NOVELTY - A Pichia kudriavzevii ZJPH0802 strain, collected in China Center for Type Culture Collection (CCTCC), the collection data is September 24, 2012, and deposited under CCTCC NO: M 2012373, is new.    USE - The strain is useful for preparing curcumin derivatives by biotransformation (claimed).    ADVANTAGE - The pharmacological or biological activity of structurally modified matters of the curcumin can be improved to different extents relative to a curcumin substrate before modification so as to be conductive to development of new pharmaceutical preparations. The method for obtaining the curcumin derivatives by adopting the biotransformation method, is simpler and environment-friendly, where a biological catalyst is a microbial thallus. The strain has the advantages of self-fermentation and production, stable quality and low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for preparing curcumin derivatives by biotransformation comprising using the Pichia kudriavzevii ZJPH0802 strain for fermentation and culturing as enzyme sources to curcumin as a substrate, in a phosphate buffer medium for the conversion reaction, and post treating the reaction solution after completion of the conversion reaction to obtain the derivatives of curcumin.
NOVELTY - Manufacture of high-purity lithium aqueous solution involves removing impurity including magnesium, boron and calcium contained in saline water by injecting sodium hydroxide into the saline water, precipitating lithium phosphate by adding phosphoric acid or phosphate into impurities-removed saline water and heating, dissolving precipitated lithium phosphate in phosphoric acid to obtain lithium phosphate aqueous solution, and performing electrolysis of lithium phosphate aqueous solution using electrolysis device, to produce hydrogen gas and lithium hydroxide aqueous solution.    USE - Manufacture of high-purity lithium aqueous solution from saline water (claimed).    ADVANTAGE - The high-purity lithium aqueous solution is economically manufactured, with reduced energy consumption.    DETAILED DESCRIPTION - Manufacture of high-purity lithium aqueous solution involves removing impurity including magnesium, boron and calcium contained in saline water by injecting sodium hydroxide into the saline water, precipitating lithium phosphate by adding phosphoric acid or phosphate into impurities-removed saline water and heating, dissolving precipitated lithium phosphate in phosphoric acid to obtain lithium phosphate aqueous solution, and performing electrolysis of lithium phosphate aqueous solution using electrolysis device, to produce hydrogen gas and lithium hydroxide aqueous solution. The produced hydrogen gas is used as hydrogen supply source of fuel cell power generation facility. Electricity generated during fuel cell power generation is supplied to power source of electrolysis device of sodium chloride aqueous solution for manufacture of the sodium hydroxide.
NOVELTY - A saturated gas is injected to carbon nanotube sheet and maintained at low temperature, to obtain carbon nanotube sheet. The carbon nanosheets are dispersed in a solvent phase.    USE - Method of dispersing carbon nanosheet used for carbon nanotube dispersion sheet (claimed).    ADVANTAGE - The method enables efficient dispersion of carbon nanosheet, without damage of carbon nanosheet.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for carbon nanotube dispersion sheet.
NOVELTY - Culture medium comprises 150 kg substrate, 30-40 kg urea formaldehyde foam particle, 60-70 kg peat, 20 kg organic material, 0.5-1 kg probiotic powder, 5-10 g adhesive agent, 0.5-1 g plant growth regulator and 3.203 kg microelement.    USE - The culture medium is useful for ecological restoration and slope protection by growing a lawn, plant, shrub, and tree (all claimed), and used on slopes, elevations and bare rock surfaces bad for plants to grow.    ADVANTAGE - The culture medium is suitable for restoration of, improving and stabilizing bare rock and ecological fragility areas as well as other environment bad for plants to grow easily. The culture medium is suitable for a restorated surface to quickly form a self-supply microecosystem, thus the whole curing condition and cost can be lowered.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of preparing the above-cited culture medium, which involves (a) crushing the urea-formaldehyde foam into particles of uniform size and 3-8 mm diameter, for further use, (b) preparing probiotic powder by culturing Bacillus cereus and B.megaterium respectively until the optical densities at 600 nm (OD600) of the cultures are greater than or equal to 1.5, centrifuging the cultures, collecting and pulverizing the pellets, and mixing the B.cereus powder and B.megaterium powder in a mass ratio of 2:1, and (c) mixing the products obtained in the steps (a) and (b) with the substrate, plant growth regulator and microelement, adding water and uniformly stirring the mixture.
NOVELTY - Invention relates to a method of producing hydrogen from water and can be used in chemical industry, for processing hydrocarbons, as well as in systems for accumulating and transporting energy and as fuel in transportation and fixed power installations. Catalytic steam conversion of methane-containing gas is carried out to obtain reaction products which contain hydrogen and carbon dioxide. A portion of hydrogen is separated from the rest of the reaction products. The rest of the reaction products are directed to production of synthesis gas and oxygen in a high-temperature electrochemical process, after which a methane-containing gas, which is returned to the beginning of the conversion process, is obtained from synthesis gas on a catalyst. The high-temperature electrochemical process is carried out while feeding the rest of the reaction products to the input of the cathode space of the high-temperature electrochemical process, while oxygen is extracted in the anode space which is separated from the cathode space by an electrolytic layer. The portion of hydrogen is separated from the rest of the reaction products by adsorption or membrane separation of gases.    USE - Chemistry.    ADVANTAGE - Invention reduces heat expenditure at the process of obtaining hydrogen from water, and also provides efficient use of heat energy of the nuclear reactor.12 cl
NOVELTY - By-product gases are collected and carbon monoxide gas is collected from the collected by-product gases, and hydrogen gas is generated using collected carbon monoxide gas. The remaining portion of hydrogen gas is generated by reaction of methane to synthesis gas containing carbon monoxide gas and collected, to obtain synthetic natural gas.    USE - Manufacture of synthetic natural gas (claimed).    ADVANTAGE - The synthetic natural gas is efficiently manufactured.
NOVELTY - Invention relates to gas-flame processing of materials with hydrogen-oxygen mix, particularly, to electrolytic cells to this end. Electrolytic cell may be filter-press or box-type device. Note here that some electrodes of the cell are unipolar while some of them are bipolar electrodes. It consists of flat or shaped parallel electrodes with holes of slots making gas and electrolyte passages. Space between electrodes is filled with electrolyte while electric current is supplied to extreme electrodes. Said electrodes are interconnected by current conducting buses to make sets, two extreme of which comprise n+1 electrodes while other include 2n+1 electrodes, where n is natural number. Note here that central electrodes of every said set with 2n+1 electrodes are located between two adjacent sets while other 2n electrodes of this set are arranged at the center of gap between electrodes of adjacent sets with contact with said buses.    USE - Process engineering.    ADVANTAGE - Multifold reduction in area (diameter) of electrodes rated at 100 A and higher. 1 dwg
NOVELTY - Fuel pellet (I) comprises: petroleum coke, having a sulfur content up to 5.5%; a biomass constituent; an alkali constituent adapted to capture sulfur dioxide emissions by reacting with sulfur of the petroleum coke upon burn of the pellet; and an iron oxide catalyst to capture sulfur dioxide emissions over 90%, where the petroleum coke, the biomass constituent, the alkali constituent, and the iron oxide catalyst are combined to form a fuel pellet with decreased sulfur dioxide emission at temperatures at or above 750 degrees C.    USE - Used as the pellet.    ADVANTAGE - The pellet is generated from high sulfur fuel waste materials has reduced sulfur dioxide emission. The pellet (in non-powdered forms) is utilized to avoid product loss, potential health impact, and/or environmental impact due to increased dust concentration in a powdered form.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) generating a fuel pellet from high sulfur fuel waste materials, comprising: processing petroleum coke into granule form; processing biomass constituent and alkali constituent to capture sulfur dioxide during combustion of fuel mixture; and combining the petroleum coke, the biomass constituent and the alkali constituent to form fuel mixture; and    (2) a fuel pellet (II) comprising: petroleum coke, having a sulfur content up to 5.5%; a wood fiber to provide volatiles; sulfur dioxide sorbent to capture sulfur dioxide emissions upon bum of the pellet; and ferric oxide catalyst, where the ferric oxide increases a capture of sulfur dioxide by 25-35% in comparison to the fuel pellet without the addition of the ferric oxide and the petroleum coke, where the wood fiber, the sulfur dioxide sorbent, and the ferric oxide are combined to form a fuel pellet with maximized British thermal unit (BTU) value and reduced sulfur dioxide emission at temperatures at or above 750 degrees C.
NOVELTY - Biochar made from a thermochemical conversion of biomass feedstock having a size of 0.5-4 mm, is claimed, where the biomass feedstock comprises woody biomass and/or herbaceous crops.    USE - The biochar is useful in a substrate for growing plants, where the plant grown is any species of plant, preferably a lettuce, basil, tomato, Chrysanthemum or Gomphrena or any type of plant material, preferably seed, cutting or transplant (all claimed). Test details are described but no results given.    ADVANTAGE - The biochar: is utilized as a greenhouse substrate replacement, and can replace peat moss or pine bark to more efficiently grow different types of plants; does not need to be composted, and does not shrink in volume due to decomposition, thus no volume shrinkage needs to be considered when biochar is utilized for any container plants with long or short production cycle; kills pathogens, weed seeds, insects, and other organisms harmful to plants, thus pasteurization is not necessary; is made from byproducts and renewable materials that are fast enough to regenerate; creates a large surface area for contact with roots and provides for excellent water and nutrient retention capacity; and is a suitable, sustainable, and economical alternative to the currently available substrates.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a substrate for growing plants comprising the biochar;    (2) a method (M1) of making a substrate for growing plants in a container, comprising: providing biomass from at least one plant; and processing the biomass to produce a first biochar suitable for use as a component of the substrate for plant growth, where the first biochar is made from the thermochemical conversion of biomass feedstock; and    (3) a method (M2) of growing a plant, comprising: providing at least one plant; and contacting the plant with the substrate comprising the biochar.
NOVELTY - The method involves providing substrate (52) in form of sheet (50). The fuel is provided that having hydrogen-containing material that releases hydrogen gas when heated. Pellets (50A-50J) of fuel are arranged on substrate to form fuel sheets. A non-cylindrical fuel sheet assembly is formed from fuel sheets by moving fuel sheet portions to position pellets adjacent to each other so that adjacent sides of adjacent pellets lie in essentially parallel planes. A non-cylindrical fuel unit is produced from fuel sheet assemblies.    USE - Method for producing fuel unit for hydrogen generator (all claimed) of fuel cell battery for portable electronic device.    ADVANTAGE - The hydrogen generator can be capable of producing large total volume of hydrogen gas per unit of mass and per unit of volume of the hydrogen generator. The hydrogen generator can be capable of controlling the release of hydrogen to provide hydrogen based on requirement without producing the excessive internal pressure. The hydrogen generator can be capable of operating at or below desired maximum temperature. The hydrogen generator can be capable of replacing spent materials with fresh materials, long term durability and reliability. The hydrogen generator can be capable of manufactured easily and economically in efficient manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a method for producing hydrogen gas; and    (2) a fuel unit.    DESCRIPTION OF DRAWING(S) - The drawings show the schematic views of the fuel sheet.    Sheet (50)    Pellets (50A-50J)    Substrate (52)
NOVELTY - An electric power generation system (1) comprises fuel cell (4) which uses gas containing carbon monoxide (CO) supplied from gas supply apparatus (14) as fuel and CO shift reaction device (17) to which temperature of fuel is reduced rather than the operating temperature of fuel cell while generating steam which is provided by steam supply part (38). The fuel cell has fuel electrode (6) into which the fuel that passes CO shift reaction device is introduced.    USE - An electric power generation system (claimed).    ADVANTAGE - Acceleration of cooling of fuel cell which uses gasifying gas as fuel can be achieved, and decline in electric power generation efficiency is suppressed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for cooling method of fuel cell (4).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a hybrid power system. (Drawing includes non-English language text).    Electric power generation system (1)    Fuel cell (4)    Fuel electrode (6)    Gas supply apparatus (14)    CO shift reaction device (17)    Steam supply part (30)
NOVELTY - The biomass gasifier (100) has an outer chamber (135), a reaction zone (125) and a disruption device (140). The reaction zone is positioned within the outer chamber. The disruption device is maneuvered within the outer chamber, so as to ensure a steady flow of a feedstock material (110,130) into the reaction zone without bridging. The disruption device is comprised of a shaft (150) and a drive device (180) to maneuver the shaft within the outer chamber.    USE - Biomass gasifier used for converting feedstock material e.g. solid fuel such as wood and agricultural waste into synthetic gas.    ADVANTAGE - The internal disruption device can be configured to prevent the bridging of biomass and other types of feedstock materials. Thus constant output of synthetic gas can be ensured without requiring manual operator intervention.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of operating gasifier to produce synthetic gas utilized as fuel in engine to produce electricity and utilized for generating chemical product such as Fisher Tropsch liquid.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the gasifier with disruption device.    Biomass gasifier (100)    Feedstock materials (110,130)    Reaction zone (125)    Outer chamber (135)    Disruption device (140)    Shaft (150)    Drive device (180)
NOVELTY - The mill has housing (3) which forms classification chamber (17). Pulverization table (5) is accommodated in lower portion of housing. Pulverization groove (10) is set in upper surface of pulverization table. Pressure roller (12) is pressed by pulverization groove. Blower outlet is set to eject primary air from circumference of pulverization table. Wood type biomass is supplied to center of pulverization table. Drive unit is made to rotate speed-up unit (31) through rotation pipe (23). Contracted flow path is formed between classification restriction unit (42,43) and chute (22).    USE - Biomass mill such as vertical mill used for grinding wood pellet.    ADVANTAGE - The discharge out of the mill of wood type biomass can be stimulated easily. The increase of the grinding capacity can be attained.    DETAILED DESCRIPTION - The classification restriction unit is provided between pressure roller units. Inversion cone curved surfaces are formed in upper surface respectively. Cylindrical curved surfaces are formed in the inner end of classification restriction units. Inversion cone curved surface carries out perimeter continuation. Fan is set with several rotary blades. Speed-up unit is arranged at equal intervals in circumferential direction, and is extended in vertical direction. Air inlet door is opened toward contracted flow path on lower surface. Primary air is attracted from air inlet door, by rotation of rotary blade. Contraction cone is provided in lower portion of chute.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the biomass mill. (Drawing includes non-English language text)    Housing (3)    Pulverization table (5)    Pulverization groove (10)    Pressure roller (12)    Classification chamber (17)    Chute (22)    Rotation pipe (23)    Speed-up unit (31)    Classification restriction unit (42,43)
NOVELTY - Mixture comprises 65-93 wt/wt.% herbaceous plants, 2-8 wt/wt.% oil, and 5-27 wt/wt.% wood.    USE - The mixture is useful as fuel in a biomass boiler, preferably a basic furnace.    ADVANTAGE - The mixture is environmentally friendly and can be prepared in cost-effective manner; and ensures improved burning characteristics.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of arrangement of a combustion chamber of multi-cyclone separator for flue gas cleaning (Drawing includes non-English language text).    Boiler outlet (1)    Flue gas cleaning (2)    Flue gas (3)
NOVELTY - The device has an auger screw heated from outside by flue gas generated by firing wood chips, so as to produce water vapor. A pyrolysis auger (2) is heated from outside, where dried wood chips are filled into a gasification pipe located underneath the pyrolysis auger through a shaft (7). Two gasification augers (4) are fed in opposite directions with respect to each other at a moderate rotation speed so as to obtain higher dwelling time for gasification of biomass. A stumbling auger (10) is subjected to heat by firing fresh material and residue carbon obtained after gasification.    USE - Device for gasification of biomass generated from short rotation coppice (SRC) cultivation for generation of heat energy and electric energy.    ADVANTAGE - The device allows feeding the residue carbon with the fresh wood for firing, so that only the ash of the wood chips, which can be used as fertilizer, remains as residue, thus avoiding pollution, and obtaining high electrical generation efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic side sectional view of a biomass gasification device.    Material container (1)    Pyrolysis auger (2)    Gasification augers (4)    Shaft (7)    Stumbling auger (10)
NOVELTY - A waste glycerol recycled fuel manufacturing apparatus (1) has heating unit (2) which heats waste glycerol and makes into a waste glycerol melt, additive addition unit (4) which adds an additive and uses as waste glycerol liquid of liquid completely heating and stirring waste glycerol melt, heat-source unit (3) which supplies the heat for a heating to the heating unit and an additive addition unit, filtration unit (5) which filters the waste glycerol liquid from the additive addition unit, and fuel oil mixing unit (6) which mixes a fuel oil with liquid from filtration unit.    USE - Waste glycerol recycled fuel manufacturing apparatus (claimed).    ADVANTAGE - The waste glycerol recycled fuel is efficiently manufactured using the waste glycerol recycled fuel manufacturing apparatus.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of waste glycerol recycled fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of waste glycerol recycled fuel manufacturing apparatus. (Drawing includes non-English language text)    Waste glycerol recycled fuel manufacturing apparatus (1)    Heating unit (2)    Heat-source unit (3)    Additive addition unit (4)    Filtration unit (5)    Fuel oil mixing unit (6)
NOVELTY - The structure (1) has electrolyte solution inflow portion (1a) which makes electrolyte solution flow in into electrolysis portion (1e) which electrolyzing solution. An electrolyte solution outflow portion (1b) is provided to flow of electrolysis gas emitted in electrolysis portion while making solution flow out of electrolysis portion. A liquid flow distribution portion (1c) is provided for pouring solution from inflow portion to whole inside of electrolysis portion. The inflow portion and outflow portion are provided in peripheral position of electrolysis portion.    USE - Electrolysis chamber structure of electrolysis cell unit for electrolysis cell stack used in hydrogen producing apparatus (all claimed).    ADVANTAGE - Since the electrolyte solution flows into electrolysis portion from the inflow portion, the fall of flow rate of the electrolyte solution is avoided, so that solution moves rapidly in the inside of the electrolysis portion. Since the electrolysis gas emitted in the electrolysis portion can be discharged efficiently, increase of the electricity supply resistance by the bubble of electrolysis gas existing on the surface of an electrode plate can be prevented. Hence the current efficiency and hydrogen-producing efficiency can be improved.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) an electrolysis cell unit;    (2) electrolysis cell stack; and    (3) an hydrogen producing apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of the electrolysis chamber structure.    Electrolysis chamber structure (1)    Electrolyte solution inflow portion (1a)    Electrolyte solution outflow portion (1b)    Liquid flow distribution portion (1c)    Electrolysis portion (1e)
NOVELTY - The invention relates to a process for preparing a fuel for Diesel engines. According to the invention, the process consists in the trans-esterification of sunflower oil with methyl alcohol in enzymatic catalysis with immobilized Candida antarctica lipase B, at temperatures of 30...40 degrees C, in a tert-butanol medium, after which the raw fuel is separated from glycerol and is subjected to distillation to result in a purified fuel.
NOVELTY - The invention relates to a complex installation for producing and storing the biogas obtained from biodegradable organic materials, mainly meant for stock raising micro-farms and individual agricultural farms. According to the invention, the installation comprises two fermentation basins, namely a main basin (1) and a secondary basin (2), placed in a location made on a natural field, insulated with a layer of mineral wool and a membrane and placed on a reinforced concrete plate, the basins having the shape of cylindrical vats inter-connected by means of a connection tube (4), the main fermentor being provided with a vertically positioned tube (3) for supplying a fermentescible material, and a discharge tube (5) provided with a sealing cover (9) connected to the secondary fermentor basin, both fermentors having some sealing covers (6 and 7) fixed on the connection belts (10) thereof, some valves (12) for closing and opening the gas circuits, an apparatus (14) for metering the discharged gas, a system (15) for stirring the fermentescible mixture, manually or electrically actuated by means of a gearmotor (M) and a heat exchager (16) for regulating the temperature inside the fermentors.
NOVELTY - Producing methane and biogas involves processing organic residue in a mixer or homogenizer in presence of methanogenic bacteria. An acceleration device is also utilized where the device contains a watertight tank and a recirculation unit for flowing carbon, nitrogen and phosphorus.    USE - Anaerobic method for producing methane and biogas.    ADVANTAGE - The anaerobic method enables to produce methane and biogas efficiently and automatically.
NOVELTY - The dryer (1) has a drying furnace (5) whose inner side is formed with a fluidized-bed (3) when supplied moisture fuel flows with fluidization vapor. A heat transfer unit i.e. heat exchanger tube (33), is provided in the drying furnace, and heats supplied moisture fuel. A compressor (161) compresses the vapor discharged from the drying furnace and supplies the compressed vapor to the heat transfer unit. The heat transfer unit circulates the vapor supplied from the compressor toward upstream from downstream of flow direction of the moisture fuel.    USE - Fluidized bed dryer for use in a gasification composite power generation equipment (claimed) i.e. integrated coal gasification combined cycle power generation apparatus, for drying moisture fuel e.g. low grade coal such as wood coal, with fluidization vapor i.e. water vapor. Can also be used for drying high grade coal, biomass, coppiced timber, waste material tree, driftwood, grass, waste material, sludge and tire.    ADVANTAGE - The dryer allows wood coal to be heat-dried with the vapor for drying with few ratios of non-condensable gas in a gaseous phase such that temperature difference of temperature of the wood coal and temperature of the vapor for drying is securable in the pre-heating area, so that the wood coal can be preheated even if the temperature of the vapor for drying falls and the vapor of low quality with ratios of non-condensable gas in the gaseous phase is effectively utilized, thus collecting vapor latent heat in an efficient manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a gasification composite power generation equipment    (2) a drying method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a fluidized bed dryer.'(Drawing includes non-English language text)'    Fluidized bed dryer (1)    Fluidized-bed (3)    Drying furnace (5)    Heat exchanger tube (33)    Compressor (161)
NOVELTY - The gasifier (1) has a fuel input unit positioned on a gasification reactor (3). A fuel delivery system (2) supplies fuel to the gasification reactor. A chamber body is provided with an ash vent. A rotation stoker supplies a gasification agent to an upper portion of a grate unit. A rotary shaft rotates the grate unit. The grate unit is provided with multiple through-holes. A pivoted gas injector (50) supplies the gasification agent to the upper portion of the rotary shaft. Four pivoted gas injectors are positioned in a gasification chamber along tangential direction.    USE - Pinned-layer biomass gasifier.    ADVANTAGE - The pivoted gas injector supplies the gasification agent to the upper portion of the rotary shaft such that the gasification agent can be selected in the gasification layer within the gasification reactor in an efficient manner. The gasifier has wide application range, and prevents synthetic gas in a tar component by utilizing a catalyst chamber in the outlet of the gasification reactor, thus increasing synthetic gas product quantity.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a pinned-layer biomass gasifier.    Pinned-layer biomass gasifier (1)    Fuel delivery system (2)    Gasification reactor (3)    Heat exchanger (5)    Pivoted gas injector (50)
NOVELTY - Method of converting ligno-cellulosic biomass materials into ethyl ester and hydrocarbon involves subjecting biomass material chemical-catalytic conversion and obtaining ethyl levulinate, light ethyl ester and other products including diethyl ether, using alcohol as reactant and solvent in dilute acidic medium in presence of oxidizing agent, and subjecting product to chemical-catalytic conversion with acid nanocatalyst.    USE - Method of converting ligno-cellulosic biomass materials into ethyl ester and hydrocarbon (claimed) for producing biofuel and biochemical.    ADVANTAGE - The method efficiently and economically converts ligno-cellulosic biomass materials into ethyl ester and hydrocarbon.
NOVELTY - Granular fertilizer is prepared by mixing liquid manure containing starch component, and compost which is obtained by compositing a compost material containing 50 %mass or more of organic materials.    USE - The granular fertilizer is used in agricultural and horticultural fields.    ADVANTAGE - The granular fertilizer has long term sustainability, does not flow along with water, exhibits immediate effect, as it has liquid manure which flows out gradually with rain water, causes no damage to environment, does not affect fertility of soil, improves yield of crops.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the granular fertilizer, which involves composting a compost material containing 50 %mass or more organic materials to obtain a compost, adding liquid manure containing a starch component to the compost, and molding the mixture into granular form.
NOVELTY - The apparatus (100) has modifier (1) that generates hydrogen-containing gas by reforming reaction. Recycle gas flow path (9) allows hydrogen-containing gas added to source gas before flowing into hydrodesulfurization device (2). Other ON-OFF valve (5) is provided in source gas flow path downstream rather than connection point of source gas flow path and recycle gas flow path. Controller (6) is controlled to open ON-OFF valve after stopping generation of hydrogen-containing gas, to supply source gas to recycle gas flow path while closing other ON-OFF valve.    USE - Hydrogen generating apparatus of fuel cell system (claimed).    ADVANTAGE - Since the controller is controlled to open ON-OFF valve after stopping generation of hydrogen-containing gas, to supply source gas to recycle gas flow path while closing other ON-OFF valve, the amount of condensed water produced in recycle gas flow path is reduced, and the water clogging of recycle gas flow path is suppressed.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a fuel cell system; and    (2) an operating method of hydrogen generating apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen generating apparatus. (Drawing includes non-English language text)    Modifier (1)    Hydrodesulfurization device (2)    ON-OFF valve (5)    Controller (6)    Recycle gas flow path (9)    Hydrogen generating apparatus (100)
NOVELTY - Molecular weight reduction of organic substance involves mixing water vapor with waste gas (g0) generated with gasified melting furnace, contacting obtained mixed gas (g) to organic substance, and modifying the organic substance, such that modified organic has reduced molecular weight. The waste gas (g0) contains carbon dioxide and hydrogen.    USE - Molecular weight reduction of organic substance e.g. waste plastic, oil-impregnated sludge, waste oil and biomass used during operation of iron mill (all claimed).    ADVANTAGE - The molecular weight of organic substance is economically reduced by simple method.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for operation method of iron mill, which involves collecting reforming material of organic substance obtained after performing molecular weight reduction method and utilizing reforming material as fuel and/or reducing agent of iron mill.
NOVELTY - Device, preferably a microreactor for thermochemical splitting of water, is claimed.    USE - The device is useful for thermochemical splitting of water.    ADVANTAGE - The device can be manufactured in a simple manner, is a closed reactor, and thus it is safe, has light-weight, and thus it can be used in mobile applications e.g. in motor vehicles, and is compact and easy to handle.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the device for thermochemical splitting of water.    Heat insulator (a)    Membrane (b)    Anode (c)    Cathode (d)    Reaction of magnesium chloride with water to obtain 2 moles hydrochloric acid and magnesium oxide (1)
NOVELTY - Utilization of biomass group waste material (W) involves mixing at least one of dust (D) obtained by dust-collecting combustion gas extracted from kiln bottom (13) of cement kiln (12) from the kiln waste gas flow path to lowermost stage, calcined cement raw material and biomass waste material and calcium oxide, and using as fuel and/or raw material for cement manufacture.    USE - Utilization of biomass group waste material for manufacturing cement.    ADVANTAGE - The biomass group waste material is effectively utilized, and cement is quickly and economically manufactured.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for cement raw-fuel forming apparatus of biomass group waste material, which has mixing apparatus for mixing dust obtained by dust-collecting combustion gas extracted from kiln bottom of cement kiln from the kiln waste gas flow path to lowermost stage, calcined cement raw material and biomass waste material and calcium oxide, supply apparatus for supplying mixture (M) discharged from mixing apparatus to cement manufacturing apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view explaining utilization of biomass group waste material.    Cement kiln (12)    Kiln bottom (13)    Dust (D)    Powder having high specific gravity (H)    Portion having low specific gravity (L)    Mixture (M)    Biomass group waste material (W)
NOVELTY - A biodiesel fuel-proof component consists of a crosslinked fluororubber. The crosslinked fluororubber is obtained by crosslinking the fluororubber composition containing fluororubber (A) and carbon black (B). The crosslinked fluororubber has elastic modulus of 400-6000 KPa at 160 degrees C measured in the dynamic viscoelasticity test and static tension value of 157 cN, at constant force loading conditions of the strain during dispersion with 1% tensile strength and 10 Hz frequency.    USE - Biodiesel fuel-proof component used as hoses or as sealing materials (all claimed). Uses included but are not limited to turbocharger hose for turbo system in diesel engine, fuel hose, exhaust gas recirculation hose, cylinder head gasket, seal for hydraulic equipment, crankshaft seal, cam-shaft seal, sealing material for valve-operating system of motor vehicle engine, piston ring, mechanical seal, oil seal, etc.    ADVANTAGE - The component has excellent biodiesel fuel-proof property, moldability, flexibility, thermal aging resistance, tractive characteristics and crack resistance at high temperature.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of the mixing method for the manufacture of fluororubber composition.    Open roll (10)    Primary roll (11)    Secondary roll (12)    Intermediate composition (13)    Composition after carrying out sheeting (14)
NOVELTY - A hydrogen-producing apparatus (101) consists of two cells (102) clamped between electroconductive plates (103, 104) which electrically form a closed circuit, units (105) for supplying liquid fuel containing organic substance and water through electroconductive plate, unit for supplying air or humidified air to cathode through the electroconductive plate, and unit for supplying liquid fuel to the cathode, of the cells. The cells comprise solid polymer electrolyte membrane interposed between the electrodes. The cathode of the second cell produces hydrogen.    USE - Hydrogen-producing apparatus is used in fuel cell system e.g. alkaline fuel cells (claimed) and hydrogen fueled engines.    ADVANTAGE - The hydrogen-producing apparatus has simple structure, is compact and can easily control the production of hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows the perspective view of the hydrogen-producing apparatus.    Hydrogen-producing apparatus (101)    Two cells (102)    Electroconductive plates (103, 104)    Liquid fuel supplying unit (105)    Fuel discharge units (106, 110)
NOVELTY - The paper making materials containing carbon short fiber (A), carbon fiber precursor short fiber (b) and/or fibril-like fiber (b'-1) are manufactured, treated with oxygen and heat processed at 300-450 degrees C for 10-300 seconds, to obtain substrate precursor sheet. The precursor sheet is carbonized at 2000-3000 degrees C in nitrogen atmosphere, dried and molded, to obtain porous carbon electrode base material. When the paper making material does not contain any carbon fibers, then the material is impregnated with thermosetting resin before heat processing.    USE - Manufacture of porous carbon electrode base materials are used for polymer electrode fuel cells.    ADVANTAGE - The porous carbon electrode base materials has excellent electroconductivity and tensile strength. The carbonization yield is improved without mixing resin components, and the electrode base material is manufactured economically.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of heat processing, which involves heating using far infrared ray.
NOVELTY - The method involves photosynthesizing micro algae (8), when sunlight (T) is light-injected in the process waste water (W) in the aerator (3), so that micro algae exhaust gas (E) is cultured within the process waste water of the aerator. The sludge (S2) containing the micro algae cultured by the aerator are collected and the collected sludge are methane-fermented with the methane fermentation apparatus (9) and the carbon dioxide gas is converted into a biogas fuel.    USE - Carbon-dioxide-gas reduction method of sewage treatment equipment (claimed).    ADVANTAGE - The capacity of the carbon dioxide gas can be reduced effectively, as the collected sludge are methane-fermented with the methane fermentation apparatus and the carbon dioxide gas is converted into the biogas fuel. The obstruction of the flow path of the process waste water by adhesion is not generated. The process waste water can be purified effectively. The bad influence of the hot exhaust gas on the micro algae in the aerator can be prevented effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for sewage treatment equipment.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the sewage treatment equipment. (Drawing includes non-English language text)    Aerator (3)    Micro algae (8)    Methane fermentation apparatus (9)    Exhaust gas (E)    Sludge (S2)    Sunlight (T)    Process waste water (W)
NOVELTY - An ethanol-based fuel comprises: 40-90 vol.% of ethanol, 60-10 vol.% of castor oil, and optionally additives in a total amount of up to 10 wt.% of the total weight of the ethanol and castor oil.    USE - As ethanol-based fuel for operating an internal combustion engine (i.e. self-ignition internal combustion engine), where the operation comprises switching over an internal combustion engine between an operation with pyrolysis oil and an operation with a crude oil-based fuel (preferably diesel fuel, light fuel oil, and heavy fuel oil), while continuously operating the internal combustion engine (all claimed).    ADVANTAGE - The ethanol-based fuel provides CO2 neutrality at low operation costs; provides high power generation efficiency; and is suitable for continuous (long-time) operation of internal combustion engines.
NOVELTY - Fermenting solid, stackable biomass (2) in a fermenter (1), comprises introducing the solid, stackable biomass into the fermenter, and fermenting in an anaerobic fermentation phase after a starting phase for producing methane containing biogas. The volume of the fermenter, preferably the volume of the head space of the fermenter is reduced during the transition of the starting phase in the fermentation phase before switching of gas stream discharged from the fermenter from the inlet of an exhaust system to the inlet of a biogas utilization system.    USE - The method is useful for fermenting solid, stackable biomass in a fermenter.    ADVANTAGE - The method reduces the methane losses, and prevents the nitrogen and oxygen entry into the gas system.    DETAILED DESCRIPTION - Fermenting solid, stackable biomass (2) in a fermenter (1), comprises introducing the solid, stackable biomass into the fermenter, and fermenting in an anaerobic fermentation phase after a starting phase for producing methane containing biogas, where a shut-down phase is carried out after the fermentation phase, and a gas stream (5) is discharged from the fermenter. The volume of the fermenter, preferably the volume of the head space of the fermenter is reduced during the transition of the starting phase in the fermentation phase before switching of gas stream discharged from the fermenter from the inlet of an exhaust system to the inlet of a biogas utilization system, and/or during the transition of the fermentation in the shut-down phase before switching of gas stream discharged from the fermenter from the inlet of a biogas utilization system to the inlet of a lean-gas system or an exhaust system.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the process flow of the method of fermenting solid, stackable biomass.    Fermenter (1)    Biomass (2)    Separating element (3)    Gas stream (5)
NOVELTY - The solid-fuel rod (10) has circular profile center hole (13) that is penetrated even from the one end to the other end. The center hole is channel for air ventilation when carrying out the extrusion of the biomass feedstock with extruder. The outline of the cross section of the solid-fuel rod main portion is in triangle like arrangement when the convex-shaped curved line (11) and the concave shape curved line (12) are connected.    USE - Solid-fuel rod for press-hardening biomass feedstock such as chaff, grinding rice straw and wood chip.    ADVANTAGE - The generation of the stress concentration at the time of extrusion can be suppressed by the cross-sectional form of the solid-fuel rod and sufficient air inflow property can be exhibited.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing apparatus of solid-fuel rod, has screw that is positioned in the cylindrical main portion and is driven by a motor. The screw positioned in cylindrical main portion is extruded out by extrusion opening of dice. The biomass feedstock which is attached at the front-end of cylindrical main portion is press hardened by rotation of the screw. Several screw blades are attached to the central axis.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the solid fuel rod.    Solid-fuel rod (10)    Convex-shaped curved line (11)    Concave shape curved line (12)    Circular profile center hole (13)
NOVELTY - The integrated bipolar electrolytic cell comprises a tubular ring and a dielectric semicircular metal electrode inserted axially in median position inside the ring. The dielectric semicircular metal electrode is designed on top and hole equalization level of electrolyte. The tubular dielectric ring includes a bracket which is disposed asymmetrically. The hole equalization level of electrolyte of the semicircular metal electrode plate is closed to the fixing projection.    USE - Integrated bipolar electrolytic cell used for manufacturing water electrolyzer for obtaining hydrogen and oxygen by electrolysis.    ADVANTAGE - The integrated bipolar electrolytic cell comprises a tubular ring and a dielectric semicircular metal electrode inserted axially in median position inside the ring, and thus provides cost-effective construction and maintenance.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the cells in serial with lid and clamping terminal fence.    Sealing caps (10)    Clamping plates (11)    Hole (12,14)    Outlets (15)
NOVELTY - The apparatus has a fuel feeding system (200) equipped with a fuel tank (201) for supplying hydrogen and oxygen to a fuel cell system (100). A battery (300) is connected to a control unit (400). The fuel cell system generates electricity through electrochemical reaction and supplies the generated electricity to the battery through the control unit. A pure water supply unit (202) supplies pure water to a reformer in the fuel feeding system. The reformer reforms fossil fuel. The fuel cell system is provides electrical balance to a plant.    USE - Power supply apparatus for a submarine.    ADVANTAGE - The apparatus has prolonged service life. The apparatus steadily provides high power, improves operation efficiency of a submarine and occupies less space.    DETAILED DESCRIPTION - The fossil fuel is methane and natural gas or diesel oil. The battery is a lead accumulator battery, a lithium battery, a metal-air battery or sodium-sulfur battery.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a power supply apparatus.'(Drawing includes non-English language text)'    Fuel cell system (100)    Fuel feeding system (200)    Fuel tank (201)    Pure water supply unit (202)    Battery (300)    Control unit (400)
NOVELTY - The method involves preparing an air electrode reaction prevention layer that is laminated on a zirconium dioxide group solid electrolyte layer of a substrate using a warm isostatic press (WIP) process. A binder and a plasticizer in a green sheet of the air electrode reaction prevention layer are removed. The air electrode reaction prevention layer is compression-molded by a cold isostatic press (CIP) process. A cathode layer is formed on the air electrode reaction prevention layer. A fuel anode layer is formed on the cathode layer.    USE - Method for manufacturing a solid oxide fuel cell for a fuel cell power generation system (claimed) in e.g. transportation machinery, mobile equipment and portable apparatus.    ADVANTAGE - The method enables extraordinarily manufacturing the cathode layer and the air electrode reaction prevention layer with high density in low temperature, avoiding a separate thermal process for densifying the air electrode reaction prevention layer, preventing interfacial reaction of a solid electrolyte layer, reducing manufacturing cost of a solid oxide fuel cell, providing thermal heat in cyclic manner, avoiding mechanical impact and vibration of a fuel cell power generation system and improving mechanical reliability and commercialization of the solid oxide fuel cell.
NOVELTY - Polarized glyceryl ester sulfate production involves using crude glycerin originated from biodiesel production process, where water molecule is removed from glycerin molecule. Sulfuric acid is added into the glycerin with a catalyst to conduct chemical reactions. The reaction mixture is heated at 120 degrees C. An additive for increasing calorific value.    USE - Method for producing polarized glyceryl ester sulfate for use as fuel for boilers and for use in waterproofing layer to form rubber, such as tires and other utensils (all claimed).    ADVANTAGE - The method produces polarized glyceryl ester sulfate in a simple manner with high yield of 80%, which replaces low density mineral oils in chemical industries, various kinds of vegetable oils, diesel or petrol, produces biodiesel with carboxylic acid, and reduces emission of greenhouse gases and sulfur dioxide.
NOVELTY - The method involves preparing raw materials for forming a vapor phase after hydrolysis reaction. Hydrolyzate is comprised of hydrolysis fermentable sugars, lignin and water. Sugary phase is obtained from the fermentable sugars after separation of lignin. Mash is prepared during fermentation process. Fermentable sugars and lignin are separated after enzymatic hydrolysis. Ethanol is distilled in a substrate. The obtained crude ethanol is refined to obtain anhydrous bio-ethanol that is used to generate electricity.    USE - Method for single-stage hydrolysis of lignocellulosic materials.
NOVELTY - The apparatus has fuel cell system (100) which is provided with fuel to produce electricity with electrochemical reaction. A fuel tank (201) of fuel feeding system supplies fuel to the fuel cell system and the battery (300) stores the electricity generated in the fuel cell system. The fuel is hydrogen and oxygen and fossil fuel is selected from group of methane, nitroarginine (NG), propylene glycol (PG) and the diesel oil.    USE - Power supply apparatus for drifting buoy.    ADVANTAGE - The maintenance and repair of the power supply apparatus can be simplified and the power supply apparatus is environment friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the power supply apparatus.(Drawing includes non-English language text)    Fuel cell system (100)    Fuel tank (201)    Battery (300)
NOVELTY - Processing domestic animal carcass comprises placing animal carcass in a sealed container under pressure and steam, and adding potassium hydroxide solution or potassium hydroxide powder to the carcass and then stirring.    USE - The method is useful for processing carcass of domestic animal such as pig and poultry for producing a by-product that is useful in a fertilizer (all claimed).    ADVANTAGE - The method rapidly and economically processes the domestic animal carcass in an environmental friendly manner.
NOVELTY - Isolated polypeptide comprising: e.g. (a) a polypeptide comprising the amino acid sequence of SEQ ID No: 2 (a 241 amino acid sequence fully defined in the specification) or SEQ ID No: 4 (a 238 amino acid sequence fully defined in the specification); or (b) a polypeptide having 70% or more identity with the amino acid sequence of SEQ ID No: 2 or 4 and having a function of enhancing the saccharifying activity of cellulase, is new.    USE - The isolated polypeptide is useful in a saccharification method, and for producing alcohol (all claimed), preferably ethanol.    ADVANTAGE - The isolated polypeptide enhances the saccharifying activity of cellulase within reaction temperature regions of general fermenting microorganisms other than heat-resistant yeast.    DETAILED DESCRIPTION - Isolated polypeptide comprising: (a) a polypeptide comprising the amino acid sequence of SEQ ID No: 2 (a 241 amino acid sequence fully defined in the specification) or SEQ ID No: 4 (a 238 amino acid sequence fully defined in the specification); (b) a polypeptide having 70% or more identity with the amino acid sequence of SEQ ID No: 2 or 4 and having a function of enhancing the saccharifying activity of cellulase; or and (c) a polypeptide having an amino acid sequence that has a substitution, a deletion, an addition, or an insertion of one or more amino acid residues with respect to the amino acid sequence of SEQ ID No: 2 or 4, and having a function of enhancing the saccharifying activity of cellulase, is new. INDEPENDENT CLAIM included for:    (1) a gene encoding the polypeptide;    (2) an expression vector containing the gene;    (3) a saccharification method, comprising saccharifying cellulosic biomass with cellulase in the presence of the polypeptide; and    (4) producing alcohol, comprising saccharifying cellulosic biomass with cellulase in the presence of the polypeptide, and performing alcohol fermentation using a sugar component as a raw material.
NOVELTY - An optionally substituted benzonitrile is coupled with a dialkylsulfone, and the coupled product is hydrolyzed to obtain ( beta )-ketosulfone. The ( beta )-ketosulfone is reacted with a chiral auxiliary to form a chiral enamine. The chiral enamine is reduced to obtain an N-protected aminosulfone. The N-protected aminosulfone is optionally deprotected, to obtain phenylmethanamine-type compound (I), or its pharmaceutically acceptable salt, hydrate, solvate or polymorph.    USE - Preparation of phenylmethanamine-type compound useful for preventing and/or treating inflammatory conditions including arthritis, related arthritic conditions (e.g. osteoarthritis, rheumatoid arthritis and psoriatic arthritis), inflammatory bowel disease (e.g. Crohn's disease and ulcerative colitis), sepsis, psoriasis, atopic dermatitis, contact dermatitis, and chronic obstructive pulmonary disease.    ADVANTAGE - The phenylmethanamine-type compound is prepared with high productivity and yield in a short period of time by efficient and environmentally-friendly process.    DETAILED DESCRIPTION - An optionally substituted benzonitrile is coupled with a dialkylsulfone, and the coupled product is hydrolyzed to obtain ( beta )-ketosulfone. The ( beta )-ketosulfone is reacted with a chiral auxiliary to form a chiral enamine. The chiral enamine is reduced to obtain an N-protected aminosulfone. The N-protected aminosulfone is optionally deprotected, to obtain phenylmethanamine-type compound of formula (I), or its pharmaceutically acceptable salt, hydrate, solvate or polymorph.    R=CH(1-6C alkyl)Ar or H;    R1=1-6C alkyl;    R2-R6=H, halo,1-6C alkyl, 1-6C alkoxy, -CF3, -CN or -NO2;and    Ar=aryl.    INDEPENDENT CLAIMS are included for the following:    (1) phenylmethanol-type compound of formula (III), or its salt, hydrate, solvate or polymorph; and    (2) phenylmethanamine-type compound of formula (IV), or its salt, hydrate, solvate or polymorph.
NOVELTY - The method involves forming lamination on a buffer layer. The buffer layer is laminated on a side of an electrolyte that is connected with a fuel anode supporter. The fuel anode supporter is made of fuel anode support material that is provided with metal oxide powder. The electrolyte is connected with an oxygen ion conductor that is provided with yttrium-stabilized zirconia.    USE - Method for manufacturing a metal supported solid oxide fuel cell.    ADVANTAGE - The method enables reducing manufacturing time and cost of a metal supported solid oxide fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a metal supported solid oxide fuel cell manufacturing method.'(Drawing includes non-English language text)'
NOVELTY - Recovering ethylene, comprises recovering a stream comprising methane, ethylene and nitrogen oxides from an ethylene production process and an ethylene recovery process, separating the ethylene-containing stream (102) via extractive distillation using a solvent comprising 2-5C hydrocarbon absorbent to produce an overhead fraction (106) comprising methane and nitrogen oxides and a bottom fraction (108) comprising the solvent and ethylene, where the extractive distillation is operated at specific temperatures and pressures to prevent conversion of nitrogen oxides to nitrous trioxide.    USE - The method is useful for recovering ethylene (claimed) from refinery offgas, where the ethylene is useful for producing various chemical and polymer products used in consumer products and applications.    ADVANTAGE - The method allows safe and reliable recovery of ethylene from the refinery offgas in less capital and operating costs and with high stability.    DETAILED DESCRIPTION - Recovering ethylene, comprises recovering a ethylene-containing stream (102) comprising methane, ethylene and nitrogen oxides from at least one of an ethylene production process and an ethylene recovery process, separating the ethylene-containing stream via extractive distillation using a solvent comprising a 2-5C hydrocarbon absorbent to produce an overhead fraction (106) comprising methane and nitrogen oxides and a bottom fraction (108) comprising the solvent and ethylene, where the separating step comprises operating the extractive distillation at temperatures and pressures sufficient to prevent any conversion of nitrogen oxides to nitrous trioxide.    DESCRIPTION OF DRAWING(S) - The figure shows a simplified flow diagram of a process for recovering ethylene.    Extractive distillation system (10)    Ethylene containing stream (102)    Solvent stream (104)    Overhead fraction (106)    Bottom fraction. (108)
NOVELTY - Method for preparing organic fertilizer, involves (a) collecting cow manure from cow manure storage areas, and removing odor and moisture after 1 year of storage, (b) collecting poultry manure from poultry farm, and removing harmful components from poultry manure, (c) mixing 20-30 pts. wt. cow manure, 10-20 pts. wt. poultry manure, 10-15 pts. wt. crushed pine bark, 25-35 pts. wt. peat and 20-30 pts. wt. cultivated mushroom, and stirring the mixture for 30 minutes-2 hours, and (d) uniformly mixing the mixture, and performing fermentation for 15-30 days.    USE - The method is useful for preparing organic fertilizer (claimed).    ADVANTAGE - The fertilizer is rich in organic materials and thus provides all kinds of nutrients necessary for the plant growth, and prevents acidification of soil.    DETAILED DESCRIPTION - Method for preparing organic fertilizer, involves (a) collecting cow manure from cow manure storage areas, and removing odor and moisture after 1 year of storage, (b) collecting poultry manure from poultry farm, where the poultry manure is stacked for 3 years, and removing harmful components from poultry manure, (c) mixing 20-30 pts. wt. cow manure, 10-20 pts. wt. poultry manure, 10-15 pts. wt. crushed pine bark, 25-35 pts. wt. peat and 20-30 pts. wt. cultivated mushroom, and stirring the mixture for 30 minutes-2 hours, and (d) uniformly mixing the mixture, and performing fermentation for 15-30 days.
NOVELTY - Drying apparatus for a biogas plant for drying a liquid product, preferably a biomass, comprises a drying zone (11), which is provided with at least a portion of thermal energy from the biogas plant, for operating; and a heat supply device with a first wall (15), which defines the drying zone, where the heat supply device is connected to at least one of the outer surface of the first wall for heating an outer side of the drying zone.    USE - The drying apparatus is useful for a biogas plant for drying a liquid product, preferably a biomass.    ADVANTAGE - The drying apparatus has a simple structure, and ensures drying of liquid product in simple-, improved- and/or economical manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for drying the liquid product, preferably the biomass using the drying device, comprising supplying the liquid product to the drying zone of the drying apparatus, evaporating the liquid portion of the liquid product, for separating the liquid portion from a solid portion of the liquid product within the drying zone, using thermal energy from the biogas plant and/or a cogeneration plant, where the drying zone is heated from the outside.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic cross-sectional side view of drying apparatus.    Drying zone (11)    First wall (15)    Further wall (23)    Segments (25)    Outlet (29)
NOVELTY - Method provides for degreasing of buckwheat straw with 100% acetone. The degreased straw is extracted in 5 l of 70% ethyl alcohol in boiling water bath for 1 hour. The extracted raw materials are separated by filtration to produce alcohol extract. The produced alcohol extract of the stimulant is concentrated under vacuum, cleaned from admixtures with ethyl acetate and dried to prepare target product.    USE - Biotechnologies.    ADVANTAGE - Invention makes it possible to increase yield of yeast biomass.2 tbl, 2 ex
NOVELTY - The method involves esterifying 10-20% mass of fatty acid with methanol and ethanol at 60-90 degrees C and 1-3 atmospheric pressure in presence of sulfuric acid, sodium sulfate or potassium sulfate. The reaction is carried out in continuous or discontinuous type closed reactor containing exit to evaporation of residual alcohol distilled in anhydrous state. The reaction is carried out for 50-140 minutes.    USE - Method for performing direct esterification of free fatty acids for producing biodiesel.    ADVANTAGE - The method produces high purity (97-99%) biodiesel in a simple and cost-effective manner by direct esterification of free fatty acids without generating effluents. The produced biodiesel allows immediate use as fuel.
NOVELTY - The fuel additive composition comprises 35-65 wt.% of an ignition promoter belongs to group of alkoxylated glycerols, and 2-15 wt.% of a lubricant containing one or multiple alkoxylated alkylamines. 25-50 wt.% of solvent is provided for facilitates interaction between lubricant and fuel. The fuel additive forms a stable solution with fuel when added 2-20 wt.%, preferably 10 wt.% of the total solution.    USE - Fuel additive composition used in fuels or biofuels (claimed).    ADVANTAGE - The fuel additive composition provides high alcohol ignition, enhances lubricity of fuel, and provides stable solution.
NOVELTY - The equipment comprises a roll-on/roll-off type closed container (1) which is made of carbon steel plate or stainless steel plate and structured profile with ribs bent carbon steel. A top cover (2) is designed with entire length with 2-3 nozzles (3), where a container is installed on the profile. A floor grate (4) of rigid modules is deigned on bottom of the container. The nozzles are provided for inputting and outputting biogas with flanges, where an outlet nozzle is connected to an internal tube collector.    USE - Equipment for desulfurization of biogas produced by anaerobic reactor.    ADVANTAGE - The equipment comprises a roll-on/roll-off type closed container which is made of carbon steel plate or stainless steel plate and structured profile with ribs bent carbon steel, and thus provides simple design, efficiently removes hydrogen sulfide and other mercaptans, and corrosive components of biogas, and facilitates functional characteristics as product durability.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic top perspective view of the equipment for desulfurization of biogas.    Closed container (1)    Top cover (2)    Nozzles (3)    Grate (4)    Side nozzles (5)
NOVELTY - The invention relates to a process for producing a Diesel-type biofuel. According to the invention, the process consists in the pre-filtering of vegetable oil waste, the thermal and/or enzymatic hydrolysis, at an oil:enzyme ratio of 1:40...1:60, of mono-, di- and triglycerides, at 40 degrees C for 30...60 min and a pressure of 1 atm, while continuously stirring, wherefrom there result free fatty acids, separation the glycerine and transesterification of fatty acids with methyl or ethyl alcohol, in the presence of an acid catalyst with a concentration of 0.2...0.8 %, for 30...90 min, at 70...130 degrees C and pressure of 4...5 atm, while continuously stirring at 500...550 rpm, at an alcohol:oil ratio of 4:1...10:1, there resulting methyl/ethyl esters which are separated by vacuum distillation and thin layer drying.
NOVELTY - Organic solid waste treatment involves mounting windrow with organic matter in a bay of a site. The windrow is kept for biodegradation (composting) for some time. The windrow contents are ground and shifted after composting. Raw organic material is milled and sieved in a bay of another site. A swath of organic matter is mounted in the same bay of the first site. The windrow is treated repeatedly three times to obtain multiple bays consecutively with time interval between each bay.    USE - Method for treatment of organic solid waste (claimed).    ADVANTAGE - The organic waste treatment method enables to produce less amount of carbon-nitrogen product in conventional way with requiring short time period.
NOVELTY - The station has a drying area (1) whose floor is heated by a fluid that is fed through a set of pipes (2), where the fluid is heated by a heating system that comprises a solar heating device (3) for converting solar energy into thermal energy. The solar heating device comprises a system of boilers that is fed with biogas from anaerobic digestion tanks (5). Internal pipes are penetrated through the drying area. A lower part of the floor of the drying area is provided with a thermal insulation material for achieving low thermal conductance between ground and the floor of the drying area.    USE - Drying and disinfecting station for bio-solids of a sewage treatment plant and an urban waste.    ADVANTAGE - The station fertilizes the bio-solids in a safe and efficient manner, increases soil microbiological activity and provides environmental and economic benefits to society, and has better chemical and physical fertility structures. The lower part of the floor of the drying area is provided with the thermal insulation material for achieving low thermal conductance between ground and the floor of the drying area to prevent heat loss.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a process for drying and disinfecting bio-solids.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a drying and disinfecting station.    Drying area (1)    Pipes (2)    Solar heating device (3)    Anaerobic digestion tanks (5)    Homogenizer (11)    Treadmill (12)
NOVELTY - The reactor comprises an agitation element, a heating element, a components separating element, and products refining element. The components separating element includes a system of electrostatic separation of glycerin and flash distillation system for alcohol recovery. The refining element is system of filters.    USE - Reactor for performing various unit operations, such as stirring, heating, separation, sedimentation filtration, esterification, transesterification or hydrolysis.    ADVANTAGE - The reactor produces good quality biofuel in only one reactor by performing whole process, replaces one or multiple stages of physical or chemical processes, optimizes residence time of raw materials in plant, enhances reaction yield, reduces energy consumption and waste production, and maintains quality of the final product.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for performing the various unit operations in the reactor for producing esters (biodiesel), glycerol, inorganic salts, soaps (crude glycerin), free fatty acids or water.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the reactor in biofuel production. (Drawing includes non-English language text).
NOVELTY - The method involves using biogas collector to collect biogas from municipal landfill in upper portions, which is mixed with methane directly to barometric fluctuation and changing gas quality.    USE - Method for collecting biogas from a landfill.    ADVANTAGE - The method involves using biogas collector to collect biogas from municipal landfill in upper portions, and thus facilitates increased uptake of biogas for later use as alternative energy, and inhibits microbial anaerobic fermentation.
NOVELTY - Biodiesel production involves using frying oils and edible vegetable oils, where free fatty acids are removed from oils by semiconductor accelerated stable solids and ultraviolet lamps. Thermal transesterification is performed for triglycerides of oils.    USE - Method for producing biodiesel by using zinc oxide silica photocatalyst.    ADVANTAGE - The method obtains high-quality biodiesel in a cost-effective manner without using expensive refined vegetable oils. The produced biodiesel meets required quality standards for use and marketing.
NOVELTY - Biodecomposting device comprises an equipment with modified and combined elements in different layouts.    USE - Biodecomposting device for small volumes of organic matter (claimed).    ADVANTAGE - The biodecomposting device is economic, practical, functional and safe, and ensures convenience to users and environment benefit.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspectiv view of a biodecomposting device.
NOVELTY - This utility model claims a biomass fuel carbon dioxide cycle without oxygen gasification equipment, mainly comprising a gasification furnace, a waste heat exchanger, a waste heat boiler, a cyclone dust remover, a scrubber tower, a reaction tower, a desulfurizing tower, a synthesis gas removing tower, catalytic synthesis tower and tail gas decarburization tower are connected in turn; And only using the carbon dioxide and biomass solid fuel gasification is high quality synthesis gas as gasifying agent, and recovering synthesis gas by carbon dioxide gas in the synthesis gas and the subsequent process using carbon dioxide gas generated by the gasification cycle so as to achieve a complete set of system greenhouse gas carbon dioxide discharge amount is zero. The utility model is provided with no oxygen consumption, high quality to prepare synthesis gas, the cooling medium gas rate is high, the system is simple to operate, and the whole system is a gas discharging amount of carbon dioxide is zero and so on;
NOVELTY - The utility model claims a suction type paragraphs fixed bed biomass gasification furnace, belonging to the biomass gasification field. This utility model is composed of a feeding pipe, a distributor, a throat section, a gasification furnace wall, a fire grate, an ash hopper, a biomass raw material enters from the feeding pipe, the distributing device are distributed in the hearth, the throat section to form material layer, gas raw material to generate the air from the bottom of the fire grate gasification furnace with biomass fuel gas outlet passes through the side wall of throat section away from the gasification furnace. Gasification furnace through provided with the reaction temperature of the secondary wind and a bottom control hearth of the lower part to ensure stable operation of the system and realize biomass raw material pass through is set on the upper part of the throat section to seal the gas. This utility model has stable structure, convenient feeding, stable operation and so on. The device raw material adaptability, capable of processing a plurality of kind of biomass.
NOVELTY - Flue gas reduction desulfurization and denitration catalyst comprises 80-99.9 mass% carrier i.e. active carbon, 0.1-10 mass% active component yttrium oxide, and 0-10 mass% cocatalyst.    USE - Flue gas reduction desulfurization and denitration catalyst.    ADVANTAGE - The catalyst is suitable for single desulfurization and denitration and simultaneous desulfurization and denitration, has simple preparation and desulfurization and denitration rate of more than 90%, and provides no secondary pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for application of flue gas reduction desulfurization and denitration catalyst comprising placing the catalyst in a fixed bed reactor, and under the condition of normal pressure, gas hourly space velocity of 1000-6000/hour, and reaction temperature of 300-500 degrees C, conducting single desulfurization or simultaneous desulfurization and denitration of flue gas.
NOVELTY - The furnace has a heat insulating shell (1) which is provided with a combustion chamber (2). A heat transfer chamber (3) is connected with an oil outlet (19) and an oil port (20). An explosion-proof opening (21) is connected with thermoelectric heat transfer chamber (22). A fan (10) is connected with air outlet three-way valve (11) that is connected with the combustion chamber of a secondary air pipe (12), a pyrolysis chamber (4) and air inlet (8). An oil pump (14) is connected with an oil pipe (16). An ignition device (18) is provided under a nozzle (17).    USE - Biomass-diesel dual-use heat-conducting oil furnace.    ADVANTAGE - The energy shortage caused by the influence of the production can be prevented. The selection range of the fuel can be enlarged.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the heat-conducting oil furnace.    Heat insulating shell (1)    Combustion chamber (2)    Heat transfer chamber (3)    Pyrolysis chamber (4)    Air inlet (8)    Fan (10)    Three-way valve (11)    Secondary air pipe (12)    Oil pump (14)    Oil pipe (16)    Nozzle (17)    Ignition device (18)    Air outlet (19)    Oil port (20)    Explosion-proof opening (21)    Thermoelectric heat transfer chamber (22)
NOVELTY - The furnace has a biomass burner, a high temperature crucible furnace and a pulverized coal burner (11) which are connected sequentially. The hearth (15) of the furnace end is connected with a cracking chamber (8) of a cracking device and the biomass burner. The other end of the furnace is connected with a combustion head (18) of the pulverized coal burner.    USE - Biomass-pulverized coal dual-purpose crucible furnace.    ADVANTAGE - Complexity in working condition of the furnace can be prevented. The combustion stability of the furnace can be improved. The crucible furnace is energy-saving and environment friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the dual-purpose crucible furnace.    Hopper (1)    Cracking chamber (8)    Pulverized coal burner (11)    Hearth (15)    Combustion head (18)
NOVELTY - Corn fertilizing method involves selecting biogas slurry and biogas residue, soaking seeds with the biogas slurry, applying base fertilizer, spreading the fertilizer directly to the field and ploughing the soil immediately, applying additional fertilizer, and performing fertilization, where the three fertilizing periods are needed, namely, jointing fertilizer, spike fertilizer and particle fertilizer.    USE - The method is useful for fertilizing corn (claimed).    DETAILED DESCRIPTION - Corn fertilizing method involves selecting biogas slurry and biogas residue from normally producing biogas for two months or more, soaking seeds with the biogas slurry for 10 hours, applying base fertilizer, where the base fertilizer comprises 700 kg biogas residue, 40 kg calcium superphosphate, 25 kg potassium chloride and 25 kg ammonium chloride, and the 3 kg polyaspartic acid is mixed with the 40% base fertilizer, spreading the fertilizer directly to the field and ploughing the soil immediately with the depth of 6-9 cm, applying additional fertilizer, performing fertilization, where the three fertilizing periods are needed, namely, jointing fertilizer, spike fertilizer and particle fertilizer, the period of jointing fertilizer is to spray mixed solution of the 20-30 kg biogas slurry and polyaspartic acid to the surface of leaves in the first three days of jointing, the period of spike fertilizer is to additionally apply 40 kg ammonium chloride 10 days before spike outgrowth in the large bell mouth period of corn, and the period of particle fertilizer is to spray the biogas slurry on the surface of leaves one day before and after corn pollination, and spraying biogas slurry diluted with water at a concentration of 10-15 kg/acre.
NOVELTY - This utility model claims a kind of carbonizing device. It comprises a tunnel kiln carbonizing furnace body, a heating unit, a smoke dust collecting processing unit is further set with box, track type material, the sintering box is placed on the loading track type vehicle, wherein the heating unit comprising hearth, a flame, a fuel gas pipeline, gas pipeline, straw is set in the loading material in the sintering, and to the carbonization furnace, after sealing by the gas pipe and combustion-supporting gas pipe in the heating unit to the flame supply fuel gas and combustion-supporting gas, and the flame into the hearth burning heat, the hearth, raising the temperature to 480 to 550 heat preservation for 5 to 8 hours and cooling to obtain. This utility model device carbonization using a biological straw resource, and is provided with carbonization ratio is high, the carbon emission is low, the resource is fully used, carbonizing efficiency is high, the energy consumption is low, and is suitable for large-scale production is environment-friendly and so on.
NOVELTY - Kiln fermentation method for preparing bioorganic fertilizer, involves uniformly mixing raw materials comprising animal manure, ground organic wastes, lignite and biological strains, adding the materials into a fermentation tank, carrying out fully-enclosed anaerobic fermentation, ventilating the fermentation tank, opening the discharge gate to move the materials out of the fermentation tank after the temperature of the materials exceeds 70 degrees C, carrying out oxygen consumption fermentation for 2 days, and airing to obtain fertilizer.    USE - The kiln fermentation method is useful for preparing bioorganic fertilizer (claimed).    ADVANTAGE - The method enables improve putrescibility of organic materials to more than 90% and fertility of the fertilizer, and reduce fermentation time to 10-15 days, time cost and loss of raw material.    DETAILED DESCRIPTION - Kiln fermentation method for preparing bioorganic fertilizer, involves uniformly mixing raw materials comprising animal manure, ground organic wastes, lignite and biological strains, adding the materials into a fermentation tank, carrying out fully-enclosed anaerobic fermentation for 8-13 days after the fermentation tank is filled with the materials, ventilating the fermentation tank after the temperature of the materials increases to 60-70 degrees C, opening the discharge gate to move the materials out of the fermentation tank after the temperature of the materials exceeds 70 degrees C, carrying out oxygen consumption fermentation for 2 days, and airing to obtain fertilizer.
NOVELTY - Preparing resveratrol comprises reacting 5-(chlorocarbonyl)isophthalate compound (I) with styrene 4-carboxylate compound (II) in presence of transition metal salt catalyst in ionic liquid for 0.1-2 hours at 40-100 degrees C, by using N-methyl-2-pyrrolidone (NMP) as a ligand in base to obtain (E)-5-(4-carboxylatostyryl)isophthalate compound (III), acidifying (III), then saponifying and recrystallizing. The transition metal salt is e.g. acetate, chloride or sulfate of ruthenium, rhodium, palladium or platinum. The base is e.g. trisodium phosphate, tripotassium phosphate or cesium carbonate.    USE - The method is useful for preparing resveratrol (claimed).    ADVANTAGE - The method has high yield, low cost and convenient post-processing; and is simple, environmentally friendly and suitable for industrial production.    DETAILED DESCRIPTION - Preparing resveratrol comprises reacting 5-(chlorocarbonyl)isophthalate compound of formula (I) with styrene 4-carboxylate compound of formula (II) in presence of transition metal salt catalyst in ionic liquid for 0.1-2 hours at 40-100 degrees C, by using N-methyl-2-pyrrolidone (NMP) as a ligand in base to obtain (E)-5-(4-carboxylatostyryl)isophthalate compound of formula (III) with yield of 99-100%, acidifying (III), then saponifying and recrystallizing. The transition metal salt is acetate, chloride or sulfate of ruthenium, rhodium, palladium, platinum or other transition metal. The base is trisodium phosphate, tripotassium phosphate, cesium carbonate, calcium carbonate, potassium carbonate, sodium carbonate or any other inorganic base. The ionic liquid is of formula (AX).    R = 1-8C alkyl or phenyl;    A = 1-butyl-3-methylimidazolium; and    X = tetrafluoroborate, hexafluorophosphate, hexafluoroantimonate, trifluoromethanesulfonate or bis(trifluoromethylsulfonyl)imide.
NOVELTY - A soilless culture substrate comprises 3-6 pts. vol. zeolite, 2-5 pts. vol. corn stalk fermented organic fertilizer, and 1-3 pts. vol. vermiculite. The substrate is prepared by crushing natural zeolite into 10 meshes; crushing freshly harvested corn stalks, water wetting to adjust water content to 70-80 wt.%, mixing with 2 kg organic material-decomposing agent and 5 kg urea, stacking, covering with plastic film, and fermenting for 28-30 days while turning once every 10 days to obtain organic fertilizer; and mixing zeolite, organic fertilizer and vermiculite, and high-temperature sterilizing.    USE - Soilless culture substrate used for pseudoginseng (claimed).    ADVANTAGE - The culture substrate has no pathogenic bacteria and reduces the occurrence of pseudoginseng disease. The zeolite has rich trace element content, good air permeability, and strong ability to retain water and nutrients. The organic fertilizer has rich nutrition.
NOVELTY - Method for preparing liquid fertilizer, involves collecting animal blood at a size of 10-30 mesh to remove unnecessary substances, steaming the collected blood at 100-120 degrees C for 80-120 minutes, separating heated blood into solid content and filtrate, adding the filtrate into a fermenting tub which is fixed with a whisk and an aerator, vaccinating the filtrate by Bacillus sonorensis and fermenting the mixture at 30-40 degrees C for 10-20 days, and mixing the fermented filtrate with ceramic powder which is turned into particle type from melting mineral mixtures.    USE - The method is useful for preparing liquid fertilizer (claimed) which is used as organic fertilizer.
NOVELTY - Purification of sucrose 6-ethylester comprises treating esterified liquid sucrose at 50-60 degrees C, condensing, adding organic solvent and separating out white solid; raising temperature to 30-40 degrees C for 1-3 hours to dissolve white solid, reducing temperature to - 5-5 degrees C for 1-3 hours, filtering and keeping temperature at 40-45 degrees C to obtain 97-99% purity.    USE - Purification of sucrose 6-ethylester.    ADVANTAGE - The process produces stable property, high purity, little impurity, reduces raw material consumption, reduces time and difficulty of refining, reduces cost, improves yield, shortens production period, saves energy and reduces emission.
NOVELTY - Synthesis of benzylidene malononitrile and its derivatives comprises reacting while stirring aromatic aldehyde and malononitrile in the presence of 0.5-1.5 g alkali catalyst per mol of aromatic aldehyde, stirring, filtering, washing with water and drying, where the alkali catalyst is triethylamine, sodium hydroxide or sodium carbonate.    USE - Synthesis of benzylidene malononitrile and its derivatives (claimed).    ADVANTAGE - The solvent-free, heating-free, energy-saving and economical method has mild reaction condition, simple operation and high yield.
NOVELTY - 8-12 pts. wt. p-Hydroxyphenylacetic acid, 6-12 pts. wt. phthalide, and 8-12 pts. wt. sodium methoxide are prepared, and the resultant product is dissolved in dimethylacetamide, and heated at 80-170 degrees C for 3-10 hours under 0.1-10 Pa and crystallized. 4-(2-Carboxybenzyloxy)phenylacetic acid is dissolved in glacial acetic acid, 3-52 pts. wt. polyphosphoric acid is added, heated at 30-100 degrees C for 3-12 hours under 0.1-10 Pa, cooled and crystallized, to obtain isoxepac crude product. The isoxepac crude product is dissolved in ethyl acetate, refined, decolorized and dried, to obtain isoxepac.    USE - Preparation of isoxepac (claimed).    ADVANTAGE - The method economically and environmentally-friendly provides isoxepac with high purity and yield under short period of time.
NOVELTY - The method involves adding 30-98% fine coal or brown coal with 5-15% waste material, and adding 1-10% binder material with 1-20% bio-booster. The fine coal, the waste material, the binder material and the bio-booster are thoroughly mixed to form dough, which is extruded to a pea plant through a high pressure equipment.    USE - Method for producing fuel briquettes using fleet sludges from a sewage treatment plant.    ADVANTAGE - The method enables providing basic charge and mineral with high calorific value.
NOVELTY - The installation has a blower pipe to drain helium concentrate. Two membrane gas separation units comprise an input and output of high pressure gas unit and a low pressure gas output unit. Each membrane gas separation unit is comprised with parallel-connected gas utilities membrane modules. Each module is separated by selectively permeable membranes of the high pressure chamber and a low-pressure chamber. The output of high-pressure gas of next gas separation unit, is in communication with the gas inlet pressure of the initial gas separation unit.    USE - Installation to extract helium from natural gas.
NOVELTY - Metal ions and organic precursor are dissolved in a solvent to mixture. Pore derivative is added to mixture. The resulting mixture is heated for less than 4 hours, to obtain metal organic source skeleton structure.    USE - Manufacture of metal organic source skeleton structure used for gas storage applications.
NOVELTY - Chlorosulfonating para-ester with thionyl chloride opening vacuum air pumping valve, adding chlorosulfonic acid, stirring at 5-60 revolutions/minute and cooling at 25 degrees C; adding acetanilide to react, and stirring for 30-50 minutes; sulfonating into high temperature sulfonated kettle, slowly increasing temperature to 50 degrees C, adding thionyl chloride for 5 hours, stirring for 4-5 hours, sampling and analyzing content of more than 90%; and closing jacket steam valve, opening jacket circulation water valve, and discharging to obtain acetyl sulfonic acid chloride.    USE - Method of production of p-ester thionyl chloride chlorosulfonate (claimed).    ADVANTAGE - The method reduces acid hydrolysis and wastewater discharge amount, is simple and more environment-friendly, reduces material consumption, and improves quality of the product.    DETAILED DESCRIPTION - Chlorosulfonating para-ester with thionyl chloride comprises opening vacuum air pumping valve, adding chlorosulfonic acid, metering groove to sulfonating pot, adding chlorosulfonic acid, stirring at 5-60 revolutions/minute and cooling at 25 degrees C; processing sulfonation at 25 degrees C, adding acetanilide to react, and stirring for 30-50 minutes; sulfonating into high temperature sulfonated kettle, slowly increasing temperature to 50 degrees C, adding thionyl chloride for 5 hours, adding sulfonated kettle to react, stirring for 4-5 hours, sampling and analyzing content of more than 90%; and closing jacket steam valve, opening jacket circulation water valve to reduce temperature at 40 degrees C, and discharging to obtain acetyl sulfonic acid chloride.
NOVELTY - The method involves transferring a catalyst layer (M22) of a catalyst layer transfer sheet (M20) to an electrolytic membrane (M12) of an electrolytic membrane sheet (M11). A membrane electrode assembly (M40) is formed on a catalyst layer base material sheet (M21). The catalyst layer base material sheet is advanced in direction different from an advancing direction of the membrane electrode assembly. The catalyst layer base material sheet is peeled from the membrane electrode assembly sheet by spraying air on a peeling start part of the catalyst layer base material sheet.    USE - Membrane electrode assembly manufacturing method for a fuel cell.    ADVANTAGE - The method suppresses the generation of slack of the membrane generated by peeling of the base material sheet at the time of membrane electrode assembly manufacture.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an apparatus for manufacturing a membrane electrode assembly.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an apparatus for manufacturing a membrane electrode assembly. '(Drawing includes non-English language text)'    Electrolytic membrane sheet (M11)    Electrolytic membrane (M12)    Catalyst layer transfer sheet (M20)    Catalyst layer base material sheet (M21)    Catalyst layer (M22)    Membrane electrode assembly (M40)
NOVELTY - The cell has multiple cylindrical-shaped small cells (301) arranged along a central axis and electrically connected in series with a current collection part (310). The current collection part is connected with a center convex part that connects a solid surface (307) with an area that is enclosed by multiple fuel-supply holes (305) in an end surface of one of small cells. A surrounding wall part is connected with an air electrode layer (304) formed in a side surface of another small cell.    USE - Fuel cell for generating electric power.    ADVANTAGE - The cylindrical-shaped small cells are arranged along the central axis and electrically connected in series with the current collection part, so that the cell can reduce loss of electric power by Joule heat.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for manufacturing a fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a fuel cell.    Cylindrical-shaped small cells (301)    Air electrode layer (304)    Fuel-supply holes (305)    Solid surface (307)    Current collection part (310)
NOVELTY - The fuel cell (10) includes at least one metal separator (16,18) formed by integrally molding a sealing piece (32) with a metal plate (31). The metal plate includes a hole which connects a fuel gas flow channel and a fuel gas inlet communicating hole (24a,24b). The sealing piece includes a coating portion (42a,42b) which covers the inner peripheral surface of the hole of the metal plate to form an insulated communicating hole (30a,30b).    USE - Fuel cell for generating electric power.    ADVANTAGE - Prevents exposure of a metallic part to the insulated communicating hole, thus preventing an electrical short circuit between the metal separator and generated water or condensed water, and reliably preventing corrosion of the metal separator using a simple structure. Enables easy and reliable formation of insulated communicating hole with desired shape. Facilitates efficient manufacturing of metal separator.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a manufacturing method for metal separator for fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic sectional view of a portion of the fuel cell.    Fuel cell (10)    Metal separator (16,18)    Fuel gas inlet communicating hole (24a,24b)    Insulated communicating hole (30a,30b)    Metal plate (31)    Sealing piece (32)    Coating portion (42a,42b)
NOVELTY - Increasing (I) sugar yield in a bio-product production, comprises pretreating at least one size-adjusted lignocellulosic biomass particle with a pretreatment, where the size-adjusted lignocellulosic biomass particle (LCB) forms a substrate with the particle having an average particle size of greater than 5 mm in at least one dimension.    USE - The method is useful for increasing sugar yield in a bio-product production where the bio-product is animal feed produced and a biofuel (ethanol or butanol) (claimed).    ADVANTAGE - The method: utilizes lignocellulosic biomass which is readily-available low cost feedstock and reduces greenhouse gas emissions; improves production yields of various bio-products; allows ammonia treatment which is capable of opening up cell wall in agricultural residues with greatly reduced degradation products; efficiently recover high yields of soluble pentose sugars; and increases downstream sugar yield and cost-effective.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) animal feed produced and a biofuel produced by the method (I);    (2) a method (II) of using a substrate to increase downstream sugar yield comprising pretreating the substrate containing size-adjusted LCB with pre-treatment; and    (3) a system comprising: a size-adjusting device for producing size-adjusted non-fine biomass; and a pretreatment facility for pretreating the size-adjusted biomass to produce pretreated size-adjusted biomass, where the pretreated size-adjusted biomass increases sugar yield in a bio-product production facility as compared to fine biomass.
NOVELTY - Treating biomass comprises subjecting biomass to microbial digestion, preferably anaerobic microbial digestion to produce volatile fatty acids (VFAs) and/or solvents followed by wet oxidation to reduce biosolid volume while retaining or increasing the concentration of the VFAs and/or solvents.    USE - The methods are used for treating biomass and producing a fuel or fuel precursor (all claimed).    ADVANTAGE - An improved or alternative process for treatment of waste effluents containing organic material to result in a reduction of sludge volume and the production of useful chemical by-products is provided.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a process of producing a fuel or fuel precursor by processing at least one of the separated VFAs or solvents produced according to the method above into a fuel or fuel precursor.
NOVELTY - Device for simulation of the processes of artificial biological purification of sewage liquids comprises three sequentially connected container- corridors and sumps, isolated by partitions, where the device has installed in the container-corridors by the system of bubbly aeration and stirring devices, the container-corridors are designed with the possibility of the accounting of the correspondence with the conditions of hydromechanical similarity of hydraulic effects and are made with the possibility of work in the anaerobic mode.    USE - As device for simulation of the processes of artificial biological purification of sewage liquids (claimed).    DETAILED DESCRIPTION - Device for simulation of the processes of artificial biological purification of sewage liquids comprises three sequentially connected container-corridors and sumps, isolated by partitions, where the device has installed in the container-corridors by the system of bubbly aeration and stirring devices, the container-corridors are designed with the possibility of the accounting of the correspondence with the conditions of hydromechanical similarity of hydraulic effects and are made with the possibility of work in the anaerobic mode, the aerobic mode for investigating different technological modes of operation of construction of artificial biological purification based on hydrodynamics flow during motion of the corridors of construction and experimental determination of required technological parameters for effective biological purification in the full-scale structure.
NOVELTY - Solid fuel granular composition comprises: carbonaceous components, coal dust and/or coke fines comprising particulate activated product of low-temperature pyrolysis of waste rubber products, preferably pyrocarbon with specific surface area of 5000-8000 cm2/g, present at 50-70 wt.%; vegetable waste comprising sawdust present at 20-30 wt.%; binder comprising aqueous solution of polymer plasticizer containing no chlorine with total moisture content of 10-35 wt.% i.e. present at 5-10 wt.%; and combustion intensifying component comprising nitrogen-containing substance i.e. present at 5-10 wt.%.    USE - The solid fuel granular composition is useful as a fuel propellant (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing the granular solid fuel propellant composition, comprising: metering and mixing of the carbonaceous components, vegetable waste and sawdust, and their activation; mixing with a binder and granulating the mixture to form agglomerates or pellets, where at first the sawdust and nitrogen-containing substances are mixed, the resulting mixture is crushed and subjected to mechanical activation in speed ball mill until the specific surface area of 5000-8000 cm2/g is achieved, and then the resulting mixture is mixed with pyro-carbon and a binder; and pressing the mixture at a humidity of 10-20 wt.% and a specific pressure of 20-115 MPa.
NOVELTY - Conditioning waste materials with initial dryness comprises forcly drying the material with initial dryness to obtain the material with reduced dryness, and shaping the reduced dryness material to obtain a compacted solid material used as a fuel.    USE - The method is useful for conditioning waste materials such as wood, wood derivatives, wet biomass that are compacted to form solid fuels (all claimed) such as coal, gas and oil that are fed to boilers, stoves and heat generating devices for a heating system, where the waste materials comprise household wastes, industrial wastes, agriculture wastes and livestock wastes, biological sludge i.e. sewage sludge, manure and digestion products.    ADVANTAGE - The method is capable of forcly drying the materials to get reduced dryness material with reduced energy consumption so that the solid fuel can be produced in an economical manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a waste material conditioning device comprising a drying unit (21) for forcibly drying the material to obtain the material with reduced dryness, and a shaping unit (22) for shaping the dryness reduced material to obtain a compacted solid material usable as fuel.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic view of a waste material conditioning device.    Drying unit (21)    Shaping unit (22)    Endless screw (23)    Drier (24)    Pellet shaping machine. (26)
NOVELTY - Preparing benzimidazole derivatives (III) comprises reacting an aniline compound (I) with an excess amount of a 2,2-difluoroacetaldehyde compound (II) in the absence of an aromatic solvent.    USE - The process is useful for preparing (III) (claimed), which is useful as: an intermediate for preparing pyrimidine derivatives or their salts; and potential anti HIV-1 bioactive agent. No biological data given.    ADVANTAGE - The process easily, rapidly and economically provides (III) with high yield and purity without using any aromatic solvent in an environmental friendly manner.    DETAILED DESCRIPTION - Preparing benzimidazole derivatives of formula (III) comprises reacting an aniline compound of formula (I) with an excess amount of a 2,2-difluoroacetaldehyde compound of formula (R2-C(=O)-CH(F)2) (II) in the absence of an aromatic solvent.    R1 = H, hydroxyl, alkoxy, alkyl, carbonyl, carboxyl, carboxylic acid ester groups, amido, cyano, halogenated aliphatic group, nitro or amino groups, preferably H, nitro, methoxyl group, -COOethyl, -CF3 or -CF2Cl;    R2 = hydroxyl, Cl, F, Br, amino or alkoxy;    X = NH, O or S; and    n = 0-4.
NOVELTY - Pretreating of biodiesel stock oil involves adding buffer solution which does not cause saponification and absorber into biodiesel stock oil having lower fatty acid with acid value of more than 5 mg potassium hydroxide/g at 30-150 degrees C under pH of 6-7.9.    USE - Pretreating of biodiesel stock oil (claimed).
NOVELTY - The ecological biodiesel fuel preparation involves obtaining industrialization mixtures of methyl esters produced by esterification and transesterification of triglycerides in vegetable oils and fats. Bentonite clay is used a catalyst for generating a cleaner operation.    USE - Method for preparing ecological biodiesel fuel used in diesel engines, agricultural machinery and pumping.    ADVANTAGE - The method provides biodiesel having excellent combustion properties and a high ecological behavior without generating sulfur emissions, and allow a clean combustion to carbon dioxide.
NOVELTY - Composter comprises a semi-cylindrical geometry surrounded with bottom and finished at top by a cover (2). A shaft-engine is arranged inside the cover provided with ellipsoidal geometry blades, which have uniform holes distributed over its entire surface to save weight and facilitate passage for aeration. A renewal crossed system comprises a gas forced air element (3b), where a loading and unloading system comprises guides secured to a casing (5) or corona-pinion gears.    USE - Composter for non-human consumption products of aquaculture (claimed).    ADVANTAGE - The composter maximizes rate of decomposition of organic material to obtain stable product in shortest period of time, and the composter is easy to handle.    DETAILED DESCRIPTION - Composter comprises a semi-cylindrical geometry surrounded with bottom and finished at top by a cover. A shaft-engine is arranged inside the cover provided with ellipsoidal geometry blades, which have uniform holes distributed over its entire surface to save weight and facilitate passage for aeration. A renewal crossed system comprises a gas forced air element, where a loading and unloading system comprises guides secured to a casing or corona-pinion gears. An assembly carrier comprises a metallic structure, which allows rotation of shell and easy transportation by wheels fitted with a brake (6). A feedback system (8) is provided to control and record process parameters, such as temperature, humidity of air and speed of shaft rotation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a composter.    Cover (2)    Gas forced air element (3b)    Casing (5)    Brake (6)    Feedback system (8)
NOVELTY - Active organic bacterial fertilizer comprises plant ash, industrial and agricultural wastes containing organic matters, and an inorganic fertilizer as raw materials. The active organic bacterial fertilizer is prepared by once continuously fermenting, pelletizing, drying and sieving strains bred from the raw materials.    USE - Used as an active organic bacterial fertilizer.    ADVANTAGE - The preparation method consume large amount of wasted industrial and agricultural wastes containing the organic matters, reduces the environmental pollution, and also solves the problems of soil hardening, fertilizer efficiency reduction and environmental pollution caused by long-term fertilizer application in the crops cultivation and urban landscaping processes. The preparation method of the active organic bacterial fertilizer can provide the novel fertilizer source for the agricultural production.
NOVELTY - Seedling matrix comprises vinegar residue, plant ash, vermiculite, grass peat, perlite and a small amount of inorganic fertilizer.    USE - The seedling matrix is useful for solanaceous vegetables (claimed) e.g. hot peppers, eggplants and tomatoes in seedling cultivation.    ADVANTAGE - The seedling matrix has high nutrient content, porous permeability, and retains moisture and fertilizer.
NOVELTY - Seedling substrate comprises vinegar residue, cassava residue, plant ash, vermiculite, grass peat and inorganic fertilizer.    USE - The seedling substrate is useful for cabbage e.g. kale (claimed), cauliflower, broccoli and other cabbage vegetables.    ADVANTAGE - The vinegar residue and cassava residue are fermented into compost materials, so that waste materials are changed into valuable things, and harmful substances are changed into benefits things. The seedling substrate has high nutrition content, loosing and permeability, water and fertilizer maintenance.
NOVELTY - A kind of energy saving type electrolytic tank, comprising a cylinder body, an end plate, a electrolysis electrode plate, electrolyte, copper bar, the cylinder is composed of a plurality of electrolysis unit is connected with the copper bar in series, and the two ends of the electrolysis cell is provided with an end plate, the electrolytic pole plate is provided with multiple holes, pass through corresponding to the electrolysis electrode plate in the electrolyte, the first hole of each electrolysis polar plate, then argon arc welding connection, at the same time, an electrolytic polar plate sealing rubber ring is electrolytic polar plate sleeve, the adjacent electrolytic pole plate connected with the copper bar, and end plate, is at the same time reduced working distance between the electrolyte. This utility model is by increasing the resistance value of the electrolytic cell, reduces the working current, and increases the electrolysis electrode plate area and reduce electrolyte working distance for the same production rate so as to save the electric energy, reduce the energy consumption and reduces the production cost and prolongs the service life of the electrolytic bath.
NOVELTY - Plant protecting agent comprises 40-60 pts. wt. discarded tobacco leaves, 2-7 pts. wt. licorice, 5-15 pts. wt. rhizoma arisaematis, 2-15 pts. wt. rhizoma gastrodiae, 5-15 pts. wt. dangshen, 2-7 pts. wt. radix sophorae flavescentis, 2-7 pts. wt. cortex phellodendri, 1-3 pts. wt. Aloe, 2-7 pts. wt. asiatic moonseed rhizome, 2-9 pts. wt. fructus xanthii, 0.5-1 pts. wt. mountain seed oil, 0.1-3 pts. wt. surfactant and 2-10 pts. wt. thickening agents.    USE - As plant protecting agent (claimed).    ADVANTAGE - The agent is environmentally-friendly and free of pollution, as it is prepared using traditional Chinese medicinal plants, prepared simply and cost-effectively, and suitable for industrialized mass production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the plant protecting agent, which involves extracting the above-mentioned raw materials twice using water with quantity of eight times and six times (each time for two hours), filtering and combining the medicine liquid, concentrating the medicine liquid until the relative density reaches 1.15-1.25, adding alcohol to enable the alcohol concentration to reach 60%, precipitating the filtered liquid to obtain a supernatant, performing spin steaming to remove the alcohol, fully mixing the mixture by adding the surfactant, mountain seed oil and thickening agent, and emulsifying to an uniform solution to obtain product.
NOVELTY - Method for purifying waste gas involves introducing industrial waste gas into a gas inlet of a purification device, mounting a filter screen in a gas inlet pipe of the device to filter solid dust, mounting a circulating cold water pipe at the periphery of the gas inlet pipe, cooling the waste gas using cold water, introducing the filtered waste gas into the purification device by a suction pump, aerating obtained gas into microbubbles through a built-in aerator, reacting microbubbles with absorption liquid, and discharging the obtained carbon dioxide gas fertilizer from a gas outlet.    USE - Method for purifying waste gas (claimed).    ADVANTAGE - The method enables purification of waste gas with reduced industrial waste gas emission by environmentally-friendly process.
NOVELTY - Preparing acetic acid alcohol ester comprises carrying out ester exchange reaction in the presence of transesterification catalyst, reacting with butyl alcohol, contact reacting acetic acid ester, and separating the obtained product.    USE - Method for preparing acetic acid alcohol ester (claimed).    ADVANTAGE - The method is simple, has low requirement of production equipment, easily obtained raw material, low energy consumption and reduced production cost, does not need to use acetic acid and sulfuric acid, and reduces device corrosion and environmental pollution.    DETAILED DESCRIPTION - Preparing acetic acid alcohol ester of formula (CH3-C(=O)-O)(n-x)R1-(OH)x (I) comprises carrying out ester exchange reaction in the presence of transesterification catalyst, reacting with butyl alcohol, contact reacting acetic acid ester, and separating the obtained product (I).    R1=5-20C alkyl, aryl, 5-12C cycloalkyl or 7-20C aryl;    n=1-5; and    x=0-4 or less than n.
NOVELTY - The device has a fermentation tank (1) that is divided into a fermentation layer (2) and a raw material layer (4). A turning plate (3) is arranged between the fermentation layer and raw material layer. A pressure sensor is arranged on the fermentation layer to transmit a pressure signal of the fermentation layer to a single chip. The single chip controls movement of the turning plate through a relay according to the pressure signal so as to add a raw material in the fermentation layer.    USE - Intelligent device used in methane production method.    ADVANTAGE - Intelligent control is realized, operation is simplified and safety is achieved since the methane fermentation tank is intelligently controlled through the single chip and the filler is controlled according to the pressure information of the methane in the fermentation tank.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the intelligent device. (Drawing includes non-English language text).    Fermentation tank (1)    Fermentation layer (2)    Turning plate (3)    Raw material layer (4)
NOVELTY - Trace element-containing fertilizer preparation comprises adding water to livestock excrement, garbage, leaves, rice husk, weeds, crop straw, and colza cake at 70-80:2-4:2-4:12-15:4-8:8-10:2-3 mass ratio, stirring uniformly, adding the mixed raw material with composite microbial inoculum, fermenting at 38-42 degrees C for 8 days, adding 1 mass% trace element, stirring uniformly and pelleting, and sieving. The composite microbial inoculum comprises 30.2 wt.% anaerobic bacteria, 28.5 wt.% actinomycete, 16.3 wt.% Lactobacillus, 22.9 wt.% microzyme, and 2.1 wt.% millet.    USE - Preparation of microelement-containing fertilizer (claimed) for pumpkin.    ADVANTAGE - The microelement-containing fertilizer prolongs the life cycle of pumpkin and improves the product quality and yield.
NOVELTY - Methanol ethanol gasoline additive comprises 30-60 pts. wt. isopropanol, 20-40 pts. wt. heptane, 3-8 pts. wt. polyoxyethylene sorbitan monooleate, 1-4 pts. wt. ethyl oleate, 2-4 pts. wt. polyisobutylene amine and 7-10 pts. wt. dimethylbenzene.    USE - Used as methanol ethanol gasoline additive.    ADVANTAGE - The additive: has oil antiknock property; has sulfur content, aromatic hydrocarbon, olefin content, benzene content, oxygen content and other quality indexes, which meets the required quality standards; has simple preparation; has good economic and social benefit; improves blending of ethanol and gasoline components; and increases the economic benefit of refineries.
NOVELTY - Low proportion methanol gasoline complex additive comprises 40-60 wt.% power promoter and 40-60 wt.% anti-phase separating agent. The power promoter is obtained by using aviation paraffin and unsymmetrical dimethylhydrazine as raw materials, refluxing and reacting under the action of cerium nitrate and vacuum separating. The anti-phase separating agent is obtained by mixing 15-25 wt.% methoxy ethoxy methane mixture, 30-40 wt.% acetal, 20-30 wt.% isooctanol, 15-25 wt.% xylene and 0.1-0.5 wt.% polyethenoxy ether surfactant, heating and refluxing for 4-5 hours.    USE - Used as a low proportion methanol gasoline complex additive.    ADVANTAGE - The additive improves dynamic property and stability of methanol gasoline and can be used in small amounts.
NOVELTY - The plant has a container (1) provided with a fermentation chamber (2), chamber pumps (3) and a percolate chamber (4) that are arranged in series, and another container (5) mounted with a spraying system (9) and provided with perforated walls. A base plate is mounted with a valve (14) and arranged on a digester.    USE - Mobile biogas plant.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a mobile biogas plant.    Container (1)    Fermentation chamber (2)    Chamber pumps (3)    Percolate chamber (4)    Container (5)    Spraying system (9)    Valve (14)
NOVELTY - Herbicide suspending agent comprises 25-45 wt.% dithiopyr, 40-70 wt.% water, 1.5-2.5 wt.% cosolvent, 1-3 wt.% wetting agent, 1.5-3.5 wt.% dispersing agent, 0.5-1 wt.% defoaming agent, 1-2 wt.% thickening agent and 0.5-1 wt.% preservative.    USE - As herbicide suspending agent (claimed).    ADVANTAGE - The agent does not produces dust at the time of application, has small particle size and thus is convenient for plants to absorb, excellent stability and anticorrosion effect, and is active even at low temperature, environmentally-friendly and easy to transport and store.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the herbicide suspending agent, involves adding dithiopyr, cosolvent and water to kettle and stirring to obtain slurry, preparing colloid from slurry and grinding colloid into coarse material for 2-3 hours, transferring the coarse material to a bead mill and milling the coarse material to obtain particles having size of 3 micron or less, completely mixing the obtained particles with wetting agent, dispersing agent, defoaming agent, thickening agent and preservative to obtain a mixture, testing the mixture, transferring the mixture to storage tank, and packing and storing the mixture.
NOVELTY - Glufosinate agent comprises glufosinate; surfactant i.e. phenylethyl phenol polyoxyethylene ether, alkylphenol formaldehyde condensate polyoxyethylene ether, alkylbenzene sulfonate, phenylethyl phenol polyoxyethylene ether sodium sulfate or phosphate, sorbierite polyethenoxy ether, alkyl polyglucoside, and/or amine polyoxyethylene ether; preservative i.e. sodium salicylate, Nipagin (RTM: p-hydroxybenzoate), sodium benzoate, and/or potassium sorbate; synergistic agent i.e. modified trisiloxane compound, azone, ammonium sulfate, and/or ammonium chloride; and deionized water.    USE - Glufosinate agent used as agricultural herbicide.    ADVANTAGE - The glufosinate agent is safe and environment-friendly.    DETAILED DESCRIPTION - Glufosinate agent comprises (wt.%) glufosinate (10-50), surfactant (1-15), preservative (0.1-1), synergistic agent (1-5), and deionized water (balance). The surfactant is phenylethyl phenol polyoxyethylene ether, alkylphenol formaldehyde condensate polyoxyethylene ether, alkylbenzene sulfonate, phenylethyl phenol polyoxyethylene ether sodium sulfate or phosphate, sorbierite polyethenoxy ether, alkyl polyglucoside, and/or amine polyoxyethylene ether. The preservative is sodium salicylate, Nipagin (RTM: p-hydroxybenzoate), sodium benzoate, and/or potassium sorbate. The synergistic agent is modified trisiloxane compound, azone, ammonium sulfate, and/or ammonium chloride. An INDEPENDENT CLAIM is included for preparation of glufosinate agent comprising adding glufosinate, surfactant, preservative, synergistic agent, and deionized water into a mixing kettle; starting the stirrer for uniform mixing; and reaching to the standard technical index through quality checking.
NOVELTY - Method for recycling food waste, involves (a) crushing organic substances and water-insoluble polymer of carbohydrate, protein, fat, fiber, and phospholipid combined with liquidity and not separated into individual components, (b) increasing ion concentration of water contained in food with high-temperature and high-pressure and decomposing ion in food, (c) separating organic acid solution and oil-containing liquid, and (d) decomposing organic acid component of aqueous solution, where the total concentration of lactic acid component is more than 500 mg/l.    USE - The method and device are useful for recycling food waste (all claimed).    ADVANTAGE - The method recycles food waste into organic acid solution as microbial nutrients and oil-containing liquid as biodiesel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for recycling food device, which comprises crushing unit for crushing organic substances and water-insoluble polymer of carbohydrate, protein, fat, fiber, and phospholipid, ion decomposition unit for increasing ion concentration of water contained in food with high-temperature and high-pressure and decomposing ion in food, and solid-liquid separation unit for separating solid and oil-containing liquid.
NOVELTY - The method involves separating a component (4) having content of hydrogen and carbon monoxide added together from 10 to 95 percent by volume from a synthesis raw gas. Decomposition is carried out in carbon dioxide product, acidic gas fraction, residual gas (60) and the component. A two-column process is utilized to carry out a cryogenic gas separation into multiple fractions. The residual gas is returned into a hydrogen- or carbon monoxide methane separation unit such that a lossless methane process operation is performed. The residual gas is conducted over a reconducting compressor (Vr).    USE - Method for producing gas product and a product containing methane containing part from hydrogen-, carbon monoxide- and methane containing components (all claimed).    ADVANTAGE - The method enables returning the residual gas into the hydrogen- or carbon monoxide methane separation unit such that a lossless methane process operation is performed, thus enabling enhanced utilization of the resulting residual gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a gas product producing device.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a gas product producing device.'(Drawing includes non-English language text)'    Reconducting compressor (Vr)    Heat exchangers (W1, W2)    Component (4)    Residual gas (60)    Mass flow (105)
NOVELTY - A reactor (100) for distillation of biomass comprises environmental control units and chambers (101) arranged vertically along a vertical axis, where each is independently connected to at least one environmental control unit (131) and each chamber is capable of having an independently controlled internal environment.    USE - As reactor for distillation of biomass (claimed), used for efficiently drying biomass, torrifying biomass, distilling biomass.    ADVANTAGE - The biomass valve reduces or inhibits vapor transfer from the first chamber to the second chamber and creates a temperature controlled, pressure controlled, and vapor controlled environment inside the first chamber relative to a second chamber.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for distilling biomass in a reactor, where the reactor having chambers, in which temperature, internal vapor pressure, vapor composition and vapor flow can be independently controlled in each chamber, comprising introducing biomass into at least a first chamber of the chambers of the reactor, and transferring the biomass from the first chamber to another chamber of the chambers, where the biomass is cellulosic material (preferably wood, or grass).    DESCRIPTION OF DRAWING(S) - The figure shows cross-sectional view of reactor for distillation of biomass.    Reactor (100)    Chamber (101)    Trays (112)    Biomass inlet (114)    Biomass outlet (116)    Vapor inlet (124)    Vapor outlet (126)    Environmental control unit (131)    Slot (139)
NOVELTY - The method involves forming a rubber sheet structure (51) comprising a rubber sheet (40) with frame shape level-difference portions. A sealing element precursor (52) is formed by stamping the rubber sheet, and removing an unnecessary portion as a sealing element. The level-difference portions of the rubber sheet and a peripheral portion of an electrode element, are combined. A molding die comprising the precursor, the electrode element, and the separators, is clamped. The rubber sheet is cross-linked by heating the molding die.    USE - Manufacturing method of fuel cell assembly.    ADVANTAGE - The cut is formed between the side level-difference portion and the outside step portion, while adjoining. The inside side level-difference portion is easy to isolate from the outside step portion. The inner side level-difference portions are easy to move. The number of processes is reduced, and the fuel cell assembly is manufactured at lower-cost in a short time.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the fuel cell assembly. (Drawing includes non-English language text)    Rubber sheet (40)    Polyethylene-terephthalate film (50)    Rubber sheet structure (51)    Sealing element precursor (52)    Supply roll (90)
NOVELTY - Cyclic process for catalytically converting a solid particulate biomass material, comprises: (i) a biomass conversion cycle comprising contacting a stream of solid biomass particles with a fluidized catalyst bed; and (ii) a catalyst regeneration cycle comprising contacting the fluidized catalyst bed with an oxygen containing gas at a temperature of 500-800 degrees C.    USE - The process is useful for catalytically converting a solid particulate biomass material (claimed) and small-scale operation of biomass catalytic cracking.    ADVANTAGE - The process: is suitable for lab scale and pilot plant operation, as well as for small-scale commercial operation; is suitable for simulating a continuous biomass catalytic cracking process.    DESCRIPTION OF DRAWING(S) - The figure illustrates a sectional view of a fluid bed reactor.    Reaction feed fluidizer (30)    Removable top head (32)    Heat source (33)    Inlet (34)    Outlet (35)
NOVELTY - Manufacture of fine coal fuel involves crushing wooden construction waste material and coppiced timber in the shape of half-split chopsticks by crusher.    USE - Manufacture of fine coal fuel used for cement generation and thermal power generation in central institute of electric power industry.    ADVANTAGE - The fine coal fuel is efficiently manufactured.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing apparatus of fine coal fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows the apparatus of fine coal fuel.    Crusher (2)    Water tank (4)    Spherical rotational flow hot-air-drying furnace (5)    Roller mill crusher (6)
NOVELTY - A fluorescent substance is cerium-and-erbium-doped yttrium-aluminum-gallium oxide.    USE - Fluorescent substance is used for light source of methane gas sensors (claimed).    ADVANTAGE - The fluorescent substance improves methane gas-detecting efficiency of sensor. Since luminescence peak of fluorescent substance shifts to the absorption wavelength side of methane gas, power consumption is reduced.    DETAILED DESCRIPTION - A fluorescent substance is cerium-and-erbium-doped yttrium-aluminum-gallium oxide having composition of formula: Y3(Al,Ga)5O12:Ce3+,Er3+. An INDEPENDENT CLAIM is included for light source of methane gas sensor.
NOVELTY - A catalyst is formed by carrying platinum, ruthenium and chlorine to the monoclinic crystal zirconium oxide carrier which has specific surface area of 2-60 m2/g. The catalyst is used for carrying out oxidation removal of the methane in the waste gas containing sulfur oxide.    USE - Catalyst is used for oxidation removal of methane in waste gas containing sulfur oxide.    ADVANTAGE - The catalyst has excellent resistance with respect to activity inhibition, high methane oxidation activity with reduced usage-amount of expensive noble metal, and economical.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of catalyst, which involves carrying out oxidation removal of methane in waste gas containing sulfur oxide, and impregnating solution containing platinum, ruthenium, and free-chlorine ion with monoclinic crystal zirconium oxide carrier.
NOVELTY - Producing a composite component, comprises either: digesting waste fibrous material through an anaerobic digester to produce digested biomass, wet-mat forming and cold-pressing the digested biomass, and drying the formed wet-mat under heat and pressure to produce a composite component; or digesting waste fibrous material through an anaerobic digester to produce digested biomass and liquid effluent, wet-mat forming and cold-pressing a composition comprising digested biomass and liquid effluent, and drying the formed wet-mat under heat and pressure to produce a composite component.    USE - The method is useful for producing a composite component (claimed) which is useful for producing aligned-fiber cement composite that is used as or is formed into a three dimensional shape for roof or wall panels.    ADVANTAGE - The method provides composite components: in the absence of resins (claimed) or without the need of waxes, sizing components or earthworms; that are less susceptible to warping and show higher resistance to mold, fungal and bacterial attack; and that have increased water-repellency, improved strength, and can be molded in any shape.
NOVELTY - Trifunctional bimetallic catalyst comprising heteropolyacid (HPA) in the form of monomer, an IA or IIA group element (Z), a VIIB or VIIIB group metal (M1) and a IB or IIB group metal (M2) is new.    USE - The trifunctional bimetallic catalyst is useful for the conversion of lignocellulosic material into low oxygenated biofuel at 500 degrees C, preferably 400-470 degrees C (all claimed).    ADVANTAGE - The biofuel is abundant and easily accessible and is very rich in carbon. This catalyst is economical to prepare, and reduces the environmental pollution.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparing the trifunctional bimetallic catalyst; and    (2) converting a lignocellulosic material into low oxygen biofuel comprising mixing the lignocellulosic material consisting of crushed wood and catalyst to obtain a mixture containing the crushed wood (1-20 g, preferably 10 g) and catalyst (0.001-2 (preferably 1) g), heating the mixture under hydrogen to obtain heterogeneous mixture containing a liquid consisting of water and organic molecules and a solid consisting of wood and catalyst, distilling the liquid to obtain a liquid consisting of an aqueous phase and an organic phase, where the organic phase contains aromatic oxygenated molecules and aromatic or non-aromatic, saturated or unsaturated hydrocarbon mixture containing oxygen content ( less than or equal to 5%, preferably 3.5%%) and octane content (90-120).
NOVELTY - A nozzle with a biochemical tank, relating to the technical field of sewage treatment, comprising a water storage tank, the water storage tank is provided with partition wall, wherein the reservoir is a rectangular structure, the isolation wall divides the reservoir divided purifying area, wherein each purification size are the same, the upper part of each partition wall are provided with vent-pipe, the vent-pipe each are the same size, the same shape. The utility model structure is reasonable, the operation is simple and the using effect is obvious.
NOVELTY - Producing mono-alcohols from glycols involves: a) providing a biomass derived glycol feed; b) partially hydrogenating the glycol feed with a hydrogenation catalysts to produce a mono-alcohol, where the hydrogenation reaction occurs at a temperature and pressure that selectively deoxygenates one of the two hydroxyls; c) isolating at least one mono-alcohol; d) recycling unreacted glycol to (a); and e) blending the mono-alcohol in a fuel.    USE - For producing mono-alcohols as fuel blendstocks from glycols (claimed).    ADVANTAGE - The hydrotreating processes are selectively convert glycols to mono-alcohols that can be blended as biofuels. The commercial hydrotreating catalysts such as cobalt molybdenum (CoMo) or nickel molybdenum (NiMo), can selectively convert glycols to mono-alcohols. The method increases mono-alcohol selectivity and catalyst life.
NOVELTY - Integrated process for the conversion of a ligno-cellulosic biomass feedstock comprised of lignin and carbohydrates, involves pretreating the ligno-cellulosic biomass feedstock with treatment water to create a pre-treated ligno-cellulosic biomass feedstock; converting the carbohydrates of the pre-treated feedstock into carbohydrate conversion products e.g. alcohols; charging the lignin; converting at least a portion of the lignin of the pre-treated feedstock into lignin conversion products by contacting lignin with hydrogen; and removing the lignin conversion products.    USE - For conversion of ligno-cellulosic biomass feedstock comprised of lignin and carbohydrates into lignin conversion products (claimed).    ADVANTAGE - The continuous lignin conversion process provides high yields i.e. recovers 80% of the available lignin in the feedstock as usable products.    DETAILED DESCRIPTION - Integrated process for the conversion of a ligno-cellulosic biomass feedstock comprised of lignin and carbohydrates, involves pretreating the ligno-cellulosic biomass feedstock with treatment water which includes steam explosion to create a pre-treated ligno-cellulosic biomass feedstock; converting at least a portion of the carbohydrates of the pre-treated ligno-cellulosic biomass feedstock into carbohydrate conversion products selected from alcohols, polyols, glucans, gluco-lignins and cellulose; charging the lignin from the ligno-cellulosic biomass feedstock into a lignin conversion reactor having a lignin conversion pressure via a stream comprised of lignin from the ligno-cellulosic biomass feedstock; converting at least a portion of the lignin of the pre-treated ligno-cellulosic biomass feedstock into lignin conversion products by contacting the lignin with hydrogen in the presence of a first catalyst at a lignin conversion temperature; and removing the lignin conversion products from the lignin conversion reactor.
NOVELTY - Method for producing a saccharification product, involves treating the starting material derived from potato tubers with secretase solution of a filamentous fungi having a highly resolving cell-wall containing a hydrolytic enzyme.    USE - The method is useful for preparing saccharification product which is used in preparation of liquid fuel.    ADVANTAGE - The method can hydrolyze efficiently.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method (M2) for preparing alcohol, which involves performing alcoholic fermentation of the saccharide obtained in the above-mentioned method (M1).
NOVELTY - A zeolite film complex comprises CHA-type aluminosilicate zeolite. An X-ray diffraction pattern is obtained by irradiating zeolite film to film surface using X-rays, the peak intensity near 2( theta ) of 17.9 degrees having value less than 0.5 times the peak intensity near 2( theta ) of 20.8 degrees , and the peak intensity near 2( theta ) of 9.6 degrees having value 2-4 times the peak intensity near 2( theta ) of 20.8 degrees , and the zeolite film being formed on an inorganic porous support.    USE - Zeolite film complex is used for transmitting and separating highly permeable components from gas mixture or liquid mixture containing components.    ADVANTAGE - The zeolite film complex has excellent chemical resistance, heat resistant, stability, oxidation resistance, pressure resistance and separation of gaseous mixture and liquid compound with high separation factor, and high wet heat stability. The separation of gaseous mixture using zeolite film complex, is highly efficient and economical with low energy consumption and high purity.    DETAILED DESCRIPTION - A zeolite film complex comprises CHA-type aluminosilicate zeolite. An X-ray diffraction pattern is obtained by irradiating zeolite film to film surface using X-rays, the peak intensity near 2( theta ) of 17.9 degrees having value less than 0.5 times the peak intensity near 2( theta ) of 20.8 degrees , and the peak intensity near 2( theta ) of 9.6 degrees having value 2-4 times the peak intensity near 2( theta ) of 20.8 degrees , and the zeolite film being formed on an inorganic porous support. The zeolite film complex is used for transmitting and separating highly permeable components from gas mixture or liquid mixture containing components.
NOVELTY - Preparation (P1) of isoidide from isosorbide, involves subjecting an aqueous solution of isosorbide to epimerization in the presence of hydrogen under the influence of a catalyst comprising ruthenium on a support, at a starting pH of greater than 7.    USE - For the preparation of isoidide from isosorbide and glucose (claimed) which is used as a building block for making polymers such as polyesters.    ADVANTAGE - The process is economical; can be conducted using a relatively low hydrogen pressure, and leads to a desired distribution of epimers, favoring isoidide over isomannide and isosorbide; and produces isoiodide in good yields in a more moderate reaction condition, and avoids side reaction which leads to undesirable mass loss as a result of hydrodeoxygenation.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) use of a catalyst comprising ruthenium on a carbon support, in the epimerization of isosorbide into isoidide; and    (2) preparation (P2) of isoidide from glucose, involving subjecting glucose to hydrogenation to form sorbitol, subjecting the sorbitol to dehydration to form isosorbide, and subjecting isosorbide to catalyzed epimerization into isoidide, using a catalyst comprising ruthenium on a carbon support in accordance with the process (P1).
NOVELTY - A system for continuous gasification of biomass feedstock comprises fuel conditioning zone, gasification zone containing controllable system for introducing air into the biomass, and char cooling area having gas capturing system for recovering gas released by the char cools. The carbon content of char is adjusted by varying one or more of feed rate of fuel and air into the system.    USE - System for continuous gasification of biomass feedstock e.g. high-ash feedstock and animal manure (all claimed) is used for electricity production.    ADVANTAGE - The system enables continuous gasification of biomass feedstock with high quality.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass gasification system.
NOVELTY - An oil (344) is extracted from plant containing oligosaccharides and/or polysaccharides which are converted to monosaccharide. A portion of obtained monosaccharide is fermented to form oil and biochemical. A portion of fermented product is separated to obtain oil product having 0.05-2 wt.% free fatty acid.    USE - Manufacture of oil product for manufacture of alcohol such as ethanol. Uses include but are not limited to animal feed supplement, industrial application, biodiesel production and human grade edible oil.    ADVANTAGE - The oil product is produced at high yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for oil product comprising 0.05-2 wt.% fatty acid and 10 wt.% or less alcohol esters.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram for manufacture of oil product.    Corn (302)    Fermentation system (322)    Beer (326)    Oil (344)    Ethanol (356)
NOVELTY - A recombinant photoautotroph or photoheterotroph microorganism that produces 1-butanol, is new, where the alcohol is produced through a malonyl-coenzyme A (CoA) dependent pathway.    USE - The recombinant photoautotroph or photoheterotroph microorganism is useful for producing 1-butanol (claimed) which is used as biofuel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing an alcohol, which involves (a) providing the microorganism, (b) culturing the microorganism in the presence of conditions suitable for the conversion of the substrate alcohol, and (c) purifying the alcohol.
