydrogenation reaction.
NOVELTY - This utility new type claims a one for a microorganism of sewage treatment device, belonging to the sewage processing device manufacturing technology field. Provide a one sewage treatment efficiency is high, not need to restart a microorganism culture time each sewage secondary treatment of microorganism used for sewage treatment of a device. A device include a sewage treatment tank, with a set with a sewage input opening at the bottom of a sewage treatment pool, a sewage treatment tank on the side in a lower part set with the clean water output port, further comprise fixed microorganism culture frame, set with a fixing microorganism culture process area and a microorganism culture process inner area a of the sewage treatment pool, a said fixed microorganism culture frame set on the inner of said fixed microorganism culture treatment area, rear from a sewage input port input said sewage processing inner tank of a sewage treatment area and a culture of a microorganism culture circulation process of processing area through said fixing of said microorganisms from a clean water output port output.
NOVELTY - A one rotational flow type sewage treatment device, comprise four spiral tank, a first spiral with the same high bottom of second spiral tank, bottom of second spiral tank is higher than bottom of third spiral tank, a third spiral tank and the bottom of fourth spiral pool with high, inner lane of first spiral tank set with a first distributor, a first water distributor and the water inlet connecting tube, external ring and the outer of second spiral pool ring of first spiral tank connected, inner lane of second spiral tank is set with dropping water hole, a third spiral tank inner lane is set with second water distributor, the water falling hole and second water distributor connecting with a flow guide tube, external ring and the outer of fourth spiral pool ring of third spiral tank connected, inner lane of fourth spiral tank is set with drain hole, drainage hole connecting with the drain pipe, a spiral four inner tank from lower to top in turn set with gravel layer, gravel layer and substrate layer. The device has a simple structure, a sewage amount is large, small floor area, a high efficiency, shock resistance ability of strong, at the same time, it beautifies the environment.
NOVELTY - This utility new type claims a one kitchen garbage processing system, comprise the dehydration device, used for kitchen garbage for a dehydration process, crushing spike device, used for kitchen garbage for a dehydration treatment process, and a kitchen garbage in adding a organic fertilizer of auxiliary material fermentation device, for kitchen garbage crushing of a fermentation process, forming organic fertilizer, cooling device, include set with vent hole and used for steel belt conveying of organic fertilizer and a said blower with blowing of steel. Set like this, this utility new type provide a kitchen garbage treatment system, the can for a process to make the kitchen waste into organic fertilizer.
NOVELTY - This new type utility claims one biological diesel oil side product glycerol of a production device, comprise side product glycerine pre-heater, static mixer, reaction tank, a disc centrifuge, acidifying oil groove, coarse glycerol groove, potassium chloride groove and pipeline, exit of said side product glycerol pre-heater through pipeline connected static mixer of entrance, exit of static mixer through a pipeline connected entrance of reaction tank, exit of said reaction tank through pipeline connected entrance of disc-type centrifuge, a disc centrifuge of three exit a connected acidifying oil groove through a pipeline, crude glycerine groove and groove of potassium chloride. Present a separate device is normal centrifuge, so it need the glycerine with acidified and then one time separate, this utility new type disc centrifuge can be acidified using glycerol and slag directly, the use is more convenient and efficient.
NOVELTY - This utility new type claims a marsh gas mix one stir fermenting, adding water by tube, motor, marsh gas outlet tube, stir shaft, stir fin, a feeding port cover, a tank body, a liquid discharging tube, the fermentation cavity, nozzle, using the tank body set with stir fin of stir shaft, the new and old material liquid mix uniform, making the raw material fully contact, promote biochemical reaction process, further causing a solid dispersed in the material liquid, suspension to increase the contact surface of microorganism to promote digestion of the substance, at the same time, but also avoids the substance deposition or incrustation, and increase the biogas tank body gas-liquid speed of fermentation, effectively increase a production rate.
NOVELTY - This utility new type claims a one by using kitchen waste oil of a fermenting marsh gas, oil water separator and include anaerobic reactor, a water oil separator comprise water mix oil cavity, oil cavity and side wall upper part position of water cavity, said oil water mix cavity set with first opening and said oil cavity of connected, side wall lower part position of said oil water mix cavity set with second opening and a water cavity connected a, said oil cavity and said anaerobic generator of oil entrance is connected, said oil water separator further include for the oil water mix liquid in said oil water mix pipe of cavity, the exit of said pipe is located at the bottom position of said oil water mix cavity, and exit direction of said conduit. Set like this, this utility new type provide a by using kitchen waste oil of fermenting marsh gas system, the valid can increase the fermentation of biogas pneuma amount.
NOVELTY - This utility new type claims a one constant voltage methane tank, comprise: biogas pneuma bottom tank and a cover on the upper opening of the bottomless marsh gas tank cover a biogas pneuma bottom tank, the marsh gas tank cover of bottomless pneuma biogas pool bottom is a little smaller, the bottomless marsh gas tank cover according to a quantity of marsh gas inner marsh gas tank up and down freely, the bottomless marsh gas tank upper cover set with a manure outlet, pipe and gas-guide tube. This utility new type of bottomless marsh gas tank cover can be according to how many free up and down movement amount of gas so that the pressure of the marsh gas tank inner pressure is constant, solves the problem that the existing marsh gas tank pressure change in a.
NOVELTY - This utility new type category environmental protection technology field, relating to a soil amphotericin one slag harmless processing of a device, the device to soil amphotericin a slag storage tank, an alkali liquid tank, alkali reaction tank, a regulating tank, a liquid tank, an anaerobic ASBR reactor, the residual sludge storage tank, slag collecting tank as the main body, further comprise temperature probe and a water quality on-line monitoring system is connected with a temperature control box and so on, of a first heat reaction pool into soil amphotericin alkali slag and alkali liquid a preprocessing process, and then the mix liquid is in regulating tank, a rear regulating pH is ASBR into the anaerobic reactor, at the same time, injecting a surplus sludge anaerobic reactor inner regulating C/N ratio, carrying out anaerobic digestion rear, biogas generated by using as a clean fuel, harmless biogas residue in the biogas residue collecting pool as a raw material for producing organic fertilizer. This utility new type device and improves the technique a residue organic matter of soil amphotericin utilization efficiency, and realize the soil amphotericin a slag harmless and reclamation.
NOVELTY - This utility new type belongs to the environment protection technology field, specific relates to a head of a one pixel a slag harmless processing of device, wherein the device comprise head of a pixel a slag storage tank, an ultrasonic processing tank, a reaction tank base, alkali liquid tank, a regulating tank, a liquid tank, an anaerobic ASBR reactor, waste acid tank, a residue collecting tank and so on, first built-in head of a pixel a slag a ultrasonic processing tank, a rear ultrasonic alkali into a reaction tank, mix liquid rear two level preprocessing is in regulating tank, a rear regulating pH is ASBR into the anaerobic reactor, supernatant of same inner cow dung acidification tank regulating C/N ratio, carrying out anaerobic digestion rear, biogas generated by using as a clean fuel, slag is identified as harmless in the biogas residue collecting pool as a raw material for producing organic fertilizer. This utility new type the ultrasonic + alkali a preprocessing technology and anaerobic biological treatment technology process organically combines and improves the head of a pixel a residue of organic matter and utilization efficiency;
NOVELTY - This utility new type claims a one for garbage percolate regulating pool of deodorizing device, include a floating cover, floating cover system include a cover on a multi-floating regulating pool of geomembrane and set on bottom of geomembrane, said deodorizing device is further used for collecting methane include a discharge system, a floating block crossly set with a discharge channel, a discharge with a discharge channel connected. This utility new type of garbage percolate regulating pool for a deodorization device with safety efficient, good deodorization effect, easy to carry out and of low cost.
NOVELTY - This utility new type relates to a sludge one straw pelleting drying machine, comprise sleeve, pelletizer, speed reducing box, motor, shaft, bearing, microwave generator, sleeve upper end set with a sleeve is connected with a bucket, motor and speed reducing box, screw rod shaft is set in the whole inner sleeve, upper end of screw rod shaft through shaft joint and speed reducing box and the motor connect the pelletizer the sleeve is divided into feeding area and drying area, screw rod shaft through pelletizer, pelletizer and set with bearing, screw rod shaft system part feeding area set with a feeding spiral blade, the area of drying part set with stir blade, a pelletizer drilled connected feeding area and material discharging small hole of drying area, sleeve upper of side wall pelletizer is set with microwave generator and discharge hole and straw feeding port, sleeve of the bottom set with row material used for a door. This utility new type high integration, using a new sludge granulation technology, increase the production efficiency and reduces the production cost.
NOVELTY - This new type utility claims one intelligent marsh gas reactor of a teaching model, comprise a reactor tank body, a reactor tank body is double layer heat-preserving cylinder shape, the outer cylinder and inner cylinder is equipped with a feed port, exit, slag exit, an outer cylinder side is provided with a water inlet and a water outlet, the outer cylinder and inner cylinder top using an annular connecting plate, and using the cover plate cover, the cover plate is opened with a gas exit, temperature sensor interface, a stir bar interface, PH value sensor interface and screw hole, marsh gas exit through air inlet pipe connecting bottle, a bottle outlet drain pipe connecting water outlet through a water bath, water pump of inner water bath through water supply pipe connecting the water inlet of marsh gas reactor, rear full water from the water outlet through the water pipe overflow the water bath. This utility new type is simple, safety, efficient, it can discharge and add material, at the same time, solves the problem that the traditional plastic or glass marsh gas reactor sealing property in the process of marsh gas fermentation is easy to crack, a heat preservation.
NOVELTY - Cultivating peanut involves plowing hard soil of pH value 6-7 and adding fertilizer to soil. Processed and peeled peanut seed is sowed in planting hole, where hole is covered and supplied with water to germinate seedling. Weeds are removed from near areas of seedling and then fertilizer in required amount applied to fields. Monopotassium phosphate solution is sprayed on upper leaf surface of seedling to remove yellowing of leaves and protect plant from various diseases.    USE - Method for cultivating peanut (claimed).    ADVANTAGE - The method enables to cultivate peanut that ensures high yield and increased quality of peanut in eco-friendly manner.
NOVELTY - A black fungus cultivating method involves preparing rods by placing cultivating material into a bag, inoculating the material, placing the control rods outside the oxygen bag, transferring the complete bagging rod material into greenhouses, stacking the rods in parallel, and allowing forced ventilation using spray cooling to control greenhouse temperature to 25-33 degrees C and relative humidity of 60-70% for the months of August-September followed by puncturing hairy fungus to obtain a finished product.    USE - Method for cultivating black fungus.
NOVELTY - Pot composition comprises (in %): grass (36), potato (24), dairy manure (15), stearic acid (0.5), urea-formaldehyde resin (2.5), alum (2) and additive.    USE - Pot composition used for cultivating plant (claimed).    ADVANTAGE - The pot composition is biodegradable, and has fertilizer property.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing pot composition, which involves:    (A) mixing grass and potato into water (20mg/kg), homogenizing with alum at 70 degrees C and then extruding to obtain pulp;    (B) fermenting cow dung or other animal feces with pulp and then mixing uniformly stearic acid, urea-formaldehyde resin and additive according to their respective ratio to obtain a wet material; and    (C) treating the wet material wet into a pressure molding machine, and then drying to obtain the desired product.
NOVELTY - Comprehensive usage of straw comprises: (i) preparing straw powder; (ii) preparing a composite microbial inoculum; (iii) adding fine straw powder and microbial inoculum in a reactor, adding water, sealing and fermenting under anaerobic conditions for 2 days to obtain a fermented product; (iv) adding 1000-8000 kg straw powder, sealing and fermenting under anaerobic conditions for 15 days to obtain a fermented product; (iv) neutralizing; (vi) filtering to obtain a filter liquid and a filter residue; (vii) performing decompression distillation of the filter liquid to obtain alcohol.    USE - The method is useful for producing alcohol, activated carbon, liquid fuel, feed and biomass carbon fertilizer from straw (all claimed).    ADVANTAGE - The method enables production of multiple products from straw by integrated chemical and biological engineering and hence solves the problems that straw turns rotten or invalid, which is a cause of environmental pollution and a resource waste.    DETAILED DESCRIPTION - Comprehensive usage of straw comprises: (i) preparing straw powder; (ii) preparing a composite microbial inoculum using 3-15 pts. wt. yeast, 12-20 Aspergillus niger and 8-15 pts. wt. Aspergillus flavus; (iii) adding 1000 kg fine straw powder and 0.6-3 kg microbial inoculum in a reactor, adding water to wet the mixture, sealing and fermenting under anaerobic conditions for 2 days to obtain a fermented product; (iv) adding 1000-8000 kg straw powder, sealing and fermenting under anaerobic conditions for 15 days to obtain a fermented product; (iv) adding hydrochloric acid to the fermented product, sterilizing, and adding an alkali carbonate for neutralization to obtain a reaction product; (vi) filtering the reaction product to obtain a filter liquid and a filter residue; (vii) performing decompression distillation of the filter liquid to obtain alcohol.
NOVELTY - Carbon dioxide trapping agent comprises 32-38 mass% of microalgae, 0.7-1.3 mass% of colloidal agent, 0.5-1 mass% of water absorbing agent, 5-6 mass% of yeast and 54-61 mass% of water.    USE - Carbon dioxide trapping agent.    ADVANTAGE - The carbon dioxide trapping agent reduces the usage of fertilizer, promotes the production of crops, and can be prepared in an economical and eco-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the carbon dioxide trapping agent comprising adding the above raw materials into a reaction kettle under a stirring of normal temperature and pressure for more than 3 hours.
NOVELTY - Preparing metal organic frame (MOF) material for absorbing carbon dioxide in marsh gas comprises e.g. dissolving cobalt acetate tetrahydrate, citrate monohydrate, and alkaline compounds in organic solvent to obtain mixed solution, placing mixed solution in a hydrothermal kettle, placing in an oven, heating, cooling, filtering the mixed solution, washing using diethyl ether, naturally drying at room temperature to obtain purple prismatic crystals of MOF material, activating the resulting MOF material, removing water and organic solvent to obtain activated UTSA series of MOF material.    USE - The method is useful for preparing metal organic frame (MOF) material for absorbing carbon dioxide in marsh gas (claimed).    ADVANTAGE - The material has pore diameter of 4.5 A, rhombic surface area of 3.3x 5.4 A2, and is suitable for carbon dioxide gas adsorption at ambient condition.    DETAILED DESCRIPTION - Preparing metal organic frame (MOF) material for absorbing carbon dioxide in marsh gas, comprises dissolving cobalt acetate tetrahydrate, citrate monohydrate, and alkaline compounds in organic solvent and mixing to obtain mixed solution, placing the mixed solution in a hydrothermal kettle, and then placing in an oven, heating the mixed solution at room temperature of 100-140 degrees C for 0.5-1 hour, thermal insulating at 100-140 degrees C for 36-48 hours, then cooling to room temperature at a rate of 4-6 degrees C/hour, filtering the mixed solution of hydrothermal kettle, washing using diethyl ether, naturally drying at room temperature to obtain purple prismatic crystals of MOF material, adding the resulting MOF material under 90 degrees C and 5 MmHg condition, and activating for 24 hours, removing water and organic solvent, to obtain activated UTSA series of MOF material.
NOVELTY - A deodorant comprises composite deodorizing microorganism and microorganism growth promoter in which composite deodorizing microorganism comprises nitrite-oxidizing bacteria, sulfur-oxidizing bacteria, and phosphorus bacteria, and microorganism growth promoter contains 0.04-0.06 pt. wt. potassium, 0.13-0.15 pt. wt. calcium, 0-0.04 pt. wt. magnesium, 0.002-0.003 pt. wt. iron, 0.15-0.17 pt. wt. sodium, 0.00015-0.00018 pt. wt. copper, 0.00075-0.00085 pt. wt. zinc, 0.015-0.025 pt. wt. silicon, 0.78-0.85 pt. wt. chlorine, 0.07-0.09 pt. wt. nitrogen, and 0.03-0.04 pt. wt. phosphorus.    USE - A deodorant for domestic sewage, industrial sewage, domestic garbage, and industrial waste.    ADVANTAGE - Deodorant is environment-friendly, fast, and effective, converts hydrogen sulfide, mercaptan, and ammonia into harmless odorless substances, and has simple preparation.    DETAILED DESCRIPTION - A deodorant comprises composite deodorizing microorganism and microorganism growth promoter in which composite deodorizing microorganism comprises nitrite-oxidizing bacteria, sulfur-oxidizing bacteria, and phosphorus bacteria, and microorganism growth promoter comprises 0.04-0.06 pt. wt. potassium, 0.13-0.15 pt. wt. calcium, 0-0.04 pt. wt. magnesium, 0.002-0.003 pt. wt. iron, 0.15-0.17 pt. wt. sodium, 0.00015-0.00018 pt. wt. copper, 0.00075-0.00085 pt. wt. zinc, 0.015-0.025 pt. wt. silicon, 0.78-0.85 pt. wt. chlorine, 0.07-0.09 pt. wt. nitrogen, 0.03-0.04 pt. wt. phosphorus, 0.7-0.8 pt. wt. sulfate ion, 0.06-0.07 pt. wt. nitrate ion, 0.03-0.04 pt. wt. phosphate ion, and 1000 pts. wt. water.
NOVELTY - Recycling garbage involves leaching the garbage, where the obtained leachate is concentrated, and then stacked in a pile. Microflora (bacterial) is added to the stacked pile in order to accelerate the degradation process through an enzyme produced by the bacteria. Methanogenic bacteria are also added to the stacked pile, where an alkali is also added to the stacked pile to adjust its pH value. Water is added to the stacked pile to obtain weak base stacked garbage pile. The leached liquid is obtained in the concentrated form by recycling garbage.    USE - Method for recycling garbage (claimed) for refilling small and medium sized landfill.    ADVANTAGE - The method enables to recycle garbage in an economical and convenient manner.
NOVELTY - A high-efficiency aerobic sludge composting comprises mixing sludge in mixing tank, dewatering through sludge dewatering pumps, filtering through membrane filter press, conveying into mud cake crushing mixer through belt conveyor, crushing, heating through baker, mixing with composite strain, fermenting, and transporting.    USE - Method for high-efficiency aerobic sludge composting (claimed).    ADVANTAGE - The method greatly reduces fermentation floor area, increases quality of compost product, has short fermentation time and reduced operation cost.
NOVELTY - The biological organic fertilizer comprises nitrogen-phosphorus-potassium compound fertilizer, zinc sulfate, and wheat straw organic fertilizer.    USE - Biological organic fertilizer used for cotton soil testing and formulated fertilization (claimed) and cotton planting area in China.    ADVANTAGE - The fertilizer has lasting nutrient supply, can comprehensively balance nutrient of cotton, and increases quality and yield of cotton.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biological organic fertilizer comprising crushing 90-160 pts. wt. wheat rice straw and sieving through 60 meshes; adding wheat rice straw, 15-25 pts. wt. pig manure, 1-3 pts. wt. Streptomyces hygroscopicus, and 1-3 pts. wt. Coriolus versicolor into fermentation tank, adding 35-55 pts. wt. water, and stirring; fermenting at 22-29 degrees C for 5-7 days, re-fermenting at 25-27 degrees C for 20-30 days, and stirring once every two days to obtain wheat straw organic fertilizer; and uniformly mixing nitrogen-phosphorus-potassium compound fertilizer, zinc sulfate, and wheat straw organic fertilizer, drying at 80-120 degrees C, and cooling until water content of 8-15%.
NOVELTY - Microbial fertilizer comprises (in kilograms): biological carbon (500-900), mixed bacterial solution (20-40), chitosan hydrolyzate (55-75), animal blood hydrolyzate (25-40), urea (40-60), monoammonium phosphate (40-60), potassium sulfate (40-60) and composite microelement (15-25).    USE - Microbial fertilizer used for promoting growth of pumpkin, pepper, cucumber and towel gourd (all claimed), preventing and treating plant diseases and controlling insect pests.    ADVANTAGE - The microbial fertilizer improves soil acidification and reduces soil hardening and continuous cropping obstacles.
NOVELTY - Fertilizer comprises (in pts.wt.): nitrogen-phosphorus-potassium (18-30), Chinese herbal medicinal composition (10-20), matrine (1-3), humic acid (30-80), trace element (2-5), biological agent (0.5-3) and water (20-40). Trace element comprises calcium, magnesium, sulfur, silicon, iron, boron, manganese and zinc. Chinese herbal medicinal composition comprises Platycodon root, Lycoris radiate, oleander, horsetail, Equisetum, elderberry, Ailanthus, cocklebur and rhizoma polygonati in weight ratio of 1: 1: 2: 2: 1: 1: 3: 1:1 respectively.    USE - Fertilizer.    ADVANTAGE - The fertilizer alleviates soil compaction caused by use of chemical fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fertilizer, which involves:    (A) weighing raw materials;    (B) grinding Chinese herbal medicinal composition and then extracting with water for 3 hours to obtain extract;    (C) adding humic acid into obtained extract and then mixing to obtain mixture;    (D) adding biological agent into obtained mixture and then fermenting for 7-14 days to obtain fermentation product;    (E) drying fermentation product and then adding nitrogen-phosphorus-potassium, matrine and trace element to obtain the mixture; and    (F) granulating mixture to obtain the product.
NOVELTY - A farm cultivation manure biological drying system comprises mixing system (1), conveying system (2), automatic batching system (3), aeration system (4), biological drying system (5), ventilation system (6), and deodorizing system (7).    USE - Farm cultivation manure biological drying system.    ADVANTAGE - The method biological drying system does no cause secondary pollution.    DETAILED DESCRIPTION - A farm cultivation manure biological drying system comprises mixing system (1), conveying system (2), automatic batching system (3), aeration system (4), biological drying system (5), ventilation system (6), and deodorizing system (7). The biological drying of farm cultivation manure comprises mixing manure and auxiliary material in mixing system, conveying into biological drying system conveying system, automatically distributing through automatic batching system, installing aeration system on bottom part and ventilation system on top part, pumping steam into deodorizing system to carry out air purification.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of farm cultivation manure biological drying system.    System (1)    Conveying system (2)    Automatic batching system (3)    Aeration system (4)    Biological drying system (5)    Ventilation system (6)    Deodorizing system (7)
NOVELTY - Acidic soil conditioning agent comprises plant ash, shell powder and stone powder according to a weight ratio of 1-100:1-100:1-100.    USE - Acidic soil conditioning agent.    ADVANTAGE - The acidic soil conditioning agent can be economically prepared with high waste resource utilization rate and rich nutrition content, and without pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing acidic soil conditioning agent comprising (1) high temperature calcining of oyster shell, scallop shell and/or clamshell at 700-1000 degrees C and then mixing, (2) crushing the stone and then mixing with the calcined shell powder, crushing the mixture into 50-80 meshes, and (3) adding the crushed product with the plant ash.
NOVELTY - Composite solid fuel comprises anthracite, biomass and auxiliary agent. The composite solid fuel is prepared by crushing anthracite and biomass and then steaming at more than 60 degrees C for 22-26 hours, fermenting biomass powder into a drying machine for drying, mixing crushed anthracite, biomass powder, corn starch and water with a container and then fermenting and drying, sinking the dried mixture at normal temperature for 10-12 hours and then pressing, molding in a press-molding machine and drying obtained product.    USE - Composite solid fuel.    ADVANTAGE - The composite solid fuel is eco-friendly, and has high fuel heat productivity and low sulfur content.
NOVELTY - This utility new type relates to one manufacturing agricultural organic fertilizer of a device, specifically to a organic fertilizer fermenting one solidified into a whole device. Organic fertilizer fermenting solidified into a whole device, inner stirring material groove is penetrated the stir shaft, the stir shaft one end fixed with the main wheel, wheel, and the other end fixed with a centrifugal shaft, a centrifugal shaft one end mounting with a material isolating valve, the other one end is hinged with a discharging propeller, centrifugal shaft tail end fixing shaft fixed on the upper end of the centrifugal jar is set with one valve pneuma; the stirring material groove top end is set with one material inlet bucket, a main wheel through chain is hinged with a motor a, a primary wheel and a transmission wheel through the chain hinge, a transmission wheel and a transmission shaft connecting, and transmission shaft penetration inner clutch, the clutch and the jar body contact surface outer centrifugal jar controllable distance between the stirring groove to the centrifugal jar set with material discharging tube.
NOVELTY - And is higher than the outer inner of this utility new type claims a one simple organic waste anaerobic fermentation device, include anaerobic fermenting tank (1), a methane pipeline (2) and liquid level inspection shaft (3), an anaerobic fermenting tank (1) and liquid level inspection shaft (3) of the top surface are connected with the soil (10) of c, liquid level checking well (3) of the bottom connected through pipeline (4) is connected with the anaerobic fermenting tank (1) in a connected part, an anaerobic fermenting tank (1) of the periphery set with filling hole (5), an anaerobic fermenting tank (1) is paved with an anti-osmosis membrane (6), an anti-osmosis membrane (6) edge is set on a landfill pit (5) inner, landfill pit (5) fill with inner backfill (7), the top part of anaerobic fermentation tank (1) with a cover (8), gas pipeline (2) one end of the anaerobic fermentation tank (1) and higher than the inner ground, and the other end the anaerobic fermenting tank (1). This utility new type set on the ground, there is no need to machinery component can be a function of the traditional anaerobic reaction tank, reduces the manufacturing cost of the marsh gas.
NOVELTY - Treating sewage and reducing carbon dioxide to produce methanol using microorganism electrolytic cell comprises inoculating anaerobic activated sludge containing organic sewage in an inoculum culture medium in the absence of oxygen, then placing in the anode containing carbon dioxide and hydrogen, and generating electricity, adding microorganisms and inoculating into inorganic salt medium, passing mixed gas of methane and air, adding the obtained cell suspension into the cathode and electrochemically activating the cathode using biological catalysts to produce methanol.    USE - The method is useful for treating organic sewage and reducing of carbon dioxide to produce methanol, where organic sewage is domestic sewage, food processing waste water, starch processing waste water or beer waste water (all claimed).    ADVANTAGE - The method is capable of rapidly, efficiently and economically treating organic sewage and reducing carbon dioxide to produce methanol with low energy consumption and reduced carbon dioxide emission in an eco-friendly manner.    DETAILED DESCRIPTION - Treating sewage and reducing carbon dioxide to produce methanol using microorganism electrolytic cell including a proton exchange film, an anode chamber and a cathode chamber containing carbon dioxide and hydrogen, comprises inoculating anaerobic activated sludge containing organic sewage in an inoculum culture medium in the absence of oxygen, then placing in the anode and generating electricity, adding microorganisms and inoculating into inorganic salt medium, passing mixed gas of methane and air in a ratio of 1:1, culturing at 35 degrees C to obtain cell suspension, adding the obtained cell suspension into the cathode, and electrochemically activating the cathode using biological catalysts to produce methanol. The anode and cathode chambers are connected to a high potential end of a direct current power supply and a low potential end of conductor.
NOVELTY - At 0-5 degrees C, a photoinitiator, dimethyl carbonate, and chlorine gas are photoreacted. The reaction is stopped and the obtained chloro-dimethyl carbonate is separated by distillation. At 70-100 degrees C, a catalyst is added, chloro-dimethyl carbonate and isopropanol are added to control the reflux ratio in the distillation column, and methanol is distilled by normal-pressure steam distillation. After reaction completion, excess isopropanol is distilled off under reduced pressure to obtain chloromethyl isopropyl carbonate.    USE - Synthesis of chloromethyl isopropyl carbonate (claimed).    ADVANTAGE - The method enables simple and environmentally-friendly synthesis of chloromethyl isopropyl carbonate with low energy consumption and high raw-material utilization rate.
NOVELTY - Bis(2-diisopropyl-aminoethyl)ether is synthesized by mixing N,N-dialkyl ethanolamine, N,N-dialkylamine, and acetylene raw materials with molar ratio of 4:3:1-2:1:1, placing in high pressure reaction container, reacting with catalyst and solvent at sealed state at 50-120 degrees C for 3-7 hours in which amount of catalyst is 2-10.5 wt.% of raw material total weight, opening container when reaction is complete, filtering, collecting filtered liquid, and rectifying.    USE - Synthesis of bis(2-diisopropyl-aminoethyl)ether (claimed).    ADVANTAGE - Synthesis process is simple and environment-friendly, has convenient operation, shortened reaction process, high atom economical efficiency and raw material utilization rate, reduced cost, wide raw material source, and mild reaction conditions, and does not produce halogen-containing reaction intermediate.
NOVELTY - This utility new type belonging to the biomass energy utilization technology field, specific relates to a roller type biomass pyrolysis one multi-joint of device. The device comprise a feeding system, drying system, roller type pyrolysis reactor, a gas-solid separate system, pneuma condensing system, gas combustion system, solid coke collecting box, a liquid collecting tank and a gas storage tank, wherein the pressure roller pyrolysis reactor by supporting belt, transmission roller, driving system, seal reaction room, high temperature smoke heat exchange coil tube pneuma and multi-level transfer a pressure roller. The biomass raw material drying by entering into rear pressure roller pyrolysis reactor, a operation on the supporting belt is subjected to forced roller pressure of multi-stage transfer a pressure roller and fast pyrolysis, and pyrolysis product to one part of a flame by burning a high temperature smoke pneuma pneuma, used for heating roller surface, biomass pyrolysis and the supply of heat. The device using multi-stage transfer a pressure roller and a finishing roller forcing pressure and heat transfer for biomass raw material to make the fast pyrolysis, a pyrolysis process of self-heat type.
NOVELTY - The method involves filling a chamber with a cation exchange membrane. An anode electrode part and a cathode electrode part are arranged in the chamber. The cathode electrode part is coated with active microorganism. An external lead is connected between an anode electrode and a cathode electrode. The anode electrode is fixed in an inner side of the chamber. The cathode electrode is coated with organic compound. A metal precursor is provided with the cathode electrode part and filled with buffer solution.    USE - Method for manufacturing a microbial fuel cell of hydrogen and metal nanoparticles.    ADVANTAGE - The method enables producing hydrogen and metal nanoparticles without utilizing outer side powder, so that monocrystal quality of the hydrogen and metal nanoparticles can be improved in an effective manner.    DETAILED DESCRIPTION - The cathode electrode is selected from one among a carbon paper, a carbon cloth, a carbon felt and a metal cloth. The anode electrode is selected from one among Rhodoferax ferrireducens, Shewanella putrefaciens, Geobacteraceae sulfurreducens and Geobacter metallireducens. The metal precursor is made of gold, silver, copper, nickel, palladium, platinum, zinc, cadmium, cobalt, rhodium or iridium. An INDEPENDENT CLAIM is also included for a microbial fuel cell for hydrogen and metal nanoparticles.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a method for manufacturing a microbial fuel cell of hydrogen and metal nanoparticles.'(Drawing includes non-English language text)'
NOVELTY - A hydrogen generating device (100) comprises a reformer (6) that generates hydrogen-containing gas by way of a reforming reaction of a source gas, a burner (14) that heats the reformer (6) by diffusion combusting the source gas and combustion air, an auxiliary air flow rate regulator (16) that supplies a flow of auxiliary air to be added to the source gas, and a controller (30) that controls the auxiliary air flow rate regulator (16) so that the flow rate for gas mixture of the source gas and the auxiliary air is a prescribed value.    USE - Hydrogen generating device is used for fuel cell system.    ADVANTAGE - The hydrogen generating device enables stable ignition of combustor.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of fuel cell system.    Reformer (6)    Burner (14)    Auxiliary air flow rate regulator (16)    Controller (30)    Hydrogen generating apparatus (100)
NOVELTY - Manufacture of incense stick involves mixing mixture of cyclodextrin clathrate having fragrance and component chosen from triethyl citrate, diethyl phthalate and isoparaffin-type hydrocarbon.    USE - Manufacture of incense stick (all claimed).    ADVANTAGE - The method enables manufacture of incense stick high aroma retainability and fragrance, and excellent brightness and freshness. The volatilization of fragrance is suppressed during manufacture of incense stick.
NOVELTY - Catalyst comprising particles of nickel dispersed in a porous silica matrix.    USE - The catalyst is useful: for catalyzing a methanation reaction, preferably for catalyzing a feedstock including coal gasification effluent and/or biomass gasification effluent comprising carbon monoxide and hydrogen; for reducing carbon monoxide content of a gas mixture comprising carbon monoxide and hydrogen (all claimed); for producing natural gas.    ADVANTAGE - The catalyst has higher sulfur tolerance so as to minimize the costs of substitute natural gas production.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) methanation of a feedstock including carbon monoxide and hydrogen comprising contacting the feedstock with the catalyst; and    (2) reducing the carbon monoxide content of a gas mixture comprising exposing the gas mixture to the catalyst.
NOVELTY - Stabilizing a biomass of microalgae containing oxidation-sensitive metabolites, comprises fermenting the biomass in heterotrophic conditions including culture phase in a nutrient deficient factor, and storing the dry biomass in which the oxidation-sensitive metabolites are stabilized.    USE - The method is useful for stabilizing a biomass of microalgae containing oxidation-sensitive metabolites including carotenoids (i.e. lutein), monounsaturated and polyunsaturated fatty acids (e.g. palmitoleic acid, oleic acid and linoleic acid), chlorophyll pigments (e.g. chlorophyll A and B) and/or vitamins (e.g. vitamin B9 and/or B12) (claimed). The carotenoids, preferably alpha , beta -carotene and lycopene are useful in animal feeds, and for prevention of cancer and other human diseases.    ADVANTAGE - The carotenoids can be easily stored and handled, and has improved antioxidant properties.
NOVELTY - Method for recovering phosphoric acid residue involves performing dephosphorization to molten iron, collecting dephosphorization residue, /-3% citric acid soluble phosphoric acid residue and collecting solid residue, dissolving carbon dioxide in water, stirring solid residue with dissolved carbon dioxide for performing carbonation, eluting dephosphorization residue using belite phase, repeating carbonation of solid residue for several times and collecting phosphorus residue from second or subsequent treated water.    USE - The method is useful for recovering phosphoric acid residue which is useful as raw material for fertilizer (claimed).    ADVANTAGE - The method is simple and cost-effective and solid residue obtained after carbonation process is recycled as raw material for making iron.
NOVELTY - Process for planting and/or harvesting plants in an area between traffic area and an agriculturally exploited land, involves planting vegetation predetermined for producing biomass in an area between traffic area and an agriculturally exploited land, harvesting vegetation grown in the area and processing biomass obtained from the harvested plants in bioenergy plant.    USE - The process is useful for planting and/or harvesting plants, which is used as biomass for producing bioenergy.
NOVELTY - The system has a reactor (1) defining an internal cavity for containing water and for causing water to disassociate into hydrogen and oxygen gas. The ports (25,26) are provided in fluid communication with internal cavity for venting through disassociated hydrogen and oxygen gas. The open top axial end of each cathode tube of the cathode matrix (15) is extended upwardly in the redox chamber (6) such that space within bore of each cathode tube defined between side wall of cathode tube and hydrogen collector tube (17) received is in gaseous communication with one chamber of redox chamber.    USE - Portable hydrogen and oxygen supply system for producing gaseous hydrogen and gaseous oxygen from water, for use in industrial application, hospital, cabin condition and academic use.    ADVANTAGE - As highly electro-conductive polymers or highly electro-conductive carbon aerogels are used, the longer life of the diode material is ensured. The pure atomic hydrogen and pure atomic oxygen gasses from common water is provided and the need for distillation is avoided. The greater yield of gasses at lower voltage is ensured. The environmentally safe emission is achieved. The efficiency of the reaction is enhanced and the possible introduction of electro-conductive cold spots and hot spots is minimized. The improved electro-conductive material to create water disassociation is achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a left side view of a hydrogen and oxygen supply system.    Reactor (1)    Redox chamber (6)    Cathode matrix (15)    Hydrogen collector tube (17)    Ports (25,26)
NOVELTY - Device comprises a rotatable drum to contain fermented material, and a shaftless screw extending inside the drum.    USE - The device is useful for brewing material, preferably fermented material (claimed) for producing a compost.    ADVANTAGE - The device is capable of economically, homogeneously, effectively and rapidly brewing the fermented material without generating unpleasant smell.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for brewing material, preferably fermented material using the device, comprising introducing the material in the drum, rotating the drum so that shaftless screws are driven in rotation to the drum for brewing the material and to split the agglomerates of material, and discharging a portion of material from the drum.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic view of a device for brewing a fermented material.    Movement transmitting system (3)    Rear flange of drum (10)    Inlet (15)    Longitudinal axis (16)    Opening. (19)
NOVELTY - Method for recovering cellulose from a biomass comprising lignocellulosic material, involves: heating the biomass to a temperature 100 degrees C and subjecting it to mechanical defibration, where the biomass is contacted with a bacterial laccase (CotA) before it is heated to a temperature 100 degrees C.    USE - For recovering cellulose from biomass comprising lignocellulosic material (claimed) use producing paper.    ADVANTAGE - The method reduces the energy requirements of the production of wood pulp.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) new isolated nucleic acid encoding a protein having laccase activity and a primary amino acid sequence that is at least 99% identical with the sequence of bacterial laccase (Cot2) containing amino acid sequence having 539 amino acids as given in the specification (SEQ ID NO: 2);    (2) new isolated nucleic acid encoding a protein having laccase activity and a primary amino acid sequence that is at least 83% identical with the sequence of bacterial laccase (Cot1) containing amino acid sequence having 513 amino acids as given in the specification (SEQ ID NO: 1);    (3) new isolated polypeptide having laccase activity encoded by the isolated DNA sequence;    (4) new isolated polypeptide having laccase activity with a primary amino acid sequence that is at least 99% identical with the sequence of COT2 (SEQ ID NO: 2);    (5) new isolated polypeptide having laccase activity with a primary amino acid sequence that is at least 83% identical with the sequence of COT1 (SEQ ID NO: 1); and    (6) wood chips comprising the isolated CotA polypeptide where the CotA laccase has a primary amino acid structure that is at least 60% identical to the sequence of COT1 (SEQ ID NO: 1) or COT2 (SEQ ID NO: 2).
NOVELTY - Controlling weeds in agricultural field using acetate having a pH of 2.3-2.5, is claimed.    USE - The method is useful for controlling weeds in agricultural field (claimed). No biological data given.    ADVANTAGE - The method is capable of economically and simply controlling the weeds in an eco-friendly manner.
NOVELTY - A succinic acid dialkyl ester compound (II) is reacted with alkyl ester compound (III) in presence of strong base, to form aldehyde compound (IV). The compound (IV) is reduced, to form triol compound (V). The compound (V) is subjected to dehydration-cyclization reaction in presence of acid catalyst, to obtain 3-(hydroxymethyl)tetrahydrofuran (I).    USE - Synthesis of 3-(hydroxymethyl)tetrahydrofuran used as intermediate for dinotefuran used as insecticide.    ADVANTAGE - The 3-(hydroxymethyl)tetrahydrofuran is manufactured efficiently and economically with high yield and less pollution, by simple method.    DETAILED DESCRIPTION - A succinic acid dialkyl ester compound of formula (II) is reacted with alkyl ester compound of formula (III) in presence of strong base, to form aldehyde compound of formula (IV). The compound (IV) is reduced, to form triol compound of formula (V). The compound (V) is subjected to dehydration-cyclization reaction in presence of acid catalyst, to obtain 3-(hydroxymethyl)tetrahydrofuran of formula (I).    R,R'=1-5C alkyl.
NOVELTY - Solid-liquid separating agent comprises 30-85 wt.% polyacrylamide flocculant, 0.2 wt.% microorganisms (solid), 0.1-0.4 wt.% fulvic acid, 5-8 wt.% bentonite, 5-30 wt.% sawdust with moisture content of less than or equal to 10%, and 0.02-0.1 wt.% gluconates with magnesium, iron (II), calcium, zinc and potassium.    USE - Solid-liquid separating agent used for reducing emissions in urine (claimed).    ADVANTAGE - The agent is inexpensive.
NOVELTY - The method involves forming an electrode catalyst layer opposing on both sides of an electrolytic membrane film (20F), and preparing the electrolytic membrane film. The prepared film is conveyed in a cutting zone (Cz) cut to product shape as a membrane electrode assembly, and the electrolytic membrane film is cut to the product shape in the cutting zone. Shape of the catalyst layer is contrasted with the film with the compatible electrode shape, and the shape suitability of the catalyst layer is determined. Cutting to the product shape is performed when shape fitness is determined.    USE - Method for manufacturing a membrane electrode assembly of a fuel cell.    ADVANTAGE - The method enables improving division precision of the membrane electrode assembly of the cutting completed to product shape, or simplifying equipment configuration and the work process accompanying the division.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an apparatus for manufacturing a membrane electrode assembly of a fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic perspective view of a cutter structure in which a film cutting apparatus is connected with an electrode joining completed electrolytic membrane film.    Cutting zone (Cz)    Electrolytic membrane (20)    Electrolytic membrane film (20F)    Anode (21)    Cathode (22)
NOVELTY - The solid oxide fuel cell has oxidant gas electrode (92) to which oxidant gas is supplied, and a solid electrolyte (94) placed between the fuel electrode (90) and oxidant gas electrode. The fuel electrode comprises a composite material containing nickel. The solid oxide fuel cell prevents shrinkage caused by oxidation of the fuel electrode by maintaining the fuel electrode in an oxygen-free atmosphere until, after electrical generation stops, the temperature of the fuel electrode falls to 350 degrees centigrade.    USE - Solid oxide fuel cell for generating electricity by reacting hydrogen and oxidant gas in fuel cell unit.    ADVANTAGE - Reduces the operating temperature of solid oxide fuel cells in generating bodies containing fuel cell unit fuel electrodes and air electrodes. Reduces the supply amount of generating air results in the discharge of high temperature air, while avoiding the risk of reverse flow, when a certain amount of time has elapsed, since shutdown and pressure on the fuel electrode has dropped.    DESCRIPTION OF DRAWING(S) - The drawing shows the partial cross-sectional view showing an individual fuel cell unit in a fuel cell apparatus.    Fuel cell units (16)    Electrode terminals (86)    Fuel gas flow path (88)    Fuel electrode (90)    Oxidant gas electrode (92)    Solid electrolyte (94)    Conductive seal material (96)
NOVELTY - Method for processing biomass, involves (a) obtaining biogas by processing waste liquid containing surfactant using methane-fermenting microbial cell before methane fermentation, (b) performing methane fermentation, and souring process, (c) adding calcium salt to fermented material for aggregating surfactant.    USE - The method and apparatus are useful for processing biomass (all claimed).    ADVANTAGE - The method enables to recover energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biomass processing apparatus.
NOVELTY - A wooden fuel pellet is obtained by mixing dried wood powder (1) having particle size of 0.2 mm or less and water content of 2-7 wt.%, with 0.1-wt.% rosin.    USE - Wooden fuel pellet (claimed).    ADVANTAGE - The wooden fuel pellet has excellent crack resistance, damp-proof property, and improved combustion efficiency by containing rosin having excellent combustibility, and low water content.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of wooden fuel pellet, which involves drying woody raw material by naturally falling from height of 3-6 m in indoor facility at room temperature of 5-45 degrees C under humidity of 20-80% having attached ventilating fan and vent hole, seasoning, drying woody raw material to water content of 3-8 wt.%, grinding woody raw material to particle size of 0.2 mm or less, grinding pine wood to particle size of 0.1 mm or less, mixing raw material and 5-50 wt.% pine wood powder (2), performing component adjustment, heating at 90-150 degrees C and pressing at high temperature by applying pressure of 150-190 kg/cm2.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of coupling structure of wooden fuel pellet. (Drawing includes non-English language text)    Wood powder (1)    Pine wood powder (2)    Film of rosin, oleic acid and linoleic acid (3)
NOVELTY - Removing phosphorus from synthetic wastewater reactor, comprises repeatedly performing anaerobic-aerobic process by using microorganisms and glucose and acetate as carbon source at 25-30 degrees C under pH of 6-8, where the microorganism strain used is Bacillus sp. 3434BRRJ.    USE - The method is useful for removing phosphorus from synthetic wastewater reactor (claimed) useful in sewage treatment plant.    ADVANTAGE - The method removes microorganisms that inhabits within the process, and improves water quality.
NOVELTY - Method for treating wastewater, involves performing pretreatment process which decomposes organic wastewater biologically under anaerobic conditions, and subjecting the treated water to biological treatment using aerobic organism.    USE - The method is useful for treating wastewater (claimed) e.g. industrial wastewater from foodstuff factory, paper pulp factory, and chemical plant.    ADVANTAGE - The method enables to remove organic substance in organic wastewater intensively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for wastewater treatment system.
NOVELTY - Organic waste is processed by subjecting liquid (L) containing organic waste to methane fermentation, recovering part of biogas (G) emitted by methane fermentation, removing ammonia from recovered biogas, and returning biogas from which ammonia is removed to liquid for fermentation. Process of recovering part of biogas and process of returning to liquid which circulates biogas are repeated. Circulation ratio, defined as ratio of circulation load of biogas with respect to generation amount of biogas per unit time, is 5-300.    USE - Processing method of organic waste (claimed).    ADVANTAGE - Excellent ammonia removal efficiency can be achieved. Processing method of organic waste can be easily performed at low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for processing apparatus (1) of organic waste comprising fermenter (10) for subjecting liquid (L) containing organic waste to methane fermentation, absorption cell (11) for removing ammonia from biogas (G) emitted by methane fermentation, biogas circulation line (18) for transferring biogas from fermenter to absorption cell, biogas circulation line (19) for returning biogas from which ammonia is removed to liquid of fermenter, and circulation ratio control unit for controlling circulation ratio to 5-300.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the processing apparatus of organic waste.    Processing apparatus (1)    Fermenter (10)    Absorption cell (11)    Biogas circulation line (18, 19)    Biogas (G)    Liquid (L)
NOVELTY - A hydrogen generating apparatus (1) comprises hydrodesulfurization device (3) which makes sulfur component contained in source gas react with hydrogen and removes sulfur component, modifier (30) for generating fuel gas containing hydrogen by modifying source gas through sulfur component removal, carbon monoxide reduction device (31) which reduces carbon monoxide in fuel gas supplied from modifier, 1st piping (2) which supplies source gas to hydrodesulfurization device and is connected to hydrodesulfurization device, and 2nd piping (32) which supplies source gas to modifier.    USE - A hydrogen generating apparatus for fuel cell power generating device.    ADVANTAGE - Hydrodesulfurization device connection points can be prevented from being damaged, service life of hydrogen generating apparatus can be extended, and failure of hydrodesulfurization device can be prevented.    DETAILED DESCRIPTION - A hydrogen generating apparatus (1) comprises hydrodesulfurization device (3) which makes sulfur component contained in source gas react with hydrogen, and removes sulfur component, modifier (30) for generating fuel gas containing hydrogen by modifying source gas through sulfur component removal, carbon monoxide reduction device (31) which reduces carbon monoxide in fuel gas supplied from modifier, 1st piping (2) which supplies source gas to hydrodesulfurization device and is connected to hydrodesulfurization device, and 2nd piping (32) which supplies source gas to modifier and connects modifier and hydrodesulfurization device. Hydrodesulfurization device may be attached and fixed to parts other than the modifier. Heat exchange between hydrodesulfurization device and modifier is possible.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional diagram of the hydrogen generating apparatus.    Hydrogen generating apparatus (1)    1st piping (2)    Hydrodesulfurization device (3)    Modifier (30)    Carbon monoxide reduction device (31)    2nd piping (32)
NOVELTY - Increasing biomass of a recombinant microorganism during fermentation, comprises: (a) providing a fermentation medium comprising a recombinant microorganism consisting of an engineered butanol biosynthetic pathway in a fermenter, where the fermentation occurs under variable conditions, one or more of the conditions has a set point; (b) monitoring one or more controlled variables; and (c) adjusting one or more variable fermentation conditions to maintain the set point of the controlled variable.    USE - The process is useful for increasing biomass of a recombinant microorganism and production of butanol during fermentation (all claimed), where the butanol is useful a fuel additive, a feedstock chemical in the plastics industry, and as a food grade extractant in the food and flavor industry.    ADVANTAGE - The process maximizes biomass production and minimizes product or byproduct formation under normal culture condition.    DETAILED DESCRIPTION - Increasing biomass of a recombinant microorganism during fermentation, comprises: (a) providing a fermentation medium comprising a recombinant microorganism consisting of an engineered butanol biosynthetic pathway in a fermenter, where the fermentation occurs under variable conditions, one or more of the conditions has a set point which the condition may be controlled to where a controlled variable is provided, and one or more variable fermentation conditions is manipulated to adjust the controlled variable; (b) monitoring one or more controlled variables; and (c) adjusting one or more variable fermentation conditions to maintain the set point of the controlled variable, where the biomasss of the recombinant microorganism is increased during fermentation. An INDEPENDENT CLAIM is included for increasing production of butanol from the recombinant microorganism during fermentation, comprising the step of (a), (b) and (c) as above per se.
NOVELTY - Converting at least one component in a carbon-bearing material to a different product comprising at least one hydrocarbon, comprises contacting the microorganism consortium with a composition that causes an increase or decrease of a relative population of at least one species of microorganism in the consortium relative to at least another species of microorganism in the consortium, to enhance a yield or selectivity or alter a rate of the process, as compared to an identical process carried out in the absence of the composition.    USE - The method is useful for converting at least one component in a carbon-bearing material, preferably coal, to a different product comprising at least one hydrocarbon such as methane, in a subterranean formation and ex-situ formation (all claimed).    ADVANTAGE - The method is capable of promoting the yield, rate and/or selectivity of the conversion process.    DETAILED DESCRIPTION - Converting at least one component in a carbon-bearing material to a different product comprising at least one hydrocarbon, comprises contacting the microorganism consortium with a composition that causes an increase or decrease of a relative population of at least one species of microorganism in the consortium relative to at least another species of microorganism in the consortium, to enhance a yield or selectivity or alter a rate of the process, as compared to an identical process carried out in the absence of the composition, where the composition is a composition that directly or indirectly affects an intracellular pathway of the species of microorganism and a composition that affects an intercellular signaling pathway that involves the species of microorganism.
NOVELTY - Co-evolving fermentation composition comprises: a metabolite-dependent bacterium whose propagation is dependent on a first metabolite; a metabolite-producing bacterium that produces the first metabolite and requires an essential nutrient for propagation; and a co-evolving bacteriophage that propagates in and co-evolves with the metabolite-producing bacterium.    USE - The co-evolving fermentation composition is useful for producing methanol.    ADVANTAGE - The composition provides the target metabolite in a high yield.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a method (M1) for developing a bacterial strain that produces a target metabolite comprising: exposing at least two co-dependent bacterial strains and at least one co-evolving bacteriophage to a selection medium having an initial concentration of exogenous target metabolite, where a first bacterium is target metabolite-dependent bacterium and a second bacterium is a first target metabolite-producing bacterium, and the co-evolving bacteriophage is selective for the target metabolite-producing bacterium; incubating the selection medium comprising the co-dependent bacteria and co-evolving bacteriophage; reducing the concentration of exogenous target metabolite; and isolating a second target metabolite-producing bacterium that has evolved from the first target metabolite-producing bacterium that produces the target metabolite at levels greater than the first target metabolite-producing bacterium; and    (2) a method (M2) for producing methanol comprising: incubating a production medium containing an evolved methanol-producing bacteria; and isolating methanol from the production medium.
NOVELTY - The method involves supplying carbon source gas and a silicon substrate to a silicon pillar structure. The silicon pillar structure is provided with iron-molybdenum catalyst solution and the silicon substrate. The silicon pillar structure is formed in a side part of the silicon substrate. A coating part is coated with metal through carbon nanotube three dimensional (3D) networks. The carbon nanotube 3D networks are formed between the silicon pillar structure and a metal oxide part. The coating part is coated with platinum, copper and chrome.    USE - Metal or metal oxide nanostructure manufacturing method.    ADVANTAGE - The method enables depositing a hierarchy structure so as to improve an electrochemical process. The method enables improving the nanostructure manufacturing process so as to reduce the nanostructure manufacturing process time. The method enables improving performance of the metal or metal oxide nanostructure.    DETAILED DESCRIPTION - The carbon source gas is methane, ethylene, acetylene, benzene, hexane, ethanol, methanol or propanol. An INDEPENDENT CLAIM is also included for a metal or metal oxide nanostructure.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a metal or metal oxide nanostructure manufacturing method.
NOVELTY - The method involves drying the biomass (B) in a drier (13) to produce dried biomass (BT). The exhaust air (A) of the drier in a flue (15) is discharged to the environment. The dried biomass in a portion of the plant is processed. The exhaust air containing moisture is sprayed with water (W) in a spraying tower (2) between the drier and the flue. The moisture is condensed into condensate (K) in the spraying tower by the accompanying cooling of the exhaust air, so that waste water (AW) arising from the condensate is to moisten or control the temperature of biomass.    USE - Method for processing biomass in plant used for production of paper, pellets or material sheets.    ADVANTAGE - The necessary use of fresh water is reduced and the efficiency of the plant is increased by reusing the low-calorific energy. The flue gases are controlled to avoid heat loss of the dryer for reuse. The water consumption is significantly reduced. The less expensive air cleaning of the exhaust gases with respect to the regenerative thermal oxidation or a wet electrostatic precipitator is enhanced. The drying energy and reuse is increased either directly or indirectly. The relative humidity in the air before cleaning device or the fireplace is reduced significantly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for system for processing biomass in plant.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the plant.    Spraying tower (2)    Drier (13)    Flue (15)    Exhaust air (A)    Waste water (AW)    Biomass (B)    Dried biomass (BT)    Condensate (K)    Water (W)
NOVELTY - Producing-1 a low emission biomass fuel composition from waste material, comprises: evaluating selected waste material; treating the evaluated waste material with an additive comprising an emission sponge and a filler; and forming solid fuel structures from the treated waste material.    USE - The process is useful for producing low emission biomass fuel composition from waste material, where the fuel composition is useful in place of or combined with coal, in coal burning structures and devices.    ADVANTAGE - The process provides solid fuel formations, which produces lower gas emission than coal alone.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) producing-2 a low emission biomass fuel composition from waste material, comprising measuring the moisture content of selected waste material, measuring the gas emissions levels of the selected waste material when the waste material is burned, formulating an additive to be combined with the selected waste material, sizing the selected waste material to a uniform size of not greater than one half inch in diameter, adjusting the moisture content of the selected waste material to be between 12 and 25 wt.%, coating the treated material with the additive formulated for use with the selected waste material soaking the sized waste material at at least 130 degrees F for at least one minute; and    (2) low emission biomass fuel composition comprising treated waste material and the additive composition formulated to adjust the gas emissions levels of the treated waste material to a predetermined target level.
NOVELTY - The purification device includes an activated carbon filter to purify or reduce number of radioactive particles from radon-222 contained in natural gas.    USE - Purification device for natural gas radon and gas consumption optimizer.    ADVANTAGE - The purification device improves combustion of natural gas or other related hydrocarbons by bringing an element in driving gas mechanically, achieves improved heat capacity of the gas, reduces emissions of poisonous gasses to environment, and thus reduces carcinogenic effects.    DESCRIPTION OF DRAWING(S) - The drawing shows a vertical sectional view of the gas optimization mechanism.    Mouthpiece (1)    Spiral tube (2)    Outlet (3)    Turbulence form (4)
NOVELTY - Safety emulsion explosive composition as the oxidising phase comprises water, ammonia and sodium nitrate, carbamide or potassium chloride, taken in the eutectic or near eutectic ratio, as hydrocarbon phase - emulsifier for industrial explosives, individually or in a mixture of tall oil or pine gum rosin, with liquid or solid chloroparaffin and possible additives of oil of industrial or fine-grained paraffin, powdered sodium or potassium chloride as a flame arrester, and as sensitiser - glass or polymeric microspheres "Expancel" DR (T) with the size capsules of 60-80 micron, containing combustible gas inclusions of isopropane or isobutane in shells of copolymers or gas-generating additives of aqueous solution of sodium nitrite and providing the controlled density of the final product in the range of 1.05-1.20 g/cm3.    USE - Blasting operations.    ADVANTAGE - Good operational and explosive characteristics, including safety at the level of class III-IV, physical and chemical stability during long term of storage.2 cl, 5 ex
NOVELTY - The dry high temperature type methane-fermenting apparatus (10) has a receiving chamber (C) in which methane gas raw material is put. A gas exhaust port (117) is formed to eject the methane gas generated from the methane gas raw material. Multiple gas collection modules (100) are provided with a cover (140) that covering an opened portion of a cylindrical container (110). One side of the container is opened. The gas collection module is laminated to top and bottom of the container, and is installed on the container.    USE - Dry high temperature type methane-fermenting apparatus used for collecting methane gas generated from organic trash such as plant garbage, sprouting from food waste, farmhouse, forest, livestock and human excrement. Can also be used in methane gas for cooking.    ADVANTAGE - The transportability of the dry high temperature type methane-fermenting apparatus is good, and the installation of the apparatus is eased. The use of the apparatus is facilitated, as the temperature of the apparatus is increased. Since the mixing process is smoothly performed in the apparatus, the efficiency of the apparatus is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the dry high temperature type methane-fermenting apparatus.    Dry high temperature type methane-fermenting apparatus (10)    Gas collection module (100)    Container (110)    Gas exhaust port (117)    Cover (140)    Receiving chamber (C)
NOVELTY - An Agaricus blazei cultivation material comprises 70-80 pts. wt. coix rod, 15-20 pts. wt. poultry manure, 5-10 pts. wt. bran or wheat bran, 3-5 pts. wt. seed cake, 3-5 pts. wt. corn flour, 1 pt. wt. gypsum powder, 1 pt. wt. lime, and 60 pts. wt. water.    USE - Agaricus blazei cultivation material.    ADVANTAGE - The method is environment-friendly, achieves comprehensive utilization of agricultural waste, and has economic and ecological benefits.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of cultivation material by collecting coix seed rod with no molds, chopping into 15-20 mm long, mixing with remaining raw materials, fermenting, and steam-heating to 50-55 degrees C to carry out secondary fermentation for 3-5 days.
NOVELTY - Preparation of alprostadil combination drug involves mixing 70-15 wt.% alprostadil, 20-35 wt.% vitamin C, 5-20 wt.% folic acid and 30-60 wt.% glycine, performing ultra-filtration with interception molecule, adjusting pH value to 6.1-6.5 with hydrochloric acid, sterilizing at 121 degrees C for 20 minutes and cooling to 20-22 degrees C.    USE - Method for preparing alprostadil combination drug used for treating myocardial infarction, thrombosis, occlusive arteriosclerosis, thromboangiitis obliterans and chronic atherosclerosis (claimed).    ADVANTAGE - The method is energy-saving and environmental friendly. The alprostadil combination drug is safe and stable.
NOVELTY - Processing of ammonia absorbing tail gas using sulfur recovery device comprises filling first-stage absorber top part with tail gas, spraying lower part with absorbing liquid, counter-current contacting, absorbing, oxidizing, gas-liquid separating, contacting, absorbing, washing, defogging and discharging. Sulfur recovery device comprises electric defogger (2), baffle plate defogger (3), washing absorber (4), three absorbers (6,9,10), absorption-oxidation tower (7) and exhaust (27).    USE - Method of processing absorbing tail gas using sulfur recovery device (claimed).    ADVANTAGE - The device reduces sulfur dioxide emission concentration to less than or equal to 50mg/Nm3 and ammonia escape amount to less than or equal to 10 mg/m3. The processing method is simple and environment-friendly. The byproduct can be used as fertilizer.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of sulfur recovery device.    Electric defogger (2)    Baffle plate defogger (3)    Washing absorber (4)    Absorber (6,9,10)    Absorption-oxidation tower (7)    Exhaust (27)
NOVELTY - The method involves performing a primary rubbish crushing process. Biomass micro-organism strain is sprayed according to the primary rubbish crushing process. A high temperature steam sterilization process is performed. A light material is separated to form air separating heavy substances. The light material is cracked at temperature of 1200 degrees Celsius. A high temperature furnace cracking process is performed to obtain a liquid fuel product.    USE - Municipal domestic waste high temperature cracking RDF6-type gas production method.    ADVANTAGE - The method enables optimizing the liquid fuel product. The method enables producing RDF3-type fuel granule. The method enables recording overall production process corresponding to national standards and stringent international standards. The method enables enclosing gas production process.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram illustrating a municipal domestic waste high temperature cracking RDF6-type gas production method.'(Drawing includes non-English language text)'
NOVELTY - Preparation of activated carbon from Xanthoceras sorbifolia biodiesel processing residue comprises drying Xanthoceras sorbifolia biodiesel processing residues at 100-120 degrees C to moisture content of 5-10%, crushing, adding 40-60% zinc chloride solution, mixing, stirring, soaking, carbonizing at 200-300 degrees C for 3-5 hours in box-type furnace under nitrogen atmosphere at flowrate of 500 mL/minute, activating at 500-550 degrees C for 60-120 minutes, adding 8-12% dilute hydrochloric acid solution, repeatedly washing with deionized water until neutral, drying, crushing, grinding and sieving.    USE - Method for preparing activated carbon from Xanthoceras sorbifolia biodiesel processing residue (claimed).    ADVANTAGE - The method is simple, cost-saving and environment-friendly. The product has large specific surface area, developed pore structure and good adsorption performance.    DETAILED DESCRIPTION - Preparation of activated carbon from Xanthoceras sorbifolia biodiesel processing residue comprises drying Xanthoceras sorbifolia biodiesel processing residues at 100-120 degrees C to moisture content of 5-10%, crushing into 80-120 mesh particles, adding 40-60% zinc chloride solution at solid-liquid ratio of 2:1-3:1, mixing, stirring, soaking for greater than or equal to 30 minutes, carbonizing at 200-300 degrees C for 3-5 hours in box-type furnace under nitrogen atmosphere at flowrate of 500 mL/minute, activating at 500-550 degrees C for 60-120 minutes, adding 8-12% dilute hydrochloric acid solution, repeatedly washing with deionized water until neutral, drying at 100-120 degrees C for 24-48 hours to moisture content of less than or equal to 10%, crushing, grinding and sieving.
