NOVELTY - Cationic antimicrobial agent comprises methyl compound (I).    USE - The cationic antimicrobial agent is useful in antimicrobial composition which is used as fabric softener, detergent, cleaning agent, medicine, food additive, aromatic agent, cosmetic material, quasi-drug or agricultural chemical composition, preferably cleaning agent chosen from shampoo, soap and body cleanser (all claimed), for exhibiting activity against bacteria, fungi and virus and manufacturing hair-dye, deodorizing agent, hair removal agent, and dentifrice. The antimicrobial agent is in the form of liquid, suspension, granule, acida, syrup, aerosol, ointments, emulsion, eye drop, injection, spirit, capsule, cream or pill.    ADVANTAGE - The agent is cost-effective and environmentally-friendly, and can be prepared simply.    DETAILED DESCRIPTION - Cationic antimicrobial agent comprises methyl compound of formula: R-N+(- CH3)(-CH3)-A (I).    R=linear or branched 6-18C alkyl and/or alkenyl;and    A=CHCH2(O), CHOHCH2OH, CH2CHCHOH, CH2CHCH2(O) and/or CH2CHOHCH2OH.
NOVELTY - Converting a carbon source into a hydrocarbon or hydrocarbon precursor via a microorganism catalyzed aerobic reaction, comprises cultivating the microorganism in the presence of the carbon source and oxygen, where the cultivation is carried out in a reaction vessel having a capacity of greater than or equal to 2000 l and the reaction vessel comprises an aeration system for supplying oxygen to the microorganism during its cultivation.    USE - The method is useful for converting a carbon source into a hydrocarbon or hydrocarbon precursor via a microorganism catalyzed aerobic reaction, where the hydrocarbon or hydrocarbon precursor is useful as biofuel component (all claimed), such as a gasoline, kerosene or diesel fuel component, and the hydrocarbon is alkanes, alkenes, cyclic hydrocarbons, naphthenic hydrocarbons or aromatic hydrocarbons.    ADVANTAGE - The method economically provides hydrocarbons in a continuous or batch wise manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) an apparatus for converting the carbon source into the hydrocarbon or hydrocarbon precursor via the microorganism-catalyzed aerobic reaction, comprising the reaction vessel, and the aeration system for supplying oxygen to the vessel;    (2) a method-1 for constructing apparatus, comprising fitting the reaction vessel with the aeration system for supplying oxygen to the vessel; and    (3) a process for producing a biofuel component, comprising using the conversion method and/or apparatus in order to generate the hydrocarbon or hydrocarbon precursor which is suitable for use as, or conversion to, a biofuel component.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic diagram of an apparatus.    Reaction vessel (1)    Cultivation mixture (2)    Pump (3)    Conduit (4)    Air source. (5)
NOVELTY - Isolated and purified microalga Scenedesmus sp. Novo obtained from an alga collected at latitude 35.769 and longitude 106.692, or their progeny, capable of producing a biomass of 10.41x 106 cells per ml and at least 4 mu g/ml of carotene in a culture including tris-acetate-phosphate (TAP) medium under outdoor growth conditions comprising temperatures reaching greater than or equal to 40 degrees C, is new.    USE - The isolated and purified microalga Scenedesmus sp. Novo is useful: for inhibiting growth of microorganisms including bacteria, viruses, parasites, and fungi (all claimed); in the production of algal biofuels, fertilizers, dietary nutrients, pharmaceuticals, polymers, biofilters to remove nutrients and other pollutants from wastewaters; and in space technology, laboratory research system and many biotechnological applications. No biological data given.    ADVANTAGE - The isolated and purified microalga Scenedesmus sp. Novo is extremophilic, and is capable of producing: a biomass of 10.41x 106 cells per ml; at least 4 mu g/ml of carotene under outdoor growth conditions comprising temperatures reaching greater than or equal to 40 degrees C; at least 5.8 mu g/ml of chlorophyll- alpha (claimed); and high levels of lipids.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a culture of the isolated and purified microalga cultivated in nutrient-enriched waste water;    (2) a dried algal biomass produced by drying microalgae, where the dried algal biomass has less than 5% water content; and    (3) culturing and harvesting extremophilic microalgae.
NOVELTY - The method comprises exposing the biological sludge to microwave irradiation at a power density of 10 W/ml for 10-30 seconds. The microwaves have a frequency of 0.915-2.45 GHz. An enzyme is mixed with the sludge before microwave irradiation exposure. A flocculating agent is mixed with the sludge following microwave irradiation. The method further comprises subjecting the sludge to dewatering by mechanical units. The microwave irradiation is applied as continuous wave irradiation.    USE - The method is useful for treating biological sludge with microwave irradiation to dewater the sludge (all claimed).    ADVANTAGE - The method allows treatment of the biological sludge with microwave irradiation in an economical manner thus improving dewaterability, turbidity/flocculation, and settlability and coagulation effect of the sludge.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of dewatering sludge.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic view of a belt press/centrifuge apparatus for exposing sludge to microwave irradiation.
NOVELTY - Oil comprises substantially no sterol glycosides, and material obtained from a culture comprising one or more oleaginous microorganisms.    USE - The oil is useful for the production of a biofuel (claimed), which is useful: in compression engines; as transportation fuels in land vehicles, marine vehicles and aviation vehicles; and for power generation such as raising steam, exchanging energy with a suitable heat transfer media, generating syngas, generating hydrogen and making electricity.    ADVANTAGE - The oil produces the biofuel with high yield and quality in an economical manner. The biofuel has reduced carbon emissions to the atmosphere, and is substantially free of sterol glycosides.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a biofuel, comprising substantially no sterol glycosides, and at least one fatty acid 1-4C alkyl ester derived from an oil obtained from a culture comprising one or more oleaginous microorganisms;    (2) a method-I of producing a feedstock for the production of the biofuel, comprising growing a culture of an oleaginous microorganism in a presence of a carbon source;    (3) a method-II of producing a fatty acid derivative composition, comprising growing a culture of an oleaginous microorganism in the presence of a carbon source, lysing the microorganism to produce a lysate, and isolating an oil from the lysate;    (4) a fatty acid methyl ester composition comprising substantially no sterol glycosides, and at least one fatty acid methyl ester derived from the oil obtained from a culture;    (5) a fatty acid triglyceride composition comprising substantially no sterol glycosides, and at least one fatty acid triglyceride obtained from the culture; and    (6) a production system comprising a fatty triglyceride production vessel adapted to receive a carbon source, and a culture of an oleaginous microorganism.
NOVELTY - Preparing an anthracene-9-carbonitrile compounds (T1) involves reacting solution of anthracene compound with a saturated solution of carbon dioxide (CO2) under a potential of -1.5 V to -2 V; adding an alkylating agent, in a concentration in 2-50 fold molar excess; and bubbling the resultant solution under inert gas.    USE - For preparing anthracene-9-carbonitrile compounds which are used as starting materials for the synthesis of spiro-(9,10-dihydroanthracene)-9,3'-pyrrolidine (SPAN) derivatives, particularly alkyl-10-cyano-9,10-dihydro-9-anthracenecarboxilate if compound (I) is used as a starting material, and alkyl-10-cyano-10-methyl-9-hydro-9-anthracenecarboxilate if compound (II) is used as a starting material (claimed), where the SPAN derivatives are used as antidepressant and anti-anxiety agents.    ADVANTAGE - The process is environmentally friendly; provides good yields; and uses easily available and cheap starting reactants (10-substituted-9-cyanoanthracene) and CO2.    DETAILED DESCRIPTION - Preparing an anthracene-9-carbonitrile compound (T1) selected from compounds of formulae (I)-(III), involves (a) reacting a solution of anthracene compound (i) with a saturated solution of carbon dioxide (CO2) under a potential of -1.5 V to -2 V; (b) adding an alkylating agent Y'X', in a concentration in 2-50 fold molar excess; and (c) bubbling the resultant solution under inert gas.    Y'=alkyl or benzyl;    R1=H or methyl;    X'=I, Br or Cl.    An INDEPENDENT CLAIM is included for new intermediate of compound (I) and (II).