NOVELTY - An isolated polypeptide having cellulolytic enhancing activity, is new, where the polypeptide comprises an amino acid sequence exhibiting at least 90% sequence homology to amino acid residues at position 26-253 of a 253 amino acid sequence (SEQ ID NO: 2) fully defined in the specification.    USE - The isolated polypeptide is useful for degrading a cellulosic material, producing a fermentation product and fermenting a cellulosic material (all claimed). The cellulosic material includes corn stover, corn fiber, corn cob, orange peel, rice straw, wheat straw, switch grass, Miscanthus and bagass.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method (M1) for degrading a cellulosic material, involves treating the cellulosic material with an enzyme composition in the presence of the polypeptide;    (2) method (M2) for producing a fermentation product, involves (a) saccharifying a cellulosic material with an enzyme composition in the presence of the polypeptide, (b) fermenting the saccharified cellulosic material with one or more fermenting microorganisms to produce the fermentation product, and (c) recovering the fermentation product from the fermentation; and    (3) method (M3) of fermenting a cellulosic material, involves fermenting the cellulosic material with one or more fermenting microorganisms, where the cellulosic material is saccharified with an enzyme composition in the presence of a polypeptide.
NOVELTY - A method (M1) for enzymatic hydrolysis of cellulose using whole cell cultures of cellulase-producing microbes involves the following steps: a) cultivating the cellulase-producing microbes at a first temperature to produce cellulases; b) deactivating the cellulase-producing microbes at a second temperature, where the second temperature is at a higher temperature level than the first temperature; and c) hydrolyzing cellulose to produce glucose using the cellulases.    USE - For enzymatic hydrolysis of cellulose using whole cell cultures of cellulase-producing microbes to form product in the form of fermentation product, co-product or enzyme (claimed). The cellulose is also used in the large scale production of fuels, chemicals, biodiesels, and biofuels.    ADVANTAGE - The method promotes the cellulose hydrolysis by extracellular cellulases resulting in continuous hydrolysis of cellulose to glucose without the risk of glucose being consumed by the deactivated cells. The cellulose is low cost and sustainable and provides environmental, economical and social benefits. The enzymatic hydrolysis eliminates the use of large amount of chemical, achieves high glucose yield and avoids the formation of inhibitory by-products. The method is cost-effective; and provides a one pot, 2-step process for the enzymatic hydrolysis of cellulose using whole cell cultures. The whole process is able to be conducted in one pot without the requirement of any separation steps. In the method, whole cell cultures are utilized to catalyze the hydrolysis of cellulose without the requirement of isolating the cellulase enzymes from the broth. The enzyme production and cellulose hydrolysis can be conducted in 1 pot by 2-steps by simply changing the temperatures in the pot (and optionally adding cellulose to the reaction broth).
NOVELTY - A biomass fuel comprises portion or whole of fuel containing raw material derived from coconut, and has cylindrical shape.    USE - Biomass fuel is source of industrial resources used for biomass combustion apparatuses, such as electricity generation.    ADVANTAGE - The biomass fuel is economical, has excellent heat emitting property and achieves carbon neutrality easily.
NOVELTY - Potassium chloride and sulfuric acid are fine ground at 0-100 degrees C to produce hydrogen chloride and composition comprising potassium hydrogen sulfate. The obtained composition and potassium chloride are fine ground continuously at 0-100 degrees C, to obtain hydrogen chloride and potassium sulfate.    USE - Manufacture of hydrogen chloride and potassium sulfate based salt(s) used as fertilizer.    ADVANTAGE - The method produces environmentally-friendly hydrogen chloride and potassium sulfate based salt(s).    DESCRIPTION OF DRAWING(S) - The drawing shows a flow sheet for producing hydrogen chloride and potassium sulfate based salt(s)
NOVELTY - A fuel oil comprises biofuel as main component and alkyl ester of caprylic acid, capric acid, myristic acid, palmitic acid, stearic acid and/or oleic acid, as effective pour depressant.    USE - Fuel oil (claimed).    ADVANTAGE - The fuel oil has improved cold temperature flow characteristics.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for usage of alkyl ester.
NOVELTY - The livestock manure treatment system comprises a processing unit, in which a livestock manure is passed, for removing bacteria and fungi in manure, suppressing emission of gases and odors, reducing smell of manure and promoting oxidation in the primary manure mixed with 0.01-1 wt.% of vinegar, where the manure is placed in a set of micro-organisms mixed batches including Bacillus subtilis GU01. The processing unit is provided with an activation tank. A solid-liquid division part removes activated sludge in the manure.    USE - The system is useful for treating livestock manure (claimed).    ADVANTAGE - The system treats the livestock manure in a less time, and reduces the bad smell even when the livestock excretions are in the acid state.    DETAILED DESCRIPTION - The livestock manure treatment system comprises a processing unit, in which a livestock manure is passed, for removing bacteria and fungi in manure, suppressing emission of gases and odors, reducing smell of manure and promoting oxidation in the primary manure mixed with 0.01-1 wt.% of vinegar, where the manure is placed in a set of micro-organisms mixed batches including Bacillus subtilis GU01 having colony-forming unit of 1x 108, the treatment process includes cooling, condensation, separation, aging, filtering and then evaporating and pyrolyzing liquid in the manure, and extracting including from leaf, stem, root, berries and plant flower. The processing unit is provided with an activation tank. A solid-liquid division part removes activated sludge in the manure.
NOVELTY - A primary gas mixture is received and separated into component containing major amount of hydrogen gas and component containing mixture of remaining gas. The component containing mixture of remaining gas is channeled into an apparatus, a system or composition for conversion into electric power. Thus, gas source is generated for conversion into electric power.    USE - Method for generating gas source for conversion into electric power (claimed).
NOVELTY - Improved substrate (S1) is prepared using raw materials comprising straw, manure, mushroom residue and sludge.    USE - The improved substrate is useful for slope (claimed), and construction of greening of road slope and urban landscaping.    ADVANTAGE - The improved substrate is environmentally-friendly.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for preparing the substrate, involves obtaining 1-15 cm straw, manure, mushroom residue and sludge, uniformly mixing the raw materials, stacking, adding water and ferrous sulfate solution, stacking, maintaining good ventilation condition, covering soil or mud paste on the stacking surface, drying, crushing and sieving to obtain finished product; and    (2) substrate (S2) comprising 10-30 wt.% improved substrate, 0-25 wt.% fiber, 50-80 wt.% planting soil, and 0-5 wt.% other material, where the other material comprises compound fertilizer, organic fertilizer and microbial fertilizer, water retention agent, caking agent, and pH adjusting agent.
NOVELTY - A negative pressure device comprises a guide drip device (1), a balance pipe joint (2), a nitrogen pipe interface, an oil discharging joint, a balance valve (3) connected to an ammonia gas pipeline, a nitrogen valve (4) connected to a nitrogen gas source, a watering pipe, and a negative pressure device guide drip valve (5) connected to the watering pipe, an oil spraying guide pipe, an oil-spraying valve connected to a waste oil recycling slot.    USE - A negative pressure device for outlet oil way of ammonia synthesis.    ADVANTAGE - The device is safe and environment-friendly, has simple structure and high working efficiency, and ensures heat exchange effect of an ammonia-cooling device.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a negative pressure device.    Guide drip device (1)    Balance pipe joint (2)    Balance valve (3)    Nitrogen valve (4)    Negative pressure device guide drip valve (5)
NOVELTY - Separating mixed 4C, comprises separating butene and butane from mixed 4C through extractive distillation process using an extraction agent to obtain 3C containing butadiene, alkyne and isobutene, where the mixed 4C contains n-butane, iso-butane, 1-butylene and 2-butylene, separating the mixed 3C to obtain iso-butane, 1-butylene and 2-butylene and the byproduct of crude n-butane through the extractive distillation process using an solvent in a non clear-clear separation method, and removing extracted crude iso-butane from 4C.    USE - The method is useful for separating mixed 4C containing n-butane, iso-butane, 1-butylene and 2-butylene (claimed).    ADVANTAGE - The method allows separation of mixed 4C containing n-butane, iso-butane, 1-butylene and 2-butylene in an energy efficient and economical manner.    DETAILED DESCRIPTION - Separating mixed 4C, comprises separating butene and butane from mixed 4C through extractive distillation process using an extraction agent to obtain 3C containing butadiene, alkyne and isobutene, where the mixed 4C contains n-butane, iso-butane, 1-butylene and 2-butylene, separating the mixed 3C to obtain iso-butane, 1-butylene and 2-butylene and the byproduct of crude n-butane through the extractive distillation process using an solvent in a non clear-clear separation method, removing extracted crude iso-butane from 4C, pre-removing butane at a pressure of 0.3-0.7 MPa through steam heating using a heating device, separating 1-butylene and 2-butylene by stripping, extracting and separating, isobutane and n-butane at a pressure of 0.3-0.8 MPa from 4C. An INDEPENDENT CLAIM is included for a device for separating mixed 4C, comprising heater as a heat source and a butene tower kettle reboiler as a pre-debutanizer kettle reboiler.
NOVELTY - Refining crude comprises taking lenalidomide, adding isopropyl alcohol-water solution, heating to dissolve, adding activated carbon and nano ceramic powder, filtering, cooling, crystallizing and drying.    USE - Method for refining crude (claimed).    ADVANTAGE - The method has low toxicity, high safety and simple technique with high product content and refining yield.
NOVELTY - Treatment of flocculate of heparin sodium enzymatic hydrolysate involves preparing heparin sodium enzymatic hydrolysate, adding 3-5 wt.% flocculant into the prepared heparin sodium enzymatic hydrolysate, stirring uniformly for 15-30 minutes in rate of 100-150 rpm, maintaining the resultant solution for 5-6 hours at room temperature, performing centrifugal filtering in a centrifugal machine for 10 minutes in rate of 2000-3000 rpm, and removing solid impurities.    USE - Treatment of flocculate of heparin sodium enzymatic hydrolysate (claimed).    ADVANTAGE - The method efficiently enables treatment of flocculate of heparin sodium enzymatic hydrolysate, by a simple process.
NOVELTY - The furnace has a hopper that is arranged below coal feeding device (1) and is connected with rotary stocker. The rotary stocker is connected with coal distributor. The coal distributor is connected with discharge pipes through sleeves. A plate is arranged at upper portion of coal distributor. The lower end of each discharge pipe is connected with straight pipe through moving sleeve. A refractory material masonry is arranged in furnace case. A high material level measuring hole, low material level measuring hole and observation hole are arranged on control chamber.    USE - Coal pyrolysis furnace.    ADVANTAGE - The production efficiency can be improved, and the production cost can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the coal pyrolysis furnace.    Coal feeding device (1)    Combusting coal pre-heating device (2)    Pre-heating furnace device (3)    Focus modifying device (5)    Coke dry quenching device (6)
NOVELTY - The device comprises a ball heating furnace (1), heat carrier biomass ball dosing machine (2), mobile pyrolysis material layer (4), moving-bed pyrolyzing furnace unit (5) and a biomass storage bin (6) that are connected together. The heat transfer medium is inert solid ball. The heat transfer process of the inert solid heat carrier is radiation heat transfer and contact heat transfer.    USE - Solid heat-carrying moving bed biomass pyrolysis device.    ADVANTAGE - The pyrolyzed coal mixed gas is avoided, so as to improve the coal quality. The pyrolysis gas as fly ash content is greatly reduced. The power consumption is reduced. The tar dust content is reduced. The operation cost is reduced. The system heat efficiency is greatly improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the solid heat-carrying moving bed biomass pyrolysis device. (Drawing includes non-English language text)    Ball heating furnace (1)    Heat carrier biomass ball dosing machine (2)    Mobile pyrolysis material layer (4)    Moving-bed pyrolyzing furnace unit (5)    Biomass storage bin (6)
NOVELTY - The cracker has an ash room (4) that is arranged at the lower portion of the combustion chamber (1). The cracking chamber (2) is connected with the combustion chamber. The movable sealing door (8) is provided at the upper portion of the pyrolysis chamber (3). The material loading plate is connected between the combustion chamber and the cracking chamber. A fire grate (7) is connected to the combustion chamber. The lifting guide rail (20) is installed on the ignition unit. One end of the non-metal soft tube is connected to the air outlet of the gas storage chamber (18).    USE - Fire height adjustable biomass cracker used for boiler.    ADVANTAGE - The height of the fire port can be adjusted freely. The application range of the cracker is improved. The accuracy of the cracker can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fire height adjustable biomass cracker.    Combustion chamber (1)    Cracking chamber (2)    Pyrolysis chamber (3)    Ash room (4)    Fire grate (7)    Movable sealing door (8)    Gas storage chamber (18)    Lifting guide rail (20)
NOVELTY - The biogas digester has a regulating wheel (6) that is arranged in the middle of the biogas digester and connected with a regulating rod (5). Supporting wheels (2) are arranged outside the biogas digester. A straw tank (7) is installed with a conveying belt (3), which bypasses the regulating wheel and the supporting wheels. A handle (1) is installed on the supporting wheel on one side.    USE - Special straw biogas digester.    ADVANTAGE - Charging and discharging are easy and carried out continuously, thus biogas is generated in a balanced manner and floating and crusting phenomena are not generated.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of the structure of a special straw biogas digester.    Handle (1)    Supporting wheel (2)    Conveying belt (3)    Regulating rod (5)    Regulating wheel (6)    Straw tank (7)
NOVELTY - Preparing compound enzyme system comprises activating Trichoderma reesei or its derived strain, preparing spore suspension from activated Trichoderma reesei or its derived strain, inoculating the spore suspension into a seed culture medium and then culturing in a shaking table, inoculating a seed culture medium inoculated with the Trichoderma reesei strains or its derivative into a fermentation culture medium using microcrystalline cellulose and corn core as carbon source in a mixing ratio of 1:4, and performing in a fermentation tank culture.    USE - The method is useful for preparing compound enzyme system that is useful for high-efficient degrading lignocellulose (claimed).    ADVANTAGE - The method economically prepares the compound enzyme system with less pollution.    DETAILED DESCRIPTION - Preparing compound enzyme system comprises activating Trichoderma reesei or its derived strain, preparing spore suspension from activated Trichoderma reesei or its derived strain, inoculating the spore suspension into a seed culture medium and then culturing in a shaking table at 28-30 degrees C and rotating speed of 17-200 revolutions per minute for 24-36 hours, inoculating a seed culture medium inoculated with the Trichoderma reesei strains or its derivative into a fermentation culture medium using microcrystalline cellulose and corn core as carbon source in a mixing ratio of 1:4, and performing with fermentation tank culture.
NOVELTY - Heating using organic waste comprises adding organic waste collected from daily life into a sealed fermentation tank to produce marsh gas, mounting a pressure sensor in the fermentation tank, setting relays at the outlet, where the pressure sensor and the relay is connected with the single chip, which controls marsh gas outflow according to the signal passed from the pressure sensor through relay, and using the produced marsh gas for heat boiler heating.    USE - The method is useful for heating using organic waste (claimed).    ADVANTAGE - The method reuses domestic waste ; utilizes fermentation tank to produce marsh gas, which is used for heating; and is environmentally friendly.
NOVELTY - Preparing marsh gas comprises taking a peat as raw material, drying the peat to crush into 6-100 meshes and then sieving to obtain peat fine powder, adding 10 g of enzyme liquid with the obtained peat powder to enzymolysis at 20-60 degrees C for 1-6 hour and then adding 10-30% of active sludge with water to adjust solid-liquid ratio of 1:5-1:20, adding sodium hydroxide solution with the mixed liquid to adjust pH value of 6.5-7.5 and then anaerobic fermenting at 30-55 degrees C for 1-30 days and then stirring and performing yeast fermentation in saturated salt water drainage and collecting methane.    USE - The method is useful for preparing marsh gas, preferably methane (claimed).    ADVANTAGE - The method economically prepares marsh gas by utilizing fossil energy in environment-friendly manner.
NOVELTY - A membrane electrode preparing method involves adopting a platinum-ruthenium black catalyst and a platinum black catalyst respectively as a cathode catalyst and an anode catalyst, and isopropyl alcohol and distilled water as dispersing agents, mixing materials to form catalyst slurry, adding catalyst slurry under inert gas atmosphere, dispersing mixture ultrasonically, fixing PTFE film as a transfer medium between heating ultrasonic spraying system of negative pressure sucking disk, controlling temperature and naturally drying to form a catalyst layer.    USE - Method for preparing membrane electrode that is utilized for manufacturing direct methanol fuel cell.    ADVANTAGE - The method enables preparing membrane electrode with high-efficiency.    DETAILED DESCRIPTION - A membrane electrode preparing method involves adopting a platinum-ruthenium black catalyst and a platinum black catalyst respectively as a cathode catalyst and an anode catalyst, and isopropyl alcohol and distilled water as dispersing agents, mixing materials to form catalyst slurry, adding catalyst slurry under inert gas atmosphere, dispersing mixture ultrasonically, fixing PTFE film as a transfer medium between heating ultrasonic spraying system of negative pressure sucking disk, controlling temperature and naturally drying to form a catalyst layer. The resultant product is set on the negative pressure sucker heater, followed by heating resultant product to 50-80 degrees C, adding Nafion (RTM: Perfluorosulfonic acid-PTFE copolymer) solution on one side of the proton exchange membrane, applying pressure, heating resultant product to 120-135 degrees C for 2-5 minutes to obtain a catalyst layer and a complex compound, and arranging hydrophobic treated carbon product on two sides of the composite to obtain a membrane electrode.
NOVELTY - A kind of Mycelial Pellet as carrier aerobic denitrification reactor, relating to the technical field of water treatment, comprising a closed reactor, the bottom of the reactor with aeration head, a water inlet pipe, water outlet pipe are respectively provided with the upper and lower side of the reactor is provided with biomass, said biomass carrier is mycelium, mycelium film is aerobic denitrifying bacteria, the reactor can make the nitrobacteria and the aerobic denitrifying bacteria under the full period aerobic condition, at the same time, good for the growth and propagation to stabilize the simultaneous nitrification and de-nitrification effect, using bioflocculant with mycelium pellet as carrier, which can solve power aerobic denitrifying bacteria, is hard to form superior bacteria cause a large loss caused by the whole system stable operation period is short, the key long-term stable running of the whole reactor system of the system.
NOVELTY - This utility model claims a comprehensive biochemical filter tank, comprising a tank body, a tank body middle part is equipped with a guide cylinder, the four sides of the guide cylinder is uniformly provided with a plurality of the inner part is filled with aeration biological filter tank for biological ceramsite, an aeration biological filter tank is suspended is set with the upper part of the anaerobic area, each aeration biological filter tank is connected with the water tank is set with water outlet pipe is connected with the upper part on the outer side wall of the tank body, the water tank is connected with the back washing pipe and aeration biological filter tank. By setting the adjusting water tank, when working, under the control of the controller and a valve, the filter set to the adjusting water tank, and wherein a number of the first aeration biological filter tank through a back washing providing reverse washing water, the reverse washing aeration biological filter tank, a water supply mode of the back washing water to recycle use of the back-flushing water, reduces the loss of the back-flushing water, and this utility model can realize uninterrupted continuous operation, improves the sewage processing capability. This utility model can be applied to sewage treatment.
NOVELTY - The utility model claims a biologic trickling filter device for sewage treatment, comprising a main body (4), the main body (4) is connected with mesh filler supporting frame (6), a filler support frame (6) is filled with filling material (5), filling material (5) above the main body cavity is water chamber (10), a filler support frame (6) is provided with a water chamber (11), a water spraying chamber (10) is provided with a ventilation port (14) and a sewage inlet (2), a sewage inlet (2) is connected with a water spraying chamber (10) and a second nozzle (3), the water chamber (11) is provided with a sewage outlet (8), wherein the ventilating port (14) is provided with a first ventilating device (1), a water chamber (11) corresponding to the main body (4) of the side wall is provided with a second ventilating device (7). This utility model claims a kind of ventilation efficiency of the biologic trickling filter device for sewage treatment.
NOVELTY - A kind of pressure adding alkali ammonia system, comprising a residual ammonia water, ammonia, ammonia water tank and a vacuum system, the outlet of the residual ammonia water tank orderly by the first pump, a heat exchanger is connected to the inlet of the outlet of the ammonia evaporation tower top part and pre-heater and connected to the finished product ammonia water tank through the pump and a cooler, the finished product ammonia water is connected with a vacuumizing system, a waste water outlet of the ammonia evaporation tower is connected to the heat exchanger by the third pump, wherein it further comprises a slot and a tail gas recycling device, a pipeline of alkali liquid in the alkali liquid groove by metering pump at the same time, adding to the rest ammonia water inlet and outlet, the residual ammonia water tank and vacuum-pumping system at the same time is connected to the tail gas recycling device. This utility model change is the most simple process, less investment, improves the pressure ammonia evaporation waste water, the research process of decompressing and distilling, which is good for pushing the popularization and application of decompressing distillation process.
NOVELTY - A kind of new-type aerobic composting reaction device, belonging to the field of environmental equipment field. Aerobic composting reaction device is composed of air compressor through air inlet pipe is connected with the bottom of the aerobic composting reactor is connected with the aerobic compost reactor is provided with a stirrer, the upper part is provided with collecting port, the gas collecting port is connected with the exhaust pipe, the tail gas absorbing tank, is formed from a mixture of sludge and biomass charcoal stacking layer stacking in the aerobic composting reactor. Aerobic composting reaction device provided with a programmable logic controller control panel operating state of real time monitoring device. This utility model device for composting organic matter content is high, the content of heavy metal is low, the input and can effectively improve the soil fertility of the soil, and can accelerate the aerobic composting rate and improves combining efficiency, reduces the bad smell.
NOVELTY - The utility model claims a fertilizer production device, especially a kind of high efficiency synchronous slow release special fertilizer for wheat comprises a use of fast sulphur melting machine, comprising an upper end enclosure of the shell, is set with a skirt on a shell body, the upper end socket is provided with a feeding port, the lower end of the shell is provided with a cleaning opening, wherein the side wall of the shell body is provided with a steam inlet and a steam outlet, a discharge port, a shell body provided with two ends of the heating coil, heating coil pipe are respectively connected with the steam inlet and steam outlet, and the inner wall of the shell is provided with a heating water channel, a heating water path is spiral, the inlet end of the heating channel is connected with the steam inlet through the inlet three-way, the outlet end of the heating passage is connected with the steam outlet through the outlet. The method for using inner and outer two layers of heating coil sulphur fast fuser, simple structure, high heat efficiency, can be produced continuously, it saves energy.
NOVELTY - A kind of processing device for garbage fermentation, comprising a fermentation device and storage device, the fermentation device comprises an annular water tank, a fermenting tank, a sedimentation tank, a transparent glass cover, the air storage device comprises a gas storage tank, a movable cover, a shaft and a shaft sleeve; Using this utility model of garbage fermentation process device for processing domestic garbage, the treatment cost is low, there is no pollution, and it is convenient to popularize.
NOVELTY - This utility model claims a kind of dry biomass biogas reaction device, comprising a dry anaerobic fermentation tank and a dry anaerobic fermentation tank is connected with the feeding tank and a discharging port, and an outer wall of the dry anaerobic fermentation tank provided with increasing heat preservation device, the tank is provided with a spiral stirrer, a spiral stirrer is fixed through the stirrer shaft, a stirrer of the tank body to two ends of the rotating shaft in the axial direction is provided with a rotating handle, the feed box is in turn set with the first motor through the feeding switch is externally connected with a feeding screw driver and feeding port and the dry anaerobic fermentation tank is connected with the inlet of the outlet of the dry-type anaerobic fermentation tank are provided with the second motor through the discharging switch and a discharging screw driver and the discharge hole are connected with the air inlet box is connected with the dry-type anaerobic fermentation tank, and then the marsh gas outlet, a gas conveying pipeline of the gas tank and is equipped with a valve of the cooker are connected with each other. This utility model can improve the utilization efficiency of the reaction device at the same time to solve the rural area waste of biomass energy.
NOVELTY - This utility model claims a marsh gas generating device, comprising an inner container, a sealing liner of a soft tank is provided with an exhaust nozzle and the feed opening on the top of the inner container is set with waste outlet, an exhaust nozzle, a feed port and a waste discharge port are respectively connected with the inner part of the inner container at the bottom of the inner container, the biogas generating device further comprises a shell, the shell is a hard cylindrical shell shape and the inner outline shape corresponding to the matching, a shell for containing the inner container, and the inner container is provided with the bottom of the shell of the waste outlet corresponding to the through-hole, a waste outlet of the inner container through the bottom of the shell through hole extends outwards. This utility model has simple structure, high reliability, low manufacturing cost, convenient to move and can waste can automatically discharge, convenient operation, light labour intensity, high safety, strong practicability and so on.
NOVELTY - The invention relates to a hydrogen generator producing it from water, by using microwaves, and to an autonomous hydrogen-producing station using the same. According to the invention, the hydrogen generator comprises a microwave generator (A) with simple or multiple waveguide (1) and magnetron (2), and at least one electrolyser (B) with solid electrolyte, coupled with the open end of the waveguide (1) by a horn-antenna (4) containing balls (b) or porous ceramics or corundum particles (b'), in order to convert the water fed thereinto by a nozzle (3) with an electrically-operated valve (5), the electrolyser (B) comprising within a ceramic or metallic tank (6) some porous metallic electrode-plates (7 and 7') made of Ni or stainless steel with Ni, provided with some extensions (h) for electrical connection, fixed in an insulating support (i), between the electrode-plates (7 and 7') there being placed two or three successive layers, as follows: a first insulating layer (m) made of porous ceramic balls, a second semiconductor layer (m') made of silicon carbide and a third conductor layer made of metal powder of Ni or steel with Ni, within the third layer there being placed some thin separating blades (12) of porous ceramics, each of them being plated on its face with a coat (n and n') of porous Ni and fixed in the support (i) in which there is also fixed a micro porous membrane (9) permeable only for the produced Brown gas, and an insulating plate (10) for separating the electric connections of the extensions (h), the so produced Brown gas being collected through an outlet (l) from an electrically insulating cap (11), positioned between the insulating plate (10) and the membrane (9). The hydrogen station uses generators with two horn-antennas (4 and 4') with electrolysers (B and B') coupled to a waveguide (1) opened at both ends and is supplied with electric power produced by a wind turbine (D) or by a solar panel (19).
NOVELTY - This utility model claims a kind of home drinking water to a cylinder type electrolytic hydrogen water generator, comprising a tube, an electrolytic hydrogen generator and split-type base. Electrolytic hydrogen generator is provided with reaction chamber. The horizontal middle part of the reaction chamber is provided with a high-molecular film, the cathode electrode and the anode electrode from the upper and lower clamping macromolecule film. The upper and lower surfaces of the cathode electrode, an anode electrode, pressing a cathode and anode electrode elastic sheet, cathode and anode electrode elastic sheet is respectively connected with the split-type middle part of the base of the annular electrode and punctate electrode wiring. Split-type pedestal is provided with cathode pole conversion switch, and positive and negative direct current power source input switching is transmitted to the cathode electrode and the anode electrode, which is good for removing the ionized layer. This utility model has scientific and reasonable structure of hydrogen water, the rate of the hydrogen, the hydrogen solubility in water, the mass of hydrogen, a device for providing drinking electrolytic hydrogen water well, convenient and safe for the family.
NOVELTY - The utility model claims a power-free printing and dyeing waste water processing system, belonging to the printing and dyeing waste water treatment and energy utilization field. System, adjusting pool is provided with an aeration device, an adjusting pool through a water guide pipe is connected with the anaerobic fermenting tank, the anaerobic fermentation tank is provided with a strain fixed bed, an anaerobic fermentation pool generated by gas-guide tube and gas collecting tank connected with the anaerobic fermenting tank and sludge collecting tank connected with the marsh gas collecting tank is connected with the biogas electric generator set is connected with the marsh gas dehydrating and desulfurizing process and via a gas tube enter into marsh gas; biogas electric generator set are respectively connected with degradation pool and an external load, degradation tank is provided with a water outlet, a degradation tank and the anaerobic fermenting tank; This utility model can effectively by using anaerobic fermentation and a releasing, collecting and utilizing biogas energy for supplying electrolytic degrade electric energy and other electric equipment without power, high efficiency for treating printing and dyeing waste water, at the same time, the structure is simple and the cost is low.
NOVELTY - This utility model claims a kind of controlled release biological compound fertilizer particle, its shape is sphere, including silicate bacteria to prepare core particle, wherein the core particle is set outside the inorganic fertilizer in the middle layer, the middle layer is set outside the humic acid. According to the core particle, inorganic fertilizer in the middle layer, the outer layer of humic acid are in the release agent. Inorganic fertilizer is urea, monoammonium phosphate, potassium sulphate, the utility model is a controlled release biological compound fertilizer particle as the controlled release agent and silicate bacteria as core granules, and urea as a layer, monoammonium phosphate, potassium sulphate and humic acid layer and the outer layer of the fully mixing, melting and uniformly distributed of fertilizer particles, using a controlled release biological compound fertilizer particle can be controlled release nutrient according to the requirement of the plant absorbing nutrient, high utilization ratio of fertilizer.
NOVELTY - The utility model claims a system for treating organic waste material, comprising an arc-shaped treatment tank and a material, the arc-shaped processing tank comprises inlet aerobic zone and the anaerobic zone and aerobic zone, the anaerobic zone is at the bottom of the arc-shaped treatment pool, the anaerobic zone at the two sides are symmetrically provided with an inlet outlet aerobic zone and aerobic zone and the anaerobic zone is connected with the top part of the arc-shaped treatment tank is provided with a gas-guide tube with the arched top and the anaerobic region corresponding to the position of through opening the aerobic zone and the anaerobic zone and aerobic zone outlet at the bottom of the pool is arc-shaped processing tank is provided with a track. This utility model is material acidification is inlet, then into the anaerobic fermentation for preparing biogas section, at the same time, provided with marsh gas compressing refluxing and stirring in anaerobic area and reduces the fermentation blind area and improve the methane yield, fermentation of the type and character of the original is not further limited, at the same time, reduces the operation and the construction cost.
NOVELTY - The utility model claims a marsh gas producing device, especially relates to a kind of anaerobic dry fermentation marsh gas device, belonging to the technical field of new energy. This utility model is composed of a marsh gas fermenting tank and a soft storage bag, a soft storage bag is installed on marsh gas fermenting tank. A main body of the marsh gas fermenting tank is a cylinder, the bottom is , and the top edge is provided with a connected with a soft storage bag of the flange, the flange is provided with a plurality of screw holes. Soft storage bag is a foldable cylinder structure, the a position to the upper part from the storage bag is provided with a plurality of fixed ring, the top of the flexible storage bag is equipped with a blind plate, a blind plate centre is provided with marsh gas discharge port, the bottom edge of the flexible storage bag is equipped with a flange, the flange is provided with a plurality of screw holes. This utility model is simple and practical in structure, can fast and high efficiently dispose organic sewage, and use waste water of formaldehyde resin to produce energy, having low energy consumption, the cost is low, and the production process is clean, environment-friendly and so on.
NOVELTY - Efficient two-phase anaerobic fermentation device comprises a hydrolysis acid production reactor, a high-temperature hydrolysis device and at least one methanogenesis reactor, where a bottom percolate storage chamber of the hydrolysis acid production reactor is connected with the bottom of the methanogenesis reactor; the lower part of the hydrolysis acid production reactor is provided with a cavity stainless cone-shaped bracket with holes; and the bottom of the cone-shaped bracket is connected with the high-temperature hydrolysis device.    USE - The efficient two-phase anaerobic fermentation device is useful for anaerobic digestion of organic wastes.    ADVANTAGE - The device is simple in manufacturing procedure, reasonable in structure, easy in maintenance, high in fermentation efficiency and stable and reliable in performance, and meets the large-scale production requirement.    DETAILED DESCRIPTION - Efficient two-phase anaerobic fermentation device comprises a hydrolysis acid production reactor, a high-temperature hydrolysis device and at least one methanogenesis reactor, where a bottom percolate storage chamber of the hydrolysis acid production reactor is connected with the bottom of the methanogenesis reactor; the lower part of the hydrolysis acid production reactor is provided with a cavity stainless cone-shaped bracket with holes; the bottom of the cone-shaped bracket is connected with the high-temperature hydrolysis device; the methanogenesis reactor is provided with an upper discharge hole and a lower discharge hole; the upper discharge hole and a feed inlet form a self-circulation pipeline; the lower discharge hole of the hydrolysis acid production reactor is connected with a rotary sprayer; the high-temperature hydrolysis device is used for receiving large particle solid separated by the cone-shaped bracket; and solid-liquid separation is carried out by a biogas residue press filter at the outlet.
NOVELTY - Induction smelting of titanium-containing hydrogen storage alloy comprises taking titanium iron manganese material as titanium-containing hydrogen storage alloy raw material; ultrasonic cleaning with dilute hydrochloric acid or dilute sulfuric acid for 5-10 minutes; drying at 10-20 degrees C for 5-40 hours; charging cleaned alloy into calcium zirconate crucible; putting crucible into vacuum induction furnace; performing vacuum evacuation and filling inert gas; vacuumizing; and repeatedly washing for 3-5 times under protection of inert gas or under vacuum conditions.    USE - Induction smelting of titanium-containing hydrogen storage alloy.    ADVANTAGE - The method produces smelted titanium-containing hydrogen storage alloy with low oxygen content, effectively controlled alloy components, and can be easily activated. It provides easy absorption and desorption of hydrogen at room temperature.    DETAILED DESCRIPTION - Induction smelting of titanium-containing hydrogen storage alloy comprises taking titanium iron manganese material (TiFe0.86Mn0.10) as titanium-containing hydrogen storage alloy raw material; ultrasonic cleaning with dilute hydrochloric acid or dilute sulfuric acid for 5-10 minutes; drying in muffle furnace at 10-20 degrees C for 5-40 hours; charging cleaned alloy into calcium zirconate crucible; putting crucible into vacuum induction furnace; performing vacuum evacuation and filling inert gas; vacuumizing; repeatedly washing for 3-5 times under protection of inert gas or under vacuum conditions; controlling heating power rate of vacuum induction melting furnace at 1-50 degrees C/minute; measuring infrared melting zone temperature; adjusting bath temperature at higher than melting point of hydrogen storage alloy at 10-50 degrees C for 10-120 minutes; and adjusting casting direction of crucible for casting titanium-containing hydrogen storage alloy.
NOVELTY - Astilbin is extracted from rhizoma smilacis glabrae by crushing rhizoma smilacis glabrae, screening using 1-40 mesh sieves, adding 40-80 vol.% ethanol aqueous solution to the powder at a ratio of 8-16:1, subjecting to ultrasonic extraction at 26-40 kHz for 0.5-1 hour, heating at 20-50 degrees C for 10-60 minutes, filtering, adding ethyl acetate to the filtrate at a ratio of 1-4:1, extracting for 1-5 hours, adding ethyl acetate to the filtrate, vacuum concentrating at 20-40 degrees C, adding 30-70 vol.% ethanol solution, and concentrating to obtain crude extract.    USE - Method of extracting astilbin from rhizoma smilacis glabrae (claimed).    ADVANTAGE - The method is simple, short, convenient, and environment-friendly; prepares product having less impurity; and has low extracting temperature, high extracting rate, and low energy consumption.    DETAILED DESCRIPTION - Astilbin is extracted from rhizoma smilacis glabrae by crushing rhizoma smilacis glabrae, screening using 1-40 mesh sieves, adding 40-80 vol.% ethanol aqueous solution to the powder at a ratio of 8-16:1, subjecting to ultrasonic extraction at 26-40 kHz for 0.5-1 hour, heating at 20-50 degrees C for 10-60 minutes, filtering, adding ethyl acetate to the filtrate at a ratio of 1-4:1, extracting for 1-5 hours, adding ethyl acetate to the filtrate, vacuum concentrating at 20-40 degrees C, adding 30-70 vol.% ethanol solution, concentrating to obtain crude extract having a concentration of 0.25-1 g/ml, subjecting to high speed centrifugal sedimentation, separating supernatant, subjecting supernatant to micro-filtration membrane, subjecting filtrate to ultra-filtration, subjecting filtrate to nano-filtration, collecting the filtrate, crystallizing at 4-25 degrees C, centrifuging, filtering, washing the filter cake, and drying until water content is less than 5%.
NOVELTY - A two-phase type high-concentration organic solid waste fermentation apparatus, comprises an acid production reactor and a methane production reactor which are independent mutually; the methane production reactor is provided with a methane collecting device; and leachate circulation is carried out between the acid production reactor and the methane production reactor.    USE - Two-phase type high-concentration organic solid waste fermentation apparatus (claimed).    ADVANTAGE - Due to the adoption of the mutually independent acid production reactor and the methane production reactor in the solid waste treatment apparatus, the acidization process and the methane production process in the anaerobic digestion process are respectively carried out in the acid production reactor and the methane production reactor, and thus, the optimal survival conditions of acid-forming bacteria and methanogens are respectively formed, and the solid organic waste treating capacity and the operation stability of the reactors are greatly improved. Meanwhile, leachate backflow is adopted, so that the microbial activity can be efficiently improved, the nutrient utilization efficiency can be greatly increased, mass transfer is promoted, and retention regions are prevented from appearing in the reactors.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a two-phase type high-concentration organic solid waste fermentation apparatus.    Temperature controller (1)    Control device (2)    Temperature sensor (3)    Acid producing reactor (4)    Motor (5)    Discharge hole (6)    Heater (7)    Methane producing reactor (8)    Gas hole (9)    Incubator (10)
NOVELTY - This utility model belongs to waste straw biomass carbon prepared by crop of the carbonizing device, especially a kind of energy-saving mobile carbonization furnace, the bottom furnace ring and a furnace ring are respectively composed of a cone-shaped steel ring wall, the upper part from the upper to the lower in turn is equipped with taper are orderly increased on the upper opening of the furnace bottom, and adjacent to the upper opening and the lower opening of the furnace are matched with each other, wherein the bottom furnace ring and the outer wall of the opening on the furnace ring base is provided with a base, the furnace bottom ring flange and the upper part is connected with the lower opening of the furnace ring is matched with the base of the furnace ring and the upper part is connected with the lower opening of the furnace ring is matched with the position on the top of the furnace ring and the outer wall of the base is installed with the upper part cover, grate is set at the lower part of the bottom furnace ring, the ring wall of the base ring lower part are evenly distributed on fire grate is provided with a chimney. This utility model can make the crop straw carbonizing anoxic carbonization decomposition the semi-low temperature, straw biomass carbon, and the structure is simple, the carbonization time is short, the yield is high, the cost is low, convenient to move, capable of carrying out carbonization to disperse the straw, it is convenient to use.    USE - Energy-saving mobile carbonization furnace.    ADVANTAGE - The furnace has simple structure, short carbonization time, high yield and low cost. It is also convenient to move, capable of carrying out carbonization to disperse straw and convenient to use.
NOVELTY - This utility model claims a focusing utilization of solar energy, especially a solar energy point-focusing solar energy mirror, and applied to a fixed point array solar biomass gasification system. This utility model comprises at least one solar energy mirror or a set of points, at least one biomass gasification device and tracking control device, a solar mirror is arranged on the solar mirror bracket, biomass gasification device is set on the point-focusing solar energy mirror, the tracking of the focus solar energy during the solar energy mirror, a point keep in focus all the time in the biomass gasification device, tracking control device controls the solar energy mirror to focus the sunshine to at least one biomass gasification device when the sunlight change in the solar tracking process of biomass gasification device is connected with the solar mirror is not the solar mirror to move together, the biomass gasification device and the ground is remained relatively stationary, the solar energy tracking focusing.    USE - Fixed point array solar biomass gasification system.    ADVANTAGE - The system has simple structure and high heat utilization rate.
NOVELTY - The cracker has a heat conduction tank whose top seal is fixed with an oil cylinder that is provided with a feeding port. Left and right cracking tubes are respectively connected with left and right spiral propellers. A lower discharging pipe is connected with a series-wound circulating heat carrier heater. A slag pipe is connected with a slag outlet sealed type cycling heat carrier heater box. The heat conduction tank is provided with a combustion chamber. Two sides of the combustion chamber are matched with an upper part of a smoke outlet.    USE - Plastic, rubber, oil shale and biological straw industrial cracker.    ADVANTAGE - The cracker is inexpensive, and has high working efficiency, and avoids unctuous material evaporating phenomenon and realizes industrial continuous working process.
NOVELTY - A water electrolysis condensing liquid recycling system of hydrogen has gas condenser connected with deoxidation/dehydrogenation unit and condensation liquid collecting tube, condensing liquid return pipe and pressure compensating pipe. A liquid trap is provided between condenser and gas-liquid separator in the height direction. The liquid collecting device is connected with bottom through condensing liquid return pipe and gas-liquid separator. The liquid collector is connected with side through pressure compensation pipe which is connected with gas-liquid separator.    USE - Water electrolysis condensing liquid recycling system of hydrogen.    ADVANTAGE - The recycling system solves problem that gas flow generated in low-pressure side condensed liquid cannot flow back to high voltage side.
NOVELTY - Controlling pest on garden plant comprises preparing pest control agent by taking musk, camphor wood oil, toosendanin, neochamaejasmine, croton oil, polyvinyl alcohol and flobond adhesive, stirring uniformly at 15-25 degrees C and spraying or coating solution on leaf surface.    USE - Controlling pest on garden plant.    ADVANTAGE - The method is environment-friendly, pollution-free and easy to carry out.
NOVELTY - A 5-hydroxy-7,3',4'-trimethoxy flavone is separated and purified by taking fine hair of honeysuckle dry bud, adding 70-90 vol.% ethanol, combining the extracted solution, recovering the solvent to obtain thin felt feather honeysuckle extract, taking felt hair honeysuckle total extract, adding water to prepare the solution, putting the solution on macroporous absorption resin column, eluting with water and 80 vol.% ethanol, eluting with 90-95 vol.% ethanol, collecting 90-95 vol.% ethanol part, recycling the solvent, and passing through a silica gel column chromatography.    USE - Separation and purification of 5-hydroxy-7,3',4'-trimethoxy flavone (claimed).    ADVANTAGE - The method separates and purifies trimethoxy flavone with high purity.    DETAILED DESCRIPTION - A 5-hydroxy-7,3',4'-trimethoxy flavone is separated and purified by taking fine hair of honeysuckle dry bud, adding 70-90 vol.% ethanol, combining the extracted solution, recovering the solvent to obtain thin felt feather honeysuckle extract, taking felt hair honeysuckle total extract, adding water to prepare the solution, putting the solution on macroporous absorption resin column, eluting with water and 80 vol.% ethanol, eluting with 90-95 vol.% ethanol, collecting 90-95 vol.% ethanol part, recycling the solvent, passing through a silica gel column chromatography, eluting with cyclohexane-ethyl acetate-methanol system of 20:0:1 ratio, preferably 5:0:1 ratio to carry out gradient elution, collecting eluent, detecting thin layer, dissolving with methanol after recycling the solvent, and recycling to obtain the 5-hydroxy-7,3',4'-trimethoxy flavone. INDEPENDENT CLAIMS are included for:    (1) separation and purification of beta -sitosterol; and    (2) separation and purification of beta -daucosterol.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow chart of the felt feather honeysuckle total flavone part chemical constitution separation. (Drawing includes non-English language text).
NOVELTY - Straw biogas produced by anaerobic fermentation accelerator contains 0.02-0.2 g cobalt chloride, 0.04-0.4 g nickel chloride, 0.02-1 g ferrous chloride, 5-100 g pyruvic acid salt, 10-300 g fly ash, 10-300 g bentonite, 10-200 g organic matter, and 6-80 phosphate (P2O5).    USE - Straw biogas produced by anaerobic fermentation accelerator (claimed).    ADVANTAGE - Straw dry matter yield can be increased by 15-25%, straw biogas component is easy to obtain, preparation process is simple, side effect is not produced, production rate is improved, and biogas fertilizer value is increased.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of straw biogas which involves performing anaerobic fermentation by drying raw materials at 50-60 degrees C, crushing into 100-120 meshes, and uniformly mixing.
NOVELTY - Methanol diesel oil is prepared by uniformly stirring methanol and latent solvent to obtain modified methanol, adding diesel oil to modified methanol, and stirring.    USE - Preparation of methanol diesel oil (claimed).    ADVANTAGE - Methanol diesel oil has good stability and has physical and chemical index of fuel in accordance with national standard, raw materials are easy to obtain, and preparation method is simple.
NOVELTY - Biodiesel oil is prepared by adding methanol solution to glass reactor with jacket, adding catalyst, stirring, adding 50 ml soybean oil, stirring for 10 minutes, circulating hot water after heating to reaction temperature, separating catalyst by centrifuging, and distilling to remove methanol for chromatographic analysis.    USE - Preparation of biodiesel oil for diesel engine.    ADVANTAGE - Biodiesel oil is easily prepared, and production cost of biodiesel is reduced.
NOVELTY - Biodiesel oil is prepared by adding short chain alcohol, oil, water, and complex enzyme in a reaction container and reacting at 30-50 degrees C for 48-72 hours. Mole ratio short chain alcohol:oil is 3:1, amount of water is 40-100 wt.%, and amount of enzyme is 4-22 U/g soybean oil.    USE - Preparation of biodiesel oil used for expression in pichia pastoris (claimed).    ADVANTAGE - Preparation process does not require organic solvent and is environment-friendly and low cost, product is easy to separate, and ester yield is 98%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biodiesel oil which is used for expression in pichia pastoris containing south-polar Candida antarctica lipase B which is a recombinant plasmid pPICZ alpha A-CALB.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph of the relationship between water content and fatty acid methyl ester yield. (Drawing includes non-English language text).
NOVELTY - A water-mixed fuel contains 54-75 wt.% methanol, 1-2 wt.% acetone additive, 1-2 wt.% petroleum ether, 3-5 wt.% ferrocene, 5-10 wt.% n-propyl ammonium, 3-8 wt.% benzotriazole, 5-8 wt.% polyvinyl chloride, and 5-11 wt.% saturated sodium chloride solution.    USE - A water-mixed fuel for automobiles.    ADVANTAGE - Fuel has high heat value, flash point, and ignition point and is low cost and safe.
NOVELTY - The purifying system comprises a character garbage transmission conduit (10) for reducing falling speed of food waste that is installed at building inside or high-rise apartment in vertical downward. A waste dumping pipe is provided with the character garbage transmission conduit. An opening/closing plate is provided for food waste falling down from the character garbage transmission conduit. A food waste processing unit (40) is provided for discharging food waste residue.    USE - Purifying system for waste for use as fodder for domestic animals or high-quality organic fertilizer.    ADVANTAGE - The purifying system comprises a character garbage transmission conduit for reducing falling speed of food waste that is installed at building inside or high-rise apartment in vertical downward, and thus prevents bad small generation, and rapidly removes moisture contained in food waste in a cost-effective and eco-friendly manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic perspective view of the waste purifying system.    Character garbage transmission conduit (10)    Food waste processing unit (40)
NOVELTY - A Chlorella sp M082 strain (KCTC 11998BP) having carbon dioxide resistance at high temperature, is new.    USE - The Chlorella sp strain is useful for fixing carbon dioxide in coal-fired exhaust gas, and producing lipid for manufacturing biodiesel (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for fixing carbon dioxide in coal-fired exhaust gas, involves using the above-mentioned strain;    (2) method for culturing the above-mentioned strain, involves inoculating the strain in coal-fired exhaust gas and incubating at high temperature;    (3) method for producing lipid, involves culturing the above-mentioned strain, or inoculating the strain in coal-fired exhaust gas, incubating at high temperature and recovering the lipid from the cultured strain; and    (4) method for manufacturing biodiesel, involves performing trans-esterification of lipids and fatty acid esters.
NOVELTY - A Chlorella N113 strain capable of fixing carbon dioxide, is new.    USE - The Chlorella N113 strain is useful for preparing biodiesel (all claimed).    ADVANTAGE - The Chlorella N113 strain has excellent carbon dioxide fixing capability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) Method (M1) for fixing carbon dioxide, involves fixing carbon dioxide contained in coal-fired exhaust gas into Chlorella N113 strain; (2) Method (M2) for producing lipid, involves culturing Chlorella N113 strain in a medium containing coal-fired exhaust gas; and (3) Method (M3) for manufacturing biodiesel, involves transesterifying the lipid obtained in method (M2).
NOVELTY - Method for stereoselective synthesis of (+)-tetrabenazine, involves reacting 5-methyl-3-methylenehexan-2-one and 6,7-dimethoxy-3,4-dihydroisoquinoline in presence of asymmetric organic catalyst.    USE - The method is useful for stereoselective synthesis of (+)-tetrabenazine which is useful for treating Huntington chorea.    ADVANTAGE - The method synthesizes (+)-tetrabenazine at a yield of 50-70%, and is cost-effective and environmentally-friendly.
NOVELTY - The method involves dipping a pair of electrolyte in inside of reaction bath. The electrolytes are separated by an ion exchange membrane. An anode and a cathode are connected by an external circuit. The air or oxygen is supplied to a specific electrolyte of respective reaction bath. The electron and hydrogen ion is generated and passed through ion exchange membrane. The hydrogen ion is moved to specific electrolyte, while the electron is moved to cathode according to the external circuit.    USE - Method for manufacturing hydrogen peroxide using biological electrochemical cell.    ADVANTAGE - By dipping the pair of electrolytes in inside of reaction bath, the chemical substance can be produced effectively. The processing of effluent or biomass can be performed effectively, so that the quality of hydrogen peroxide can be improved. The manufacturing efficiency of hydrogen peroxide can be improved. The energy required for producing the hydrogen peroxide can be reduced. The construction of dispersion electric power system can be performed effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for manufacturing hydrogen peroxide and performing seawater desalination.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biological electrochemical cell.
NOVELTY - Powdered fertilizer anti-caking agent comprises (in %mass): carmine (0.1-0.5), lemon yellow (0.1-0.5), brilliant blue or fruit green (0.1-0.5) and modified talc (99.5-99.9), where the above-mentioned components are mixed using grinder.    USE - As powdered fertilizer anti-caking agent.    ADVANTAGE - The powdered fertilizer anti-caking agent is prepared by simple method, biodegradable, cost-effective and environmentally-friendly, has excellent anti-caking performance, provides a film on fertilizer, and achieves the loose rate of 90% or more. The powdered fertilizer anti-caking agent with corresponding colors which are respectively red, yellow, blue and green can be provided based on the appearance of the fertilizers with different colors, and hence the fertilizer is saturated in hue, and has consistent inside and outside colors, no color difference, no smudged materials, stable color without fading and discoloring, and light and heat resistant performances, and can be served as an anti-fake label of the fertilizer.
NOVELTY - Invention relates to an improved method of recycling a glycerine-containing by-product of producing biodiesel fuel from renewable plant material containing more than 70% glycerine. The present task is solved by that, after distilling residual methanol, the glycerine-containing product is esterified by 3-10 fold molar excess of C4-C6 monobasic carboxylic acids in the presence of 0.5-1.5 wt % acid catalyst, at temperature of 90-120 degrees C, using azeotrope-forming agents for 8-10 hours, which are needed to obtain triglycerides of C4-C6 carboxylic acids with output of 90%, which, after vacuum distillation, are a quality end product - plasticiser for PVC compositions. The obtained product is transparent, has no smell and has hazard class 4.    USE - Chemistry.    ADVANTAGE - Obtained product matches domestic and foreign plasticiser samples used in producing linoleum on basic characteristics. 3 tbl, 1 ex
NOVELTY - Electrolytic splitting of water involves using a composite comprising a carbon-based support and a manganese oxide (MnOx).    USE - The processes are useful for electrolytic splitting of water; and for preparing composite comprising nanoparticular manganese oxide having an oxidation state which is selected from Mn (+III), Mn (+IV) or its mixtures, or for preparing composite comprising a nanoparticular manganese oxide having an oxidation sate which is selected from Mn(+II), Mn (+III) or its mixtures (all claimed).    ADVANTAGE - Process is provided for splitting water under neutral electrolyte conditions, i.e. under environmental acceptable conditions which e.g. allow the splitting of waste water and/or seawater, while achieving a high, and preferably an improved, electrolytic activity and in particular a low overpotential in an oxygen evolution reaction, yet being stable and inert vis-a-vis the oxidizing conditions seen during the oxygen evolution reaction. Additionally, process for preparing a material for the splitting of water under neutral conditions, while employing practical, inexpensive and scalable techniques which can be effectively used in an industrial setting is provided.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a process for preparing a composite which is optionally used in the process above, involving: (a) providing a carbon-based support with a solution of a manganese oxide precursor; (b) drying the obtained product at a temperature of 20-80 degrees C; and (c) calcining the product of step (b);    (2) a composite obtainable by the process, where the composite comprises a carbon-based support and a nanoparticular manganese oxide which is homogenously dispersed and deposited on the carbon-based support; and    (3) an electrode or a photoelectrochemical water splitting device comprising the composite.
NOVELTY - The apparatus (100) has an electric power converting section (103) that converts the direct current (DC) power supply outputted from the fuel cell (102) into the alternating current (AC) power source used in the electric power system. A control unit (104) blocks the connection between an electric power system and an electric power converting section, and applies the surplus power except for the electricity required among the electricity generated in the fuel cell from the operation of the fuel cell system in the load device.    USE - Power controlling apparatus of fuel cell system.    ADVANTAGE - Since the fuel supplied to the fuel cell is reduced, the stability assurance and damage to the fuel cell system can be minimized by consuming the electricity generated in the fuel cell system through the load device. The load of the load device in the fuel cell system can be reduced to the single step, when the operation of the fuel cell system is stopped.    DETAILED DESCRIPTION - A balance of plant (BOP) (105) is connected between the electric power converting section and electric power system. A load device in the electric power converting section is connected into the AC power source through the electric power converting section. An INDEPENDENT CLAIM is included for power controlling method of fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the power controlling apparatus of fuel cell system.(Drawing includes non-English language text)    Power controlling apparatus (100)    Fuel cell (102)    Electric power converting section (103)    Control unit (104)    BOP (105)
NOVELTY - The apparatus has a reactor (110) provided with internal space. A purifying gas vent (112) is formed in an upper portion of purification space (111). The purification space accepts high-capacity waste gas. The purification space is formed in the reactor and connected with the internal space. A plasma combustor (130) is arranged in an end of another reactor (120). The plasma combustor emits plasma flame to the latter reactor. A waste gas inlet port is arranged in a side of outer periphery of the latter reactor for supplying waste gas from an outer side.    USE - Large flux amount non-degradable waste gas treating apparatus.    ADVANTAGE - The apparatus efficiently purifies non-degradable waste gas by utilizing the plasma flame in a quick manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a large flux amount non-degradable waste gas treating apparatus.'(Drawing includes non-English language text)'    Reactors (110, 120)    Purification space (111)    Purifying gas vent (112)    Plasma combustor (130)    Pressure controlling part (140)
NOVELTY - This innovation is related to a method for improving efficiency of mono-sugar fermentation. This method is conducted by adding lignocellulosic material into bioreactor for cultivation. After cultivation, the inoculum is poured into bioreactor filled with liquid prepared for fermentation. After fermentation, product can be purified by applying separation and purification. By using method which is related to adding well-processed lignocellulosic material into bioreactor for cultivation, the efficiency of fermentation can be improved effectively.
NOVELTY - The thickness of a current collector (14) is set greater than or equal to three times of the curvature of a single cell (11). The current collector is accommodated in a recessed portion (121) of a fuel electrode interconnector (12). The single cell is arranged on the current collector. An air electrode interconnector (13) is pressed on the fuel electrode interconnector for connecting the air electrode interconnector and the fuel electrode interconnector.    USE - Method of manufacturing solid oxide fuel cell.    ADVANTAGE - The fuel gas is supplied uniformly to the single cell even when a groove or protrusion is not formed in the interconnector. The manufacturing cost of the solid oxide fuel cell is reduced by reducing the manufacturing cost of interconnector.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the structure of the solid oxide fuel cell.    Single cell (11)    Fuel electrode interconnector (12)    Air electrode interconnector (13)    Current collector (14)    Recessed portion (121)
NOVELTY - Producing hydrogen, gasoline and middle distillate involves i) dehydrogenation of a heavy naphtha in presence of reforming catalyst to obtain a stream of dehydrogenated naphtha; ii) alkylation of the dehydrogenated naphtha with olefinic stream; iii) separation of the mixture obtained in step (ii) in middle distillate fraction and a fraction rich in gasoline; iv) optionally recycling the fraction rich in gasoline to the olefinic stream; and v) separating hydrogen produced in step (i) to obtain a stream of hydrogen.    USE - For producing hydrogen, gasoline and middle distillate (claimed).    ADVANTAGE - The method minimizes the investment; and provides better yield of middle distillate.    DETAILED DESCRIPTION - Producing hydrogen, gasoline and middle distillate involves i) dehydrogenation of a heavy naphtha in the presence of at least one reforming catalyst, to obtain a stream of dehydrogenated naphtha; ii) alkylation of the stream of dehydrogenated naphtha with an olefinic stream in the presence of a solid acid catalyst; and iii) separation of the mixture obtained in step (ii) in at least a middle distillate fraction and a fraction rich in gasoline; iv) optionally recycling the fraction rich in gasoline to the olefinic stream to the inlet of alkylation; and where a total or partial separation of hydrogen produced in step (i) can be carried out between steps (i) and (ii) or between steps (ii) and (iii) in order to obtain a stream of hydrogen.
NOVELTY - System (300) for drying sludge, preferably digested sludge, industrial sludge, sewage sludge or paper sludge, comprises at least one device (200) for conveying the sludge between at least one product inlet (204) and at least one product outlet (206), where the device exhibits at least one trough (100) in which at least one heated conveying screw is arranged for conveying and/or circulating the sludge. The water vapor can be condensed via at least one capacitor and the resulting condensate can be returned during conveying and/or circulating the sludge.    USE - The system is useful for drying sludge, preferably digested sludge, industrial sludge, sewage sludge or paper sludge.    ADVANTAGE - The system operates in cost efficient manner and increases the dry matter content.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic top view of the system.    Trough (100)    Device (200)    Product inlet (204)    Product outlet (206)    System (300)
NOVELTY - Large-scale treatment of biomass, comprises grinding the biomass using a water cutter operated by a liquid. The biomass is supplied to cutter using a supply device (3), which comprises a feed screw or a screw conveyor (7), and which is enclosed on all sides for holding the biomass and adjusting its cross-section to the inner diameter of the cutter at least in its end portion (8) on the output side by a guide surface (9) in the form of a cylinder or cone. The cutter is arranged on drive end of the supply device, and interacts with a counter-blade formed at output end (11)of the supply device.    USE - The biomass is useful for energy production.    ADVANTAGE - The method consumes less energy, and achieves a production of cost-efficient, environmentally friendly- and economical product.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an apparatus for treating the biomass, comprising: a crushing device, which has at least one first cutting beam in a water cutter; and a supply device for the metered supply of biomass to the water cutter, where the water cutter is formed on the output end of the feeding device and cooperates with a counter-blade formed at the output end of the supply device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the apparatus for treating the biomass.    Supply device (3)    Screw conveyor (7)    End portion (8)    Guide surface (9)    Output end (11)
NOVELTY - Biogas generation system comprises a separator (3) arranged between a hydrolysis apparatus (2) and a fermenter (4), where a hydrolysis material from the hydrolysis apparatus, is separated into a liquid fraction and a solid fraction using the separator. The separator comprises a return pipe for guiding the liquid fraction to the hydrolysis apparatus, and a connection for guiding the solid fraction to the fermenter.    USE - Used as a biogas generation system.    ADVANTAGE - The biogas generation system: is suitable for digesting fibrous materials, preferably grass, corn stalks, and straws; enables a stable process; achieves higher and economical biogas production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biogas generation system retrofit kit comprising at least one hydrolysis apparatus and an upstream fermenter, where a biogas device is retrofitted by the separating device present between the hydrolysis apparatus and the fermenter.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic flow diagram of a biogas plant.    Hydrolysis apparatus (2)    Separator (3)    Fermenter (4)    Conditioning device (8)    Paddle stirrer (9)
NOVELTY - A biomass is introduced to a reactor and heated in accordance with predetermined set of operating parameters attuned to the biomass to produce a stable biochar core. Heating is carried out at heating rate of 0.1-50 degrees C/second, which is controlled to within 10 degrees C/second, for more than 0.001 days.    USE - Preparation of biochar core. Uses include but are not limited to soil amendment, potting mix, substitute in growing media including peat and/or compost media, horticultural media, carbon sequestration agent, fertilizing agent, turfgrass establishment, bioremediation agent, and delivery agent for fungi or bacterial population.    ADVANTAGE - A stable biochar core having excellent degradation resistance is efficiently produced. The biochar enhances agricultural output, horticultural qualities or turf grass, and improves the yield of agricultural crop and resistance of the crop to detrimental environmental effects.    DESCRIPTION OF DRAWING(S) - The drawing shows the flow sheet explaining production of functionalized biochar.
NOVELTY - A polymer electrolyte comprises poly(benzimidazoleco-benzoxazole).    USE - Polymer electrolyte for manufacturing a fuel cell (claimed).    ADVANTAGE - The polymer electrolyte provides a fuel cell with high proton conductivity and mechanical strength.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a method for preparing a polymer electrolyte which involves introducing benzoxazole units into polybenzimidazole to form poly(benzimidazole-co-benzoxazole)    (2) a method for producing a polymer electrolyte membrane which involves casting polycondensed poly(benzimidazole-co-benzoxazole)onto a support, and allowing the resultant support to stand under ambient condition to form a polymer electrolyte membrane doped with phosphoric acid in-situ.
NOVELTY - Producing biofuel using brown algae comprises adding at least one hydrolysis catalyst to the brown algae, and saccharifying the brown algae to produce monosaccharides; where at least one hydrolysis catalyst is selected from an isolated bacterium from Bacterium antarctica; an isolated bacterium; a culture solution comprising an isolated bacterium; a supernatant prepared by centrifuging the culture solution comprising an isolated bacterium; and a lysate of an isolated bacterium.    USE - The method is useful for producing biofuel using brown algae (claimed).    ADVANTAGE - Saccharification with the hydrolysis catalyst is effective in saccharification of the brown algae. New and renewable energy resources such as ethanol and butanol, hydrogen and methane may be produced using brown algae, waste algae may be effectively treated, and surplus resources of algae are effectively available.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) an isolated bacterium comprising 16S rRNA having at least 95% sequence identity to fully defined 1022 bp (SEQ ID NO. 1) given in the specification, where the bacterium has hydrolyzing activity of brown algae, and where the bacterium generates or activates alginase;    (2) a culture solution comprising the bacterium;    (3) a supernatant prepared by centrifuging the culture solution; and    (4) a lysate of the culture solution.
NOVELTY - Producing a fatty acid-rich biomass from crude waste glycerol, involves (i) providing crude glycerol culture medium that is free of soaps and methanol; and (ii) culturing species of Schizochytrium, Phaeodactylum, Thraustochytrid, Ulkenia, and/or Labyrinthulea in the crude glycerol culture medium under conditions that permit the Schizochytrium, Phaeodactylum, Thraustochytrid, Ulkenia or Labyrinthulea to use glycerol in crude glycerol culture medium as a carbon source to give a fatty acid-rich biomass.    USE - For producing a fatty acid-rich biomass, particularly omega-3 fatty acid-rich biomass comprising docosahexaenoic acid (DHA) and/or eicosapentaenoic acid (EPA) (claimed) which is useful for algal growth, and used as a food source or food additive, where the DHA is used in treating heart disease, Alzheimer's disease and retinitis pigmentosa, and the EPA is used in treating cardiovascular diseases, cancers, schizophrenia and Alzheimer's disease.    ADVANTAGE - The method is an economical and environmentally sensitive; provides fatty acid-rich biomass; and addresses the problem of the accumulation of excess crude glycerol. The use of crude glycerol in method enables the production of fatty acid-rich biomass.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: 1) a Schizochytrium biomass (A1) comprising docosahexaenoic acid (DHA), where at least a portion of the biomass and at least a portion of the DHA is produced by Schizochytrium using crude glycerol as a substrate; and 2) a Phaeodactylum biomass (A2) comprising eicosapentaenoic acid (EPA), where at least a portion of the biomass and at least a portion of the EPA is produced by Phaeodactylum using crude glycerol as a substrate.
NOVELTY - The device has a rotary shaft (41) extended into a stirring and shredding subchamber (311) along an axis. A shredding blade unit (42) is provided with leading and trailing blade segments (42a, 42b) that are angularly displaced from each other about the axis, where the segments are provided with forward-facing major surfaces. The surfaces are oriented to be inclined relative to the axis, so that a kitchen waste is forced by the surfaces to advance forward to a discharge port by rotating the shredding blade unit with the shaft. A drive unit (5) drives the shaft to rotate about the axis.    USE - Waste disposal device for stirring, shredding and drying kitchen waste.    ADVANTAGE - The device can efficiently stir, shred, heat and dry kitchen waste by moving the shredding blade unit along a spiral path around the axis while the forward-facing major surface is oriented to be inclined relative to the axis. The device ensures reduction in leakage of unpleasant odor through an access opening of housing.    DESCRIPTION OF DRAWING(S) - The drawing shows an exploded perspective view of a waste disposal device.    Housing chamber (20)    Grinder tank (31)    Rotary shaft (41)    Shredding blade unit (42)    Leading blade segment (42a)    Trailing blade segment (42b)    Bottom end (203)    Stirring and shredding subchamber (311)    Front bearing wall (315)    Rear bearing wall (316)
NOVELTY - Isolated polypeptide sequence having an amino acid sequence with at least 95% identity to the amino acid sequence of cytochrome P450-4G1 (SEQ ID NO: 2) (comprising a fully defined sequence of 486 amino acids as given in the specification) and having cytochrome P450 monooxygenase activity, is new.    USE - The isolated polypeptide is useful for catalyzing hydrocarbon formation to produce hydrocarbon which is useful as a biofuel (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) an isolated polynucleotide sequence that encodes the polypeptide sequence of or a polypeptide sequence having an amino acid sequence with at least 95% identity to the amino acid sequence of cytochrome P450-4G2 (SEQ ID NO: 1) (comprising a fully defined sequence of 559 amino acids as given in the specification) and having cytochrome P450 monooxygenase activity;    (2) producing a polypeptide having oxidative decarbonylase activity;    (3) catalyzing hydrocarbon formation comprising contacting a sample comprising a fatty aldehyde with the polypeptide;    (4) a transgenic host cell produced by inserting the polynucleotide into the host cell;    (5) producing (M1) a hydrocarbon comprising culturing the transgenic host cell of under conditions sufficient to produce hydrocarbons;    (6) a recombinant nucleic acid sequence comprising a promoter operably linked to a nucleic acid sequence encoding peptide comprising of a sequence of SEQ ID NO: 1 or SEQ ID NO: 2, or a sequence sharing 95% sequence identity with SEQ ID NO: 1 or SEQ ID NO: 2;    (7) a cell comprising the recombinant nucleic acid sequence; and    (8) making a hydrocarbon comprising culturing the cell comprising the recombinant nucleic acid sequence under conditions sufficient to produce hydrocarbon.
NOVELTY - Decomposing soft biomass by contacting soft biomass with (a) enzyme preferably exo-type cellulase comprising an amino acid sequence of SEQ ID NO: 2, or amino acid sequence having 90% or more sequence homology to amino acid sequence of SEQ ID NO: 2, or (b) microorganisms capable of producing enzymes chosen from (i) exo-type cellulase, (ii) exo-type cellulase and endo-type cellulase, and (iii) exo-type cellulase, endo-type cellulase and processive endo-type cellulase. Sequences not defined here may be found at ftp://ftp.wipo.int/pub/published_pct_sequences/publication.    USE - The method is useful for decomposing soft biomass preferably rice straw or bagasse, used for producing one or more target substances chosen from ethanol, acetic acid, butyric acid, lactic acid, formic acid and hydrogen (all claimed).    ADVANTAGE - The method enables direct decomposition of the soft biomass in presence of enzyme, hence preprocessing steps of the biomass are not require to be performed. The method is simple and can be performed easily.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for enzyme or enzyme complex which comprises (a) the above-mentioned exo-type cellulase, and/or (b) endo-type cellulase comprising an amino acid sequence of SEQ ID NO: 4, or amino acid sequence exhibiting 90% or more sequence homology to the amino acid sequence of SEQ ID NO: 4, and/or (c) processive endo-type cellulase comprising an amino acid sequence of SEQ ID NO: 6, or amino acid sequence exhibiting 90% or more sequence homology to the amino acid sequence of SEQ ID NO: 6. Sequences not defined here may be found at ftp://ftp.wipo.int/pub/published_pct_sequences/publication.
NOVELTY - Method for decomposing soft biomass, involves contacting enzyme comprising exocellulase having an amino acid sequence which has 90% or more identity with amino acid sequence of SEQ ID NO: 2 with soft biomass.    USE - The method is useful for decomposing soft biomass (claimed).    ADVANTAGE - The method is simple.    DETAILED DESCRIPTION - Method for decomposing soft biomass, involves contacting enzyme comprising exocellulase having an amino acid sequence which has 90% or more identity with amino acid sequence of SEQ ID NO: 2 with soft biomass. Sequences not defined here may be found at ftp://ftp.wipo.int/pub/published_pct_sequences/publication. INDEPENDENT CLAIMS are included for the following:    (1) method for preparing target substance from soft biomass, involves decomposing soft biomass by the decomposition method of the soft biomass;    (2) enzyme or group of enzymes for decomposing soft biomass comprising exocellulase having an amino acid sequence which has 90% or more identity with amino acid sequence of SEQ ID NO: 2, endocellulase having an amino acid sequence which has 90% or more identity with amino acid sequence of SEQ ID NO: 4 and processive endocellulase having an amino acid sequence which has 90% or more identity with amino acid sequence of SEQ ID NO: 6; and    (3) group of enzymes comprising exocellulase having an amino acid sequence which has 90% or more identity with amino acid sequence of SEQ ID NO: 2, endocellulase having an amino acid sequence which has 90% or more identity with amino acid sequence of SEQ ID NO: 4.    Sequences not defined here may be found at ftp://ftp.wipo.int/pub/published_pct_sequences/publication.
NOVELTY - Forming a metal oxide composite, comprises: mixing a metal oxide, at least two monomers and a dispersant to produce a slurry; gel casting the slurry to produce a green metal oxide composite; and sintering the green metal oxide composite.    USE - The metal oxide composite is useful for catalyzing hydrolysis of metal borohydride, preferably sodium borohydride to produce hydrogen gas (all claimed), which is useful for vehicular machines, unmanned aerial vehicles, portable power applications and stationary power applications.    ADVANTAGE - The method provides self-supported metal oxide composite in an economical and environmentally friendly manner.    DETAILED DESCRIPTION - The metal oxide composite formed by the method.    DESCRIPTION OF DRAWING(S) - The figure shows a flow chart of a method for forming metal oxide composites.
NOVELTY - The generator (20) has several thermal conductors whose outer wall together to form housing. The fuel pellets are provided on the thermal conductors (50) and is provided with a hydrogen-containing reactant. A compartment (22) removably contains a cartridge (40). A heating system has several heating elements (30) that are provided in the compartment such that each heating element is in thermal communication with thermal conductors, when the cartridge is provided within the compartment to generate heat to fuel pellets (44) to initiate a reaction to produce hydrogen gas.    USE - Hydrogen generator for providing hydrogen gas to fuel cell system (claimed) used in portable electronic device.    ADVANTAGE - The hydrogen can be produced efficiently on an as-needed basis without producing the excessive internal pressure within the hydrogen generator. The hydrogen generator in the fuel cell system can be replaced efficiently after reactants have been consumed. The durability and reliability of the hydrogen generator can be ensured. The manufacturing cost of the hydrogen generator is reduced, as the hydrogen generator with simplified structure can be obtained.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the hydrogen generator. (Drawing includes non-English language text)    Hydrogen generator (20)    Compartment (22)    Heating element (30)    Cartridge (40)    Fuel pellet (44)    Thermal conductor (50)
NOVELTY - Method for preventing freezing of ammonium sulfate, involves mixing the solution comprising particulate-form ammonium sulfate and oligosaccharide for fertilizers to obtain a solute, when solvent in the solution evaporates, the saccharides coat the surface of the ammonium sulfate.    USE - The method is useful for preventing freezing of ammonium sulfate which is useful in preparation of ammonium sulfate mixed fertilizer (claimed).    ADVANTAGE - The method is environmentally-friendly, and suppress the moisture content in the ammonium sulfate particle.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the ammonium sulfate mixed fertilizer, which involves performing freezing prevention process of the particulate form ammonium sulfate using above-mentioned method, blending the ammonium sulfate by which the freezing prevention process was carried out, and preparing a fertilizer.
NOVELTY - A catalyst composition comprises a catalyst system comprising in situ grown zeolites into an aluminosilicate clay matrix having a hierarchical pore structure of 50-5000 Angstrom , and a feedstock having a carbon 14C isotope content of 107 pMC.    USE - A catalyst composition for conversion of biomass (claimed).    ADVANTAGE - The composition exhibits hierarchical pore structures, is cheap, and reduces thermoconversion cost of biomass process.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a method of making a biomass catalytic cracking catalyst system comprising preparing a slurry precursor mixture by mixing an aluminosilicate clay material with a pore regulating agent and optionally a binder; shaping the mixture into shaped bodies; removing the pore regulating agent to form porous shaped bodies; preparing an aqueous reaction mixture comprising the porous shaped bodies in presence of a seeding material; thermally treating the aqueous reaction mixture to form the catalyst system; and contacting the catalyst system with biomass particles; and    (2) a process of catalytic thermolysis of cellulosic biomass comprising heating the cellulosic biomass to a conversion temperature in presence of the catalyst system.    DESCRIPTION OF DRAWING(S) - The drawing is a graph showing non limiting comparison of characterization by X-ray Diffraction of the microspheres and a computer simulated melt flow index.
NOVELTY - A catalyst system comprises a zeolite having a hierarchical pore structure having pore size of 5-20 Angstrom , a non-zeolitic matrix with hierarchical pore structure having pore size of 100-5000 Angstrom , and a binder.    USE - Catalyst system is used for composition, catalytic thermolysis of biomass and catalytic upgrading of bio-oil (all claimed).    ADVANTAGE - The catalyst system exhibits hierarchical porosity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparation of catalyst system, which involves modifying zeolite to form modified zeolite having hierarchical microporous-mesoporous structure, preparing slurry precursor mixture by mixing modified zeolite, non-zeolitic inorganic matrix, binder and combustible organic compound in water, shaping the mixture to form shaped component, and thermally treating the shaped component to remove the combustible organic compound;    (2) composition, which contains catalyst system comprising a zeolite having high silica to aluminum ratio and a hierarchical pore structure, non-zeolitic matrix, and binder;    (3) process for catalytic thermolysis of biomass, which involves heating the biomass to conversion temperature in presence of the catalyst system; and    (4) process for catalytic upgrading of bio-oil.
NOVELTY - Method for producing a bio fuel using genetically modified bacteria, involves providing genetically modified bacteria to oxidize elemental sulfur and reduce iron (SOIRB) and to include a specific metabolic pathway to generate a biofuel, feeding ferric iron to the SOIRB, feeding sulfur, water, and carbon dioxide to the SOIRB, oxidizing the sulfur, reducing the ferric iron, and producing at least one of the biofuel, ferrous iron, sulfate, excess ferric iron, and an SOIRB biomass.    USE - The method or system is useful for producing a bio fuel using genetically modified bacteria chosen from SOIRB, SOB and IOB (all claimed).    ADVANTAGE - The method produces biofuel cost-effectively.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) system for producing biofuel using genetically modified SOIRB, comprising a bioreactor comprising genetically modified SOIRB to generate first particular biofuel, a first source of ferric iron in fluid communication with the bioreactor, a source of water in fluid communication with the bioreactor, a source of sulfur in fluid communication with the bioreactor, and a source of carbon dioxide in fluid communication with the bioreactor; and    (2) method for producing a chemical or bio fuel using genetically modified sulfur-oxidizing (SOB), involves providing a genetically modified SOB to generate a first particular chemical or biofuel, feeding sulfur, water, carbon dioxide, and oxygen to the SOB, oxidizing the sulfur, and producing at least one of the chemical or biofuel, sulfate, and an SOB biomass.
NOVELTY - The system has a compression subsystem (10) treating a natural gas feed stream (12) to remove first portion of a liquid waste stream (24). A gas pretreatment subsystem (30) treats a pressurized natural gas stream to remove a second portion of the liquid waste stream and cool and filter the pressurized stream to form a filtered natural gas stream. An acid gas separation subsystem (14) separates the filtered stream into a sweetened gas stream and a first portion of a gaseous waste stream. A destruction subsystem incinerates the first portion of the gaseous waste stream to form a flue gas.    USE - System for separating and/or destroying sour and acid gas e.g. sweetened gas stream, liquid waste stream and gaseous waste stream, for use on maritime platforms, and land-based sour and/or acid gas sources and on or near ocean.    ADVANTAGE - The system produces usable natural gas from sour and acid gas, and eliminates carbon and sulfur dioxide atmospheric pollution produced by burning of contaminated natural gas. The apparatus ensures that driver can utilize the treated gas from the system as a fuel source, thus making the compression subsystem energy independent.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for separating natural gas feed stream into sweetened gas stream, liquid waste stream and gaseous waste stream, and for discharging, recovering or destroying liquid waste stream and gaseous waste stream.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a system for separating and/or destroying sour and acid gas.    Compression subsystem (10)    Natural gas feed stream (12)    Acid gas separation subsystem (14)    Liquid waste stream (24)    Gas pretreatment subsystem (30)
NOVELTY - Obtaining lipids from algae comprises: either (a) synchronizing germination of zygospores in a culture of algae cells, (b) lysing the zygospores just prior to release of progeny cells from the zygospores, and (c) harvesting lipids released from the zygospores; or (a1) forming zygospores of the algae, (b1) purifying the zygospores, (c1) washing the zygospores, (d1) storing the zygospores, (e1) synchronizing zygospore germination, (f1) lysing the zygospores, just prior to release of progeny cells to release lipids, and (g1) recovering the lipids.    USE - The method is useful for obtaining lipids from algae such as Chlamydomonas monoica (all claimed), where the lipids are useful as biodiesel and in food supplements.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for obtaining lipids from Chlamydomonas monoica algae comprising forming zygospores from the algae in a vegetative state by depriving it of nitrate and phosphate, purifying the zygospores by separating the zygospores from other cells, the step (c1) as above per se, storing the zygospores for 3-4 weeks in darkness without nutrients at a temperature of 4-25 degrees C, synchronizing zygospore germination by substantially simultaneously providing the zygospores with a nutrient medium containing nitrate and phosphate and subjecting the zygospores to substantially continuous light, lysing the germinated zygospores, just prior to release of progeny cells, to release lipids, and recovering the lipids.
NOVELTY - Composition comprises 95-98% ethanol, 3% perfume, 0.04-0.06% 5-chloro-(2,4-dichlorophenoxy)phenol or triclosan, which is replaceable by 3,4,4'- trichlorocarbanilide or triclocarban, 0.03-0.06% ((2R)-2,5,7,8-tetramethyl-2-((4R,8R)-4,8,12-trimethylsilyl)chroman-6-yl)acetate or tocoferol acetate, propane and butane.    USE - The composition is useful for odor remover which is used for jackets, shoes and socks, safety helmets, car air-conditioners, headscarves or indoor cigarette odor (claimed).    ADVANTAGE - The composition is waterless, environmentally-friendly and glass house impact-free aerosol, and enables to eliminate weakness attached in the products, such as ability to kill bacteria, not to leave stains, to dry rapidly (not wet) and not to stimulate dandruff on the head skin.
NOVELTY - A biofuel comprises hydrotreated renewable diesel and petroleum diesel cold flow improver additive.    USE - Biofuel for use in non-tropical applications.    ADVANTAGE - The biofuel has improved cold flow properties, high viscosity, high paraffin content and high degree of saturation of the hydrotreated renewable diesel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method of preparing a biofuel.
NOVELTY - A carbonaceous compact comprises a body comprises a carbonaceous biomass composition and an adhesive additive comprising a starch and a hydroxide.    USE - Carbonaceous compact.    ADVANTAGE - The carbonaceous compact has high durability and high working efficiency, and is inexpensive.
NOVELTY - Processing lignocellulosic biomass comprises providing lignocellulosic biomass feedstock; pretreating the biomass feedstock by continuous hydrothermal pretreatment in a pressurized reactor; measuring xylan number or lignin number in the output stream of pretreated biomass from the pretreatment reactor; and controlling the pretreatment reactor so as to maintain, in the output stream of pretreated biomass, a pre-determined level of measured xylan number or lignin number.    USE - The method is useful for processing lignocellulosic biomass (claimed).    ADVANTAGE - The method allows for continuously controlling the digestibility of a lignocellulosic biomass during the step of pretreatment, and accordingly provides a continuous estimate of the severity of the pretreatment. Using feedback control of pretreatment, based on either of the composite end point measures, reactor conditions can be rapidly adjusted to accommodate variability of incoming feedstocks in production scale, thus minimizing the incidence of pretreatment inefficiencies.
NOVELTY - Additives comprise at least 50 mass% of monoester and/or diester of polyglycerol, where the polyglycerol having 2-5 glycerol units per molecule is the ester units derived from fatty acid, which is optionally having one or more ethylene unsaturation, and the majority (over 50%) of fatty chains contains 12-24C.    USE - The additives are useful for preparing diesel or biodiesel fuels (claimed).    ADVANTAGE - The additives exhibit improved wear resistance and lubricity, improved sulfur content, and superior quality.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) an additives packages for biodiesel fuel comprising the additives and at least one or more other functional additives, such as filler reducers/dispersants, antioxidants, combustion improvers, corrosion inhibitors, cold resistance additives (improving cloud point, sedimentation rate, filterability and/or cold flow), dyes, demulsifiers, metal deactivators, antifoaming agents, cetane number improving agent, cosolvents, compatibilizing agents, other lubricity additives, antiwear additives and/or friction modifiers, and optionally one or more solvents; and    (2) a biodiesel fuel composition comprising the additives and the other functional additives.
NOVELTY - Treating a slurry comprising digested organic material comprises (1) obtaining an acidic slurry at a pH of less than 7, (2) adding an oxidizing agent to the acidic slurry and reacting, (3) adding an alkaline compound to the slurry to obtain a pH of greater than or equal to 8, (4) adding a flocculating polymer to the slurry obtained in (3), and (5) separating the slurry obtained in (4).    USE - The process is useful: for treating a slurry comprising digested organic material including the digestate from a biogas plant (all claimed), biomass, sludge, effluent waste stream or water and organic waste (preferably a biomass waste); and in variety of applications, where low amounts of suspended solids are required for the reject water, due to requirements in subsequent processes, e.g. for ammonia removal by stripping from reject water, or for reducing the amount of suspended solids for following biological or membrane processes or for recycling the reject back to the process.    ADVANTAGE - The process efficiently precipitates the solids at alkaline process conditions to remove the existing suspended solids and provides an improved reduction in chemical oxygen demand and a total amount of phosphorus.
NOVELTY - The method involves integrating a plant for melting-gasification of phosphorus-containing materials in the plants for exclusive energy recovery. The melting-gasification plant generates a molten metal, a heavy metal-lacking chalk-silicon-phosphorus-containing waste and a combustion gas. The combustion gas is guided into the plants for the exclusive energy recovery as a combustion fuel. The powdered phosphorus-containing wastes in the high-temperature zone of the melting-gasification are supplied with oxygen.    USE - Method for recovery of phosphorus-containing wastes in plants for their exclusive energy recovery, such as mono-incinerators for sewage sludge or animal meal during co-incineration in power stations or during additional firings in furnaces of the cement industry or comparable furnaces of the other industrial sector.    ADVANTAGE - The method involves integrating a plant for melting-gasification of phosphorus-containing materials in the plants for exclusive energy recovery, and hence ensures cost effective operation of the recovery method with reduced energy consumption, and improved efficiency of melting-gasification of materials for use in organic substances with higher ash fractions.
NOVELTY - Plant for anaerobic stabilization of pumpable organic waste materials, comprises at least one closed and rectangular-shaped container (1,2), an inlet for untreated waste materials, an outlet for treated waste materials, a device for discharging biogas, a device for heating the waste materials, a device for mixing the waste materials in the container, and a machine housing (3), whose wall is formed by a wall of the container.    USE - The plant is useful for anaerobic stabilization of pumpable organic waste materials.    ADVANTAGE - The plant is economically feasible for lesser quantities of waste materials, and makes use of rectangular-shaped containers, which require less space.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of a plan view of the system.    Closed rectangular-shaped containers (1, 2)    Machine housing (3)    Common wall (4)    Slope modules (5)    Circulation pumps (8)
NOVELTY - Method for preparing sugar liquid, involves (a) subjecting cellulosic biomass to pretreatment process using agent comprising ammonia to obtain pretreated processed material, (b) subjecting the pretreated processed material to enzyme saccharification process to obtain ammoniated sugar liquid, and (c) refining the ammoniated sugar liquid by removing formed amide and/or imides products in the ammoniated sugar liquid to obtain refined sugar liquid, where refined sugar liquid contains 10-1100 parts per million amide and/or imides products after the refining process.    USE - The method is useful for preparing sugar liquid useful as fermentation raw material used for producing ethanol (all claimed).    ADVANTAGE - The method enables preparation of the sugar liquid having improved fermentation efficiency, as fermentation inhibitors chosen from amide and/or imide based products are removed from the sugar liquid, hence the sugar liquid also enables production of the ethanol at high yield.
NOVELTY - The system has aerators that decompose organic substance in wastewater while activating microorganisms by aeration with respect to wastewater sent from inflow adjustment tank. The air for aeration is supplied, so that oxidation-reduction potential (ORP) value reaches upper limit of range of 104mv-120mv from lower limit of range of 1mv--1.8mv within 9 minutes. Air supply is stopped after reaching upper limit. The intermittent supply of air for aeration is performed repeatedly after resulting in lower limit, so that oxidation-reduction processes are promoted in aerator.    USE - Wastewater treatment system.    ADVANTAGE - The wastewater treatment system can decompose the protein and ammonia in a wastewater into nitrogen gas (N2) efficiently by intermittent supply of the air for aeration.    DESCRIPTION OF DRAWING(S) - The drawing shows the graphical views illustrating the raise of oxidation-reduction potential (ORP value), raise of fall state and dissolved oxygen amount (DO value) in aerator. (Drawing includes non-English language text)
NOVELTY - A reformer has a combustor (14) for receiving at least fuel and converting fuel into heat to provide heat to a reformer unit (15) disposed annularly above the combustor. The reformer unit and combustor are separated by wall (10). The combustor contains a structured catalyst support coated with a catalyst to induce fuel combustion reactions. Reformer unit receives fuel and produces a reformate containing primarily hydrogen, and further contains reforming catalyst pellets or a structured catalyst support coated with a catalyst to induce the fuel reforming reactions.    USE - Reformer for production of hydrogen in integrated steam reformer/combustor assembly used in fuel processing system (claimed). Hydrogen is used in ammonia synthesis, oil refining, oil hydrogenation plant, glassblowing operation, cooling application and photovoltaic material processing.    ADVANTAGE - The reformer is compact, and efficiently enables production of hydrogen rich stream at mild conditions.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for integrated steam reformer/combustor assembly used in fuel processing system.    DESCRIPTION OF DRAWING(S) - The drawing shows the perspective view of heat integrated reformer.    Cylindrical wall (10)    Reforming unit (14)    Combustion zone (15)    Combustion catalyst (22)    Fuel and air mixture (32)    Flow passage (41)
NOVELTY - Preparation of 5-chloro-N-(((5S)-2-oxo-3-(4-(3-oxo-4-morpholinyl) phenyl)-1,3-oxazolidin-5-yl)methyl)-2-thiophene-carboxamide (rivaroxaban) (I), involves: reacting a compound 4-(4-((5S)-5-(aminomethyl)-2-oxo-1,3-oxazolidin-3-yl)phenyl)morpholin-3-one (II) with a compound 5-chloro-thiophene-2-carboxylic acid (III) in the presence of boric acid and/or optionally substituted phenyl boronic acid to give the compound (I).    USE - In the preparation of 5-chloro-N-(((5S)-2-oxo-3-(4-(3-oxo-4-morpholinyl) phenyl)-1,3-oxazolidin-5-yl)methyl)-2-thiophene-carboxamide, for the prevention of venous thromboembolism in adult patients undergoing elective hip or knee replacement surgery and for non-valvular atrial fibrillation to reduce stroke risk in cardiac patients.    ADVANTAGE - The process avoids the use of hazardous reagents like thionyl chloride and intermediate 5-chloro-thiophene-2-carbonyl chloride and carcinogenic reagent pyridine which were used in prior art process; used reagents like boric acid or optionally substituted phenyl boronic acids that are cheaper and commercially available and also does not give rise to the formation of impurities or side products unlike in prior art processes; avoids base and process step like decomposition, extractions and washings; is carried out in single step; avoids the complicated chromatographic purification of the product (I); provides final product with higher yields (preferably 80-90%) and higher purities; is simple, ecofriendly, inexpensive, reproducible and robust process; and is suitable for commercial scale production of rivaroxaban (I).
NOVELTY - A transgenic Escherichia coli capable of producing ethane-1,2-diol from D-xylose, and obtained by knocking out D-xylose isomerase gene and/or D-xylose dehydrogenase gene from genomic DNA of the E.coli and/or transforming the E.coli with expression vector comprising xylose dehydrogenase gene of Caulobacter crescentus (cxylB) gene, is new.    USE - The transgenic E.coli is useful for producing ethane-1,2-diol from D-xylose (all claimed) containing biomass.    ADVANTAGE - The transgenic E.coli enables efficient and large scale production of the ethane-1,2-diol from the biomass in higher concentrations and at high yield as biosynthetic pathway of the ethane-1,2-diol is optimized, hence environmental concerns and increasing cost and limited supply of fossil fuels can be overcome.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) preparation of the above-mentioned transgenic E.coli; and (2) method for preparing the ethane-1,2-diol, involves culturing the above-mentioned transgenic E.coli in culture medium, and collecting ethane-1,2-diol from the culture medium.
NOVELTY - Method (M1) for converting biomass to biofuel, comprises (a) co-culturing biomass with a first cellulolytic, thermophilic microorganism and a second hemicellulolytic, extremely thermophilic, xylose-fermenting microorganism for a time and under conditions sufficient to ferment hexose and pentose sugars produced as the biomass is hydrolyzed and converted to biofuel and to ferment the sugars at a substrate conversion rate of at least 50%.    USE - The method is useful for converting biomass to biofuel comprising ethanol and/or acetate (all claimed).    ADVANTAGE - The method: provides the substrate conversion rate of at least 50%, preferably at least 75% (claimed); utilizes two groups of thermophilic microorganisms that effectively hydrolyze cellulose and hemicellulose in a single fermentation, hence it is efficient; and reduces the number of fermentation tanks needed, hence it is cost effective.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for (1) a culture medium comprising 50% medium for Thermophilic clostridia blended with 50% Hamilton-Brehm medium; and (2) a method (M2) for producing cellulosic ethanol, comprising: the step (a) as above per se to produce ethanol at a substrate conversion rate of at least 50%; and recovering the ethanol.
NOVELTY - Preparing methionine compounds (III) or their salts, comprises (a) contacting 2-amino-4-hydroxy-butyric acid (I) with a carbonyl donor to form 2-oxo-(1,3)oxazinane-4-carboxylic acid (II), and (b) contacting (II) with a methyl compound (IV).    USE - The method is useful for preparing (III) (claimed).    ADVANTAGE - The method prepares (III) with large amount in cost effective manner and environmentally friendly manner.    DETAILED DESCRIPTION - Preparing methionine compounds of formula (CH3-Z-CH2-CH2-CH(NH2)-COOH) (III) or their salts, comprises (a) contacting 2-amino-4-hydroxy-butyric acid (I) with a carbonyl donor to form 2-oxo-(1,3)oxazinane-4-carboxylic acid (II), and (b) contacting (II) with a methyl compound of formula (MeZ) (IV).    Me = methyl; and    Z = S or Se.    An INDEPENDENT CLAIM is included for preparing (II) comprising contacting (I) with a carbonyl donor, where the carbonyl donor is urea or its derivative, a cyclic carbonate, a dialkyl carbonate, a diaryl carbonate, an alkyl aryl carbonate, an alkyl carbamate, an aryl carbamate or a halocarbonyl.
NOVELTY - Equipment comprises elements for grinding, pressing and composting in integrated manner.    USE - Equipment for accelerated composting of waste (claimed).    ADVANTAGE - The equipment occupies smaller spaces for installation and operation of composting.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for processing accelerated composting of organic waste, which involves crushing, pressing, dehumidification or desiccation, and composting to obtain final product.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of grinding or pressing unit of an equipment.    Feeding mouth (1)    Protection cover (2)    Knife grinder (3)    Electric motor (4)    Retractor (6)
NOVELTY - A dehydrogenation catalyst comprises dinuclear metal complex (I).    USE - Dehydrogenation catalyst is used for dehydrogenation of formic acid and manufacture of hydrogen gas, deuterium gas, tritium gas, deuterated or tritiated hydrogen gas (all claimed).    ADVANTAGE - The hydrogen gas is efficiently and economically manufactured using the dehydrogenation catalyst, by a simple process under mild reaction conditions. The hydrogen gas does not contain carbon monoxide.    DETAILED DESCRIPTION - A dehydrogenation catalyst comprises dinuclear metal complex of formula (I), or its salt, tautomer or stereoisomer.    M1,M2=transition metal;    Q1-Q6=C or N;    R1-R6=H, alkyl, phenyl, nitro, halo, sulfo, carboxy, alkoxy or alkylamino;    L1,L2=aromatic anion ligand or aromatic ligand;    Y1,Y2=optionally ligands;and    m=positive integer, 0 or negative integer.    INDEPENDENT CLAIMS are included for the following:    (1) dehydrogenation of formic acid, which involves react solution containing formic acid and/or formate in presence of dehydrogenation catalyst;    (2) manufacture of hydrogen gas, which involves reacting solution containing formic acid and/or formate in presence of dehydrogenation catalyst;    (3) manufacture at least one of deuterium gas, tritium gas, deuteratedor tritiated hydrogen gas by using heavy water or tritiated water as solvent for the dehydrogenation of formic acid in the presence of dehydrogenation catalyst; and    (4) manufacture at least one of deuterium gas, tritium gas, deuteratedor tritiated hydrogen gas by dehydrogenation of heavy formic acid or formate in the presence of dehydrogenation catalyst.
NOVELTY - A kind of pump suction type multi-parameter sensor of the utility model comprises the sensor shell body and is provided with a plurality of gas detection control circuit in the safety micro vacuum pump, gas path switching device is provided with a data transmission interface and four air suction tube interface on the sensor shell, the air pumping tube interface is connected with the air path switching device is connected with the gas detection control circuit is respectively connected with the micro vacuum pump and a safety circuit, micro-gas path switch device is the vacuum pump is respectively connected with the gas detection control circuit and a gas path switching device, the data transmission interface is connected with the gas detection control circuit. Because of adopting the micro vacuum pump is less than the cost of water ring vacuum pump, is small and light, does not need special installation space, directly according to normal mine sensor is set with the same that is capable of using is simple, the construction is convenient, in addition, it adopts multi-parameter integrated detection circuit can detect methane, carbon monoxide, carbon dioxide, oxygen, temperature and other parameters, high density of integration, low cost, simple structure and convenient maintenance.
NOVELTY - Production of rhizoma Cyperi extract comprises taking raw rhizoma cyperi, removing impurities, putting in a pot, heating until yellowish, mixing 8-12% vinegar-processed rhizoma Cyperi, 1-3% salt, 4-5% white spirit, and 2-4% honey, adding into a pot, adding pure water, heating by low heat, mixing, taking out, and cooling to obtain the product.    USE - Production of rhizoma Cyperi extract (claimed).    ADVANTAGE - The production method has high production efficiency and high yield and is energy saving. The planting method is simple and green, has low cost, greatly improved yield, and high nutrient content, and reduces environmental pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for planting method of rhizoma Cyperi including selecting good quality seed, drying, 20-25 days before seeding, soaking the seeds in medicine soaking liquid for 12-15 hours, where medicine soaking liquid contains 80-100 ppm gibberellin, 1-2% acetic acid, 1-2% ammonium molybdate, 1-2% sodium selenite, and 1-2% manganese sulfate aqueous solution, and seeding time is on the 9th-10th month, taking out the seed, selecting the soil with loose texture, turning the soil, mixing peat, fly ash, iron ore tailing, and lees at 5:7:3:9-11 ratio, adding phosphorus and potash fertilizer, digging seeding holes, each having a depth of 25-32 cm, filling with 12-16% urea and 20-30% organic fertilizer, covering with soil, uniformly spreading 2-3 seeds in the seeding hole, covering with a little soil, weeding for every 2-3 months each year, fertilizing once with (per mu): 5-10 kg slow-release urea, 3-5 kg potassium chloride, 10-15 kg monocalcium phosphate, 2-3 kg ferrous sulfate, 0.5-1.0 kg borax, and 0.2-0.3 kg ammonia, preventing and treating insect pests by spraying with disease-preventing agent, weeding once after spraying, and harvesting.
NOVELTY - High-stability gold (Au)-copper (Cu)/lanthanum manganite (LaMnO3) catalyst preparation comprises adding hydrogen tetrachloroaurate and copper nitrate solution in beaker, adding carrier LaMnO3 to form mixed solution, adjusting pH with sodium hydroxide to 9=11, magnetically stirring at room temperature for 2-4 hours, washing with deionized water, filtering until no chloride, and obtaining the catalyst.    USE - Method of high-stability gold (Au)-copper (Cu)/lanthanum manganite (LaMnO3) catalyst preparation (claimed).    ADVANTAGE - The catalyst has good catalytic conversion of carbon monoxide activity and stability.    DETAILED DESCRIPTION - High-stability gold (Au)-copper (Cu)/lanthanum manganite (LaMnO3) catalyst preparation comprises weighing mol ratio of 1:1 of lanthanum nitrate and manganese nitrate, adding citric acid at room temperature, stirring uniformly, adjusting pH to 9-10 by ammonia water, transferring to hydrothermal reaction kettle, putting into constant temperature 160-180 degrees C, crystallizing for 24-48 hours, naturally cooling, obtaining gel for 80 hours at 60-100 degrees C, and drying at 400-600 degrees C, and grinding for 2-4 hours to obtain carrier LaMnO3; and adding hydrogen tetrachloroaurate and copper nitrate solution in beaker, adding carrier LaMnO3 to form mixed solution, adjusting pH with sodium hydroxide to 9=11, magnetically stirring at room temperature for 2-4 hours, washing with deionized water, filtering until no chloride, and obtaining the catalyst.
NOVELTY - Herbicide-fertilizer composition comprises active ingredient comprising mefenacet and/or bensulfuron methyl, synergistic ingredients and fertilizer composition., The synergistic ingredients comprise humic acid and 1-chloromethylsilatrane and the fertilizer composition is organic fertilizer or organic-inorganic fertilizer. The weight ratio of the active ingredient, synergistic ingredients and the fertilizer composition is 1-10: 10-250: 100-5000.    USE - Used for anti-weed and promoting the growth of crops, where the crop is eggplant, tomato, potato, sweet potato, radish, sorghum, tobacco, wheat, rice, corn, cucumber, peanut, coconut, balsam pear, bean, tea tree, rubber, sugar cane, pea, white gourd, pear, banana, pawpaw, green soy bean, mango, watermelon, orange, orange, kiwi fruit, strawberry, pineapple, pepper, apple, persimmon, grape, cherry, and/or litchi fruit, preferably rice (claimed).    ADVANTAGE - The composition prevents and removes weeds at the same time to promote the growth of crops and reduces injury. The fertilizer composition increases production efficiency, improves efficiency and saves cost, simple and convenient operation.
NOVELTY - Organic fertilizer comprises 20-35 pts. wt. rice straw, 25-45 pts. wt. fly ash, silicic acid slag, coal gangue or low grade coal, 2-7 pts. wt. soybean, 5-20 pts. wt. rice hull powder, 10-20 pts. wt. calcium superphosphate, 3-10 pts. wt. urea, and 1-5 pts. wt. potassium sulfate.    USE - Used as an organic fertilizer.    ADVANTAGE - The fertilizer: is prepared using agricultural and industrial waste, thus recycling the waste; is economical and environmentally friendly; completely satisfies the need of various plants to balance the nutrition; has quick fertilizing effect with ling lasting effect; does not cause any damage; improves the soil and its fertility; does not cause environmental pollution; saves resources; and has social and economic benefits in the production and usage process.
NOVELTY - Preparing carotenoid comprises inoculating photosynthetic bacteria into culture solution of sugar and cellulose and then culturing using culture medium and hydrolyzing the cells to obtain single cell protein, where the culture medium comprises 0.2-20% of ether, 1% ammonium sulfate, 0.1 % of potassium dihydrogen phosphate, 0.5% of magnesium sulfate and 0.01% of ferrous sulfate, and has a pH value of 2-7.    USE - The method is useful for preparing carotenoid, which is useful as water quality improving agent for aquaculture and sewage treatment or leaf fertilizer.    ADVANTAGE - The method effectively utilizes high temperature pyrolysis product of cellulose biomass for producing provides carotenoid, in an eco-friendly manner.
NOVELTY - This utility model claims a kind of solid aerobic fermentation sludge treatment and treatment integrated device, comprising a pre-mixing device, transmission device, a lifting device, a fermentation tank, the fermentation tank and sieving device. Pre-mixing device and lifting device are connected through the transmitting device, a lifting device and a fermentation tank is connected with the first groove and the second fermentation yeast tank is connected, the second fermentation tank is connected with the screening device. The first fermenter comprises four compartments, each compartment of the lower part is provided with a hollow storage tank, each of the hollow storage tank containing a heat-conducting medium. This utility model can compact the device structure design to realize the aerobic fermentation of organic matter in the sludge, the reduction, stabilization and harmless and recycling treatment.
NOVELTY - This utility model claims a full automatic fertilizer turning machine, which is suitable for a fertilizer station or a small mixing fertilizer factory fast for fertilizer, comprising a feeding hopper, a lifting mechanism, a blender, a storage hopper and a weighing device, wherein the stirrer is installed on the lower part of the frame through the supporting wheel assembly, a vehicle frame is provided with a walking wheel, a stirrer is set at the side lifting frame, lifting hopper capable of moving up and down on the lifting frame, a weighing mechanism is set with the storage hopper by the lifting mechanism, wherein the stirrer is provided with feeding hopper, and a stirring blade, stirrer under a roller assembly, a blender is installed with big gear ring so that the stirrer capable of rotating, stirrer device is provided with high automation degree, uniform taing, energy-saving and environment-friendly, wide adaptability and so on.
NOVELTY - A kind of marsh gas tank, marsh gas relates to the technical field, comprising a fermentation tank, a collecting tank, wherein the fermentation tank is not two layers which are respectively located under the biogas slurry layer and water layer at the upper part of the marsh gas tank comprises a fermentation tank of the greenhouse, the top part of the greenhouse is made of transparent material. This utility model has simple structure, good fermentation effect, is convenient to manage.
NOVELTY - This utility model claims a constant temperature automatic slag-discharge biomass pool, comprising a fermentation tank, an electromagnetic valve, a heater, a stirrer, a liquid level switch, the liquid level switch, a temperature sensor, a controller and a motor, the fermentation tank is provided with a material inlet, a heater installed in the fermentation tank, and connected with the main controller by a stirrer is installed in the fermentation tank, and connected with the motor is connected with the main controller, a temperature sensor is set on the fermenting tank, and connected with the total controller, a liquid level switch and a liquid level switch is installed on the inner wall of the fermenting tank, and connected with the main controller, a controller and a motor arranged in the fermentation pool. The device can keep the constant temperature state, tank, at the same time, provided with liquid level control of the liquid level switch can automatically discharge the redundant biogas residue and biogas slurry according to cell, which not only can keep high yield of marsh gas in the tank, but also can save the labour time cleaning the redundant biogas residue and biogas slurry.
NOVELTY - Separation and purification of epigallocatechin gallate (EGCG) by medium-pressure polymeric reversed-phase chromatography comprises (i) carrying out acidification of aqueous ethanol solution using organic acid to obtain acidified aqueous ethanol solution; (ii) dissolving tea polyphenol raw material in acidified aqueous ethanol solution as a mobile phase to obtain mixed solution; (iii) filtering using microfiltration film; (iv) degassing and placing statically; (v) subjecting to chromatographic separation; (vi) passing through nanofiltration film and concentrating; and (vii) freeze-drying.    USE - The method is useful for separation and purification of EGCG by medium-pressure polymeric reversed-phase chromatography (claimed).    ADVANTAGE - The method: is simple, ensures convenient operation, has short production period and produces high purity product; utilizes ethanol as a solvent, which is non toxic and can be recycled; is environmentally friendly and avoids the safety hazard caused by using organic solvent.    DETAILED DESCRIPTION - Separation and purification of epigallocatechin gallate (EGCG) by medium-pressure polymeric reversed-phase chromatography comprises (i) carrying out acidification of aqueous ethanol solution using organic acid to obtain acidified aqueous ethanol solution; (ii) dissolving tea polyphenol raw material in acidified aqueous ethanol solution as a mobile phase to obtain mixed solution; (iii) filtering the mixed solution using microfiltration film with pore size of less than less than 1 mu m; (iv) degassing the filtrate and placing statically; (v) subjecting the filtrate to chromatographic separation using CCTRI-1 monodispersed polymeric reversed phase chromatographic column; (vi) passing the fractions through nanofiltration film, if EGCG content is more than 97%, or again performing step (v), if the EGCG content is less than 97%, and concentrating to 6-20%; and (vii) subjecting the concentrate to freeze-drying.
NOVELTY - Planting method for producing agricultural product, comprises adding angelica traditional Chinese medicine dregs and biological organic fertilizer to water to produce liquid biofertilizer, performing homogenization treatment of the biofertilizer, spraying edible fungi angelica extract nutrient solution to fungus, preparing edible fungi dregs in a culture medium and then performing homogenization treatment to obtain a fungi and angelica effective composition for 10-15 days and then extracting, adding a bast tissue to the extract, and adding water to the extract to uniformly dilute.    USE - The planting method is useful for producing an agricultural product (claimed).    ADVANTAGE - The agricultural product has enhanced health care effect.
NOVELTY - Producing liquid ammonia comprises performing three-level segregation of crude ammonia gas to remove most of water and hydrogen sulfide under conditions, cooling the segregated ammonia gas to a temperature of -30 to 20 degrees C to convert the ammonia gas into liquid ammonia, increasing pressure of the liquid ammonia to 1.3-3 MPa, and removing water and hydrogen sulfide from the liquid ammonia in a desulfurization dehydrator at a temperature of -30 to 50 degrees C and an operation pressure of 1.3-3 MPa.    USE - The method is useful for producing liquid ammonia (claimed).    ADVANTAGE - The method enables production of the liquid ammonia without producing secondary pollutions in a safe and a reliable manner.    DETAILED DESCRIPTION - Producing liquid ammonia comprises performing three-level segregation of crude ammonia gas to remove most of water and hydrogen sulfide under conditions, where the conditions of the three-level segregation includes a temperature of a first-level segregation of 120-200 degrees C and a pressure after the segregation of 0.6-2 MPa, a temperature of a second-level segregation of 90-150 degrees C and a pressure after the segregation of 0.55-1.5 MPa and a temperature of a third-level segregation of 30-70 degrees C and a pressure after the segregation is 0.5-1 MPa, cooling the segregated ammonia gas to a temperature of -30 to 20 degrees C to convert the ammonia gas into liquid ammonia, increasing pressure of the liquid ammonia to 1.3-3 MPa, and removing water and hydrogen sulfide from the liquid ammonia in a desulfurization dehydrator at a temperature of -30 to 50 degrees C and an operation pressure of 1.3-3 MPa.
NOVELTY - N-phosphonomethyliminodiacetic acid (PMIDA) is prepared by putting iminodiacetic acid and water to reaction kettle, controlling temperature to less than 80 degrees C, preferably less than 60 degrees C, and dropping phosphorus trichloride; keeping temperature for 0.5-10 hours, preferably 0.5-2 hours, raising temperature to 90-120 degrees C, preferably 105-112 degrees C, adding formaldehyde edge, after finishing dripping, and preserving temperature for 0.5-5 hours, preferably 1-2 hours; and in reaction kettle adding quantitative water, measuring solution in normal pH value of discharge pressure and filtering.    USE - Method for preparing glyphosate intermediate iminodiacetic acid (claimed).    ADVANTAGE - The method saves energy and has reduced technique steps. It also has reduced process equipment, environmental protection and emission reduction.    DETAILED DESCRIPTION - N-phosphonomethyliminodiacetic acid is prepared by:    (A) putting iminodiacetic acid and water to reaction kettle, controlling temperature to less than 80 degrees C, preferably less than 60 degrees C, and dropping phosphorus trichloride at vacuum degree of - 0.01 to - 0.1 MPa, preferably - 0.01 to - 0.03 MPa;    (B) after dropping, keeping temperature for 0.5-10 hours, preferably 0.5-2 hours, raising temperature to 90-120 degrees C, preferably 105-112 degrees C, adding formaldehyde edge, after finishing dripping, and preserving temperature for 0.5-5 hours, preferably 1-2 hours; and    (C) in reaction kettle adding quantitative water, measuring solution in normal pH value of discharge pressure and filtering to obtain N-phosphonomethyliminodiacetic acid.
NOVELTY - Producing biological organic fertilizer, comprises taking pig manure (19-22%), dairy manure (12-15%), chicken manure (3%), sheep manure (5%), lees (5%), vinegar residue (2%), cassava bagasse (6%), furfural residue (6%), clean river mud (8%), corn straw (10%), straw (4%), rape straw (6%), cottonseed (4%), plant ash (3%), 1% Azotobacter, 0.8% potassium bacteria (sic), 1.2% rhizobium bacteria and 1.5% phosphorus activator as raw material.    USE - The process is useful for producing biological organic fertilizer (claimed).    ADVANTAGE - The biological organic fertilizer improves physical and chemical properties of the soil and quality of agricultural products, and stimulates growth of crops.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the fertilizer which comprises crushing the manure, lees, vinegar residue, cassava bagasse, furfural residue and clean river mud in a fermenting tank, crushing the remaining components and adding to the fermentation tank.
NOVELTY - The utility model claims a kind of using electronic bombardment in a hydrogen-oxygen separating device, comprising a water storage tank, a heating device is set on the lower part of the reservoir, vapor cavity is provided with the upper part of the water storage tank, the air outlet is connected with the steam cavity on the steam chamber is provided with a cathode, the steam cavity upper part is provided with a positive electrode, a negative electrode and a positive electrode through the power supply, the water storage tank is provided with a hydrogen storage tank and oxygen. The beneficial effect of the utility model is: the water of water molecules through hydrogen bond so as to link to, water molecule is composed of composed of a hydrogen-oxygen element. Hydrogen, oxygen combustion-supporting, the product is pure water, impossible to the environment pollution. Energy from the water in a low cost separating hydrogen and oxygen, or benzotriazole can solve energy problem. It can be widely applied to various aspects of spaceflight, aviation, road traffic and thermal power generation and so on.    USE - Hydrogen-oxygen separating device used in spaceflight, aviation, road traffic and thermal power generation.    ADVANTAGE - The device solves energy problem.
NOVELTY - Organic waste composite fertilizer comprises modified furfural slag, sheep manure, corn straw, rape seed cake fertilizer and benzylpenicillin at ratio of 0.45-0.55:0.2-0.27:0.15-0.3:0.03-0.05.    USE - Organic waste composite fertilizer.    ADVANTAGE - The fertilizer improves soil water holding capacity, increases total porosity and capillary porosity i.e. non-capillary porosity, and can obviously increase soil organic matter.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a preparation of organic waste composite fertilizer comprising mixing modified furfural slag, sheep manure, corn straw, and rape seed cake fertilizer to obtain mixture, adding 4.5-5 kg CO(NH2)2 in each ton of mixture, with carbon/nitrogen (C/N) ratio of 25:1, adding water to adjust water content of 5-55%, mixing uniformly, filling pre-dug depth of 2, width of 2.5, length of 4 m, stacking and fermenting for 15 minutes and drying for 28-30 days, and passing 20 mm meshes sieve to obtain product.