NOVELTY - A Lysinibacillus sp. FS1 (CCTCC NO. M 2013561) is new.    USE - The Lysinibacillus sp. FS1 is useful for decolorizing dyes and sewage treatment (claimed).    ADVANTAGE - The Lysinibacillus sp. FS1 is used for efficiently decolorizing dyes. The Lysinibacillus sp. FS1 is environment-friendly, grows rapidly and has strong environment adaptability and broad dye spectrum.
NOVELTY - An organic sewage is converted into liquid fuel by preprocessing organic sewage in sewage collecting pool, taking into sewage regulating pool, adding biological agent, and purifying and deodorizing, the biological agent comprising insecticide and deodorant; at normal temperature and normal pressure, and anaerobic condition, taking pre-treated organic sewage through multi-microorganism fungus fermentation process; and taking through multilevel biochemical reaction device, and through the action of multi-microorganism fungi, the organic sewage is converted into liquid fuel.    USE - Method for converting organic sewage into liquid fuel (claimed).    ADVANTAGE - The method is simple, inexpensive and convenient for industrial production.
NOVELTY - A sludge compost wood surface conditioning agent is carbonized by taking wood conditioning agent, and carbonizing surface by physical or chemical carbonization.    USE - Method for carbonizing sludge compost wood surface conditioning agent (claimed).    ADVANTAGE - The process reduces volatilization and dehydration, forms layer with uniform thickness and microporous structure, preserves conditioning agent strength, improves adsorbing ability, reduces ammonia and harmful gas content, improves sludge utilization, and increases nitrogen content of the compost product.
NOVELTY - An agricultural microbial fertilizer comprises Actinomyces, Lactobacillus, yeast, photosynthetic bacteria and nitrogen-fixing bacteria.    USE - Agricultural microbial fertilizer for improving disease, lodging and pest resistance of corn, Sorghum, soybean and rice, and improving soil.    ADVANTAGE - The microbial fertilizer improves product quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of agricultural microbial fertilizer comprising adding Actinomyces, Lactobacillus, yeast, photosynthetic bacteria, nitrogen-fixing bacteria, straw powder, sludge source and cow manure, stirring, heating to 60-70 degrees C, and fermenting at 60-70 degrees C for 5-15 days.
NOVELTY - Grifola frondosa culture medium comprises 50-60 wt.% Chinese medicine residue, 20-25 wt.% Pleurotus waste material, 4-8 wt.% nutrients, 10-15 wt.% forest soil and 3-5 wt.% rice husk ash.    USE - Grifola frondosa culture medium.    ADVANTAGE - The method is environment-friendly and has less than 40-45% raw material cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of Grifola frondosa culture medium comprising mixing raw materials, adding water, controlling moisture content to 60-63% and pH value to 7.5-8.0, mixing, bottling, sterilizing at 110-140 degrees C for l-4 hours, cooling to 25-30 degrees C, inoculating Grifola frondosa parent species into the bottle, placing in culture chamber and culturing at 23-28 degrees C for 15-35 days.
NOVELTY - A flower cultivation nutrient medium comprises 200-300 pts. wt. silt, 100-300 pts. wt. rapeseed shell, 80-150 pts. wt. sawdust, 50-120 pts. wt. corn stalk, 8-12 pts. wt. urea, 50-85 pts. wt. livestock manure, 10-20 pts. wt. fermentation bacteria and water.    USE - Flower cultivation nutrient medium used for improving germination rate, rooting rate and survival rate of flowers.    ADVANTAGE - The balanced nutrient medium has stable physical property and simple preparation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of nutrient medium comprising spreading field as bottom silt base, crushing corn stalk to 100-200 mesh particles, mixing corn stalk particles, wood chips and urea, adding water, stirring, adding fermentation bacteria, stirring, spreading on bottom base, covering with rapeseed shell, sealing with plastic film, and fermenting at 50-60 degrees C by turning for 15-20 days.
NOVELTY - A biological special fruit tree fertilizer comprises 1 pt. wt. Bacillus mucilaginosus, 40-60 pts. wt. soybean meal, 30-50 pts. wt. chicken manure, 10-30 pts. wt. straw, 20-40 pts. wt. monosodium glutamate dreg, 20-50 pts. wt. pepper, 20-40 pts. wt. holly root, 10-50 pts. wt. common cnidium fruit, 40-60 pts. wt. neem bark, 50-70 pts. wt. Quisqualis indica, 30-50 pts. wt. gallnut, 5- 15 pts. wt. yeast powder and 5-10 pts. wt. microelement additive.    USE - Biological special fruit tree fertilizer.    ADVANTAGE - The fertilizer has stable property, no poison and side effect, promotes absorption of nutrition component in soil, and increases fruit yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biological special fruit tree fertilizer comprising cleaning pepper, holly, common cnidium fruit, neem bark, Quisqualis indica and gallnut, crushing, soaking in water for 2 hours, adding water, reflux extracting for 1-3 hours, concentrating to relative density of 1.01-1.05 at 30 degrees C to obtain extract, placing soybean meal, chicken manure, straw and monosodium glutamate dreg into fermenter, adding yeast powder, microelement additive and extract, inoculating with Bacillus mucilaginosus, fermenting at 30-40 degrees C for 5-15 days, drying, and crushing.
NOVELTY - A vegetable biofertilizer comprises 1 pt. wt. Rhodobacter sphaeroides, 1-5 pts. wt. arbuscular mycorrhizal agent, 30-50 pts. wt. potato, 40-60 pts. wt. straw, 10-20 pts. wt. ammonium dihydrogen phosphate, 10-20 pts. wt. calcium hydrophosphate, 5-15 pts. wt. potassium dihydrogen phosphate and 2-8 pts. wt. microelement additive.    USE - Vegetable biofertilizer.    ADVANTAGE - The fertilizer has stable property, no poison and side effect, promotes absorption of nutrition component in soil, increases fruit yield, capable of secreting anti-biocontaminant, restrains soil transfer pathogen, and prevents insect pests.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of vegetable biofertilizer comprising crushing potato and straw, placing into fermenter, adding 1000 pts. wt. purified water and Rhodobacter sphaeroides, fermenting at 30-40 degrees C for 5-10 days, adding arbuscular mycorrhizal agent, continuously fermenting to 30-40 degrees C for 1-3 days, adding ammonium dihydrogen phosphate, calcium hydrophosphate, potassium dihydrogen phosphate and microelement additive, mixing, placing in ice for 24-48 hours, drying, and crushing.
NOVELTY - A biological carbon-based slow-release compound fertilizer comprises 22-78 pts. wt. tobacco straw biomass charcoal and 40-50 pts. wt. nitrogen-phosphorus-potassium compound fertilizer containing nitrogen, phosphorus pentoxide, and potassium oxide at mass ratio of 8-22:8-22:10-24. The tobacco straw biomass charcoal is prepared by pyrolyzing tobacco stem at 380-450 degrees C under anaerobic environment.    USE - Biological carbon-based slow-release compound fertilizer used for tobacco (claimed).    ADVANTAGE - The fertilizer has improved physical and chemical properties of soil and microbial activity in tobacco fields, increases soil carbon sequestration potential role, increases soil organic matter, soil cation exchange capacity and aggregate structure, prevents soil compaction, and improves soil water and heat conditions. The tobacco stalk biomass charcoal delays soil nutrient release, reduces nutrient losses, and improves fertilizer use efficiency. The fertilizer has wide source, cheap, and easy to get raw materials. The method has low production costs and high ecological and agricultural waste utilization and is easy to operate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of fertilizer comprising taking tobacco straw biomass charcoal; and mixing with the rest of components, stirring, drying, and granulating.
NOVELTY - An oyster mushroom cultivation material comprises 30-4800 kg corncob, 50-2800 kg bean dregs, 20-400 kg clam shell, 12-240 kg hydrochloric acid solution, 4-152 kg lime powder, 1-76 kg light calcium carbonate, and 0.1-2 kg zinc sulfate.    USE - Oyster mushroom cultivation material.    ADVANTAGE - The cultivation material has increased amount of calcium. The method utilizes waste clam shell and does not pollute the environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of cultivation material comprising:    (A) crushing corncob, adding 2-4% lime powder, and fermenting to 8-28 degrees C for 4-7 days to obtain fermented corncob;    (B) drying bean dregs until water content is less than 40%, adding remaining lime powder, and fermenting to 8-28 degrees C for 4-7 days to obtain fermented bean dregs;    (C) crushing clam shell, adding hydrochloric acid solution, mixing uniformly, and fermenting to 10-28 degrees c for 3-10 days to obtain fermented clam shell powder;    (D) mixing fermented corncob and fermented bean dregs, adjusting water content to 55-65%, and fermenting to 5-28 degrees C for 5-10 days to obtain fermented mixture; and    (E) mixing fermented clam shell with zinc sulfate and light calcium carbonate, adjusting water content to 35-45%, mixing with fermented mixture, adjusting water content to 60-65%, and fermenting to 5-30 degrees C for 5-16 days.
NOVELTY - Cresol is synthesized by performing toluene chlorination and controlling reaction conversion rate to 95-98% to obtain mixed chlorotoluene comprising p-chlorotoluene, o-chlorotoluene and m-chlorotoluene; adding mixed chlorotoluene with 3 times alkali liquid and performing hydrolysis reaction at conversion rate of 95-98%; and cooling reaction product, layering, extracting and distilling, rectifying, and performing tert-butylation to prepare o-cresol, m-cresol and 2,6-di-tert-butyl-p-cresol.    USE - Method for synthesizing cresol (claimed).    ADVANTAGE - The method has increased yield, and does not require separation of mixed chlorotoluene to reduce consumption of material resource and labor and also reduce rectifying high boiling process and discharge of pollutant.
NOVELTY - Synthesis of 2-amino-propanol comprises subjecting glycerol as raw material and metal catalyst into gas-solid or liquid-solid phase reaction to obtain dihydroxyacetone; and subjecting dihydroxyacetone solution without separating or isolating pure hydroxyacetone into hydrogenation with ammonia synthesis catalyst and under hydrogen atmosphere to obtain 2-amino-propanol.    USE - Synthesis of 2-amino-propanol.    ADVANTAGE - The method can be carried out in tank batch mode or fixed-bed continuous production. It is environment friendly, economical and highly efficient, and has small investment of glycerol to synthesize 2-amino propanol.
NOVELTY - Preparation of chlorocarbonyl(4-(trifluoromethoxy)phenyl)methyl carbamate comprises mixing trifluoromethoxyaniline, methylchloroformate and toluene, cooling, and dropping sodium carbonate solution; heating, washing with water, filtering, and refluxing until no more water content to obtain dry mixture; dissolving diphosgene in toluene, adding alkali, and reacting; adding with dry mixture, heating, washing with water, extracting, drying, and distilling off solvent; and adding petroleum ether, precipitating white crystals, and filtering.    USE - Method for preparation of chlorocarbonyl(4-(trifluoromethoxy)phenyl)methyl carbamate (claimed).    ADVANTAGE - The method obtains high purity product and it has mild operation, short reaction period, and reduced energy consumption and production cost.    DETAILED DESCRIPTION - Preparation of chlorocarbonyl(4-(trifluoromethoxy)phenyl)methyl carbamate comprises:    (A) mixing trifluoromethoxyaniline, methylchloroformate and toluene, cooling to - 5-5 degrees C, and dropping sodium carbonate solution;    (B) heating to 30-40 degrees C for 1.5-5 hours, washing with water, filtering, and refluxing until no more water content to obtain dry mixture;    (C) dissolving diphosgene in toluene and controlling temperature to 5-10 degrees C;    (D) adding alkali, reacting to 0-10 degrees C for 20-30 minutes;    (E) adding with dry mixture, reacting to - 5-5 degrees C until addition is completed, heating to 25-35 degrees C, washing with water, extracting, drying, and distilling off solvent; and    (F) adding petroleum ether, precipitating white crystals, and filtering.
NOVELTY - 2-deoxy-D-glucose is prepared by reacting 3,4,5-tri-O-acetyl-D-glucal which forms 3,4,5-trihydroxy-2-deoxy-D-glucal or directly reacting 3,4,5-trihydroxy-2-deoxy-D-glucal with solid acid in solvent at specified temperature and time, filtering off solid acid, cleaning solid acid using washing solution, adding activated carbon to bleach, filtering, recovering solvent under vacuum, recrystallizing in recrystallization solvent, cooling, filtering, washing with recrystallization solvent, and vacuum drying to obtain white solid.    USE - Preparation of 2-deoxy-D-glucose (claimed).    ADVANTAGE - Process is environment-friendly, simple, low cost, safe, reliable, avoids acidification and extraction process, uses recyclable solid acid and less raw material, and has high yield and mild reaction conditions.    DETAILED DESCRIPTION - 2-deoxy-D-glucose of formula (III) is prepared by reacting 3,4,5-tri-O-acetyl-D-glucal of formula (I) which forms 3,4,5-trihydroxy-2-deoxy-D-glucal of formula (II) or directly reacting 3,4,5-trihydroxy-2-deoxy-D-glucal (II) with solid acid in solvent at specified temperature and time, filtering off solid acid, cleaning solid acid using washing solution, adding activated carbon to bleach, filtering, recovering solvent under vacuum, recrystallizing in recrystallization solvent, cooling, filtering, washing with recrystallization solvent, and vacuum drying to obtain white solid.
NOVELTY - Hepta-O-acetyl-1-mercapto- beta -D-maltose is synthesized by performing acylation reaction to D-maltose raw material to obtain octa-O-acetyl- alpha -D-maltose, carrying out bromination reaction to obtain hepta-O-acetyl- alpha -D-bromo-maltose, adding thiourea, reacting to obtain mixture containing hepta-O-acetyl- beta -D-maltose isothiourea hydrobromide, adding water and organic solvent mixture, extracting, separating hepta-O-acetyl- beta -D-maltose isothiourea hydrobromide aqueous solution, and hydrolyzing.    USE - Synthesis of hepta-O-acetyl-1-mercapto- beta -D-maltose for drug intermediate.    ADVANTAGE - Synthesis process is simple and environment-friendly, has high product yield and purity and mild reaction conditions, and uses cheap and easy to obtain raw materials.
NOVELTY - Preparation of 17 alpha -hydroxyprogesterone involves performing Grignard reaction of 4-androstenedione-diketone as raw material, acetone cyanohydrin, triethyl orthoformate and ethanol for protecting carbonyl group in 3 position, and vinyl butyl ether for protecting hydroxyl group in 17 position and hydrolyzing.    USE - Preparation of 17-alpha-hydroxyprogesterone (claimed).    ADVANTAGE - The method stably and economically provides 17-alpha-hydroxyprogesterone having high yield and selectivity, with reduced environmental pollution, by a simple process in a short period of time under mild reaction conditions.
NOVELTY - Spironolactone derivatives (Q) comprising S-((7R,8R,9S,10R,12R,13R,14S,17R)-12-hydroxy-10,13-dimethyl-3,5'-dioxo-spiro(2,6,7,8,9,11,12,14,15,16-decahydro-1H-cyclopenta(a)phenanthrene-17,2'-tetrahydrofuran)-7-yl) (I) and S-((2R,7R,8R,9S,10R,13S,14S,17R)-2-hydroxy-10,13-dimethyl-3,5'-dioxo-spiro(2,6,7,8,9,11,12,14,15,16-decahydro-1H-cyclopenta(a)phenanthrene-17,2'-tetrahydrofuran)-7-yl) (II), are new.    USE - (Q) are useful for promoting urination (claimed).    ADVANTAGE - (Q) can be prepared in a simple and economical manner with strong pollution-resistant ability, high yield and safety and reduced toxicity.    DETAILED DESCRIPTION - Spironolactone derivatives (Q) comprising S-((7R,8R,9S,10R,12R,13R,14S,17R)-12-hydroxy-10,13-dimethyl-3,5'-diocxo-spiro(2,6,7,8,9,11,12,14,15,16-decahydro-1H-cyclopenta(a)phenanthrene-17,2'-tetrahydrofuran)-7-yl) of formula (I) and S-((2R,7R,8R,9S,10R,13S,14S,17R)-2-hydroxy-10,13-dimethyl-3,5'-dioxo-spiro(2,6,7,8,9,11,12,14,15,16-decahydro-1H-cyclopenta(a)phenanthrene-17,2'-tetrahydrofuran)-7-yl) of formula (II), are new. An INDEPENDENT CLAIM is included for the preparation of (Q).
NOVELTY - L-alanine-L-glutamine compound is prepared by reacting thionyl chloride and glycolic acid-containing compound to obtain dichloroketene-containing compound, adding glutamine under basic condition to obtain chloroethanone-containing compound, adding ammonia water, and performing ammonolysis reaction.    USE - Preparation of L-alanine-L-glutamine compound (claimed).    ADVANTAGE - Process is simple, low cost, and environment-friendly, does not use flammable reagent, and has mild reaction condition, high safety, and has short reaction period, raw material is easy to obtain, and product has high yield.    DETAILED DESCRIPTION - L-alanine-L-glutamine compound of formula (11) is prepared by reacting thionyl chloride and glycolic acid-containing compound of formula (8) to obtain dichloroketene-containing compound of formula (9), adding glutamine under basic condition to obtain chloroethanone-containing compound of formula (10), adding ammonia water, and performing ammonolysis reaction.    R=1-20C alkyl.
NOVELTY - High purity white spine amphotericin B nucleus is prepared by regulating pH of white spine amphotericin B nucleus solution to 4-4.5 using acid, adding polyacrylamide flocculating agent to sediment impurity, adding filter aid, uniformly stirring, dispersing, performing solid-liquid separation to obtain primary filtrate, adjusting pH to 6-6.5 using alkali solution, adding filter aid, uniformly stirring, dispersing, performing solid-liquid separation to secondary filtrate, decoloring with macroporous decoloring resin to obtain decoloring solution, absorbing with absorbing resin, and analyzing.    USE - Preparation of high purity white spine amphotericin B nucleus for production of pharmaceutical grade raw material.    ADVANTAGE - Process is simple, environment-friendly, and low cost, and product has high purity and yield and improved quality.    DETAILED DESCRIPTION - High purity white spine amphotericin B nucleus is prepared by regulating pH of white spine amphotericin B nucleus solution to 4-4.5 using acid, adding polyacrylamide flocculating agent to sediment impurity, adding filter aid, uniformly stirring, dispersing, performing solid-liquid separation to obtain primary filtrate, adjusting pH to 6-6.5 using alkali solution, adding filter aid, uniformly stirring, dispersing, performing solid-liquid separation to secondary filtrate, decoloring with macroporous decoloring resin to obtain decoloring solution, absorbing with absorbing resin, analyzing using aqueous acid solution, performing high-performance liquid chromatography (HPLC) detection, collecting analytical solution, concentrating to obtain concentrated solution, regulating pH to 6-6.5, performing polystyrene or divinylbenzene resin column chromatography, analyzing using aqueous acid solution containing ethanol, performing HPLC detection, collecting chromatography solution, and freeze-drying.
NOVELTY - Preparing high molecular water-absorbing resin comprises mixing sodium hydroxide aqueous solution with 1500 g of acrylic acid and then reacting for 20 minutes and cooling to 60-70 degrees C, adding 1200 g of phosphoric acid and 500 g of urea and then stirring, mixing crosslinking agent with 8 g of ethylene glycol and 4 g of potassium persulfate initiator, performing graft copolymerization reaction of the mixture, and aging the reaction mixture in a polymerization reactor and then polymerizing for 10-20 minutes and drying to obtain solid product, and crushing the solid product into particles.    USE - The method is useful for preparing high molecular water-absorbing resin (claimed).    ADVANTAGE - The method is capable of preparing the high molecular water-absorbing resin with good quality, stability and absorbency of 300 g/g, phosphorus content of more than 45% nitrogen content of more than 9% in an eco-friendly manner.    DETAILED DESCRIPTION - Preparing high molecular water-absorbing resin comprises (a) preparing 800 g of sodium hydroxide aqueous solution with concentration of 30%, (b) mixing sodium hydroxide aqueous solution with 1500 g of acrylic acid with purity of 99.5% and then reacting for 20 minutes and cooling to 60-70 degrees C, adding 1200 g of phosphoric acid and 500 g of urea and then stirring at speed of 110-120 revolutions per minute (rpm), (c) mixing crosslinking agent with 8 g of ethylene glycol and 4 g of potassium persulfate initiator, performing graft copolymerization reaction of the mixture at 100-115 degrees C for 15-20 minutes, and aging the reaction mixture in a polymerization reactor and then polymerizing for 10-20 minutes and drying to obtain solid product, and (d) crushing the solid product into particles.
NOVELTY - Combined biofuel oil and polyol formulation contains 0-70 pts. wt. methanol-modified complex, 5-70 pts. wt. oleic acid, 5-50 pts. wt. n-butanol, 1-8 pts. wt. surfactant, 1-15 pts. wt. modifying additive, and 0-45 pts. wt. industrial pure water in which methanol-modified complex is formed by condensing methanol and alcohol with ether and/or condensing methanol and acid with ester, and industrial pure water is deionized water.    USE - A combined biofuel oil and polyol formulation for kitchen stove, industrial furnace, and diesel engine vehicle.    ADVANTAGE - Process is low cost, energy-saving, and environment-friendly, and product is easy to transport and store and has high flash point, low pour point and cold filter plugging point, corrosion resistance, and reduced smoke emission.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of combined biofuel oil and polyol formulation which involves regulating hydrophile-lipophile balance of surfactant to 10-14, uniformly mixing n-butanol into water, adding oleic acid, methanol-modified complex, and modifying additive, and uniformly mixing.
NOVELTY - A combined biodiesel oil and polyol formulation contains 5-85 pts. wt. petrochemical diesel oil, 0-70 pts. wt. methanol-modified complex, 5-70 pts. wt. oleic acid, 2-45 pts. wt. n-butanol, 1-5 pts. wt. surfactant, 1-8 pts. wt. modifying additive, and 0-35 pts. wt. industrial pure water in which methanol-modified complex is formed by condensing methanol with ether and/or ester, industrial pure water is deionized water, and addition amount of industrial pure water and methanol-modified complex are not 0 pt. wt.    USE - A combined biodiesel oil and polyol formulation for kitchen stove, industrial furnace, and diesel engine vehicle.    ADVANTAGE - Process is low cost, energy-saving, and environment-friendly, and product is easy to transport and store and has high cetane number and flash point, low pour point and cold filter plugging point, corrosion resistance, improved calorific value, and reduced smoke emission.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of combined biodiesel oil and polyol formulation which involves regulating hydrophile-lipophile balance of surfactant to 10-14, uniformly mixing n-butanol into water, adding oleic acid, petrochemical diesel oil, methanol-modified complex, and modifying additive, and uniformly mixing.
NOVELTY - Combined biodiesel oil and polyol formulation contains 5-85 pts. wt. petrochemical diesel oil, 0-70 pts. wt. methanol-modified complex, 5-70 pts. wt. oleic acid, 5-75 pts. wt. methanol and/or ethanol, 1-5 pts. wt. surfactant, 1-8 pts. wt. modified additive, and 0-35 pts. wt. industrial pure water in which methanol-modified complex is formed by condensing methanol with ether or ester, industrial pure water is deionized water, and addition amount of industrial pure water and methanol-modified complex are not 0 pt. wt.    USE - Combined biodiesel oil and polyol formulations for kitchen stove, industrial furnace, and diesel engine vehicle.    ADVANTAGE - Process is low cost, energy-saving, and environment-friendly, and product is easy to transport and store and has high cetane number and flash point, low pour point and cold filter plugging point, corrosion resistance, improved calorific value, reduced smoke emission, and long period of stability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of combined biodiesel oil and polyol formulation which involves regulating hydrophilic-lipophilic balance of surfactant to 10-14, uniformly mixing methanol and/or ethanol into water, adding oleic acid, petrochemical diesel oil, methanol-modified complex, and modified additive, and uniformly mixing.
NOVELTY - Alcohol-based fuel is produced by pretreating waste frying oil into methanol and n-hexanol, mixing octanol and oleic acid, and adding 0.6 mass% ferrocene in which volume ratio methanol:waste frying oil:oleic acid is 100:12:8.    USE - Production of alcohol-based fuel (claimed).    ADVANTAGE - Process reduces dehydrogenation reaction and thermal cracking reaction and improves combustion efficiency, and product has good solubility and combustion effect.
NOVELTY - An alcohol-based fuel contains 85-96 pts. wt. methanol, 2-6 pts. wt. ethanol, 1-5 pts. wt. butanone, 1-2 pts. wt. paraffin oil, 0.5-2 pts. wt. water, and 0.1-0.2 pt. wt. ferric chloride.    USE - Alcohol-based fuel for diesel oil and fuel oil.    ADVANTAGE - Alcohol-based fuel has low cost and improved fuel combustion effect.
NOVELTY - A polyol biofuel composition contains not greater than 85 pts. wt. methanol-modified composite, 5-70 pts. wt. oleic acid, 5-80 pts. wt. methanol and/or ethanol, 1-8 pts. wt. surfactant, 1-15 pts. wt. modifying additive, and 0-45 pts. wt. industrial water in which methanol-modified composite is methanol condensed with alcohol ether and/or methanol condensed with acid ester and industrial water is deionized water.    USE - Polyol biofuel composition for fuel oil (claimed) used for kitchen stove, industrial furnace, and diesel engine vehicle.    ADVANTAGE - Polyol biofuel composition has increased cetane number, good versatility, and long storage life, and is environment-friendly. Fuel oil used with polyol biofuel composition has high flash point, low freezing point, low cold filter plugging point, corrosion resistance, low emission, and low cost.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparation of polyol biofuel composition which involves adjusting hydrophilic-lipophilic balance value of surfactant to 10-14, adding methanol and/or ethanol and water, mixing, adding methanol-modified composite, oleic acid, and modifying additive, and mixing; and    (2) application for fuel oil which involves mixing polyol biofuel composition and petrochemical diesel or methanol diesel.
NOVELTY - A pre-obtained plant exhaust gas is processed by subjecting solution containing carbon dioxide and/or carbon monoxide and/or hydrogen gas into reaction system, performing catalyst purification to remove harmful substances, and reacting carbon dioxide and hydrogen gas and/or carbon monoxide and hydrogen gas to generate methane gas to obtain natural gas containing greater than or equal to 1 hydrogen gas.    USE - Process of pre-obtained plant exhaust gas for preparation of natural gas (claimed).    ADVANTAGE - Process is energy-saving, environment-friendly since carbon dioxide emission is reduced, and resource-saving and has increased synthesis rate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for pre-obtained plant exhaust gas system comprising steam drum, boiler pumps, methanation synthesis reactor, heat exchange columns, heaters, water cooler, water separator, methane concentrating component, compressor, and steam turbine which are connected to each other in which steam drum is connected to steam turbine and methanation synthesis reactor contains external drum, pumps, and heaters.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of pre-obtained plant exhaust gas process. (Drawing includes non-English language text).
NOVELTY - Biogas purification cogeneration of nano-calcium carbonate is performed by preparing lime milk seminal plasma with calcium hydroxide concentration of 3-10 mass%, adding 0.1-1 mass% dispersant, mixing, passing through membrane reactor, passing through biogas reactor, reacting at less than or equal to 60 degrees C with pressure of less than or equal to 0.4 MPa until pH is less than or equal to 7 to obtain calcium carbonate emulsion, centrifuging to obtain calcium carbonate filter cake, drying, and crushing.    USE - Biogas purification cogeneration of nano-calcium carbonate (claimed).    ADVANTAGE - Biogas purification cogeneration process avoids agglomeration of product and has high purification rate. Device has simple structure and low cost and is environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for device for biogas purification cogeneration of nano-calcium carbonate comprising raw material storage tank (2) sequentially connected to membrane reactor a (5), gas-liquid separator a (6), membrane reactor b (7), gas-liquid reactor b (8), and product storage tank (12) in which membrane reactor b is separately connected to biogas tank (11) and biogas delivery assembly, gas-liquid reactor b is connected to outlet of membrane reactor a, membrane reactor a is connected to outlet of carbon dioxide sensor (15), and gas-liquid separator a and raw material storage tank are set with splitting device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of device for biogas purification cogeneration of nano-calcium carbonate.    Raw material storage tank (2)    Membrane reactor a (5)    Gas-liquid separator a (6)    Membrane reactor b (7)    Gas-liquid reactor b (8)    Biogas tank (11)    Product storage tank (12)    Carbon dioxide sensor (15)
NOVELTY - A paper making waste recovery system (300) comprises 1st regenerative fuel granulator (301) which is used for removing slag material precipitate in washing tank bottom and 2nd regenerative fuel granulator (302) which is used for removing paper slurry discharge. Waste recovery is performed by feeding into 1st regenerative fuel granulator, granulating, extruding using screw extruder, feeding into 2nd regenerative fuel granulator, granulating, and extruding using screw extruder to obtain solid-derived fuel which contains slag material and slurry.    USE - A paper making waste recovery system for manufacturing solid-derived fuel (claimed).    ADVANTAGE - The method conserves energy, is environment-friendly, and produces clean and renewable alternative energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the paper making waste recovery system. (Drawing includes non-English language text).    Paper making waste recovery system (300)    1st regenerative fuel granulator (301)    2nd regenerative fuel granulator (302)    Storage barrel (303)    Centrifugal separation barrel (304)
NOVELTY - A biomass carbon powder additive contains 50-70 mass parts curing agent, 0.05-3 mass parts crosslinking agent, 0.05-3 mass parts catalyst, 0.05-3 mass parts flame retardant, and 30-50 mass parts filler.    USE - A biomass carbon powder additive (claimed).    ADVANTAGE - The method is simple, environment-friendly, and does not reduce fixed carbon content in powder, raw materials are readily available, and product is low cost, has improved anti-drop property and compressive strength, and is safe.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biomass carbon powder additive which involves crushing curing agent using crusher to obtain powder, adding crosslinking agent and catalyst, uniformly mixing, adding filler, crushing to obtain mixture (1), adding flame retardant in mixer, adding water, dissolving, drying to obtain mixture (2), and uniformly mixing mixtures (1) and (2).
NOVELTY - Preparing biological diesel oil involves adding oleaginous microbial strains to the reaction vessel and then mixing with low-carbon alcohol. The mixed material is proceeded esterification reaction of biological diesel oil after adding catalyst. The obtained material after esterification reaction is kept for layering and then the upper layer is removed. The obtained upper layer is mixed with hydrophobic organic solvent. The mixed material is centrifuged to obtain oil phase and then the oil phase is distilled in a solvent to recover the biological diesel oil from hydrophobic organic solvent.    USE - Method for preparing biological diesel oil (claimed).    ADVANTAGE - The method enables to prepare biological diesel oil in simple and energy efficient manner, and with good quality.
NOVELTY - Ellipsoid FRP household biogas digesters, comprises glass household biogas digesters, which is characterized by the pool for recumbent elliptical-shaped, the material for glass fiber reinforced plastic body; top of the ellipsoid is provided with skylights, skylight design tubes in the middle; between design pressure and on the side of the pool outlet, inlet design on the other side. Via the water outlet with the pool design has a feeding tube (5) and inlet feed pipe with the pool design.    USE - As ellipsoid FRP household biogas digesters (claimed) used to fertilize farm waste and straw into soil.    ADVANTAGE - The operation is convenient for user and daily management, efficient and environment-friendly.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic diagram of biogas digester.    Fermentation tank (1)    Feed opening (2, 3, 4)    Feed tube (5)    Slag opening (6)    Dreg tube (7)    Sucking tube (10)    Gas-guide tube (11)
NOVELTY - The system has a biogas biological fermentation device (1), a methane storage room (2), a safety discharge device (3) and a gas water separating device (4) that are connected with a biogas purification desulphurization device (5), a methane pressurizing device (6) and a biogas cooker device (7). The biogas biological fermentation device, methane storage room, safety discharge device and gas water separating device are connected through a clamp. The upper portion of biogas biological fermentation device is connected with bottom portion of the methane storage room.    USE - Combined-type biogas biological fermentation preparation system.    ADVANTAGE - The volume occupied by the biogas biological fermentation preparation system is reduced so that the transportation cost is decreased. Since the mounting process of biogas storage room, safety discharge device and gas water separating device in the biogas biological fermentation device is simplified, the occurrence of leakage is avoided. Hence the safety of the system is increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the combined-type biogas biological fermentation preparation system.    Biogas biological fermentation device (1)    Methane storage room (2)    Safety discharge device (3)    Gas water separating device (4)    Biogas purification desulphurization device (5)    Methane pressurizing device (6)    Biogas cooker device (7)
NOVELTY - Culturing bagasse to form biological film involves screening bagasse using mesh having diameter of 250-600 microns, cleaning, sterilizing and loading into 60 meshes silk mesh bag, then placing mesh bag into inner container; and placing the container into cultivation pool of seawater, adjusting an amount of dissolved oxygen at 5-6 mg/l, adding Bacillus species powder into the container and adding NH4Cl and molasses as nutrients, and after 10-15 days culturing under conditions, where sea water salinity is 22-35%, temperature is 28-33 degrees C and pH is 7.5-8.5, for 25-30 days.    USE - For culturing bagasse as carrier to form biological film (claimed).    ADVANTAGE - The present method is simple, feasible and cost-effective. The obtained biological membrane has long service life.    DETAILED DESCRIPTION - Culturing bagasse as carrier to form biological film involves: screening bagasse using mesh having diameter of 250-600 microns, cleaning, sterilizing and loading into 60 meshes silk mesh bag, each bagasse has thickness of 1.5-2.5 cm, then placing the mesh bag into an inner container; and placing the inner container into a cultivation pool of seawater, adjusting pneumatic amount of dissolved oxygen at 5-6 mg/l according to water volume, adding 106-107 cfu/ml active Bacillus species strain BZ-5 powder into the inner container and adding NH4Cl and molasses as nutrients, and after 10-15 days, and culturing under conditions where sea water salinity is 22-35%, temperature is 28-33 degrees C, lower pH is 7.5-8.5, for 25-30 days, to obtain cultured biological film.
NOVELTY - A methanol fuel composite formulation comprises 90-95 mass parts methanol, 1-5 mass parts ether, 0.01-0.5 mass part initiator, 1-5 mass parts ignition agent, 0.1-1 mass part lubricant, 0.01-0.5 mass part evaporation inhibitor, 0.01-0.5 mass part stabilizing agent, and 0.01-0.5 mass part binary fuel crosslinking agent.    USE - A methanol fuel composite formulation (claimed).    ADVANTAGE - Methanol fuel composite formulation is environment-friendly, stable, and energy-saving, has complete combustion, can be mixed with any ratio of diesel, and does not generate smoke.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of methanol fuel composite formulation which involves high-shear stirring raw materials in synthesis reaction container for 20-40 minutes, high-speed stirring emulsion material and methanol into main synthesis reaction container for 40-80 minutes, and storing into warehouse.
NOVELTY - Methanol gasoline formulation contains 50-80 mass% methanol, 20-50 mass% petrochemical gasoline, 10-20 mass% xylene, 0.05-0.3 mass% n-butanol, 0.5-2 mass% nitrobenzene, 0.05-0.2 mass% dicyclohexylamine nitrite, 0.2-0.4 mass% glycerol triacetate, 0.005-0.03 mass% 1,2-dibromoethane, 0.05-0.3 mass% isopropanol, 2-5 mass% chlorobenzene, 10-20 mass% ethylbenzene, 0.05-0.2 mass% isobutylamine, and 0.002-0.05 mass% octane.    USE - Methanol gasoline formulation for vehicle fuel.    ADVANTAGE - Formulation is environment-friendly, energy-saving, stable, does not corrode machine, does not for water layer, and has anti-swelling properties and reduced cost.
NOVELTY - A composite additive contains 30-60 wt.% cleaning dispersant which is 2-hydroxyphosphono-acetic acid isooctyl ester or 2-hydroxyphosphono-acetic acid lauryl ester, 10-30 wt.% oil-soluble surfactant which is fatty alcohol ethoxylate AEO-3 (RTM: Lauryl alcohol ethoxylate) or sorbitan fatty acid ester S-80 (RTM: Sorbitan monooleate), 4-8 wt.% organic amine, and 20-40 wt.% solvent with respect to 100% total.    USE - Composite additive for improving atomization performance of biodiesel (claimed).    ADVANTAGE - Additive is simple, stable, reduces kinematic viscosity and improves atomization performance of biodiesel, and reduces nozzle coking and power shortage.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparation of composite additive which involves heating solvent to 40-50 degrees C, adding cleaning dispersant, stirring, adding oil-soluble surfactant, stirring, adding organic amine, and stirring to react; and    (2) application of 0.005-0.05 wt.% composite additive to biodiesel.
NOVELTY - Biological composite fertilizer comprises 10-45 pts. wt. manure, 5-25 pts. wt. bran, 0.1-3 pts. wt. inoculant, 15-60 pts. wt. inorganic fertilizer, 5-20 pts. wt. mushroom residue, 0.1-5 pts. wt. superphosphate, 0.1-5 pts. wt. trace element, 2-15 pts. wt. soybean/vegetables, 0.1-5 pts. wt. Bacillus subtilis, 0.1-5 pts. wt. actinomycete and 0.1-5 pts. wt. photosynthetic bacteria.    USE - Biological composite fertilizer.    ADVANTAGE - The fertilizer is environmental-friendly, safe, efficient, convenient to use, and has simple preparation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of biological composite fertilizer comprising weighing raw materials, mixing, regulating water content, fermenting at 55-65 degrees C for 7-10 days, crushing and sieving through 40-60 mesh sieve.
NOVELTY - Preparation of Solanaceae calcium deficiency nutrient solution comprises adding pig manure, chicken manure and human manure into fermentation tank, and anaerobically fermenting; adding into second stage fermentation tank to carry out secondary fermenting to obtain biogas slurry; filtering, discharging into sedimentation tank, precipitating, filtering clear biogas slurry, and discharging into leaching pool; and adding calcium superphosphate, sealing, and dissolving.    USE - Method for preparation of Solanaceae calcium deficiency nutrient solution (claimed).    ADVANTAGE - The method is environment-friendly, solves the calcium deficiency problem, greatly increases the yield and value of crops, and it has low cost.    DETAILED DESCRIPTION - Preparation of Solanaceae calcium deficiency nutrient solution comprises:    (A) adding 45-55 wt.% pig manure, 30-35 wt.% chicken manure and 15-25% human manure into fermentation tank, anaerobically fermenting for 15-25 days;    (B) adding into second stage fermentation tank to carry out secondary fermenting for 15-25 days to obtain biogas slurry;    (C) filtering through 20 mesh filter screen, discharging into sedimentation tank, precipitating, filtering clear biogas slurry on upper layer through 20 mesh filter screen, and discharging into leaching pool; and    (D) adding calcium superphosphate at weight ratio of 40:0.05-0.15, sealing leaching pool, and dissolving to 10-35 degrees C for 10-20 days.    An INDEPENDENT CLAIM is included for application of nutrient solution on Solanaceae comprising diluting nutrient solution in 2-2.5 L water, performing first drip irrigation, diluting nutrient solution in 2-3 L water, and performing second drip irrigation. The first and second drip irrigation has interval of 5-7 days.
NOVELTY - Fertilizer composition preparation involves taking (in pts.wt.): ammonium chloride (200-700), dolomite powder (25-100), potassium chloride (50-300), ammonium sulfate (25-80), monoammonium phosphate (100-300), urea (300-400) and magnesium sulfate (25-100), where urea is powder with 50-60 meshes size, purity of monoammonium phosphate is 55-58%, water content of potassium chloride is 3%, fineness of dolomite powder is 200-300 meshes and water content of ammonium sulfate is 2%. The obtained material is stirred uniformly into a vessel, and then water is sprayed on the obtained material.    USE - Method for prepare fertilizer composition (claimed).    ADVANTAGE - The method enables to prepare fertilizer composition in simple and eco-friendly manner, ensures improved efficiency, and saves energy.    DETAILED DESCRIPTION - Fertilizer composition preparation involves taking (in pts.wt.): ammonium chloride (200-700), dolomite powder (25-100), potassium chloride (50-300), ammonium sulfate (25-80), monoammonium phosphate (100-300), urea (300-400) and magnesium sulfate (25-100), where urea is powder with 50-60 meshes size, purity of monoammonium phosphate is 55-58%, water content of potassium chloride is 3%, fineness of dolomite powder is 200-300 meshes and water content of ammonium sulfate is 2%. The obtained material is stirred uniformly into a vessel, and then water is sprayed on the obtained material. Urea is added to the obtained material with stirring for 2-3 minutes. The obtained material is discharged from the vessel, and then the obtained material is extruded and granulated. The obtained material is packed to obtain the finished product, where pressing force of extruding and granulating is 2.5-3 tons.
NOVELTY - Fertilizer composition comprises solution of fermented product, radix sophorae flavescentis powder, bean dregs, weathered coal, potassium permanganate solution and yeast powder.    USE - Fertilizer composition used for growing flowering plants and grass.    ADVANTAGE - The fertilizer composition is eco-friendly, and has wide industrial applicability.
NOVELTY - Fertilizer composition comprises plant oil of waste powder, fly ash, sodium dodecyl benzene sulfonate, dry animal abdominal organs powder, natural yeast, deionized water, hydrogen peroxide and potassium permanganate solution.    USE - Fertilizer composition used for new-type garden planting (claimed).    ADVANTAGE - The fertilizer composition is conveniently used, shows improved activity of fertilizer, and has improved nutrient content.
NOVELTY - Preparing fertilizer involves utilizing (in pts.wt.): fermented solution of fruit and vegetable (10-15), radix sophorae flavescentis powder (6-8), fermented product of bean dregs (6-8), weathered coal (8-10), potassium permanganate solution (3-7) and yeast powder (1-2.5). Fermented solution of fruit and vegetable is filtered and heated at 40 degrees C to obtain a block shaped substance. The block shaped substance is dried and ground to obtain powder, and then radix sophorae flavescentis powder, weathered coal, bean dregs and yeast powder are mixed with stirring in a vessel to obtain a mixture.    USE - Method for preparing fertilizer used during plantation of flowering plant (claimed).    ADVANTAGE - The method is easy to operate, enables to prepare fertilizer in a simple and eco-friendly manner.    DETAILED DESCRIPTION - Preparing fertilizer involves utilizing (in pts.wt.): fermented solution of fruit and vegetable (10-15), radix sophorae flavescentis powder (6-8), fermented product of bean dregs (6-8), weathered coal (8-10), potassium permanganate solution (3-7) and yeast powder (1-2.5). Fermented solution of fruit and vegetable is filtered and heated at 40 degrees C to obtain a block shaped substance. The block shaped substance is dried and ground to obtain powder, and then radix sophorae flavescentis powder, weathered coal, bean dregs and yeast powder are mixed with stirring in a vessel to obtain a mixture. The mixture is fermented at 40 degrees C for 72-120 hours, fermentation temperature is higher than potassium permanganate solution is added and mixture is covered by a plastic film, and then kept for 10-12 hours to obtain a product. The product is heated to dry and then crushed through 10-20 meshes to obtain the fertilizer.
NOVELTY - Fertilizer composition comprises chicken manure powder, bone powder, phosphate, dried leaf powder, glucose, yeast powder, deionized water and hydrogen peroxide.    USE - Fertilizer composition used during plantation of flowering plant (claimed) and increasing smell of flower and purifying indoor air.
NOVELTY - Cultivating fertile matrix involves taking organic agricultural wastes, which comprise (in wt.pts.): manioc waste (40-60), waste mushroom (10-30), palm (5-15) and perlite (15-25). The organic agricultural waste is preprocessed by crushing and stirring uniformly, and then stacking to obtain a buttress. The obtained buttress is heated to reach the internal temperature to 50-55 degrees C, and then turned the obtained material. The obtained material is fermented for 1-2 months, where water content is 20%.    USE - Method for cultivating fertile matrix for vegetable seedling (claimed).    ADVANTAGE - The method enables to cultivate fertile matrix for vegetable seedling in eco-friendly manner and ensures stability.    DETAILED DESCRIPTION - Cultivating fertile matrix involves taking organic agricultural wastes, which comprise (in wt.pts.): manioc waste (40-60), waste mushroom (10-30), palm (5-15) and perlite (15-25). The organic agricultural waste is preprocessed by crushing and stirring uniformly, and then stacking to obtain a buttress. The obtained buttress is heated to reach the internal temperature to 50-55 degrees C, and then turned the obtained material. The obtained material is fermented for 1-2 months, where water content is 20%. Bactericide and acidity regulator of composite fertilizer (0.5-3kg per m3) are added to the obtained material at room temperature, and then re-stacking the obtained material. The obtained material is fermented for 1-2 months to obtain a semi finished product matrix, where composite fertilizer is nitrogen phosphorus and potassium are in ratio 12-15:13-20:15-25. The obtained material is dried, and then the obtained material is performed for sieving. The obtained material is checked for certain parameter, i.e. pH 6.5-7, water content 40%. The obtained qualified material is metered and packed to obtain the finished product.
NOVELTY - Fertilizer composition during plantation of flowering plant, comprises dried food waste powder, soil phosphorus activator, urea, dried leaf powder, yeast, calcium carbonate, magnesium carbonate, deionized water and potassium permanganate solution.    USE - Fertilizer composition during plantation of flowering plant (claimed).    ADVANTAGE - The fertilizer composition is eco-friendly, easy to use without peculiar smell, rich in potassium, phosphorus, calcium, magnesium and boron elements and soluble in water, and has quick effect.
NOVELTY - Producing fertilizer involves mixing (in pts.wt.): dried food waste powder (20-25), soil phosphorus activator (2-4), urea (5-8), dried leaf powder (8-14), yeast (1-4), calcium carbonate (3-6), magnesium sulfate (4-5), deionized water (12-18) and potassium permanganate solution (5-7) to obtain a mixture. The mixture is mixed with deionized water (5-8 pts.wt.) and stirred and then covered by a plastic cloth. The mixture is fermented at 45 degrees C for 48-56 hours and then dried at 45 degrees C to obtain a fermented product.    USE - Fertilizer used during plantation of flowering plant (claimed).    ADVANTAGE - The method is easy to use, enables to produce fertilizer in a simple and cost-effective manner, and has improved fertility effect and disease resistant property.    DETAILED DESCRIPTION - Producing fertilizer involves mixing (in pts.wt.): dried food waste powder (20-25), soil phosphorus activator (2-4), urea (5-8), dried leaf powder (8-14), yeast (1-4), calcium carbonate (3-6), magnesium sulfate (4-5), deionized water (12-18) and potassium permanganate solution (5-7) to obtain a mixture. The mixture is mixed with deionized water (5-8 pts.wt.) and stirred and then covered by a plastic cloth. The mixture is fermented at 45 degrees C for 48-56 hours and then dried at 45 degrees C to obtain a fermented product. The fermented product is crushed through 23-40 meshes and then dried to obtain fertilizer in powder form.
NOVELTY - Composite microbial inoculants comprise photosynthetic bacteria, lactic acid bacteria and yeast such as Bacillus subtilis, Bifidobacterium animalis, Bifidobacterium bifidum, Bifidobacterium longum, Lactobacillus acidophilus, Lactobacillus casei, Lactobacillus delbrueckii, Lactobacillus fermentum, Lactobacillus plantarum, Lactococcus lactis, Rhodopseudomonas palustris, Streptococcus thermophilus, Saccharomyces cerevisiae and 13 different microorganisms.    USE - Composite microbial inoculants used for treatment of sludge (claimed).    ADVANTAGE - The composite microbial inoculants reduce corrosion which occur from a device and maintenance cost.
NOVELTY - This utility new type provide one of a continuous biomass carbonization device, comprise: biomass gasification furnace, a feeding device and a discharging seal device and biomass gasification carbonization furnace include furnace body and furnace plate, a furnace body comprise liner and outer shell, and forming a gas channel in the inner container and outer shell, and the inner shell is a cylindrical top opening, inner bottom of the material input port, the shell is the carbon outlet, inner of upper half inner container installed in the shell, a upper edge and the shell of edge of inner container connect as a whole, gas channel gas outlet on the top part of furnace body, the bottom of the shell, inner container of a gas channel connected feeding device from the material input port input material, seal the discharging device with the carbon outlet connected. This utility new type continuous biomass carbonization device of the biomass gasification and biomass carbonizing efficient by the biomass raw material is suitable for each of a shape, size, can realize and carbonization of biomass gas.
NOVELTY - A one continuous biomass gasification furnace of this utility new type provide a, comprise a furnace body, and the furnace body set with a stove body comprise inner liner and outer shell, and gas channel forming in the inner container and a shell, an inner container set of upper inner shell, upper edge on the upper edge of a container connecting with the shell as a whole, gas channel gas outlet on the top part of furnace body, the lower half of the shell is the bottom of the furnace chamber is a furnace cavity, a fuel gas channel connected the plate has a bottom closed inner container opening of a first position, and downwards on the opening at the bottom of the inner container, the material into second position in furnace chamber of, in between the first position to second position of any position. This utility new type provides a continuous biomass gasification carbonizing the biomass gasification and carbonization efficient by the biomass raw material is suitable for each of a shape, size, can realize and carbonization of biomass gas.
NOVELTY - In dry and wet integrated biomass fuel gas fractional condensation oil pneuma separate device of upper, lower tube corresponding inner set with upper, lower pipe and upper, lower cavity to responsible for fractional condensation, in inner tube is set with inclined chamber plate and the conical air station to charge air and oil, use time, fuel gas through the gas inlet,,, lower pipe, lower cavity plate, cavity plate, a side air inlet, side air outlet, a cavity plate, a pipe, a sealing plate, a back seal and the gas exit, the condensing medium flow path for a condensation port, a cooling cavity, connected pipe, lower cooling cavity, lower condenser, a feedback value according to temperature sensor adjust condensation medium to control gas in different condensing temperature of the flow rate and residence time of inner cylinder body to separate out different of biological oil, cold water cooling are a pneuma. The design not only has strong controllability, biological oil of a high efficiency, and the condensing effect is strong, application range is wide, to increase quality of biological oil and biomass gas.
NOVELTY - This utility new type claims a one and a water alcohol ether clean fuel. c, in turn include circulation connecting a star agent feeding pump, dehydrating dryer, comprising a material inlet of reactor, in turn connecting a gas-liquid separator, heat exchanger and air remover, a gas-liquid separator has gas exit, said initiator feeding pump, dehydrating dryer in parallel connecting with exit of main reactor, a dehydrating dryer, pre-reactor in parallel connect to a gas-liquid separator, a heat exchanger connecting with vacuum pump, further set with steam injection pump between a gas-liquid separator, a heat exchanger. This utility new type relates to a removing water of alcohol ether fuel.. clean high dehydrating efficiency, water content of material of reaction is low, the rear vacuum pump load, saving electric energy.
NOVELTY - This utility new type claims a non-cylinder one hollow machine-made charcoal, crop straw, rice hull, and all kinds of shrub, residual branch as raw material, crushing, drying, low temperature carbon through the mill to carbon powder, the carbon powder into the inner mixer according to a certain ratio, adding biomass tar, stir to uniform slurry is sent to the extruder inner extrusion type carbon of each shape into a molding machine, the charcoal is hollow-shaped, a is quadrangle or hexagon. The outer diameter is 35 to 37 mm, inner diameter is 10 to 12 mm, the length is 450 to 500 mm. This utility new type is designed according to a non-cylinder hollow machine-made charcoal, length, thickness and uniformity, is designed to be hollow, combustion and air contact area is large, the time and combustion, the combustion is full, the energy is saved, which is beneficial to environment protection, a is quadrangle or hexagon, and convenient to transport.
NOVELTY - This utility new type claims a non-cylinder one hollow mechanism, is selected from crop straw, rice hull, and all kinds of shrub, residual branch as raw material, crushing, after drying, the molding machine pressing, the stick is hollow-shaped, a is quadrangle or hexagon. The outer diameter is 50 to 55 mm, inner diameter is 15 to 20 mm, the length is 450 to 500 mm. This utility new type according to a design mechanism, length, thickness and uniformity, is designed to be hollow, combustion and air contact area is large, the time and combustion, the combustion is full, the energy is saved, which is beneficial to environment protection, a is quadrangle or hexagon, and convenient to transport.
NOVELTY - This utility new type claims a dyeing and finishing one industrial waste water of biological treatment with carrier, comprise shell, the bottom of the shell body set with a water inlet, a water inlet and the bottom of the shell of the top part a. one with a aeration, side surface of shell is set with an arc-shaped water outlet, set with two layer hard bracket between the arc-shaped water outlet with the water inlet, a surface of hard bracket set with fabric layer, a hard connecting bracket and a shell set with a pressure sensor, the arc water outlet set with a movable stop plate, set with a horizontal impeller and a discharge tube, a drain tube is set with valve, a drain tube connecting to filter sedimentation tank on the two layer fabric layer. This utility new type can be improved is not enough of the existing technology, reduces the leakage of the sludge for water quality, and can be a. produce sludge amount, for a fast collecting sludge, maintain the filter treatment effect of carrier long time.
NOVELTY - A one environment-friendly kitchen garbage fermentation device, to include a kitchen garbage fermentation tank, a tank body of fermentation tank feeding port set with a movable seal cover of the said fermentation tank set with a circle of axis vertical to the tank body set with the embedding of the fermentation tank of the embedding part set with the fermentation tank of the tank body on the ground, embedding the lower part expose in the air in a set with underground buried of tank body, tank body of side wall set with a plurality of used for the oxygen and the fertilizer of penetration hole. This utility new type is set with fermentation tank through a tank body on the ground and underground tank body, tank body set with a penetration hole, a the edge for edge and process through a penetrating hole, which saves the fertilizing a trouble such that fermentation of odour would not leak, the fertilizer effect, environment-friendly, and prevents the intrusion of animal, at the same time, the device a circulation, low manufacturing cost.
NOVELTY - This new type utility claims one a closed mud a compost turning material guiding device, a machine frame and include the set of closed mud compost expansion cylinder, the feeding chamber and a sealed sludge compost bin a two end, a closed mud compost a connecting driving around the axial direction with a turning of power device, wherein a feeding bin, a bin inner wall set with a radial material flow-guiding blade, radial material guide plate of terminal set with a discharging port, the discharging opening connecting a closed mud compost a, a closed mud compost inner wall set with a multi-group material-pushing Leak turning. This utility new type has simple structure, valid propulsion compost material and guide forward inner expansion cylinder fermentation.
NOVELTY - A biodiesel oil additive comprises 5-78 pts. wt. oleic acid, 5-45 pts. wt. butanol, 1-31 pts. wt. surfactant, 1-42 pts. wt. modified additive, and not greater than 73 pts. wt. deionized water.    USE - A biodiesel oil additive.    ADVANTAGE - The biodiesel oil additive allows improved combustion of low carbon, thus saving petroleum resource and saves energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the diesel fuel additive, comprising adjusting hydrophilic lipophilic balance of surfactant at 10-14, adding butanol and water, uniformly mixing, and adding oleic acid and modified additive.
NOVELTY - Biological organic fertilizer special for circulation water tank. Current biological organic fertilizer of test platform needed of a flushing water, use amount of water is large, and biological organic fertilizer of fermentation tank is also need a large amount of a water washing, the water use one time throw off is waste, and also increase the biological organic fertilizer of manufacturing cost. A biological organic fertilizer special for one circulation water tank, composed of a comprise the shell (1), the shell connecting filter clapboard (2), the filter plate of the lower of the shell connect a polyurethane foam layer (3), polyurethane foam layer of the lower surface of said shell connecting filter screen (4), the bottom of the shell connecting rotating shaft (5), the rotating shaft connecting eccentric wheel (6), a eccentric wheel connecting a motor output shaft (7). This utility new type used for biological organic fertilizer production process in sewage treatment.
NOVELTY - This utility new type claims a one oxygen-enriched water biological turntable sewage treatment device, include rotating disk sheet, reaction groove, a baffle plate, a sewage circulation pump and water quantity adjusting valve, a turntable disc bearing mounting through the inner reaction groove and can freely rotate, a baffle plate around the bear uniform multi-mounting to one side surface of rotary plate piece, reaction groove in a lower part or bottom of the water regulating valve of one end connecting the other end water regulating valve of sewage circulation pump and a water inlet connecting water outlet of sewage circulation pump and the first sewage tube end of connecting, the upper part second end sewage tube side of disk of the turntable and used for draining to baffle the upper rotary plate piece rotate. This utility new type through the baffle plate, sewage circulation pump and water quantity adjusting valve, a the hydraulic driving rotary plate piece rotate through a circulation water and a rotating speed, and to replace the traditional of the motor drive, simplifies the daily management and maintenance for a biological turntable sewage treatment device and operation management is simpler.
NOVELTY - A one a novel anaerobic sludge fluidized bed reactor, comprise tank body, tank bottom side set with water inlet, the top part side face set with the water outlet, the tank body in a most bottom layer, a water distributor connecting with the water inlet, the bottom of inner tank body is also set with a baffle, the baffle water distributor, middle baffle plate set with flow guide hole, the guide hole mounting guide plate, the top and middle of inner tank body set with three phase separator, three phase separator above the baffle plate, and the baffle plate does not contact the inner three phase separator distribute with a multi-reflection plate, reflection plate is a bent plate, the top end of three phase separator connecting with the water outlet and a collecting pneuma room. The utility model is new type can increase the mass transfer effect, reduces energy consumption, which solves the rising flowing speed, blocking while preventing sludge loss, it has stable operation, energy-saving and environment-friendly, small floor area, low investment, it is convenient of operation management.
NOVELTY - This utility new type relates to one used for sewage treatment of a fixed bed microorganism carrier, a carrier main body, a carrier main body is a mesh cylinder by a cylindrical wire formed by weaving a; a cylindrical wire of each outer surface is uniformly distributed with burr, the utility model is new type used for sewage treatment of the fixed bed microorganism carrier is a microorganism can provide a good growth environment, and it can ensure can bear larger hydraulic impact load, is a microorganism provide a good growth environment, and the carrier is based on a denitrification treatment, and the treatment effect is good.
NOVELTY - In this utility new type claims a solar energy film method one drop filter device, comprise: sewage entrance, bar, inner the sewage entrance; oxidizing pond, bar through the sewage entrance connected, in oxidation with regulating valve and set with hard joint of filter tube lifting pump, is placed directly in water collection pool, used for the oxidation pond through the sewage pump to a biological trickling filter film, a secondary sedimentation tank, and the entrance to the biological drip irrigation under film device exit connected, in secondary sedimentation tank set with solar energy aerator, biology filter bed, exit of the entrance to the secondary sedimentation tank connected, in biological filter bed with regulating valve and set with hard joint of filter tube, exit connecting a biological filter bed mixing container, mixing with the medicine preparation tank connecting container, container is also set with the water discharge exit. Wherein, bar, a lifting pump and solar energy aerator are power supply by solar energy battery component. This utility new type operation cost is very low, the sewage treatment efficiency is high.
NOVELTY - A high efficiency, one slot kitchen garbage processor of energy-saving. Three relative independent of a fermenting groove with stir, heating, aeration of a fermentation waste decomposing device, small floor area, saves energy, is convenient for operation control, full closed design, a whole garbage material without exposed, for no pollution to the environment.
NOVELTY - This utility new type claims a new-type one of household garbage decomposing, include machine cover, seal glue ring, an air inlet hole, the limit line, operation panel, discharge hole, a shell, a deodorization device, groove, a machine cover fixed on the decomposing groove upper part, a seal glue ring and the machine connecting cover, said air inlet hole is decomposing groove of a side groove, a limit in decomposing groove in middle position of said operation panel in the shell upper part, a discharge hole through out of the shell and the decomposition groove connecting, said stir blade located on the rotating upper shaft, a foot rest lower part located in the shell, a deodorization device connecting with the foot rest, a motor is set lower part of decomposition groove, a rotating shaft is connected with motor connecting, a decomposing groove a upper rotating shaft part. The decomposed into carbon dioxide, pure water, solid powder, solid matter is non-toxic and harmless, a as organic fertilizer for use environment pollution is small, working when power consumption is small, the noise is of the following 50 decibels, for a little influence to the user.