NOVELTY - Catalyst comprises iridium oxide and a high surface area inorganic oxide, having a Brunauer, Emmett and Teller (BET) surface area of 30-200 m2/g, where the inorganic oxide is present at 25-70 wt.%.    USE - The catalyst is used: as anode catalyst in electrodes, catalyst-coated membranes and membrane-electrode-assemblies for polyelectrolyte membrane water electrolyzers; for water electrolysis; in regenerative fuel cells, sensors, electrolyzers and other electrochemical devices; and in polyelectrolyte membrane fuel cells for improvement of start-up/shut-down characteristics (all claimed).    ADVANTAGE - The catalyst: has an electrical conductivity (as detected by powder measurements) of greater than 0.01 S/cm, preferably greater than 0.1 S/cm (claimed) and high current density, and leads to a lower specific energy consumption per volume of hydrogen produced, and thus offering higher hydrogen production rates at a given cell voltage; utilizes the inorganic oxides which provide a long lifetime and high endurance of the polyelectrolyte membrane electrolyzer unit; exhibits improved performance and stability; and allows reduced precious metal loadings.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for manufacture of the catalyst, comprising: dissolving an iridium precursor compound and optionally a ruthenium precursor compound in the presence of an inorganic oxide having a BET surface area of 30-200 m2/g,in an aqueous solution; precipitating the iridium oxide (optionally in combination with the ruthenium oxide) by adjusting the pH of the mixture to 6-10; separating and drying the catalyst; and heat treating the catalyst at 300-800 degrees C.
NOVELTY - An alcohol is fermented by adding 4x 10-8-4x 10-2 mg% (w/v) amygdalin per first mash capacity of alcohol fermentation ingredient while performing alcoholic fermentation using yeast or Zymomonas genus bacteria.    USE - Fermentation of alcohol for drinks and fuels.    ADVANTAGE - The method is efficient and saves energy. Fermentation time is short, and capacity utilization efficiency and labor productivity are improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph of the relationship of carbon-dioxide-gas generation amount and fermentation time. (Drawing includes non-English language text).
NOVELTY - Alcohol fermentation promoting agent comprises clathrate compound which is obtained by contacting cyclodextrin and fruit or fruit skin of Japanese pepper (Zanthoxylum piperitum) or volatile component of fruit.    USE - The alcohol fermentation promoting agent is useful for preparing alcohol (claimed) which is useful as fuel and drink.    ADVANTAGE - The alcohol fermentation promoting agent prepares alcohol cost-effectively, as it does not use expensive apparatus (e.g. bioreactor) and does not require labor. The method prevents contamination and enables to save resources and consumes less energy. The agent stably prepares alcohol. The alcohol is prepared in a short period of time and can be mass produced easily. The fermentation capacity of the microorganism is increased.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for fermenting alcohol, involves adding the above-mentioned 0.04-2 weight/volume% alcohol fermentation promoting agent to raw material of alcohol fermentation before alcoholic fermentation starts; and    (2) alcohol, obtained by the above-mentioned method.
NOVELTY - An alcohol fermentation promoter contains adsorbate which allows fruit skin of Japanese pepper (Zanthoxylum piperitum) or volatile component of fruit to be adsorbed to ion exchange resin or gel filtration material.    USE - Alcohol fermentation promoter for fermentation of alcohol (claimed) used for fuel.    ADVANTAGE - The alcohol fermentation promoter exhibits excellent alcohol fermentation enhancement effect. Fermentation ability of alcohol fermentation microorganisms can be increased, fermentation rate can be improved, fermentation period can be shortened, cost reduction can be attained, and labor productivity can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for alcohol fermentation method which involves adding alcohol fermentation promoter in alcohol fermentation ingredient and fermenting, wherein addition amount of alcohol fermentation promoter is 0.04-2% (w/v) with respect to mash capacity of first alcohol fermentation ingredient.
NOVELTY - Quality determination of deodorizing-type biosolid fuel product involves coating activated charcoal powder on a surface of biomass feedstock dry granular material obtained by drying and granulating sewage sludge, obtaining deodorizing-type biosolid fuel product, measuring surface color of obtained deodorizing-type biosolid fuel product in real time by spectroscopy chromatometer, determining degree of adhesion of activated charcoal powder for deodorizing of biosolid fuel product surface, and determining quality of the resultant deodorizing-type biosolid fuel product.    USE - Quality determination of deodorizing-type biosolid fuel product (claimed).    ADVANTAGE - The method efficiently and stably enables quality determination of deodorizing-type biosolid fuel product.    DETAILED DESCRIPTION - Quality determination of deodorizing-type biosolid fuel product involves coating activated charcoal powder on a surface of biomass feedstock dry granular material obtained by drying and granulating sewage sludge, obtaining deodorizing-type biosolid fuel product, measuring surface color of obtained deodorizing-type biosolid fuel product in real time by spectroscopy chromatometer based on Lasteriskaasteriskbasterisk colorimetric system of International Commission on Illumination, determining degree of adhesion of activated charcoal powder for deodorizing of biosolid fuel product surface, and determining quality of the resultant deodorizing-type biosolid fuel product.
NOVELTY - Production of octenes from ethylene, involves: a) dimerizing ethylene to butenes in the presence of catalyst; and dimerizing the butene to octene in the presence of a catalyst.    USE - For production of octenes from ethylene (claimed) which is used as a component of automobile fuels and/or as a feed for a hydroformylation process for the synthesis of aldehydes and alcohols.    ADVANTAGE - Using a fluid catalytic cracking C4 cut or steam naphtha cracking cut is that there is no need to carry out any purification. In particular, isobutene does not have to be eliminated, because the n-butenes obtained from dimerization do not contain any of it. In fact, the process can be carried out without a purification step between the ethylene dimerization step and the butenes dimerization step. In addition, the butenes obtained by the dimerization of ethylene are free of butane, which has the advantage of not diluting the olefinic reagent in the feed for the dimerization process. The butenes formed by dimerization do not contain oxygen-containing impurities. Thus, they do not have to be purified.
NOVELTY - A precursor containing sulfur and molybdenum is pulverized, and a material including a solvent is mixed with pulverized precursor. A catalyst is prepared by providing the mixed material into a reactor and reacting the mixed material under a high-pressure hydrogen gas atmosphere, and prepared catalyst is activated, to obtain direct methanation catalyst.    USE - Production of direct methanation catalyst (claimed) used for producing synthetic natural gas.    ADVANTAGE - The direct methanation catalyst is economically produced with high dispersibility, specific surface area, poisoning resistivity and reaction durability, and improved direct methanation efficiency.