NOVELTY - Preparing reducing monosaccharide from biomass hydrolysis comprises: putting lignocellulose biomass in a stirring reactor, hydrolyzing under a normal pressure or a pressure close to the normal pressure by using a dilute acid as a catalyst; washing residues after the hydrolysis is finished; and performing enzyme hydrolysis in the same reactor.    USE - The method is useful for preparing reducing monosaccharide from biomass hydrolysis (claimed).    ADVANTAGE - With the method, pretreatment of the biomass can be carried out in a mild condition and performed with enzyme hydrolysis in the same reactor, thus significantly reducing pretreatment cost.
NOVELTY - Synthesizing 7- alpha -methoxy-3-desacetylcephalothin benzathine salt comprises (a) adding cephalothin into organic solvent, adding sodium methoxide and halogenated reagent, carrying out 7-methoxy substitution reaction and hydrolyzing to obtain 7- alpha -methoxycephalothin; (b) adding 7- alpha -methoxycephalothin in an aqueous solution and converting into sodium salt or ammonium salt; (c) carrying out deacetylation of sodium salt or ammonium salt in aqueous solution by enzymolysis reaction to obtain 3-deacetylated product; and (d) reacting 3-deacetylated product with N,N'-dibenzyl ethylenediamine diacetate.    USE - The method is useful for synthesizing 7- alpha -methoxy-3-desacetylcephalothin benzathine salt (claimed).    ADVANTAGE - The method has mild reaction conditions and simple operation; and is environmentally friendly and suitable for industrial production.    DETAILED DESCRIPTION - Synthesizing 7- alpha -methoxy-3-desacetylcephalothin benzathine salt comprises (a) adding cephalothin into organic solvent, adding sodium methoxide and halogenated reagent at -100 to -60 degrees C, carrying out 7-methoxy substitution reaction to obtain 7-methoxy substituted product and hydrolyzing to obtain 7- alpha -methoxycephalothin; (b) adding 7- alpha -methoxycephalothin in an aqueous solution and converting into sodium salt or ammonium salt; (c) carrying out deacetylation of sodium salt or ammonium salt in the aqueous solution through enzymolysis reaction at 10-40 degrees C to obtain 3-deacetylated product; and (d) adding 3-deacylated product in the aqueous solution and reacting with N,N'-dibenzyl ethylenediamine diacetate to obtain 7- alpha -methoxy-3-desacetylcephalothin benzathine salt.
NOVELTY - Separating podophyllotoxin and kaempferol from Podophyllum hexandrum comprises: soaking P. hexandrum powder in solvent at 1:5 solvent and powder mass ratio, reacting at room temperature for 24-100 hours, separating podophyllotoxin and podophyllotoxin slag; adding 0.5-5% alkali solution to podophyllotoxin slag, adjusting pH to 8-12, filtering to obtain product C; taking liquid portion of C, adding 0.5-10% acid solution, adjusting pH to 2-5, filtering, discarding liquid, collecting product E; and drying and roasting solid E, dissolving in solvent, and recrystallizing.    USE - Method for separating podophyllotoxin and kaempferol from P. hexandrum (claimed).    ADVANTAGE - The method is simple and does not need silica gel or resin column to obtain pure product. It has low energy consumption, low equipment investment and low production cost.    DETAILED DESCRIPTION - Separating podophyllic ester and kaempferol from P. hexandrum powder comprises: soaking P. hexandrum powder in solvent at 1:5 solvent and powder mass ratio, reacting at room temperature for 24-100 hours, separating podophyllotoxin and podophyllotoxin slag; adding 0.5-5% alkali solution to podophyllotoxin slag at 1:15-20 mass of slag/volume of solution ratio, adjusting pH to 8-12, filtering to obtain product C; taking liquid portion of C, adding 0.5-10% acid solution, adjusting pH to 2-5, filtering, discarding liquid, collecting product E; and drying and roasting solid E, dissolving in solvent at 1:1-20 mass of powder/volume of solvent ratio, recrystallizing to obtain kaempferol. The solvent is ethanol, methanol, toluene, benzene, chloroform or methylene chloride.
NOVELTY - Extracting hypaphorine from Caragana microphylla comprises crushing small leaf of Caragana microphylla into 20-80 meshes of powder, performing supercritical extraction of the powder using carbon dioxide and entrainer at a pres sure of 5-9 MPa and temperature of 40-60?oC for 30-60 minutes, adding water to the extract to dissolve and adding ethanol to precipitate with pH of 5-6, separating obtained product using high speed counter-current chromatography, on line monitoring the product using a UV detector, collecting obtained product and decompressing and drying the product.    USE - The method is useful for hypaphorine from Caragana microphylla.    ADVANTAGE - The method allows simple extraction of the hypaphorine with high extraction rate and purity in an eco-friendly manner.
NOVELTY - 3,4-Dichlorobenzotrifluoride and resorcinol as raw materials are reacted at 50-200 degrees C in a catalysis system comprising a copper-containing compound, an acid binding agent and a N-alkylpyridine ion liquid (I). The reaction liquid is subjected to separation purification to obtain 1,3-bis(2-chloro-4-trifluoromethylphenoxy)benzene as intermediate of herbicide. The copper compound is copper oxide, copper chloride, copper bromide, copper acetate or copper sulfonate. The acid-binding agent is sodium hydroxide, potassium hydroxide, potassium carbonate or sodium carbonate.    USE - Synthesis of 1,3-bis(2-chloro-4-trifluoromethylphenoxy)benzene used as intermediate of herbicide.    ADVANTAGE - The herbicide intermediate of high purity is produced at high yield using reduced amount of solvent without affecting the environment. The method reduces discharge of three wastes.    DETAILED DESCRIPTION - 3,4-Dichlorobenzotrifluoride and resorcinol as raw materials are reacted in ratio of 2-10:1 at 50-200 degrees C in a catalysis system comprising a copper-containing compound, an acid binding agent and a N-alkylpyridine ion liquid of formula (I). The reaction liquid is subjected to separation purification to obtain 1,3-bis(2-chloro-4-trifluoromethylphenoxy)benzene as intermediate of herbicide. The copper compound is copper oxide, copper chloride, copper bromide, copper acetate or copper sulfonate. The acid-binding agent is sodium hydroxide, potassium hydroxide, potassium carbonate or sodium carbonate. The mass ratio of copper-containing compound and resorcinol is 0.01-0.2:1. The mass ratio of acid binding agent and resorcinol is 0.1-2:1. The mass ratio of N-alkyl pyridine ionic liquid to resorcinol is 0.1-2:1.    R=1-8C alkyl;and    X-=F4B-, F6P-, F3CSO3- or (F3CSO2)2N-.
NOVELTY - Invention relates to microbiological industry, yeast and alcohol production and is intended for treatment of liquid organic wastes, mainly, manure or excrements to produce pollution-free organic fertilisers and combustible biogas. Proposed biological reactor comprises body with partitions. Reactor body represents a vertical sealed and heat-isolated tank with walls connected by dome or stiff roof to create a space between biomass surface and roof for pre-accumulation of biogas. Tank inner space is divided by partitions in, at least, two sections. Said partitions are installed vertically at the tank center and over bioreactor height and connected with the tank walls. Biomass overflow openings are made in every partition between first section, between midsections and between last section, at lower peripheral part. Bottom of every said section is inclined both from the center to periphery and toward the next section. Every section if equipped with manifold for makeup feed, heat exchanger, mixer, pH and eH gages and temperature gage. First section loading assy is composed of the manifold with shutoff valves for biomass loading while discharge assembly represents the manifold with shutoff valves for discharge of risen biomass. Biomass level gages are arranged at top lateral part of the last section.    USE - Process engineering.    ADVANTAGE - Higher efficiency, lower costs.11 cl, 6 dwg
NOVELTY - Sericite, sepiolite, smectite and illite are mixed to obtain a mixture. The mixture is pulverized to 400-600 mesh and heated at 400-600 degrees C. 1-3 l Water is added per 1 kg mixture and the mixture is formed into particles having a size of 10-50 mu m, to obtain ceramics. Sericite taken from Eumseong-gun has a germanium content of 20-60 ppb, a silver content of 20-40 ppb, and a cerium content of 10-20 ppb.    USE - Manufacture of ceramics for fertilizers, construction materials, fungicides, antidotes, health supplements, dermatological agents, animal feed additives, soil improvers, adsorption agents for malodor and poisonous gases, deodorizing materials, electromagnetic-interference shielding materials, clothing, and yarn.    ADVANTAGE - The method enables manufacture of ceramics which provide environmentally-friendly construction materials, saving unique property of natural minerals.
NOVELTY - The generators (15,16) is provided with a main water tank, a separator tank, a two gas generators, a gas filter tank, a gas appliance, a cooling/heating exchanger, an appliance heat, a circulation pump and a power inverter. The power inverter switches the generators in such frequency to provide the decomposition of water into gas.    USE - Generators for production of gas.    ADVANTAGE - Frequency generator generates a certain frequency to provide the decomposition of water in the two halves of an even number of generators at the lowest power the highest production of gas, so that gas production efficiency can be improved and manufacturing cost can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the of inverter power connection.    Switch (14)    Generators (15,16)
NOVELTY - A catalyst fine particles provided with an outermost layer which covers the central particles are prepared (S1), and electrochemical surface area of the catalyst fine particles is computed. The amount of hydrogen peroxide is computed (S2) by performing oxygen reductive reaction measurement of the catalyst fine particles, and coverage of the outermost layer which covers the central particles is computed (S3) from the value of the electrochemical surface area and production amount of the hydrogen peroxide. Thus, the coverage calculation method of catalyst fine particles is enabled.    USE - Coverage calculation method of catalyst fine particles used for evaluating catalyst fine particles (claimed) for catalytic reaction in fuel cell.    ADVANTAGE - The catalyst activity and quality of the catalyst fine particles is evaluated accurately by calculating coverage value of the catalyst fine particles.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for evaluation method of catalyst fine particles, which involves comparing (S4) computed coverage value with a predetermined reference value. When the computed coverage value is more than the reference value, the catalyst fine particles are qualified (S5). When the computed coverage value is less than the reference value, the catalyst fine particles are disqualified, and the process of computing the coverage is further carried out.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow chart explaining evaluation method of catalyst fine particles. (Drawing includes non-English language text)    Preparing catalyst fine particles (S1)    Computing electrochemical surface area and product amount of hydrogen peroxide (S2)    Computing coverage of catalyst fine particles (S3)    Comparing coverage of catalyst fine particles with predetermined reference value (S4)    Determining catalyst fine particles to be qualified (S5)
NOVELTY - Preparing a 4-cyclopropyl-1,2-difluoro-benzene compound (VI) comprises providing a 1-(3,4-difluorophenyl)propan-1-ol compound (V), converting the hydroxyl group of (V) to a better leaving group, and converting the obtained compound by cyclization in the presence of a base to provide (VI).    USE - The process is useful for preparing: (VI) and ticagrelor (all claimed), which is useful for treating or preventing thrombotic events such as stroke, heart attack, acute coronary syndrome or myocardial infection with ST elevation, other coronary artery diseases and arterial thrombosis; and (trans-(1R,2S)-2-(3,4-difluorophenyl)cyclopropylamine). No biological data given.    ADVANTAGE - The process provides (VI) with high chiral purity in an environmentally friendly manner.    DETAILED DESCRIPTION - Preparing a 4-cyclopropyl-1,2-difluoro-benzene compound of formula (VI), comprises providing a 1-(3,4-difluorophenyl)propan-1-ol compound of formula (V), converting the hydroxyl group of (V) to a better leaving group, and converting the obtained compound by cyclization in the presence of a base to provide (VI).    R = group convertible to carboxyl group comprising CN, trihalomethyl or COOR1; and    R1 = linear or branched 1-6C-alkyl.    INDEPENDENT CLAIMS are included for:    (1) propyl 4-(3,4-difluorophenyl)-4-hydroxy-butanoate (Va) or 4-(3,4-difluorophenyl)-4-hydroxy-butanenitrile (Vb);    (2) propyl (1R)-2-(3,4-difluorophenyl)cyclopropanecarboxylate (VIa), (1R)-2-(3,4-difluorophenyl) cyclopropanecarbonitrile (VIb) or methyl (1R)-2-(3,4-difluorophenyl)cyclopropanecarboxylate (VIc);    (3) a metal salt of a (1R)-2-(3,4-difluorophenyl)cyclopropanecarboxylic acid (VII); and    (4) a (1R)-2-(3,4-difluorophenyl)cyclopropanecarboxylate compound of formula (VIIa).
NOVELTY - Bioreactor comprises: an elongated reactor vessel (2) with a bottom (4), on which the biomass is placed, and a first end (12) and a second end (14); a first gas-tight port (16) for loading the reactor vessel with a fresh biomass arranged at the first end; a biogas extraction port; and a second gas-tight port for discharging spent biomass from the reactor vessel, which is arranged at the second end.    USE - The bioreactor is useful for methanizing biomass by dry fermentation (claimed).    ADVANTAGE - The bioreactor reduces the risk of contamination of the biomass during the fermentation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biogas plant comprising multiple of the above mentioned biogas reactors for generating biogas in a batch-operation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional representation of the bioreactor with two ports.    Reactor vessel (4) Bottom (12) First end (14) Second end (16) First gas-tight port (2)
NOVELTY - A coating process of coating material involves contact process which makes to-be-treated material contact a supercritical solvent at precursor and/or supercritical fluid (2) that carries out dissolution of coating material, and heating process which heats to-be-treated material to temperature to which solubility with respect to precursor and/or supercritical solvent of coating material falls when absorption factor of to-be-treated material irradiates the electromagnetic waves of wavelength higher than absorption factor of the supercritical solvent to to-be-treated material.    USE - Coating process of coating material used for manufacturing electrode for fuel cells (claimed).    ADVANTAGE - Yield of coating materials is improved. Coating volume of coating material, electrolyte resin and metal catalyst is ensured.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a manufacture of electrode for fuel cells which involves contact process which makes carbon nanotube (3) orientated on board (4) contact a supercritical fluid (2) which dissolves precursor and/or electrolyte resin of metal catalyst in supercritical solvent, and heating process which heats carbon nanotube to temperature to which solubility with respect to precursor of metal catalyst and/or supercritical solvent of electrolyte resin falls when absorption factor of the carbon nanotube irradiates the electromagnetic waves of wavelength higher than the absorption factor of supercritical solvent to carbon nanotube.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the temperature distribution at the time of electromagnetic irradiation and 1st electromagnetic irradiation form in the coating process. (Drawing includes non-English language text).    Pressure vessel (1)    Supercritical fluid (2)    Carbon nanotube (3)    Board (4)    Base layer (5)
NOVELTY - Free-fatty acid residual oil and monohydric alcohol are reacted in presence of cation exchange resin, esterification process is carried out, and resultant product is subjected to back stage treatment process which processes the esterification production liquid with anion exchange resin, to obtain fatty acid ester.    USE - Manufacture of fatty acid ester used as biodiesel diesel (claimed).    ADVANTAGE - The method enables efficient manufacture of fatty acid ester with high quality, high conversion ratio and high purity.
NOVELTY - An anaerobic water purification system (2) comprises a container (4) for liquid for treatment provided during use with a sludge bed; a supply conduit connected to the container for supplying the liquid for treatment; a distribution system connected to the supply conduit for distributing the liquid over the sludge bed from above; a carrier material which is arranged during use in the container and to which anaerobic sludge material can attach; and a gas roof arranged at or on the container and provided with a volume which can be adapted during use to the biogas production.    USE - Anaerobic water purification system for treating liquid, particularly wastewater flow from the process industry.    ADVANTAGE - The system can carry out purification in a more effective manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) conversion kit for converting an existing container to an anaerobic water purification system, comprising a gas roof, connecting mechanism, supply and discharge mechanism, and a carrier material; and    (2) a method for anaerobic treatment of liquid in a container comprising arranging a gas roof on a container and a discharge for the biogas; providing on or in the container, supply conduit(s) and a distribution system for distributing the liquid from above over a sludge bed provided in the container; a quantity of carrier material; and a discharge conduit for guiding treated liquid out of the container from below, where the discharge conduit is operatively connected to a riser pipe for keeping the container filled during use.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the anaerobic water purification system.    Anaerobic water purification system (2)    Container (4)    Gas membrane (12)    Outer roof (14)    Pump (20)
NOVELTY - The method involves arranging fluidized catalytic cracking (FCC) and hydrocracking (HC) processes in parallel. Feedstock segregation is performed to each of the processes depending on a content of aromatic hydrocarbons. A common fractioning column (8) is arranged for both output streams from the HC and FCC processes. An unconverted fraction is recycled towards the FCC unit. A portion of a HC reactor effluent is used to preheat a feed to a same reactor for reducing a temperature before mixing with a FCC unit effluent and entering the common fractioning column.    USE - Method for producing diesel fuel e.g. petrodiesel and biodiesel, which is used for a diesel engine and a heating equipment.    ADVANTAGE - The utilization of the FCC and HC processes produces the diesel fuel with improved yield and quality, and allows control of carbon balance in the FCC unit.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a process for recycling a portion of a decanted gasoil stream to a HC unit, mixing a remaining portion of a stream with an unconverted heavy gasoil, and recycling a resulting mixed stream towards a FCC unit.    Hydrocarbon stream (1)    HC unit (3)    FCC unit (4)    Hydrogen stream (5)    Common fractioning column (8)
NOVELTY - Method for processing biomass containing cellulosic material, involves (a) contacting biomass below pH 6.5 with a magnesium hydroxide (suitable amount) to increase the pH of the biomass to 7, (b) treating the biomass comprising magnesium hydroxide at an elevated temperature and pressure, and (c) contacting the treated biomass with saccharification enzymes under conditions sufficient to hydrolyze at least portion of the cellulose to fermentable sugars.    USE - The method is useful for processing biomass (claimed).    ADVANTAGE - The method does not require acid pretreatment step, and utilizes magnesium hydroxide for providing a safer alternative to using ammonium hydroxide for pH adjustment, a more stable, buffered environment for improved operability in pH control, with similar or improved conversion of biomass to fermentable sugars, and similar or improved reduction of inhibitors during the subsequent hydrolysis or saccharification process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for acid-free method for processing biomass containing a cellulosic material, which involves (a) contacting the biomass with magnesium hydroxide at a concentration suitable to raise the pH of the biomass at least 0.2 pH units to 4-8, (b) treating the biomass comprising magnesium hydroxide at an elevated temperature and pressure, and (c) contacting the treated biomass following (a) and (b) with saccharification enzymes under conditions sufficient to convert at least a portion of the cellulose to fermentable sugars.
NOVELTY - Producing ethanol (M1) comprises hydrogenating acetic acid in the presence of a catalyst comprising at least one active metal and cesium on a support comprising tungsten or their oxides.    USE - The process is useful for producing ethanol (claimed) that is used in fuels, solvents, chemical feedstocks, pharmaceutical products, cleansers, sanitizers, hydrogenation transport or consumption.    ADVANTAGE - The process utilizes catalyst that exhibits increased activity, stability (productivity decline of less than 6% per 100 hours of catalyst usage) and performance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing product (M2) having ethanol comprising contacting a feedstock comprising acetic acid and hydrogen in a reaction zone at hydrogenation conditions including a temperature of 125-350 degrees C, a pressure of 10-3000 kPa and a hydrogen to acetic acid molar ratio of greater than 2:1, with a catalyst composition comprising platinum and/or palladium, tin and 0.01-0.5 wt.% cesium on a silica support material comprising from 0.1-50 wt.% tungsten or their oxides.
NOVELTY - A Ettlia sp. strain (KCTC 12109BP), is new.    USE - The strain of Ettlia sp. is useful in composition, preferably food composition and cosmetic composition, for producing biodiesel and carotenoid material (all claimed), and in drug.    ADVANTAGE - The Ettlia sp., preferably Ettlia sp. strain YC001 has superior carbon dioxide fixation ability and lipid producing ability, enables content of lipid and composition of fatty acid to be controlled according to cultivation condition and/or cultivation period, production of high quality biofuel, and high industrial availability as large amount of carotenoid and pigment can be accumulated in cells.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for composition, which comprises homogenate of the above-mentioned strain or the strain.
NOVELTY - The bioreactor (100) has two gas supply heads (60,61) that are arranged vertically within a culture barrel (20). First and second injection nozzles are connected to outer peripheral surface of the gas supply heads, and are arranged at certain angle downward toward the inner wall surface of the culture barrel. The gas from the first injection nozzle (62) is sprayed downward toward the inner wall surface of the culture barrel. The gas from the second injection nozzle (63) is sprayed upward toward the central portion of the culture barrel.    USE - Methane fermented microorganism bioreactor for inducing activation of anaerobic digestion of organic waste such as sewage and wastewater sludge used for recovery of energy acid including the thermal power, electricity etc.    ADVANTAGE - The methane fermented microorganisms can be cultivated conveniently in the culture barrel containing organic contaminants. The methanogenesis yield can be increased and the anaerobic digestion efficiency of the organic waste can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the bioreactor.    Culture barrel (20)    Heating tube (50)    Gas supply heads (60,61)    Controller (70)    Bioreactor (100)
NOVELTY - Fermentation end-product(s) are produced by combining first biomass comprising non-cellulosic saccharides with a saccharide stream comprising 6C monosaccharides to produce a blended feedstock in a broth; contacting the blended feedstock with biocatalysts; and fermenting the non-cellulosic saccharides of the first biomass and the 6C monosaccharides of the saccharides stream to produce fermentation end-products comprising alcohol and polyol. An alcohol yield is increased and a polyol yield is decreased in comparison to fermentation of the first biomass without the saccharide stream.    USE - Method for producing fermentation end-product(s) comprising ethanol and glycerol (claimed).    ADVANTAGE - The method increases alcohol yield by 1-100% relative to fermentation of the first biomass without the saccharide stream. The alcohol is produced at a rate that is faster relative to fermentation of the first biomass without the saccharide stream and the polyols yield is decreased by 1-100% relative to the non-fed batch fermentation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing a 6C-enriched hydrolysate comprising treating a biomass comprising cellulose and hemicellulose and/or lignin to solubilize the hemicellulose and/or lignin; separating the solubilized hemicellulose and/or lignin from the cellulose; and hydrolyzing the cellulose.    DESCRIPTION OF DRAWING(S) - The drawing is a graph showing trajectory of how biomass is converted from solids into liquefied 6C sugars during hydrolysis using cellulase enzymes.
NOVELTY - Manufacture of electrode material involves carrying out ultrasonic irradiation treatment of carbon material in solution of organic compound having hydrophilic property and water-containing alcohol, covalently bonding a surface of the carbon material to nitrogen-containing functional group, performing electrolytic reduction process of the carbon material, and diazotizing the resultant carbon material in sulfuric acid obtained by dissolving sodium nitrite.    USE - Manufacture of electrode material used for fuel cell (claimed). Uses include but are not manufacture of hydrogen by electrolysis of water, electrochemical sensor, oxygen-reduction catalyst electrode and biosensor.    ADVANTAGE - The method provides electrode material having excellent oxidation-reduction characteristics, without using catalyst metal e.g. platinum.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell.
NOVELTY - A seawater is subjected to ion-exchange reaction to exchange hydrogen ions for sodium ions in seawater such that the pH of seawater is lowered to less than 6.5.    USE - Treatment of seawater in electrolytic reactor used for electrolytic process for producing carbon dioxide and hydrogen gas (claimed).    ADVANTAGE - The method enables economical treatment of seawater, using anode and cathode having excellent chemical stability and electrochemical property.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for electrolytic process for producing carbon dioxide and hydrogen gas.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the acidification apparatus.    Ion-exchange compartment (12)    Anode compartments (14,16)    Tanks (201,203)    Ion-exchange apparatus (208)    Power supply (209)
NOVELTY - The hydrogen production apparatus (10) has a window portion (13) into which light, which the photocatalyst receives is injected. An electrode connection portion (42) and a pipe line connection portion are arranged by each side surface of a frame. A cathode and an anode (21), and the electrode connection portion are connected, respectively. The pipe line connection portion can be closed while connecting with the electrolyte solution accommodation space.    USE - Hydrogen production apparatus.    ADVANTAGE - A number of hydrogen production apparatus can be connected into arbitrary arrangement forms, and arranged in a space of various shape Desired quantity of hydrogen is manufactured at high efficiency, cost is reduced, and maintenance check is performed easily. The hydrogen production apparatus has small number of parts and simple structure. Adjacent hydrogen production apparatuses can be connected easily and reliably since each member and frame can be coupled easily.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the hydrogen production apparatus. (Drawing includes non-English language text).    Hydrogen production apparatus (10)    Window portion (13)    Anode (21)    Electrode connection portion (42)    Water circulation piping (61)
NOVELTY - The invention relates to a process for treating acid petroleum wastes stored in catch pits, with a view to obtaining a neutral granular product to be easily stored or used as a fuel or in the construction materials industry, and to an equipment for carrying out the process. According to the invention, the process consists in treating acid petroleum wastes with granular materials, such as coke, coal, cement, power plant ash, blast-furnace slag, followed by grinding and neutralizing the same with solid substances, such as calcium oxide, potassium oxide, to finally result in a product which is processed within a special equipment where there take place the final neutralization and grinding until the desired fineness is obtained.
NOVELTY - The apparatus has closed fermenting tank which includes inlet opening receiving sewage sludge to be processed. A horizontally arranged rotatable driving axle (11) and disks (12) are fastened in given distance on driving axle in inner space of fermenting tank. The disks are dipped into sewage in fermenting tank. The driving axle of disks is driven by motor arranged outside the tank. Finishing knife (16) is arranged between disks. The finishing edges are provided parallel to side surfaces of corresponding disks and are arranged in pre-defined distances from disks.    USE - Apparatus for producing biogas from sewage sludge.    DESCRIPTION OF DRAWING(S) - The drawing shows the apparatus for producing biogas from sewage sludge.    Horizontally arranged rotatable driving axle (11)    Disk (12)    Finishing knife (16)
NOVELTY - The steam boiler (300) has an outer shell (302) in which two inner tubes (318,320) are arranged spaced away from one another. A twisted ribbon (336,338) is positioned inside each of the inner tubes.    USE - Steam boiler for generating steam used in reforming reaction for generating hydrogen used in fuel cell system (claimed).    ADVANTAGE - A surface area between two fluids is increased due to the spacing between the inner tubes, thus heat transfer to the water is increased, allowing steam to form over a shorter distance. The twisted ribbon positioned inside each of the inner tubes facilitates mixing of the water as it flows through the inner tubes, thus heat transfer is further increased, further reducing the distance over which steam is formed, providing a more compact steam boiler while efficiency of the steam boiler is maintained or increased.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a steam reformer.    DESCRIPTION OF DRAWING(S) - The drawing shows an enlarged cross-sectional view of part of the steam boiler.    Steam boiler (300)    Outer shell (302)    Inner tubes (318,320)    Wires (324,326)    Twisted ribbons (336,338)
NOVELTY - The method involves using crude gas (3) as a fluidized medium, and carrying out cooling and removal of tar components from the crude gas. The crude gas is cooled indirectly in a fluidized bed cooler (1) and simultaneously contacted with a solid as a fluidizable. The fluidizable has adsorptive properties. The cooling of the fluidized bed takes place with the boiling water by a cooling register (2). The temperature is maintained in the cooling register by stabilized pressure. The cooling register of a liquid coolant is flowed with a temperature of over 50 degree Celsius.    USE - Method for treatment of crude gas from gasification of carbonaceous materials, such as wood, crop residues, specifically produced biomass, waste burly fuels or coal in a fluidized bed cooler.    ADVANTAGE - The method involves using raw gas as a fluidized medium, and carrying out cooling and removal of tar components from the crude gas, and thus enables reducing effort for recycling quench water to remove deposited dust and tar from the quench water, and enables reducing great expense by removing indirect cooling of the gas, and ensures simultaneous cooling of the gas and tar removal from the crude gas in terms of gas purification by avoiding large amounts of waste water, and enables preventing reaction of carbon monoxide in the sense of a declining boudouard reaction extent by rapid cooling and by efficiently setting of the boudouard equilibrium tar, and enables avoiding condensation reactions of primary tar components to high molecular tar products for simultaneous refrigerating of the gas and tar removal from the raw gas in the sense of a gas cleaning.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of crude gas treatment method.    Fluidized bed cooler (1)    Cooling register (2)    Raw gas (3)    Dust collector (8)    Gas cooler (9)
NOVELTY - The system has fuel cell unit (2) that generates power using fuel gas, and system main portion forces circulation of gas including fuel gas between fuel cell unit and fuel generation unit. A gas circulation volume setting unit determines the circulation volume of gas circulating between fuel cell unit and fuel generation unit in relation to estimated value of power demand per unit time at given instant. Setting unit sets circulation volume of gas circulating between fuel cell unit and fuel generation unit such that circulating volume per unit time at given instant is attained.    USE - Secondary battery type fuel cell system for generating electric power supplied to domestic various electric appliances.    ADVANTAGE - Lack of fuel gas can be prevented from being generated by making the unit time into comparatively long time according to the fuel cell system, without requiring fine control of supply amount of fuel gas. Since the fuel gas is not used in the fuel cell unit again supplied and utilized for the fuel cell unit by circulation according to the fuel cell system, the uselessness of fuel gas can be prevented from being generated. Operating efficiency of the fuel cell system can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fuel cell system. (Drawing includes non-English language text)    Fuel generation unit (1)    Fuel cell unit (2)    Container (3)    Gas distribution channel (5)    Controller (7)
NOVELTY - A kind of used for the dust chimney device for steam recovery of urea prilling tower, mainly solving the urea dust from entering the atmosphere to pollute the environment with the flue gas. Wherein the dust chimney device for steam recovery further comprises a bottom vertical flue (4), the top end of the vertical gas channel (2) and the bottom end of the vertical gas channel (4) passes through a dust collecting groove (7) is inclined flue (5) are connected, wherein the top end of a vertical gas duct (2), and the bottom end of vertical flue (4) and inclined flue (5) are arc transition, and the flue are cylindrical, the inclined flue (5) and the outer wall is attached with a coated anti-corrosive material is glass fibre reinforced plastic layer (6), the dust collecting groove (7) by a movable door is closed. One is used for the dust chimney device for steam recovery of urea prilling tower, it can effectively control the discharged into the dust in the air, improves the production efficiency, which meets our country saving energy and reducing the emission.
NOVELTY - The utility model claims a sludge and water with high solid composite processing technology for organic wastes system and comprehensive treatment, said system comprises a lime treatment system and a matched with the aerobic fermentation system, the lime treatment system is provided with a reaction device, the high temperature aerobic fermentation system is provided with aerobic fermentation device and depth decomposing device (if any), the mixing reaction device is provided with a feeding port, a feeding port and a lime mixed material outlet, the aerobic fermentation device is provided with a material inlet and a material outlet, the fermented rotten depth device (if any), and is provided with a material inlet and a fermentation depth decomposed material outlet, the device comprising a mixing workshop, fermenting workshop and depth decomposed in the same building. This utility model uses " compost + lime technology, realize the flexible switching of two kinds of processing technique is mainly used for sewage and sludge with high water content of the solid organic waste treatment.
NOVELTY - The utility model claims a room construction field, especially relates to a kind of using biological fermentation warming of the greenhouse wall composting system. And the a chamber wall composting system comprises fertilizer tank, stacking, wherein the compost tank side wall is wall and a chamber. This utility model wall and side walls as a compost tank by using greenhouse, using the agricultural waste in a cycle at the same time improves the temperature and reduces the greenhouse heating energy consumption, at the same time to realize the CO2 automatic fertilizing cold season, and the greenhouse wall reasonably;
NOVELTY - The utility model relates to an agricultural waste treatment device, comprising a tank body (1), a motor (2), a stirrer (3) and a heating device, wherein the side wall of the tank body is divided into an inner sleeve (4) and outer sleeve (5), upper part of the tank body is opened with a feeding port (6), and the bottom is provided with a discharging port (7), a discharge port is provided with a control valve, a stirrer in the tank body, and the stirrer is connected with the motor, the heating device comprises a heating pipe (8), a heater (9), a PLC (10) and temperature sensing probe (11), a heating pipe is set in the sleeve and the sleeve side wall of the tank body, a temperature sensing probe is installed on the inner wall of the tank body on the side wall of the input end of the temperature sensing probe and a PLC connected with the output end of the PLC is connected with the heater, the heater is connected with the heating pipe. This utility model can carry out precise control to the whole fermentation process waste, changes the present fermentation process control temperature is not accurate, the fermentation time, the fermentation quality.
NOVELTY - Activating bio-fermentation microbial agent involves performing primary and secondary activation using chicken manure, earthworm manure and raw mud sludge.    USE - The method is useful for activating bio-fermentation microbial agent (claimed).    ADVANTAGE - The method enables preparation of bio-fermentation microbial agent having good strain activation effect in a cost-effective manner using wide raw material source.
NOVELTY - Preparing glycyl-L-glutamine comprises protecting an N-end of glycine with tert-butoxycarbonyl anhydride to obtain N-(tert-butoxycarbonyl)-glycine, synthesizing N-(tert-butoxycarbonyl)-glycine-L-glutamine from the N-(tert-butoxycarbonyl)-glycine and L-glutamine by condensation with chloroformate through a mixed anhydride method, performing deprotection through trifluoroacetic acid to obtain a crude product of the glycyl-L-glutamine, and performing recrystallization to obtain high-purity glycyl-L-glutamine.    USE - The method is useful for preparing glycyl-L-glutamine (claimed).    ADVANTAGE - The method enables economic and easy preparation of highly purified glycyl-L-glutamine without using highly toxic solvents such as benzene in an environmentally friendly manner.
NOVELTY - Producing methane by chicken manure comprises adding crushed straw and water with mass ratio of 1:2 to wet and then adding inoculum, stirring and sealing the inoculum mixture, fermenting the sealed mixture into a fermentation tank using the straw and then adding fresh chicken manure with 91-95% of water and then diluting, discharging the dilute mixture into sealed anaerobic fermentation reactor and then fermenting to generate marsh gas, and leading out the marsh and then discharging mixed liquid material and carrying out solid-liquid separation.    USE - The methane is useful as organic fertilizer.    ADVANTAGE - The methane continuously produces a marsh gas and ensures the gas used for long time, in eco-friendly manner.    DETAILED DESCRIPTION - Producing methane by chicken manure comprises: (a) adding crushed straw and water with mass ratio of 1:2 to wet and then adding inoculum, stirring and sealing the inoculum mixture for 3-7 days, and fermenting the sealed mixture with the straw into a fermentation tank with mass ratio of 1:1 and then adding fresh chicken manure with 91-95% of water and then diluting; and (b) discharging the dilute mixture into sealed anaerobic fermentation reactor and then fermenting at 35-50 degrees C to adjust pH value of 6.8-7.2 for 12 hours in interval of 5 days to generate marsh gas, and leading out the marsh and then discharging mixed liquid material and carrying out solid-liquid separation.
NOVELTY - Water biological organic fertilizer comprises 25-35 pts. wt. leguminous plant fiber, 35-45 pts. wt. livestock manure, and 25-35 pts. wt. urban organic waste, which are fermented by 0.01-0.02 pt. wt. microbial strain to obtain compost material, and added with 0.1-0.2 pt. wt. agricultural water-retaining agent.    USE - Water biological organic fertilizer for guava (claimed).    ADVANTAGE - The water biological organic fertilizer changes waste into treasure and improves the soil structure.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of water biological organic fertilizer comprising mixing leguminous plant fiber, livestock manure, urban organic waste, and microbial strains, adding water, stirring and mixing uniformly, making the water content of the mixed material be at 50-60% degrees C, fermenting the mixed material for 10-15 days at 60-7 degrees C to obtain compost materials, drying to make the water content be at 20-40%, adding solid nitrogen, phosphorus, potassium, zinc, boron, calcium, and magnesium, satisfying the total mass fraction of nitrogen (N), phosphorus, and potassium at greater than 5%, where ratio of N, phosphorus pentoxide (P2O5), and potassium oxide (K2O) is 8-10:3-5:4-6, and the content of zinc, boron, calcium, and magnesium is greater than 0.18%, 0.03%, 0.14%, 0.16%, respectively, adding agricultural water retention agent, and uniformly mixing to obtain the product.
NOVELTY - 2-(2,5-Dioxo-2,5-dihydro-1H-pyrrol-1-yl)ethyl acetate (I) is new.    USE - (I) is useful: for inhibiting gram-positive bacteria, gram-negative bacteria and Escherichia coli; and as biomolecular probe, and polypeptide and drug molecules linker (all claimed).    ADVANTAGE - (I) is obtained from cheap raw material with low production cost. The preparation method is simple and environmentally friendly; has easy product separation; and produces high purity product with yield of 30-35%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparation of (I).
NOVELTY - Preparing florfenicol solid dispersoid comprises mixing florfenicol and carrier, adding the mixture into a high pressure reaction kettle, starting constant temperature circulating water bath and a metering pump, passing into a heater via carbon dioxide buffer tank, heating, opening the air inlet valve, starting the compressor, passing carbon dioxide into the reaction kettle so as to maintain constant pressure in the kettle, reacting the auxiliary material carrier and medicine under the action of pressure, and combining with hydrogen bond, collecting solid dispersoid, crushing, and sieving.    USE - The solid is dispersoid useful for treating bacterial diseases (caused by sensitive bacteria) of beasts and birds.    ADVANTAGE - The solid dispersoid: is prepared by combination of rapid supercritical gas expansion technology and a super micro powder technology; does not require organic solvent; has improved solubility in water, improved bioavailability; is harmless and environmentally friendly. The preparation process is simple and easy to operate.    DETAILED DESCRIPTION - Preparing florfenicol solid dispersoid comprises uniformly mixing 10-20 pts. florfenicol and 40-80 pts. carrier, adding the mixture into a high pressure reaction kettle, starting constant temperature circulating water bath and a metering pump, passing into a heater via carbon dioxide buffer tank, heating to 35-60 degrees C, opening the air inlet valve, starting the compressor, passing carbon dioxide into the reaction kettle so as to maintain constant pressure of 11.5-25.5 MPa in the kettle, fully reacting the auxiliary material carrier and medicine under the action of pressure, and combining with hydrogen bond, where the reaction time is 5-8 hours, depressurizing and opening the reaction kettle, collecting solid dispersoid, super-fine crushing the solid dispersoid, and sieving through 400 meshes screen to obtain the finished product.
NOVELTY - A kind of application in composting process of the ventilation device is composed of a hollow circular pipe and hollow circular tube II, a hollow circular pipe and hollow circular tube II is sleeved, the lower hollow circular pipe I end 1/5 is provided with a sealing ring and the 3/7 end of the lower hollow circular pipe of the closed circular ring is hollow circular tube I and the separating the space between the hollow circular tube II, a ventilation space is divided into an upper part and a lower part air space, the utility model claims a composting process ventilation device at the same time with natural ventilation, forced ventilation and ventilation function, it can widely used in composting treatment of solid waste in our country rural area and city, it can freely change direction ventilation system for compost, the air generated in the process of local temperature is not uniform, but also can be conveniently provided with a ventilation position of air uniform in compost, and is not easy to be blocked, the washing is convenient, this utility model consumes low energy consumption, pressure, and compost in oxygen uniformly, composting time is short, the environmental temperature is small, suitable for four seasons compost.
NOVELTY - Kitchen garbage slurry impurities removal machine comprises box body provided with tensioning box and driving box, chain-type impurity removing mechanism, and stirrer. The impurity removing mechanism is provided with a tension chain wheel on the tensioning box, a drive box, and a driving chain wheel driven by a power device. Upper driving transmission chain is provided with scum spraying mechanism. The tension box is provided with a precipitate outlet end in tension.    USE - Kitchen garbage slurry impurities removal machine.    ADVANTAGE - The machine can ensure precipitation of heavy material and remove inorganic substances, so as to ensure gas production effect of the anaerobic fermentation.
NOVELTY - Fertilizer comprises 55 wt.% chicken manure, 20 wt.% bran, 19 wt.% flue-cured tobacco straw, 1 wt.% effective microorganism (EM), 1 wt.% basalt powder, and 4 wt.% tea shell powder.    USE - The fertilizer is useful for killing pest and promoting growth of crops.    ADVANTAGE - The fertilizer is environmentally-friendly as it utilizes agricultural waste as nutrient, and suitable for all types of food crop, fruit and vegetables, provides rich elements as calcium, magnesium, sulfur, iron, copper, zinc and cobalt necessary for the crops, and enables the soil fertilizer efficiency to last 4 months with one time fertilization and average increase of the crop to 15% and thus reduces intensity during agricultural production and improves soil ecological balance and soil permeability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves (a) crushing and deodorizing the chicken manure, and drying the crushed manure, (b) crushing flue-cured tobacco straw, (c) uniformly mixing the chicken manure obtained in step (a) with bran and 0.6% EM, and then stacking for 25-35 days for anaerobic fermentation, where the stack is turned once for every 2-4 days, and maintaining the temperature at 35-65 degrees C, (d) adding 0.4% EM and crushed tobacco to the fermented mixture, when the temperature is reduced to 20-30 degrees C, and fermenting the above mixture for 6-8 days, where the stack is turned everyday, (e) drying the fermented mixture, until the moisture content is 25%, and (e) crushing the dried mixture and uniformly mixing the crushed mixture with basalt powder, and tea shell powder, and screening the obtained product, where the grain diameter of the product is 0.5 mm or less.
NOVELTY - Synthesis of entecavir compound (I) comprises taking Corey lactone diol as raw material, protecting hydroxyl group, reducing with lithium aluminum hydride, selectively protecting primary hydroxyl group with tert-butyl dimethylchlorosilane, performing Mitsunobu reaction with 6-substituted guanosine, removing silicon-protecting group, removing alkene, cutting ozone and reducing, removing hydroxyl alkene and removing protection.    USE - Method for synthesizing entecavir compound (I) (claimed).    ADVANTAGE - The method is simple, convenient, easy to control, environment-friendly and has cheap and easy-to-obtain raw materials. It is suitable for industrial production.    DETAILED DESCRIPTION - Synthesis of entecavir compound of formula (I) comprises taking Corey lactone diol as raw material, protecting hydroxyl group, reducing with lithium aluminum hydride, selectively protecting primary hydroxyl group with tert-butyl dimethylchlorosilane, performing Mitsunobu reaction with 6-substituted guanine, removing silicon-protecting group, removing alkene, cutting ozone and reducing, removing hydroxyl alkene and removing protection.    R=H, Ph or MeOPh;    R1=halo, OH, CSH, benzyloxy, 1-6C alkoxy or 1-6C thioalkyl;    R4,R5=H or NH2-protecting group; and    R3=halo or sulfonate.
NOVELTY - Method for preparing organic compost using duck excrements and rice hulls involves spreading rice hulls on a duck-breeding cage, mixing the rice hulls with duck excrements, fermenting microorganism cell line with the obtained mixture, and packing the fermented product.    USE - The method is useful for preparing organic compost (claimed).
NOVELTY - The utility model claims a pre-processing anaerobic biochemical adjusting device, comprising an adjusting pool, a water inlet pipe and a water outlet pipe, the adjusting tank is provided with a maintenance hole and a liquid level alarm device, an adjusting pool comprises two parallel arranged with the tank body and the tank body II, on the adjusting tank body and the tank body II is provided with a connecting pipe, the connecting pipe is provided with a control series of a tank body of the gate valve I, the tank body and the tank body II are respectively provided with not less than 2 of the diving stirrer, the tank body and the tank body II is provided with a venting hole and a biogas collecting device, a pre-processing anaerobic biochemical adjusting device adjust water storage function at the same time pre-processing of the percolate and the tank body water quality becomes uniform, which can prolong the cleaning period, is provided with explosion-proof, explosion and convenient maintenance;
NOVELTY - This utility model claims a kind of capable of measuring anaerobic fermentation biogas experiment device belongs to the technical field of experimental device technology field, comprising an anaerobic reactor (1), gas cylinder 2, a gas collecting bag (3), the one-way valve (4), a rubber stopper 5, a sampling pipe 6, gas pipe I7, a gas flow meter I8, a gas flow meter II9, rubber tube 10, a sampling pipe valve (11), gas-guide tube (II12). Carried out by improving the traditional anaerobic fermentation biogas device, control the experiment process is added into two gas flow meter, it can realize online monitoring anaerobic fermentation condition, convenient, anaerobic marsh gas volume biogas fermentation and methane generated in the process of accurately measure the volume in a certain time, calculating the content of methane, so as to provide accurate subsequent experimental analysis of experimental data, enhancing the accuracy of experiment conclusion, at the same time, the tail part of the gas-guide tube I in the gas bottle is provided with a one-way valve, which can effectively prevent the converse suction; the utility model is simple in structure, convenient in operation and strong in adaptability.
NOVELTY - This utility model claims an improved anaerobic fermentation biogas experiment device belongs to the technical field of experimental device technology field, comprising an anaerobic reactor, washing bottle, bottle, bottle, a rubber plug, a sampling pipe, a gas-guide tube I, a gas flow meter, a one-way valve, a connecting tube, a sampling valve, a connecting pipe, a gas-guide tube II, a gas-guide tube. Carried out by improving the traditional anaerobic fermentation biogas device, control the experiment process is added to a gas flow meter, capable of realizing on-line monitoring, anaerobic fermentation, anaerobic marsh gas volume biogas fermentation and methane generated in the process of accurately measure the volume in a certain time, calculating the content of methane, so as to provide accurate subsequent experimental analysis of experimental data, enhancing the accuracy of experiment conclusion, at the same time, the tail part of the gas-guide tube I in the gas bottle is provided with a one-way valve, which can effectively prevent the converse suction, the utility model has simple structure, convenient operation and strong adaptability.
NOVELTY - The fuel cell apparatus has a heat exchanger (200) heats the fuel mixture containing water of a water line (110) and fuel of a fuel line (120) of a fuel introduction portion (100). A fuel cell stack (300) produces the electricity using fuel mixture and exhausts the fuel cell anode exhaust gas. An air process unit (400) processes exhaust gas with an air dissolver to form the desalination air which is processed with a dehumidifier for producing the dehumidifying processing air. An air heating unit (500) heats the dehumidifying processing air from the air process unit.    USE - Fuel cell apparatus for vessel.    ADVANTAGE - The salinity in the air can be removed efficiently. The frequent maintenance and repair of the filter can be avoided. The economical efficiency of the fuel cell apparatus can be improved. The dehumidifying processing of the air can be performed. The moisture emission with the use of the dehumidifier can be performed smoothly. The moisture ejected from the dehumidifier can be recycled in the desalination.    DESCRIPTION OF DRAWING(S) - The drawing shows a circuit diagram of the fuel cell apparatus. (Drawing includes non-English language text)    Fuel introduction portion (100)    Water line (110)    Fuel line (120)    Heat exchanger (200)    Fuel cell stack (300)    Air process unit (400)    Air heating unit (500)
NOVELTY - The apparatus has a load leveling unit controlled in an emergency control mode through a control signal of a fuel feeder. The fuel feeder is connected with a fuel cell stack and an electric power inverter. The load leveling unit diverges a part among output from the fuel cell stack. The fuel feeder fluctuates output power of the fuel cell stack according to change of load consumable power of the fuel cell stack and the electric power inverter. The fuel feeder confirms load consumable power change in an extraordinariness generate mode.    USE - Fuel cell emergency power supply apparatus for use in a low load fuel cell generation system.    ADVANTAGE - The apparatus improves operating performance of a low load fuel cell generation system. The apparatus ensures better stability and improves reliability of a power supply. The apparatus improves consumed power load amount and fuel cell amount output power according to requirement, thus improving operating efficiency during an emergency generate mode.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a fuel cell emergency power supply apparatus.'(Drawing includes non-English language text)'
NOVELTY - Hydrogen reduction method of carbon dioxide involves subjecting vacuum vessel which has polygon by setting rotating shaft as substantially vertical direction with respect to the cross section to internal cross-sectional shape rotation or pendulum operation, sputtering powdery support in the vacuum vessel, stirring, rotating, making surface of the powdery support to carry out dispersion support of nanoparticles and producing catalyst, contacting gas containing carbon dioxide and hydrogen with catalyst, and reducing carbon dioxide.    USE - Hydrogen reduction method of carbon dioxide (claimed) discharged from power station, iron mill and chemical plant.    ADVANTAGE - The method efficiently and economically reduced carbon dioxide with high conversion rate at 200 degrees C or less.    DETAILED DESCRIPTION - Hydrogen reduction method of carbon dioxide involves subjecting vacuum vessel which has polygon by setting rotating shaft as substantially vertical direction with respect to the cross section to internal cross-sectional shape rotation or pendulum operation, sputtering powdery support in the vacuum vessel, stirring, rotating, making surface of the powdery support to carry out dispersion support of nanoparticles and producing catalyst, contacting gas containing carbon dioxide and hydrogen with catalyst, and reducing carbon dioxide. The nanoparticles are material particles containing elements chosen from iron, cobalt, nickel, copper, ruthenium, rhodium, palladium, silver, iridium, platinum and gold, or metal particles.
NOVELTY - Compost collector, which discharges rain- and dirty water into the outer barrel from an inner compost bin, is claimed.    USE - Used as a compost collector.    ADVANTAGE - The compost collector: achieves solid consistency of separately collected rain- and dirty water; and allows easy emptying of the outer barrel.
NOVELTY - The compost ventilation pipes comprise ventilation holes at regular intervals.    USE - Used as compost ventilation pipes.    ADVANTAGE - The compost ventilation pipes allow better ventilation, prevention of mold formation and the better quality of the compost.
NOVELTY - A surfactant-free oil-in-water-type emulsification cleansing agent composition comprises 5-60 wt.% oil-phase component (A) containing 20 wt.% or more volatile oil agent, water-based component (B) containing 50-80 wt.% soluble constituent chosen from sugar, sugar derivative (excluding polyphenol glycoside), sugar alcohol, sugar-alcohol derivative and betaine, and emulsifying component chosen from polyphenol and polyphenol glycoside. The content of soluble constituent is 60 wt.% or more with respect to all soluble constituents in the water-phase component.    USE - Surfactant-free oil-in-water-type emulsification cleansing agent composition is used for forming sheet-like cleansing (claimed).    ADVANTAGE - The surfactant-free oil-in-water-type emulsification cleansing agent composition has excellent moistness, aging stability, cleansing effect, makeup remover effect, usability, and safety with respect to skin.    DETAILED DESCRIPTION - A surfactant-free oil-in-water-type emulsification cleansing agent composition comprises 5-60 wt.% oil-phase component (A) containing 20 wt.% or more volatile oil agent, water-based component (B) containing 50-80 wt.% soluble constituent chosen from sugar, sugar derivative (excluding polyphenol glycoside), sugar alcohol, sugar-alcohol derivative and betaine, and emulsifying component chosen from polyphenol and polyphenol glycoside, and does not contain nonionic surfactant, anionic surfactant, cationic surfactant and amphoteric surfactant. The content of soluble constituent is 60 wt.% or more with respect to all soluble constituents in the water-phase component. An INDEPENDENT CLAIM is included for sheet-like cleansing, which contains 1.5-5 pts. wt. surfactant-free oil-in-water-type-emulsification cleansing agent composition, impregnated with respect to 1 pt. wt. sheet base material.
NOVELTY - The moving structure (1) has a battery (24) in which electric power generated by an auxiliary electric power generating apparatus is stored. An inverter (25) transforms the electric power of direct current into the electric power of alternating current. The hydrogen oxygen mixed gas generator (26) electrolyzes the water by alternating current power output by an inverter. The implosion of hydrogen oxygen mixed gas generated by hydrogen oxygen mixed gas generator is performed. The gas is supplied to the engine (21) through a gas supply line path.    USE - Moving structure such as motor vehicle, boat, ship, hybrid vehicle and fuel cell electric vehicle.    ADVANTAGE - The improvement of energy saving efficiency in the moving structure can be attained.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the supplementary-fuel system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the moving structure. (Drawing includes non-English language text)    Moving structure (1)    Engine (21)    Battery (24)    Inverter (25)    Hydrogen oxygen mixed gas generator (26)
NOVELTY - Obtaining oil degradation product involves treating sewage containing limestone by using Bacillus subtilis, Rhizobium sp. and Pseudomonas fluorescens for transforming urea, monoammonium phosphate, calcium carbonate, manganese sulfate, sodium chloride, monopotassium phosphate, sodium chloride, disodium hydrogen phosphate and potassium dihydrogen phosphate. The materials are transformed for producing lipase and esterase.    USE - Method for obtaining product for degradation of oil and grease by treating sewage.    ADVANTAGE - The method enables degradation of oil and grease and treat sewage efficiently.
NOVELTY - The apparatus has an outer side cylindrical transparent container whose outer side hydrogen-flow exit (622) and the inner side hydrogen-flow exit (782) of an inner side cylindrical transparent container are connected. The generated hydrogen is taken out from the inner side of the container. The rotary blade (750) is currently fixed in the inner side cylindrical transparent container which receives motive power, when electrolyte aqueous solution flows in from an electrolyte aqueous solution inflow port (612) and flows out of an electrolyte aqueous solution outflow port (614).    USE - Apparatus for producing hydrogen from water.    ADVANTAGE - The hydrogen and oxygen can be obtained separately. The rotary blade which is supporting the photo-catalyst by supply of electrolyte aqueous solution is rotated. The detachment from the photo-catalyst of hydrogen and oxygen of the photo-catalyst and electrolyte aqueous solution are contacted and produced can be accelerated. The detachment from the photo-catalyst of hydrogen and oxygen can be accelerated by simple structure, without using the separate motive power source which rotates the rotary blade.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for hydrogen production method.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the hydrogen generating apparatus. (Drawing includes non-English language text)    Electrolyte aqueous solution inflow port (612)    Electrolyte aqueous solution outflow port (614)    Outer side hydrogen-flow exit (622)    Rotary blade (750)    Inner side hydrogen-flow exit (782)
NOVELTY - Method for preparing liquid fertilizer, involves immersing the fowl excrement fermentation processed material comprising at least one of incinerated ash or carbide, soil fungus, and poultry manure in water which is used as immersion portion, and fermenting by maintaining the immersion portion for more than 3 days under anaerobic condition with the water temperature of 25-35 degrees C, and after fermenting obtaining the liquid fertilizer.    USE - The method is useful for preparing liquid fertilizer which is useful in preparing manure and non-tilling cultivation method (all claimed) for improving gardening and farmland soil.    ADVANTAGE - The method is simple to perform, reduces the burden of local plowing operation performed for cultivation, and prepared liquid fertilizer which is environmentally-friendly.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for preparing manure, involves fermenting the above-mentioned liquid fertilizer to adhere on the cattle feces or pig feces under anaerobic conditions; and    (2) non-tilled cropping method, involves sprinkling the obtained liquid fertilizer in soil, and growing without plowing the soil.
NOVELTY - The method involves emitting gas in a fermentation chamber (1) by a fermentation outdoor as exhaust gas, and spraying ultrafine particle of water with respect to a path that discharges the exhaust gas. Adsorption of an offensive odor component is performed in exhaust gas, where temperature of exhaust gas is controlled by adjusting amount of ultrafine particle of the water. A stirring blade (2b) is provided in the fermentation chamber at a rotating shaft (2a), and the rotating shaft is rotationally driven by an electric motor (3).    USE - Method for processing an organic waste material i.e. crushed soybeans, for tofu-production in a home and a restaurant. Can also be used for processing vegetable refuse such as vegetable debris, and animal refuse such as fish and meat.    ADVANTAGE - The method enables efficiently removing offensive odor in waste gas emitted by waste disposal in a waste processing apparatus by fermentation process, processing an organic refuse from an organic-refuse generation source, cooling process target gas by microparticles of water, and generating micro-particles of water at low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a fermentation process apparatus for organic waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a waste processing apparatus.    Fermentation chamber (1)    Rotating shaft (2a)    Stirring blade (2b)    Electric motor (3)    Circulating water tank (10)
NOVELTY - The hydrogen production apparatus (10) has a frame (12), which forms an electrolyte solution accommodation space inside while holding a cathode and an anode (21). The anode is electrically connected to an electrical connection portion (42). The anode has a board to which a photocatalyst is adhered at one side, and an electrically conductive film extended and formed even in the other side. The electrical connection portion is connected to an electrically-conductive board, which contacts the electrically conductive film formed in the other surface in the peripheral portion of the board.    USE - Hydrogen production apparatus.    ADVANTAGE - A number of hydrogen production apparatus can be connected into arbitrary arrangement forms, and arranged in a space of various shape. The hydrogen production apparatus has simplified structure. The electrically-conductive board and electrically conductive film are reliably connected and maintained by a frame.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the hydrogen production apparatus. (Drawing includes non-English language text).    Hydrogen production apparatus (10)    Frame (12)    Window portion (13)    Anode (21)    Electrical connection portion (42)
NOVELTY - The method involves thermally decomposing and gasifying dewatered sludge (S1) and dried sludge (S2) by using thermal decomposition gasifier (5). The generated pyrolysis gas (G1) and carbonized material (C) are separated in solid-gas separation portion (7), when sludge is thermally decomposed. The oxygen-containing gas (G3) is supplied after separating pyrolysis gas and carbonized material. The pyrolysis gas is introduced into combustion furnace (6) through piping (9) of thermal decomposition gas line (8) provided with oxygen-containing gas.    USE - Method for suppressing generation of thermal decomposition deposit such as tar in thermal decomposition gasification system (claimed) such as carbonization system installed in thermal decomposition gasification facility for manufacturing carbonized fuel for electric power generation from sewage sludge and woody biomass.    ADVANTAGE - The generation of the thermal decomposition deposit in the thermal decomposition gasification system is suppressed by using the method for suppressing generation of the thermal decomposition deposit in the thermal decomposition gasification system, during operation of the thermal decomposition gasification system, when the oxygen-containing gas is supplied to pyrolysis gas after separating pyrolysis gas from the carbonized material. The obstruction of the piping and the deterioration of the impeller are prevented.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a thermal decomposition gasification system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the carbonization system. (Drawing includes non-English language text)    Thermal decomposition gasifier (5)    Combustion furnace (6)    Solid-gas separation portion (7)    Thermal decomposition gas line (8)    Piping (9)    Carbonized material (C)    Pyrolysis gas (G1)    Oxygen-containing gas (G3)    Dewatered sludge (S1)    Dried sludge (S2)
NOVELTY - The method involves immobilizing a fuel on a working electrode of a capacitor by exposing the working electrode to fuel, charging the capacitor by biasing working electrode such that it becomes positively charged and biasing a counter electrode of capacitor such that it becomes negatively charged. The working electrode is exposed to an oxidant after the fuel is immobilized on the working electrode. Electrical power is generated by connecting an electrical load between the working electrode and the counter electrode.    USE - Method for generating electricity from fuel and oxidant using capacitor.    ADVANTAGE - The process is simple and can yield high power densities and fuel efficiency. The quick response time and low operating temperature enhance automotive and portable power applications. Oxygen reduction reaction (ORR) catalyst is improved, poisoning of the hydrogen oxidation reaction (HOR) catalyst is prevented, and higher temperature proton conducting membranes are developed. Membrane wetness is maintained without flooding, reliability is improved, and the cost is lowered.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the metal-insulator-metal device and sample holder.
NOVELTY - Producing levulinic acid from biomass involves: treating biomass with a first aqueous acidic solution at a pH, for a time, and temperature such that at least a portion of pentosans contained within the biomass is extracted from the biomass, to yield pentosan-extracted biomass; and treating the pentosan-extracted biomass with a second aqueous acidic solution at a pH, for a time, and a temperature, such that at least a portion of hexosans contained within the pentosan-extracted biomass are converted to levulinic acid.    USE - For producing levulinic acid from biomass (claimed), which is widely used in the cosmetic, food, and medicinal industries.    ADVANTAGE - The present process is a two-stage acid-catalytic conversion of carbohydrates into levulinic acid which provides a higher actual yield of levulinic acid than a single-stage process.
NOVELTY - Mixture of modified compounds useful for producing ethanol-containing biogas, comprises: 20-40 vol.% of condensate; and 80-60 vol.% of anticorrosion and antiphase separation additive, where the anticorrosion and antiphase separation additive is a mixture of isopropanol, triethylamine and 2-ethylhexanol with a ratio of 3:2:0 or 3:2:1.    USE - The mixture of modified compounds is useful for producing ethanol-containing biogas.    ADVANTAGE - The mixture of modified compounds is cost-effective.
NOVELTY - Processing unit has three stainless steel tanks (1,2,3), where the tanks are provided for storing potassium hydroxide, drinking water and pressurized gas. An electrolysis chamber (4) is provided for performing electrolysis by using water. The electrolysis chamber contains a series of electrodes and is connected to a circuit and generator that provide electric current at low voltage and high current. A battery pack (14), a computer (15) and a power source (13) are also provided.    USE - Processing unit for generating electricity by using oxygen lance.    ADVANTAGE - The processing unit ensures continuous generation of electricity.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a processing unit.    Stainless steel tanks (1,2,3)    Pump (5)    Power source (13)    Battery pack (14)    Computer (15)
NOVELTY - The portable dry cell kit comprises 316L stainless steel plates (1) cut into specific size with rubber sealing system (2) for high temperature and pressure, and polyvinyl chloride plates (3) that are provided in acrylic for visualization of process of electrolysis and water level. A cooling system is provided with radiator for covering passage of water tank (4), where non-return valves (6) are mounted with screws (7).    USE - Portable dry cell kit for use in hydrogen gas generation system.    ADVANTAGE - The portable dry cell kit facilitates quick and secure installation in internal combustion engines for replacing components of fossil fuels, reduces emission of composition gases, and instantly consumes generated hydrogen gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the portable dry cell kit.    Stainless steel plates (1)    Rubber sealing system (2)    Polyvinyl chloride plates (3)    Water tank (4)    Non-return valves (6)    Screws (7)
NOVELTY - The method involves calcining a mixture of potassium citrate and silica gel with organic solvent, and heating calcined product at 300-450 degrees C.    USE - Method for obtaining heterogeneous potassium silica catalyst for preparing esters of fatty acid sources of triglyceride and alcohol comprising biodiesel in chemical and agricultural sectors.    ADVANTAGE - The method enables to obtain the heterogeneous potassium silica catalyst in a cost-effective and eco-friendly manner.
NOVELTY - This utility model claims a cover for removing nitrogen and phosphorus in municipal sewage system, the system comprises an adjusting pool and an integrated escape device. The adjusting pool provided with liquid level monitor. According to the integrated escape device comprising a tank body, a phase separator and an electric control cabinet. The side wall of the tank body is provided with a water inlet and a water outlet, the bottom is set with an aeration device. According to the two phase separator is fixed on the inner wall of the tank body through the metal bracket. The electric control cabinet is set in the PLC control box and an air pump, wherein the top surface of the device, and is connected with the solar energy power device. This utility model can effectively remove the organic pollutant in the water and nitrogen, it does not need the special sedimentation tank to realize the effective separation of mud, it can fully ensure the water quality, at the same time, the system has compact structure, the solar energy power supply device of refrigeration device, realizing the sewage treatment is complete without power consumption, which saves space resource and energy.
NOVELTY - This utility model claims a kind of particle fertilizer drying adding active device, wherein one side of the liquid microbial strain storage tank is connected with a high-pressure water pump through a pipeline, the output end of the high pressure water pump is connected with the second pipe and the working inner cavity of the fertilizer machine; Through said setting, this utility model and a granular fertilizer drying and sieving, then adding active bacteria, which completely solves the microorganism fertilizer drying active bacteria survival rate is low.
NOVELTY - This utility model claims a high-efficient straw anaerobic marsh gas preparing device, comprising a straw crusher (1), a straw crusher (1) through the guide (2) pre-processing the homogenate tank (3), a pre-processing homogenate tank (3) is connected with the pipeline of the efficient anaerobic reactor (4), one end is inserted in the high-efficient anaerobic reactor (4), the other one end of the high-efficient anaerobic reactor (4) is spiral conveyor (5), a spiral conveyer (5) is connected through the discharging pipe (6) of the biogas tank (7). This utility model claims a high-efficient straw anaerobic marsh gas preparing device, the structure is reasonable, the operation is convenient, wide application range, high degree of automation, marsh gas producing efficiency is high, which can use resource and reduces environment pollution, and has good economic benefit and social benefit.
NOVELTY - This utility model claims a kind of organic anaerobic fermentation device for urban solid waste integrated device, comprising a garbage crusher (1), a pre-processing tank is connected with the garbage crusher (1), (2), a pre-processing tank (2) through the pipeline connected with the feeding tank (3) is connected with the feeding tank (3) of the homogenizing tank (4), a homogenizing tank (4) through the pipeline connected with the efficient anaerobic reactor (5), the high-efficient anaerobic reactor (5) is connected with a bottom side of the biogas liquid tank (6), a high-efficient marsh gas output pipe and marsh gas dehydrating device (7) and a biogas devulcanizer of the anaerobic reactor (5) is (8), the desulfurizer (8) is connected with the wet gas storage tank (9). This utility model claims the organic integrated device anaerobic fermentation device for urban solid waste, the structure design is reasonable, complete performance, high degree of automation, convenient operation, wide application range, and it has important significance for environmental protection.
NOVELTY - This utility model claims a kind of cattle marsh gas generating tank, comprising a marsh gas generating tank, the marsh gas generating tank is a sealed structure, the marsh gas generating tank is connected with a marsh gas pipe, the marsh gas generating pool is set on the side wall of the material feeding port, the marsh gas generating tank is provided with the middle part of the layer, the layer is provided with a sedimentation tank, the layer is provided with a coil, the coil of the water inlet and outlet pipe extend out of the marsh gas tank, the sedimentation tank is set on the side wall of the washing pump. This utility model reinforced waste fermentation utilization rate, avoid marsh gas pool.
NOVELTY - The utility model claims a kind of shell breaking type anaerobic fermentation device, comprising a tank body, upper part of the tank body is a feeding system, a discharging system and an air outlet, wherein the tank body is further provided with a vertical shell breaking stirring system, wherein said vertical shell breaking stirring system comprises a vertical tank body and upper end is extended to the tank body is connected with a motor rotating shaft, wherein the fermentation liquor and transversely fixed mixing blade and the rotating shaft and the liquid with a breaking blade, said breaking blade is inclined upwards and extending out of the liquid surface. The utility model is provided with the following beneficial effects: provided with breaking blade in the tank body, for breaking incrustation is fermentation liquid surface is suitable for livestock and poultry dung dirt and so on is higher than the processing containing suspended matter of the organic waste and improve the utilization rate of the organic waste, changing waste into valuable, improving enzyme activity of strain producing ((/zhaolu:)), and it is good for safe operation of an intelligent device, adding stirring plate, which is good for further mixing and fermentation liquid, improving enzyme activity of strain producing marsh gas amount, a stirring system is also good for fermentation liquid surface cracking.
NOVELTY - A living garbage treating device, comprising a first heating cavity, wherein it further comprises a second heating cavity, a heating cavity and a heating cavity are set independently, after the second heating cavity is located on the first heating cavity and the two are connected with each other. This utility model adopts double layer structure for sufficient heat to be processed, by layered heating structure, one can heat value and quality of the oil and decomposition product carbon improves the garbage, wherein the diode, the first layer greatly improves the cracking efficiency so as to improve the productivity of the garbage treatment product, wherein, when heating is capable of removing acidic gas, so as to prevent to produce dioxin, which greatly reduces the tail gas processing cost, wherein the four, a layered heating structure is good for shortening the length of the heat cracking furnace, designing and manufacturing device;
NOVELTY - This utility model belongs to livestock and poultry breeding technology and device, equipment field, specifically claims a kind of filling with air cushion layer for a control culture fermenting bed, wherein it is provided with a full-area cushion layer is fermentation cushion layer (1) at the lower part or centralized drain region provided with a zone air cushion layer in livestock, in the cushion layer natural air flow or mechanical air supply system, upper layer floor is composed of anti-seepage layer (6) and a graded material layer (3), graded material layer (3) is provided with a horizontal opening vent pipe (7), vent-pipe (7) is connected with the mechanical air supply system of the fan (10) is connected with a fermentation cushion layer (1), a temperature control sensor (12), a controller of the probe with the mechanical air supply system for humidity control sensor (13) connected with the controller is connected with the fan (10) is connected, the product can be used in the omni-directional control livestock breeding fermentation bed microorganism sewage digestion atmosphere, the fermentation bed to place in a suitable aerobic and anaerobic state, strengthening fermenting bed cultivation condition, the load for optimizing the working state of the fermentation bed fermentation bed extend service life.
NOVELTY - Preparation of traditional Chinese medicine fertilizer comprises adding animal feathers into 20-30% sulfuric acid to hydrolyze for 8-10 hours, generating amino acid, adding lime to neutralize, adding 1-2 pts. wt. chitosan, and mixing uniformly; and mixing traditional Chinese medicine extract with 38-40 pts. wt. urea, 15-18 pts. wt. diammonium phosphate, 28-30 pts. wt. potassium chloride and zinc sulfate to obtain the product.    USE - Method for preparing traditional Chinese medicine fertilizer (claimed).    ADVANTAGE - The method has low cost.    DETAILED DESCRIPTION - Preparation of traditional Chinese medicine fertilizer comprises adding animal feathers into 20-30% sulfuric acid to hydrolyze for 8-10 hours, generating amino acid, adding lime to neutralize, adding 1-2 pts. wt. chitosan, and mixing uniformly to obtain amino acid chelated liquid; adding 2-5 pts. wt. rotten apple, 4-8 pts. wt. rotten watermelon and rotten cabbage leaf, mixing uniformly, and pulping to obtain rotten fruit and vegetable slurry; mixing 3 pts. wt. rotten fruit and vegetable slurry, 5-8 pts. wt. amino acid chelated liquid and bamboo charcoal, 1-2 pts. wt. sepiolite powder, 1-2 pts. wt. chitosan, 20-25 pts. wt. sheep manure, 10-15 pts. wt. straw, 1-2 pts. wt. brown sugar, 1-2 pts. wt. EM microbial inoculum and 10-12 pts. wt. tea leaf, sealing to ferment for 6-8 days to obtain fermentation material; and adding 5-8 pts. wt. rose, 2-4 pts. wt. radix stemonae, 5-7 pts. wt. unbracteolated spurge root and 1-2 pts. wt. pumpkin, uniformly mixing, soaking for 4-6 days, taking out water and vinegar to obtain the traditional Chinese medicine extract, fermenting material, mixing traditional Chinese medicine extract with 38-40 pts. wt. urea, 15-18 pts. wt. diammonium phosphate, 28-30 pts. wt. potassium chloride and zinc sulfate to obtain the product.
NOVELTY - A kind of new hydrogen and oxygen generator, comprising a controller, an air storage tank, a separating tank and a water pump, a rinsing tank and a pump, an operation pump, a cooling fan, a phase shift trigger controller, an electrolytic tank, wherein the air storage tank, a separating tank and a water pump, a rinsing tank and a pump, an operation pump, a cooling fan are orderly connected in series and then connected with the controller, phase shift trigger controller is connected with the electrolytic cell connected in series, an access controller. The reactive power loss consumption and peak current of this utility model phase shift trigger control integrated integrated circuit design, which avoids the electronic primary component inherent defect, effectively inhibiting impact current, improve the electric energy utilization ratio, reduces the damage to the electrolytic cell, electrolytic cell so as to improve the service life.
NOVELTY - Sewage treatment reaction device comprises shell (1) provided with water inlet (2), and upper part is provided with water outlet (3). The shell is filled with filler (4), and provided with S-shaped baffle plate (5) with micropores.    USE - Sewage treatment reaction device.    ADVANTAGE - The biological filler effectively controls two sides of reactor for full contact of sewage with microorganism during reaction, which achieves full decomposition of organic impurities.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of sewage treatment reaction device.    Shell (1)    Water inlet (2)    Water outlet (3)    Filler (4)    S-shaped baffle plate (5)
NOVELTY - A 4-biphenylacetic acid is synthesized by mixing 4-methyl benzene, palladium chloride as catalyst, triphenylphosphine ligand, a base, and a solvent; subjecting mixture to carbonylation reaction in the presence of carbon monoxide; acidifying; and separating.    USE - Method of synthesizing 4-biphenylacetic acid (claimed).    ADVANTAGE - The method has high yield, is environment-friendly, and can be applied to industrial production.
NOVELTY - Synthesizing gliclazide comprises reacting with N-((4-methyl phenyl) sulfonyl)-hydrazide formamide with 1,2-dibromo methyl cyclopentane.    USE - The method is useful for synthesizing gliclazide (claimed).    ADVANTAGE - The method prepares the gliclazide high yield and good quality, and without oxidization of amino heterocycle and environment pollution.
NOVELTY - A domestic liquid communicating vessel biogas digester comprises a big fermenting tank, a slag discharge basin installed on same side, a pressure basin, a feed pipe, a slag-discharge pipe and a pressure pipe. An air-storage chamber is arranged on upper portion of the big fermenting tank. A small-fermenting tank is installed on one side of middle inside big fermenting tank. The side of middle inside big fermenting tank is close to pressure basin, a support below small fermenting tank is fixed on inner wall of bottom of the big fermenting tank.    USE - Domestic liquid communicating vessel biogas digester (claimed).    ADVANTAGE - The domestic liquid communicating vessel biogas digester is simple in structure and economical, and has high durability.    DETAILED DESCRIPTION - A domestic liquid communicating vessel biogas digester comprises a big fermenting tank, a slag discharge basin installed on the same side, a pressure basin, a feed pipe, a slag discharge pipe and a pressure pipe. An air-storage chamber is arranged on the upper portion of the big fermenting tank. A small fermenting tank is installed on one side of the middle inside the big fermenting tank. The side of the middle inside the big fermenting tank is close to the pressure basin, a support below the small fermenting tank is fixed on the inner wall of the bottom of the big fermenting tank. An air-storage chamber is arranged above the small fermenting tank. The feed pipe and the small fermenting tank in the big fermenting tank are connected to form a communicating vessel. One end of the slag discharge pipe is communicated into the bottom of the big fermenting tank, and the other end of the slag discharge pipe is communicated into the slag discharge basin and extends to 20-30 cm higher than the base plane of the slag discharge basin. One end of the pressure pipe is communicated with the big fermenting tank, and the other end of the pressure pipe is communicated with the pressure basin.
NOVELTY - Method for preparing biogas by lees fermentation, involves adding 15-25 wt.% fresh pig manure to lees, stirring the mixture, and performing anaerobic digestion to the mixture, where the fermentation is performed at pH of 7-8.5 and 30-45 degrees C for 38-42 days.    USE - The method is useful for preparing biogas which is useful as energy source of higher heat of combustion, fertilizer for improving soil, fertilizing land, and cultivating edible mushrooms.    ADVANTAGE - The method is environmentally-friendly as it utilizes lees for preparing biogas.
NOVELTY - The device comprises a housing installed inside a gas collecting pipe that is provided with sealing water. The housing accepts the sealing water and isolates inside and outside parts of the gas collecting pipe. A plug prevents the leakage of coke oven gas from the housing. A unit supplies the sealing water to a side of the housing. A hollow drain is formed in a lower part of the housing for ejecting the sealing water to the outside of the housing. An overflow protecting opening part ejects the sealing water to the outside of housing to maintain constant level height of the sealing water.    USE - Used as a gas collecting pipe sludge removal device.    ADVANTAGE - The plug in the housing is opened so that the coke oven gas does not gush out to the outside of the housing thus effectively removing the sludge and hence preventing gas poisoning and environmental contamination to the operator.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a sludge removing method.
NOVELTY - Mobile fermentation method for producing a concentrated fertilizer through humic acid, comprises adding a base fermentation substance in a dried material mixer to mix, puffing the mixed material through a twin-screw extruding and puffing machine, conveying the puffed material to a wet material mixer, adding yellow water to reduce the temperature to 30-35 degrees C, inoculating a mixed bacteria liquid, fully mixing, filling the mixture into a ventilating film fermenting bag, then packing and sealing, and fermenting in a fermentation chamber.    USE - The mobile fermentation method is useful for producing a concentrated fertilizer through humic acid (claimed).    DETAILED DESCRIPTION - Mobile fermentation method for producing a concentrated fertilizer through humic acid, comprises adding a base fermentation substance in a dried material mixer to mix, puffing the mixed material through a twin-screw extruding and puffing machine, conveying the puffed material to a wet material mixer, adding yellow water to reduce the temperature to 30-35 degrees C, inoculating a mixed bacteria liquid, fully mixing, filling the mixture into a ventilating film fermenting bag, then packing and sealing, and fermenting for 5-10 days in a fermentation chamber at constant temperature to obtain the concentrated fertilizer, where: the base fermentation substance is prepared by uniformly mixing yellow humic acid (50-60 pts. wt), vinasse (10-20 pts. wt.), powdered maize straw (10-20 pts. wt.), urea (5-10 pts. wt.), diammonium hydrogen phosphate (1-2 pts. wt.) and potassium chloride (5-10 pts. wt.) and adding yellow water (10-20 pts. wt.) to the substance with a moisture content of 20-30 wt.%; and the mixed bacteria liquid includes bacteria liquid of Trichoderma harzianum, wet fiber monospora, Bacillus latersprorus, Bacillus megaterium, Azotobacter chroococcum, Bacillus mucilaginosus and Lactobacillus plantarum.
NOVELTY - Preparation of high purity cefdinir antibiotic comprises carrying out alkylation reaction of (2-Amino-thiazol-4-yl)-((Z)-hydroxyimino)-acetic acid ethyl ester and triphenylmethanol with di(m)ethyl carbonate solvent in the presence of boron trifluoride catalyst, performing hydrolysis reaction in alcohol solvent with added inorganic base solution, adding DNA in halogenated alkane solvent under pyridine compound catalyst and dropping triethyl phosphate and triethylamine mixture.    USE - Method of preparing high purity cefdinir antibiotic (claimed).    ADVANTAGE - The reaction process is simple to operate, environment-friendly, easy to recycle and use; has high yield, low cost and non-toxic.    DETAILED DESCRIPTION - Preparation of high-purity cefdinir antibiotic comprises:    (A) carrying out alkylation reaction of cefotaxime and triphenylmethanol with di(m)ethyl carbonate solvent in the presence of boron trifluoride catalyst to obtain S-2-Benzothiazolyl ( Z )-2-(2-aminothiazol-4-yl)-2-trityloxyiminothioacetate;    (B) carrying out hydrolysis reaction in alcohol solvent with added inorganic base solution to obtain (Z)-(2-(Formamido)thiazol-4-yl)(methoxyimino)acetic acid; and    (C) adding DNA in halogenated alkane solvent under pyridine compound catalyst and dropping triethyl phosphate and triethylamine mixture to obtain finished product.
NOVELTY - The bioreactor has a reactor tank portion (2) that is included with a curtain membrane component (3) and a perforated aeration pipe (5). The reactor is connected to a suction pump (6) and an electromagnetic air compressor (4). The suction pump is connected with a flat screen iron electrode (1) located in parallel at sides of the curtain membrane component. The flat screen iron electrode is connected with a lead (9) connected with adjustable direct current stabilized voltage supply (7) which is connected with an electric control device (8).    USE - Electro-coagulation polymembrane bioreactor for treating and recycling domestic wastewater, printing and dyeing wastewater, and pharmaceutical wastewater.    ADVANTAGE - The bioreactor structure can be simplified while reducing the chemical reagents. The operating cost of the bioreactor can be reduced. The bioreactor can be easily operated and managed. The automated control of bioreactor can be realized while increasing the efficiency, and reducing the energy consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a sewage treatment method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the electro-coagulation polymembrane bioreactor. (Drawing includes non-English language text)    Flat screen iron electrode (1)    Reactor tank portion (2)    Curtain membrane component (3)    Electromagnetic air compressor (4)    Perforated aeration pipe (5)    Suction pump (6)    Adjustable direct current stabilized voltage supply (7)    Electric control device (8)    Lead (9)
NOVELTY - Manufacture of organic and inorganic composite fertilizer involves drying pig manure until the moisture content is 60-70%, adding materials into 0.3-0.5% cultured fermentative bacterium solution, performing heap fermentation for 10-15 days, maintaining pH at 5-7, drying the fermented materials until the moisture content is less than 20%, crushing, sieving, removing impurities, detecting, and packaging obtained product.    USE - Manufacture of organic and inorganic composite fertilizer (claimed).    ADVANTAGE - The method enables to manufacture organic and inorganic composite fertilizer cost-effectively. The fertilizer is rich in nutrients, contains several necessary macroelements and microelements for the growth and development of plants, improves disease and pest resistance, lodging resistance, thermal resistance and drought resistance of the plants, and contains microbial flora having special effects on nutrition for roots of the plants and a large amount of organic substances, has improves utilization ratio.
NOVELTY - Purifying probenecid comprises: (a) reacting probenecid crude product and an alkaline substance in water until probenecid is completely dissolved; (b) cooling the obtained solution, crystallizing at low-temperature and stirring until crystallization is complete; (c) filtering, dissolving the obtained filter cake in water, and adding acid to adjust the pH of the obtained solution to acidic; and (d) filtering, washing the obtained filter cakes with water, then filtering and drying to obtain probenecid pure product.    USE - The method is useful for purifying probenecid (claimed).    ADVANTAGE - The method: has simple purification process; does not utilize organic solvents and hence reduces costs and environmental pollution; achieves probenecid purification in aqueous environment; and satisfies the requirements for clean production.
NOVELTY - A N-carbobenzoxy-3-fluoro-4-morpholinyl benzene is synthesized by dissolving 3-methyl-4 morpholinyl nitrobenzene in ethyl acetate at a ratio of 1:5-20, adding 10 wt.% palladium carbon, reacting at 20-50 degrees C and pressure of 2-5 MPa for 1-3 hours, filtering, decompressing and concentrating the filtrate, adding acetone, water and alkali reagent, stirring, cooling to 0-5 degrees C, adding dropwise chlorocarbonic acid(4-(benzoyl)benzyl)ester, stirring at room temperature for 2-3 hours, decompressing and condensing, crystallizing, filtering, washing the filter cake with water, and drying.    USE - Method of synthesizing a N-carbobenzoxy-3-fluoro-4-morpholinyl benzene (claimed).    ADVANTAGE - The method is simple and environment-friendly, has high yield, obtains product having good property, and can be applied to industrial production.    DETAILED DESCRIPTION - A N-carbobenzoxy-3-fluoro-4-morpholinyl benzene is synthesized by dissolving 3-methyl-4 morpholinyl nitrobenzene in ethyl acetate at a ratio of 1:5-20, adding 10 wt.% palladium carbon, reacting at 20-50 (preferably 40) degrees C and pressure of 2-5 (preferably 2) MPa for 1-3 hours, filtering, decompressing and concentrating the filtrate, adding acetone, water and alkali reagent, stirring, cooling to 0-5 degrees C, adding dropwise chlorocarbonic acid(4-(benzoyl)benzyl)ester, stirring at room temperature for 2-3 hours, decompressing and condensing, crystallizing, filtering, washing the filter cake with water, and drying. The volume ratio of concentrated filtrate and acetone is 1:10-50. The volume ratio of concentrated filtrate and water is 1-5:1. The mole ratio of cooled product and chloro-carbonic acid benzyl ester is 1:0.8-1.
NOVELTY - Enriching and purifying total phenylethanoid glycoside by adopting macroporous adsorption resin method comprises adding ethanol solution into crushed guangdong beautyberry medicinal material, ultrasonically extracting the mixture, filtering the mixture and mixing the extracting solutions, decompressing and recycling an ethanol solvent, eluting the concentrated solution passing through chromatographic column, eluting the concentrated solution using ethanol solution, decompressing and concentrating ethanol eluent, and spraying and drying the concentrated solution.    USE - The method is useful for enriching and purifying total phenylethanoid glycoside (claimed).    ADVANTAGE - The method is capable of simply and economically enriching and purifying the total phenylethanoid glycoside with little pollution.    DETAILED DESCRIPTION - Enriching and purifying total phenylethanoid glycoside by adopting macroporous adsorption resin method comprises adding 30-100% of ethanol solution into crushed 6-15 times of guangdong beautyberry medicinal material, ultrasonically extracting the mixture for 2-4 times with a temperature of 30-60 degrees C for 1-2 hours, filtering the mixture and mixing the extracting solutions, decompressing and recycling an ethanol solvent, eluting the concentrated solution passing through a chromatographic column, which is filled with macroporous resin by water for 3-8 times to remove impurities, eluting the concentrated solution using 10-70 wt.% of ethanol solution with a flow velocity of 1-4 BV/hours, decompressing and concentrating the ethanol eluent, and spraying and drying the concentrated solution.
NOVELTY - A nano biofuel comprises 75-85 wt.% drainage oil, 5-10 wt.% water, 1.5-3.5 wt.% hydrophilic agent, 5-10 wt.% lipophilic agent, 5-10 wt.% oil regulating agent and 0.05-0.3 wt.% quality improving agent.    USE - The biofuel is used as substitute of diesel fuel for diesel engine.    ADVANTAGE - The energy-saving, environment-friendly and economical biofuel has high heating value, low production cost and does not easily deteriorate and form layers.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of nano biofuel comprising:    (A) removing impurities of drainage oil, degumming, bleaching and dehydrating to obtain standard oil raw material;    (B) static mixing standard oil raw material and methanol at mol ratio of 10:1, adding 1 wt.% catalyst and carrying out pre-esterification reaction at 70 degrees C for 4 hours to obtain pre-esterified liquid;    (C) mixing pre-esterified liquid and methanol at mol ratio of 20:1, adding 6 wt.% catalyst, stirring and carrying out atmospheric esterification reaction at 70 degrees C for 4 hours;    (D) standing, centrifuging, separating, where upper layer is crude biofuel and lower layer is glycerin, catalyst and methanol and distilling crude biofuel to obtain biofuel; and    (E) adding biofuel, water and hydrophilic agent in reactor, slowly adding lipophilic agent, stirring for 40-60 minutes until clear and transparent, adding oil regulating agent and quality improving agent, stirring for 10-20 minutes, standing and curing for more than 24 hours ensuring clear and transparent liquid.
NOVELTY - An ethanol gasoline emulsifier comprises 10-20% xylene, 1-8% sodium hydroxide, 20-30% n-octanol, 15-25% cetyl alcohol, 10-12% alum, 25-35% isopropyl alcohol and 25-38% n-decanol.    USE - Ethanol gasoline emulsifier.    ADVANTAGE - The emulsifier does not cause harm to human body and engine. It helps achieve combustion, improves anti-knocking index, reduces air resistance and removes carbon. The oil system is cleaner, thus prolonging service life of engine.
NOVELTY - Biological diesel oil is prepared by cleaning natural biomass, drying, crushing, soaking crushed material in 0.01-0.1 mol/l weakly acidic amino acid organic solution at 35-55 degrees C for 2-5 hours to obtain the acidified natural biomass, soaking acidified natural biomass in 0.1-0.2 mol/l dipeptide compound or composition at 35-55 degrees C for 2-3 hours, drying at 50-80 degrees C, adding 3-7 wt.% heterogeneous catalyst and short chain alcohol having a ratio of 1:3-12, esterifying at 60-120 degrees C for 1-10 hours, decompressing and evaporating, and separating catalyst and glycerin.    USE - Method of preparing biological diesel oil (claimed).    ADVANTAGE - The method has improved yield, reduces preparation cost, and has improved yield.
NOVELTY - A natural biomass solid acid catalyst is prepared by washing natural biomass, drying and crushing, impregnating in 15-75% acid solution for 1.5-5 hours, taking out and drying at 80-100 degrees C; dipping acidified biomass in metal salt solution for 1-5 hours, and taking out and drying at 80-100 degrees C; and placing in muffle furnace for calcining at 100-270 degrees C for 2 hours, naturally cooling to room temperature, and obtaining natural biomass solid acid catalyst.    USE - Method for preparing natural biomass solid acid catalyst for biodiesel (claimed).    ADVANTAGE - The method uses natural reproducible biomass as raw material directly, without carrying out carbonization process. It has low cost and the obtained catalyst provides high biological diesel yield. The catalyst has good mechanical strength, good particle size, and does not cause secondary pollution.    DETAILED DESCRIPTION - Preparing natural biomass solid acid catalyst for biodiesel comprises:    (A) washing natural biomass, drying and crushing, impregnating in 15-75% acid solution for 1.5-5 hours, taking out and drying at 80-100 degrees C;    (B) dipping acidified biomass in metal salt solution for 1-5 hours, and taking out and drying at 80-100 degrees C;    (C) placing in muffle furnace for calcining at 100-270 degrees C for 2 hours, naturally cooling to room temperature, and obtaining natural biomass solid acid catalyst; and    (D) adding the prepared catalyst, short chain alcohol and oil into reaction kettle, heating at 60-120 degrees C, stirring to carry out esterification and ester exchange reaction for 2-10 hours, decompressing and evaporating excess short chain alcohol, and standing.
NOVELTY - A biological diesel oil is prepared by impregnating fly ash in acid solution for 1-12 hours; impregnating acidified fly ash in metal salt solution for 1-12 hours; placing into muffle furnace, gradually raising temperature to 420-480 degrees C, keeping for 1.8-2.5 hours, stopping heating, and naturally cooling to room temperature to obtain solid acid catalyst; and placing the solid acid catalyst and oil into reaction kettle, adding short chain alcohol, stirring, and heating to 60-120 degrees C to carry out esterification and ester exchange reaction.    USE - Method for preparing biological diesel oil using fly ash solid acid catalyst (claimed).    ADVANTAGE - The method is simple, and makes use of catalyst that is easy to separate and recycle, thus avoiding environment pollution.    DETAILED DESCRIPTION - Preparing biological diesel oil by fly ash solid acid catalyst comprises:    (A) taking fly ash with particle size of more than 0.15 mm, impregnated in acid solution for 1-12 hours, taking out at 30-200 degrees C, and obtaining the acidified fly ash;    (B) impregnating acidified fly ash in metal salt solution for 1-12 hours, taking out at 30-200 degrees C and drying to obtain fly ash containing metal salt;    (C) placing into muffle furnace, gradually raising temperature to 420-480 degrees C, keeping for 1.8-2.5 hours, stopping heating, and naturally cooling to room temperature to obtain solid acid catalyst; and    (D) placing the solid acid catalyst and oil into reaction kettle, adding short chain alcohol, stirring, heating to 60-120 degrees C to carry out esterification and ester exchange reaction, reacting for 2-10 hours, decompressing and evaporating the rest of short chain alcohol, and standing and separating the catalyst and glycerin to obtain biological diesel oil.    The solid acid catalyst is 3-7 wt.% and a mole ratio of the short chain alcohol and oil is 3-12:1.
NOVELTY - A refrigerant comprises 40-90 pts. wt. propane, 6-17 pts. wt. isobutane, 6-24 pts. wt. propylene and 2.5-9.5 pts. wt. trifluoroiodomethane.    USE - A refrigerant.    ADVANTAGE - The refrigerant is environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of refrigerant comprising cleaning pressure vessel using cleaning agent, placing 40-90 pts. wt. propane, 6-17 pts. wt. isobutane, 6-24 pts. wt. propylene and 2.5-9.5 pts. wt. trifluoroiodomethane, and mixing.
NOVELTY - The utility model claims a biomass hydrolysing and liquefying device, especially a kind of tube-type supercritical biomass hydrolysing and liquefying device. The utility model comprises a feeding hopper, a tin tank, a temperature controller, a cooling pipe, a solid-liquid separator, the solid outlet pipe, a liquid outlet pipe, a cooling water tank, a box-type electric heating furnace, a hydrolysis reaction. Feeding hopper passes through the box-type electric heating furnace and is connected with the hydrolysis reaction of a box-type electric heating furnace, a box-type electric heating furnace is provided with a tin tank, tin tank is connected with a temperature controller, hydrolysis reaction pipe passes through the box-type electric heating furnace and connected with box-type electric heating lower part cooling exhaust device of high-power induction cooker in the water tank of the cooling pipe and the cooling pipe through the cooling water tank and is connected with the solid-liquid separator lower part cooling water tank, solid-liquid separator side and liquid outlet pipe is connected with the bottom is connected with the solid outlet pipe. This utility model is designed to be tubular, increase the heating area of the raw material, accelerating reaction speed.
NOVELTY - The utility model claims a biomass hydrolysing and liquefying device, especially a kind of ultrasound-enhanced supercritical biomass hydrolysing and liquefying device. This utility model comprises supercritical hydrolyzing reaction device, a cooling device, a solid-liquid separating device and rectifying device, supercritical hydrolyzing reaction device by a pipeline orderly connected cooling device, a solid-liquid separating device and rectifying device, each device directly on a water pump pipeline and a valve. This utility model in the reaction kettle as raw material of liquid heating and constant temperature, shortening in the reaction kettle to a supercritical fluid for a time, reduces the pyrolysis and carbon deposit in the reaction, ultrasonic transducer by cavitation effect of the ultrasonic wave, mechanical fluctuation effect and thermal effect, the biomass is easier, reduces the liquid pressure and temperature, to obtain pure product of fuel through the whole device.
NOVELTY - This utility model claims a solar energy storage battery dry fermentation methane tank, comprising a methane tank, an aqueduct, a water storage tank, a solar photovoltaic, a controller, an inverter, a storage battery, a controller and a temperature sensor; the marsh gas tank storage chamber is set in a fermentation room, air port is set on the storage chamber and the fermentation time, water guide pipe is set on the storage chamber, biogas outlet, a feeding port, a temperature sensor, a heater and a discharging port is set on the fermentation time, aqueduct and water tank connected with the marsh gas outlet and the feed opening is arranged at the upper end of the marsh gas tank, the discharge hole is set at the lower part of the marsh gas tank, solar photovoltaic panel is connected with the controller, the temperature sensor is connected with a temperature controller, the controller is connected with the heater, an inverter and a storage battery to form a loop. This utility model into electric energy by using solar photovoltaic, heating fermentation tank reach constant temperature whole day has convenient use, energy saving, low cost and so on.
NOVELTY - The utility model claims analysis tower for biogas purifying, the invention claims a method for combined analysis tower for biogas purifying, comprising an upper tower and a lower tower, a tower, a tower from top to bottom in turn, the upper and the lower tower through pipeline, the pipeline is provided with an adjusting valve, the tower is provided with a steam outlet, the tower wall is provided with a liquid inlet, and the top of the lower tower wall is provided with a gas outlet, the bottom is provided with a liquid discharge port. This utility model is featured with simple structure, small floor area, depth analysis of the carbon dioxide in the washing liquid, and improves the stability and safety of the analysis system, which greatly reduces the production cost and improves the economic benefit.
NOVELTY - This utility model claims one kind of based on a difference spectrum marsh gas detecting and purifying control system. The purpose is that the provided system has high detection precision, low cost and long service life. Technical solution is as follows: a kind of a marsh gas detecting and purifying control system for a differential absorption spectroscopy, comprising a control centre and a processing unit, wherein the system further comprises a structure of: A, Marsh gas tank is connected with dehydrating tower, desulfurizing tower, decarburization tower and storage tank B through the pipeline in turn. Specifically the dehydrating tower, a desulfurizing tower, a decarburization tower and methane gas storage tank is set with pipeline inlet sampling port, each sampling port pre-treating device are connected in turn through an air pipe and an air chamber C is a detection centre. Information to the processing unit belong to a wave band infrared light source for emitting infrared light for detecting the gas to the gas chamber, and a detector for receiving and detecting the infrared light and detecting, and then obtaining the data processing, at last, conveyed to the control centre.
NOVELTY - This utility model is a kind of using kitchen garbage to prepare for vehicle natural gas device, comprising a device for pre-processing kitchen garbage paste homogenizing heating device, an anaerobic digestion tank, a marsh gas storage cabinet, a desulfurizing device and pressure swing adsorption device, the device for pre-processing kitchen garbage comprises the upper part is connected to the bracket of the box body, the top of the box body is provided with a material inlet, the bottom of the box body is provided with a slurry outlet, the box body is horizontally penetrated main shaft protecting tray for crusher, wherein the crusher main shaft is connected with a crushing cutter head, a box body on one side of the upper part is provided with an air outlet towards the fan in the box body, the air outlet is on the side of the light box body is provided with a material outlet, the box body is provided with a connecting main shaft protecting tray for crusher of the driving motor I, the slurry homogenizing heating device comprising a tank body is long tubular, the tank body cavity is penetrated with the spiral blade of the main shaft, the main shaft is connected with a drive motor II, the upper part of the front end of one end of the tank body is provided with a feeding opening, the other end of the tank body is provided with a discharging port, the tank body is covered with a jacket.
NOVELTY - Methanol gasoline complex additive comprises 35-50% metal corrosion inhibitor, 5-15% rubber swelling inhibitor, 1-5% triphenyl phosphate ester anti-wear lubricant, and 30-60% low carbon alcohol containing 1-5 carbon atoms.    USE - Used as methanol gasoline complex additive.    ADVANTAGE - The additive: is suitable for methanol gasoline with more than M70 and M5-M30 standards; inhibits high and low proportion methanol gasoline engine and corrosion of the metal parts and high and low proportion methanol gasoline vehicle oil supply system rubber; prevents swelling of rubber material; and reaches wearable lubrication effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the methanol gasoline complex additive, comprising adding the above mentioned components into a reaction kettle, stirring and reacting at 40-60 degrees C for 1-2 hours under sealed conditions.
NOVELTY - Preparation of graphene load magnetite nanoparticle comprises taking graphite oxide and dimethyl sulfoxide, adding N-hydroxysuccinimide and dicyclohexylcarbodiimide, stirring, filtering, washing and drying; dissolving in dimethyl sulfoxide, adding polyamide amine, reacting, stirring, filtering, washing and drying; adding concentrated ferric trichloride, reacting, adjusting pH value, adding solid sodium borohydride with ammonia water, reacting, filtering, washing and drying.    USE - Method of preparing graphene load magnetite nanoparticle used for sewage treatment and enzyme sensor.    ADVANTAGE - The nanoparticle does not need protection of nitrogen or argon, does not need high temperature, has mild reaction condition and reduced preparation cost of material.    DETAILED DESCRIPTION - Preparation of graphene load magnetite nanoparticle comprises:    (A) taking 100 mg graphite oxide and 20 mL dimethyl sulfoxide, adding 1-2 g N-hydroxysuccinimide and 1 g dicyclohexylcarbodiimide, stirring at 35 degrees C for 3 hours, filtering, washing and drying;    (B) dissolving in 30 mL dimethyl sulfoxide, adding polyamide amine, reacting at 20-60 degrees C, stirring for 1-5 hours, filtering, washing and drying; and    (C) adding 10 mL concentrated ferric trichloride, reacting at 60 degrees C for 2 hours, adjusting pH value to 7.5-11, adding 100 mg solid sodium borohydride with ammonia water, reacting at 60 degrees C for 3 hours, filtering, washing and drying.
NOVELTY - A Dysosma versipellis extract comprises 20-50 wt.% podophyllotoxin, 3-8 wt.% kaempferol and 8-15 wt.% flavones.    USE - The D.versipellis extract is useful in skin disinfectant or pharmaceutical composition for treating condylomata acuminate. The pharmaceutical composition is external preparation, preferably lotion, ointment or gel, more preferably lotion (all claimed).    ADVANTAGE - The D.versipellis extract has high content of effective components and less impurity, and causes less side effects. The method is cost-effective, yields high, causes low environment pollution, and has high practicability and advanced process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the above-cited D.versipellis extract, which involves (a) taking D.versipellis, adding ethanol as solvent to the above-mentioned raw material, extracting the mixture, condensing and drying the extracted solution to obtain extract A, (b) washing the obtained extract A with ethyl acetate, filtering the mixture, condensing and drying the filtrate to obtain extract B, (c) adding mixed organic solvent to the obtained extract B, heating, refluxing and washing the mixture, filtering and condensing the filtrate to obtain extract C, and (d) drying and crushing the obtained extract C, where the mixed organic solvent is obtained by mixing low polar organic solvents chosen from petroleum ether, ethyl ether, hexane, cyclohexane, acetone and ethyl acetate, and the mixed organic solvent is mixture of ethyl acetate and cyclohexane in a volume ratio of 1:1-4:1.
NOVELTY - Preparation of rabeprazole sodium comprises adding rabeprazole sulfide and sodium ion-containing alkaline material into water, adding sodium hypochlorite solution, stirring, and reacting at 0-20 degrees C.    USE - Preparation of rabeprazole sodium (claimed).    ADVANTAGE - The method does not need extracting, concentrating, and reducing steps, does not use organic solvent, is safe and environment-friendly and suitable for industrial production, and has low cost.
NOVELTY - Preparation of dexrazoxane involves reacting (S)-1, 2-diaminopropanoic acid and formamide under conditions of reduced pressure at 140-160 degrees C; decompressing to react for 3-8 hours; heating the reaction mixture and removing methyl amide in the system with water, heating and raising the temperature to 70-100 degrees C, cooling to 30 degrees C, separating out crystal, filtering, collecting the filter cake, and drying to obtain dexrazoxane. The (S)-1, 2-diaminopropanoic acid is prepared by (S)-1, 2-diaminopropane-tetraacetate.    USE - For preparation of dexrazoxane (claimed) as anti-tumor agent.    ADVANTAGE - The method needs only one step to obtain (S)-1, 2-tetra-acetate, which not only shortens the production period and reduces the production cost. At the same time, avoids high temperature, long period toxicity and reaction condition, is environmentally friendly, and dexrazoxane is more suitable for use in the pharmaceutical field.    DETAILED DESCRIPTION - Preparation of dexrazoxane involves reacting (S)-1, 2-diaminopropanoic acid and formamide under conditions of reduced pressure at 140-160 degrees C; decompressing to react for 3-8 hours; heating the reaction mixture and removing methyl amide in the system with water, heating and raising the temperature to 70-100 degrees C, cooling to 30 degrees C, separating out crystal, filtering, collecting the filter cake, and drying to obtain dexrazoxane. The (S)-1, 2-diaminopropanoic acid is prepared by (S)-1, 2-diaminopropane-tetraacetate. The (S)-1, 2-diaminopropane-tetraacetate is prepared by reacting (S)-1, 2-diaminopropane or (S)-1, 2-diaminopropane hydrochloride and chloroacetic acid ester in alkali or alkaline solvent at 30-82 degrees C to agitate and react for 8-20 hours, filtering the reaction liquid, collecting the filtrate, and concentrating to obtain (S)-1, 2-diaminopropane-tetraacetate.
NOVELTY - The utility model claims a biochemical tank cooling device, comprising a fan, a ventilation pipeline, a compressor and an air cooler, and one end of the ventilation pipe is connected with the other end of the ventilating pipeline is air outlet, the compressor is connected with a ventilating pipe, the air cooler and compressor. This utility model compared with the existing technology, has the following advantages and effects: energy saving and emission reduction, so that the biochemical sewage treatment ability is high, the processing effect is good, the biochemical pool water is controlled below 36 degrees centigrade, simple structure, convenient use and convenient installation and long service life.    USE - Biotank cooling device.    ADVANTAGE - The cooling device has energy saving and emission reduction, has high biochemical sewage treatment ability and good processing effect. It also has simple structure, convenient use, convenient installation and long service life.
NOVELTY - Wherein the utility model claims a kind of agricultural use of calcium ammonium nitrate large grain recycling device, relating to a kind of recovery device, solves the problem that the large particle of calcium ammonium nitrate recycle use, large viscosity, easy to be blocked, the labour intensity is large and the environment pollution is serious. A kind of agricultural use of calcium ammonium nitrate large particle recycling device, comprising a pipeline is provided with a self-adjusting valve are connected with the chemical material slot, a filter press by a finished product recycling tank, recycling pump, tank, further comprising a liquid pump and two mixer, in which a liquid pump is installed on the fertilizer material bottom of the No. 1 stirrer is installed on the fertilizer material groove, 2 # stirrer is mounted in the distribution groove. This utility model effectively reduces the labour intensity, increases the yield, and greatly satisfies the use of section calcium ammonium solution, improves the environment pollution.    USE - Agricultural calcium ammonium nitrate large particle recycling device.    ADVANTAGE - The device reduces labor intensity, increases yield, and satisfies use of section calcium ammonium solution, and improves environment pollution.
NOVELTY - This utility model claims a kind of new amino acid chelate organic-inorganic compound fertilizer production device, belonging to the field of organic-inorganic compound fertilizer, the device mixing machine is composed of organic fertilizer, inorganic fertilizer mixing machine, a crusher, a fermenting tank, a pelletizer, a drying device, a urea, monoammonium phosphate, potassium sulphate, a mixture of dry pig manure and cow dung, the mixture of peanut straw and rape straw, the cotton seed cake and rape seed cake, rice hull and wheat bran to mixture, drying without pollution canal mud, plant ash, lees, biogas residue organic fertilizer fermenting, sterilizing, amino acid chelate calcium, amino acid chelate copper, amino acid chelated iron, amino acid chelate manganese, a zinc amino acid chelate, ammonium molybdate for the production of a microorganism containing microelement chelate to organic-inorganic compound fertilizer as raw material, the fertilizer is rich in inorganic substance, organic matter and microelement, nutrient, long fertilizer efficiency, the yield increasing effect is obvious.    USE - Amino acid chelate organic-inorganic compound fertilizer production device.    ADVANTAGE - The device produces fertilizer which is rich in inorganic substance, organic material and microelement. The fertilizer has long fertilizer efficiency.
NOVELTY - Bacterial composition capable of degrading kitchen waste comprises 15-30 wt. pts. Bacillus subtilis single microbial inoculum, 10-25 wt. pts. Saccharomyces cerevisiae single microbial inoculum, 10-30 wt. pts. Aspergillus niger single microbial inoculum, 10-30 wt. pts. Sporotrichum thermophile single microbial inoculum and 10-30 wt. pts. Geotrichum candidum single microbial inoculum.    USE - The bacterial composition is useful for degrading kitchen waste (claimed).    ADVANTAGE - The bacterial composition and the preparation method have the benefits of low productive investment, low manufacturing cost, convenience in use and good degrading effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for preparing bacterial composition capable of degrading kitchen waste comprising culturing the strains of Bacillus subtilis, Saccharomyces cerevisiae, Aspergillus niger, Sporotrichum thermophile, and Geotrichum candidum at a high density respectively, and then inoculating to shake flasks containing culture media with the volume ratios of 15-30% for active culture; the cultured strains are inoculated to fermentation tanks containing fermentation culture media with the volume ratios of 50-70% for fermentation enlarging culture; the cultured strains are absorbed by carriers respectively to be prepared into dried single microbial inoculums.
NOVELTY - Organic matter energy regeneration system comprises waste preprocessing unit, organic waste sterilizing unit, organic wastes cracking unit, energy power generation and steam regeneration unit, organic material solid-liquid separation unit, liquid organic material regeneration unit, and solid organic material regeneration unit. Each unit processes value signal set to central control system to adjust and control remote monitor automatic adjusting unit. The waste preprocessing unit performs screening and crushing solid organic waste, and solidifying into organic waste processing raw material.    USE - Organic matter energy regeneration system.    ADVANTAGE - The energy regeneration system can decompose and ferment animal organic waste into regenerative liquid and solid organic substance to be used as organic fertilizer or animal feed, thus effectively producing green energy resources, resource recycling, purifying environment, saving energy, and reducing carbon emission. It recycles organic waste into usable product and reduces landfill incineration treatment.
NOVELTY - Preparing 4-formoxyl benzofuroxan comprises reacting 4-methyl benzene, furan and methenamine at -10 degrees C to 120 degrees C for 1-8 hours to generate a quaternary ammonium salt intermediate and hydrolyzing the quaternary ammonium salt intermediate under an acidic condition at 10-100 degrees C for 5 minutes to 3 hours, where the amount of the methenamine is 1-5 times of 4-methyl benzene and furan and the quaternary ammonium salt intermediate is optionally separated in reduction reaction system.    USE - The process is useful for preparing 4-formoxyl benzofuroxan (claimed).    ADVANTAGE - The process: produces 4-formoxyl benzofuroxan with improved yield and purity and mild reaction condition in a simple manner; and can reduce the pollution of the environment, and is suitable for industrial, commercial production.
NOVELTY - Acquiring grape alga single cells and extracellular tissues comprises removing partial moisture on the surface of wet alga.    USE - The method is useful for acquiring grape alga single cells and extracellular tissues; for cultivating algae and genetically engineered algae; for natural seed breeding; mutation breeding of seed in pigment production or algae oil extraction; and for producing aviation kerosene (all claimed).    ADVANTAGE - The method has the advantages of simpleness, easiness in operation, low cost, and efficient acquisition of high-activity grape alga single cells, and simultaneously oil extraction is easily carried out on the acquired extracellular tissues.
NOVELTY - A herbicidal microcapsule comprises 10-30 wt.% bispyribac, 0.1-2 wt.% wetting agent, 1-8 wt.% dispersant, 0.1-5 wt.% capsule material, 0.1-4 wt.% adhesive and 1-5 wt.% antifreezing agent.    USE - Herbicidal microcapsule.    ADVANTAGE - The microcapsule is provided with good weeding effect, little pollution to environment, simple and convenient package, storage and transportation to crop field.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of herbicidal microcapsule comprising taking all raw materials, adding proper amount of water, mixing uniformly, putting in horizontal sand mill to sand grind, stirring and mixing.
NOVELTY - Slow release fertilizer comprises (in pts. wt.): starch (1-99); fertilizer (1-99); plasticizer (50); and reinforcing agent (50).    USE - Used as slow release fertilizer.    ADVANTAGE - The fertilizer is environmental friendly, and has good mechanical performance and radioactive nuclide enrichment function.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the slow release fertilizer, comprising mixing and stirring starch, fertilizer, plasticizer and reinforcing agent for 5-20 min to obtain mixture, adding the mixture into a double screw extruder for extruding at 80-180 degrees C under a pressure of 0.1-1 MPa for 5-10 minutes, cooling the extruded mixture, and cutting the cooled product.
NOVELTY - The gasket has fluorine rubber cloth which is wrapped around the periphery of diaphragm gasket main portion.    USE - Wrapping diaphragm gasket for electrolysis hydrogen generation device.    ADVANTAGE - The sealing effect of gasket can be improved effectively. The diaphragm pad is elastic, so that loss of gas can be avoided effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the wrapping diaphragm gasket.
NOVELTY - A mixed refrigerant comprises 1-10 wt.% trifluoroiodomethane having combustion inhibiting and explosion suppression effect, 20-40 wt.% 1,1,1,2-tetrafluoroethane, and 50-75 wt.% propane.    USE - A mixed refrigerant.    ADVANTAGE - The mixed refrigerant has ozone depletion potential (ODP) value of zero, global warming potential (GWP) value far less than hydrofluorocarbons (HFCs) normal work, and has good oil solubility. It can directly substitute R22 working medium and there is no need to greatly change the refrigeration system. Flammable refrigerant is greatly reduced even non-combustible, so that cooling safety of the system is greatly improved.
NOVELTY - Middle-high temperature heat pump mixed working fluid comprises 4-90 mass% n-butane (R600), 5-91 mass% 1,1,1,3,3-pentafluoropropane (R245fa) and 5-91 mass% 1,1-difluoroethane (R152a).    USE - Middle-high temperature heat pump mixed working fluid.    ADVANTAGE - The working fluid is suitable for 60-100 degrees C low temperature organic Rankine cycle system. It does not damage ozone layer and greenhouse effect potential is low to meet the requirements of environment protection according to the engineering parameter. It has good cycle performance, can be directly poured in air conditioning system compressor, and does not need additional medium. COP is 4, and unit mass output net work is more than 150 kJ/kg.