NOVELTY - This utility new type belongs to the field of agricultural machinery, more exactly speaking, it is a one turn a fertilizer machine, suitable for the organic fertilizer processing production of compound fertilizer. A turn fertilizer machine by machine frame, a walking wheel, a driving shaft, a driving shaft, a speed reducer semi-shaft sliding operation mechanism and so on, wherein walking wheel device on the turbine speed reducer device on the machine frame a, a sliding half shaft and the turbine speed reducer connected match, drive shaft of the walking wheel and the turbine speed reducer match, the running mechanism by transmission shaft, a belt, a belt wheel, a turning and crushing pole, running mechanism one end driving shaft fixed on the machine frame through a driving shaft and cycloid speed reducer match. This utility new type of advantages to turbine speed reducer is a power driving machine move to cycloid speed reducer is drives the power running mechanism, a fertilizer tank inner continuous to work, it has uniformity, high efficiency, and is suitable for industrial production of.
NOVELTY - This new utility model claims of one of waste smoke leaf fertilizer and special manufacturing equipment group, used for using the waste smoke leaf manufacturing is organic or inorganic fertile fertile, belonging to fertilizer production device technology area. The discharging port and dust-removing system pulverizer comprises the smoke leaf pulverizer, leaves connected smoke, ash and cyclone dust collector and dust-removing system through spiral transporting machine and second level mixing system connected, spiral transport machine middle part set with spiral transporting machine and connect the auxiliary material adding device, second level mixing system via belt transmitter I and rotten pool connected, prepared pool through belt transmitter II and drying system connected. The special equipment group using smoke leaf pulverizer, a dust removing system, second level mixing system, prepared pool, drying system, waste smoke leaf sequence in turn through crushing process of smoke leaf pulverizer, dust removing and dust removing system process, drying process after the decomposing process, drying system and decomposing pool is made of organic or inorganic fertile fertile, waste use rate of smoke leaves high, production period short, group equipment cost low.
NOVELTY - A one aerobic charcoal, include furnace tank, a furnace inner tank inner is set with bridge, furnace bridge is provided with combustion room, combustion room set with a nozzle, the upper part box body is provided with a box cover, the box cover is set with discharge hole, combustion room is provided with the pneuma hole, connecting with the water tank and a high pressure oxygen tank. This utility new type of beneficial effects: burning room inner set with a spray pipe connected with a high pressure oxygen tank and water tank, in the charcoal burning process, it can according to need water or a furnace inner box, the soft wood burning into charcoal, but also can increase content of oxygen in charcoal, so as to increase quality of charcoal.
NOVELTY - This utility new type relates to one a clean burning a biomass gasification furnace, comprise feeding device, one gasification furnace, a gasification furnace, the feeding device and the input end of gasification furnace is connected with one end of a gasification furnace and one input end of a gasification furnace is connected with the feeding device comprise a feeding box, blast pipe, a fan, a feed box is equipped with the blast pipe, the pipe connecting with the fan. This utility new type has simple structure, through two-time vaporizing biomass granule for a for a complete combustion of a biomass, which not only can increase the utilization rate of biomass granule, but also can reduce the valid a biomass full combustion of waste pneuma produce pollution and protect the environment.
NOVELTY - This utility new type relates to water seal type biomass fuel gas filter, a valid solves the biomass gasification process in gas is easy to return, technology solution is as follows: a second separate room cavity of fire grate, furnace grate is the body between the condenser, and the condenser body upper part of the body with a feeding port, the body is provided with a vertical centre of the body middle part is provided with a horizontal first separate room is configured to upper part and lower part of a, first separate room inner is used for seal of water to form water seal section, inner second separate room is used for filter of adsorbent particles, lower part and upper part of first separate room set with air inlet and a water inlet on the upper body, a part of second separate room air outlet is set up on the body, the top part of body is set with the bottom of the cold water port, the body is connected with the inlet of the condenser is connected set with a exit is connected with the condenser of the cooling water outlet, this utility new type having dust and coke, cooling and a multi function, valid to prevent the backflow of gas, use is convenient and the effect is good.
NOVELTY - This utility new type relates to biomass fuel gas filter, a valid solves biomass gasification purification device filter purification effect is bad, technology solution is as follows: a second separate room cavity of fire grate, furnace grate is the body between the condenser, and the condenser body device body is a hollow structure, the upper part of the body with a feeding port, the body is provided with a vertical centre of the body middle part is provided with a horizontal first separate room is configured to upper part and lower part of a, furnace grate under a multi-set with a downwards inclined shape of spoiler, bottom of first separate room is downwards inclined, the lowest part in the upper body set with tar exit, lower part of first separate room set with air inlet on the upper body, a part of second separate room air outlet is set up on the body, the top part of body is set with the bottom of the cold water port, a body connected with the condenser of the condenser exit is connected set with a cold water inlet, this utility new type having dust and coke, cooling and so on a multi-function, is convenient to use, and the effect is good. up the inner wall of first separate room
NOVELTY - This utility new type claims a straw fuel forming machine through curing one production device, include a feed hopper, a crusher, and further set with a mixing tank and a spiral conveyor, a mixing tank set with material adding opening, water spraying device and stir device, spiral conveyer outer side mounting a heating set. This utility new type crushing, transporting and mix, pressing, molding and screening process, a level compression process the straw can be directly pressed into bar-shaped fuel, using spiral pre-pressing and mould pressing of, and adding auxiliary material and water and a stir mixing tank of the compression front set, a select set of heating device on the spiral, so that the device for straw of different physical property can get big weight proportion and big, small volume, combustion of a curing, a replace coal, oil and other conventional energy and has good popularization value in use a processing time.
NOVELTY - This utility new type relates to a one for marsh gas engineering material water of the sand tank. It solves the need is valid can be a raw material, a sand settling and sand removing, ensuring stable operation of the subsequent anaerobic fermentation system and so on. This utility new type is mainly by tank body (2), a stirrer (10), a material inlet (11) and material exit (12), wherein the inner tank body set with tank bottom heating disk tube (5), the heating water inlet tube (6), a heating water outlet tube (7), the tank body (2) is a tank wall is set with a opening seal door (8).
NOVELTY - This utility new type refers to a kind of intelligent control of one section can emission the electrolytic groove comprises reactor, generating hydrogen and oxygen mixed gas in the electrolytic water in the electronic control device, comprising electronic display and input unit, intelligent digital controller, a pulse wide power source controller and relay, wherein, the electronic control device can according to inner combustion engine and/or the energy-saving and emission reduction device of parameter can, automatically regulating gas production rate. This utility model also comprises at least one new number detecting unit, the parameter for feedback to intelligent digital controller, intelligent digital controller for the energy-saving and emission reduction device can carry out the corresponding regulation. This new utility model use single chip machine control circuit, the structure is simple, and color touch screen design and intuitionistic, suitable need different set of parameter, suitable operating safety.
NOVELTY - Liquefied natural gas and high purity nitrogen producing device. A traditional separate high pure nitrogen device of development and separate supply way of cold quantity needed to solve is not good would increase into a system and the system of' consumption caused by nitrogen gas separate device is not complete. A one liquefied natural gas and high purity nitrogen producing device, the comprise of the compressor (9), a feeding tube of the compressor is connected with the inlet of the refrigerant tube connecting the raw material, a discharging tube and a heat exchanger section of the compressor (1) through connecting pipeline, the heat exchanger is a section of the discharge tube and the feed tube of a feeding tube of natural gas pneuma raw material, separate hydrocarbon tank (2), a first refrigerant separate tank (6) of the feeding tube, the third refrigerant separate tank (8) of the feeding tube, the refrigerant raw material feeding tube connecting. This utility new type used for liquefied natural gas and high purity nitrogen generation.
NOVELTY - A straight chain alkane is isomerized by introducing straight chain hydrocarbon material into reactor, and contacting with isomerization catalyst under hydrogen atmosphere. Isomerization catalyst contains group VIII metal component and solid superacid sulfate/zirconium dioxide.    USE - Method for isomerizing straight chain alkane (claimed).    ADVANTAGE - The method has low reaction temperature, balance high conversion rate and good selectivity.    DETAILED DESCRIPTION - Wherein the isomerization reaction condition is as follows: reaction temperature is 70-450 degrees C, the pressure is 0.4-10.0MPa, the hydrogen and straight chain alkane of raw material is (1 to 10): 1, straight chain alkane raw material of the weight hourly space velocity is 0.5-10.0 to-1, wherein a straight chain alkane of raw material is C4-C6 of positive one or a mixture of several in paraffin. Wherein the Group VIII metal component selected from Pt, Pd and Ni in a one or a several.
NOVELTY - Synthesizing curcumin comprises stirring uniformly tri-n-butyl Borate, N-vanillin, acetylacetone, boric acid, N,N-dimethyl formamide at 40-45 degrees C to obtain acetylacetone complex of boric anhydride, adding dropwise n-butylamine catalyst, carrying out the reaction continuously, adding acetic acid to obtain a curcumin crude product.    USE - Method for synthesizing curcumin (claimed).    ADVANTAGE - The method is simple and environment-friendly, has low energy consumption and increased product yield by 20%, can easily control reaction condition, and is suitable for industrial production.
NOVELTY - Enzalutamide (V) is prepared by subjecting 2-fluoro-4-amino-methyl-benzamide (I) and 2-bromomethyl isobutyrate (II) to substitution reaction in presence of acid-binding agent to obtain 2-(3-fluoro-4-(methyl-carbamoyl) phenylamino)-2-methyl propionate (III); and adding compound (III) and 4-isothiocyanato-2-(trifluoromethyl) benzonitrile (IV) into mixed solvent of toluene and dimethyl sulfoxide and performing cyclization reaction to obtain compound (V).    USE - Method for preparing enzalutamide (claimed).    ADVANTAGE - The method is safe to perform and environment-friendly and has simple operation and high yield.    DETAILED DESCRIPTION - Preparation of enzalutamide of formula (V) comprises subjecting 2-fluoro-4-amino-methyl-benzamide of formula (I) and 2-bromomethyl isobutyrate of formula (II) to substitution reaction in presence of acid-binding agent to obtain 2-(3-fluoro-4-(methyl-carbamoyl) phenylamino)-2-methyl propionate of formula (III); and adding compound (III) and 4-isothiocyanato-2-(trifluoromethyl) benzonitrile of formula (IV) into mixed solvent of toluene and dimethyl sulfoxide and performing cyclization reaction to obtain compound (V).
NOVELTY - Aztreonam (IV) is prepared by reacting (S)-3-amino-2-oxo-1-azetidine-sulfonic acid compound (I) with (Z)-2-amino- alpha -1-tert-butoxycarbonyl-1-methyl-ethoxy-4-thiazolyl imino acid benzothiazole-thiol ester compound (II) in organic solvent to obtain (3S-(3 alpha (Z),4 beta ))-3-(((2-amino-4-thiazolyl)-((1-tert-butoxycarbonyl-1-methyl-ethoxy) imino)-acetyl) amino)-4-methyl-2-oxo-1-azetidine sulfonic acid compound (III); and adding compound (III) in formic acid, adding benzaldehyde, dripping hydrochloric acid, adding ethyl acetate, filtering, and drying filter cake to obtain aztreonam.    USE - Method for preparing aztreonam (claimed).    ADVANTAGE - The method utilizes easy to avail raw materials, has low cost, short reaction period, simple and convenient operation, high yield and high product purity and little three wastes, does not cause environment pollution, and is suitable for industrial production.    DETAILED DESCRIPTION - Preparation of aztreonam of formula (IV) comprises dissolving (S)-3-amino-2-oxo-1-azetidine-sulfonic acid compound of formula (I) and (Z)-2-amino- alpha -1-tert-butoxycarbonyl-1-methyl-ethoxy-4-thiazolyl imino acid benzothiazole-thiol ester compound of formula (II) in organic solvent, adding alkali at room temperature, stirring, then cooling to - 20 degrees C to 10 degrees C, adding trifluoroacetic acid, stirring, filtering, drying filter cake to obtain (3S-(3 alpha (Z),4 beta ))-3-(((2-amino-4-thiazolyl)-((1-tert-butoxycarbonyl-1-methyl-ethoxy) imino)-acetyl) amino)-4-methyl-2-oxo-1-azetidine sulfonic acid compound of formula (III); and adding compound (III) in formic acid, adding benzaldehyde, cooling to - 20 degrees C to 10 degrees C, dripping hydrochloric acid, stirring, and then adding ethyl acetate, stirring, filtering, washing filter cake, and drying to obtain aztreonam, and optionally, recrystallizing the aztreonam using 1-4C alcohol/water mixed solvent.
NOVELTY - A dry fermentation injectable reinforced mass and heat transfer device comprises bracket of dry fermentation tank (6) in which bracket has elevatable injection device (8), injection device comprises horizontal injection duct, lower part of injection duct is equipped with vertical injection needle tube, lower end of injection needle tube is pivotally supported with pair of duckbill-shaped injection nozzle comprising retractable injection head, upper outer of both injection nozzles were extended at level shank, and injection nozzles are equipped with tension spring in normally closed state.    USE - A dry fermentation injectable enhanced mass and heat transfer device (claimed).    ADVANTAGE - Dry fermentation injectable enhanced mass and heat transfer device solves dosing problems of fermented material crusts to ensure biogas slurry heat and mass transfer effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a dry fermentation injectable enhanced mass and heat transfer device.    Biogas slurry tank (1)    Outer liquid valve (3)    Dry fermentation tank (6)    Motor (7)    Injection device (8)
NOVELTY - Tourmaline product composition preparation involves cutting tourmaline into bocks. The pieces of blocks are added with livestock manure and straw. The mixture is stirred in a methane tank to obtain desired product.    USE - Method for preparing tourmaline product composition used for preparing marsh gas (claimed).    ADVANTAGE - The method enables to prepare tourmaline product composition with high yield.
NOVELTY - An asymmetrical hollow fiber gas separation membrane is formed using soluble aromatic polyimide having repeating unit (I).    USE - Asymmetrical hollow fiber gas separation membrane is used for selectively separating-and-recovering carbon dioxide gas or methane gas from mixed gas (claimed).    ADVANTAGE - The highly-efficient asymmetrical hollow fiber gas separation membrane has improved gas-separation property, and excellent gas permeability, and selectively separates-and-recovers methane gas from mixed gas containing carbon dioxide gas and methane gas.    DETAILED DESCRIPTION - An asymmetrical hollow fiber gas separation membrane is formed using soluble aromatic polyimide having repeating unit of formula (I).    B'=tetravalent unit containing 20-60 mol% diphenylsulfone structure-based tetravalent unit (B1) and 80-40 mol% diphenyl hexafluoro propane structure-based tetravalent unit (B2);    A=bivalent unit containing 20-100 mol% sulfur-containing heterocyclic structure-based bivalent unit (A1) chosen from bivalent unit of formula (A1b) and bivalent unit of general formula (A1a), in which 20-100 mol% of A contains bivalent unit (A1), and bivalent unit (A1) is divalent unit obtained by removing amino group from 3,7-diamino-dimethyldibenzothiophene=5,5-dioxide;    R,R'=H or organic group;    X=-CH2- or -CO-;and    n=0, 1, or 2.    An INDEPENDENT CLAIM is included for method for selectively separating-and-recovering carbon dioxide gas or methane gas from mixed gas containing carbon dioxide gas and methane gas using the asymmetrical hollow fiber gas separation membrane.
NOVELTY - A methane fermentation system (1) consists of fermenter (5) for fermenting organic waste, and warm water jacket (6) having undulating flow path for circulating warm water to undulating state in the outer wall surface of the fermenter.    USE - Methane fermentation system is used for producing biogas.    ADVANTAGE - The methane fermentation system efficiently ferments organic waste even when it's dry.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of methane fermentation system.    Methane fermentation system (1)    Supply conveyor (2)    Crusher (3)    Fermenter (5)    Warm water jacket (6)
NOVELTY - Method for recycling methane involves providing carbonaceous feedstock into a fluidized bed reactor to produce synthesis gas containing methane, carbon monoxide and hydrogen, then recovering methane from the synthesis gas to produce methane-rich gas, and delivering at least a portion of the recovered methane-rich gas to the fluidized bed reactor.    USE - Method for recycling methane (claimed).    ADVANTAGE - The method efficiently provides recycled methane having high purity, by economical process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for gasification system, which comprises fluidized bed reactor, methane recovering apparatus, and methane delivery device.
NOVELTY - An inhibition of methane production by methanogen involves contacting the methanogen with effective amount of composition containing red yeast rice, vitamin B10 derivative or ethanesulfonate or any combination of red yeast rice, vitamin B10 derivative or ethanesulfonate sufficient to cause inhibition of methane production.    USE - An inhibition of methane production by methanogen (claimed).    ADVANTAGE - Methane production is inhibited during anaerobic reductive dechlorination process.
NOVELTY - A gas collection apparatus in fluid communication with retort of a biomass reactor consists of gas collection pipes in fluid communication with spaced apart sections of the retort, and a gas collection manifold in separate fluid communication with each of the pipes.    USE - Gas collection apparatus used in biomass pyrolysis system (claimed) for producing biocoal, biochar and torrified wood used in agricultural, forestry, and industrial applications.    ADVANTAGE - The gas collection apparatus suppresses the mixing of gas collected by pipe with the gas collected by other pipe.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) biomass pyrolysis system; and    (2) syn-gas management system.
NOVELTY - An input starting material containing furfural or hydroxymethylfurfural is mixed with hydrogen gas, and optionally with a carrier fluid. The obtained fluid mixture is resided in a reactor assembly in presence of catalyst such that catalyst, in presence of hydrogen gas, promotes decarbonylation, hydrogenolysis and/or hydrogenation of the furfural or hydroxymethylfurfural, to produce primary alcohol, alpha -olefin, secondary alcohol, ketone, aldehyde, alkane, alkene, cyclic ether, lactone and/or 1, omega -diol in a product mixture.    USE - Method for producing alcohol, diol, cyclic ether and lactone used for fuels.    DETAILED DESCRIPTION - An input starting material containing furfural or hydroxymethylfurfural is mixed with hydrogen gas, and optionally with a carrier fluid, such that a fluid mixture results. The fluid mixture is resided in a reactor assembly in the presence of a catalyst at a temperature (T) under pressure (P) for time (t) such that the catalyst, in the presence of the hydrogen gas, promotes decarbonylation, hydrogenolysis and/or hydrogenation of the furfural or hydroxymethylfurfural, to produce a primary alcohol, alpha -olefin, secondary alcohol, ketone, aldehyde, alkane, alkene, cyclic ether, lactone and/or 1, omega -diol in a product mixture. The product mixture is collected. An INDEPENDENT CLAIM is included for catalyst, which comprises at least three metallic elements chosen from scandium, titanium, vanadium, manganese, iron, cobalt, nickel, copper and zinc, and is capable of catalyzing the reaction of hydrogen with furfural or hydroxymethylfurfural.
NOVELTY - The method involves processing raw gas streams (b) fed to processing units e.g. gas cleaning unit (2), gas synthesis unit (3), refinery unit (4), to obtain intermediate products (c, d) and by-products of a hydrocarbon product in first operating mode. Organic insert materials (a) of an organic feedstock (f) e.g. straw, chaff, are processed in a second operating mode exclusively from a portion of the hydrocarbon product or from portion of the intermediate products or from the portion of the by-products obtained in the first operating mode.    USE - Method for producing hydrocarbon product i.e. biomass-to-liquid (BTL) fuel from a fixed organic insert material i.e. biomass (claimed).    ADVANTAGE - The organic insert materials of the organic feedstock are processed in a second operating mode exclusively from a portion of the hydrocarbon product or from portion of the intermediate products or from the portion of the by-products obtained in the first operating mode, thus producing hydrocarbon product from the fixed organic insert material in a reliable and efficient manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a system for producing hydrocarbon product from fixed organic insert material.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a system for manufacturing a hydrocarbon product from a fixed organic insert material.    Organic insert material (a)    Raw gas-stream (b)    Intermediate products (c, d)    Organic feedstock (f)    Gas cleaning unit (2)    Gas synthesis unit (3)    Refinery unit (4)
NOVELTY - Column is filled with surface-processed carrier, surface-processed mesh, or surface-processed line mixer, where the surface carrier surface, surface-processed mesh, and surface-processed line mixer are processed using transmitter inhibitor which inhibits microorganisms (M1) receiving the transmitter which promotes production of metabolite by microorganisms, or carrier immobilizing microorganism (M2) which is capable of producing enzyme decomposing the transmitter promoting production of the metabolite by microorganisms (M1).    USE - The column is useful for treating water (claimed) including seawater, estuarine water, underground water, and sewage.
NOVELTY - Method for processing wastewater containing reducible sulfur compound by aeration process, involves placing plastic carriers in activated sludge containing 106 colony-forming units (cfu)/ml or more sulfur oxidizing bacteria i.e. Halothiobacillus SAB-1 strain (NITE P-1543), allowing formation of biofilm containing the sulfur oxidizing bacteria on the surface of the plastic carriers, placing plastic carriers immobilized with the Halothiobacillus in biological treatment tank, and performing aeration inside the tank.    USE - The method is useful for processing wastewater containing reducible sulfur compound (claimed).    ADVANTAGE - The method enables rapid and improved treatment of the reducible sulfur compound containing wastewater within short period of time, and purifies the water in a cost-effective and environmentally-friendly manner, when compared to existing biological treatment methods, and is suitable to perform in a narrower wastewater drainage site, as wastewater treatment equipment utilized in the method does not require additional installation of settling tank.
NOVELTY - An antifouling coating composition comprises a triorganosilyl ester-containing copolymer (A) obtained from a mixture of triorganosilyl (meth)acrylate monomer (a) (I) and ethylenically unsaturated monomer (b) copolymerizable with triorganosilyl (meth)acrylate monomer, and hydrate (B) of calcium sulfate. The content of hydrate (B) of calcium sulfate with respect to total solid content of antifouling coating composition is 5-50 %mass in terms of solid conversion.    USE - Antifouling coating composition is used for forming antifouling coating film for forming coated material (all claimed) used in boat, ship, fishery tool and underwater structure.    ADVANTAGE - The antifouling coating composition has excellent long-term storage stability. The environmentally-friendly coating film formed using the coating composition has excellent antifouling characteristics and crack resistance even when exposed to seawater for a long period of time.    DETAILED DESCRIPTION - An antifouling coating composition comprises a triorganosilyl ester-containing copolymer (A) obtained from a mixture of triorganosilyl (meth)acrylate monomer (a) of formula (I) and ethylenically unsaturated monomer (b) copolymerizable with triorganosilyl (meth)acrylate monomer, and hydrate (B) of calcium sulfate. The content of hydrate (B) of calcium sulfate with respect to total solid content of antifouling coating composition is 5-50 %mass in terms of solid conversion.    R1=H or methyl;and    R2-R4=branched 3-6C alkyl or phenyl in alpha -position.    An INDEPENDENT CLAIM is included for coated material, which consists of antifouling coating film formed using the antifouling coating composition on surface.
NOVELTY - Improved process for preparing (S)-N-((3-(3-fluoro-4-(4-morpholinyl)phenyl)-2-oxo-5-oxazolidinyl)methyl)phthalimide (II), comprises reacting carbamate compound (III) with (S)-glycidyl phthalimide (IV) using a base or quaternary ammonium salt and in the presence or absence of a solvent.    USE - The process is useful for preparing (II), which is useful as an intermediate for the preparation of linezolid (I) (all claimed). (I) is useful for treatment of infections caused by susceptible strains of microorganisms such as Vancomycin-Resistant Enterococcus faecium, nosocomial pneumonia, complicated skin and skin structure infection, uncomplicated skin and skin structure infections. No biological data given.    ADVANTAGE - The improved process is simple, commercially viable, safe and environmental friendly, and provides (II) with high yield using less expensive reagents, thus reducing the process cost.    DETAILED DESCRIPTION - Improved process for preparing (S)-N-((3-(3-fluoro-4-(4-morpholinyl)phenyl)-2-oxo-5-oxazolidinyl)methyl)phthalimide of formula (II), comprises reacting carbamate compound of formula (III) with (S)-glycidyl phthalimide of formula (IV) using a base or quaternary ammonium salt and in the presence or absence of a solvent.    X = O, NR1a, C(R2a)2; either    R1a = H, 1-5C alkyl, aryl or aralkyl; or    R1a+N+R = an aryl, heteroaryl or heterocyclyl; and    R2a = H, 1-5C alkyl, or halo.    Provided that when: X is O or NR1a, then R represents H, 1-5C alkyl, aryl, or aralkyl; and when X is C(R2a)2, then R represents H, halo, 1-5C alkyl, aryl, or aralkyl. INDEPENDENT CLAIMS are included for:    (1) N-((R)-3-(1,3-dioxo-1,3-dihydro-isoindol-2-yl)-2-hydroxy-propyl)-N-(3-fluoro-4-morpholin-4-yl-phenyl)-formamide compound of formula (V); and    (2) a process for the preparation of linezolid of formula (I), comprising converting the compound (II) to (I).
NOVELTY - Mixtures of monounsaturated alcohols e.g. 9-octadecanol, 11-eicosenol, 13-docosenol and 15-tetracosenol from jojoba oil are produced by transesterification of jojoba oil with alcohol of low and half molecular weight to obtain mixture of alcohol monounsaturated primary aliphatic and fatty acid ester of jojoba, and separation and division of alcohol of esters by column chromatography and cryogenic crystallization or direct separation of alcohol and ester from transesterification by fractional crystallization using nonpolar/polar solvent system.    USE - Production of mixtures of monounsaturated alcohols e.g. 9-octadecanol, 11-eicosenol, 13-docosenol and 15-tetracosenol from jojoba oil used for biodegradable biodiesel or products.    ADVANTAGE - Obtained alcohols are pure.
NOVELTY - Liberation (p1) of erythromycin (I) from erythromycin thiocyanate (II) involves treating erythromycin thiocyanate (II) with a base such as ammonia in presence of water as the liquid medium.    USE - For liberation of erythromycin (claimed) which is useful for treating gram-positive and gram negative bacteria.    ADVANTAGE - The present method is carried out in water as a solvent, thus avoids use of any organic solvent especially chlorinated solvents; is environmentally friendly; avoids tedious steps such as separation of organic solvent, concentration of solvent etc during isolation of erythromycin base and erythromycin stearate; is economical and industrially viable; and provides erythromycin base with more than 95% purity by avoiding further purification process.    DETAILED DESCRIPTION - Liberation (p1) of erythromycin of formula (I) from erythromycin thiocyanate of formula (II) involves treating erythromycin thiocyanate (II) with a base such as ammonia in presence of water as the liquid medium. An INDEPENDENT CLAIM is included for preparation (p2) of erythromycin stearate involving reacting erythromycin with stearic acid in presence of water; or reacting erythromycin thiocyanate with a base such as ammonia in presence of water at 30-80 degrees C to liberate erythromycin, treating the liberated erythromycin with stearic acid in presence of water, and filtering the obtained reaction mass followed by drying the product to obtain desired erythromycin stearate.
NOVELTY - Generating chemical products comprises generating electrical energy through a renewable energy source; generating hydrogen using electrical energy generated by the renewable energy source; and producing a chemical product utilizing the hydrogen generated by the electrical energy. The renewable energy source comprises a high altitude wind system. The hydrogen is generated using an electrolysis cell or a chlor-alkali process. The chlor-alkali process is a membrane, diaphragm, or a mercury process.    USE - Method for generating chemical products such as ammonia, methanol, and/or an olefin (claimed).    ADVANTAGE - The method utilizes energy locally and is readily adaptable to the amount of energy produced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an apparatus for generating chemical compositions, comprising a renewable energy source, a hydrogen generation module powered by the generated electrical energy, and a chemical generation module for processing the generated hydrogen.
NOVELTY - Production of protoporphyrin IX, comprises: cultivating a strain of Shewanella bacteria in a culture medium under conditions suitable for growth, the strain of Shewanella bacteria comprising at least one mutant hemH gene which is incapable of normal expression, thus causing an accumulation of protoporphyrin IX; and recovering the protoporphyrin IX from the culture medium.    USE - The method is useful for producing protoporphyrin IX (claimed).    ADVANTAGE - The method produces protoporphyrin IX in a cost-effective, contamination-less, environment-friendly, and safe manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a mutant strain of Shewanella bacteria comprising at least one mutant hemH gene which is incapable of normal expression, thus causing an accumulation of protoporphyrin IX during cultivation of the mutant strain of Shewanella bacteria in a culture medium.
NOVELTY - The apparatus has a pyrolysis jacket (22) heat-decomposing solid constituent (2) in outer circumference of a hollow reforming furnace (6) that is fixed in a gas collection tank (48). The gas collection tank collects synthetic gas of steam, carbon, carbon monoxide and hydrogen. An oxygen tank (12) feeds oxygen and hydrogen, and is connected to a burner (8). A guide pipe (46) is fixed with a carbon gas channel. An insulating material (24) is formed in the reforming furnace. The reforming furnace stores the synthetic gas. The burner supplies the hydrogen and oxygen to the reforming furnace.    USE - Apparatus for performing pyrolysis of biomass waste.    ADVANTAGE - The pyrolysis jacket places the solid constituent in the reforming furnace that is fixed in the pyrolysis jacket to simplify a structure of a reformer. The apparatus supplies steam and cracking gas to a bound side of the reforming furnace and a helix blade to improve reduction reaction efficiency at the reforming furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an apparatus for performing pyrolysis of biomass waste.    Solid constituent (2)    Hollow reforming furnace (6)    Burner (8)    Oxygen tank (12)    Pyrolysis jacket (22)    Insulating material (24)    Guide pipe (46)    Gas collection tank (48)
NOVELTY - Extracting shrimp oil, comprises: (a) obtaining an effluent for treating a marine organism; (b) adding a flocculant to the treatment liquid of the step (a) and separating an aqueous phase of the solid flocculant on a surface to recover the solids; (c) separating the solid recovered in the step (b) into a solid phase and a liquid phase and then recovering; (d) subjecting the liquid phase obtained in the step (c) to a vertical centrifuge to obtain an aqueous phase and an oil; and (e) recovering the separated oil.    USE - The method is useful for extracting a solid residue and a shrimp oil that is useful: as a food additive in aquaculture feed, preferably animal feed; and for producing a food or a food supplement intended for human use, animal, poultry, or aquaculture, where the food supplement is useful for combating radical oxidation in animal, and the animal is a human, a pet, a farm animal, or a bird (all claimed). No biological data given.    ADVANTAGE - The method is capable of extracting the shrimp oil that is enriched in astaxanthin with reduced energy consumption in an environmentally-friendly manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) the oil obtained by the above method;    (2) a solid residue obtained by the above method;    (3) a composition comprising the oil mixed with an excipient; and    (4) a mold for supplying at least one high fish hatchery, comprising the oil and the solid residue.
NOVELTY - The uniform agitation system (1000) has two feeding units (200,500) that include two motor for supplying bio-fuel and heavy oil to pumping operation, respectively. Two motor controllers (300,600) control two injection rates of bio-fuel and heavy oil input through two feeding units, respectively. Two temperature controllers (120,720) control the temperature of heat of bio-fuel applied in two containers (100,700). A fuel storing container (400) is provided for storing bio-fuel sprayed through nozzle based on predetermined mixing ratio.    USE - Uniform agitation system of bio-diesel fuel and heavy oil, for use in renal sinus power industry.    ADVANTAGE - Two temperature controllers are pre-possessed, so that the heat of the constant temperature is applied in the first heater in which the bio-fuel is filled. Thus the bio-fuel and heavy oil are evenly mixed within the fuel storing container. The bio-fuel with different specific gravity is compared by controlling the injection rate of bio-fuel and heavy oil. The thermal efficiency of the system is improved. The pressure about the income from fuel is reduced and the satisfaction about the use of fuel to purchase and majority nations is maximized. The energy of the system is saved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a driving method of uniform agitation system of bio-fuel and heavy oil.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of uniform agitation system of bio-fuel and heavy oil. (Drawing includes non-English language text)    Containers (100,700)    Temperature controllers (120,720)    Feeding unit (200,500)    Motor controllers (300,600)    Fuel storing container (400)    Uniform agitation system (1000)
NOVELTY - Manufacture of biodiesel involves mixing sewage sludge containing water with methanol or ethanol and acid catalyst, performing transesterification of mixed solution and xylene or toluene in reactor, heating, cooling, condensing methanol aqueous solution or ethanol aqueous solution and recycling to reactor, and separating biodiesel, aqueous solvent mixture and residual solid. The volume ratio of methanol or ethanol and acid catalyst is 1:0.01-1:0.05.    USE - Manufacture of biodiesel (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing apparatus of biodiesel.
NOVELTY - Biogas generation is an age-old technology that involves conversion of organic matter into methane and other gases in the absence of air by several different colonies of microbes working together. This process is known as anaerobic digestion and the vessel built for the conversion is known as a digester. When large amount of waste is available such as in a dairy, sugar mill or municipal waste collection, large cement & brick based digesters are built. When smaller quantity of organic wasteis available, pre-fabricated biogas digesters have been developed that convert organic waste into biogas. But they have faced negative customer feedback. Most prefabricated digesters have a dome that floats on the slurry in the digester and collects the biogas that is generated.The gasholder dome is provided with a gas pipe to convey the gas to the kitchen for cooking. Prior art designs suffer from several deficiencies such as tilting and jamming of the gasholder dome, gas pipe requiring frequent draining of the condensate, digester content becoming acidic and low production of biogas in cooler climes. Such challenges call for a dramatically different pre-fabricated design, incorporating a durable, easy to operate, efficient and near-zero maintenance biogas plant. Described in these filing is a do-it-yourself solution that has many applications in rural and urban areas.
NOVELTY - Present invention provides an up flow anaerobic sludge blanket (UASB) reactor with Mesophilic Jacket (Temperature Jacket) for controlling temperature which helps to produce higher biogas means higher energy production and with the help of which required temperature of the feed in the UASB reactor can be maintained in the reactor and with the help of mesophilic and thermophilic microorganisms the biogas production can be increased and which mainly comprises of feeding tank, funnel, 3 phase separator, peristaltic pump, effluent pipe, water jacket, thermostat controller, etc. Following invention is described in detail with the help of Figure 1 of sheet 1 showing schematic diagram of bench scale UASB reactor.
NOVELTY - Method of processing livestock excretion involves (a) selecting soil microorganism based on viability and determining pH and temperature requirements for the growth of selected microorganism, (b) adding the selected microorganism into livestock excretion after separating liquid and solid components to obtain mixed liquid, (c) transferring the resulting mixed liquid through circulating pumps and fermenting transferred liquid at 30-60 degrees C to obtain fermented liquid, and (d) evaporating the fermented liquid and recovering vaporized residue to obtain liquid fertilizer.    USE - The method is useful for processing livestock excretion for preparing liquid fertilizer (claimed).    ADVANTAGE - The method is environmentally-friendly.
NOVELTY - Manufacturing solid fuel from sludge, involves (a) drying sewage sludge having moisture content of more than 97-99% until the moisture content of dried sewage sludge material is 60-70%, and drying flammable waste until the moisture content of the dried flammable waste is 10-15% and crushing the dried waste, (b) mixing dried flammable waste and dried sewage sludge material, adding 0.94-1.1 wt.% chlorine, 5.2-6 wt.% water, 16.1-20.1 wt.% ash and 0.02-0.1 wt.% raw flour, and molding the mixture, (c) processing the molded mixture, and (d) pelletizing the mixture.    USE - The method is useful for manufacturing solid fuel from sludge (claimed).    ADVANTAGE - The method manufactures solid fuel by inexpensive process.    DETAILED DESCRIPTION - Method for manufacturing solid fuel from sludge, involves (a) drying sewage sludge having moisture content of more than 97-99% until the moisture content of dried sewage sludge material is 60-70%, and drying flammable waste until the moisture content of the dried flammable waste is 10-15% and crushing the dried flammable waste, (b) mixing dried flammable waste and dried sewage sludge material in a ratio of 4:6-2:8, adding 0.94-1.1 wt.% chlorine, 5.2-6 wt.% water, 16.1-20.1 wt.% ash and 0.02-0.1 wt.% raw flour, and molding the mixture such that the mixture has calorific value of 4700-4924 kcal/kg, (c) processing the molded mixture such that the mixture has calorific value of 5500 kcal/kg or more and the moisture content of the mixture is 10-15%, and (d) pelletizing the mixture.
NOVELTY - Purification method of low-density biomethane involves carrying out anaerobic digestion process of organic food waste, supplying generated biomethane gas into ammonia absorption tank, processing, then supplying into hydrogen sulfide absorption tank, processing using organic acid-iron chelate aqueous solution, supplying processed gas into electromagnetic resonance apparatus and electrochemical dissolution apparatus in order, and purifying.    USE - Purification method of low-density biomethane (claimed).    ADVANTAGE - The method provides low-density biomethane having high purity.
NOVELTY - Manufacture of synthetic natural gas involves preparing a synthesis gas by gasifying fuel, purifying the resulting synthesis gas, performing water gas conversion process of purified synthesis gas, carrying out Fischer-Tropsch reaction, separating 1-4C lower hydrocarbon obtained from reaction product, and mixing methane and 1-4C lower hydrocarbon isolated from synthesis gas.    USE - Manufacture of synthetic natural gas (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing device of synthetic natural gas.
(AT513486-B1)   NOVELTY - The method of loading and unloading of a hydrogen reservoir, is claimed. The hydrogen reservoir includes a tank (1) having a storage body (5) made of a metallic storage material. The storage body is heated, under successive charging and discharging cycles, with metal hydride and hydrogen. The hydrogen is recovered from the metallic storage material through recirculation of the metal hydride. The storage body is subjected to an external electrostatic field. The charge distribution capacity of the storage body is determined by a charging state of the hydrogen reservoir.    USE - The method is useful for loading and unloading of a hydrogen reservoir (claimed).    ADVANTAGE - The method is capable of loading and unloading of the hydrogen reservoir with less heat consumption.    DETAILED DESCRIPTION - The method of loading and unloading of a hydrogen reservoir, is claimed. The hydrogen reservoir includes a tank (1) having a storage body (5) made of a metallic storage material. The storage body is heated, under successive charging and discharging cycles, with metal hydride and hydrogen. The hydrogen is recovered from the metallic storage material through recirculation of the metal hydride. The storage body is subjected to an external electrostatic field. The charge distribution capacity of the storage body is determined by a charging state of the hydrogen reservoir. The tank is connected to a charging and discharge line (7). The storage body is arranged between electrodes (3) of a capacitor (2) such as plate capacitor. The electrodes have an electrically insulating layer relative to the storage body. An INDEPENDENT CLAIM is included for a device for loading and unloading of a hydrogen reservoir.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic view of a device for loading and unloading of a hydrogen reservoir.    Tank (1)    Capacitor (2)    Electrodes (3)    Storage body (5)    Charging and discharge line. (7)
NOVELTY - A 1-nitramine-2,4-nitroimidazole energetic ionic salt (I) is new.    USE - 1-Nitramine-2,4-nitroimidazole used for energetic material technology field.    ADVANTAGE - The simple and environment-friendly method has mild condition and high yield. The ionic salt has density of 1.70-1.93 g^/cm3, impact sensitivity of 4-40 J, explosion velocity of 8370-9209 m^/second and explosion pressure of 29.3-40.5 GPa.    DETAILED DESCRIPTION - A 1-nitramine-2,4-nitroimidazole energetic ionic salt of formula (I) is new.    X=cation comprising groups of formulae (i)-(vii).    An INDEPENDENT CLAIM is included for preparation of compound (I).
NOVELTY - A process of tar cracking or tar reforming to form a gas product, involves cracking or reforming tar of a tar-containing gas at preset temperature and a moisture content to form the gas product, carrying out online measurement of a content of at least one tar compound in the gas product using a photo ionization detector (PID) and controlling the temperature and/or the moisture content in cracking process based on the tar content(s) measured.    USE - Process of tar cracking or tar reforming is used for forming gas product.    ADVANTAGE - The method enables rapid and reliable process of tar cracking or tar reforming, with reduced steam consumption.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) process of gasification of biomass to form a gas product;    (2) system for cracking or reforming of tar;    (3) gasification system; and    (4) naphtha cracking or reforming system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of gasification and tar cracking/reforming process.    Supply line (107)    Gas product line (108)    Sample line (109)    Computing and control device (111)    Oxygen regulating valve (112)
NOVELTY - A polyvinylidene fluoride (PVDF) hollow fiber separation membrane comprises thermoplastic resin, which contains 2-50 pts. wt. at least one selected from polyethylene glycol-methacrylate-based and polyvinylpyrrolidone-methacrylate-based amphiphilic polymer, and having weight average molecular weight (Mw) of 10000-200000, based on 100 pts. wt. PVDF resin, and has a porous hollow fiber structure.    USE - As polyvinylidene fluoride hollow fiber separation membrane (claimed) useful in not only for water treatment, but also in sewage treatment field, such as domestic waste water, industrial wastewater and also used in various industrial fields, such as food field, medicine field, water purification facilities, separation of microorganism from fermented solution and purification of proteins.    ADVANTAGE - The hollow fiber separation membrane has significantly excellent contact angle and pure water permeability, which means that hydrophilicity has been significantly improved. Excellent physical properties were also exhibited in terms of alkali resistance, and thus it was confirmed that the hollow fiber separation membrane may exhibit excellent performance when applied to various separation membranes. The membrane has excellent effects in terms of productivity and economic efficiency; and is used for long time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing PVDF hollow fiber separation membrane involving preparing a spinning solution by using thermoplastic resin; spinning the spinning solution through a nozzle for preparing hollow fiber; and subjecting the spinning solution to coagulation process to prepare porous hollow fiber.
NOVELTY - Catalyst comprising a mixed oxide of magnesium and manganese, where the catalyst further comprises lithium and boron dopants and at least one doping element of groups 4, 9, 12 and/or 13, is new. The catalyst comprises a 2C-selectivity of greater than 50% and a methane conversion of greater than 20% when the catalyst is employed as a heterogeneous catalyst in the oxidative coupling of methane at a temperature of 750 degrees C or less.    USE - The catalyst is useful: in a catalytic reaction including oxidative coupling of methane; and for preparing a downstream product of ethane and/or ethylene, where the ethylene includes low density polyethylene, high density polyethylene, ethylene dichloride, ethylene oxide, ethylbenzene, ethanol, vinyl acetate, or natural gasoline including 1-hexene, 1-octene, hexane, octane, benzene, toluene and xylene (all claimed), and the catalyst includes a heterogeneous catalyst and a homogenous catalyst and is useful for the oxidative dehydrogenation of hydrocarbons such as alkanes, alkenes, and alkynes.    ADVANTAGE - The catalyst improves yield, selectivity and conversion of the oxidative coupling of methane reaction and other catalyzed reactions.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) use of the catalyst in a catalytic reaction; and    (2) preparing a downstream product of ethane and/or ethylene, comprising converting methane into ethane and/or ethylene in the presence of the catalyst, and further oligomerizing the ethylene to prepare a downstream product of ethylene.
NOVELTY - A fuel composition comprises a fuel component; an alcohol component; a water component; a microemulsion blend including lower grade fatty acid derivative(s) being present in an amount effective for fuel, alcohol, and water components to form a microemulsion blend; and a cetane-enhancer component.    USE - Fuel composition used for internal-combustion engines.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of formulating a fuel composition comprising:    (A) providing (102) a fuel; and    (B) forming (108) the fuel composition by adding to the fuel, a microemulsion blend comprising lower grade fatty acid derivative(s) being present in an amount effective for the fuel, alcohol, and water components to form the microemulsion blend, where the microemulsion blend includes mixture of oleic acid, ethanol, ammonia, water and cetane enhancer.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic block diagram of the method for synthesizing and formulating a fuel composition.    Fuel providing step (102)    Alcohol component providing step (104)    Microemulsion blend providing step (106)    Fuel composition forming step (108)
NOVELTY - A fuel composition comprises lower grade fuel component; and microemulsion comprising at least one of hydrous component, renewable component and polar component.    USE - As fuel composition, such as biodiesel useful in internal-combustion engines (claimed).    ADVANTAGE - The fuel composition enhances lubricity, corrosion and water stability without the use of other additives and inhibitors. The composition comprises increased concentration of renewable contents. The composition is formed on large scale and such that it reduces carbon intensity in internal combustion engines. The composition reduces emissions of NOx, particulate matter and other criteria pollutants. The composition allows flashpoint to stay below 38C for microemulsion concentration of greater than 1% but the flashpoint increases for microemulsion concentrations that are below 1%. The composition forms spontaneously upon blending, and maintains clarity at low temperatures, upon freeze-thawing, and for prolonged periods.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for formulating fuel composition involving providing fuel; and adding microemulsion comprising at least one of hydrous component, renewable component and polar component to the fuel.    DESCRIPTION OF DRAWING(S) - The figure shows schematic block diagram of method for synthesizing and formulating fuel composition.
NOVELTY - Method for processing organic wastewater involves (a) dehydrating sludge (A) containing excrement and/or organic sludge which is added with surplus sludge and coagulant and (b) directly dehydrating sludge (B) containing excrement and/or organic sludge without adding surplus sludge and coagulant, obtaining supernatant liquid from the dehydrated sludge and treating supernatant liquid biologically.    USE - The method is useful for processing organic wastewater (claimed).    ADVANTAGE - The method enables processing of organic wastewater with reduced requirement of cost and maintenance and reduces moisture content and volume of dehydrated sludge.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for organic wastewater processing apparatus.
NOVELTY - Method of producing fermentation bacteria is performed by using multiple types of organic substances as raw materials.    USE - Method of producing fermentation bacteria for decomposition method of raw sewage (claimed) used for raw sewage disposal.    ADVANTAGE - Amount of waste material is reduced, and simplification of processing apparatus and reduction of processing cost are achieved.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) manufacturing method of 2nd fermentation bacteria which involves using fermentation bacteria which decompose raw sewage; and    (2) manufacturing method of 3rd fermentation bacteria which involves using product of raw sewage decomposed by 2nd fermentation bacteria.
NOVELTY - A metal tin-carbon composite comprises metal tin nanoparticles (B) included in matrix (A) containing carbon. The metal tin nanoparticles (B) have particle size of 0.2-5 nm, and do not contain coarse metal tin particles having particle size of 1 mu m or more.    USE - Metal tin-carbon composite is used for active substance for negative electrode for nonaqueous lithium secondary battery (all claimed). Can also be used as hydrogen storage material of energy-related raw material of lithium cell periphery, solar cell and fuel cell, hybrid capacitor, catalyst-related exhaustion process and organic substance synthesis.    ADVANTAGE - The metal tin-carbon complex is manufactured by simple and economical method. The battery containing the metal tin-carbon complex has high capacity and excellent cycling characteristics.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of metal tin-carbon composite, which involves baking precursor containing cation polymer, tin compound and sulfuric acid;    (2) negative electrode active substance, which consists of metal tin-carbon composite;    (3) negative electrode, which contains the negative electrode active material and a binder; and    (4) nonaqueous lithium secondary battery, which has negative electrode and positive electrode.
NOVELTY - Fermentation heat utilization system comprises fermentation chamber (2) which is configured to be able to house organic waste (200) and ferments the organic waste to generate fermentation heat and radiator (4a) which is provided in the fermentation chamber and configured to be able to cause a first thermal absorption portion to flow, and absorbs the fermentation heat to increase the temperature of the first thermal absorption portion, where the fermentation heat utilization system is configured to be able to utilize the fermentation heat of the organic waste.    USE - The fermentation heat utilization system is useful for fermenting organic waste.    ADVANTAGE - The system improves utilization efficiency of fermentation heat, suppresses adhering of organic wastes and promotes fermentation of the organic waste.    DESCRIPTION OF DRAWING(S) - The drawing shows sectional view of fermentation heat utilization system.    Fermentation chamber (2)    Radiator (4a)    Boiler (6)    Heater (13)    Detection portion (14)    Control portion (15)    Organic waste (200)
NOVELTY - Preparing (P1) 3-oxo-tetrahydrofuran involves reacting 3-hydroxy-tetrahydro-furan (II) with 0.5-2 mol equivalents of trichloroisocyanuric acid (IIa) in the presence of 0.001-1 mol equivalent 2,2,6,6-tetramethylpiperidine-N-oxyl (TEMPO) in a solvent selected from dichloromethane, ethyl acetate, isopropyl acetate, acetone, acetonitrile and toluene at -20 to 40 degrees C.    USE - For preparing 3-oxo-tetrahydrofuran (claimed) useful as intermediate in manufacture of pharmaceutical active compounds.    ADVANTAGE - The process provides simple, inexpensive, chemoselective and environmentally friendly process for the manufacture of 3-oxo-tetrahydrofuran that can be run under mild conditions. The process does not require the use of NaHCO3 buffering, NaBr or other additives and delivers 3-oxo-tetrahydrofuran with good yields and in high quality without toxic by-products and transition metal wastes.    DETAILED DESCRIPTION - Preparing (P1) 3-oxo-tetrahydrofuran involves reacting 3-hydroxy-tetrahydro-furan of formula (II) with 0.5-2 mol equivalents of trichloroisocyanuric acid of formula (IIa) in the presence of 0.001-1 mol equivalent 2,2,6,6-tetramethylpiperidine-N-oxyl (TEMPO) in a solvent selected from dichloromethane, ethyl acetate, isopropyl acetate, acetone, acetonitrile and toluene at -20 to 40 degrees C. An INDEPENDENT CLAIM is included for preparing (P2) 3-oxo-tetrahydrofuran involving conversion of butane-1,2,4-triol in the presence of an acid to 3-hydroxy-tetrahydrofuran, followed by oxidation of 3-hydroxy-tetrahydrofuran.
NOVELTY - Method of preparing compost in a biofermenter comprises the preparation of the fermented mixture, transferring the mixture into the fermenter with the pressure air ducts, and the subsequent aerobic fermentation of the mixture, and the control over the fermentation process is carried out by non-contact temperature measurement using mobile infrared sensors over the entire surface of the fermented mixture. At that, a linear time schedule of temperature change in the range of from 20?oC to 30?oC, from 30?oC to 60?oC and from 60?oC to 70?oC with a tolerable deviation of \|;3?oC is provided by supply of air in the system of pressure air ducts of the fermenter to the zones of temperature measurement, and the temperature measurements and the air supply is carried out at intervals of 1-2 hours.    USE - Agriculture.    ADVANTAGE - Invention enables to improve manufacturability of the method and to reduce the time of maturation of the finished product.2 dwg
NOVELTY - Composting fermentation device comprises a composting device (1) comprising a cover (4) at the top, which is provided in middle with a threaded hole, and a discharge opening at the bottom; a spray equipment (2); and an air collection device (3). The threaded rod extends in the composting device and is provided with a pressure plate. The distance between the pressure plate and the composting device is 5 cm. The threaded rod is provided on the other side with a handle. The composting device is provided on one side with an object opening which corresponds to a first sealing lid.    USE - Used as a composting fermentation device.    ADVANTAGE - The device is environmentally-friendly.    DETAILED DESCRIPTION - Composting fermentation device comprises a composting device (1) comprising a cover (4) at the top, which is provided in the middle with a threaded hole corresponding to a threaded rod, and a discharge opening at the bottom; a spray equipment (2); and an air collection device (3). The threaded rod extends in the composting device and is provided with a pressure plate. The distance between the pressure plate and the composting device is 5 cm. The threaded rod is provided on the other side with a handle. The composting device is provided on one side with an object opening which corresponds to a first sealing lid. The lid is connected with the spray equipment by an air pipe. The spray equipment is connected with the air collection device at the bottom by an air tube (6). The spray equipment is provided on the bottom with a discharge opening. The air collection device is provided on one side with an air discharge tube which is provided with a second sealing lid.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the composting fermentation device.    Composting device (1)    Spray equipment (2)    Air collection device (3)    Cover (4)    Air tube (6)
NOVELTY - A xylanase-active enzyme cel10-CBM6-KG61 gene comprising a 1821 base pair sequence (SEQ ID NO: 1) fully defined in the specification, is new. The gene is isolated from Capra hircus aegagrus rumen microorganism.    USE - The xylanase-active enzyme cel10-CBM6-KG61 gene is used in recombinant vector for producing transformed host cell used for producing xylanase active enzyme protein which is used in feed additive and detergent composition and for producing biofuel (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) glycoside hydrolase 10 comprising a 606 amino acid sequence (SEQ ID NO: 2) fully defined in the specification, where the glycoside hydrolase 10 is isolated from C.hircus aegagrus rumen microorganism, and carbohydrate-binding module (CBM) 6 of the glycoside hydrolase 10 is encoded by the above-mentioned gene; (2) recombinant vector comprising the above-mentioned gene; (3) host cell transformed with the recombinant vector; and (4) manufacturing method of biofuel, involves adding the xylanase active enzyme protein in biomass matter, and hydrolyzing the biomass.
NOVELTY - Preparing sugars from biomass, comprises (a) contacting the biomass with a catalyst to hydrolyze components of the biomass to sugars under conditions of high-shear agitation to produce a mixture of solids and a liquid comprising sugars, (b) separating the mixture into a liquid stream comprising sugars and a solid stream comprising solids, and (c) incubating the solid stream under conditions suitable to hydrolyze components of the solids to sugars to produce additional sugars.    USE - The method is useful for preparing sugars e.g. glucose from biomass, preferably lignocellulosic biomass or pretreated biomass, where the sugars are converted into ethanol, biofuels, biochemicals, or other chemical products (all claimed), the biomass includes agricultural products such as grains e.g. corn, wheat and barley, sugarcane, corn stover, corn cobs, bagasse, Sorghum and other inedible waste parts of food plants, food waste, switchgrass, and forestry biomass, such as wood, paper, board and waste wood products, and the other sugars include xylose, arabinose, mannose and galactose.    ADVANTAGE - The method ensures improved conversion of cellulosic biomass to sugars e.g. glucose with improved yield.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic flow diagram of a method for preparing sugars from biomass.
NOVELTY - A biodiesel crystallization depressant composition comprises triacylglycerol dimer, (E)-1-(1-(oleoyloxy)-3-(stearoyloxy)propan-2-yl) 18-(1-(oleoyloxy)-3-(stearoyloxy)propan-2-yl) octadec-9-enedioate.    USE - The composition is useful as biodiesel crystallization depressant (claimed).    ADVANTAGE - The dimers, due to their particular structure and conformation, disrupt the regular packing of linear saturated fatty acid methyl esters, thus delaying nucleation and mitigating crystal growth.
NOVELTY - A biodiesel crystallization depressant composition comprises: triacylglycerol containing 1,3-dioleoyl-2-palmitoyl glycerol (OPO). The glycerol (OPO) is mixed with a biodiesel fuel comprising methyl palmitate to a desired molar fraction, X-OPO, where X is 0-1, and further the glycerol (OPO) begins crystallization depression from inception of addition down to a maximum at molar fraction 0.45-OPO.    USE - As biodiesel crystallization depressant composition (Claimed).    ADVANTAGE - The depressant composition suppresses the crystallization of biodiesel and delays the rate of nucleation and/or crystal growth processes. At the nucleation level, the depressant composition delays the formation of critical nuclei from embryo clusters through molecular-level interactions between the crystallizing host molecules and the interfering depressant composition molecules. Thus the crystal growth is delayed when the depressant composition prevents the adsorption and incorporation of crystallizing host molecules at the growing crystal surfaces. The polymorphism and microstructure of and the properties of triacylglycerols and fatty acid methyl esters, as well as their combined mixtures, in a biodiesel fuel, helps to understand the fundamental mechanisms of their crystallization so as to design biodiesel fuels with improved low temperature characteristics.
NOVELTY - Pre-drying of hydrolytic lignin involves blending hydrolytic lignin having relative moisture content of 55-80% with hydrolytic lignin having relative moisture content of 0-45%, to produce hydrolytic lignin product having moisture content of less than 55%. The ratio of hydrolytic lignins is 1:6-10:1.    USE - Pre-drying during drying of hydrolytic lignin (claimed) used as sorbent material and solid fuel.    ADVANTAGE - The hydrolytic lignin is dried by explosion and fire-safe method.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for drying of hydrolytic lignin.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the drying apparatus used for drying hydrolytic lignin.    Hopper (1)    Hydrolytic lignin raw material (2)    Tube dryer (4)    Feed chute (5)    Drying apparatus (100)
NOVELTY - A system for the production of hydrothermally carbonized (HTC) biomass comprises an infeed (40) for accepting biomass feed material; twin screw extruder (80) connected with respect to infeed, twin screw extruder (TES) having length between infeed and outlet; water heater (50) connected with respect to at least one inlet along length of the TES, where inlet generally corresponds with pressure boundary within the TES; and pressure sustaining valve (100) connected between length of the TES and outlet.    USE - As system for the production of hydrothermally carbonized (HTC) biomass using twin-screw extruder (claimed).    ADVANTAGE - The system is capable of fast start up times to full production capacity and efficient energy consumption resulting in a carbonized biomass with various applications.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of HTC biomass involving feeding biomass feed material to infeed of TES; operating mixing elements and reversing elements within the TES; injecting hot water (60) from water heater into inlet along the length of the TES; and adjusting pressure sustaining valve connected between length of the TES and outlet to control the production of HTC biomass.    DESCRIPTION OF DRAWING(S) - The figure shows schematic cross-sectional side view of a system.    Infeed (40)    Water heater (50)    Hot water injection port (60)    Twin-screw extruder (80)    Cooled barrels (85)    Pressure sustaining valve (100)
NOVELTY - A sealing material (1) comprises a crystalline polyester resin, a noncrystalline polyester resin, an epoxy resin, and an isocyanate type crosslinking agent. The sealing surface of the sealing material is formed by a hot-melt adhesive formed by crosslinking the polyester resins by the crosslinking agent.    USE - Sealing material is used for sealing circumference of electrolytic membrane of fuel cells which generate electric power by reaction with hydrogen and oxygen.    ADVANTAGE - The sealing material has excellent heat-and-moisture resistance, and provides fuel cells with excellent sealing reliability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for hot-melt adhesive.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic plan view of the sealing material and a schematic sectional view of the cross-section in the top view. (Drawing includes non-English language text)    Sealing material (1)    Base material layer (10)    Adhesive bond layer (20,20a,20b)
NOVELTY - The system (10) has an auger feeder (20) for receiving material to be gasified and feeding the material. An outlet tube (30) is connected to the feeder such that the tube receives the material from the feeder. A gasifier is connected to the tube such that the gasifier receives the material from the tube. A drop chute (600) provides the material to the feeder. A slide gate is adapted to open to allow the material to enter the chute and adapted to close to provide an airtight seal to the feeder. A body (32) includes an inner wall that defines an opening to receive the material from the feeder.    USE - System for processing/extruding feedstock material i.e. municipal solid waste (MSW), for a gasifier i.e. plasma furnace. Can also be used for processing/extruding organic material, fossil-based carbonaceous material e.g. coal and petroleum coke, biomass material and waste-derived feedstock e.g. wood, plastic, aluminum, refuse-derived fuel (RDF), agricultural and industrial waste, sewage sludge, switchgrass, various crop residues and black liquor, for a counter-current fixed bed, co-current fixed bed, fluidized bed, entrained flow gasifier and a free radical gasifier.    ADVANTAGE - The system densifies the material such as sorted MSW, up to about six times to eliminate free air in the feedstock material that is provided to the gasifier to provide an air tight seal, thus vastly improving efficiency of the gasifier. The system isolates an area or flow of material, and creates the airtight seal with flow of a continuous plug of material to the gasifier.    DETAILED DESCRIPTION - The outlet tube is a water-cooled outlet tube.    DESCRIPTION OF DRAWING(S) - The drawing shows a side elevational view of a system for processing/extruding material for a gasifier.    System for processing/extruding feedstock material (10)    Auger feeder (20)    Outlet tube (30)    Body (32)    Drop chute (600)
NOVELTY - The hydrogen production apparatus has a hydrogen separation membrane which is arranged to outer peripheral surface of modification-catalyst and support portion, while arranging modification-catalyst and support portion at intervals in an outer peripheral surface side of interpolating tube. The reformed gas is generated by modification-catalyst and support portion and made to flown between interpolating tube and modification-catalyst and support portion. The highly purified hydrogen is produced by purifying generated reformed gas using hydrogen separation membrane.    USE - Hydrogen production apparatus.    ADVANTAGE - The reformation efficiency of the hydrogen production apparatus is improved and the amount of hydrogen production by the hydrogen production apparatus is increased. The manufacturing cost of the hydrogen production apparatus is reduced. The modification catalyst is effectively utilized in wide range in the modification-catalyst and support portion.    DETAILED DESCRIPTION - The degree closer to the front-end portion enlarges the diameter of several emitting holes arranged in the interpolating tube. The interpolating tube is provided with a hollow portion which is a flow path of source gas. The front-end portion which reforming reaction follows actively is made to increase by shortening the length of the modification-catalyst and support portion. The internal peripheral surface of the modification-catalyst and support portion is considered as an uneven surface. A centrifugal fan is rotatably positioned in the hollow portion. The reformed gas is produced by forcedly sending in between the interpolating tube and the modification-catalyst and support portion.    DESCRIPTION OF DRAWING(S) - The drawing shows the explanatory and schematic views of the hydrogen production apparatus. (Drawing includes non-English language text)
NOVELTY - The method comprises introducing biological substances with combustion exhaust gases into a gas engine for less than 10 minutes, converting the substances into stream, supplying the combustion gases to the stream, adding sulfuric acid and soil additives, preferably herb oils to the substances, and removing water from the substances by evaporation and then cooling. A temperature of the combustion exhaust gases is 350 degrees C during the introduction step.    USE - The method is useful for processing biological substances such as digestate from biogas plants or manure (claimed), where the digestate is useful for producing fertilizer.    ADVANTAGE - The method is capable of processing the biological substances with less energy consumption thus reducing the cost of a landfill or other disposal of the digestate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for processing biological substances.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a gas engine.    Exhaust system (2)    Three-way control valve (3)    Line (4)    Container (5)    Funnel. (6)
NOVELTY - Producing biogas comprises fermenting stackable biomass using at least one solid fermentation chamber, and applying percolate repeatedly to the stackable biomass into the solid fermentation chamber (40, 42). The percolate is generated from a stirrable fermentation substrate of a liquid fermentation plant (2).    USE - The method is useful for producing biogas (claimed).    ADVANTAGE - The stackable biomass that is associated with the liquid fermentation plant is processed in an efficient manner. The stirring ability of the liquid fermentation substrate is improved in the liquid fermentation plant by reducing the introduction of the stackable biomass or solids into the liquid fermentation plant, thus the power consumption for the corresponding stirrers is reduced and significant energy saving is achieved, improving the plant efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for producing the biogas, comprising at least one solid fermentation chamber for fermenting the stackable biomass, provided with at least one percolate nozzle (50) for applying the percolate to the stackable biomass. A percolate treatment device (5) is provided for producing the percolate from the stirrable fermentation substrate of the liquid fermentation plant, for introducing into the solid fermentation chamber.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of a device for producing the biogas.    Liquid fermentation plant (2)    Percolate treatment device (5)    Solid fermentation chamber (40)    Percolate nozzle (50)    Percolate recycling line (52)
NOVELTY - Microorganism strain comprising Raoultella, Klebsiella, Bacillus or Paenibacillus containing a Escherichia coli pyruvate oxidase (poxB) gene, where the poxB gene is inactivated, and the sugar such as pentose is derived from hemicellulose, is new.    USE - The microorganism strain is useful for the fermentation production of 4C-products such as 2,3-butanediol or acetoin that are useful as a carbon-source for fermenting sugar, where the sugar is pentose, preferably xylose (all claimed).    ADVANTAGE - The microorganism strain is capable of efficiently producing the 4C-products with reduced cost in an industrial and rapid manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the fermentation production of 4C-products from sugars occurring in a lignocellulose-containing biomass by the microorganism strain.