NOVELTY - System comprises (a) a vessel including a solid inlet, a solid outlet, a liquid inlet and a liquid outlet, where a biomass enters the vessel through the solid inlet and flows in the vessel from the solid inlet towards the solid outlet, and liquid enters the vessel through the liquid inlet, flows in the vessel from the liquid inlet towards the liquid outlet and exits the vessel through the liquid outlet as a hydrolysate, the liquid contacts the biomass and the biomass flows inside the vessel, and (b) a unit for conveying the hydrolysate from the liquid outlet back into the vessel.    USE - The system is useful for pretreating a biomass (claimed) and increasing carbohydrate and lignin concentration in hydrolysate of biomass pretreatment to improve the conversion efficiency of biomass to biofuels, such as ethanol.    ADVANTAGE - The system pretreats the biomass with reduced energy and water consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for pretreating biomass, comprising (a) mixing the biomass with a first inflow in a vessel, where the first inflow is a liquid and the biomass and the first inflow flow in opposite directions in the vessel, (b) obtaining a first effluent as the first inflow exits the vessel after making contact with the biomass and (c) allowing the first effluent to pass through a conduit and enter the vessel as a second inflow.
NOVELTY - Preparing glycerol tert butyl ether from glycerol comprises: (a) reacting tert butanol and a heterogenous catalyst at temperature ranging between 90 and 100 degrees C with stirring ranging between 600 and 800 rpm for a period ranging between 15 and 30 minutes to obtain isobutylene; and (b) passing isobutylene as obtained in step (a) over glycerol and a heterogenous catalyst at temperature ranging between 40 and 90 degrees C, autogenous pressure, at 500-1100 revolutions per minute (rpm) and for a period ranging between 8 to 16 hrs to obtain glycerol tert butyl ether.    USE - The process is useful for preparing glycerol tert butyl ether from glycerol. The glycerol tert butyl ether is useful for improving cold flow property of biodiesel; and is used as oxygenate fuel to improve emission performance of diesel, gasoline biodiesel and blends of these (all claimed).    ADVANTAGE - Improved process for production of bio-oxygenates, particularly for converting glycerol, a byproduct of biodiesel process, to glycerol tertiary butyl ethers, is provided.
NOVELTY - Preparation of darifenacin hydrobromide involves reaction of 3-(S)-(+)-(1-carbamoyl-1,1-diphenylmethyl) pyrrolidine or its acid addition salt with 5-(2-bromoethyl)-2,3-dihydrobenzofuran in an organic solvent, optionally in presence of water and in presence of potassium carbonate at 60-80 degrees C; cooling the reaction mixture and filtering; concentrating the organic layer, dissolving the residue containing darifenacin in acetone and treating with hydrobromic acid.    USE - For preparation of darifenacin hydrobromide (claimed) used for oral treatment of urinary incontinence.    ADVANTAGE - The process provides darifenacin hydrobromide having impurity level conforming to regulatory specifications. The formation of the impurities is significantly brought under control resulting in darifenacin hydrobromide with high purity and good yield. The process is convenient and industrially scalable process which avoids use of chromatographic separations or successive crystallizations to get rid of the impurities generated during the preparation of darifenacin hydrobromide.
NOVELTY - Method for preparing crystalline form A of lacosamide, involves (a) providing a solution of lacosamide in an organic solvent, (b) optionally, filtering the solution to remove any particles, (c) maintaining the solution at low temperatures, (d) optionally, combining the solution with an antisolvent, and (e) isolating the crystalline form A of lacosamide.    USE - The method is useful for preparing crystalline form A of lacosamide which is useful in pharmaceutical composition (all claimed) as anticonvulsants, and for treating partial-onset seizures and CNS diseases. The pharmaceutical composition is in the form of granule, pellet, powder, tablet, injection, oral solution, syrup, suspension, dispersion or emulsion.    ADVANTAGE - The crystalline form A of lacosamide prepared by the method has excellent stability and bioavailability, and is environmentally-friendly and cost-effective. The crystalline form A of lacosamide is chirally pure lacosamide having 0.1-1% S-isomer (as determined using chiral HPLC). The crystalline form A of lacosamide has purity of 99.8% or more, and contains no single impurity (in amounts greater than 0.1% by HPLC). The crystalline form A of lacosamide has particle size distribution of 100 mu m or less, preferably 20 mu m or less.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for crystalline lacosamide form A, which is obtained by the above-mentioned method, where the crystalline lacosamide form A has characteristic X-ray diffraction (XRD) peaks at 8.4, 9.6, 13.2, 14.3, 16.5, 17.8, 18.6, 19.9, 20.1, 23.2, 24.9 and 25.8 plus minus 0.2 degrees 2- theta .
NOVELTY - This utility model claims a kind of urea-formaldehyde condensed water recycling treatment device, comprising a recycling tank, reaction kettle and urea-formaldehyde caking agent melting groove are connected with the recycling pool, urea formaldehyde condensed water recycling and treating device further comprises a water tank and , the condensed water in the recovery tank into the water tank through the water pump and pumping into a , boiler is connected with a water tank. The beneficial effect of the utility model is that: the device for recycling the steam generated by heating the condensed water and the recycled condensed water fully, then adding the acid solution to neutralize the alkaline composition in water, a soft water tank improves the water quality, at the same time, fully considers the amount of water, the water also can be used in the urea-formaldehyde into the reaction kettle for dissolving urea, the device reduces the environmental pollution and saving the coal, it has simple structure, safety and reliability, saving cost;
NOVELTY - Preparation of fuel from biomass (waste) comprises collecting agricultural wastes, drying, crushing, mixing, forming, drying and packaging.    USE - Method for preparing fuel for use in stoves as coal alternative (claimed).    ADVANTAGE - The fuel has high thermal energy and long combustion time.
NOVELTY - Oil tank temperature control system comprises an oil tank, a steam coil pipe located in the tank, a pneumatic control valve, and a distributed control system provided between the oil tank and the pneumatic control valve. A steam outlet and a steam inlet of the steam coil pipe are connected with a steam pipe. The steam inlet of the steam coil pipe is connected on the steam pipe provided with the pneumatic control valve.    USE - Used as an oil tank temperature control system.    ADVANTAGE - The temperature control system can control the raw material oil at a stable temperature range in biodiesel production to avoid pipeline blockage of the subsequent section, reduces coke and carbon deposition resulting from esterification reaction process and product separating and purifying process, and ensures prolonged operation period.
NOVELTY - The device has a combustion chamber (2) connected with a gasification furnace (1) and a boiler device (3). A coal saving device is connected with a gasification furnace. The gasification furnace and the boiler device are provided with water inlet pipes, respectively. The water inlet pipe of the gasification furnace is connected with the water inlet pipe of the boiler device. The boiler device has an upper boiler barrel (31), a lower boiler barrel (32) and a water-cooling wall pipe. A fire grate (8) is arranged at a lower end of an ash outlet (9). A gas outlet is connected with the chamber.    USE - Biomass gasification furnace combustion device for use by a farmer.    ADVANTAGE - The device requires less space. The utilization of the water-cooling wall pipe reduces the energy consumption. The device reduces the cost by 40 % than directly using natural gas, reduces cost by more than 150% than using oil as compared to coal, and reduces sulfur emission to meet the requirements of environment protection and clean production, at the same time it increases farmer income.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic side view of a biomass gasification furnace combustion device.    Gasification furnace (1)    Combustion chamber (2)    Boiler device (3)    Fire grate (8)    Ash outlet (9)    Upper boiler barrel (31)    Lower boiler barrel (32)
NOVELTY - Accurate pair-roller synchronous powerful extrusion forming biomass granulator comprises two roller mold pressing wheels and two transmission groups, where two roller mold pressing wheels and two transmission groups are matched with each other, and each roller mold pressing wheel comprises two rollers and a circular mold wheel. A coaxial connecting gear is connected to each roller mold pressing wheel. Each transmission group comprises two-stage reduction synchronous gear, two-stage reduction large gear, belt wheel, first stage reduction small gear, synchronous gear and speed regulating motor.    USE - The extrusion forming biomass granulator is useful for producing wood pellets.    ADVANTAGE - The granulating machine is simple in wood pellets production process, inexpensive, and produces good quality wood pellets.