NOVELTY - The obtaining method involves performing decomposition of water into hydrogen and oxygen under the influence of electromagnetic field resonant frequency of n-th harmonic that is close to the natural frequency of water. The decomposition of water into hydrogen and oxygen takes place under the action of two electromagnetic resonance field voltage vector electric fields that change the direction of 180 degrees at a constant direction perpendicular to electric field the total intensity of magnetic fields of circuit inductance.    USE - Method for obtaining hydrogen from water.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a hydrogen cell.
NOVELTY - A yellow paecilomyces cicadae is provided as raw material, dried, pulverized, sieved having size of 20-80 meshes into an extraction kettle, extracted at 40-50 degrees C under pressure of 15-25 MPa, and supercritically extracted through the carbon dioxide liquid. The extract is analyzed from the separating kettle at 50-60 degrees C under pressure of 6-10 MPa, obtained extract is purified by high-speed counter-current chromatography, on-line monitoring is ultraviolet detected, target component is collected and reagent is recycled, to obtain yellow cicada octyl.    USE - Preparation of yellowish cicada octyl (claimed).    ADVANTAGE - The yellowish cicada octyl is efficiently prepared with improved extracting efficiency, by simple method.
NOVELTY - Ternary slow release fertilizer comprises a cement-coated slow release organic-inorganic fertilizer and microbial inoculum, and the weight of the microbial inoculum is 0.5-5 wt.% of the cement-film-coated slow release fertilizer.    USE - Used as ternary slow release fertilizer.    ADVANTAGE - The method includes adhering of microbial agent on the surface of the coating, so that affects on the activity and the group number of beneficial micro-organisms caused by inorganic salt and high impurity-bacterial rate of an inorganic fertilizer are avoided, and the effective viable count is maintained to reach the standard; is simple and convenient to operate and mild in condition, and can be used for realizing the industrial production by being cooperated with the traditional technical apparatus.    DETAILED DESCRIPTION - An INDEPENDENT CLIAM is also included for preparing the ternary slow release fertilizer, comprising preparing cement-coated slow release organic-inorganic fertilizer, and then adhering the microbial inoculum on the coating surface.
NOVELTY - A sewage treatment device comprises mud tank body having water inlet and water outlet, cylindrical guide device, fixed guide reflection part with reflection working surface, low carbon source, and conical bottom end. A weir is connected to the tank body where lower part is provided with water outlet. The guide device is provided at the upper part of water inlet. The water inlet end of water inlet pipe and upper part of the pool body is connected with water inlet. The bottom end of guide device is a downward opening of water outlet end.    USE - Sewage treatment device.    ADVANTAGE - The device does not need extra carbon source.
NOVELTY - Preparation of (3R)-(-)-3-(2-acetamino)-5-methylhexanoic acid involves salifying ( plus minus )-3-(2-acetamino)-5-methylhexanoic acid racemic material as raw material and (S)-(-)-1-phenylethylamine in a mixed solvent of alcohol and halogenated hydrocarbon, precipitating out unnecessary S-shaped chiral isomer salts, filtering, concentrating filtrate, dissolving product into water, reacting by using an acid and refining. The purity and yield of product is 98-99% and 80-90%, respectively.    USE - Preparation of (3R)-(-)-3-(2-acetamino)-5-methylhexanoic acid used as antiepileptic medicament pregabalin intermediate (claimed).    ADVANTAGE - The method efficiently and economically provides (3R)-(-)-3-(2-acetamino)-5-methylhexanoic acid having high chiral monomer purity. The method is environmentally-friendly, and utilizes less amount of raw materials.
NOVELTY - 2-((4-Fluorophenyl)carbonyl)aniline and 2-bromo-1-cyclopropylethan-1-one are condensed and product is reacted with 7-(2-cyclopropyl-4-(4-fluorophenyl)-3-quinolinyl)-5-carbonyl-(3R)-3- alkylbenzene sulfonate-6-alkynyl enanthate, to obtain carbonyl group-containing compound (I). Alkynyl in product is reduced, to obtain carbonyl group-containing compound (II). Product is subjected to hydroboration reduction, to obtain pitavastatin calcium crude drug intermediate ((4R,6S,7E)-8-(2-cyclopropyl-4-(4-fluorophenyl)-1,2,3,4-tetrahydroquinolin-3-yl)-4,6-dihydroxyoct-7-en-2-one).    USE - Preparation of pitavastatin calcium crude drug intermediate (claimed).    ADVANTAGE - The pitavastatin calcium crude drug intermediate having excellent stereospecificity is prepared with high yield under mild reaction conditions by environmentally-friendly and economical method.    DETAILED DESCRIPTION - 2-((4-Fluorophenyl)carbonyl)aniline and 2-bromo-1-cyclopropylethan-1-one are subjected to condensation reaction, to obtain 3-bromo-2-cyclopropyl-4-(4-fluorophenyl)-1,2,3,4-tetrahydroquinoline. The resulted product is reacted with 7-(2-cyclopropyl-4-(4-fluorophenyl)-3-quinolinyl)-5-carbonyl-(3R)-3- alkylbenzene sulfonate-6-alkynyl enanthate, to obtain carbonyl group-containing compound of formula (I). The alkynyl in the resulted product is reduced using bis(2-methoxy-ethyoxyl)aluminum sodium hydride reducing agent, to obtain trans-olefin of carbonyl group-containing compound of formula (II). The resulted product is subjected to hydroboration reduction and hydrolysis reaction, to obtain pitavastatin calcium crude drug intermediate.    R1=alkylbenzene sulfonate, in which alkyl is 1-12C alkyl;and    R2=1-8C alkyl.
NOVELTY - Synthesis of 4-(2-(2-amino-4-oxo-4,7-dihydro-3H-pyrrolo(2,3-d)pyrimidin-5-yl)-ethyl)-benzoic acid comprises performing Heck reaction of substituted methyl benzoate (I) and allyl alcohol, adding sodium bisulfite, adding nitromethane, performing Henry reaction, reacting with methanesulfonamide chloride in the presence of triethylamine, reacting with 2,4-diamino-6- hydroxypyrimidine, performing Nef reaction in the presence of potassium hydroxide to obtain crude pemedolac, adding organic weak base salt and purifying with hydrochloric acid.    USE - Synthesis of 4-(2-(2-amino-4-oxo-4,7-dihydro-3H-pyrrolo(2,3-d)pyrimidin-5-yl)-ethyl)-benzoic acid (claimed).    ADVANTAGE - The energy-saving and environment-friendly method has high yield, mild reaction conditions and produces high-purity product. The solvent is convenient to recycle.    DETAILED DESCRIPTION - Synthesis of 4-(2-(2-amino-4-oxo-4,7-dihydro-3H-pyrrolo(2,3-d)pyrimidin-5-yl)-ethyl)-benzoic acid comprises performing Heck reaction of substituted methyl benzoate of formula (I) and allyl alcohol, adding sodium bisulfite to obtain 3-(4-methoxycarbonyl) phenyl-1-hydroxypropyl sulfonate, deprotecting using deprotecting reagent, adding nitromethane, performing Henry reaction to obtain 4-(3-hydroxy-4-nitrobutyl) methyl benzoate, reacting with methanesulfonamide chloride in the presence of triethylamine to obtain 4-(4-nitro-3-butenyl) methyl benzoate, reacting with 2,4-diamino-6- hydroxypyrimidine to obtain 4-(3-(2,6-diamino-oxopyrimidin-5-yl)-4-nitrobutyl) methyl benzoate, performing Nef reaction in the presence of potassium hydroxide to obtain crude pemedolac, adding organic weak base salt and purifying with hydrochloric acid.    X=I or Br.
NOVELTY - The tower has a lower seal head whose lower end is welded on a tower body. A synthetic ammonia air outlet pipe is connected to an upper end enclosure. An ammonia water outlet pipe is installed at a lower end enclosure. A swirl nozzle is connected to an annular water distributing pipe.    USE - Mist spray nozzle ammonia washing tower.    ADVANTAGE - The tower has large contact area, better absorption effect and high ammonia water concentration, and reduces pollution to the environment.
NOVELTY - The device has a main heat exchanger provided with a compression air purifying unit that is connected with air inlet and outlets of a raw material. A liquid nitrogen outlet of a gas-liquid separator is formed with a liquid nitrogen product opening that is connected with a liquid nitrogen heat exchanger for circulating pressure liquid nitrogen. An outlet part of the separator is connected with a liquefied natural gas (LNG) heat exchanger for reheating a circulating pressure nitrogen return port. A low temperature circulating nitrogen compressor is provided with a nitrogen inlet.    USE - LNG cold energy utilizing liquid-air separation device.    ADVANTAGE - The device is energy-saving, and reduces energy consumption, and improves social benefit and economic benefit and ensures safety of an air separation device body.
NOVELTY - Organic-based fertilizer comprises 50-60 wt.% cow and sheep droppings, 35-45 wt.% biogas, 1-1.5 wt.% potassium fulvate, 0.5-1 wt.% phosphoric acid, and 2-3 wt.% organic calcium, magnesium, zinc and iron.    USE - The organic-based fertilizer is useful for grape (claimed).    ADVANTAGE - The fertilizer is environmentally-friendly as it eliminates pollution to soil and grape caused by chemical fertilizers, reduces damage caused by pest and disease, improves soil, and yield and quality of grapes, avoids alkalization and salination, and enables storage of grape for a long period of time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing organic-based fertilizer, which involves (a) adding sodium hydroxide to the saturated solution of potassium fulvate, allowing the mixture to react in a acid tank, and generating potassium humate, (b) mixing calcium oxide, magnesium oxide, zinc oxide and ferric oxide with saturated solution of amino acids, allowing the mixture to react in the acid tank, and generating organic calcium, magnesium, zinc and iron, (c) mixing the cow and sheep droppings, biogas, potassium fulvate, phosphoric acid, organic calcium, magnesium, zinc, iron and strain liquid, repeatedly stirring the mixture, uniformly mixing the mixture, stacking the mixture, performing fermentation, turning and crushing the fermented product after 20-30 days, and packaging the product.
NOVELTY - The device has a column-shaped casing which is fixed with the heat treatment reactor. A hollow square shaped steel pipe is provided in casing. A material inlet is provided in upper portion of casing. The spiral propeller and end portion of shaft are connected with each other, so as to prevent the gas leakage. A speed regulating motor is used to drive the spiral propeller to rotate. The heating chamber is surrounded by heat preservation insulation wall. The ends of chamber are respectively connected to the flue gas inlet. A discharge port is connected with sealing screw slag remover.    USE - Device for extracting fuel oil from oil sand and organic waste.    ADVANTAGE - The coking of oil can be prevented. Continuous production of oil can be ensured. The fuel oil recovery rate can be improved. The device is simple in structure and convenient to maintain. The processing cost of the device can be reduced.
NOVELTY - A high-temperature reformer reacted with hydrocarbon fuel and water, and produces hydrogen, a carbon monoxide shifter which shifts carbon monoxide, a carbon monoxide remover removes the carbon monoxide which is remained after the carbon monoxide shifting, and a burner portion transmits the heat generated by combusting the hydrocarbon fuel to the high temperature reformer. The combustion gas generated in the burner portion is heat-exchanged with the carbon monoxide shifter or the carbon monoxide remover so that the carbon monoxide shifter or the carbon monoxide remover is preheated.    USE - Method for operating reformer used for modifying system (claimed) for fuel cell.    DETAILED DESCRIPTION - A high-temperature reformer reacted with hydrocarbon fuel and water, and produces hydrogen, a carbon monoxide shifter which shifts carbon monoxide unavoidably generated in the high temperature reformer, a carbon monoxide remover removes the carbon monoxide which is remained after the carbon monoxide shifting, and a burner portion transmits the heat generated by combusting the hydrocarbon fuel to the high temperature reformer. The combustion gas generated in the burner portion is heat-exchanged with the carbon monoxide shifter or the carbon monoxide remover so that the carbon monoxide shifter or the carbon monoxide remover is preheated. An INDEPENDENT CLAIM is included for modifying system.
NOVELTY - Cold flow improving method of biodiesel derived from vegetable oil and animal fat involves adding element (a) to biodiesel derived from vegetable oil and animal fat, forming the saturated fatty acid methyl ester, cohering inclusion compound, and removing inclusion compound.    USE - Cold flow improving method of biodiesel derived from vegetable oil and animal fat.    ADVANTAGE - The method enables efficient cold flow improving method of biodiesel derived from vegetable oil and animal fat with excellent low-temperature characteristics.
NOVELTY - The rocket apparatus (100) has a protection element (153) which penetrates to one end of launching fixing unit (151). A blocking plate is formed in upper side of launching supporting element (152). A fixing unit (156) is equipped with fixing groove (131c). A piezoelectric ceramic switch (155) is connected with launching fixing unit. One end of launching fixing unit is penetrated to launching supporting element. A launching brave fighting pole rod (154) is equipped in launching supporting element.    USE - Rocket apparatus.    ADVANTAGE - The rocket has low manufacturing cost. The electrolytic development can be confirmed by the naked eye confirmed and the learning effect can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the rocket apparatus.    Rocket apparatus (100)    Fixing groove (131c)    Launching fixing unit (151)    Launching supporting element (152)    Protection element (153)    Launching brave fighting pole rod (154)    Piezoelectric ceramic switch (155)    Fixing unit (156)
NOVELTY - The fuel cell generation system has solar heat generator that heats up air using the solar energy. The heated air supplied from the solar heat generator is changed to the vapor. The steam separator (134) is provided to collect the predetermined gas ejected from the fuel cell for generating the oxygen and electricity using the hydrogen generated from the electrolyzer (122). The steam separator is provided to preheat the water at specific room temperature and specific gas ejected from the fuel cell.    USE - Fuel cell generation system.    ADVANTAGE - The efficiency of the fuel cell generation system can be improved. The management cost of the fuel cell generation system can be reduced, since fuel consumption can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic block diagram of the fuel cell generation system. (Drawing includes non-English language text)    Collector (111)    Storage unit (113)    Steam generator (114)    Electrolyzer (122)    Steam separator (134)
NOVELTY - Extraction of stock oil for biodiesel involves preparing microalgae slurry including water (200-1000 parts weight) with respect to dried microalgae (100 parts weight), obtaining pre-processed microalgae by irradiating microalgae slurry for 3-8 minutes, and extracting stock oil from pre-processed microalgae.    USE - Extraction of stock oil used for manufacture of biodiesel (claimed).    ADVANTAGE - The stock oil is extracted, with improved yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of biodiesel.
NOVELTY - An organic sulfur compound-removing adsorbent comprises activated charcoal oxide as an active ingredient.    USE - Organic sulfur compound-removing adsorbent is used for fuel gas desulfurization-purification system (claimed) for desulfurization-purification of fuel gas used for production of hydrogen.    ADVANTAGE - The economical system containing the adsorbent efficiently removes organic sulfur compound contained in the fuel gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel gas desulfurization-purification system.
NOVELTY - The refinement and recovery system has a refinement filter (50) that removes the tar in the synthetic gas separated by a gas separator (20) from solid particle. A fluidized-bed gasification unit (10) heats-decomposes synthetic gas provided with hydrogen and carbon monoxide as main component to separate dust and fluid yarn. Another gas separator (40) separates the additional synthetic gas from solid particle made of biomass, such that the tar separated from the solid particle is reused by heating source of fluidized-bed gasification unit as raw material for synthetic fuel.    USE - Tar refinement and recovery system using solid particle.    ADVANTAGE - The installation cost and the running cost of the facility are reduced by using the fluidized-bed gasification unit. The need of additional tar refinement apparatus is eliminated in the tar refinement and recovery system, thus the cost of the facility is reduced. The energy consumption of the tar refinement and recovery system is reduced by the absorbing the tar in the solid particle being injected in the synthetic gas generated through the fluidized-bed gasification unit. The tar absorbed to the solid particle is reused to the fuel of the fluidized-bed gasification unit, thus the tar refinement and recovery system is used effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the tar refinement and recovery system. (Drawing includes non-English language text)    Fluidized-bed gasification unit (10)    Gas separators (20,40)    Refinement filter (50)    Blower fan (60)    Discharge pipe (211)
NOVELTY - Preparing adipic acid by oxidation cyclohexanol, involves oxidizing the cyclohexanol, in presence of hydrogen peroxide and catalyst comprises titanium-silicon molecular sieve and poly-metal oxygen acid and/or its salt.    USE - For preparing adipic acid (claimed) used as food, ester plasticizer and textile treatment agent, and for producing the medicine, pesticide, spice, adhesive and flux.    ADVANTAGE - The method is environment friendly, provides high yield of adipic acid, and does not produce harmful discharge.
NOVELTY - Preparing a carbon dioxide absorbent based on natural biomass, comprises (a) carbonizing a plant biomass material containing alkali metals or alkaline earth metals, and (b) pulverizing the carbonized biomass material.    USE - The method is useful for preparing a carbon dioxide absorbent based on natural biomass (claimed) which is used for dry carbon dioxide absorption processes necessary to recover carbon dioxide contained in flue gases, which arise from the conversion of fossil fuels in industrial facilities e.g. thermal power stations, before release into the atmosphere.    ADVANTAGE - The method: produces the carbon dioxide in an environmentally friendly and economical manner without artificial addition of alkali metals and alkaline earth metals, contributing to cost reduction; provides recovering the metal components which have been discarded after use, by burning carbon components; and utilizes the alkali metal or alkaline earth metal components which are in a highly dispersed state in the natural biomass material, thus avoiding maintaining a highly dispersed state of the active components upon addition, contributing to a drastic reduction in processing cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for the carbon dioxide absorbent based on natural biomass prepared by the method.
NOVELTY - The method involves locating two permeable electrodes (16,18) in an electrolysis apparatus (10) and immersing in a chamber (20) equipped with inlet (26) and two outlets (28,30). The solution is passed into the chamber through inlet. A voltage is applied to the apparatus across the electrodes to electrolyze the solution between the electrodes so that the specific combustible fluids are formed on the respective electrodes and passed into the respective outlets. The two electrodes are located in relative close proximity to one another in a range of between 1 mm and 6 mm.    USE - Method for producing combustible fluid such as hydrogen gas and oxygen gas (claimed) from liquid alkaline electrolytic solution during electrolysis process.    ADVANTAGE - The two electrodes are located in relative close proximity to one another in a range of between 1 mm and 6 mm so that the catalytic effectiveness of the electrodes can be enhanced. The gas bubbles forming on the electrodes can be immediately removed with the flow of electrolyte. The effective conduction area of the electrode can be increased with reduced effective voltage requirement. The efficiency of the electrolysis apparatus can be improved at reduced operating cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an electrolysis apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross sectional view of the electrolysis apparatus.    Electrolysis apparatus (10)    Permeable electrodes (16,18)    Chamber (20)    Inlet (26)    Outlets (28,30)
NOVELTY - Transferring heat produced by a fuel cell module positioned onboard an aircraft comprises coupling a loop heat pipe (LHP) module (218) to the fuel cell module (202), where the LHP module includes a first fluid; and channeling the first fluid through the LHP module, where the first fluid absorbs the heat from the fuel cell module.    USE - Method for transferring heat produced by a fuel cell module positioned onboard an aircraft.    ADVANTAGE - The method increases fuel cell efficiency for use in an airplane galley and/or decreases a quantity of airplane generated power required to operate the airplane during flight, and also decreases an amount of power used by galleys through energy storage, uses combined heat and power from fuel cells, and efficiently transfers the heat from the fuel cell to galley insert loads.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a fuel cell cogeneration system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a fuel cell cogeneration system.    Fuel cell cogeneration system (200)    Fuel cell module (202)    Fuel (204)    Air (206)    LHP module (218)
NOVELTY - The gasifier has a gasification reactor (32) including a pyrolysis unit (14), an oxidization unit (16), and a reduction unit (18). A supplying unit (10) supplies biomass into the pyrolysis unit. A conveying unit conveys the biomass by the pyrolysis unit. An opening (42) supplies gasification agent into the oxidization unit. A dissipation unit (20) drives off product gas (22) e.g. hydrogen gas, from the reduction unit of the gasification reactor. A supplying unit is opened to supply the gasification agent in a middle part of the oxidization unit.    USE - Biomass gasifier for recovering product gas e.g. hydrogen gas and carbon monoxide gas, by gasification of biomass.    ADVANTAGE - The supplying unit is opened to supply the gasification agent in the middle part of the oxidization unit, thus enhancing operation of the gasifier, and enabling cleaning process of the raw material i.e. hogged wood, and part of the contaminants in the gasifier in a simple and inexpensive manner. The design of the gasifier allows the contaminants and slag to be conveniently and simply delivered during operation of the gasification reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic side view of a biomass gasifier with a single-piece conveyor of a pyrolysis unit.    Supplying unit (10)    Pyrolysis unit (14)    Oxidization unit (16)    Reduction unit (18)    Dissipation unit (20)    Product gas (22)    Gasification reactor (32)    Opening (42)
NOVELTY - Growing and/or harvesting algae involves: mixing seawater with feather additive in a bioreactor; growing algae by digesting the additive with algae; harvesting the algae; and drying a biomass formed in harvesting step, where at least 20 vol.% of bioreactor is filled with the additive. The growing step is carried out in bioreactor and feather additive serves as a physical structure for the algae to grow on. A majority of undissolved solid materials in the mixture of the seawater and the feather additive, is the feather additive. The feather additive is in the form of unprocessed feathers.    USE - For growing and/or harvesting algae of Nannochloropsis genus (claimed) including Nannochloropsis gaditana, Nannochloropsis granulate, Nannochloropsis limnetica, Nannochloropsis oceanica, and/or Nannochloropsis salina; and for producing concentrated biomass to produce an omega 3 nutrient source for human and animal consumption, fertilizer, vitamins, oil, biofuel, cosmetics, and other products. The harvested algae used in various applications including, but not limited to, biofuel, oil production, nutrient supplements, and cosmetics.    ADVANTAGE - The present method utilizes seawater to produce valuable algal by-products, particularly recycles seawater and feather waste into valuable by-products; grows plants or microorganisms, e.g. halophytes or brine shrimps, in the remaining solution; desalinates remaining seawater from microalgae production process in order to further purify the seawater source for human or animal consumption; utilizes the recycled seawater and the recycled feather additive to reproduce, grow, and harvest algae.
NOVELTY - Fatty acid ester is continuously produced by performing process (a) by supplying mixture of raw material composition containing fat and oil, free fatty acid, and water and lower alcohol to catalytic reaction tube (10), performing process (b) by introducing effluent from catalytic reaction tube into glycerol separation tank (40) and contacting effluent and glycerin layer, performing process (c) by collecting upper layer and mixing upper layer and lower alcohol, performing process (d) by supplying resulting mixture to catalytic reaction tube, and repeating processes (b)-(c).    USE - Continuous production of fatty acid ester for biodiesel fuel.    ADVANTAGE - Fatty acid ester can be continuously produced under mild reaction conditions.    DETAILED DESCRIPTION - Fatty acid ester is continuously produced by performing process (a) by supplying mixture of raw material composition containing fat and oil, free fatty acid, and water and lower alcohol to catalytic reaction tube (10), performing process (b) by introducing effluent from catalytic reaction tube into glycerol separation tank (40) and contacting effluent and glycerin layer, performing process (c) by collecting upper layer and mixing upper layer and lower alcohol, performing process (d) by supplying resulting mixture to catalytic reaction tube, and repeating processes (b)-(c). Catalytic reaction tube of reaction apparatus is filled with lipase. Reaction apparatus has glycerol separation tank in downstream of catalytic reaction tube.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of an enzyme packed bed reactor. (Drawing includes non-English language text).    Catalytic reaction tube (10)    Pressure gauge (20)    Raw material tank (30)    Glycerol separation tank (40)    Pump (50)
NOVELTY - The method involves supplying gas e.g. oxygen, air, carbon dioxide or vapor, leaving from a fluidized bed gasifier (1) to a gas cooler (4), and cooling the gas with temperature from 100 degrees Celsius to 250 degrees Celsius. The cooled gas is supplied to a dust removal device (5) that is operated at temperature of 250 degrees Celsius. Sorbent e.g. activated aluminum oxide, china clay, bentonite or silicon oxide, is supplied to the gas flow in the gasifier before supplying the gas to the dust removal device.    USE - Method for heavy metal-deposition during fluidized bed gasification of charcoal and biomass (all claimed).    ADVANTAGE - The cooled gas is supplied to the dust removal device that is operated with temperature of 250 degrees Celsius, and the sorbent is supplied to the gas flow in the gasifier before supplying the gas to the dust removal device, thus ensuring simple deposition of heavy metal during fluidized bed gasification of the biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a method for heavy metal-deposition during fluidized bed gasification.'(Drawing includes non-English language text)'    Fluidized bed gasifier (1)    Feed supply (2)    Gas cooler (4)    Dust removal device (5)    Quench (6)
NOVELTY - The method involves supplying the bottom product (7) of fluidized bed gasifier (2) to a buffer tank (10). The bottom product from the buffer tank is supplied to the fluidized bed (14) in a pressure tank (12) provided with cooling system and pressure relaxation system. The temperature and pressure of the fluidized bed in the pressure tank are set to 1.5 degrees c and 40 bar respectively.    USE - Method for refrigerating and depressurizing bottom product resulting during fluidized-bed gasification of biomass, brown coal and hard coal.    ADVANTAGE - The bottom product resulting during fluidized-bed gasification of biomass, brown coal and hard coal can be cooled efficiently in a cost-effective manner, by cooling the bottom product using the cooling system of the pressure tank. The depressurization of cooled product can be performed reliably using the pressure relaxation system of pressure tank.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for plant for refrigerating and depressurizing bottom product resulting during fluidized bed gasification of biomass, brown coal and hard coal.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the plant for refrigerating and depressurizing bottom product resulting during fluidized bed gasification of biomass, brown coal and hard coal.    Fluidized bed gasifier (2)    Bottom product (7)    Buffer tank (10)    Pressure tank (12)    Fluidized bed (14)
NOVELTY - Coated sulfur particle of 0.05-200 mu m diameter and a coating thickness of 0.05-50 mu m, is claimed. The coating includes at least 80 wt.% inorganic components and not greater than 20 wt.% short-chain alkyl groups.    USE - The coated sulfur particles powder is useful for converting a plastic rubber-mass into a cross-linked elastomeric phase (claimed).    ADVANTAGE - The coated sulfur particle is environmentally friendly, makes use of compatible shell materials including fillers and additives during rubber processing, ensures storage-stability of sulfur-rubber-finished mixtures, enables the rubber-fabricators production in a simple manner, and increases cost efficiency and increased product quality with product safety.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the coated sulfur particle, comprising suspending or dispersing the sulfur particle having a diameter of 0.05-200 mu m and a silica sol or water glass in water or in an aqueous suspension medium, stirring with a dispersing agent such that the sulfur particle are kept in suspension, and drying the resulting mixture.
NOVELTY - Solid carriers of microbial inoculants obtaining involves grinding fine schist and shale derived from shale pyrolysis, and passing the product through sieve of 2mm, where pH of crushed schist or thin shale is maintained at 7.0. Moisture content of the crushed schist or thin shale is maintained at 30-40%. Small amount of crushed schist or thin shale is packed and treated for sterilization procedure, where the product is packed in plastic packages of low density polyethylene. The package is sterilized by gamma radiation of 50 kilogray.    USE - Method for obtaining solid carriers of microbial inoculants for biological fixation of nitrogen (claimed).    ADVANTAGE - The solid carriers of microbial inoculants obtaining method is suitable for agriculture, and enables to produce higher productivity with better cost-benefit and less environment impact.    DETAILED DESCRIPTION - Solid carriers of microbial inoculants obtaining involves grinding fine schist and shale derived from shale pyrolysis, and passing the product through sieve of 2mm, where pH of crushed schist or thin shale is maintained at 7.0. Moisture content of the crushed schist or thin shale is maintained at 30-40%. Small amount of crushed schist or thin shale is packed and treated for sterilization procedure, where the product is packed in plastic packages of low density polyethylene. The package is sterilized by gamma radiation of 50 kilogray. Inoculum is developed in liquid medium with nutrients and polymer under conditions that meet freatures of each type of inoculum. The inoculum is added to each pack containing crushed schist or thin shale. The inoculant is stored at 25-28 degrees C.
NOVELTY - Preparation of substituted 5-(bis-carboxymethyl-amino)-4-cyano-thiophene-2,3-dicarboxylic acid compounds (IV) comprises reacting substituted 5-amino-4-cyano-thiophene-2,3-dicarboxylic acid compounds (III) with chloroacetate compounds, in the presence of a base, and an iodide source as a reaction rate enhancer in a solvent.    USE - The process is useful for preparing substituted 5-(bis-carboxymethyl-amino)-4-cyano-thiophene-2,3-dicarboxylic acid compounds (IV) which are useful for preparing strontium ranelate or its hydrates (all claimed) that are useful for treating osteoporosis. No biological data given.    ADVANTAGE - The process: is economically viable, industrially feasible and environmentally benign process; provides increased purity and yield of the product with minimized contaminants and byproducts; and produces the strontium ranelate which increases deposition of new bone osteoblasts and reduces the resorption of bone by osteoclasts.    DETAILED DESCRIPTION - Preparation of substituted 5-(bis-carboxymethyl-amino)-4-cyano-thiophene-2,3-dicarboxylic acid compounds of formula (IV) comprises reacting substituted 5-amino-4-cyano-thiophene-2,3-dicarboxylic acid compounds of formula (III) with chloroacetate compounds of formula (ClCH2COOR1), in the presence of a base, and an iodide source as a reaction rate enhancer in a solvent.    R1, R2 = optionally branched or alicyclic 1-6C alkyl.    INDEPENDENT CLAIMS are also included for:    (1) substituted 5-(bis-carboxymethyl-amino)-4-cyano-thiophene-2,3-dicarboxylic acid compounds (IV) obtained by the process;    (2) strontium ranelate or its hydrates obtained by the process; and    (3) crystalline forms of strontium ranelate having characteristic peaks as given in the specification.
NOVELTY - Compound microbial inoculum comprises Rhodococcus erythropolis fermentation liquid, Acinetobacter fermentation liquid, Rhodopseudomonas palustris fermentation liquid, and Bacillus subtilis fermentation liquid, where the concentration of the fermentation liquid is above 109 colony forming unit (cfu)/ml.    USE - The compound microbial inoculum is useful for treating municipal sewage (claimed).    ADVANTAGE - The compound microbial inoculum achieves the synergistic degrading effect that each strain cannot achieve separately by the synergistic effect of each microbial strain of different proportions, and has guiding significance and reference value for the municipal sewage treatment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the above-mentioned inoculum involves obtaining the above-mentioned strains, activating the obtained strains in a solid culture medium at -80 degrees C, inoculating the activated bacterial colony in a liquid culture medium, and culturing until the concentration of bacteria reaches at least 109 cfu/ml, mixing the obtained bacterial culture with the above-mentioned four fermentation liquid to obtain liquid microbial inoculum.
NOVELTY - A microorganism belongs to Trichoderma into which beta -glucosidase gene (bgl1) derived from microorganism of genus Aspergillus connected under the control of a promoter for egl1 of the microorganism of Trichoderma, is new, where the expression of the bgl1 gene is introduced into the microorganism of Trichoderma.    USE - The microorganism is useful for producing sugar and ethanol from cellulose biomass (claimed).    ADVANTAGE - The method enables to perform saccharification process with small quantity of cellulose biomass, and produce ethanol cost-effectively.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) saccharogenic amylase of the cellulose biomass produced from the above-mentioned microorganisms;    (2) method for producing saccharogenic amylase involves culturing the above-mentioned microorganism;    (3) method for producing sugar from cellulose biomass involves performing saccharification of cellulose biomass in the presence of saccharogenic amylase; and    (4) method for producing ethanol involves performing fermentation of the obtained sugar.
NOVELTY - Producing a bio-coal comprises lowering (11) the moisture content of a fiber residue obtained after oil extraction of oil palm fruit to less than 25%, cutting (12) the fiber residue, pelletizing (13) the fiber residue into shortfiber pellets, drying (14) the short-fiber pellets to reduce the moisture content of the short-fiber pellets to below 10%, and carbonizing (15) the short-fiber pellets at a temperature of below 300 degrees C.    USE - The method is useful for producing a bio-coal (claimed).    ADVANTAGE - The method provides the bio-coal with high yield and calorific value. The bio-coal products are easy to preserve and transport.    DESCRIPTION OF DRAWING(S) - The figure shows a flow chart of a method for producing a bio-coal.    Lowering the moisture content of a fiber residue (11)    Cutting the fiber residue (12)    Pelletizing the fiber residue into shortfiber pellets (13)    Drying the short-fiber pellets (14)    Carbonizing the short-fiber pellets. (15)
NOVELTY - Forming a fuel blend, comprises providing a biomass solid, contacting the biomass solid with a solvent and direct aqueous phase reforming (APR) catalyst in the presence of hydrogen in a reactor to form oxygenated intermediates by providing an oxygenated intermediate stream, where a first portion of the oxygenated intermediates is recycled to form the solvent, and processing at least a second portion of the oxygenated intermediates to form the fuel blend.    USE - The method is useful for forming the fuel blend (claimed) that is useful as a fuel additive.    ADVANTAGE - The method: converts bio-based feedstocks including biomass or lignocellulosic feedstocks into liquid fuels with high yield of greater than or equal to 60% or greater than or equal to 70%; reduces the amount of unwanted byproducts; and improves carbohydrates extracted from the bio-based feedstock.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a direct aqueous phase reforming system of biomass comprising an APR reactor containing an APR catalyst comprising an inlet for receiving the biomass, solvent and hydrogen, and an outlet for discharging an oxygenated intermediate stream, and a separator comprising an inlet for the oxygenated intermediate stream, where a first portion of the oxygenated intermediate stream is recycled to the APR reactor as the solvent and a second portion of the oxygenated intermediate stream is provided to a fuel processor reactor, and a fuels processing reactor comprising an inlet for receiving the second portion of the oxygenated intermediate stream and an outlet for discharging a fuel blend.
NOVELTY - The gasification system (10) includes one or more conveyance tanks (18) which receive solid carbonaceous fuel powder. One or more solid pumps (20) are connected with the corresponding conveyance tanks and arranged at a downstream side. A gasifier (14) is fluid-connected with one or more solid pumps and arranged at the downstream side.    USE - Gasification system for solid carbonaceous fuel powder. Uses include but are not limited to coal, bitumen, soot, biomass, petroleum cokes, or their combinations.    ADVANTAGE - Allows use of one or more solid pumps to make the flow of solid powder more uniform and stable. Ensures low energy consumption by drying the solid powder conveyed in the gasifier through the solid pump. Allows the gasifier to be reliably and stably operated using one or more supply apparatuses, a buffer container, and a buffer hopper.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a solid carbonaceous fuel powder gasification method.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic block diagram of gasification system. (Drawing includes non-English language text).    Gasification system (10)    Conveyance unit (12)    Gasifier (14)    Conveyance tanks (18)    Solid pumps (20)
NOVELTY - Selectively producing hydrogen or ethane from methane involves: selecting a temperature suitable for a metal catalyst and a feed gas including methane to produce a product having a controlled hydrogen/ethane ratio, predominately hydrogen and a solid carbon product or predominately ethane and hydrogen; and contacting the feed gas with the metal catalyst at the selected temperature to produce the product.    USE - For selectively producing hydrogen or ethane (claimed).    ADVANTAGE - The present method increases selectivity and efficiency of methane conversion compared to competitive processes of oxidative coupling, thermal coupling, plasma coupling and non-oxidative catalytic coupling, which are not selective and often require a great deal of energy or temperatures in excess of 1000 degrees C. While thermal decomposition of methane results in production of solid carbon products and hydrogen and can reduce or eliminate greenhouse gas emission, this process typically can require temperatures greater than 1300 degrees C for complete conversion. Particularly the method allows decomposition of methane to hydrogen and solid carbon products in a selective manner thus significantly improves the commercial viability of methane conversion.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing hydrogen involving contacting a feed gas including methane with a ruthenium nanoparticle on a silica nanoparticle support at a temperature suitable to produce a product gas including hydrogen.
NOVELTY - Filter system for fluids, comprises a container (1) filled with vegetable charcoal as a filter layer, where a bottom (3) of the container comprises a drain (4), a device for supplying the liquid, a device for supplying fresh vegetable charcoal, and a device for extracting vegetable charcoal.    USE - The filter system is useful: in agriculture for cleaning livestock liquid manure, biogas slurry and domestic wastewater; and for cleaning wastewater from sewage treatment plants and industrial wastewater.    ADVANTAGE - The filter system: utilizes a filter layer made of vegetable charcoal, which absorbs gases containing climate-damaging pollutants, and thus it is environmentally friendly; and is constructed using high quality steel, and thus it is resistance to the highly corrosive liquid.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing fertilizers, comprising providing a filter layer made of vegetable charcoal in a filtration system; passing a liquid derived from biomass through vegetable charcoal; removing the coal vegetable charcoal from the filter layer; and using the vegetable charcoal as a fertilizer or as a raw material for fertilizer.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of filter system.    Container (1)    Bottom (3)    Drain (4)    Vibrating screen (6)    Feeding screw (8)
NOVELTY - Producing hydrogen and volatile fatty acids involves processing vinasse, molasses, bagasse and cane juice by using microorganisms such as Clostridium, Enterobacter, Escherichia, Klebisella, Bacillus and Alcaligenes in a culture medium at 20-60 degrees C for 3-6 days. The vinasse waste is obtained during processing sugar or during distillation of ethanol. A carbon source, nitrogen, carbon dioxide, argon, hexose, pentose and its polymers, sugarcane juice, molasses and hydrolyzed bagasse are added to the culture medium.    USE - Method for producing hydrogen and volatile fatty acids.    ADVANTAGE - The method enables the obtaining hydrogen and volatile fatty acids efficiently.    DETAILED DESCRIPTION - Producing hydrogen and volatile fatty acids involves processing vinasse, molasses, bagasse and cane juice by using microorganisms such as Clostridium, Enterobacter, Escherichia, Klebsiella, Bacillus and Alcaligenes in a culture medium at 20-60 degrees C for 3-6 days. The vinasse waste is obtained during processing sugar or during distillation of ethanol. A carbon source, nitrogen, carbon dioxide, argon, hexose, pentose and its polymers, sugarcane juice, molasses and hydrolyzed bagasse are added to the culture medium. Water supplemented with urea, nitrate salts, metals, is also added to the culture medium. A reducing agent such as sodium bicarbonate and cysteine- hydrochloric acid is also added to the culture medium.
NOVELTY - Method (M1) for manufacturing raw material, involves processing plant biomass containing lignocellulose using ammonia, transferring type-I crystal form of at least one portion of cellulose in lignocellulose to type-III crystal form, where the lignocellulose is processed by liquid ammonia or ammonia gas at 0-190 degrees C, and performing ester bond cleavage process for cleaving at least one portion of ester bond between lignin and hemicellulose in lignocellulose to obtain raw material.    USE - The method (M1) is useful for manufacturing raw material for manufacturing saccharide which is useful for producing ethanol (claimed).    ADVANTAGE - The method utilizes less amount of ammonia when compared to existing methods, does not utilizes sulfuric acid that is used in existing methods and thus is environmentally-friendly, enables recycling of ammonia, is cost-effective, and consumes less time to process lignocellulose.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for manufacturing saccharide, which involves saccharifying the raw material using an enzyme.
NOVELTY - Producing levulinic acid, comprises supplying a feed of a six-carbon carbohydrate-containing material and/or of furanic dehydration product from a six-carbon carbohydrate-containing material to a reactor in a controlled manner over time up to a desired feed level, and acid hydrolyzing the feed to produce a product including levulinic acid.    USE - The process is useful for producing levulinic acid (claimed), which is useful for producing succinic acid, 1,4-butanediol, 1,4-pentanediol, tetrahydrofuran, gamma -valerolactone, ethyl levulinate, 2-methyl-tetrahydrofuran, resins, polymers, herbicides, flavoring agents, solvents, plasticizers, antifreeze agents and biofuels/oxygenated fuel additives.    ADVANTAGE - The method is capable of energy-efficiently producing levulinic acid with high yield.
NOVELTY - Preparing methyl-1-benzyl-4-anilinopiperidine-4-carboxylate, comprises reacting 1-benzyl-4-piperidone and a nucleophile in tetrahydrofuran in presence of chloroform and sodium methoxide followed by warming and stirring for 10-45 hours.    USE - The process is useful for preparing methyl-1-benzyl-4-anilinopiperidine-4-carboxylate (claimed), which is useful as an intermediate for the synthesis of substituted fentanyl derivatives having different functional groups as 4-methoxycarbonyl and 4-methoxymethyl groups, where the fentanyl is useful for surgical analgesia and sedation.    ADVANTAGE - The single pot process allows simple and rapid preparation of methyl-1-benzyl-4-anilinopiperidine-4-carboxylate with high yield (55%) and purity (99%) and without toxicity in an eco-friendly manner thus rapidly synthesizing the fentanyl derivatives with high analgesic potency and good therapeutic index value.
NOVELTY - Preparing azilsartan medoxomil (I), comprises cyclising azilsartan amidoxime.    USE - (I) is useful for treating hypertension. No biological data given.    ADVANTAGE - The simple process provides (I) with high yield and high purity in an eco-friendly manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparing the azilsartan amidoxime, comprising (i) coupling substituted amidoxime acid of formula (II) or its salt with medoxomil chloride to obtain a substituted (5-methyl-2-oxo-1,3-dioxol-4-yl)methyl 2-ethoxy-3-((4-(2-(N'-hydroxycarbamimidoyl)phenyl)phenyl)methyl)benzimidazole-4-carboxylate compound of formula (III), and (ii) if appropriate, deprotecting (III); and    (2) preparing amidoxime acid or its salt, comprising hydrolyzing substituted amidoxime alkyl ester of formula (IV).    R = H or OH-protecting group; and    R1 = 1-5C-alkyl.
NOVELTY - This utility model claims a high temperature anaerobic digestion bio-reaction device, comprising a reactor for high temperature anaerobic digestion, high-efficient heat energy recycling device and a heating device. The reactor used for the high temperature environment in the sewage so as to generate marsh gas and biogas slurry, and biogas outlet, biogas outlet and the liquid inlet. High-efficiency Heat energy recovery device, which is used for the biogas slurry and sewage, to exchange heat with heat. Heating device, heat sewage passes through marsh gas. First generated biogas slurry and sewage carried out heat exchange heat through the reactor, and the reactor generated by methane combustion heat sewage, sewage to make the temperature of the high temperature reaction, does not need external energy consumption sewage heat of the reactor to continue operation.
NOVELTY - This utility model claims a high-efficient energy-saving device for degrading nitrosodimethylamine in waste water, an anaerobic digestion degrading nitrosodimethylamine in waste water bio-reaction unit generating biogas liquid and biogas, biogas slurry and waste water to exchange heat with heat, marsh gas is used for generating electricity to generate electric energy and heat energy, the heat is further heated, the temperature of the waste water meet the temperature and reacting, wherein the motor can be used for electro-catalysis oxidative degradation biogas system does not need other external energy consumption heating and providing electric energy for electro-catalysis oxidative degradation, can be generated by the sewage to a sewage treatment, sewage degradation is efficient and energy-saving, the system can continue operation, and the system is integrated, has high automation degree, can greatly save land resource.
NOVELTY - This utility model claims a mobile plasma dangerous waste treatment device, the technical problem to be solved is scattered; This utility model is the movable plasma dangerous waste processing device, the container is provided with a feeding system, a plasma reactor and gas purification system, a feeding system, a plasma reactor and gas purification system is set on the vehicle trailer, the flue gas purifying system is composed of the combustion chamber and quench tower, tower and a draught fan. This utility model compared with the existing technology, the mobile treating hazardous waste, processing efficiency is high, the cost is low, and it can effectively treat place scatter, toxicity, small lot size concentration liquid organic contaminants, gaseous contaminants, realise local processing, which avoids the dangerous waste transfer and improves the economical efficiency, safety, it is also applied to the dangerous waste environment accident, the need for emergency treatment.
NOVELTY - This utility model claims a kind of prison, watching the sewage by utilizing energy station, a waste outlet pipe is composed of a prison, kitchen sewage pipeline, inspecting well, mixing tank, mixing tank feeding port, marsh gas pool, a gas conveying pipe, a supplying station, gas supply pipe and gas is composed of the inspection well is set on the prison sewage pipeline and kitchen sewage pipeline is provided with the mixing pool is built in the sewage pipeline, the upper part of the marsh gas tank is set with gas conveying pipe, a gas conveying pipe is connected with a sand supplying station. This utility model make gas-forming substance content, fermenting more fully improves the gas production rate. The and yeast can be used as organic value higher planting fertilizer of marsh gas pool outlet out changing waste into valuable increases the economic benefit. Marsh gas recycling economy, air supply is stable, increasing expenditure as energy fuel is clean and sanitary, and saving energy and reducing emission, safety feasibility, good economic practicability, especially suitable for all kinds of our country prison, the guard.
NOVELTY - A kind of garbage sorting and recycling breeding tank for floating type organism and using system, comprising a feeding system, a sorting system, a drying packaging system, breeding tank for floating type organism system in turn, the garbage is sent to the sorting system classified by feeding system, a garbage sorting and classifying, a garbage is sent to the drying packaging system. The system mainly comprises a sorting and sieving all-in-one machine, a sieving all-in-one machine of a bracket (1), (3), protective cover (4), a feeding device (5), a transmission device (2), a deodorizing air separation device (7), using the solution of the garbage treating system, waste treatment process, sieving, winnowing is integrated, energy-saving and environment-friendly, small floor area, and the organic matter in the garbage can be recycled for yellow or as plant fertilizer.
NOVELTY - Preparing amlodipine besylate comprises: weighing 158 parts of amlodipine and benzenesulfonic acid; mixing 5 parts of amlodipine, 409 parts of benzenesulfonic acid and 28 parts of water; grinding the mixture at normal temperature for 5-6 hours; and drying the mixture at a temperature of 40-45 degrees C to obtain the amlodipine besylate, where the grinding step is carried out under the protection of nitrogen.    USE - The method is useful for preparing amlodipine besylate (claimed).    ADVANTAGE - The method easily provides the amlodipine besylate with good quality in an environment-friendly manner.
NOVELTY - Production of environment friendly bio-organic fertilizer comprises filtering fermentation substrate by screw bulking machine, conveying to wet mixer, cooling and adding microelement mineral salt, inoculating mixed bacterial liquid to fully mix, inoculating and mixing fermentation substrate into silica gel; mixing uniformly into fermentation substrate, and adding mixed solution containing anode Bacillus pumilus chain mold spores, Clostridium butyricum, pseudomonas bacteria, bacterial liquid of brown spherical solid nitrogen bacteria and Rhizopus oryzae.    USE - Method of production of environment friendly bio-organic fertilizer (claimed).    DETAILED DESCRIPTION - Production of environment friendly bio-organic fertilizer comprises filtering fermentation substrate by screw bulking machine, conveying to wet mixer, cooling and adding microelement mineral salt, reducing temperature to 30-35 degrees C, inoculating mixed bacterial liquid to fully mix, inoculating and mixing fermentation substrate into silica gel, packing by automatic metering packing system, and sealing; fermenting for 5-7 days in constant-temperature fermentation chamber, adding 50-60 pts. wt. distiller, 5-10 pts. wt. humic acid, 5-15 pts. wt. sunflower shell powder, 5-10 pts. wt. ammonium sulfate, 5-10 pts. wt. potassium chloride, and 5-10 pts. wt. corn, mixing uniformly into fermentation substrate, controlling fermentation substrate water content of 30-40 wt.%, and adding mixed solution containing anode Bacillus pumilus chain mold spores, Clostridium butyricum, pseudomonas bacteria, bacterial liquid of brown spherical solid nitrogen bacteria and Rhizopus oryzae.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the production of environment friendly bio-organic fertilizer.
NOVELTY - This utility model is one kind of soft marsh gas pool. Soft marsh gas pool is a cuboid, the middle position thereof is provided with parallel to the baffle wall of the long side, the two sides of the baffling wall of one end of the cylinder are respectively provided with a feeding pipe and a rectangular multifunctional discharging pipe, the other end of the baffle wall and the end surface keep a certain distance above the baffle wall is welded with a return port, an air nozzle is set on the multifunctional discharging pipe is welded with an overflow port, the slag pumping pipe and return pipe is multi-functional discharging a proper height. This utility new soft methane tank can realize industrial production, the integrity of the construction, installation and use, convenient management and maintenance and so on becomes simple, sustainablly, increases the construction safety of the pool at the same time improves the key pool success rate and continuous use.
NOVELTY - Producing ginsenoside Rg3 from ginseng total saponin involves taking ginseng total saponin, ethanol (69-70 vol.%), and aqueous acetic acid (69-8 vol.%); preparing total saponin of panax ginseng at 80-85 degrees C; hydrolyzing for 90-100 minutes; and recycling using hydrolysis solution, to produce ginsenoside Rg3.    USE - For producing ginsenoside Rg3 from ginseng total saponin (claimed).    ADVANTAGE - The process provides large scale ginsenoside Rg3; is simple process; and has low cost and high yield.
NOVELTY - The utility model claims a high speed ferment natural organic garbage processing system, the system is composed of six parts, a lifting device, a sorting, crushing and dehydrating device, a fermentation device, a purifying tower, a pelleting device. The six parts are connected in turn is composed of a high speed ferment natural organic garbage processing system. The system effect, energy-saving high, and the operation is convenient.
NOVELTY - This utility model claims a kind of new biomass gasification furnace, comprising a hearth, a fire grate, an operating handle and a shaft, an operating handle are connected by a shaft and the grate on the grate is the grate in the hearth in the lower end, a fire grate also comprises connected with fire grate, a cooling air inlet and a hot air furnace at one side of air outlet pipe, the fire grate is a hollow structure, and is provided with inner part is hollow, the periphery of the honeycomb is through ash hole on the surface. Through said method, the utility model can solve the problem that the water-cooling fire grate caused by waste of water resource, and improves the operation cost and inconvenient dust cleaning of the whole device and so on, it has fire grate extend service life, dust cleaning;
NOVELTY - This utility model claims a kind of recycling system, the recycling system comprises a first portion and a second portion, the first portion is connected with the second part, the first part is marsh gas tank for generating marsh gas and biogas residue and biogas slurry, and a second part comprising a heating zone, separation zone and a breeding area, the heating area is connected with the marsh gas tank, marsh gas to recycle the use, the biogas separating area is connected with the marsh gas tank so as to separate the biogas residue and biogas slurry, the breeding area is connected with the biogas residue biogas liquid separating section for receiving the separated biogas slurry, the breeding area is connected with the marsh gas tank, providing raw material to the marsh gas pool.
NOVELTY - A smart root nematodes drip prevention device comprises ozone generating device, refrigerator (2), heat exchanger (3), liquid collecting pipe (4), and liquid storage pipe. The heat exchanger has circulating water inlet and outlet connected with inlet and outlet of first heat exchanger. The ozone generating device comprises filter (7), air pump (8), ozone generator (9) and ozone generating controller (10).    USE - A smart root nematodes drip prevention device.    ADVANTAGE - The device does not create pollution.    DETAILED DESCRIPTION - Smart root nematodes drip prevention device comprises ozone generating device, refrigerator (2), heat exchanger (3), liquid collecting pipe (4), and liquid storage pipe. The heat exchanger has circulating water inlet and outlet connected with inlet and outlet of first heat exchanger. The ozone generating device comprises filter (7), air pump (8), ozone generator (9) and ozone generating controller (10). An outlet of the filter, through the air pump, is connected with the ozone generator. The air outlet of the ozone generator is connected with the heat exchanger through first electromagnetic valve (11). The ozone generating controller is electrically connected to the other of the first cooling inlet of the heat exchanger through second electromagnetic valve. A liquid collecting tank has liquid inlet electromagnetic valve. The liquid storage tank contains plant extracting solution.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of the smart root nematodes drip prevention device.    Refrigerator (2)    Heat exchanger (3)    Liquid collecting pipe (4)    Filter (7)    Air pump (8)    Ozone generator (9)    Ozone generating controller (10)    First electromagnetic valve (11)
NOVELTY - Preparing chicken feed comprises weighing motherwort, glossy privet fruit, honeysuckle, dandelion, barbary wolfberry fruit, radix cirsii japonici, Serissa serissoides, Angelica and dry ginger, adding 4-5 times of water in the medicine mixture and then boiling at low temperature for 1-2 hours, cooling the boiled mixture, filtering using a eight-layer gauze and adding 2-3 times of water in the filtrate, heat preservation for 1-2 hours, adding white sugar in the filtrate, and fermenting the filtrate using yeast to obtain a fermented solution.    USE - The method is useful for preparing chicken feed (claimed) that is useful for improving immunity function, preventing disease and nourishing blood of the chicken.    ADVANTAGE - The method is capable of preparing chicken feed with high healthcare function and without toxicity in an environment-friendly manner. The feed improves the egg production of the chicken.    DETAILED DESCRIPTION - Preparing chicken feed comprises weighing motherwort (30-40 pts. wt.), glossy privet fruit (10-15 pts. wt.), honeysuckle (15-20 pts. wt.), dandelion (10-15 pts. wt.), barbary wolfberry fruit (5-8 pts. wt.), radix cirsii japonici (10-15 pts. wt.), Serissa serissoides (3-5 pts. wt.), Angelica (3-5 pts. wt.) and dry ginger (2-3 pts. wt.), adding 4-5 times of water in the medicine mixture and then boiling at low temperature for 1-2 hours, cooling the boiled mixture, filtering using a eight-layer gauze filter and adding 2-3 times of water in the filtrate, heat preservation the mixture for 1-2 hours, adding white sugar in the mixture, and fermenting the mixture using yeast.
NOVELTY - High-silicon iron ore tailings are used for producing soil fertilizer by preparing high-silicon iron ore tailings, magnetizing the high-silicon iron ore tailings at 800-2000 gauss, adding 55-65 pts. wt. high-silicon iron ore tailings with 6-10 pts. wt. heavy metal ion removing agent, 10-15 pts. wt. peat soil, 8-12 pts. wt. humic acid, 7-11 pts. wt. plant growth regulator, and 0.5-2 pts. wt. plant adhesive, mixing and stirring, crushing, adding water for humidifying, extrusion forming, granulating, double layer sieving, drying and hardening, grinding, and particle vibration screening.    USE - High-silicon iron ore tailings are used for producing soil fertilizer (claimed) useful for improving physical and chemical properties of soil, providing nutrients needed by the plant, and restoring heavy metal-polluted land.    ADVANTAGE - The soil fertilizer provides abundant nutrients for various crops. The use of high-silicon iron ore tailings reduces environmental pollution.
NOVELTY - Tea organic fertilizer comprises 15-30 wt.% tea stem residue, 5-10 wt.% oil cake, and 65-80 wt.% sheep manure.    USE - Tea organic fertilizer.    ADVANTAGE - The tea organic fertilizer provides disease resistance, no pollution, and abundant nutrients, has simple preparation, comprehensively uses the waste resource, does not require a lot of space upon preparation, and is convenient to use.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of tea organic fertilizer comprising collecting tea stem residue of the 11th month of each year, crushing until 70-80 mass% of the total mass has a granularity of 3-5 mm, drying the crushed material to a water content of 10-20%, putting the material in a bag, naturally fermenting, composting by covering the surface with a cover film, keeping the fermentation mixture temperature at 60-70 degrees C, and fermenting for 2-3 months until the material becomes white in color and has no peculiar smell.
NOVELTY - Treating high-concentration organic waste water by Bacillus comprises: adding Bacillus into an anoxic reactor and an aerobic reactor, where the Bacillus is Bacillus subtilis, Bacillus cereus, Bacillus licheniformis, Bacillus megaterium and Bacillus natto; injecting high-concentration organic waste water into the anoxic reactor and the aerobic reactor; and adding an activator, an accelerator and curing agent during an aerobic reaction.    USE - The method is useful for treating high-concentration organic waste water by Bacillus (claimed).    ADVANTAGE - The water can be treated with strong organic load-resistant capability, high salt resistance, high ammonia nitrogen resistance, acid resistance, alkali resistance and high/low temperature resistance. The high-concentration organic waste water treatment is efficiently performed using bacillus, Bacillus activator, curing agent and promoter, and through control of growth conditions and growth parameters of the bacillus.
NOVELTY - Method for processing chemical sludge involves (a) performing anaerobic fermentation on waste sludge, and collecting generated methane gas, (b) adding flocculating agent to the fermented sludge, performing air-flotation treatment, and depositing the sludge, (c) discharging the sludge into a plate-frame filter for dehydration to obtain sludge filter cakes, and (d) adding a silicate into the filter cakes, and performing high-temperature sintering process.    USE - The method is useful for processing chemical sludge (claimed).
NOVELTY - Additive composition comprises effective microorganism bacteria raw liquid (2 wt.%), urea (0.75-2.1 wt.%), and ferrous sulfate (1-5 wt.%).    USE - The additive composition is useful for promoting growth of crop straw and treating peanut straw or rice straw (claimed).    ADVANTAGE - The additive composition has high working efficiency and improved utilization rate.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) method of utilizing additive composition comprising adding effective microorganism bacteria raw liquid, and ferrous sulfate into the mixture, uniformly mixing and adding urea to adjust carbon/nitrogen in the ratio of 20-30, adding distilled water to adjust water content of the mixed system to 60-70 wt.%, performing ventilation culture at 25-30 degrees C for 50-60 days and every two days; and    (2) Use of additive composition for treating peanut straw or rice straw.
NOVELTY - Producing biomass fertilizer by straw comprises laying wheat rice on a bottom of an enclosed container and wetting the wheat rice having a height of 1/10-1/5 by spraying biogas liquid to form a layer of biogas residue on the wheat rice, laying the crop straw on the biogas residue and inserting a hollow pipe into the straw, introducing air into the enclosed container for 30-120 minutes through the hollow pipe, drying the material in sun light for 35-50 days to obtain straw decomposition and preparing the biomass fertilizer by mixing the composition with fertilizer and then stirring.    USE - The method is useful for producing biomass fertilizer (claimed).    ADVANTAGE - The method allows economical production of the biomass fertilizer with increased soil organic matters, beneficial micro-organism and improved soil ecological structure.    DETAILED DESCRIPTION - Producing biomass fertilizer by straw comprises laying wheat rice on a bottom of an enclosed container and wetting the wheat rice having a height of 1/10-1/5 by spraying biogas liquid to form a layer of biogas residue on the wheat rice, laying the crop straw on the biogas residue and inserting a hollow pipe into the straw, introducing air into the enclosed container for 30-120 minutes through the hollow pipe, drying the material in sun light for 35-50 days to obtain straw decomposition and preparing the biomass fertilizer by mixing the composition with fertilizer and then stirring, where the fertilizer comprises nitrogenous (15-20 wt.%), phosphate (15-25 wt.%), potassium (10-15 wt.%), and straw decomposition (balance amount).
NOVELTY - An excess sludge is used for preparing organic-inorganic fertilizer by subjecting residual mud to anaerobic fermentation to obtain hydrolysis acidification liquid, adjusting pH value, adding dolomite while controlling pH value, stirring, centrifuging, filtering, adjusting pH value of filtrate, stirring, centrifuging, filtering, adding magnesium sulfate to the filtrate, adjusting pH value, stirring, centrifuging, filtering, and drying the filter cake.    USE - Method of using an excess sludge (claimed) for preparing organic-inorganic fertilizer.    ADVANTAGE - The method is short, does not require inorganic nutrient, and obtains cheap and environment-friendly fertilizer that meets GB 18877-2009.    DETAILED DESCRIPTION - An excess sludge is used for preparing organic-inorganic fertilizer by subjecting residual mud to anaerobic fermentation to obtain hydrolysis acidification liquid, adjusting pH value to 4-4.5, adding dolomite while controlling pH value at 4-4.5, stirring for 6 hours, centrifuging, filtering to obtain filtrate having 800 mg/l calcium ion and 400 mg/l magnesium ion, adjusting pH value of the filtrate to 8-10, stirring for 5-60 minutes, centrifuging, filtering, adding magnesium sulfate to the filtrate at a ratio of 0.3-1.6:1, adjusting pH value to 8.5-10, stirring for 5-30 minutes, centrifuging, filtering, and drying the filter cake.
NOVELTY - Producing microbial fertilizer composition using a combination of liquid coating and solid coating mode, comprises dissolving microbial powder composition in coating oil, metering the coating oil containing microbial inoculum via a coating machine located on a continuous production line and coating the coating oil, and adding pure organic coating powder material to obtain fertilizer composition, or organic-inorganic fertilizer composition from the drum on production line, where sufficient amount of microbial inoculum can be added to produce fertilizer composition with high quality.    USE - The method is useful for producing microbial fertilizer composition using a combination of liquid coating and solid coating mode (claimed).    DETAILED DESCRIPTION - Producing microbial fertilizer composition using a combination of liquid coating and solid coating mode, comprises dissolving microbial powder composition in coating oil, metering the coating oil containing microbial inoculum via a coating machine located on a continuous production line and coating the coating oil, and adding pure organic coating powder material to obtain fertilizer composition, or organic-inorganic fertilizer composition finished product from the drum on the production line to achieve coating and prevention of agglomeration in the coating machine, where sufficient amount of the microbial inoculum can be added to produce microbial fertilizer composition with high quality.
NOVELTY - Water-retaining and soil-fertilizing synergist comprises 5-10 wt.% sodium polyacrylate, 5-10 wt.% polyacrylamide, 3-8 wt.% catalyst, 1-3 wt.% microbial strain and 70-80 wt.% rotten domestic waste.    USE - The water-retaining and soil-fertilizing synergist is useful for improving soil in deserts, saline lands or stony deserts, and used as organic fertilizer in dry and water-deficient area.
NOVELTY - An aryl-substituted indole derivative (I) is new.    USE - New aryl-substituted indole derivative used for the preparation of antitumor drugs (claimed).    ADVANTAGE - The method has good reaction selectivity, mild reaction condition, simple preparation technique, low production cost and environment-friendly synthesis route.    DETAILED DESCRIPTION - An aryl-substituted indole derivative (I) is new.    R1=1-naphthyl, 2-naphthyl, phenyl or phenyl substituted 1-4C alkyl, 1-4C alkoxy, halo, trifluoromethoxy, formyl or trifluoromethyl;    R2,R3=H or Me; and    R4=CN.    An INDEPENDENT CLAIM is included for the preparation of aryl-substituted indole derivative.
NOVELTY - Extraction of hyperoside enzyme comprises taking senticosus meal, adding water, cellulase and pectinase, adjusting pH value, heating, carrying out enzymolysis and heating to obtain activated hydrolyzate compound; adding ethanol, dipping, percolating, collecting diacolation liquid, diluting with water, filtering, adding macroporous absorption resin, washing, eluting with ethanol, collecting eluent, recycling ethanol, decompressing and drying; carrying out reversed phase resin column chromatography, eluting with ethanol, collecting eluent, recycling ethanol and crystallizing.    USE - Method of extracting hyperoside enzyme (claimed).    ADVANTAGE - The method is environment-friendly with convenient operation and reduced production cost.    DETAILED DESCRIPTION - Extraction of hyperoside enzyme comprises taking senticosus meal, adding 2-3 times volume water, adding cellulase and pectinase at mass ratio of 2-3:1, adjusting pH value to 4.0-5.0, heating to 40-60 degrees C, carrying out enzymolysis for 1.5-2 hours and heating to 70-80 degrees C to obtain activated hydrolyzate compound; adding 90-95% ethanol, dipping, percolating, collecting diacolation liquid, recycling ethanol, diluting with 2-3 times volume water, filtering, adding macroporous absorption resin, washing, eluting with 70-75% ethanol, collecting eluent, recycling ethanol, decompressing and drying; carrying out reversed phase resin column chromatography, eluting with 20-30% ethanol, collecting eluent, recycling ethanol and crystallizing.
NOVELTY - Preparing agricultural water-retaining agent, comprises e.g. removing dust from crop straws, crushing the crops to obtain straw powder, adding 30% acrylic acid and potassium hydroxide solution, stirring the mixture to obtain acrylate solution, mixing flour and straw powder with a ratio of 1:0.5-1, adding the mixture with water, heating the mixture, and reducing the temperature, adding acrylate solution in the mixture, adding 5-8% of initiator in the mixture, stirring the mixture, and adding water and 8-14% of crosslinking agent in the stirred mixture.    USE - The agricultural water-retaining agent is useful for cultivating edible fungi.    ADVANTAGE - The method provides agricultural water-retaining agent with high water absorptivity, gel strength and biodegradability in a cost-effective and environment-friendly manner.    DETAILED DESCRIPTION - Preparing agricultural water-retaining agent, comprises: (a) removing dust from crop straws, crushing and passing the crops through 40 meshes sieve to obtain straw powder; (b) adding 30% acrylic acid and potassium hydroxide solution, stirring the mixture for 30 minutes to obtain acrylate solution with a concentration of 65-75%; (c) mixing flour and straw powder with a ratio of 1:0.5-1, adding the mixture with water, heating the mixture to 80-95 degrees C for 30-60 minutes, and reducing the temperature to 60-70 degrees C, adding 65-75% concentration of acrylate solution in the mixture, where the mass ratio of mixed powder to acrylate solution is 1:0.6-1, adding 5-8% of initiator in the mixture, stirring the mixture for 5-10 minutes, adding water and 8-14% of crosslinking agent in the stirred mixture, performing propylene polymerization on the mixture for 15-30 minutes to form a mesh structured mixture, soaking the mixture with 0.9% of salt water for 30 minutes to obtain slurry; and (d) washing and drying the slurry using ethanol, cutting, drying, and crushing the dried mixture.
NOVELTY - The method involves filling oil gas in a membrane filtering device (100). The membrane filtering device is connected with a film filter element (110). The film filter element is connected with a porous material framework that is arranged with a reforming catalyst unit. The reforming catalyst unit is connected with a base body. Average pore diameter of the base body is about 20 microns. The framework is made of nickel-aluminum intermetallic compound porous material. The reforming catalyst unit is made platinum, rhodium, iridium and palladium metal material.    USE - Catalytic reforming method.    ADVANTAGE - The method enables utilizing the filter element to filter dust in air to perform hydrocarbon molecule catalytic reforming process in oil, avoiding reforming catalyst coking phenomenon to a certain extent and reducing reforming catalyst loss.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a catalytic reforming reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a catalytic reforming reactor.    Membrane filtering device (100)    Film filter element (110)
NOVELTY - A methanol-diesel oil solubilizer comprises a hydrazine compound, a guanidine compound and an azole compound in weight ratio 1:(1.1-1.7):(4-5.5).    USE - Methanol diesel-oil solubilizer used for improving intermiscibility of diesel oil and methanol.    ADVANTAGE - The methanol and diesel oil are uniformly mixed and generation of layering is prevented, when using the methanol-diesel oil solubilizer.
NOVELTY - Biomass briquette comprises 35-42 wt.% of agriculture and forestry wood fiber carbonized powder, 30-35 wt.% of coal powder, 3-5 wt.% of bonding agent, 1-1.5% of desulfurizing agent, and water (balance).    USE - The biomass briquette is useful for a lime shaft kiln (claimed).    ADVANTAGE - The biomass briquette can be economically prepared with high quality in an environmentally friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the biomass briquette, comprising mixing agriculture and forestry wood fiber carbonized powder, coal powder, bonding agent, desulfurizing agent and water at normal temperature to prepare the biomass briquette.
NOVELTY - Preparing refuse derived fuel from household waste and organic waste, comprises drying the straw type material, crushing, mixing excrement with the crushed straw type material, drying, dehydrating the sludge, carrying out anaerobic digestion, disinfecting, and changing the hydrophobic materials to prepare particles, carrying out primary sorting, primary fermentation, secondary sorting and secondary fermentation on the household waste to prepare a bio-organic fertilizer, mixing e.g. the straw type material and the excrement, and bio-organic fertilizer, and adding e.g. a chlorine fixing agent.    USE - The method is useful for preparing refuse derived fuel from household waste and organic (claimed).    ADVANTAGE - The method solves the problems of secondary pollution caused by the excrement, the straws, the sludge and the household waste, land resources occupied in large amounts are and secondary pollution generated by direct combustion; saves energy, and reduces fuel cost.    DETAILED DESCRIPTION - Preparing refuse derived fuel from household waste and organic waste, comprising (a) drying the straw type material, and crushing; (b) mixing excrement with the crushed straw type material, and then drying; (c) dehydrating the sludge, carrying out anaerobic digestion, disinfecting, and changing the hydrophobic materials to prepare particles; (d) carrying out primary sorting, primary fermentation, secondary sorting and secondary fermentation on the household waste to prepare a bio-organic fertilizer; and (e) uniformly mixing the straw type material and the excrement, the sludge particles, and the bio-organic fertilizer in a mass ratio of (2-4): (7-9): (7-9), and adding a chlorine fixing agent, a sulfur fixing agent and a thickener to prepare the refuse derived fuel.
NOVELTY - Coconut stem essential oil extract, prepared by crushing coconut stem, extracting by traditional extraction method with a solvent to obtain an extract, then concentrating until the solvent separates out and obtaining Coconut stem essential oil extract, is claimed.    USE - The essential oil extract is useful for preparing Oryctes rhinoceros (Linnaeus) attractant (claimed).    ADVANTAGE - The essential oil extract is economical and environmentally friendly, and has simple preparation process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for the use of coconut stem essential oil extract for preparing Oryctes rhinoceros (Linnaeus) attractant.
NOVELTY - Preparing betamethasone dipropionate atomizing inhalation agent comprises dispersing betamethasone dipropionate in water to obtain suspension, homogenizing under pressure of 200-2000 bar and sterilizing.    USE - The method is useful for preparing betamethasone dipropionate atomizing inhalation agent (claimed).    ADVANTAGE - The method: is environmentally friendly; simplifies the operation steps; ensures continuous operation; has short operation time; ensures sterile and clean production; and is suitable for industrial production. The inhalation agent: has good dispersion stability, high pulmonary deposition rate, high bioavailability and low toxicity and side effects; and requires small dosage.
NOVELTY - Improved acid catalyzed one pot synthesis of a 2-styryl quinoline compound (IV) from a (2-aminophenyl)(aryl/alkyl)methanone compound (I), an alkylacetoacetate compound (II) and an aldehyde compound (III), is claimed.    USE - (IV) is useful in AIDS therapy. No biological data given.    ADVANTAGE - The improved one pot process provides (IV) in high yield.    DETAILED DESCRIPTION - Improved acid catalyzed one pot synthesis of a 2-styryl quinoline compound of formula (IV) from a (2-aminophenyl)(aryl/alkyl)methanone compound of formula (I), an alkylacetoacetate compound of formula (CH3-C(=O)-CH2-C(=O)-O-R1) (II) and an aldehyde compound of formula (R2-C(=O)-H) (III), is claimed.    R, R2 = alkyl, arylalkyl or (hetero)aryl (optionally substituted by electron donating or withdrawing groups);    R1 = 1-6C-alkyl, pyrrolidine, morpholine or thiomorpholine; and    X = aryl ring substituted with H, halide, nitro, CN, halogenated alkyl, alkyl or alkyloxy.
NOVELTY - Decomposition fermentation type environmental protection dustbin comprises barrel body of cylindrical container, barrel cover provided at an upper part of barrel body, garbage fermentation chamber having one side provided with yeast plate, which is provided with water absorbing cloth, and cloth baffle plate tightly connected with fungus liquid circulation chamber. The barrel body is sequentially provided with smell isolating rubber plate, arc-shaped storage bowl, fermentation bacteria liquid adding device, garbage storage chamber, and buffer, yeast, and bacterial liquid circulating chamber.    USE - Decomposition fermentation type environmental protection dustbin.    ADVANTAGE - The decomposition fermentation type environmental protection dustbin has simple structure, is convenient to use, avoids the emission of peculiar smell, and provides high yield of fertilizer for indoor and outdoor use.    DETAILED DESCRIPTION - Decomposition fermentation type environmental protection dustbin comprises barrel body of cylindrical container, barrel cover provided at an upper part of barrel body, garbage fermentation chamber having one side provided with yeast plate, which is provided with water absorbing cloth, and cloth baffle plate tightly connected with four sides of fungus liquid circulation chamber. The barrel body is sequentially provided from top to bottom with smell isolating rubber plate, arc-shaped storage bowl, fermentation bacteria liquid adding device, garbage storage chamber, and buffer, yeast, and bacterial liquid circulating chamber. One side of the barrel body comprises drainage pipe and liquid droplet circulating ring pipe provided on an edge of arc-shaped storage bowl. The drainage pipe is for filling with fermentation liquid. It is fixedly provided on the barrel body. A circulating pipe is provided on sterile solution circulation chamber.
NOVELTY - Biogas slurry stirring and breaking of the circulating biogas pipeline to an anaerobic reactor, an auxiliary device of anaerobic reactor belongs to methane fermentation. The utility model is provided with biogas slurry circulating pipe at the outside of the anaerobic reactor, a circulating pipe in series is set with biogas slurry circulating pump, circulating the biogas slurry is pumped into the anaerobic reactor. Further provided with a liquid distributor on the top of the anaerobic reactor to impact rupture of the biogas liquid and biogas slurry stirring. The utility model is more easy to make the reactor is kept, and the structure is simplified, it is convenient to maintain and the cost is reduced.
NOVELTY - Enhancing biogas generation capability in anaerobic fermentation of rice hull and duck manure comprises (1) composting the raw material containing rice hull and duck manure and then adjusting the moisture content to 60%, turning the raw material once for every five days, controlling carbon and nitrogen in the raw material, (2) mixing sodium hydroxide with the raw material, (3) adjusting the pH value of the obtained mixture solution and then neutralizing, and (4) mixing regulation fluid in an inoculum, and then fermenting and stirring.    USE - The method is useful for enhancing biogas generation capability in anaerobic fermentation of rice hull and duck manure (claimed).    ADVANTAGE - The method can efficiently and rapidly treat the rice hull and performs solid-liquid separation in manure fermentation in a highly stable manner thus improving anaerobic biogas generation.    DETAILED DESCRIPTION - Enhancing biogas generation capability in anaerobic fermentation of rice hull and duck manure comprises (1) composting the raw material containing rice hull and duck manure for 20 days and then adjusting the moisture content to 60%, turning the raw material once for every five days, controlling carbon and nitrogen in the raw material in the ratio of 20:1-30:1, (2) introducing the obtained raw material into a stirring tank, mixing sodium hydroxide (15 kg) with the raw material and then standing for 48 hours, (3) adjusting the pH value of the obtained mixture solution to 7-7.2 and then neutralizing by adding hydrochloric acid, and (4) introducing the mixture solution into an anaerobic fermentation tank and then mixing regulation fluid (10%) in an inoculum, adjusting triplicate value of the solid to liquid content matter to 8-10%, and then fermenting at temperature of 35 degrees C for 12 hours and then stirring at speed of 120 revolutions per minute (rpm) for 10 minutes.
NOVELTY - This utility model claims a kind of decomposing steam and make it burn, comprising a water tank body, wherein one end of the box body with the water pipe, and the other end is connected with the steam pipe is provided with a water quantity adjusting valve, a water tank box body is set on the combustion zone of the furnace in a steam pipe is set on the water inlet pipe. This utility model with low cost is water as raw material, carrying out high temperature heat of a high temperature furnace of the steam is decomposed into hydrogen and oxygen and burning, the cost is low, the structure is simple, energy-saving, high combustion efficiency, wide application, and has no pollution, it is environment-friendly, has wide popularizing and applying value.
NOVELTY - This utility model is a kind of movable forced oxygen supply composting device, comprising a box body, an oxygen supply device and a box cover on the box body, the box body is provided with at least one mounting hole, an oxygen supply device comprises oxygen feeding pump, and is consistent with the mounting holes of the grinding ball, ball is set on the mounting hole, the ball sand ball nozzle passes through the mounting hole, the ball sand ball through oxygen pipe and the oxygen feeding pump. This utility model solves the problem that the existing of the compost device, large energy consumption, bad effect, low efficiency, the box body is connected with the oxygen feeding pump through the sand ball and oxygen-adding pipe is set at the bottom of the box, providing oxygen to the excrement and organic powder piled in the box body, a compost, oxygen is uniformly distributed, good effect and high efficiency.
NOVELTY - This utility model claims a pushing type using metallurgy rotary hearth furnace flue gas pyrolysis form preparing fermentable reducing sugar from biomass carbon device, comprising a pusher, an outlet gas duct, a condenser, a gas-liquid separator, a furnace body, a flue inlet, a cooling device, a pre-heating section in the furnace chamber in the furnace body, heating I section, heating II section, soaking section, a pre-heating section, a lower part heating I section and II section is provided with a combustion chamber, the combustion chamber is provided with an air inlet and a fuel gas inlet, the utility model is continuous carbon, it is possible to ensure the carbonization quality, and the metallurgy high temperature flue gas as heat source, the carbon can be used for smelting metal by regulating the pushing speed smoke gas flow and so on, it has the prospect of the smelting enterprise.
NOVELTY - This utility model claims a kind of crop straw continuous carbonizing furnace, comprising a furnace wall, a furnace cover, a furnace bottom, a furnace cover is provided with a feeding port and a shaft hole, the feeding port is provided with a plug hole matched with a hollow shaft, the hollow shaft on the upper end of the circumferential direction is provided with a first air inlet, the lower end of the hollow shaft on the circumference surface is provided with a second gas inlet, the first gas inlet is matched with air inlet pipe, the air inlet pipe is provided with a gas flow rate control valve, the furnace wall comprises an insulating layer, a furnace liner and furnace outer liner, an insulating layer on the furnace liner and furnace outer liner, the diameter of top of the furnace liner and the furnace liner are gradually increased, the thickness of insulating layer is gradually increased; the furnace cover port and the air inlet port is closed, the bottom furnace cover, a furnace wall and a furnace to form a sealed cavity. The utility model creates a safe and reliable, the cost is low, the service life is long, the carbon discharging period is short, the carbon discharging is stable, the production efficiency is high, and it can realize automatic and continuous feeding and the carbon is worthy of application and popularization.
NOVELTY - A container type flow stirring device, comprising a main shaft, the main shaft is located on the pool wall of the pool wall is equipped with biogas slurry, wherein the main shaft of the lower end is fixed with the lower stirring impeller, the main shaft is fixedly connected with the upper end provided with a stirring impeller, the tank outside of the side wall is provided with a circulating water pump, the circulating water pump of the water pumping pipe is connected with the outlet of the circulating water pump is connected with the water outlet pipe, the water outlet and the water pumping opening of the pumping pipe are located on the pool wall, and the upper stirring impeller and a pumping opening are located in the biogas slurry, the water outlet and the lower stirring impeller, and circular intersection of the horizontal line and the lower stirring impeller of the water outlet. Using the circulating water of the circulating water pump to realize automatic stirring impeller, the cost is low, the stirring effect is good, which can effectively prevent marsh gas pool floating block, the shell and precipitate.
NOVELTY - This utility model claims a kind of low electric resistance water saving device, wherein comprising an electrolytic cell, wherein it further comprises a power supply, a control system, a high temperature alkali liquid circulating system, a steam cooling system, a gas-liquid separating system, washing system fire retardant, wherein the electrolytic cell is a reactance electrolytic tank, wherein the control system is respectively connected with the power supply, an electrolytic bath, high temperature alkali liquid circulating system, a steam cooling system, a gas-liquid separating system, washing system is connected with the fire retardant, and the power supply is connected with the electrolytic bath, and the electrolysis groove through gas-liquid separating system, a high temperature alkali liquid circulating system to form a circulating loop, and the gas-liquid separating system by steam cooling system, washing system fire retardant with high temperature alkali liquid circulating system. This utility model can reduce the consumption of the hydrogen-oxygen process, so as to save the electrolysis manufacturing hydrogen by reducing the cost of the power consumption, at the same time, this utility model also can recycle energy and environment-friendly.
NOVELTY - The utility model claims a lithium bromide absorption-type heat pump is propylene propane fractionation system by using lithium bromide absorption type heat pump machine set to generate heat to propylene and propane, the utility model is equipped with lithium bromide absorption heat pump of propylene propane fractionation system. This utility model using oil refining enterprise production process by a plurality of secondary heat exchange to a temperature hot water as driving heat source, the lithium bromide absorption-type heat pump use the solution with gas fractionation device, not only can fully use the waste heat resource, but also optimizes the structure of the energy, oil refining enterprise has many times of heat exchange medium-temperature hot water is completely discharged not only wastes large amount of energy, but also increase the cost of the enterprise. Is the part of a hot water recycling, the lithium bromide absorption type heat pump as the heat source is very suitable to save the energy, which is good for energy-saving and environment-friendly.
NOVELTY - An ion exchange membrane is a single membrane obtained by melting and blending perfluorosulfonic acid ion exchange resin and sacrificial short fiber, carrying out extrusion, coating hydrophilic zirconia on both sides of obtained single membrane, performing functional transformation process of obtained single membrane, and treating using supercritical fluid to obtain three-phase separated continuous crosslinking integral structure. The staggered channels are formed in the membrane after the dissolution of sacrificial short fiber.    USE - Ion exchange membrane (claimed).    ADVANTAGE - Ion exchange membrane has low sheet resistance, high current efficiency and excellent mechanical strength, and efficiently separates chlorine gas having high purity when operating under super-high current density.    DETAILED DESCRIPTION - An ion exchange membrane is a single membrane obtained by melting and blending perfluorosulfonic acid ion exchange resin and sacrificial short fiber, carrying out extrusion, coating hydrophilic zirconia on both sides of obtained single membrane, performing functional transformation process of obtained single membrane, and treating using supercritical fluid to obtain three-phase separated continuous crosslinking integral structure. The staggered channels are formed in the membrane after the dissolution of sacrificial short fiber. The sacrificial short fiber is chosen from polyester fiber, cellulose fiber and polyamide fiber. The ion exchange membrane has crystalline phase, amorphous phase, ionic phase and three-phase separated crosslinking continuous integral structure. An INDEPENDENT CLAIM is included for preparation of ion exchange membrane.
NOVELTY - A hydroxyl group-containing compound (I), is new.    USE - New hydroxyl group-containing compound is used for preparing cabazitaxel (claimed) for injection.    ADVANTAGE - The hydroxyl group-containing compound is economically prepared, without environmental pollution. The cabazitaxel having high quality is economically prepared with high yield, with reduced side reactions. The total impurity of hydroxyl group-containing compound is less than 0.1%.    DETAILED DESCRIPTION - A hydroxyl group-containing compound of formula (I), is new.    R=methyl or substituted derivative;and    R'=H, methyl or 2,2,2-trichloroethoxycarbonyl.    INDEPENDENT CLAIMS are included for the following:    (1) preparation of hydroxyl group-containing compound; and    (2) preparation of cabazitaxel, which involves decarboxylating hydroxyl group-containing compound of formula (X) to obtain (1S,2S,3R,4S,7R,9S,10S,12R,15S)-4-(acetyloxy)-1,15-dihydroxy-9,12-dimethoxy-10,14,17,17-tetramethyl-11-oxo-6-oxatetracyclo(11.3.1.03,10.04,7)heptadec-13-en-2-yl benzoate, reacting (1S,2S,3R,4S,7R,9S,10S,12R,15S)-4-(acetyloxy)-1,15-dihydroxy-9,12-dimethoxy-10,14,17,17-tetramethyl-11-oxo-6-oxatetracyclo(11.3.1.03,10.04,7)heptadec-13-en-2-yl benzoate and tert-butyl (5R)-5-(dihydroxymethyl)-2-(4-methoxyphenyl)-4-phenyl-1,3-oxazolidine-3-carboxylate to obtain tert-butyl-(5R)-5-((1R,2S,3S,4R,7R,9S,10S,12R)-5-acetyl-1,4-dihydroxy-9,12-dimethoxy-10,20,20-trimethyl-11-oxo-2-(phenoxycarbonyl)-6,15,17-trioxapentacyclo(11.6.1.03,10.04,7.014,18)icos-13-en-16-yl)-2-(4-methoxyphenyl)-4-phenyl-1,3-oxazolidine-3-carboxylate and processing tert-butyl-(5R)-5-((1R,2S,3S,4R,7R,9S,10S,12R)-5-acetyl-1,4-dihydroxy-9,12-dimethoxy-10,20,20-trimethyl-11-oxo-2-(phenoxycarbonyl)-6,15,17-trioxapentacyclo(11.6.1.03,10.04,7.014,18)icos-13-en-16-yl)-2-(4-methoxyphenyl)-4-phenyl-1,3-oxazolidine-3-carboxylate.
NOVELTY - Preparation of key intermediate (16 alpha ,17 alpha -d) methyl oxazoline steroidal compound involves: dissolving 16 alpha ,17 alpha -epoxy-20-methyl pyrrolidin-hydrazino-1,4-diene-3,11-dione with chloroform and additive and adding pressure reaction kettle, stirring and introducing ammonia to a certain pressure to reaction kettle and reacting at certain temperature to obtain the crude product; dissolving the crude product in glacial acetic acid, adding certain amount of acid anhydride, and controlling reaction temperature; and pouring the reaction liquid into cold sodium hydroxide solution.    USE - For preparation of key intermediate (16 alpha ,17 alpha -d)methyl oxazoline steroidal compound (claimed).    ADVANTAGE - The method achieves safe deflazacort clean production, helps to reduce environmental pollution, shortens the production cycle, reduces production costs, and significantly improves production safety, social, environmental and economic benefits.    DETAILED DESCRIPTION - Preparation of key intermediate (16 alpha ,17 alpha -d) methyl oxazoline steroidal compound involves: dissolving (16 alpha ,17 alpha -epoxy-20-methyl pyrrolidin-hydrazino-1,4- diene-3,11-dione) with chloroform and additive, adding pressure reaction kettle, stirring and introducing ammonia to a certain pressure to the reaction kettle and reacting at a certain temperature to obtain the crude product; dissolving the crude product in glacial acetic acid, stirring and adding a certain amount of acid anhydride, and controlling reaction temperature; pouring the reaction liquid into a cold sodium hydroxide solution, stirring for 1 hours, filtering to obtain the key intermediate (16 alpha ,17 alpha -d) methyl oxazoline steroidal compound.
NOVELTY - Organic solid waste-regenerated resources processing comprises subcritical hydrolysis step and anaerobic fermentation process. The anaerobic fermentation process is for subcritical hydrolysis for energy supply. The subcritical hydrolysis process is end processing comprising processing anaerobic fermentation to produce biogas.    USE - Organic solid waste-regenerated resources processing.    ADVANTAGE - The method reduces energy consumption, protects the environment and reduces pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for organic solid waste-regenerated resources processing device and system.    DESCRIPTION OF DRAWING(S) - The drawing shows a process flow diagram of organic solid waste treatment process (Drawing includes non-English language text).
NOVELTY - Production of ornamental plant fertilizer from waste phosphating solution comprises determining types and amounts of microelements of waste phosphating solution and adjusting pH.    USE - Production of ornamental plant fertilizer from waste phosphating solution (claimed).    ADVANTAGE - The energy-saving, environment-friendly and economical method has high regeneration efficiency.
NOVELTY - Manufacturing organic fertilizer comprises separating solid from tobacco extract liquid to obtain purified tobacco extract and the solid, concentrating the purified tobacco extract liquid and adding microbial inoculum with the purified tobacco extract liquid to ferment.    USE - The method is useful for manufacturing organic fertilizer (claimed), which is useful for crops.    ADVANTAGE - The organic fertilizer can be manufactured with high nutritional value and insecticidal effect, and improves microorganism propagation and physical and chemical properties and biological activity of soil and insecticidal effect.
NOVELTY - Preparation of clopidogrel hydrogensulfate crystal polymorph I comprises dropping concentrated sulfuric acid or 2-methyl tetrahydrofuran solution of concentrated sulfuric acid to clopidogrel free alkali of 2-methyl tetrahydrofuran solution to obtain mixed solution; reducing mixed solution temperature at - 10 degrees C to 5 degrees C; standing mixed solution and raising temperature at 10-35 degrees C; stirring to crystallize; separating out crystal; and drying to obtain clopidogrel hydrogen sulfate crystal polymorph I.    USE - Preparation of clopidogrel hydrogensulfate crystal polymorph I.    ADVANTAGE - The method is simple and easy to perform and has good reproduction quality. It provides clopidogrel hydrogensulfate crystal polymorph I with high purity via High Performance Liquid Chromatography, low cost, good stability, high solvent recovery rate, and environment friendly.
NOVELTY - Restoring carbon dioxide (CO2) to produce methane and acetic acid by utilizing a biological electrochemical system, comprises preparing biocathode in electrochemical system, CO2 aeration in cathode chamber and anode chamber, setting polarization of cathode potential, where the cathode is enriched by inoculating anaerobic sludge that is methanogen and acetic acid bacteria and other bacteria, directly obtaining electric and/or generated from the electrode from the electrodes of the hydrogen to obtain the electric CO2 reduction, and generating methane and acetic acid.    USE - The method is useful for restoring CO2 to produce methane and acetic acid by utilizing biological electrochemical system (claimed).    ADVANTAGE - The electrodes do not need to use expensive catalyst, and are low in cost. The method for restoring the CO2 to produce the methane and the acetic acid by utilizing the biological electrochemical system is rapid in production rate of the methane and the acetic by restoring the CO2, and has important application prospect for fixedly converting the CO2 and synthesizing organic chemicals.
NOVELTY - An Aspergillus fumigatus ZJUTZQ160 strain, which is preserved in the China center for type culture collection on May 31, 2012 and has a preservation number of CCTCC NO: M 2012199, is new.    USE - The Aspergillus fumigatus ZJUTZQ160 strain is useful for microbially preparing (R,R)-3-phenylglcidol (claimed).    ADVANTAGE - The method has the advantages of mild reaction conditions, high stereoselectivity and environmental benefits.
NOVELTY - 3-Fluoro-4-morpholinyl bromobenzene is reacted with a chiral oxazolidinone compound (I) in the presence of a catalyst, to obtain linezolid (II) (when G is acetyl). The compound (II) is processed and the obtained (S)-5-aminomethyl-3-(3-fluoro-4-morpholin-4-yl-phenyl)-oxazolidin-2-one is further processed, to obtain linezolid (when G is hydrogen, benzyl, t-butoxycarbonyl, methoxycarbonyl or diformylbenzene).    USE - Preparation of linezolid (claimed).    ADVANTAGE - The method environmentally-friendly enables preparation of linezolid with high yield, by simple process.    DETAILED DESCRIPTION - 3-Fluoro-4-morpholinyl bromobenzene is reacted with a chiral oxazolidinone compound of formula (I) in the presence of a catalyst, to obtain linezolid of formula (II) (when G is acetyl). The compound (II) is processed and the obtained (S)-5-aminomethyl-3-(3-fluoro-4-morpholin-4-yl-phenyl)-oxazolidin-2-one is further processed, to obtain linezolid (when G is hydrogen, benzyl, t-butoxycarbonyl, methoxycarbonyl or diformylbenzene).
NOVELTY - A water-retaining type organic fertilizer comprises 40-50 wt.% vegetable oil blend bran cake, 45-54 wt.% organic waste, 2.5-7 wt.% regulator, and 0.5-1 wt.% microbial inoculation agent. The vegetable oil blend bran cake is obtained from processing edible plant oil blend through filter press to remove oil and form cake. The organic waste is mushroom residue and/or chicken manure. The regulator is waste liquid from monosodium glutamate production. The microbial inoculation agent is organic waste fermentation bacteria.    USE - Water-retaining type organic fertilizer.    ADVANTAGE - The organic fertilizer does not contain harmful chemical component, uses organic raw materials containing large amount of thalli protein, and has water retention function so as to prevent drought, nutrient loss and poor crop yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the water-retaining type organic fertilizer, comprising:    (A) crushing vegetable oil blend bran cake and organic waste, mixing and stirring, spraying regulator and microbial inoculation agent, and adjusting pH value of the mixture to 6-8, carbon nitrogen ratio to 25-35:1, organic matter content to 45-65%, and water content to 43-48% to obtain fermentation material;    (B) putting the fermentation material to a fermentation tank, carrying out fermentation process, turning for the first time, when temperature reaches 65-70 degrees C, turning for the second time and turning every 1-2 days, fermenting for 12-15 days, then fermenting the material in the greenhouse for 5-8 days, naturally cooling, evaporating water when the temperature of the material is reduced to normal temperature, and controlling the water in the material to less than 30 wt.%; and    (C) conveying fermented material to a vibration sieve and sieving to obtain fine material as the organic fertilizer.
NOVELTY - Glyphosate oil suspending agent comprises 1-60 wt.% glyphosate, 10-80 wt.% vegetable oil, 1-15 wt.% dispersant, 1-10 wt.% thickener, 2-10 wt.% stabilizer, 10-40 wt.% emulsifier, 0.1-5 wt.% pH regulator, and 1-5 wt.% synergistic agent.    USE - Used as a glyphosate oil suspending agent.    ADVANTAGE - The agent consumes less filler in the production process, is environmentally friendly, and has high-efficient broad spectrum characteristics.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing glyphosate oil suspending agent, comprising (i) mixing and dispersing glyphosate, emulsifier, thickener and dispersant according to the above mentioned ratio, (ii) grinding in a sand mill for 1.5-2.5 hours, circulating water for cooling to make the temperature not greater than 50 degrees C, and the grain diameter is less than or equal to 5 microns, (iii) conveying into kettle after grinding, adding pH regulator, synergistic agent, stabilizer, and vegetable oil according to the above mentioned ratio, and uniformly stirring, and (iv) filtering the blend product using a filter screen of 30-50 meshes to obtain the finished product.
NOVELTY - An active liquid fuel comprises 80 vol.% methanol, 18 vol.% gasoline, and 2 vol.% methanol denaturant.    USE - An active liquid fuel for vehicle (claimed).    ADVANTAGE - Power of combustion performance is improved, and fuel is environment-friendly.
NOVELTY - Biogas is purified to natural gas by performing desulfurization to remove hydrogen sulfide (H2S), performing decarburization to remove carbon dioxide (CO2), and drying to remove impurities.    USE - A purification of biogas to natural gas (claimed).    ADVANTAGE - Biogas purification to natural gas is convenient and simple, is low cost, and meets natural gas standards.
NOVELTY - Alkaline ionic liquid contains Lewis base and Bronsted base functional group-containing compound as catalyst. Biological diesel fuel is prepared by reacting fatty acid of plant oil and methanol in the presence of catalyst, obtaining ester compound and glycerol, and heating and refluxing under normal pressure to obtain biological diesel oil.    USE - Alkaline ionic liquid for preparation of biological diesel fuel (claimed).    ADVANTAGE - Alkaline ionic liquid has high catalyst activity, excellent thermal stability, and low cost and is environmentally friendly and reusable, reaction condition is mild, and reaction process is stable.    DETAILED DESCRIPTION - Alkaline ionic liquid contains Lewis base and Bronsted base functional group-containing compound as catalyst of formula (I). Biological diesel fuel is prepared by reacting fatty acid of plant oil of formula (Ia) and methanol (CH3OH) in the presence of catalyst, obtaining ester compound of formula R-C(=O)-O-CH3 (Ib) and glycerol of formula OH-CH2-CH(OH)-CH2-OH (Ic), and heating and refluxing under normal pressure to obtain biological diesel oil.    R=carbon chain of fatty acid of plant oil.
NOVELTY - A 7-(4-Chlorophenyl)-5, 6-dihydro-7aH-benzo (h) 1, 2, 4-triazolo-(3, 4-b)quinazoline-5,6-dione (I) is new.    USE - 7-(4-Chlorophenyl)-5, 6-dihydro-7aH-benzo (h) 1, 2, 4-triazolo-(3, 4-b)quinazoline-5,6-dione (I).    ADVANTAGE - The compound (I) has stronger activity, is green and environment-friendly, and has wide availability of raw material, simple operation and high yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of compound (I).
NOVELTY - Recycling triethyl phosphate from pesticide intermediate slag comprises: adding first solvent mixture to slag, reacting at 25-55 degrees C for 1-3 hours, adding dropwise catalyst, reacting for 1-3 hours, separating solid and liquid, crystallizing, distilling under vacuum to obtain mother liquor by-product; neutralizing by alkali, adding second mixed solvent, taking upper organic phase, distilling under reduced pressure to obtain intermediate product, and distilling to obtain triethyl phosphate.    USE - Method for recycling triethyl phosphate from pesticide intermediate slag.    ADVANTAGE - The triethyl phosphate has 99.5% purity. The method is simple and easy. The manufacturing cost is low.
NOVELTY - Fungicidal composition comprises epoxiconazole and kresoxim-methyl in mass ratio of 1:8.5-28.    USE - As fungicidal composition in form of water dispersible granule (claimed).    ADVANTAGE - The fungicidal composition is prepared by simple method, suitable for continuous production, easy to use and environmentally-friendly, consumes low energy, and has excellent dispersibility, foamability and disintegration and suspension rates.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the composition, which involves (a) mixing epoxiconazole, kresoxim-methyl, dispersing agent, wetting agent, fertilizer, disintegrating agent and inert filler, (b) crushing the mixture to 600-800 mesh size using ultra-jet mill, to obtain fine powder, (c) mixing the obtained powder with water and kneading the mixture, (d) granulating the kneaded mixture, and (e) drying the granule.
NOVELTY - Magnetic bioorganic fertilizer comprises 300 parts mass silicate mineral, 300 parts mass soy meal, 200 parts mass soybean molasses, 80 parts mass tobacco juice, 100 parts mass plant ash, and 20 parts mass mixed strain, where the mixed strain comprises Trichoderma pseudokoningii and Bacillus subtilis. The silicate mineral comprises 52% available silicon (silicon dioxide), 25% available calcium (calcium oxide), 10% iron, 7.2% potassium and trace elements chosen from boron, zinc, molybdenum and selenium.    USE - As magnetic bioorganic fertilizer (claimed).    ADVANTAGE - The clean pollution-free magnetic bioorganic fertilizer is rich in diversified nutrients and synergistic, and has stable physical and chemical indicators.    DETAILED DESCRIPTION - Magnetic bioorganic fertilizer comprises 300 parts mass silicate mineral, 300 parts mass soy meal, 200 parts mass soybean molasses, 80 parts mass tobacco juice, 100 parts mass plant ash, and 20 parts mass mixed strain, where the mixed strain comprises Trichoderma pseudokoningii and Bacillus subtilis. The silicate mineral comprises 52% available silicon (silicon dioxide), 25% available calcium (calcium oxide), 10% iron, 7.2% potassium and trace elements chosen from boron, zinc, molybdenum and selenium. The soybean molasses comprises 9% soybean whey protein, 20% sucrose, 12% monosaccharide, 16% soybean oligosaccharides, 15% stachyose and raffinose, 3% soy isoflavones, 6% lipids and phospholipids, phosphorus, calcium, magnesium, potassium and iron. The plant ash comprises 12% potassium, 2% phosphorus, calcium, magnesium, silicon, iron, manganese and zinc. The fertilizer is prepared by carrying out magnetization at strength of 300-600 A/m and excitation power of 1-5 KW for 4-8 seconds.
NOVELTY - A method for pyrolysis of water without the use of an added catalyst or additive, involves (A) splitting water to form fine droplets using high-speed rotation of a magnetic suspension bearing, magnetic dynamical force rotation system and a carbon fiber super-gravity screen; (B) pre-cracking by subjecting it to ultrasound and strong electronic nuclear magnetic resonance technology; and (C) carrying out pyrolysis under high temperature, by passing through ultrasonic electric arc.    USE - For pyrolysis of water, particularly sea water, sewage, mineral water, tap water etc to produce energy used as e.g. electricity, gas fuel.    ADVANTAGE - The method enables pyrolysis of water to form a high energy fuel, in a safe, economically and feasible manner, and proceeds in absence of an added catalyst or additive.
NOVELTY - A ketonic group protection is carried out with respect to a dicarbonyl group-containing compound (a) (VII) to obtain keto group-protected compound (b) (VI). A nucleophilic substitution reaction is carried out with respect to the compound (b) and 2-aminopyridine to obtain a pyridinylamine compound (c) (V). A ketonic group deprotection is carried out with respect to the compound (c), and then cyclized, to obtain an imidazole compound (d) (IV). The compound (d) is hydrolyzed, diphosphorylated and recrystallized, to obtain minodronic acid hydrate.    USE - Preparation of minodronic acid hydrate (claimed).    ADVANTAGE - The minodronic acid hydrate is economically, environmentally-friendly and safely prepared under mild reaction conditions, by simple process.    DETAILED DESCRIPTION - A ketonic group protection is carried out with respect to a dicarbonyl group-containing compound (a) of formula: X-CH2-C(=O)-CH2-C(=O)-O-R (VII) to obtain keto group-protected compound (b) of formula: X-CH2-C(-R1)-CH2-C(-R2)-O-R (VI). A nucleophilic substitution reaction is carried out with respect to the compound (b) and 2-aminopyridine to obtain a pyridinylamine compound (c) of formula (V). A ketonic group deprotection is carried out with respect to the compound (c) and then cyclization reaction is carried out, to obtain an imidazole compound (d) of formula (IV). The compound (d) is hydrolyzed, to obtain (1,8a-dihydro-imidazo(1,2-a)pyridin-3-yl)-acetic acid (e). Diphosphorylation is carried out with respect to the compound (e) to obtain minodronic acid (f), and the compound (f) is recrystallized, to obtain minodronic acid hydrate (g).    X=halo;    R=1-4C alkyl;    R1,R2=1-4C alkyl;and    or R1+R2=2-4C alkylene.    An INDEPENDENT CLAIM is included for preparation of minodronic acid.
NOVELTY - Method for manufacturing organic fertilizer, involves mixing coffee waste and herbal medicine waste, where mixing step is performed twice, supplying mixture to earthworm as feed, collecting the earthworm castings from the earthworm, and mixing the earthworm castings with the coffee waste.    USE - The method is useful for manufacturing organic fertilizer (claimed) used for maintaining soil fertility, and improving organic content of soil.    ADVANTAGE - The method manufactures organic fertilizer with carbon/nitrogen rate of 20-25.
NOVELTY - Preparation of lurasidone comprises adding 3-(1-piperazinyl)-1,2-benzisothiazole to toluene, adding (IR, 2R)-1,2-bis (methanesulfonyloxymethyl)cyclohexane and inorganic alkali, heating to 110-130 degrees C, refluxing and reacting for 12-36 hours, adding (3aR,4S,7R,7aS) 4,7-methano-1H-isoindole-1,3(2H)-dione, decompressing, adding ethyl acetate to residue, washing with 5% hydrochloric acid solution, filtering the drying agent, concentrating, filtering to obtain lurasidone crude product, dissolving in water, extracting with ethyl acetate, decompressing and distilling, and filtering.    USE - Method for the preparation of lurasidone (claimed) used for treating schizophrenia.    ADVANTAGE - The method recycles solvent, and has a simple operation.    DETAILED DESCRIPTION - Preparation of lurasidone comprises adding 3-(1-piperazinyl)-1,2-benzisothiazole to toluene, stirring to dissolve, adding (IR, 2R)-1,2-bis (methanesulfonyloxymethyl)cyclohexane and inorganic alkali, heating to 110-130 degrees C, refluxing and reacting for 12-36 hours, detecting if 3-(1-piperazinyl)-1,2-benzisothiazole spots disappears by TLC, adding (3aR,4S,7R,7aS) 4,7-methano-1H-isoindole-1,3(2H)-dione, stirring and heating to 110-130 degrees C, refluxing, reacting for 4-12 hours, cooling, decompressing and recycling toluene, adding ethyl acetate to residue, stirring to dissolve, washing with 5% hydrochloric acid solution for 2-3 times, separating organic layer, drying for 20-120 degrees C, filtering the drying agent, concentrating, dropping concentrated hydrochloric acid, separating out solid, filtering to obtain lurasidone crude product, dissolving in water, stirring, adding saturated sodium hydroxide water solution to adjust pH to 9-10, extracting for 2 times with ethyl acetate, adding anhydrous magnesium sulfate for 2 hours, decompressing and distilling, dropping concentrated hydrochloric acid solid, and filtering.
NOVELTY - Preparation of biodiesel involves heating soybean oil into a reactor at 30-70 degrees C for 1-90 minutes, adding methanol solution dissolved with ionic liquid, stirring, reacting for 30-150 minutes, maintaining the resultant reaction solution at room temperature, layering, adding water to wash, maintaining until the resultant solution divided into layers, and separating the resultant upper layer material.    USE - Preparation of biodiesel.    ADVANTAGE - The method efficiently provides biodiesel having excellent stability and recyclability. The biodiesel is environmentally-friendly.
NOVELTY - Coalification manufacture of solid fuel involves sequentially performing high-liquid separation process of organic waste, adulteration elimination process, coalification process, atomization, polycondensation process, cooling and drying.    USE - Coalification manufacture of solid fuel.    ADVANTAGE - The coalification manufacture of solid fuel is environmentally-friendly.
NOVELTY - Tertiary-butyl acetate and strong base are added to toluene under the protection of nitrogen in the mole ratio of 1:1-1.15, temperature is slowly raised at 105-110 degrees C, stirred and reacted for 3-7 hours, and heat is preserved for 2-4 hours, to obtain alpha -sodium acid t-butyl. The material is cooled by conventional refrigerator at -30 degrees C to 0 degrees C, then mixed solution containing ethyl (3R)-4-cyano-3-hydroxybutanoate and tetrahydrofuran is dropped in the material, dropped for 0.5-2 hours, and heat is preserved for 2-4 hours, to obtain atorvastatin calcium chiral side chain.    USE - Preparation of atorvastatin calcium chiral side chain.    ADVANTAGE - The atorvastatin calcium chiral side chain is efficiently prepared with improved yield.    DETAILED DESCRIPTION - Tertiary-butyl acetate and strong base are added to toluene under the protection of nitrogen in the mole ratio of 1:1-1.15, temperature is slowly raised at 105-110 degrees C, stirred and reacted for 3-7 hours, and heat is preserved for 2-4 hours, to obtain alpha -sodium acid t-butyl. The material is cooled by conventional refrigerator at -30 degrees C to 0 degrees C, then mixed solution containing ethyl (3R)-4-cyano-3-hydroxybutanoateand tetrahydrofuran is dropped in the material, dropped for 0.5-2 hours, and heat is preserved for 2-4 hours, to obtain atorvastatin calcium chiral side chain. The molar ratio of ethyl (3R)-4-cyano-3-hydroxybutanoate and butyl acetate is 0.3-0.5:1. The weight ratio of tetrahydrofuran and ethyl (3R)-4-cyano-3-hydroxybutanoate is 1-2.
NOVELTY - Waste is mixed in large bowl with binding agent and optionally with water. By using machine tool with film, cylindrical briquettes are formed from mixed material and wrapped in film. The formed briquettes are removed from mechanical machine tool and pre-dried for 5 hours. Film is removed from formed briquette, and further dried for 12-13 hours to obtain biofuel briquettes.    USE - Manufacture of biofuel briquettes (claimed).    ADVANTAGE - The method efficiently provides biofuel briquettes having high energy emission and excellent light- and damp-proof property and moisture resistance, without using heat, electricity and technical equipment with reduced consumption of energy, without affecting the environment.
NOVELTY - Bedding for animal husbandry, preferably horse husbandry, comprises several bedding particles formed as pellet made of pressed wood chip and sawdust, where the pellet has a disk shaped or polygonal geometry, or rectangular, pyramidal or tetrahedral geometry with a diameter of greater than or equal to 6 cm and a thickness of 1.5-3 cm.    USE - The bedding is useful for animal husbandry, preferably horse husbandry.    ADVANTAGE - The bedding: is planar, and cost-efficient; can be easily disposed after using; and does not get stuck in the hoof region of horse.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for operating a wood chip furnace, preferably a wood chip-small power plant, comprising mixing the bedding for the animal husbandry with 40 vol.%, preferably 30 vol.% fuel.    DESCRIPTION OF DRAWING(S) - The figures 1 and 2 show a schematic representation of the disk-shaped pellets having line-shaped breaking point, and a schematic representation of tetrahedral-shaped pellet, respectively.    Disk-shaped pellet (1)    Predetermined breaking point (2)    Contact line (4)    Cavity (5)    Tetrahedral-shaped pellet (6)
NOVELTY - The device has a spare components supply unit (100) that supplies the spare components to be laminated sequentially on a fuel cell stack (10). A spare components transportation unit (300) transfers the spare components loaded in the spare components supply unit to a work table (200). A task table driving unit (400) controls the height and posture of the work table. A stack connecting unit (500) screws the fuel cell stack laminated with spare components in the work table.    USE - Apparatus for manufacturing fuel cell stack assembly.    ADVANTAGE - The occurrence of the misalignment during the lamination of the fuel cell stack can be prevented, so that the generation of the fault in the fuel cell stack assembly can be avoided. The quality of the fuel cell can be improved by uniformly distributing the joint pressure power of spare component in the fuel cell stack.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for manufacturing fuel cell stack assembly.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the fuel cell stack manufacturing apparatus.    Fuel cell stack (10)    Spare components supply unit (100)    Work table (200)    Spare components transportation unit (300)    Task table driving unit (400)    Stack connecting unit (500)
NOVELTY - Synthesizing metal nanoparticles involves: submerging an electrically conductive substrate in a polysaccharide solution containing a predetermined concentration of a metal salt; applying an electric potential between the substrate and polysaccharide solution for a predetermined period of time to form a polysaccharide layer containing metal nanoparticles on the electrically conductive substrate; dissolving the polysaccharide layer to form a solution containing the polysaccharide and the metal nanoparticles; and separating the metal nanoparticles from polysaccharide.    USE - For synthesizing metal nanoparticles (claimed), particularly palladium nanoparticles. The metal nanoparticles have useful applications in a variety of fields including material synthesis, fuel cells, supercapacitors, and batteries.    ADVANTAGE - Use of common stainless steel, ubiquitous chitosan, and small amounts of metal salts, along with simple processing, results in significant cost savings over other processes and the process works with chitosan from multiple sources, with varying degrees of deacetylization. The process is rapid, occurring at room temperature, and eliminates the use of hazardous reducing agents to obtain metal nanoparticles. The process is easily adaptable for production of other nanoparticles and different substrates can be used for electrodes.
NOVELTY - Producing a biofuel, comprises: providing a biological hydrocarbon producing organism selected using a nanoscale detection process, where the providing step further includes growing the biological hydrocarbon producing organism under conditions controlled by at least one nanotechnological material or process; exposing the biological hydrocarbon producing organism to conditions to cause substantial release of a hydrocarbon from the biological hydrocarbon producing organism; isolating at least a portion of the hydrocarbon; and processing the isolated hydrocarbon to produce the biofuel.    USE - The method is useful for producing a biofuel (claimed) which is biodiesel or ethanol.    ADVANTAGE - The method: produces biofuels with high yield and low cost; reduces greenhouse gas by producing hydrocarbon fuels from carbon dioxide gas; and provides greater precision control, nanoscale control and accuracy with respect to the organisms used in the production of biofuels and enables the tuning of the system to drive the selected production of a desired metabolite over unwanted products.
NOVELTY - Water containing a photocatalyst and divalent cobalt ion is prepared, light is irradiated to the photocatalyst and water is decomposed into hydrogen and oxygen. Thus, water is decomposed.    USE - Decomposition of water used for manufacturing hydrogen and oxygen.    ADVANTAGE - The water is economically decomposed with high yield, by simple method.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing apparatus of hydrogen and oxygen containing gas recovery apparatus, which has reactor which introduces the water containing photocatalyst and divalent cobalt ion.