NOVELTY - Coalescence media comprises an emulsion-contacting sheet formed as a single dry layer from a wet laid process using a single homogenously distributed, wet-laid furnish of a mixture of fibrous components of kraft fibers, fibrillated fibers or glass micro fibers, and at least one non-fibrous component comprising a dry strength additive or a wet strength additive. The fibrous components of the coalescence media constitute at least 70% of the coalescence media, having a pore structure sufficient to coalescence water droplets having a droplet size of less than 3.5 mu m.    USE - The coalescence medium is useful for separating water-hydrocarbon emulsions in biodiesel blends or in surfactant stabilized water-hydrocarbon emulsions (claimed).    ADVANTAGE - The coalescence media have improved pore size, permeability, surface area, thickness, permeability for the effective separation of water-hydrocarbon emulsions.
NOVELTY - Coumarin derivative (I) preparation involves mixing and stirring benzaldehyde derivative (II) with pivaloyl chloride (III) in organic solvent, dimethylaminopyridine and triethylamine at 5-40 degrees C to obtain a reaction liquid, and adding dichloromethane to the reaction liquid, and treating with saturated aqueous sodium chloride solution. The product is washed with anhydrous magnesium sulfate, and then dried to obtain 4-formylphenyl 2,2-dimethylpropanoate derivative (IV).    USE - Method for preparing coumarin derivative (claimed).    ADVANTAGE - The method enables preparing coumarin derivative with 77.4% yield at industrial level in a simple, eco-friendly, easy and cost-effective manner.    DETAILED DESCRIPTION - Coumarin derivative of formula (I) preparation involves mixing and stirring benzaldehyde derivative of formula (II) with pivaloyl chloride of formula (III) in organic solvent, dimethylaminopyridine and triethylamine at 5-40 degrees C to obtain a reaction liquid, and adding dichloromethane to the reaction liquid, and treating with saturated aqueous sodium chloride solution. The product is washed with anhydrous magnesium sulfate, and then dried to obtain 4-formylphenyl 2,2-dimethylpropanoate derivative of formula (IV). 4-Formylphenyl 2,2-dimethylpropanoate derivative of formula (IV) is dissolved in organic solvent B, and then stirred at 100 degrees C to obtain compound of formula (V).    R1=H, methoxy, ethoxy or nitro group;    R3=H, methoxy, hydroxy or nitro group; and    R2=hydroxyl, methoxy or nitro group.
NOVELTY - Preparing (E)-3-(2,2-Difluoro-benzo(1,3)dioxol-4-yl)-acrylonitrile involves refluxing triphenylphosphine with 2-bromoacetonitrile in toluene for 4 hours to obtain 2-bromo-2-(triphenyl-(5)-phosphanyl)acetonitrile (white solid). 2,2-Difluoro-1,3-benzodioxole is treated with 2-bromo-2-(triphenyl-(5)-phosphanyl)acetonitrile in presence of cyclohexane, n-butyl lithium and tetrahydrofuran, and then N,N- dimethylformamide is slowly added to the product. The product is processed with hydrochloric acid. The product is extracted with ethyl acetate, and then washed with brine.    USE - Synthetic method for preparing (E)-3-(2,2-Difluoro-benzo(1,3)dioxol-4-yl)-acrylonitrile (claimed).    ADVANTAGE - The method enables to prepare intermediate of fludioxonil in an eco-friendly and cost-effective manner.    DETAILED DESCRIPTION - Preparing (E)-3-(2,2-Difluoro-benzo(1,3)dioxol-4-yl)-acrylonitrile involves refluxing triphenylphosphine with 2-bromoacetonitrile in toluene for 4 hours to obtain 2-bromo-2-(triphenyl-(5)-phosphanyl)acetonitrile (white solid). 2,2-Difluoro-1,3-benzodioxole is treated with 2-bromo-2-(triphenyl-(5)-phosphanyl)acetonitrile in presence of cyclohexane, n-butyl lithium and tetrahydrofuran, and then N,N- dimethylformamide is slowly added to the product. The product is processed with hydrochloric acid. The product is extracted with ethyl acetate, and then washed with brine. The washed product is dried with anhydrous sodium sulfate. The product is dissolved in dichloromethane, and then processed with sodium hydroxide solution to obtain the desired product.
NOVELTY - Preparing (1-(3-Ethyl-phenyl)-ethyl)-dimethyl-amine comprises mixing dimethylamine hydrochloride and a base to carrying out alkali reaction under the presence of tetraisopropyl titanate to obtain dimethyl amine and then reacting with inter-methoxy-acetophenone in the presence of a catalyst at 0-50 degrees C for 5-24 hours, introducing hydrogen gas into the reaction at 20-100 degrees C for 12-72 hours, where the reactions are carried out under atmospheric pressure.    USE - The method is useful for preparing (1-(3-Ethyl-phenyl)-ethyl)-dimethyl-amine (claimed).    ADVANTAGE - The method is capable of simply, economically and safely preparing rivastigmine at normal pressure and mild reaction condition without pollution.
NOVELTY - A carboxamide compound is prepared by performing carbamylation reaction of 2-benzyloxyaniline-containing compound and formylation reagent with solvent to obtain formanilide-containing compound, and removing hydroxyl protecting group using hydrogen on palladium/carbon catalyst.    USE - Preparation of carboxamide compound for impurity standard sample used for formoterol medicine detection (all claimed).    ADVANTAGE - Process has mild reaction conditions, high conversion rate and product yield, and good purity.    DETAILED DESCRIPTION - A carboxamide compound of formula (6) is prepared by performing carbamylation reaction of 2-benzyloxyaniline-containing compound of formula (4) and formylation reagent with solvent to obtain formanilide-containing compound of formula (5), and removing hydroxyl protecting group using hydrogen on palladium/carbon catalyst.
NOVELTY - A triacylglycerol oil derived from a Pythium biomass comprises: greater than 20% w/w dry cell weight cell lipid; and/or greater than 10% of total fatty acids is eicosapentaenoic acid (EPA).    USE - The triacylglycerol oil is useful in food production, and various skin preparations, cosmetics, soaps, skin cleansers, lotions, sun screen, hair products and other preparations.    ADVANTAGE - The triacylglycerol oil contains beneficial amount of EPA with enhanced anti-inflammatory properties.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a process of producing at least one triacylglycerol oil, comprising: (i) providing a suitable amount of Pythium cultures; (ii) growing a Pythium biomass using a substrate from the suitable amount of Pythium cultures; (iii) extracting a triacylglycerol oil from the Pythium biomass, where the at least the triacylglycerol oil comprises greater than 20% w/w dry cell weight cell lipid and greater than 10% of total fatty acids contained in the at least one triacylglycerol oil is EPA.
NOVELTY - Method of converting hydrocarbon into hydrogen and carbon material, involves heating hydrocarbon and catalyst in a reactor (102), forming hydrogen and carbon material which does not contain carbon dioxide, operating fuel cell (104) to generate electrical energy and heat using the hydrogen formed in the reactor and repeating the step of heating using the heat generated in the fuel cell.    USE - Method of converting hydrocarbon into hydrogen and carbon material used for solid oxide fuel cell (claimed).    ADVANTAGE - The method economically enables the conversion of hydrocarbon into hydrogen and carbon material. The solid oxide fuel cell operates using hydrogen generated by the method has overall energy efficiency of 25-46%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for system (100) for converting hydrocarbon into hydrogen and carbon material.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of system for converting hydrocarbon into hydrogen and carbon material.    System for converting hydrocarbon into hydrogen and carbon material (100)    Reactor (102)    Fuel cell (104)    Pipe (108)    Hydrogen-transport element (110)
NOVELTY - Producing (P1) non-polar lipid in a plant part involves expressing in the plant part at least one exogenous polynucleotide which encodes at least Wrinkled 1 (WRI1) and diacylglycerol acyltransferase (DGAT), where co-expression of WRI1 and DGAT has an effect on non-polar lipid accumulation in the plant part that is larger than an additive effect of the individual effects of each of WRI1 and DGAT expressed alone.    USE - For producing non-polar lipid such as a fatty acid, and modified level of total sterols, non-esterified sterols, steroyl esters or steroyl glycosides relative in a plant part (claimed), which is useful for producing alkyl esters of the fatty acids which are suitable for renewable biodiesel fuel.    ADVANTAGE - The process increases the yield of non-polar lipid; and increases the oil content, which is of great significance for production of biofuels and other industrial products derived from oil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a process of feeding an animal involving providing to the animal a plant part which comprises at least one exogenous polynucleotide which encodes at least Wrinkled 1 (WRI1) and diacylglycerol acyltransferase (DGAT), where co-expression of WRI1 and DGAT has an effect on non-polar lipid accumulation in the plant part that is larger than an additive effect of the individual effects of each of WRI1 and DGAT expressed alone.
NOVELTY - Converting bio-oil (10), comprises subjecting a feedstock comprising bio-oils or their fractions with at least one alcohol (20) comprising 1-30C alcohol or its mixture to an azeotropic distillation to yield a liquid component (40), and subjecting the liquid component to alcoholysis.    USE - The converted bio-oil product is useful as heating oil and as starting material for producing fuels, fuel components, fine chemicals, chemical building-blocks and solvents (claimed).    ADVANTAGE - The process produces the converted bio-oil product with improved (storage)stability and reduced acid number and acidity.    DESCRIPTION OF DRAWING(S) - The figure shows a flow diagram of the process for converting bio-oil.    Bio-oil (10)    Alcohol (20)    Gaseous component (30)    Liquid component (40)    Separation unit. (50)
NOVELTY - Preparing an alkyl compound or its mixture involves preparing ketene compound; reacting the compound (I) to form a self-addition product; and hydrogenating the self-addition product in the presence of a metal catalyst to form the alkyl compound or its mixture.    USE - For preparing alkyl compound comprising 1-butanol, 2-butanol, 4-heptanol and 2-heptanol, and hydrocarbon product (claimed) used as fuels and industrial chemicals.    ADVANTAGE - The method produces fuels and chemical that offers the potential for higher energy fuels that are readily compatible with existing automotive and transportation infrastructure; synthesizes fuels and chemicals from non-petroleum sources such as biomass, coal and natural gas; and produces fuel which has a calorific values closer to gasoline and higher than ethanol and butanol fuel.    DETAILED DESCRIPTION - Preparing an alkyl compound or its mixture involves preparing ketene compound of formula R1-C(R2)=C=O; reacting the compound (I) to form a self-addition product; and hydrogenating the self-addition product in the presence of a metal catalyst to form the alkyl compound or its mixture.    R1=H or 1-6C alkyl;    R2=H or 1-6C alkyl.    An INDEPENDENT CLAIM is included for a method for preparing a hydrocarbon product comprising: a) preparing ketene; b) dimerizing the ketene to diketene; c) hydrogenating the diketene to butyric acid; d) ketonizing the butyric acid to 4-heptanone; e) hydrogenating the 4-heptanone to 4-heptanol; f) dehydrating the 4-heptanol to 3-heptene; and g) hydrogenating the 3-heptene to the hydrocarbon product.
NOVELTY - Artificial enzyme comprises a core particle, and reactive components introduced to the core particle.    USE - The artificial enzyme is useful for hydrolytic degradation of biomass (claimed) preferably cellulose-based biomass.    ADVANTAGE - The enzyme does not induce environmental contamination during hydrolysis, reduces sensitivity of the enzyme to external conditional change, maintains long term activity, and performs hydrolysis of the biomass with increased efficiency in an economical manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a method for producing artificial enzyme comprising preparing a core particle, preparing a reactive component, and introducing the reactive component into the core particle; and    (2) hydrolytic degradation method of biomass.
NOVELTY - Use of an acidogenic leachate for soil washing, where acidogenic leachate is obtainable by incomplete decomposition of organic waste under anaerobic conditions, is claimed.    USE - Acidogenic leachate for soil washing, where the soil consists of predominantly fine particles, and leachate is different types of ordinary household waste, such as food waste, or organic material including sewage sludge, manure, or industrial waste such as wood waste or forest residues.    ADVANTAGE - The method enables soil washing in simple, easy and cost effective manner. The acidogenic leachate provides an acidic environment that reduces the valence of the arsenic ions, which makes it more soluble and forms complexes.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a plant for soil washing comprising a washing container for exposing contaminated soil to acidogenic leachate to produce washed soil and contaminated leachate, liquid providing unit arranged to provide a liquid to the washing container and first separating unit arranged to separate the contaminated acidogenic leachate from the washed soil    (2) a method for soil washing, which involves exposing contaminated soil to an acidogenic leachate for a first period of time to produce a suspension of leachate and washed soil, thus fatty acid molecules in the acidogenic leachate form complexes with contaminants in the soil, resulting in a contaminated leachate, and separating the soil from the contaminated leachate to produce washed soil.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a plant for soil washing.    Large open first container (11)    Soil (13)    Tap (15)    Second container (17)    Large sack (19)
NOVELTY - Separating an aqueous solution of glucan from an aqueous fermentation broth containing biomass and glucans in a filtration unit, comprises: (a) supplying a feed stream comprising the aqueous fermentation broth into the filtration device, (b) passing the feed stream through at least a symmetrical tubular membrane, which is of cylindrical design and has pores; and (c) withdrawing a permeate stream comprising the aqueous solution of glucans. The symmetrical tubular membrane has an inner diameter of 2-6 mm.    USE - The method is useful for separating an aqueous solution of glucan from an aqueous fermentation broth containing biomass and glucans (claimed).    ADVANTAGE - The method is simple and ensures improved cleaning efficiency.
NOVELTY - A system for generating power and recovering methane from methane hydrates comprises a low emissions power plant (102) to generate power, an exhaust gas from the low emissions power plant provides a gas mixture comprising nitrogen and carbon dioxide, and a methane recovery system (104) to recover methane from methane hydrates by injecting the nitrogen and the carbon dioxide from the gas mixture into the methane hydrates.    USE - System is used for generating power and recovering methane from methane hydrates (claimed).    ADVANTAGE - The system enables effective recovery of methane from methane hydrates.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for generating power and recovering methane from methane hydrates, which involves producing power via a low emissions power plant, and recovering methane from methane hydrates by injecting the nitrogen and the carbon dioxide from the gas mixture into the methane hydrates.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of system for generating power and recovering methane from methane hydrates.    Low emissions power plant (102)    Methane recovery system (104)    Methane hydrate formation (108)    Arrows (110)    Separation facility (114)
NOVELTY - The system (100) has a combined cycle power plant (106) for producing electricity (108). A dehydration system (116) dehydrates the gas mixture (110) of nitrogen and carbon dioxide (114) from the plant exhaust gas to generate a nitrogen refrigerant stream (120). A refrigeration system (122) generates LNG (126) from a natural gas stream (124) using the nitrogen refrigerant stream. Preferably, carbon dioxide is separated from the gas mixture through amine or potassium carbonate separation process.    USE - System for generating power and producing LNG.    ADVANTAGE - The gas mixture of exhaust gas from the power plant is dehydrated to remove sufficient water from the refrigerant stream so that ice or frost formation at cryogenic conditions in the refrigeration system is avoided. Low emissions power generation and LNG production can be combined in one system.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for generating power and producing LNG.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of a system for power generation and LNG production.    System for power generation and LNG production (100)    Power plant (106)    Electricity (108)    Gas mixture (110)    Carbon dioxide (114)    Dehydration system (116)    Nitrogen refrigerant stream (120)    Refrigeration system (122)    Natural gas stream (124)    LNG (126)
NOVELTY - Separating solids from liquids of slurry comprises saccharifying a biomass and applying the saccharified biomass to a surface (e.g., the outer portion) of a filter device.    USE - The method is used for separating solids from liquids of slurry (claimed). The method is used for processing biomass feedstocks (e.g., plant biomass, animal biomass, and municipal waste biomass) to produce useful products, such as fuels.
NOVELTY - Handling a material comprises conveying recalcitrance-reduced biomass along interior portions of a screw conveyor.    USE - The method is useful for handling a material such as biomass including lignocellulose material, wood, particle board, sawdust, agricultural waste, sewage, silage, grasses, rice hulls, bagasse, cotton, jute, hemp, flax, bamboo, sisal, abaca, straw, corn cobs, corn stover, switchgrass, alfalfa, hay, coconut hair, seaweed and/or algae (all claimed), where the material is useful as animal feed, biocompost materials, and for producing fuels.    ADVANTAGE - The method allows low electrical energy usage thus reducing the manufacturing cost and lowering greenhouse gas emissions.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for processing a material comprising providing a material to a first treatment cell equipped with a first electron beam device, irradiating the material with electron beams using the first electron beam device, and cooling and conveying the material with a screw conveyor from the first treatment cell.
NOVELTY - Method of upgrading process stream of biomass material, which involves removing undesired component from saccharified biomass liquid using simulated moving bed chromatography system.    USE - Method of upgrading process stream of biomass material e.g. plant biomass, animal biomass and municipal waste biomass used for producing intermediates and products e.g. energy, fuel, food and material. Uses include but are not limited to composite, filler, binder, plastic additive, adsorbent, and controlled release agent.    ADVANTAGE - The method enables efficient and economical upgrading process stream of biomass material having excellent impact resistance.
NOVELTY - Making a product involves producing one or more acids from saccharified biomass sugars; converting one or more acids into one or more esters; and hydrogenating one or more esters utilizing a catalyst and hydrogen to produce one or more products including alcohols; or making a product involves converting the product of the fermentation of a saccharified treated lignocellulosic material to an ester, and producing an alcohol by passing the ester over a first catalyst in the presence of hydrogen.    USE - The method is useful for making product (claimed), e.g. alcohols, acids, esters, and sugars.    ADVANTAGE - In the method, advantageously, no additional nutrients (other than a nitrogen source, e.g. urea or ammonia) are required during fermentation of corncobs or cellulosic or lignocellulosic materials containing significant amounts of corncobs. Mechanical feed preparation systems can be configured to produce streams with specific characteristics such as, for example, specific maximum sizes, specific length-to-width, or specific surface areas ratios. Physical preparation can increase the rate of reactions, improve the movement of material on a conveyor, improve the irradiation profile of the material, improve the radiation uniformity of the material, or reduce the processing time required by opening up the materials and making them more accessible to processes and/or reagents, such as reagents in a solution.
NOVELTY - Method for removing salts, preferably ionized acids or fully ionized acids from saccharified biomass liquids involves utilizing electrodialysis system.    USE - The method is useful for removing salts, preferably ionized acids or fully ionized acids from saccharified biomass liquids (claimed).
NOVELTY - The system (100) has an electrolytic unit whose cathode electrode (103) is coupled to a cathode screw at front end and anode electrode (104) coupled to an anode screw at front end. Cathode plate is provided with two holes. A large hole is aligned with and does not make electrical contact with anode spacer and cathode spacer. A diameter of large hole is greater than diameter of anode and cathode spacers. A small hole is aligned with cathode and anode inserts, so as to make electrical contact with cathode and anode inserts.    USE - System for electrolysis used to produce hydrogen based fuel.    ADVANTAGE - The same plate is used as neutral plate and anode plate and smaller number of custom portions are designed and built, so that the manufacturing cost is reduced and manufacturing process is simplified. The non-conducting screws and electrode buffer plate ensures that unwanted electrolysis is minimized or eliminated. The washer either stepped or flat is inserted to ensure desired separation between plates.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the system for electrolysis.    System for electrolysis (100)    Power source (102)    Cathode electrode (103)    Anode electrode (104)    Pump (108)
NOVELTY - Device comprises two compartments or superposed bins, separated by a grid (or screen) built for sorting fresh raw waste or during decomposition, compost fine particles, which are collected or stored in the second compartment or collection bin located below the first compartment.    USE - The device is useful for composting biodegradable components by fermentation (claimed).    ADVANTAGE - The device is capable of sorting waste in an automatic manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the use of the device for composting biodegradable components by fermentation, in which the wastes were stirred periodically by hand or using a utensil to obtain fine particles, which are transferred to the second compartment under mechanical effect.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a device for composting biodegradable components by fermentation.
NOVELTY - The process comprises: compressing a biogas from a fermenter; dividing the compressed biogas into two streams by a selective gas permeable membrane, where one of the streams contains higher proportion of methane, and the other stream comprises reduced proportion of methane; generating a pressure difference across the membrane; supplying a sufficient proportion of methane-containing gas stream as a product gas; continuously measuring the methane gas content in the product gas; and increasing the pressure difference across the membrane if the methane content falls below a predetermined value.    USE - The process is useful for recovering high purity methane from biogas (claimed).    ADVANTAGE - The process permanently maintains the quality of the product gas without any significant flow changes in the control process.    DETAILED DESCRIPTION - The process comprises: compressing a biogas from a fermenter; dividing the compressed biogas into two streams by a selective gas permeable membrane, where one of the streams contains a higher proportion of methane, and the other stream comprises a reduced proportion of methane; generating a pressure difference across the membrane; supplying a sufficient proportion of methane-containing gas stream as a product gas for further use; continuously measuring the methane gas content in the product gas; and increasing the pressure difference across the membrane if the methane content in the product gas falls below a predetermined value, such that a vacuum is created or an existing vacuum is increased on a low pressure side of the membrane. An INDEPENDENT CLAIM is included for a plant for recovering high-purity methane from biogas.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a plant for recovering high-purity methane from biogas.    First outlet line (3)    Compressor (9)    Vacuum pump (15)    First quality sensor (17)    First control unit. (26)
NOVELTY - Gas mixture containing components (A) and (B) is passed through separation membrane having feed side and permeate side. A driving force is provided for transmembrane permeation, in order to obtain permeate stream enriched in component (A) from permeate side, and residue stream depleted in component (A) from feed side. The separation membrane has a selective layer comprising copolymer with perfluorodioxolane monomer (a) (I), and perfluorodioxolane monomer (b).    USE - Separation of components of gas mixture used for recovering hydrogen from synthesis gas, for removing carbon dioxide from synthesis gas, for adjusting the ratio of hydrogen and carbon dioxide in synthesis gas, and for producing helium through gas extraction and purification.    ADVANTAGE - The method enables effective separation of gas mixture using the separation membrane containing copolymer with high gas selectivity.    DETAILED DESCRIPTION - Gas mixture containing components (A) and (B) is passed through separation membrane having feed side and permeate side. A driving force is provided for transmembrane permeation, in order to obtain permeate stream enriched in component (A) from permeate side, and residue stream depleted in component (A) from feed side. The separation membrane has a selective layer comprising copolymer with perfluorodioxolane monomer (a) of formula (I), and perfluorodioxolane monomer (b).
NOVELTY - The apparatus has extraction side slit (16) provided in circumferential direction to outer periphery of reaction container (10) in outlet side. An extraction side clamping unit (30) clamps outer periphery of container in position of extraction side slit by extraction side clamping element (31). A control unit (50) in clamping unit, controls bolting and release of clamping element and pressurizing particle raw material in container. The control unit releases clamping of outer periphery of container by clamping unit, when molding is extruded from outlet (15) of container.    USE - Molding apparatus for manufacturing molding e.g. biomass solid molding.    ADVANTAGE - The molding is easily extruded from the outlet of the container while pressurizing the particle raw material completely. The expansion of the molding in the reaction container is suppressed so that the deterioration in quality of the molding is prevented.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing method of molding.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of the molding apparatus. (Drawing includes non-English language text)    Reaction container (10)    Outlet (15)    Extraction side slit (16)    Extraction side clamping unit (30)    Extraction side clamping element (31)    Control unit (50)
NOVELTY - A methane fermentation system (1) consists of a methane fermentation equipment (2) having an acid production tank (4) for processing organic wastewater introduced by acid production microbe (a1), and producing acid, and a methane fermentation tank (5) for introducing treated water from the acid production tank, and methane-fermenting treated water, an aerobic-treatment tank (3) for accommodating and carrying out aerobic treatment of aerobic sludge containing acid production microbe (a2), and a line (L5) for supplying portion of aerobic sludge to acid production tank.    USE - System is used for methane fermentation method (claimed) for processing organic wastewater.    ADVANTAGE - The methane fermentation system has excellent removal rate of organic substance in organic wastewater, and methane fermentation efficiency.    DETAILED DESCRIPTION - A methane fermentation system consists of a methane fermentation equipment having an acid production tank for processing organic wastewater introduced by acid production microbe (a1), and producing acid, and a methane fermentation tank for introducing treated water from the acid production tank, and methane-fermenting treated water, an aerobic-treatment tank for accommodating and carrying out aerobic treatment of aerobic sludge containing acid production microbe (a2), and a line for supplying portion of aerobic sludge to acid production tank or its upstream from aerobic treatment tank. An INDEPENDENT CLAIM is included for methane fermentation method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of methane fermentation system. (Drawing includes non-English language text)    Methane fermentation system (1)    Methane fermentation equipment (2)    Aerobic-treatment tank (3)    Acid production tank (4)    Methane fermentation tank (5)    Line (L5)
NOVELTY - The system has recirculation line (44) that returns exhausted fuel in fuel gas discharge line to fuel gas supply line. A fuel flow volume controlling valve (52) adjusts flow volume of fuel gas passing through fuel gas supply line. A vapor flow amount control unit (63) outputs the valve-opening degree instruction to vapor flow amount controlling valve (58), to compensate for output timing of valve-opening degree instruction to fuel flow volume controlling valve based on electric-power-generation-amount instruction by fuel flow volume control unit (62).    USE - Fuel cell system.    ADVANTAGE - The amount of water vapor flow supplied to cell stack is increased, when the flow volume of fuel gas is increased, so that the responsiveness of increase in electric power generation amount is improved and the size reduction and simplification of fuel cell system are realized and fuel cost is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for control method of fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the fuel cell system. (Drawing includes non-English language text)    Recirculation line (44)    Fuel flow volume controlling valve (52)    Vapor flow amount controlling valve (58)    Fuel flow volume control unit (62)    Vapor flow amount control unit (63)
NOVELTY - A fuel cell apparatus comprises modifier (30) which modifies hydrogen-containing fuel which flows in from an inflow port and generates a hydrogen enrichment fuel, fuel cell which produces electric power by arranging under modifier and making the hydrogen enrichment fuel and oxidizing agent react, off gas combustion part which burns off gas emitted from upper end part of fuel cells and maintains fuel cells in high temperature state, and waste gas flow path which discharges generated waste gas that flows along wall surface of modifier.    USE - A fuel cell apparatus (claimed).    ADVANTAGE - Temperature distribution of the modifier is equalized.    DETAILED DESCRIPTION - A fuel cell apparatus comprises modifier (30) which modifies hydrogen-containing fuel which flows in from an inflow port and generates a hydrogen enrichment fuel, fuel cell which produces electric power by arranging under modifier and making the hydrogen enrichment fuel and oxidizing agent react, off gas combustion part which burns off gas emitted from upper end part of fuel cells and maintains fuel cells in high temperature state, and waste gas flow path which discharges generated waste gas that flows along wall surface of modifier and makes flow volume of waste gas that flows along wall surface of 1st part which is inflow port (37) side part of modifier may be increased compared with flow volume of waste gas which flows along the wall surface of 2nd part which are parts other than inflow port side part.    DESCRIPTION OF DRAWING(S) - The drawing shows a plane cross-sectional view of the fuel cell apparatus. (Drawing includes non-English language text).    Modifier (30)    Left side casing (31)    Vaporization part (35)    Modification part (36)    Inflow port (37)
NOVELTY - The apparatus has pre-processor (100) that removes foreign substance from sewage. Recess tag (200) sediments the pre-processed sewage. Flux control unit (300) transfers the pre-processed sewage to microorganism aeration processing unit (400) used to remove the organic material in sewage processed at recess tag using microorganism. Solid-liquid division unit (500) separates solid and liquid substances from sewage processed at microorganism aeration processing unit. Sterilization process unit (600) performs the final disinfection of solid/liquid substances separated sewage.    USE - Sewage disposal apparatus for use in ship and fish farm.    ADVANTAGE - The simple and compact structured sewage disposal apparatus used in ship and fish farm is capable of effectively processing high concentration excrements and sewage.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the sewage disposal apparatus used in ship and fish farm. (Drawing includes non-English language text)    Pre-processor (100)    Recess tag (200)    Flux control unit (300)    Microorganism aeration processing unit (400)    Solid-liquid division unit (500)    Sterilization process unit (600)
NOVELTY - Preparing a fuel comprises mixing food waste with water, removing moisture content and foreign substance from the mixture, adding sawdust and supplementary material including rice hulls and straw in the mixture and then drying, molding the dried mixture by pressing in a molder to a fixed size, fermenting the molded mixture for 1-3 weeks, adding small quantity of microbial enzyme in the mixture, and artificially drying or naturally drying the mixture in a drying room at a room temperature and then packaging.    USE - The method is useful for preparing a fuel (claimed).    ADVANTAGE - The method is capable of economically, simply and conveniently preparing the fuel.
NOVELTY - The method involves processing food waste by shredding, fermenting, evaporating, molding and mixing with other substances to obtain high value food refuse derived fuel (FRDF).    USE - FRDF producing method.    ADVANTAGE - The method enables ensuring that FRDF has intrinsic characteristics of solid state, unique dimension and homogeneous content, so that the FRDF is easy to be stored or transported with high efficiency and low pollution rate.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic illustration of a food waste.
NOVELTY - A manure utilizing method involves adding manure from mink farm with 15-30 wt.% straw cereals and/or Miscanthus straw and 10-20 wt.% mineral fertilizer to obtain mixture. The mixture arranged in a prism is aerated or loosely arranged to provide a volume of air in piles by periodic stirring. The prism is sprayed, followed by carrying out composting process at less than 70 degrees C for 2-3 months.    USE - Method for utilizing manure from mink farm.
NOVELTY - NOVELTY -Marsh gas anaerobic fermentation producing organic fertilizer system, comprise sequentially connecting a sewage tank, fermenting excrement preprocessing tank, solar energy water heater, a controllable container fermentation room, a discharging tank, a sedimentation tank, a rough, a stir mix device, secondary filtration, drying, moulding and granulating device and packaging machine, controllable fermentation room container set with a water inlet, a gas exit, and exit and liquid return port. The utility model is new type has reasonable design, simple structure, good sealing property, a for excrement sewage in anaerobic fermentation process stir uniform, which helps to increase efficiency and anaerobic fermentation marsh gas yield, the biogas residue and a series of processing, finally preparing into organic fertilizer, strong practicability and easy popularization and application.
NOVELTY - A 3-(3-amidofurazan-4-yl)-4-hydroxy-1-oxo-2,4-diazaspiro-2-alkene compound is synthesized by stirring and reacting 3-amino-4-gem-dihydroxyimino furazan and organic solvent at 20-25 degrees C in reaction container, adding cyclohexanone, tetrahydropyranone, tetrahydrothiophene-3-one, or 4-acetamido cyclohexanone, stirring and reacting at 0-40 degrees C, for 30 minutes to 12 hours, evaporating organic solvent to obtain product, and purifying by column chromatography in which molar ratio 3-amino-4-gem-dihydroxyimino furazan:cyclic ketone is 1:1-5, and organic solvent is methanol, ethanol, or acetonitrile.    USE - Synthesis process of 3-(3-amidofurazan-4-yl)-4-hydroxy-1-oxo-2,4-diazaspiro-2-alkene compound (claimed).    ADVANTAGE - The process is safe and environment-friendly, has high yield and low temperature condition, does not need catalyst, and generates only water.    DETAILED DESCRIPTION - A 3-(3-amidofurazan-4-yl)-4-hydroxy-1-oxo-2,4-diazaspiro-2-alkene compound of formula (I) is synthesized by stirring and reacting 3-amino-4-gem-dihydroxyimino furazan of formula (II) and organic solvent at 20-25 degrees C in reaction container, adding cyclohexanone, tetrahydropyranone, tetrahydrothiophene-3-one, or 4-acetamido cyclohexanone, stirring and reacting at 0-40 degrees C, for 30 minutes to 12 hours, evaporating organic solvent to obtain product, and purifying by column chromatography in which molar ratio 3-amino-4-gem-dihydroxyimino furazan:cyclic ketone is 1:1-5, and organic solvent is methanol, ethanol, or acetonitrile..
NOVELTY - Tenofovir derivative preparation involves reacting (((1-(6-amino-9H-purin-9-yl)propan-2-yl)oxy)methyl)phosphonic acid or (((1-(6-amino-9H-purin-9-yl)propan-2-yl)oxy)methyl)propan-2-yloxy phosphinic acid with L-CH2OC(O)OCH(CH3)2 (III) in presence of phase transfer catalyst in an organic solvent. The reaction is accomplished at 30-90 degrees C for 1-12 hours in presence of organic alkali.    USE - Method for preparing tenofovir (claimed).    ADVANTAGE - The method prepares tenofovir in a simple, eco-friendly and cost-effective manner by using cheap raw material under mild reaction conditions, and produces high yield and high purity.    DETAILED DESCRIPTION - Tenofovir derivative preparation involves reacting (((1-(6-amino-9H-purin-9-yl)propan-2-yl)oxy)methyl)phosphonic acid or (((1-(6-amino-9H-purin-9-yl)propan-2-yl)oxy)methyl)propan-2-yloxy phosphinic acid with L-CH2OC(O)OCH(CH3)2 of formula (III) in presence of phase transfer catalyst in an organic solvent. The reaction is accomplished at 30-90 degrees C for 1-12 hours in presence of organic alkali.    L=halogen.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic nuclear magnetic resonance of the tenofovir.
NOVELTY - An organoborane reagent is reacted with a pyrimidine compound (II) or its salt and intramolecular cyclization is induced in the reaction product using a zero-valent palladium catalyst in presence of an alkali metal hydroxide, to obtain tricyclic compound (I).    USE - Manufacture of tricyclic compound used as intermediate for preparing pharmaceutical products.    ADVANTAGE - The method efficiently and economically provides tricyclic compound with high yield with reduced byproduct generation.    DETAILED DESCRIPTION - An organoborane reagent is reacted with a pyrimidine compound of formula (II) or its salt and intramolecular cyclization is induced in the reaction product using a zero-valent palladium catalyst in presence of an alkali metal hydroxide, to obtain tricyclic compound of formula (I).    m=0-2;    n=0 or more;    m+n=0-3;    X=halo;    R1=H or functional group;    at least one of R2 and R2'=lower alkylsilyl, lower alkyl-diphenylsilyl, lower-alkyl lower-alkoxy phenylsilyl or hydroxy protected by protecting group chosen from lower alkoxy diphenylsilyl, amino group or 1-6C alkylamino group protected by optionally substituted alkyloxycarbonyl, aralkyl, benzyloxymethyl, benzylthiomethyl, lower-alkoxycarbonyl, 2,2,2- trichloroethoxycarbonyl or thiol group protected by protecting groups chosen from 9-fluorenyl methoxycarbonyl, tert-butyl sulfanil group, or 3-nitro-2-pyridine sulfenyl group, and other is H;and    R3=optionally substituted amino group.    An INDEPENDENT CLAIM is included for tricyclic compound of formula (I').    R3=optionally substituted amino group;and    at least one of R6 and R6'=amino group or 1-6C alkylamino group protected by optionally substituted alkyloxycarbonyl and other is H.
NOVELTY - Method for recovering energy from plant biomass, involves crushing the plant biomass to elute carbohydrate, lipid and protein, producing hydrogen and ethanol by inoculating yeast or bacterial strain in carbohydrate component and performing anaerobic fermentation, preprocessing protein component with enzyme or acid, producing bioalcohol from preprocessed protein component using yeast or bacteria, dehydrating the remaining biomass, and extracting lipids from the dehydrated biomass and separating fatty acid methyl ester (FAME).    USE - The method, system or apparatus is useful for recovering energy chosen from bioalcohol (e.g. butanol, propanol or ethanol), hydrogen and FAME from plant biomass, preferably aquatic plant or microalgae (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) system for recovering energy using the plant biomass; and    (2) energy recovering apparatus.
NOVELTY - A baicalein nicotinamide cocrystal is prepared by mixing baicalein and nicotinamide at 1:1 molar ratio, and ball milling at rate of 200-700 revolutions per minute for 1-5 hours; where it exhibits an X-ray powder diffraction pattern with peaks given in the specification.    USE - Method for preparing baicalein nicotinamide cocrystal (claimed).    ADVANTAGE - The method is simple, low-cost, high product yield and environment-friendly.
NOVELTY - The present invention provides an improved and highly efficient catalyst-free process for the synthesis of secondary or tertiary by direct one-pot reductive amination of aryl/hereroaryl/alicyclic aldehydes and cyclic ketones with aryl/heteroaryl amines using hantzsch ester as reducing agent in presence of suitable solvent particularly fluorous alcohols.
NOVELTY - The disposal apparatus has sealing element (376) that prevents outflow of microorganism. A mobile tool moves an inhaled microorganism to grinding portion. A microorganism feeding unit (270) includes microorganism storage tank (272), injector (274) and supply control unit (276) that is provided for controlling injector. A gap between a feeding unit (370) and injector is sealed hermetically. A delivery hose (372) is provided for supplying microorganism supplied from injector to grinding portion. A connection plunger is provided for connecting delivery hose and grinding portion.    USE - Apparatus for disposing food garbage generated in home and dining room.    ADVANTAGE - The crushing and process efficiency of the food waste is improved. The water pollution due to indiscriminate exhaustion of the food waste and the environmental contamination is prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the food garbage disposal apparatus.    Microorganism feeding unit (270)    Microorganism storage tank (272)    Injector (274)    Supply control unit (276)    Feeding unit (370)    Delivery hose (372)    Sealing element (376)
NOVELTY - Increasing lipid accumulation in Pulcherrima cells by culturing a yeast in a culture medium under conditions suitable for promoting production of Pulcherrima cells and inhibiting sporulation, is claimed.    USE - The method is useful for increasing lipid accumulation in Pulcherrima cells; for producing oleaginous biomass, which is used to produce a fuel, fuel substitute, base for cosmetics, plastic or animal feed (all claimed), where the lipid is extracted as oil from the cells, and the oil is useful as biodiesel.    ADVANTAGE - The method: cultures the yeast in a substantially open reactor comprising an open raceway pond; utilizes unsterilized culture medium (claimed); blocks sporulation, thus triggering vegetative Pulcherrima cells to accumulate oil and form oil-rich cells at high cell density; provides increased production of Pulcherrima cells and an accumulation of lipid in the cells; provides oil using inexpensive non-sterile conditions; performs the second step following depletion of nitrogen and/or sulfur from the culture medium to a level at which normal growth of the yeast is not sustained; provides oil that has a dynamic viscosity of 0.58 Pas measured at 40 degrees C, and an energy density of 27.33 MJ/kg; and utilizes Pulcherrima cells that demonstrate good flexibility on being cultured with different types and amounts of nitrogen, sulfur and micronutrients.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for: (1) an oil comprising a lipid profile comprising 0-50% sterol, 50-100% glyceride and 0-10% free fatty acids; (2) a fuel, fuel substitute, base for cosmetics, animal feed or plastic comprising the oil; (3) use of Pulcherrima cells for production of oleaginous biomass; (4) a yeast culture comprising Pulcherrima cells at greater than 0.1 wt/vol.%; and (5) a Pulcherrima cell comprising lipid at 25-80 wt/vol.%.
NOVELTY - Preparing an alkyl acetoacetate compound (VI), comprises adding carbon dioxide to a enolate salt of alkyl acetoacetate compound (V) in water to provide carbonic acid in situ and acidifying (V).    USE - The process is useful for preparing (VI), which is useful for preparing (I) (all claimed), preferably ethyl 3-difluoromethyl-1-methyl-1H-pyrazole-4-carboxylic acid ester used for producing fungicides.    ADVANTAGE - The process ensures that (VI) prepares (I) with high yield and purity and reduced amount of chemical waste and without using strong acid and requiring specially equipped manufacturing facilities or special corrosion resistant reaction apparatus in an economical and eco-friendly manner.    DETAILED DESCRIPTION - Preparing an alkyl acetoacetate compound of formula (VI), comprises adding carbon dioxide to an enolate salt of alkyl acetoacetate compound of formula (V) in water to provide carbonic acid in situ and acidifying (V).    M = sodium (preferred), potassium or lithium;    R1 = 1-6C-alkyl, preferably ethyl; and    R2 = CF2H, CF3 (both preferred), CFH2, CCl2H, CClH2 or CCl3.
NOVELTY - Manufacturing biodiesel comprises adding biodiesel feedstock and catalyst into a chamber through a feed pump and then performing primary transesterification process by an ultrasonic waves having fixed flow rate generated by an ultrasonic reactor to obtain a primary reaction product, transferring the primary product into a microwave reactor through a primary product storage tank and then performing secondary transesterification process on the primary reaction product using microwaves generated by a magnetron, and passing the secondary product into a vessel to separate biodiesel and glycerin.    USE - The method is useful for manufacturing biodiesel (claimed).    ADVANTAGE - The method is capable of rapidly manufacturing the biodiesel with reduced amount of catalyst and high quality in an environmentally friendly manner.
NOVELTY - The method involves utilizing principle of a solar energy source that is most commonly used resource in thermal conversion processes. The used biomass is driven by reducing greenhouse gas emissions and waste agricultural products.    USE - Method for producing bio-oil, biofuel, biogas and coal.    ADVANTAGE - The method provides renewable sources, and reduces emissions of sulfur and carbon dioxide gases with an attractive option from an ecological point of view as a fuel for power generation.
NOVELTY - An apparatus for production of gasified vapor powder of solid fuel; the apparatus comprising; a stainless steel retort (22) connected to a muffled furnace (23) at one end and a cooling frame network (31) at the other end; an inner surface of said retort lined with metal ore (26) and an outer surface of said retort enclosed with asbestos rope layers (27); an inner surface of said furnace wound around the nichrome element network (25) which is closely connected to the retort (22) and outer surface of the furnace enclosed with glass wool stuffing (24); said retort provided with a lid (28) at top of the furnace and an inlet (29) having co-axial non-returnable valve near to the cooling frame network (31); said framework (31) provided an inlet pipe (30) at one end which is connected to the retort (22) and outlet pipe (32) at the other end to receive the atomized solid fuel.
NOVELTY - An apparatus to cure plural thermal pulverization for bulk manufacturing of solid hydrogen fuel; the said apparatus (55) comprising: a stainless steel vessel (56) packed in the muffle (57) comprising a cement coated nichrome element (58) and a shallow tube (59) for thermocouple; said tube connected to a digital thermal controller (60); said vessel provided with valve (61) and an inlet for nitrogen gas (62) at top and a butterfly valve (63) at bottom connected to a blender pulverising machine (64) which is further connected to motor (65) through belt driver (66); said blender pulverizing machine provided with cutting blades (67) uniformely located on a shaft (68) and a outlet (69) for removal of solid fuel.
NOVELTY - A waste converting machine for converting waste into manure comprising motor, Rolling blades, cutting blades, handle, Trolley, Belt, Gear Box, Drum and opening lid. The product is capable of processing all type of wet or dry food waste in huge quantities. The product is capable to avoid harmful items like glass, plastic or paper while processing waste. The product is eco friendly which can work continuously for long hours.
NOVELTY - Preparation of rapeseed biodiesel involves crushing rapeseed using mill to particle size of 30 mesh, 60 mesh, 100 mesh and 120 mesh, extracting the rapeseed using Soxhlet extraction method at 50-70 degrees C for 2-8 hours, adding methanol in amount of 3-6 times of obtained rapeseed oil in container, then adding catalyst in amount of 0.5-1 %mass of rapeseed oil, heating at 60-65 degrees C for 3-5 hours under stirring, processing obtained liquid at 55 degrees C in vacuum rotary evaporator, centrifuging resultant liquid, washing obtained product using distilled water and separating.    USE - Preparation of rapeseed biodiesel (claimed).    ADVANTAGE - The biodiesel is economically prepared by simple method.    DETAILED DESCRIPTION - Preparation of rapeseed biodiesel involves crushing rapeseed using mill to particle size of 30 mesh, 60 mesh, 100 mesh and 120 mesh, extracting the rapeseed using Soxhlet extraction method at 50-70 degrees C for 2-8 hours, adding methanol in amount of 3-6 times of obtained rapeseed oil in container, then adding catalyst in amount of 0.5-1 %mass of rapeseed oil, heating at 60-65 degrees C for 3-5 hours under stirring, processing obtained liquid at 55 degrees C in vacuum rotary evaporator, centrifuging resultant liquid with rotating speed for 2000-3000 rpm for 10 minutes, washing obtained product using distilled water and separating using separating funnel.
NOVELTY - Treatment of dry gas from oil refinery comprises catalytically oxidizing refinery dry gas in the presence of catalyst; introducing in waste heat boiler; switching valve, catalytically oxidizing dry gas in the presence of catalyst, cooling exhaust gas in second step, and reintroducing to waste heat boiler; switching gas line, introducing into first catalytic oxidation reactor, switching valve, cutting off low temperature waste heat boiler exhaust, introducing into second catalytic oxidation reactor, catalytically oxidizing, cooling, and recovery heat; and repeating first to fourth steps.    USE - Method for treating dry gas from oil refinery (claimed).    DETAILED DESCRIPTION - Treatment of dry gas from oil refinery comprises catalytically oxidizing refinery dry gas in the presence of catalyst; introducing in waste heat boiler for recycling energy; switching valve when temperature in first catalytic oxidation reactor is higher than 700 degrees C, catalytically oxidizing dry gas in the presence of catalyst, cooling exhaust gas in second step, and reintroducing to waste heat boiler; switching gas line when temperature in second catalytic oxidation reactor is greater than 700 degrees C, introducing into first catalytic oxidation reactor, switching valve, cutting off low temperature waste heat boiler exhaust, introducing into second catalytic oxidation reactor, catalytically oxidizing, cooling, and recovery heat; and repeating first to fourth steps.
NOVELTY - A straw biogas fermentation system has double-layer cylindrical structure fermentation tank provided with feeding pipe and gas pipe (3) at top part and slag discharging port (4), outer wall at outer layer, uniformly distributed drainage holes at inner surface, cylindrical separator which is located coaxial to outer wall and is connected to fermentation tank top and lower end which is provided with bottom plate. Bottom plate and concave arc plate-like member separator provided with drainage holes are connected to slag discharging port lower end at certain inclination.    USE - A straw biogas fermentation system (claimed).    ADVANTAGE - The fermentation system prevents caking and agglomeration, improves contact of materials, has high fermentation efficiency, and is low cost and convenient to operate.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of straw biogas fermentation system.    Gas pipe (3)    Slag discharging port (4)    Sealing cover (12)    Ring snap element (14)    Stopper (15)
NOVELTY - A straw composting agent comprises peat and microbial flora-containing active component in which active component is Bacillus, nutrient, or spore, and microbial flora is Trichoderma harzianum, Bacillus subtilis, Saccharomyces cerevisia, and Metarrhizium anisoplia, and content of microbial flora is 0.5-500000000/peat.    USE - A straw composting agent (claimed).    ADVANTAGE - Straw composting agent inhibits growth and propagation of diseases, and improves physical and chemical properties of soil to promote crop growth, quality, and stress resistance, and increase crop yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of straw composting agent which involves activating T. harzianum strain in shake flask culture, culturing in seed tank and fermenting to obtain T. harzianum fermentation liquid, activating B. subtilis strain in shake flask culture, culturing in seed tank and fermenting to obtain B. subtilis fermentation liquid, activating S. cerevisia strain in shake flask culture, culturing in seed tank and fermenting to obtain S. cerevisia fermentation liquid, activating M. anisoplia strain in shake flask culture, culturing in seed tank and fermenting to obtain M. anisoplia fermentation liquid, mixing T. harzianum, B. subtilis, S. cerevisia, and M. anisoplia fermentation liquid to obtain mixed bacteria liquid, mixing with peat, and crushing.    DESCRIPTION OF DRAWING(S) - The drawing shows a process flow chart of manufacturing straw composting agent. (Drawing includes non-English language text).
NOVELTY - Geobacillus kaustophilus strain NJRC-14 preserved under number of CGMCC No. 8422, is new.    USE - The Geobacillus kaustophilus strain NJRC-14 is useful in a microbial organic fertilizer for preventing continuous cropping soil blight disease caused by bacteria (claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) use of Geobacillus kaustophilus strain NJRC-14 in a microbial organic fertilizer for preventing continuous cropping soil blight disease; and (2) preparing microbial organic fertilizer comprising (a) selecting Geobacillus kaustophilus strain NJRC-14, inoculating into a potato-dextrose agar (PDA) culture liquid, fermenting at 30-50 degrees C under natural pH growth range and stirring speed of 180-300 revolutions per minute to carry out an anaphase in spore form, where the amount of spore is more than 1x 1010/ml, and (b) selecting PDA solid fermentation as organic carrier material and Geobacillus kaustophilus strain NJRC-14, adding 10-20 l of bacterial antagonistic liquid into 1 ton of the PDA solid fermentation, fermenting at 30-50 degrees C, where the antagonistic bacteria is more than 5x 108/g, and then fermenting under low condition at temperature of not more than 60 degrees C for water evaporation to below 30% and packaging.
NOVELTY - A one new type multifunctional machine, it relates to the field of medical device technology field, it further comprises exhaust gas processing device, a waste gas discharging device, a damping device and anaesthetic depth monitoring device, an emergency breathing device, disk, the bottom of transparent cover, set with rack wheel, cabinet is set on the machine frame upper, connecting device of upper cabinet set with control device, and the control cabinet is set with sterilizing disk, upper disk and set with transparent cover, upper control device set with anaesthetic depth monitoring device, waste gas processing device to an emergency breathing device are connected with a connecting device, a waste gas discharging device and the waste processing device connecting pneuma, a damping device is set on the cabinet and the machine frame. Function, it can treat waste anesthetic gas, reduces the environment pollution, at the same time, improves the accuracy of anesthetic dosage, convenient taking smoothly and improves the efficiency of operation.
NOVELTY - The present invention illustrates a method for an odour-free process for handling of organic solid wastes for biomethanation and simultaneous production of bio-fuel/ manure. It includes a novel concept for converting organic solid wastes into biogas using a combination of mechanical and biological methods by maintaining an odour free environment throughout. The first phase involves mechanical pre-treatment of the waste to produce organic rich leachate. The solid residues generated after extraction of the leachate by mechanical treatment are converted into solid bio-fuel (briquettes) /good quality manure. The second phase includes a biological conversion of the leachate to biogas by using a hybrid anaerobic reactor operating at an ambient temperature of 30 +/- 5 degree C. The effluent from the reactor is used as a soil conditioner. The biogas produced from the leachate can be used for thermal applications or electricity generation and the sludge from the bottom of the reactor can be used as manure after composting.
NOVELTY - Straw decomposition agent (I) comprises Arthrobacter YO-H strain under an accession No. CGMCC No.4119.    USE - The agent is useful for decomposing the straw at low temperature (claimed).    ADVANTAGE - The agent rapidly decomposes straw at low temperature, improves decomposing cellulase activity and the rotten time of 3-4 days.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing (I) comprising culturing Arthrobacter YO-H strain, Bacillus subtilis, Saccharomyces cerevisiae, Aspergillus niger and Trichoderma with a concentration of 108/ml, according to the volume ratio of 1:1:1:2:2 and then mixing to obtain the mixed bacteria liquid, inoculating mixed bacteria liquid and culture of wheat bran in a ratio of 1:10 and then culturing for 10 days, where the moisture content of wheat bran is 50%, then drying wheat bran until the moisture content is less than 25%, adding 1-1.5% of cellulose into wheat bran and uniformly mixing.
NOVELTY - Pseudomonas fluorescens KY-03 (I) under a preservation number CGMCC No.8525, is new.    USE - (I) is useful for degrading complex of organic matter and anaerobic digestion reaction (all claimed) in industrial waste water biological processing.    ADVANTAGE - (I) does not influences the upper anaerobic digestion reaction system of stability, improves the efficiency of sludge organic matter decomposition rate of anaerobic biogas, has low cost and no secondary pollution, and is convenient to culture.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for use of (I) for anaerobic digestion reaction, where the application method comprises inoculating (I) in enrichment medium, then shaking to the logarithmic growth phase at 30 degrees C, where the bacteria concentration is 106-1010 colony forming unit/ml, centrifuging broth supernatant, measuring catabolic ability of the supernatant for cellulose decomposition of organic matter by 3,5-dinitrosalicylic acid reducing sugar colorimetric method national standard GB/T 23881-2009, inoculating 0.1-0.5% of the inoculum into anaerobic digestion reaction system for anaerobic digestion reaction.
NOVELTY - A (R)-(3,5-bis(trifluoromethyl)phenyl)ethanol using ionic liquid-containing reaction system is prepared by using Trichoderma strain ZJPH0810 fermentation culture wet mycelium as catalyst, 3,5-bis(trifluoromethyl) acetophenone as substrate, amino acid ionic liquid containing substituted quat.-ammonium salt cation and natural amino acid anion, and buffer liquid with pH of 5.5-8 which constitute reaction system, reacting at 25-45 degrees C for 6-50 hours with 100-300 rpm rotation speed, extracting reaction liquid using same volume of n-hexane, and separating and purifying extraction liquid.    USE - Preparation of (R)-(3,5-bis(trifluoromethyl)phenyl)ethanol using ionic liquid-containing reaction system for aprepitant drug chiral intermediate.    ADVANTAGE - Preparation method is environment-friendly, has high yield, improves reaction efficiency, and uses amino acid ionic liquid which is non-toxic, renewable, and biodegradable, and promotes coenzyme regeneration.    DETAILED DESCRIPTION - A (R)-(3,5-bis(trifluoromethyl)phenyl)ethanol using ionic liquid-containing reaction system is prepared by using Trichoderma strain ZJPH0810 fermentation culture wet mycelium as catalyst, 3,5-bis(trifluoromethyl) acetophenone as substrate, amino acid ionic liquid containing substituted quat.-ammonium salt cation and natural amino acid anion of formula (I), and buffer liquid with pH of 5.5-8 which constitute reaction system, reacting at 25-45 degrees C for 6-50 hours with 100-300 rpm rotation speed, extracting reaction liquid using same volume of n-hexane, and separating and purifying extraction liquid in which reaction system wet mycelium adding amount based on mycelium dry weight is 10-50 g/L, reaction system initial substrate concentration is 20-200 mM, and reaction system amino acid ionic liquid concentration is 0.1-30 mass%.    R1, R2, R3, R4=1-4C alkyl.
NOVELTY - The present disclosure relates to a process for the preparation of a compound represented by formula I, said process comprising oxidizing a compound of formula II, in a medium comprising at least one oxidizing agent and a solvent system comprising at least one solvent selected from the group consisting of methanesulfonic acid, triflic acid, tetrachlorobutyric acid, ethylenedichloride, methylenedichloride, trifluoroacetic acid, trichloroacetic acid and tribromoacetic acid at a temperature ranging between 0 degree C and 50 degree C, preferably between 0 degree C and 30 degree C.The medium may optionally includeat least one corrosion inhibiting agent.
NOVELTY - Ibuprofen and 2-(hydroxymethyl)pyridine are reacted in presence of a condensing agent and a catalyst to obtain ibuprofen piconol.    USE - Preparation of ibuprofen piconol (claimed).    ADVANTAGE - The method economically and safely provides ibuprofen piconol without using thionyl chloride and other toxic reagent, without affecting the environment.
NOVELTY - This utility new type provide the one a garbage processing system, belonging to the field of environmental protection, comprising a destructive distillation cracking system and oil product purifying sub-system, destructive distillation cracking system comprises a connecting of dry distillation device, first hot exchange device, a sub-oil product purifying system comprises a connecting of the mixed crude oil storing device, a rectifying device, a first hot exchange device and a mixed oil storage device connect. Garbage through distillation, produce gas and solid, the gas purification, can obtain for oil resource of industrial application, using such a technical solution for garbage treatment process and recovered resource rear processing, which can greatly relieve the pollution of environment, at the same time, for the resource and obtain of, relieving petroleum shortage can be up to a certain degree of.
NOVELTY - This utility new type for large biomass gasification furnace in the operation process, ash is not uniformity of atomized water, provide the one comprises a biomass gasification furnace can realize uniformity ash gasification furnace of atomizing device, wherein said atomizing device comprises an atomizing water pump and atomization pipeline, wherein said atomizing pipeline of main pipe and the atomizing water in said gasification furnace is divided atomizing annular tube and atomizing folded tube, and a water pump and the water pipe, wherein said annular atomizing tube distance a grate 5 to 10 cm and the said ash chamber is parallel to the fire grate, and the radius is 1/2 bar; a atomizing folded tube is divided into a horizontal section and vertical section and the horizontal section on the distance a atomizing annular tube 5 to 10 cm into said ash chamber and a fire grate, parallel to the vertical ash along the center axis extends downwardly until the bottom distance a furnace bottom slag is 10 to 15 cm.
NOVELTY - Producing calcium-magnesium fertilizer in iron smelting blast furnace involves calculating the reduction amount and recovery rate of nickel iron during preparation of phosphorus ore pellet containing nickel, manganese and iron. Calcining operation of phosphate ore pellet is performed in ore calcining kiln, with air flow set to not less than 170 cubic meter per minute. The roasting temperature of phosphate ore pellet is controlled at 800 to 1000 degrees Celsius for 14 to 20 minutes. The phosphate ore pellet is quickly cooled by setting the ore calcining kiln at specific humidity using high pressure humidifying device.    USE - Used for producing calcium-magnesium fertilizer in iron smelting blast furnace (claimed).    ADVANTAGE - Calcium-magnesium fertilizer is obtained in the blast furnace with increased coal gas combustion efficiency and gas purification efficiency, at low cost. Improves product yield of calcium-magnesium fertilizer produced without creating waste residue which can pollute the environment.    DESCRIPTION OF DRAWING(S) - The drawing shows the flow block diagram of the smelting process in furnace. (Drawing includes non-English language text).