NOVELTY - Combustible gas generating device using biomass fuel comprises a gasification furnace, a smoke filtering cylinder and an air pump. The gasification furnace comprises a furnace tube connected with a dust discharging passage, which are connected with furnace or is provided with an air outlet hole with furnace plate. The lower part of the furnace wall is set with an air outlet hole. The smoke filtering cylinder comprises a sealing shell provided with a filter core. The upper part of the sealing shell is connected with the gasification furnace via the pipeline connected with the air outlet hole.    USE - Used as a combustible gas generating device using biomass fuel.    ADVANTAGE - The device can save the recycling cost, is simple in structure, has high filtration and purification rate, is environmentally friendly, and does not pollute.
NOVELTY - Automatic production line forming machine of biomass fuel comprises a crushing sieving machine, a conveying device, a drying device provided with a discharging port, a mixing device, a sawdust granulating device and a packaging machine, which are connected in turn. The crushing sieving machine comprises a crusher and a screening machine. The conveying device comprises a belt conveyer and a spiral conveyor. The mixing device comprises a storage bin. The granulating device comprises a feeder and granulator connected with one end of feeder. The conveying belt is connected with packaging machine.    USE - Used as an automatic production line forming machine of biomass fuel.    ADVANTAGE - The machine has good technical performance, low energy consumption and low production cost, and produces environmentally friendly products.
NOVELTY - Continuous reaction device of biological diesel oil, comprises a mixing tank, two sets of reaction columns, and two separating tanks. An outlet of the mixing tank upper part is connected with an inlet of the reaction column lower part. A separating tank is set between each set of the reaction column.    USE - Used as a continuous reaction device of biological diesel oil.    ADVANTAGE - The device can carry out the different stages of transesterification reaction of biological diesel oil respectively to overcome the problems resulting from different stages of transesterification reaction, and improves reaction conversion rate.
NOVELTY - Biogas digester heater comprises heating chip connected with upper portion of a heating pipe, and a heating sheet with lower return pipe assembled into square.    USE - As biogas digester heater.
NOVELTY - Device comprises a block (1), which is preferably rectangular, and has multiples panels (2) of stainless steel inside the block with vertical holes. The vertical holes divide the block to create a series of internal spaces (3) for formation of beads, where each block comprises a detachable and mobile lateral section (4).    USE - Device for producing vermicompost (claimed).    ADVANTAGE - The device ensures soil protection infrastructures for preventing contamination.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for producing vermicompost, which involves:    (A) pre-composting of material;    (B) extracting worms;    (C) processing and dehydrating pre-composting product, which includes organic matter, carbon-rich materials, nitrogen-rich materials; and    (D) processing the mixture in proportion of 25:1-35:1 of carbon-nitrogen ratio.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a device.    Block (1)    Panels (2)    Internal spaces (3)    Mobile lateral section (4)    Sewer system (5)
NOVELTY - A microbial composite inoculum comprises Paracoccus denitrificans, Bacillus megaterium, Bacillus subtilis, Bacillus badius, Bacillus thuringiensis, Bacillus licheniformis, Acinetobacter calcoaceticus, Bacillus laterosporus, and Bacillus cereus.    USE - A microbial composite inoculum used for treating sewage, household organic garbage, sewage plant sludge, or human and animal excreta (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing microbial composite inoculum, comprising mixing B. megaterium B. subtilis, B. badius, B. thuringiensis, B. licheniformis, A. calcoaceticus, B. laterosporus, and B. cereus; inserting a liquid culture medium; ferment culturing to obtain a bacteria concentration in the liquid fermentation liquor of not less than 1\10asterisk8/mL; and mixing.
NOVELTY - Preparing benzene, toluene and xylene (BTX) by catalytic pyrolysis of biomass using tetracobalt nitride catalyst, comprises taking tetracobalt nitride as catalyst and biomass as raw material, mechanically mixing the catalyst and biomass in a ratio of (5:1)-(1:20), performing rapid pyrolysis under anaerobic condition at 700-1000 degrees C, performing gas-solid separation, and then condensing the pyrolysis gas to obtain BTX-rich liquid product.    USE - The method is useful for preparing BTX by catalytic pyrolysis of biomass using tetracobalt nitride catalyst (claimed).    ADVANTAGE - The tetracobalt nitride catalyst promotes the biomass pyrolysis to form BTX in the process and inhibits the formation of other organic matters to obtain BTX-rich liquid product.
NOVELTY - A high-grade bio-oil preparing method involves utilizing tetracobalt nitride as a catalyst, and subjecting biomass to flash pyrolysis under an anaerobic condition at 400-600 degrees C. High-temperature pyrolysis gas is led into a reactor, which is filled with the tetracobalt nitride catalyst under the action of the catalyst. The pyrolysis product is subjected to reactions, such as pyrolysis, dehydration and rearrangement. The pyrolysis gas is condensed rapidly to room temperature, and a liquid product is collected to obtain liquid fuel.    USE - Method for preparing high-grade bio-oil through on-line catalytic cracking of a biomass flash pyrolysis product.    ADVANTAGE - The method enables preparing bio-oil with stable performance and quality.
NOVELTY - The system has a food and drink garbage tank (1) that is arranged above a material conveying machine (2). A crushing separating device (3) is connected with the material conveying machine. A slurry storage tank (4) is connected with the crushing separating device. A lifting pump (5) is connected with the slurry storage tank and food waste feeding pipe (7). A sludge feeding pipe (6) and food garbage feeding tube are connected with an anaerobic tank (8) in which a gas storage device (11) and a heating device (10) are installed. A stirrer (9) is set in the bottom of the anaerobic tank.    USE - Anaerobic treatment system for treating food waste-sludge mixture.    ADVANTAGE - Energy saving and environmental-friendly anaerobic treatment system can be obtained. Energy utilization ratio can be increased. Biomass energy can be generated efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the anaerobic treatment system.    Food and drink garbage tank (1)    Material conveying machine (2)    Crushing separating device (3)    Slurry storage tank (4)    Lifting pump (5)    Sludge feeding pipe (6)    Food waste feeding pipe (7)    Anaerobic tank (8)    Stirrer (9)    Heating device (10)    Gas storage device (11)
NOVELTY - The filler has a first filler layer, and a second filler layer placed above the first filler layer. The first filler layer is filled with porous material and the second filler layer is filled with zeolite, saw dust and fertilizer. The porous material is active carbon, porous ceramsite, fly ash or zeolite. Height of the first filler layer is 0.2 m and height of the second filler layer is 0.8 m. Gas is uniformly distributed in a gas distribution device.    USE - Composite filler for a biological filter tank.    ADVANTAGE - The filler has good deodorization effect and low operation cost, and avoids the need of extra air.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biological deodorization method by compost fermentation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biological filter tank.
NOVELTY - Denitration catalyst comprising a carrier shell and active nano ion core, is new, where: the carrier shell is titanium-based nano-tube; and the active nanometer ion core is oxide of cerium and manganese or and soluble salt of cerium and manganese.    USE - The denitration catalyst is useful in industrial furnace tail gas and flue gas biomass fuel such as solid toxic component with high content of waste gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the denitration catalyst.