NOVELTY - A hydrogen production apparatus consists of photocatalyst pole positioned spaced apart from counter electrode (3) inside water tank (5). The photocatalyst pole is adhered on one surface of substrate (2) by low-order titania layer (1).    USE - Apparatus for producing hydrogen used as fuel for fuel cell.    ADVANTAGE - The hydrogen production apparatus enables manufacture of hydrogen efficiently using ultraviolet-rays and visible light. The generation of electric power in fuel cells is high.    DETAILED DESCRIPTION - A hydrogen production apparatus consists of photocatalyst pole positioned spaced apart from counter electrode inside water tank. The photocatalyst pole is adhered on substrate by low-order titania (TiOx, where x is 1-2) layer.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of hydrogen producing apparatus.    Titania layer (1)    Substrate (2)    Counter electrode (3)    Electrolyte solution (4)    Water tank (5)
NOVELTY - A hydrogen production apparatus comprises frame which forms electrolyte solution accommodation space inside while holding a cathode material and anode material (21), anode material which is equipped with board to which photocatalyst is made to adhere at one side, electrically conductive film which is formed in one surface, and electrical connection part which is connected to electrically-conductive board which contacts electrically conductive film formed in one surface in peripheral part of the board.    USE - A hydrogen production apparatus (claimed).    ADVANTAGE - Size of the board is reduced and hydrogen can be manufactured at high efficiency. Structure is simple and electrical resistance is low.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the hydrogen production apparatus. (Drawing includes non-English language text).    Hydrogen production module (10)    Outer frame (11)    Inner frame (12)    Anode material (21)    Water circulating piping (61)
NOVELTY - Biomass composition (I) comprises (relative to the total dry weight of the composition): (a) 5-35 dry wt.% biomass solid particles with a D50 of 0-250 mu m and D90 of less than 400 mu m; and (b) 95-65 dry wt.% dispersant, where the dispersant comprises an oil, fat and/or wax and the biomass solid particles comprise plant derived solid particles of oilseed meal.    USE - The biomass composition is useful for coating on a fertilizer particle or animal feed particle (claimed).    ADVANTAGE - The biomass composition: provides the particles that have good flowability (during storage and handling), with the residual coating readily absorbed into the environment; and exhibits good anti-caking performance, thus enabling less processed biomass to be used and resulting in less hazardous fine dust formation.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a coated fertilizer comprising fertilizer particles coated with the biomass composition;    (2) a coated animal feed comprising feed particles coated with the biomass composition; and    (3) producing the biomass composition, comprising dispersing the biomass solid particles in the dispersant, and grinding an initial biomass composition until the solid particles have a D50 of 0-250 mu m, where the initial biomass composition comprises solid particles with a D50 of 100-5000 mu m and comprises at most 25 wt.% water, relative to the weight of the total initial biomass composition.
NOVELTY - Method for generating hydrogen, involves processing target object which comprises at least one of ion source, organic component and water, adding the above-mentioned target object to zinc oxide, reacting target object with the zinc oxide in presence of anaerobic microbe that is capable of producing hydrogen sulfide, and preventing or suppressing production of the hydrogen sulfide by the microbe under anaerobic conditions.    USE - The method is useful for generating hydrogen (claimed), preferably hydrogen gas used for producing biogas which is used in sludge deposition field, construction field and waste material deposition field.    ADVANTAGE - The method prevents production of poisonous gas e.g. hydrogen sulfide gas that has offensive odor, is environmentally-friendly, utilizes waste materials and hence cost-effectively produces hydrogen, and requires less effort.
NOVELTY - Method for producing compost and methane gas from biomass resources, involves using crushed pieces of the biomass resources in the shape of a rod in a fixed ratio as raw material, filling the biomass-resource crushed piece by gravity fall in a cylindrical net bag, inserting the cylindrical net bag containing the biomass resource crushed piece into methane fermentation tank at 90 degrees , circulating reaction liquid from outside, allowing to flow down from the upper portion of the filled layer of biomass resources, and performing methane fermentation.    USE - The method is useful for producing compost and methane gas from biomass resources, used as organic fertilizer.    ADVANTAGE - The method utilizes waste material which cannot be utilized, destroyed by fire or buried, thus coincides with objective of prevention of global warming by reducing generation of greenhouse gases, increases rate of methane fermentation, as it improves the circulation of reaction liquid inside the cylinder, prevents decrease in fermentation rate by compression and obstruction of raw material filled layer over a long period of time, maintains favorable fermentation state, and utilizes biomass resources that can be stored simply, and conveniently.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for drying and storing biomass resource, involves, placing cylindrical net bag filled with coarse pulverized biomass resources on a pedestal assembled by wooden material or iron, where the central axis of the tube is horizontal or vertical, covering with a tarpaulin and performing natural drying.
NOVELTY - Producing oil comprises applying cavitation to a grain-based liquid medium processing stream in one or more locations of an oil separation process at a power and frequency effective to increase oil yield and reduce the residual oil levels in the processed stream when applied before to and/or immediately after the oil separator.    USE - The method is useful for producing oil (claimed), where the oil is useful in cooking oils, pharmaceuticals, paints, soaps, candles, perfumes, cosmetics, animal feed and bio-diesel.    ADVANTAGE - The method effectively produces the oil with high yield, less energy consumption and reduced chemical addition requirements.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a system for oil production comprising: an oil separation system for grain consisting of corn, rye, sorghum, wheat, barley, oats and/or rice, where the oil separation system has an grain-based liquid medium processing stream, and the liquid medium processing stream includes whole stillage, thin stillage, inner evaporator effect thin stillage concentrate, concentrated thin stillage syrups, oil from separator, syrup discharge from separator and the mixture of wetcake and syrup before to the distillers dried grains dryer; and a cavitation unit positioned in at least one location along the grain-based liquid medium processing stream of the oil separation system, where the cavitation unit operates at a power and frequency effective to increase oil yield and reduce the residual oil levels in the processed stream when applied before to and/or immediately after the oil separator.
NOVELTY - Producing nitro-chitosan derivative involves contacting chitosan with a solvent to form chitosan solution; adding an acid selected from hydrochloric acid, hypochlorous acid and/or organic acids to the chitosan solution to reduce the pH of solution to 1-7; applying a negative potential of -1 to -5 volts to the solution by introduction of cathode and anode into the solution; forming hydrogel comprising nitro-chitosan derivative on cathode; and recovering nitro-chitosan derivative from cathode.    USE - For producing nitro-chitosan derivative for removing chromium from groundwater or soil (claimed); as chelating agent for removing contaminants including heavy metals from environment.    ADVANTAGE - The process utilizes electrochemical methods to functionalize and/or modify amine and/or hydroxyl groups present on chitosan, to form new derivatives. The altered cationic affinity of these derivatives make them excellent candidates for environmental applications, including water and waste treatments, and fertilizers. The chitosan derivatives obtained have higher affinity for toxic metals, e.g. chromium, a known contaminant in soil and water. The electrochemical synthetic processes are scalable and provide facile process control parameters. The limited use of toxic oxidizing and reducing agents in the process provides an environmentally friendly process. The nitro-chitosan derivatives are better chelating agents compared to pure chitosan for contaminants including chromate and/or other toxic metal ions such as uranyl, and have higher metal binding capacities than chitosan. Thus, the nitro-chitosan derivatives perform better than nitro-chitosan in environmental applications, including soil treatments, groundwater treatments, water filtration, and fertilizers, as well as drug delivery devices, cosmetics, pharmaceuticals.
NOVELTY - Method for producing fuel oil base, involves (a) aerobically culturing microalgae Euglena under nitrogen-deficient conditions, (b) adding nutrient source to solution containing the cultured microalgae Euglena, setting the dissolved oxygen concentration of the solution at 0.03 mg/l or less, performing anaerobic fermentation of the microalgae Euglena and obtaining wax ester, and (c) hydrogenating stock oil containing the wax ester to obtain fuel oil base.    USE - The method is useful for producing fuel oil base used for producing fuel oil composition (all claimed).    ADVANTAGE - The fuel oil composition satisfies specification value of aviation turbine fuel oil specified by ASTM D7566-11, and reduces emission of carbon dioxide into the environment, thus is environmentally-friendly. The method enables to easily produce fuel oil base for aviation fuel having carbon number distribution of 10-16, reliably increases esterification and production efficiency of wax, and utilizes nutrient source that has high availability, thus is cost-effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing fuel oil composition, which involves using the fuel oil base produced by the above-mentioned method, and obtaining the fuel oil composition having precipitation point of -47 degrees C or less and sulfur content of 10 parts/million or less.
NOVELTY - Method for producing Euglena having high wax ester content, involves aerobically culturing micro-alga Euglena in nitrogen poor conditions, adding nutrient to the culture solution and maintaining a cell under in an anaerobic condition.    USE - The method is useful for producing Euglena having high wax ester content (claimed), which is used for producing biofuel.    ADVANTAGE - The method is cost-effective and requires low energy.
NOVELTY - Ethanol composition comprises at least 92 wt.% of ethanol, less than 1000 weight parts per million (wppm) of isopropanol, acetaldehyde, and less than 10 wppm of methanol, where the amount of acetaldehyde is less than the amount of isopropanol.    USE - The ethanol composition is useful: in a variety of applications including fuels application (to make gasoline for motor vehicles such as automobiles, boats and small piston engine aircrafts), solvents, chemical feedstocks, pharmaceutical products, cleansers, sanitizers, hydrogenation transport or consumption; as a solvent for toiletry and cosmetic preparations, detergents, disinfectants, coatings, inks and pharmaceuticals, as a processing solvent in manufacturing medicinal products, food preparations, dyes, photochemicals and latex processing and as a chemical feedstock to make other chemicals such as vinegar, ethyl acrylate, ethyl acetate, ethylene, glycol ethers, ethylamines, aldehydes and higher alcohols, preferably butanol.    ADVANTAGE - The ethanol composition exhibits high purity.
NOVELTY - Preparing a polymer, comprises performing polymerization of a dispersed phase in the presence of a reactive stabilizer, and providing, in aqueous phase, at least one dispersed ethylenically unsaturated monomer, at least one free radical source and the reactive stabilizer comprising a polymeric chain including monomer units of N-vinyl lactam and a thiocarbonylthio group.    USE - The process is useful for preparing a polymer, preferably block polymers in the form of micelles, which are useful as polymerization sites for controlled radical polymerization, where the polymer is useful for producing a polymeric dispersion, which is useful for producing paints, coatings, adhesives, for the production of building materials, in cosmetic or personal care compositions, or in plant protection formulations for agriculture or in fluids for oil extraction (all claimed).    ADVANTAGE - The process is capable of easily preparing the polymer in an eco-friendly manner with less toxicity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a polymeric dispersion comprising the polymer obtained by the process.
NOVELTY - Separation of ammonia from biogas plants comprises: (a) separating gaseous ammonia present in the process fluid from the biogas plant of the bioreactor; (b) drying gaseous ammonia; (c) drying a partial stream of formed raw biogas in the bioreactor; (d) contacting the dried ammonia and the dried partial stream of the raw biogas in a reaction chamber; and (e) converting ammonia and carbon dioxide contained in the partial flow of the raw biogas to form ammonium carbamate.    USE - The process is useful for the fermentation of nitrogenous substrates in a biogas plant of a bioreactor, where the nitrogen-containing substrate is poultry manure, dry chicken manure, chicken manure and/or liquid manure and for the separation of ammonia from biogas plant (all claimed), which is useful as fertilizer. No biological data given.    ADVANTAGE - The process provides ammonia in high yield.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a flow diagram of the separation of ammonia from the biogas plant (Drawing includes non-English language text).
NOVELTY - The apparatus has reformer (200) which is provided to generate anode gas including hydrogen by reforming source gas. A fuel cell stack (250) is arranged below reformer. A restriction protrusion (900) is configured to restrict relative position between cathode gas flow passage portion (600) and reformer in perpendicular direction (M) to vertical direction (H) of housing (800). The variation of flow passage width (L1) of intermediate exhaust gas flow passage (303) formed between reformer and cathode gas flow passage portion is restricted.    USE - Fuel cell apparatus such as solid oxide fuel cell apparatus, solid polymer fuel cell apparatus, phosphoric acid fuel cell apparatus, and molten carbonate fuel cell apparatus.    ADVANTAGE - The assembling errors occurred during timing of assembling of the fuel cell apparatus can be prevented. The stability of the combustion characteristics of the anode-off gas in the combustion portion can be improved. The stability of temperature of the reformer heated by combustion in combustion portion can be improved. The concentration of hydrogen of anode gas generated by reformer is stable. The power generation reaction of the fuel cell stack is stable. The durability of the fuel cell apparatus can be improved. The power generation performance of the stack can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross sectional view of the fuel cell apparatus.    Reformer (200)    Fuel cell stack (250)    Intermediate exhaust gas flow passage (303)    Cathode gas flow passage portion (600)    Housing (800)    Restriction protrusion (900)    Vertical direction (H)    Flow passage width (L1)    Perpendicular direction (M)
NOVELTY - Continuous fermentation method, involves using aggregate that comprises lactic acid bacteria, preferably Lactobacillus plantarum, and yeast, where the fermentation is performed under pH of 5 or less.    USE - The continuous fermentation method is useful for producing ethanol (claimed), organic acid, and phenyl ethyl alcohol, where the ethanol is used as biofuel.    ADVANTAGE - The method avoids contamination of fermentation medium, consumes less time, provides high yield of ethanol, is simple to perform and cost-effective, and utilizes waste material as raw material.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for lactic acid bacteria NITE P-1112 strain (HP9).
NOVELTY - A chaff-containing molded product (30) is obtained by blending 100 parts weight chaff (10) obtained from agricultural waste with regenerated polyethylene resin (20) used as binder resin, which is darkened by heat compression, and molding mixture by heat compression. The chaff-containing molded product has bending elastic modulus of 800-3000 MPa based on JIS K 7171..    USE - Chaff-containing molded product (claimed).    ADVANTAGE - The chaff-containing molded product having excellent mechanical properties and recyclability is provided without controlling moisture in chaff or conducting dewatering treatment, and is lightweight and economical.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of chaff-containing molded product. The mixture of chaff and regenerated polyethylene resin is bonded at 150-180 degrees C and 2-10 KgF/cm2, and volume compression of 12-90%.    DESCRIPTION OF DRAWING(S) - The drawing shows the structure of chaff-containing molded product.    Chaff (10)    Regenerated polyethylene resin (20)    Chaff-containing molded product (30)
NOVELTY - Degrading or converting a cellulosic material, involves treating the cellulosic material with an enzyme composition in the presence of a reducing agent.    USE - For degrading and converting a cellulosic material (claimed) to sugars for producing substances e.g. fuel, potable ethanol, and fermentation products e.g. acids, alcohols, ketones, gases.    ADVANTAGE - The method recovers the reducing agent and recycled back to a new saccharification reaction; and is implemented by using any conventional biomass processing apparatus.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) producing a fermentation product involving 1) saccharifying a cellulosic material with an enzyme composition; 2) fermenting the saccharified cellulosic material with at least one fermenting microorganism to produce the fermentation product; and optionally 3) recovering the fermentation product from the fermentation, where step (1) is carried out in the presence of a reducing agent, and/or step (2) is carried out in the presence of a reducing agent; and    (2) fermenting a cellulosic material, involving fermenting the cellulosic material with at least one fermenting microorganism, where the cellulosic material is saccharified with an enzyme composition in the presence of a reducing agent.
NOVELTY - Syngas biomethanation process involves producing a synthesis gas from pyrolysis of a feedstock (A), and adding the synthesis gas to an anaerobic digester (1).    USE - Syngas biomethanation process (claimed).    ADVANTAGE - The syngas biomethanation process is economically carried out with reduced energy consumption.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) apparatus for transferring syngas to digestate, which has a pipe between a source of digestate and a digester, a pump to create a flow of digestate in the pipe, an ejector, and microbubble pump or gas transfer membrane in communication with pipe having an inlet connected to source of the syngas; and    (2) process and apparatus for treating wastewater, which involves treating the wastewater to generate a sludge, feeding the sludge to an anaerobic digester to produce biogas and digestate (B), dewatering the digestate to produce a cake (E), thermally drying the cake to produce a dried cake (G), pyrolysing the dried cake to produce char (J) and syngas, and feeding the syngas to the anaerobic digester.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow chart explaining anaerobic digestion system and pyrolysis system.    Anaerobic digester (1)    Feedstock (A)    Digestate (B)    Dried cake (G)    Char (J)
NOVELTY - A microorganism carrier for organic-refuse processing apparatus comprises microorganisms which ferment organic refuse while contacting with organic refuse in which the apparatus fermentation-processes, decomposes, and weight-reduces an organic refuse. Microorganisms which ferment organic refuse are adsorbed by porous sponge carrier (A) by forming 1 side of hexahedron having size of 10 mm with polyurethane-type material which has specific gravity of less than or equal to 20 kg/m3 and tensile strength of 0.77 kg/cm2.    USE - A microorganism carrier for organic-refuse processing apparatus used for sink cabinets (all claimed).    ADVANTAGE - Organic refuse can be fermentation-processed continuously without adding new microorganisms, lifetime of microorganisms is extended, and operation noise is decreased by abrasion reduction of carrier and apparatus.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for organic-refuse processing apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional diagram of an organic-refuse processing apparatus filled with microorganism carrier.    Insertion opening (1)    Cyclic sprinkler (2)    Reaction container (3)    Rotary blade (4)    Porous sponge carrier (A)
NOVELTY - Oxidizing water, involves: providing amorphous cobalt tungstate; providing water; and placing the water into contact with the amorphous cobalt tungstate, where the amorphous cobalt tungstate catalyzes the oxidation of water.    USE - For oxidizing water (claimed), to produce hydrogen and oxygen gases.    ADVANTAGE - The catalytic activity of the amorphous cobalt tungstate as measured by current density is at least 200% greater than a catalytic activity of crystalline cobalt tungstate. The electrochemical cell offers a highly efficient method of splitting water using solar illumination, without the need for an applied potential.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a cell for oxidizing water comprising: water and amorphous cobalt tungstate in contact with the water, where the amorphous cobalt tungstate catalyzes the oxidation of water.
NOVELTY - Preparing a polymer comprises dispersed phase polymerization of an aqueous phase comprising at least one dispersed ethylenically unsaturated monomer, at least one free radical source and a reactive stabilizer comprising a polymeric chain including monomer units of N-vinyl lactam and a thiocarbonylthio group.    USE - The process is useful for preparing a polymer, preferably block polymers in the form of micelles, which are useful as polymerization sites for controlled radical polymerization, where the polymer is useful for producing a polymeric dispersion, which is useful for producing paints, coatings, adhesives, for the production of building materials, in cosmetic or personal care compositions, or in plant protection formulations for agriculture or in fluids for oil extraction (all claimed). No biological data given.    ADVANTAGE - The reactive stabilizer used in the process has reduced toxicity hence the process is eco-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a polymeric dispersion comprising the polymer obtained by the process.
NOVELTY - The method involves forming a stack (50), and circulating calibration fluid in an anode compartment (59a) and a cathode compartment (59b) of the stack. Differential pressure between a fluid inlet (60) and a fluid outlet (62) of the anode and cathode compartments is measured. Compressive force is applied on opposite ends of the stack until final compression force reaches the measured differential pressure, where the compressive force is greater than or equal to a high threshold force. The compressive force is increased by measuring length of the stack.    USE - Method for manufacturing a fuel cell for generation of an electric current in a transportable or stationary energy source integrate device e.g. car and boat.    ADVANTAGE - The compressive force is applied on the opposite ends of the stack until the final compression force reaches the measured differential pressure, where the compressive force is greater than or equal to the high threshold force, thus enabling reduction of inhomogeneousness of power between the stacks of the fuel cells.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a stack of a fuel cell during a manufacturing process.    Stack (50)    Anode compartment (59a)    Cathode compartment (59b)    Fluid inlet (60)    Fluid outlet (62)
NOVELTY - Producing urea from any waste composition comprises (a) producing a synthesis gas comprising carbon monoxide, carbon dioxide and hydrogen by high-temperature treatment of waste in a reactor with oxygen, which is produced by a cryogenic air separation process; (b) reacting carbon monoxide contained in the synthesis gas with water to produce carbon dioxide and hydrogen and separating carbon dioxide from hydrogen; (c) reacting obtained hydrogen with nitrogen, which comes from the cryogenic air separation from the step (a) to form ammonia; and (d) reacting ammonia with carbon dioxide.    USE - Urea is useful as nitrogen-rich artificial fertilizer. No biological data given.    ADVANTAGE - The process provides urea in high yield and without any gaseous emissions e.g. carbon dioxide, hence ecofriendly.    DESCRIPTION OF DRAWING(S) - The figure shows a block diagram for producing urea (Drawing includes non-English language text).
NOVELTY - The reactor has a central process unit for monitoring and controlling other units and providing a displaying and operating interface. An inner surface of a cylindrical chamber sleeve and a surface of a spiraling separation fin are coated with catalyst particles for methane conversion. A thermal control unit controls temperature of a reactor assembly. A flow reactor adopts spiral air grooves. A circulation pump intakes gas from surrounding environment and feeds into the moisturizer unit through a bubbler. Reactor tubes are interconnected in serial and parallel through elbow tubes.    USE - Photocatalytic reactor for performing methane conversion for flammable and explosive gas e.g. methane in coal, oil and gas in energy industries i.e. trillion-dollar industries, and ethylene and acetylene in petrochemical industries.    ADVANTAGE - The reactor adopts a circulating mode, and has low manufacturing cost and time. The reactor allows larger interconnected pore networks to enhance accessibility of an inner surface to gas molecules and UV photons.    DETAILED DESCRIPTION - The reactor assembly is a photocatalytic reactor and an individual photocatalytic oxidation (PCO) system. The catalyst particles are selected from a group consisting of titanium dioxide, metal-ion doped titanium dioxide, tungsten trioxide or tungsten anhydride, nickel oxide, vanadium oxide/vanadium pentoxide, chromium monoxide or chromium oxide, ferrous oxide, copper oxide or cupric oxide, zinc oxide, metal-on-silica and silicates. INDEPENDENT CLAIMS are also included for the following:    (1) a methane conversion device    (2) a method for facilitating methane conversion.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a photocatalytic system.
NOVELTY - Photoreduction of molecules, involves illuminating a fluid sample comprising the molecules to be reduced and hydrogen surface-terminated diamond having a negative electron affinity with light comprising a wavelength that induces the emission of electrons from the diamond into the fluid sample, where the emitted electrons induce the reduction of the molecules to form a reduction product; and collecting the reduction product.    USE - For photoreduction of molecules (claimed).    ADVANTAGE - The method uses diamond having a negative electron affinity as a photocatalyst, that act as a solid-state electron emitter that is capable of inducing reductions without the need for reactants to adsorb onto its surface.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a reaction system for the photoreduction of molecules, comprising a reduction cell comprising a fluid sample comprising the molecules to be reduced and hydrogen surface-terminated diamond having a negative electron affinity; a light source configured to illuminate at least a portion of the reduction cell with light comprising a wavelength capable of inducing the emission of electrons from the diamond into the fluid sample to induce the reduction of the molecules to form a reduction product; and a reduction product collection cell configured to collect the reduction product emitted from the reduction cell.
NOVELTY - The lead wire connection structure has a laminated solid oxide fuel cell (1) is a chip-shaped element, which has a rectangular parallelepiped shape. An anode (2) and cathode (3) are laminated on the laminated solid oxide fuel cell through an electrolyte. The anode is exposed to a pair of surface, which is opposed by the chip shaped element. The cathode is exposed to another pair of surface. A terminal electrode (11) is electrically connected to the anode. Another terminal electrode (12) is connected to the cathode. A surface electrode (13) is connected with the former terminal electrode.    USE - Lead wire connection structure for laminated solid oxide fuel cell for producing electric power using a flame.    ADVANTAGE - The anode and cathode are laminated on the laminated solid oxide fuel cell through an electrolyte, and thus enables preventing disconnection of a lead wire by improving restrain property of connection unit, and enables improving service life of laminated solid oxide fuel cell module for making the lead wire connection of the laminated solid oxide fuel cell, and enables improving electric power generation efficiency by arranging partition units between solid electrolyte and adjacent solid electrolyte, and enables reducing manufacturing cost of lead wire connection structure by reducing number of lead wires.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a laminated solid oxide fuel cell.    Laminated solid oxide fuel cell (1)    Anode (2)    Cathode (3)    Terminal electrodes (11,12)    Surface electrode (13)
NOVELTY - The method comprises continuously cutting wood wool cables (4) into individual cable sections (10) by a cutting device (5), wetting an outer surface and end faces of the individual cable sections with a molten fuel, and cooling the individual cable sections wetted with the molten fuel, where the fuel is a slowly solidifying fuel. The individual cable sections are partially immersed with the molten fuel during the wetting step. The wetting step is carried out in a molten bath of the fuel. The individual cable sections are completely immersed in the molten bath by a transport device.    USE - The method is useful for producing firelighters (claimed) for solid fuels.    ADVANTAGE - The method enables reliable and economic production of the firelighters with high quality and productivity and less consumption of energy.    DETAILED DESCRIPTION - The method comprises continuously cutting wood wool cables (4) into individual cable sections (10) by a cutting device (5), wetting an outer surface and end faces of the individual cable sections with a molten fuel, and cooling the individual cable sections wetted with the molten fuel, where the fuel is a slowly solidifying fuel. The individual cable sections are partially immersed with the molten fuel during the wetting step. The wetting step is carried out in a molten bath of the fuel. The individual cable sections are completely immersed in the molten bath by a transport device. The wood wool cables are: directly guided to the cutting device by a clamping device that fixes the wood wool cables during the cutting step; and simultaneously cut by the cutting device, where each wood wool cables is associated with its own cable wool cutting blade.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic view of a device for producing firelighters.    Firelighters (2)    Feeding device (3)    Wood wool cables (4)    Cutting device (5)    Individual cable sections. (10)
NOVELTY - A hydrogen-producing catalyst comprises ammonia combustion active component and ammonia decomposition active component which does not form difficultly-reducible complex oxide even after processing at 850 degrees C in air atmosphere for 2 hours. When portion of ammonia in gas containing oxygen and ammonia is burnt, residual ammonia is decomposed to hydrogen and nitrogen, by using hydrogen-producing catalyst.    USE - Hydrogen-producing catalyst is used for auto thermal reformer for producing hydrogen (all claimed) used as fuel.    ADVANTAGE - The hydrogen is stably produced over a long period of time, using hydrogen-producing catalyst by decomposition of ammonia.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of hydrogen, which involves producing hydrogen from ammonia and oxygen, using hydrogen-producing catalyst.
NOVELTY - Nitrogen is separated from hydrocarbon gas containing methane as main component and nitrogen by using adsorption agent for nitrogen separation consisting of synthetic clinoptilolite which has strontium to ion exchange site.    USE - Nitrogen separation from hydrocarbon gas (claimed).    ADVANTAGE - Nitrogen in hydrocarbon gas can be separated and removed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for nitrogen separation apparatus containing adsorption agent for nitrogen separation consisting of synthetic clinoptilolite which has strontium to ion exchange site.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph of the relationship between methane concentration and elapsed time from gas introduction time with respect to space velocity. (Drawing includes non-English language text).
NOVELTY - The device comprises a composting area, formed by four side boundaries, a close off and a compost liquid drain, two side walls, a rear wall, where the side and rear walls are firmly mounted, and compost removal plates (4) that are releasably mounted at vertical supports (1) so that a composting space is limited on the underside by a perforated base (7) and is covered from above with a cover plate in an inclined arrangement. Discharge sheets are disposed in an inclined plane under the perforated base, where a leachate and a compost liquid are received from the composting area.    USE - The composting device is useful for the recycling of garden and household waste.    DETAILED DESCRIPTION - The device comprises a composting area, formed by four side boundaries, a close off and a compost liquid drain, two side walls, a rear wall, where the side and rear walls are firmly mounted, and compost removal plates (4) that are releasably mounted at vertical supports (1) so that a composting space is limited on the underside by a perforated base (7) and is covered from above with a cover plate in an inclined arrangement. Discharge sheets are disposed in an inclined plane under the perforated base, where a leachate and a compost liquid are received from the composting area and are passed into a collecting channel that is drained into a removable collection container. The compost removal plate is conically tapered towards the bottom. The cover plate is partially divided. The perforated base is a grating and/or an expanded metal or sieve construction. The side walls, the rear wall, the compost removal plates, the cover plate and the discharge sheets are made of non-putrescible plastic, and all other parts are protected against corrosion.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic front side view of a composting device.    Vertical supports (1)    Compost removal plates (4)    Perforated base (7)    Surface the installation site. (8)
NOVELTY - A cathode formation material of solid oxide fuel cell (50) comprises composite containing oxides of perovskite type.    USE - Cathode formation material for manufacturing solid oxide fuel cell (claimed).    ADVANTAGE - Electrode performance is outstanding, and durability and battery characteristics are improved.    DETAILED DESCRIPTION - A cathode formation material of solid oxide fuel cell (50) comprises composite containing oxides of perovskite type of formulae (La1- xSrx)(CoyFe1-y)O3-(delta) (1) and (La1-xSrx)(TiyFe1-y)O3-(delta) (2).    x,y=0.1-0.5; and    (delta)=value which becomes settled so that electric charge neutral condition may be satisfied.    INDEPENDENT CLAIMS are included for:    (1) solid oxide fuel cell comprising anode (10), solid electrolyte (20) and cathode (30) in which cathode is oxide of perovskite type of formulae (1) and (2); and    (2) manufacture of solid oxide fuel cell which involves preparing anode solid electrolyte laminated body which consists of anode and solid electrolyte formed on the anode, providing a material to surface at side of solid electrolyte of laminated body and forming cathode by baking laminated body to which material is provided.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the electric power generation system with solid oxide fuel cell (SOFC). (Drawing includes non-English language text).    Anode (10)    Solid electrolyte (20)    Cathode (30)    Junction part (40)    Solid oxide fuel cell (50)
NOVELTY - The biodegradable vegetable oil compound comprises 5-35% of terephthalic acid, 5-25% of polyethylene terephthalate, and 50-80% of glycolic base, glyceridic base or vegetable oil from any source. 2-30% of different types of soaps including calcium sulfonate, lithium sulfonate, and others Bentone (RTM: rheological additive).    USE - Biodegradable vegetable oil compound used for biodiesel.    ADVANTAGE - The biodegradable vegetable oil compound shows excellent lubricity than conventional base oil without having any toxic effect and good rust resistant property, meets all technical specifications required for any type of application, and can be converted into biodiesel biofuel after use through transesterification process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for obtaining vegetable biodegradable lubricant components in oil form, which involves:    (A) mixing polyethylene terephthalate with alcoholic base, preferably diethylene glycol, polyglycerol or propanetriol on a reaction catalyst for 2 hours at 226 degrees C; and    (B) mixing the obtained reaction mixture for 4 hours at 240 degrees C.
NOVELTY - Invention relates to the method of recycling solid domestic wastes (SDW) into fuel for furnaces of high-temperature synthesis of a cement clinker, including sorting of initial SDW so that at first such incombustible fractions such as batteries, stones, fragments of glass and faience, then secondary materials are extracted, including ferrous and non-ferrous metals. The remaining mass is previously ground to the fraction of 50-100 mm, dried to humidity of 5-10%, and then ground to the fraction of 8-10 mm. The ground raw materials are heated to 160-200 degrees C and exposed to thermoplastic extrusion to produce fuel pellets.    USE - Power engineering.    ADVANTAGE - Method makes it possible to increase physical and mechanical strength of RDF fuel, to eliminate water absorption due to capsulation of granules in process of their manufacturing, to prevent possibility of rotting and self-ignition, to reduce costs during storage and transportation, to reduce energy intensity of its production, to improve environment, also to reduce volume of SDW removed to SDW landfills, to eliminate capital costs for construction of plants for wastes management in connection with usage of equipment of existing cement production facilities.1 cl, 4 dwg
NOVELTY - Production of cerium sulfide pigment, involves: a) cloning of the genes involved in sulfide production i.e. dissimilatory sulfite reductase (dsrAB) in Escherichia coli BL21 (DE3) containing pT7-MAT1 expression vector; b) inducing the recombinant at A(600) value of 0.5 with isopropyl- beta -D-1-thiogalactopyranoside (IPTG) (0.05 mM) for 4 hours at 37 degrees C with 200 revolution per minute (rpm); c) treating the biomass with the acidic stock solution of cerium sulfate; and d) incubating the treated mixture at 55 degrees C for 5 days followed by drying the precipitate at 70 degrees C for 3 hours.    USE - For the production of cerium sulfide pigment (claimed) which is used for the coloration of plastics.    ADVANTAGE - The process is environment friendly as compared to conventional chemical processes which use very high temperature and/or pressure and environmentally constrained gases like carbon disulfide. The microbial method completely eliminates the use of high temperature, pressure and toxic chemicals such as carbon disulfide; and is cost effective and eco-friendly as compared to chemical method.
NOVELTY - A sustained-release fertilizer comprises nitrogen nitrification inhibitor, biological fermenting composite amino acid, soil modifying agent, active layered silicate, and composite microelement.    USE - As sustained-release fertilizer for crops (claimed).    ADVANTAGE - The sustained-release fertilizer reduces volatilization loss; stimulates plant root growth; can absorbs NH4+, K+ and improves air permeability of soil and water; improves the nutrient utilization rate and reduces the nitrogen loss; improves the validity of the nitrogen fertilizer; and increases the crop yield.
NOVELTY - (4-Fluoro-benzyl)-(2-piperazin-1-yl-ethyl)-amine (I) is new.    USE - For preparing medicine for preventing and treating diseases caused by fungal infection, and for treating cardiovascular disease (claimed), where the fungal infection is Candida albicans infection.    ADVANTAGE - The compound (I) shows minimal inhibiting concentration (MIC) value of 0.5-1 mg/ml; and is capable of inhibiting the growth of fungi. The preparation method of compound (I) is simple; and provides low cost and small pollution, which is good for energy saving and emission reduction under the condition of large-scale production and industrialization prospect.
NOVELTY - This utility model claims a kind of new biomass cracking furnace, comprising a furnace outer wall, between the inner wall of the hearth and grate, hearth, outer wall is poured with high temperature, fire grate is fixed on the lower end of the furnace end to the inner wall surface tangential with burnout air jet hole on the hearth outer wall, and the end is provided with two secondary wind nozzles of classification in the burnout air jet hole, the left and right two sides of the through near-wall air, a tangential spray cracking into the air. Slag by the fuel cracking method, this utility model can solve the problem that the hearth in the efficiency is not high, exhaust gas concentration is large, which is good for preventing furnace slag to realize the complete combustion of the biomass particles, improve cracking rate, reduce the emission of harmful gas.
NOVELTY - This utility model claims a straw gasification furnace, it can solve the problem of straw gasification furnace, using effect is not good and is not sanitary, and the bottom of the furnace body is equipped with air inlet pipe, the upper part is set at one end of the air inlet pipe in the furnace body is provided with a plurality of blowing holes, the upper part is set at one end of the air inlet pipe in the furnace body is provided with ash damper, the other end of the air inlet pipe outside of the furnace body is connected with the fan, the external part is connected with the first gas filter of the furnace body is connected with the first gas filter is connected with the second flue gas filter, second gas filter is connected with the upper part is connected with a tar filter, a tar filter is connected with the second oil filter, composed of a flue gas filtering device, the outer edge of the upper part are provided with six smoke filter, each flue gas filtering device of the second tar filter the smoke outlet through the pipeline is connected with the oven, each of the first gas filter through pipeline is connected with the blower, a furnace body is open type, novel and unique structure, convenient use, wide fuel source.
NOVELTY - And the utility model claims a biomass cracking method for accelerating chamber of a fuel cracking rate, comprising a furnace body, wherein a hearth in the furnace body, and the hearth arranged in the furnace body above the furnace cover, a hearth and a furnace body to form a cooling cavity, the inner wall of the hearth is provided with a tangential feeding port, the lower end is filled with air, the cooling cavity cooling air conveying pipe, a furnace body and a hearth surface is dust cleaning door, with a secondary air inlet pipe is set on the outer wall of the upper end of the furnace body, a secondary air inlet pipe are connected with the inner wall of the hearth, and the other end is connected with a cooling layer vent-pipe. Through said method, the utility model can solve the problem that the cracking chamber in the cracking is not completely discharged flue gas is not can make full use of the energy and environmental pollution caused by a problem faster fuel cracking rate, reduces the smoke discharge.
NOVELTY - This utility model claims a biomass fuel gas water sealing safety, comprising a base (1), an air inlet pipe (2), a bottom plate (4), a liquid level meter interface (5), a cylinder (6), a water feeding pipe (7), a liquid level meter (8), a cover plate (11), a pressure gauge joint (12), an air outlet pipe (13), the rims (15) and the lower rims (16), buoy (17), a hand hole pipe (20), wherein the cylinder body (6) is a cylinder, the cylinder body (6) is welded on one side of the air outlet pipe (13), the cylinder (6) at the lower part is provided with a hand hole (20), the air inlet pipe (2) is opening welding air inlet flange (3), an air inlet pipe (2) through the bottom plate (4) into the cylinder (6), the upper part, the air inlet pipe (2) is welded on the bottom plate (4), a bottom plate (4) is placed on the floating barrel (17). The biomass fuel gas water sealing safety, simple structure and reasonable design, high manufacture precision is safe and reliable.
NOVELTY - A kind of floating action for removing butane tower, which comprises removing butane tower main body, a feeding heater, air cooler, the tower top reflux tank, reflux pump and the tower bottom reboiler and the feeding heater is connected to the fourth tower main body internal space to the raw material into the internal space for reaction, the top of the fourth tower main body is connected with one end of the air cooler, the other end of the air cooler is connected to the tower top reflux tank, and the tower-top backflow tank is connected to the waste butylene removing boundary zone and the reflux pump, a reflux pump is also connected to the top of the fourth tower main body, the air cooler is further provided with the frequency converter, the utility model improves the quality of the product, a quantity is reduced to 838KG/H degrees centigrade from the original 1734KG/H degrees centigrade, saving a lot of money for the factory at the same time to ensure the quality of the product, reduces the labour intensity, stable system and ensure the quality of the target energy-saving.
NOVELTY - Producing empty palm fruit bunch fiber originated biomass comprises treating an empty palm fruit bunch fiber with acid, and obtaining the empty palm fruit bunch fiber originated biomass through alkali processing.    USE - The method is useful for producing an empty palm fruit bunch fiber originated biomass that is useful for preparing ethanol (all claimed).    ADVANTAGE - The method is capable of effectively producing the biomass with an increased cellulose content and reduced lignin component.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for saccharifying and fermenting an empty palm fruit bunch fiber originated biomass to prepare ethanol.    DESCRIPTION OF DRAWING(S) - The diagram shows a flow chart of a method for producing an empty palm fruit bunch fiber originated biomass (Drawing includes non-English language text).
NOVELTY - A phytase comprising a 467 amino acid sequence (SEQ ID NO: 1) fully defined in the specification, is new.    USE - As phytase. The engineered strain of A.niger is useful for producing phytase which is used as feed.    ADVANTAGE - The produced phytase enables to improve phosphorus absorption capacity, reduce phosphorus discharge, and increase breeding benefits, and is environmentally-friendly.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) nucleic acid molecule encoding the above-mentioned phytase comprising a 1404 base pair sequence (SEQ ID NO: 2) fully defined in the specification; and (2) engineered strain of Aspergillus niger (CCTCC NO: M2012502) capable of expressing phytase.
NOVELTY - A lucid ganoderma is artificially cultivated by inoculating liquid lucid ganoderma strain in solid culture medium to culture, and obtaining lucid ganoderma fruiting body.    USE - Method for artificial cultivation of lucid ganoderma (claimed).    ADVANTAGE - The method shortens developing period of lucid ganoderma, reduces mixed fungi pollution rate, has low production cost, is simple and convenient, and is more suitable for industrialized and standardized production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a lucid ganoderma solid culture base.
NOVELTY - The method involves providing an aerobic treatment system (12) for receiving a supply of wastewater (10). The microbial cells are ruptured to produce treated activated sludge (36) containing an increased liquid to solid ratio and an increased degradation potential in comparison to untreated sludge. The supply of treated activated sludge is conveyed to aerobic treatment system. The supply of treated activated sludge is degraded in the aerobic treatment system.    USE - Method for degrading sludge produced by treatment of wastewater derived from pulp mill.    ADVANTAGE - The need for sludge dewatering and disposal can be eliminated. The amount of nutrient additives required to sustain the aerobic wastewater treatment process can be reduced. The rate of accumulation of sludge-derived solids in the aerobic treatment system can be reduced. The cost and complexity of handling and disposal of sludge can be reduced or eliminated. The treated sludge can be used as nutrient source so that the need to add nitrogen and phosphate-based fertilizers to the wastewater treatment stream can be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a wastewater treatment system for treating wastewater derived from effluent supply.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram illustrating the process for degrading sludge produced by treatment of wastewater.    Wastewater (10)    Aerobic treatment system (12)    Anaerobic digester (24)    Sludge treatment unit (34)    Treated activated sludge (36)
NOVELTY - Performing advanced treatment of printing and dyeing wastewater, comprises reacting wastewater and magnetite/ferric oxide solid heterogeneous catalyst loaded in a multi-phase catalytic oxidation fluidized bed reactor, adding 30% hydrogen peroxide (oxidant) and ferrous sulfate (homogeneous reaction catalyst), illuminating, aerating, passing wastewater into a reaction tank for further reaction, adding polyacrylamide coagulant aid via the reaction tank back end, coagulating, passing wastewater into a sedimentation tank for sludge-water separation and discharging effluent at emission standards.    USE - The method is useful for performing advanced treatment of printing and dyeing wastewater (claimed).    ADVANTAGE - The method: adopts illumination and aeration processes to mobilize hydroxy ions from the reactor base with strong oxidation potential (more than 2.80 V), which ensures chain reaction of various active metals and oxidation of organic matter in wastewater; ensures development of water quality characteristics of non-biodegradable wastewater; and can achieve efficient removal of COD and chromaticity.
NOVELTY - A compound fertilizer is prepared by mixing livestock and poultry manure, garbage, leaves, rice husk, straw and weeds, crop straw and rapeseed cake, adding water, and uniformly stirring; adding composite microbial inoculum and fermenting; and adding nitrogenous fertilizer, uniformly stirring, granulating, and sieving.    USE - Method for preparing compound fertilizer (claimed).    ADVANTAGE - The fertilizer is environment-friendly and has low cost.    DETAILED DESCRIPTION - Preparation of compound fertilizer involves mixing livestock and poultry manure, garbage, leaves, rice husk, straw and weeds, crop straw and rapeseed cake, adding water, and uniformly stirring; adding composite microbial inoculum and fermenting at 38-42 degrees C for 8 days; and adding nitrogenous fertilizer, uniformly stirring, granulating, and sieving. The weight ratio of livestock and poultry manure, garbage, leaves, rice husk, straw and weeds, crop straw, rapeseed cake and nitrogenous fertilizer is 60-70:3-5:2-4:8-15:4-8:8-10:2-3:4-7, preferably 65:4:3:11:6:9:2:6. The composite microbial inoculum comprises 19.6 wt.% Azotobacter, 20.2 wt.% anaerobic bacteria, 18.9 wt.% Actinomycetes, 16.3 wt.% Lactobacillus, 22.9 wt.% microzyme, and 2.1 wt.% millet.
NOVELTY - A soil modifier comprises 50-80 pts. wt. mycelium, 20-40 pts. wt. protein residue and 2-10 pts. wt. organic acid mother liquor, where the soil modifier has pH of 2.5-4.0 and water content of less than or equal to 15%.    USE - The modifier is used for developing roots and adjusting pH of soil of agricultural crops such as blueberries.    ADVANTAGE - The modifier increases the organic matter content of soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of soil modifier comprising weighing mycelium, protein residue and organic acid mother liquor, mixing and stirring, putting into granulator, adding organic acid mother liquor granulating agent, adjusting pH to 2.5-4.0, drying until water content is less than or equal to 15% and packing.
NOVELTY - The equipment has combustion device (2) that is provided in lower portion of drying furnace (1) for drying organic waste. Fire chamber is installed in combustion device, for heating-up drying furnace. Fuel feeding input (12) is set in upper portion of combustion chamber (5), to feed the solid fuel into chamber. Blasting section (6) is installed at side of combustion device, to supply the air to fire chamber. Heater is installed within fire chamber. Transfer device is installed in fire chamber lower end portion so as to transfer the solid fuel in fire and eject the ash finally.    USE - Treatment equipment of organic waste such as livestock excretion and farming byproduct.    ADVANTAGE - The organic waste of many amounts can be dried to solid fuel with low calorie and the solid fuel like the pellet can be mass-produced. The cost of fuel can be reduced, as the organic waste is used as fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the treatment equipment of organic waste.    Drying furnace (1)    Combustion device (2)    Combustion chamber (5)    Blasting section (6)    Fuel feeding input (12)
NOVELTY - The process comprises crushing kitchen garbage, removing metal and plastic, placing the crushed garbage and waste oil in a sterilization boiler under a pressure of 0.5-0.7 MPa and then sterilizing for 30-60 minutes, eliminating bacteria and grease, separating the oil, adding the separated oil in methanol and catalyst to carry out alcoholysis reaction at a temperature of 250-260 degrees C and a pressure of 0.098 MPa to obtain crude methyl ester and then distilling and purifying to obtain biological diesel oil, and performing fermentation process at 70-80 degrees C for 7 days to obtain biogas.    USE - The process is useful for treating kitchen waste (claimed) to produce biogas and organic fertilizer.    ADVANTAGE - The process is capable of energy-efficiently and rapidly treating the kitchen waste in an environmentally friendly manner.
NOVELTY - Fertilizer degerming agent comprises (in wt.%): marine organism (10-15); seaweed polysaccharide (8-12); chitosan (5-8); garlic mucus (6-8); bighead Atractylodes rhizome (5-7); nevadensin (4-6); aloe juice (2-4); fish bone powder (4-6); eggshell powder (4-6); and purified water.    USE - The fertilizer degerming agent is useful for removing bacteria in aquatic ornamental flower.    ADVANTAGE - The degerming agent is in expensive, simple to prepare, environmental friendly, low in toxicity and free of harm to a human body, has high degerming rate of 99.99%, stable chemical properties and rich nutrient substances. The agent absorbs harmful substances, and has reduced consumption of pesticides.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the fertilizer degerming agent, comprising: cleaning, drying, crushing and extracting bighead atractylodes rhizome, Chlorophytum comosum and aloe to obtain plant active substance, adding water and plant active substance into a reaction kettle to dilute, slowly adding marine organism, polysaccharide and chitosan and water into the reaction kettle, washing and drying the garlic extract thick liquid, adding into the reaction kettle, uniformly stirring, adding fish bone powder, egg shell powder and water into the reaction kettle, heating the mixture at 30 degrees C to react for 15 minutes, and cooling and packaging the end product.
NOVELTY - The utility model claims a GPRS-based intelligent detection is the infrared gas sensor. It comprises a battery, a micro-controller chip, a GPRS module, an LED indicating lamp, a water level sensor, a methane sensor, the battery is respectively connected with a GPRS module, a microcontroller chip, an infrared gas sensor, a GPRS module connected with the microcontroller chip, a microcontroller chip is further connected with a gas sensor. The utility model combustion type sensor is replaced by catalytic for a gas sensor, thus improving detection can be applied to almost all kinds of gas and improves the practicability of the product. In addition, a infrared gas sensor with high precision, good selectivity, high reliability, no poisoning, does not depend on the oxygen environment interference factor is small, large dynamic range, fast response time and long service life and so on;
NOVELTY - This utility model claims a kind of automatic machine, which is suitable for a fertilizer station or a small mixing fertilizer factory fast for fertilizer, comprising a feeding hopper, stirrer, a lifting mechanism, a storage hopper and a weighing device, wherein the stirrer is installed on the lower part of the frame through the supporting wheel assembly, a vehicle frame is provided with a walking wheel, a stirrer is set at the side lifting frame, lifting hopper by the lifting mechanism is set on the lifting bracket to move up and down, is set with weighing mechanism is provided with the feeding port, discharge port and a stirring blade on the lower part of storage hopper lifting frame, the stirrer is below a stirrer roller assembly, a blender is installed with big gear ring so that the stirrer capable of rotating stirrer device is provided with high automation degree, uniform taing, energy-saving and environment-friendly, wide adaptability and so on.
NOVELTY - A kind of caking device, comprising a guide tube, a compressor, a sleeve, an oil groove, oil pipe and machine, the compressor passes through the conduit and the connecting machine is sleeved with the sleeve in the guide tube, the oil tank is connected with the front end of the machine by the envelope oil pipe. This utility model is convenient to make, low energy consumption and low cost of the chromatography.
NOVELTY - This utility model claims a kind of multi-level type reverse turning bed feeding device. The feeding device comprises a shell and a motor, a feeding port and a discharging port set on the shell, a motor through a motor seat fixed on the shell, and it is divided into a plurality of sealed cavity is composed of multiple reverse turning bed in the shell, each reverse turning bed fixed on each lower material cavity bottom, is provided with the output shaft of the motor in order to drive each block reverse turning bed rotating of the rotating mechanism by turning control mechanism, a rotating mechanism to rotate under the control of the motor and abutted with the control end of each reverse turning bed turning control mechanism. This utility model has simple structure, safe and stable, convenient, effectively prevent a reaction furnace (pit) high temperature gas reverse surge or air leakage phenomenon to achieve the continuous and quantitative feeding at regular time and can be suitable for matching utility is a kind of biomass reaction furnace, it has high practical value.
NOVELTY - This utility model claims a gasification furnace used for the sieving mechanism, comprising a gasification furnace of furnace body, the inside of the furnace body is provided with anaerobic combustion chamber, the inside of the furnace body is located at the bottom of anaerobic combustion chamber is set with a rotary round sieve. This utility model has simple structure, reasonable design, the vibration sieve is replaced by rotating the round sieve, reduces the damage rate of the screen, indirectly improves the working efficiency of the enterprise, meets the production requirement of the enterprise.
NOVELTY - A water electrolysis hydrogen-oxygen production device comprises inner shell having inner cavity filled with electrolyte; a hydrogen-oxygen generator sleeved on the inner shell; and an air duct housing in which the inner shell forms a cooling air channel. Top of the inner shell is provided with cavity for leading out hydrogen-oxygen gas and is communicated with a hydrogen-oxygen gas delivery tube. A negative electrode terminal is fixed in the cavity and sealed. The air duct housing is provided with air inlet and air outlet of cooling air channel and is arranged with a blower.    USE - Water electrolysis hydrogen-oxygen production device.    ADVANTAGE - The device has high water electrolysis efficiency, reduced volume, low manufacturing cost, low power consumption and low usage cost.
NOVELTY - The polar plate has an electrode plate (2) that is provided between two sides of a frame (1). Two end faces of the electrode plate are sealed with the frame by a gasket (3).    USE - Ultrathin polar plate.    ADVANTAGE - The Ultrathin polar plate is simple in structure and convenient in use. The ultrathin polar plate has low cost and low labor intensity.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the ultrathin polar plate.    Frame (1)    Electrode plate (2)    Gasket (3)
NOVELTY - Pyrolysis of biomass hydrogen-rich synthesis gas comprises fluidized bed pyrolysis of biomass and catalytic reforming. The fluidized bed cracking condition comprises protection of nitrogen at 450-550 degrees C and 0.01-0.08 MPa, and a mass ratio of biomass and vapor at 0.5-2:1. The obtained biological oil steam enters into microwave catalytic reforming under protection of nitrogen at 650-900 degrees C and normal pressure, with microwave frequency of 2400-2500 MHz.    USE - Method for pyrolysis of biomass hydrogen-rich synthesis gas (claimed).    ADVANTAGE - The method reduces energy consumption, and improves hydrogen and biomass production.
NOVELTY - A plant fertilizer comprises 10-20 g pulverized coal ash, 1-2 g magnesium chloride, 5-10 g egg shell powder, 5-10 g manure, 2-3 g ferrous sulfate, 5-10 g rice husk ash, 2-5 g urea, 1-2 g acrylic acid, 20-35 g rice straw residue, 0.1-0.2 g biological fermenting agent and 1-3 g polyacrylamide.    USE - The fertilizer is used for controlling land desertification, agricultural and forestry planting, landscaping and promoting plant growth.    ADVANTAGE - The fertilizer reduces the loss of soil water content and provides the necessary microelements for plant growth.
NOVELTY - Production of rose agricultural product comprises planting and culturing rose flower agricultural products using a biological organic fertilizer prepared by rose flower dregs in an adaptive phase and injecting a rose extract nutritional solution with high concentration in affinity phase.    USE - Method for production rose agricultural product (claimed).    ADVANTAGE - The method provides a special flavor of the original product and a special flavor and health care function of rose.    DETAILED DESCRIPTION - Production of rose agricultural product comprises using rose flower slag biological organic fertilizer to fertilize each year for a fruit kind of agricultural products, adding irrigation water in rose flower slag for preparing biological liquid fertilizer, carrying out homogenization treatment to make edible fungi, and injecting rose extract nutrient solution at the fruit of the crops while harvesting fruits front 10-15 days on each branch and the fruit of the handle base of 0.5-1 cm subcutaneous phloem tissue disposable injection fruit crops rose extract nutrient solution. The injection dosage is 0.1 mL. The fruit crops rose extract nutrient solution is prepared by diluting 10 g rose extract with water to 100 ml. For fungus product before harvesting, the edible mushrooms affinity period is for 3-5 days. The edible fungi rose extract nutrient solution is sprayed to the fungus, each day later each one time spraying. The edible bacteria rose extract nutrient solution is prepared by adding 1 g rose extract with water to 100 mL.
NOVELTY - Production of medlar agricultural product includes using biological organic fertilizer, injecting high affinity period of medlar extract nutrient solution, planting, and cultivating according to the fruit-type agricultural products and fungus agricultural products.    USE - Method for the production of medlar agricultural product (claimed).    ADVANTAGE - The method has the special flavor of the original product, and has special flavor and health care function of medlar.    DETAILED DESCRIPTION - Production of a medlar agricultural product comprises using medlar dregs biological organic fertilizer for fruit type agricultural products during planting, fertilizing each year, adding water for irrigation, adding medlar dregs to produce liquid bio-fertilizer, carrying out homogenization treatment to make edible fungi, cultivating, injecting the affinity period of medlar extract nutrient solution while harvesting fruits front 10-15 days on each branch and the fruit of the handle base of 0.5-1 cm under the skin toughness, injecting fruit crops medlar extract nutrient solution at 0.1 mL, and adding water to prepare medlar extract to extract the primary intermediate product from medlar. The fruit crops medlar extract nutrient solution is prepared by diluting 10g medlar extract in water to 100 ml. The edible mushroom is harvested for 3-5 days. Edible fungi medlar extract nutrient solution is uniformly sprayed every morning and night. It is prepared by adding 1 g medlar extract in water to 100 mL.
NOVELTY - The device has a limit rotating device with a fixing device and four vertical supporting bearing devices, where the fixing device is set on an upper part of a storage tank. A limit rotating device is set on a lower part of the storage tank. Four vertical supporting bearing device is set at two sides of the lower part of the storage tank. The fixing device comprises a supporting frame, an elastic plate and a hollow cylinder, where the supporting frame is fixed on an outer container. The elastic plate is fixed on the supporting frame. The cylinder is fixed on an inner container.    USE - Support device for a large vacuum heat insulating liquid hydrogen storage tank.    ADVANTAGE - The device can bearing weight of containing medium, change container working temperature free shrink, avoid generation of restriction, and withstand axial impact load by the fixing device.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a support device.
NOVELTY - Synthesis of vitamin B1 hydrochloride comprises processing vitamin B1 sulfate water solution by ion exchange resin, removing sulfate, concentrating, and crystallizing to obtain the product.    USE - Synthesis of vitamin B1 hydrochloride (claimed).    ADVANTAGE - The method does not use organic solvent, avoids the residual organic solvent in the product, saves hydrochloric acid gas, and reduces environmental pollution.
NOVELTY - An emulsified biodiesel comprises 80-90 wt.% biodiesel, 1-5 wt.% emulsifying agent, 5-15 wt.% crude glycerine and 4-14 wt.% water.    USE - Emulsified biodiesel (claimed).    ADVANTAGE - The emulsified biodiesel is economically and environmentally-friendly manufactured.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of emulsified biodiesel.
NOVELTY - Recycling cells using pH controlled alcoholic fermentation process comprises: culturing and recycling ethanol fermentation bacteria; utilizing the pH value to monitor an ending state of ethanol fermentation; and automatically controlling the operation of yeast recycling.    USE - The method is useful for recycling cells using a pH controlled alcoholic fermentation process (claimed) to prepare fuel ethanol.    ADVANTAGE - The method is capable of economically, rapidly and efficiently recycling cells using pH controlled alcoholic fermentation process and reducing the synthesis of lead to a substrate and improving the percent conversion of substrate to product.
NOVELTY - The biomass hydro-thermal preprocessing reactor has flange (5) which is screwed on bolt. A temperature sensor probe is inserted into test tube (12). A magnetic force stirring system is provided to drive stirring paddle (10). A fixing sleeve (2) is connected with lifting screw (17). The fixing sleeve is connected with lifting screw rod. The reaction kettle is integrally placed in oil bath. The oil barrel upper opening of reaction kettle is entered into oil bath. The water tank is located in reaction kettle. The fixing sleeve is connected with lifting screw rod.    USE - Biomass hydro-thermal preprocessing reactor used for corn straw, rice straw, wheat straw, beanstalk, sorghum, sweet sorghum, peanut shell, crop straw, alfalfa, king-grass, reed, wood chip, sawdust, small branch woody plant, silver grass, switch grass, and energy plant.    ADVANTAGE - The reactor can be adjustable in three stirring modes for processing different kinds of biomass, thus the practicability and treatment effect of reactor can be enhanced. By adopting dual-cooling and quick heating system, the time for reaching pretreatment reaction and the cooling time after the reaction ends can be effectively shortened, the occurrence of side reaction can be effectively reduced, and the pretreatment efficiency can be increased. The reactor can be flexible to operate. The kettle main portion and kettle cover can be lifted and lowered separately or in combined manner. The positions of the heating system and the cooling system of the reactor can be exchanged, thus the system safety and convenience in operation can be improved in efficient manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass hydro-thermal preprocessing reactor.    Fixing sleeve (2)    Flange (5)    Stirring paddle (10)    Test tube (12)    Lifting screw (17)
NOVELTY - In pyrolysis of carbonaceous material, catalytic heat carrier, is used, where the catalytic carrier is selected from thermal oxide and/or sulfide of transition metal, molecular sieve is used as the clay mineral, a transition metal containing ore, waste and/or tailing.    USE - In pyrolysis of carbonaceous material selected from coal, coal direct liquefaction residuals, heavy oil, biomass, carbonaceous industrial wastes and tailing, tar pitch, asphalt, oil sand, shale oil, coke, petroleum coke, synthetic plastic, synthetic polymers, waste tyre, municipal solid waste, and natural asphalt (claimed).    ADVANTAGE - The catalytic heat carrier exhibits catalytic activity, and oxygen and/or hydrogen transfer capacity so as to obtain solid, gas and liquid product. The method for pyrolysis of carbonaceous material is environment-friendly and low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of catalytic heat carrier particles, involving: a) crushing and/or grinding catalytic heat carrier material to fine powder particle diameter of 5-50 microns of; b) mixing fine powder obtained in the step a) and inorganic adhesive agent to obtain the uniform mixture slurry; and c) spray-drying the mixture slurry, a catalytic heat carrier particle.
NOVELTY - A high-temperature-resistant synthetic natural gas methanation catalyst comprises 15-60% active components, 30-70% carrier and 3-20% auxiliary agent. The active components are 12-50 %mass nickel oxide, 2-8 %mass chromium oxide and 2-8 %mass molybdenum oxide. The carrier is alumina, zirconia, titania and silica. The auxiliary agent is lanthanum oxide, cerium oxide, neodymium oxide and samarium oxide as rare-earth metals and magnesium oxide, calcium oxide, strontium oxide and barium oxide as alkaline-earth metals.    USE - High-temperature-resistant synthetic natural gas methanation catalyst (claimed).    ADVANTAGE - The catalyst has high activity, selectivity, high-temperature stability, and workability for long time at high temperature and high pressure.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of catalyst, which involves preparing active components of precipitate using soluble salt solution of active components and precipitator, preparing high-temperature carrier by high-temperature heating, uniformly mixing the active components, carrier and auxiliary agent, forming by tabletting and calcining.
NOVELTY - Methanation furnace comprises a synthesis gas inlet located on left and right sides of the furnace, a catalyst bed layer, and a methane gas outlet located at the bottom of the furnace. The center part of the methanation furnace is provided with a gas collector central pipe. The bottom of the gas collector central pipe is connected to a methane gas outlet. The outer diameter of the gas collector center tube is provided with the catalyst bed layer. The outer radial part of the catalyst bed layer is provided with a gas distributor. The gas distributor is connected with a synthesis gas inlet.    USE - The furnace is useful for producing methane using coal synthesis gas (claimed).    ADVANTAGE - The furnace has good cooling effect, controllable reaction temperature, and high industrial application value.
NOVELTY - Organic fertilizer bar buttress-type aerobic fermentation air pipe comprises vent holes at its pipe wall. The air pipe is circular in shape and made of PVC material and adopts snake-shaped connection.    USE - Used as an organic fertilizer bar buttress-type aerobic fermentation air pipe.    ADVANTAGE - The air pipe ensures oxygen supply and moisture loss during aerobic fermentation stage of the organic fertilizer, shortens the aerobic fermentation period, and is economical and simple in structure.
NOVELTY - A combined type biomass briquette comprises 70-74 wt.% eucalyptus bark powder, 24-30 wt.% bamboo bran and 2-3 wt.% calcium oxide powder.    USE - Combined type biomass briquette.    ADVANTAGE - The briquette has improved fuel heat value and reduced pure bamboo bran.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the briquette comprising milling eucalypt bark and bamboo bran calcium oxide powder and processing, uniformly mixing, and using extrusion molding machine extrusion device.
NOVELTY - Preparing microbial fertilizer coating agent, comprises mixing 10-60 of wt.% of curing agent, grease, surface active agent and microbial culture, melting the mixture at 30-65 degrees C with a density range of 0.7-1.2 g/cm3, adding mixture of higher alkane and 5-15 wt.% of film forming agent into the melted mixture.    USE - The method is useful for preparing microbial fertilizer coating agent (claimed).    ADVANTAGE - The method is capable of preparing microbial fertilizer coating agent in an environmental-friendly manner.    DETAILED DESCRIPTION - Preparing microbial fertilizer coating agent, comprises mixing 10-60 of wt.% of curing agent, grease, surface active agent and microbial culture, melting the mixture at 30-65 degrees C with a density range of 0.7-1.2 g/cm3, adding mixture of higher alkane and 5-15 wt.% of film forming agent into the melted mixture, where: the grease is animal oil, plant oil or petroleum extract, the coating agent is present in an amount of 35-75 (preferably 3-6) wt.%; the surface active agent is normal non-ionic surface active agent; the microbial culture is Bacillus subtilis, Azotobacter, Actinomycetes, Yeasts or filamentous fungi formation of vegetative cells, and has a concentration of 10-500 billion of bacteria/g; and the film forming agent is present in an amount of 10-55 wt.%.
NOVELTY - The method involves entering first gas into heating regeneration of rotating furnace gas variable temperature adsorber (1). Other gas is entered into coke-oven gas heating regeneration absorber (3). Two gases are mixed, and mixed gases are heated through a heater (6). Mixed gasses are entered in to regenerative coke-oven gas pre-purifying absorber, and gas is regenerated by cooler (7) and fuel gas pipe network.    USE - Method for utilizing absorption regeneration heat of coke-oven gas and transfer furnace gas for preparing methanol.    ADVANTAGE - Adsorbent regeneration heat can be effectively utilized with save energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the process for utilizing absorption regeneration heat of coke-oven gas and transfer furnace gas for preparing methanol. (Drawing includes non-English language text)    Rotating furnace gas variable temperature adsorber (1)    Coke-oven gas heating regeneration absorber (3)    Heater (6)    Cooler (7)    Gas pipelines (8-15)
NOVELTY - Europium oxide-cobalt oxide-zirconium oxide composite catalyst (I), is new. The molar ratio of cobalt and zirconium is 4:6, and the amount of the rare earth europium is 1-10% of the total mass of cobalt and zirconium.    USE - (I) is useful for synthesizing methane by carbon dioxide hydrogenation (claimed).    ADVANTAGE - (I) has excellent catalytic performance. The method is simple, fast and consistent, meets the requirements of green chemical principle, and achieves industrialized production.    DETAILED DESCRIPTION - Europium oxide-cobalt oxide-zirconium oxide composite catalyst of formula (Eu2O3-Co3O4-ZrO2) (I), is new. The molar ratio of cobalt and zirconium is 4:6, and the amount of the rare earth europium is 1-10% of the total mass of cobalt and zirconium. An INDEPENDENT CLAIM is also included for preparing I.
NOVELTY - The component has level grid layer that is composed of multiple component units arranged in parallel. Each component unit is arranged according to interlaced guide plate and baffle plate. The guide plate is welded on a baffle plate, and two guide plates are provided opposite to adjacent component unit of guide plate. Adjacent component unit of guide plate is arranged opposite to upper and lowers adjacent two layers of level grids corresponding to guide plate. Clapboard is vertically set, whose height is 2-30 mm. Height of guide plate is 1-1.5 mm, and width of guide plate is 2-40 mm.    USE - Component of fluidized bed reactor for synthesizing natural gas produced methane.    ADVANTAGE - Contact effect between gas-solid two phases can be increased, so as to greatly enhance the mass transfer and heat transfer effect performance of air.
NOVELTY - Microbial liquid composition comprises Pseudomonas YT3, Saccharomyces cerevisiae and Lactobacillus casei.    USE - The microbial liquid composition is useful for promoting cherry plant growth and preparing bio-organic fertilizer (all claimed).    ADVANTAGE - The composition reduces dehiscent fruit, improves yield and water logging resistance of the sweet cherry plant. The bioorganic fertilizer can improve water logging resistance of the sweet cherry.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) method (M1) for preparing microbial agent, involves mixing the microbial liquid composition and auxiliary stabilizer in a weight ratio of 100:(4-7), where the colony forming unit (CFU) ratio of Pseudomonas YT3, S.cerevisiae and L.casei is 10:2-3:2-3; and (2) bio-organic fertilizer involves mixing the above-mentioned composition with organic fertilizer in the ratio of 10:2 weight/volume.
NOVELTY - An alcoholized oil kitchen fuel comprises 90 wt.% methanol or ethanol, 6 wt.% biological diesel oil, 3 wt.% cosolvent, 0.8 wt.% heat value enhancing agent, 0.2 wt.% combustion accelerant, and 0.1 wt.% aerator.    USE - Alcoholized oil kitchen fuel.    ADVANTAGE - The fuel has high heat value, simple preparation, and low volatility; is easier to degrade; is environment-friendly and safe; exhibits complete combustion; reduces discharge of harmful substance; and has no toxic and side effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fuel by providing above raw components, putting into kettle, and uniformly stirring.
NOVELTY - A main frame comprises a frame main body (1) with a central hole (2) where the rear section is provided with a circular groove (3) connected to the central hole.    USE - Main frame of water hydrolysis apparatus for hydrogen production.    ADVANTAGE - The electrolysis groove length is shortened and is light, thus reducing the assembling difficulty, saving material and reducing cost.    DESCRIPTION OF DRAWING(S) - The drawing is a cross section of the frame.    Frame (1)    Central hole (2)    Circular groove (3)
NOVELTY - Improving quality and enhancing aroma of upper leaves of flue-cured tobacco, comprises adding 800-1000 kg decomposed farmyard manure as base fertilizer per acre based on traditional tobacco ridging-fertilizing process, harvesting tobacco middle part leaves, spraying foliar fertilizer on both sides of upper part leaves, and delaying normal maturation harvesting time for 4-9 days and completely harvesting at once, where decomposed farmyard manure is prepared by adding cake fertilizer, phosphate fertilizer and quick lime to farmyard manure, stirring and performing stacking fermentation.    USE - The method is useful for improving quality and enhancing aroma of upper leaves of flue-cured tobacco (claimed).    ADVANTAGE - The method is simple, and improves the use value and usability of the components of tobacco upper part leaves.    DETAILED DESCRIPTION - Improving quality and enhancing aroma of upper leaves of flue-cured tobacco, comprises adding 800-1000 kg decomposed farmyard manure as a base fertilizer per acre based on the traditional tobacco ridging-fertilizing process, harvesting tobacco middle part leaves, uniformly spraying foliar fertilizer on both sides of the upper part leaves, and delaying the normal maturation harvesting time for 4-9 days and completely harvesting at once, where the decomposed farmyard manure is prepared by adding 2.5-5 kg cake fertilizer, 0.4-0.6 kg phosphate fertilizer and 0.2-0.4 kg quick lime to 100 kg farmyard manure, uniformly stirring and performing stacking fermentation; and the foliar fertilizer comprises 15-45 wt.% borax, 15-45 wt.% zinc sulfate, 15-45 wt.% manganese sulfate, 3-12 wt.% sodium molybdate, 1.5-4.5 wt.% copper sulfate and 0-0.001 wt.% jasmonic acid.
NOVELTY - Method for extracting flavonoid compound from camphor tree, involves (a) obtaining branches of camphor tree, drying and crushing the branches, performing shaking extraction using organic solvent, filtering the extract, and concentrating the filtrate to obtain crude extract, (b) dissolving the crude extract using distilled water, performing extraction, and collecting extract, and (c) concentrating the obtained extract, drying the concentrate, performing purification using silica column, eluting the column using mixed solution, and collecting the eluate.    USE - The method is useful for extracting flavonoid compound from camphor tree, where the flavonoid compound is used as fungicide for plants for controlling wheat root rot, corn leaf blight, Fusarium wilt of cotton, Fusarium wilt of watermelon, and early blight of tomato (all claimed).    ADVANTAGE - The method is simple and convenient to perform, saves energy, and provides high extraction rate.    DETAILED DESCRIPTION - Method for extracting flavonoid compound from camphor tree, involves (a) obtaining branches of camphor tree, drying and crushing the branches at room temperature, performing shaking extraction using organic solvent, filtering the extract, and concentrating the filtrate to obtain crude extract, (b) dissolving the crude extract using proper amount of distilled water, performing extraction using ethyl acetate, where the volume ratio of distilled water and ethyl acetate is 1:1, and collecting extract, and (c) concentrating the extract obtained in the step (b), drying the concentrate, performing purification using silica column, eluting the column using mixed solution of chloroform and acetone, where the volume ratio of the chloroform and acetone is 20:1, and collecting the eluate to obtain flavonoid compound.
NOVELTY - Production of compost involves mixing one or more of dewatered sludge, waste lees and silica gel sludge which are discharged through beer production, determining pH of the resultant materials to 7-7.5, regulating water content to 55-60%, adding the resultant materials into a compost reactor, feeding air into reactor, stacking for 13-17 days to finish the composting under aerobic state, detecting pH, temperature, oxygen uptake rate and humification coefficient of the stack, measuring content of elements of the resultant end product compost, screening, stabilizing, grinding and drying.    USE - Production of compost (claimed).    ADVANTAGE - The method economically provides compost, by a simple process without environmental pollution.    DETAILED DESCRIPTION - Production of compost involves mixing one or more of dewatered sludge, waste lees and silica gel sludge which are discharged through beer production, determining pH of the resultant materials to 7-7.5, regulating water content to 55-60%, obtaining mixed material, adding the resultant mixed material into a compost reactor, continuously feeding air into the reactor, stacking for 13-17 days to finish the composting under aerobic state, turning the stack once every 2-3 days, detecting pH, temperature, oxygen uptake rate and humification coefficient of the stack, measuring content of elements of the resultant end product compost, screening, stabilizing, grinding, drying, and directly applying the resultant material to organic fertilizer or organic or inorganic compound fertilizer.
NOVELTY - Preparing lipase inhibitor comprises fermenting Streptomyces lipstatin producing strain mycelium, and then suspending in an extracting agent to clean, carrying out microbial cell crushing to obtain mixture of lipstatin containing extracting liquid and simvastatin, centrifuging the lipstatin mixture to collect supernatant fluid, decompressing and concentrating the supernatant to obtain lipstatin crude product, introducing the lipstatin crude product in a solvent and then carrying out catalytic hydrogenation under the action of catalyst palladium.    USE - The method is useful for preparing lipase inhibitor (claimed).    ADVANTAGE - The method simply, economically and rapidly prepares the lipase inhibitor reagent without pollution and with high yield.    DETAILED DESCRIPTION - Preparing lipase inhibitor comprises (1) fermenting Streptomyces lipstatin producing strain mycelium, and then (2) suspending in an extracting agent having pH value of 4-9, to clean, carrying out microbial cell crushing to obtain mixture of lipstatin containing extracting liquid and simvastatin, (3) centrifuging the lipstatin mixture to collect supernatant fluid, (4) decompressing and concentrating the supernatant to obtain lipstatin crude product, introducing the lipstatin crude product in a solvent, (5) carrying out catalytic hydrogenation under the action of catalyst palladium to obtain orlistat, (6) recrystallizing the orlistat to obtain orlistat crude product, and (7) dissolving the orlistat crude product in the solvent to absorb by macroporous resin for 2-5 hours, adding two eluents with the orlistat to carry out gradient elution and then condensing and drying.
NOVELTY - Preparing sustained release pellet, comprises uniformly covering the sustained release micro-pill by venlafaxine hydrochloride and medicine-containing layer on a release film, where the medicine-containing layer comprises hydrochloric acid and talcum powder, the weight ratio of the: hydrochloric acid and talcum powder is 12:1-8:1 and venlafaxine hydrochloride and sustained release micro-pill is 4:10-8:10; sustained-release film comprises slow release material; and content of the sustained release micro-pill is 4-12%.    USE - The method is useful for preparing sustained release micro-pill (claimed).    ADVANTAGE - The method reduces the venlafaxine hydrochloride in a presence of aqueous solution so as to improve the medicine speed, and economically and eco-friendly produces the micro-pill at high yield and low oxicity and good stability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing sustained release pellet comprising (a) adding venlafaxine hydrochloride with ethanol water solution (50-95%) to prepare saturated solution or supersaturated suspension, and adding talcum powder in the solution and then stirring, spraying the drug-containing solution on the sustained release micro-pill, where the drug containing solution comprises hydrochloric acid, talcum powder and ethanol water solution, where the spraying process is carried out at an air inlet temperature of 50-65 degrees C, material temperature of 40-50 degrees C and speed of 50 revolutions per minute (rpm), fan frequency of 25 Hz and atomizing pressure of 0.14 Mpa, and (b) spraying the prepared slow release coating liquid and ethanol aqueous solution to prepare slow release micropill preparation, where the process is carried out at an air inlet temperature of 45-55 degrees C, material temperature of 35-45 degrees C and a speed of 65 rpm, fan frequency of 25 Hz, and atomizing pressure of 0.12 Mpa.
NOVELTY - Sewage treatment system comprises mixing crusher, humic substance device, biogas purifier, biogas storage tank, solid-liquid separator, purifier, dryer and catalyst.    USE - The system is used for treating sewage containing feces (claimed).    ADVANTAGE - The system is economical and resource-saving.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for treatment of sewage using the treatment system comprising catalyzing, solid-liquid separating, purifying to prepare liquid biological fulvic acid and drying to prepare solid biological fulvic acid.
NOVELTY - Producing organic and inorganic compound fertilizer by lignin (30-30 pts. wt.), nitrogen, phosphorus potassium fertilizer (50-60 pts. wt.), composite microbial inoculum (0.2-0.5 pts. wt.), concentrated sulfuric acid (3-5 pts. wt.), liquid ammonia (2.5-3.5 pts. wt.) and bonding agent (5-15 pts. wt.), is claimed.    USE - The method is useful for producing organic and inorganic compound fertilizer (claimed), which is useful for improving growth of crops.
NOVELTY - Refrigerant comprises 10 wt.% trifluoroiodomethane, 20-40 wt.% 1,1-difluoroethane and 50-75 wt.% propane.    USE - Used as refrigerant.    ADVANTAGE - The refrigerant is non-combustible, and has good oil solubility, good explosion suppression effect and improved cooling effect.
NOVELTY - Biomass particle fuel comprises 80-95 pts. wt. tobacco waste leaf, 0.20-10 pts. wt. potassium permanganate, 0.30-15 pts. wt. sodium hydroxide, 0.30-15 pts. wt. lime, 1.0-8.0 pts. wt. coal, and 0.2-5.0 pts. wt. grease.    USE - Biomass particle fuel.    ADVANTAGE - The biomass particle fuel is produced without producing wastewater and waste gas, thus solving environmental pollution problem of tobacco leaf waste incineration process. It has good ignition performance, large heat productivity, can replace raw coal into boiler for burning, and produces environment friendly clean energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biomass particle fuel by crushing tobacco waste leaf into powder with grain diameter of 20 mm; respectively adding potassium permanganate, sodium hydroxide, lime, coal powder, and grease; uniformly stirring to obtain mixture; putting mixture in fermenting marsh gas tank for stack fermentation, in which stacking height of mixture is 2-3 meter; extruding fermented mixture into cylindrical particles; cutting into desired length; discharging particles; and drying particles at 90-110 degrees C until moisture content of granules is 5-15% to obtain biomass particle fuel.
NOVELTY - Preparation of refuse-derived fuel comprises subjecting generated household garbage malodorous gas through filtering adsorption and biodegradation; sterilizing biological filter material to remove toxic and harmful gases; screening non-combustible material; drying at 100-160 degrees C to reduce moisture content of biological material to less than 20%; recycling metal material; adding preservative, binder and chlorine agent; and crushing and mixing biological filter material with domestic waste compost product, wood chips, and rice straw or husk.    USE - Preparation of refuse-derived fuel.    ADVANTAGE - The method is simple and does not require crushing and sorting. It provides product with stable quality, high heat value, and good combustion performance. It achieves efficient removal of malodorous gases, thus reducing secondary pollution emissions while achieving waste reduction and resource utilization.    DETAILED DESCRIPTION - Preparation of refuse-derived fuel comprises putting generated household garbage malodorous gas into regeneration tank, washing tower and double biological filter tank to undergo combined action of filtering adsorption and biodegradation; sterilizing biological filter material to remove toxic and harmful gases; screening non-combustible material; drying at 100-160 degrees C to reduce moisture content of biological material to less than 20%; recycling metal material through magnetic separation; adding preservative, binder and chlorine agent; and crushing and mixing biological filter material with domestic waste compost product, wood chips, and rice straw or husk at weight ratio of (0.5:1:2)-(10:1:0.5).    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a process for preparing refuse-derived fuel (Drawing includes non-English language text).
NOVELTY - An Aspergillus flavus (CGMCC No. 4292), is new.    USE - The A.flavus is useful for decoloring wastewater from molasses based distillery (claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) screening and isolating A.flavus; and (2) method of decoloring wastewater from molasses based distillery, involves (a) diluting the wastewater until the absorbency value at 475 nm (A475) reaches 3.5, (b) mixing the diluted wastewater with culture medium, (c) inoculating spore suspension of A.flavus in the culture medium and performing decoloration process, (d) filtering and separating the cells, and (e) calculating decolorization rate by measuring absorbance at 475 nm.
NOVELTY - Acidic and alkaline ionic water are prepared, and biomass is pretreated by contacting with acidic and alkaline ionic water sequentially in any order.    USE - Pretreatment of biomass e.g. cellulose, hemicelullose and lignin (all claimed).    ADVANTAGE - The method enables economical and environmentally-friendly pretreatment of biomass without enzyme hydrolysis inhibitor production.
NOVELTY - Biological composite diesel oil contains diesel oil e.g. refined diesel oil or national standard diesel oil of any label, methanol which is greater than or equal to 99% of industrial methanol, industrial vegetable oil with 0.89-0.955 density, and additive which is complexing agent e.g. non-ionic surfactant and surfactant.    USE - A biological composite diesel (claimed).    ADVANTAGE - Biological composite diesel oil solves alternative energy issues, reduces emissions, is environment-friendly, and reduces fuel cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biological composite diesel oil which involves adding and stirring uniformly 65 pts. wt. diesel oil and 30 pts. wt. industrial methanol and 10 pts. wt. vegetable oil, 0.3 pts. wt. S-80, 0.1 pts. wt. T-80, 0.1 pts. wt. OP-10, 0.3 pts. wt. n-butanol, 0.2 pts. wt. isobutyl alcohol, 0.3 pts. wt. isopropyl alcohol, 0.1 pts. wt. ethyl acetate, 0.1 pts. wt. triethanolamine, 1-5 pts. wt. oleic acid, 0.1-0.5 pts. wt. 2-ethyl hexyl nitrate ester, and 0.1-0.5 pts. wt. fatty acid alkanolamide.
NOVELTY - Preparation of xanthohumol involves crushing European hop spike material, warm-soaking crushed hop material in 5-10 times amount of 50-70% ethanol, extracting 2-3 times, recovering ethanol in an obtained extraction liquid, filtering obtained extraction liquid in an ultrafiltration membrane system, concentrating a permeate in a nanofiltration membrane system, absorbing obtained concentrate using polyamide resin, eluting using ethanol, concentrating obtained elution liquid, refluxing and dissolving dehydrated ethanol, refrigeration-crystallizing, and drying obtained crystal.    USE - Preparation of xanthohumol used in production of foodstuffs and medicines.    ADVANTAGE - The method enables safe preparation of xanthohumol with high quality and low energy consumption by simple and environmentally-friendly process.    DETAILED DESCRIPTION - Preparation of xanthohumol involves crushing European hop spike material, warm-soaking crushed hop material in 5-10 times amount of 50-70% ethanol, extracting 2-3 times, recovering ethanol in an obtained extraction liquid, filtering obtained extraction liquid in an ultrafiltration membrane system, concentrating a permeate in a nanofiltration membrane system, absorbing obtained concentrate using polyamide resin, eluting using 5-8 times amount of 15-25% ethanol, concentrating obtained elution liquid, refluxing and dissolving dehydrated ethanol, refrigeration-crystallizing, and drying obtained crystal.
NOVELTY - Forming saponin from rhizoma bolbostemmae involves: crushing rhizoma bolbostemmae dry bulb stem into rough powder, adding methanol, followed by extracting/filtering/combining/decompressing/concentrating to obtain crude extract; adding water into crude extract, extracting by methylene dichloride solution, extracting water layer by water saturated n-butyl alcohol, separating n-butanol layer, decompressing/recycling n-butyl alcohol to obtain saponin; adjusting pH of saponin, performing heat preservation enzymolysis using bio-enzyme, then reacting with cyclohexane and recrystallizing.    USE - For the preparation of saponin from rhizoma bolbostemmae (claimed).    ADVANTAGE - The present method avoids use of column chromatography, and is simple process; utilizes organic solvent again and again; and has low energy consumption with mild reaction condition.    DETAILED DESCRIPTION - Preparing saponin from rhizoma bolbostemmae involves: crushing rhizoma bolbostemmae dry bulb stem into rough powder, adding methanol at room temperature and extracting, filtering and repeating the operations for 2-3 times, combining the filtrate, decompressing and concentrating the filtrate to extract to obtain crude extract of rhizoma bolbostemmae; adding small amount of water into rhizoma bolbostemmae extract, extracting by methylene dichloride solution, taking water layer and the dichloromethane layer, extracting water layer by water saturated n-butyl alcohol, separating the upper layer, that is, normal butanol layer, decompressing and recycling the n-butyl alcohol to obtain saponin; adjusting pH of the obtained saponin to 4.5-5.5, adding bio-enzyme and performing heat preservation enzymolysis for 15-24 hours, decompressing and concentrating the extracting solution, centrifuging to obtain crude product; and reacting the crude product with cyclohexane and heating to dissolve, recycling the reagent, then using methylene dichloride methanol recrystallization, filtering and drying.
NOVELTY - A compound treatment system comprises wastewater vertical-flow constructed wetland, a phosphorus removal membrane bioreactor unit, a wastewater horizontal-flow constructed wetland, a compound nitrogen and phosphorus removal unit, a carbon source improvement unit, a reaction tank unit, chlorinated tank, primary sedimentation tank, secondary sedimentation tank and a reservoir.    USE - Compound treatment system is used as agricultural fertilizer.    ADVANTAGE - The compound treatment system is economically processed without polluting the environment.    DETAILED DESCRIPTION - A compound treatment system comprises wastewater vertical-flow constructed wetland, a phosphorus removal membrane bioreactor unit, a wastewater horizontal-flow constructed wetland, a compound nitrogen and phosphorus removal unit, a carbon source improvement unit, a reaction tank unit, chlorinated tank, primary sedimentation tank, secondary sedimentation tank and a reservoir. The horizontal bottom wetlands uses the cement concrete ponds. The cement concrete ponds are provided on the bottom side of pipe and connected to the primary precipitation tank and a reaction tank. Reactor is provided through a pipe connected to a secondary sedimentation tank, and secondary sedimentation tank is connected to the chlorinated tank. An INDEPENDENT CLAIM is included for processing of compound treatment system.
NOVELTY - A multi-layered structure of large particles slow-release fertilizer comprises granular fertilizer (1), sulfur coating (2) and fertilizer coating (3).    USE - A multi-layered structure of large particles slow-release fertilizer.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparation of granular fertilizer comprising: melting 40-90 pts. wt. urea, adding 0-50 pts. wt. humic acid or 150-300 mesh weathered coal, adding 0-8 pts. wt. sodium hydroxide, stirring at 110-130 degrees C for 10-30 minutes, adding 0-30 pts. wt. monoammonium phosphate, adding 0-30 pts. wt. potassium chloride or potassium sulfate, adding 0-30 pts. wt. ammonium nitrate, adding 0-30 pts. wt. ammonium sulfate, stirring at 110-130 degrees C, pouring in infusion machine and forming in 2.5-12 cm spherical mold and cooling;    (2) composition of fertilizer coating comprising: 40-90 pts. wt. urea, 0-50 pts. wt. monoammonium phosphate and 0-50 pts. wt. potassium chloride or potassium sulfate;    (3) preparation of fertilizer coating comprising: melting urea, adding monoammonium phosphate, adding potassium chloride or potassium sulfate, adding ammonium nitrate, ammonium sulfate and trace elements, and stirring uniformly; and    (4) heating box.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of multi-layered structure of large particles slow-release fertilizer.    Granular fertilizer (1)    Sulfur coating (2)    Fertilizer coating (3)
NOVELTY - A crop fertilizer comprises: 40-50 pts. wt. urea, 20-30 pts. wt. calcium phosphate, 20-30 pts. wt. potash, 10-15 pts. wt. zinc sulfate, 5-10 pts. wt. magnesium sulfate, 2-5 pts. wt. borax, 2-5 pts. wt. ferrous sulfate, 15-20 pts. wt. feathers, 4-6 pts. wt. carboxymethyl cellulose, 20-25 pts. wt. 35% sulfuric acid, 5-10 pts. wt. lime, 2-5 pts. wt. Celastrus angulatus, 2-5 pts. wt. sanguinarine and 2-5 pts. wt. azadirachtin.    USE - A crop fertilizer for treating crop foliar diseases (claimed) is also used for controlling rotting of sweet potato, and treating corn roll heart disease, tip dry corn diseases, maize streak mosaic virus, cotton mosaic disease, legumes yellow leaf dwarf disease and red rice blight.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of crop fertilizer comprising: hydrolyzing feather with sulfuric acid for 8-10 hours to obtain amino acid, adding lime, carboxymethyl cellulose, zinc sulfate magnesium sulfate, borax and ferrous sulfate to generate amino acid chelate; and mixing urea, calcium phosphate and potash to obtain mixed fertilizers; mixing mixed fertilizers, Celastrus angulatus, sanguinarine, azadirachtin and amino acid chelate, and stirring.
NOVELTY - A fuel generating system comprises separating and filtering unit (1) for receiving high temperature waste gas to pipeline in which carbon dioxide in high temperature waste gas and water vapor are separated, generating unit (3) which is set on pipeline, pipe (2) where high temperature waste gas flow through, and 1st reaction unit (4) to receive carbon dioxide and water vapor and uses electric power to tranform carbon dioxide and water vapor into fuel.    USE - A fuel generating system for power plant operation (claimed).    ADVANTAGE - Additional energy is not required, and discharge of waste gas is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel generation method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a fuel generating system. (Drawing includes non-English language text).    Separating and filtering unit (1)    Pipe (2)    Generating unit (3)    Reaction unit (4)    Multi-stage heat exchange element (31)
NOVELTY - Preparation of tiopronin involves reacting alpha -chloropropionic acid with thionyl chloride, obtaining alpha -chloropropionyl chloride, reacting obtained product with glycine, obtaining alpha -chloroglycine, further reacting obtained product.    USE - Preparation of tiopronin (claimed).    ADVANTAGE - The method efficiently provides tiopronin with high yield without polluting the environment.
NOVELTY - Method for preparing pesticide involves adding 0.3-0.5 wt.% caustic soda to biogas slurry, fermenting mixture in closed environment for one year, filtering impurities to obtain filtrate, adding 0.6-1 wt.% perfuming agent to the filtrate, uniformly stirring mixture, adding 0.4-0.5 wt.% dispersing agent and 0.5-0.6 wt.% curing agent to the mixture and uniformly stirring the mixture.    USE - The method is useful for preparing pesticide (claimed).    ADVANTAGE - The method is simple and cost-effective, and consumes less energy and utilizes wide raw material sources.
NOVELTY - A gasification, cracking reaction device comprises a material returning valve (10), a loose air chamber (11), an air chamber (12), a reaction chamber (13), and an upper part of a wind cap (16). The reaction chamber comprises a gas outlet (14), a material inlet and a circulating ash inlet (1), a horizontal air distributing plate (5), two inclined air distribution plate (6), a chamber (7), and a side air chamber (8).    USE - A gasification, cracking reaction device used for black liquor, biomass, or coal gasification or pyrolysis.    ADVANTAGE - The device achieves uniform solid fuel mixing.    DESCRIPTION OF DRAWING(S) - The drawing is a sectional view of the gasification, cracking reaction device.    Circulating ash inlet (1)    Horizontal air distributing plate (5)    Inclined air distribution plate (6)    Chamber (7)    Side air chamber (8)    Material returning valve (10)    Loose air chamber (11)    Air chamber (12)    Reaction chamber (13)    Gas outlet (14)    Wind cap (16)
NOVELTY - Co-production of ethanol, fiber, lignin, pectin, xylose and yeast using corn straw, comprises degrading corn straw as raw material using degradable substances such as polysaccharide, pectin and starch into soluble substance aqueous solution through acidolysis method to realize the separation of the residue from the degradable substances, fermenting the residue using soluble substance aqueous solution, extracting ethanol fuel, pectin and xylose, and producing fiber and lignin using residue by organic solvent method.    USE - The method is useful for co-production of ethanol, fiber, lignin, pectin, xylose and yeast using corn straw (claimed).    ADVANTAGE - The method allows simple and economical production of ethanol, fiber, lignin, pectin, xylose and yeast with high efficiency and improved yield in an eco-friendly manner.
NOVELTY - A rare earth doped nano titanium dioxide wettable powder, comprises (mass.%): rare earth doped nano titanium dioxide (60), wetting dispersant (2-8), emulsifier (1-5) and carrier (30-40).    USE - As pesticide auxiliary agent (claimed).    ADVANTAGE - The rare earth doped nano titanium dioxide wettable powder overcomes the defects of easy delamination of the rare earth doped nano titanium dioxide in water, where the rare earth doped nano titanium dioxide can not only uniformly disperse in the water, but also can more uniformly and durable adsorb at the plant surface or surface soil through adding auxiliaries system, thus improving the effect of degrading pesticide; is convenient to use for directly adding water to dilute; can be directly used for processing the dosage forms of some high toxic and high residual pesticides to reduce high residual pollution in the environment after using the pesticides; requires low and easily obtained material; has good adhesiveness, and little drift; and is free from organic solvent and convenient to store and transport.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the rare earth doped nano titanium dioxide wettable powder involving: mixing uniformly the rare earth doped nano titanium dioxide, the wet dispersant, the emulsifier and the carrier, and crushing till that 98% of materials can pass 200-400 meshes of sieve, to obtain the rare earth doped nano titanium dioxide wettable powder.
NOVELTY - Method (M1) for pretreating brown algae involves crushing brown algae and obtaining particles, performing decomposition reaction in the presence of sodium salt catalyst, preferably liquid phase catalyst, at 100-170 degrees C for 20-70 minutes and separating alginic acid of brown algae.    USE - The method (M1) is useful for pretreating brown algae, preferably kelp used for producing bioenergy (all claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method (M2) for producing bioenergy, which involves performing the above-mentioned steps of method (M1), adding acid to the pretreated brown algae and carrying out hydrolysis and generating sugar, and performing fermentation using microorganism and producing ethanol.
(CZ201100816-A3)   NOVELTY - An ethanedinitrile preparing method involves subjecting hydrogen cyanide to oxidation process on a catalytic system, and immobilizing onto polymeric organic cation exchange resin in presence of organic solvent or homogeneous or heterogeneous mixture with water at 5-65 degrees C in atmosphere of oxygen, air, hydrogen peroxide or mono-or disubstituted alkyl or acyl derivatives.    USE - Method for preparing ethanedinitrile.    DETAILED DESCRIPTION - An ethanedinitrile preparing method involves subjecting hydrogen cyanide to oxidation process on a catalytic system by utilizing iron-copper component (Fem+/Cun+), where m is 2 or 3 and n is 1 or 2, optionally a bidentate oxygenous or nitrogenous ligand, and immobilizing onto a polymeric organic cation exchange resin in presence of organic solvent or homogeneous or heterogeneous mixture with water at 5-65 degrees C in atmosphere of oxygen, air, hydrogen peroxide or mono-or disubstituted alkyl or acyl derivatives.
NOVELTY - Manufacture of electrode involves forming a multiporous sprayed layer on a Hastelloy (RTM: nickel-chromium-iron-molybdenum alloy) or nickel plate coating by spraying.    USE - Manufacture of electrode (claimed) used for hydrogen generation for electrolyzer.
NOVELTY - The treatment system has anaerobic digester from which carbon dioxide processing water is inflowed into anoxic chamber. The anaerobic digester is provided to degas the ammonia and precipitate the struvite in the processing water. The carbon dioxide included in biogas is absorbed by the pH controlled processing water to emit high concentration methane gas. A membrane bio reactor (MBR) is provided to remove the nitrogen and eject the filtered water filtered through a membrane.    USE - Treatment system for wastewater e.g. livestock wastewater, food waste water and return sludge of sewage disposal plant.    ADVANTAGE - By using membrane bio reactor, the water quality is improved. The nitrogen and phosphorus content in the wastewater can be removed efficiently.
NOVELTY - Producing taxifolin, comprises: stacking wood particles in a percolator; extracting the wood particles in the percolator using ethanol; discharging the ethanol extract from the percolator; and purifying the ethanol extract, comprising e.g. : producing a mixture of water and the ethanol extract; mixing the mixture to dissolve taxifolin in the water phase of the mixture; cooling the mixture to separate and discharging the resin phase and the oil phase from the water phase; adding taxifolin seed crystals to the water phase; and separating the crystallized taxifolin from the mother liquor.    USE - The method is useful for producing taxifolin.    ADVANTAGE - The method is environmentally friendly, and ensures an economic production of large quantities of taxifolin.    DETAILED DESCRIPTION - Producing taxifolin, comprises: stacking wood particles in a percolator; extracting the wood particles in the percolator using ethanol, to dissolve at least resins, oils, and taxifolin; discharging the ethanol extract from the percolator; and purifying the ethanol extract, comprising: producing a mixture of water and the ethanol extract; mixing the mixture at 70-99 degrees C to dissolve taxifolin in the water phase of the mixture; cooling the mixture to below 65 degrees C to separate and discharging the resin phase and the oil phase from the water phase; adding taxifolin seed crystals to the water phase; tempering the temperature of the water phase to 0-30 degrees C to crystallize the taxifolin; and separating the crystallized taxifolin from the mother liquor.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic process flow for extracting (Drawing includes non-English language text).    Crushing the wood (S1)    Layering the crushed wood particles (S2)    Introducing ethanol (S3)    Discharging ethanol extract (S4)    Evaporating the ethanolic extract (S5)
NOVELTY - The method involves adding a fastening load to a fastening bolt (26) equal to specified load in the direction of reaction force received from a fuel cell stack. The length of load fastening bolt is acquired. The difference value of load stack length and load fastening bolt length is acquired. The projecting length of several load adjustable screws clamped in surface of fuel cell stack is adjusted corresponding to difference value for fastening specified load of fuel cell stack, after adjustment of projecting length amount using fastening bolt.    USE - Manufacturing method of fuel cell such as solid polymer type fuel cell.    ADVANTAGE - The projecting length of several load adjustable screws clamped in surface of fuel cell stack is adjusted corresponding to difference value for fastening specified load of fuel cell stack, hence the use of fastening bolt can be realized. The simplified manufacturing process can be achieved. The fuel cell stack can be fastened appropriately.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the manufacturing process of fuel cell. (Drawing includes non-English language text)    Fuel cell (12)    Pressure plate (14)    End plate (16)    Stack case (22)    Fastening bolt (26)
NOVELTY - Operating an electrolyzer (2) for generating hydrogen by decomposing water, comprises: storing waste heat produced within the electrolyzer in a heat transfer medium; supplying the heat transfer medium to a water treatment plant (10); and producing deionized water from raw water in the water treatment plant by the waste heat.    USE - The method is useful for operating an electrolyzer for generating hydrogen by decomposing water.    ADVANTAGE - The method: improves the efficiency of electrolysis process; increases production rate of ultra-pure water; allows monitoring of water quality of the distilled water in water treatment plant; and ensures sufficient fresh water supply to electrolyzer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an electrolyzer system (1) for generating hydrogen and oxygen through electrolysis of water by the above mentioned method.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of an electrolyzer system.    Electrolyzer system (1)    Electrolyzer (2)    Water treatment plant (10)    Cooling device (12)    Closed circuit (30)
NOVELTY - Water displacing composition comprises a linear, branched or cyclic 4-9C-hydrocarbon, and a 3-6C-alcohol.    USE - The water displacing composition is useful for restoring operation of a personal electronic device having wet circuitry (claimed), and of a microelectronic device including cellular telephones, computers, tablet computers, e-readers, pagers, flash drives, digital cameras, digital camcorders, dictation devices, insulin pumps, Holter monitors, global positioning satellite system receivers and personal entertainment (i.e. DVD) playback devices.    ADVANTAGE - The water displacing composition rapidly restores function to a microelectronic device that has been immersed or otherwise detrimentally exposed to water without requiring resorting to device disassembly by leaving a residual corrosion inhibitor to protect internal components of the device, and does not interfere with the functionality or appearance of the visual displays and touch screens associated with the subject device.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for restoring operation of a personal electronic device having wet circuitry, comprising exposing the circuitry to the composition, and allowing sufficient time for the water to be displaced from the circuitry to restore operation to the personal electronic device.
NOVELTY - A thioxanthone compound (I), is new.    USE - Thioxanthone compound used for treating disorders positively influenced by inhibition of p53-mouse double minute 2 (MDM2) homolog or p53-mouse double minute 4 (MDMX) homolog interaction, preferably for treating cancers of breast, colorectal, prostate, kidney, lung, melanoma, osteosarcoma or embryonal nephroma, and for use in medicine or pharmaceutical composition (all claimed).    ADVANTAGE - The thioxanthone compound shows enhanced stability, and can be produced efficiently through synthetic process in a simple and eco-friendly manner with high yield.    DETAILED DESCRIPTION - A thioxanthone compound of formula (I), its salt or ester, is new.    Y'=O, S, CH2 or NH;    Z=C=O, CH2, CH-OH, C=NOH, C=NOCH3, NO, NOH, SO or SO2, and    R1-R8=H, hydroxy, aldehyde, halo, trifluoromethyl, acetylene, carboxy, cyano, nitro, SO2NH2, aryl or heteroaryl substituted by halo or hydroxy or methoxy, amino, aminoalkoxy, aminoaryl, imino, alkyl, cycloalkyl or haloalkyl, or    2 of R1-R8= aminoalkyl, alkoxy, alkylene(di)oxypyranyl (optionally pyranyl substituted by alkyl), furanyl or dioxanyl (optionally substituted by aryl optionally substituted by halo, hydroxy, alkoxy or alkylene(di)oxy),    where 1 or R1-R8 is amino and/or aminoalkyl with a counterion comprising HCO3-, CO32-, Cl-, NH2C6H4SO3-, 1-CH3C6H2-3-OH-4-(CHCH3)-6-SO2-. (sic).    An INDEPENDENT CLAIM is included for a pharmaceutical composition, which comprises thioxanthone compound of formula (I) and a chemotherapeutic agent, such as etoposide.
NOVELTY - A cotton seeding matrix comprises vinegar residue, cassava slag, vermiculite, grass carbon and ash and little inorganic fertilizer.    USE - Cotton seedling matrix.    ADVANTAGE - The matrix utilizes organic waste as raw material.
NOVELTY - This utility model claims a kind of biomass micro focus and low-emission combustion gas generating furnace is provided with a secondary air inlet pipe is connected with a secondary wind nozzle on the furnace bottom plate of the outer shell inner side of oven shell is fixedly connected with the inner wall of the lower end of the movable furnace bridge the resistance on the furnace bridge plate layer and a high temperature area, flame retardant coating on the end of movable furnace liner, furnace upper end of the shell is connected with a furnace head, a water sealing cover in a sealing groove is provided on the upper end of the furnace end. Also connected with outer air inlet pipe of air inlet pipe and the secondary air inlet pipe connected to the furnace head inner cavity and the inner cavity of the shell. A fuel gas output pipe and two ends of thick gas output pipe is connected with the furnace cavity and furnace inner cavity of the shell is further connected with a filter, the upper part of the filter is connected with a flue gas discharge pipe, the lower section of filter is connected with gas output pipe and a drain pipe. This kind of fuel gas generator because of the high temperature area, biomass particle material is high temperature pyrolysis fission generated during the wood tar can be re-burning, gas containing tar and low in discharge of the smoke through the filter purifying, and has popularization and application value.
NOVELTY - A green chemical fertilizer comprises rhenium, compost, and biomass fermentation residue.    USE - As green chemical fertilizer which is useful as plant fertilizer (claimed).    ADVANTAGE - The green chemical fertilizer decomposes pesticide residue toxicity; reduces plant diseases and insect pests; promotes photosynthesis; shortens growth period; and has freeze-proof ability.
NOVELTY - An irrigation fermentation liquid fertilizer for greenhouse crop, prepared by using 65-80 parts by weight of poultry manure, 8-15 parts by weight of peanut bran, 3-6 parts by weight of phosphate fertilizer, 8-12 parts by weight of potassium dihydrogen phosphate, and 0.8-1.2 parts by weight of EM (not defined) original dew; where the preparation method involves removing EM original dew, stirring the raw materials uniformly, putting the air into a fermenting tank to ferment for 50-70 days at 20-32 degrees C, adding EM original dew, air to ferment for 50-70 days, and packing.    USE - As irrigation fermentation liquid fertilizer for greenhouse crop (claimed).    ADVANTAGE - The fermentation liquid fertilizer contains a protein, nitrogen, phosphorus, potassium, multiple vitamins and microelement, that shows good promoting effect for the growth of crops and good fertilizing effects; and is convenient operation.
NOVELTY - Method for preparing biopellet, involves drying water hyacinth, and heat-decomposing the water hyacinth using a pyrolysis device at 200-350 degrees C for 60-120 minutes.    USE - The method is useful for preparing biopellet (claimed).    ADVANTAGE - The method enables to provide high combustion efficiency, reduce generation amount of fine dust, and increase calorific value and intensity of the pellet.
NOVELTY - This utility model claims a wind-proof type biomass wild cooking furnace, comprising a furnace body, wherein the furnace body is surrounded by a furnace of the hearth, wherein the hearth is set at the lower part matched with the fire grate, wherein the upper part of the hearth is set with an oil pipe connected with the burner, the burner is set on the upper part is connected with the combustion basin, wherein the furnace shell and the furnace liner to form an air flow cavity. This utility model of wind-proof biomass wild cooking furnace, is small and light, ecological and environment-friendly, low in cost, capable of using various straws, branches and so on biomass directly into combustion, the combustion is full, but also can control the fire according to the actual need, it is suitable for all kinds of occasions.
NOVELTY - The utility model claims a kind of used for garbage fermentation processing system of purification tower, a purification tower comprises table-board, purifying tower surface, a purifying tower frame, a sorting opening, a water collecting box, purifying tower surface is set on the purifying tower, a purifying tower surface are arranged around surface, is provided with a corresponding to the water outlet of the cylindrical wall surface of the air inlet part, one side of the purifying tower surface of the replacing opening is provided with an active carbon (groups) purifying tower surface is set at the lower part of the water collecting box. A fermentation gas discharged by tower three the purifying active carbon filtering, and spraying the clean water, and finally by detecting the harmless and tasteless removing the gas to the atmosphere.
NOVELTY - This utility model claims a kind of new biomass cracking furnace, belonging to the biomass pyrolysis furnace, comprising furnace outer wall, the inner wall and grate in the hearth, the outer wall is poured with high temperature, fire grate is fixed on the lower end of the hearth, the existing technology, the surface of the inner wall along the tangential direction on the lower end of the hearth centre one side of the plane outer wall of the upper end of the hearth is further provided with two tangential holes through two secondary wind. , By the method, the utility model can solve the problem of the existing cracking chamber hearth fuel cracking is not complete, a large capacity of the fan, is easy to cause environment pollution and so on, through the tangential wind driven particle as tangential motion to prolong the cracking room of the residence time and improve cracking efficiency, reduce the emission of harmful gas, the cooling air into the cracking chamber as the secondary wind, so as to reduce the total air flow, reduces fan volume, reduces the equipment cost.
NOVELTY - This utility model claims a kind of high thermal value of the biomass gasification furnace, comprising a furnace body is set on the first side of the spiral feeding device, a hopper, a spiral feeding device is set in the hearth in the furnace body, are respectively provided with the upper end of the air outlet pipe and the lower end of the cold air inlet tube on the other side of the furnace body is provided with air supply device and dust cleaning device is set in the furnace body, an air supply device for the top plane of the semi-spherical, and is provided with an air supply hole is set on the semi-sphere surface of the device is connected with the bearing of the rotary frame. Through said method, the utility model can solve the problem that the gasification furnace low thermal value, low tar content is high, is provided with gasification fully, reduce the tar as temperature, dust cleaning is convenient and quick.
NOVELTY - This utility model claims a kind of combustible garbage fuel gas generator, comprising a combustion chamber, a garbage bin, a flame lighter, a fan, a hanging basket is provided with the lower port of the garbage bin, the four sides and the bottom of the hanging basket by a spacer provided with a rod, the bottom of the combustion chamber and the lower part of the hanging basket is opposite to the lower end is provided with a grate, the upper part of the furnace shell is provided with a cavity, the upper smoke chamber surrounded by the combustion chamber upper end plate and T-shaped cavity, a smoke cylinder wall and the furnace wall of the ash chamber, a cavity of the lower end plate and the annular smoke chamber is under the lower end plate surrounded by the annular smoke chamber, wherein the hanging basket is set in the smoke chamber above the combustion chamber, fire tube is in the smoke chamber, wherein a cavity of the outer fire pipe on two ends are respectively connected with the upper end plate of the lower smoke chamber and a T-shaped cavity wall and is connected with the upper and lower smoke chamber, a fan inlet and outlet are respectively connected with the ash bin of the lower smoke chamber and a combustion chamber furnace grate, the lower smoke chamber and the high pressure gas tank is provided with a connecting pipe, the connecting pipe is provided with a high-pressure fan. This utility model can be used for producing building material by urban garbage combustion gas.
NOVELTY - This utility model claims a kind of fully cracking the biomass pyrolysis, comprising a hopper, a spiral conveying device, air supply device and cracking, making the existing cracking is improved mainly from the upper part of the hearth outer wall of the grate in the hearth wall of the two rows of tangential to the wall surface in the hearth of the holes, each row 5 of adjacent two holes and the central line is 30 degrees, and is fixed on the hearth on the outer wall of the first semi-arc thin plate cooling interlayer on the lower end, and the plane on the basis of the central line is set with two vertical thin plate on the outer wall of the hearth; Through said method, the utility model can solve the problem that the cracker cooling wind utilization efficiency is not high, the biomass fuel cracking is not enough, the fan has large volume and so on, it has improve the cracking efficiency, reduce the total air flow to prevent tempering.
NOVELTY - This utility model claims a biomass gasification furnace with two-grade purification system for purifier, comprising a connected to the first level purifier and second level purifier, the purifier comprises a cylindrical shell and a baffle plate to 10 to 20 degrees at the inner wall of the cylindrical shell one side inclined angle, secondary purifier comprising: a second cylindrical shell and is composed of two pieces of mesh filter plate and absorbing material of the filtering device. Through said method, the utility model can solve the problem that the purifying system for purifying efficiency is low and the cost is high, the application range is limited, operation and inconvenient maintenance and so on, it has good purifying effect, and it has simple structure, is easy to be unpicked, internal filtering material and material is wide, the cost is low, it can large scale popularization and application.
NOVELTY - This utility model claims a kind of sludge, refuse derived fuel combined fuel gas-steam combined cycle power generation system, relating to the sludge, refuse derived clean conversion and utilization technical field of fuel heat energy, which is mainly composed of garbage sorting device, a sludge dewatering device, RDF-5 device, RDF-6 device, RDF-7 device, a boiler, a turbine generating set, a waste heat boiler, a steam pipe, a wheel generating set and gas processing device is composed of a set of cycle power generation system, the utility model is novel, it is good for reducing dioxin generated from the source, it can realize high efficiency of waste heat energy conversion and utilization, and at the same time the garbage, but also can process sewage sludge, solves the problem that is hard to treat urban sewage and sludge of the city waste to obtain the comprehensive treatment, improves the economical efficiency of the urban waste.
NOVELTY - The decomposing processor has a stirring shaft (2) that is mounted on the stirring tank. The ends of the stirring shaft are connected with the stirring groove (1). The blades (3) are evenly fixed on the stirring shaft and are positioned perpendicular to the stirring shaft. The blades are uniformly distributed on the stirring shaft. The blades are gradually changed in length and step size. The blade is provided with reinforcing rib (4).    USE - Biological decomposing processor for livestock excrement.    ADVANTAGE - The degradation speed of the livestock excrement can be effectively improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biological decomposing processor for livestock excrement.    Stirring groove (1)    Stirring shaft (2)    Blades (3)    Reinforcing rib (4)
NOVELTY - Preparation of endophytic nitrogen-fixing bacteria fertilizer comprises taking 55-70 wt.% organic fertilizer, carrying out composite microbial fermentation, adding 10 wt.% water, mixing at 60-70 degrees C, cooling, turning every 24-36 hours, reducing temperature to 35-45 degrees C, carrying out secondary fermentation and stacking for 15-20 days.    USE - Preparation of endophytic nitrogen-fixing bacteria fertilizer.    ADVANTAGE - The method improves soil fertility and agricultural production.
NOVELTY - A plant fertilizer comprises 70-80 pts. wt. organic fertilizer, 10 pts. wt. diammonium phosphate, and 0.03-0.05 pts. wt. trace element.    USE - Plant fertilizer.    ADVANTAGE - The fertilizer improves plant yield and quality, and has low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of plant fertilizer by crushing garbage, leaves and crop straw at mass ratio of 10-20:3-5:45-50; spraying lime water at mass ratio of 25-30:1; adding livestock manure at mass ratio of 10-5:1; and sealing and fermenting at room temperature; and adding diammonium phosphate and trace element, uniformly stirring, pelletizing, and sieving.