NOVELTY - Synthesis of carfilzomib involves condensing carboxyl group-containing compound (I) and amine derivative (II) and carrying out decarboxylation of protecting group to obtain morpholine derivative (V), then condensing amine derivative (III) and tert-butyl carbamate derivative (IV) and deprotecting amino group to obtain amine derivative (VI), then condensing compound (V) and compound (VI) and carrying out decarboxylation of protecting group to obtain morpholine derivative (VII), and condensing compound (VII) and oxirane derivative (VIII).    USE - Synthesis of carfilzomib (claimed).    ADVANTAGE - The method enables synthesis of carfilzomib with high yield, by simple and environmentally-friendly process.    DETAILED DESCRIPTION - Synthesis of carfilzomib involves condensing carboxyl group-containing compound of formula (I)(Sic) and amine derivative of formula (II) using condensing agent (C1) in presence of organic solvent (S1) and organic base (B1) and carrying out decarboxylation of protecting group to obtain morpholine derivative of formula (V), then condensing amine derivative of formula (III) and tert-butyl carbamate derivative of formula (IV) using condensing agent (C2) in presence of organic solvent (S2) and organic base (B2) and deprotecting amino group to obtain amine derivative of formula (VI), then condensing compound (V) and compound (VI) using condensing agent (C3) in presence of organic solvent (S3) and organic base (B3) and carrying out decarboxylation of protecting group to obtain morpholine derivative of formula (VII), and condensing compound (VII) and oxirane derivative of formula (VIII).    R, R1=primary group of hydrochloride, sulfate, acetate, citrate, nitrate, benzenesulfonate or p-toluene sulfonate, in which primary group is 1-5C linear or branched chain group.
NOVELTY - The present invention relates to an economical, environment friendly and industrially feasible process for preparation of highly pure CDP-choline and its pharmaceutically acceptable alkali metal salts. More particularly, the present invention relates to process for preparation of highly pure monosodium salt of CDP-choline comprising steps of reacting cytidine-5 -monophosphate with morphol ine in presence of dicyclohexylcarbodiimide in methanol to obtain cytidine 5-monophosphate morpholidate; condensing cytidine 5- monophosphate morpholidate with phosphorylcholine chloride calcium salt in presence of hydrochloric acid followed by addition of anti-solvent to precipitate crude CDP-choline; purifying crude CDP-choline using-ion-exchange resin and eluting fractions of CDPcholine with acidic solution; concentrating the eluted fractions using nanofilteration technology; charcoalizing the concentrated solution of CDP-choline; converting CDP-choline to monosodium salt of CDP-choline, isolating monosodium salt of CDP-choline and purifying it with methanol.
NOVELTY - A single pyrolysis gasification loop (100) comprises reactor auger (102) operatively connected to biomass inlet (106) and/or vapor outlet (108) and return auger (104). Reactor auger and return auger are operatively connected by reactor outlet (110) and/or return outlet (112). Reactor auger is operated to advance biomass material to return auger via reactor outlet. Return auger is operated to advance biomass material to reactor auger via return outlet. Reactor auger is operated to pyrolyze biomass material.    USE - A single pyrolysis gasification loop for pyrolyzing biomass material, gasifying char material (all claimed), and producing low oxygen biological oil or syngas.    ADVANTAGE - The single pyrolysis gasification loop has compact structure and minimal parasitic loss and may not require fluidization gas, associated auxiliary equipment required for conventional thermochemical conversion technologies, and separate continuous heating system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the single pyrolysis gasification loop operating in pyrolysis mode.    Single pyrolysis gasification loop (100)    Reactor auger (102)    Return auger (104)    Biomass inlet (106)    Vapor outlet (108)    Reactor outlet (110)    Return outlet (112)
NOVELTY - Biomass thermal conversion system comprises fixed bed drying zone, fixed bed pyrolysis zone fluidly connected to drying zone, combustion zone fluidly connected to the pyrolysis zone by a material path, and comminution mechanism arranged across the material path between the pyrolysis zone and the combustion zone, configured to grind char off a pyrolyzed surface of solid biomass and reduce a dimension of the solid biomass below a threshold size.    USE - As biomass thermal conversion system.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for thermal conversion of solid biomass.
NOVELTY - Fuel composition comprises a lignin conversion product prepared by (a) contacting hydrogen, in the presence of a catalyst, with a mixture of lignin and an aromatic-containing solvent under reaction conditions effective to convert at least a portion of the lignin and provide a lignin conversion effluent having an increased quantity of aromatic hydrocarbons relative to the mixture, and (b) separating the lignin conversion product from the lignin conversion effluent.    USE - The fuel composition is useful as a motor fuel composition, a gasoline composition including petroleum derived gasoline and gasoline blending components such as ethanol, and as a blending component for a transportation fuels including aviation fuel.    ADVANTAGE - The fuel composition can be prepared by rapid and high conversion of lignin to aromatic hydrocarbons in one stage without the addition of a base such as sodium hydroxide or potassium hydroxide and requiring high costs of reagents and equipment, thus saving the production cost.    DETAILED DESCRIPTION - Fuel composition comprises a lignin conversion product prepared by (a) contacting hydrogen, in the presence of a catalyst, with a mixture of lignin and an aromatic-containing solvent under reaction conditions effective to convert at least a portion of the lignin and provide a lignin conversion effluent having an increased quantity of aromatic hydrocarbons relative to the mixture, and (b) separating the lignin conversion product from the lignin conversion effluent. The aromatic-containing solvent contains at least 50 vol.% of the aromatic hydrocarbons and the reaction conditions include a hydrogen partial pressure of 700 kPa (100 psig) to 21 MPa (3000 psig).
NOVELTY - Raloxifene oxalate is new.    USE - The raloxifene oxalate is useful for treating or preventing osteoporosis, breast cancer and/or cartilage degradation in a patient (claimed), preferably postmenopausal women. No biological data given.    ADVANTAGE - The raloxifene oxalate: is highly stable against moisture and humidity, and thus enhances the efficacy of the parent molecule in lower doses; can be obtained at high yield and purity; is substantially non-hygroscopic and has good flow characteristics; and can be prepare in a simple and eco-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM are also included for preparing raloxifene oxalate.
NOVELTY - Method for producing molasses, involves (a) repeating process of preparing slurry of pretreated cellulose-containing biomass, (b) hydrolyzing the slurry using cellulase from filamentous fungi and then subjecting the hydrolyzate to solid-liquid separation into a solution component and hydrolysis residue, (c) filtering the solution component and recovering the cellulase from filamentous fungi as a non-permeate, and (d) recovering molasses as permeate.    USE - The method is useful for producing molasses (claimed).    ADVANTAGE - The method produces molasses at low cost, and suppresses adsorption of cellulase from filamentous fungi to hydrolysis residue of cellulose-containing biomass, and recover and/or reuse beta -glucosidase.
NOVELTY - The gasification system has first gasifier that is positioned to receive a feed of low rank fuel. First gasifier gasifies the low rank fuel to produce hydrocarbons (26) and fixed carbon (24). Second gasifier produces a syngas stream (46) using received fixed carbon. First conduit recycles a portion of syngas stream to first gasifier to facilitate heating low rank fuel within first gasifier. The recycled syngas stream (80) is mixed with hydrocarbons to produce hydrocarbon-rich syngas stream (82). Second conduit is coupled to first gasifier to receive hydrocarbon-rich syngas stream.    USE - Gasification system used in integrated gasification combined-cycle power generation plant (claimed), for use with low rank fuel such as low rank coal, petroleum, coke, biomass, wood-based material, agricultural waste, tar, coke oven gas and asphalt, and/or other carbon containing feedstock, for producing synthetic natural gas (SNG).    ADVANTAGE - The gasification system is enabled to utilize lower cost, low rank fuels to produce SNG and/or electrical power.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) an integrated gasification combined-cycle power generation plant; and    (2) a method for gasifying a low rank fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the gasification system.    Fixed carbon (24)    Hydrocarbons (26)    Syngas stream (46)    Recycled syngas stream (80)    Hydrocarbon-rich syngas stream (82)
NOVELTY - A feedstock comprising bio-oil (10) chosen from bio-oils and/or fractions is subjected to azeotropic distillation with alcohol(s) (20) chosen from 1-30C alcohols to obtain a liquid component (40). The obtained liquid component is subjected to alcoholysis, to obtain converted bio-oil (90).    USE - Process for converting bio-oil used as heating oil, as starting material in processes for producing fuels, fine chemicals, chemical building-blocks, solvents, and fuel components (all claimed) e.g. transportation fuel.    ADVANTAGE - The method provides converted bio-oil product having excellent storage stability and thermal stability, and reduced acidity, with high productivity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for usage of converted bio-oil product as heating oil, as starting material in processes for producing fuels, fuel components, fine chemicals, chemical building-blocks, and solvents.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view explaining process for converting bio-oil.    Feedstock comprising bio-oil (10)    Alcohols (20,70,110)    Gaseous component (30)    Liquid component (40)    Reactor (100)
NOVELTY - Biogas purification method comprises: injecting biogas into a pressure vessel (102); cooling the pressure vessel to a first predetermined temperature; pressurizing the pressure vessel to a predetermined pressure; visually monitoring separation of a biogas impurity from a product gas during an induction period; isolating the product gas from the biogas impurity at a clathrate formation equilibrium by removing the product gas from the pressure vessel; and passing the product gas through water to yield a purified gas.    USE - The method is useful for purification of biogas.    ADVANTAGE - The method utilizes less amount of water and avoids the need for a high pressure spray.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for separating components of a gaseous mixture comprising injecting the gaseous mixture into a pressure vessel, injecting an aqueous solution into the pressure vessel having a predetermined concentration of an anionic surfactant, cooling the pressure vessel to a predetermined temperature, pressurizing the pressure vessel, visually monitoring separation of a gas impurity from a product gas during an induction period, and isolating the product gas from the gas impurity at a clathrate formation equilibrium by removing the product gas from the pressure vessel.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of mobile biogas purification apparatus.    Biogas purification apparatus (100)    Pressure vessel (102)    Gas inlet (104)    Gas outlet (106)    Pressure gauge (108)
NOVELTY - The fuel cell (1) has an anode (6) and a cathode (7) which are mutually opposingly arranged. An electrolytic membrane (5), e.g., anion exchange membrane, is provided between the anode and the cathode and configured to isolate a second fuel (Y) from a second fuel chamber (4) against a first fuel (X) from a first fuel chamber (3). The first fuel chamber has an electro-osmotic flow pump (2) which allows the first fuel chamber to generate an electro-osmotic flow arranged facing to the anode from the electrolytic membrane side.    USE - Fuel cell.    ADVANTAGE - Prevents fuel cross-over since the fuel can be rapidly supplied. Improves generating efficiency since the first fuel chamber has an electro-osmotic flow pump which allows the first fuel chamber to generate an electro-osmotic flow arranged facing to the anode from the electrolytic membrane side.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the fuel cell    Fuel cell (1)    Electro-osmotic flow pump (2)    First fuel chamber (3)    Second fuel chamber (4)    Electrolytic membrane (5)    Anode (6)    Cathode (7)    First fuel (X)    Second fuel (Y)
NOVELTY - A hexa-coordinate iron (II) complex (I) is new.    USE - Hexa-coordinate iron (II) complex used for preparing alcohols or non-racemic alcohol and amine products used in manufacturing of chemical products, pharmaceuticals, biotechnology, agrochemical, food, flavours, essential oils, personal care and advanced materials industries.    ADVANTAGE - The hexa-coordinate iron (II) complex is economically and efficiently manufactured with high yield and enantiopurity without polluting the environment.    DETAILED DESCRIPTION - A hexa-coordinate iron (II) complex of formula (I) is new.    R1=phenyl;    A=group of formula (i);    R4=H;    R5-R8=group chosen from group of formulae (ii) or (iii) optionally substituted by one or more substituents chosen from 1-8C alkyl, 1-8C alkoxyl and halo;    L1=CH3CN;    L2=CH3CN, CO or CNtBu;and    m=+2.
NOVELTY - The generator (1) has an electrolytic cell (2), an electrolyte reservoir (3), a water container (4), a control sub-system and a cooling sub-system (6) arranged in a support frame (7). A separating vessel (17) is connected with an outlet pipe. A main block of the control sub-system is fixed with control units, a power unit, an intermediate unit and a power supply unit. Processor software is installed in the control units. Parts of the control units are fixed with a data recording system. Sensors are connected with the control unit and placed in the generator.    USE - Modular hydrogen generator.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a modular hydrogen generator.    Modular hydrogen generator (1)    Electrolytic cell (2)    Electrolyte reservoir (3)    Water container (4)    Cooling sub-system (6)    Support frame (7)    Separating vessel (17)
NOVELTY - An artificial grass comprises Kosteletzkya virginica straw fermented product, and Glomus mosseae microbial inoculum.    USE - Artificial grass for seedling growth culture medium or agricultural production applications (claimed).    ADVANTAGE - The artificial grass has main nutrition index which is higher than grass substrate. It has low cost and easy operation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of artificial grass comprising: (A) mixing 0.1-0.3 pt. wt. Aspergillus niger, 0.1-0.3 pt. wt. Penicillium, 0.2-0.4 pt. wt. Trichoderma viride and 0.2-0.5 pt. wt. Coprinus, inoculating in liquid shaking bottle, inoculating in fermentation tank, pressing in plate and frame filter press, solid-liquid separating, collecting mycelium, and adsorbing to prepare fermentation agent; (B) cutting Kosteletzkya virginica straw to sections with size of 8-12 cm, crushing, mixing with water to water content of 60-70 wt.%, and adding 1-3 wt.% urea or ammonium sulfate to carbon/nitrogen ratio of 45-70; (C) adding 6-10 wt.% fermentation agent to Kosteletzkya virginica straw, uniformly mixing, piling in bamboo pole and covering plastic thin film; and (D) fermenting at 25-30 degrees C for 7-10 days, sterilizing using steam, disinfecting, cooling to room temperature, shredding, and adding Glomus mosseae microbial inoculum.
NOVELTY - Synthesizing trichloromethoxy-chlorobenzene comprises carrying out photochemical chlorination by reacting 4-chloroanisole, 3-chloroanisole and/or 2-chloroanisole and chlorine gas in the presence of a chlorinated solvent to obtain corresponding reaction product including 4-(trichloromethoxy)-chlorobenzene, 3-(trichloromethoxy)-chlorobenzene, and/or 2-(trichloromethoxy)-chlorobenzene. The chlorinated solvent is ortho-di(trifluoromethyl)benzene, meta-di(trifluoromethyl)benzene and/or para-di(trifluoromethyl)benzene.    USE - The method is useful for synthesizing trichloromethoxy-chlorobenzene (claimed).    ADVANTAGE - The method: is simple; has mild reaction conditions; does not discharge any waste; meets the requirement of environmental friendly chemical product; and ensures easy separation of the product and the solvent.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for synthesizing trifluoromethoxy-aniline, comprising (a) synthesizing trichloromethoxy-chlorobenzene as aforementioned, (b) adding trichloromethoxy-chlorobenzene into a high pressure kettle, adding anhydrous hydrogen fluoride, carrying out fluorination reaction under heating, distilling the fluorinated reaction product, to obtain trifluoromethoxy chlorobenzene, adding into a high pressure kettle, adding water and aqueous ammonia, and catalyst, raising the temperature to carry out amination reaction and purifying the reaction product.
NOVELTY - A tea waste is crushed into the extraction tank, ethanol is added after stirring and extract is heated. The extract is concentrated under reduced pressure and decompressed through macroporous adsorption resin column, washed using deionized water and eluted using anhydrous ethanol. Extract eluate is concentrated, and freeze-dried, to obtain epigallocatechin gallate crude product. The epigallocatechin gallate crude product is dissolved in deionized water, washed using water, eluent is decompressed and freeze-dried, to obtain epigallocatechin gallate.    USE - Extraction of epigallocatechin gallate (claimed).    ADVANTAGE - The method efficiently enables the extraction of epigallocatechin gallate having reduced energy consumption without polluting the environment.    DETAILED DESCRIPTION - A tea waste is crushed into the extraction tank, ethanol is added after stirring and extract is heated. The extract is concentrated under reduced pressure until no alcohol, decompressed through macroporous adsorption resin column, washed using deionized water, eluted using anhydrous ethanol, eluent is collected and eluate is concentrated under reduced pressure until no alcohol. The concentrate liquid is decompressed using the constant-flow pump in the medium-pressure chromatographic column, washed using water, eluted using anhydrous ethanol to the detector and eluent is collected. The extract eluate is concentrated under reduced pressure, and freeze-dried, to obtain catechin gallate crude product. The epigallocatechin gallate crude product is dissolved in deionized water by upper gel column, washed using water, then eluted using anhydrous ethanol, epigallocatechin gallate is collected, concentrated eluent is decompressed and freeze-dried, to obtain epigallocatechin gallate.
NOVELTY - Heavy oil processing comprises introducing heavy oil to cracking unit, adding contact agent, reacting to produce dry gas, liquefied petroleum gas, gasoline, diesel oil, wax and carbon residue, gasifying with steam and gasification catalyst to obtain carbon monoxide-rich gas and hydrogen-rich gas, and dry reforming to obtain carbon dioxide-rich gas and methane-rich gas.    USE - Method for processing heavy oil (claimed).
NOVELTY - The system has a shell (1) arranged at a bottom part of a supporting foot (6). A direct oxidation system and an inner water circulation system are located in the shell. A PLC control system is located on a top part of the shell. The direct oxidation system is provided with a direct current stabilization power supply (5) and a high energy direct oxidation device (8). The direct oxidation device is provided with a drain-pipe (9). A PLC control panel (2) is connected to the direct current stabilization power supply, a circulating pump (7) and the drain-pipe.    USE - Pesticide residue degrading system.    ADVANTAGE - The system is convenient to operate, and ensures low reacting time, avoids secondary pollution without utilizing agents and prevents food inherent nutrient content from being affected.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a pesticide residue degrading system.    Shell (1)    PLC control panel (2)    Direct current stabilization power supply (5)    Supporting foot (6)    Circulating pump (7)    High energy direct oxidation device (8)    Drain-pipe (9)
NOVELTY - Producing hydrogen and sulfur from the destruction of hydrogen sulfide, comprises injecting a stream of hydrogen sulfide-containing gas and a stream of oxygen or oxygen-rich gas into a reactor comprising a plasma zone. The gas streams are wholly or partially combined with one another before or during contact with the plasma.    USE - The process is useful for producing hydrogen and sulfur from the destruction of hydrogen sulfide (claimed).    ADVANTAGE - The process reduces the specific energy required to generate hydrogen, below the thermodynamic equilibrium calculated energy requirement under the same nominal conditions by the addition of small amounts of oxygen to the plasma dissociation of hydrogen sulfide, thus maintaining good hydrogen sulfide destruction efficiencies and reducing the overall cost.    DETAILED DESCRIPTION - Producing hydrogen and sulfur from the destruction of hydrogen sulfide, comprises injecting a stream of hydrogen sulfide-containing gas and a stream of oxygen or oxygen-rich gas into a reactor comprising a plasma zone. The gas streams are wholly or partially combined with one another before or during contact with the plasma. The molar ratio of hydrogen sulfide to oxygen injected into the reactor is 3-100. The plasma provides energy to the reactor with the hydrogen sulfide/oxygen gas streams of 0.1-1.5 eV/hydrogen sulfide molecule. The method provides hydrogen at a specific energy requirement of less than 2.5 eV/molecule of hydrogen.
NOVELTY - Modifying bio-oil involves: (a) reacting a feedstock comprising bio-oil with a reducing agent selected from sodium borohydride (NaBH4) and sodium dithionite (Na2O4S2) in at least one polar solvent; and (b) obtaining bio-oil.    USE - The process is useful for modifying bio-oil. The modified bio-oil product is useful as heating oil, and as starting material in processes for producing fuels, fuel components, fine chemicals, chemical building-blocks, and solvents (all claimed).    ADVANTAGE - The process can effectively and economically modify bio-oil. The stability of the bio-oil is improved or increased and composition is altered. The modified bio-oil is maintained in liquid form for long periods of time and it can be stored without problems for more than 6 months.
NOVELTY - A hydrogen-producing apparatus has steam chamber which produces water vapor from water, catalyst pipe (3) containing a stainless steel material formed adjacent to the steam chamber, and heating apparatus which heats the steam chamber and catalyst pipe. The catalyst pipe is empty at 700 degrees C more or less.    USE - Apparatus is used for producing hydrogen for hydrogen boiler, motor vehicle, fuel cell, boat and ship.    ADVANTAGE - The apparatus produces hydrogen for a long period of time.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the apparatus.    Catalyst pipe (3)
NOVELTY - The method involves mixing a graphite resin material at mass ratio of 90:10-70:30. An ion conductivity part is inserted by an electrode plate (1). A platinum part is supported by a cathode electrode plate. A separator (2) supplies hydrogen gas and oxygen gas to an electrode (5). A convex part is formed in a groove channel (4). The electrode is provided with copper foils. An electric power generation gas distribution part is formed in the separator. A hot-pressure molding is acquired during heat processing at 190 degree Celsius. The separator is formed with a groove.    USE - Method for manufacturing a fuel cell separator.    ADVANTAGE - The graphite resin material is mixed with mass ratio of specific value, and the main body surface roughness is in specific value, so that manufacture of the fuel cell can be simplified, production time of a battery stack assembly can be suppressed, failure at time of battery operation can be prevented and outstanding electro-conductivity of the fuel cell can be achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a fuel cell separator.    Electrode plate (1)    Separator (2)    Gas flow path (3)    Groove channel (4)    Electrode (5)
NOVELTY - A refrigeration oil comprises base oil, 0.01-2 %mass sulfide compound and 0.1-5 %mass orthophosphate ester. The refrigeration oil has kinematic viscosity of 3-500 mm2/s at 40 degrees C.    USE - Refrigeration oil used in working fluid composition (claimed). Uses include but are not limited to refrigerator, air conditioner for motor vehicles, dehumidifier, refrigerated warehouse, automatic vending machine, showcase, cooling device in chemical processing plant, residential air conditioner, hot water heat pump, etc.    ADVANTAGE - The refrigeration oil provides working fluid composition having high abrasion resistance even under lubricated conditions, long-term reliability, and long-term stability. The refrigerant provides air conditioning system with low-global warming potential and high cooling efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for working fluid composition, which comprises refrigeration oil and refrigerant having global warming potential of 700 or less.
NOVELTY - An additive comprises 0.05-25.0 (m/m)%, preferably 1.0-20.0 (m/m)% biocidal substance, 1.0-90.0 (m/m)% hydrocarbon solvent, 0.5-50.0 (m/m)% co-solvent and 0.5-60.0 (m/m)% oxidation inhibitor, where the biocidal substance comprises methylene-bis (thiocyanate), 2-(thiocyanomethylthio) benzothiazole, N-butyl-1,2-benzisothiazolone-3, 3,3-methylene-bis (5-methyl-1,3-oxazolidine), 2-octyl 4-isothiazolone-3, and/or 7-ethylbicyclooxazolidine.    USE - Additive for stabilizing hydrocarbon fuel and biofuel containing biocomponents such as methyl esters of fatty acid.    ADVANTAGE - The additive has improved biocidal action.
NOVELTY - A fuel cell power production system (1) comprises a high-temperature fuel cell (2) including anode compartment (3) which receives fuel from a fuel supply path and outputs anode exhaust, and cathode compartment (4) which receives oxidant gas and outputs cathode exhaust, a water transfer assembly (9) which transfers water in anode exhaust, and a hydrogen utilization device (30) which receive oxidant gas, water-separated anode exhaust and gas derived from water-separated anode exhaust and outputs hydrogen utilization device exhaust including oxidant gas.    USE - Fuel cell power production system is used for producing power (claimed).    ADVANTAGE - The power is efficiently produced using the economical fuel cell power production system with reduced emission.    DETAILED DESCRIPTION - A fuel cell power production system comprises a high-temperature fuel cell including anode compartment which receives fuel from a fuel supply path and outputs anode exhaust, and cathode compartment which receives oxidant gas and outputs cathode exhaust, a water transfer assembly which transfers water in anode exhaust, and a hydrogen utilization device which receive oxidant gas, water-separated anode exhaust and gas derived from water-separated anode exhaust and outputs hydrogen utilization device exhaust including oxidant gas. The hydrogen utilization device comprises internal combustion engine, diesel engine, combustion turbine, microturbine and low-temperature carbon dioxide and carbon monoxide tolerant engine. The hydrogen utilization device exhaust is used to provide oxidant gas to cathode. An INDEPENDENT CLAIM is included for power production method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of fuel cell power production system.    Fuel cell power production system (1)    High-temperature fuel cell (2)    Anode compartment (3)    Cathode compartment (4)    Water transfer assembly (9)    Hydrogen utilization device (30)
NOVELTY - The method involves supplying natural gas to carbon dioxide removal roofing tile moist. Impurity of dust and moisture are removed by a mixed-refrigerant circulation part. The natural gas is cooled by a heat exchanger, where the gas passes through a fabrication process part. The fabrication process part is provided with the heat exchanger. The natural gas is cooled by the fabrication process part that supplies heat to the heat exchanger according to a pass box liquefy propane heat exchangers. A gas stream mixer provides a gas stream.    USE - Method for liquefying natural gas passing through a heat exchanger.    ADVANTAGE - The method enables separating the gas stream from the heat exchanger so as to improve the natural gas liquidizing process. The method enables passing the natural gas through the heat exchanger so as to reduce the electric power energy due to the heat recovery of the mixed-refrigerant.    DESCRIPTION OF DRAWING(S) - The drawing shows a circuit diagram of a heat exchanger.
NOVELTY - The flow output pipeline has a main body which forms an electrolytic groove, and has an upper cover (11) and a lower cover. Air tubes (51-56) are provided which are connected with a gas collecting module and the other end portion is connected with a pneuma collecting tube. The electrolytic groove flows the water mist of hydrogen-oxygen gas from opening (500) of vent tube into the air tube, and to the pneuma collecting tube.    USE - Flow output pipeline of hydrogen and oxygen producing machine used in motor vehicle.    ADVANTAGE - Water mist is smoothly collected to air outlet joint opening of vent tube or collecting module. Water liquid are filtered and atomized, which improves the hydrogen proportion and purity and produces hydrogen-oxygen gas as alternative energy use.    DESCRIPTION OF DRAWING(S) - The drawing shows the top perspective view of flow output pipeline of hydrogen and oxygen producing machine.    Upper cover (11)    Air tubes (51-56)    Fixing piece (91)    Air outlet (110)    Opening (500)
NOVELTY - A biodiesel is synthesized by adding waste oil in reaction container, uniformly mixing ionic liquid with concentrated sulfuric acid and premixed composite catalyst, quickly adding methanol and composite catalyst, uniformly mixing to obtain mixed liquid in which molar ratio waste oil:methanol:composite catalyst is 1:5-20:0.05-0.1, heating to 50-100 degrees C, reacting, standing to form layers in which upper layer is biodiesel crude product and lower layer is composite catalyst for circulation, vacuum-distilling biodiesel crude product to recover methanol, washing by water, and vacuum-distilling.    USE - Synthetic process of biodiesel (claimed).    ADVANTAGE - The process is simple and clean, has convenient operation, low cost, no volatilization, and high conversion rate, and obtains biodiesel which is easy to separate.    DETAILED DESCRIPTION - A biodiesel is synthesized by adding waste oil in reaction container, uniformly mixing ionic liquid with concentrated sulfuric acid and premixed composite catalyst, quickly adding methanol and composite catalyst, uniformly mixing to obtain mixed liquid in which molar ratio waste oil:methanol:composite catalyst is 1:5-20:0.05-0.1, heating to 50-100 degrees C, reacting for 2-10 hours, standing to form layers in which upper layer is biodiesel crude product and lower layer is composite catalyst for circulation, vacuum-distilling biodiesel crude product to recover methanol, washing by water, and vacuum-distilling.
NOVELTY - Decomposing inoculant comprises 1x 108 cells/ml Trichoderma sp. spore suspension, 1% kaolin, and potato juice. The inoculant is prepared by mixing the above-mentioned components in ratio 10 kg:20-100 ml:100-1000 ml.    USE - The inoculant is useful for degrading pine withered waste (claimed) pine including pine needles and pine branches.    ADVANTAGE - The inoculant degrades pine waste rapidly within short period of time, promotes rapid return of nutrients and kills pests effectively.
NOVELTY - Preparation of ibrutinib (I) involves using 4-phenoxy benzoyl chloride as raw material and subjecting to condensation and oxidation reaction with malononitrile and dimethyl sulfate, obtaining 4-phenoxy-phenyl (methoxy) vinylidene cyanide as intermediate compound, subjecting obtained intermediate compound 1-(3R-hydrazino-1-piperidinyl)-2-propen-1-one to pyrazole cyclization reaction, obtaining 1-((3R)-(3-(4-phenoxyphenyl)-4-carbonitrile-5-amino-1H-pyrazol-yl)-1-piperidinyl)-2-propen-1-one, and subjecting obtained product and pyrimidine ring to cyclization reaction.    USE - Preparation of ibrutinib (claimed).    ADVANTAGE - The method enables economical and environmentally-friendly preparation of eleuthera erlotinib by a simple process using easily available raw materials.    DETAILED DESCRIPTION - Preparation of ibrutinib of formula (I) involves using 4-phenoxy benzoyl chloride as raw material and subjecting to condensation and oxidation reaction with malononitrile oxide dimethyl sulfate, obtaining 4-phenoxy-phenyl (methoxy) vinylidene cyanide as intermediate compound, subjecting obtained intermediate compound 1-(3R-hydrazino-1-piperidinyl)-2-propen-1-one to pyrazole cyclization reaction, obtaining 1-((3R)-(3-(4-phenoxyphenyl)-4-carbonitrile-5-amino-1H-pyrazol-yl)-1-piperidinyl)-2-propen-1-one, and subjecting obtianed product and pyrimidine ring to cyclization reaction.
NOVELTY - Enhancing soil water retention comprises inserting rod-like structure fertilizer comprising cation exchange resin, sea buckthorn, hairy vetch, chicken manure, phosphate rock, photosynthetic bacteria, ammonium sulfate, and fermentative bacteria to saline-alkali soil at every 20 cm of ridge, and exposing 1-2 cm of fertilizer to surface; adding corn starch to water, heating to 70-75 degrees C for 1 hour, cooling to 45 degrees C to obtain paste, and spraying on soil to obtain thin film; and inserting rod-like structure fertilizer to other side of ridge every 20-25 days, rotating, and spraying with paste.    USE - Method for enhancing soil water retention (claimed).    ADVANTAGE - The method is simple and convenient to use, reduces salt content of soil, enhances activity of microorganism and enzyme, promotes plant root growth system, and has simple product ratio.
NOVELTY - Cinepazide maleate preparation involves adding acetyl chloride and pyrrolidine in dichloromethane as reaction solvent to form a precipitate. The formed precipitate is collected and purified to obtain white flaky solid-chloroacetyl-pyrrole. The obtained acetyl pyrrole and anhydrous piperazine are reacted to form acetyl pyrrolidine, where redundant piperazine is removed by distillation at 80-100 degrees C to give 1 acetyl pyrrolidine.    USE - Method for preparing cinepazide maleate (claimed).    ADVANTAGE - The method prepares the high purity cinepazide maleate in a simple, cost-effective and eco-friendly manner with high yield without generating impurity and pigment.    DETAILED DESCRIPTION - Cinepazide maleate preparation involves adding acetyl chloride and pyrrolidine in dichloromethane as reaction solvent to form a precipitate. The formed precipitate is collected and purified to obtain white flaky solid-chloroacetyl-pyrrole. The obtained acetyl pyrrole and anhydrous piperazine are reacted to form acetyl pyrrolidine, where redundant piperazine is removed by distillation at 80-100 degrees C to give 1 acetyl pyrrolidine. The distillation is water vapor distillation or temperature high vacuum distillation performed by using acetone and petroleum ether mixed solvent. The obtained acetyl pyrrolidine is treated with 3,4,5-trimethoxy cinnamoyl chloride with an alkali to obtain piperidine hydrochloride, which is dissociated with sodium hydroxide aqueous solution to obtain high purity cinepazide maleate.    DESCRIPTION OF DRAWING(S) - The drawing shows a proton nuclear magnetic resonance spectrum of high purity cinepazide maleate.
NOVELTY - Duloxetine preparation involves refluxing 1-chloroethyl-N-methyl-((S) -3-(naphthalen-1-yloxy)-3-(thiophen-2-yl)-propyl)-carbamate in organic solvent A at 50 degrees C to obtain reaction liquid, and adding organic solvent B and alkali to reaction liquid to obtain a solution. The alkali is selected from potassium hydroxide, sodium hydroxide or lithium hydroxide.    USE - Method for preparing duloxetine (claimed).    ADVANTAGE - The method enables quickly preparing duloxetine at industrial level in an eco-friendly and safe manner.
NOVELTY - Lapatinib salt (I), is new.    USE - Lapatinib salt used for preparing anticancer medicine for curing metastatic breast cancer.    ADVANTAGE - The lapatinib salt is safe and reproducible, and has low moisture absorption, and is simply prepared.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing lapatinib salt of formula (I)..
NOVELTY - Purification method of allopurinol involves dissolving allopurinol crude product in the polar organic solvent at 100-190 degrees C, decolorizing resultant solution, hot-filtering, cooling the obtained filtrate, crystallizing and separating purified allopurinol crystal.    USE - Purification method of allopurinol (claimed).    ADVANTAGE - The method efficiently purifies allopurinol having high yield, and purity of more than 99.88% without polluting the environment, by a simple method.
NOVELTY - Preparation of folic acid comprises taking 2,4,5-triamino-6-hydroxypyrimidine sulfate, adding 1-4C alcohol, tetrahydrofuran, dimethylformamide and/or dimethylacetamide, mixing, adding tetrabutyl ammonium halide, 1,2,3-trihalogenpropene and N-(4-aminobenzoyl)-L-glutamic acid, reacting at 10 degrees C, adjusting pH value to 5-6 by adding alkali solution dropwise, reacting for 1-5 hours, cooling at 18-22 degrees C, adding mixture of 20-35 wt.% hydrogen peroxide, 20-35 wt.% peracetic acid and peroxybenzoic acid, stirring at 10-30 degrees C for 2-10 hours, filtering and collecting filter cake.    USE - Method for preparing folic acid (claimed).    ADVANTAGE - The method is simple, environment-friendly, has low production cost and high purity.
NOVELTY - Mibemycin oxime derivative (I) is new.    USE - Mibemycin oxime derivative (I).    ADVANTAGE - The method is simple, and has inexpensive raw materials, mild reaction, low cost and high yield.    DETAILED DESCRIPTION - Mibemycin oxime derivative of formula (I) is new.    X-Y'=CH(CH), CH2-CH(OH), CH2-CH2, CH2-O or CH2-NH;    R=H, halo, alkyl, alkoxy, haloalkyl, alkylcarbonyl, alkoxycarbonyl, aryl, amino group, alkylamino, nitro or hydroxy; and    R1, R2=H, alkyl, alkylcarbonyl, or alkoxycarbonyl.    An INDEPENDENT CLAIM is included for preparation of compound (I).
NOVELTY - Preparation of erythromycin-9-oxime comprises dissolving crude sulfur red, hydroxylamine inorganic acid salt, and water-soluble alkali in a polar solvent; adding drying agent, carrying out oximation of erythromycin A, cooling to room temperature, adding a liquid alkali to regulate pH at 5.5, adding water to completely precipitate the oxime salt, and filtering to obtain oxime salt; and adding a polar solvent to the oxime salt, adding strong alkali to dissolve the oxime salt, adding filter aid, stirring, filtering, dropwise adding water to obtain crystals, filtering, and drying.    USE - Method for the preparation of erythromycin-9-oxime (claimed) used as an intermediate for synthesizing azithromycin, clarithromycin, and roxithromycin, and erythromycin derivatives.    ADVANTAGE - The method is inexpensive, and is environment-friendly.
NOVELTY - Synthesis of capecitabine comprises dissolving 2',3'-di-o-acetyl-5'-deoxy-5-fluorocytidine in an organic solvent, adding chloroformic acid n-amyl ester, carrying out aminoacylation reaction at - 10-0 degrees C to obtain 5'-deoxy-5-fluoro-N-((pentyloxy)carbonyl)cytidine solution, directly adding alkali aqueous solution, adding alcohol substance, and carrying out hydrolysis at - 20-20 degrees C.    USE - Method for the synthesis of capecitabine (claimed) used in a medicine for treating cancer such as colon cancer and breast cancer.    ADVANTAGE - The method has simple and short operation, is inexpensive, and is environment-friendly.
NOVELTY - Preparation of polymer absorbent resin fertilizer includes providing sodium hydroxide solution; adding the prepared NaOH solution dropwise continuously to acrylic acid in a neutralization reaction, adding acrylamide and diammonium phosphate, and cooling; after the reaction, adding the solution with straw powder, stirring and cooling, adding methylenedioxyphenyl bisacrylamide crosslinking agent, adding ammonium persulfate initiator, heating, carrying out graft copolymerization reaction; drying, aging, reacting, mixing liquid into solid, and naturally drying; and crushing.    USE - Method for preparing polymer absorbent resin fertilizer (claimed).    ADVANTAGE - The method is environment-friendly and safe, and has stable product quality.    DETAILED DESCRIPTION - Preparation of polymer absorbent resin fertilizer comprises:    (A) providing 21000 g of 31.7% sodium hydroxide solution;    (B) adding the prepared NaOH solution dropwise continuously to 26000 g acrylic acid having more than 99.5% purity in a neutralization reaction for 20 minutes, adding 2200 g acrylamide and 22000 g diammonium phosphate, and cooling to 50-60 degrees C;    (C) after the reaction, adding the solution with 10400 g straw powder (100-200 mesh), stirring and cooling to 50-40 degrees C at 100-120 revolutions/minute, adding 8 g methylenedioxyphenyl bisacrylamide crosslinking agent, adding 10 g ammonium persulfate initiator, heating at 65-70 degrees C, carrying out graft copolymerization reaction, and controlling the reaction at 110-115 degrees C for 15 minutes;    (D) drying the reaction liquid flow to mix in the polymerization reactor, aging, reacting for 10-20 minutes, mixing liquid into solid, and naturally drying; and    (E) crushing the solid product into particles to obtain the finished product.
NOVELTY - The system has output of methanol storage station (13) that is connected to the input of the groove solar energy absorbing reactor (14), while the output of the solar energy absorbing reactor is connected to the hydrogen pressure swing absorbing and purifying device (15). The output of the carbon monoxide hydrogen pressure swing absorbing and purifying device of is connected to the municipal tube network system (16).    USE - Integrated storage system for solar and biomass gasification-based hydrogen production output.    ADVANTAGE - By using the storage system, a renewable energy source can be efficiently used to generate hydrogen with high-quality support, efficient storage and efficient transportation.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the integrated storage system for solar and biomass gasification-based hydrogen production output. (Drawing includes non-English language text).    Methanol storage tank (11)    Methanol storage station (13)    Groove solar energy absorbing reactor (14)    Hydrogen pressure swing absorbing and purifying device (15)    Municipal tube network system (16)
NOVELTY - The reactor has a connecting pipeline (6) connected with a gasification furnace (3). A combustion gas device is distributed with a fish-type material (4). The pipeline is connected with a chiller (9). The chiller is fixed with a laser cold air cooling section, a heat exchanger cooling section and a discharging system (7). An upper wall of a lower side of the chiller is fixed with a cold laser air entrance (8) and a cold water inlet. An upper part of the laser cold air cooling section and the heat exchanger cooling section are fixed with a heat exchanger (10).    USE - Dual-section oxygen-enriched steam biomass gasification reactor for use in a rural area and a forest area.    ADVANTAGE - The reactor improves gas energy efficiency and increase tar content range of hydrogen gas and carbon mono-oxide gas. The reactor generates diesel oil gas by utilizing F-T synthesis process after performing purification process and realizes crop waste centralized processing operation.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a dual-section oxygen-enriched steam biomass gasification reactor.'(Drawing includes non-English language text)'    Gasification furnace (3)    Fish-type material (4)    Connecting pipeline (6)    Discharging system (7)    Cold laser air entrance (8)    Chiller (9)    Heat exchanger (10)
NOVELTY - The device has a tubular mixing chamber whose tail end part is provided with a cone-shaped heat carrier gas inlet pipe. The mixing chamber is provided with a feeding port. High temperature catalyst and a normal temperature biomass raw material are entered into the mixing chamber through a through-hole. Heat carrier gas enters into the mixing chamber by the heat carrier gas inlet pipe. The mixing chamber is utilized for uniformly mixing the catalyst and the biomass raw material for supplying sufficient heat to a biomass gasification furnace to perform a cracking process.    USE - Feeding device for a biomass gasification furnace.    ADVANTAGE - The device is simple in structure. The device can mix the biomass raw material and the catalyst in a uniform manner so as to improve contact heat exchanging efficiency of the biomass gasification furnace. The device produces combustion gas with high thermal value during gasification process.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a feeding device.
NOVELTY - The system has pneuma that is sent to methanation unit for cooling process, and a separate sewage oil water is produced. The separate impurity is sent to the combustion furnace fuel feed port (4a), or is sent to the gasification furnace fuel feed port (4b), or is sent to a deep processing by methanation unit, using low temperature methanol washing process. The low temperature methanol washing process produces carbon dioxide to gasification furnace. A by-product of the methanation process of water vapor is sent to gasification furnace, or complementary methanation unit.    USE - Double multi-joint gasification-combustion system for solid fuel staged.    ADVANTAGE - Maximizes utilization efficiency of secondary product, since low temperature methanol washing process produces the characteristic of carbon dioxide, while the water vapor and carbon dioxide mix oxygen as gasification agent being recycled in gasification furnace.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a double multi-joint gasification-combustion method for staged solid fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the double multi-joint system of solid fuel staged gasification-combustion.    Combustion boiler (1)    Combustion furnace fuel feed port (4a)    Gasification furnace fuel feed port (4b)    Air distribution unit (6b)    Flue gas channel (8)
NOVELTY - The device has a support shaft fixed with a biomass gasification furnace body that is fixed with a total air outlet. An end of the support shaft passes through a rear cover. A fixing end of a driving device is sleeved on a lower part of the support shaft that is equipped with a cylindrical filter core. The filter core is formed with multiple through holes. Diameter of the through holes is 4+/-0.5 mm. Height of the filter core is 250-350 mm. The filter core is connected with a fuel gas exit and the total air outlet. The filter core is made of a high temperature resistant material.    USE - High temperature dust-removing device for use in a biomass gasification furnace.    ADVANTAGE - The device is simple in structure. The device can directly remove dust from combustion gas under high temperature condition. The device improves dust removing efficiency and reduces combustible gas heat loss.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a high temperature dust-removing device in partial section.
NOVELTY - Complete combustion alcohol-based fuel contains petroleum ether, hydrogen peroxide, benzene, glycerin, water, and mixed methanol, ethanol, and propanol with volume ratio of 10-50:1-5:1-5:1-5:10-20, and dissolved solid ferrocene with concentration of 0.1-1%.    USE - Complete combustion alcohol-based fuel (claimed).    ADVANTAGE - The complete combustion alcohol-based fuel generates iron oxide particles with relatively large surface area, reduces combustion dehydrogenation and thermal cracking, and has high heat and combustion efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of complete combustion alcohol-based fuel which involves placing petroleum ether, hydrogen peroxide, benzene, glycerol, and water in mixing tank to obtain emulsifying agent, mixing methanol, ethanol, and propanol to obtain mixture, mixing emulsifying agent and mixture, adding 0.1-1% dissolved ferrocene.
NOVELTY - An alcohol-based fuel comprises 10-95 wt.% methanol, 10-80 wt.% aromatic hydrocarbon, 5-15 wt.% heavy benzene, 0.5-2 wt.% combustion improver, 2-8 wt.% co-solvent and 3-3.5 wt.% antioxidant, and does not contain gasoline components.    USE - Alcohol-based fuel is used for vehicle.    ADVANTAGE - The alcohol-based fuel is economically prepared with reduced energy consumption, by environmentally-friendly process.
NOVELTY - Bio-jet fuel is prepared using mesoporous molecular sieve by adding nickel nitrate hexahydrate (Ni(NO3)2.6H2O) and ammonium molybdate tetrahydrate ((NH4)6Mo7O24.4H2O) in deionized water, stirring, adding mesoporous molecular sieve to form mixture, magnetically stirring, drying, calcining in muffle furnace under air atmosphere, heat preserving to obtain calcined product, heating in tubular furnace under air atmosphere, heat preserving to obtain catalyst, placing bio-oil in high temperature high pressure reactor, adding catalyst, passing hydrogen gas, reacting, and centrifuging.    USE - Preparation of bio-jet fuel using mesoporous molecular sieve (claimed).    ADVANTAGE - Process improves microalgae oil quality, increases hydrocarbon content and yield of bio-jet fuel, and reduces aromatic content of bio-jet fuel.    DETAILED DESCRIPTION - Bio-jet fuel is prepared using mesoporous molecular sieve by adding 2.37-23.7 g Ni(NO3)2.6H2O and 1.32-13.2 g (NH4)6Mo7O24.4H2O in 10-100 ml deionized water, stirring to obtain solution, adding 4.8-48 g mesoporous molecular sieve to form mixture, magnetically stirring at 25 degrees C for 6-12 hours, drying at 70-80 degrees C for 8-16 hours, calcining in muffle furnace under air atmosphere at 550 degrees C, heat preserving for 4-8 hours to obtain calcined product, heating in tubular furnace to 500 degrees C under air atmosphere, heat preserving for 4-8 hours to obtain catalyst, placing 100-500 ml bio-oil in high temperature high pressure reactor, adding 5-25 g catalyst, passing hydrogen gas to obtain pressure of 1-5 MPa, reacting at 330-410 degrees C for 480 minutes, stirring at 500 r/minute, centrifuging reaction mixture at 400 r/minute for 5 minutes, and collecting supernatant liquid.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow chart of preparation of bio-jet fuel using mesoporous molecular sieve. (Drawing includes non-English language text).
NOVELTY - A cerium oxide-based catalyst comprises cerium-lanthanum oxide (I) as carrier, and cobalt(II,III) oxide as active component of load.    USE - Cerium oxide-based catalyst is used for catalytic combustion of methane.    ADVANTAGE - The cerium oxide-based catalyst has excellent activity and stability, and is prepared by environmentally-friendly method.    DETAILED DESCRIPTION - A cerium oxide-based catalyst comprises cerium-lanthanum oxide of formula: CeLaxO2+-1.5x (I) as carrier, and cobalt(II,III) oxide as active component of load.    x=0-0.25.    An INDEPENDENT CLAIM is included for preparation of cerium oxide-based catalyst, which involves preparing mixed solution (A) of citric acid, cerium nitrate and water in molar ratio of 0.8-1.4:1:278, supplying citric acid, cerium nitrate, lanthanum nitrate, and water into sealed reaction vessel, such that the molar ratio of citric acid, cerium nitrate, lanthanum nitrate and water is 6:4-5:0-1:1000, performing hydrothermal treatment at 70-120 degrees C for 12-48 hours, obtaining product (B), drying, obtaining solid oxide by calcining at 700-800 degrees C for 3-5 hours, immersing in mixed solution (A), aging at room temperature for 10-12 hours, drying, and calcining at 700-800 degrees C for 3-5 hours.
NOVELTY - A biogas purification system comprises gas storage tank (150), multi-stage desorption tower, water storage tank (110), and reflux pipeline (1) in which water storage tank contains 1st water storage tank water inlet and 1st water storage tank water outlet, 1st water storage tank water inlet, 1st water storage tank water outlet and end-stage desorption tower of last-stage desorption tower forms 1st circulating loop, 1st end of reflux pipeline is connected to gas storage tank, 2nd end of reflux pipeline is connected to last-stage desorption tower, and reflux pipeline contains switch valve.    USE - A biogas purification system (claimed).    ADVANTAGE - Biogas purification system is simple and easy to operate and reduces start-up time, energy cost, and operating cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of biogas purification system.    Reflux pipeline (1)    1st stage desorption tower (50)    3rd stage desorption tower (60)    Water storage tank (110)    Gas storage tank (150)
NOVELTY - Manufacture of artificial coal involves extracting highest value of heat from waste liquid fuel, reducing smoke emission by utilizing latent heat in fuel combustion applications, regulating heat value of artificial coal by solid fuel and liquid fuel.    USE - Manufacture of artificial coal (claimed).    ADVANTAGE - The artificial coal is manufactured by environmentally-friendly method.
NOVELTY - A low-ash phosphorus-free anti-wear complexing agent comprises 10-30 wt.% alkyl diphenylamine, 15-35 wt.% 3,5-di-tert-butyl-4-hydroxyphenyl propionate, 20-50 wt.% boronated succinimide, 15-35 wt.% calcium alkyl salicylate, 10-30 wt.% diamyl urethane and 5-10 wt.% diluted oil.    USE - Low-ash phosphorus-free anti-wear complexing agent is used for preparation of alcohol fuel engine oil oxidation inhibitor (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of alcohol fuel engine oil oxidation inhibitor, which involves heating diluent oil, adding boronated succinimide, adding alkyl dimethylamine, 3,5-di-tert-butyl-4-hydroxyphenyl propionate and calcium alkyl salicylate, stirring, adding diamyl urethane, and constantly stirring.
NOVELTY - Biodiesel purification involves feeding biology diesel oil into biology diesel oil purifying system and heating the purifying system for forming gaseous mixture. The formed gaseous mixture is entered into a condensation device for condensing gases into liquid, where the condensed liquid is transferred into another condensing device.    USE - Method for purifying biodiesel (claimed).    ADVANTAGE - The method purifies biodiesel reduces complexity of purifying process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a biodiesel purification system, which comprises a fatty acid methyl ester storage tank (12), two condensing devices (21,31), two temporary storage tanks (24,33), and a methyl ester storage tank (12).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biodiesel purification system. (Drawing includes non-English language text).    Fatty acid methyl ester storage tank (12)    Methyl ester storage tank (12)    Condensing devices (21,31)    Temporary storage tanks (24,33)    Jar (33)
NOVELTY - Immobilized hydrolase is prepared by crosslinking hydrolytic enzyme and glutaraldehyde and absorbing into surface of magnetic chitosan composite microsphere in which magnetic chitosan composite microsphere contains ferric oxide (Fe3O4) nanoparticle and chitosan.    USE - Preparation of immobilized hydrolase for hydrolysis of sludge (claimed).    ADVANTAGE - Process is simple and low cost, and product is recyclable, does not easily inactivate, promotes hydrolytic degradation of organic matter, and has high ionic strength and good absorption property.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for application of immobilized hydrolase which involves adding immobilized hydrolase into sludge and anaerobically hydrolyzing at 48-52 degrees C for 4-5 hours under oscillating speed of 100-120 rpm.
NOVELTY - Method for producing ethanol by simultaneous saccharification and fermentation of starch-based biomass involves performing saccharification in saccharification kettle using alpha -amylase and glucoamylase, collecting saccharified liquid from saccharification kettle, feeding to the filter, returning solid phase to the saccharification kettle, feeding the filtered liquid to fermentation vessel, and fermenting the liquid using yeast culture at the same time fermentation broth of same volume is recycled back to the saccharification kettle.    USE - The method is useful for producing ethanol by simultaneous saccharification and fermentation of starch-based biomass one or more chosen from corn, wheat and tapioca using device (all claimed).    ADVANTAGE - The method avoids fractional saccharification of glucose, is cost-effective and requires less amount of enzyme.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for device, which comprises saccharification kettle for saccharification of starch-based biomass, centrifugal pump for extracting liquid from the kettle, centrifugal pump for feeding to filtering device, filtering device for extracting liquid from a centrifugal pump, fermentation vessel for fermentation and centrifugal pump for recycling the liquid.
NOVELTY - Preparing reducing sugar using cellulose-containing raw material, involves mixing pre-processed cellulose-containing raw material and cellulase together, and hydrolyzing the mixture. The pre-processed cellulose-containing raw material is prepared by mixing cellulose-containing raw material with an acidic solution and subjecting to microwave digestion at 50-200 degrees C, 0.05-2 mPa and 0.5-5 GHz microwave frequency for 1-60 minutes.    USE - The method is useful for preparing reducing sugar using cellulose-containing raw material which is at least one chosen from corn stalk, wheat straw, rice straw, sugarcane straw, broomcorn straw, cotton straw, soybean straw and water hyacinth (all claimed).    ADVANTAGE - The method increases yield of the reducing sugar.
NOVELTY - Producing fluorine and hydrogen gas involves electrolyzing potassium fluoride, hydrogen fluoride and hydrofluoric acid in mole ratio of 1:1-2:1:0.5 at 70-110 degrees C using 4-6 Amperes electric current and voltage of 10 volts to obtain fluorine and hydrogen gas at cathode, where anode is made of coarse nickel particles. Potassium fluoride, hydrogen fluoride and anhydrous hydrofluoric acid are added in electrolytic groove made of copper. Groove is heated at 70 degrees C to obtain solution that is heated at 90 degrees C for completion of electrolysis.    USE - Method for producing fluorine and hydrogen gas (claimed).    ADVANTAGE - The method for producing fluorine and hydrogen gas is simple and reasonable.
NOVELTY - Processing biomass involves crushing the raw material, conveying and steaming under reduced pressure to obtain mixed raw material. The mixed raw material is sprayed with acid or an acid anhydride to obtain the product.    USE - Method for processing biomass (claimed).
NOVELTY - This utility new type provide the livestock and poultry cultivation wastewater marsh gas tank comprise tank body, a water inlet tube, a water distributor, a pneuma device water outlet tube, a gas storage room pneuma and marsh gas tube, a pneuma. lifting the tank body, the tank body divided into upper, lower two a area, the upper area is a precipitation zone, a lower part area is a reaction area, a water outlet tube and the settling zone connected; a water distributor located at inner reaction area, and the tube connected with the water inlet, a pneuma room storage tank body located on the top of said gas tube and the pneuma room connected. This utility new type disclosed livestock and poultry cultivation wastewater marsh gas pool, pneuma lifting device has gas load into the hydraulic load, it can increase efficiency of waste water anaerobic digestion, and set with the reaction area and a precipitation zone, a valid reduces the marsh gas for lifting effect of sludge, which avoids the excessive loss, so the biogas liquid in sludge content, for the subsequent process creates beneficial condition of a sludge. This utility new type a for a livestock and poultry cultivation waste water.
NOVELTY - A one intensified de-nitrification multi-medium soil layer system claims a reinforced multi-medium one soil layer system of denitrification, it can remove valid water body contamination, surface source pollution, at the same time through structure optimization, valid increase denitrification effect. This utility new type which comprise water distribution system and nitrogen removal system, a water raw water tank through a pump and a connecting nitrogen, denitrification system is device inner shell is divided into the water layer, a soil layer a lower two layer, the bottom is the water tube. A claims structure of this utility new type not only can satisfy for removal of organic matter and nitrogen, phosphorus, at the same time, can solve the problem that the traditional soil water filter system for total nitrogen removal rate is not high, it is not easy to be blocked, a use life is long. This utility new type not only can be used for river treatment, further a used for other sewage treatment.
NOVELTY - This utility new type relates to sewage treatment field, especially one with balance weight body of a biological carrier. Biological carrier with balance weight body of this utility new type provide a include biological carrier and a balance weight body, a biological carrier packed balance weight, a biological carrier is porous structure, said biological carrier comprise first attached layer and second adhered layer, a first attaching layer and second adhered layer set with a support layer, a first attaching layer is provided with a connected hole. With balance weight body of the biological carrier can make the nutrition substance in a external water easily entering into the biological carrier, which is good for biological carrier to a microorganism of the growth and propagation, with balance weight body so as to make the biological carrier has more of a biological adhesion area.
NOVELTY - This utility new type provide a one removing sewage treatment device of nitrate in underground water. Said sewage processing device comprise water pump, argon bottle pneuma and sewage treatment reaction column, a sewage processing reaction column is a hollow cavity of upper, lower seal, lower from the inner sewage treatment reaction column of hollow upwards in turn fill quartz sand layer, attapulgite/nano-iron composite material-microorganism coupling reaction layer and quartz sand, a water pump and the argon bottle a pneuma connected through the top part of the water inlet tube and the pneuma tube and sewage treatment reaction column body, is provided with a water outlet at the bottom of the sewage treatment reaction column. This utility new type via attapulgite/nano-iron composite material-microorganism coupling absorbing and degrading the nitrate, the nitrate into nitrogen and most other gaseous nitride, the nitrate pollution in underground water a valid treatment, the device for sewage process does not produce ammonia nitrogen, not for water would cause a secondary pollution.
NOVELTY - A one tube type excrement and organic garbage sewage treatment device, comprise: anaerobic fermentation part, a gravity filter part and fertilizer water conveying part. The upper anaerobic fermentation part include: first collecting pipe, anaerobic fermentation tube, marsh gas output tube, pneuma taking pneuma valve, second collecting pipe, a tube bottom, filter vent hole, fertilizer discharge pipe a, first collecting tube connecting tube anaerobic fermentation, anaerobic fermentation tube connecting with a marsh gas output tube, a marsh gas output tube mounting with a biogas pneuma taking pneuma valve, marsh gas output tube of bottom part with a bottom tube, a tube bottom with a filter through hole, anaerobic fermentation tube connecting with plural second collecting pipe, a right end of anaerobic fermentation tube connect with water discharge pipe. The first time the it with the pipeline seal, and a first-in first-out according to the the discharge, at the same time, lengthened pipeline conveying to the field in need of head.
NOVELTY - This utility new type relates to a one farm sewage recycling treatment system, a separate dry-wet system, solid-liquid separate system, sewage treatment integrated system, efficient composite ecological system, farm waste water recycling system, wherein the sewage treatment integrated system include regulating pool, a hydrolysis acidification pool, biological contact oxidation tank, efficient composite ecological system include efficient composite biological pond, farm waste water recycling system comprise solar energy ozone sterilizing tank and recycling tank, solid-liquid separate tank, a regulating tank, a hydrolysis acidification pool, biological contact oxidation pond, efficient composite biological pond, solar energy ozone sterilizing tank and recycling tank in turn. The system design one set suitable for breeding field waste water recycling new mode, realize the cultivation farm dung dirt near zero emission of, promoting the virtuous circulation and sustainable development of industry of farm waste.
NOVELTY - This utility new type claims a new-type efficient one aerobic composting device comprise blast device, compost reactor, stir device, collecting port, tapping, circular sampling hole, circular baffle plate, small holes. A part cylindrical part of collecting pneuma compost reactor by opening the upper part set with the lower part of the conical part is composed of compost reactor upper part cylindrical part with the lower part conical connecting part set with circular baffle is provided with a small hole, a circular baffle plate set with filter cloth, forming aeration room. Drum wind device through the bottom of a pipeline and the compost reaction device, in compost reactor is equipped with a spiral stirrer stir shaft, a compost reactor upper part cylindrical part is divided into left and right two part, the left and right two movable connecting part, seal. Compost reactor upper part cylindrical part along the vertical direction set with sampling hole, compost reactor lower cone part set with opening. This utility new type is convenient, is convenient to remove osmosis liquid, which is good for uniform aeration and so on.
(CN203683476-U)   NOVELTY - This utility new type claims a one hot air heating type biomass cracking machine, include cracking chamber, said cracking chamber is mainly composed by a shell and a charging barrel is set on the inner shell, material cylinder between the periphery of the inner wall and the outer shell of a gap between said shell and one end close to the material barrel of the gap is connected set with a hot air discharging tube, a shell and close to the other end a material barrel of the gap is connected set with a hot air discharging tube, a air discharging tube set with a exhaust fan. In said gap and set with spiral air channel along the axial direction of material cylinder, two end a spiral air channel of a connected with said air discharging tube and hot air discharge tube, so as to prolong the hot air in the shell inner of residence time, to realize fully heat exchange of. Because of using said hot air heating of structure forms, which not only reduces the energy consumption and has energy saving and environment protection, and a biomass heating more uniform, but also has good effect of cracking.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the hot-air heating type biomass pyrolysis machine.    Shell (1)    Cylinder (2)    Hot-air inlet pipe (3)    Hot-air outlet pipe (6) Exhaust fan (4)
NOVELTY - The utility model is a new type claims a one environment-friendly energy-saving furnace, comprise straw furnace and combustion stove, a connect with one air inlet tube on the top part of furnace and the bottom of the straw combustion cooking range and connect with one air inlet tube, the air inlet tube are connected with one air blower is connected with lower part of straw furnace one side surface through gas tube connecting with one a gas purification chamber, the top surface middle part of gas purification chamber downwards extending with one set with a clapboard, lower clapboard and the gas purification chamber bottom end there is a gap between the upper part of two side baffle plate and a gas purification chamber lower part two side wall inclined set with the upper and lower fin, a fin and a purification chamber wall and a lower fin and a set with a gap between the clapboard, gas purification chamber top surface the other side through an air outlet tube in turn connect with a water jacket boiler and one of said combustion stove.