NOVELTY - A biological organic fertilizer granulator comprises feeding hopper (1), extruding device, vacuum dewatering device, cutting device (8), drying device, blasting device and accessory.    USE - As a biological organic fertilizer granulator (claimed).    ADVANTAGE - The granulator has less energy consumption in the process of drying. The fertilizer granulator has water content of less than 28%, which ensures presence of bacteria.    DETAILED DESCRIPTION - A biological organic fertilizer granulator comprises feeding hopper (1), extruding device, vacuum dewatering device, cutting device (8), drying device, blasting device and accessory. The device is a double-shaft stirring machine (2). The vacuum dewatering device is composed of vacuum chamber (3), vacuum tank (4), a dehydration tank (5) through an air pipe and a vacuum pump (7). The cutting device is composed of a screw extruder, mold and a mold of spiral cutter (6). The blasting device is composed of a first stage granulator (11), second stage granulator (12), and third stage granulator (13). The drying device is a high-energy infrared lamp (10), and is respectively set on the first stage granulator, the second stage granulator and third stage granulator.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of the granulator.    Feeding hopper (1)    Double-shaft stirring machine (2)    Vacuum chamber (3)    Vacuum tank (4)    Dehydration tank (5)    Spiral cutter (6)    Vacuum pump (7)    Cutting device (8)    First stage granulator (11)    Second stage granulator (12)    Third stage granulator (13)
NOVELTY - The processing device comprises a plate-and-frame pressing filter, high-concentration organic waste water, coal powder mixer and burning fluidized bed. The plate-and-frame pressing filter is set on the coal powder mixer with high-concentration organic waste water. The wastewater pipe is set between plate-and-frame pressing filter and coal powder mixer. The coal powder mixer is connected with the coal powder burning fluidized bed through the water-coal slurry pipe according to the waste water pipeline. The water-coal-slurry pipe is provided with switch.    USE - Device for processing food waste within high-concentration organic wastewater of kitchen.    ADVANTAGE - The processing device is simple in structure, high in use rate, little in investment, easy to maintain, and effective to process the kitchen garbage. The occurrence of secondary pollution during processing of garbage water can be prevented.
NOVELTY - The device has a box portion that is provided with a discharging port. The discharging port is provided with a cover plate which is hinged with one side of the box portion. Specific end of box portion is provided with an opening hook. The cover plate and the box portion are provided with a supporting frame. The cover plate is provided with a feeding cylinder which is provided with an inner shielding plate. The inner shielding plate is provided with a rotating main shaft which is hinged with an outer wall of feeding cylinder.    USE - Device for retting organic fertilizer.    ADVANTAGE - By carrying out retting process in organic waste, the organic fertilizer can be manufactured effectively. The structure of organic fertilizer retting device can be simplified. Hence, economic and practical organic fertilizer retting device can be obtained.
NOVELTY - Domestic rubbish biological compost sleeve device comprises an upper box body and a lower box body. The upper box body is divided into a self-control chamber and a turning chamber. The lower box body is divided into an air chamber and biological compost chamber. A blower is connected with an air pipe, which is connected with a first valve. A dehumidifier is connected with a heater. The device further comprises a flow meter, temperature and humidity sensor, and a pressure sensor. The turning chamber is mounted vertical screw turning machines, walking tracks and associated control cables.    USE - Used as domestic rubbish biological compost sleeve device.
NOVELTY - The biological growth particle has a microorganism group that is sequentially covered with a Chinese medicine layer and a mineral layer. The microorganism group is provided with an organic matter layer.    USE - Biological growth particle for plant.    ADVANTAGE - By providing the Chinese medicine layer and mineral layer, the plant diseases and insect pests can be prevented effectively. Thus, the growth of plant can be promoted effectively.
NOVELTY - A preset amount of sodium tungstate dihydrate and disodium hydrogen phosphate are dissolved in boiling water, stirred continuously, preset amount of concentrated hydrochloric acid is added to resulting mixture, cooled, diethyl ether is added and dried to obtain phosphotungstic acid. Phosphotungstic acid solution is prepared. Cesium carbonate is added to phosphotungstic acid solution, stirred for preset time, allowed to stand at room temperature for preset time, and evaporated at preset temperature to obtain white solid cesium phosphotungstate catalyst.    USE - Preparation of solid catalyst used for producing biodiesel (claimed).    ADVANTAGE - The method provides solid catalyst having high specific surface area, high acidity, and conversion rate of 91%, at low temperature.
NOVELTY - Febuxostat prepared by mixing 2-hydroxy-5-cyanobenzaldehyde and sodium hydrogensulfide, reacting 3-aldehyde-4-thiobenzamide with 2-halogenated ethyl acetoacetate, reacting ethyl 2-(3-formyl-4-hydroxyphenyl)-4-methyl thiazole-5-carboxylate with hydroxylamine in formic acid solution, reacting ethyl 2-(3-formyl-4-hydroxyphenyl)-4-methyl thiazole-5-carboxylate with halogenated isobutane and removing ester group from 2-(3-cyano-4-isobutoxyphenyl)-4-methyl-5-thiazolecarboxylic acid by hydrolysis, is claimed.    USE - The febuxostat is useful in medicine field.    ADVANTAGE - The febuxostat can be simply, economically and rapidly prepared with low toxicity, less pollution, high yield rate and without using cyanide.    DETAILED DESCRIPTION - Febuxostat prepared by (1) mixing 2-hydroxy-5-cyanobenzaldehyde and sodium hydrogensulfide to obtain 3-aldehyde-4-thiobenzamide, (2) reacting 3-aldehyde-4-thiobenzamide with 2-halogenated ethyl acetoacetate to form a closed loop of ethyl 2-(3-formyl-4-hydroxyphenyl)-4-methyl thiazole-5-carboxylate, (3) reacting obtained product with hydroxylamine in formic acid solution to obtain ethyl 2-(3-cyano-4-hydroxyphenyl)-4-methyl-1,3-thiazole-5-carboxylate, (4) reacting obtained product with halogenated isobutane under the action of potassium carbonate to obtain 2-(3-cyano-4-isobutoxyphenyl)-4-methyl-5-thiazolecarboxylic acid, and (5) removing ester group from obtained product by hydrolysis, is claimed.
NOVELTY - The method involves separating leachate of kitchen rubbish, and breaking a rubbish bag. The rubbish material is crushed by a crusher (5), where the material is crushed into 20 mm to 40 mm of small blocks. A material feeding device is dehydrated by an extrusion dehydrator, and the material is accumulated according to a limit height of paving by a bag-breaking spreader.    USE - Kitchen rubbish pre-treating method.    ADVANTAGE - The method ensures high material sorting process rate, pre-treating the subsequent kitchen waste with easy corrosion and high temperature aerobic fermentation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a pre-processing system for kitchen rubbish, comprising a magnetic separation device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a pre-processing system for kitchen rubbish.    Receiving mechanism (1)    Cloth breaking machine (2)    Magnetic separation device (3)    Crusher (5)    Storage hopper (7)
NOVELTY - An ionic liquid is used for the production of fermentable sugar, where the method comprises adding biomass into ionic liquid, damaging crystalline structure of cellulose of biomass, hydrolyzing in ionic liquid in reactor, adding hydrochloric acid and water to generate fermentable sugar and hydrolyzing glucose to ethanol using yeast.    USE - The ionic liquid is used for production of fermentable sugar for generating ethanol (claimed).    ADVANTAGE - The total sugar is 70%.