NOVELTY - A compound fertilizer comprises livestock excrement, garbage, leaves, rice husk, straw and weeds, crop straw and colza cake at mass ratio of 60-70:3-5:2-4:8-15:4-8:8-10:2-3. It is prepared by dissolving all raw materials in proper amount of water, stirring uniformly, adding composite microbial inoculum to ferment at 38-42 degrees C for 8 days, adding 2-20 wt.% aminosulfonic acid spray and drying at normal temperature.    USE - Compound fertilizer.
NOVELTY - Preparation of garbage compound fertilizer comprises dissolving livestock excrement, garbage, leaves and crop straw in proper amount of water, stirring uniformly, adding composite microbial inoculum to ferment at 25-30 degrees C for 6 days, adding nitrogenous fertilizer, phosphate fertilizer and potash fertilizer, stirring uniformly, pelleting and sieving.    USE - Preparation of garbage compound fertilizer.    ADVANTAGE - The fertilizer reduces environment pollution, increases crop yield, reduces fertilizer cost and increase profit.
NOVELTY - This utility model claims a kind of combined processing method of organic exhaust gas, wherein the combined organic exhaust gas process device comprises an air inlet pipe, an exhaust pipe, a photo-catalytic oxidation device and the biochemical filter element device, the photo-catalytic oxidization device and the biochemical filter device through pipeline, the air inlet pipeline is set in the photo-catalytic oxidization device, the exhaust pipe is arranged on the biochemical filter element device. The combined organic exhaust gas process device, a light catalytic oxidation + biochemical spray filter combined technique, wherein the technique combines the physical, chemical, technology, linked to, the third kind of technology are organically combined into a whole, solves the problem that the physical and chemical method for processing organic waste gas is not complete, but also solves the problem that the biological method for processing organic waste microorganism is easy to be toxic;
NOVELTY - Preparing fuel ethanol by using kelp residue, comprises collecting industrial waste of kelp mud residue, rinsing the kelp mud residue using clean water, carrying out ultrasonic treatment on the kelp mud slag, adding water and feed liquid into treated kelp residue, adding 0.3% of yeast powder, 0.5% of peptone, 0.02% of urea, 0.4% of magnesium sulfate and diammonium hydrogen phosphate into kelp residue feed liquid, inserting 8 wt.% of high activity Saccharomyces cerevisiae, adding and fermenting 15-25 u/g of cellulose, and filtering the fermentation and distilling the filtrate.    USE - The method is useful for preparing fuel ethanol by using kelp residue (claimed).    ADVANTAGE - The method prepares fuel ethanol without wasting resource in simple, feasible, environmental friendly and cost effective manner.    DETAILED DESCRIPTION - Preparing fuel ethanol by using kelp residue, comprises collecting industrial waste of kelp mud residue, and rinsing the kelp mud residue using clean water to remove chemical substance, carrying out ultrasonic treatment on the kelp mud slag, adding water and feed liquid into treated kelp residue in proportion of (1:5)-(1:20) (g/ml), adding 0.3% of yeast powder, 0.5% of peptone, 0.02% of urea, 0.4% of magnesium sulfate and 0.01% of diammonium hydrogen phosphate into kelp residue feed liquid, inserting 8 wt.% of high activity Saccharomyces cerevisiae, adjusting the pH value of the mixed solution to 4.5-5.5, adding 15-25 u/g of cellulose, and fermenting at 34 plus minus 2 degrees C under a speed of 110-150 revolutions per minute (rpm) for 24-72 hours, and filtering the fermentation and distilling the filtrate.
NOVELTY - A cassava residue is used as microbial inoculum carrier or microbial inoculum.    USE - Cassava residue used as microbial inoculum carrier or microbial inoculum (claimed).    ADVANTAGE - The method has low cost, simple process technique, environment-friendly and energy-saving.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of microbial inoculum carrier comprising preparing cassava starch, adding cassava alcohol residue and soybean meal, drying, crushing and sieving, mixing, redrying, sterilizing, mixing and drying until water content is below 10%.
NOVELTY - A biological organic fertilizer comprises 50-80 pts. wt. dewatered sludge, 10-50 pts. wt. protein residue, 0-10 pts. wt. urea, 0-10 pts. wt. activated carbon and 0.2-1 pt. wt. functional bacterial strain. The dewatered sludge is continuous stirred tank reactor (CSTR) anaerobic fermentation mycelium or expanded granular sludge bed (EGSB) anaerobic fermentation-aerobic treatment sludge. The protein residue is itaconic acid or sodium gluconate production residue. The functional bacterial strain is nitrogen-fixing bacteria, organic phosphate bacteria and/or potassium bacteria.    USE - A biological organic fertilizer.    ADVANTAGE - The fertilizer has small investment and simple preparation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of biological organic fertilizer comprising preparing functional bacterial strain, placing in liquid culture at 108-1010 cfu/ml; mixing dewatered sludge and protein residue, adjusting pH to 6.5-7.5, adding urea or activated carbon, adjusting carbon/nitrogen (C/N) ratio to 35:1-25:1, adding functional bacterial strain, carrying out aerobic fermentation; and drying fermented product to 15-20 wt.% water content, crushing, sieving and granulating.
NOVELTY - Preparing penicillin-G sulfoxide, comprises (i) taking penicillin-G fermenting liquid, and dropping peroxyacetic acid to obtain solution I, (ii) filtering the solution I through 5-200 nm ceramic film to obtain filtrate, passing the filtrate through nano-filtration membrane, and concentrating to obtain concentrated solution, (iii) adjusting pH, and filtering to obtain crude penicillin G sulfoxide, and (iv) dissolving crude penicillin-G sulfoxide in aqueous methanol solution, crystallizing, cooling, filtering to obtain crystal, washing using methanol, and drying.    USE - The method is useful for preparing penicillin-G sulfoxide (claimed).    ADVANTAGE - The method has simple preparation process, short processing period, does not require large amount of organic solvent for extracting process, and is economical and environmentally friendly.    DETAILED DESCRIPTION - Preparing penicillin-G sulfoxide, comprises (i) taking 6000-120000 mu /g of penicillin-G fermenting liquid, and dropping 20-38% peroxyacetic acid at 0-8 degrees C to obtain solution I, (ii) filtering the solution I through 5-200 nm ceramic film to obtain filtrate, passing the filtrate through nanofiltration membrane (molecular weight cut-off is 100-500 kDa), and concentrating to obtain concentrated solution, (iii) adjusting the pH of concentrated solution to 1-1.5 using sulfuric acid, and filtering to obtain crude penicillin G sulfoxide, and (iv) dissolving the crude penicillin-G sulfoxide in 9-80% aqueous methanol solution, crystallizing at 40-48 degrees C, cooling to 0-10 degrees C, filtering to obtain crystal, washing using methanol, and drying (preferably microwave drying) to obtain the final product.
NOVELTY - Straw returning fiber decomposing bacterial strain (Burkholderia sp.XWS-12) having preservation number of CGMCC NO. 6386, is new.    USE - The straw returning fiber decomposing bacterial strain is useful in a straw preservative agent (claimed).    ADVANTAGE - The straw returning fiber decomposing bacterial strain is prepared as a microbial agent such that the problems of unstable and unsatisfactory effects of the straw preservative agent in the application processes are solved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a straw preservative agent comprising a straw returning fiber decomposing bacterial strain and peat bacteria.
NOVELTY - A biogas residue breeding nutrient block comprises 60-70 wt.% cattle manure, 15-20 wt.% rice straw, 10-15 wt.% plant ash, 3-5 wt.% urea, 1-3 wt.% calcium superphosphate, 0.5-1 wt.% boric acid, 0.2-0.5 wt.% cellulose and 0.3-0.5 wt.% sodium alginate.    USE - Biogas residue breeding nutrient block.    ADVANTAGE - The block improves soil organic matter content and soil structure, thus, prevents hardening of soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biogas residue breeding nutrient block comprising: taking biogas residue and biogas slurry, performing solid-liquid separation, drying to water content below 30%, adding rice straw, water and fermenting bacteria and fermenting for 1 month, adding crushed urea and calcium superphosphate, putting into mixing machine, stirring uniformly and pressing with seeding holes.
NOVELTY - Preparation of bio-organic compound fertilizer comprises: forming fermenting tank using plastic cloth or waterproof fabric, providing cover; crushing fresh pig manure, edible fungi waste residue, nitrogen-phosphorus-potassium, trace elements and microbial strains at 800:200:9.5:0.5:1 mass ratio, stirring, placing in fermenting tank; fermenting at 45-65 degrees C for 7-15 days under aerobic and stirred condition; and drying, crushing and packaging. The microbial strain is composite Azotobacter, phosphorus bacteria, potassium bacteria, and dust or fiber bacteria.    USE - Method for preparing bio-organic compound fertilizer (claimed).    ADVANTAGE - The method is simple. The production cost is low.
NOVELTY - Preparing cracking C3 fraction hydrogenation catalyst, involves dissolving copper(II) nitrate as soluble salt in de-ionized water; pre-treating alumina carrier by dipping alumina carrier in copper(II) nitrate solution; and drying and roasting to obtain cracking C3 fraction hydrogenation catalyst.    USE - For preparing cracking C3 fraction hydrogenation catalyst (claimed).    ADVANTAGE - The method prepares catalyst has high hydrogenation activity, and high impurity removing rate.
NOVELTY - Recycling soluble manganese and magnesium from electrolytic manganese slag comprises mixing electrolytic manganese slag with water, stirring, filtering, performing chelating resin adsorption of manganese in filtrate, eluting chelating resin using 5-10% sulfuric acid to regenerate and obtain manganese sulfate eluent, adding aqueous ammonia and ammonium carbonate into effluent to precipitate magnesium carbonate, filtering, washing and drying.    USE - The method is used for producing ammonium sulfate for preparing fertilizer and producing electrolytic manganese (claimed).    ADVANTAGE - The method solves the problem regarding the water-soluble manganese salt of electrolytic manganese slag which pollutes the underground water and surface water.
NOVELTY - Preparation of high purity bulleyaconitine A comprises selecting fresh grass aconite root, washing with clean water, soaking aconite root into homogenate machine, extracting for 10-20 minutes, filtering, and collecting filtrate, homogenizing and extracting; racemic solid-liquid extracting for 4 times, passing through ion exchange resin column chromatography and macroporous absorption resin column chromatography gradient elution; and mixing with 65-80% ethanol aqueous solution, heating at 40-60 degrees C, filtering, cooling filtrate to room temperature, standing to crystallize, and washing.    USE - Method of preparation of high purity bulleyaconitine A (claimed).    ADVANTAGE - The method reduces the use of organic solvent, has low cost and reduces environment pollution.    DETAILED DESCRIPTION - Preparation of high purity bulleyaconitine A comprises selecting fresh grass aconite root, washing with clean water, using acid water solution and material liquid at ratio of 1:2-1:4 for 24 hours, with acid water solution of 0.1-0.4 mol/L hydrochloric acid or sulfuric acid aqueous solution, soaking aconite root into homogenate machine, extracting for 10-20 minutes, filtering, and collecting filtrate, homogenizing and extracting; racemic solid-liquid extracting for 4 times, each time extracting for 30-60 minutes, filtering and collecting filtrate, mixing filtrate of two times, concentrating, passing through ion exchange resin column chromatography and macroporous absorption resin column chromatography gradient elution to obtain bulleyaconitine A crude product; and at ratio of 1:10-1:20 of material liquid and bulleyaconitine A crude product, mixing with 65-80% ethanol aqueous solution, heating at 40-60 degrees C under water bath to dissolve, filtering, cooling filtrate to room temperature, standing to crystallize, and repeatedly washing with ethanol aqueous solution.
NOVELTY - Catalytic esterification comprises reacting bio-oil and methanol using cation exchange resin CD650 as catalyst.    USE - Catalytic esterification is used for producing esterified bio-oil (claimed).    ADVANTAGE - The esterified bio-oil has reduced density, moisture content and kinematic viscosity and improved heating value. It can be stored for 3 months at 25 degrees C without deterioration.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for test reaction device of catalytic esterification which uses Box-Behnken design method to obtain model test reaction for optimizing temperature, time and catalyst quantity, where the test results are analyzed by design software analysis.
NOVELTY - High temperature methanation catalyst comprising 45-75 wt.% of nitric oxide, 0-10 wt.% of chromium(III) oxide and 25-55 wt.% of magnesium oxide modified vector, is new.    USE - The methanation catalyst is useful in a methanation reactor for converting coal-based synthetic gas into coal gas and natural gas (claimed), where coal-based synthetic gas is carbon monoxide.    ADVANTAGE - The methanation catalyst exhibits high catalytic performance, activity and stability, and provides carbon monoxide gas at a yield of greater than 21%.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparing the methanation catalyst; and    (2) use of the catalyst in a methanation reactor for city coal gas and natural gas device, where: the coal synthesis gas is obtained in the methanation reactor by hydrogenating the coal synthesis gas at a pressure of 1-6 MPa and a temperature of 250-700 degrees C in an oxidation tower to form methane gas and removing methane gas and water from the tower; and the gas phase volume space velocity of the methanation reactor is 6000-10000 hour1.
NOVELTY - Synthesizing 4,5-diphenyl-1H-imidazole compounds (I), comprises reacting 1,2-diphenylethane-1,2-dione (II) with aldehyde compounds (III) and ammonium acetate in the presence of organic solvent and enzyme under enzyme catalysis condition, where the enzyme is alpha -amylase from pig pancreas, amylase from Aspergillus oryzae, trypsin NB from porcine pancreas, lipase AT30 or protease albumin from bovine.    USE - The method is useful for synthesizing (I) (claimed).    ADVANTAGE - (I) have mild reaction condition and high yield and are environment-friendly.    DETAILED DESCRIPTION - Synthesizing 4,5-diphenyl-1H-imidazole compounds of formula (I), comprises reacting 1,2-diphenylethane-1,2-dione (II) with aldehyde compounds of formula (OHC-R) (III) and ammonium acetate in the presence of organic solvent and enzyme under enzyme catalysis condition, where the enzyme is alpha -amylase from pig pancreas, amylase from Aspergillus oryzae, trypsin from pig pancreas, lipase AT30 or protease albumin from bovine.    R= heteroaryl or aryl (both optionally substituted with 1-3C alkyl, 1-3C alkoxy, nitro, halo or phenyl), where the hetero aryl is pyridyl or thienyl and the aryl is phenyl.
NOVELTY - Manufacture of trans-6,8-dibromo-3-(trans-4-hydroxy-cyclohexyl)-1,2,3,4-tetrahydro-quinazoline (ambroxol impurity B) involves reacting ambroxol and formaldehyde-releasing compound in presence of organic solvent.    USE - Manufacture of trans-6,8-dibromo-3-(trans-4-hydroxy-cyclohexyl)-1,2,3,4-tetrahydro-quinazoline (claimed).    ADVANTAGE - The ambroxol impurity B is manufactured efficiently with high quality and excellent productivity with reduced toxicity, by simple and environmentally-friendly method.
NOVELTY - Producing biodiesel from algal lipid with dimethyl carbonate, is claimed.    USE - The method is useful for producing biodiesel from algal lipid with dimethyl carbonate.    ADVANTAGE - The method increases the reaction rate of transesterification for biodiesel production from algal lipid, and produces eco-friendly biodiesel without glycerol.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for the biodiesel without glycerol, produced by the method.
NOVELTY - Enhancing soil growth using biomass fractionator apparatus (BMF) char, comprises rendering a surface of the BMF char hydrophilic, exposing the BMF char to microorganisms, and adding the BMF char to soil.    USE - The method is useful for enhancing soil growth using biomass fractionator apparatus char (claimed), which is useful for producing fuels for combustion in automobile or aviation engines.    ADVANTAGE - The method is capable of energy efficiently enhancing the soil growth and maintaining soil health and productivity by directly adding the BMF char to the soil and allowing to self-neutralize for extended periods of time without significantly disturbing the underlying soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing an agent for enhancing soil growth, comprising grinding a biomass feedstock to produce ground biomass particles, subjecting the ground biomass particles to a biofractioning process including an auger reactor, selectively collecting at least one volatile component as it is released from the ground biomass particles, collecting a last remaining nonvolatile component comprising BMF char, rendering a surface of the BMF char hydrophilic, exposing the BMF char to microorganisms, and adding the BMF char to soil.
NOVELTY - Waste water treatment comprises adding at least one polysaccharide and polyacrylic acid as flocculant or a mixture of at least one polysaccharide and polyacrylic acid in solid or dissolved form as a gel, where at least one polysaccharide has a cationic charge, and is added in excess to the polyacrylic acid.    USE - The method is useful for waste water treatment.    ADVANTAGE - The method utilizes natural flocculants, thus it achieves improved separation result in waste water treatment with good shear stability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for flocculated organic and/or inorganic suspended solids of waste water, comprising flakes of organic and/or inorganic turbidity and cationically charged polyelectrolyte complexes of at least one polysaccharide and polyacrylic acid.
NOVELTY - Pretreatment of biomass solids involves hydrating biomass solids to form a biomass slurry, shear treating biomass solids to reduce the particle size of biomass solids, modify particle or slurry morphology (300), or rupture the cell walls of the biomass solids; and hydrolyzing the biomass solids in the presence of reactive enzymes in a pressure hydrolysis zone (400), where the pressure hydrolysis zone comprises high-shear, high-pressure, low-temperature heat exchange and reaction zone and low-pressure, low-temperature polishing zone.    USE - For pretreatment of biomass solids, use in biofuel production processes, sugar-rich aqueous solution suitable for subsequent chemical, biochemical or enzymatic conversion to valuable fuels, chemicals, or solvents, for synthesis of gasoline-like, jet fuel-like, or diesel-like surrogates, additives (claimed).    ADVANTAGE - The direct integration of enzyme introduction with high shear treatment enables substantial increases in short-term saccharification rates, decreases in overall time required for saccharification, and increases in ultimate sugars yield.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of system for pretreatment of biomass solids.    Biomass dispersion/hydration zone (200)    Disperser (210)    Gravity hopper (220)    Water supply (230)    Heat exchanger/reactor (240)    Modify particle/slurry morphology (300)    Pressure hydrolysis and enzyme introduction zone (400)
NOVELTY - The method involves fabricating a power generator (1000) and power generator is adapted to produce electricity from water. A conductive frame is provided for conducting electrical energy. The conductive frame comprises a metal, metal alloy, graphite, graphene, graphene oxide, hybrid graphene composite, and carbon/metal alloy, hydrogen pathway (1009) and oxygen/air pathway (1013). The insulating plastic frame/other frame is coated with a conductive coating. The conductive coating comprises a solid state material having a band gap material and an electrically conductive material.    USE - Method for generating power from water such as tap water, sea water, urinated water, waste water, distilled water, soft cola, fruit flavored drink, juice, water mix with water soluble solvents.    ADVANTAGE - amount of generated hydrogen gas can be sufficient to provide at least 1000 amperes-hour when the hydrogen gas passes through an effective fuel cell system. In certain exemplary embodiments, the specific reduction reaction using specific chemical combination can produce hydrogen gas at a relatively low cost comparable with energy produced from the combustion of fossil and/or petroleum fuel sources.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the system for generating power from water.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the power generator.    Power generator (1000)    Hydrogen pathway (1009)    Oxygen pathway (1013)    Hydrogen fuel cell system (1014)    Hydrogen generation system (1200)
NOVELTY - The device (1) has a steam supply pipe (21) which is formed with the garbage inlet (11). A microorganism inlet port (12) is protruded towards the stirred tank (2). The steam absorption pipe (72) inhales the steam generated in the stirred tank. A sawdust inlet port (13) injects the microorganism powder into the stirred tank. An electronic valve (84a,84b,85a,85b) opens and closes a condenser (8a,8b) provided with product which entrances into the stirred tank by the generated steam, so that condensed water is ejected through leachate exhaust line (83).    USE - Device for treating food waste in home and restaurant.    ADVANTAGE - The toxicity ejected from the fertilizer raw material can be prevented effectively, so that food waste can be recycled efficiently. The pollution to the environment can be prevented efficiently. The structure of the food Waste treating device is simple, so that food Waste treating device can be assembled/disassembled easily. The shipment cost of the agricultural product can be reduced effectively, so that productivity of the fermented manure can be heightened. The production cost of the agricultural product can be lowered.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing method of food waste treating device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the food waste treating device.    Food waste treating device (1)    Stirred tank (2)    Condensers (8a,8b)    Garbage inlet (11)    Microorganism inlet port (12)    Sawdust inlet port (13)    Steam supply pipe (21)    Steam absorption pipe (72)    Leachate exhaust line (83)    Electronic valves (84a,84b,85a,85b)
NOVELTY - The system has a dry sludge reservoir (55) which exports stored organic waste. A cooling device cools the ejected and dried organic waste. A collector collects the ejected grime and the bad smell inhaled in sludge reservoir (1). A dehydrator (10) is provided with an electrifying unit which moves the organic waste supplied from the sludge reservoir to the dryer input hopper. A dehydration unit accelerates the exhaustion of the moisture ejected from organic waste and collects moisture ejected from organic waste with generated current flow.    USE - Organic waste recycling system.    ADVANTAGE - The drying efficiency of the organic waste can be enhanced, as the dehydration unit is provided for accelerating the exhaustion of the moisture ejected from organic waste. The organic waste can be recycled effectively. The pollution material is not ejected, so that pollution to the environment can be prevented effectively. The facility total energy playback rate is reduced by the percentage of water content of the dryer entry former sludge is drastically lowered. The energy loss rate at the dryer can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the organic waste recycling system. (Drawing includes non-English language text)    Sludge reservoir (1)    Dehydrator (10)    Dry sludge reservoir (55)    Air pre-heater (60)    Dust scrubber (72)
NOVELTY - The device has microorganism culture dispersion unit that is installed at end of solution supply pipe to disperse discharged culture medium (w). An outside air inflow pipe (50) is installed so that one end is connected to outlet pipe side and other end is exposed by outside of upper portion of nutrient solution culture tub. A pair of opening/closing valve (52,62) is installed in end of the solution supply pipe. The bubble is generated in the nutrient solution accommodated in inner side of culture tub and is ejected through outside air inflow pipe to discharge tube.    USE - Nutrient solution manufacturing device installed in livestock excretion processing facility and stockbreeding farmhouse.    ADVANTAGE - The structure of the nutrient solution manufacturing device can be simplified so that the installation can be performed effectively. The contamination of the water quality or soil can be prevented. The nutrient solution can be manufactured using the livestock excretion efficiently. Environmental friendly nutrient solution manufacturing device can be attained. Economical charge of the livestock excretion processing facility and stockbreeding farmhouse can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the nutrient solution manufacturing device.    Transport pipe (30)    Absorption pipe (31)    Outside air inflow pipe (50)    Opening/closing valve (52,62)    Culture medium (w)
NOVELTY - A planetary type full-automatic sludge aerobic fermentation device comprises a cylindrical reactor (3) provided with the aeration system and percolate collecting pipeline system (4), and a stirring system. The reactor sealing cover body is provided with a belt opposite to the distributing system of the axis the cylindrical reactor is equipped with a discharging port. The stirring system comprises an inclined auger which is inclined upwards to the cylindrical reactor, and provided with a gas discharging hole of the reactor sealing cover.    USE - A planetary type full-automatic sludge aerobic fermentation device.    ADVANTAGE - The device has improved aerobic fermentation efficiency, and high degree of automation.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram of the planetary type full-automatic sludge aerobic fermentation device.    Cylindrical reactor (3)    Percolate collecting pipeline system (4)    Percolate collecting tank (20)    Drain pump (21)    Wastewater processing device (22)
NOVELTY - A printing plate frame made of mesh, is placed on a frame, and a conducting sheet is placed under the printing plate. The conducting sheet is maintained at 50-100 degrees C, and solidified to form gasket. The outer portion of the formed product is hardened by supplying heat, such that raw material supplied to the frame is delivered from conducting sheet to obtain fuel cell bipolar plate.    USE - Manufacture of fuel cell bipolar plate (claimed).    ADVANTAGE - The method efficiently provides fuel cell bipolar plate.
NOVELTY - The system has exhausting unit which repowers and exhausts the currently driven material to the material extract portion (40). The deodorizing unit is set with the circulation screw to supply the compost to the material input unit (10). The chain transfer conveyor is set to circulate the compost ejected through the conveyor belt (41). The material extract portion is set with the conveyor belt to extract the eject compost.    USE - System for fermenting mix compost by aerobic treatment of fertilizer raw material.    ADVANTAGE - The influence on the fermentation of compost artificially can be removed at the proper time. The lifetime of the concrete hopper can be prolonged. The cost reduction of the system can be attained. The quality and stability of the product can be improved effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the system for fermenting mix compost.    Material input unit (10)    Dispersion tube (34)    Concrete hopper (36)    Material extract portion (40)    Conveyor belt (41)
NOVELTY - Dry anaerobic high temperature fermentation for producing organic biogas, where the aerobic and anaerobic fermentation processes are carried out in the same container.    USE - Dry anaerobic high temperature fermentation for producing organic biogas (claimed).    ADVANTAGE - In an organic matter fermentation process, odor cannot leak at the aerobic fermentation stage to pollute the external environment. Organic matters can be shifted from an aerobic fermentation process to a dry anaerobic fermentation process seamlessly. The method fully utilizes the heat dissipated in the aerobic process of the organic matters so as to accelerate the biogas production rate and shorten the fermentation cycle of the organic matters under a dry anaerobic high temperature condition, and improve product quality, thus reaching the purposes of lowering running cost, reducing labor intensity, eliminating secondary pollution and improving economic benefits of enterprises. Also, the leachate generated by anaerobic fermentation is utilized as a strain.
NOVELTY - Breeding wastewater processing method comprises dividing wastewater into washing water and waste liquid; collecting washing water, carrying out processing, and breeding wastewater so as to reach the discharge standard; concentrating waste liquid to obtain a clear liquid; recycling concentrated clear liquid; and fermenting concentrated liquid to obtain organic bio-fertilizer.    USE - Method for processing breeding wastewater.    ADVANTAGE - The breeding method avoids the mixing of ammonia-nitrogen and mutual influence of chemical oxygen demand. The waste liquid is used as liquid fertilizer, which provides excellent fertilizer source for agriculture. The washing water after being processed is better than the wastewater discharge standard, and realizes standard discharge of wastewater or water recycling. The method is energy-saving and environment-friendly.    DESCRIPTION OF DRAWING(S) - The drawing is a block diagram of a method for processing breeding wastewater (Drawing includes non-English language text).
NOVELTY - Organic fertilizer comprises 40-60 wt.% of excrement, 3-15 wt.% of straw, 5-10 wt.% of deodorization strains, 4-10 wt.% of calcium superphosphate, 4-10 wt.% of oil cake, 2-5 wt.% of sugar liquid, 1-6 wt.% of plant ash, 1-6 wt.% of zeolite powder and 3-9 wt.% of functional bacteria.    USE - Used as organic fertilizer.    ADVANTAGE - The organic fertilizer is capable of effectively controlling stink of manure and reducing fermentation time to avoid environmental pollution, and reducing the production cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the organic fertilizer, comprising: (a) fermenting the excrement and straw, uniformly stirring the mixture to obtain a mixture, adding water and functional bacteria to the mixture for the fermentation, and dehydrating the mixture to reduce weight percentage to 70-80 wt.%; and (b) adding calcium superphosphate, oil cake, sugar liquid, plant ash, zeolite powder and functional bacteria to the reaction mixture and stirring uniformly, and then stacking and crushing to obtain a finished product.
NOVELTY - Organic fertilizer comprises 60-80 pts. wt. of rabbit dung, 5-8 pts. wt. of Chinese herbal medicine, 10-20 pts. wt. of crop straw powder, 10-20 pts. wt. of plant ash, 10-20 pts. wt. of bagasse, 30-40 pts. wt. of sodium humate, 10-20 pts. wt. of nano-carbon and 10-15 pts. wt. of palygorskite.    USE - The organic fertilizer is useful for reducing insect pests in crops.    ADVANTAGE - The organic fertilizer improves yield and quality of crop and controls the loss of fertilizer in soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the organic fertilizer, comprising mixing the rabbit dung, crop straw powder, plant ash, bagasse and nano carbon, and then adding proper amount of water and stirring, stacking the mixture in a fermentation tank and fermenting for 10-14 days, fermenting the mixture at a temperature of 50-60 degrees C, and drying at 120 degrees C, crushing, mixing the Chinese herbal medicines in the mixture, extracting using water or alcohol by a conventional method, freezing and drying the extract, and passing the dried traditional Chinese medicine extract through a 120-150 meshes sieve to obtain Chinese herbal medicine powder, grinding the palygorskite into powder and then mixing with sodium humate, uniformly mixing, granulating and drying the mixture to obtain the reaction product, or adding wt.% of zeolite and 10-15 wt.% of hydrochloric acid in water, soaking the mixture for 3-4 hours with 10-12% of sodium bicarbonate solution, washing the mixture using de-ionized water until it is neutral, reacting the washed mixture at 500-530 degrees C for 4-5 hours and crushing into a powder, adding 4-5% of sodium lauryl sulfate, 1-2% of zeolite, 3-5% of aluminum hydroxide at 1200-1500 rpm and stirring to obtain a dispersion liquid, and spraying the dispersion liquid on bio-organic fertilizer particle and drying.
NOVELTY - The device has a main reaction cylinder (7) that is provided with several sampling ports (12). A water tank (1) is connected with a water inlet pipe (13) passed through a water inlet of a water inlet pump (2). The water inlet pump is located in the main reaction cylinder that is installed with a DO probe (4) and a pH probe (6). The DO probe is connected with a DO measuring instrument (3). An outer circulating pipe (8) is connected with the main reaction cylinder whose bottom is provided with a sludge discharging pipe (11).    USE - Device for realizing single stage self-cultivation denitrification of urban sewage by inhibiting nitrobacteria.    ADVANTAGE - The device is simple in structure, convenient to manage, small in volume, low in operation cost and high in processing efficiency. The quick and effective inhibition of the nitrobacteria can be realized so that the nitrogen in the sewage can be removed effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for realizing single stage self-cultivation denitrification of urban sewage.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for realizing single stage self-cultivation denitrification of urban sewage.    Water tank (1)    Water inlet pump (2)    DO measuring instrument (3)    DO probe (4)    pH probe (6)    Main reaction cylinder (7)    Outer circulating pipe (8)    Sludge discharging pipe (11)    Sampling ports (12)    Water inlet pipe (13)
NOVELTY - Preparing formestane, comprises epoxidizing (10R,13S)-10,13-dimethyl-1,6,7,8,9,10,11,12,13,14,15,16-dodecahydro-2H-cyclopenta(a)phenanthrene-3,17-dione in the presence of methanol as solvent under the action of hydrogen peroxide and strong base water solution, adding aqueous solution of reducing agent after finishing reaction to stop reaction and then decompressing, concentrating and elutriating to obtain (10R,13S)-10,13-dimethyl-dodecahydro-20-oxa-cyclopropa(4,5)cyclopenta(a)phenanthrene-3,17-dione, and adding solvent and carrying out ring-opening reaction.    USE - The method is useful for preparing formestane (claimed), which is useful for treating breast cancer.    ADVANTAGE - The method allows simple preparation of formestane with mild reaction condition and high yield (more than 43%) and purity (more than 93%) in an eco-friendly manner.    DETAILED DESCRIPTION - Preparing formestane, comprises epoxidizing (10R,13S)-10,13-dimethyl-1,6,7,8,9,10,11,12,13,14,15,16-dodecahydro-2H-cyclopenta(a)phenanthrene-3,17-dione in the presence of methanol as solvent under the action of hydrogen peroxide and strong base water solution, adding aqueous solution of reducing agent after finishing reaction to stop reaction and then decompressing, concentrating and elutriating to obtain (10R,13S)-10,13-dimethyl-dodecahydro-20-oxa-cyclopropa(4,5)cyclopenta(a)phenanthrene-3,17-dione, adding solvent and carrying out ring-opening reaction using solid acid catalyst, filtering solid acid after reaction, and concentrating the filtrate by elutriating or reduced pressure and then filtering, drying and recrystallizing.
NOVELTY - The biological reaction device has a methanol tank, an oil tank, a sulphuric acid overhead tank, a flow meter, a reaction kettle, and a separating tank. The methanol tank, oil tank, and sulphuric acid overhead tank are respectively connected with the flow meter and reaction kettle. The outlet pipe of first reaction kettle is connected to inlet formed on the side of the middle portion of second reaction kettle.    USE - Biological reaction device.    ADVANTAGE - The problems related to the low use rate of the reaction kettle and bad reaction column continuous reaction effect can be solved. The biological reaction device is featured with fast and continuous reaction.
NOVELTY - Composition comprises 15-35 pts. wt. propolis, 15-40 pts. wt. rhizoma alismatis, 15-35 pts. wt. myrobalan, 15-45 pts. wt. Poria, 15-35 pts. wt. Grifola, 15-35 pts. wt. fructus forsythiae, 15-35 pts. wt. Akebia stem, 15-40 pts. wt. Astragalus, 15-35 pts. wt. seaweed, 15-30 pts. wt. dandelion and 15-35 pts. wt. licorice.    USE - The composition is useful for treating urate deposition syndrome of broiler chicken (claimed).    ADVANTAGE - The composition is prepared simply, pollution-free and does not cause toxic side effect or drug residue.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the composition, which involves ultra-micro crushing the above-mentioned raw materials by 700 sieve, (b) mixing propolis, rhizoma alismatis, myrobalan, Poria, and Grifola uniformly, mixing the remaining raw materials uniformly, combining the mixture evenly and continuously and obtaining product.
NOVELTY - Producing ageratum and perilla farm product involves fertilizing fruit of agricultural products and agricultural products in the planting process, each year by the purple perilla oil slag biological organic fertilizer, and adding irrigation water with perilla oil residue to produce liquid bio-fertilizer; preparing fungus by using edible perilla oil residue; injecting skin bast tissue in one time fruit crops purple perilla extract nutrient solution; preparing fruit crops purple perilla nutrient solution, and extracting purple perilla to form ageratum and perilla farm product.    USE - For producing ageratum and perilla farm product (claimed).    ADVANTAGE - The method prepares product that has original flavor, and perilla product nutritive value and health care function.    DETAILED DESCRIPTION - Producing ageratum and perilla farm product involves fertilizing fruit of agricultural products and agricultural products in the planting process, each year by the purple perilla oil slag biological organic fertilizer, after fertilizing and adding irrigation water with perilla oil residue to produce liquid bio-fertilizer; preparing fungus by using edible perilla oil residue as culture medium to culture, and homogenization treatment; injecting skin bast tissue in one time fruit crops purple perilla extract nutrient solution; fruit crops purple perilla nutrient solution is prepared by adding the purple perilla water, and extracting purple perilla to form ageratum and perilla farm product. The fruit crops purple perilla extract nutrient solution preparation method involves uniformly diluting purple perilla extract in water; the fungus product before harvesting the edible mushrooms for 3 to 5 days, spraying edible fungi purple perilla extract nutrient solution to the fungus, spraying to flammulina velutipes noodle in the bead.
NOVELTY - Processing kitchen wastes using microbial agent, is claimed.    USE - The method is useful for processing kitchen wastes using microbial agent including Bacillus subtilis, Bacillus megaterium, Bacillus licheniformis,Cellulomonas flavigena, Bacillus cereus, Bacillus firmus or Bacillus laterosporus (all claimed).    ADVANTAGE - The microbial agent efficiently decomposes the kitchen wastes through screening and separating a set of microbes from natural soil, purifying, acclimatizing and burdening, and is added and uniformly stirred so that the source weight loss rate of the kitchen wastes reaches above 96%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the microbial agent comprising mixing a strain in a culture medium at 28-35 degrees C for 2-30 hours, putting the strain in a sterilized wood chips, crushing the solid culture medium and uniformly mixing the solid culture medium, where the culture medium is nutrient agar culture medium.
NOVELTY - The device has reactor unit provided with packed bed catalytic reactor, two-position four-way valve, two-way stop valve and connection pipe. The lower ends of catalytic reactor are provided with respective gas inlet openings. A heat exchange device is provided with raw material preheating heat exchanger and heat recovery heat exchanger. The raw material pre-heating heat exchanger is set with air outlet pipe through which raw material gas enters into reactor unit. The heat recovery heat exchanger is connected to raw material preheating heat exchanger through pipeline.    USE - Synthetic gas methanation flow conversion reactor.    ADVANTAGE - The synthetic gas methanation flow conversion reactor is provided with high stability, low investment and operation cost and prolonged service life.
NOVELTY - Red mud-added ecological concrete comprises cementing material, aggregate, water and naphthalene-based superplasticizer.    USE - The concrete is useful for purifying sewage (claimed).    ADVANTAGE - The use of red mud improves the pollutant purifying effect of ecological concrete, and simultaneously realizes turning of waste into valuable, and thus it is replaced with cementing materials e.g. cement, and substantially reduces the ecological concrete production cost. The ecological concrete has good strength and considerable practical application values.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the red mud-added ecological concrete, comprising uniformly mixing ore Portland slag cement, aggregate, water, red mud and naphthalene-based superplasticizer.
NOVELTY - An abscisic acid additive is used for promoting quick agricultural waste composting.    USE - An abscisic acid additive is used for promoting quick agricultural waste composting (claimed).    ADVANTAGE - The additive can induce catalase, superoxide dismutase and ascorbate peroxidase active substance scavenging ability, and improves antimicrobial anaerobic ability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the application of abscisic acid additive in agricultural waste composting comprising: mixing 1-10 ppm abscisic acid additive and urban compost material, adding livestock manure or chemical fertilizer, and adjusting carbon/nitrogen (C/N) ratio to 26-30/1, moisture content to 60-65% and stack height to 1.5 m.
NOVELTY - Doxepin hydrochloride (I) is prepared by performing addition reaction between 6H-dibenzo(b,e)oxepin-11-one and 3-chloropropyl-t-butyl ether to obtain the alcohol compound; adding the alcohol compound in concentrated hydrochloric acid under the condition of eliminating hydroxy to obtain olefin-based compound; reacting olefin-based compound and thionyl chloride in reaction solvent for coupling, reacting the obtained chlorinated compound with dimethylamine and forming compound (I).    USE - Method for preparing doxepin hydrochloride (claimed).    ADVANTAGE - The method has good selectivity and high yield. It is environment-friendly, and the catalyst can be used circularly by simple filtering, which reduces production cost. The operation is simple, the raw material is easy to obtain, and the cost is low.
NOVELTY - Preparing microbial fertilizer, comprises culturing photosynthetic bacteria, Actinomyces, and Azotobacter and then amplifying, taking Bacillus subtilis and then culturing and amplifying, mixing mannitol, alginic acid and sodium alginate solution and then stirring, taking obtained biological bacteria, Bacillus subtilis, sodium alginate slurry, monosodium glutamate waste liquid, auxiliary agent, honey, and water and then fermenting, metering the obtained fermentation liquor, and packaging the product.    USE - The method is useful for preparing microbial fertilizer (claimed).    ADVANTAGE - The method simply provides microbial fertilizer with wide application range.    DETAILED DESCRIPTION - Preparing microbial fertilizer, comprises (S01) culturing photosynthetic bacteria, Actinomyces, and Azotobacter and then amplifying to obtain the biological bacteria, (S02) taking Bacillus subtilis and then culturing and amplifying to obtain Bacillus subtilis agent, (S03) mixing mannitol, alginic acid and sodium alginate solution and then stirring to obtain the sodium alginate slurry, and (S04) taking obtained biological bacteria (1-3 in pts. wt.); Bacillus subtilis (5-10 in pts. wt.); sodium alginate slurry (20-30 in pts. wt.); monosodium glutamate waste liquid (20-40 in pts. wt.), auxiliary agent (5-9 in pts. wt.), honey (12-20 in pts. wt.), and water (105-125 in pts. wt.) and then fermenting at 28-35 degrees C to obtain fermentation liquor, and (S05) metering the obtained fermentation liquor, and packaging the product.
NOVELTY - Preparing biological organic fertilizer using carbon dioxide (CO2) and yeast residue comprises: (A) adjusting water content in fermentation waste slag to 50-70%, as fermentation substrate; (B) mixing microbial inoculum with water to obtain mixed liquid microbial inoculum; and (C) mixing mixed microbial inoculum and substrate, stacking on furrow surface of fertilizer, and covering plastic film with moisture, stacking height is 35-45 cm, fermenting for 6-8 days at 15-40 degrees C, to obtain biological organic fertilizer.    USE - Preparing biological organic fertilizer (claimed).    DETAILED DESCRIPTION - Preparing bio-organic fertilizer using carbon dioxide (CO2) and yeast residue comprises:    (A) adjusting water content in fermentation waste slag to 50-70%, as fermentation substrate;    (B) mixing microbial inoculum with water to obtain mixed liquid microbial inoculum; microbial inoculum, fermentation substrate is at a mass ratio of 4-6:1000, weight ratio of water to fermentation substrate is 10-20:1000; and    (C) mixing mixed microbial inoculum and substrate, stacking on furrow surface of fertilizer, and covering plastic film with moisture, stacking height is 35-45 cm, fermenting for 6-8 days at 15-40 degrees C, to obtain biological organic fertilizer.
NOVELTY - Mitoguazone is prepared by reacting pyruvic aldehyde dimethyl acetal and aminoguanidine carbonate in the presence of methanol as reaction medium, adding hydrochloric acid to adjust pH value to 0.8-1.1, freeze drying at 5-10 degrees C, filtering, washing the filter cake with methanol, and drying.    USE - Method of preparing mitoguazone (claimed).    ADVANTAGE - The method has improved yield, improves product quality, reduces preparation cost, is environment-friendly, and recycles solvent.
NOVELTY - Refrigerant comprises a mixed working medium comprising butane (R600) and trifluoroiodomethane (R13I1), where the mass ratio of the butane (R600) to the trifluoroiodomethane (R13I1) is 2-97:3-98.    USE - The refrigerant is useful in heat pump or air conditioner system.    ADVANTAGE - The refrigerant does not damage ozone layer, and has low greenhouse potential effect.
NOVELTY - Preparing ethanol gasoline comprises: (A) adding salt to ethanol, adding water and gasoline, mixing uniformly, where volume percentage of ethanol concentration is 20-90%; and (B) separating phase to obtain ethanol gasoline.    USE - Preparing ethanol gasoline.    ADVANTAGE - The method has simple technique, low equipment investment, and does not discharge harmful substance.
NOVELTY - A non-methane hydrocarbon recovering method involves sequentially subjecting adsorption tower to steps such as low-pressure adsorption, uniform pressure rising, pressure rising, high-pressure adsorption, uniform pressure dropping, replacing, reverse releasing, evacuation and pressure rising in circulating mode.    USE - Process for recovering non-methane hydrocarbon from polyolefin tail gases.    ADVANTAGE - The process enables recovering non-methane hydrocarbon from polyolefin tail gases in a simple and easy manner with high yield and with less consumption of energy.
NOVELTY - Preparation of L-alanyl-L-glutamine involves adding solvent in reaction container, stirring, adding N-phthaloyl-L-alanyl-L-glutamine, conducting ice bath, dripping short chain amine solution to clear solution, adding rest of short chain amine solution, finishing dripping, reacting, concentrating, crystallizing, filtering, and drying filter cake at normal pressure to obtain a crude product, adding water to dissolve the crude product at room temperature, stirring and dripping short chain alcohol for crystallizing and purifying.    USE - Preparation of L-alanyl-L-glutamine (claimed).    ADVANTAGE - The L-alanyl-L-glutamine is manufactured efficiently with high safety, high purity, excellent workability and optical rotation, and reduced impurity content.    DETAILED DESCRIPTION - Preparation of L-alanyl-L-glutamine involves adding solvent in reaction container, stirring, adding N-phthaloyl-L-alanyl-L-glutamine, conducting ice bath, dripping short chain amine solution to clear solution, removing ice bath, adding rest of short chain amine solution, finishing dripping, reacting at room temperature, concentrating by decompressing with ice bath to remove excess of the short chain amine to adjust pH to 6-7, crystallizing, filtering, and drying filter cake at normal pressure to obtain a crude product, adding water to dissolve the crude product at room temperature, stirring and dripping short chain alcohol for crystallizing and purifying.
NOVELTY - Insecticide prepared by (i) dissolving cypermethrin in 0.5-5 pts. vol. cosolvent completely to form a mixed solution, (ii) adding 5-10 pts. vol. vegetable oil into the mixed solution and stirring, and (iii) adding 0.5-3 pts. vol. emulsifying agent and mixing uniformly, where the total volume ratio of cypermethrin with the cosolvent, vegetable oil and emulsifying agent is 0.04-0.05 kg/l is claimed.    USE - Used as an insecticide.    ADVANTAGE - The insecticide uses vegetable oil instead of light aromatic organic solvents; does not contain benzene, toluene or xylene; is environmentally friendly; and exhibits better insecticidal effect when compared with the existing miscible oil preparation with the same dosage.
NOVELTY - Preparing fertilizer, comprising dry rabbit manure powder, sheep bone powder, pig bone powder, shrimp powder, lobster powder, soybean straw powder, sorghum straw powder, hawthorn powder, distillers grain powder, rhizoma gastrodiae powder, Eucommia bark powder, garlic powder, Schisandra berry powder, Pinellia powder, Angelica powder, Coptis and largehead Atractylodes rhizome powder, is claimed.    USE - The fertilizer is useful for culturing giant knotweed (claimed).    ADVANTAGE - The method has simple preparation procedures. The fertilizer is economical, and easily available; facilitates dense and rapid growth of good quality giant knotweed having good taste, produces fresh and delicious plants rich in nutrition, and having high medicinal value, and 100 wt.% natural green giant knotweed; and provides high light absorbing and disease preventing performance to the plant.    DETAILED DESCRIPTION - Preparing fertilizer, comprising 10-16 wt.% dry rabbit manure powder, 8-12 wt.% sheep bone powder, 12-16 wt.% pig bone powder, 6-8 wt.% shrimp powder, 10-12 wt.% lobster powder, 4-8 wt.% soybean straw powder, 2-6 wt.% sorghum straw powder, 2-6 wt.% hawthorn powder, 1-3 wt.% distillers grain powder, 2-4 wt.% rhizoma gastrodiae powder, 1-3 wt.% Eucommia bark powder, 8-10 wt.% garlic powder, 2-4 wt.% Schisandra berry powder, 2-4 wt.% Pinellia powder, 2-4 wt.% Angelica powder, 2-4 wt.% Coptis and 2-4 wt.% largehead Atractylodes rhizome powder, is claimed.
NOVELTY - Preparing daidzein from kudzu root comprises cleaning kudzu root, cutting into pieces; fine crushing kudzu root, putting in the fermentation tank, adding water and nutrient and uniformly stirring; carrying out sterilizing treatment; adding water strain for fermentation in the fermentation tank; and fermenting.    USE - The method is used for preparing daidzein from kudzu root (claimed).    ADVANTAGE - The daidzein preparation method above is improved, low cost, and environment-friendly and produces daidzein of high yield and purity.    DETAILED DESCRIPTION - Preparing daidzein from kudzu root comprises (a) cleaning kudzu root, cutting into pieces with 2 cm in length, 1 cm in width, and 0.8 cm height; (b) fine crushing kudzu root to form 3-5 mm, putting in the fermentation tank, adding water and nutrient and uniformly stirring; (c) carrying out sterilizing treatment to the mixture in the fermentation tank; (d) adding water strain for fermentation in the fermentation tank; and (e) fermenting, mixing liquid by macro-porous absorption resin, where absorbing speed is 3-5 ml/minute and absorbing time is 1-3 hours, adding 75-95% ethanol, decompressing and evaporating ethanol, drying to obtain the high purity daidzein.
NOVELTY - A nanocarbon biological bacteria fertilizer comprises Actinomyces microflavus, nanocarbon material, an organic fertilizer, and inorganic nutrient elements.    USE - A nanocarbon biological bacteria fertilizer for apple.    ADVANTAGE - The fertilizer has improved bacteriostatic ability and inhibiting effect to plant pathogenic bacteria, improves apple root development, increases root length by more than 30%, improves coloring rate of apple by 37-45%, makes apple skin crisp and have good mouthfeel and sweet taste, improves sugar content of apple by 17-25%, lightens apple ski, and prolongs apple tree life.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the nanocarbon biological bacteria fertilizer comprising fermenting A. microflavus at 38-42oC for 60-70 hours using a Gause culture medium while controlling fermentation pH value at 6-8, inoculating 0.05-0.7 wt.% obtained product to 20-40 meshes organic fertilizer added with nano carbon material, adding inorganic nutrient elements, covering with plastic, and fermenting at 38-58 degrees C for 8-10 days while controlling pH value to 6-8 and turning over every 24 hours.
NOVELTY - A sweet potato seedling bed special fertilizer comprises 77-88 wt.% oil slag, 10-20 wt.% ammonium sulfate, 0.5-1.2 wt.% potassium sulfate, 0.5-1.2 wt.% monoammonium phosphate, 0.7-1.7 wt.% urea, and 0.006-0.01 wt.% agricultural streptomycin. The oil slag is prepared by crushing sesame oil extraction residue to obtain powder having a size of 2-5 mm, adding 50-60 wt.% water, mixing, covering with plastic film, fermenting for 30-60 days, and drying until water content is 10 wt.%.    USE - A sweet potato seedling bed special fertilizer.    ADVANTAGE - The fertilizer is rich in nutrition, meets potassium and nitrogen requirement, has long fertilizer efficiency and stable performance, and has cheap raw materials and simple preparation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the sweet potato seedling bed special fertilizer comprising preparing oil slag, screening to obtain powder having a size of 2-5 mm, adding remaining raw materials, and mixing.
NOVELTY - Recycling acetaminophen from mother liquor comprises (i) heating and filtering the mother liquor of the acetaminophen to obtain filtrate, (ii) washing the filtrate by using a simulated moving bed ion exchange system equipped with resin for the adsorption of acetamidophenol, eluting adsorbed acetamidophenol by using acetic acid solution, and collecting excess acetic acid eluent, and (iii) concentrating the eluent to obtain crystal.    USE - The method is useful for recycling acetaminophen from mother liquor.    ADVANTAGE - The method: utilizes simulated moving bed ion exchange system to remove the residual mother liquor of acetaminophen; recycles acetaminophen with a purity of more than 98.5%; is economical and environmentally friendly; and reduces the discharge of waste water without organic solvent and impurities.
NOVELTY - Preparing organic fertilizer by fermenting rapeseed cakes, involves (a) drying and crushing rapeseed cake, adding corn meal, bran or rice bran, fermenting the obtained mixture, and diluting product, (b) mixing sawdust and rapeseed cake solution, and scattering microbial strains, (c) covering piles, and (d) increasing temperature to 60 degrees C or more, and turning piles once, where the fermentation is completed after the piles are totally turned twice to three times.    USE - The method is useful for preparing organic fertilizer (claimed) which is useful for inhibiting plant diseases, and controlling insect pests in plants.    ADVANTAGE - The method is simple and convenient to perform. The fertilizer improves soil condition e.g. pH value which is good for growth of crops.    DETAILED DESCRIPTION - Method for preparing organic fertilizer by fermenting rapeseed cakes, involves (a) drying and crushing 1-1.5 tons rapeseed cake, adding 5-10 kg corn meal, bran or rice bran to the crushed rapeseed cake, mixing the obtained mixture, fermenting the obtained mixture, and diluting the fermented product without adding water, (b) mixing sawdust and rapeseed cake solution uniformly, scattering microbial strains while the rapeseed cakes are mixed, and adjusting moisture to 60-65%, (c) maintaining heights of the fermentation piles to 1.5 m, width to 2m and the total volume to not less than 3 m3, covering piles by air permeable coverings to keep out from light and rain, and (d) increasing temperature to 60 degrees C or more within 1-3 days of initiation of fermentation treatment, and turning piles once, where the fermentation is completed after the piles are totally turned twice to three times.
NOVELTY - Device comprises to-be-processed wastewater storage tank which is connected with reactor through water pipeline and pump. The reactor is also connected with treated wastewater storage tank through water pipeline and pump. The reactor is provided with sieve of filler layer at bottom plate which is provided with filler layer. The reactor is also provided with air compressor and aerator. The bottom of the reactor is provided with sludge discharging pipe.    USE - The device is useful for biochemical treatment of high concentration organic wastewater (claimed).    ADVANTAGE - The device optimizes the type of filler and structure of reactor, preferably programmable controller (PLC) automatic control system, improves processing efficiency, and degrades high concentration organic wastewater and hence achieves purpose of directly discharging the water.    DETAILED DESCRIPTION - Device comprises to-be-processed wastewater storage tank which is connected with reactor through water pipeline and pump. The reactor is also connected with treated wastewater storage tank through water pipeline and pump. The reactor is provided with sieve of filler layer at bottom plate which is provided with filler layer. The reactor is also provided with air compressor and aerator. The bottom of the reactor is provided with sludge discharging pipe. The filler layer comprises spherical hydrophilic polyurethane foam, and combination of modified plastic suspension ball and ceramic ring filler.
NOVELTY - Preparation of water-soluble clopyralid choline salt involves, reacting the choline aqueous solution and clopyralid raw material medicine, using the water as a medium, stirring, reacting for 30-60 minutes when the pH is 6.0-10.0 at 35-75 degrees C; and adding surfactant (2-8 mass%), stirring, obtaining the water-soluble clopyralid choline salt, where the mole ratio of the choline and clopyralid in the choline solution is 1:0.8-1.1, and the water amount is determined according to the choline solution and the moisture of the clopyralid choline salt.    USE - For the preparation of water-soluble clopyralid choline salt (claimed) which is used as an herbicide.    ADVANTAGE - The preparation method is simple, and does not waste water, distillate and mother liquid, thus has good environmental protection. The obtained clopyralid choline product has high purity, strong stability without dust, and good solubility; is convenient to use; and is cost-effective and environmental friendly.
NOVELTY - Plastic pole frame electrode plate capable of measuring water electrolysis voltage in hydrogen electrolysis comprises metal main electrode plate (1), electrolytic voltage measuring pole, and engineering plastic electrode frame (2), where the engineering plastic electrode frame is integrally formed and wrapped on the main board to the outer edge of the pole. The first pole of the main electrode plate is measured, and the other passes through the exposed engineering plastic electrode frame.    USE - Plastic pole frame electrode plate capable of measuring water electrolysis voltage in hydrogen electrolysis.    ADVANTAGE - The electrode plate has excellent electric insulating performance. It can detect the electrolytic voltage of each electrolysis chamber. The process is simple, and the main electrode plate is convenient to weld without deformations.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation method of electrode plate comprising measuring electric pole on the metal main electrode plate, and injection molding with engineering plastic electrode frame.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the plastic pole frame electrode plate capable of measuring water electrolysis voltage in hydrogen electrolysis.    Metal main electrode plate (1)    Engineering plastic electrode frame (2)
NOVELTY - Field cultivation of grassland white mushroom includes using artificial cultivation method to cultivate stock culture, rejuvenating stock culture, cultivating stock seed and cultivar, preparing cultivation material according to biological characteristic of grassland white mushroom, processing into cultivating bag in-built cultivation material by using jute sheet, where cultivating strain is added in the bag, placing under the canopy frame in selected planting plan area, and following the geoherbalism of grassland white mushroom.    USE - Field cultivation of grassland white mushroom (claimed).    ADVANTAGE - The method realizes raw white mushroom artificial culturing under the original ecological environment, keeps the rich nutrients of raw white mushroom according to its biological characteristics, fresh flavor, and edible, medical, and healthcare value, does not use fertilizer and agrochemicals, does not damage the grassland ecology, keeps the natural non-polluting characteristics of wild grassland white mushroom, and protects the grassland ecological environment.    DETAILED DESCRIPTION - Field cultivation of grassland white mushroom comprises using artificial cultivation method to cultivate stock culture, rejuvenating stock culture, cultivating stock seed and cultivar, preparing cultivation material according to biological characteristic of grassland white mushroom, processing into cultivating bag in-built cultivation material by using jute sheet, where cultivating strain is added in the bag, placing under the canopy frame in selected planting plan area, following the geoherbalism of grassland white mushroom, and taking advantage of the local climate and natural vegetation condition in the grassland white mushroom original ecology area, where grassland white mushroom is produced in a large scale assisted with manual intervention measures.
NOVELTY - The system has heat insulating cover modules (10) which are combined to seal upper portion of bioreactor (1). A deodorization furnace is mounted with deodorizing panel for absorbing bad smell. An air flow channel is formed in left and right portions of bottom of blower (34). A bad smell adsorption media is built in panel. A polygonal microorganism deodorization filter medium area is combined in adsorption media outer periphery. A second concavo-convex region of upper portion of second deodorization panel is combined to first concavo-convex region of upper portion of panel.    USE - System for heat insulating covering of bio reactor for public sewage treatment facilities with offensive odor treatment function.    ADVANTAGE - The trimethylamine, the methyl mercaptan, the methyl sulfide, acetaldehyde, the dimethyl disulfide, the styrene, etc., are removed from the public sewage by using the natural energy as generated heating source or the air-supply at low power consumption.    DETAILED DESCRIPTION - The synthetic resin of 20-65 weight%, and starch of 10-40 weight% and inorganic material of 10-70 weight% are synthesized to remove bad smell.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of system for heat insulation covering of bio reactor.    Bio reactor (1)    Heat insulation covering modules (10)    Blower (34)    Cover (42)    Air outlet (44)
NOVELTY - The installation has a logic controller (3) connected to a pressure sensor (2) and a fuel cell (4). The controller calculates output gas flow rate of pressurized fuel gas e.g. hydrogen, tank (1) from variation of pressure (P) measured by the sensor in the tank, and theoretical electric charge produced by the cell from the flow rate. The controller calculates real electric charge (C) produced by the cell for being compared with the theoretical electric charge. The controller detects a gas leakage in the installation when the theoretical charge exceeds the real charge by a given threshold.    USE - Fuel cell installation.    ADVANTAGE - The logic controller enables detecting and locating the gas leakage in a high pressure circuit and a low pressure circuit of the installation in an accurate manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for detecting a fuel gas leakage in a fuel cell installation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic and partial view of an installation for supplying fuel gas to a fuel cell.    Real electric charge (C)    Pressure (P)    Pressurized fuel gas tank (1)    Pressure sensor (2)    Logic controller (3)    Fuel cell (4)
NOVELTY - Phenolic compounds (A) comprising 3-(dimethylamino)-1-(3-hydroxyphenyl)-2-methylpropan-1-one (VII) and (2S)-3-dimethylamino-1-(3-hydroxyphenyl)-2-methyl-propan-1-one (V), are new.    USE - (A) are useful as an intermediate for preparing tapentadol.    ADVANTAGE - (A) provide tapentadol with high yield in a simple, cost-effective, eco-friendly and commercially viable manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a substituted dimethyl-((R)-2-methyl-3-phenyl-pentyl)-amine compound of formula (IIIa);    (2) preparing 3-((R)-3-dimethylamino-1-ethyl-2-methyl-propyl)-phenol (II), comprising (a) acylating 3-((S)-3-dimethylamino-1-ethyl-1-hydroxy-2-methyl-propyl)-phenol with an acylating agent to obtain (IIIa), (b) hydrogenolyzing (IIIa) using a suitable catalyst in a reactioninert solvent in the presence of hydrogen to obtain (II), and (c) optionally converting (II) into an acid addition salt;    (3) preparing 3-((S)-3-dimethylamino-1-ethyl-1-hydroxy-2-methyl-propyl)-phenol (IV), comprising (a1) reacting 1-(3-hydroxyphenyl)propan-1-one with dimethylamine hydrochloride and paraformaldehyde under Mannich reaction conditions in an inert reaction medium to obtain beta -dimethylaminoketone of (VII), (b1) resolving (VII) with one or more of suitable resolving agent, and (c1) reacting the resolved compound and (V) with an ethyl magnesium halide in an inert reaction medium under Grignard conditions to obtain (IV);    (4) tapentadol hydrochloride containing less than 0.2% of the impurity N-desmethyl, N,N-didesmethyl and (2S,3R)-1-(dimethylamino)-3-(3-hydroxyphenyl)-2-methyl-3-pentanol; and    (5) a tapentadol or its salt, preferably tapentadol hydrochloride or tapentadol hydrobromide having an X-ray powder diffraction pattern value as given in the specification.    Acyl = CH3-CO, CF3-CO, CH2Cl-CO-, CHCl2-CO-, CCl3-CO-, CH3OCO-, CH3CH2O-CO, CH3O-CO-CO-, CH3CH2O-CO-CO-, phenyl-CO- or meta-CH3COO-phenyl-CO-.
NOVELTY - The apparatus has scum-mixing crusher (31) whose upper portion is provided with sampled biogas in acid fermenter (20). Organic waste is transferred through a feed pump (27) from the acid fermenter, and gas inlet is connected to an outer fringe upper side of separator main portion along tangential direction. A vent is configured to eject the fine dust. The sludge flowed in from a lower portion of acid fermenter through acid fermenter circulation inducing path (61) is heated and sent to the acid fermenter through acid fermenter circulation outlet channel (62).    USE - Temperature selectable apparatus for anaerobic treatment of organic waste.    ADVANTAGE - Moisture and impurity contained within the biogas can be efficiently separated, and scum generated among the anaerobic digestion operation can be controlled. Stable operation of biogas can be achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the anaerobic digestion system. (Drawing includes non-English language text)    Acid fermenter (20)    Feed pump (27)    Scum-mixing crusher (31)    Acid fermenter circulation inducing path (61)    Acid fermenter circulation outlet channel (62)
NOVELTY - The apparatus has a crusher (120) that is installed in a main portion (110) in the lower end of an input hopper (111) for smashing the lumber in the input hopper. The input hopper is formed in the upper side of the main portion. A press machine is installed at the lower portion of a pulverizing device (130) which is installed in the lower portion of a hopper (140). The pulverizing device is provided to pulverize and collect the sawdust crushed in the crusher. A pellet storage box (170) stored the pellet which is installed at the cutting blade.    USE - Apparatus for manufacturing integrated miniature pellet such as sawdust, waste tire and food waste.    ADVANTAGE - Since the apparatus performs fracturing, drying and molding of the pellet together, volume of the pellet can be reduced. Hence the portability and installation nature of the apparatus is increased and the convenience of the user is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the integrated miniature pellet manufacture apparatus.    Main portion (110)    Input hopper (111)    Crusher (120)    Pulverizing device (130)    Hopper (140)    Pellet storage box (170)
NOVELTY - The method involves crushing the food waste, and removing the foreign substance in food waste. The dehydrating liquid of food sludge obtained by the food dehydrator (200) is removed by a deintercalation screen (300). The collected supernatant sludge is passed to an oil scum segregation unit (400) that separates oil and scum. The mixed solution containing liquid mixed with hydroxyl radical is transferred to mixed solution reservoir (600). The oil contained in organic waste is used as bio-diesel fuel. The removed food sludge and separated scum are mixed with the compost or fodder.    USE - Method for recovering organic waste such as food waste used for producing liquid fertilizer, bio-diesel fuel and biogas. Can also be used in industrial waste water treatment, and food source for microorganism.    ADVANTAGE - The oil contained in the organic waste can be recycled and used bio-diesel fuel. The processing time of supernatant sludge can be reduced. The environmental contamination can be prevented. The processing cost can be reduced. The degradable material can be analyzed easily, since the hydroxyl radical is provided to the mixed solution reservoir.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram illustration the process for recovering organic waste. (Drawing includes non-English language text)    Crashing-separator (100)    Food dehydrator (200)    Deintercalation screen (300)    Oil scum segregation unit (400)    Mixed solution reservoir (600)
NOVELTY - This utility model claims a methanol fuel cell testing system for tail gas processing device, comprising a condensing device, the second condensing device, a first electromagnetic valve, a second electromagnetic valve and a water pump, the fuel cell stack anode outlet is connected with a condensing device, a condensing device from the gas discharge to the outside, the first condensing device from the liquid through the first electromagnetic valve through the water pump to the outside, fuel cell stack cathode outlet is connected with the second condensing device is connected with the second condensing device from the gas discharge to the outside, the second condensing device from the liquid through the second electromagnetic valve through the water pump to the outside, it is a tail gas processing effect is good.
(CN202798114-U)   NOVELTY - A kind of fuel battery power supply system. The power supply system for driving a load, and comprises a main power device and a spare power supply device. Main electric power equipment according to a commercial power, a main power to the load. When the commercial power is not in accordance with a first preset condition, the spare electric power device provides a spare electric power to a load, and comprises a recombination unit, a fuel cell unit, a switch unit and a control unit. Recombination unit recombination a methanol composition, for generate a hydrogen composition. Fuel battery unit receives the hydrogen component for generating a first power. Switch unit detects commercial power and converting the first power to generate electric power for further use. When the commercial power is not in accordance with a preset condition, the control unit enabling recombination device, a fuel cell unit and a conversion unit, which is used for generating electric power for further use.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a power supply system.    Power supply system (10)    Main power apparatus (110)    Recombination unit (121)    Fuel cell unit (122)    Transformation unit (123)    Control unit (124)
NOVELTY - N-substituted indole diketone compound (I) is new.    USE - New N-substituted indole diketone compound (I) used as drug molecules active skeleton or as organic synthesis intermediates in pharmaceutical chemistry.    ADVANTAGE - The compound (I) has easy to obtain raw materials, high reaction yield reaching 85%, and wide substrate application. It is prepared using existing solvent, has simple operation, mild reaction condition, and environment friendly.    DETAILED DESCRIPTION - N-substituted indole diketone compound of formula (I) is new.    R1=OMe or OEt;    R2=phenyl group of formula (1a), 1-12 C alkyl, isopropyl, cyclopropyl, benzyl, alkyl, phenethyl, hydroxyethyl, furan-2-ylmethyl, or naphthalen-1-yl; and    R3=H, Me, -OMe, -OEt, -Br, -Cl or -COOEt.    An INDEPENDENT CLAIM is included for preparation of compound (I).
NOVELTY - Preparing culture fertilizer for culturing Acanthospermum using 16-20 wt.% peanut cake powder, 12-16 wt.% bean cake powder, 8-12 wt.% bean powder, 10-14 wt.% towel gourd powder, 1-3 wt.% largehead Atractylodes rhizome powder, 1-3 wt.% garlic powder, 15-17 wt.% liquorice powder, 4-6 wt.% prepared rhizome of Rehmannia powder, 2-4 wt.% radix paeoniae alba powder, 4-6 wt.% malt powder, 2-4 wt.% and 1-3 wt.% radix pseudostellariae powder, 1-3 wt.% pine needle powder, 1-3 wt.% pumpkin powder, 1-3 wt.% Asparagus powder, and 1-3 wt.% sheep bone powder is claimed.    USE - The method is useful in preparing culture fertilizer for culturing Acanthospermum (claimed).    ADVANTAGE - The method has simple preparation process. The fertilizer is economical; is prepared using easily available raw materials; improves quality of vegetable with dense and strong growth; improves light absorbing efficiency of plant; improves the disease resistance property, and enhance freshness, taste, and nutrition of the vegetable, which is 100% natural green vegetable with high medicinal value.
NOVELTY - A multi-effect methanol gasoline additive contains 15-20 pts. wt. isobutanol, 3.08-9.39 pts. wt. isoamylol, 10-13 pts. wt. acetone, 16-21 pts. wt. xylene, 12-15 pts. wt. tert.-butanol, 21-25 pts. wt. methyl tert.-butyl ether, 1-1.7 pts. wt. cerium nitrate, 0.7-1.6 pts. wt. 2,4-dimethyl-6-tert.-butyl-phenol, 0.22-0.35 pt. wt. 102 TB corrosion inhibitors, and 6-8 pts. wt. iron cyclopentadiene.    USE - A multi-effect methanol gasoline additive (claimed).    ADVANTAGE - Raw material is easy to obtain, and multi-effect methanol gasoline additive is low cost, has good anti-knock property, has good volatility and stability, is environment-friendly, has anti-oxidant component which has dispersed sediment particle with anti-polymerization rubber stabilizing effect of oil, avoids filter and nozzle pollution and blockage, and improves safety of methanol gasoline.
NOVELTY - Synthesizing varenicline intermediate 2,3,4,5-tetrahydro-1,5-methano-1H-3-benzazepine hydrochloride, comprises (i) performing Mannich reaction of 2-indanone, benzyl amine compound (I) and paraformaldehyde under alkaline or acidic condition to generate 10-benzyl-10-azatricyclo(6.3.1.02,7)dodeca-2,4,6-trien-12-one compound (II); and (ii) reacting (II) with a reducing agent under the acidic or basic condition to reduce the carbonyl into methylene and performing debenzylation.    USE - The method is useful for synthesizing varenicline intermediate 2,3,4,5-tetrahydro-1,5-methano-1H-3-benzazepine hydrochloride.    ADVANTAGE - The method has wide material source mild reaction conditions, simple operation, easy product purification, and high total yield; and is economical, environmentally friendly, and suitable for industrial production.    DETAILED DESCRIPTION - Synthesizing varenicline intermediate 2,3,4,5-tetrahydro-1,5-methano-1H-3-benzazepine hydrochloride, comprises (i) performing Mannich reaction of 2-indanone, benzyl amine compound of formula (I) and paraformaldehyde under alkaline or acidic condition to generate 10-benzyl-10-azatricyclo(6.3.1.02,7)dodeca-2,4,6-trien-12-one compound of formula (II); (ii) reacting (II) with a reducing agent under the acidic or basic condition to reduce the carbonyl into methylene and performing debenzylation.    R = H, methyl, ethyl, isopropyl or tert-butyl.
NOVELTY - Preparing N-(5-methoxycarbonyl-2-hydroxyphenyl)amino-acid ester compound, comprises e.g. reacting N-aryl reagent with amino acid methyl ester in an organic solvent in presence of a catalyst and a dehydrating agent, then cooling, filtering, concentrating, and separating and/or recrystallizing, where the N-aryl reagent is methyl 3-dehydroshikimate, ethyl 3-dehydroshikimate or propyl 3-dehydroshikimate, the catalyst is p-toluenesulfonic acid, formic acid, acetic acid, sulfuric acid, phosphoric acid, ferric chloride, aluminum chloride or zinc chloride, and the reaction temperature is 20-100 degrees C.    USE - The method is useful for preparing N-(5-methoxycarbonyl-2-hydroxyphenyl)amino-acid ester compound.    ADVANTAGE - The method: utilizes cheap and easily available methyl 3-dehydroshikimate as N-aryl reagent, which belongs to renewable non-food biomass resources; has mild reaction condition without noble metal catalysis, and simple operation and high product yield; is suitable for large scale production; and produces (I) with phenolic hydroxy group at 2nd position and methyl carboxylate group at 5th position of benzene ring, which further provides a good space for derivatization.    DETAILED DESCRIPTION - Preparing N-(5-methoxycarbonyl-2-hydroxyphenyl)amino-acid ester compound, comprises reacting N-aryl reagent with amino acid methyl ester in an organic solvent in presence of a catalyst and a dehydrating agent, then cooling, filtering, concentrating, and separating and/or recrystallizing, where molar ratio of N-aryl reagent to amino acid methyl ester is 1:1-1.2, molar ratio of N-aryl reagent to the catalyst is 1:0.01-0.1, the N-aryl reagent is methyl 3-dehydroshikimate, ethyl 3-dehydroshikimate or propyl 3-dehydroshikimate, the catalyst is p-toluenesulfonic acid, formic acid, acetic acid, sulfuric acid, phosphoric acid, ferric chloride, aluminum chloride or zinc chloride, and the reaction temperature is 20-100 degrees C.
NOVELTY - The method involves subjecting a biomass feedstock to pretreatment for removing mechanical impurities such as soil and sand and crushing the feedstock to a size of about 1-5mm. The feedstock is subjected to pyrolysis to demoisturize and obtain a solid product at a temperature of 180-400 degree centigrade. The solid product is gasified at a temperature of 700-1200 degree centigrade by utilizing nickel/dolomide as catalyst. The synthesis gas is cooled to remove plastic and water.    USE - Method for gasifying a biomass feedstock to obtain synthesis gas utilized for small or industrial scale production. Uses include but are not limited to straw, rice husk, peanut shell, sawdust and wood.
NOVELTY - Accelerating an electrolysis device comprising an electrolyzer (1), which is arranged downstream to a reactor tank (3), comprises reacting oxygen with hydrogen to form water, such that an oxygen content in a hydrogen gas stream rising from the electrolyzer is reduced, where during accelerating the electrolyzer, the hydrogen gas stream rising from the electrolyzer is directed into the reactor tank via a bypass line. The electrolysis device operates at a predetermined operating pressure.    USE - The method is useful for accelerating an electrolysis device.    ADVANTAGE - The method and the device are simple and safe, and avoid the use of expensive nitrogen or other inert gas for flushing the reactor tank and the system during accelerating the electrolysis device.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an electrolysis device comprising an electrolyzer and a reactor vessel, where a bypass line is provided in the electrolysis device, for bypassing a hydrogen gas stream rising from the electrolyzer into the reactor vessel.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of a portion of electrolysis device.    Electrolyzer (1)    First assembly (2)    Reactor tank (3)    Second assembly (4)    First valve (5)
NOVELTY - Preparing dronedarones (I), comprises either reacting N-(3-benzoyl-2-butyl-benzofuran-5-yl)-methanesulfonamide compounds (II) with 3-dibutylamino-propan-1-ol (III), or reacting (2-butyl-5-nitro-3-benzofuranyl)(4-hydroxyphenyl)methanon (VIII) with activated form of a sulfur dioxide compound (IX), isolating the obtained product, if desired, and converting into their salts.    USE - The method is useful for preparing (I) (claimed) for treating arrhythmia. No biological data given.    ADVANTAGE - The method provides (I) with high yield and good purity using simple and environmentally compatible reagents.    DETAILED DESCRIPTION - Preparing dronedarones (I) or their salts, comprises either reacting N-(3-benzoyl-2-butyl-benzofuran-5-yl)-methanesulfonamide compounds of formula (II) with 3-dibutylamino-propan-1-ol (III), or reacting (2-butyl-5-nitro-3-benzofuranyl)(4-hydroxyphenyl)methanon (VIII) with activated form of a sulfur dioxide compound of formula (HO-SO2-L2) (IX), isolating the obtained product, if desired, and converting into their salts.L, L2 = leaving group.    INDEPENDENT CLAIMS are included for:    (1) the compounds (II) or their salts;    (2) preparing (II), comprising reacting 2-butyl-5-methanesulfonylamido-benzofuran (IV) with benzoyl chloride of formula (V) when L is halogen, or mesylation of (5-amino-2-butyl-benzofuran-3-yl)-phenyl-methanone compounds of formula (VI), when L is different from halogen, isolating the obtained product, if desired, and converting into their salts;    (3) the compounds (VI) or their salts;    (4) preparing (VI), comprising hydrogenating (2-butyl-5-nitro-benzofuran-3-yl)-phenyl-methanone compounds of formula (VII), isolating the obtained product, if desired, and converting into their salts;    (5) the compounds (VII); and    (6) preparing (VII) comprising reacting (VIII) with (IX).    L1 = leaving group different from halo; and    Hal = halo.
NOVELTY - Container assembly of a biogas plant, comprises a first container (1) having a bottom and a circumferential wall, where the wall of the first container is supported outwardly against at least one second container (3).    USE - The container assembly is useful for a biogas plant.    ADVANTAGE - The container assembly: is assembled at the construction site using prefabricated elements in a simple and rapid manner; is simple, and can be transported in a compact manner; and exhibits large container volume.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for container of the container assembly, comprising at least one clamping element within the container, which stiffens the second container against bending forces from the internal pressure of the first container resulting on the second container, and a wall section as window surface that is surrounded by a reinforcing frame.    DESCRIPTION OF DRAWING(S) - The figures 1-4 show a schematic representation of the container assemblies.    First container (1)    Second container (3)
NOVELTY - Ethanol is manufactured by reacting cellulose biomass simultaneously with hydrolase, yeast which is fermented microorganisms, and organic waste e.g. garbage, foodstuff waste material, agricultural waste material, livestock farming waste material, sewage sludge, and/or organic sludge. The initial stage addition dry weight of yeast per reaction tank is 0.125-0.0025 g/kg.    USE - Manufacture of ethanol using biomass (claimed).    ADVANTAGE - Initial stage usage-amount of microorganisms for fermentation can be reduced, and stable reaction can be achieved.
NOVELTY - Producing biofuel involves growing 5-30wt.% (particularly 18-25wt.%) microalgae in ponds or suitable containers containing water and nutrients. A device is provided for delivering carbon dioxide in the water present in pond or containers. Nutrients such as carbohydrates and proteins are added to the container, where water is natural or artificial fresh water or salt water. Hydrothermal treatment of biomass is performed and then the biomass is recovered and heated for one minute. The obtained material is cooled in order to transfer the material into biofuel.    USE - Integrated method for producing biofuel from microorganisms, such as heterotrophic phototrophs.    ADVANTAGE - Integrated method enables to produce single biofuel or multiple biofuels simultaneously.
NOVELTY - The method involves heating the waste or organic byproduct for decreasing humidity, and performing dehydration of the waste or organic byproduct. The dehydrated waste or organic byproduct is pasteurized by adjusting the humidity. The pasteurized product is stabilized, milled, refined, screened and preserved to obtain the desires product.    USE - Method for treating, stabilizing and recovering waste or organic byproduct.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a system treating, stabilizing and recovering waste or organic byproduct.
NOVELTY - Feedstock saccharification system comprises: a tank (136) configured to contain a biomass feedstock and a liquid medium; a dispersing system configured to disperse the biomass feedstock in the liquid medium, and optionally configured to add additional feedstock to the tank; and a jet mixer configured to mix the contents of the tank, where the initial solids concentration of the biomass feedstock dispersed in the liquid medium is at least 20 wt.%.    USE - The system is useful for saccharifying the feedstock into fermentable sugars, which is useful for producing ethanol.    ADVANTAGE - The system: facilitates an efficient dispersion of feedstock, hence reduces liquification time; provides rapid and effective wetting of a relatively high solids level of feedstock; provides the saccharification of the feedstock in a rapid and cost effective manner; is portable, hence it can be transported easily from one location to another; prevents the feedstock from blowing out of the tank and/or contaminants from entering the tank; and maintains the microorganisms in a viable condition throughout the process, hence enhances the reaction rate and improves the efficiency of the process.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of the saccharification system.    Hopper (130)    Tank (136)    Mixture of liquid medium, feedstock and saccharifying agent (138)    Positive displacement pump (139)    Viscometer (141)
NOVELTY - Method for producing a chemical substance through continuous fermentation, involves filtering culture solution of a microorganism using separation membrane, retaining unfiltered portion of the culture solution in the culture solution or refluxing the unfiltered portion through the culture solution, adding new fermentation raw material to the culture solution and collecting product from the culture solution, where the microorganism can undergo catabolite inhibition and the fermentation raw material comprises a hexose and a pentose.    USE - The method is useful for producing a chemical substance through continuous fermentation, where the chemical substance includes biofuels, such as ethanol, biodegradable polymer raw materials such as lactic acid, alcohol e.g. ethanol, isobutanol, isopropanol, n-butanol, 1, 3-propanediol, 1,4-butanediol, 2,3-butanediol and glycerol, organic acid e.g. acetic acid, lactic acid, pyruvic acid, succinic acid, malic acid, itaconic acid, citric acid and adipic acid, amino acid, and nucleic acid, enzyme, antibiotics, and recombinant protein.    ADVANTAGE - The method provides high yield of chemical substance even in the presence of microorganism that undergoes catabolite inhibition, does not utilize edible biomass, thus is cost-effective, and enables long term stable filtration of culture solution. The produced chemical substance is life-cycle assessment compatible product, and does not discharge carbon dioxide to the environment.
NOVELTY - Method for producing a chemical substance through continuous fermentation, involves filtering a culture solution of microorganism using separation membrane, retaining unfiltered portion of the culture solution in the culture solution or refluxing the unfiltered portion through the culture solution, adding new fermentation raw material to the culture solution and collecting product from the culture solution, where the fermentation raw material comprises pentose and hexose.    USE - The method is useful for producing chemical substance through continuous fermentation, where the chemical substance includes biofuels, such as ethanol, biodegradable polymer raw materials such as lactic acid, alcohol e.g. ethanol, isobutanol, isopropanol, n-butanol, 1, 3-propanediol, 1,4-butanediol, 2,3-butanediol and glycerol, organic acid e.g. acetic acid, lactic acid, pyruvic acid, succinic acid, malic acid, itaconic acid, citric acid and adipic acid, amino acid, and nucleic acid, enzyme, antibiotics, and recombinant protein.    ADVANTAGE - The method provides high yield of chemical substance, does not utilize edible biomass, thus is cost-effective, and enables long term stable filtration of culture solution. The produced chemical substance is life-cycle assessment compatible product, and does not discharge carbon dioxide to the environment.    DETAILED DESCRIPTION - Method for producing a chemical substance through continuous fermentation, involves filtering a culture solution of microorganism using separation membrane, retaining unfiltered portion of the culture solution in the culture solution or refluxing the unfiltered portion through the culture solution, adding new fermentation raw material to the culture solution and collecting product from the culture solution, where the fermentation raw material comprises pentose and hexose and the microorganism has a pathway through which a pentose can be metabolized with a pentose reductase and a pentol dehydrogenase.
NOVELTY - Method for producing chemical substance through continuous fermentation, involves filtering culture solution of a microorganism using separation membrane, retaining unfiltered portion of the culture solution in the culture solution or refluxing the unfiltered portion through the culture solution, adding new fermentation raw material to the culture solution and collecting product from the culture solution, where the fermentation raw material comprises pentose and hexose and the microorganism has pathway through which pentose can be metabolized with pentose isomerase.    USE - The method is useful for producing chemical substance through continuous fermentation, where the chemical substance includes biofuels, such as ethanol, biodegradable polymer raw materials such as lactic acid, alcohol e.g. ethanol, isobutanol, isopropanol, n-butanol, 1, 3-propanediol, 1,4-butanediol, 2,3-butanediol and glycerol, organic acid e.g. acetic acid, lactic acid, pyruvic acid, succinic acid, malic acid, itaconic acid, citric acid and adipic acid, amino acid, and nucleic acid, enzyme, antibiotics, and recombinant protein.    ADVANTAGE - The method provides high yield of chemical substance, does not utilize edible biomass, thus is cost-effective, and enables long term stable filtration of culture solution. The produced chemical substance is life-cycle assessment compatible product, and does not discharge carbon dioxide to the environment.
NOVELTY - Enhancing a characteristic of a plant, comprises administering Bacillus subtilis FB17 to the plant, the seed of the plant or soil surrounding the plant or the seed to produce an enhanced characteristic in the plant compared to an untreated plant, where the enhanced characteristic comprises greater biomass, greater drought tolerance, decreased lignin content, increased rate of seed germination, increased iron concentration and increased tolerance to pathogens.    USE - The method is useful for producing greater biomass in a plant, increasing the drought tolerance of a plant, producing a decreased lignin concentration in a plant, producing a greater iron concentration in a plant or inhibiting fungal infection in a plant and producing a biofuel, where the plant is a corn plant, a soybean plant, a rice plant, a tomato plant, a barley plant, a Zinnia plant, a bioenergy crop plant and Brachypodium distachyon (all claimed). Tests details are described but no results given.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) method-I for producing a biofuel comprising converting the biomass of the plant that is administered Bacillus subtilis FB17 to the biofuel; (2) an agricultural carrier comprising Bacillus subtilis FB17; (3) a plant seed coating comprising Bacillus subtilis FB17; and (4) a plant seed comprising the coating.
NOVELTY - A Corynebacterium having improved putrescine production capability and comprising altered preferably attenuated or deleted activity of protein comprising an amino acid sequence of SEQ ID NO: 18 or 20, is new. Sequences not defined here may be found at ftp://ftp.wipo.int/pub/published_pct_sequences/publication.    USE - The Corynebacterium preferably C.glutamicum is useful for producing putrescine (all claimed).    ADVANTAGE - The recombinant Corynebacterium enables high yield production of the putrescine. The production method is environmentally-friendly and requires low energy consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing the putrescine, which involves culturing the above-mentioned recombinant Corynebacterium and separating the putrescine produced from the cultured Corynebacterium.
NOVELTY - Making hydroxymethylfurfural from an aqueous solution including at least one hexose, comprises subjecting aqueous hexose solution to an acid-catalyzed dehydration to produce a product mixture including hydroxymethylfurfural and residual unconverted sugars and separating the product mixture into an hydroxymethylfurfural product and a residual sugars product.    USE - The process is useful for making hydroxymethylfurfural (claimed) that: is used to produce polymers, solvents, surfactants, pharmaceuticals, and plant protection agents, furfuryl dialcohols, dialdehydes, esters, ethers, halides and carboxylic acids; has antibacterial properties; develops biofuels and treats sickle cell anemia. No biological data given.    ADVANTAGE - The process: provides residual sugars that are free of ethanol fermentation inhibitors, and used directly as a feed to a fermentation process for producing ethanol, lysine, lactic acid, or as a feed for making sugar alcohol; recycles at least a portion of the residual sugars product to make additional hydroxymethylfurfural (all claimed); provides hydroxymethyl furfural that exhibits anti-corrosive properties; and provides reduced byproducts and simple separation and recovery steps.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for making an hydroxymethylfurfural ether from the aqueous solution, comprising subjecting the hexose solution to dehydration in the presence of an alcohol to produce a product mixture including the hydroxymethylfurfural ether and residual unconverted sugars and separating the product mixture into an hydroxymethylfurfural ether product and the residual sugars product.
NOVELTY - Storing a gas comprises (i) exposing an organometallic compound or a complex of metal hydride in a gas or a mixture of gases, and (ii) luminous irradiating of photostrictive compound.    USE - The method is useful for: storing a gas or a mixture of gases within the organometallic compound or metal hydride complex; and the controlled release of a gas or a gas mixture that is stored in the organometallic compound or metal hydride complex, where the stored gas is hydrogen. The organometallic compound or metal hydride complex is useful for: the manufacture of fuel cells or photosensitive sensors; and drug delivery in human or animal body (all claimed).    ADVANTAGE - The process is capable of storing the hydrogen gas with large capacity for a long period of time in a rapid and economical manner without any energy loss.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a photostrictive compound, where a gas or a mixture of gases is stored, obtained by the process comprising pores having a diameter of less than 3 nm and a diameter of 3-20 Angstrom .
NOVELTY - The method involves introducing a stream of gas into a bed of weakly basic ion exchange resin provided with amine groups at temperature and pressure conditions under which carbon dioxide is adsorbed to the resin and content of water in the bed of ion exchange resin amounts more than 35 % of total weight of the ion exchange resin and water. The adsorbed carbon dioxide is desorbed from the resin by increasing the temperature and lowering the pressure in the bed, and the gas is upgraded by separation of the carbon dioxide from methane.    USE - Method for upgrading or cleaning gas e.g. flue gas and bio gas (all claimed), by separation of carbon dioxide from the gas utilized in a power plant. Can also be used for natural gas e.g. shale gas and fossil gas, and town gas in enterprises e.g. greenhouse enterprises or brewery enterprises.    ADVANTAGE - The method enables upgrading or cleaning the gas within modest space in a robust and an effective manner. The method enables providing an effective, efficient, simple and durable procedure for separation of the carbon dioxide from the gas in an environment-friendly manner and avoiding need for continuous supply of extraneous, industrial chemicals.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a power plant in which upgrading of gas is performed.
NOVELTY - The system has a fermenter (3) which generates biogas (1) that ferments organic waste and contains methane gas and hydrogen sulfide. The biogas from fermenter and air supplied from an air supply portion (31) are introduced from downward direction. The desorption ammonia containing air (13) is introduced into a carrying portion (8) from downward direction of biodesulfurization column (7) through supply line (12). The oxygen supplied from air supply portion and oxygen supplied from desorption ammonia containing air is supplied from downward direction of carrying portion.    USE - Biogas production system.    ADVANTAGE - The circulating water can be neutralized efficiently. The activity of sulfur oxidizing bacteria can be maintained without using neutralizing agent separately. Cost reduction of biogas production system can be achieved.    DETAILED DESCRIPTION - The biodesulfurization column oxidizes the hydrogen sulfide in biogas by the sulfur oxidizing bacteria carried by the carrying portion, and performs biological desulfurization process. Circulating water (15) is sprinkled from the upper portion of carrying portion in biodesulfurization column. An external circulation liquid tank (19) discharges hydrogen sulfide from the bottom of the biodesulfurization column. Ammonia desorption tower (11) supplies air to the fermented liquor and desorbs ammonia.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biogas production system.    Biogas (1)    Fermenter (3)    Biodesulfurization column (7)    Carrying portion (8)    Ammonia desorption tower (11)    Supply line (12)    Desorption ammonia containing air (13)    Circulating water (15)    External circulation liquid tank (19)    Air supply portion (31)
NOVELTY - Saccharogenic amylase composition comprises endoglucanase which does not contain cellulose binding domain, cellobiohydrolase containing cellulose binding domain, and beta -glucosidase containing cellulose binding domain.    USE - The saccharogenic amylase composition is useful for carrying out saccharification process of lignocellulosic biomass as substrate and preparing saccharification solution (all claimed).    ADVANTAGE - The saccharogenic amylase composition reduces the usage amount of saccharogenic amylase.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing saccharification solution, which involves adding saccharogenic amylase to the lignocellulosic biomass as a substrate to obtain substrate and saccharogenic amylase mixture, adding saccharogenic amylase composition to the substrate, and carrying out saccharification of the substrate and saccharogenic amylase mixture to obtain saccharification solution.
NOVELTY - A ruthenium catalyst layer is arranged as a preliminary modification catalyst, which does not convert nitrogen into ammonia in the low-temperature area of front stage of platinum-rhodium alloy type steam reforming catalyst layer, and heavy hydrocarbon is converted into methane. The steam reforming catalyst layer is arranged such that carbon deposition on the steam reforming catalyst layer is prevented and reformed gas is produced. Thus, usage of steam reforming catalyst is enabled.    USE - Usage of steam reforming catalyst for producing hydrogen in hydrogen production system for fuel cells (all claimed).    ADVANTAGE - The carbon deposition on platinum-rhodium alloy group steam reforming catalyst is prevented. The generation of ammonia is suppressed.    DETAILED DESCRIPTION - A ruthenium catalyst layer is arranged as a preliminary modification catalyst, which does not convert nitrogen into ammonia in the low-temperature area of front stage of platinum-rhodium alloy type steam reforming catalyst layer, and heavy hydrocarbon is converted into methane. The steam reforming catalyst layer is arranged such that carbon deposition on the steam reforming catalyst layer is prevented and reformed gas is produced. The carbon monoxide modification portion and carbon monoxide removal portion of hydrogen production system are connected with steam reforming device containing combustion unit and modification unit. Thus, usage of steam reforming catalyst is enabled. INDEPENDENT CLAIMS are included for the following:    (1) production of hydrogen; and    (2) hydrogen production system.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view explaining arrangement of ruthenium catalyst and platinum-rhodium catalyst. (Drawing includes non-English language text)
NOVELTY - Method for elicitating Lepidium sativum callus culture using fungus involves (a) establishing suspension culture using Murashige and Skoog (MS) medium fortified with different concentration of hormones, (b) isolating the root adhering fungus for mass cultivation, (c) elicitating the callus after transferring the callus into to the suspension medium of the step (a) and fungal extract of the step (b) to obtain compound.    USE - The method is useful for elicitating L.sativum callus culture which is used to enhance production of compound in the form of product used in antileishmania and antifertility drugs, and providing antiovulatory functions (all claimed).    ADVANTAGE - The method is reliable and reproducible. The method provides a rapid source of lepidine extraction from cells without the intervention of plant tissue.
NOVELTY - Process for obtaining biofuel consisting of dimethyl furan involves dissolving cellulose in N-alkyl imidazolium chloride (NAIC), 37% hydrochloric acid and alcohol; hydrolyzing cellulose into acetal of glucose; evaporating alcohol and water; dehydrating glucose acetal to acetal of hydroxymethyl furfural; extracting with alcohol; mixing alcohol concentrate with ketone and diluted hydrochloric acid solution to convert to corresponding chloride; extracting; evaporating ketone; mixing concentrate with alcohol; hydrogenating alcohol concentrate and isolating dimethyl furan by distillation.    USE - For converting cellulose into liquid biofuel consisting of dimethyl furan.    ADVANTAGE - The process produces liquid fuels from cellulose which is renewable and an abundant source of raw materials for liquid fuels suitable for energy supply to transportation and industry. The cellulose is dissolved in ionic liquid, instead of traditional processes that use water and organic solvents, thus forming a stable glucose acetal. The chloride ions are effectively eliminated to avoid poisoning of the catalyst during hydrogenation step.    DETAILED DESCRIPTION - A process for obtaining biofuel consisting of dimethyl furan, by successively dissolving cellulose in mixture of N-alkyl imidazolium chloride (NAIC), 37% hydrochloric acid and an alcohol, hydrolyzing cellulose into the acetal of glucose, evaporating alcohol and water, dehydrating glucose acetal to acetal of hydroxymethyl furfural, adding to the reaction mixture a water solution of sodium chloride, extracting with an alcohol, concentrating alcohol extract by distillation, mixing alcohol concentrate with ketone and diluted hydrochloric acid solution in order to convert to corresponding chloride (NAIC), extracting, evaporating ketone, mixing concentrate with alcohol, hydrogenating alcohol concentrate and isolating dimethyl furan by distillation.
NOVELTY - A fuel cell comprises steam reforming apparatus (10) which is equipped with combustion part and performs steam reforming of fuel gas with combustion heat produced in combustion part, battery stack (30) consisting of cathode, anode, and battery cell which produces electric power according to electrochemical reaction of oxidant gas supplied to cathode and reformed fuel gas from steam reforming apparatus supplied to anode, radiant tube burner (20) consisting of radiant tube (22) arranged in a row by burner which burns fuel gas, and burner.    USE - A fuel cell (claimed).    ADVANTAGE - Steam reforming apparatus and battery stack can be heated directly, required temperature rising time is shortened, energy efficiency is improved, and size reduction of fuel cell is achieved.    DETAILED DESCRIPTION - A fuel cell comprises steam reforming apparatus (10) which is equipped with combustion part and performs steam reforming of fuel gas with combustion heat produced in combustion part, battery stack (30) consisting of cathode, anode, and battery cell which produces electric power according to electrochemical reaction of oxidant gas supplied to cathode and reformed fuel gas from steam reforming apparatus supplied to anode, radiant tube burner (20) consisting of radiant tube (22) arranged in a row by burner which burns fuel gas, and burner which is positioned between battery stack and steam reforming apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a fuel cell.    Casing (2)    Steam reforming apparatus (10)    Radiant tube burner (20)    Radiant tube (22)    Battery stack (30)
NOVELTY - Producing liquid fuel and liquid water from a gas stream comprising carbon dioxide and water vapor, involves: contacting the gas stream with at least one adsorbent material, where carbon dioxide and water vapor are adsorbed to the adsorbent; desorbing carbon dioxide and water from the adsorbent materials; reacting carbon dioxide and water to form a liquid fuel; and condensing excess water to form liquid water.    USE - For producing liquid fuel such as methanol and liquid water from a gas stream comprising carbon dioxide and water vapor. The liquid water is used for domestic purposes and agricultural purposes (claimed).    ADVANTAGE - The process produces liquid fuel from carbon dioxide recovered from a dilute gas stream. The process uses carbon dioxide and water vapor from ambient air. The use of ambient air offers the additional advantage that it can be carried out on a small scale. The adsorption unit supplies significant amounts of liquid water, resulting in further cost savings that help defray the cost of the installation. The temperature for desorption is close to the reaction temperature, so that no excess energy is needed for the desorption step.
NOVELTY - The device comprises a storage tank containing excrements that is fractured using an agitating blade, a first device for spraying microorganism composition using organic acid through a spray nozzle for odor reduction of excrements inside the storage tank, a tank for mixing supplementary raw material with excrements, a fermentation tank, a second device that is equipped with fermentation tank and adapted for spraying microorganism composition to ferment the mixture of supplementary raw material and excrement, and a moisture control equipment to control moisture in fermented excrements.    USE - The device is useful for producing organic fertilizer (claimed) for crops.    ADVANTAGE - The device prevents the soil contamination and water pollution during the production of organic fertilizer.    DETAILED DESCRIPTION - The device comprises a storage tank containing excrements that is fractured using an agitating blade, a first device for spraying microorganism composition using organic acid through a spray nozzle for odor reduction of excrements inside the storage tank, a tank for mixing supplementary raw material with excrements, a fermentation tank, a second device that is equipped with fermentation tank and adapted for spraying microorganism composition to ferment the mixture of supplementary raw material and excrement, a moisture control equipment to control moisture in fermented excrements using hot air, and a fertilizer molding apparatus for molding the dried fermented excrements to form the solid fertilizer. The moisture control device comprises a flue gas supply unit, a hot air supplying unit, outdoor air supply unit so that the water content is 20-30%. The first spray device and the second spray device are sprayed with composition to adjust the pH to 2-4.
NOVELTY - Device (100) comprises (i) at least one heat exchanger for cooling a substance stream to be reprocessed, (ii) at least one separating unit for purifying the substance stream (3) to be reprocessed to obtain a hydrogen- and methane-rich substance stream (5), (iii) at least one cooling unit for cooling the hydrogen-and methane-rich substance stream, and (iv) at least one cryogenic gas separating unit for separating the hydrogen and methane-rich substance stream (6) into at least one hydrogen-rich substance stream and at least one methane-rich substance stream.    USE - The device is useful for processing a substance stream containing hydrogen and methane (claimed).    ADVANTAGE - The device facilitates processing of product gas mixtures ensuring a high purity of the processed hydrogen in an economical manner, and maintains the substance stream at a constant temperature level before it enters the cryogenic gas separation unit, thus its stabilizes cryogenic gas separation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for processing the substance stream containing hydrogen and methane, comprising (a) cooling the substance stream to be reprocessed in at least one heat exchanger, (b) purifying the substance stream to be reprocessed into the hydrogen- and methane-rich stream in at least one separating unit, (c) cooling the hydrogen- and methane-rich substance stream in at least one cooling unit, and (d) separating the hydrogen- and methane-rich substance stream into at least one hydrogen-rich stream and at least one methane-rich stream in at least one cryogenic gas separation unit.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic flow diagram for processing the substance stream containing hydrogen and methane.    Substance stream (1.1)    Hydrogen- and methane-rich substance stream (5)    Device (100)
NOVELTY - Method for preparing lignin degradation product, involves (a) saccharifying lignocellulose raw material using enzyme and obtaining saccharification residue, (b) heating the saccharification residue obtained in step (a) in a mixed solvent containing water and organic solvent having a solubility of 90 g/l or more (in 20 degrees C water), and obtaining heat-treated solution containing lignin degradation product, and (c) performing solid-liquid separation, and removing insoluble fractions.    USE - The method is useful for preparing lignin degradation product (all claimed) which is useful in agriculture, cosmetics, engineering plastics, cement dispersing agent and battery.    ADVANTAGE - The method prepares versatile lignin degradation product at higher yield having solvent solubility with low denaturation. The lignin degradation product prepared by the method has 10% or more aldehyde, when measured by alkaline nitrobenzene oxidation method. The lignin degradation product is suitably used in agriculture, cosmetics, engineering plastics, cement dispersing agent and battery, as conversion of low molecular weight aromatic compounds is made easy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for lignin degradation product prepared by the above-mentioned method.
NOVELTY - Hydroisomerization process comprises contacting a hydrocarbon feed stream comprising predominantly normal and singly branched 4-7C paraffins, under hydroisomerization conditions, with a catalyst comprising an aluminosilicate SFV type zeolite and at least one group VIII metal to form an isomerized product having a higher concentration of doubly and singly branched paraffins than the feed stream and having a 2,3-dimethylbutane to 2,2-dimethylbutane mole ratio of at least 1.    USE - The process is useful for isomerizing light paraffins using a catalyst comprising an SFV-type zeolite and at least one Group VIII metal.    ADVANTAGE - The improved hydrocarbon hydroisomerization catalyst provides high selectivity for producing high octane isomers of light paraffins, and is highly active, environmentally benign and readily regenerable.
NOVELTY - Antiperspirant composition comprises (a) at least one antiperspirant aluminum salt (greater than 25-40 wt.%), (b) 0-5 wt.% of free water based on the weight of a propellant-free composition, (c) 30-75 (preferably 54-64) wt.% of a mixture of cosmetic oils in the form of liquid under normal conditions, and (d) cyclomethicone (0 to less than 1 wt.%) based on the weight of the propellant-free composition.    USE - The antiperspirant composition is useful in a cosmetic product for personal body care in the form of a sprayable or atomizable blowing agent or with a blowing agent suspension (all claimed), where the cosmetic product includes hair sprays, deodorants and oral sprays.    ADVANTAGE - The antiperspirant composition exhibits improved active ingredient release, and reduces the soiling of textiles.    DETAILED DESCRIPTION - Antiperspirant composition comprises (a) at least one antiperspirant aluminum salt (greater than 25-40 wt.%), (b) 0-5 wt.% of free water based on the weight of a propellant-free composition, (c) 30-75 (preferably 54-64) wt.% of a mixture of cosmetic oils in the form of liquid under normal conditions, where the cosmetic oils are not essential oil, have no fragrance, 60-90 wt.% of an oil blend consisting of at least one volatile isoparaffin or a volatile mixture of paraffins, each of which has a vapor pressure of 8-250 Pa at 20 degrees C, and 10-40 wt.% of the oil blend consisting of one non-volatile ester oil or a non-volatile ester oil mixture each having a vapor pressure of less than 2.66 Pa (0.02 mm Hg) at 20 degrees C, and (d) cyclomethicone (0 to less than 1 wt.%) based on the weight of the propellant-free composition. An INDEPENDENT CLAIM is included for an antiperspirant cosmetic product comprising at least one propellant and an aerosol-dispensing device.
NOVELTY - A fly maggot chitin microorganism fertilizer comprises 2-10% fly maggot chitin, 5-20% amino acid and 70-93% microbial bacterium liquid.    USE - Fly maggot chitin microorganism fertilizer.    ADVANTAGE - The fertilizer is organic, has no pollution, and low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a production of the fertilizer comprising mixing raw materials and microorganism bacteria liquid.
NOVELTY - The method involves adding pesticide acephate polluted soil with alkaline substance and/or material and/to reacting hydroxide with water to acephate or acephate in pesticide polluted soil through electrochemical method. The alkaline material comprises sodium hydroxide. Voltage is applied between negative and positive electrodes in the acephate pesticide polluted soil, so as to make the acephate anode electrochemical oxidation and the cathode area reduction reaction. Methylamine phosphorus usage is eliminated for repairing the soil.    USE - Acephate pesticide-polluted soil repairing method.    ADVANTAGE - The method enables effectively damaging the molecular structure of acephate, so as to completely remove the soil in the acephate, and realize the complete restoration of polluted soil. The method enables reducing repairing cost for large scale.
NOVELTY - Method for preparing base fertilizer for mature persimmon trees, involves mixing 20-22 wt.% dry pig manure, 8-10 wt.% dry human manure, 3 wt.% animal residues, 10 wt.% peanut straws, 5 wt.% carrot seedlings, 5 wt.% bean seedlings, 10 wt.% water hyacinth, 5 wt.% sesame meal, 5 wt.% castor bean meal, 3 wt.% seaweed shells, 10 wt.% plant ash, 2 wt.% organic fertilizer leavening agents, 2 wt.% urea, 2 wt.% monoammonium phosphate, 5 wt.% potassium chloride, 4 wt.% humic acid chelated iron, and 0.5 wt.% humic acid chelated calcium, and fermenting the obtained mixture.    USE - The method is useful for preparing base fertilizer for mature persimmon trees (claimed).    ADVANTAGE - The base fertilizer improves growth, yield, disease resistance, drought resistance, cold resistance and quality of fruits of the mature persimmon trees, and supplements nutrients to soil.
NOVELTY - Method for preparing longan mature tree base fertilizer, involves using 25-27% dry pig manure, 8-10% dry chicken manure, 10% rape straws, 5% sweet clover, 10% vetch, 4% castor cakes, 4% tea seed cakes, 17% dry pollution-free pond sludge, 2% organic fertilizer leavening agent, 3%urea, 4% diammonium phosphate, 4% potassium nitrate, 0.4% iron amino acid chelate, 0.4% calcium amino acid chelate, 0.3% magnesium amino acid chelate, 0.2% selenium humic acid chelate, 0.3% manganese humic acid chelate and 0.4% copper humic acid chelate as raw materials.    USE - The method is useful for preparing longan mature tree base fertilizer (claimed).    ADVANTAGE - The prepared fertilizer increases yield, improves disease resistance, heat resistance and drought resistance of mature longan trees, improves quality of fruits, and enables longan to be tender in pulp, juicy, sweet and delicious.
NOVELTY - Preparing base fertilizer comprising 18-20% dry dairy manure, 8-10% dry sheep manure, 6% dried chicken manure, 8% fallen leaves, 5% dry grass, 6% ryegrass, 7% fertile radish, 10% rape seed cake, 10% dry clean pond scum, 2% organic fertilizer leavening agent, 3% urea, 5% diammonium phosphate, 4% potassium sulfate, 5% amino acid waste liquid, 4% iron amino acid chelated, 5% calcium amino acid chelate, 0.1% magnesium amino acid chelate, is claimed.    USE - The base fertilizer is useful for Guoguang date trees (claimed).    ADVANTAGE - The base fertilizer can fully meet the demand on fruit development and root growth of the Guoguang date trees, improves the quality of fruits, has remarkable effects of improving the fruit shape and the quality of dates, improves the resistance of the date trees to diseases, drought and coldness, and realizes the effects of high yield and high-quality output.
NOVELTY - Crystalline and anhydrous forms of tolvaptan monohydrate (I), are new.    USE - The crystalline and anhydrous forms of (I) are useful for treating hyponatremia associated with congestive heart failure, cirrhosis, and syndrome of inappropriate antidiuretic hormone. No biological data given.    ADVANTAGE - The crystalline and anhydrous forms of (I) can be efficiently and economically prepared without contamination of other polymorphic form in a safe and eco-friendly manner, and have purity of greater than 99.8% using high-performance liquid chromatography.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of crystalline and anhydrous forms of (I).
NOVELTY - One pot process for preparing N-protected L-tert-leucine, comprises: converting trimethyl pyruvic acid (IV) into L-tert leucine (III) by reductive amination; converting (III) into N-protected L-tert-leucine (II); optionally isolating (II); and converting (II) into its corresponding salt (I).    USE - The process is useful for preparing N-protected L-tert-leucine or (I), which is useful in preparation of antiretroviral drug of the protease inhibitor comprising atazanavir or telaprevir (claimed).    ADVANTAGE - The process provides simple, cost effective and environmentally-friendly one pot enzymatic preparation of (I) with high yield and purity.    DETAILED DESCRIPTION - One pot process for preparing N-protected L-tert-leucine, comprises: converting trimethyl pyruvic acid (IV) into L-tert leucine (III) by reductive amination; converting (III) into N-protected L-tert-leucine compounds of formula (R-NH-CH(C(CH3)3)-C(=O)-OH) (II); optionally isolating (II); and converting (II) into its corresponding salt of formula (R-NH-CH(C(CH3)3)-C(=O)-O- (C6H5)2NH) (I).    R = alkyl, aryl or aralkyl.
NOVELTY - Producing nanoinduced biological phosphorus fertilizer, comprises: isolating fungal isolate from arid soil zone; inoculating soil fungal isolate in a culture to obtain grown fungus; separating biomass from the fungus to obtain fungal extracellular secrets; and incubating fungal extracellular secrets with precursor metal salts and an organic process using biosynthesized nanoparticle and absorbent comprising isolated fungal isolate originated from arid soil environment.    USE - The method is useful for producing nanoinduced biological phosphorus fertilizer (claimed).    ADVANTAGE - The method allows simple, rapid, economical and efficient production of eco-friendly nanoinduced biological phosphorus fertilizer with long life span and without toxicity and harmful by-product in a reliable manner thus increasing crop productivity. The phosphorus fertilizer is easy to handle, enhances native phosphorus availability in rhizosphere, and increases phosphorus use efficiency by plants.
NOVELTY - Bacillus subtilis strain having a preservation number of CGMCC No.6788, is new.    USE - The Bacillus subtilis strain is useful for preventing and treating plant fungal disease, where the fungi is Pythium aphanidermatum, fusarium roseum, Sclerotinia sclerotiorum and botrytis cinerea (all claimed), and for promoting plant growth. The biological fertilizer is useful for resisting premature senility and preventing dead seedlings rot.    ADVANTAGE - The Bacillus subtilis strain inhibits the plant pathogenic fungi growth capacity, has high genetic stability, and does not pollute the environment. The biological fertilizer increases the quality and yield of the crop.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparing microbial inoculum, comprising culturing the Bacillus subtilis in potato dextrose agar culture medium at 27 degrees C under a speed of 200 revolution per minute for 5 days, and filtering and adjusting the bacterial liquid cell number to 109 per ml; and    (2) preparing biological fertilizer, comprising mixing the Bacillus subtilis microbial inoculum with inorganic fertilizer and organic fertilizer in a ratio of 1:6:13, where the inorganic fertilizer is nitrogenous fertilizer, phosphate fertilizer and potash fertilizer, the nitrogen fertilizer is urea or ammonium sulfate, the phosphate fertilizer is ammonium phosphate or calcium phosphate, the potassium fertilizer is potassium sulfate or potassium chloride, and the organic fertilizer is biogas fertilizer.
NOVELTY - Production of marsh gas using processed sewage includes adding sewage with water to dilute, adding the diluted sewage into an adjusting tank and stirring continuously, carrying out natural deposition to remove the sand, suspended material, and large granular inorganic material, standing, fully mixing the materials, flowing into solid anaerobic reaction tank to carry out anaerobic process, generating marsh gas, dehydrating, desulfurizing, dehydrating and drying, and using the separated biogas residue for producing organic fertilizer.    USE - Production of marsh gas using processed sewage (claimed).    ADVANTAGE - The process has simple technique and short preparation period.    DETAILED DESCRIPTION - Production of marsh gas using processed sewage comprises adding sewage with water to dilute, adding the diluted sewage into an adjusting tank through a hopper and stirring continuously, carrying out natural deposition to remove the sand, suspended material, and large granular inorganic material, standing for 8-15 days, fully mixing the materials, flowing into solid anaerobic reaction tank by a lifting pump to carry out anaerobic process, generating marsh gas, introducing marsh gas into dewatering tank through marsh gas pipe for dehydration treatment, desulfurizing marsh gas, introducing to second desulfurization tank through marsh gas pipe for second time desulfurization, introducing into dewatering tank for dehydrating and drying, introducing dry marsh gas into gas storage cabinet through the marsh gas pipe, separating the biogas residue, conducting pollution treatment, comprehensively recycling the excess biogas slurry to water collecting tank for aerobic treatment, and using the separated biogas residue for producing organic fertilizer.
NOVELTY - An organic fertilizer comprises 80-90 pts. wt. organic fertilizer and 20-30 pts. wt. urea.    USE - Organic fertilizer.    ADVANTAGE - The fertilizer improves crop yield, nourishes organic matter in soil and protects ecological environment with cheap and easy production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of organic fertilizer comprising taking crop straw, crushing, spraying lime water at mass ratio of 25-30:1, adding rotten manure and compost mixture and sealing.