NOVELTY - This new type utility claims one a rural biomass energy comprehensive utilization system. It comprise orderly connected a marsh gas generator, a pre-processing device, a liquefied, the liquefied natural gas storage tank, the liquefied natural gas carburettor, pneuma engine, a preprocessing device for the refrigeration device, an absorber or reactor, said reactor is alkaline solution and metal oxide, a reactor of removing carbon dioxide and sulfureted hydrogen in biogas; said liquefied device is a refrigeration device or low temperature fluid supply heat exchanger of cold quantity. The utility model is a new type based on energy utilization technology of the traditional biomass into the low temperature liquefaction process and a containing about 50-70 wt % of a biogas purifying and is converted into liquefied natural gas of high purity, increase the application value of biological marsh gas, expands the application field of biomass utilization field provide the a one hot, cold and so on multi-element generate a new method.
NOVELTY - This utility new type relates to a one continuous layered tower biology diesel oil preparation device, belonging to the field of chemical industry. This utility new type include center tube I, a main tower, raw oil, catalyste, water and sulphuric acid inlet tube, separate disk, methyl filter, valve I, a valve II, a centre tube II, an evaporation disk, methanol, main reaction disk, pump, methanol tank, pre-heating disk, a condenser, a methanol steam tube, support pole I, pole II support, said tower is a four layer structure, the first layer is pre-heating device by centre tube I, pre-heating disk is composed of the second layer main reaction disk, support pole I, third layer is a centre tube II, an evaporation disk, fourth layer is a separate disk, support pole. This utility new type the preheating, ester exchange reaction, separate a methanol recovery and the glycerol and methyl ester is divided into four in one tower inner layer, a simple structure, low cost and high efficiency.
NOVELTY - This new type utility claims one a hydrogen-oxygen generator, comprise shell and set in the shell of the electrolytic groove and the inner electrode group, wherein, a further comprise: power supply converter, input end of said power supply converter is connected with an external power source connecting, a converter of power supply output end and a connecting group, a power supply converter converts the external power source of a voltage convert is low voltage, and the low voltage is transmitted to said a group. This utility new type embodiment is connected with the power source through the hydrogen-oxygen generator on the outer set between the anode and the cathode electric source converter, the outer is connected with the power source a voltage convert is low voltage, and the low voltage is transmitted to said a group, so it can prevent electrolytic solution due to the high voltage occurs, the hydrogen-oxygen generator cell of the hydrogen purity increase, hydrogen a mass, and a lower low electrolytic voltage, such that the whole device temperature maintain stable in the operation process, so as to prolong the use life of hydrogen-oxygen generator.
NOVELTY - This new type utility claims one a hydrogen-oxygen generator, belonging to the field of electrochemical device field. Oxyhydrogen generator comprise: a shell, a fixing plate, a lower shell, a group, a pneuma hole and guide cylinder, a shell, a fixing plate and lower shell from the upper to the lower in turn connecting, a group set on the lower shell, the pneuma hole set up on the fixing plate, an air cylinder set with a shell, an air cylinder set on the upper fixing plate, an air cylinder and the guide hole connected pneuma, working time, a group a cell in the lower shell, for producing metallic titanium by electrolysing hydrogen and oxygen through a guide hole, entering into a air cylinder shell. This utility new type through the pneuma hole and set with a guide cylinder on the fixing plate to make the hydrogen and oxygen for producing metallic titanium by electrolysing up from a lower shell is injection shaped entering into shell, which can effectively of the hydrogen for producing metallic titanium by electrolysing and oxygen mix uniformity, the stable gas from the utility model is a new type in a, time as auxiliary fuel can be a stable combustion-supporting, the utility model is new type detachable and easy to clean, valid of the use thereof.
NOVELTY - This new type utility claims one electrode group and a hydrogen-oxygen generator, said electrode group include: a multi-electrode plate and a grid plate, a location grid plate set up with a multi-grid, said a multi-grid are set up on a a gate plate, a multi-electrode a a sheet is inserted in the said multi-correspond to a grid groove in. This utility new type spline of fixed electrode plate through a grid plate in, and restrain the distance of between the electrode, to make a sheet of uniform interval, such that produce a hydrogen also, so that electrolytic produce hydrogen is faster and more smoothly and increase hydrogen production quality, and a grid plate has reinforcing effect, which avoids the working process in a produce shaking so that the whole device steady working, and using a grid plate mounting a chip operation is simple and convenient, increase the mounting efficiency.
NOVELTY - This utility new type claims a one inhibitor oscillation type hydrogen-oxygen generator, belonging to the field of electrochemical device field. Said oscillation suppression type oxyhydrogen generator comprise: a shell, a fixing plate, a lower shell, a group, oscillation plate, pneuma hole and guide cylinder, a shell, a fixing plate and lower shell from the upper to the lower in turn connecting, a group set in the shell, the lower plate set with a group on the inner wall of the lower shell, oscillating plate for preventing the electrolyte, the pneuma hole set up on the fixing plate, an air cylinder set with a shell, and guide cylinder set up on the fixing plate, an air cylinder and the guide hole connected pneuma. This utility new type through the pneuma hole set on the fixing plate and a pneuma hole connected with a gas guide cylinder, the hydrogen and oxygen for producing metallic titanium by electrolysing up from a lower shell is injection shaped entering into shell of the hydrogen for producing metallic titanium by electrolysing and oxygen mix uniform, time the gas as auxiliary fuel can be a stable combustion-supporting, the utility model is new type detachable and easy to clean, valid of the use thereof.
NOVELTY - This utility new type relates to a clean energy of one preparation device, in particular to a one through electrolytic water to producing hydrogen, a hydrogen-oxygen of oxygen, comprise a, through cable connecting a power supply of the electrolytic groove, connected with the electrolytic groove through connecting a liquid storage tank, an electrolytic groove of groove body of a one a side wall set with an electrolytic groove liquid inlet, a relative side wall set with a groove with an electrolysis liquid and electrolysis groove outlet, a liquid storage tank through a pipeline and the electrolytic groove liquid inlet of a electrolytic groove, the electrolytic groove liquid, the electrolytic groove is connected with air outlet, set with a liquid circulation pump up one of pipeline between the liquid storage tank and the electrolytic groove liquid inlet, liquid storage tank is connected in series with water cooling tank in turn pneuma and separate liquid tank through a pipeline connecting a pipeline between washing pneuma tank, a liquid storage tank with the pneuma; a pneuma washing tank through gas output valve connect with gas output pipeline, this utility new type has electrolytic efficiency is high,' consumption, low temperature control effect is good, control is simple, malfunction rate is low, the property of..
NOVELTY - This new type utility claims one a hydrogen-oxygen generator, belonging to the field of electrochemical device field. A hydrogen-oxygen comprise shell, rooms, a group, a group base, spacer film and electric conduction joint, electrolytic room set in the shell, a group set with the electrolytic room at lower side in the base, a group in a group set with a base, a group in each two adjacent of the electrode sheet are a. with a thin film, thin film separating the each two adjacent a of a sheet, electric conduction joint set in a group base and electric conduction joint and a connecting group and is a group. This utility new type through thin film spacer set between the adjacent electrode, the two sheet adjacent a sheet, the each one piece electrode plate produce a gas would not with other electrode sheet produce a gas mix, a high purity of hydrogen and oxygen, and this utility new type has simple structure, convenient processing, low cost and a wide application prospect.
NOVELTY - Waste incinerator generator comprises a garbage incinerator, preprocessing system, sorting system, crusher and a dewatering machine.    USE - Waste incinerator generator used for treating sludge by generating electric catalytic oxidation pool.    ADVANTAGE - Waste incinerator generator is eco-friendly and cost-effective.
NOVELTY - The furnace has a grate (1.3) connected with a gas generator (1), which is arranged at bottom part of an ash storage chamber (1.4). An inner surface of a hearth (2.2) is fixed with a fire-resisting layer (1.8). A combustion chamber (3) is located with a secondary air inlet and a regulating valve. A lower part of the hearth furnace is connected with a flue gas inlet (2.7). The flue gas inlet is connected with a chimney (4) and a furnace port (2.1). A water tank is located with an air suction furnace (2).    USE - Lower suction type biomass gasification furnace for family.    ADVANTAGE - The furnace reduces fuel consumption, and is convenient to add the material and easy to process, manufacture and clean, and has simple structure of the hearth.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a lower suction type biomass gasification furnace.    Gas generator (1)    Grate (1.3)    Ash storage chamber (1.4)    Fire-resisting layer (1.8)    Air suction furnace (2)    Furnace port (2.1)    Hearth (2.2)    Flue gas inlet (2.7)    Combustion chamber (3)    Chimney (4)
NOVELTY - Smoldering involves collecting agriculture and forestry waste. The obtained material is stirred uniformly, and then crushed to obtain powder biomass or biomass granule. The obtained material is set in a smoldering cabinet to separate biomass fuel layer and catalytic filter layer. The obtained biomass fuel layer and catalytic filter layer are placed in a standardized fuel smoldering cabinet. The obtained material is ignited. The obtained material is processed in a fuel tank for cleaning combustion residue (plant ash), where bulk density of biomass fuel layer is 200-300 kilogram per cubic meter.    USE - Method for smoldering (claimed).    ADVANTAGE - The method is simple and eco-friendly.    DETAILED DESCRIPTION - Smoldering involves collecting agriculture and forestry waste. The obtained material is stirred uniformly, and then crushed to obtain powder biomass or biomass granule. The obtained material is set in a smoldering cabinet to separate biomass fuel layer and catalytic filter layer. The obtained biomass fuel layer and catalytic filter layer are placed in a standardized fuel smoldering cabinet. The obtained material is ignited. The obtained material is processed in a fuel tank for cleaning combustion residue as plant ash, where the bulk density of biomass fuel layer is 200-300 kilogram per cubic meter. The thickness of fuel layer and catalytic filter layer is more than 30 centimeters, and 5-6 centimeters, respectively. Catalytic filter layer is biomass ash, which comprises a mixture of non-crystallized metal oxide and silicon dioxide.
NOVELTY - This utility new type belongs to the vehicle maintaining oil saving field, especially claims a vehicle hydrogen oxygen maintenance oil saving system, include power supply, water electrolysis hydrogen-oxygen generator, an intelligent controller and a capacity sensor, a capacity sensor with the intelligent controller set on the water electrolysis hydrogen-oxygen generator of inner electric connecting, a water electrolysis hydrogen-oxygen generator of inner set with a temperature sensor, a temperature control component and the water level sensor, the temperature sensor, the temperature control part and the water level sensor are electrically connecting with the intelligent controller, water electrolysis hydrogen-oxygen generator of gas output end set with an air outlet tube, the the pneuma tube with the gas-liquid separate device is connecting, gas-liquid separate device of air outlet is provided with an air outlet set with a pipeline, the pipeline is set with the air inlet of vehicle air filter, an intelligent controller and the ignition/flameout and brake circuit of a vehicle key connect, the device engine in the carbon to catalytic combustion with the fuel so as to save oil and emission reduction, the purpose of maintaining engine.
NOVELTY - This utility new type claims a biomass secondary cracking of one device, comprise feeding port, an exhaust port, a combustion room and a slag discharging port, a feeding port connecting with the combustion chamber, discharge port set in the combustion room above the slag discharging port set below the combustion chamber, combustion room comprise drying area, reducing area, reaction area, a gas space, the catalyste bed and heat collecting device, drying area, area reduction and oxidation reaction area located on the combustion chamber below the drying area and the reducing area, reduction area and reaction area is connected, space is located above the drying area, the catalyste bed set in the gas space above the waste heat collecting device set in the combustion room. The utility model reduces the valid smoke dust and harmful gas SO2, NOX discharge of smoke and to make the environment-friendly energy-saving index is far better than the national standard, saves electrical energy about more than 30%, convenient maintenance, saves maintenance cost for biomass catalytic pyrolysis gasification and boiler combined.
NOVELTY - This utility new type claims a light non-infrared gas detector, infrared light source comprise, pneuma room, an infrared sensor, sensor measurement and control system, as improved, of said infrared light source is a pulse infrared light source, a pre-amplification circuit of said infrared sensor integrated infrared sensor a, a of infrared light source, pneuma room, an infrared sensor set on the same one light axis a. This utility new type gas detector through using electric modulating pulse infrared light source, which saves the traditional method of machinery in a part, pre-amplification circuit of infrared sensor integrated infrared sensor a, attenuating the infrared sensor a weak signal and a external signal interference. Infrared sensor at high precision by narrow band filter integrated circuit and a single-beam double-wave length, match of easily detachable coating pneuma room and data collect system, it can realize CO2, CO, NOx, fast real time of CH4 and SO2 gas measuring time.
NOVELTY - A reduction agent is prepared by isolating sample from soil and river using modern microbial separation and purification, adding microbial agent containing photosynthetic bacteria:Bacillus subtilis:Serratia marcescens:lactic acid:anaerobic Clostridium:denitrifying bacteria:Sphaerotilus:fermented filamentous bacteria with ratio of 6:4:3:3:5:3:4:5, culturing to obtain bacteria seed, inoculating in liquid composite culture medium, culturing at 28 degrees C, and adjusting pH to 7-9 in which weight ratio of bacteria seed:liquid composite culture medium is 1:30-80.    USE - Preparation of reduction agent for degradation of organic sludge (claimed).    ADVANTAGE - Product has high degradation rate and good deodorizing effect and is environment-friendly and safe to humans.    DETAILED DESCRIPTION - A reduction agent is prepared by isolating sample from soil and river using modern microbial separation and purification, adding microbial agent containing photosynthetic bacteria:Bacillus subtilis:Serratia marcescens:lactic acid:anaerobic Clostridium:denitrifying bacteria:Sphaerotilus:fermented filamentous bacteria with ratio of 6:4:3:3:5:3:4:5, culturing to obtain bacteria seed, inoculating in liquid composite culture medium, culturing at 28 degrees C, and adjusting pH to 7-9 in which weight ratio of bacteria seed:liquid composite culture medium is 1:30-80 and weight ratio of bacteria seed:liquid composite culture medium:water is 1:1:2, and culturing in liquid composite culture medium.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of preparation of reduction agent. (Drawing includes non-English language text).
NOVELTY - Biofertilizer comprises 20-40 pts. wt. Bacillus subtilis, 20-40 pts. wt. Bacillus megaterium, 10-30 pts. wt. Bacillus mucilaginosus, and 30-50 pts. wt. Azotobacter.    USE - The biofertilizer is useful for: promoting growth of a plant; and preventing bacterial diseases in plant.    ADVANTAGE - The biofertilizer exhibits improved synergistic effect and improves quality of the agricultural products.
NOVELTY - Efficient enzymatic organic fertilizer manufacturing method comprising fermentation of raw materials, is claimed.    USE - The method is useful for manufacturing efficient enzymatic organic fertilizer (claimed).    ADVANTAGE - The method is pollution-free, increases product quality, restrains soil-borne disease, enhances stress resistance of crops by promoting earliness of crops and directly increases the soil organic matter e.g. nitrogen, phosphorus, potassium and other nutrient.
NOVELTY - Preparing organic fertilizer comprises (a) crushing crop straw and poultry feather and carrying out steam explosion treatment to obtain a straw blasting material and feather blasting material, (b) mixing the straw blasting material, the feather blasting material and aerobic activated sludge to obtain mixture, (c) carrying out compost fermentation of the mixtures, and (d) drying the post-fermentation mixture, crushing and drying the crushed material.    USE - The method is useful for preparing an organic fertilizer (claimed) used as a soil improver.    ADVANTAGE - The method prepares organic fertilizer by: replacing chemical process using steam explosion treatment; and degradation of poultry feather and crop straw thus promoting fermentation to regulate the C/N ratio.
NOVELTY - Improved efficient flower fertilizer comprises plant ash, carbon slurry, bean dregs and dreg mixture, hydrogen peroxide solution, yeast, diluted beer liquid, lime powder, aqueous ammonia and deionized water.    USE - Used as an improved efficient flower fertilizer.    ADVANTAGE - The fertilizer is economical, uses easily available raw materials, is prepared by simple preparation process, has strong fertility and faster fertilizer effect, has improved disease resistance ability, and assures strong and vigorous growth of flower.
NOVELTY - Improved flower fertilizer comprises dregs of fermenting solution, rapeseed cake fermented solution, bovine heart sub-powder, pyrethroid, potassium permanganate solution, fallen leaves humus soil and diluted beer liquid.    USE - The fertilizer is useful for improving soil vitality, and increasing the resistance of flowers.    ADVANTAGE - The fertilizer has pleiotropic effect, and trace elements required for flowers, and shelf-life of up to 6 months,a nd no side effects; is rich in nutrients, chlorine, phosphorus pentoxide and potassium oxide; promotes complete nutrient absorption by the flowers. The method utilizes adequate sources of raw materials; is simple, economical, and environmental friendly; and has high efficiency.
NOVELTY - Producing liquid substance slow release carrier using industrial waste material comprises adding water into the waste liquid, adding silicon and aluminum containing waste substances and thermal catalyst waste, heating the waste to form covalently bonded ceramic, and crushing into cluster or powder; or adding water into the waste liquid, adding thermal catalyst waste, heating the waste to form covalently bonded ceramic, and crushing into cluster or powder.    USE - The slow release carrier is useful for improving soil absorption capacity and in plant cultivation (claimed) as artificial soil.    ADVANTAGE - The slow release carrier improves soil quality and prolongs the release time of the liquid substance. The method eliminates use of potential toxic components and thus reduces accumulation of waste, and is economical and environmentally friendly.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) the liquid substance slow release carrier useful in plant cultivation material, comprising aluminum compound, silicon compound and covalently bonded ceramic structure, where the particle size of the carrier is 0.5-100 mm; and    (2) use method of the liquid substance slow release carrier, comprising spreading the carrier on the soil to improve soil absorption capacity, where the particle size of the carrier is 1-300 mm.
NOVELTY - Clean gasoline comprises 30 pts. wt. methanol, 25 pts. wt. 190 solvent oil, 15 pts. wt. light hydrocarbon oil, 25 pts. wt. condensate, 5 pts. wt. methyl tertiary-butyl ether, 1.2 pts. wt. isopropyl alcohol, 1 pts. wt. ethylene glycol, 1-3 pts. wt. aniline, 0.5 pts. wt. isopropanolamine, 1 pts. wt. ether, 0.3 pts. wt. acetamide, 0.5 pts. wt. formic acid pentyl ester, and substances including 0.00001-0.00005 pts. wt. polyisobutylene succimide dispersant (T152), 0.1 pts. wt. benzotriazole fatty acid amine salt (T406) and 0.2 pts. wt. zinc dialkyl dithio phosphate (T202).    USE - The clean gasoline is useful for a vehicle.    ADVANTAGE - The clean gasoline has high octane content and improved anti-knock performance, and can be energy-efficiently prepared in an environmentally friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the clean gasoline comprising mixing raw materials including 25 pts. wt. 190 solvent oil, 15 pts. wt. light hydrocarbon oil, 25 pts. wt. condensate, 5 pts. wt. methyl tertiary-butyl ether, 30 pts. wt. methanol, 1.2 pts. wt. isopropyl alcohol, 1 pts. wt. ether, 1-3 pts. wt. aniline, 0.5 pts. wt. isopropanolamine, 0.3 pts. wt. acetamide and 0.5 pts. wt. formic acid pentyl ester in a tank, and uniformly stirring the mixture at a temperature of 70 degrees C for 20-30 minutes.
NOVELTY - Processing oil from soapberry seed, comprises separating fruit, kernel and shell from soapberry using an air separation equipment, then boiling the fruit using a steam boiler by adding activated carbon carrier, steaming and frying the fruit using a continuous steaming and frying device, pressing the seed using a spiral presser to obtain oil, and then filtering the oil.    USE - The method is useful for processing oil from soapberry seed, where the oil is used as biodiesel oil (claimed).    ADVANTAGE - The method produces the oil with rich fat, protein and starch content, acid value of 4 mg (potassium hydroxide)/g and high quality.
NOVELTY - Processing soapberry biodiesel comprises squeezing soapberry nucleolus to extract crude oil, mixing the crude oil with methanol and acid catalyst, preheating, and esterifying; carrying out dealcoholation; adding dealcoholated oil phase into separator, reacting with glycerol and methyl ester, so as to separate soapberry; mixing methanol, soapberry oil and alkali catalyst dissolved in methanol; adding into dealcoholated column, and conducting dealcoholation; reacting with glycerol and methyl ester; washing the separated methyl ester and drying to obtain crude methyl ester; and flash refining.    USE - The method is useful for processing soapberry biodiesel (claimed).    ADVANTAGE - The method: uses high acid value grease as raw material; is simple, has low device investment and production cost; has short reaction time short, and produces the product with quality stable, so as to reach the international standard; and is environmentally-friendly.    DETAILED DESCRIPTION - Processing soapberry biodiesel comprises (i) squeezing soapberry nucleolus to extract crude oil, and mixing the crude oil with methanol and acid catalyst, preheating, adding into esterification reactor, and esterifying at 100-110 degrees C under the gas phase; (ii) adding into dealcoholation tower, and flash distilling to remove alcohol; (iii) adding the dealcoholated oil phase into the separator, reacting with glycerol and methyl ester, so as to separate soapberry; (iv) mixing methanol, soapberry oil and alkali catalyst dissolved in methanol, and adding into alcoholysis reactor, and conducting alcoholysis; (v) adding into dealcoholated column, and conducting dealcoholation; (vi) adding the reaction solution into the separation column, and separating by reacting with glycerol and methyl ester; (vii) washing the separated methyl ester with water, and drying to obtain crude methyl ester; and (viii) flash refining the crude methyl ester.
NOVELTY - Biodiesel prepared by mixing tetramethylammonium hydroxide as a catalyst, with methanol, Cyperus esculentus oil, and fatty acid ester including fatty acid methyl ester and glycerol, is claimed. The tetramethylammonium hydroxide is mixed with the methanol to increase the activity of methanol, and the mixture is heated to 60 degrees C and refluxed for 0.5 hours to prepare alcohol salt.    USE - Biodiesel.
NOVELTY - Preparing bortezomib, comprises e.g. (i) protecting isobutylboronic acid with pinanediol to obtain a compound (I), (ii) subjecting (I) to hydrogen abstraction, and carrying out rearrangement to obtain compound (II), (iii) reacting (II) with hexamethyldisilazane to obtain compound (III), (iv) removing trimethylsilyl groups of (III) to obtain compound (IV), (v) protecting (IV) with tert-butoxycarbonyl (Boc)-L- phenylalanine, (vi) removing Boc protecting group to obtain (VI), (vii) carrying out condensation of (VI) with pyrazine-2-carboxylic acid, and (viii) removing pinanediol protecting group.    USE - The method is useful for preparing bortezomib (claimed).    ADVANTAGE - The method: utilizes cheap and easily available raw materials; has mild reaction conditions, simple operation, low production cost and less demand for production equipment; does not utilizes heavy metal compounds; produces product with purity of 99.5% and yield of 82%; and is suitable for industrial production.    DETAILED DESCRIPTION - Preparing bortezomib, comprises (i) protecting isobutylboronic acid with pinanediol to obtain a condensation compound (I), (ii) subjecting (I) to hydrogen abstraction, and carrying out rearrangement reaction to obtain compound (II), (iii) reacting (II) with hexamethyldisilazane to obtain compound (III), (iv) removing trimethylsilyl groups of (III) to obtain compound (IV), (v) protecting (IV) with tert-butoxycarbonyl (Boc)-L- phenylalanine to obtain compound (V), (vi) removing Boc protecting group of (V) to obtain (VI), (vii) carrying out condensation of (VI) with pyrazine-2-carboxylic acid to obtain (VII), and (viii) removing pinanediol protecting group of (VII) under action of isobutylboronic acid to obtain final product.
NOVELTY - An intelligent control system comprises greater than or equal to 1 solar energy water heater (1) and biogas digester (2) in which water temperature probe (3) is set in solar energy water heater, tank temperature probe (4) is set in biogas digester, solar energy water heaters are connected in series to biogas digester by pipe (5), pipe is mounted with intelligent temperature controller (6), intelligent control circulating pump (7) is installed between intelligent temperature controller and biogas digester, and control valve (9) is installed on inlet pipe (8) of solar water heater.    USE - An intelligent control system for heating solar energy biogas digester during medium-temperature fermentation (claimed).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of intelligent control system.    Solar energy water heater (1)    Biogas digester (2)    Water temperature probe (3)    Tank temperature probe (4)    Pipe (5)    Intelligent temperature controller (6)    Intelligent control circulating pump (7)    Inlet pipe (8)    Control valve (9)
NOVELTY - Preparation of functional organic fertilizer, involves (a) pulverizing tourmaline to a particle size of 300 nm-1, (b) crumbling rice straw to 1-10 cm long, (c) mixing livestock manure and straw solids in weight ratio of 1:0.5-5, adding crushed 1-2 kg tourmaline into mixture, mixing the mixture uniformly, following basic flow of biogas, fermenting the mixture, cleaning biogas digesters in tourmaline, and obtaining product.    USE - The method is useful for preparation of the functional organic fertilizer (claimed).    ADVANTAGE - The method increase biogas yield, increases yield to 20-50%, increases chemical oxygen demand removal rate to 8-18%.
NOVELTY - A device for regulating chicken laying hen comprises egg laying unit integrated into composite sheet comprising foam core in middle, magnesite material in outer side, and glass fiber composite, heat preservation and ventilation unit for ventilating the egg laying hen from underground, and sealed fermentation unit for collecting and fermenting chicken manure, where fermented chicken manure is discharged by delivering unit.    USE - Device for regulating chicken laying hen.    ADVANTAGE - The device saves energy more than 20%, increases beneficial value by 35%, and is environmentally-friendly and cost-effective.
NOVELTY - This utility new type claims a one town household energy-saving ring maintaining a balance device, it relates to micro-ecological farm device technology field, one end of water purifier through second net water return water tube and the fish main connecting bucket, upper end of water purifier through micro-organic matter input tube and the organic liquid fertilizer for connecting, organic liquid fertilizer for one end of organic liquid fertilizer conveying tube through one end and the organic vegetable planting area of connecting pipeline, and the other end the organic vegetable planting area of pipeline through organic fertilizer waste water recovery tube with organic fertilizer waste water recoverer connect. It structure design is reasonable, operation is convenient to use, accessory combination and maintenance is easy to change, it not only can fish a vegetable is combined with the balcony roof also can be a flower combination, solves the problem that the valid instant fish using safety of residents, family young children know the agriculture, ecological agriculture knowledge increases, the old man and a household as, a, adding harmonious with domestic happiness.
NOVELTY - Regulator comprises 6-10 wt.% of Astragalus, 7-12 wt.% of bighead Atractylodes rhizome, 6-10 wt.% of rhizoma polygonati, 5-9 wt.% of licorice, 8-12 wt.% of nutmeg, 5-9 wt.% of caulis polygoni multiflori, 6-11 wt.% of basil leaves, 8-12 wt.% of Ginkgo biloba, 6-9 wt.% of mulberry, 8-14 wt.% of tea, 1-3 wt.% of probiotics, 1-3 wt.% of lysine, 1-3 wt.% of thiamine, 1-3 wt.% of cysteine, 6-10 wt.% of pine needle powder, 0.01-0.03 wt.% of metallothionein crude extract powder and 5-11 wt.% of barley flour.    USE - The regulator is useful in feed for improving meat flavor of pork (all claimed).    ADVANTAGE - The regulator can be prepared in a cost effective and eco-friendly manner with high resource utilization rate and without adding any antibiotic and chemical medicines, improves physiological function and immunity of pig and increases production property of pig.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for feed comprising 1-8 wt.% of regulator.
NOVELTY - Feed immunity enhancer comprises Cordyceps militaris bioactive components and other nutrients.    USE - Feed immunity enhancer used for regulating immune function and improving disease prevention and disease resistance of poultry, livestock and aquatic animals.    ADVANTAGE - The feed immunity enhancer avoids drug abuse, ecological environment degradation, drug resistance and drug residue, while increasing feed utilization rate and promoting animal growth; and has low cost. Preparation method is simple and environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for feed immunity enhancer production by culturing C. militaris for 50-60 days, picking fruiting bodies, and precrushing Cordyceps base into 2-4 mm; vacuum drying at low temperature until water content is 7-8%; ultrafine crushing into 100-200 meshes with high-velocity gas stream; and sieving and uniform mixing.
NOVELTY - Preparation of prasugrel tablet comprises mixing prasugrel drug as raw material and additives comprising mannitol, gelatin, polyvinyl pyrrolidone and/or hydroxypropyl cellulose, setting twin-screw melt extruder at 100-150 degrees C, extruding materials, pulverizing to obtain 80-120 mesh powder, and pressing.    USE - Method for preparing prasugrel tablet.    ADVANTAGE - The tablet has high dissolution rate and good stability when subjected to acceleration test after 6 months. The simple, energy-saving and environment-friendly method has high degree of automation and meets industrial production requirement.
NOVELTY - Preparation of traditional Chinese medicine comprises mixing Uncaria, radix bupleuri, Angelica, rhizoma ligustici wallichii, rhizoma atractylodis, tuckahoe and licorice, adding ethanol-water or water to carry out reflux, combining extracts, and concentrating until no more alcohol taste; and eluting through macroporous resin column with ethanol-water gradient system, collecting ethanol eluent, and recovering solvent to carry out separation of medicine valid parts.    USE - Method for preparation of traditional Chinese medicine used for treating senile dementia (claimed).    ADVANTAGE - The method utilizes separation and modern pharmacological experimental method and it has neuroprotective effect.    DETAILED DESCRIPTION - Preparation of traditional Chinese medicine comprises mixing 6 pts. wt. Uncaria, 4 pts. wt. radix bupleuri, 6 pts. wt. Angelica, 6 pts. wt. rhizoma ligustici wallichii, 8 pts. wt. rhizoma atractylodis, 8 pts. wt. tuckahoe and 3 pts. wt. licorice, adding 5-15 times ethanol-water or water to carry out reflux 2-4 times for 1.5-4 hours, combining extracts, and concentrating until no more alcohol taste; and eluting through macroporous resin column with 6-10 times 0-95% ethanol-water gradient system, collecting 30-50% ethanol eluent, and recovering solvent to carry out separation of medicine valid parts.
NOVELTY - Preparation of double ginger tablet comprises taking 200 g rhizoma curcumae longae, 200 g purple ginger, 200 g radix stephaniae epigaeae, 200 g grassleaf sweelflag and 200 g rapeseed, crushing, adding ethanol, extracting, concentrating, adding Diaion HP-10 (RTM: Adsorbent resin), eluting with ethanol, recovering ethanol, concentrating, drying, extracting, adding starch, pelletizing, drying and encapsulating.    USE - Method for preparing double ginger tablet used for treating stomach ache and inhibiting murine Leydig tumor cell line-1 propagation (all claimed).
NOVELTY - Preparing molten state ion exchanged molecule sieve membrane comprises (a) loading the metal salt having the melting point lower than the calcination temperature on templating agent removed molecule sieve membrane; and (b) drying and performing ion exchange reaction at a temperature below the calcination temperature and higher than the melting point of the metal to salt to get molten state ion exchanged molecule sieve membrane, where the calcination temperature is removing the templating agent from molecular sieve membrane.    USE - The molten state ion exchanged molecule sieve membrane is useful for separating gas from acid gas system (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for the use of molten state ion exchanged molecule sieve membrane in gas separation process from acid gas system, where the acid gas system is carbon dioxide-methane system, carbon dioxide-hydrogen system and carbon dioxide-nitrogen system.
NOVELTY - A magnesium-oxide solid alkali catalyst contains magnesium element and oxygen element.    USE - Magnesium-oxide solid alkali catalyst is used in preparation of biodiesel oil (claimed).    ADVANTAGE - The magnesium-oxide solid alkali catalyst is manufactured efficiently with excellent workability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of magnesium-oxide solid alkali catalyst; and    (2) usage of magnesium-oxide solid alkali catalyst.
NOVELTY - Preparing solid alkali catalyst comprises dissolving sodium acetate solid powder in distilled water to obtain 200g/l of sodium acetate solution, impregnating obtained sodium acetate solution with aluminum oxide for 24 hours, and drying the impregnated solution at 105 degrees C for 4 hours and then calcining at 500 degrees C for 3 hours, and naturally cooling.    USE - The method is useful for preparing solid alkali catalyst that is useful for preparing biodiesel (all claimed).    ADVANTAGE - The method is capable of preparing the solid alkali catalyst, which improves yield of biodiesel to 85.4%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing biodiesel using sodium oxide/aluminum oxide supported solid alkali catalyst, comprising adding methanol, soybean oil, and catalyst into 250 ml of three-necked flask according to a certain mole ratio and then stirring at constant temperature using a magnetic stirrer, heating the stirred mixture to react, filtering the reaction mixture, placing the filtered mixture in a separator funnel and then standing for 3 hours to obtain crude biodiesel and crude glycerin, and then decompressing and distilling obtained crude biodiesel and crude glycerin.
NOVELTY - The method involves placing a convex part with rectangle and triangle or wave-shaped upper and lower molds. Two block metal plates are formed with a cavity. An injection liquid working medium is fixed with the cavity. The liquid working medium is connected through a booster pump. An inner wall of the lower mold is fixed with the cavity to obtain a desired shape of a fuel cell bipolar plate. A sub-mold and a back mold are formed with a hole.    USE - Method for manufacturing a fuel cell bipolar plate.    ADVANTAGE - The method enables saving production time. The method enables simplifying manufacturing process in a simple and easy manner and ensuring low processing cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a fuel cell bipolar plate.
NOVELTY - A SAPO-34 molecular sieve membrane is prepared by mixing aluminum source, tetraethyl ammonium hydroxide (TEAOH), water, silicon source and phosphorus, heating, crystallizing, centrifuging, washing, drying to obtain adding SAPO-34 molecular sieve crystal seed coating, adding to porous carrier inner surface, mixing aluminum source, phosphorus source, silicon source, TEAOH, di-N-propylamine, water and fluoride to obtain synthetic mother liquid, heating, aging, crystallizing, and oven drying.    USE - Method for preparing SAPO-34 molecular sieve membrane used for separating carbon dioxide-methane, carbon dioxide-hydrogen gas and carbon dioxide and nitrogen gases (claimed).    ADVANTAGE - The molecular sieve has increased uniformity and stability. It has high gas permeability and carbon dioxide-methane selectivity.    DETAILED DESCRIPTION - A SAPO-34 molecular sieve membrane is prepared by mixing aluminum source, tetraethyl ammonium hydroxide (TEAOH), water, silicon source and phosphorus, heating at 170-210 degrees C, crystallizing for 4-7 hours, centrifuging, washing, drying to obtain adding SAPO-34 molecular sieve crystal seed coating, adding to porous carrier inner surface, mixing aluminum source, phosphorus source, silicon source, TEAOH, di-N-propylamine, water and fluoride to obtain synthetic mother liquid, heating at 80 degrees C, aging at 15-24 degrees C for 2-8 hours, crystallizing for 3-24 hours, and oven drying at 370-700 degrees C for 2-8 hours.
NOVELTY - Sewage or slurry is subjected to single-stage or multi-stage electro-flocculation treatment, floating slag is removed, and obtained product is processed. The electro-flocculation treatment is carried out using metal material of anode and cathode by applying constant current. The flow amount of biogas is 0.5-3 vvm.    USE - Method for removing hydrogen sulfide in biogas (claimed).    ADVANTAGE - The method economically enables removal of hydrogen sulfide in biogas with high processing capacity, by a simple process.
NOVELTY - Ecological floating bed device comprises wetland groove (1), aerator (2), perforated aeration pipe device (3), straw matrix (4), large aquatic plant (5), silk screen (6), and floating body (7) in which top of wetland groove is open, bottom of wetland groove is set with water hole, perforated aeration pipe device is connected with wetland groove and aerator, straw matrix is spread on perforated aeration pipe device, large aquatic plant is uniformly planted on straw matrix, straw matrix is covered with silk screen, and floating body is mounted on top of wetland groove.    USE - An ecological floating bed device for restoration of eutrophic water (claimed).    ADVANTAGE - Device has reasonable structure, retention effect, and excellent denitrification effect.    DETAILED DESCRIPTION - Ecological floating bed device comprises wetland groove (1), aerator (2), perforated aeration pipe device (3), straw matrix (4), large aquatic plant (5), silk screen (6), and floating body (7) in which top of wetland groove is open, bottom of wetland groove is set with water hole, perforated aeration pipe device is connected with wetland groove and aerator, straw matrix is spread on perforated aeration pipe device, large aquatic plant is uniformly planted on straw matrix, straw matrix is covered with silk screen, floating body is mounted on top of wetland groove, top to bottom sidewall of wetland groove is 1st over-water area (8) and 2nd over-water area (9), and straw matrix is rice straw stalk.    DESCRIPTION OF DRAWING(S) - The drawing shows an ecological floating bed device.    Wetland groove (1)    Aerator (2)    Perforated aeration pipe device (3)    Straw matrix (4)    Large aquatic plant (5)    Silk screen (6)    Floating body (7)    1st over-water area (8)    2nd over-water area (9)
NOVELTY - A refuse landfill is operated by filling waste garbage bulk layer, covering waste layer with yellow linen, removing yellow linen, and continuously pouring garbage waste layer.    USE - Operation of refuse landfill (claimed).    ADVANTAGE - Process is simple, convenient, low cost, safe, and environment-friendly.
NOVELTY - Method for degrading azo dyes in wastewater using bacteria, involves (a) inoculating Aeromonas DH-6 strain to Luria-Bertani (LB) medium, and performing culturing at 25-35 degrees C under speed of 150-200 revolutions/minute (rpm) in a shaker overnight to obtain large number of bacteria, and (b) inoculating 2-8% overnight culture to wastewater containing azo dyes, and regulating the pH at 3-7 and temperature at 5-45 degrees C for more than 4 hours.    USE - The method for degrading azo dyes in wastewater using bacteria (claimed).    ADVANTAGE - The method uses bacteria strong environment adaptability, and does not produce second pollution.
NOVELTY - Comprehensive treatment and resource utilization of aminonaphthol sulfonic acid comprises hydrolyzing 2-naphthylamine-1-sulfonate with 30-40% wastewater, reacting, extracting sodium sulfate, reverse extracting wastewater and extracting aminonaphthol sulfonic acid. Extractant comprises 10-30 wt.% trioctylamine and/or trialkyl tertiary amine, and 30-70 wt.% diluent.    USE - Method for comprehensively treating and resource utilizing aminonaphthol sulfonic acid (claimed).    ADVANTAGE - The method is economical and environment-friendly.
NOVELTY - Chicken manure biogas composition comprises (in wt.%): straw (35-40), Tibetan chicken manure (40-55) and microbial inoculum (1-5).    USE - Chicken manure biogas composition.    ADVANTAGE - The chicken manure biogas composition is simple to process and eco-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing chicken manure biogas composition, which involves adding straw, Tibetan chicken manure and microbial inoculum in a marsh gas tank to obtain desired product.
NOVELTY - Aquaculture device comprises an anaerobic assembled tank and a tank body, where a steel plate is connected with the assembled tank through a connecting bolt. A flexible pneuma cabinet increases the fermentation rate of the marsh gas. The tank body is made of polyvinyl chloride, where the tank body is filled with fresh pig manure and sewage. Water is added in the tank body. The raw material is adjusted by continuous-flow stirred-tank reactor integrated device, where biogas is generated by dehydration and desulfurization.    USE - Aquaculture device.    ADVANTAGE - The aquaculture device ensures improved thermal conductivity.    DETAILED DESCRIPTION - Aquaculture device comprises an anaerobic assembled tank and a tank body, where a steel plate is connected with the assembled tank through a connecting bolt. A flexible pneuma cabinet increases the fermentation rate of the marsh gas. The tank body is made of polyvinyl chloride, where the tank body is filled with fresh pig manure and sewage. Water is added in the tank body. The raw material is adjusted by continuous-flow stirred-tank reactor integrated device, where biogas is generated by dehydration and desulfurization. The biogas slurry is transferred in a concentrate tank for solid-liquid separation.
NOVELTY - Harmless treatment method of dead animal and organic waste, involves collecting all kinds of diseased livestock and poultry dead body and all kinds of livestock and poultry, and organic waste as processing material, mixing processing material with wooden meal and rice husk, adding water, mixing complex microbial agents and material, dividing decomposition process, adding microbial enzyme, sterilizing, stirring, killing common viruses, bacteria and parasite eggs in material, discharging tank, cooling bag, and processing mixture into organic fertilizer.    USE - The harmless method is useful for treatment of dead animal and organic waste (claimed).    ADVANTAGE - The method is simple, convenient to operate, energy-saving and environmentally-friendly.    DETAILED DESCRIPTION - Harmless treatment method of dead animal and organic waste, involves (a) collecting all kinds of diseased livestock and poultry dead body and all kinds of livestock and poultry, and organic waste as processing material, (b) mixing processing material with wooden meal and rice husk in a weight ratio of 5:1, and adding water until moisture content is 50-60%, (c) mixing complex microbial agents and material in a weight ratio of 1000:0.5-5, (d) dividing decomposition process into three stages, heating treatment tank, enhancing material temperature to 40-45 degrees C, maintaining constant temperature for 2-4 hours, regularly stirring mixture, providing air and good oxygen, mixing material at 65-70 degrees C, maintaining constant temperature for 6-8 hours, regularly stirring mixture, adding microbial enzyme, sterilizing mixture at 75-80 degrees C, maintaining constant temperature for 8-10 hours, regularly stirring, and killing common viruses, bacteria and parasite eggs in material, and (e) discharging tank, cooling bag, and processing mixture into organic fertilizer.
NOVELTY - An animal manure organic fertilizer is prepared by taking animal manure, putting in tank, and stirring.    USE - Method for preparing animal manure organic fertilizer (claimed).
NOVELTY - Method for preparing organic fertilizer using biogas residue, involves fermenting biogas residue using microorganism under aerobic condition, and adjusting pH of the fermented product.    USE - The method is useful for preparing organic fertilizer using biogas residue (claimed).
NOVELTY - Food source organic waste degradation carrier comprises 0.1-10% dispersion material, 0.1-10% absorbent or water retention material, and absorbent or support material (remainder).    USE - As food source organic waste degradation carrier.
NOVELTY - A biological organic fertilizer comprises 1-10 pts. wt. yeast, 2-8 pts. wt. lactic acid bacteria, 1-6 pts. wt. cellulose decomposing bacteria, 1-2 pts. wt. azobacter, 1-2 pts. wt. silicate bacteria, 1-5 pts. wt. photosynthetic bacteria and 1-5 pts. wt. Pseudomonas.    USE - Biological organic fertilizer.    ADVANTAGE - The fertilizer improves soil fertility.
NOVELTY - Pine farm fertilizer comprises 5-10 wt.% dairy manure, 50-60 wt.% dry pine, 20-30 wt.% rice, and 5-10 wt.% rice bran.    USE - As pine farm fertilizer (claimed).    ADVANTAGE - The pine farm fertilizer is cost-effective-effective.
NOVELTY - An organic fertilizer comprises 30-35 pts. wt. chinaberry seed and leaf, 40-45 pts. wt. waste edible matrix, 15-20 pts. wt. livestock and poultry manure, 10-15 pts. wt. soybean meal and 5-10 pts. wt. humic acid. The waste matrix is planting and cultivating material waste, livestock manure is dairy manure and humic acid is natural macromolecule aromatic hydroxyl carboxylic acid.    USE - Organic fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of organic fertilizer comprising taking raw materials, mixing, fermenting for 7 days, turning when temperature reaches 60-70 degrees C, mixing, fermenting, sterilizing at 100 degrees C, fermenting 30 degrees C for 2 weeks, drying, granulating, and bagging.
NOVELTY - Culture material fermentation comprises preprocessing straw and dairy manure; uniformly mixing straw, alfalfa, dairy manure, rapeseed cake, calcium superphosphate, gypsum powder, lime, urea and ammonium carbonate, controlling water content and pH, placing the mixture in tunnel, closing the tunnel, maintaining temperature with steam, and ventilating once a day to supplement oxygen content in culture material; fermenting for 13 days and regulating water content at 65% and pH at 7.5-8; and adding fermented culture material to aquaculture pond soil.    USE - Method for culture material fermentation (claimed).    ADVANTAGE - The method is resource-saving and environment-friendly.    DETAILED DESCRIPTION - Culture material fermentation comprises:    (A) cutting straw into 5-15 cm sections, rolling, penetrating with 0.5% lime water, and destroying stratum corneum and epicuticular wax to allow easy water absorption; and prewetting straw 2-3 days before heap stacking;    (B) prewetting dry manure and controlling water content at 60% 3-4 days before heap stacking;    (C) uniformly mixing, per 40 m2 cultivation area, 600-800 kg straw, 275-280 kg alfalfa, 375-400 kg dairy manure, 100-150 kg rapeseed cake, 50-100 kg calcium superphosphate, 50-100 kg gypsum powder, 40-60 kg lime, 15-25 kg urea and 5-8 kg ammonium carbonate, controlling water content at 70% and adjusting pH to 7-7.5, placing the mixture in tunnel, closing the tunnel, maintaining temperature at 65 degrees C with steam, and ventilating once a day for 20-30 minutes to supplement oxygen content in culture material, in which after 2 days, humic mycophenolate fungi, thermophilic Actinomycetes and thermophilic bacteria grow successively in decomposing matrix;    (D) fermenting for 13 days and regulating water content at 65% and pH at 7.5-8; and    (E) adding 30-40% fermented culture material to 50-60% aquaculture pond soil.
NOVELTY - Vegetable seedling matrix comprises 20-40 pts. vol. edible mushroom residue, 5-10 pts. vol. livestock and poultry manure, and 50-70 pts. vol. cassava dregs. The edible mushroom residue is waste material obtained after harvesting mushroom product and has particle size of 1-5 mm. The livestock and poultry manure is chicken manure, duck manure, cattle manure, and/or pig manure. The cassava dregs comprise waste material obtained after cassava starch and alcohol production, and have particle size of 1-3 mm.    USE - Vegetable seedling matrix.    ADVANTAGE - The seedling matrix reduces peat resource consumption, protects ecological environment, reduces cultivation cost, and realizes industrialized vegetable seedling growth.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for vegetable seedling matrix preparation by uniformly mixing edible mushroom residue, livestock and poultry manure and cassava dregs; and stacking the mixture and controlling water content at 50-65%, aerobically fermenting at 45-65 degrees C until temperature of stack material is equal to environment temperature, aging, mixing 50-99 pts. vol. fermented material with 1-50 pts. vol. inorganic material, and adjusting pH to 5.5-7.5. The inorganic material is perlite or vermiculite.
NOVELTY - Culture medium preparation involves fermenting fungi, which is gray, non-tacky, non-sticky, elastic and transparent, where water content is 66.3%, pH value is 7.5 and amount of nitrogen is 2.15%. The culture material comprises pond culture (70%), bran (30%), alfalfa (275 kg), dairy manure (375 kg), rapeseed cake (100kg), calcium superphosphate (50 kg), gypsum powder (50 kg), lime (40 kg), urea (15 kg), ammonium carbonate (5 kg) and water (70%). The pH value of culture medium is adjusted to 7.5, and then temperature of culture medium is maintained.    USE - Method for preparing culture medium used for culturing strain (claimed), and improving yield of mushroom.    ADVANTAGE - The method enables to prepare culture medium in cost-effective and eco-friendly manner.    DETAILED DESCRIPTION - Culture medium preparation involves fermenting fungi, which is gray, non-tacky, non-sticky, elastic and transparent, where water content is 66.3%, pH value is 7.5 and amount of nitrogen is 2.15%. The culture material comprises pond culture (70%), bran (30%), alfalfa (275 kg), dairy manure (375 kg), rapeseed cake (100kg), calcium superphosphate (50 kg), gypsum powder (50 kg), lime (40 kg), urea (15 kg), ammonium carbonate (5 kg) and water (70%). The pH value of culture medium is adjusted to 7.5, and then temperature of culture medium is maintained at 60-62 degrees C for 8 hours, and then culture medium is sterilized per hour. Temperature of culture medium is reduced to 55 degrees C, and then culture medium is sterilized per hour. The temperature is maintained at 50-52 degrees C for 3-5 days, and then culture medium is ventilated to remove harmful gas and increase fresh air.
NOVELTY - Humic acid type fluid or solid organic fertilizer composition, comprises 6-100 pts. wt. organic fertilizer, 1-20 pts. wt. element fertilizer, and 1-20 pts. wt. trace element fertilizer, where the organic fertilizer comprises filter mud fermentation product, filter mud from sugar refinery, alcohol plant, monosodium glutamate factory and yeast plant.    USE - The humic acid type fluid or solid organic fertilizer composition is useful for increasing crop blade chlorophyll content and/or increasing crop root ratio and/or increasing crop yield. The crop is cucumber (all claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for increasing crop blade chlorophyll content and/or increasing crop root ratio and/or increasing crop yield which involves spraying 40-60 kg fluid or solid organic fertilizer composition to seedling of plant during growing period, where 3-6 kg solid organic fertilizer is diluted for 15-30 times.
NOVELTY - Fertilizer comprises (in pts.wt.): filter mud fermentation liquid (50-100), fertilizer element (1-5), microelement fertilizer (1-5), where filter mud is selected from sugar-refinery, alcohol plant, plant or yeast monosodium glutamate.    USE - Fertilizer.    ADVANTAGE - The fertilizer ensures increased chlorophyll content and yield of cucumber.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing fertilizer, which involves:    (A) adding water to fermentation tank, and then heating to 50-80 degrees C;    (B) adding fresh filter mud and fermentation microbial inoculums to the tank;    (C) filtering the fermentation liquid and fermenting for 5-10 days;    (D) keeping fermentation liquid at normal temperature for 5-10 hours, and then collecting fermentation liquid;    (E) concentrating ferment at 60-80 degrees C;    (F) regulating pH value of the liquid to 6-8 to obtain the filter mud fermentation liquid;    (G) selecting fermentation microbial inoculum from Aspergillus oryzae, Aspergillus niger, Bacillus cereus, Bacillus megaterium or nitrogen fixation root nodule;    (H) selecting fertilizer from urea, ammonium nitrate, potassium dihydrogen phosphate, calcium superphosphate, potassium chloride or potassium nitrate;    (I) selecting element fertilizer from calcium sulfate, magnesium sulfate or magnesium chloride;    (J) selecting trace element fertilizer from zinc sulfate, manganese sulfate, zinc chloride, copper sulfate or ammonium molybdate; and    (K) selecting wetting osmotic agent from sodium alkyl glycoside, trisiloxane polyethenoxy ether or methyl oleoyl taurate.
NOVELTY - Fertilizer comprises (in wt.%): organic raw material (25-35), urea (18-26), monoammonium phosphate (10-20), potassium chloride (5-15), clay (18-26), boron (0.1-1.5) and microbial strain (0.01-0.15), where organic raw material is mixture of (in wt.%): animal manure (70-90) and wood (10-30).    USE - Fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fertilizer, which involves:    (A) mixing organic raw material at 50-70 degrees C;    (B) fermenting mixture for 12-18 days;    (C) keeping fermented product for 55-65 days;    (D) mixing remaining ingredients;    (E) crushing and granulating obtained mixture; and    (F) drying and cooling granules to obtain product that is packed.
NOVELTY - Biomass fertilizer composition comprises (wt.%): pyrolyzed carbon biomass (55-70), urea (23-40) and alkali lignin (4-12), where nitrogen and water content in urea is 46% and 1% respectively, and alkali content in alkali lignin is 90%, pH is 6.5, water content is 2% and ash content is 5%.    USE - Biomass fertilizer composition.    ADVANTAGE - The biomass fertilizer composition is prepared in simple, cost-effective manner, and eco-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing biomass fertilizer composition, which involves:    (A) crushing and pyrolyzing agricultural waste at 400 degrees C to obtain pyrolyzed carbon biomass;    (B) mixing urea and alkali lignin with the obtained material, and then adding water to them;    (C) heating the obtained material at 60 degrees C for 5-10 minutes;    (D) pouring the obtained material into mold; and    (E) drying the obtained material at 45 degrees C for 2 hours to obtained finished product.
NOVELTY - Phenolic compounds are extracted from directly liquefied coal oil by subjecting oil to extraction-distillation distillation column (T1), dividing phenol-rich oil fractions into 1st and 2nd phenol-rich oil fractions (1), extracting and distilling phenol-rich oil using solvent e.g. glycerol triacetate and/or sulfolane to remove oil in extraction and distillation column, entering phenol-rich solvent stream (3) in solvent recovery column (T2) to obtain phenolic compounds and circulation solvent (5), cooling phenolic compounds (4), and repeating process for 2nd phenol-rich oil fraction.    USE - Extraction of phenolic compounds from directly liquefied coal oil (claimed).    ADVANTAGE - Relative volatility of phenolic compound and oil is improved, high purity phenolic compound is obtained with high recovery rate, process reduces energy consumption and does not produce wastewater, and waste acid and alkali do not corrode the device, reducing device investment.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of extracting and distilling phenolic compounds from directly liquefied coal oil.    1st or 2nd phenol-rich oil fraction (1)    Entering phenol-rich solvent stream into solvent recovery column (3)    Phenol product (4)    Circulation solvent (5)    Extraction-distillation column (T1)    Solvent recovery column (T2)
NOVELTY - Forming charcoal from coffee grounds involves pyrolyzing coffee grounds to form pyrolyzed coffee grounds; mixing the pyrolyzed coffee grounds with a binding agent to form a mixture; and pressing the mixture into a charcoal cube.    USE - For forming charcoal from coffee grounds (claimed).    ADVANTAGE - The present method recycles used coffee grounds for forming charcoal so as to prevent them from being thrown in a landfill.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for charcoal formed from coffee grounds comprising: pyrolyzed coffee grounds and a binding agent, where the pyrolyzed coffee grounds are mixed with the binding agent and pressed into a charcoal cube.
NOVELTY - Converting bio-oil (10) comprises a feedstock comprising bio-oil which is subjected to oxidation in the presence of an oxidant (20) to yield an oxidation product (90) and subjecting the oxidation product to condensation carried out in the presence of a basic catalyst to obtain converted bio-oil.    USE - The process is useful for converting bio-oil as heating oil, and as starting material in processes for producing fuels, fuel components, fine chemicals, chemical building-blocks, and solvents (claimed).    ADVANTAGE - The process converts bio-oil as heating oil with improved stability and less complication, with decreased acidity and which can be maintained in liquid form for long periods of time.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of the process for converting bio-oils.    Bio-oil (10)    Oxidant (20)    Solvent (30)    Water (60)    Oxidation product (90)
NOVELTY - Converting gaseous products, comprises: subjecting a feedstock comprising gaseous products obtained from thermal processing of biomass to oxidation in the presence of an oxidant to yield an oxidation product; and subjecting the oxidation product to condensation carried out in the presence of a basic catalyst to obtain a bio-oil product.    USE - The process is useful for converting gaseous products to obtain bio-oil products, which is useful as heating oils, and as starting material in processes for producing fuels, fuel components, fine chemicals, chemical building-blocks, and solvents (all claimed).    ADVANTAGE - The process is capable of effectively and economically retrieving the bio-oil with improved viscosity and stability.
NOVELTY - Method for manufacturing cathode catalyst layer, involves forming precursor layer containing catalyst support particle and an ionomer, and irradiating an ultrasonic wave to the precursor layer.    USE - The method is useful for manufacturing cathode catalyst layer which is used for manufacturing polymer electrolyte fuel cell (all claimed).    ADVANTAGE - The method manufactures the cathode catalyst layer which improves the battery characteristics of the polymer electrolyte fuel cell.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) cathode catalyst layer manufactured by the above-mentioned method;    (2) method (M1) for manufacturing a polymer electrolyte fuel cell provided with the cathode catalyst layer, involves manufacturing the cathode catalyst layer; and    (3) polymer electrolyte fuel cell manufactured by the above-mentioned method (M1).
NOVELTY - A biofuel comprises emulsified oil component and crushed algae. The emulsified oil component contains water and oil component, in which the algae is produced.    USE - Biofuel is used as fuel for boiler.    ADVANTAGE - The biofuel is economical and manufactured efficiently, without performing extraction and purification of the oil component.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of biofuel, which involves stirring the oil component strongly, and emulsifying the oil component.
NOVELTY - Polypeptide having a sequence that is derived from a native mannanase of coprophilic ascomycete filamentous fungus, preferably Podospora anserina and is characterized by increased catalytic efficiency of 25% with respect to the catalytic efficiency of the native mannanase, is new.    USE - The polypeptide is useful: for the degradation of compounds comprising mannans, preferably lignocellulosic biomass (all claimed); for the production of biofuels (such as bioethanol and biobutanol) and other industrial products; for paper and pulp industry, agriculture and food industry, coffee extraction, oil drilling and detergent; for stimulation of oil wells and gas by hydraulic fracturing; for the production mannose or mannooligosaccharides from the compounds comprising mannans; for producing mannitol; as dietary supplement and as a cooking ingredient; for the extraction of palm oil; for bleaching of paper pulp; for desizing and bleaching textile fibers; and for the elimination of biofilms, where the lignocellulosic biomass includes herbaceous agricultural residues, forestry residues, municipal solid waste, paper type waste and pulp and stationery residues.    ADVANTAGE - The polypeptide exhibits improved enzymatic efficiency, and ensures efficient and economical degradation of lignocellulosic biomass.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a polynucleotide encoding a polypeptide;    (2) a vector comprising polynucleotide;    (3) a host cell comprising the vector or the polynucleotide; and    (4) a composition comprising the polypeptide, polynucleotide, the vector or the host cell.
NOVELTY - Method of producing biogas from animal waste includes pretreatment of an organic substrate by bringing moisture content thereof to 90%, followed by crushing the substrate to particle size of 0.5-0.7 cm. An organic catalyst is added, fermentation is carried out in an anaerobic medium and biogas is collected. The organic catalyst used is dairy wastes in amount of 5-10% of the mass of the organic substrate. Fermentation in an anaerobic medium is carried out at temperature of 17-22 degrees C.    USE - Chemistry.    ADVANTAGE - Invention intensifies the process of methane fermentation of manure to increase output of biogas and increase content of methane therein.2 cl, 1 dwg
NOVELTY - Preparing an alkyl compound or its mixture, comprises preparing a ketene compound (I), and hydrogenating (I) in the presence of a metal catalyst.    USE - The process is useful for preparing an alkyl compound or its mixture including ethanol, a 4C alcohol (including 1-butanol and 2-butanol), isopropanol, 2-pentanol, 1-hexanol, 2-hexanol, 2-heptanol, 4-heptanol, 3-methyl cyclohexanol, 2,6-dimethyl-4-heptanol, an ester used for producing an aldehyde, alcohol and a hydrocarbon and/or ketone (including 2-butanone, 2-pentanone, 2-heptanone and 4-heptanone), which are useful for producing a fuel (all claimed) including automotive fuel for transportation, solvents, and industrial chemicals for producing polymers, plastics, pharmaceuticals, paints and other important chemicals.    ADVANTAGE - The process ensures easy isolation of the alkyl compound e.g. butanol from broths along with its toxicity to microbes using less water consumption, and provides higher energy fuels such as alcohols and alkanes that are readily compatible with existing automotive and transportation infrastructure.    DETAILED DESCRIPTION - Preparing an alkyl compound or its mixture, comprises preparing a ketene compound of formula (R2-C(R1)=C(=O)) (I), and hydrogenating (I) in the presence of a metal catalyst.    R1, R2 = H (preferred) or 1-6C-alkyl.    An INDEPENDENT CLAIM is included for synthesizing a fuel using the alkyl compound.
NOVELTY - The apparatus comprises two electrodes, a current source, a compartment containing water, a gas pipe formed in the vicinity of the cathode for removing the formed hydrogen gas, where the gas pipe is connected to a ventilator apparatus, from which ventilation gas is added to the hydrogen.    USE - The apparatus is useful for electrolytic production of hydrogen (claimed), which is useful in a ventilator that is useful for providing artificial respiration to patients affected with respiratory diseases including asthma and chronic obstructive pulmonary disease, trauma, heart attack, stroke, and severe infectious diseases such as avian flu and Severe acute respiratory syndrome (SARS).    ADVANTAGE - The apparatus is capable of electrolytically producing hydrogen using less equipment expense, limits the amount of current for generating hydrogen, and prevents accidents caused by flammable hydrogen gas.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of an apparatus for electrolytic production of hydrogen (Drawing includes non-English language text).