NOVELTY - Liquid fertilizer is prepared by taking cottonseed meal as a raw material, leaching the raw material for pretreatment, fermenting the raw material and hydrolyzing the raw material using sulfuric acid, neutralizing and deacidifying the raw material using light calcium carbonate, and adsorbing the extracted amino acid mother solution through activated carbon.    USE - As liquid fertilizer.    ADVANTAGE - The fertilizer is prepared by utilizing a large amount of high quality cottonseed meal resources in Xinjiang province, so as to realize the cyclic utilization of agricultural resources, reduce the use of chemical fertilizer, and accelerate the sustainable development of low carbon agriculture and food safety production. The amino acid extracted by the liquid fertilizer is extracted from plant elemental protein, can be directly absorbed and utilized by the plants. The fertilizer has high absorption rate, is nontoxic and environment-friendly.
NOVELTY - Removal of odor substance from biogas slurry comprises oxidation and absorption function of ozone and activated carbon for removing odor substance in biogas liquid.    USE - Method for removing odor substance from biogas slurry.    ADVANTAGE - The method does not influence the nutrient content of the biogas slurry.
NOVELTY - The reactor (2) has a reactor main portion whose lower end includes a penetrating groove. The reactants are separated by an air distribution plate (9) and groove. A fan is inserted into an air distribution plate. The reactor main portion is arranged on the outer wall of heat preservation interlayer (3). The upper portion cover (5) is covered on the opening of a percolate return spraying system (6). The end of liquid flow pipe is inserted into the percolate return spraying system, while the other end is inserted in the penetrating fluid of groove through a water pump.    USE - Compost reactor for recycling organic waste such as cooking waste and crop waste.    ADVANTAGE - The temperature rise in the reactor can be prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the compost reactor.    Compost reactor (2)    Heat preservation interlayer (3)    Upper portion cover (5)    Percolate return spraying system (6)    Air distribution plate (9)
NOVELTY - Method for producing ecological organic fertilizer from excess sludge, involves mixing domestic sewage, treated residual sludge, drainage sludge and livestock manure, adding yeast strain and carbamide or ammonium carbonate to sludge mixture and adding, forming a layer of sludge mixture, stacking layers of product, covering the product with a black film externally for natural fermentation, turning the materials, fermenting and drying the materials, and screening and packing the product.    USE - The method is useful for producing ecological organic fertilizer from excess sludge (claimed).    ADVANTAGE - The ecological organic fertilizer is environmental-friendly, solves problems of residual recycling and city environmental pollution, and provides rich fertilizer source for green vegetable planting.    DETAILED DESCRIPTION - Method for producing ecological organic fertilizer from excess sludge, involves mixing domestic sewage, treated residual sludge, drainage sludge and livestock manure with yeast strain and carbamide or ammonium carbonate, adding 5-10 kg yeast strain, 30-100 kg carbamide or ammonium carbonate to 3000-5000 kg sludge mixture, adding water to product, until the moisture content reaches 60%, forming a layer of sludge mixture, yeast strain and carbamide or ammonium carbonate, stacking the product for 10-15 layers, covering with a black film externally for natural fermentation, turning the materials once in every 20 days, fermenting the product for 50 days, drying the materials, and screening, packing and storing the product for long time.
NOVELTY - The turning device has a cross beam portion (4) that is provided with motor (5). A lower portion of the cross beam portion is provided with inverted V-shaped bracket (7). An end portion of the bracket is provided with a turning wheel (10). The turning wheel is connected with motor belt in transmission manner.    USE - Turning device for preparing organic fertilizer raw material.    ADVANTAGE - The structure of the turning device can be simplified and hence the manufacturing cost of the turning device can be reduced. The efficiency of the turning device can be improved. The power consumption of the device can be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for turning method for preparing organic fertilizer raw material.    DESCRIPTION OF DRAWING(S) - The drawing shows the perspective view of the turning device for preparing organic fertilizer raw material.    Engine box (2)    Cross beam portion (4)    Motor (5)    Inverted V-shaped bracket (7)    Turning wheel (10)
NOVELTY - Preparation of ethanol-diesel oil emulsifier using leather waste grease comprises refining leather waste grease by boiling, filtering residue and separating water; preparing fatty acid methyl ester by carrying out reaction of methanol and catalyst, separating ester layer, and vacuum distilling; and preparing ethanol-diesel oil emulsifier by reacting ethanolamine and fatty acid methyl ester, in the presence of a catalyst.    USE - Preparation of ethanol-diesel oil emulsifier (claimed).    ADVANTAGE - The ethanol-diesel oil emulsifier has good and stable performance.    DETAILED DESCRIPTION - Preparation of ethanol-diesel oil emulsifier using leather waste grease comprises:    (A) extracting in boiling water leather waste grease, boiling, filtering to remove residue, cooling filter liquid, separating water, to obtain pure oil;    (B) preparing fatty acid methyl ester by adding certain amount of pure oil methanol and catalyst, reacting for a certain time at a certain temperature, standing mixed solution, separating ester layer at normal pressure, distilling at 70 degrees C and under vacuum, washing and drying to obtain pure fatty acid methyl ester; and    (C) preparing ethanol-diesel oil emulsifier by adding certain amount of ethanolamine, adding certain amount of catalyst, then adding certain amount of fatty acid methyl ester, slowly raising temperature, keeping certain temperature continuously reacting for certain time to obtain amide emulsifier, that is ethanol-diesel oil emulsifier.
NOVELTY - Synthesis of capecitabine comprises contacting a 5-fluorocytosine in the presence of an alkali and n-pentyl chloroformate in an organic solvent reverse amidation reaction to obtain a fluorocytosine-containing compound (I); dissolving compound (I) in an organic solvent, adding the resulting solution to Lewis acid, silylating reagent, and 1, 2, 3-O-acetyl-5-deoxy-D-ribofuranose; and reacting at 25-110 degrees C to obtain a methyltetrahydrofuran-containing compound (II); and carrying out hydrolysis reaction.    USE - Method for the synthesis of capecitabine (claimed).    ADVANTAGE - The method does require separation of key intermediate, has a simple post-treatment and mild reaction condition. It is simple, safe, and environment-friendly.    DETAILED DESCRIPTION - Synthesis of capecitabine comprises contacting a 5-fluorocytosine in the presence of an alkali and n-pentyl chloroformate in an organic solvent reverse amidation reaction to obtain a fluorocytosine-containing compound of formula (I); dissolving compound (I) in an organic solvent, adding the resulting solution to Lewis acid, silylating reagent, and 1, 2, 3-O-acetyl-5-deoxy-D-ribofuranose; and reacting at 25-110 degrees C to obtain a methyltetrahydrofuran-containing compound of formula (II); and carrying out hydrolysis reaction.
NOVELTY - A wood biomass alcoholysis-liquefying method involves synthesizing sulfonic acid type ionic liquid, pretreating wood biomass, and performing alcoholysis-liquefaction on resultant wood biomass.    USE - Method for alcoholysis-liquefying wood biomass with sulfonic acid type ionic liquid.    ADVANTAGE - The method enables producing alcoholysis-liquefying wood biomass with high purity and avoiding corrosion of a processing equipment.
NOVELTY - Production of biodiesel from waste cooking oil comprises filtering waste cooking oil to remove solid impurities, washing with hot water 2-3 times to remove water-soluble impurities, separating water, adding pretreated waste cooking oil in preheated methanol and sodium hydroxide, reacting while stirring at constant temperature, standing to obtain layers, separating oil layer to obtain crude oil, atmospheric-distilling at 60 degrees C, evaporating residual methanol and washing distilled oil with hot water until neutral.    USE - Production of biodiesel from waste cooking oil (claimed).    ADVANTAGE - The biodiesel has physical and chemical properties which meet the national standard. The yield of biodiesel is 93.6%.