NOVELTY - The plant organic residue treatment and fertilizer utilization process, comprises pre-processing vegetable residues, green vegetables, solanaceous vegetables, fruits and tuber vegetables and then crushing and uniformly mixing, sterilizing the mixture at a temperature of 80 degrees C for 4-6 hours, cooling the mixture at 40 degrees C and culturing for 1 hour, and stacking the mixture for 7 days to improve fertilizer effect. An INDEPENDENT CLAIM is included for a device for performing plant organic residue treatment and fertilizer utilization process.    USE - The plant organic residue treatment and fertilizer utilization process is useful for processing vegetable residues (claimed) to produce active organic fertilizer.    ADVANTAGE - The process is capable of rapidly processing the vegetable residues in an environmentally friendly manner thus producing high quality organic fertilizers with excellent characteristics such as color, odor and nutrient value.
NOVELTY - Production of microbial fertilizer comprises: mixing Azotobacter, phosphorus bacteria and potassium bacteria strain to get microbial inoculum; mixing microbial inoculum, distillers waste, beans, rice bran and quail manure, fermenting for 35-55 hours; mixing 50-60 pts. wt. composite quail manure, 20-30 pts. wt. distillers waste, 12-17 pts. wt. wheat bran and straw bran, 10-15 pts. wt. bean cake cypress and/or vegetable oil cake Chinese arborvitae and 5-10 pts. wt. calcium-magnesium phosphate powder, aerobic fermenting at 7-7.4 pH for 50-70 hours; and drying and packaging.    USE - Method for producing microbial fertilizer (claimed).    ADVANTAGE - The method is simple and easy to control.    DETAILED DESCRIPTION - Production of microbial fertilizer comprises: mixing Azotobacter, phosphorus bacteria and potassium bacteria strain at 2:1:1 mass ratio to get microbial inoculum; mixing 10-15 pts. wt. microbial inoculum, 30-40 pts. wt. distillers waste, 15-20 pts. wt. beans, 10-20 pts. wt. rice bran and 30-40 pts. wt. quail manure, fermenting at 7-7.4 pH for 35-55 hours; mixing 50-60 pts. wt. composite quail manure, 20-30 pts. wt. distillers waste, 12-17 pts. wt. wheat bran and straw bran, 10-15 pts. wt. bean cake cypress and/or vegetable oil cake Chinese arborvitae and 5-10 pts. wt. calcium-magnesium phosphate powder, aerobic fermenting at 7-7.4 pH for 50-70 hours; and drying and packaging.
NOVELTY - Circulating water sterilizing algae-removing adhesive sludge stripping process, comprises (i) adding corrosion inhibitor before using circulating water, (ii) adding acid or alkali to adjust the pH value to be 7 plus minus 0.3, (iii) adding 200 ppm sodium dichloroisocyanurate to the circulating water, maintaining water level, allowing it to stand for 2-4 days, and (iv) transferring the circulating water into the cooling system, and processing the circulating water.    USE - The method is useful for circulating water sterilizing algae-removing adhesive sludge stripping process (claimed).    ADVANTAGE - The method has simple processing techniques, provides good sterilization and stripping effect, thus restoring smoothness of pool wall after stripping sludge for 3-4 days, and can change vacuum end difference.
NOVELTY - An automatic proportioning device comprises transmission device, control system, mixing device, transmission stirring wheel (8) and transmission stirring shaft (9).    USE - Automatic proportioning device used for granular fertilizer (claimed).    ADVANTAGE - The device improves utilization rate and efficiency with high degree of automation, high precision, simple structure, convenient operation, good stability, good economic benefit and ecological environmental benefit. It improves grain yield of 5-15% and save waste fertilizer of 18-35%.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view schematic diagram of automatic proportioning device.    Transmission stirring wheel cylinder (8)    Transmission stirring shaft (9)    Fertilizer box (13)    Bearing seat (15)    Connecting plate (16)
NOVELTY - A recombinant bacterial strain of Escherichia coli preserved under BL2ItrxB (DE3)-pET28a (+) ECU0416CGMCCNo. 6114 preservation number is new.    USE - For preparation of aloe-emodin (claimed) having anti-tumor, antiviral, and anti-oxidation activity, and used in medicine, health food, cosmetic, and cleaning article industries.    ADVANTAGE - The preparation method uses cheap microorganism producing enzyme barbaloin as catalyst to prepare aloe-emodin of high nutrition value, requires mild reaction condition, does not need special equipment, has low energy consumption, is environment-friendly, has conversion rate of more than 65%, and provides aloe-emodin with purity of more than 98%. The strain allows production of aloe-emodin under mild reaction condition. The strain provides aloe-emodin having very high application value and wider market application prospect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of aloe-emodin involving: culturing the recombinant bacterial strain of Escherichia coli BL21trxB (DE3)-pET28a (+) ECU0416CGMCC CGMCC No. 6114 by fermentation, purifying the reaction product containing aloe-emodin, subjecting to enzymatic hydrolysis by culturing the Escherichia coli fermentation liquid, freezing, centrifuging to obtain supernate fluid as enzyme source, and substrate with aloin, where aloin is present in 0.05-7.5 g/l, and adding amount of the enzyme is 20 to 300U/g of substrate, at pH 5.0-9.0, and subjecting to hydrolysis reaction in phosphate buffer solution, where reaction temperature is 20-50 degrees C and reaction time is 2-24 hours. The phosphate buffer solution is disodium hydrogen phosphate buffer solution, where the concentration is 20-200 mmol/l.
NOVELTY - Preparing pregabalin intermediate comprises hydrogenating 3-cyano-5-methylhexanoic acid ethyl ester in the presence of ammonia and/or organic amine as organic solvent and a catalyst.    USE - The method is useful for preparing pregabalin intermediate (claimed).    ADVANTAGE - The method simply provides pregabalin intermediate with high conversion rate and device utilization rate, and wide application range in an eco-friendly manner.
NOVELTY - The device has a mobile processing unit and storage tank. The bacteria are added to the depth of storage tank. A platform is provided with a reaction tank main portion. A garbage rubbish hopper is set at the lower portion of a sorting device and a crusher. A conveying pump is connected with the feeding port of the reaction tank main portion. The reaction tank is connected with a strain tank through a port.    USE - Mobile distributed processing device for kitchen garbage.    ADVANTAGE - Since the mobile distributed processing device is provided with a simple structure, the manufacturing cost of the mobile distributed processing device is reduced. The processing efficiency of the mobile distributed processing device is improved. The mobile distributed processing device is carried conveniently. The flexibility of the mobile distributed processing device is improved.
NOVELTY - Device comprises to-be-processed mother liquor storage tank, an adsorption tank, a filter and a finished product mother liquor storage tank. The to-be-processed mother liquor storage tank is connected with an inlet of the adsorption tank. An outlet of the adsorption tank is connected with the inlet of the filter. The outlet of the filter is connected with the finished product mother liquor storage tank.    USE - The device is useful for removing secondary impurities in methionine mother liquor (claimed).    ADVANTAGE - The device: can reduce the accumulation of impurities in the mother liquor; produce mother liquor with high quality; improves the yield of methionine and sodium sulfate; can reduce the load of waste water treatment and time consumption; and has high quality recovery technology.
NOVELTY - A plant growth-promoting rhizobacteria (PGPR) bio-organic fertilizer comprises: mixing 35-45 wt.% pig manure and Stevia rebaudiana residue, stirring uniformly; laying mixed material, sprinkling 1-5 wt.% fermenting agent, adding water to 55-65 wt.% water content, keeping pile temperature at 54-70 degrees C, fermenting under anaerobic condition for 7-10 days to obtain fermented material with 20-30 wt.% water; adding 13-18 wt.% humic acid and 1-2 wt.% inorganic nutrients, mixing, grinding into powders; adding 1-2 wt.% PGPR strain, mixing, granulating, drying, cooling and sieving.    USE - A plant growth-promoting rhizobacteria (PGPR) bio-organic fertilizer.    ADVANTAGE - The fertilizer has high organic matter content and strong biological activity.
NOVELTY - Preparing 3-hydroxybenzenepropanal from cinnamaldehyde, comprises (i) dissolving proline or 4-hydroxyproline with distilled water, adjusting the pH of the solution, and using water to dilute the concentration to obtain proline or 4-hydroxyproline solution; (ii) adding proline or 4-hydroxyproline solution with cinnamaldehyde, and placing in a sealed reactor at room temperature to obtain mixed solution; and (iii) extracting the mixed solution with ethyl acetate, stratifying to separate 3-hydroxybenzenepropanal and amino acid, and recycling proline or 4-hydroxyproline solution.    USE - 3-hydroxybenzenepropanal is useful for chiral drug synthesis.    ADVANTAGE - The method: has mild reaction condition, low production cost and high solid selectivity; utilizes the raw materials and reagent, which are harmless to human body health; and utilizes the catalyst and extracting agent, which can be recycled.    DETAILED DESCRIPTION - Preparing 3-hydroxybenzenepropanal from cinnamaldehyde, comprises (i) taking proline or 4-hydroxyproline (specific amount), adding distilled water (specific amount) to dissolve, adjusting the pH of the solution to 10 using concentrated sodium hydroxide solution, and using water to dilute the concentration to 0.50 mol/l to obtain proline or 4-hydroxyproline solution (0.50 mol/l); (ii) adding 10 ml proline or 4-hydroxyproline solution (0.50 mol/l) with 1.2 mmol cinnamaldehyde, placing in a sealed reactor at room temperature for 24 hours to obtain mixed solution of 3-hydroxybenzenepropanal and proline or 4-hydroxyproline solution; and (iii) extracting the mixed solution obtained in the step (ii) with 20 ml ethyl acetate, stratifying to separate 3-hydroxybenzenepropanal and amino acid (proline or 4-hydroxyproline), and recycling proline or 4-hydroxyproline solution to obtain 3-hydroxyphenylpropionaldehyde, where catalytic activity of proline or 4-hydroxyproline solution does not change.
NOVELTY - Comprehensively utilizing distillate spirit vinasse spot comprises: (a) selecting distiller to the marsh gas station; (b) converting organic matter into marsh gas by using distiller into the anaerobic digestion tank for anaerobic microorganism anaerobic fermentation process; (c) using marsh gas boiler for cold, heat and power combined supplying system of multi-fuel; (d) using biogas slurry as reflux of anaerobic digestion tank; and (e) drying the residue in boiler fuel to generate steam for producing.    USE - The method is useful for comprehensively utilizing distillate spirit vinasse spot (claimed).    ADVANTAGE - By the aid of the method, the distillate spirit vinasse can be subjected to spot treatment in the spirit factory, raw materials cannot be transported for a long distance, water and chemical medicines are not required to be added during the production and treatment process, products can be applied in the spirit factory completely and are not affected by seasons and market requirements, and the system energy utilization efficient is high.    DETAILED DESCRIPTION - Comprehensively utilizing distillate spirit vinasse spot comprises: (a) selecting distiller to the marsh gas station; (b) converting organic matter into marsh gas by using distiller into the anaerobic digestion tank for anaerobic microorganism anaerobic fermentation process; (c) using marsh gas boiler for cold, heat and power combined supplying system of multi-fuel, anaerobic fermenting liquid after solid-liquid separation to obtain the biogas slurry and biogas residue; (d) using biogas slurry as reflux of anaerobic digestion tank, the redundant part is discharged factory sewage processing system or is used as liquid fertilizer; and (e) drying the residue in boiler fuel to generate steam for producing, or directly processed into biogas residue organic fertilizer for agricultural production.
NOVELTY - A N-methyl-N,N'-phenylurea is prepared by mixing diphenylamine and methyl amino methyl acyl halide, and subjecting mixture to alkylating reaction.    USE - Method of preparing a N-methyl-N,N'-phenylurea (claimed).    ADVANTAGE - The method is simple and environment-friendly, utilized cheap and easy to obtain raw materials, and is short and stable.
NOVELTY - A nitroguanidine is produced by stirring concentrated sulfuric acid at a speed of 68-69 revolutions/minute (rpm), adding slowly salt aqueous solution controlled at - 10 degrees C, adding guanidine nitrate while controlling temperature at 30-40 degrees C, mixing, drying at 39-41 degrees C for 1 hour, adding water controlled at a 5-10 degrees C while stirring at a speed of 68-69 rpm, stirring at not greater than 30 degrees C, hydrolyzing at 20-30 degrees C for 20 minutes, adding sulfuric acid, neutralizing at not greater than 60 degrees C until the pH is 3-3.5, cooling to 20-25 degrees C, centrifuging, filtering, washing the filter cake with water, and recycling the filtrate.    USE - Method of producing a nitroguanidine (claimed).    ADVANTAGE - The method has a yield of more than 95%, produces product having a purity of higher than97%, and is environment-friendly.
NOVELTY - A Shewanella putrefaciens CR7 (CGMCCNo.6192) is new.    USE - The S. putrefaciens CR7 (CGMCCNo.6192) is used in processing organic waste, composting fermentation, and preparing a corrosion accelerating agent produced by livestock excrement organic fertilizer (all claimed).    ADVANTAGE - The S. putrefaciens CR7 (CGMCCNo.6192) is used for rapid composting fermentation, and for improved, low cost and high yield organic fertilizer preparation.
NOVELTY - A Xanthomonas campetris XC2460 (CGMCC No. 6583) is new.    USE - The X. campetris XC2460 is used in biomass conversion, preferably for extracellular accumulation of glucose in cellulose biological conversion process (all claimed).    ADVANTAGE - The X. campetris XC2460 is used for increased and improved extracellular accumulation of glucose.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for obtaining X. campetris XC2460.
NOVELTY - Water retention nutritive soil comprises 0.1-0.5 wt.% water retention agent, 10-50 wt.% humus, 1-10 wt.% sheep manure and remaining amount of planting soil.    USE - Used as water retention nutritive soil.    ADVANTAGE - The water retention nutritive soil avoids loss of moisture in the soil and improves the utilization rate of water; conveniently allows the delivery of nutrient substances of humus and sheep manure in the wet soil; and promotes plant germination, rooting, and growth; and increases plant survival rate.
NOVELTY - Preparing bio-organic fertilizer using recycled water flocculation sludge of mechanical pulp production, comprises taking recycled water flocculation sludge of mechanical pulp production as main raw material, and preparing granular bio-organic fertilizer by adding humic acid, and trace element, adjusting nutritional ratio, composting and fermenting using microbial composite strain, and granulating to obtain bio-organic fertilizer.    USE - The method is useful for preparing bio-organic fertilizer using recycled water flocculation sludge of mechanical pulp production.    ADVANTAGE - The method uses mechanical pulping process to prepare bio-organic fertilizer; has simple production techniques, is economical; solves the problem of solid waste production; and provides economic benefit. The fertilizer contains large amount of organic matter and beneficial microorganism, which can improve the utilization rate of crops to nitrogen, phosphorus, and potassium, promote the growth of crops, and improve the yield and soil ecological environment, which is good for agriculture sustainable development.
NOVELTY - A lower-temperature cobalt Fischer-Tropsch synthetic catalyst comprises 15-40 (preferably 15-30) wt.% molybdenum modified alumina as carrier, and 0.01-2 wt.% cobalt as active component.    USE - A lower-temperature cobalt Fischer-Tropsch synthetic catalyst.    ADVANTAGE - The catalyst has desired carbon monoxide conversion rate and excellent methane selectivity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of preparing a lower-temperature cobalt Fischer-Tropsch synthetic catalyst comprising mixing platinum sol and aluminum sol at a ratio of 1:30-100; heating at 50-90 degrees C while stirring for 10-24 hours to form a gel; drying; calcining at 250-550 degrees C for 2-15 hours; adding 0.001-0.05 mol/l chlorine molybdate solution; drying at 100-180 degrees C for 2-60 minutes; soaking dried material in a cobalt salt solution having a pH of 3 for ; drying; calcining; and soaking in alkali solution for surface modification treatment.
NOVELTY - 2,5-dichlorophenol as raw material is sulfonated and brominated to obtain 4-hydroxy-2,5-dichloro-3-bromobenzenesulfonic acid. 4-hydroxy-2,5-dichloro-3-bromobenzenesulfonic acid is treated using magnesium or lithium alkyl metal complex, and electrophilic addition reaction is carried out with carbon dioxide to obtain 5-sulfo-3,6-diclorsalicylic acid. The resulting material is subjected to o-methylation reaction, to obtain 3,6-dichloro-2-methoxybenzoic acid (dicamba).    USE - Synthesis of 3,6-dichloro-2-methoxybenzoic acid (claimed).    ADVANTAGE - The method environmentally-friendly provides 3,6-dichloro-2-methoxybenzoic acid having high quality with high yield, by a simple process.
NOVELTY - Producing fuel ethanol by using processing corncob leftover comprises (a) preparing corncob leftover and complex enzyme preparation containing 5-30 g/L cellulose enzyme, 30-90 g/L excision enzyme and 1-20 g/L beta -glucosidase; and (b) mixing corncob leftover and complex enzyme preparation at 45-60 degrees C for 0-36 hours, then adjusting the temperature to 24-44 degrees C so as to dry yeast, adding Saccharomyces cerevisiae, saccharifying and fermenting.    USE - The method is used for producing fuel ethanol (claimed).    ADVANTAGE - The method provides fuel ethanol with high yield, and requires low energy consumption.
NOVELTY - A biodiesel preparing method involves adding methanol into a glass reactor with a jacket, and starting an electromagnetic stirrer. Catalyst and rapeseed oil are added into the reactor, and hot water is circulated into the reactor. The reactor is heated to 56-65 degrees C, and heat is preserved for 2.5 hours.    USE - Method for preparing biodiesel.    ADVANTAGE - The method enables effectively catalyzing ester exchanged rapeseed oil to prepare the biodiesel, so that yield rate of the obtained biodiesel can reach 91%. The catalyst used in the method has high catalyst alkalinity, better heat stability and low solubility in alcohol.
NOVELTY - A refrigerant mixture comprises propane (R290), 1,1,1,3,3-pentafluoropropane composition (R245fa), chloro-1,2,2,2-tetrafluoroethane composition (R124), and chloro-1,1-difluoroethane composition (R142b).    USE - A refrigerant mixture for heat pump or air conditioning system.    ADVANTAGE - Refrigerant mixture can be directly poured into compressor air conditioning system without requiring additional medium, does not damage the ozone layer, and has low greenhouse effect potential, good cycle performance, low COP designed working condition of 4, and unit mass output net work of greater than or equal to 150 kJ/kg.
NOVELTY - A refrigerant mixture comprises isobutane (R600a), 1,1,1,3,3-pentafluoropropane (R245fa), trifluoroiodomethane (R1311), difluoro-1,1-ethane (R152a), chloro-1,1-difluoroethane (R142b), and 1-chloro-1,2,2,2-tetrafluoroethane (R124).    USE - A refrigerant mixture for heat pump or air conditioning system.    ADVANTAGE - Refrigerant mixture does not damage ozone layer, has low greenhouse effect potential, good cycle performance, low coefficient performance of 4, and mass output net work of greater than or equal to 150 kJ/kg, and can be directly poured to compressor air conditioning system without requiring additional medium.
NOVELTY - A composite liquid fuel is manufactured by collecting sewage, deploying sewage into regulating pool, adding microbial agents for sewage purification and deodorization, fermenting sewage microorganisms under aerobic condition at room temperature and atmospheric pressure, and continuous multi-stage filtering in which sewage gas is introduced into composite liquid fuel.    USE - Manufacture of composite liquid fuel(claimed).    ADVANTAGE - Manufacturing process is simple, low cost, capable for industrial production and application, technology is provided with good economic benefits, environment-friendly, and develops bio-renewable energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a process flow diagram of the manufacture of composite liquid fuel. (Drawing includes non-English language text).
NOVELTY - A hydrogen-oxygen mixed gas generator comprises gas generation system having electrolytic tank with electrolysis chamber (11), electrolytic cell (1), hydrogen outlet (2), oxygen outlet, hydrogen tank water seal unit, oxygen tank (4), hydrogen discharge pipe and oxygen discharging tube; electrolyte circulating supplying system having liquid tank, liquid outlet opening and pipeline.    USE - Hydrogen-oxygen mixed gas generator used to separate hydrogen and oxygen.    DESCRIPTION OF DRAWING(S) - The drawing shows a sketch map of hydrogen-oxygen mixed gas generator.    Electrolytic cell (1)    Hydrogen outlet (2)    Oxygen tank (4)    Electrolysis chamber (11)    Diaphragm (12)
NOVELTY - An endoglucanase gene Cel6 of an encoding glycosyl hydrolase family 6, where the nucleotide sequence is shown as fully defined 999 bp (SEQ ID NO: 1), given in the specification, is new.    USE - The gene and the protein are useful for degrading cellulose (claimed).    ADVANTAGE - The enzyme can be effectively used in the decomposition of cellulose, and can be used in the production of cost-effective fuels.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) an expression vector, comprising the gene; and    (2) a host cell, comprising the expression vector, where it is a prokaryotic cell or a eukaryotic cell.
NOVELTY - Processing biomass gas, comprises adding crushed biomass raw material into a cracking multistage reactor, converting isolated air into residual gas mixture, passing into reaction system for removing residual to obtain gas phase product by pyrolysis sections-I and II, carrying out steam reaction for catalytic cracking to obtain cracking product such as hydrogen and methane, synthesizing gas and light hydrocarbon component by a gas filter and thermal type flow meter to obtain gas product i.e. hydrogen with a volume content of 89-92.5%.    USE - The processing of biomass gas is useful for producing hydrogen (claimed).    ADVANTAGE - The method provides improved hydrogen content of 89-92.5% with mild reactions and without secondary reactions.
NOVELTY - Processing pig farm nitrogen phosphorus slurry comprises pumping biogas slurry after recovering of nitrogen phosphorus in the pig farm to from a settling tank and a top of the biological aerated filter tank by a water pump, enabling the biogas slurry to flow down and then entering into a filter material layer, simultaneously performing aeration and oxygenation on the filter material layer by a roots blower, enabling outlet water to enter a back-washing clear water tank from the bottom of the biological aerated filter, and overflowing and draining the outlet water from the tank.    USE - The method is useful for processing pig farm nitrogen phosphorus slurry for recycling biogas (claimed).    ADVANTAGE - The method is capable of processing the pig farm nitrogen phosphorus slurry with improved water quality.
NOVELTY - A biomass-containing slurry comprises lignite, caustic alkali mixed at normal pressure and room temperature, where biomass, lignite and caustic alkali is at a mass ratio of 1:(0.5-1):(0.05-0.18).    USE - Biomass-containing slurry used for fixed bed furnace coal gasification (claimed).    ADVANTAGE - The slurry realizes high-efficiency biomass gasifying, reduces dependence on fossil resources, and realizes low carbon discharge to a certain degree.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing fixed bed coal gasification furnace comprising:    (A) mixing into slurry biomass, lignite, caustic alkali, water according to ratio, under normal pressure and room temperature; and    (B) adding slurry obtained to coal, stirring uniformly, obtaining mixture, pressing and forming, and drying, where, anthracite, lignite and biomass mixture total weight is 100% and biomass is 5-10 wt.%.
NOVELTY - A lipase catalyst immobilized on sepiolite, is claimed.    USE - The lipase catalyst immobilized on sepiolite is useful for preparing biodiesel (claimed).    ADVANTAGE - The dosage of the immobilized lipase catalyst is low, and the immobilized lipase catalyst can be reused by 10 times. The biodiesel prepared from the catalyst is high in reaction activity and high in reaction speed, reaction conditions are mild relatively, reaction can be carried out under atmospheric pressure at low temperature, and reaction energy consumption and cost can be reduced. The production process is environmentally-friendly, an operation process is simple, and erosion to equipment is low.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for preparing immobilized lipase catalyst, involves (a) carrying out acid modification to the sepiolite, and (b) immobilizing the lipase on the sepiolite obtained by step (a) of the acid modification; and    (2) method for preparing biodiesel by enzymatic method, involves obtaining 0.8-10 wt.%, preferably 1-8 wt.% lipase catalyst, and 100 wt.% vegetable oil, adding vegetable oil, methanol and immobilized lipase catalyst to a reaction container, performing enzymatic catalytic reaction, pumping to recycle the lipase, distilling the filtrate, recycling methanol, filtering out glycerol by the remaining portion, where the remaining portion is the biodiesel, where the molar ratio of vegetable oil and methanol is 1:2-1:5, preferably 1:3, the methanol is added to the container within three times, the adding frequency is 22-25 hours for once, preferably 24 hours for once, the reaction is 30-40 degrees C, the total reaction time is 66-78 hours, preferably 72 hours.
NOVELTY - Multiple layer is provided, crushed, added to carbon dioxide extraction device, diester is provided as entrainer in solvent and extracted, to obtain extract. The obtained extract is added to macro-porous adsorption resin column, ethanol is eluted and decompressed. Dialcohol is recycled, concentrated and added to silica gel chromatography column and dichloromethane-methanol mixed solvent. The collected portion is eluted, decompressed and solvent is recycled, concentrated, acetone is added, separated and crystallized, and washed and dried, to obtain tylophorine.    USE - Method for extracting tylophorine from tylophora florlbunda (claimed).    ADVANTAGE - The method for extracting tylophorine from tylophora florlbunda with high purity is economically enabled without polluting the environment, by simple method.    DETAILED DESCRIPTION - Multiple layer is provided, crushed, added to carbon dioxide extraction device, diester is provided as 2-5% entrainer in total extraction solvent under extracting pressure of 30-40 MPa at 50-60 degrees C, and extracted for 80-120 minutes, to obtain extract. The obtained extract is added to macro-porous adsorption resin column, 50-70% ethanol is eluted, 3-8 times column is collected and decompressed. Dialcohol is recycled, concentrated, and added to the silica gel chromatography column and dichloromethane-methanol mixed solvent in the ratio of 4:1. The collected portion is eluted, 5-9 parts eluent is combined, decompressed and solvent is recycled, and concentrated, acetone is added, separated and crystallized, and washed and dried, to obtain tylophorine.
NOVELTY - Preparing bifenthrin, comprises (i) carrying out esterification reaction of 3-(2-chloro-3,3,3-trifluoro-1-propenyl)-2,2-dimethylcyclopropan-carboxylic acid and low molecular weight alcohol compound (I) in presence of an acid catalyst to obtain 3-(2-chloro-3,3,3-trifluoro-1-propenyl)-2,2-dimethylcyclopropan-carboxylate compound (II); and (ii) carrying out transesterification reaction of (II) and (2-methylbiphenyl-3-yl)methanol in presence of titanate catalyst to obtain the product.    USE - The method is useful for preparing bifenthrin.    ADVANTAGE - The method is simple, environmentally friendly, and suitable for industrial Production; and produces highly pure product.    DETAILED DESCRIPTION - Preparing bifenthrin, comprises (i) carrying out esterification reaction of 3-(2-chloro-3,3,3-trifluoro-1-propenyl)-2,2-dimethylcyclopropan-carboxylic acid and low molecular weight alcohol compound of formula (R-OH) (I) in presence of an acid catalyst to obtain 3-(2-chloro-3,3,3-trifluoro-1-propenyl)-2,2-dimethylcyclopropan-carboxylate compound of formula (II); and (ii) carrying out transesterification reaction of (II) and (2-methylbiphenyl-3-yl)methanol in presence of titanate catalyst to obtain the product.    R = 1-4C alkyl.
NOVELTY - Azelaic acid and isooctanol are esterified in the mass ratio of 1:2.0-3.0 using catalyst loaded with heteropoly acid at 140-250 degrees C for 2-10 hours under protection of nitrogen to obtain diisooctyl nonane diacid crude product. The catalyst in the crude product is removed and the filtrate is heated at 150-250 degrees C under vacuum of 0-500 Pa, and distilled for 40-120 minutes to obtain diisooctyl azelate.    USE - Manufacture of diisooctyl azelate (claimed).    ADVANTAGE - The diisooctyl azelate is manufactured by a simple, economical and environmentally-friendly process with yield of 96%.
NOVELTY - Producing dimethyl disulfide by methyl mercaptan oxidation, comprises: taking methyl mercaptan as raw material, oxygen or sulfur as oxidant, nitrogen dioxide as catalyst, and acetone, dimethylformamide and dimethyl sulfoxide as emulsifier; feeding methyl mercaptan, oxygen and nitrogen dioxide into tower type reactor, performing oxidation reaction in presence of an emulsifier, and allowing the reaction product to stand, separating, and then obtaining dimethyl disulfide crude product by separating technology, and obtaining qualified dimethyl disulfide product by rectifying process.    USE - The method is useful for producing dimethyl disulfide by methyl mercaptan oxidation.    ADVANTAGE - The method has great social benefit and economic effect of reducing the product cost, comprehensively utilizes the resource, and reduces the environment pollution.    DETAILED DESCRIPTION - Producing dimethyl disulfide by methyl mercaptan oxidation, comprises: taking methyl mercaptan as raw material, oxygen or sulfur as oxidant, nitrogen dioxide as catalyst, and acetone, dimethylformamide and dimethyl sulfoxide as emulsifier; feeding methyl mercaptan, oxygen and nitrogen dioxide in a ratio of 4:1.25:0.2 into tower type reactor, performing the oxidation reaction in the presence of the emulsifier, where the methyl mercaptan and emulsifier molar ratio is 1:10-30, the reaction temperature is 10-150 degrees C, the pressure is 0.01-0.1 MPa, and allowing the reaction product to stand for 10-20 minutes, separating at different liquid level, and then obtaining dimethyl disulfide crude product by separating technology, and obtaining qualified dimethyl disulfide product by rectifying process.
NOVELTY - Preparing drospirenone, comprises reacting (3S,5R,10R,13S,15S,16S)-3,5-dihydroxy-10,13-dimethyl-1,2,3,4,5,8,9,10,11,12,14,15,16,20-tetradecahydro-13H-cyclopropa(15,16)cyclopenta(a)phenanthren-17-one with methyl iodide, reacting obtained 5a-methyl-tetradecahydro-cyclopropa(l)phenanthrene-1b,3-diol compound (II) with bromo methyl ester, reacting obtained 5a,8-dimethyl-tetradecahydro-cyclopropa(l)phenanthrene-1b,3-diol compound (III) with sodium ethoxide and reacting obtained 5a-methyl-tetradecahydro-cyclopropa(l)phenanthrene-1b,3-diol compound (IV) with sodium hypochlorite.    USE - The method is useful for preparing drospirenone (claimed).    ADVANTAGE - The method is capable of preparing drospirenone with high yield, high purity, good quality and good stability in a cost-effective and environmental-friendly manner.    DETAILED DESCRIPTION - Preparing drospirenone, comprises reacting (3S,5R,10R,13S,15S,16S)-3,5-dihydroxy-10,13-dimethyl-1,2,3,4,5,8,9,10,11,12,14,15,16,20-tetradecahydro-13H-cyclopropa(15,16)cyclopenta(a)phenanthren-17-one with methyl iodide in the presence of zinc-copper to obtain (1bR,3S,5aR)-5a-methyl-tetradecahydro-cyclopropa(l)phenanthrene-1b,3-diol compound of formula (II), reacting (II) with bromo methyl ester in the presence of lithium tetrahydrofuran (Li/THF) solution to obtain (1aR,1bR,3S,5aR,8R,9bR)-5a,8-dimeth yl-tetradecahydro-cyclopropa(l)phenanthrene-1b,3-diol compound of formula (III), reacting (III) with sodium ethoxide in the presence of dimethylformamide solution to obtain (1aR,1bR,3S,5aR,9bR)-5a-methyl-tetr adecahydro-cyclopropa(l)phenanthrene-1b,3-diol compound of formula (IV), and reacting (IV) with sodium hypochlorite in the presence of p-toluenesulfonic acid and tetrahydrofuran.
NOVELTY - Mixed bacteria, are new. The mixed bacteria comprise Acinetobacter lwoffii (CGMCC 5973), Pseudomonas fluorescens (CGMCC 5974) and Wickerhamomyces anomalus (CGMCC 5975).    USE - The mixed bacteria are useful for producing cellulose which is useful in preparation of additives (all claimed).    ADVANTAGE - The mixed bacteria produce environmentally-friendly cellulose, as the mixed bacteria convert waste liquid into organic fertilizers directly rather than being discharged. The method is cost-effective and causes no pollution, as compared to existing method, and consumes less energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing cellulose used for preparing additive, which involves uniformly mixing the above-mentioned strains in a mass ratio of 1-2:1-2:2-3 to obtain strain solution, slicing woody raw materials or cutting herbal raw materials, and soaking the sliced product in water for swelling, preparing fiber by defibering, biodegradation, and steam sterilization, and collecting fibers, and sterilizing fibers and grounding the obtained fibers.
NOVELTY - Preparing biodiesel, comprises subjecting fatty acid alkylester and glycerol to transesterification, and converting biomass to a porous material through thermal process.    USE - The method is useful for preparing biodiesel (claimed) such as direct non catalytic biodiesel.    ADVANTAGE - The biodiesel can be economically and rapidly prepared with high purity.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic view of a method for producing biodiesel.
NOVELTY - Chloro-phenoxy acrylate, nitrogen-containing organic alkali and ferrous chloride are reacted in the molar ratio of 1:0.15-0.25:1.1-1.25, at 50-100 degrees C to obtain quaternary ammonium salt reaction liquid. Ethanolamine is added to the reaction liquid and reacted at 80-90 degrees C for more than 2 hours. The mol ratio of ethanol amine and the chlorophenoxy acrylate is 1.00:1.00-1.10. Toluene, monohydric alcohol and active carbon are added to the reaction liquid and decolored. The decolored reaction liquid is filtered, cooled and crystallized to obtain meclofenoxate hydrochloride.    USE - Manufacture of meclofenoxate hydrochloride used as psychostimulant.    ADVANTAGE - The meclofenoxate hydrochloride is manufactured economically under mild and easily controlled reaction conditions. The manufacturing process is environmentally-friendly. The meclofenoxate hydrochloride of high purity and stable quality is manufactured.    DETAILED DESCRIPTION - Chloro-phenoxy acrylate, nitrogen-containing organic alkali and ferrous chloride are reacted in the molar ratio of 1:0.15-0.25:1.1-1.25, at 50-100 degrees C to obtain quaternary ammonium salt reaction liquid. Ethanolamine is added to the reaction liquid and reacted at 80-90 degrees C for more than 2 hours. The mol ratio of ethanol amine and the chlorophenoxy acrylate is 1.00:1.00-1.10. Toluene, monohydric alcohol and active carbon are added to the reaction liquid and decolored. The decolored reaction liquid is filtered, cooled and crystallized to obtain meclofenoxate hydrochloride. The nitrogen-containing organic alkali is triethylamine or diisopropylethylamine.
NOVELTY - Method for growing plants by using space waste and wastewater involves (a) preparing soil substrate for plants by mixing fermented waste and vermiculite, where the fermented waste is obtained by subjecting wheat straw to microbial fermentation, (b) preparing plant nutrient solution by mixing treated wastewater, tap water and Hoagland full-nutrient solution, where the treated wastewater is obtained by subjecting wastewater to microorganism treatment, and (c) growing plants in the prepared soil substrate, and watering the prepared plant nutrient solution.    USE - The method is useful for growing plants using space waste and wastewater (claimed).    ADVANTAGE - The method enables to grow plants in a controlled ecological life support system under a space condition by using renewable resources, and improve the closure of the system as the method uses analog wastewater and waste renewable resources for plants is researched on the basis of using the method of waste and wastewater renewable resources recycling method in agricultural and industrial productions for reference and according to the characteristics of a sealed ecosystem.    DETAILED DESCRIPTION - Method for growing plants by using space waste and wastewater involves (a) preparing soil substrate for plants by mixing fermented waste and vermiculite in a ratio of 1:1, where the fermented waste is obtained by subjecting wheat straw to microbial fermentation, (b) preparing plant nutrient solution by mixing treated wastewater, tap water and Hoagland full-nutrient solution in a ratio of 1:1:2, where the treated wastewater is obtained by subjecting wastewater to microorganism treatment, and (c) growing plants in the prepared soil substrate obtained in the step (a) and watering plant nutrient solution obtained in the step (b).
NOVELTY - Pesticide and bactericide composition, comprises an antiseptic, a solvent, an anti-freezing agent, a thickening agent, an emulsifying agent and deionized water, where: the bactericide comprises azoxystrobin and propiconazole; the solvent comprises e.g. methyl pyrrolidone compound, lower mono-alcohol compound, isophorone, methylene dichloride, acetonitrile, ethyl acetate, toluene and xylene; the anti-freezing agent comprises ethylene glycol; the thickening agent comprises carboxymethyl cellulose; and the emulsifying agent comprises polyoxyethylene-polyoxypropylene block polymer compound.    USE - The pesticide and bactericide composition is useful for treating sub-leaf spot disease, glume blight disease, downy mildew and rice blast.    ADVANTAGE - The pesticide and bactericide composition has less toxicity, and can be economically prepared in an environmentally friendly manner.    DETAILED DESCRIPTION - Pesticide and bactericide composition, comprises an antiseptic, a solvent, an anti-freezing agent, a thickening agent, an emulsifying agent and deionized water, where: the bactericide comprises 100-180 g/l of azoxystrobin and propiconazole; the solvent (150-300 g/l) comprises methyl pyrrolidone compound, lower mono-alcohol compound, isophorone, methylene dichloride, acetonitrile, ethyl acetate, toluene, xylene, N,N-dimethyl formamide, acetone, hexane and cyclohexane; the anti-freezing agent (50-100 g/l) comprises ethylene glycol; the thickening agent comprises carboxymethyl cellulose; and the emulsifying agent comprises 5-10 g/l of polyoxyethylene-polyoxypropylene block polymer compound or 50-100 g/l of alkylphenol polyoxyethylene ether.
NOVELTY - Nutrient soil, comprises humus, phosphorus, peat soil, organic fertilizer, and trace elements in a mass ratio of 7-8:1-3:1-3:0.5-1.5:0.001.    USE - The nutrient soil is useful for yew (claimed).    ADVANTAGE - The nutrient soil improves growth and development of yew, contains different mineral nutrients based on the growth requirements of yew, is capable of loosening and ventilation, preserves moisture and fertility, prevents diseases and pests, greatly prolongs indoor curing time of yew, and improves indoor curing survival rate of yew.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the nutrient soil, which involves (a) selecting soil having humus content of 2.8-3.2% and pH of 6-7 as main substrate and mixing the above-mentioned components, (b) uniformly mixing the components and spraying 0.5-0.8 ml insecticide, and (c) spraying 0.5-1.5 ml sterilizing agent, covering the mixture with plastic film for fermentation and turning the mixture once after 5 days for 1 month.
NOVELTY - N-Acyl-N-methyl-taurine is obtained by methylating sodium N-acyl taurate using dimethyl sulfate under alkaline conditions, and acidifying.    USE - Synthesis of N-acyl-N-methyl-taurine (claimed).    ADVANTAGE - The method enables simple, easy and environmentally-friendly synthesis of N-acyl-N-methyl-taurine under mild reaction conditions on an industrial scale.
NOVELTY - Metronidazole is dissolved in a solvent, benzoyl chloride is added and esterified at 50-700 degrees C in a solvent. Salt-free water is added to the reaction product and cooled, and solid is completely dissolved. The organic phase is cooled to obtain benzoyl metronidazole crude product. The crude product is added into ethanol solvent, dissolved, and active carbon is added, filtered, cooled, crystallized, filtered, washed and dried to obtain benzoyl metronidazole. The amount of ethanol is 40-60 volume%.    USE - Manufacture of benzoyl metronidazole.    ADVANTAGE - The benzoyl metronidazole is manufactured with high yield and high quality without affecting environment.    DETAILED DESCRIPTION - Metronidazole is dissolved in a solvent, benzoyl chloride is added and esterified at 50-700 degrees C in a solvent chosen from tributylamine, tri-n-butylamine-toluene binary mixture, tri-n-butylamine-acetone binary mixture, tri-n-butylamine-toluene acetone ternary mixture. Salt-free water is added to the reaction product and cooled, and solid is completely dissolved. The organic phase is cooled to obtain benzoyl metronidazole crude product. The crude product is added into ethanol solvent, dissolved, and active carbon is added, filtered, cooled, crystallized, filtered, washed and dried to obtain benzoyl metronidazole. The amount of ethanol is 40-60 volume%.
NOVELTY - Catalytic oxidation of hydroxyzine involves using palladium-metal/carbon catalyst.    USE - Catalytic oxidation of hydroxyzine used for manufacturing cetirizine.    ADVANTAGE - The catalytic oxidation of hydroxyzine is carried out by a short process using inexpensive raw material, with high conversion rate and high selectivity. The organic solvent used in the process can be recycled, and the catalytic oxidation process is environmentally-friendly.
NOVELTY - A carrier gas with purity of more than 99.999% is purified and supplied into chromatographic column (I), and absorbing and desorbing. Argon and oxygen, nitrogen, methane, carbon dioxide and nitrous oxide of the sample is fed into electron-capture detector. Simultaneously, carrier gas and argon and oxygen, nitrogen, methane, carbon dioxide and nitrous oxide are fed into chromatographic column (II) and absorption and desorption is carried out. The sample is fed into thermal conductivity cell detector and flame ionization detector for detection, and a chromatogram is obtained.    USE - Detection of argon and oxygen, nitrogen, methane, carbon dioxide and nitrous oxide in sample (claimed).    ADVANTAGE - The analysis method is simple and easy, provides high accuracy data and shortens the measurement period.    DETAILED DESCRIPTION - A carrier gas with purity of more than 99.999% is purified and supplied into s chromatographic column for placing a sample to-be-detected in a gas chromatograph (I), and absorbing and desorbing at 25-250 degrees C. Argon and oxygen, nitrogen, methane, carbon dioxide and nitrous oxide of the sample to-be-detected is fed into an electron-capture detector, and carbon dioxide and nitrous oxide are detected at 90-350 degrees C. The detected data is fed into a chromatographic work station in the gas chromatograph. Simultaneously, the carrier gas and argon and oxygen, nitrogen, methane, carbon dioxide and nitrous oxide are fed into a chromatographic column (II) and absorption and desorption is carried out. The sample to-be-detected is fed into a thermal conductivity cell detector and a flame ionization detector for detection in sequence. The data obtained is fed into a chromatographic work station to obtain a chromatogram with an analysis result.
NOVELTY - Solar heat supply superconductivity heat radiator warming controllable biological fermentation chamber device comprises a circulating water pump, an upper water pipe, a water supply tower, a water supply pipe, a solar water heater, a downcomer, a hot water tap, walls, a superconducting heating radiator, an air exchange device, an information window (thermocouple), and a feeding and discharging door, where the starting of the water circulating pump supplies water to water supply tower through upper water pipe and water in the tower enters solar water heater through water supply pipe.    USE - Used as a solar heat supply superconductivity heat radiator warming controllable biological fermentation chamber device.    ADVANTAGE - The device can ensure uniformity in fermentation and decomposition, where the decomposition degree can reach upto 80%; and has simple structure with simple and convenient operation; thus provides a feasible biological fermentation device for industrial production of organic fertilizer, and is suitable for the organic fertilizer factory and household waste fertilizer factory of different scales.
NOVELTY - The device has front cabin, rear cabin, control system, and exhaust system. The control system has electric control box, temperature sensor, humidity sensor, and indicator lamp. The aeration system has aeration fan, aeration pipe and aeration valve. The bottom corners of front cabin have fixing pins. The front cabin is provided with clapboard for dividing front cabin into upper and lower cabin portions. The exhaust pipe set on top of front cabin, is connected to aeration fan. The lower cabin portion is connected to drainage valve. The rear cabin is provided with a damping pin.    USE - Modular type processing device for treating garbage in rural areas.    ADVANTAGE - The energy consumption of the device can be reduced and the structural design of the device can be improved. The heat insulating property, waterproof function and durability of the device can be improved. The garbage treatment effect can be improved by the environment-friendly garbage processing device. The occupied space of the device can be reduced and the manufacturing cost of the device can be lowered. The maintenance property and operability of the device can be improved.
NOVELTY - Preparation of 6-gingesulfonic acid involves a) crushing dry stem of ginger, adding 70% of ethanol water solution extracted by ultrasonic wave for 2-3 times, filtering to obtain extracting solution, condensing and drying solution until there is no alcohol taste, purifying crude product in a macro-porous resin column using normal hexane, ethyl acetate, ethanol and water as solvent system, where upper phase is fixed phase, and lower phase is mobile phase, at room temperature to give 6-gingesulfonic acid crude product, and separating by high speed counter-current chromatography.    USE - For preparation of 6-gingesulfonic acid (claimed) useful for treating hydrochloric acid/ethanol induced gastric ulcer.    ADVANTAGE - The method is safe, pollution-free and environmentally-friendly, which allows preparation of highly pure (purity of more 95%) 6-gingesulfonic acid with high molecular weight.
NOVELTY - Method for manufacturing environmentally-friendly fertilizer, involves mixing yogurt, dry-yeast, sugar and fermented soybeans to obtain mixture, adding warm water of 35-45 degrees C to the mixture to obtain raw materials, fermenting the raw materials at 35-45 degrees C 7-10 days, and adding cool water to fermented raw materials.    USE - The method is useful for manufacturing fertilizer (claimed).    ADVANTAGE - The method is environment-friendly.
NOVELTY - Aerobic close box type compost fermenting device comprises blower, air supply pipe, closed compost box, air distribution device, feeding port, temperature time controller, temperature sensor, ozone treatment device, exhaust fan, plastic plate, air outlet, and air inlet. The closed compost box is provided at the bottom of air distribution device. It is provided with exhaust port connected with air supply pipe and exhaust fan. The air inlet is connected with exhaust fan through air supply pipe in the closed compost box body.    USE - Aerobic close box type compost fermenting device.    ADVANTAGE - The device can provide fresh air into the compost material; is harmless; achieves fast decomposition process; can be widely applied for any weather condition; processes the harmful gas before releasing to the atmosphere; and reduces pollution to the atmosphere.
NOVELTY - Straw methane is manufactured by air drying straw, crushing to less than or equal to 2 cm, inoculating anaerobic sludge from sewage treatment plant for greater than or equal to 1 week, fully immersing chopped straw in aqueous ammonia, where ammonia is 2% of dry weight of straw, aqueous ammonia is 30-90%, and total amount of water is 60-90%, in a vacuum sealed bag, storing at 25-35 degrees C for 90-110 hours, mixing 50-100 g TS/L pre-treated straw and 15 gMLSS/L anaerobic sludge in anaerobic fermentation reactor, adding water to total volume of 80-90%, supplying nitrogen, sealing with rubber stopper, and agitating at 32-37 degrees C.    USE - Manufacture of straw methane for clean energy.    ADVANTAGE - Anaerobic fermentation period is shortened, manufacturing cost is greatly reduced, and methane production is increased.    DETAILED DESCRIPTION - Straw methane is manufactured by air drying straw, crushing to less than or equal to 2 cm, inoculating anaerobic sludge from sewage treatment plant for greater than or equal to 1 week, fully immersing chopped straw in aqueous ammonia, where ammonia is 2% of dry weight of straw, aqueous ammonia is 30-90%, and total amount of water is 60-90%, in a vacuum sealed bag, storing at 25-35 degrees C for 90-110 hours, mixing 50-100 g TS/L pre-treated straw and 15 gMLSS/L anaerobic sludge in anaerobic fermentation reactor, adding water to total volume of 80-90%, supplying nitrogen, sealing with rubber stopper, and agitating at 32-37 degrees C. The amount of total solids (TS) and total volatile solids (VS), daily gas production, and % content of methane are determined.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph of the pH value change with respect to time. (Drawing includes non-English language text).
NOVELTY - A Chinese herbal medicine Ophiopogon nutrient fertilizer is prepared by combining (g) dry sheep manure (2000), dry rabbit manure (1150), dry pig manure (1300), dry duck manure (3000), broomcorn cake powder (3000), bone powder (1000), bean cake powder (6000), corn cake powder (2000), rice straw powder (2000), urea (1000), manganese fertilizer (2000), calcium superphosphate (600), chlorothalonil (300), dichlorodiphenyltrichloroethane (1000), and polyoxin (2000).    USE - Method for preparing Chinese herbal medicine Ophiopogon nutrient fertilizer (claimed) used for stimulating growth of Ophiopogon and resisting disease and insect pests.    ADVANTAGE - The method can prepare fertilizer which has no pollution and no mites and is rich in nutrients.
NOVELTY - Zeolite is obtained by mixing an alkali-free glass and an alkaline solution, and carrying out hydrothermal synthesis by heating the mixture at 70-150 degrees C for 3-100 hours.    USE - Manufacture of zeolite e.g. A-type zeolite, for molded products, water purification agents, soil modification agents, and fertilizer preservatives (all claimed). Can also be used for catalysts.    ADVANTAGE - The method reduces energy consumption, enables effective usage of alkali-free glass recovered from LCD device, does not require high-temperature melting, and is efficient, economical and environmentally-friendly. The obtained zeolite has excellent ion-exchange capacity.
NOVELTY - The system performs inflow process into which the liquid (1) contains an organic substance in the fuel cell for carrying out anaerobic microbe functions on an electrode. The electric power generation process is performed to generate electric-power while the liquid containing organic substance in microbial fuel cell is processed biologically. The separation process is performed to carry out the solid liquid separation of liquid processed by microbial fuel cell (4).    USE - Microorganism fuel cell system.    ADVANTAGE - Since the density of microorganisms can be raised, the collection efficiency of energy of the microorganism fuel cell system can be improved effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the microorganism fuel cell system.    Liquid containing an organic substance (1)    Pretreatment facility (2)    Flow volume adjustment tank (3)    Microbial fuel cell (4)    Pump (5)
NOVELTY - Biofuel in the form of pellets, comprises up to 30 wt.% of coal and 60-70 wt.% of a mixture of at least two exits of agricultural products obtained from sorting operations, calibration, screening of cereals, oilseeds and/or protein such as broken grains, glumes, glumellae, pods, leaves or stems.    USE - The biofuel is useful for thermal power plants to reduce emissions (such as nitrogen gas and carbon monoxide gas) of greenhouse gas from the thermal power plants during their operation, and for boilers including vibrating grid and circulating fluidized bed, automatic grate boiler or volcano fire tube boiler.    ADVANTAGE - The biofuel efficiently improves the performance and life of the thermal power plants without altering their properties and with improved energy density.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing the biofuel comprising mixing the above components, grinding the components and performing a second phase of mixing the grinded mixture, and granulating the mixture.
NOVELTY - Solid fuel, in the form of a powder, comprises at least one powdered lignocellulosic component comprising particles having a mean diameter and median diameter (d50) of less than 35 mu m, preferably 10-20 mu m, and a moisture level of at most 15 wt.%, preferably less than or equal to 2 wt.%.    USE - The powdered lignocellulosic component is useful for producing a solid fuel for an internal combustion engine or in a burner (claimed).    ADVANTAGE - The powdered solid fuel: is less abrasive and easily storable and transportable; reduces wear of the engine; and increases the combustion speed and quality.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparing the powdered lignocellulosic component comprising (a1) grinding cereal straw to obtain powdered particles having a mean diameter and a median diameter (d50) of greater than 0 to 3000 mu m, preferably 200-2000 mu m, (a2) grinding the obtain powdered particle to obtain a powdered powder having a mean diameter and a median diameter (d50) of less than or equal to 150 mu m, preferably less than or equal to 135 mu m, and (a3) grinding the obtained powdered particle to obtain a powdered particle having a mean diameter and median diameter (d50) of less than or equal to 35 mu m, preferably 10-20 mu m; and    (2) producing energy comprising introducing the solid fuel in the form of a powder alone or in mixture with an oxidizing gas or a liquid fuel to form a suspension, passing the fuel or the suspension on a controlled flow with an ignition source, and initiating combustion of the fuel and the suspension or burning the fuel in the form of a powder, to produce energy.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of process for producing the solid fuel.
NOVELTY - Method for in situ consolidation of soil comprises: (a) injecting a solution of calcifying bacteria, prepared from bacteria powder, in a volume of soil to be treated; (b) injecting a calcifying solution; (c) washing the volume of the soil to be treated with water; (d) measuring the concentration of ammonium ions in the washing water and in the treated soil; and (e) recycling the washing water in the process.    USE - The method is useful for in situ consolidation of soil or several parcels of soil (all claimed).    ADVANTAGE - The method: provides soil with improved porosity and enriched nutrients; is carried out in an environmentally friendly manner; is compatible with the conditions of building site; allows a flexible management of the characteristics of the biomass; and does not require important and expensive installations for the preparation of the solutions of bacteria to be injected.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for in situ consolidation of several parcels of soil comprising performing the above method for each of the parcels.
NOVELTY - The grid has a concentric plate rings whose primary set is arranged at various levels to form a conical downwards tapering structure. A supporting structure is provided with an annular supporting beam (25) below the set of rings and supporting beams are ex-tended radially. A secondary group of rings is formed by rings arranged between a primary rings and has nozzle openings for leading air and other fluidizing gas into the reactor.    USE - Grid structure for fluidized bed gasifier used for producing gasification gas from wood-based fuel.    ADVANTAGE - The fixing of the beams to the supports is accomplished by sliding shaft at the support sleeves, which allows thermal expansion of the beam structure in the direction of the radius of the grid and eliminates torque caused to the supports located on the wall due to bending of the beam structure. Thus, the supporting structure is supported at the outer edges of the beams and middle point is not fixed inflexibly, and the supporting structure is freely suspended at the center. The ash discharge pipe is connected flexibly to the ash discharge opening of the grid, and the lateral motion of the supporting structure is not prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the grid structure.    Planar plate ring (20)    Opening at bottom of grid (23)    Discharge duct (24)    Annular supporting beam (25)    Radial supporting beam (26)
NOVELTY - Recovering anhydrosugar alcohols from a mixture containing sugar alcohols, comprises: contacting the mixture with an adsorbent, where the anhydrosugar alcohols are selectively adsorbed; separating the adsorbent from the mixture; and desorbing anhydrosugar alcohols from the adsorbent by contacting the adsorbent with a desorbing solvent.    USE - The method is useful for recovering an anhydrosugar alcohol including anhydroxylitols and isosorbide from a mixture of sugar alcohols comprising xylitol and sorbitol (all claimed), where the recovered anhydrosugar alcohol is useful for making polymers, pharmaceuticals and fuel additives.    ADVANTAGE - The method effectively and safely recovers the anhydrosugar alcohol from the mixture of sugar alcohols, and prevents the degradation of isosorbide by maintaining the process at very low temperature in an environmentally friendly manner.
NOVELTY - The method involves collecting waste and separating coconut residue, where the coconut residue is carbonized. The carbonized coal material is milled and then mixed with binding agent. The obtained mixture is extruded and then dried through a briquetting unit. The formed briquettes are refrigerated and stored for a minimum period of two days for curing for making stable and uniform. The briquetting unit includes a hammer mill (1), interconnection mats (2), a raw material dosing unit (3), a mixer (4), briquette machine (5), tunnel dryer (6), and packer (7).    USE - Method for manufacturing fine charcoal briquettes from waste coconut for use as solid biofuel.    ADVANTAGE - The method manufactures charcoal briquettes in a clean and eco-friendly manner, which enables to replace firewood and charcoal kilns in various sectors of industry such as baking, pizzerias, steakhouses and others, and results a higher density fuel product with great mechanical resistance, low smoke generation, and uniform shape and sizes.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a briquetting unit.    Hammer mill (1)    Interconnection mats (2)    Raw material dosing unit (3)    Mixer (4)    Briquette machine (5)    Tunnel dryer (6)    Packer (7)
NOVELTY - A fuel modification catalyst comprises rhodium as catalyst component, and lanthanum aluminate formed using aluminum oxide particles. The rhodium is supported by the surface of lanthanum aluminate. The fuel modification catalyst generates reformed gas containing hydrogen.    USE - Fuel modification catalyst is used in fuel reforming system for generating reformed gas containing hydrogen (all claimed) and for internal combustion engine of motor vehicle.    ADVANTAGE - The fuel modification catalyst efficiently accelerates reforming reaction even under low temperature condition, and reduces load of rhodium on fuel modification catalyst.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of fuel modification catalyst, involves providing aluminum oxide powder having primary particle diameter of 0.2-1 mu m as starting material of aluminum oxide;    (2) fuel reforming system, which consists of fuel reforming reaction apparatus comprising fuel modification catalyst, fuel-injection apparatus and air supply apparatus installed in the system of an exhaust gas circulation system; and    (3) method of fuel reformation, which involves operating fuel reforming reaction apparatus under oxygen concentration contained in the exhaust gas discharged from the internal combustion engine of 1.2 vol.% or less.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of particle structure of fuel modification catalyst.
NOVELTY - Excess water vapor (BB) is added to exhaust gas (AA) containing carbon monoxide produced by metallurgical furnace and shift reaction is carried out to obtain mixed gas (CC) containing hydrogen, carbonic acid gas and excess water vapor or water (DD). The mixed gas is contacted with an organic substance and reforming reaction is carried out to reduce the molecular weight of the organic substance. Steam reforming the reaction product is carried out to produce hydrogen. The organic substance is plastics, oil-impregnated sludge, waste oil and/or biomass.    USE - Manufacture of hydrogen used for operation of blast furnace and as source gas, reducing agent and fuel for operation of iron mill (all claimed).    ADVANTAGE - The hydrogen is manufactured efficiently and economically, with reduced generation of carbonaceous material. Since a special measuring device and flow path switching valve are not required, the manufacturing process is carried out using a simple facility. The organic substance can be modified at a lower temperature. The emission of carbon dioxide is reduced, by utilizing the carbon dioxide for the modification of the organic substance.    DESCRIPTION OF DRAWING(S) - The drawing shows the explanatory view of the hydrogen manufacturing equipment. (Drawing includes non-English language text)    Exhaust gas (AA)    Water vapor (BB)    Mixed gas (CC)    Water (DD)    Hydrogen-rich mixed gas (EE)
NOVELTY - The furnace has a furnace body (1) provided with a double-layer water jacket (2), and a gasification chamber (3) provided with a vertical gas pipe. A fuel gas pipe (10) is connected to a combustion chamber, and the gasification chamber is provided with a wind cover (18). A blast pipe (13) is provided with a control valve (12) whose lower section is equipped with another control valve (15). The blast pipe at a lower end of a governing part (16) is connected with the gasification chamber of the wind cover.    USE - Double-control straw gasification furnace.    ADVANTAGE - The furnace has stable and full combustion condition, no air flow loss, simple structure and low cost, and is convenient, safe and reliable to operate.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross sectional view of a double-control straw gasification furnace.    Furnace body (1)    Double-layer water jacket (2)    Gasification chamber (3)    Fuel gas pipe (10)    Control valves (12, 15)    Blast pipe (13)    Governing part (16)    Wind cover (18)
NOVELTY - Preparation of biochemical fertilizer comprises culturing strain by taking Bacillus subtilis natto, culturing for 6-8 hours to obtain seed liquid, preparing fermentation material by taking livestock excrement, garbage, leaves, crop straw, weed, nitrogenous fertilizer, phosphate fertilizer and potash fertilizer at mass ratio of 40-50:0-7:7-12:8-15:3-5:10-12:8-10:4-7, fermenting cultivated seed liquid, mixing uniformly, culturing for 30-37 days at 50-60 degrees C and reducing temperature to 35-45 degrees C.    USE - Preparation of biochemical fertilizer (claimed).    ADVANTAGE - The method reduces cost of fertilizer, nourishes organic substance in soil and protects ecological environment.
NOVELTY - Producing biodiesel oil comprises reacting water, pectin, protein, waste animal and vegetable oil into a reactor and then adding sulfuric acid, sodium and methanol, raising the temperature of the mixture and then stirring, heating and increasing the temperature of stirred mixture and then recycling methanol, adding methanol with the heated mixture and then reacting, and standing the reacted mixture and then discharging lower layer of vitriol, sodium bisulfate and glycerol, centrifugally separating upper layer material and then remaining liquid into the distillation tower.    USE - The method is useful for producing biodiesel oil (claimed).    ADVANTAGE - The method produces the biodiesel oil in a convenient manner with low acid value.    DETAILED DESCRIPTION - Producing biodiesel oil comprises: (a) introducing water, pectin, protein, waste animal and vegetable oil into a reactor to remove impurities and then adding 1-1.2 mass% of sulfuric acid, 1.5-2.2 mass% of sodium and 8-10 mass% of methanol, where the methanol content is more than 85%, raising the temperature of the mixture at 65-70 degrees C for 1 hour and then stirring; (b) continuously heating and increasing the temperature of stirred mixture at 105-115 degrees C and then recycling methanol, adding 15-20 mass% of methanol (more than 98%) with the heated mixture and then reacting for 6-7 hours, and standing the reacted mixture for 0.8-2 hours and then discharging lower layer of vitriol, sodium bisulfate and glycerol to obtain upper layer material; and (c) centrifugally separating the 7-9 mass% of upper layer material using sodium carbonate aqueous solution and then separating out water and soap and passing remaining liquid into a distillation tower, where the biodiesel product has light fraction of diesel oil and heavy fraction of plant asphalt.
NOVELTY - Control of poultry farming pollution comprises separating dry excrement, sewage source, water and rainwater, carrying out sludge treatment by performing solid-liquid separation, conveying into liquid biological fermentation reactor to process, separating carbon-containing material using solid aerobic fermenting device, aging, sewage processing, biologically deodorizing and discharging.    USE - Control of poultry farming pollution.    ADVANTAGE - The method realizes resource-saving and environment-friendly treatment of waste.
NOVELTY - Vacuum dehydration device has vacuum chamber (2), vacuum tank (3), dehydration tank (4) and vacuum pump (5) sequentially connected through air pipes, where one end of the vacuum chamber is connected with a double-shaft stirring granulation machine (1) and the other end is connected with a spiral extruder (6).    USE - Vacuum dehydration device for biotic organic fertilizer granulating machine (claimed).    ADVANTAGE - The device is excellent in pumping out water present in biotic organic fertilizer by adoption of vacuum pressure, before granulation and thus makes the fertilizer suitable for granulation.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of vacuum dehydration device.    Double-shaft stirring granulation machine (1)    Vacuum chamber (2)    Vacuum tank (3)    Dehydration tank (4)    Vacuum pump (5)    Spiral extruder (6)
NOVELTY - Preparing fertilizer involves mixing starch, potassium nitrate, monopotassium phosphate, magnesium, agar and water, sterilizing mixture, inoculating Actinomycete, allowing the inoculate to stand and eluting to obtain eluate, soaking rice and water, sterilizing the soaked mixture, inoculating the eluted liquid, shaking the inoculated culture to obtain broth, mixing manure, wheat bran and calcium carbonate to obtain fermentation raw material, adjusting water content, carrying out sterilization process, inoculating bacterial spores and fermenting product.    USE - The method is useful for preparing fertilizer (claimed).    ADVANTAGE - The method replaces artificially synthesized culture medium by waste-biogas residues and biogas slurry (to be used as fermentation substrate), and hence cost for culturing Actinomyces is reduced.    DETAILED DESCRIPTION - Method for preparing fertilizer, involves uniformly mixing 2-2.5 pts. wt. starch, 0.1-0.2 pts. wt. potassium nitrate, 0.03-0.05 pts. wt. monopotassium phosphate, 0.001-0.002 pts. wt. magnesium, 2-2.2 pts. wt. agar and 95-96 pts. wt. water, sterilizing the mixture, inoculating Actinomycetes in the sterilized mixture at 28-32 degrees C, allowing the inoculate to stand for 48-96 hours and eluting with 1 ml sterile water to obtain eluate, soaking rice and water in the mass ratio of 1:12 for 20-24 hours, sterilizing the soaked mixture, inoculating the eluted liquid in the culture medium at 28-32 degrees C, shaking the inoculated culture for 72-120 hours to obtain broth, uniformly mixing 70-90 pts. wt. manure, 10-30 pts. wt. wheat bran and 0.5-2 pts. wt. calcium carbonate to obtain fermentation raw material, adjusting water content to 40-45%, carrying out sterilization process, inoculating 0.5-5% bacterial spores with the sterilized mixture, fermenting the mixture at 28-32 degrees C for 70-96 hours, and continuing the fermentation process, where the mixture containing raw material has thickness of 10-20 cm.
NOVELTY - Preparation of bio-organic fertilizer comprises taking 100-150 pts. wt. hickory nut cattail, 40-50 pts. wt. poultry manure, 20-30 pts. wt. bagasse, 20-30 pts. wt. mineral slag soil, 15-20 pts. wt. humic acid, and 0.1-0.2 pts. wt. fermenting agent; crushing hickory nuts, fully mixing with other raw materials; fermenting for 30-50 days while turning every 5-10 days; reducing temperature from 60-70 degrees C to 20-30 degrees C; standing and stacking for 10-20 days; adding fermented material with 10-15% biological composite bacterial liquid; and granulating to obtain bio-organic fertilizer.    USE - Preparation of bio-organic fertilizer.    ADVANTAGE - The method is resistant to insect pests, improves soil aggregate structure, and improves crop quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for coating of bio-organic fertilizer by weighing bio-organic fertilizer equivalent to 8-10 wt.% of sepiolite; soaking sepiolite into 10-15% hydrochloric acid for 3-4 hours; washing with deionized water; soaking in 10-12% sodium hydroxide solution for 3-4 hours; washing with deionized water until neutral; calcining at 500-530 degrees C for 4-5 hours; crushing into powder; adding sepiolite with 5-6 times water, then adding sepiolite with 3-3% sodium lauryl sulfate, 1-2% Peregal 0 (RTM: Fatty alcohol-polyoxyethylene ether), 4-5% wintergreen, and 3-5% aluminum hydroxide; high speed mixing for 1200-1500 revolutions per minute to obtain dispersion liquid; spraying dispersion liquid to bio-organic fertilizer particle; drying; re-spraying fertilizer particle with pyrethroid ester mixture; and optionally drying.
NOVELTY - Organic fertilizer comprises 65-75 %mass chicken, 20-30 %mass mushroom residue, 1-2 %mass biological agents and 3-5 %mass deodorant.    USE - The organic fertilizer is useful for resisting disease in plants.    ADVANTAGE - The method is simple in flow, and easy to operate, has short in production period (composting can be finished in 15-20 days), low environmental pollution, as it fully utilizes the raw materials, and low cost and provides organic fertilizer with high additional value. The environmental pollutants caused by bioorganic fertilizer are converted into fertilizer substances required by agricultural production, so that waste is changed into valuable. The viable count of the bioorganic fertilizer is extremely high, so the hardened soil can be effectively improved and repaired.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the organic fertilizer, which involves mixing 1-2 %mass biological agents with 500-1000 times water to form concentrated broth, maintaining the product in room temperature for 8-10 hours, adding 65-75 %mass chicken manure and 20-30 %mushroom residue, crushing the product to 50-80 mesh granule using crusher, preparing material layer having thickness of 15-20 cm using crushed product, spraying the concentrated broth on material layer, adding 3-5 %mass deodorant to material layer, adjusting water content of material layer to 50-60%, forming the material layer into piles in the fermentation tank, where the pile has 1-1.2 m height, 3-4 m lower width, and width 1-1.5 m, initially fermenting the product for 7-10 days, compositing the piles for 17-20 days, fermenting the finished product for 18-20 days during which temperature is checked for every 6 hours, heating the product, until the temperature exceeds more than 65 degrees C, spray cooling the product, drying, extruding and granulating the product, packaging the product and qualifying the packed product.
NOVELTY - Production of allantoin involves adding glyoxylic acid aqueous solution, urea and catalyst to the reactor, stirring, heating to react for 6.5-24 hours, cooling reaction mixture to room temperature, filtering, washing, filtering and drying. The catalyst is mixture of bisulfate and sulfuric acid, mixture of hydrogen phosphates salt and phosphoric acid, or hydrophosphate.    USE - Production of allantoin (claimed).    ADVANTAGE - The allantoin is efficiently produced with improved yield without polluting the environment.
NOVELTY - A porous solid alkali catalyst comprises dolomite as raw material and 3-11C fatty acid as template agent. The mass ratio of fatty acid to dolomite is 1:1-1:10. Catalyst is prepared by mixing above materials with water solvent at 25-100 degrees C 0.5-3 hours, transferring to crucible at 550-850 degrees C and heating for 1-10 hours, cooling, grinding and preparing with mesoporous, and preparing desired catalyst.    USE - Porous solid alkali catalyst used for catalyzing plant oil to carry out ester exchange reaction for preparing biodiesel.    ADVANTAGE - The catalyst has high catalytic performance and improves wear resistance of catalytic-efficiency for more than 20%.
NOVELTY - Synthesis of docetaxel comprises reacting (2R,3S)-3-phenylisoserine methyl ester and bromoacetaldehyde catalyst to generate intermediate 2, processing ester hydrolysis with intermediate 2 to obtain side chain prepared docetaxel 3, condensing, ring-opening and side chain amino protecting, and hydrolyzing; reacting in the presence of organic alkali and trichloroacetyl chloride, condensing, side-chain amino protecting, reacting with C-13 oxazole ring-opening side chain, reacting to obtain side-chain amino protection and di-tert-butyl dicarbonate under alkali of intermediate 8, and hydrolyzing.    USE - Method for synthesizing docetaxel (claimed).    ADVANTAGE - The method has simple synthesis steps, less side reaction, high yield and no isomer by-product, low impurity content, high yield and high purity, and low cost.    DETAILED DESCRIPTION - Synthesis of docetaxel comprises reacting (2R,3S)-3-phenylisoserine methyl ester and bromoacetaldehyde catalyst to generate intermediate 2, processing ester hydrolysis with intermediate 2 to obtain side chain prepared docetaxel 3, condensing, ring-opening and side chain amino protecting, and hydrolyzing; reacting in the presence of organic alkali and trichloroacetyl chloride, condensing with condensing agent and alkali, side-chain amino protecting, reacting with C-13 oxazole ring-opening side chain to obtain intermediate 7, reacting to obtain side-chain amino protection and di-tert-butyl dicarbonate under alkali of intermediate 8, and hydrolyzing intermediate 8 with ammonia, ammonium hydroxide, ammonium acetate and ammonium chlorideto remove 7-OH and 10-OH protecting group to obtain docetaxel under acidic condition.
NOVELTY - Airflow type large rapid straw carbonization constant pressure reaction furnace comprises a heating hearth and exhaust fans with maximum exhaust air rate of 25000 m3/hour arranged on the top of the furnace. Humidity is an important factor of furnace for affecting dehydration in order to accelerate the humidity-discharging and to accelerate straw dehydrating speed, and simultaneously to provide greater power to heating hearth hot air to enter the carbonization furnace. The total exhaust air rate reaches to 15000 m3/hour. The exhaust fan is able to discharge 42 m3/second hot humid air.    USE - Used as an airflow type large rapid straw carbonization constant pressure reaction furnace.    ADVANTAGE - The furnace saves energy, achieves large scale industrial straw charcoal production with its large capacity and large tonnage rapid speed, adopts an airflow type heating dehydration working principle, an airflow type cooling working principle and a carbonization stage working principle; ensures rapid dehydration and carbonization period, and is capable of producing 150 tons of straw carbonized finished product with volume of 1100 m3 for every 2 hours.
NOVELTY - Aqueous fertilizer preparation comprises 80-92 wt.% rotten chicken manure, 3-10 wt.% calcium superphosphate, 1-5 wt.% potassium dihydrogen phosphate, 0.5-5 wt.% calcium carbonate, 0.02-0.35 wt.% zinc sulfate, 0.04-0.7 wt.% manganese sulfate, 0.1-0.6 wt.% copper sulfate, 0.5-1 wt.% magnesium sulfate, 0.5-1 wt.% magnesium chloride, 0.1-0.7 wt.% ferrous sulfate heptahydrate, 0.02-0.2 wt.% ammonium citrate, and 0.02-0.35 wt.% citric acid.    USE - The aqueous fertilizer preparation is used for culturing purple pearl (claimed).    ADVANTAGE - The fertilizer is mixed with the phytoplankton and zooplankton necessary for nitrogen-phosphorus-potassium (N-P-K) and trace element to prepare organic fertilizer; and can provide sufficient organic nutrient, N-P-K and trace elements for culturing purple pearl.
NOVELTY - A watercress culture fertilizer is prepared by combining (wt.%) dry rabbit manure (6-10), dry duck manure (24-28), dry human excrement (22-26), bagasse (4-6), mung bean straw powder (2-6), pine needle powder (3-5), Coptis powder (4-6), ginger powder (2-6), wild anise powder (4-8), pepper leaf powder (2-4), mulberry powder (1-3), Asiatic moonseed rhizome powder (1-3), and bellflower powder (4-6).    USE - Method of preparing watercress culture fertilizer (claimed).    ADVANTAGE - The method has low cost, utilizes easy to obtain materials, is simple in steps, and can obtain fertilizer which can improve quality of grown watercress and can provide watercress with disease resistance, fresh taste, and rich nutrients including carbohydrate and vitamin C and coarse fiber.
NOVELTY - Method for producing vitamin E containing bio-oil, involves preparing and processing citrus pericarp material, subjecting prepared citrus pericarp material to thermal decomposition by vapor-phase pyrolysis, and condensing product obtained by vapor-phase pyrolysis.    USE - The method is useful for producing vitamin E containing bio-oil chosen from formaldehyde, acetaldehyde, methanol, acetone, 2,3-butanedione, 2-butanone, 2-methylfuran, glycolaldehyde, acetic acid, hydroxyacetone, pyruvic acid methyl ester, furfural, 2-hydroxycyclopent-2-en-1-one, phenol, limonene, 3-methyl-1,2-cyclopentanedione, 2,5-dimethyl-4-hydroxy-3(2H)-furanone, 3,5-dihydroxy-6-methyl-2,3-dihydro-4H-pyran-4-one, 5-hydrxoymethylfurfural, 2-methoxy-4-vinylphenol, ethyl- alpha -d-glucopyranoside, and n-hexadecanoic acid (all claimed).    ADVANTAGE - The method enables production of the vitamin E containing bio-oil with high yield of 35% or more.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for vitamin E containing bio-oil produced by the above-mentioned method.
NOVELTY - Invention relates to cleaning and separation of helium-bearing fuel gases including natural and associated oil gases. Proposed method comprises creating the flow of dried green gas cleaned of carbon dioxide and sulfuric compounds, cryogenic processing with removal and derivation of methane product fractions and heavy hydrocarbon fractions, and processing aimed at helium extraction and helium concentrate flow production. Processing with extraction of helium till cryogenic processing is carried out by diaphragm gas separation with feed of compressed green gas to high-pressure inlet of the primary diaphragm gas separation unit and forcing of said green gas along diaphragm helium-permeable surface. Gas flow penetrated through diaphragm is discharged as low-pressure helium concentrate while high-pressure gas not penetrated the diaphragm is fed to cryogenic processing.    USE - Process engineering.    ADVANTAGE - Lower costs, higher yield, simplified process.7 cl, 3 dwg
NOVELTY - Invention relates to agriculture. The method of obtaining liquid mineral fertiliser based on industrial waste water from production of nitrogen-phosphorus-potassium fertilisers (NPK), which is characterised by that the industrial waste water is analysed and its composition is determined; the amount of substances ZnSO4.7H2O; MnSO4.7H2O; H3BO3; CuSO4.5H2O; (NH4)2MoO4; FeSO4.7H2O; Ca(H2PO4)2; MgCl2; KNO3 is determined, wherein when preparing the solution of the liquid mineral fertiliser, the substances are weighed, each is separately dissolved in a small amount of waste water; 200-300 ml of waste water is then poured into a 1 litre vessel and the prepared solutions are added successively while stirring; further, more waste water is added until obtaining a volume of 1 litre and then packaged; pH of the obtained liquid mineral fertiliser is in the range of 5.5-6; when watering plants, 50 ml of the fertiliser is dissolved in 1 litre of water.    USE - Chemistry.    ADVANTAGE - Invention ensures wasteless production, enables to recycle waste water, obtain liquid mineral fertiliser therefrom and use said fertiliser to grow plants in open and closed fields, as well as using hydroponic and ionitoponic methods.2 tbl, 3 ex
NOVELTY - Apparatus comprises: a mix tank (12) for mixing cellulosic material with a solvent into a slurry; a generator (14) having an exhaust; a stir tank reactor (18) for converting the slurry to a solution containing lignin-like carbon and liquid; a separator (31) for separating the lignin-like carbon and liquid; an anaerobic digester for decomposing liquid received from the stir tank into methane and liquid components; and a carbon dioxide scrubber (28) for scrubbing the methane component of carbon dioxide.    USE - The apparatus is useful for producing methane gas (claimed), synthetic hydrocarbon gas (for electrical generation, or separated and used or stored as separate products), synthetic petroleum, fertilizer, and high value solid carbon.    ADVANTAGE - The apparatus: provides synthetic hydrocarbon gas that has high British thermal unit content and rich in hydrocarbons; provides low molecular weight hydrocarbons (propane and butane); and utilizing cellulosic material results in a boiler fuel with higher volatile composition, which leads to decrease in the synthetic petroleum and gas products.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing methane gas from cellulosic material comprising: mixing cellulosic material with a solvent into slurry; converting the slurry to a solution containing lignin-like carbon and liquid; separating the lignin-like carbon and liquid; decomposing the liquid into methane and liquid components; and scrubbing the methane component of carbon dioxide.    DESCRIPTION OF DRAWING(S) - The figure shows a flow chart of the methane gas, synthetic hydrocarbon gas, synthetic petroleum and, high value carbon using apparatus.    Mix tank (12)    Generator (14)    Stir tank reactor (18)    Carbon dioxide scrubber (28)    Separator (31)
NOVELTY - Making a fuel or fuel additive comprises producing isobutanol from unpurified mixtures of carbon substrates from renewable feedstocks during fermentative growth of yeast comprising an engineered biosynthetic isobutanol pathway, where the fermentative growth occurs under anaerobic or microaerobic conditions with mineral supplementation.    USE - The method is us used for making a fuel or fuel additive (claimed).    ADVANTAGE - An environmentally responsible, cost-effective process for the production of isobutanol as a single product is provided.    DETAILED DESCRIPTION - Making a fuel or fuel additive comprises producing isobutanol from unpurified mixtures of carbon substrates from renewable feedstocks during fermentative growth of yeast comprising an engineered biosynthetic isobutanol pathway, where the engineered biosynthetic pathway comprises (i) an acetolactate synthase (ALS) enzyme having a defined sequence of 571 amino acids (SEQ ID NO: 178), given in the specification, and (ii) a heterologous branched chain keto acid decarboxylase with decreased affinity for pyruvate compared to native pyruvate decarboxylase, and where the fermentative growth occurs under anaerobic or microaerobic conditions with mineral supplementation.
NOVELTY - The circuit (1) has a synchronization circuit (10) generating a synchronization signal (Sv1), where the circuit is operated in a normal operation mode. The synchronization circuit generates the synchronization signal dependent on an external voltage (V1) in the normal operation mode. A converter unit of a set of converter units (2-1-2-n) receives the synchronization signal and to regulate a generation of an output current (i1-1-i1-n) such that a frequency and a phase of the output current is dependent on the synchronization signal in the normal operation mode.    USE - Power circuit for converting direct current (DC) input voltage generated by photovoltaic cell i.e. fuel cell (claimed), into analog current (AC) output voltage to be supply to AC national power grid.    ADVANTAGE - The circuit is efficiently transforming relatively low DC supply voltages into the AC supply voltage that is consistent with a power grid voltage in an effective manner. The circuit allows an operation mode controller to measure the output power provided by the circuit to the power grid and adjusts the phase difference between the output current out and the external AC voltage dependent on the output power, so that the phase difference increases so as to increase the reactive power provided to the circuit when the output power provided by the circuit increases.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a power supply system comprising output terminal    (2) a method for operating a power converter circuit.    DESCRIPTION OF DRAWING(S) - The drawing shows a circuit diagram of a power converter circuit including a set of DC/AC converter units connected in series and a voltage measurement circuit.    Synchronization signal (Sv1)    External voltage (V1)    Output current (i1-1-i1-n)    Power converter circuit (1)    Converter units (2-1-2-n)    Synchronization circuit (10)
NOVELTY - Earthwork material contains fly ash (A) containing elution amount of fluorine, boron, arsenic and selenium which exceeds soil environmental standard, calcium aluminate (B), aluminum sulfate (C), lime (D) and alkali-metal phosphate (E).    USE - Earthwork material is used for backfill material, road surfacing material admixture for concrete product, banking material and soil improvement material.    ADVANTAGE - Since the elution amount of fluorine which is toxic substance contained in fly ash or paper sludge ash is reduced below tow soil environmental standard, the environment safety of earthwork material is high. The earthwork material has excellent elution inhibitory effect for long period of time.
NOVELTY - A carbon-carbon bond-type heavy fluorous alcohol (I), is new.    USE - New carbon-carbon bond-type heavy fluorous alcohol. Uses include but are not limited to manufacture of pharmaceutical, food additive and cosmetics, liquid crystal, electronic material, polymeric-material monomer, functional material, medical material, peptide, carbohydrate, nucleic acid, and organic synthesis e.g. oxidation reaction, reductive reaction and radical reaction.    ADVANTAGE - The carbon-carbon bond-type heavy fluorous alcohol has excellent chemical stability and recyclability, and is manufactured environmentally-friendly by economical process. Since, the carbon-carbon bond-type heavy fluorous alcohol has methylene group(s) adjacent to the functional group and the steric hindrance of three fluorous chain is reduced, various linkers required for the organic synthesis can be introduce easily.    DETAILED DESCRIPTION - A carbon-carbon bond-type heavy fluorous alcohol of formula: Z-(CH2)n-Y'-C(-Y'-Rf)3 (I), is new.    Rf=1C or more perfluoro organic group;    Y'=hydrocarbyl;    Z=functional group;and    n=1 or more.    INDEPENDENT CLAIMS are included for the following:    (1) compound (a), which is derived from the carbon-carbon bond-type heavy fluorous alcohol; and    (2) method to extract a compound in the fluorous solvent, which involves using the compound (a).
NOVELTY - A microorganism comprising first nucleic acid sequence encoding polyketide synthase gene i.e. sarcoglycan epsilon (sgcE) or its functional equivalent, is new.    USE - The microorganism is useful in system for producing hydrocarbon compound, preferably olefin or alkane compound more preferably pentadecane which is used as biofuel. The system (S1) is useful for converting microorganism to obtain recombinant microorganism. The system (S2) is useful for preparing biofuel (all claimed). The method (M2) is useful for preparing fat alkane and intermediate alkenes.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) system (S1) for converting the above-mentioned microorganism;    (2) method (M1) for recombination of microorganism, involves converting the above-mentioned microorganism using the above-mentioned system to obtain recombinant microorganism;    (3) method (M2) for producing hydrocarbon compound, involves cultivating the above-mentioned microorganism and separating the hydrocarbon compound;    (4) hydrocarbon compound prepared by the above-mentioned method (M2); and    (5) system (S2) comprising a biological reactor filled with the above-mentioned microorganism for producing the hydrocarbon compound.
NOVELTY - Method for preparing ethanol, involves making pressurized hot water to act on biomass, and hence hemicellulose contained in the biomass is selectively degraded, making solid acid catalyst to act on the degraded product at 90-110 degrees C to obtain saccharified product containing xylose, and making microorganisms to act on the resulting saccharified product, where the microorganisms have the ability to ferment xylose.    USE - The method and apparatus are useful for preparing ethanol (all claimed).    ADVANTAGE - The method saccharifies and ferment hemicellulose contained in woody materials and produce ethanol.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus for preparing ethanol, which has pressurized hot water reaction apparatus for performing pressurized hot water reaction, catalytic reaction apparatus for heating decomposed product, and fermentation apparatus for making microorganisms to act on saccharified product.
NOVELTY - Fertilizer material comprises: a first fertilizer product including an ammoniacal fertilizer comprising ammoniacal nitrogen-containing fertilizer and a partial calcium salt of a first copolymer comprising maleic and itaconic monomers, where the partial calcium salt is mixed with the ammoniacal fertilizer as an aqueous liquid product and has a pH of 1-3.5; and a second fertilizer product including a phosphorus fertilizer and a partial sodium salt of a second copolymer comprising maleic and itaconic monomers.    USE - The fertilizer material is useful for fertilizing a crop (claimed) such as corn, wheat, oats, barley, sorghum, milo, rice, cotton, soybean, and alfalfa, and other forage crops. No biological data given.    ADVANTAGE - The fertilizer material improves the crops yield, and has synergistic effect.    DETAILED DESCRIPTION - Fertilizer material comprises: a first fertilizer product including an ammoniacal fertilizer comprising ammoniacal nitrogen-containing fertilizer and a partial calcium salt of a first copolymer comprising maleic and itaconic monomers, where the partial calcium salt is mixed with the ammoniacal fertilizer as an aqueous liquid product and has a pH of 1-3.5; and a second fertilizer product including a phosphorus fertilizer and a partial sodium salt of a second copolymer comprising maleic and itaconic monomers, where the partial sodium salt is mixed with the phosphorus fertilizer as an aqueous liquid product and has a pH of 5-10, and first and second fertilizer products are present in synergistically effective amounts, such that the coordinated amounts of the first and second fertilizer products give crop yields greater than a mere additive effect obtained through the use of the respective first and second fertilizer products alone in the same amounts. An INDEPENDENT CLAIM is included for fertilizing a crop, comprising applying the fertilizer material onto soil in which the crop grows.
NOVELTY - Preparing a compound (T) comprising a carbamate or urea compound (I) or an aryl amine compound (II) comprises (a) providing a hydroxamic acid compound (Q) and (b) reacting (Q) with an organic carbonate of formula (V) in the presence of a tertiary amine.    USE - The carbamates are useful for preparing insecticides, fungicides, herbicides or sleeping pills; as protecting groups n organic synthesis of amines (e.g. in the synthesizing peptides) and as intermediates in organic synthesis; and in oleochemicals. No biological data given.    ADVANTAGE - The process: provides (Q), preferably carbamates in high yield, under mild reaction conditions and without using toxic substances such as bromine and sodium hydroxide, hence ecofriendly and the formation of by-products.    DETAILED DESCRIPTION - Preparing a compound (T) comprising a carbamate or urea compound of formula (R1-NH-CO-Nu1) (I) or an aryl amine compound of general (R3-NH2) (II) comprises (a) providing a hydroxamic acid compound (Q) of formula (R1-CO-NH-OH) (III) or (R3-CO-NH-OH) (IV) and (b) reacting (Q) with an organic carbonate of formula (R2 O-CO-OR2) (V) in the presence of a tertiary amine.    Nu1 = alkoxy group of formula OR2 or an alkyl amine group of formula NHR1;    R1 = optionally substituted, linear, branched or cyclic 1-50C-alkyl, alkenyl or allyl;    R2 = optionally substituted, linear, branched or cyclic 1-50C-alkyl (preferably CH3), allyl, 6-50C-aryl or 4-50C-heteroaryl; and    R3 = 6-50C-aryl or 4-50C-heteroaryl.
NOVELTY - The apparatus generates methane containing gas which supplies hydrogen to source gas containing carbon dioxide. The remainder of hydrogen is supplied to reaction mixed gas by reactor (R1). The reaction temperature of reactor is adjusted by adjusting hydrogen supply amount to the reactor including second reactor (R2) which adjusts amount of hydrogen required for reaction, and the multi-tubular-type reactor (R3) which adjusts composition of generated gas which comes from second reactor.    USE - Methanation reaction apparatus for changing carbon dioxide into methane.    ADVANTAGE - Since the reactors which adjust reaction temperature, the amount of hydrogen required for reaction, and the composition of generated gas respectively, the conditions of reactor can be adjusted flexibly. The temperature rise of the catalyst layer in reactor can be suppressed in permissible range by adjusting the reaction temperature of reactor.    DETAILED DESCRIPTION - The apparatus has reactor whose reaction temperature is adjusted by supplying water vapor to reactor. The composition of generated gas in multi-tubular-type reactor is adjusted with adjustment of the temperature or pressure in the reactor. The catalyst layer in reactor is diluted by mixing of catalyst particles and a ceramic ball.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the methanation reaction apparatus. (Drawing includes non-English language text)    Adsorption tower (A)    Tank (B1)    Reactors (R1,R2,R3)    Thermometer (T1)    Regulating valve (V1)
NOVELTY - Biomass saccharification method, involves (a) performing first enzymatic-reaction by decomposing biomass processed material containing cellulose and lignin using saccharogenic amylase, decomposing the cellulose into water-soluble sugar content, subjecting the obtained processed material to solid-liquid-separation process, and separating solid portion and liquid containing water-soluble sugar, and (b) performing second enzymatic-reaction by decomposing the obtained solid portion to decompose remaining water-soluble cellulose in the solid portion.    USE - The biomass saccharification method is useful for producing ethanol (bioethanol) which is used as fuel.    ADVANTAGE - The method is cost-effective and consumes less time.
NOVELTY - Optimizing energy by recovering energy component and nutrients from the biomass crop comprises recovering one part of energy in the form of biogas; and further filtering digestate obtained after biomethanation process by appropriate filtration method to produce solid residue and liquid filtrate.    USE - The process is useful for optimizing energy by recovering the energy component and nutrients from the biomass crop (claimed).    ADVANTAGE - The process reduces the retention time and brings down the capital cost of the plant without sacrificing the energy contained in the organic matter of the biomass (claimed). It transforms biomass and biomass products into optimum energy; involves an additional recovery of energy and nutrients from the digestate obtained after biomethanation process; and acts as a substitute for fuel, preferably a substitute for coal. The process is a cost effective method of increasing the total energy content from energy crops.
NOVELTY - The module has a freeze control domain arranged on a cooling module for ejecting methane. An expansion valve is mounted between a separation unit (100) and a cooling module. Sour gas is generated in a stranded gas well (900) that is provided with a separation unit. A flash chamber (300) is connected with the separation unit to separate carbon dioxide according to gas and liquid. The flash chamber is connected with a flow control valve (320) to control supply quantity of the carbon dioxide. A pressure control valve (340) is mounted on a gas out-flux pipe for discharging gas carbon dioxide.    USE - Carbon dioxide processing module for a vessel.    ADVANTAGE - The module enables controlling sour gas produced from limit gas well and easily processing liquid carbon dioxide. The module reduces construction cost of a processing facility and drastically reduces amount of gas carbon dioxide ejected to an airborne. The module has low installation cost, and is environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a carbon dioxide processing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a carbon dioxide processing module.    Separation unit (100)    Flash chamber (300)    Flow control valve (320)    Pressure control valve (340)    Stranded gas well (900)
NOVELTY - Preparing (M1) tetrahydrofuran-2,5-dimethanol (TDM) involves contacting isosorbide with hydrogen in the presence of a first hydrogenation catalyst at a first temperature of 150-400 degrees C and at a first pressure of 500-5000 psi to form a first product mixture comprising TDM.    USE - For preparing tetrahydrofuran-2,5-dimethanol (TDM), useful precursors in the synthesis of industrially useful chemicals such as pharmaceuticals, herbicides, stabilizers, and polymers; useful in adhesives, sealants, coatings, solvents, resins, and polymer materials; also as an intermediate in the synthesis of 1,6-hexanediol used in the production of polyesters for polyurethane elastomers, coatings, adhesives and polymeric plasticizers.    ADVANTAGE - The method produces tetrahydrofuran-2,5-dimethanol and 1,6-hexanediol from biomass-derived starting materials, such as isosorbide which in turn can be derived from a renewable biosource.
NOVELTY - 2,6-Dihalo-5-alkoxy-4-substituted-pyrimidine compound or 2,6-dihalo-5-alkoxy-4-pyrimdine carbaldehyde compound is new.    USE - For preparation of 2,6-dihalo-5-alkoxy-pyrimidine-4-carboxylic acid and herbicide (claimed) for broad spectrum of weed control.    ADVANTAGE - The compound prepares herbicide that has superior herbicides activity with broad spectrum of weed control against broadleaf weeds as well as grass and sedge weeds and with excellent crop selectivity at low use rates, and possesses excellent toxicological or environmental profiles.    DETAILED DESCRIPTION - 2,6-Dihalo-5-alkoxy-4-substituted-pyrimidine compound of formula (I) or 2,6-dihalo-5-alkoxy-4-pyrimdine carbaldehyde compound of formula (II) is new.    X1=halogen;    R1=hydrocarbon chain;and    Q=1-2C alkoxy.    INDEPENDENT CLAIMS are included for the following:    (1) preparation of compound (I) and (II);    (2) preparation (M1) of herbicide by using 2,6-dihalo-5-alkoxy-4-substituted pyrimidine compound (I) comprising a pyrimidine ring having hydrocarbon chain at the 4 position and halogen at the 6 position, involving contacting the hydrocarbon chain at the 4 position with an oxidant to form a carbonyl group at the 4 position; contacting the carbonyl group at the 4 position with bromine in an alcohol to form a carboalkoxy group at the 4 position; and contacting the halogen at the 6 position with an amine to form an amino group at the 6 position; and    (3) preparing 2,6-dihalo-5-alkoxy-pyrimidine-4-carboxylic acid by using 2,6-dihalo-5-alkoxy-4-substituted pyrimidine (I), contacting 2,6-dihalo-5-alkoxy-4-substituted pyrimidine comprising pyrimidine ring comprising hydrocarbon chain at the 4 position with oxidant to form 2,6-dihalo-5-alkoxy-pyrimidine-4-carboxylic acid having carboxyl group at the 4 position.
NOVELTY - The method involves combining liquid water with an organic compound to produce a wet form of the compound and transferring the wet form of the compound into a reaction processing chamber (102). The wet form of the compound is heated within the reaction chamber such that elements comprising the wet form of the compound dissociate and react to obtain reaction product that comprises hydrogen gas. The hydrogen gas is processed to generate electrical power or heat. Inert gas is introduced into the chamber, where the inert gas comprises argon or nitrogen.    USE - Method for generating electrical power from an organic compound such as carbon, oxygen, hydrogen, cellulose and lignin (all claimed), by processing hydrogen gas using a fuel cell. Can also be used for generating electrical power from organic compound by processing liquid fuel such as methanol, natural gas and gasoline.    ADVANTAGE - The method enables converting cellulose into hydrogen for power generation to reduce production of carbon dioxide generation, thus avoiding global warming issue, hence enhancing recycling of cellulose products and turn cellulose waste into power generation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a system for conversion of organic compounds into hydrogen.    Reaction processing chamber (102)    Water supply line (106)    Controller (112)    Gas supply line (114)    Exhaust line (118)
NOVELTY - Producing ethanol comprises: hydrogenating acetic acid from an acetic acid feed stream in a reactor to form a crude ethanol product comprising ethanol, ethyl acetate, acetic acid and water; separating at least a portion of the crude ethanol product in a first column at a first pressure into a first distillate comprising ethanol, ethyl acetate, and low concentration of water, and a first residue comprising acetic acid and water; and separating at least a portion of the first distillate in a second column at a second pressure to yield an ethanol product stream and an ethyl acetate stream.    USE - The process is useful for producing ethanol (claimed), which is useful as fuels (including gasoline for motor vehicles such as automobiles, boats and small piston engine aircraft), solvents (for toiletry and cosmetic preparations, detergents, disinfectants, coatings, inks, and pharmaceuticals), chemical feedstocks (to make other chemicals such as vinegar, ethyl acrylate, ethyl acetate, ethylene, glycol ethers, ethylamines, aldehydes, and higher alcohols, especially butanol), pharmaceutical products, cleansers, sanitizers, and hydrogenation transport.    ADVANTAGE - The process provides anhydrous form of ethanol in an economical manner.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a process for producing ethanol.    System (100)    Reaction zone (101)    Separation zone (102)    Reactor (103)    Hydrogen feed lime. (104)
NOVELTY - The master controller (120) has a pre-processing module (122) which determines a prediction length by dividing a predefined prediction horizon by a predefined time interval. An operating power determinator of an optimization module (124) produces an operating power value for the electrolyzer. A post-processing module (126) determines whether to send to the electrolyzer instructions including a start command, a stop command, or the optimized operating power value produced by the operating power determinator.    USE - Master controller of power system (claimed), used for selectively activating electrolyzer for producing hydrogen gas from source material using electricity.    ADVANTAGE - Since the post-processing module utilizes the results from the pre-processing and optimization modules to assemble instructions to control the electrolyzer, the optimization of the power system can be performed in real time. The operating power value of the electrolyzer can be determined by considering the electrolyzer operating constraints, without the use of non-linear programming.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a computer program product for enabling optimization of power system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the power system.    Electrolyzer (110)    Master controller (120)    Pre-processing module (122)    Optimization module (124)    Post-processing module (126)
NOVELTY - Reforming method of heavy hydrocarbon distillate involves treating heavy hydrocarbon distillate and lignocellulosic biomass using solvent.    USE - Reforming method of heavy hydrocarbon distillate (claimed).    ADVANTAGE - The method efficiently reforms heavy hydrocarbon distillate with high production efficiency, and excellent dissolution ability.
NOVELTY - A combined generation system comprises a natural gas synthesizing apparatus for receiving coal and oxygen, generating synthetic gas by a gasifier (110), and permitting the synthetic gas to pass through a methanation (160) reactor which synthesizes methane, a fuel cell apparatus (200) for receiving fuel containing methane from the natural gas synthesizing apparatus and generating electrical energy, and a generating apparatus for producing electrical energy using the fluid discharged from the fuel cell apparatus.    USE - Combined generation system (claimed).    ADVANTAGE - The combined generation system is economically manufactured, and efficiently produces energy with reduced carbon dioxide.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of capturing carbon dioxide of combined generation system, which involves reacting ejected carbon dioxide from the anode of fuel cell with hydrogen which converts carbon dioxide to sample in natural gas synthesizing apparatus, and supplying the remaining carbon dioxide into the cathode of the fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart explaining the process of combined generation system.    Supply portion (101)    Gasifier (110)    Primary reactor (140)    Secondary reactor (150)    Methanation (160)    Fuel cell apparatus (200)    Anode (220)    Cathode (230)
NOVELTY - The air injection system comprises a pipe for supplying air to an air compressor. A power source is connected with a solar energy generating apparatus. An air preheating part preheats the air that is passed via an inner side of the branch portion. The air pump is coupled to an end of the air supply pipe and injects air into the air supply pipe. A condensing lens is located in a circular through-hole. A convex back mirror is located along a reflecting surface of the lens, where the lens is located at a front portion of a recess portion. An optical fiber group is located in the through-hole.    USE - The air injection system is useful for purifying sewage (claimed) or domestic waste water.    ADVANTAGE - The system can suppress anaerobic decomposition so that the bad smell generated in the sewage is prevented and the generation of the toxic material can be prevented.    DETAILED DESCRIPTION - The air injection system comprises a pipe for supplying air to an air compressor. A bubbling portion generates bubble within an open ditch of the drain pipe, where an end of the bubbling portion is provided with a conduit line connection. A branch portion is equipped in a connection part of the air supply pipe. The bubbling portion operates the air preheating part and an air pump in the branch portion. A power source is connected with a solar energy generating apparatus. The solar energy generating apparatus is equipped with the air compressor. An air preheating part preheats the air that is passed through an inner side of the branch portion. The air pump is connected to an end of the air supply pipe and injects air into the air supply pipe. A condensing lens is located in a circular through-hole. A convex back mirror is located along a reflecting surface of the condensing lens, where the condensing lens is formed at a front portion of a recess portion. An optical fiber group is located in a through-hole.
NOVELTY - Hydroisomerization process of light paraffin involves contacting hydrocarbon feed stream comprising predominantly normal and singly branched 4-7C paraffin, under hydroisomerization condition, with catalyst comprising aluminosilicate sodium formaldehyde sulfoxylate-type zeolite and at least one group (VIII) metal, and forming an isomerized product having doubly and singly branched paraffin with concentration more than the feed stream. The mol ratio of 2,3-dimethylbutane to 2,2-dimethylbutane in feed stream is 1 or more.    USE - Hydroisomerization process of light paraffin used for gasoline for automobile engine.
NOVELTY - Additive composition comprises (a) at least one hindered phenol (alkylphenol) antioxidant and (b) at least one metal passivator.    USE - The additive compositions is useful for superior quality diesel and biodiesel fuels for improving the lacquering resistance of the fuels (claimed), which are useful for engines provided with Euro 4 to Euro 6 fuel injection systems, and for power engines with compression ignition or diesel engines fitted to motor vehicles such as passenger cars, vans or trucks.    ADVANTAGE - The additive composition avoids, reduces and/or delays: slowing the response of the fuel injector; gluing the internal parts, which can cause loss of control of the injection time and the amount of fuel delivered by injection; handling loss of vehicle; changes in power; increase in fuel consumption; increase in pollutants; an increase in noise generated by the engine; and a decline in the quality of combustion in the long term. The composition has improved spray quality.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a superior quality diesel and biodiesel fuel; and    (2) preparing the additive composition comprising mixing the above components in one or more steps at room temperature.
NOVELTY - The system has optical demodulation and gas detection unit (14) integrated with optical modulation drive unit (12) to modulate laser beam and light-receiving unit (13) to receive reflected light from target and convert to electric signal, and provided to demodulate received signal from light-receiving unit and to measure concentration of methane gas from absorption of methane gas. A warning unit (15) generates alarm, when measured concentration of methane gas exceeds predetermined concentration. A control unit (3) controls warning display for displaying alarm on LCD (7).    USE - Camera system for camera mount (claimed), for recording photographed image data. Uses include but are not limited to photographed image data of plant construction, installation work, repair work, electrical work, gas and water supply, ventilation place such as manhole, pump well, sewage pipe, underground embedding work, tunneling work, respiration process, under-ground component of microorganism and dangerous place to which oxygen concentration is falling.    ADVANTAGE - The camera system having toxic-gas detecting function can easily perform image photography by providing the warning unit that generates alarm, when measured concentration of methane gas exceeds predetermined concentration.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for camera mount.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram illustrating the operation of the camera system. (Drawing includes non-English language text)    Control unit (3)    LCD (7)    Optical modulation drive unit (12)    Light-receiving unit (13)    Optical demodulation and gas detection unit (14)    Warning unit (15)
NOVELTY - Enzymatic hydrolysis method of starch involves preprocessing starch using direct pressure and adding enzyme in preprocessed starch.    USE - Enzymatic hydrolysis method of starch used for manufacturing biofuel (claimed).    ADVANTAGE - The enzymatic hydrolysis method of starch having improved energy efficiency is efficiently enabled, by simple method.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of oligosaccharide; and    (2) manufacture of biofuel.
NOVELTY - The device has a bottom layer formed on a combustion fuel layer. A carbon dioxide contact reducing layer is adhered with a combustible gas carbon monoxide layer. Carbon monoxide is continuously mixed with supplementary fuel. A door (6), an air duct (5) and an air outlet pipe (3) are connected with each other. The air duct and a hearth (2) are connected with a feeding port (4). The feeding port is distributed on a circle ring. The air outlet pipe is vertically connected with the hearth and a pipe body.    USE - Vertical air inlet device for a biomass gasification furnace (claimed).    ADVANTAGE - The device has air channel preventing function, and is formed with a waste outlet so as to ensure better waste discharging effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a vertical air inlet device.    Hearth (2)    Air outlet pipe (3)    Feeding port (4)    Air duct (5)    Door (6)
NOVELTY - Composting sludge, comprises controlling the temperature of the sludge to 3-5 degrees C and then keeping at 75 degrees C for 5-8 hours, adding fertilizer and then killing stack of parasites and bacteria to control humidity, ventilating the sludge using blower, degrading the organic matter of solid waste at a high temperature and then cooling and decomposing.    USE - The method is useful for composting sludge (claimed).    ADVANTAGE - The method is capable of simply composting sludge with high accuracy and good sanitary condition.
NOVELTY - Preparing fertilizer comprises uniformly mixing bone powder, fish meal, buckwheat peel and bagasse powder according to a ratio of 2.5-3.5: 3-6:4-8:5-10 in a fertilizer tank, and adding 5% of phosphate with water for 100-150 times and then stirring, fermenting the stirred mixture for 4-5 months, and extracting the supernatant liquid.    USE - The method is useful for preparing fertilizer for planting balloon flower and digitalis flower (claimed).    ADVANTAGE - The fertilizer can effectively and rapidly promote the plant growth with excellent quality.
NOVELTY - A sludge treatment device comprises several sludge fermentation device connected with oxygen ventilation device, where the ventilation device is connected with a fan, and is provided with multiple temperature sensors that collect temperature data; and temperature control device that is connected with the ventilation device.    USE - As sludge treatment device (claimed) for making organic fertilizer.    ADVANTAGE - The sludge treatment device is environment-friendly device.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic diagram of sludge treatment device.
NOVELTY - Air-floating water purifying residual bath treatment technique of algae residue, involves adding dehydrating agent and algae residue pressure filter, where the dehydrating agent is mass fraction of 10% of ferrate; a photo-catalysis technique processing filter water.    USE - As air-floating water purifying residual bath treatment technique of algae residue (claimed), used to remove algae in algae water.    ADVANTAGE - The method provides simple process, has high efficiency, low cost, convenient operation, green and is environment-friendly without secondary pollution.
NOVELTY - Chicken manure fertilizer, comprises: fresh chicken manure (50-55 parts by weight (pts.wt.)), corn flour (10-15 pts.wt.), wheat flour (10-15 pts.wt.), wheat bran (5-10 pts.wt.), brown sugar (4-5 pts.wt.), lime (3-4 pts.wt.), dinoflagellate (1-1.5 pts.wt.), yeast (1-2 pts.wt.), lactic acid bacteria (1-2 pts.wt.), and high temperature actinomycetes (0.5-0.8 pts.wt.).    USE - As chicken manure fertilizer (claimed) used as poultry feed.    ADVANTAGE - The fertilizer cost is low, can decompose chemical fertilizer remained in the soil to form a nitrate and secondary salt, so as to achieve disease resistance, lodging, improve the function of crop yield, increases the air permeability of the soil, reduces and remove the hardening of the soil and, at the same time also can reduce chemical fertilizer and farm chemical dosage, reduces the production cost, less pollution and optimizes ecological environment of soil, the soil ecological balance, the crop mature in advance, improve the quality of crop, reduces and removes the residual species of toxic and harmful heavy metal residue to make the crops green and environment-friendly.
NOVELTY - Producing a compost having reduced ammonia content from egg chicken excremen involves: taking straws, cutting into 2-3 cm long; mixing egg chicken manure and rice bran with the straw according to mass ratio of 28:9:1, where initial water content of the raw material is 55 5%; composting for 30 days to obtain a fertilizer where the product is subjected to turning on the following days 3, 7, 11, 15, 19 and 25 to supply oxygen.    USE - For producing a compost having reduced ammonia content from egg chicken excrement (claimed).    ADVANTAGE - The method reduce ammonia volatilization peak value, volatilizing time, reduces ammonia generation in egg chicken manure, rice bran, promote decomposition and use of water-solubility carbon, promote composite, and shorten compost. The method is simple in operation, the raw material cost is low, practical value is high, nitrogen loss is 8%, and the chicken manure fertilizer of nitrogen loss rate is as high as 23-65%.
NOVELTY - A flower planting device, comprises a cover body (2), where a container (1) of container edge and cover body at bottom of screw fasten, the container is set in middle of first container is integrated with a bump, the bump is set in middle of vent hole (4), vent hole and bottom of container is provided with an exhaust valve, the vent valve is set on valve body (8) of vent hole, a vent hole and an exhaust cavity is set in exhaust chamber which is connected with valve ball of connecting rod, the lower part of container is provided with a base (5).    USE - As flower planting device for flower planting the anger fertilizer (claimed).    ADVANTAGE - The device effectively avoid the occurrence of accident, is simply and easy to use.    DETAILED DESCRIPTION - A flower planting device, comprises a cover body (2), where a container (1) of the container edge and the cover body at the bottom of screw fasten, the container is set in the middle of the first container is integrated with a bump, the bump is set in the middle of the vent hole (4), the vent hole and the bottom of the container, and is provided with an exhaust valve is set in the vent hole, the vent valve is set on the valve body (8) of the vent hole, a vent hole and an exhaust cavity in the valve body, the valve ball is set in the exhaust chamber is connected with the valve ball of the connecting rod is connected between the metal spring sheet and the metal elastic sheet and the upper end of the valve body is provided with a spring, the lower part of the container is provided with a base, the bump is set lower than the height of the container.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a flower planting device.    Container (1)    Cover body (2)    Bulge (3)    Vent hole (4)    Base (5)    Container, along port (6)    Handle (7)    Valve body (8)
NOVELTY - A symmetrical front-mounted dumper, comprises traction device (1), turning device (2), power input device (13), torque clutch device (14), walking device (3), balancing device and folding device.    USE - As a symmetrical front-mounted dumper (claimed) for composting domestic garbage and garbage layer stack, and accelerating garbage fermentation.    ADVANTAGE - The symmetrical front-mounted dumper is convenient for long distance runner; optimizes the turning effect, which reduces the operation difficulty; and is suitable for each kind of turning operation.    DETAILED DESCRIPTION - A symmetrical front-mounted dumper, comprises traction device (1), turning device (2), power input device (13), torque clutch device (14), walking device (3), balancing device and folding device. The turning device is arranged along the central axis of the traction device. The upper end of the turning device is connected to the proximal end of the traction device and to the distal end of the walking device. The turning device is provided with a rotary cutter shaft (4). The rotary cutter shaft is present along the axial direction blade (5). The walking device is provided with a roller. The traction device is transmitted to the power input device. The balancing device comprises balancing block (15) and balancing rod (16).    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a symmetric front-mounting type turning machine.    Traction device (1)    Turning device (2)    Walking device (3)    Rotary cutter shaft (4)    Blade (5)    Power input device (13)    Torque clutch device (14)    Balancing block (15)    Balancing rod (16)
NOVELTY - The invention relates to a process for preparing a liquid fuel for internal combustion engines. According to the invention, the process consists in selectively extracting biobutanol resulting from butanol fermentation process with motor vehicle gasoline or with a hydrocarbonate component employed in the preparation thereof, at a solvent : fermentation solution ratio of 1:1...10:1, in a discontinuous or continuous system, at temperatures of 80 degrees C at the most, the resulting mixture being employed as such in the preparation of motor vehicle gasoline.