NOVELTY - The method involves flowing a portion of an LNG stream (110) through an air separation unit (ASU) (104) to form a portion of a natural gas (NG) stream (112). The heat from airflow in the ASU is removed to separate an oxygen stream (106) from the airflow. The oxygen stream and a fuel stream is combusted in a power plant (114). A portion of the LNG stream is flowed through a gaseous carbon dioxide (C02) chiller to form a portion of the NG stream. A liquefied CO2 stream (118) is formed in the CO2 chiller.    USE - Method for regasifying LNG used in power plant.    ADVANTAGE - The liquid natural gas regasification techniques and systems reduces emissions associated with fuel-fired vaporizers and improves the flexibility of utilizing LNG cold.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a system for regasifying liquefied natural gas; and    (2) a method for cryogenically distilling a gas mixture.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the LNG terminal illustrating the use of cold from the LNG to purify the air stream for use in the power plant.    Air separation unit (104)    Oxygen stream (106)    LNG stream (110)    Natural gas stream (112)    Power plant (114)    Liquefied CO2 stream (118)
NOVELTY - Waste paper recycling system for making densified refuse derived fuel (RDF) is provided. The waste paper recycling system includes a first RDF granulation machine used to remove water from a first slurry settling at the bottom of a washing separator, and perform granulation by a screw extrusion; and a second RDF granulation machine used to remove water from a second slurry of a paper machine, and perform granulation by a screw extrusion, wherein the RDF includes the first slurry and the second slurry.
NOVELTY - A refrigerant composition comprises propane and/or propylene.    USE - Refrigerant composition is used as refrigerant in cooling/heating device and refrigerator/freezer device (all claimed). Uses include but are not limited to vehicle, business use air-conditioner, freezer and refrigerator apparatus.    ADVANTAGE - The refrigerant composition reduces power consumption of device without requiring device modification.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for usage method of refrigerant composition, which involves causing heat-exchanging effect within a cooling/heating device or a refrigerator/freezer device, by using the refrigerant.
NOVELTY - Method for pre-processing biomass, involves improving contacting efficiency between cellulose and/or hemicellulose and cellulose- and/or hemicellulose-degrading enzyme in the biomass, placing the biomass in a container having ventilation hole that is communicated with outside of the container, then heating the biomass with water at a temperature that is equal to or lower than the boiling temperature of water while continuously opening the ventilation hole, and thus removing a substance that contains at least an organic acid from the biomass.    USE - The method is useful for pre-processing biomass for manufacturing saccharides (claimed), and producing ethanol.    ADVANTAGE - The saccharides can be manufactured at high yield using small amount of enzyme.    DETAILED DESCRIPTION - Method for pre-processing biomass, involves improving contacting efficiency between cellulose and/or hemicellulose and cellulose- and/or hemicellulose-degrading enzyme in the biomass, placing the biomass in a container having ventilation hole that is communicated with outside of the container, then heating the biomass with water at a temperature that is equal to or lower than the boiling temperature of water while continuously opening the ventilation hole, and thus removing a substance that contains at least an organic acid from the biomass, where the biomass is utilized for manufacturing saccharides as main component of glucose. An INDEPENDENT CLAIM is included for method for manufacturing saccharides as main component of glucose, which involves pre-processing cellulose and/or hemicellulose and cellulose- and/or hemicellulose-degrading enzyme in the biomass.
NOVELTY - Method for producing ethanol involves contacting Paenibacillus macerans NS-1 strain (FERM P-22124) with glycerol waste liquid under anaerobic environment without carrying out neutralization process, where the glycerol waste liquid is byproduct obtained from production of biodiesel fuel using fat, oil and primary alcohol as raw material under presence of alkali catalyst.    USE - The method, composition and bioreactor are useful for producing ethanol. The bioreactor is further useful for inhabiting P.macerans NS-1 strain (claimed).    ADVANTAGE - The method is cost-effective, efficient and short as it does not undergo neutralizing process and does not require acid.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) composition comprising P.macerans NS-1 strain (FERM P-22124); and (2) bioreactor.
NOVELTY - Solid fuel is manufactured by inoculating (S130) brown rot fungi in wood-type biomass.    USE - Manufacture of solid fuel for powdered coal boiler.    ADVANTAGE - Pulverization of wood-type biomass can be easily performed, mechanical strength of wood-type biomass can be reduced, and manufacturing cost of solid fuel can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of the manufacturing method of solid fuel. (Drawing includes non-English language text).    Brown rot fungi culture process (S110)    Nutrient removal process (S120)    Inoculation process (S130)    Determination process (S140)    Decay suppression or stopping process (S150)
NOVELTY - Preparation of 3,4-dimethoxytoluene (I) comprises extracting biological oil to obtain 4-methyl guaiacol (II) as raw material and brominating.    USE - Method for preparing 3,4-dimethoxy toluene (claimed).    ADVANTAGE - The method is simple, environment-friendly and suitable for industrial production, has short reaction period, and avoids the use of halogen-containing and other toxic agent.    DETAILED DESCRIPTION - Preparation of 3,4-dimethoxytoluene of formula (I) comprises extracting biological oil to obtain 4-methyl guaiacol of formula (II) as raw material and brominating.
NOVELTY - A photocatalyst preparing method involves calcining an amorphous hydrous titanium dioxide modified with copper salt and subjecting to photo-deposition process in the presence of methanol and UV radiation, where the copper salt is copper acetate or copper nitrate, and the weight ratio of copper and titanium dioxide in reaction mixture is 0.5:9.5-2:8.    USE - Method for preparing photocatalyst for preparing mixture of hydrogen, methane and higher aliphatic hydrocarbon.
NOVELTY - This new utility model claims of a kind of biologic organic fertile one special production device, the crushing chamber fixed on upper frame, and on the crushing chamber lower separately set with feedstock mouth and discharging mouth, crushing drive electric machine fixedly installed in crushing chamber on the transmission rod is inserted in the crushing chamber, the crushing chain the crushing cabin, one end fixed on the transmission rod and drive motor of smashing, smashing vibration electric engine fixed on outer side wall of the crushing chamber, wherein the crushing chamber inside also is set with clapboard with screen; fixed on the bottom frame at the upper part of the present, its lower part is set with with hopper, the side part is set with arrange material port, the roller sieve moving installed in at , and driving motor installed on of well and roller sieve transmission connected with, the sieve plate inclined shape installed in present in and the roller sieve is below the lower end of the plate to sieve the material port is arrange side part, wherein the roller sieve the feedstock transport belt at the lower end position, this utility new type has advantages as: structure reasonable design. Production efficiency high, simple operation suitable, and set of sieving in every one step of crushing and sieving the link, it is very suitable for biological organic fertile production is needed.
NOVELTY - This utility new type relates to a one using solar energy to a garden waste of automatic fermentation device, the automatic fermentation device comprise an outer shell, an insulating layer, automatic control device, the fermentation storage bin, a solar energy heat collecting device, heat exchange device, solar energy power generation device, an electric energy storage device, ventilation device and percolate collecting device, this utility new type is an aerobic fermentation device heat preservation, heating, ventilation is a whole and is suitable for garden waste compost fermentation.
NOVELTY - Straw mushroom culture material preparation involves adding lime to a mixture of waste material (60-80 parts) and dry cow manure (20-40 parts) to adjust pH 8. The obtained mixture is arranged in film stack, and then fermented at 55 degrees C for 8-11 days. The obtained material is maintained 70-80% humidity, and then fermented them at 50-65 degrees C for 20-25 days. The fermented material is cooled naturally to 30 degrees C, and then kept for 13 days to obtain finished product.    USE - Method for preparing straw mushroom culture material (claimed).    ADVANTAGE - The method enables to prepare straw mushroom culture material ensures improved yield.
NOVELTY - Rivaroxaban (I) preparation involves hydrolyzing oxomorpholin compound (II) and then performing acylation reaction to form rivaroxaban.    USE - Method for preparing rivaroxaban (claimed).    ADVANTAGE - The method prepares rivaroxaban in a simple manner by using mild reaction condition with high reaction yield, avoids use of toxic and harmful reagents, and reduces environment pollution.    DETAILED DESCRIPTION - Rivaroxaban (I) preparation involves hydrolyzing oxomorpholin compound (II) and then performing acylation reaction to form rivaroxaban.    R=phenyl, halo phenyl or alkyl phenyl group.
NOVELTY - Manufacture of anhydrosugar alcohol involves performing dehydrogenation of hydrogenated sugar, adding resultant converted liquid to distillation column, distilling by thin film distillation process and separating anhydrosugar.    USE - Manufacture of anhydrosugar alcohol e.g. isosorbide, isomannide and isoidide. Uses include but are not limited to plasticizer, biodegradable polymer, water-soluble lacquer and solvent for adhesive, cosmetic field, food industry, plastic industry and medicine field for treating blood vessel disease, adhering patch and oral cancer.    ADVANTAGE - The method enables manufacture of anhydrosugar alcohol having high purity of more than 99% by environmentally-friendly and economical process.
NOVELTY - The chemical plant gasifies particles of biomass in presence of steam to produce low carbon dioxide synthesis gas including hydrogen, carbon monoxide gas and less than 15% carbon dioxide by total volume generated in gasification reaction of particles of biomass. The heat source is in thermal communication with radiant heating tubes to internally heat tubes, such that heat exchanges through wall of tube to refractory lined vessel where particles biomass and natural gas are flowed to cause operating temperature of between 900-1600 degrees C in radiant heat-driven chemical reactor.    USE - Biocidal product directive (BPD) chemical plant for producing liquid fuel from biomass.    ADVANTAGE - The gas byproducts from migrating back up into the radiant heating tube area of the refractory lined vessel is prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic flow diagram of steam explosion unit having an input cavity to receive biomass as a feedstock, steam supply inputs, and stages to pre-treat the biomass for subsequent supply to biomass gasifier.    Steam explosion unit (108)    Chip of biomass (451)
NOVELTY - The system (100) has a heat radiator 16 that thermally radiates the anode off gas discharged from an anode (12), and recovers condensed water. First heat exchanger (18) with which the anode off gas is supplied is heat-exchanged. A combustor (20) is provided to burn the anode off gas passed through first heat exchanger after discharging from anode off gas heat radiator. The hydrogen-containing-gas is generated using raw material and the condensed water supplied from anode off-gas heat radiator. A modifier (22) is provided to supply the hydrogen-containing-gas to anode.    USE - Solid oxide fuel cell system.    ADVANTAGE - The modifier heated with combustion exhaust gas is reduced in size.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the solid oxide fuel cell system. (Drawing includes non-English language text)    Anode (12)    Heat exchanger (18)    Combustor (20)    Modifier (22)    Solid oxide fuel cell system (100)
NOVELTY - Pre-treating wastewater using a polymer film, comprises (a) forming polymer film by depositing a cationic polymer on surface of a support; and (b) removing bacteria from wastewater by stirring wastewater and polymer film.    USE - The method is useful for culturing microalgae (claimed) to produce bio-compound, drugs, health functional food, biofuels and protein hydrolysate.    ADVANTAGE - The method maximizes microalgae productivity; and is economical.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for culturing microalgae, comprising pre-treating wastewater as above, and culturing microalgae in a medium of bacteria removed wastewater.
NOVELTY - Antimicrobial composition comprises quaternary ammonium salt compound derived from vegetable oil.    USE - As antimicrobial composition.    ADVANTAGE - The antimicrobial composition is environmentally-friendly.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) tertiary amine compound comprising the cyclic compounds of formulae (I), (II), (III) and (IV); and    (2) method for preparing the above-mentioned antimicrobial composition, involves reacting vegetable oil having an epoxy group and dialkyl amine, and reacting the obtained mixture with the tertiary amine compound and compound of formula: R3X (V) to produce quaternary ammonium salt compound.    R1,R2=1-20C linear hydrocarbon or branched or cyclic alkyl;    R3=alkyl having 1-20C hydrocarbon or aryl having 3-30C hydrocarbon;    X=hydroxide (OH-), sulfate (SO42-), hydrogen sulfate (HSO4-), nitrite (NO2-), nitrate (NO3-), cyanide (CN-), cyanate (OCN-), isocyanate (NCO-), thiocyanate (SCN-), isothiocyanate (NCS-), phosphate (PO43-), hydrogen phosphate (HPO42-) and (H2PO4-), primary phosphite (H2PO3-), secondary phosphite (HPO32-), ortho-borate (BO33-), metaborate ((BO2)33-), penta borate (B5O8-), penta borate hydrate (B5H4O10-), tetrafluoroborate ((BF4)-), tetrachloro-borate ((BCl4)-), tetraphenylborate ((B(C6H5)4)-), hexafluorophosphate ((PF6)-), hexafluoroantimonate ((SbF6)-), hexafluoroarsenate ((AsF6)-), tetrachloroaluminate ((AlCl4)-), tetrabromo-aluminate ((AlBr4))-, trichloroacetic zincate ((ZnCl3)-), carbonate (CO32-), hydrogen carbonate (HCO3-), fluoride (F-), fluorosulfonate (R'-COO)- or sulfonate (R'-SO3)-;and    R'=linear or branched alkyl having 1-12C, cycloalkyl, aryl unsubstituted hydrogen of 5-18C or halo, 5-18C aryl or 1-6C (un)substituted alkyl.    Where (i) R1 and R2 are connected to form ring structure having less than 30 carbon atoms.
NOVELTY - The method involves providing a metal substrate i.e. metal plate (12). A set of precious metal islands i.e. gold islands (13), is deposited on a surface of the metal substrate. Titanium oxide is grown on the surface on areas that are not covered by the precious metal island using a thermal oxidation process. Another set of precious metal islands i.e. isolated platinum islands (11), is deposited on another surface of the substrate, where the former precious metal island is different than the latter precious metal island. Carbon material is deposited on the latter surface of the substrate.    USE - Method for coating a metal substrate in an electrochemical device (claimed) i.e. electrolyzer, utilized for splitting water into hydrogen and oxygen using electrical power.    ADVANTAGE - The method enables growing the titanium oxide on the surface on areas that are not covered by the precious metal island using the thermal oxidation process, so that oxide surface scale of the metal substrate prevents corrosion and electrical conductive materials such as precious metals, provide the surface electrical conductance of metallic components, thus producing metal components for electrolyzers with high electrical conductance and corrosion resistance for long term operation at low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an electrochemical device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a bipolar plate comprising precious metals on two sides of the plate.    Isolated platinum island (11)    Metal plate (12)    Gold island (13)    Thick oxide layer (14)
NOVELTY - Composition comprises 23-27.9 wt.% of microbial flora, 1.5-2.5 wt.% of pesticide, 2.1-2.4 wt.% of a releasing agent, and balance amount of water.    USE - The composition is useful for increasing the yield of grapes (claimed).    ADVANTAGE - The composition can be stored for a long time and utilized in a cost effective manner, and has good degradation property.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the composition, comprising mixing N-acyl sarcosinate, N-acetylglutamate, N-alkyl beta -aspartate and potassium phosphate to obtain an organic separating agent, mixing microbial flora bacteria and the organic separating agent in a reaction kettle and then stirring at 25 degrees C for 30 minutes, adding fertilizer and pesticide into the reaction kettle and then mixing, stirring and bottling.
NOVELTY - This utility new type claims a dry one illegal cooking oil of preprocessing device, comprise one level in turn set with a raw material tank, an electric flocculation tank, pressure filter pump, a bag-type filter and a level raw material tank, and the said each component connected pipeline of this utility new type using electric flocculation method a raw material groove, produce solid impurity a little, there is no other produce waste, so the green environment-friendly, and pollution is small.
NOVELTY - This utility new type claims a one continuous ester exchange reaction of a device, include raw material tank, a material tank, a first reactor, second reactor, third reactor, an ultrasonic stirrer, a finished product tank and pipeline, a raw material tank and exit of auxiliary tank connecting first reaction kettle through pipeline of entrance, a first reaction kettle, reaction kettle and second reaction kettle are equipped with one third a ultrasonic stirrer, the first reaction kettle and the second reaction kettle and the second reaction kettle and third reaction kettle through pipeline connected, a third reaction kettle of exit connecting the finished product tank. This utility new type using three-level reaction, using ultrasonic stirrer and a stir, the reaction device of this utility new type reaction process does not generate acid waste water, waste water processing difficulty is reduced, and using methanol as raw material, which avoids the methanol for the environment of pollution.
NOVELTY - Collecting device, and hydrogen water and the gas collecting device is connected with a hydrogen of this utility new type claims a one instant manufacturing hydrogen water of device, wherein it comprise hydrogen generating device, used for fighting hydrogen generating device produce a the water device and a tap water inlet water device, hydrogen generating device and the gas collecting device through the connected pipeline connecting, and a connected pipeline, hydrogen water of the water device, the tap water inlet device set with a control valve, the control valve and the hydrogen generating device are connecting with a control device, the utility model is new type has simple structure, time saving water, a moment a high concentration hydrogen water.
NOVELTY - Converting coal to fuel involves generating heat from coal to generate carbon dioxide as by-product; generating first hydrogen product and carbon black/coke from coal; re-circulating carbon dioxide to react with carbon black/coke to form carbon monoxide; generating a second hydrogen product; reacting carbon monoxide with first and second hydrogen products to form a first hydrocarbon group having at least one alkene or olefin; and converting at least a portion of the olefins in first hydrocarbon group to form at least one of 1-40C alcohols, kerosene, gasoline, diesel fuel and jet fuel.    USE - For converting coal to liquid fuel e.g. 1-40C alcohols, kerosene, gasoline, diesel fuel and jet fuel used as finished fuels and in diesel engine electricity generators to generate electricity for electrolyzing water (claimed).    ADVANTAGE - The process significantly reduces carbon waste of the total system, carbon dioxide exhaust by-products, and improves total energy output of the fuels production system, compared to traditionally employed coal-to-liquid fuel and coal-to-electricity production methods. The process reduces environmental pollutants and reduces global warming. Kerosene, gasoline, diesel fuel, and/or jet fuel are optionally blended with 1-40C alcohol combinations for most efficient utilization of all available carbon and to improve combustion characteristics of the finished fuels.
NOVELTY - A support comprises a substrate including highly-crystalline carbon, and a crystalline carbon layer formed on the substrate.    USE - Support is used for catalyst layer for electrode e.g. cathode and anode of membrane electrode assembly for fuel cell system (all claimed) e.g. direct-oxidation fuel cell and polymer electrolyte membrane fuel cell for generating electricity.    ADVANTAGE - The fuel cell has high energy density and operativity, and is lightweight.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparation of support, which involves adding a monomer to a highly-crystalline carbon liquid and preparing a mixture, adding a polymerization initiator to the mixture, polymerizing and preparing polymerization product, stabilizing the polymerization product and obtaining stabilized product, heat-treating the stabilized product thrice and then graphitizing the resultant product;    (2) electrode for fuel cell, which comprises an electrode substrate, and a catalyst layer on the electrode substrate. The catalyst layer includes the support and an active metal supported on the support;    (3) membrane-electrode assembly for a fuel cell, which comprises a cathode and an anode facing each other, and a polymer electrolyte membrane between the cathode and anode; and    (4) fuel cell system (1), which comprises at least one electricity-generating element (3) including the membrane-electrode assembly (17) and a separator (19) positioned at each side of the membrane-electrode assembly, a fuel supplier (5) which supplies fuel to the electricity-generating element and an oxidant supplier (7) which supplies oxidant to the electricity-generating element.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic structure of fuel cell system.    Fuel cell system (1)    Electricity-generating element (3)    Fuel supplier (5)    Oxidant supplier (7)    Membrane electrode assembly (17)    Separator (19)
NOVELTY - Digested sludge is decomposed by inoculating microorganisms in culture solution containing water and digested sludge and culturing for 7 days at temperature of 30 degrees C and pH of 5 in which digested sludge is the only source of nutrient in culture solution. Microbial reduction rate (%) after culture process is greater than or equal to 10%. Microorganisms are Penicillium janthinellum, Cunninghamella bainieri, Neosartorya fischeri, and/or Umbelopsis isabellina.    USE - Decomposition method of digested sludge for industrial waste treatment.    ADVANTAGE - Large amount of digested sludge can be decomposed at low cost, and significant reduction of industrial waste can be attained.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) microorganisms used in decomposition method of digested sludge;    (2) mixture of degradation product of digested sludge and microorganisms obtained by inoculating microorganisms in culture solution containing digested sludge and culturing; and    (3) fuel containing mixture of degradation product of digested sludge and microorganisms.
NOVELTY - A saccharified liquid comprises 0.5-30 mass% pre-processed degradation products of solubilized lignocellulosic biomass which is produced by pre-processing lignocellulosic biomass, and saccharide components.    USE - A saccharified liquid for manufacturing chemical substance (claimed).    ADVANTAGE - Saccharified liquid is excellent in fermentation characteristic.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) manufacture of saccharified liquid which involves performing enzyme saccharification, and pre-processing and removing pre-processed degradation products of solubilized lignocellulosic biomass; and    (2) utilization of saccharified liquid which involves fermenting microorganisms using the saccharified liquid as raw material, and manufacturing chemical substance.
NOVELTY - Fertilizer composition comprises (%): urea (20-40), dipotassium hydrogen (10-30), kara glue powder (8-20), starch (25-55), yeast powder (5-15) and brown sugar powder.    USE - Fertilizer composition used for growing fruit in cold and arid area (claimed).    ADVANTAGE - The fertilizer composition ensures improved yield, leaf photosynthetic reaction time, and activates soil microorganism.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fertilizer composition, which involves:    (A) mixing urea, dipotassium hydrogen and kara glue powder uniformly to form mixture A;    (B) mixing starch, yeast dry powder and brown sugar powder to form mixture B;    (C) adding water to the obtained mixture B, and then heating them at 40 degrees C with stirring to dissolve;    (D) cooling the obtained material to 28-34 degrees C, and then keeping the obtained material under anaerobic condition, for 3-5 days;    (E) adding water to the mixture A, and then heating them at 40-45 degrees C with stirring to dissolve;    (F) mixing the obtained material with the obtained mixture B with stirring uniformly; and    (G) adding fruit and aid-growing agent liquid to the obtained mixture to obtain finished product, where mass ratio of fruit and aid-growing agent liquid is 1:50-100.
NOVELTY - A trityl olmesartan intermediate compound (I) is prepared by hydrolysis of nitrobenzene containing compound (III) in the presence of a base ethyl containing compound (II); carrying out condensation reaction of compound (III) with the chlorobenzene containing compound (IV) in the presence of a catalyst; adding water, and using a halogenated solvent extraction system; and concentrating to give compound (I).    USE - Method for preparing trityl olmesartan intermediate compound (claimed).    ADVANTAGE - The method has mild reaction condition, little byproduct, high purity of the product, and high yield, and is environment-friendly and good for industrial production.    DETAILED DESCRIPTION - A trityl olmesartan intermediate compound of formula (I) is prepared by hydrolysis of nitrobenzene containing compound of formula (III) in the presence of a base ethyl containing compound of formula (II); carrying out condensation reaction of compound (III) with the chlorobenzene containing compound of formula (IV) in the presence of a catalyst; adding water, and using a halogenated solvent extraction system; and concentrating to give compound (I).
NOVELTY - This utility new type claims a one garbage treatment device, comprise: device main body, the set up with a feeding port and discharging port, biological reaction unit, a feeding port of the lower part, wherein a set of microorganism-containing powder, and further set with a stirrer inner in a biological reaction unit, the main shaft and the stir motor connecting the deodorizing unit and a biological reaction unit connect, for a biological unit. produce a gas, gas exit, set up on the said device main body, used for discharging from said deodorizing unit of gas, and dehydrating and sterilizing device, the two end a is connected with a biological reaction unit and a discharging port. This utility new type of a garbage treatment device for solid waste can be in particular a effect of kitchen garbage is obvious through micro-organism treatment technology for adding a garbage process, about 90% of garbage can convert to harmless of water vapour, carbon dioxide and heat, a harmless treatment of garbage.
NOVELTY - Circulating marsh gas anaerobic fermentation producing organic fertilizer system, include excrement sewage tank, fermenting preprocessing tank, solar energy water heater, a controllable container fermentation room, a discharging tank, a sedimentation tank, a rough, a stir mix device, secondary filtration, drying, moulding and granulating device and packaging machine, controllable fermentation room container set with a water inlet, a gas exit, and exit and liquid return port. The utility model is new type has reasonable design, simple structure, good sealing property, a for excrement sewage in anaerobic fermentation process stir uniform, which helps to increase efficiency and anaerobic fermentation marsh gas yield, the biogas residue and a series of processing, finally preparing into organic fertilizer, strong practicability and easy popularization and application.
NOVELTY - Method includes catalytic conversion of synthesis gas in a dimethyl ether synthesis reactor to obtain a mixture of products containing dimethyl ether, methanol, carbon dioxide and unreacted synthesis gas, followed by separation thereof and obtaining the end product by condensation from the gaseous phase. The synthesis gas subjected to catalytic conversion is obtained from steam gasification of charcoal which is formed from pyrolysis of pre-dried wood wastes, and after separating the mixture of products, the liquid phase is fed into a fractionation column to separate methanol, after which methanol and carbon dioxide-free unreacted synthesis gas of the gaseous phase is fed into the dimethyl ether synthesis reactor.    USE - Chemistry.    ADVANTAGE - Method increases output of the end product.1 dwg
NOVELTY - The reactor has a removable panel provided with a catalytic material and assembled in vertical to a particulate carbon tray. A gasification chamber is provided with a home page, which is formed with a crates openwork structure. A knot is embedded with a metal rod. A cylindrical surface structure is provided with the catalytic material. The gasification chamber is filled with a catalytic panel transport carbon dioxide material, which is deposited in a vertical pipe. A perforated surface is provided with a catalytic porous material.    USE - Chemical gas phase reactor for coal and biomass gasification.
NOVELTY - My invention aims to produce biodiesel from micro-algae at low cost to replace the hydrocarbon fuels. Aim is to modify the design of conventional photo-bioreactor to increase its capacity for algae growth and Increase the yield at minimal cost. By changing the design of photo-bioreactor; making it in form of long triangular structure with rectangular boxes present at each side of the triangle has provided more space for the cultivation of algae at minimal cost. There will be three photo-bioreactors one above the other with slanting side present at a varying angle of 30-60 depending upon the sunlight failing on the area. All the three photo-bioreactors will be connected via pumps and pipes to ensure continuous flow of algae water. Placing long reflectors long the side of photo-bioreactor to reflect sunlight onto them has helped to increase yield. Also the presence of solar panels on each side of photo-bioreactor provides sufficient energy required to run the machinery. The reuse of byproducts during the products has reduced the overall cost. Thus finally we are able to increase the yield of biodiesel from algae and reduce its cost.
NOVELTY - Process for reducing carbon dioxide emission in towns, involves reducing quantity of natural gas used in waste incinerators, increasing biogas production, and/or reducing emission of motor vehicles, where the biogas is used for incineration of wastes and/or operating motor vehicles.    USE - The process is useful for reducing carbon dioxide emission in towns.
NOVELTY - Olefins production involves evaporating ethanol fuel in a vaporizer, where ethylene is converted into ethanol evaporated in advance one or multiple reactors of dehydration in presence of catalyst. The catalyst is selected from alumina, silica-alumina, other metal oxides, metal impregnated alumina, silica-alumina impregnated with metals, impregnated with metals and metal oxides mixture. The feed stream is purified in ethanol evaporation by using a purification system by removal of inorganic salts.    USE - Method for producing olefins from ethanol fuel, preferably predominantly ethylene, particularly a mixture of ethylene, propylene and butene (claimed).    ADVANTAGE - The method produces olefins by dehydration of ethanol fuel with reduces occurrence of fouling and corrosion in equipment, increases efficiency of separation, reduces energy consumption by improving efficiency and reducing recycle equipment.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical representation depicting relative concentration of unwanted methane, carbon monoxide and carbon dioxide in the produced ethylene. (Drawing includes non-English language text).
NOVELTY - This utility new type relates to municipal domestic garbage treatment technology field in use of a stirrer, specifically a garbage fermentation one special stirrer, comprise a bracket, a bracket one end bottom fixed with a motor, a shaft diameter of a motor output shaft from the top surface, and the top of the bracket passes through the output shaft of fixed input belt wheel; the other end provided with a vertical downward extending, upper of said protection cylinder fixed with a bearing base, cylinder cross section of the inner cavity upper plate set with the lower bearing base of said upper bearing base coaxial, transmission shaft through a upper bearing base, lower bearing base is supported on said inner protecting cylinder, and end fixed with a belt wheel, a transmission belt tension to said input belt wheel, a belt wheel upper the said upper transmission shaft, lower transmission shaft end through a shaft joint connecting stir shaft, and end part fixed with self-sucking stir impeller low in a stir shaft. Using the stirrer a garbage can stir and oxygen supply two satisfy a requirement.
NOVELTY - This utility new type claims a compound fertilizer special for a one forming device, a stir chamber of the top of the fixing rack, stir electric machine fixed on the stir chamber, said stir inner pages is located in a stir chamber with the rotating shaft and a stir motor fixed connecting is provided with a material discharging hole at the bottom of the stir chamber, a forming roller and a crushing roller is distribute a is movably mounted on the upper rack, a roller surface of a forming roller is uniformly distributed with a concave pit, roller surface of said crushing roller is uniformly distributed with the material pole, a speed reducer fixed on the upper rack, the input end with a forming driving motor transmission connecting the output end and a forming roller transmission connect, a forming roller and crushing roller transmission connect, this utility new type has advantages as follows: simple structure, forming and particle finished, a process is greatly shortened, production efficiency is high, suitable for need of mass production work, it does not need drying process and cooling process, belonging to the cold extruding process directly, energy-saving, environment-friendly, would not pollute the environment.
NOVELTY - This utility new type claims a one industrial ammonium phosphate production system, belonging to the ammonium phosphate production technology field. Comprise in turn connected of industrial phosphoric acid storage tank, pool, neutralizing reaction device, first filter device, filter device, second-effect flash evaporation room I, II effect flash, flash evaporation cooling device, cooling and crystallizing device, centrifugal drying device, packing device and liquid ammonia storage tank and the neutralization reaction device is connected with a the centrifugal drying device is connected with a dust removing device, a settling tank of acid sludge output end with the fertilizer storage tank of phosphoric acid ammonium phosphate fertilizer production system is connected with a first filter device and second filter device filter cake output end of the slurry groove of said ammonium phosphate fertilizer production system, the filtered liquid output end of a centrifugal drying device with the slurry groove of said ammonium phosphate fertilizer production system. The system with the fertilizer ammonium phosphate production through a combined production, a recycle, reduces the environment pollution and reduces the production cost , filter cake and filter and so on waste of filtered liquid.
NOVELTY - Method for preparing tebuconazole with olefinic ketone involves obtaining chlorobenzaldehyde and pinacolone mother liquor as raw materials, adding catalyst to the raw materials, adding the mixture to methanol solvent system and reacting the mixture, cooling the mixture and extracting crystalline tebuconazole with olefinic ketone, washing and filtering obtained crystals.    USE - The method is useful for preparing tebuconazole, a fungicide using olefinic ketone (claimed).    ADVANTAGE - The method is simple, less labor intensive, pollution free, cost-effective and advanced, has increased production efficiency and reduces processing amount of mother liquor and methanol usage to 40%.
NOVELTY - Quat.-carbon center-containing pyrrolidone compound is synthesized by mixing 1-acyl-1-cyclopropane carboxamide and organic amine which acts as catalyst in anhydrous solvent, adding electron deficient olefin, stirring at 60-80 degrees C until reaction substrate disappears, cooling to room temperature, extracting organic phase, drying, rotary evaporating off solvent to obtain crude product, and subjecting to silica gel column chromatography.    USE - Synthesis of quat.-carbon center-containing pyrrolidone compound for pharmaceutical chemistry.    ADVANTAGE - Process is mild, simple, is environment-friendly, uses cheap and easy to get catalyst, does not need metal catalyst, and has high yield.    DETAILED DESCRIPTION - Quat.-carbon center-containing pyrrolidone compound of formula (I) is synthesized by mixing 1-acyl-1-cyclopropane carboxamide of formula (II) and organic amine of formula (III) which acts as catalyst in anhydrous solvent, adding electron deficient olefin, stirring at 60-80 degrees C until reaction substrate disappears, cooling to room temperature, extracting organic phase, drying, rotary evaporating off solvent to obtain crude product, and subjecting to silica gel column chromatography in which molar ratio of 1-acyl-1-cyclopropane carboxamide, electron deficient olefin, and organic amine is 1:1.05-1.3:0.05-0.5..    R1,R3=alkyl, or aryl;    R2=H, or alkyl; and    EWG=electron-withdrawing group, preferably CN, ester, or sulfonyl.
NOVELTY - A triclabendazole sulfoxide is prepared by adding triclabendazole in solvent, stirring, heating to dissolve, cooling to 20-35 degrees C, adding vanadium pentoxide catalyst, dripping hydrogen peroxide at 20-35 degrees C, preserving heat to crystallize, adding sodium sulfite to enable excessive decomposition of hydrogen peroxide, adding water, cooling to 10-20 degrees C, filtering to obtain wet product, dissolving in acetone, filtering to remove vanadium pentoxide catalyst, distilling filtrate, adding methanol or ethanol, cooling, filtering, and drying.    USE - Preparation of triclabendazole sulfoxide (claimed).    ADVANTAGE - The method does not produce secondary pollution, has high yield, and is low cost, and product has high yield, and is safe and reliable because it does not contain residual vanadium pentoxide catalyst and hydrogen peroxide.
NOVELTY - Tenofovir preparation involves taking adenine, (R)-propylene carbonate, and methyl benzenesulfonyloxy derivative (I) as raw material. The raw material is reacted in a single pot to obtain (6-amino-9H-purin-9-yl) propane derivative (II) as an intermediate. The obtained intermediate is hydrolyzed by using an acid to obtain the target compound tenofovir.    USE - Method for preparing tenofovir (claimed).    ADVANTAGE - The method prepares tenofovir in a simple, eco-friendly and cost-effective manner by using cheap raw material under mild reaction conditions, produces high yield and high purity.    DETAILED DESCRIPTION - Tenofovir preparation involves taking adenine, (R)-propylene carbonate, and methyl benzenesulfonyloxy derivative of formula (I) as raw material. The raw material is reacted in a single pot to obtain (6-amino-9H-purin-9-yl) propane derivative of formula (II) as an intermediate. The obtained intermediate is hydrolyzed by using an acid to obtain the target compound tenofovir.    R=methyl or ethyl group.
NOVELTY - Method for cultivating plant, involves applying fertilizer to soil, where the fertilizer is obtained by subjecting organic substance, minerals and soybean paste to aerobic fermentation using malt and salt.    USE - The method is useful for cultivating plant (claimed).    ADVANTAGE - The method enables to cultivate plant efficiently with fixed nitrogen of obligatory anaerobic microbe in underground place and increases yield of plant.
NOVELTY - Separating natural gas from gaseous compounds present at the wellhead using at least two adsorption columns, each containing an adsorbing solid and one operating at a higher pressure than the other, is claimed. The compression ratio is 1.1-10, and the ratio between the characteristic convective time through the column and the characteristic diffusive time in the adsorbing solid is higher than 1.    USE - The process is useful for separating natural gas from gaseous compounds (claimed), preferably acid gases including helium, nitrogen, carbon dioxide and hydrogen sulfide.    ADVANTAGE - The process is capable of separating natural gas from gaseous compounds with low energy losses using low compression ratio values, thus producing the natural gas with high yield and purity.
NOVELTY - The cell has mesh anode and cathodes (B), which contacts directly with the two ion permeable membranes adjacent to the center compartment and allow for polarity reversal. The first membrane is a sole active mediator for protons produced at the mesh anode to transfer into the center compartment. The end blocks have channels for a gas escape route behind the anode and cathode. The second membrane is a sole active mediator for cations in the center compartment that is displaced by the protons from the anode to transfer into the cathode compartment.    USE - Electrochemical cell for continuous acidifying alkaline water sources and recovering of carbon dioxide.    ADVANTAGE - The ion exchange properties of the ion permeable membrane separates the electrode compartments thus minimizing the time to achieve an acidic pH after a polarity reversal and electrical resistance to increases the long term process efficiency of carbondioxide extraction from alkaline water sources.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for continuously acidifying alkaline water sources and recovering carbon dioxide.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the acidification module.    Cation exchange membrane (A)    Center compartment (B)    Mesh electrodes (C)    Endblock (D)    Electrode stand-off (E)
NOVELTY - Preparing 2-(4-formylphenyl)propionic acid, comprises dissolving 2,2,6,6-tetramethyl-1-piperidinyloxy free radical and 2-(4-(bromomethyl)phenyl)propionic acid in a solvent, then stirring and drop wisely adding hydrogen peroxide solution at a temperature of 60-80 degrees C, adding an organic solvent into the solution after extraction and concentration, and separating the concentrate using column chromatography to obtain 2-(4-formylphenyl)propionic acid.    USE - The method is useful for preparing 2-(4-formylphenyl)propionic acid (claimed) that is useful as an intermediate in the synthesis of pelubiprofen.    ADVANTAGE - The method is capable of economically preparing the 2-(4-formylphenyl)propionic acid in an eco-friendly manner.
NOVELTY - Balance of plant system of solid oxide fuel cell comprises a burner (20), a reformer (30), a steam generator (40) and a heat exchanger (50). The burner, reformer, and steam generator are sequentially laminated from lower layer of steam generator, reformer, and burner, respectively. The flame and combustion gas which is produced by burner directly passes to reformer and steam generator which are provided to upper layer of burner. The heat exchanger flows exhaust gas discharged from steam generator and preheats processing air supplied by an air electrode of a stack (10).    USE - Used as balance of plant system of solid oxide fuel cell.    ADVANTAGE - The system minimizes heat loss, improves heat transfer efficiency of the entire device, and is cost effective.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a solid oxide fuel cell stack module comprising the burner, the reformer, the steam generator and the heat exchanger; and    (2) improving thermal efficiency of the solid oxide fuel cell, comprising (a) sequentially laminating the burner, the reformer, the steam generator and the heat exchanger from lower layer of the steam generator, the reformer, and the burner, and heating the flame and the combustion gas produced from the burner and directly passing to the reformer and the steam generator which is provided on upper layer of the of the burner, and (b) preheating the processing air supplied by the cathode of the stack to exhaust gas by the heat exchanger inlet.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of the balance of plant system of solid oxide fuel cell.    Stack (20) Burner (10)    Reformer (30)    Steam generator (40)    Heat exchanger (50)
NOVELTY - The device has an electrolyte solution storage unit (14) that recovers electrolyte solution sent to hydrogen generation cell. An oxygen side electrolyte solution circulation pipe (18) is linked to oxygen side electrolyte solution supply hole (11). An oxygen side electrolyte solution recovery pipe (20) is extended from liquid discharge port of oxygen side gas-liquid branch pipe (13) and is connected to electrolyte solution storage unit. The water is decomposed and hydrogen is generated by irradiating light to optical semiconductor electrode.    USE - Hydrogen generation device for energy system (claimed).    ADVANTAGE - The flow path which washes away electrolyte solution from lower side to an upper side through the flow-hole is considered. Thus the mixing of hydrogen and oxygen is prevented. Since the flow of the electrolyte solution in platinum counter electrode and photocatalyst electrode surface vicinity arises and the generation of hydrogen and oxygen bubble is prevented, the fall of hydrogen generation efficiency by polarization is suppressed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an energy system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen generation device.    Oxygen side electrolyte solution supply hole (11)    Oxygen side gas-liquid branch pipe (13)    Electrolyte solution storage unit (14)    Oxygen side electrolyte solution circulation pipe (18)    Oxygen side electrolyte solution recovery pipe (20)
NOVELTY - Producing methane, comprises contacting methanogenic microorganisms in a reaction vessel with hydrogen and carbon dioxide. The nitrogen concentration in the liquid phase inside the reaction vessel is 0.0001-35 mmol/l or 55-1000 mmol/l.    USE - The method is useful for producing methane (claimed) which is useful as vehicle fuel or in natural gas grid.    ADVANTAGE - The method provides higher yields of methane in a simple, cost effective and environmental friendly manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a system for the method comprising: at least one bioreactor comprising a reaction vessel suitable for growing, fermenting and/or culturing methanogenic microorganisms, at least one device for providing a gas feed of hydrogen and carbon dioxide into the reaction vessel, and at least one device for measuring the nitrogen concentration in the liquid phase inside the reaction vessel; optionally at least one device for generating electric energy from a renewable and/or non-renewable energy source; and optionally at least one device for producing hydrogen and/or oxygen by the electrolysis of water and/or brine; and    (2) use of a cell culture comprising methanogenic microorganisms and having a nitrogen concentration in the liquid phase of the cell culture of 0.0001-35 mmol/l or 55-1000 mmol/l for producing methane.
NOVELTY - Preparing bispyribac sodium, comprises condensing 2,6-dihydroxy benzoic acid with 2-(alkyl sulfonyl)-4,6-dialkoxy pyrimidine at 20-80 degrees C in the presence of at least one base (B1) and at least one solvent (S1).    USE - The method is useful for preparing bispyribac sodium (claimed), useful as herbicide. No biological data given.    ADVANTAGE - The method: is simple, economic and high yielding; provides bispyribac sodium that is non-toxic to fish, invertebrates, birds and mammals; saves time; obviates the use of strong acids; provides bispyribac sodium with high purity; and is environment-friendly.
NOVELTY - Method for producing sugar-solution, involves preparing pre-treated substance of cellulose-containing biomass and slurry of an inactivated cellulase, adding filamentous-fungus-derived cellulase to the pre-treated substance to perform hydrolysis, performing hydrolysis, and subjecting hydrolysate to solid-liquid separation to obtain solution component and hydrolysis residue, where the solution component is subsequently filtered through ultrafiltration membrane to obtain filamentous-fungus-derived cellulase as non-filtrate and sugar solution as a filtrate.    USE - The method is useful for producing sugar-solution which is used as raw material for fermentation.    ADVANTAGE - The method is cost-effective and environmentally-friendly, and enables reuse of cellulase.
NOVELTY - Production of fuels and chemicals involves forming formic acid; and non-biologically converting the formic acid to a product comprising an organic intermediate, where less than 10% of the formic acid is hydrogenated to methanol or reacted with ammonia to form formamide.    USE - For production of fuels and/or chemicals such as syngas formaldehyde, paraffins and/or olefins (preferably acrylic acid, ethane, propane, ethylene, propylene and/or butane, preferably propylene); carbohydrate containing at least five carbons (claimed).    ADVANTAGE - The process is environmentally beneficial as the method employs carbon dioxide from a natural source or carbon dioxide from an artificial chemical source which otherwise be discharged into the environment by the artificial chemical source. The carbon dioxide id converted to formic acid which is then converted to fuels or chemicals without the intermediate process of hydrogenating the formic acid to methanol or reacting formic acid with ammonia to form formamide.
NOVELTY - Producing pyruvic acid, comprises: culturing a lactate dehydrogenase gene deficient Sphingomonas sp. A1 strain in a medium containing alginic acid; and causing the strain to produce pyruvic acid from alginic acid and then to secrete pyruvic acid into the medium.    USE - The method is useful for producing pyruvic acid (claimed), which is useful as a raw material for synthesizing various chemical substances and polymers, and as an additive for foods and pharmaceutical products.    ADVANTAGE - The method: utilizes the alginic acid as a raw material contained in large amounts in marine biomass, hence it is cost effective; continuously produces and discharges the pyruvic acid outside the cells in an efficient and safe manner; does not cause the generation of carbon dioxide, a long-time reaction at a high temperature, and a high degree of environmental burden; utilizes less energy; and efficiently blocks an energy metabolic pathway without killing microorganisms.
NOVELTY - A photobioreactor system (100) for growing a biomass, comprises: a first tube oriented in a vertical direction; a second tube oriented in a vertical direction; a first lower adapter fitted to the lower end tube; and a first upper adapter fitted to the upper end tube; where the first lower adapter operates as a gas inlet for introducing a gas into the first tube.    USE - For growing biomass (claimed) or microorganisms such as microalgae.    ADVANTAGE - The photobioreactor system improves efficiency and production output at low cost.    DETAILED DESCRIPTION - A photobioreactor system (100) for growing a biomass, comprises: a first tube oriented in a vertical direction, where the first tube is elongate and having opposed first and second ends; a second tube oriented in a vertical direction, where the second tube is elongate and having first and second ends, an upper end tube connecting the first ends of the first and second tubes and a lower end tube connecting the second ends of the first and second tubes, where the first tube, the second tube, the upper tube, and the lower tube collectively establish a closed loop system; a first lower adapter fitted to the lower end tube; and a first upper adapter fitted to the upper end tube; where the first lower adapter operates as a gas inlet for introducing a gas into the first tube.    DESCRIPTION OF DRAWING(S) - The figure shows a side view of a photobioreactor system.    Photobioreactor system (100)    Single photobioreactor tube (110)    Rising or up portion (112)    Falling or down portion (114)    Light source (172)
NOVELTY - System for hydrolyzing cellulose to glucose has (a) one or more unmixed hydrolysis reactors for receiving and partially hydrolyzing aqueous slurry of pretreated cellulosic feedstock with cellulase enzyme to obtain mixture of partially hydrolyzed cellulose, and (b) one or more downstream mixed hydrolysis reactors for continuing the hydrolysis of resulting mixture to obtain glucose.    USE - The system is useful for hydrolyzing cellulose to glucose (claimed).
NOVELTY - The method involves inoculating microorganisms in a first-stage reactor to make waste materials fully fermented to produce acid. Alkaline substances (FF) are used to neutralize organic acid so as to regulate the pH value after acid production is finished. A second stage of dry fermentation (GG) is performed to produce methane.    USE - Two-stage dry digestion method for wastes.    ADVANTAGE - The method enables suppressing organic acid to a digestion process during anaerobic digestion. The method enables avoiding rinsing so that a large amount of waste water is not produced.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a two-stage dry digestion method.'(Drawing includes non-English language text)'    Wastes (AA)    Fermentative strains (DD)    Alkaline substances (FF)    Dry fermentation (GG)    Residue advanced treatment (II)
NOVELTY - A fuel reformer comprises a pair of electrode, modification catalyst provided between electrodes and accelerates reforming reaction of fuel, fuel-supply part to supply fuel to modification catalyst, electric-field formation part to form electric field in modification catalyst, and reduction process part to reduction-process modification catalyst before forming electric field in modification catalyst by electric-field formation part.    USE - A fuel reformer for hydrogen production (claimed).    ADVANTAGE - Reaction initial voltage can be reduced, and cheap fuel reformer can be provided.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph of the relationship between reduction process of modification catalyst and reaction initial voltage. (Drawing includes non-English language text).
NOVELTY - Biomass indenter (1) comprises: a base body in form of a straight hollow cylinder having two quarter lateral faces (2) in the form of circular sectors and a lateral surface (3) with two shell outer edges (4) which extend along the two outer jacket lines; a shaft (9) driven along the cylinder axis; and at least one rectangular push-flap hinged on the driven shaft, which is movable around the cylinder axis inside the cylinder chamber and which is dimensioned such that the length of the push-flap is less than the length of the base body.    USE - Used as a biomass indenter.    ADVANTAGE - The biomass indenter: allows introduction of large quantities of biomass into a fermenter; and is safe to use.    DETAILED DESCRIPTION - Biomass indenter (1) comprises: a base body in form of a straight hollow cylinder having two quarter lateral faces (2) in the form of circular sectors and a lateral surface (3) with two shell outer edges (4) which extend along the two outer jacket lines; a shaft (9) driven along the cylinder axis; and at least one rectangular push-flap hinged on the driven shaft, which is movable around the cylinder axis inside the cylinder chamber and which is dimensioned such that the length of the push-flap is less than the length of the base body and the width of the push-flap is less than the length of the radius of the quarter-cylinder. INDEPENDENT CLAIMS are also included for:    (1) a fermenter comprising the biomass indenter; and    (2) pressing biomass comprising using a fermenter, operating the driven shaft to the open position in an angle of 150-180 degrees , and filling the fermenter with biomass through the opening, where the protective cover is lowered to the opening of the biomass indenter.    DESCRIPTION OF DRAWING(S) - The figure shows a perspective view of the biomass indenter.    Biomass indenter (1)    Lateral faces (2)    Lateral surface (3)    Outer edges (4)    Shaft (9)
NOVELTY - Producing (10) methane (12) from biomass (14), comprises (a) producing acidified biomass (26), and (b) consuming acidified biomass to obtain methane. The acidified biomass is temporarily stored after its production and before its consumption.    USE - The method is useful for producing methane (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for the acidified biomass produced by the above method, comprising low molecular weight substances which comprise fatty acids, alcohols, amino acids or carboxylic acids, preferably formic acid, acetic acid, propionic acid, butyric acid or valeric acid.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of steps of the method for producing methane.    Producing methane (10)    Methane (12)    Biomass (14)    Acidified biomass (26)    Methanogenic microorganism (36)
NOVELTY - The method involves making the coating material of different color adhered in surface side and back surface side of sample structure (6,60). The wiping off process is carried out to wipe off coating material which is adhered to regions other than bottom portion and top portion of groove formed in sample structure by molding with respect to the both surface of sample structure after adhesion process. A coating-material color scheme confirmation process is carried to confirm color scheme position of coating material after carrying wiping process with respect to sample structure.    USE - Roll forming processing method of thin plate used during manufacture of solid electrolyte type fuel cell.    ADVANTAGE - The phase difference of the rotation phase of one roll blade and the rotation phase of the other roll blade is visually confirmed easily with the naked eye by the difference arising from the color scheme position of the coating material. Since the notch of the roll blade resulting from the recessed portion of the other roll blade not engaging with the convex portion of the roll blades in an appropriate position, and roll blade damage caused due to abnormal abrasion is prevented, and the manufacturing cost of the raw material is reduced. The maintenance management of the roll blade meshing type molding apparatus and static accuracy confirmation is performed easily.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the roll blade meshing type molding apparatus.    Sample structure (6,60)    Concave portions (7,61)    Convex portions (8,62)
NOVELTY - Preparing fermentation broth, comprises preparing a seed inoculum solution by mixing tea leaves, sugar including molasses, salt and vinegar; preparing a liquid nutrient medium by mixing sugar including molasses, salt and water; preparing a culture medium by mixing the seed inoculum solution, the liquid nutrient medium and a lactic acid bacteria culture fluid; fermenting and aging the mixture; and storing the mixed fermentation mixture.    USE - The method is useful for preparing fermentation broth that is useful in a composition (claimed) such as fertilizer composition used for promoting the growth of crops.    ADVANTAGE - The method is capable of eco-friendly and economically preparing the fermentation broth with high production yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a composition manufactured from the fermentation broth.
NOVELTY - Method of recovering and molding microalgae is performed by supplying (S1) culture solution containing microalgae from end surface of porous filter, filtering, storing microalgae in filtration cell, producing molded object of microalgae while recovering microalgae in filtration cell, performing backwashing process (S2) from flow path, and discharging (S3) molded object through end surface.    USE - Method of recovering and molding microalgae for production of solid fuel used for power station (claimed).    ADVANTAGE - Microalgae containing oil component can be easily recovered, and molded object of microalgae can be produced at low cost.    DETAILED DESCRIPTION - Method of recovering and molding microalgae is performed by using porous filter provided with separation membrane which does not permeate microalgae and is positioned in inner wall face of filtration cell and porous body which comprises flow path for connecting water collection cell and exterior space and permeates water in which water collection cell has sealed opening end surface and other end surface and filtration cell has end surface, other end surface, and outer peripheral surface, supplying (S1) culture solution containing microalgae from end surface of porous filter, filtering, storing microalgae in filtration cell, producing molded object of microalgae while recovering microalgae in filtration cell, performing backwashing process (S2) from flow path, and discharging (S3) molded object through end surface.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of the 1st method of recovering and molding microalgae. (Drawing includes non-English language text).    Supplying process of culture solution (S1)    Backwashing process (S2)    Discharging process (S3)    Recycling process of backwashing wastewater (S4)
NOVELTY - A ceramic component (10) has several open pores which permeate liquid and cylindrical porous support (14) having hollow portion (12) set as opening (14a). The liquid is grinding media and organic solvent for to-be-injected culture solution for culturing/spin-drying process of algae material. In the hollow portion alga material is pulverized in oil extraction process.    USE - Ceramic component is used for system for extracting algae oil (all claimed) used as biofuel for transport.    ADVANTAGE - The system containing the ceramic component extracts algae oil with high yield by simple and economical process, in short period of time.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) algae oil-extraction system, which extracts oil from algae material using ceramic component; and    (2) algae oil extracting method.    DESCRIPTION OF DRAWING(S) - The drawing shows the perspective view of ceramic component.    Ceramic component (10)    Hollow portion (12)    Porous support (14)    Opening (14a)    Filter membrane (16)    Heater electrode (18)
NOVELTY - Manufacturing silica fertilizer involves utilizing steelmaking slag produced from an iron mill. The steelmaking slag having basicity 3 or less comprises (in wt.%): soluble silicic acid (15-35) and soluble lime (30-45). The steelmaking slag is pulverized and mixed in a blast furnace and then granulated to obtain the desired product.    USE - Method for manufacturing silica fertilizer (claimed).    ADVANTAGE - The method enables to manufacture silica fertilizer in a cost-effective and eco-friendly manner such as dust-proof at time of fertilizer spreading.
NOVELTY - A radioactive substance removal apparatus (100) comprises purification box (110) with opening (112) which is positioned on bottom face and covers bottom sludge, introducing part (120) which introduces microorganisms for taking radioactive substance dissolved in water from bottom sludge and gas containing oxygen into purification box, and collection part (140) which collects microorganisms in purification box to exterior of purification box.    USE - A radioactive substance removal apparatus for removing radioactive substance adhering to bottom sludge (claimed).    ADVANTAGE - Radioactive substance can be removed from bottom sludge, therefore preventing spread of radioactive substances.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for radioactive substance removal method for removing radioactive substance adhering to bottom sludge which involves introducing microorganisms and gas containing oxygen into purification box (110) with opening (112) and collecting microorganisms in box to exterior of purification box after predetermined time.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the radioactive substance removal apparatus. (Drawing includes non-English language text).    Radioactive substance removal apparatus (100)    Purification box (110)    Opening (112)    Introducing part (120)    Collection part (140)
NOVELTY - Culture medium comprises coconut water and nitrogen source, optionally along with magnesium salt and excipient or their combinations.    USE - The culture medium is useful for enhancing growth or biomass concentration of prokaryotic or eukaryotic cell, and enhancing protein expression of recombinant protein chosen from maltose binding protein (MBP), MBP-tobacco etch virus protease (MBP-TEV) protease fusion and photo switchable florescent protein (mEos2) or their combinations in E.coli or P.pastoris (all claimed).    ADVANTAGE - The culture medium obtains uniform growth, overcomes inconsistency in growth pattern, enhances the growth or biomass concentration of E.coli and P.pastoris by 2-10 folds and 1.5-3 folds, respectively comparing with growth or biomass concentration when grown in existing media, as coconut water is normalized by nitrogen, facilitates successful expression of recombinant proteins by prokaryotes and eukaryotes, and avoids usage of animal product. The culture medium preparation method is simple, convenient and cost-effective, and favors no leaky expression in case of lactose operon (lac-operon) based systems, as lactose is not added.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method (M1) for preparing culture medium involves combining coconut water with nitrogen source, optionally along with magnesium salt and excipient or their combinations;    (2) method (M2) for enhancing growth or biomass concentration of prokaryotic cell or eukaryotic cell or enhancing its protein expression or their combinations, involves culturing the prokaryotic or eukaryotic cell in the above-mentioned culture medium; and    (3) kit comprising the above-mentioned culture media along with an instruction manual.
NOVELTY - The system has vacuum valve (251) that is connected to the vacuum pressure switch (220) for maintaining the pressure gauge (210) and the internal vacuum pressure in the upper lid (200). The rotary shaft (262) of motor (261) is perpendicularly set up in the tank (100). The rotating blade (260) is formed in the rotary shaft. The transfer pipe (320) is provided with transfer screw (322) which is rotated by the vent (301). The rotating blade (310) is rotated by the motor (311) in the vent. The fluid pressure gate (330) is operated with the hydraulic cylinder in the exit of transfer pipe.    USE - Batch aerobic and anaerobic sequential dry fermentation system.    ADVANTAGE - The methane gas is collected efficiently, and the aerobic digestion reaction and anaerobic digestion reaction processes the organic waste efficiently.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a batch aerobic, and the anaerobic consecutive dry fermentation method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the batch aerobic and anaerobic sequential dry fermentation system.    Tank (100)    Upper lid (200)    Pressure gauge (210)    Vacuum pressure switch (220)    Vacuum valve (251)    Rotating blade (260)    Motors (261,311)    Rotary shaft (262)    Vent (301)    Rotating blade (310)    Transfer pipe (320)    Transfer screw (322)    Fluid pressure gate (330)
NOVELTY - Combined generation of synthetic natural gas and methanation in fuel cell involves producing oxygen using air separation unit , producing carbon monoxide in gasifier using oxygen and coal, producing hydrogen in water gas shift reactor using carbon monoxide, generating methane gas using obtained hydrogen and carbon monoxide in methane effector, and conducting power generation by supplying fuel cell with methane gas.    USE - Combined generation of synthetic natural gas and methanation in fuel cell (claimed).    ADVANTAGE - The method is efficiently carried out with improved energy efficiency, without affecting the environment.
NOVELTY - The alkaline electrolyser, in which electrolysis is performed without separating hydrogen and oxygen gases obtained by dissociation of water by graphite electrodes (2). The electrodes are isolated by separating plates (1) and permanently attached ins a sealed tank (5) that has de-ionized water. Sodium hydroxide electrolyte with a low concentration is added into the de-ionized water. The terminal electrodes form positive pole (4) and negative pole (3). The separating plates have two holes, which form two electrolyte circulation channels (6,7) connected to electrolyte inlet and outlet channels.    USE - Alkaline electrolyser for use in electrolysis industry for the production of synthetic hydrocarbons.    ADVANTAGE - Enables to easily produce hydrogen with maximum and extremely pure yield, while costs of production are reduced and energy efficiency is increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an alkaline electrolyser. (Drawing includes non-English language text).    Separating plates (1)    Graphite electrodes (2)    Negative pole (3)    Positive pole (4)    Sealed tank (5)    Electrolyte circulation channels (6,7)
NOVELTY - Reducing level of carbon dioxide during biological purification of biogas conducted in devices for purification of biogas, involves using biofilter loaded with biological filter bed sprinkled with a mineral medium, containing immobilised microorganisms, carrying out the process under anoxic conditions using a consortium of microorganisms collected from sulfur-rich natural environments, and sprinkling the biological filter bed with a medium in the form of a solution containing nitrates of alkali metals of (I) and (II) group.    USE - The method is useful for reducing level of carbon dioxide level by at least 25% during biological purification of biogas (all claimed).    ADVANTAGE - The method effectively utilizes biogas as an energy source and also has a beneficial effect on logistics, as it makes it possible to reduce the size of biogas storage tanks, facilitates its supply into municipal natural gas infrastructure, and provides S/N value of 1-30, preferably 2-20.    DETAILED DESCRIPTION - Reducing level of carbon dioxide during biological purification of biogas conducted in devices for purification of biogas, involves using biofilter loaded with a biological filter bed sprinkled with a mineral medium, containing immobilised microorganisms capable of degrading hydrogen sulfide, carrying out the process under anoxic conditions using a consortium of microorganisms collected from sulfur-rich natural environments, and sprinkling the biological filter bed with a medium in the form of a solution containing nitrates of alkali metals of (I) and (II) group, where the concentration of nitrate ions in the medium is 20-2500 mg/l, preferably 50-1000 mg/l.
NOVELTY - The method involves determining properties of a series of 3-component blends as ethanol, butanol and gas-to-liquids (GTL) naphtha. A blend modeling tool kit is used to determine a blend space available to give an admixture with a research octane number (RON) value above 95. A series of experiments is performed with blends of n-butanol, ethanol and GTL naphtha and blends of I-butanol, ethanol and GTL naphtha is windowed. RON and RVP are measured and plotted for the blends.    USE - Method for using butanol and GTL naphtha in a transport fuel e.g. petrol such as ASTM D4814 or EN228, petrol/alcohol blend such as E85- ASTM 5798-11 or E85-CEN/TS 15293:2011, for combustion in a spark-ignited internal combustion engine. Uses include but are not limited to an E0, E10, E20 and E85.    ADVANTAGE - The method enables providing renewable feedstock for alcohol components and a potentially valuable outlet for GTL naphtha molecules.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph of impact of variation in ethanol content in a blend including 10% volume GTL naphtha and balance of blend is n-butanol.
NOVELTY - A recombinant vector comprising gene of dockerin module of cellulase, kappa-carrageenase gene, chimeric kappa-carrageenase gene, chimeric lambda -carrageenase gene, lambda -carrageenase gene or their combinations, is new.    USE - The recombinant vector is useful for producing recombinant microorganism (claimed).    ADVANTAGE - The decomposition method is simple, cost-effective and environmentally-friendly. The separation and purification of the carrageenase is cost-effective as it utilizes cheaply available cellulase.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) recombinant microorganism transformed by the recombinant vector;    (2) method for preparing kappa-carrageenase, chimeric, kappa-carrageenase, chimeric lambda -carrageenase, and lambda -carrageenase, involves culturing the above-mentioned microorganism;    (3) method for preparing carrageenase enzyme complex, involves (a) combining chimeric kappa-carrageenase gene and mini cellulose-binding protein-A, (b) combining chimeric lambda -carrageenase gene and mini cellulose-binding protein-A, or (c) combining chimeric lambda -carrageenase gene and mini cellulose-binding protein-A, where the enzyme complex comprises mini-cellulose-binding protein A gene comprising cellulose combining module (CBM) and cohesin module, and cellulose-binding protein A, and primary scaffolding subunit;    (4) carrageenase enzyme complex prepared by above-cited-method; and    (5) decomposition method of the carrageenase containing biomass involves using carrageenase gene enzyme complex.