NOVELTY - A dendrobe small mushroom F48 composite microbial inoculum, comprises: pure culture of dendrobe small mushroom F48 (3.5 pts. wt.), pure culture of Trichoderma (6.5 pts. wt.) and adhesive of 2 wt.%, where the Dendrobium is pure culture of small mushroom F48 (Mycena dendrobii Fan et Guo), contains iron and is obtained by the dendrobe Xiao-yan solid F48 block fermenting for crushing, and the pure culture of Trichoderma, is obtained by culturing Trichoderma block by solid fermentation.    USE - As dendrobe small mushroom F48 composite microbial inoculum useful in the fertilizer (claimed).    ADVANTAGE - The Dendrobium is small mushroom F48 composite microbial inoculum not only promotes the Dendrobium seedling growth speed, but also improves the biological active substance and dendrobe alkaloid content. The biological microbial inoculum composite is continuously used in agriculture, ecological agriculture, green agriculture developments for rare Dendrobium medicinal plant scale production.    DETAILED DESCRIPTION - A dendrobe small mushroom F48 composite microbial inoculum, comprises: pure culture of dendrobe small mushroom F48 (3.5 pts. wt.), pure culture of Trichoderma (6.5 pts. wt.) and adhesive of 2 wt.% by the total weight of pure culture of dendrobe small mushroom F48 and pure culture of Trichoderma, where the Dendrobium is pure culture of small mushroom F48 (Mycena dendrobii Fan et Guo), contains iron and is obtained by the dendrobe Xiao-yan solid F48 block fermenting for crushing to obtain the pure culture of Dendrobium candidum small mushroom F48, and the pure culture of Trichoderma is obtained by culturing Trichoderma block through solid fermentation to obtain pure culture of Trichoderma adhesive bait Development Center Liaoning audience information of 3A sticky powder.
NOVELTY - A dendrobe small mushroom F35 composite microbial inoculum, comprises: pure culture of dendrobe small mushroom F35 (3 pts. wt.), pure culture of Trichoderma (7 pts. wt.) and adhesive of 2 wt.%, where the Dendrobium is pure culture of small mushroom F35 (Mycena dendrobii Fan et Guo), contains iron and is obtained by the dendrobe small mushroom raw meal solid fermentation bacteria block F35 and crushing to obtain the pure culture of Dendrobium candidum small mushroom F35, and the pure culture of Trichoderma is obtained by culturing Trichoderma bacterial block by solid fermentation.    USE - As dendrobe small mushroom F35 composite microbial inoculum useful in the fertilizer (claimed).    ADVANTAGE - The Dendrobium is small mushroom F48 composite microbial inoculum not only promotes the Dendrobium seedling growth speed, but also improves the biological active substance and dendrobe alkaloid content. The biological microbial inoculum composite is continuously used in agriculture, ecological agriculture, green agriculture developments for rare Dendrobium medicinal plant scale production.    DETAILED DESCRIPTION - A dendrobe small mushroom F48 composite microbial inoculum, comprises: pure culture of dendrobe small mushroom F35 (3 pts. wt.), pure culture of Trichoderma (7 pts. wt.) and adhesive of 2 wt.% by the total weight of pure culture of dendrobe small mushroom F35 and pure culture of Trichoderma, where the Dendrobium is pure culture of small mushroom F35 (Mycena dendrobii Fan et Guo), contains iron and is obtained by the dendrobe small mushroom raw meal solid fermentation bacteria block F35 and crushing to obtain the pure culture of Dendrobium candidum small mushroom F35, and the pure culture of Trichoderma is obtained by culturing Trichoderma bacterial block by solid fermentation to obtain pure culture of Trichoderma adhesive bait Development Center Liaoning audience information of 3A sticky powder.
NOVELTY - Device comprises a vacuum pump condenser, whose inner part is provided with a U-shaped leakage net and bottom is provided with a filter, a reboiler, a pressurizing device connected to a rectifying tower through a pipe. The vacuum pump condenser is connected to the pressurizing device through a pipe. The rectifying tower is provided with a stainless steel filter screen.    USE - The device is useful for continuously rectifying biodiesel oil (claimed).    ADVANTAGE - The device: has high utilization rate; easy operation; provides stable quality product; has low energy consumption; and improves the product yield.
NOVELTY - Penicillin G acylase is added to enzymatic ampicillin crystallization mother liquid, Aqueous ammonia is added to the mixture and to adjust the pH and cracking reaction is carried out to obtain lysis solution. The lysis solution is screened, and subjected to ultrafiltration and nano-filtration. The filtered solution is decolored using active carbon, and crystallized after adding hydrochloric acid. The crystals are filtered, washed and dried to obtain solid D-(-)-phenylglycine.    USE - Recycling of D-(-)-phenylglycine from enzymatic ampicillin crystallization mother liquid (claimed).    ADVANTAGE - The D-(-)-phenylglycine is recovered economically by a simple process with reduced energy consumption, environmental pollution and resource waste.    DETAILED DESCRIPTION - Penicillin G acylase is added to enzymatic ampicillin crystallization mother liquid, Aqueous ammonia is added to the mixture and to adjust the pH and cracking reaction is carried out to obtain lysis solution. The lysis solution is screened through as sieve and the pH of the screened solution is adjusted using aqueous ammonia. Ultrafiltration concentration of the lysis solution is carried out using ultrafiltration membrane. Nano-filtration of the solution is carried out using nano-filtration membrane and active carbon is added to decolorize the filtered solution. Hydrochloric acid is added to the decolored solution to adjust the pH and the solution is cooled to form crystals. The crystals are filtered, washed and dried to obtain solid D-(-)-phenylglycine.
NOVELTY - A triazolyl containing dithiocarbamate compound (I) is new.    USE - Triazolyl containing dithiocarbamate (I) is used in preparing anti-cancer medicine. The cancer is gastric cancer, breast cancer, esophageal cancer, or prostate cancer (all claimed).    ADVANTAGE - The compound (I) is highly efficient, green and environment-friendly. It also has excellent antitumor activity.    DETAILED DESCRIPTION - Triazolyl containing dithiocarbamate compound of formula (I) is new.    n=0-4;    R1=1-7C alkyl, or 1-7C substituted alkyl; and    R2=H, 1-5C alkyl, methoxy, OH, F, Cl, Br, trifluoromethyl or fluorine-substituted or chlorine-substituted methoxy.    An INDEPENDENT CLAIM is included for preparation method of the compound (I).
NOVELTY - 3-chloro-5-aminopyridazine is synthesized by using acetaldehyde and aldehyde as initial raw materials and performing condensation, cyclization, and amination.    USE - Synthesis of 3-chloro-5-aminopyridazine for medicine and pesticide intermediates (all claimed).    ADVANTAGE - Synthesis process is shortened, use of high carcinogenic chromium metal and ammonia is prevented, waste discharge is reduced, large-scale production is possible, and yield of 3-chloro-5-aminopyradizine product is improved from 29.2% to 36.5%.
NOVELTY - The method involves heating up waste gas discharged from sewage for temperature of 2 to 40 degrees centigrade. The heated gas is discharged through a desulphurization section (3) and a hydrocarbon concentration homogenizing section (4). A solid desulfurization agent is used in the desulphurization section. A concentration homogenization substance such as active carbon, molecular sieve, silica gel, alumina and diatomite having a photo-catalysis role, is used in the hydrocarbon concentration homogenizing section.    USE - Treatment method for waste gas discharged from sewage.    ADVANTAGE - The waste gas treatment efficiency can be improved at low cost. The operation of the treatment process can be stable.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the waste gas treatment process.    Filter layer (1)    Pre-processing spraying solution (2)    Desulphurization section (3)    Hydrocarbon concentration homogenizing section (4)    Gas catalytic combustion device (6)
NOVELTY - A grid algal strain ENN33, preferably Scenedesmus sp. strain (CGMCC NO: 6347), is new.    USE - The grid algal strain ENN33 is useful for producing biodiesel, healthcare products, feed, aquatic baits, medicines, cosmetics and pigments, treating sewage water or carbon dioxide outlet, removing ion such as nitrogen, phosphorus, or heavy metal ion and degrading organic components in water for environmental protection (all claimed).    ADVANTAGE - The strain has higher growth speed, grease accumulation and oil content.