NOVELTY - The method involves crushing and drying a biomass e.g. agriculture waste fine particle, with a grain diameter of 5.40 mm. A biomass reaction and a biomass gasification agent are contacted, where an initial temperature of the agent is not less than 110 degrees centigrade and a mass ratio of the agent is 0.20 to 2.40. A reaction pressure of specific value is maintained. A reaction temperature ranging from 800 to 950 degrees centigrade is maintained. Gas is released when the reaction pressure is larger than a preset pressure. Output gas i.e. synthesis gas, is produced by condensing purification.    USE - Biomass fixed bed pressure gasification method for producing synthesis gas.    ADVANTAGE - The method conveniently adjustingly produces the clean synthesis gas with a high hydrogen/carbon monoxide ratio of larger than 2 using low equipment investment, and provides a simple condensing device.    DETAILED DESCRIPTION - The synthesis gas contains carbon monoxide, 9% of hydrogen, 2% of carbon dioxide, and methane.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a device for performing a biomass fixed bed pressure gasification method for producing synthesis gas.    Steam generator (3)    Fixed bed reactor (5)    Biomass hopper (7)    Cooling device (10)    Condensed liquid collector (11)
NOVELTY - The device has a hollow air-flow bed gasification furnace whose gas outlet is connected with a gas inlet of another hollow airflow bed gasification furnace via a pipeline. The former air-flow bed gasification furnace is provided with a feed-in injector nozzle. Top and bottom parts of the former air-flow bed gasification furnace are provided with gasification zone and a slag tank. The latter air-flow bed gasification furnace is provided with a furnace body that is fixed to a radiation waste boiler. A gas outlet of a radiation waste boiler is connected with the latter bed gasification furnace.    USE - Tanning waste gasification technique based fuel gas preparing device.    ADVANTAGE - The device is inexpensive, and has high working efficiency, and prevents environment from being polluted.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a tanning waste gasification technique based fuel gas preparing method. The feed-in injector nozzle is selected as a tri-channel combined gasification nozzle.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a tanning waste gasification technique based fuel gas preparing device.'(Drawing includes non-English language text)'
NOVELTY - The device has a pyrolysis fluidized bed (4) formed with a steam inlet (401). A bottom part of a calcined fluidized bed (9) is formed with an oxygen inlet (901). A cyclone separator (6) is formed with a synthesis gas outlet (601). Another cyclone separator (10) is formed with a smoke gas outlet (1001). Two lower parts of two U-shaped returning devices (7, 8) are respectively formed with two returning nitrogen inlets (701, 801). A lower part of the former cyclone separator is connected with a lower part of the pyrolysis fluidized bed by one of the two U-shaped returning devices.    USE - Double-fluidized bed biomass gasification technique based synthesis gas preparing device.    ADVANTAGE - The device reduces tar content and improves synthesis gas yield heat value and gasification efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a double-fluidized bed biomass gasification technique based synthesis gas preparing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a double-fluidized bed biomass gasification technique based synthesis gas preparing device.    Pyrolysis fluidized bed (4)    Cyclone separators (6, 10)    U-shaped returning devices (7, 8)    Calcined fluidized bed (9)    Steam inlet (401)    Synthesis gas outlet (601)    Returning nitrogen inlets (701, 801)    Oxygen inlet (901)    Smoke gas outlet (1001)
NOVELTY - Waste biomass raw material is cut into pieces, ground, washed, dust and impurities are removed, and dried. The dried waste biomass material is ground with a grinder, and sieved with a 20-mesh sieve and a 10-mesh sieve, to obtain biomass material. 10 L Waste oil is filled into a 12 L bucket, obtained biomass material is filled into a stainless steel mesh bag, the stainless steel mesh bag is immersed below the level of the waste oil, the stainless steel mesh bag is taken out after 1-2 hours, and the stainless steel mesh bag is naturally drained, to obtain a waste oil impregnated material.    USE - Preparation of waste oil impregnated biomass fuel (claimed).    ADVANTAGE - The waste oil impregnated biomass fuel has improved heat value of by 2-3 times compared with the heat value of the single biomass material, is prepared.    DETAILED DESCRIPTION - Waste biomass raw material is cut into pieces, ground, washed with clear water, dust and impurities are removed, and dried in a constant temperature drying oven at 85 degrees C to constant weight. The dried waste biomass material is ground with a grinder, and sieved with a 20-mesh sieve and a 10-mesh sieve, to obtain biomass material with grain size of 0.9-2 mu m. 10 L Waste oil is filled into a 12 L bucket, 200-500 g obtained biomass material is filled into a stainless steel mesh bag, the stainless steel mesh bag is immersed below the level of the waste oil, the stainless steel mesh bag is taken out after 1-2 hours, and the stainless steel mesh bag is naturally drained, to obtain a waste oil impregnated material. The waste oil impregnated material is added to a filter pressing device for filter pressing forming under the filter pressing strength of 0.3-0.5 MPa to obtain a solid waste oil impregnated biomass fuel.
NOVELTY - Phenol production device comprises ethanol oxidation tank, first stirring tank, second stirring tank, first material tank, second material tank and a quantitative perfusion device of liquid filling machine. The ethanol oxidation tank is provided with ethanol inlet, catalyst inlet and oxygen inlet. The ethanol oxidation tank is conneted to the first stirring tank via a pipeline. The first stirring tank is provided with tritolyl inlet. The first stirring tank is connected to the second stirring tank. The first material tank is provided with water inlet and dodecyl benzene sulfonic acid inlet.    USE - Used as a phenol production device.    ADVANTAGE - The device produces high quality product with simple process, does not emit toxic and harmful gas and liquid. The phenol has high efficiency, fast effect, stable performance, and is an economical disinfectant, which can quickly kill bacteria, virus, fungi, spore, and has special effect on pig disease.
NOVELTY - Preparing (R)-3-amino-1-(3-trifluoromethyl-5,6,7,8-tetrahydro-(1,2,4)triazolo(4,3-a)pyridin-7-yl)-4-(2,4,5-trifluoro-phenyl)-butan-1-one (I) comprises condensing 2-(1-hydroxy-2-(2,4,5-trifluoro-phenyl)-ethylidene)-5,5-dimethyl-cyclohexane-1,3-dione (II) with 3-trifluoromethyl-octahydro-(1,2,4)triazolo(4,3-a)pyrazine (II), aminating 1-(3-(difluoromethyl)-6,8-dihydro-5H-(1,2,4)triazolo(4,3-a)pyrazin-7-yl)-4-(3,4-difluorophenyl)butane-1,3-dione (III) and hydrogenating (Z)-3-amino-1-(3-(difluoromethyl)-6,8-dihydro-5H-(1,2,4)triazolo(4,3-a)pyrazin-7-yl)-4-(3,4-difluorophenyl)but-2-en-1-one (IV).    USE - (I) is useful as hypoglycemic agent. No biological data given.    ADVANTAGE - The method allows simple, economical, safe preparation of (I) with high yield and quality in an eco-friendly manner, and (I) is suitable for industrial application.    DETAILED DESCRIPTION - Preparing (R)-3-amino-1-(3-trifluoromethyl-5,6,7,8-tetrahydro-(1,2,4)triazolo(4,3-a)pyridin-7-yl)-4-(2,4,5-trifluoro-phenyl)-butan-1-one (I) or its acid addition salt, comprises condensing 2-(1-hydroxy-2-(2,4,5-trifluoro-phenyl)-ethylidene)-5,5-dimethyl-cyclohexane-1,3-dione (II) with 3-trifluoromethyl-octahydro-(1,2,4) triazolo(4,3-a)pyrazine (II) in presence of base and a solvent to produce 1-(3-(difluoromethyl)-6,8-dihydro-5H-(1,2,4)triazolo(4,3-a)pyrazin-7-yl)-4-(3,4-difluorophenyl)butane-1,3-dione (III), aminating (III) using aminating agent to produce (Z)-3-amino-1-(3-(difluoromethyl)-6,8-dihydro-5H-(1,2,4)triazolo(4,3-a)pyrazin-7-yl)-4-(3,4-difluorophenyl)but-2-en-1-one (IV), hydrogenating (IV) in the presence of solvent, optionally isolating (I), and optionally converting (I) to its acid addition salts. An INDEPENDENT CLAIM is included for preparing (II) comprising reacting (2,4,5-trifluoro-phenyl)-acetic acid with 2,2-dimethyl-(1,3)dioxane-4,6-dione in the presence of solvent and carbodiimide.
NOVELTY - A mixture of hydrogen-producing anaerobic microorganism and organic material is continuously fermented in a bioreactor by intermittently performing sonication of the mixture for upto 90% of time. The obtained hydrogen is drawn from a headspace above the mixture in the bioreactor. A material having organic load is fed into the bioreactor to supplement the organic load of the material in the bioreactor, and a portion of digested material is removed from the bioreactor. Thus, the organic material is anaerobically digested.    USE - Anaerobic digestion of organic material used for producing hydrogen and methane.    ADVANTAGE - The method enables efficient anaerobic digestion of organic material with improved operational reliability, and reduced odor generation and clogging performance.    DETAILED DESCRIPTION - A mixture of hydrogen-producing anaerobic microorganism and organic material is continuously fermented in a bioreactor by intermittently performing sonication of the mixture for upto 90% of time. The obtained hydrogen is drawn from a headspace above the mixture in the bioreactor. A material having organic load is fed into the bioreactor to supplement the organic load of the material in the bioreactor, and a portion of digested material is removed from the bioreactor. Thus, the organic material is anaerobically digested. The feeding of material and removal of digested material is repeated or performed continuously, to obtain a hydraulic residence time of the organic material in the bioreactor of 2-48 hours. The average rate of production of hydrogen is at least 20% of the average organic loading rate, in which the rate of hydrogen production is measured in liters hydrogen per liter bioreactor volume per unit time and organic loading rate is measured in g chemical oxygen demand per liter bioreactor volume per unit time.
NOVELTY - Preparation (M1) of methyl ester of valsartan (N-(1-oxopentyl)-N-((2'-(1H-tetrazol-5-yl)(1,1'-biphenyl)-4-yl) methyl-L-valine) involves: reacting N-((2'-cyanobiphenyl-4-yl)methyl)-N-valeryl-(L)-valine methyl ester with Tri-n-butyl tin chloride, and sodium azide in the presence of catalytic amount of water, in a suitable organic solvent such as toluene, o-xylene, m-xylene and/or p-xylene, at 80-170 degrees C to form methyl ester of valsartan.    USE - For preparation of methyl ester of valsartan which used for preparation of valsartan (claimed) for the treatment of hypertension and heart failure.    ADVANTAGE - The prepared methyl ester of valsartan is used for preparing valsartan with purity of 99.9%. The method prepares methyl ester of valsartan without heating for prolonged time and not involving tedious workup procedure; provides easy work up, cost effective and environmentally friendly process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation (M2) of valsartan involving: condensing methyl-N-((2'-cyanobiphenyl-4-yl)methyl)-L-valinate hydrochloride with valeroyl chloride in the presence of base, to form N-((2'-cyanobiphenyl-4-yl)methyl)-N-valeryl-(L)-valine methyl ester (i); reacting the compound (i) with tri-n-butyl tin chloride, sodium azide in the presence of catalytic amount of water, in toluene, o-xylene, m-xylene and/or p-xylene, to form methyl ester of N-(1-oxopentyl)-N-((2'-(1H-tetrazol-5-yl) (1,1'-biphenyl)-4-yl) methyl-L-valine; converting methyl ester of N-(1-oxopentyl)-N-((2'-(1H-tetrazol-5-yl)(1,1'-biphenyl)-4-yl) methyl-L-valine to crude barium salt of valsartan, by treating it with barium hydroxide; treating crude barium salt of valsartan with N,N-dimethyl formamide; and converting barium salt of valsartan to pure valsartan.
NOVELTY - Preparing plant source pesticide involves picking capillary artemisia in early April of tender stem and leaf, then drying and crushing to form plant source pesticide.    USE - For preparing plant source pesticide for preventing and treating root-knot nematode disease (claimed).    ADVANTAGE - The method is low cost, simple, convenient for operation, and easy to large scale; avoids environmental pollution; and provides food safety.
NOVELTY - Fuel composition is prepared by (a) mixing 19-25 wt.% pine nut shell powder, 3-5 wt.% ocher powder, 4-6 wt.% hardwood charcoal powder, 8-11 wt.% yellow soil powder, and 53-59 wt.% pine sawdust, and adding the mixture to compression molding device to solidify the mixture.    USE - As fuel composition for roasted meat.    ADVANTAGE - The fuel composition is cost-effective as it has low carbon emission.    DETAILED DESCRIPTION - Fuel composition is prepared by (a) mixing 19-25 wt.% pine nut shell powder, 3-5 wt.% ocher powder, 4-6 wt.% hardwood charcoal powder, 8-11 wt.% yellow soil powder, and 53-59 wt.% pine sawdust, and adding the mixture to compression molding device to solidify the mixture or (b) mixing 19-25 wt.% pine nut shell powder, 3-5 wt.% ocher powder, 4-6 wt.% hardwood charcoal powder, 8-11 wt.% yellow soil powder, and 53-59 wt.% atleast one including black oak saw dust, Coffea Arabica sawdust, Melaleuca wood sawdust, Eucalyptus wood sawdust, cypress wood sawdust, rice straw, Ginkgo biloba sawdust, Perilla frutescens, Gingko leaves and Cryptomeria japonica, and adding the mixture to compression molding device to solidify the mixture.
NOVELTY - The gas purifying device has a sulfuric acid tail gas pipe that is connected with a turbulent pipe. The turbulent pipe is connected with the absorption tower. The absorption tower is connected with a tail gas outlet pipe through tail gas fan.    USE - Sulfuric acid tail gas purifying device.    ADVANTAGE - The pollution to the environment can be reduced.
NOVELTY - Producing marsh gas and organic fertilizer by dry fermentation of livestock and poultry excrement and crop straw comprises preparing the crop straw and the weeds to desired particle size, adding proper amount of composite microbial inoculum, piling up for 5-7 days, adding fresh cow excrement; adjusting carbon-nitrogen ratio of the active sludge, adjusting pH to 7, placing into anaerobic fermentation tank, mixing uniformly, fermenting at high temperature; dry-wet separation, fermenting; collecting fermentation product; collecting marsh gas; and producing organic fertilizer.    USE - The method is used for producing marsh gas and organic fertilizer by dry fermentation of livestock and poultry excrement and crop straw (claimed).    ADVANTAGE - The method above provides rapid gas production, and has high fermentation efficiency. The produced organic fertilizer does not generate ammonia toxicity.
NOVELTY - Preparing glutamic acid comprises first level culturing of a strain; second level culture-shaking; third level culturing; carrying out primary level transformation in the fermentation tank; fermenting and culturing; and carrying out secondary transformation in the fermentation tank.    USE - The method is used for preparing glutamic acid (claimed).    ADVANTAGE - The glutamic acid preparation method is rapid and environment-friendly, uses strain with improved enzyme activity, and reduces emission.
NOVELTY - Extracting phospholipids, gossypol and pigment from cottonseed oil, comprises mixing cotton seed oil with low carbon alcohol according to a ratio of 1:0.1-30 vol.%, where the low carbon alcohol is gossypol, refining cotton seed oil for detoxification, adding alcohol layer by simulated moving bed chromatography separation to obtain the eluent and residual liquid, washing the residual liquid by desolventizing process to obtain the detoxified of cotton seed lecithin, and recycling the eluent by desolventizing process to obtain gossypol with purity more than 98%    USE - The method is useful for extracting phospholipids, gossypol and pigment from cottonseed oil (claimed).    ADVANTAGE - The method simply eco-friendly extracts the phospholipids, gossypol and pigment from cottonseed oil with high quality and wide application range.
NOVELTY - Special-shaped biomass circulating fluidized-bed gasifier process comprises introducing biomass and heat carrier into special circulating fluidized bed, with gasification gas and circulating ash, carrying out hydrogen thermal decomposition, carrying out first stage gas-solid separation, recycling thick semi-coke ash to special circulating fluidized bed; obtaining gasification gas with oxidizing agent and steam, together with upward circulating ash to form circular lifting conveying of materials; carrying out second stage gas-solid separation of fine ash as silicon fertilizer, and product gas.    USE - Special-shaped biomass circulating fluidized-bed gasifier process.    ADVANTAGE - The method solves the problem of low gasification heat value, and difficult process.    DETAILED DESCRIPTION - Special-shaped biomass circulating fluidized-bed gasifier process comprises introducing biomass of less than 5 mm and small amount of heat carrier into special circulating fluidized bed below middle part of reactor with gasification gas and circulating ash, carrying out hydrogen thermal decomposition, carrying out first stage gas-solid high temperature separation, recycling thick semi-coke ash to special circulating fluidized bed of turbulent fluidized bed; obtaining gasification gas with an oxidizing agent and steam at temperature of 800-1100 degrees C, together with upward circulating ash to form circular lifting conveying of materials; carrying out second stage gas-solid high temperature separation of fine ash as silicon fertilizer, and product gas.
NOVELTY - A biological organic fertilizer comprises functional microorganism, raw material composite, garlic cropping rot, cucumber cropping wilt, and watermelon cropping dead seedling.    USE - A biological organic fertilizer.
NOVELTY - Fertilizer comprises biomass power plant ash and binding agent, where the biomass power plant ash is obtained by burning chicken manure, rice hull, bamboo, and firewood in a mass ratio of 30-50:10-40:2-20:10-30, and the mass ratio of the biomass power plant ash and the binding agent is 300-990:10-30.    USE - As fertilizer.    ADVANTAGE - The fertilizer does not damage soil element balance and is free of hormones and bacteria, has slow release effect, enables to release increased amount of nutrients rapidly than organic fertilizers, and is environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves adding the biomass power plant ash and binding agent in a mass ratio of 300-990:10-30 into a granulator, adding water and uniformly stirring the mixture, and drying and crushing the obtained mixture, removing dust from the obtained mixture and cooling the obtained mixture to obtain granular fertilizer.
NOVELTY - Preparation of organic fertilizer comprises: taking 700-1000 pts. wt. wood mixtures, 200-300 pts. wt. chicken manure and 100-200 pts. wt. Chinese herbal medicine slag, uniformly mixing materials, stacking fermentation bed and adjusting water content to 50-70%; adding Effective Microorganisms, mixing material, putting in cover film and turning each stack sequence every 5-15 days for 50-70 days.    USE - Preparation of organic fertilizer.    ADVANTAGE - The method is simple and easy to control.
NOVELTY - A biological enzyme fertilizer comprises chicken manure (manure, industrial waste), rice hull powder, straw, and broomcorn straw.    USE - As a biological enzyme fertilizer having nitrogen, phosphorus, and potassium nutrient (claimed), used in agriculture industries.    ADVANTAGE - The fertilizer is capable of increasing production efficiency, improving soil, recovering fertility and improving fertilizer effect; and improves the mild water temperature, early.    DETAILED DESCRIPTION - A biological enzyme fertilizer comprises chicken manure (manure, industrial waste), rice hull powder, straw, and broomcorn straw. Preparation of the fertilizer involves crushing sorghum straw (20%), rice hull powder (20%), and chicken manure (60%), uniformly fermenting by naturally heating at 60-65 degrees C, for 3 times, to obtain rotten (smelling bouquet and soil fragrance) of large amount of mycelium, drying or naturally drying, and when the water content reaches to 8-12%, then the fertilizer soil having nitrogen (N), phosphorus (P), and potassium (K) nutrient, is obtained, which is then drying using machine for suitable shape and strength, packing and storing in storehouse.
NOVELTY - Fertilizer comprises (in wt.%): macro-element fertilizer (10-60); fertilizer element (1-5); microelement fertilizer (0.1-2); and molasses fermentation broth (100) with a concentration of 30-80%.    USE - The fertilizer is useful for Eucalyptus (claimed).    ADVANTAGE - The environment-friendly fertilizer saves work and time, has high efficiency, and improves the quality, growth and yield of the Eucalyptus.
NOVELTY - Molasses ferment liquid is used to produce water-soluble organic-inorganic complex fertilizer, comprising water-soluble nitrogen fertilizer, soluble phosphorus fertilizer and soluble potassium fertilizer, 30-75% biological bacteria, 0.5-5% molasses ferment liquid with 45-95% concentration.    USE - Molasses ferment liquid used to produce water-soluble organic-inorganic complex fertilizer (claimed).    ADVANTAGE - The method is convenient, has high nutritive element content, and low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a preparation of molasses ferment liquid comprising adding molasses ferment liquid of 45-95% concentration in fermentation tank, adding biological bacteria and raw material at a weight ratio of 0.5-5:100, uniformly stirring, fermenting at 10-40 degrees C for 30-40 hours, removing colloid in fermentation liquid, processing high temperature inactivation, filtering to remove insoluble substance, adding water soluble nitrogen fertilizer, adding phosphate fertilizer or water-soluble fertilizer to fermentation liquid, water soluble nitrogen fertilizer, soluble phosphorus fertilizer and soluble potassium fertilizer at weight ratio of 30-75:100, stirring uniformly to obtain the granulating and drying.
NOVELTY - Method for preparing culture medium using agricultural waste involves (a) preparing fermented corn waste by uniformly mixing corn waste, urea, efficient biological agent, sheep manure, calcium superphosphate, and furfural residue, and piling and fermenting the obtained mixture, (b) sterilizing furnace slag by applying high temperature steam at 100-120 degrees C and screening the furnace slag using 100 meshes sieve to obtain sterilized furnace slag, and (c) mixing the fermented corn waste, sterilized furnace slag, organic fertilizer, vermiculite and perlite.    USE - The method is useful for preparing culture medium using agricultural waste (claimed).    ADVANTAGE - The method is unique, environmentally-friendly, improves the total fertility of nitrogen phosphorus and potassium, and reduces consumption and cost of chemical fertilizer.    DETAILED DESCRIPTION - Method for preparing culture medium using agricultural waste involves (a) preparing fermented corn waste by uniformly mixing corn waste (suitable quantity), 1-5% urea, 0.01-0.05% efficient biological agent, 2-5% sheep manure, 0.2-0.5% calcium superphosphate, and 5-30% furfural residue, watering the mixture, controlling the moisture content of the mixture to 60%, piling and fermenting the obtained mixture, and raising the temperature of the mixture to 50 degrees C, turning the mixture, until the temperature is 55-65 degrees C, and stop turning when the temperature is reduced to 20-30 degrees C and moisture content is reduced to 20-30%, (b) sterilizing furnace slag by applying high temperature steam at 100-120 degrees C and screening the furnace slag using 100 meshes sieve to obtain sterilized furnace slag, and (C) mixing 50-80 wt.% fermented corn waste obtained in the step (a), 10-30 wt.% sterilized furnace slag obtained in the step (b), 2-5 wt.% organic fertilizer, 1-10 wt.% vermiculite and 1-10 wt.% perlite.
NOVELTY - Preparing organic inorganic complex fertilizer involves pre-fermenting, adding traditional Chinese medicine dregs weight into giant knotweed, traditional Chinese medicine dregs, calcined lime (5-8%), livestock manure (1%) and a certain amount of water, after stirring water content is controlled between 50-75%, (2) fermenting, The medicine of stacking to 30-200 cm, the bottom width 30-300 cm, which is ladder-shaped, fermentation, (3) turning, starting from the accumulation by 48 hours or stack center temperature. (4) obtaining organic-inorganic complex fertilizer, after the fermentation.    USE - For preparing organic inorganic complex fertilizer (claimed), used in planting the flower, vegetable, trees and other plants.    ADVANTAGE - The organic inorganic complex fertilizer is a slow and slow release fertilizer capable of improving soil.    DETAILED DESCRIPTION - Preparing organic inorganic complex fertilizer involves pre-fermenting, adding traditional Chinese medicine dregs weight into giant knotweed, traditional Chinese medicine dregs, calcined lime (5-8%), livestock manure (1%) and a certain amount of water, after stirring water content is controlled between 50-75%, (2) fermenting, The medicine of stacking to 30-200 cm, the bottom width 30-300 cm, which is ladder-shaped, fermentation, (3) turning, starting from the accumulation by 48 hours or stack center temperature, (4) obtaining organic-inorganic complex fertilizer, after the fermentation is finished, according to each ton of giant knotweed, medicine dregs adding urea (10-30%), calcium superphosphate (10-40%), plant ash (5-50%) and solid nitrogen (5-30%), phosphorus, potassium composite strain powder, then uniformly crushing and sieving to obtain the product.
NOVELTY - A 2,3,5-trimethyl pyridine-N-oxide, which is an omeprazole intermediate, is prepared by using phosphorus ammonium molybdate as catalyst, using hydrogen peroxide for 2,3,5-trimethyl pyridine oxidation, decompressing and concentrating, and distilling.    USE - Method for preparing 2,3,5-trimethyl pyridine-N-oxide (claimed).    ADVANTAGE - The method has mild reaction, high safety, and improved yield, which is more suitable for industrial production. Distilled water is directly discharged, thus there is no pollution.
NOVELTY - Scenedesmus sp. ENN34 (I) preserved in China microorganism bacterial strain preservation management committee common microorganism centre under preservation number CGMCC No. 6348 and date 13-07-2012, is new.    USE - (I) is useful for producing fatty acid including palmitic acid, stearic acid, octadecenoic acid, octadecadienoic acid, parinaric acid, alpha -linolenic acid, gamma -linolenic acid and eicosapentaenoic acid, biofuel, which is biodiesel or ethanol, drug including astaxanthin, carotene, lutein, zeaxanthin and canthaxanthin, health care products, feed, and chemical product, which is pigment or cosmetic, and for sewage treatment or carbon dioxide emissions including effluent denitrification, phosphorus and organic matter degradation and heavy metal ion adsorption (all claimed).    ADVANTAGE - (I) has rapid growing speed, accumulates the oil, and can effectively remove the nitrogen containing compound in the water.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of (I).
NOVELTY - Enzymatic synthesis of ferulic acid glycerophospholipid involves taking ferulic acid and phospholipids at mass ratio of 8:1 to 1:8 mol into organic solvent, adding molecular sieve, then adding Novozym 435 (RTM: fatty enzyme) as catalyst, and activating at 40-70 degrees C by oscillation reaction for 10-240 hours; and after finishing the reaction, filtering, and evaporating clear filtrate through rotary evaporator to remove organic solvent. The organic solvent is mixed solvent of e.g. toluene and chloroform at vol. ratio of 95:5 to 80:20.    USE - For enzymatic synthesis of ferulic acid glycerophospholipid (claimed) with increased water solubility of ferulic acid which is used in food, cosmetic, medicine as antioxidant, ultraviolet absorbent, and also for resisting bacteria and diminishing inflammation, anti-cancer and antimutagenesis.    ADVANTAGE - The present preparation method has simple operation; is environment-friendly; and repeatedly utilizes enzyme catalyst so as to obtain good amount of single product structure. The obtained ferulic acid glycerophospholipid improves water-solubility of ferulic acid.    DETAILED DESCRIPTION - Enzymatic synthesis of ferulic acid glycerophospholipid involves taking ferulic acid and phospholipids at mass ratio of 8:1 to 1:8 mol into organic solvent, adding molecular sieve, then adding Novozym 435 (RTM: fatty enzyme) as catalyst, and activating at 40-70 degrees C by oscillation reaction for 10-240 hours; and after finishing the reaction, filtering, and evaporating clear filtrate through rotary evaporator to remove organic solvent. The organic solvent is mixed solvent of toluene and chloroform, toluene and acetone, toluene and tert-butyl alcohol, where the volume ratio of the toluene and other solvents is 95:5 to 80:20.
NOVELTY - Broad-spectrum bactericide comprises (in wt.%): berberine (0.5-4.5); Astragalus (0.5-20); hemsley rockvine extract (0.5-20); aloe extracting solution (0.5-20); saponin (0.5-20); and water (balance).    USE - Used as a broad-spectrum bactericide.    ADVANTAGE - The broad-spectrum bactericide can be economically prepared in an environmentally-friendly manner.
NOVELTY - Geotrichum candidum ZJB-09214 strain preserved under China centre for type culture collection (CCTCC) under a preservation number of M2012063, is new.    USE - The Geotrichum candidum strain is useful for the biological catalysis synthesis of L-tryptophan (claimed).    ADVANTAGE - The strain synthesizes L-tryptophan with high optical purity in environmental-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for use of Geotrichum candidum for biological catalysis synthesis of L-tryptophan, where the application method comprises fermenting racemic tryptophan amide as substrate with white Geotrichum candidum, adding enzyme source having a pH value of 6.5 and buffer solution in a reaction system and performing conversion reaction at 20-45 degrees C to obtain the reaction solution which is a mixed solution of L-tryptophan, and separating and purifying the mixed solution to obtain the L-tryptophan.
NOVELTY - The method involves sampling high-purity hydrogen in quantitative double-pipe (1) by chromatograph. The impurity concentration is detected quickly. The sample gas in process by clean carrier gas is flowed to separating system for separating small amount of impurities. A pulse discharge helium ionization detector (PDD) is provided to detect impurity of sample of gas chromatograph. The thermal conductivity detector (TCD) is set to detect separated constant impurity of the sample to gas chromatograph.    USE - On-line analysis method of gas component in natural gas hydrogen production process.    ADVANTAGE - The switching process can be performed quickly for testing gas component so as to effectively reduce the time for analysis of gas component.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating on-line analysis process of gas component in natural gas hydrogen production process. (Drawing includes non-English language text)    Quantitative double-pipe (1)    Ten-way valve (2)    Pre-separating columns (3,4)    Analytical column (5A)
NOVELTY - A culture medium comprises 30-80 pts. wt. chestnut shell, 10-35 pts. wt. crop straw or corn cob, 9-25 pts. wt. dry poultry manure, 0.5-4 pts. wt. calcium superphosphate, 0.2-3 pts. wt. quicklime and 0.3-3 pts. wt. bacterial enzyme.    USE - The culture medium is used for cultivating Coprinus comatus (claimed).    ADVANTAGE - The environment-friendly method has simple operation, low-cost production and high yield and conversion rate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for cultivation of Coprinus comatus using the culture medium comprising: (A) weighing chestnut shell, crop straw or corn cob, dry poultry manure, calcium superphosphate, quicklime and bacterial enzyme, adding water and stirring uniformly to obtain substrate; (B) raising temperature of substrate to 60 degrees C for 48 hours, piling and adjusting water content to 60-70% and pH to 7-8; (C) connecting culture medium to Coprinus comatus specie bag when fermentation temperature is less than 30 degrees C, inoculating with culture medium having dry weight of 10-15% and preparing Coprinus comatus; (D) putting Coprinus comatus in sterile room at 20-25 degrees C and picking; (E) taking Coprinus comatus from bag and establishing Coprinus comatus bed at interval of 3-7 cm in soil layer having thickness of 5-7 cm; (F) performing water management and keeping air and soil wet; and (G) harvesting when the fruiting body is 6th-8th maturity.
NOVELTY - Preparing organic fertilizer using self-made complex microflora fermented bran comprises adding yeast residue, corn starch, brown sugar and wheat bran into high-quality nitrogen-phosphorus-potassium fertilizer, and producing organic fertilizer using the microbial properties of self-made aerobic complex microflora.    USE - The method is useful for preparing organic fertilizer using self-made complex microflora fermented bran (claimed).    ADVANTAGE - The method: produces high-quality and economical organic fertilizer, utilizes corn starch and brown sugar, which promotes rapid propagation of complex microflora, has high degree of mechanization, reduces fermentation and aging process to 7-10 days, and ensures complete aerobic fermentation, high degree of urban sewage sludge degradation and rapid fermentation heating (claimed); utilizes beneficial microorganisms to ferment bran; has high production efficiency and low production costs; and solves the problem of high carbon-nitrogen ratio in bran.
NOVELTY - Cucumber seedling culturing substrate comprises 2.5-3.5 pts. wt. biogas residue (pig manure biogas residue as fertilizer source) 3 pts. wt. vermiculite, 2.5-3.5 pts. wt. peat and 1 pts. wt. perlite.    USE - Used as a cucumber seedling culturing substrate containing pig manure biogas residue.    ADVANTAGE - The culturing substrate: solves the problem of conventional peat-based seedling culturing substrate, reduces the amount of peat used, reduces the substrate cost and protects the ecological environment; ensures complete utilization of pig manure biogas residue and is environmentally friendly; and reduces the incidence rate of diseases and improves disease resistance of plants.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the fertilizer for culturing cucumber seedling, comprising (i) completely fermenting the pig manure biogas residue, separating through a solid-liquid separator, drying and crushing by a crusher; (ii) culturing Bacillus subtilis in nutrient broth (NB) culture medium for 48 hours, centrifuging at 5000 revolutions/minute for 20 minutes, precipitating and removing supernatant, where NB culture medium comprises 0.5% beef extract, 1% peptone, 0.5% sodium chloride and 2% glucose; (iii) drying peat to remove moisture content, and adsorbing with metabolic product of Bacillus subtilis, where the moisture content is 18-23%; (iv) crushing vermiculite and perlite; and (v) uniformly mixing the prepared biogas residue, peat, vermiculite and perlite in a roller.
NOVELTY - Improving oxadiazon production comprises under blending condition, adding dry hydrazine salt in toluene system; controlling temperature at 40 degrees C, slowly adding sodium hydroxide powder; slowly raising the temperature to 63-73 degrees C, stirring for 1 hour, adding water, circulating water cooling to 55-60 degrees C, stirring for 1 hour, standing for half an hour, removing the lower water layer, adding quantitative agent, stirring at 55-60 degrees C, after cooling the filtrate, entering into the next working procedure.    USE - A method of improving oxadiazon production.    ADVANTAGE - The method has high yield and increased stability, reduces wastewater discharge and related equipment and operator, and is economical and environment-friendly.
NOVELTY - Device comprises a heating device, a cooling device, a recycling device, an air inlet pipe, a waste gas discharge pipe and a waste gas filtering device. The heating device is connected with the cooling device. The cooling device is connected with the recycling device. The recycling device is connected with the waste gas filtering device through the waste gas discharge pipe. The upper part of the heating device is provided with the air inlet pipe.    USE - The device is useful for separating and purifying cantharidin (claimed).    ADVANTAGE - The device: improves the yield to more than 30%, and simplifies the process; reduces the amount of organic solvent used; and is safe and environmentally friendly.
NOVELTY - Nitromethane, formaldehyde solution, and a solvent are mixed in a reactor. A liquid alkali is added at 20 degrees C, followed by addition of liquid bromine for bromination to obtain a colorless reaction liquid. The crude reaction product is adjusted to a bromic acid content of 10 ppm or less. The obtained crude product is sent to a distillation tower at -92 kPa and tower-top temperature of 45-60 degrees C, and the distilled product is centrifugally dried to obtain bronopol with a purity of more than 99 wt.%.    USE - Synthesis of bronopol (claimed).    ADVANTAGE - The method enables quick, simple and environmentally-friendly synthesis of bronopol, with high product quality and yield.    DETAILED DESCRIPTION - Nitromethane, formaldehyde solution, and a solvent are mixed in a reactor. A liquid alkali is added at 20 degrees C, followed by addition of liquid bromine for bromination to obtain a colorless reaction liquid. The crude reaction product is adjusted to a bromic acid content of 10 ppm or less. The molar ratio of nitromethane, formaldehyde, alkali liquid, and liquid bromine is 1:2.1-2.2:1-1.1:1-1.05. The obtained crude product is sent to a distillation tower at -92 kPa and tower-top temperature of 45-60 degrees C, and the distilled product is centrifugally dried to obtain bronopol with a purity of more than 99 wt.%.
NOVELTY - A linezolid crystal form VI powder has absorption peaks at diffraction angle (2 theta ) of 11.25, 16.27, 16.70, 18.95, 19.69, 22.73, 25.09, 25.31, 26.22, 26.55, 27.54 and 29.60 based on X-ray powder diffraction spectrum.    USE - Linezolid crystal form powder (claimed).    ADVANTAGE - The linezolid crystal form VI having favorable dissolution rate is prepared under mild reaction condition, with yield of 95-99.9%, reduced impact on environment and energy consumption.    DETAILED DESCRIPTION - A linezolid crystal form VI powder has absorption peaks at diffraction angle (2 theta ) of 11.25, 16.27, 16.70, 18.95, 19.69, 22.73, 25.09, 25.31, 26.22, 26.55, 27.54 and 29.60 with error range of plus minus 0.2 based on X-ray powder diffraction spectrum. An INDEPENDENT CLAIM is included for preparation of linezolid crystal form VI powder, which involves taking linezolid as an raw material, adding into water, stirring, adding hydrochloric acid in drops to dissolve completely at 0-40 degrees C, then adding sodium hydroxide aqueous solution in drops, crystallizing at 0-40 degrees C under pH of 7-12, filtering to separate obtained linezolid solid, and drying to obtain linezolid crystal form VI. The amount of water is 5-40 times of amount of linezolid. The hydrochloric acid has concentration of 1-12 mol/L. The sodium hydroxide aqueous solution has mass concentration of 10-50%.
NOVELTY - Preparing high tower melt granulation water-soluble fertilizer comprises (a) introducing ammonium nitrate or mixture containing ammonium nitrate into a melting tank, adding ammonium phosphate and water separately or after mixing, melting at 140-145 degrees C, where the ratio of ammonium nitrate or a mixture containing ammonium nitrate to ammonium phosphate is 19:1-2.33:1, (b) conveying into a mixing system, adding nitrogenous fertilizer, phosphate fertilizer, potash fertilizer and water soluble trace element and mixing at 145-152 degrees C, and (c) feeding the slurry into a pelleting system for granulating.    USE - The method is useful for preparing high tower melt granulation water-soluble fertilizer (claimed).    ADVANTAGE - The method: reduces the generation of the water insoluble content by controlling the temperature; is environmentally friendly and cost effective; consumes less energy; and provides the water soluble fertilizer which high particle smoothness, high strength, does not get hardened after storing, and has total nutrients of 35-48% and water-insoluble content of 3%.
NOVELTY - A multi-element fertilizer comprises castor, sulfuric acid, inorganic fertilizer and liquid gas.    USE - A multi-element fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of multi-element fertilizer comprising: crushing castor, screening, sieving prepared fiber powder and protein powder; crushing fiber powder, screening, sorting; hydrolyzing protein powder; and drying, cooling, screening, and mixing plant pathogenic fungi, organic waste and inorganic fertilizer.
NOVELTY - The method involves generating heat at a lower part of a catalytic cracking unit in a reactor. A catalyst containing carbon is provided under an environment to perform isomerization reaction. Reaction oil gas and the catalyst are separated to obtain ethylene, propylene, propane, butane and petrol. Catalytic wax oil is used as raw material for an oil hydro-processing unit for hydrogenation of polycyclic aromatic hydrocarbon. The hydrogenated wax oil is made to enter into another catalytic cracking unit to separate the reaction oil gas and the catalyst.    USE - High-sulfur wax oil catalytic conversion method.    ADVANTAGE - The method enables producing ethylene and propylene by providing low-carbon olefin and high-octane rating petrol production for performing clean refining production process efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a high-sulfur wax oil catalytic conversion method.'(Drawing includes non-English language text)'
NOVELTY - Preparing Akebia quinata acid comprises crushing Akebia quinata, adding ethanol solution, ultrasonically extracting for 2-4 times, primarily purifying obtained extract, extracting at room temperature, separating by high-speed countercurrent chromatography using ethyl acetate, n-butanol and water as a solvent system.    USE - The method is useful for preparing Akebia quinata acid (claimed).    ADVANTAGE - The method: does not use any solid fillers, thus there is no irreversible adsorption, and no sample loss; improves efficiency; is environmentally friendly; and produces high yield.
NOVELTY - Method for preparing composite bacteria organic fertilizer, involves adding microbial solution, crop straw powder, bran powder, corn starch, brown sugar, wheat bran and auxiliary material and carrying out an aerobic harmless treatment on urban domestic sludge using obtained product.    USE - The method is useful for preparing composite bacteria organic fertilizer, which is useful for inhibiting harmful bacteria.    ADVANTAGE - The method utilizes different characteristics of various microbes to carry out degradation treatment on urban domestic sludge, has fully mechanized operation, low labor intensity, high production efficiency and low production cost, and is suitable for industrial production. The fertilizer can be produced easily.
NOVELTY - Dehydrating piggery marsh gas tank sludge, comprises concentrating marsh gas tank sludge in a sludge concentrating tank, introducing concentrated clear liquid into a sewage treatment equipment, introducing the concentrated sludge into a sludge conditioning tank, simultaneously adding conditioning agent, mixing, introducing conditioned sludge into horizontal screw discharging sedimentation centrifuge via a screw pump for centrifugal dehydration, returning the centrifuged solution to sludge concentration tank, and conveying dehydrated cake to sludge cake car through a shaft-free spiral conveyor.    USE - The method is useful for dehydrating piggery marsh gas tank sludge (claimed).    ADVANTAGE - The method can achieve continuous automatic feeding, separating, washing and discharging process with high continuity and automation degree; requires small floor area; and has high efficiency, convenient operation, good separating ability, and good sanitary condition.    DETAILED DESCRIPTION - Dehydrating piggery marsh gas tank sludge, comprises concentrating marsh gas tank sludge in a sludge concentrating tank, introducing concentrated clear liquid into a sewage treatment equipment, introducing the concentrated sludge into a sludge conditioning tank, simultaneously adding conditioning agent to the sludge conditioning tank, uniformly mixing in the tank provided with submersible type stirrer, introducing the conditioned sludge into horizontal screw discharging sedimentation centrifuge via a screw pump for centrifugal dehydration, returning the centrifuged solution to the sludge concentration tank, and conveying the dehydrated cake to sludge cake car through a shaft-free spiral conveyor.
NOVELTY - Processing household rubbish by earthworms, comprises drilling 3-4 holes at the bottom of rubbish barrel or plastic barrel, loading the barrel with earthworm growth substrate, where the predetermined distance of the substrate is more than 10 cm away from the barrel port, placing the barrel on a plastic basin for holding water, introducing earthworms and aquafarming in shadow; where the substrate comprises 60% domestic rubbish dust and 40% wood components.    USE - The method is useful for processing household rubbish by earthworms (claimed).    ADVANTAGE - The method: can effectively decompose the domestic rubbish; utilizes earthworms, which are capable of processing the rubbish or good organic fertilizer, which can be used for planting flower and grass at home, or can be used for residential flower beds to make the environment more beautiful.
NOVELTY - A power generation fuel is made of glass fiber reinforced plastic waste and straw; preparing combustion improver by crushing straw molding carbon and diesel fuel, mixing glass fiber reinforced plastic waste material and straw, forming carbodiimide component 25-70% of power generation fuel total weight and diesel combustion improver total weight.    USE - Power generation fuel.    ADVANTAGE - The combustion of power generation fuel can reach low emission environmental protection index, and can ensure low pollution and comprehensive utilization.
NOVELTY - Potassium hydroxide is added into mixture of soybean oil triglyceride and ethanol, and ester interchange reaction is carried out to obtain soybean oil fatty acid ethyl ester.    USE - Manufacture of soybean oil fatty acid ethyl ester used as biodiesel oil and for printing ink.    ADVANTAGE - The soybean oil fatty acid ethyl ester has excellent dyeing effect and is pollution free.
NOVELTY - Trandolapril intermediate benzyl (2S,3aR,7aS)-octahydroindole-2-carboxylate is prepared by reacting cyclohexene and chloramine-T to obtain cyclohexyl aziridine; reacting cyclohexyl aziridine with allylmagnesium bromide to obtain trans-N-p-methylphenylsulfonyl-2-(2-propenyl)-cyclohexylamine; performing nitrogen protection to obtain N-protected octahydroindole-2-carboxylic acid; removing nitrogen protecting group, and then esterifying to obtain indoline-2-carboxylic acid benzyl ester; and crystallizing and separating to obtain the trandolapril intermediate.    USE - Method of preparing trandolapril intermediate benzyl (2S,3aR,7aS)-octahydroindole-2-carboxylate (claimed).    ADVANTAGE - The method utilizes low-cost raw materials, is environment-friendly, convenient to operate, and has simple post-treatment and easy separation and purification processes.    DETAILED DESCRIPTION - Preparation of trandolapril intermediate benzyl (2S,3aR,7aS)-octahydroindole-2-carboxylate comprises:    (A) reacting cyclohexene and chloramine-T to obtain cyclohexyl aziridine;    (B) reacting cyclohexyl aziridine with allylmagnesium bromide to obtain trans-N-p-methylphenylsulfonyl-2-(2-propenyl)-cyclohexylamine;    (C) N-protecting trans-N-p-methylphenylsulfonyl-2-(2-propenyl)-cyclohexylamine in presence of oxidant to obtain N-protected octahydroindole-2-carboxylic acid;    (D) carrying out deprotection reaction, removing nitrogen protecting group, and then esterifying to obtain indoline-2-carboxylic acid benzyl ester; and    (E) crystallizing and separating to obtain the trandolapril intermediate.
NOVELTY - The soft biological filler has strip-shaped wire whose one end is provided with weft component side and other side is provided with secondary length of the weft. The left and right sides of the weft yarn interleaving potion is covered with warp portion. The width of the warp portion is greater than the width of the weft yarns interleaving portion.    USE - Soft biological filler used in sewage treatment.    ADVANTAGE - The specific surface area of the soft biological filler is increased, the water resistance is reduced, the absorption is improved and the yield of filler is improved. The sludge amount is reduced, the sludge retention capacity is improved, the nitrogen and phosphorus removal effect in oil field and food waste treatment effect is improved and stability of the filler is improved.
NOVELTY - A supported catalyst comprises metal nickel and/or oxides as supported catalyst component, and mesoporous molecular sieve MCM-41. The total amount of supported catalyst is 100%. The amount of nickel metal and/or oxides is 2-20 weight%.    USE - Supported catalyst is used for preparing methane reaction catalyst from synthesis gas (claimed).    ADVANTAGE - The supported catalyst has excellent catalytic activity and thermal stability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of supported catalyst, which involves providing mesoporous molecular sieve, dipping in the loading component precursor aqueous solution, removing out mesoporous molecular sieve MCM-41 and roasting.
NOVELTY - Waste pollutants in pig farm are treated by performing anaerobic treatment on waste pollutants which enter the biogas generating pit, and killing parasites and pathogenic microorganisms through anaerobic fermentation; planting green watermifoil in primary wet area, growing green watermifoil, absorbing nitrogen and phosphorus, and harvesting watermifoil; processing secondary wetland, planting cress, planting aquatic water spinach, and wetland harvesting; and processing tertiary wet land wet land area, planting perennial cress, planting lotus root, and adding soil crucian.    USE - Method for treating waste pollutants in pig farm (claimed).    ADVANTAGE - The method has low construction cost and running cost, and is easy to operate.    DETAILED DESCRIPTION - Treating waste pollutants in pig farm comprises:    (A) building 50 m3 biogas generating pit, performing anaerobic treatment on waste pollutants which enter the biogas generating pit, and killing parasites and pathogenic microorganisms through anaerobic fermentation, the chemical oxygen demand (COD) content being reduced to 85-90% and the normal growth of aquatic plants in a wet land is facilitated;    (B) planting green watermifoil in primary wet area (100-120 m2), growing the green watermifoil, the storage water depth being 8-12 cm, absorbing nitrogen and phosphorus, and harvesting watermifoil as materials covering a tea yard and a fruit yard, the nitrogen content in plant being 30.72 g/kg, and the content of phosphorus being 1.25 g/kg;    (C) processing secondary wetland (440-460 m2), planting cress, planting aquatic water spinach, and wetland harvesting each year; and    (D) processing tertiary wet land wet land area (580-620 m2), planting perennial cress, planting lotus root, adding soil crucian.
NOVELTY - The method involves adding lignin, non-polar organic solvent and metal catalyst to a high pressure kettle according to nickel/hydrogen beta zeolite (Ni/HBEA) at normal temperature into hydrogen, and raising temperature to 40-600 degrees Celsius. The obtained product is cooled after the reaction is finished. The petrol product is dissolved in polar organic solvent. The lignin contains organic lignin, alkali lignin, sulfonated lignin, lignin or enzymolysis lignin.    USE - Method for preparing high-quality petrol from lignin raw material.    ADVANTAGE - The method enables reducing preparing cost, ensuring efficiency of reaction process and realizing simple and efficient coupling process and application prospect.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a method for preparing high-quality petrol from lignin raw material.
NOVELTY - A preparing cephalosporin C involves taking cephalosporium acremonium and preparing primary seeds and secondary seeds; taking the secondary seeds and inoculating the secondary seeds to a cephalosporium acremonium fermentation culture medium to obtain fermentation liquid; and filtering the fermentation liquid to obtain supernatant, separating and purifying to obtain cephalosporin C.    USE - For preparing cephalosporin C (claimed).    ADVANTAGE - The method provides obviously higher yield of cephalosporin C than the existing technology, has high raw material utilization rate, has low residual amount, is cost low, and generates small environment pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fermentation culture medium of cephalosporium acremonium comprising 39-76 pts.wt corn steep liquor, 9-21 pts.wt peanut powder, 4-13 pts.wt glucose, 19-31 pts.wt hydrolyzing starch, 2-9 pts.wt methionine, 49-71 pts.wt plant oil, 1.4-4 pts.wt defoaming agent, 1-6 pts.wt magnesium sulfate, 7-16 pts.wt ammonium sulfate, 0.04-0.2 pts.wt iron sulfate, 0.01-0.05 pts.wt manganese sulfate, 0.01-0.05 pts.wt zinc sulfate, 0.01-0.05 pts.wt copper sulfate, and 4-11 pts.wt calcium carbonate.
NOVELTY - An Akebia quinata Chinese medicinal herb fertilizer is prepared by mixing 16000 g dry chicken manure, 16000 g dry duck manure, 16000 g dry goose manure, 16000 g dry human excrement, 16000 g dry rabbit dung, 20000 g dry barley straw, 16000 g rapeseed meal powder, 10000 g soybean cake powder, 30000 g rice straw powder, 30000 g bean pulp powder, 30000 g grass peat powder, 30000 g lemongrass powder, 20000 g trichlorphon, 16000 g bone meal, 10000 g potash fertilizer, 10000 g zinc fertilizer, 5000 g triadimefon, 50000 g maleic hydrazide, and 15000 g epoxy resin.    USE - Method of preparing Akebia quinata Chinese medicinal herb fertilizer (claimed) used for stimulating Akebia quinata growth.    ADVANTAGE - The method has low cost, utilizes easy to obtain materials, is simple in operation, and can produce organic fertilizer that is rich in nutrients to meet growing requirements of Akebia quinata. The Akebia quinata can grow quickly, and has fleshy leaf and high content of nutrients in the leaf. Further, the obtained fertilizer can improve Akebia quinata yield and reduce fertilizing frequency.
NOVELTY - 4-((4-Methyl-piperazin-1-yl)methyl)benzoic acid is prepared by putting p-chloromethyl benzoic acid, piperazine and alkali in water and heating, reacting the obtained 4-(piperazin-1-ylmethyl)benzoic acid with methanol in the presence of catalyst to obtain 4-((4-methyl-piperazin-1-yl)methyl)benzoic acid and filtering the obtained hydrogen chloride.    USE - Used as antitumour imatinib intermediate    ADVANTAGE - The method is simple, costs low and has high yield.
NOVELTY - A fertilizer plant exhaust gas is provided in absorber with orthophosphoric acid absorption, to obtain diammonium phosphate and ammonium dihydrogen phosphate mixed solution. The mixture is absorbed with lifting pump and ammonia is absorbed. Diammonium phosphate is provided into ammonia stripping column, and organic nitrogen removal agent is added. Diammonium phosphate is decomposed into ammonium dihydrogen phosphate and ammonia. Ammonia in the catalyst is reduced into nitrogen gas, and nitrogen is re-absorbed in waste gas.    USE - Processing of fertilizer plant exhaust gas by ammonia treatment.    ADVANTAGE - The fertilizer plant exhaust gas is efficiently processed.    DETAILED DESCRIPTION - A fertilizer plant exhaust gas is provided in the absorber with orthophosphoric acid absorption, to obtain diammonium phosphate and ammonium dihydrogen phosphate mixed solution. The mixture is continuously absorbed with lifting pump, and ammonia is repeatedly absorbed until completely generate diammonium hydrogen phosphate. The generated diammonium hydrogen phosphate is provided into the ammonia stripping column, and organic nitrogen removal agent is added to 10-30 ppm. Ammonia tower installation is set with bismuth-beryllium-gallium-gadolinium-holmium-thulium-osmium/ alpha -silica catalyst. The steam is introduced to the ammonia, diammonium phosphate is decomposed into ammonium dihydrogen phosphate and ammonia. The ammonia in the catalyst is reduced into nitrogen gas, diammonium phosphate is absorbed into tower top using circulation pump, and nitrogen is re-absorbed in the waste gas.
NOVELTY - Device comprises suction vessel connected to reactor having hydrolysis fermentation, methane producing chambers, and tubes for supplying initial liquid, for removing sludge and for clarifying liquid and biogas. The reactor comprises device for magnetic, light and sound effects on microorganisms; and heaters in the form of convectors located coaxially to methane producing chambers that have immobilization device and enrichment of biogas methane.    USE - For recycling organic waste (claimed).    DETAILED DESCRIPTION - Device comprises suction vessel connected to reactor having hydrolysis fermentation, methane producing chambers, and tubes for supplying initial liquid, for removing sludge and for clarifying liquid and biogas. The reactor comprises device for magnetic, light and sound effects on microorganisms; heaters, made in the form of convectors located coaxially to methane producing chambers that have immobilization device and enrichment of biogas methane. The immobilization device is made from gas water permeable material and longitudinal fibers, supported on element that creates form of immobilization device, located under gas water permeable material, fixed to bottom part of chamber and on opposite side of material and threads are attached to a float, that is connected with top of methane producing chamber by flexible element, restricting movement of immobilization device vertically downwards. The device is modular (unit) or composed of several reactors that have offset in technological process phases.
NOVELTY - The method involves providing a fuel cell with an electrode that contains ionomer. The fuel cell is prepared during preparatory process (S100). Swelling ratio of the ionomer is saturated with respect to the prepared fuel cell during pretreatment process (S110). Parameter values are tested relevant to the swelling ratio of the ionomer with respect to the fuel cell during test process (S120-S150).    USE - Method for manufacturing a fuel cell i.e. polymer electrolyte fuel cell.    ADVANTAGE - The parameter values are tested relevant to the swelling ratio of the ionomer with respect to the fuel cell during test process, so that fall and variation of cold output of the fuel cell after shipment can be suppressed and cold output of the cell can be ensured.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow chart illustrating a fuel cell manufacturing method.'(Drawing includes non-English language text)'    Step for preparing fuel cell during preparatory process (S100)    Step for saturating swelling ratio of ionomer with respect to prepared fuel cell during pretreatment process (S110)    Step for testing parameter values relevant to swelling ratio of ionomer with respect to fuel cell during test process (S120-S150)
NOVELTY - The element has a rounded object that is provided at specific gravity of to-be-torrefied biomass material. Several heat transfer elements heat the to-be-torrefied biomass material to sever as grinding media to reduce particle size of the biomass material. Several features are formed in the surface of the rounded object. The surface features increase the traction between heat transfer elements and to-be-torrefied biomass material.    USE - Heat transfer element.    ADVANTAGE - The power consumption of heat transfer element can be reduced effectively. The particle size of biomass charge can be reduced effectively.    DETAILED DESCRIPTION - The heat capacity of heat transfer element sufficient for several heat transfer elements having total mass. The mass of biomass material are charged in the rotary furnace to heat the biomass material. The cut portions have an angle between inner edges. The heat transfer elements contain steel, stainless steel, bronze, or ceramic material. INDEPENDENT CLAIMS are included for the following:    (1) system for torrefaction and size reduction of biomass material; and    (2) method for torrefaction and size reduction of biomass material.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the rotary furnace.    Rotary furnace (100)    Furnace tube (102)    Heaters (104,106)    Low-rise spiral baffles (108)    Tube entry (110)
NOVELTY - Method (M1) for preparing monosaccharide, involves (a) exposing a biomass to pressurized hot water reaction apparatus in order to selectively decompose the hemicellulose contained in the biomass, beating the solid residue after pressurized hot water reaction, and exposing the beaten solid residue to a saccharification enzyme (primary saccharification), and (b) exposing the primary saccharification product to a solid acid catalyst (secondary saccharification).    USE - The method (M1) and apparatus are useful for preparing monosaccharide (all claimed).    ADVANTAGE - The method enables to provide monosaccharide and ethanol cost-effectively and environmentally-friendly with high yield and good reaction efficiency, where plant waste is used as starting material for biomass ethanol and the amount of enzyme used and the treatment time are reduced during the production of ethanol by saccharification enzyme reaction and fermentation.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method (M2) for preparing ethanol, involves fermenting monosaccharide obtained by the method, and producing ethanol;    (2) monosaccharide preparing apparatus comprising pressurized hot water reaction apparatus which selectively decomposes the hemicellulose which makes pressurized hot water act on biomass, beating system which beats the solid residue obtained from the reaction product of the pressurized hot water reaction apparatus, and enzyme-reaction apparatus which makes saccharogenic amylase act on the solid residue beaten by the beating system, where the apparatus has catalytic reaction apparatus which makes a solid acid catalyst act on the reaction product of the enzyme-reaction apparatus; and    (3) ethanol preparing apparatus comprising the above-mentioned monosaccharide preparing apparatus.
NOVELTY - The apparatus has an electrode assembly (38) comprising upper and lower planar electrodes with an insulator. A permanent magnet includes upper and lower surfaces, and is oriented parallel to the lower electrode, where the lower electrode lies within 0.1 inches of the upper surface of the magnet, and the angle formed between the upper surface of the upper electrode and a surface of water (40) is less than 5 degrees. A gas handling unit (24) comprises a gas separator to separate hydrogen gas, where the gas separator includes a membrane that permits or excludes passage of hydrogen gas.    USE - Apparatus for performing electrolysis of water such as purified water, distilled water, tap water, and/or reclaimed water, to generate hydrogen and oxygen gases from water.    ADVANTAGE - The apparatus enables producing and distributing hydrogen on-site, in an easy and inexpensive manner by utilizing very little energy and liquefaction, transportation, and avoiding delivery costs.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of an electrolysis device.    Container (10)    Openings (12-18)    Gas handling unit (24)    Electrode assembly (38)    Water (40)
NOVELTY - Producing a methane-rich gas comprises (a) producing synthesis gas from biomass, and (b) catalytic conversion of the synthesis gas enriched in hydrogen to form a methane-rich wet gas.    USE - The methane-rich gas is useful as fuel for a fuel cell.    ADVANTAGE - The process provides methane-rich gas using renewable energies such as hydrogen from wind energy or solar energy, hence economical and with reduced emission of carbon dioxide, hence ecofriendly.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view a method for producing a methane-rich gas (Drawing includes non-English language text).    Gasifier (10)    Gas purifying device (12)    Water separator (14)    Methanation reactor (18)    Electrolysis unit. (22)
NOVELTY - Production of renewable fuel involves charging supported catalyst into continuous reactor (10), adding catalyst activating material to activate the supported catalyst, feeding oil or fat, hydrogen and supercritical fluid into the continuous reactor, allowing hydrogenation and hydrodeoxygenation reactions of oil or fat in the supercritical fluid, and collecting renewable fuel as reaction product.    USE - Production of renewable fuel used for diesel engine vehicles.    ADVANTAGE - The method economically and efficiently provides renewable fuel with high yield.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart explaining production of renewable fuel.    Continuous reactor (10)    Preheater (20)    Heaters (30,31)    Mixer (70)    Storage tanks (100-102)
NOVELTY - A gas (b) containing a compound comprising hydrogen and/or hydrogen is introduced to a blast furnace (3). A combustible gas (f) is obtained by separating-removing nonflammable gas (g) from waste gas then discharged from the blast furnace.    USE - Manufacture of combustible gas (claimed).    ADVANTAGE - The method enables manufacture of gas having excellent combustibility. The carbon dioxide is efficiently removed from blast furnace gas.    DESCRIPTION OF DRAWING(S) - The drawing shows the apparatus for manufacturing combustible gas.    Blast furnace (3)    Gas containing hydrogen (b)    Blast furnace gas (c)    Combustible gas (f)    Nonflammable gas (g)
NOVELTY - Combustible composition comprises a heavy fuel and liquid fuels from biomass.    USE - The combustible composition is useful for feeding a furnace or boiler. The tall oil is useful as an additive for the preparation of the fuel composition having a temperature of storage lower than the temperature of storage in the absence of additive (all claimed).    ADVANTAGE - The tall oil provides combustible composition containing the heavy fuel with improved flow and reduced sulfur content.
NOVELTY - Combustible composition comprises a heavy fuel and a liquid fuel from biomass.    USE - The combustible composition is useful for feeding a furnace or boiler. The neutralized oil is useful as an additive for preparing combustible fuel composition having a storage temperature lower than the storage temperature in the absence of additive (all claimed).    ADVANTAGE - The combustible composition avoids solidification and thus can be stored for 3-6 months without heating. The neutralization oil provides the combustible composition containing the heavy fuel with improved flow and reduced sulfur content.
NOVELTY - A catalyst system comprises carbonate species comprising an inorganic carbonate and/or hydrogencarbonate, on an inert support material.    USE - As catalyst system useful for producing or upgrading a biocrude material; or useful in a catalytic pyrolysis process of a lignocellulosic biomass material (claimed).    ADVANTAGE - The present catalyst system used in the pyrolysis of solid biomass material or in an upgrading reaction of biocrude, results in a high liquid yield, low oxygen content, relatively low gas formation, and relatively low coke yield. The support material serves to provide a greater specific surface area than would be possible by using the carbonate species by themselves, and to reduce the water-solubility of the carbonate species.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a catalytic pyrolysis process (P1) involving: contacting a biomass material with the catalyst system at 200-600 degrees C (preferably 300-450 degrees C); and    (2) process (P2) for upgrading a pyrolysis oil involving: contacting the pyrolysis oil with the catalyst system at 200-450 degrees C.
NOVELTY - Combustion promotion method of incinerator (17) in complex facility (11) involves using a fermenter (12) for fermenting biomass and producing biogas, a combustor (15) for combusting the biogas, and an incinerator (17) for incerating waste material. The biogas produced in the fermenter is combusted using the combustor, and obtained combustion exhaust gas of the biogas is blown into combustion chamber (18) to which stoker of the incinerator is provided.    USE - Combustion promotion method of incinerator in complex facility (claimed).    ADVANTAGE - The combustion improvement method for incinerator in complex facility is carried out, such that biogas is effectively used and slow combustion is performed to improve combustion and reduce production of carbon monoxide and nitrogen oxide.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for complex facility.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the complex facility where combustion improvement method for incinerator is carried out. (Drawing includes non-English language text)    Complex facility (11)    Fermenter (12)    Combustor (15)    Incinerator (17)    Combustion chamber (18)    Boiler (23)
NOVELTY - A heat-exchange type pre-reformer (100) comprises a shell side (150) having a channel to which cathode exhaust gas is supplied and through which cathode exhaust gas flows such that heat is exchanged between the cathode exhaust gas and the mixture gas supplied for preforming, a catalyst layer (170) arranged to overlap one area of the shell side and formed to cause the mixture gas for pre-reforming reaction, and a tube side (180) connected to the catalyst layer to overlap the other area of the shell side and formed to pre-reformed mixture gas to exchange heat with the cathode exhaust gas.    USE - Heat-exchange type pre-reformer is used for producing hydrogen for fuel cell e.g. molten carbonate fuel cell.    ADVANTAGE - The heat-exchange type pre-reformer is economical, and has high durability and efficiency. The heat generated from the pre-reformer is controlled.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic structure of heat-exchange type pre-reformer.    Heat-exchange type pre-reformer (100)    Exhaust gas inlet port (110)    Shell side (150)    Catalyst layer (170)    Tube side (180)
NOVELTY - The apparatus has compressing device (20) which compression-molds raw material and sets as compression block. A compression block channel (30) supplies compression block to gasified melting furnace (50). A water vapor supply apparatus (43) supplies water vapor to compression block in compression block channel. A cooling unit (45) cools compression block with which water vapor is supplied, and condenses water vapor. A shielding element (44) shields that water vapor provided in compression block channel and supplied from the water vapor supply apparatus.    USE - Material supply apparatus of gasifier apparatus used for gasifing waste material and biomass as raw material, and obtains fuel gas.    ADVANTAGE - Since the gas seal can be carried out between the inside of a compression block, and a compression block and a compression block channels, the furnace internal pressure of a gas fusion furnace can be operated with a positive pressure. The gas leakage from a material supply apparatus can be prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the gasifier apparatus provided with a material supply apparatus. (Drawing includes non-English language text)    Compressing device (20)    Compression block channel (30)    Water vapor supply apparatus (43)    Shielding element (44)    Cooling unit (45)    Gasified melting furnace (50)
NOVELTY - A combustion apparatus comprises blower outlet (10) in which cover material (8) with grid window part is attached in front-end part, cylindrical burner main body (1) which accommodates biomass solid fuel which consists of short cylinder shape or circular disk-like biocoke with diameter of 20-120 mm and length of 30-200 mm, hot-air supply pipe (2) which supplies heating combustion air of 300-700 degrees C for heating biomass solid fuel in cylindrical burner main body, and fuel injection cylinder part (3) which replenishes biomass solid fuel to base end part side is connect-linked.    USE - A combustion apparatus (claimed).    ADVANTAGE - Hot air is efficiently and stably generated.    DETAILED DESCRIPTION - A combustion apparatus comprises blower outlet (10) in which cover material (8) with grid window part is attached in front-end part, cylindrical burner main body (1) which accommodates biomass solid fuel which consists of short cylinder shape or circular disk-like biocoke with diameter of 20-120 mm and length of 30-200 mm, hot-air supply pipe (2) which supplies heating combustion air of 300-700 degrees C for heating biomass solid fuel in cylindrical burner main body, and fuel injection cylinder part (3) which replenishes biomass solid fuel to base end part side is connect-linked. Blowing hot air of 800-1000 degrees C is injected from blower outlet while forming biomass combustion zone which burns with flame at 1600-2000 degrees C of biocoke. The biomass solid fuel accommodated in upstream of hot-air inflow port of hot-air supply pipe is automatically conveyed one by one by biomass combustion zone with dead weight.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional front view of the combustion apparatus.    Cylindrical burner main body (1)    Hot-air supply pipe (2)    Fuel injection cylinder part (3)    Cover material (8)    Blower outlet (10)
NOVELTY - A method of fractionating bio-oil vapors involves providing bio-oil vapors comprising bio-oil constituents; cooling the vapors in first stage comprising condenser having passages for the vapors separated by heat conducting wall from passages for a coolant, where the coolant in the condenser of the first stage is maintained at constant temperature, set at 75 to 100 degrees C, to condense first liquid fraction of liquefied bio-oil constituents in the condenser; and collecting the liquid fraction of liquefied bio-oil constituents from the condenser of the first stage.    USE - For fractionating bio-oil vapors (claimed).    ADVANTAGE - The method allows for the selective condensation and collection of bio-oil. Oil recovered by conventional process usually contains water and acid which contributes to its poor stability, corrosion during storage, poor combustion performance, and additional cost to upgrade the bio-oil to transportation fuels. The method allows water and acid to be separated from the higher molecular weight organic compounds during the oil recovery process, resulting in a much more usable and valuable oil. The method uses a multistage condensing system where each condenser stage has a unique coolant temperature. Individual condenser coolant temperatures are selected such that the bio-oils condensed in each stage do not congeal on the condenser tube walls, preventing unwanted secondary reactions. This is achieved by using a warm coolant instead of a traditionally-used cold coolant. The condensers are also designed to provide a specific cooling capacity so that the bio-oil collected at each condenser only contained bio-oil fractions having a boiling point above the vapor exit temperature of each condenser.
NOVELTY - The method involves crushing timber and filling crushed timber (H) in the drain hole (44) formed in the bottom portion of a pressurization cylinder (40). The pressure piston (43) is pressurized at pressure of 100MPa and reciprocated inside the pressurization cylinder. The moisture content contained in the crushed timber is drained from the drain hole and dried in first cytoclasis drying process. The crushed timber is injected in molding through-hole and molded to a pellet form.    USE - Manufacturing method of timber pellet.    ADVANTAGE - Since the moisture content contained in the crushed timber is drained from the drain hole, and dried, the requirement of vaporization energy is prevented and the water content can be removed rapidly without consumption of fuel. Hence the timber pellet can be manufactured at low cost.    DETAILED DESCRIPTION - The crushed timber is pressurized at the pressure of 150 MPa or more in the second cytoclasis drying process. The crushed timber is heated at the stoving process and dried. The pressurization cylinder is arranged with the opening in the upper direction.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the drying apparatus for cytoclasis drying process of the manufacturing method of the timber pellet. (Drawing includes non-English language text)    Pressurization cylinder (40)    Pressure piston (43)    Drain hole (44)    Drying apparatus (200)    Crushed timber (H)
NOVELTY - Apparatus comprises a container (10) filled with water, primary and secondary electrodes provided in the container, a power supply unit for supplying direct current power to the primary and secondary electrodes, a switching unit which turns the supply of direct current power on or off and alternates positive and negative polarities of direct current power, a sensing unit for measuring the impedance of the water, and a control unit which receives a detection signal with respect to the impedance of the water from the sensing unit.    USE - Apparatus is used for producing hydrogen water.    ADVANTAGE - The hydrogen water is efficiently produced using the apparatus with improved electrolysis efficiency, and reduced power consumption without polluting the environment.    DETAILED DESCRIPTION - Apparatus comprises a container filled with water, primary and secondary electrodes provided in the container, a power supply unit for supplying direct current power to the primary and secondary electrodes, a switching unit which turns the supply of direct current power on or off and alternates positive and negative polarities of direct current power, a sensing unit for measuring the impedance of the water, and a control unit which receives a detection signal with respect to the impedance of the water from the sensing unit and controls the electrolysis process of the water based on the detection signal.    DESCRIPTION OF DRAWING(S) - The drawing shows the perspective view of apparatus.    Container (10)    Handle (12)    Vent (14)    Cover (20)    Display unit (35)
NOVELTY - Reducible fertilizer is prepared by subjecting mixture of a microorganism or a component of a microorganism with phosphoric acid and/or potassium to a hydrothermal reaction.    USE - The reducible fertilizer is useful for enhancing growth of fruit tree or vegetable chosen from mandarin orange, dekopon citrus, iyokan, apple, persimmon, tomato, cucumber, eggplant, and strawberry.    ADVANTAGE - The fertilizer has excellent affinity for cells from root and leaf surface, thus enables effective absorption of phosphoric acid and potassium, increases yield and size of fruit in tree and can be prepared cost-effectively using abundantly available raw material e.g. waste yeast discharged from foodstuff manufacturing plants, and has low oxidation-reduction potential.
NOVELTY - Water, carbon dioxide, ethane and/OR propylene, and isobutane and n-butane in gas-phase low-purity propane are adsorbed with a molecular sieve zeolite which adsorbs water and carbon dioxide with higher priority than propane, molecular sieve activated carbon which adsorbs ethane and propylene with higher priority than propane, and activated carbon which adsorbs isobutane and n-butane with higher priority than propane. The impurities are separated from the low purity propane, to obtain propane.    USE - Purification of propane used as raw material for silicon carbide semiconductor.    ADVANTAGE - The method efficiently and highly purifies the propane with excellent energy efficiency.    DETAILED DESCRIPTION - Water, carbon dioxide, ethane and/or propylene, and isobutane and n-butane in gas-phase low-purity propane are adsorbed with a molecular sieve zeolite which adsorbs water and carbon dioxide with higher priority than propane, molecular sieve activated carbon which adsorbs ethane and propylene with higher priority than propane, and activated carbon which adsorbs isobutane and n-butane with higher priority than propane. By introducing the gas-phase low-purity propane into a partial condenser (3), propane is condensed in a state in which nitrogen and oxygen are kept in the gaseous phase. Nitrogen and oxygen in the gaseous phase are removed from the partial condenser. The impurities are separated from the low purity propane. An INDEPENDENT CLAIM is included for purification system of propane (1).    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of purification system of propane.    Purification system (1)    Adsorber (2)    Partial condenser (3)    Low purity propane supply source (5)    Highly purified propane collection receptacle (6)
NOVELTY - Steam (207) and a liquid biofuel (109) obtained by thermal decomposition of biomass (101) are supplied to the gasification space (110) in a reaction tube (201), and externally heated through the tube surface for steam reforming reaction (BB) to obtain synthesis gas (211).    USE - Manufacture of synthesis gas for use in synthesis of liquid fuel (claimed) e.g. methanol, gasoline or kerosene used for combustion in burners.    ADVANTAGE - The method enables efficient manufacture of soot-free synthesis gas having a good composition, by using a simple device, thus enabling production of high-quality liquid fuel.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) synthesis-gas manufacturing apparatus;    (2) liquid-fuel synthesis apparatus; and    (3) liquid-fuel synthesis method (212).    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the manufacturing method and apparatus of synthesis gas. (Drawing includes non-English language text)    Biomass (101)    Liquid biofuel (109)    Gasification space (110)    Reaction tube (201)    Steam (207)    Synthesis gas (211)    Liquid-fuel synthesis (212)    Reforming process (BB)
NOVELTY - Producing fuels, comprises: separating lignin from lignocellulose-containing material; hydrolyzing the obtained cellulose-containing material; fermenting the hydrolyzate from the cellulose-containing material to ethanol; separating the lignin-containing phase into a first and a second sub-stream; precipitating and processing lignin from the first sub-stream; catalytically pyrolyzing or depolymerizing the processed lignin in the first sub-stream to gasoline- and diesel-like products; and transferring the second sub-stream to conventional combustion in a soda recovery boiler.    USE - The method is useful for producing fuels for combustion engines from lignocellulose-containing material (claimed).    ADVANTAGE - The method produces fuels from lignocellulose-containing material in a simple and cost-effective manner.    DETAILED DESCRIPTION - Producing fuels from lignocellulose-containing material, comprises: separating lignin from lignocellulose-containing material, where a liquid lignin-containing phase and a solid phase of cellulose-containing material (cellulose and hemicellulose) is produced; hydrolyzing the cellulose-containing material; fermenting the hydrolyzate from the cellulose-containing material to ethanol; separating the lignin-containing phase into a first and a second sub-stream; precipitating and processing lignin from the first sub-stream; catalytically pyrolyzing or depolymerizing the processed lignin in the first sub-stream to gasoline- and diesel-like products; and transferring the second sub-stream to conventional combustion in a soda recovery boiler.
NOVELTY - Treating cellulosic and lignocellulosic biomass, comprises combining a first cellulosic or lignocellulosic biomass (300) that is treated with a microorganism to reduce its recalcitrance, and inducing the production of one or more enzymes by the microorganism by maintaining the microorganism-biomass combination under conditions that allow for the production of the enzyme(s) by the microorganism.    USE - The method is useful for treating cellulosic and lignocellulosic biomass using enzymes produced by genetically engineered microorganisms including a fungus, a bacterium, a yeast or a strain that produces high levels of cellulase, where: the fungus is Trichoderma reesei; the bacterium is Clostridium thermocellum; and the Trichoderma reesei strain consists of RUT-NG14, PC3-7, QM9414 and/or RUT-C30 (all claimed).    ADVANTAGE - The method allows effective and easy treatment of the lignocellulosic materials with high throughput and safety in an economic manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a composition comprising a liquid medium, the cellulosic or lignocellulosic biomass treated to reduce its recalcitrance, the microorganism, and enzymes made by the microorganism.    DESCRIPTION OF DRAWING(S) - The figure shows a flow diagram of a method for treating biomass.    First biomass (300)    Cellulase producing organism (310)    Second biomass (320)    End products. (330)
NOVELTY - A method (M1) for producing a product involves maintaining a combination comprising a liquid medium, a structure or carrier, and a reduced-recalcitrance cellulosic or lignocellulosic biomass disposed within the structure or carrier, under conditions that allow the passage of molecules out of and/or into the structure or carrier.    USE - For producing a product, where the product is selected from a molecule, a protein, a sugar, and/or fuel (claimed).    ADVANTAGE - The method provides improvement in conducting microbiological, biological and biochemical reactions. The method makes monosaccharides available in large quantities and at acceptable purities and prices. The method allows simplification of purification of products (such as e.g. sugars or other products of saccharification or fermentation), and can aid in the maintenance of the level of a metabolite, sugar, or nutrient.
NOVELTY - Gasoline-hydrogen hybrid with onboard hydrogen production, is claimed. The gasoline-hydrogen hybrid does not require second motor compared to hybrid electric vehicle and heavy additional batteries, and is operable without hydrogen filling station network compared to the pure hydrogen motor.    USE - Used as a gasoline-hydrogen hybrid with onboard hydrogen production.    ADVANTAGE - The gasoline-hydrogen hybrid exhibits full power in hertz mode, and can be operable in interurban and on highway.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the arrangement for onboard hydrogen production.    Water (I)    High-pressure electrolyzer (II)    Hydrogen tank (III)    Internal combustion engine (IV)    Light machine (V)
NOVELTY - The apparatus (101) has a solid-liquid separator (10) which separates the low concentration organic waste water (1) whose chemical oxygen demand (COD) value is 1000 mg/L or less into solid-liquid-separation water (2) and thickened sludge (3). A mixing tank (30) mixes the solid-liquid separation water and the souring treated water (4) processed by a souring tank (20), and separates the fermentation gas contained in mixing water. A methane fermentation processing tank (40) performs the methane fermentation treatment of the mixing tank exit water.    USE - Apparatus for processing organic waste water such as domestic waste water and sewage.    ADVANTAGE - The methane fermentation treatment can be performed favorably in the organic waste water processing apparatus, even if the temperature of the low concentration organic waste water is low. Since the fermentation gas is flowed into the methane fermentation processing tank, the generation of the scum in the gas-solid liquid separation unit in the organic waste water processing apparatus can be prevented. The electricity cost and sludge-disposal expense of the organic waste water processing apparatus can be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an organic waste water processing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the organic waste water processing apparatus.    Low concentration organic waste water (1)    Solid-liquid-separation water (2)    Thickened sludge (3)    Souring treated water (4)    Solid-liquid separator (10)    Souring tank (20)    Mixing tank (30)    Methane fermentation processing tank (40)    Organic waste water processing apparatus (101)
NOVELTY - The method involves mixing coconut fiber, cane sugar pulp fiber, sisal fiber, jute fiber and other plant fibers to obtain a mixture. The plant nutrients salt is added to the obtained mixture. Organic binder and inorganic binder are also added to the mixture to obtain the desired product. The organic binder is selected from cassava starch, organic acids, plant resins or cane molasses. The inorganic binder is selected from glycerin, alcohols, water or dust.    USE - Method for obtaining protective blanket and nutrient based-fertilizer.    ADVANTAGE - The method enables to obtain the nutrient based-fertilizer with good quality.
NOVELTY - A system for treatment of biomass comprises: (a) a vessel for mixing an agent with a hydro lysate of the biomass, where reaction between the agent and the hydrolysate causes formation of a first solid phase and a first liquid phase in the vessel, the first solid phase comprising greater than 50% of total lignin and less than 30% of total fermentable sugar in the hydrolysate; and (b) a first unit for separating the first solid phase from the first liquid phase.    USE - The system and the method are useful for treating and pre-treating biomass (all claimed).    ADVANTAGE - The system effectively treats biomass to enhance conversion efficiency from biomass to biofuels, or other useful chemicals.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for pretreatment of biomass, comprising: mixing in a vessel a hydrolysate of the biomass with an agent, where reaction between the agent and the hydrolysate causes formation of a first solid phase and a first liquid phase in the vessel, the first solid phase comprising greater than 50% of total lignin and less than 30% of total fermentable sugar in the hydrolysate.
NOVELTY - Improving anaerobic digestion of manure producing methane gas involves performing centrifugation and/or settlement processing on manure and sludge based on total solid mass ratio of 1:0.5-2, adding mixed material in an anaerobic digestion reactor, inoculating sludge in sewage treatment plant and/or methane gas station, where pH is 7.0-8.2 and total solid (TS) content is 3-13% of ammonia nitrogen is less than 2000 (preferably 100-800) mg/l, stirring to make the mixture, adding inoculated sludge (13000-17000 mg/l) in the reactor, and controlling the feeding pH to 7.2-7.6.    USE - For improving anaerobic digestion of manure producing methane gas (claimed).    ADVANTAGE - The method is simple technique with strong operability and at the same time disposing at least two of organic solid waste, and increased volatile solid yield compared with the single human excrement by 4.7-6.8 times.    DETAILED DESCRIPTION - Improving anaerobic digestion of manure producing methane gas, involves: performing centrifugation and/or settlement processing on the manure and sludge based on the total solid mass ratio of 1:0.5-2, adding the mixed material in an anaerobic digestion reactor, inoculating sludge in sewage treatment plant and/or methane gas station for digested sludge, where the pH value is 7.0-8.2, and the total solid (TS) content is 3-13% of ammonia nitrogen is less than 2000 (preferably 100-800) mg/l, stirring to make the mixture, adding inoculated sludge (13000-17000 mg/l) in the reactor so that the concentration of the material is 50-80 g TS/l, controlling the feeding pH to 7.2-7.6, optionally adjusting nitrogen of the closed anaerobic digestion reactor, where the reaction temperature is 13-57 degrees C, and continuously stirring or mixing.
NOVELTY - Adjusting pH value of marsh gas tank, comprises adding inoculum when the acidification pH of the marsh gas tank is less than 6.3, controlling the acid concentration, adding plant ash or aqueous ammonia when the fermentation concentration is normal, uniformly stirring with fermentation liquid, uniformly stirring clarified lime water with fermentation liquid, measuring pH value, preventing high alkaline conditions by adding 2-3 cm weeds doused with pig or cattle urine via a material inlet to ensure its complete contact with material liquid, and processing until the tank pH value is normal.    USE - The method is useful for adjusting pH value of marsh gas tank.    ADVANTAGE - The method maintains moderate pH value within the marsh gas tanks, and ensures complete fermentation of materials, which satisfies the requirements of marsh gas users.    DETAILED DESCRIPTION - Adjusting pH value of marsh gas tank, comprises: (i) adding inoculum when the acidification pH of the marsh gas tank is less than 6.3, stopping feeding, and controlling the acid concentration; (ii) adding plant ash or aqueous ammonia when the fermentation concentration is normal, where the concentration of aqueous ammonia is controlled at 5% (95 kg water and 5 kg ammonia), and uniformly stirring with fermentation liquid; (iii) adjusting water content using lime water, uniformly stirring 2% clarified lime water with fermentation liquid, and measuring pH value, where clarified lime water is added and stirred if the pH value is low; and (iv) preventing high alkaline conditions (normal operation of the marsh gas tank is affected at pH value of more than 8) by adding 2-3 cm weeds doused with pig or cattle urine via a material inlet to ensure its complete contact with material liquid, and processing for 2-3 days until the tank pH value is normal.
NOVELTY - Gluconic acid solution ion exchange column comprises a column body, whose top is provided with an ion exchange resin layer, which is connected with a feeding pipe and a regeneration liquid pipe. The feeding pipe and the regeneration liquid pipe are respectively provided with a feeding pipe valve and liquid pipe valve. The ion exchange resin layer is connected with a discharge pipe and a drain pipe connected to the ion exchange resin layer via a bidirectional valve. The bottom of the ion exchange resin layer is connected with a backwashing pipe set with a washing pipe valve.    USE - Used as gluconic acid solution ion exchange column.    ADVANTAGE - The device has simple structure and high ion removing ion efficiency.
NOVELTY - Processing kitchen waste comprises (a) generating the fermentation device field for the kitchen waste, placing the kitchen waste into fermentation device field, and fermenting in the presence of a strain; (b) fermenting into fermentation liquid constant-temperature transport vehicle; (c) fermenting into the fermentation tank; and (d) extracting the product and fermentation residue.    USE - The method is used for processing kitchen waste (claimed).    ADVANTAGE - The kitchen waste processing method prevents growth of spoilage bacteria, and prevents secondary pollution, is convenient, and is easy to manage and monitor.
NOVELTY - Treating sewage using intermittent switching distribution process comprises arranging percolation ditches and water distributing tank under earth surface plants, and filling special soil into the percolation ditches.    USE - The method is useful for treating sewage (claimed).    ADVANTAGE - The method allows economical treatment of the sewage with removal rate of chemical oxygen demand (more than 90%) in an eco-friendly manner and without power consumption.
NOVELTY - The device has a first heat exchanger (6) and a second heat exchanger (7) serially connected onto a first-level sewage circulating tube which is connected with a second-level sewage circulating tube through the first heat exchanger. The hot-water outlet tube of a heat-pump water heater is subjected to heat exchange through a gas waste heat recovering device (9) together with a high-temperature gas tube of the biogas generator, and connected with the first-level sewage circulating tube and heat-pump water heater through the second heat exchanger to ensure circulation.    USE - Device for producing biogas.    ADVANTAGE - Waste heat of the biogas generator is used at different temperatures during biogas power generation process. Heat energy can be provided for high or middle temperature anaerobic digestion reaction of organic sewage and waste residue through low-temperature environment heat source technique.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for starting biogas production system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biogas production system.    Anaerobic reactors (1,2)    Heat exchangers (6,7)    Waste heat recovering device (9)    Dehydrating tower (10)    Marsh gas generator (15)
NOVELTY - An alcohol alkaline extracting method of Magnolia officinalis total phenol comprises drying M. officinalis, crushing, screening using 60-100 meshes, adding 10-20 ml alcohol solution having a concentration of 50-70 vol.% to the 1 g powder, subjecting to ultrasonic extraction for 20-40 minutes, centrifuging, filtering, adding 4-8 ml alkali solution having a concentration of 0.01-0.025 N to the 1 g filter cake, subjecting to ultrasonic extraction for 10-20 minutes, centrifuging, filtering, mixing the filtrates, and concentrating the filtrate.    USE - An alcohol alkaline extracting method of M. officinalis total phenol (claimed).    ADVANTAGE - The method is simple, has high extraction efficiency and less energy consumption, and reduces production cost.    DETAILED DESCRIPTION - An alcohol alkaline extracting method of M. officinalis total phenol comprises drying M. officinalis, crushing, screening using 60-100 meshes, adding 10-20 ml alcohol solution having a concentration of 50-70 vol.% to the 1 g powder, subjecting to ultrasonic extraction for 20-40 minutes, centrifuging, filtering, adding 4-8 ml alkali solution having a concentration of 0.01-0.025 N to the 1 g filter cake, subjecting to ultrasonic extraction for 10-20 minutes, centrifuging, filtering, mixing the filtrates, concentrating the filtrate at 60-80 degrees C until the volume is 67-75% of the original volume, adding hydrochloric acid to adjust pH value to 2-3, freeze-drying at 2-6 degrees C for 6-8 hours, washing with water to neutralize, adding organic solvent, extracting, decompressing and concentrating obtained extract, washing with 0.2-0.4 wt.% alkali A, stirring, filtering, concentrating the filtrate, drying, adding hydrochloric acid to adjust pH value to 2-3, setting aside for 4-6 hours to obtain crystals, filtering, and vacuum drying.
NOVELTY - Recycling glyphosate production wastewater of glyphosate and formaldehyde comprises passing undissolved substance impurity through pre-processing filter to obtain filtrate of glyphosate mother liquid, concentrating filtrate of glyphosate mother liquid to processing kettle, slowly adding industrial urea to react, reacting at constant temperature, naturally cooling to room temperature, filtering solid slow release urea for washing with water, washing with water, removing solid in air outlet, and drying obtained solid slow-releasing urea to oven.    USE - Method for recycling glyphosate production wastewater of glyphosate and formaldehyde (claimed).    ADVANTAGE - The method has simple technique, high formaldehyde removing rate, low cost, saves energy and reduces emission.    DETAILED DESCRIPTION - Recycling glyphosate production wastewater of glyphosate and formaldehyde comprises passing undissolved substance impurity through pre-processing filter to obtain filtrate of glyphosate mother liquid, concentrating filtrate of glyphosate mother liquid to processing kettle, increasing temperature to 25 degrees C, slowly adding mol ratio of 0.4:1 industrial urea to react, maintaining temperature and reacting for 2 hours; stirring, reacting for 3 hours at constant temperature, naturally cooling to room temperature, filtering to obtain solid slow release urea and glyphosate filtrate to obtain glyphosate filtrate used directly glyphosate production; and filtering solid slow release urea for washing with water, washing with water, removing solid in air outlet, and drying obtained solid slow-releasing urea to oven.
NOVELTY - Fermenting tobacco stalk to produce marsh gas comprises (1) baking tobacco leaf and stalk into an anaerobic fermenting device for biogas fermentation to obtain biogas, biogas slurry and biogas residue tobacco stalk, (2) purifying marsh gas for generating electricity, (3) carrying out solid-liquid separation of biogas slurry and biogas residue tobacco stalk to obtain the biogas residue, (4) processing tobacco stalk biogas residue using process technique and then drying in a culture medium, and (5) recycling biogas slurry using organic fertilizer.    USE - The method is useful for fermenting tobacco stalk to produce marsh gas (claimed).    ADVANTAGE - The method is capable of simply fermenting the tobacco stalk with good stability in an economical manner.
NOVELTY - Manufacture of fuel cell bipolar plate involves heating chromium solid target, titanium target or tantalum target, connecting bias power to the resultant solid target, supplying reactive nitrogen gas, inert gas or ammonia gas, sublimating and forming chromium nitride, titanium nitride or tantalum nitride layer on stainless steel substrate.    USE - Manufacture of fuel cell bipolar plate (claimed).    ADVANTAGE - The method economically provides fuel cell bipolar plate with high productivity.
NOVELTY - 2-Amino-4-(4-hydroxyphenyl)-3-cyanopyridine derivatives (I) are new. (I) are obtained by selectively oxidizing lignin as raw material to obtain an aromatic aldehyde mixture, rectifying and separating the aromatic aldehyde mixture to obtain aromatic monoaldehyde and performing one-pot four-component reaction by using aromatic ketone, aromatic monoaldehyde, malononitrile and ammonium acetate.    USE - (I) are useful for treating tumor, preferably pancreatic cancer, gastric cancer, liver cancer and lung cancer (claimed).    ADVANTAGE - The method directly utilizes cheap lignin as the raw material, thus it reduces cost; and is more efficient, green and environmentally friendly.    DETAILED DESCRIPTION - 2-Amino-4-(4-hydroxyphenyl)-3-cyanopyridine derivatives of formula (I) are new. (I) are obtained by selectively oxidizing lignin as raw material to obtain an aromatic aldehyde mixture, rectifying and separating the aromatic aldehyde mixture to obtain aromatic monoaldehyde and performing one-pot four-component reaction by using aromatic ketone, aromatic monoaldehyde, malononitrile and ammonium acetate.    R1, R2 = H or CH3;    R3 = H, CH3 or phenyl; and    R4 = phenyl, 4-chlorophenyl, 4-ffluorophenyl, 4-bromophenyl, 4-hydroxyphenyl or 4-hydroxy-2-methoxyphenyl.    An INDEPENDENT CLAIM is also included for preparing (I).
NOVELTY - Xanthan gum prepared by taking 1-5% of xanthan gum solution as raw material, slowly adding 3-6% of calcium chloride and 1-4 parts per million (ppm) of sodium tetraborate with the xanthan gum solution under blending condition, adding 40-80% of ethanol into stirred mixture, continuously stirring the mixture to separate, and drying the separated product with water (10-13%), is claimed.    USE - Used as xanthan gum.    ADVANTAGE - The xanthan gum can be simply and economically prepared with low molecular weight, high quality and narrow molecular weight distribution in an environment-friendly manner.
NOVELTY - Lead-free black plaster comprises a therapeutic medicine and a plaster matrix comprising a vegetable oil and a paste agent as raw materials. The paste agent is zinc oxide or ferroferric oxide.    USE - Used as a lead-free black plaster.    ADVANTAGE - The plaster matrix: is harmless to human body when processing, causes no environmental pollution, does not stimulate skin when used, and contains the matrix fully mixed with the therapeutic medicine; can stimulate nerve endings, reinforce blood circulation, accelerate drug delivery and activate blood circulation; and can be prepared into different external-use plasters.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the lead-free black plaster, comprising either: (a) heating the therapeutic medicine and vegetable oil in a pot, frying, removing dregs, filtering, refining to drop water into bead, then controlling the oil temperature at 220 degrees C, adding zinc oxide to the pot, continuously heating for 2-5 hours until there is no foam black, stopping heating, and collecting paste; or (b) heating the therapeutic medicine and vegetable oil in a pot, refining to drop water into bead, adding ferroferric oxide into the pot, uniformly stirring, collecting paste and soaking the paste in water.
NOVELTY - Mistletoe is extracted, concentrated, and pH-adjusted. A bioenzyme is added and enzymolysis is carried out. The enzymolysis solution is added to a macroporous resin adsorption column and eluted, and the eluent is concentrated, crystallized and filtered to obtain a crude extract. The crude product is dissolved in methanol, added to a polyamide resin column, and methanol gradient elution is carried out. Thin layer chromatography is carried out, and eluent is concentrated, crystallized, recrystallized, and dried to obtain high-purity homoeriodictyol.    USE - Preparation of homoeriodictyol from mistletoe (claimed).    ADVANTAGE - The method enables simple, environmentally-friendly and easy industrial preparation of homoeriodictyol from mistletoe.    DETAILED DESCRIPTION - Mistletoe is crushed, 60-80% ethanol solution is added, and microwave or ultrasonic extraction is carried out 2-3 times. The extracted liquid is concentrated and pH is adjusted to 4-6 using alcohol. A bioenzyme is added and enzymolysis is carried out for 8-10 hours. The enzymolysis solution is added to a macroporous resin adsorption column, elution is carried out using 3-6 times 60-80% ethanol, and the eluent is collected, concentrated, crystallized and filtered to obtain a crude extract. The crude product is dissolved in methanol, added to a polyamide resin column, and methanol solution gradient elution is carried out. Thin layer chromatography is carried out, and high-concentration eluent is concentrated to small volume, allowed to stand, crystallized, recrystallized 2-3 times using ethanol solution, and dried to obtain high-purity homoeriodictyol.
NOVELTY - A compound microorganism additive comprises: denitrifying bacteria with content being not less than 5x106/g; white Aspergillus niger with content being not less than 8x1010/g; and Bacillus subtilis with content being not less than 4x106/g.    USE - The compound microorganism additive is useful for degrading poultry excrement (claimed).    ADVANTAGE - Compared with similar additives, the compound microorganism additive has the advantages of high safety, high efficiency, good specificity, less dosage and the like; and when the additive is used on the breeding sites for degrading the poultry excrement, the goal of zero excrement discharge on the poultry breeding sites can be achieved.
NOVELTY - A vancomycin strain M3-1 Amycolatopsis sp. with the preservation number of CGMCC No. 5238, is new.    USE - The vancomycin strain M3-1 Amycolatopsis sp. is useful for producing vancomycin; and for environment remediation, where the vancomycin strain is provided for bioremediation of pyrimidine salicylic acid pesticide-contaminated soil (all claimed).    ADVANTAGE - Production capacity of the strain is 1.27 times higher than production capacity of the existing reported strain, production performance is stable, and the strain can further be provided for bioremediation of pyrimidine salicylic acid pesticide-contaminated soil so as to effectively improve agricultural production and reduce pesticide residues in the soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for producing vancomycin by using vancomycin strain M3-1 Amycolatopsis sp. fermentation, comprising: carrying out liquid fermentation using seed culture medium comprising: beef extract 3-8 g/L, peptone 8-15 g/L, sodium chloride (NaCl) 3-5 g/L and the pH value is 6.5-7.2, culture condition having the temperature of 25-32 degrees C, the rotating speed 120-200 rpm, culturing for 24-72 hours, the fermentation culture medium is as follows: dextrin 50-100 g/L, potato dextrose agar 100-200 g/L, corn steep solution 15-50 g/L, soybean powder 20-35 g/L, NaCl 1.0-2 g/L, potassium 0.1-0.3 g/L, pH 6.6-7.2, fermenting condition is as follows: the temperature is 26-30 degrees C, the pH is 6.5-8.5, the rotating speed is 80-200 rpm and the culture time is 90-140 hours.
NOVELTY - Polypropylene tail gas and greater than or equal to 3C hydrocarbon component are purified and recycled by subjecting polypropylene tail gas to condensation process to remove high boiling point impurities, subjecting to desulfurization, dearsenication, deoxidation, and decarbonization processes, drying, purifying, and preparing mixed gas with 3C and greater than or equal to 3C hydrocarbon components.    USE - Method of purifying and recycling polypropylene tail gas and hydrocarbon component (claimed).    ADVANTAGE - Purification method is simple, cost and energy consumption are reduced, and recovery rate of propylene is high.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram explaining method of purifying and recycling polypropylene tail gas and hydrocarbon component. (Drawing includes non-English language text).
NOVELTY - Continuous preparation of bio-diesel using waste animal and vegetable oil as raw material, comprises (i) removing the impurities and water in the raw material, (ii) carrying out continuous esterification and reacting in cation exchange resin filled fixed bed reactor, (iii) separating esterification product, (iv) carrying out continuous trans-esterification reaction, and separating in the anion exchange resin filled fixed bed reactor.    USE - The method is useful for continuous preparation of bio-diesel using waste animal and vegetable oil as raw material (claimed).    ADVANTAGE - The method overcomes the problem of equipment corrosion, difficulty in separating product, and production of waste acid solution causing environmental pollution, and solves the problem of not achieving continuous production and other issues; is economical; produces product with high yield; and is environmentally friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of the continuous preparation of bio-diesel.
NOVELTY - The microcomputer has a gas sensor array which is connected with a gas sensor array and A/D converter. A single chip is connected with the A/D converter. An LED display screen and an alarm are connected with the single chip microcomputer. The gas sensor array is provided with an alcohol sensor, methane sensor and a carbon monoxide sensor.    USE - Single chip microcomputer for multi-gas detection system.    ADVANTAGE - The gas sensor array is provided with alcohol sensor, methane sensor and carbon monoxide sensor, hence gas information can be obtained efficiently. The feasible solution can be provided reliably for multi-gas detection system.
NOVELTY - Producing cow dung mixed chicken manure organic fertilizer, involves obtaining cow manure, chicken manure, auxiliary materials and water, uniformly mixing, adding microbial agent, mixing, fermenting the mixture at 60 degrees C for 4-5 days followed at 60 degrees C for 15 days to produce organic fertilizer, subjecting the organic fertilizer to second fermentation for 15-20 days at 40 degrees C to fix phosphorus, potassium and nitrogen, adding water to the fermented organic fertilizer, adding fermented organic fertilizer to the organic fertilizer and fermenting for 7 days to obtain bioorganic fertilizer.    USE - The method is useful for producing cow dung mixed chicken manure organic fertilizer.    ADVANTAGE - The method is simple and convenient to perform, inhibits plant diseases and insect pests, improves soil environment and pH value, and promotes growth of crops.
NOVELTY - A methanol-diesel oil comprises 52-76 wt.% diesel oil, 10-30 wt.% methanol, 5-15 wt.% emulsifier and 1-3 wt.% additive.    USE - Methanol-diesel oil is used as fuel for diesel engine.    ADVANTAGE - The methanol-diesel oil is environmentally-friendly, and prepared with reduced energy consumption.
NOVELTY - Estimating difficulty of biological nitrogen and phosphorus removal in wastewater treatment comprises measuring total nitrogen (TNo), total phosphorus (TPo) and biological oxygen demand BOD5 values in sewage inlet; determining the values according to sewage treatment plant discharge standard; and aging sludge according to design or process data of sewage treatment plant, and denitrifying bacteria by yield coefficient of water.    USE - Method for estimating difficulty of biological nitrogen and phosphorus removal in wastewater treatment.    ADVANTAGE - The method quickly estimates carbon source supply for wastewater treatment.
NOVELTY - A solid fuel is obtained by crushing combustible garbage to 3-100 mm, drying at 100-200 degrees C, mixing garbage with hydroxy-terminated polybutadiene, ammonium perchlorate, nitrocellulose solid particles, and toluene diisocyanate, uniformly stirring, casting the obtained mixture by pressing at 65-72 degrees C, and curing.    USE - Production of solid fuel (claimed).    ADVANTAGE - The method enables production of environmentally-friendly solid fuel, by efficiently using low-calorific-value garbage. The obtained solid fuel contributes to saving of oil, coal, and non-renewable fossil fuel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for solid fuel comprising 16-68 wt.% combustible garbage, 7-16 wt.% hydroxy-terminated polybutadiene, 3-50 wt.% ammonium perchlorate, 0.2-0.8 wt.% toluene diisocyanate, 1.5-7 wt.% nitrocellulose, 0.2-0.8 wt.% plasticizer, 10-30 wt.% stabilizer, and 0.6-3 wt.% potassium nitrate.
NOVELTY - An insecticidal composition comprises dinotefuran and cyantraniliprole at ratios of 1:80-80:1, respectively. It can be prepared into wettable powder or water dispersible granule.    USE - Insecticidal composition.    ADVANTAGE - The composition has low toxicity, high efficiency and enlarged insecticidal spectrum with reduced cost, prolonged lasting period and reduced pollution to environment and plant.
NOVELTY - Preparing Alocasia macrorrhiza nutrition fertilizer, comprising 4-6 wt.% of red flower powder, 2-4 wt.% of purple perilla powder, 2-4 wt.% of Chinese cinnamon powder, 9-11 wt.% of dry goose manure powder, 6-8 wt.% of dry chicken manure powder, 4-6 wt.% of dry duck manure powder, 7-9 wt.% of dry pig manure, 6-8 wt.% of dry rabbit manure, 7-9 wt.% of ground-nut meal powder, 6-8 wt.% of potash fertilizer, 2-6 wt.% of zinc fertilizer, 11-13 wt.% of plant ash powder, 1-3 wt.% of sawdust powder and 2-4 wt.% of broad leaf sawdust, is claimed.    USE - The method is useful for preparing Alocasia macrorrhiza nutrition fertilizer (claimed).    ADVANTAGE - The method economically and rapidly prepares Alocasia macrorrhiza nutrition fertilizer in a simple manner with high yield, good color and improved disease resistance performance.    DETAILED DESCRIPTION - Preparing Alocasia macrorrhiza nutrition fertilizer, comprising 4-6 wt.% of red flower powder, 2-4 wt.% of purple perilla powder, 2-4 wt.% of Chinese cinnamon powder, 9-11 wt.% of dry goose manure powder, 6-8 wt.% of dry chicken manure powder, 4-6 wt.% of dry duck manure powder, 7-9 wt.% of dry pig manure, 6-8 wt.% of dry rabbit manure, 7-9 wt.% of ground-nut meal powder, 6-8 wt.% of potash fertilizer, 2-6 wt.% of zinc fertilizer, 11-13 wt.% of plant ash powder, 1-3 wt.% of sawdust powder, 2-4 wt.% of broad leaf sawdust, 8-12 wt.% of phosphatic fertilizer, 4-6 wt.% of maleic hydrazide, 0.2-0.4 wt.% of broad-spectrum fungicide, 0.2-0.4 wt.% of insecticide, 0.1-0.3 wt.% of multi-effect triazole and 0.1-0.3 wt.% of epoxy resin as raw materials, is claimed.
NOVELTY - Preparing Cyclamen nutrient fertilizer comprises weighing 7-9 wt.% of dry duck dung, 3-5 wt.% of sheep dry manure, 2-6 wt.% of chicken dry manure, 7-9 wt.% of rape straw powder, 6-8 wt.% of Sorghum straw powder, 4-6 wt.% of peanut shell powder, 7-9 wt.% of sesame powder, 6- 8 wt.% of plant ash powder, 7-9 wt.% of wheat straw powder, 8-10 wt.% of loofah stem and leaf powder, 4-6 wt.% of dry thatch powder, 2-4 wt.% of phosphate fertilizer, 10-12 wt.% of sawdust, 4-6 wt.% of sludge, 6-8 wt.% of anilazine, 0.4-0.6 wt.% of paclobutrazol and 0.4-0.6 wt.% of copper sulfate.    USE - The method is useful for preparing Cyclamen nutrient fertilizer (claimed).    ADVANTAGE - The nutrient fertilizer has simple preparation, is cost-effective, provides the Cyclamen with rich nutrition and disease resistance.
NOVELTY - A flamingo flower nutrient fertilizer is prepared by mixing 1-12 wt.% dry dung, 8-10 wt.% dry duck manure, 8-10 wt.% dry chicken manure, 6-8 wt.% rapeseed meal, 10-12 wt.% peanut meal, 10-13 wt.% cottonseed hulls powder, 5-7 wt.% broad bean straw powder, 8-10 wt.% Aloe root powder, 6-8 wt.% multi-effect compound fertilizer, 1-3 wt.% potash fertilizer, 0.1-0.3 wt.% bone meal, 0.1-0.3 wt.% triadimenol, 0.2-0.4 wt.% procymidone, 0.2-0.4 wt.% chlorothalonil, 0.2-0.4 wt.% polyoxin, and 6-8 wt.% maleic hydrazide.    USE - Method of preparing a flamingo flower nutrient fertilizer (claimed).    ADVANTAGE - The method prepares cheap and rich in nutrients fertilizer that lessen withered and deciduous leaves; that improves growth; and having high growth and development rate, strong growing power, good disease-resistant performance, and high large bud and flower production.
NOVELTY - A cephalosporin antibiotics 7-phenylacetamido-3-chloromethyl-3-cephem-4-carboxylic acid p-methoxybenzyl ester (GCLE) nucleus, is prepared by performing peroxyacetic acid oxidation on penicillin G potassium salt to obtain penicillin sulfoxide; performing esterification reaction on penicillin sulfoxide and p-methoxy benzyl chloride to obtain penicillin sulfoxide ester; and performing ring-opening reaction between penicillin sulfoxide ester and 2-mercapto-benzothiazole to obtain nitrogen heterocyclic butanone sulfinic acid intermediate.    USE - Method for preparation of cephalosporin antibiotics mother nucleus GCLE (claimed).    ADVANTAGE - The method has high safety, efficiency, and yield; and is environment-friendly.    DETAILED DESCRIPTION - Preparing cephalosporin antibiotics GCLE nucleus comprises:    (A) performing peroxyacetic acid oxidation on raw material penicillin G potassium salt to obtain penicillin sulfoxide using potassium carbonate as acid-binding agent;    (B) performing esterification reaction on penicillin sulfoxide and p-methoxy benzyl chloride in dimethyl formamide to obtain penicillin sulfoxide ester;    (C) performing ring-opening reaction between penicillin sulfoxide ester and 2-mercapto-benzothiazole using a ring protection agent to obtain nitrogen heterocyclic butanone sulfinic acid intermediate; and    (D) adding the nitrogen-containing heterocyclic butanone sulfinic acid intermediate with a chlorinating agent and placing in ammonia environment to obtain cephalosporin antibiotics GCLE nucleus.
NOVELTY - The invention relates to a plant cloning fertilizer composition and a manufacturing method thereof. The plant cloning fertilizer composition of the invention comprises 50-70wt% of naphthalene acetic acid, 100-200wt% of water, 30-50wt% of phosphor, and 2000-3000wt% of talcum powder. The manufacturing method of the plant cloning fertilizer composition includes the main steps of: dissolving the naphthalene acetic acid in the water to form a solution; slowly stirring the solution with the talcum powder by adding the solution in the talcum powder so that the talcum powder is uniformly absorbed with the solution thereon; and finally slowly stirring the phosphor with the talcum powder that is absorbed with the naphthalene acetic acid. With applying the plant cloning fertilizer composition of the invention on roots of the plants that are to be grafted and cut for nursing or to be mixed with the soil, the plant may be triggered to have adventitious roots, thereby raising cut survival rate of the plant, promoting a languish plant to clone and bloom, and increasing the fruiting rate and preventing fruit drop before reaping. Accordingly, the plant cloning fertilizer composition of the invention can be provided for fertilization applications of the agricultural or ornamental plants.
NOVELTY - A bacteria, preferably Thermobifida fusca strain I-14 (FERM P-22201) or its mutant, is new.    USE - The bacteria are used in microbial mixture and microbial bed for decomposing organic matter and processing organic waste, which is used for manufacturing organic fertilizer (all claimed).    ADVANTAGE - The microbial mixture has starch decomposition activity, xylan decomposition activity, cellulose decomposition activity, and proteolysis activity as it decomposes organic waste containing cellulose, xylan, and starch at high temperature. The organic fertilizer can be obtained cost-effectively.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) microbial mixture comprising the bacteria, preferably T.fusca I-14 strain and Bacillus thermochitosensis I-8-5 strain (FERM P-22202) or its mutant; (2) method (M1) for processing organic waste, involves contacting the microbial mixture to organic material decomposition; (3) organic fertilizer obtained by performing the above-cited method (M1); (4) method (M2) for manufacturing organic fertilizer, involves performing steps in method (M1); and (5) microbial bed comprising the above-cited bacteria or the microbial mixture.
NOVELTY - Plant disease control agent comprises magnesium oxide obtained by baking magnesium hydroxide at 400-1000 degrees C.    USE - The agent is useful for controlling plant disease, e.g. tomato botrytis disease.    ADVANTAGE - The agent is environmentally-friendly and can be applied through all parts of the plant.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for controlling plant disease, which involves using the above-mentioned plant disease control agent.
NOVELTY - Synthesizing a biofuel containing butanol from sugarcane bagasse, comprises pre-treating sugarcane bagasse by steam explosion at a temperature of 220-230 degrees C for a curing time of 2-5 minutes and a compression pressure of 3-3.5 MPa, hydrolyzing the bagasse with cellulase enzyme to obtain a hydrolysis solution, performing anaerobic fermentation to the hydrolysis solution with Clostridium acetobutylicum strain to obtain a reaction solution containing butanol, and extracting the reaction solution by membrane vapor separation to obtain a liquid containing butanol.    USE - The method is useful for synthesizing a biofuel containing butanol from sugarcane bagasse (claimed).    DETAILED DESCRIPTION - Synthesizing a biofuel containing butanol from sugarcane bagasse, comprises pre-treating sugarcane bagasse by steam explosion at a temperature of 220-230 degrees C for a curing time of 2-5 minutes and a compression pressure of 3-3.5 MPa, hydrolyzing the bagasse with cellulase enzyme to obtain a hydrolysis solution, performing anaerobic fermentation to the hydrolysis solution with Clostridium acetobutylicum strain to obtain a reaction solution containing butanol, and extracting the reaction solution by membrane vapor separation to obtain a liquid containing butanol, where a ratio of acetone to butanol is less than one half , and a ratio of ethanol to butanol is less than \6.
NOVELTY - Synthesizing and purifying indirubin-3'-oxime derivatives (I) from Strobilanthes cusia, comprises preparing an indirubin-rich powder from leaves of Strobilanthes cusia having high content of indirubin as a starting material, synthesizing (I) directly from the indirubin-rich powder in the presence of commonly used solvents at a low temperature, and purifying (I).    USE - (I) are useful for inhibiting growth of cancer and metastatic cancer cells and treating cancer and other diseases. No biological data given.    ADVANTAGE - The method allows simple synthesize of (I) from the indirubin rich leaf powder of Strobilanthes cusia with less toxic and without performing indirubin purification. (I) can be simply and effectively purified based on phase transition and purification stages in different conditions without using chromatography methods and chemical agents to remove undesired impurities in an environmentally friendly manner.
NOVELTY - The device has a burner that is mounted on a base. A feed hopper is located on the burner. A gas outlet is located in a lower portion of burner. A fan is located in an upper portion of the burner near the feed hopper to supply air from outside into the burner in a direction similar to the path of rice husks from the feed hopper. An ash container is located inside the base and mounted to the burner in an airtight manner.    USE - Device for producing combustible gas from biomass resource such as rice husk.    ADVANTAGE - By locating the fan in the upper portion of burner near the feed hopper, the combustible gas can be produced from biomass resource such as rice husks in a continuous manner.
NOVELTY - The method involves subjecting waste organic material to anaerobic digestion by microorganisms in a biogas production facility, and removing impurities from crude biogas to yield a combustible fluid feedstock. A first amount of liquid transportation or heating fuel is produced by combining a second amount of renewable hydrogen derived from a third amount of combustible fluid feedstock with crude oil derived liquid hydrocarbon and an additional effective amount of hydrogen of sufficient quantity to desulfurize the crude oil derived liquid hydrocarbon.    USE - Method for transforming microbially digesting waste organic material to produce a renewable or partially renewable liquid transportation or heating fuel e.g. petrol, diesel, heating oil and jet fuel (all claimed), for fuel cell, motor vehicle engines, and non-road vehicles or non-road engines. Uses include but are not limited to plants, vegetation, municipal waste, animal waste, animal byproducts, manure, sewage sludge, food waste, food processing waste, recycled cooking and trap grease and agricultural residues such as corn stover and wheat straw.    ADVANTAGE - The method enables utilizing the energy in waste organic material to increase the renewable energy content of transportation fuels used commercially in automobiles, thus using renewable biomass to replace or reduce the quantity of fossil derived energy present in transportation and heating fuels, and hence providing a simple and cost effective system.    DETAILED DESCRIPTION - The biogas production facility is a landfill, a waste treatment facility or a manure digestion facility. An INDEPENDENT CLAIM is also included for a method for producing a combustible fluid feedstock for use in producing a transportation or heating fuel.