NOVELTY - Enzymatic composition comprises beta -glucosidase 7 (BGL7) polypeptide having at least 90% sequence identity to the amino acid sequence of SEQ ID NO: 2 (comprising a fully defined sequence of 740 amino acids as given in the specification), an endoglucanase, and a cellobiohydrolase (CBH). The BGL7 polypeptide is from a different species than EG and/or CBH.    USE - The enzymatic composition is useful for producing ethanol (claimed), and in detergent compositions and feed compositions.    ADVANTAGE - The enzymatic composition provides detergent composition that exhibits enhanced cleaning ability, and functions as a softening agent, thus improving the feel of cotton fabrics.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for: producing ethanol comprising either: contacting a biomass composition with the enzymatic composition to yield a sugar solution, adding to the sugar solution a fermentative microorganism, and culturing the fermentative microorganism under conditions sufficient to produce ethanol; or a contacting a biomass composition with the enzymatic composition and a fermentative microorganism, and culturing the fermentative microorganism under conditions sufficient to produce ethanol.
NOVELTY - Manufacturing compost comprises mixing dewatered sludge or livestock excretion sludge, manure and sawdust according to a weight ratio of 7:2:1, processing the mixture into a high speed fermentation dryer for 12 hours to obtain sludge compost and then fermenting or maturing for 30 days.    USE - The method is useful for manufacturing compost (claimed) which is useful for recycling fuel.    ADVANTAGE - The method is capable of manufacturing the compost in eco-friendly and economical manner with high-quality, and without the creation of bad smell.
NOVELTY - Dissolution or extraction of cellulose is performed by decaying plant-derived biomass or lignocellulose by microorganisms containing white-rot fungi and heat-processing plant-derived biomass or lignocellulose in ionic liquid.    USE - Dissolution or extraction of cellulose for saccharification process and bioethanol production.    ADVANTAGE - Cellulose extraction efficiency improves by 2 times, and process has low waste material, low cost, and high safety and does not require special installation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for collection of cellulose which involves decaying plant-derived biomass or lignocellulose by microorganisms containing white-rot fungi, heat-processing plant-derived biomass or lignocellulose in ionic liquid, adding aqueous solvent to ionic liquid, and separating cellulose.
NOVELTY - The present invention provides a process for the preparation of retigabine, its intermediate compounds and pharmaceutically acceptable salts thereof.
NOVELTY - An absorption tower (1) is washed by pressure reduction process which reduces pressure in absorption tower, water filling process which fills water in absorption tower until the filler in absorption tower immerses, and bubbling process which carries out gas stirring of water filled in absorption tower by sending anaerobic gas in absorption tower to which pressure fell by anaerobic gas.    USE - Washing process of absorption tower (claimed).    ADVANTAGE - Sulfur which precipitated on the sulfur oxidizing bacteria which bred on filler surface in an absorption tower is removed without using chemical such as sodium hypochlorite.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a sewage-gas purifier (100) comprising control apparatus (6) which controls washing of absorption tower (1) by which control structure is carried out so that gas stirring of water filled in absorption tower by sending anaerobic gas in absorption tower and pressure fall may be carried out by anaerobic gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the sewage-gas purifier. (Drawing includes non-English language text).    Absorption tower (1)    Sewage-gas compressor (3)    Dehumidifier (4)    Feed water pump (5)    Control apparatus (6)    Sewage-gas purifier (100)
NOVELTY - The apparatus has a detection unit that detects the amount of phosphorus of the to-be-processed water which flows in into a primary sedimentation basin (1) from system outside. An output unit outputs the signal which makes the amount of bypass inflow to-be-processed water of to-be-processed water by which bypass inflow is carried out from system outside, into predetermined value. An adjustment unit adjusts the amount of bypass inflow to-be-processed water to anaerobic tank (4) according to the output value of output unit.    USE - Apparatus for controlling biological water treatment apparatus for removing nitrogen in to-be-processed water flowed into lakes and marshes or bay.    ADVANTAGE - The quantity of phosphorus flowing out of the system is reduced reliably, even when the flow volume and the concentration of the sewage which flow in from system outside are varied.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the control apparatus of biological water treatment apparatus. (Drawing includes non-English language text)    Primary sedimentation basin (1)    Biological reactor (2)    Final sedimentation tank (3)    Anaerobic tank (4)    Regulator (127)
NOVELTY - Claimed is a method of water and permafrost soil purification from oil and oil products. The method includes the application of a bacterial suspension based on cells of nonpathogenic strain of the bacteria Pseudomonas panipatensis VKPM V-10593 with titre 1.109 microbial cells/cm3.    USE - Chemistry.    ADVANTAGE - Invention ensures a high degree of soil and water purification from oil and oil products in a wide range of temperatures.3 tbl, 4 ex
NOVELTY - A Pseudomonas strain SP2 (KACC 91720P) capable of producing vitamin B12 under aerobic condition, is new.    USE - The Pseudomonas strain SP2 is useful for producing vitamin B12 and 3-hydroxypropionic acid (all claimed).    ADVANTAGE - The Pseudomonas strain SP2 environmentally-friendly produces vitamin B12 and 3-hydroxypropionic acid using cost-effective carbon source.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) method (M1) for producing vitamin B12, involves culturing the Pseudomonas strain SP2 in culture medium containing carbon source under aerobic conditions, and obtaining vitamin B12 from the culture medium; (2) recombinant strain obtained by transducing the Pseudomonas strain SP2 with DhaB gene encoding glycerol dehydratase and gdrAB gene encoding glycerol dehydratase reactivase; and (3) method (M2) for producing 3-hydroxypropionic acid, involves culturing the above-mentioned recombinant strain in culture medium containing carbon source, and obtaining 3-hydroxypropionic acid from the culture medium.
NOVELTY - Dimethyl carbonate (I) is dripped into a mixture containing taurine (II) and aqueous solution of sodium hydroxide, heated, and the temperature is increased with reaction time. The reaction mixture is concentrated to obtain N-methyl sodium taurate (III) and byproducts such as methanol, carbon dioxide and water.    USE - Preparation of N-methyl sodium taurate (claimed).    ADVANTAGE - The method efficiently, safely and economically provides N-methyl sodium taurate having high yield and quality, by simple method with few reaction processes without affecting the environment.    DETAILED DESCRIPTION - Dimethyl carbonate of formula (I) is dripped into a mixture containing taurine of formula (II) and aqueous solution of sodium hydroxide, heated, and the temperature is increased with reaction time. The reaction mixture is concentrated to obtain N-methyl sodium taurate of formula (III) and byproducts such as methanol, carbon dioxide and water.
NOVELTY - Distillation/dehydration process for manufacture of fuel-grade bioethanol involves concentrating bioethanol fermentation liquid in separation column to obtain tertiary bioethanol vapor, providing the resultant product into dewatering tower in which bioethanol concentrate is separated and provided into separation column reflux tank, cooling the resultant product to obtain primary bioethanol vapor, providing the resultant product into rectification column in which secondary bioethanol is obtained, and then providing the resultant product into dewatering tower.    USE - Distillation/dehydration process for manufacture of fuel-grade bioethanol (claimed).
NOVELTY - The apparatus has a flux control tank (110) controls the flow rate of waste water and sludge. The sterilizing water applied from a water tank (150) is ejected to UV sterilization bath (140) for predetermined time. The UV sterilization bath delivers UV ray to drain water for purifying sterilizing water. A bioreactor (130) disassembles the organic compound of waste water using microorganism. The organic compound of waste water for decomposition is supplied to an aeration tank (120).    USE - Wastewater purifying apparatus for managing marine cage.    ADVANTAGE - The organic compound is biologically disassembled using microorganism and wastewater is purified. The purge water is discharged using quartz tube after purification and virus is sterilized effectively. The fishes and shellfishes in fish farm are maintained reliably. Since the temperature of bioreactor is maintained, the energy damping is minimized. The ozone and chlorine component remaining in purge water are ejected after evaporation, such that the drain water which is changed to cleaning water is reused.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for waste water purification method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the wastewater purifying apparatus. (Drawing includes non-English language text)    Flux control tank (110)    Aeration tank (120)    Bioreactor (130)    UV sterilization bath (140)    Water tank (150)
NOVELTY - Compost preparation device comprises case, in which feeding and transporting worm conveyors are arranged in parallel, chamfered blades radially placed in three rows of middle part of feed screw shaft, coiling provided in both sides of transporting worm conveyor, and helical winding having tooth-like form.    USE - Compost preparation device.
NOVELTY - Producing methane gas and hydrocarbons involves utilizing aquatic animals such as fish, shellfish, octopus and squid. Flesh of aquatic animals is decomposed through anaerobic fermentation by using Archaea to obtain hydrocarbons, inorganic compounds, carbohydrates, methane and other and organic compounds.    USE - Method for producing methane gas and hydrocarbons from aquatic animals.
NOVELTY - Producing organic based entomopathogenic fungi spores involve adhering organic based compound on surface of the spores, and then biodegradable oil by utilizing a machine.    USE - Method for producing organic based entomopathogenic fungi spores for biological control of pests in vegetables.    ADVANTAGE - The method enables to produce organic based entomopathogenic fungi spores in an eco-friendly manner, where spores have insecticidal property..
NOVELTY - Device comprises a fermentation chamber that is equipped with deposition of biomass with thermally insulating foundation walls. Dome shape rigid structure covers top of the fermentation chamber having two membrane layers, which form biogas storage tank. Two membrane layers are installed on opposite sides of the arched rigid structure, where diaphragm is present on lower region. Device also comprises gas passage openings, channel fan duct inlet, vertical walls, biomass tank, nozzles, channel, perforated septum, fan, return line, fixed bed and exhaust gases.    USE - Device used for producing biogas.
NOVELTY - Producing biofuel involves utilizing agavaceae family plant or biological materials which are consumed by human or animal.    USE - Method for producing biofuel.
NOVELTY - Enrichment liquid comprises sulfur particle, activated sludge and minimum medium containing 1.647 mg magnesium chloride hexahydrate, 47 mg dipotassium hydrogen phosphate, 27 mg sodium dihydrogen phosphate monohydrate, 16 mg ammonium dihydrogen phosphate and 1 g sodium bicarbonate.    USE - The enrichment liquid or apparatus is used for removal of perchlorate and nitrate (all claimed).    ADVANTAGE - The enrichment liquid has detection limit less than 0.62 mu g perchlorate and 47.6 mu g nitrate. The apparatus enables continuous removal of perchlorate and nitrate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus for continuous removal of perchlorate and nitrate using enriched sulfur-oxidizing microorganisms.
NOVELTY - Fuel chip comprises livestock sample and oyster shell powder in a weight ratio of 1:0.05-0.2.    USE - The fuel chip is useful for preparing environmentally-friendly fertilizer (all claimed).    ADVANTAGE - The chip provides economic fuel as it contains nitrogen, phosphate, potassium, magnesium and calcium components.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) environmentally-friendly fertilizer comprising the residue which remains after performing combustion of the fuel chip;    (2) method for preparing the fuel chip, involves (a) immersing the oyster shell in water and removing salinity of the oyster shell, (b) drying and pulverizing the oyster shell to obtain powder, (c) mixing the livestock sample and oyster shell powder in a weight ratio of 1:0.05-0.2, and (d) molding the mixture in the form of chip; and    (3) method (M1) for preparing environmentally-friendly fertilizer, involves performing the above-mentioned steps (a)-(d), and subjecting the obtained chip to combustion.
NOVELTY - A carbon dioxide recovering method involves generating carbonic gas in an environment free of combustion gases by combustion treatment of organic matter external to the gas-free environment, followed by purifying free carbon dioxide and/or external free environment by cooling and/or storage, and adding environmental carbon dioxide to culture medium of photosynthetic microorganisms.    USE - Method for recovering carbon dioxide that is utilized for preparing medium for cultivating photosynthetic microorganisms such as microalgae and/or cyanobacteria, preferably Spirulina spp. that is utilized in production of animal feed, food supplement for human consumption, bioremediation, bio-fertilizers, biofuels, cosmetics and/or drugs, arising out of thermal decomposition of mineral material (all claimed).    ADVANTAGE - The method enables recovering carbon dioxide with improved economic and environmental benefits.
NOVELTY - A carbon dioxide concentration measuring unit (S1,S2) is installed on exhaust gas line for measuring carbon dioxide concentration within exhaust gas. Electronic control valve (V2) is installed between hydrogen reservoir (110) and exhaust gas line (L1) for controlling injection amount of hydrogen. Biological carbon dioxide reduction container (150) converts carbon dioxide into methane and ejected. Oxygen concentration detector (S3) measures oxygen content within mixing gas. Controller (160) controls supply direction of mixing gas to biological carbon dioxide reduction container.    USE - Biological methane conversing apparatus for reducing carbon dioxide in exhaust gas.    ADVANTAGE - The carbon dioxide included in the exhaust gas is biologically converted into methane. The degradation of the pH of the injected surplus hydrogen and occurrence of the impediment in the operation is prevented by measuring concentration of the carbon dioxide and controlling the injection amount of hydrogen appropriately.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biological methane conversing apparatus.(Drawing includes non-English language text)    Hydrogen reservoir (110)    Biological carbon dioxide reduction container (150)    Controller (160)    Exhaust gas line (L1)    Carbon dioxide concentration measuring unit (S1,S2)    Oxygen concentration detector (S3)    Electronic control valve (V2)
NOVELTY - Producing Stevia liquid compost, comprises (S1) washing stems and leaves of Stevia, and extracting to obtain extract and sludge of Stevia, (S2) mixing the extract and sludge of Stevia, (S3) mixing Stevia core catalyst with the obtained mixture, (S4) fermenting the core catalyst mixed Stevia by inoculating with Bacillus strain, Lactobacillus strain and Pichia pastoris strain, (S5) aging the fermented material, and (S6) filtering the aged product.    USE - The method is useful for producing Stevia liquid compost (claimed).    ADVANTAGE - The method is simple, cost effective, and has short production time. The liquid compost increases sugar content of fruit, and beneficial microorganisms into soil, and is conservative.    DETAILED DESCRIPTION - Producing Stevia liquid compost, comprises (S1) washing stems and leaves of Stevia, and juice extracting to obtain extract and sludge of Stevia, (S2) mixing the extract and sludge of Stevia, (S3) mixing Stevia core catalyst into the obtained mixture, (S4) fermenting the core catalyst mixed material by inoculating with Bacillus strain, Lactobacillus strain and Pichia pastoris strain, (S5) aging the fermented material, and (S6) filtering the aged material. The Stevia core catalyst is produced by (a) freeze drying Stevia fresh leaves, (b) crushing and filtering the freeze dried Stevia fresh leaves, (c) hot water extracting the filtered product, and (d) drying the obtained extract to prepare Stevia core catalyst. The step (S2) is carried out by mixing Taheebo extract or coriander extract. An INDEPENDENT CLAIM is also included for Stevia liquid compost manufactured by above method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic flow chart of the method for producing Stevia liquid compost (Drawing includes non-English language text).    Washing and extracting step (S1)    Extract and sludge mixing step (S2)    Stevia core catalyst mixing step (S3)    Fermenting step (S4)    Aging step (S5)
NOVELTY - Producing tamsulosin or its salt, comprises (a) reacting 2-ethoxy phenol and ethylene carbonate to obtain 2-(2-ethoxy-phenoxy)ethanol, (b) reacting 2-(2-ethoxy-phenoxy)ethanol with methanesulfonyl halide to obtain 2-(2-ethoxy-phenoxy)ethyl methanesulfonate, and (c) reacting 2-(2-ethoxy-phenoxy)ethyl methanesulfonate with (R) (-)-5-(2-aminopropyl)-2-methoxy-benzenesulfonamide.    USE - The method is useful for producing tamsulosin or its salt (claimed).    ADVANTAGE - The method is simple, environmentally friendly; and provides tamsulosin with high purity.
NOVELTY - The manufacturing device has separation film (27) that injects magnesium, so that lightly doped low-phosphorus acid is held. Concentration of nitrogen is 0.1-0.15%. The concentration of nitrogen is reduced, and reacted with ammonia nitrogen and phosphorus. The nitrogen in liquefied fertilizer reservoir (28) is reduced. Low-phosphorus acid with low concentration is separated from precipitation separator (30). The liquefied fertilizer and crystal are separated by precipitation separator to form struvite fertilizer (32).    USE - Manufacturing device for tailor-made type liquefied fertilizer for generating station, crops greenhouse boiler and industry boiler.    ADVANTAGE - The biogas is produced easily, using the livestock excretions. The useful thermal energy is supplied effectively, and the high quality organic fertilizer is supplied, by the produced liquefied fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a tailor-made type liquefied fertilizer manufacturing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the manufacturing device of the tailor-made type liquefied fertilizer. (Drawing includes non-English language text)    Denitrification tank (24)    Separation film (27)    Liquefied fertilizer reservoir (28)    Precipitation separator (30)    Struvite fertilizer (32)
NOVELTY - Synthesizing trans-cinnamic alcohol comprises (a) adding thioanisole and a formylating reagent in an organic solvent and then reacting by a acylation reaction to prepare a mercapto-benzaldehyde, (b) mixing a basic catalyst with mercapto-benzaldehyde and acetaldehyde in an organic solvent II and then reacting by aldol condensation reaction to obtain trans-cinnamaldehyde, and (c) mixing the trans-cinnamaldehyde with a reducing agent and then reacting by a reduction reaction. The formylating agent is N,N-dimethylformamide, phosphorus oxychloride, solid phosgene, oxalyl chloride or phosgene.    USE - The method is useful for synthesizing trans-cinnamic alcohol (claimed).    ADVANTAGE - The method is capable of economically synthesizing trans-cinnamic alcohol in an eco-friendly manner with mild reaction condition.    DETAILED DESCRIPTION - Synthesizing trans-cinnamic alcohol comprises (a) adding thioanisole and a formylating reagent in an organic solvent and then reacting by a acylation reaction to prepare a mercapto-benzaldehyde, (b) mixing a basic catalyst with mercapto-benzaldehyde and acetaldehyde in an organic solvent II and then reacting by a aldol condensation reaction to obtain trans-cinnamaldehyde, and (c) mixing the trans-cinnamaldehyde with a reducing agent and then reacting by a reduction reaction. The formylating agent is N,N-dimethylformamide, phosphorus oxychloride, solid phosgene, oxalyl chloride or phosgene. The organic solvent is N,N-dimethylformamide, dichloromethane, chloroform, 1,2-dichloroethane or tetrahydrofuran. The basic catalyst is sodium hydroxide, potassium hydroxide, potassium acetate, potassium carbonate, potassium bicarbonate, potassium fluoride or tetrabutyl ammonium hydroxide. The organic solvent II is tetrahydrofuran, methanol, ethanol, isopropanol or n-butanol.
NOVELTY - Preparation of 4,6-dichloro-5-nitro-2-(propylthio)pyrimidine (I) comprises performing cyclization reaction of 2-nitro-1,3-malonic acid alkyl ester and thiourea to obtain 5-nitro-2-thioxo-sodium pentobarbital, performing sulfur alkylation reaction with halogenated propane to obtain 4,6-dihydroxy-5-nitro-2-(mercaptopropyl)pyrimidine and chlorinating with chlorinating agent.    USE - Method for preparing 4,6-dichloro-5-nitro-2-(propylthio)pyrimidine (I) (claimed) used for production of medicine.    ADVANTAGE - The simple, economical and environment-friendly method uses raw materials which are easy to obtain.    DETAILED DESCRIPTION - Preparation of 4,6-dichloro-5-nitro-2-(propylthio)pyrimidine of formula (I) comprises performing cyclization reaction of 2-nitro-1,3-malonic acid alkyl ester and thiourea to obtain 5-nitro-2-thioxo-sodium pentobarbital, performing sulfur alkylation reaction with halogenated propane to obtain 4,6-dihydroxy-5-nitro-2-(mercaptopropyl)pyrimidine and chlorinating with chlorinating agent.
NOVELTY - A pumpkin planting compound fertilizer comprises 1000-2000 kg seaweed powder, 15-20 kg compound fertilizer, 10-20 kg nitrogenous fertilizer, 50-80 kg humus, 30-50 kg phosphate rock powder, 10-15 kg aqueous ammonia, 100-200 kg chicken manure, 1-2 kg trace elements, 50-100 kg bone meal powder, and 80-150 kg talc.    USE - Pumpkin planting compound fertilizer.    ADVANTAGE - The fertilizer is simple and convenient to use, and has low cost, high yield, and good benefits.
NOVELTY - Preparation of organic animal corpse fertilizer by cutting animal corpse, crushing at 2 mm particle size, sealing, sterilizing with ozone, adding 6-15 kg nitrogen-fixing bacteria to 100 kg sterilized animal corpse, stirring at 1-40 degrees C and humidity of 40-95%, sealing, anaerobic fermenting for 10-45 days, and packaging.    USE - Method for preparing organic animal corpse fertilizer (claimed).    ADVANTAGE - The method is eco-friendly.
NOVELTY - A wet ammonium sulfate product has water content of 2-12%.    USE - Wet ammonium sulfate product used in preparation of fertilizer.    ADVANTAGE - The product is simple to prepare with low device investment and energy consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the wet ammonium sulfate product using flue gas, ammonia, air and water as raw materials and using a washing column comprises:    (1) entering the flue gas into the absorption section of the scrubber washing the upper part in close contact with absorbing solution containing ammonia, cooling the flue gas, absorbing sulfur dioxide and hydrogen chloride to form ammonium sulfate and ammonium chloride and washing the dust in the flue gas into absorbing liquid;    (2) passing the absorbing liquid solution directly into an oxidation zone of the lower part of the washing tower, oxidizing the absorbing liquid and crystallizing, adding ammonia, repeatedly absorbing and washing the flue gas and precipitating crystals of ammonium sulfate so that the absorbing liquid becomes a slurry and    (3 ) when the content of the ammonium sulfate crystals of ammonium sulfate in the slurry is over 5-20% of the slurry extracted from the oxidation of the ammonium sulfate in the crystallization stage, dewatering to obtain ammonium sulfate crystals containing 30-60% concentration of the slurry, dehydrating the concentrated slurry to obtain the wet product ammonium sulfate, dewatering the obtained supernatant mother liquor back to the washing column and repeatedly crystallizing.
NOVELTY - Preparing rifampicin by using a microreactor apparatus comprises dissolving rifamycin oxazine in an organic solvent to obtain a homogeneous solution, dissolving 1-methyl-4-nitro-piperazine in an organic solvent to obtain homogeneous solution, pumping the two homogeneous solutions into the apparatus and collecting outflow liquid which is the rifampicin crude product.    USE - Method for preparing rifampicin (claimed).    ADVANTAGE - The method uses microreactor having large specific surface area, high transfer rate, short contact time, less byproduct, very strong mass transfer ability, high safety, good operability, good portability, and high operation of elasticity.
NOVELTY - Method for preparing medicine treating dry cucumbers leaves, involves (a) obtaining e.g. oxadixyl giant knotweed, ginger, cinnamaldehyde and copper-methyl, (b) performing extraction of the giant knotweed and ginger using water or alcohol e.g. ethanol, and heating and recycling ethanol to obtain extract, and (c) adding oxadixyl, cinnamaldehyde, copper-methyl to the extract obtained in the step (b), and mixing and uniformly stirring the mixture to obtain product.    USE - The method is useful for preparing medicine for treating dry cucumbers leaves (claimed) and downy mildew of cucumber.    ADVANTAGE - The method is simple to perform, and prepares medicine which is convenient to use.    DETAILED DESCRIPTION - Method for preparing medicine treating dry cucumbers leaves, involves (a) obtaining 30 %mass oxadixyl, giant knotweed, ginger, cinnamaldehyde and copper-methyl, (b) processing, washing and drying the giant knotweed and ginger, adding the dried giant knotweed and ginger in sealed container, adding 75% ethanol solution, immersing the giant knotweed and ginger in ethanol solution for 12 hours, performing percolation, then performing extraction of the giant knotweed and ginger using water or alcohol e.g. ethanol, and heating and recycling ethanol to obtain extract, and (c) adding 30 %mass oxadixyl, cinnamaldehyde, copper-methyl to the extract obtained in the step (b), and mixing and uniformly stirring the mixture to obtain product.
NOVELTY - A device for preparing associated natural or crude natural gases via catalytic conversion, for power units, comprises: a starting system for supplying and dosing of reagent, converter, heat exchangers, control system, transducer, at least one catalyst bed, where the device convert compounds present in associated natural or crude natural gases into methane at not greater than 450 degrees C, and has low antiknock rating and friction-increasing possibility of resin and soot formation.    USE - In preparing associated natural or crude natural gases e.g. methane, for power units (claimed).
NOVELTY - The invention relates to a process and installation for simultaneously producing carbonized biomass and synthesis gas. The claimed process consists in comminuting the biomass up to a suitable grain size G20...G120, a moisture of 6...25%, which is treated at a temperature of 800...900 degrees C for 2...5 h, to result in a carbonized biomass with a porosity of 600...1200 m2/g, having an ash content of 76...86%, simultaneously with the production of a synthesis gas having a heating value of 16...18 MJ/Nm3, having 13...15.5% methane, 26...30% carbon dioxide, 29...32 % carbon monoxide, 6...9% hydrogen. The claimed installation comprises a furnace (5), a fixed flask (4) and a mobile flask (1) provided with a gas outlet (3), some stacks (6 and 7) for the outlet of flue gases through a gas pipe (8), accelerated by a vacuum pump (9), a steam injector (10) for removing the volatile substances from the biomass.
NOVELTY - Feedstock is pyrolyzed in inert atmosphere in reactor, to obtain bio-oil, bio-char and non-condensable gases. 10-99 %mass Non-condensable gases are recycled to reactor, to obtain deoxygenated bio-oil. The bio-oil is prepared in the absence of oxygen without adding catalyst externally.    USE - Preparation of bio-oil used for stationary boiler fuel and hydrocarbon transportation fuel.    ADVANTAGE - The method enables preparation of highly-aromatic bio-oil having high product quality, acidity and energy content from feedstock without using externally added catalyst.
NOVELTY - Moving bed-fermentation of a liquid carried out by microorganisms in a fermenter/reactor, where the moving bed comprises a device containing within or on its surface a porous material capable of providing anchorage to bacteria capable of performing fermentation/degradation of organic matter and the device is moveable throughout the column of the liquid in the fermenter/reactor when the device is added to the fermenting liquid and the fermenting liquid is agitated/aerated.    USE - The method is useful for moving bed-fermentation of a liquid (claimed).    ADVANTAGE - The method can be efficiently used in waste water processing, sewage treatment plants and more particularly for processing waste water for domestic and industrial use.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device containing within or on its surface a porous material capable of providing anchorage to bacteria capable of performing fermentation/degradation of organic matter and the device is moveable throughout the column of the liquid in a fermenter/reactor/aeration tank when the device is added to the fermenting liquid and the fermenting liquid is agitated/aerated.
NOVELTY - Aerosol-type sunscreen cosmetics comprise an undiluted solution which is water-in-oil emulsion containing 1-3 %mass bis-ethylhexyloxyphenol methoxyphenyl triazine (a), 5-50 %mass diester of propylene glycol and 8-10C fatty acid (b), and 5-15 %mass ethylhexyl methoxycinnamate (c), and liquefied gas as propellant. The mass ratio of component (a) with respect to components (b) and (c) is 1:10-1:20.    USE - Aerosol-type sunscreen cosmetics are used for skin or hair.    ADVANTAGE - The aerosol-type sunscreen cosmetics have high UV-protective effect and excellent usability, are free of tackiness, and are capable of being uniformly sprayed on skin or hair, by stably blending slightly-soluble ultraviolet absorber having high UV-protective ability under coexistence of liquefied gas.
NOVELTY - Preparation of fuel from biomass involves heat-treating biomass at 150-300 degrees C in a reactor (11) pressurized with steam and air, releasing pressure at the end of the heat treatment and increasing volume of the steam and other gases on pressure release temporarily and accumulating in a container (14) having flexible volume, heat-exchanging the steam and other gases in at least one heat-exchanger (13) such that condensable gases condense and releasing their heat of condensation in at least one heat-exchangers.    USE - Preparation of fuel used in generation of electricity.    ADVANTAGE - The method efficiently and economically provides fuel without generating unpleasant odor and carbon dioxide to environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus for preparation of fuel from biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic structure of apparatus for preparation of fuel from biomass.    Reactor (11)    Heat-exchanger (13)    Container (14)    Condensate (25)    Gas (26)
NOVELTY - The manufacture method involves bending a sheet of fiber carbon paper (9) so that a first surface is convex to disentangle fibers that are prone to disentanglement and cause portions of the prone fibers to protrude from the first surface. The portion of the prone fibers is shaved off to the first surface of the sheet of fiber carbon paper.    USE - Manufacture method of fuel cell GDL.    ADVANTAGE - Reduces mass transport and water permeability by using a fine pore layer between GDL and catalyst layers on photon exchange membrane.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a GDL manufacture apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows the stylized, side elevation view of manufacture method of GDL substrate.    Sheet of fiber carbon paper (9)    Spindle (11)    Roller (14)    Razor-sharp edge (17)    Stationary point (18)
NOVELTY - Oxidation of an alkane to an alkane oxygenate comprises (a) contacting the alkane and a soft oxidizing electrophile including a main group element in oxidized form, or contacting the alkane and a reduced form of the soft oxidizing electrophile and an oxidant, in an acidic medium comprising an oxygen acid, in the absence of a super-acid, at a temperature of less than 300 degrees C, to provide the alkane oxygenate and an electrophile reduction product, and (b) separating the alkane oxygenate and the electrophile reduction product.    USE - The process is useful for: the oxidation of an alkane to an alkane oxygenate, where the alkane includes methane, ethane and/or propane (all claimed); and producing liquid fuels such as methanol from a natural gas containing feedstock.    ADVANTAGE - The process efficiently, simply and economically produces the liquid fuels with high yield, improved stability and less energy consumption and without using superacids in a large scale and a cost-effective manner.
NOVELTY - Container for solid-, liquid- or gaseous media, preferably a biogas tank, comprises a bottom (1), side walls (2) and a ceiling (3), of which at least the side walls are provided on inner side with a lining comprising a medium-tight protective layer which on its side facing the side wall and/or the bottom is connected with sealing webs made of a material having low thermal expansion coefficient.    USE - The container is useful for solid-, liquid- or gaseous media (claimed).    ADVANTAGE - The container exhibits operability for long period of use, avoids the impairment of the sealing of the side walls or the bottom even at higher temperature changes, and avoids the impairment of density of the protective layer.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of the container.    Bottom (1)    Side walls (2)    Ceiling (3)    Thermal insulation (4)    Support (6)
NOVELTY - Covalently crosslinked, asymmetric porous membrane made from thermoplastic silicone elastomers, is claimed.    USE - The covalently crosslinked, asymmetric porous membrane is useful: for separation of material mixtures; for coating (claimed) a glass substrate such as quartz, lead, float or soda-lime glass substrates; and in reverse osmosis equipment for purification of drinking water and sea or brackish water, where the material mixtures include solid-solid, liquid-liquid, gas-gas, solid-liquid, solid-gas and liquid-gas mixtures, preferably oxygen/nitrogen, air, hydrogen/nitrogen, water-vapor/air, hydrogen/carbon monoxide, hydrogen/carbon dioxide, carbon monoxide/carbon dioxide, nitrogen/carbon dioxide, oxygen/carbon dioxide, hydrogen/methane, methane/carbon dioxide, methane/hydrogen sulfide, methane/water, gaseous organic compounds/air and gaseous organic compounds/nitrogen.    ADVANTAGE - The covalently crosslinked, asymmetric porous membrane has improved mechanical strength and flexibility, prolonged lifetime, improved selectivity, better mechanical properties, higher flow rate, and low manufacturing cost using the thermoplastic silicone elastomers.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the covalently crosslinked, asymmetric porous membrane comprising preparing a solution of silicone composition, which contains an alkenyl-containing thermoplastic silicone elastomer and crosslinker, and a solvent, placing the solution in a mold, contacting the molded solution with a precipitating medium to form covalently non-crosslinked membrane, removing the solvent and the precipitation from the non-crosslinked membrane, and then crosslinking the membrane.
NOVELTY - An improved process for biodiesel production in oscillatory baffled reactor (OBR) using non edible seeds Jatropha, Karanja, Neem, Simarouba, Callophyllum innophyllum, etc., or the seed cake Mustard, Rice bran, Jatropha & karanja with free fatty acid (FFA, 215%) seed size
NOVELTY - The present invention discloses one step catalytic process to convert renewable feedstock directly into hydrocarbon fuel and aromatics. Particularly, the present invention relates to hydroconversion of renewable feed stocks. More particularly, the present invention relates to hydroprocessing of triglycerides, diglycerides and free fatty acids of renewable sources waste animal fats and used cooking oils directly into petrochemical (aromatics rich) feedstock pool along with hydrocarbon based fuels ranging from C1-C30 carbon atoms using a catalyst.
NOVELTY - Method (M1) for producing alkyl esters, involves processing high free fatty acid feedstock including mixture of triglycerides and free fatty acids to remove water and solids to obtain processed feedstock, introducing and mixing the processed feedstock into reaction vessel, where the reaction vessel including water, at least one enzyme, and alcohol, separating the reacted contents into glycerin phase and an alkyl ester phase, washing the alkyl ester phase using aqueous base, and treating the alkyl ester phase with primary alcohol, and flocculant.    USE - The method is useful for producing alkyl esters (claimed) or biodiesel, which is used in diesel engines.    ADVANTAGE - The method is simple, and increases usage of low-cost raw materials.    DETAILED DESCRIPTION - Method (M1) for producing alkyl esters, involves processing high free fatty acid feedstock including mixture of triglycerides and free fatty acids to remove water and solids to obtain processed feedstock, introducing and mixing the processed feedstock into reaction vessel, where the reaction vessel including water, at least one enzyme, and alcohol, separating the reacted contents into glycerin phase and an alkyl ester phase, recycling portion of at least one enzyme from the glycerin phase, removing water and at least one alcohol from the alkyl ester phase, converting free fatty acids in the alkyl ester phase into alkyl esters, washing the alkyl ester phase using aqueous base, and treating the alkyl ester phase with primary alcohol, preferably 2 wt.% methanol and flocculant, preferably polyacrylamide cationic polymer.
NOVELTY - The manufacturing method involves supporting the polymer of an opposite electric charge, and covering the core material powder in which the polymer is supported, with the covering material particles (YSZ). The covered core material powder is baked with the covering material particles, and the fuel electrode material complex conjugation is applied. The core material powder comprises an electronic conductor, particularly nickel. The covering material particle comprises oxide ion conductor, which is zirconium oxide or cerium oxide.    USE - Manufacturing method for a fuel electrode of a solid oxide fuel cell (Claimed).    ADVANTAGE - Uniform and reliable covering of the surface of core material powder with the covering material particles is enabled with an electrostatic attraction force. Application of aggregation core material powder is prevented. Durability of fuel cell is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a fuel electrode material covered with the covering material particles.    Covering material particles (YSZ)
NOVELTY - A polyoxometalate electrode (416) contains an electrolyte membrane comprising an ionomeric polymer.    USE - Polyoxometalate electrode is used for fuel cell for producing electricity.    ADVANTAGE - The polyoxometalate electrode enables economical manufacture of fuel cell having excellent reliability, and durability, and eliminates humidification of reactive gases, and enables production of environmentally-friendly and reliable source of energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of polyoxometalate electrode.    Conductive baking (408)    Polyoxometalate electrode (416)    Intermediate (420)    Intermediate material layer (606)    Immobilized polyoxometalate layer (618)
NOVELTY - Thermal conversion of biomass (104) involves: a) thermal conversion of a biomass feedstock in a pyrolysis reactor (108); b) recovering a pyrolysis vapor (110) from the reactor; c) passing the pyrolysis vapor in contact with a cracking catalyst, a water-gas shift reaction catalyst, a hydrotreating catalyst, and an acid catalyst (102f) to produce an upgraded pyrolysis vapor; and d) converting the upgraded pyrolysis vapor into liquid product (140).    USE - For thermal conversion of biomass feedstock into biooil useful for preparing gasoline (claimed).    ADVANTAGE - The in-situ upgrading of hot pyrolysis vapor is more attractive and economical, as biooil with improved properties, such as less oxygen (30-40 wt.%) and less acidity (pH=2-5), is produced directly. This makes further upgrading into liquid transportation fuels more cost effective due to less hydrogen being required. Energy is also saved for pyrolysis vapor cooling and pyrolysis oil reheating. The liquid product has 15-25 wt.% of water content. The resulting biooil liquid product is more refined, and the overall process offers economic and energy efficiency. In in-situ upgrading, the biomass pyrolysis vapor using the series of catalysts of the present process, a liquid biooil product is obtained that is so refined that the liquid product can be directly combined with crude oil to make gasoline. No additional refining is necessary. Also, by in-situ upgrading the biomass pyrolysis vapor to have less acidity, one can attain a liquid biooil product which is easier to handle and less corrosive in post-pyrolysis treatment.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic of a process for in-situ upgrading of pyrolysis vapor using a multi-layered catalyst bed, with multiple layers of the different catalysts.    Solid acid catalyst (102f)    Biomass stream (104)    Pyrolysis reactor (108)    Pyrolysis vapor (110)    Liquid product (140)
NOVELTY - Thermal conversion of biomass involves performing thermal conversion of biomass feedstock in pyrolysis reactor, recovering a pyrolysis vapor (120) from the reactor, passing the pyrolysis vapor in contact with water-gas shift reaction catalyst (402d) and hydrotreating catalyst (402e) to produce upgraded pyrolysis vapor (430) and converting the upgraded pyrolysis vapor into a liquid product.    USE - Thermal conversion of biomass (claimed).    ADVANTAGE - The biomass is economically and efficiently converted into biooil liquid product having less corrosive property, acidity and oxygen content, and favorable handleability, with reduced energy consumption.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view explaining the thermal conversion of biomass.    Pyrolysis vapor (120)    Catalyst bed reactor (402)    Water-gas shift reaction catalyst (402d)    Hydrotreating catalyst (402e)    Upgraded pyrolysis vapor (430)
NOVELTY - Process for thermal conversion of biomass, comprises: (a) thermal conversion of a biomass feedstock (104) in a pyrolysis reactor (108); (b) recovering a pyrolysis vapor (120) from the reactor; (c) passing the pyrolysis vapor in contact with a cracking catalyst, a water-gas shift reaction catalyst, and a hydrotreating catalyst to produce an upgraded pyrolysis vapor; and (d) converting the upgraded pyrolysis vapor (630) from step (c) into a liquid product (140).    USE - The process is useful for thermal conversion of biomass into fuels such as gasoline product (claimed).    ADVANTAGE - The process: results in bio-oil liquid product which is more refined and which exhibits improved properties such as lower oxygen content and/or less acidity; and is more economical and energy efficient for converting biomass to fuels.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic process for in-situ upgrading of pyrolysis vapor using a cracking catalyst, a water-gas shift reaction catalyst, and a hydrotreating catalyst, with multiple layers of the different catalysts.    Biomass stream (104)    Pyrolysis reactor (108)    Pyrolysis vapor stream (120)    Liquid bio-oil product (140)    Upgraded pyrolysis vapor stream (630)
NOVELTY - The structure has a main portion that is provided with water-and gas-impermeable water transfer layer and a partially water-and gas-permeable thermoplastic protective layer. The water transfer layer and the thermoplastic protective layer are overlapped in overlap regions. The water transfer layer in overlap region and the protective layer are accessible for moist gases. The main portion is thermodynamically pressed in the overlap region, so that the water transfer layer in the specific overlap region is inaccessible for wet gases by the protective layer.    USE - Water transfer composite structure used in humidifier module of humidifier (all claimed) used for humidification of process gases for fuel cell.    ADVANTAGE - The number of components to be transported is simplified because the gas tightness of the water transfer layer permits regardless of the porosity of the thermoplastic protective layer gripping the water transfer composite by vacuum gripper. The large industrial manufacturecan be achieved efficiently.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) humidifier module;    (2) humidifier; and    (3) device for manufacture of water transfer composite structure, humidifier module and humidifier.    DESCRIPTION OF DRAWING(S) - The drawings show the schematic views of the water transfer composite structure.    Humidifier (1)    Humidifier module (8)    End plate (9)    Compressor (K)    Fuel cell stack (S)
NOVELTY - The fuel cell has a modifier which has an evaporation unit (20a) provided in entrance side for evaporating water, and a modification unit provided downstream than the evaporation unit. A heat exchange suppression wall portion (20j) has a wall portion main body (20l) which divides the inner side of the modifier into areas at the side of evaporation portion and modification portion side, respectively. A protrusion portion (20m) protrudes to the evaporation portion side so that a heating surface area is made small and less thermal capacity than the wall portion main body.    USE - Solid oxide fuel cell for generating electric power.    ADVANTAGE - Bumping is suppressed, and stable electric power generation is performed by moderating the rapid heating to the water in the modifier.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic perspective view of an evaporation/mixing portion partition.    Evaporation unit (20a)    Mixing portion (20b)    Heat exchange suppression wall portion (20j)    Wall portion main body (20l)    Protrusion portion (20m)
NOVELTY - Production of diesel fuel from vegetable raw material involves processing raw material at elevated temperature and hydrogen pressure in presence of crystalline zeolite-based catalyst including 10 wt.% or less modified group VIII metal of periodic table, and subjecting to pre-oxidation treatment.    USE - Production of diesel fuel from vegetable raw material (claimed).
NOVELTY - The device (200) has a power supply unit (202) that converts received alternating current (AC) power source into direct current (DC) power source and supplies the DC power source to central control unit (204). A data collecting unit (214) collects the status information of fuel cell system and provides information to control unit according to request of control unit. A switch portion (206) supplies DC power source to moving element. The control unit monitors whether the malfunction is generated in fuel cell system based on status information and controls driving of fuel cell system.    USE - Control device of fuel cell system.    ADVANTAGE - The supply of power source to the fuel cell system is blocked, if the fuel cell system is in operation alert condition. The stand-by power of the fuel cell system is reduced. The power consumption of the fuel cell system is reduced. The energy use efficiency of the fuel cell system is enhanced. The service lifetime of the fuel cell system is extended, while reducing the replacement period of fuel cell system. The overall situation of the fuel cell system is monitored and the status information of fuel cell system is displayed in the display. The supply of power to the fuel cell system is prevented if the failure occurs in the fuel cell system, so that the occurrence of safety accidents is prevented effectively.    DETAILED DESCRIPTION - The main switch portion is switched ON or OFF under the control of control unit. An INDEPENDENT CLAIM is included for the control method of fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the fuel cell system control device.(Drawing includes non-English language text)    Control device of fuel cell system (200)    Power supply unit (202)    Central control unit (204)    Switch portion (206)    Data collecting unit (214)
NOVELTY - The present invention provides an electrode catalyst for fuel cell, which comprises the conductive carrier and the nanocatalyst metal carried by the conductive carrier. In which, the conductive carrier is the iron containing hydroxylapatite (HAp), and the nanocatalyst metal is selected from platinum or platinum-ruthenium alloy. The manufacturing method of the aforementioned electrode catalyst is mainly to stir the hydroxyapatite (HAp) with the iron containing solution for exchange of partial calcium ions with iron ions; adding the platinum precursor for exchange of partial iron ions with platinum irons; adding the reducing agent to reduce all the platinum particles; after reducing, collecting and washing the powder to obtain the Pt/FeHAp catalyst powder; and, adding the carbon black powder and mixing with the nafion to form the Pt/FeHAp/C electrode catalyst.
NOVELTY - Eco-friendly bamboo pellet fuel comprises biomass feedstock, which is a mixture of bamboo materials and lignin from black liquor. The bamboo material is a mixture of bamboo and bamboo processing residues or both.    USE - Eco-friendly bamboo pellet fuel.    ADVANTAGE - The bamboo pellet fuel is reliable, cost-effective and eco-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing eco-friendly bamboo pellet fuel, which involves:    (A) selecting bamboo materials by using a screening machine to obtain biomass feed stocks of size 5 mm;    (B) performing carbonization of selected bamboo materials at 200-300 degrees C in the presence of oxygen;    (C) crushing the carbonized bamboo material, and then processing the bamboo material in the presence of low moisture content; and    (D) mixing processed bamboo material with lignin from black liquor uniformly, and then feeding the obtained biomass feed stock material into a pellet machine through repression.
NOVELTY - A transesterification catalyst consists of titanium-containing mesoporous silica containing titanium and silicon as skeleton constituent elements, and having pore diameter of 5 nm or more.    USE - Transesterification catalyst is used in manufacture of biodiesel fuel (claimed) used as automotive fuel.    ADVANTAGE - The biodiesel fuel is efficiently produced with high selectivity by simple, environmentally-friendly and economical process, using transesterification catalyst even in the presence of moisture content and free fatty acid as reaction inhibitor. The simultaneous esterification and transesterification is carried out by the recyclable catalyst without discharge of wastewater.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) use of transesterification catalyst in manufacture of biodiesel fuel by transesterification of oil, fat and alcohol; and    (2) manufacture of biodiesel fuel, which involves transesterifying oil, fat and alcohol in presence of the transesterification catalyst for obtaining fatty-acid alkyl ester.    DESCRIPTION OF DRAWING(S) - The drawing shows a view explaining the manufacturing process of the biodiesel fuel. (Drawing includes non-English language text)
NOVELTY - Device comprises multiple heating chambers for thermally decomposing biomass of biochar stored into an internal space, a heat transfer pipe (71) for communicating the multiple heating chamber with each other, a circulation pump (80) for circulating air inside the heating chamber, connected with each of the heat transfer pipe, and a control unit for controlling operation of the heating chamber and the circulation pump.    USE - The device is useful for producing biochar by recycling waste (claimed).    ADVANTAGE - The device minimizes energy consumption.    DETAILED DESCRIPTION - Device comprises multiple heating chambers for thermally decomposing biomass of biochar stored into an internal space, a heat transfer pipe (71) for communicating the multiple heating chamber with each other, a circulation pump (80) for circulating air inside the heating chamber, connected with each of the heat transfer pipe, and a control unit for controlling operation of the heating chamber and the circulation pump. The control unit is used for operating a second heating chamber (2) upon operation completion of a first heating chamber (1) of the heating chamber, and operating the circulation pump until temperature difference between the first and second heating chamber became less than the set value, before operating second heating chamber, where the second heating chamber is connected with the first heating chamber, and the circulation pump is connected with the first and second heating chambers.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of the device for producing biochar by recycling waste.    First heating chamber (1)    Second heating chamber (2)    Third heating chamber (3)    Heat transfer pipe (71)    Circulation pump unit (80)
NOVELTY - The separation processor (50) has a cutting tool (40) that cuts the palm berries cluster according to a wick and kinds formed on outside of the palm berries. A lowering transport unit (30) is installed at a progressive direction end of an alignment unit (20), for transporting the palm berries cluster in lower side. The alignment unit is provided to arrange the palm berries in upper side of a conveyor (10). The conveyor is configured to move the palm berries cluster to a handling apparatus for extracting the palm berries.    USE - Palm berries cluster separation processor for bio-fuel production.    ADVANTAGE - The palm berries are extracted and separated effectively so that the bio-fuel production efficiency is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of the palm berries cluster separation processor.    Conveyor (10)    Alignment unit (20)    Lowering transport unit (30)    Cutting tool (40)    Palm berries cluster separation processor (50)
NOVELTY - Processing palm fruit by-product, comprises (a) separating wick (2) and branch (3) from the stored palm fruit by-product using separation processor (50), (b) injecting the branch into compression device (60), and dehydrating to separate branch material, water and oil component (3b), (c) storing the branch material in a storage tank, and heating the water and oil component by transferring into a heating tank, (d) centrifuging the water and oil component by using a centrifugal separator, and removing oil, sludge and water, and re-centrifuging wick, dehydrate water and oil and centrifuged oil.    USE - The method is useful for processing palm fruit by-product to produce green biofuel (claimed).    ADVANTAGE - The method re-uses the separated palm fruit by-product.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the method for processing palm fruit by-product to produce green biofuel (Drawing includes non-English language text).    Wick (2)    Branch (3)    Water and oil component (3b)    Separation processor (50)    Compression device (60)
NOVELTY - Method of cultivating Ascomycota mushroom using nanogold colloidal solution, involves selecting good quality mushroom, preparing growth medium for mushroom, mass culturing solid or liquid bacterial seed culture, inoculating mushroom and bacterial seed culture into the growth medium, cultivating mushroom, then preparing nanogold colloidal solution by mixing gold nanoparticles in water or distilled water and adding the mixture into sterilized growth medium for mushroom cultivation.    USE - The method is useful for cultivating Ascomycota mushroom used for treating cancer and inflammation.    ADVANTAGE - The Ascomycota mushroom can be obtained in large quantities with high quality, is highly nutritious and has excellent flavor. The method is environmentally-friendly.
NOVELTY - Biological diesel zirconium oxide catalyst comprises 80-95 wt.% zirconium oxide, 2-18 wt.% alumina, 1-17 wt.% titanium dioxide, 5-25 wt.% sodium bicarbonate and 10-50 wt.% sodium chloride.    USE - Biological diesel zirconium oxide catalyst.    ADVANTAGE - The catalyst has high stability, high conversion rate, repeated utilization, good acid resistance, low bed layer resistance, stable structure, no argillization, and high catalytic activity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of biological diesel zirconium oxide catalyst comprising ball milling zirconium oxide, alumina and titanium dioxide in ball mill for 24 hours; adding sodium chloride, sodium bicarbonate and silica sol as adhesive, mixing uniformly, pelletizing, drying at 120 degrees C for 12 hours; and calcining in muffle furnace at 500 degrees C for 1 hour, heating to 1460-1600 degrees C, and roasting for 40-200 minutes.
NOVELTY - Method for treating calcium-rich wastewater, involves (a) reacting ammonium bicarbonate and calcium chloride to obtain calcium bicarbonate and ammonium chloride, (b) thermal decomposing calcium bicarbonate and ammonium chloride to produce calcium carbonate precipitate, water and carbon dioxide, and (c) again thermal decomposing calcium bicarbonate and calcium hydroxide in the waste water in presence of carbon dioxide to obtain calcium carbonate precipitate and water.    USE - The method is useful for treating calcium-rich wastewater (claimed) for producing fertilizer.    ADVANTAGE - The method prevents pollution and enables to produce high value product using waste material.
NOVELTY - Method for improving hydrolysis and aerobic digestion effect of sludge involves adding calcium peroxide into sludge, reacting for 1-24 hours, hydrolyzing the sludge, adding hydrolyzed sludge into aerobic digestion tank, performing aerobic digestion process in presence of facultative bacteria, converting organic compound in sludge into methane, carbon dioxide and water, and improving production of sludge biogas. The mass ratio of calcium peroxide and sludge is 0.01:1-0.6:1.    USE - Method for improving hydrolysis and aerobic digestion effect of sludge (claimed).    ADVANTAGE - The hydrolysis and aerobic digestion effect of sludge is economically improved with high yield, in a short period of time.
NOVELTY - Controlling sludge formation involves using bioreactor and dynamic membrane for anaerobic digestion of sludge to obtain fermentation zone and separation zone, where separation zone moves with dynamic membrane (7) that is connected with pressure gauge (8), pump and pipe (9). Upper side of fermentation zone is connected with mud tube (1), sludge discharge pipe (2), stirring unit (5) and top gas body metering device (6). Methane gas produced during process is carried by diaphragm pump (10), gas flow meter (11) and gas diffusion tube (12).    USE - Method for controlling sludge formation (claimed).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of device for controlling sludge formation.    Mud tube (1)    Sludge discharge pipe (2)    Stirring unit (5)    Gas body metering device (6)    Dynamic membrane (7)    Pressure gauge (8)    Pipe (9)    Diaphragm pump (10)    Gas flow meter (11)    Gas diffusion tube (12)
NOVELTY - Reducing water content in livestock manure during the production of organic fertilizer comprises (1) establishing a processing platform, (2) adding 0.05-0.15 times of fermentation material and 0.1-0.3 times of livestock manure into the platform, then uniformly mixing, (3) fermenting the mixture with bacterial strain at 50 degrees C, (4) then evaporating water content from the fermented mixture, (5) then depositing nutrient content and repeating the steps (2)-(5).    USE - The method is useful for reducing water content in livestock manure during the production of organic fertilizer (claimed).    ADVANTAGE - The method is capable of reducing water content in livestock manure, thus reducing the production cost and increasing the production efficiency of organic fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a system for reducing water content in livestock manure comprising a fermentation tank for fermenting the manure including livestock and poultry manures, a water regulating tank and a spraying device, where the fermentation tank comprises a conveying device to convey the manure into the fermentation tank, and a bottom part of the fermentation tank is provided with a filter tank with a filter plate.
NOVELTY - Producing waste tea branch fermented fertilizer comprises (i) crushing waste tea branch, and sieving with 20 mesh sieve; (ii) storing in the crushed tea branch in an anaerobic environment of 40-55 degrees C, fermenting for five days, placing aerobic bacteria, adequately ventilating under aerobic condition, carrying out aerobic treatment, until the humus content reach more than 80% in the tea residue; (iii) drying the humus in resulting fermented tea branch residue at 30-45 degrees C; (iv) stirring the raw material, and granulating in a granulator.    USE - The method is useful for producing waste tea branch fermented fertilizer (claimed).    ADVANTAGE - The fertilizer: can be directly used for fruit, vegetables and other green plants, and thus the green plants can directly absorb amino acids and other substances; contains polyphenols and other substances, which can increase nitrogen and phosphorus absorption in plants.
NOVELTY - Organic fertilizer comprises 9-25 wt.% of organic material, 4-7 wt.% of natural zeolite powder, 7-10 wt.% of grass and 68-80 wt.% of chicken manure.    USE - Organic fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the organic fertilizer comprising taking chicken manure and then adding organic material, uniformly spreading 30-39 wt.% of turfy soil and 32-39 wt.% of natural zeolite powder, and paving on a layer of chicken manure, stacking and sealing in a plastic cloth, fermenting at 58-62 degrees C for 6-8 days and then air drying.
NOVELTY - Preparing microbial fertilizer comprises sieving vermicompost to obtain clay-like solid powder, according to resulting powder to water mass ratio of 1:5-20, adding water added into the resulting powder, sufficiently stirring, oxygenating for 20-30 hours to obtain vermicompost mixture, then adding sucrose into the resultant vermicompost mixture, where the vermicompost mixture to sucrose mass ratio is 150-300:1, and stirring at room temperature.    USE - The method is useful for preparing microbial fertilizer (claimed).    ADVANTAGE - The treatment of heavy metal contaminated soil can significantly improve the soil urease activity, promote secretion of organic acids in green plant roots, reduce harmful heavy metal elements, and thus protects the environment.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for: (1) microbial fertilizer, prepared as mentioned above; and (2) treating heavy metal contaminated soil, comprising adding Eisenia fetida into heavy metal contaminated soil, where the inoculum amount is 5-8 worm/kg dry soil, diluting microbial fertilizer 500-1000 times so as prepare aqueous solution, and then spraying 400-600 kg/acre aqueous solution on heavy metal contaminated soil.
NOVELTY - Organic-inorganic complex fertilizer comprises 10-25% water soluble nitrogen fertilizer, water soluble phosphate fertilizer and/or water soluble potassium fertilizer, 10-20% organic substances, 20-30% anaerobic biological bacterium, 3-5% ferrous sulfate and molasses fermentation broth for making up to 100%. The molasses fermentation broth comprises 35-95% organic substances.    USE - Used as organic-inorganic complex fertilizer.    ADVANTAGE - The fertilizer: is economical and environmentally friendly; recycles the waste; removed the smell of molasses fermentation broth; dissolves organic substances, maintains nitrogen, phosphorus, potassium, humic acid, amino acids and trace elements required by plant; and is suitable for industrial production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the fertilizer, comprising (a) introducing organic material, biological bacterium, molasses fermentation broth, and ferrous sulfate into a fermentation tank, and covering the upper surface of the fermentation pool with a plastic thin film, (b) adjusting the temperature of the fermentation broth for anaerobic fermentation at 50-65 degrees C for 30-48 hours, precipitating the insoluble substances, removing colloid in the fermentation liquid, and inactivating at a high temperature, and (c) adding water soluble nitrogen fertilizer, water soluble phosphate fertilizer and water soluble potassium fertilizer, stirring uniformly and drying.
NOVELTY - Composite fertilizer comprises 10-25 wt.% of nitrogen fertilizer solution, water soluble phosphate fertilizer and/or water soluble potassium fertilizer, 10-20 wt.% of organic material, 20-30 wt.% of anaerobic bacteria, 3-5 wt.% of ferrous sulfate, and 35-95 wt.% of molasses fermentation liquid.    USE - Composite fertilizer.    ADVANTAGE - The composite fertilizer is inexpensive and rich in humic acid and amino acid without any odor of molasses fermentation liquid, and utilizes waste as raw material.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the composite fertilizer comprising (1) weighing nitrogen fertilizer solution, water soluble phosphate fertilizer and/or water soluble potassium fertilizer, organic material, anaerobic bacteria, and ferrous sulfate, (2) adding organic material, anaerobic bacteria, molasses fermentation liquid and ferrous sulfate in a fermentation tank, then covering surface of the fermentation tank using a plastic thin film, (3) carrying out anaerobic fermentation process in the fermentation tank at 50-65 degrees C for 30-48 hours, removing insoluble substance and colloidal fermentation liquid from the fermentation tank respectively by precipitating and high temperature inactivation process, (4) adding nitrogen fertilizer solution, water soluble phosphate fertilizer and/or water soluble potassium fertilizer in the obtained fermentation liquid and then uniformly stirring the liquid, and drying the liquid.
NOVELTY - Organic-inorganic complex fertilizer comprises: 10-25 wt.% water-soluble nitrogen fertilizer, water soluble phosphate fertilizer and/or water soluble potassium fertilizer; 15-40 wt.% organic material; 5-10 wt.% biological microorganism; 1-3 wt.% ferrous sulfate; and molasses fermentation broth which is made up to 100 wt.% (containing 35-95% organic matter).    USE - Used as an organic-inorganic complex fertilizer.    ADVANTAGE - The fertilizer is economical and suitable for industrial production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for manufacturing organic-inorganic complex fertilizer, comprising: (i) adding organic material, biological microorganism, 35-95% molasses fermentation broth and ferrous sulfate into a fermentation tank, stirring uniformly and passing air from the bottom of fermentation tank; (ii) carrying out fermentation for 16-28 hours at room temperature, removing insoluble material precipitation and colloid from the fermentation broth, carrying out high-temperature inactivation; and (iii) adding water-soluble nitrogen fertilizer, water soluble phosphate fertilizer and/or water soluble potassium fertilizer into the molasses fermentation broth, stirring uniformly, granulating and drying.
NOVELTY - Watermelon selenium enriched and effective microorganism (EM) microbial inoculum fermented fertilizer comprises 30-34 pts. wt. urea, 2-3 pts. wt. magnesium sulfate, 3-4 pts. wt. manganese sulfate, 2-3 pts. wt. ammonium molybdate, 1-2 pts. wt. sodium selenite, 10-12 pts. wt. activated carbon, 40-45 pts. wt. pomace, 50-55 pts. wt. soy sauce residue, 30-34 pts. wt. medicinal slag, 12-14 pts. wt. lignite, 10-12 pts. wt. sawdust, 5-8 pts. wt. zeolite, 3-4 pts. wt. EM microbial inoculum, and 4-6 pts. wt. bag film agent including e.g. 30-35 pts. wt. hydroxyethyl methacrylate.    USE - Used as watermelon selenium enriched and effective microorganism (EM) microbial inoculum fermented fertilizer (claimed).    ADVANTAGE - The fertilizer: uses low-cost organic raw materials including EM microbial inoculum, pomace, soy sauce residue and medicinal slag; shortens the compost fermentation time; comprises lignite and zeolite, which improves fertilizer efficiency and improves soil; increases the yield and quality of watermelon in comparison with conventional fertilizers; and is environmentally friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for (a) mixing activated carbon, pomace, soy sauce residue, medicinal slag and EM microbial inoculum with water, stirring uniformly, stacking and fermenting for 6-8 days, turning for once, turning for 2-3 days, until the fermentation material is completely decomposed, (b) processing lignite and zeolite into powder, mixing with the product of the step (a) and other remaining raw materials except bag film agent, and stirring uniformly, and (c) heating to 80-90 degrees C, adding bag film agent, stirring uniformly, and granulating.