NOVELTY - A tetrahydropyran derivative (I), is new.    USE - Compound (I) for preparing agricultural insecticide or pesticide in the form of miscible oil, granular formulation, water aqua, granule, wettable powder, microcapsule, or aerosol for preventing or treating army worm (claimed).    ADVANTAGE - The compound is cheap and environment-friendly, and has good insecticidal activity.    DETAILED DESCRIPTION - A tetrahydropyran derivative of formula (I), is new. The compound is fermentation product of Streptomyces diastatochromogenes. An INDEPENDENT CLAIM is included for an agricultural insecticide or pesticide comprising compound (I) and auxiliary agent.
NOVELTY - The method involves subjecting municipal solid waste to primary sorting and crushing process. The waste is passed into fluidized bed pyrolyzing furnace (2). The cyclone dust removal, heat-exchanging temperature reduction and filtering operation are performed on pyrolyzed product in sequence. The obtained pyrolyzed gas is entered into condenser (11) to recycle metal, glass, and bio-oil by decomposing dioxin substance in waste. The smoke generated by fluidized bed incinerator (20) is conveyed into waste heat boiler (24) to generate overheated steam.    USE - Comprehensive heat energy utilization method of municipal solid waste, for preparing bio-oil.    ADVANTAGE - The minimization, reclamation and harmlessness treatment of municipal solid waste are performed effectively. The bio-oil is prepared flexibly using heat energy of the solid waste, without the need of auxiliary fuels. The operation cost of the bio-oil preparation process is reduced. The secondary pollutants are prevented from being generated in the preparation process of bio-oil. The energy sources are utilized effectively, thus the recycling of resources is realized.    DETAILED DESCRIPTION - The uncondensed gas and pyrolyzed residual carbon are discharged into fluidized bed incinerator to be combusted. The heat needed by pyrolyzing the waste is provided by fluidized bed incinerator. The inert particle bed materials are took as heat carrier to be circulated between fluidized bed pyrolyzing furnace and fluidized bed incinerator. The overheated steam is utilized for power generation of steam turbine generator unit and industrial heat source.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating comprehensive heat energy utilization process of municipal solid waste, for preparing bio-oil.    Fluidized bed pyrolyzing furnace (2)    Condenser (11)    Fluidized bed incinerator (20)    Waste heat boiler (24)    Bag-type dust collector (26)
NOVELTY - Static aerobic composting treatment method for silkworm excrement, involves (a) putting an open floor on the bottom of a treatment tank, (b) spreading a layer of conditioner on the open floor, (c) pouring mixture of the silkworm excrement and the conditioner on the layer of the conditioner and spreading, or alternately poring the silkworm excrement and the conditioner to obtain several composite layer piles and spreading the piles, and (d) finally covering a layer of conditioner on the surfaces of the piles in the treatment tank.    USE - Static aerobic composting treatment method for silkworm excrement.    ADVANTAGE - A layer of mushroom residues is coated on the bottom of a silkworm excrement tank and the surface of the silkworm excrement respectively, hence direct contact between the silkworm excrement and natural environment can be avoided, and the function of heat preservation can be exerted. The different parts of silkworm excrement have the high enough temperature, hence the whole high-temperature aerobic fermentation effect of the silkworm excrement tank can be guaranteed, the fermentation and composting speed of the silkworm excrement is accelerated, and the effect of killing pathogens in the silkworm excrement can be improved.
NOVELTY - Method for preparing an organic fertilizer, involves using human excreta or poultry excrement, leaf or straw powder, corn meal and strains, stirring, pile fermenting and airing, where 1.8 tons human excreta or poultry excrement, 0.3 ton straw powder or leaf powder, 2.5 kg corn meal and 1 kg strain quick fermenting agent, controlling the moisture content of the mixed raw materials to be 40-50%, stirring and piling the mixed raw materials into strips, covering the strips by straw mats or sack pieces to perform aerobic fermentation and piling.    USE - The method is useful for preparing the organic fertilizer (claimed).    ADVANTAGE - The method prepared organic fertilizer simply, conveniently, improves the soil environment and pH value, controls diseases and pests and is beneficial to crop growth.    DETAILED DESCRIPTION - Method for preparing an organic fertilizer, involves using human excreta or poultry excrement, leaf or straw powder, corn meal and strains, stirring, pile fermenting and airing, where 1.8 tons human excreta or poultry excrement, 0.3 ton straw powder or leaf powder, 2.5 kg corn meal and 1 kg strain quick fermenting agent, controlling the moisture content of the mixed raw materials to be 40-50%, stirring and piling the mixed raw materials into strips with width of 1.5-2 m and height of 0.3-0.4 m, covering the strips by straw mats or sack pieces to perform aerobic fermentation and piling, and increasing the compost temperature to 50 degrees C within 24 hours and 60-70 degrees C within 48 hours, and killing all pathogenic bacteria, eggs and grass seeds at such high temperature in the fermentation period.
NOVELTY - Method for producing L-cystine, involves using poultry feather including drake feathers, goose feathers, pig hairs and human hair, hydrochloric acid, liquid alkali, pure water, activated carbon and liquid ammonia as raw material to obtain a finished product.    USE - The method is useful for producing L-cystine used in medicines, and as nutritional supplement and cosmetic additive.    ADVANTAGE - The method utilizes raw materials having wide sources, is simple, cost-effective and convenient for volume production, and does not discharge waste liquid.
NOVELTY - A composite ionic liquid comprises substituted methyl imidazolium hydroxide (I) and sodium alkoxide, in the mass ratio of 1:0.05-1:0.4.    USE - Composite ionic liquid used for manufacturing biodiesel (claimed).    ADVANTAGE - The composite ionic liquid has high catalytic activity, and is manufactured economically by a simple process with reduced device corrosion, and has high biodiesel conversion rate. The biodiesel of high purity is manufactured with high yield without requiring water washing, distilling and saponification, and with reduced energy consumption by an environmentally-friendly process.    DETAILED DESCRIPTION - A composite ionic liquid comprises substituted methyl imidazolium hydroxide of formula (I) and sodium alkoxide, in the mass ratio of 1:0.05-1:0.4.    R=1-6C alkyl.    An INDEPENDENT CLAIM is included for manufacture of biodiesel. Biodiesel oil is pretreated and heated to 60-80 degrees C in a reactor, and 0.17-0.85 part phosphoric acid crystals are added and stirred. 0.5-5 parts alkaline solids and O.5-2 parts white clay are added and heated to 50-90 degrees C. The reaction residue is filter-removed after 15-30 minutes and ester exchange reaction is carried out with the pretreated biodiesel and 15-40 parts short chain alcohol, at 50-80 degrees C, for 20-90 minutes. Gravity settling of the reaction solution is carried out and the organic phase is separated to obtain crude biodiesel. The crude product is heated to 80-120 degrees C and mixed with the composite ionic liquid to obtain biodiesel.
NOVELTY - A biogas membrane device comprises gas compression system, precise filtering system, temperature control heating device (9), and membrane separation control device (10) comprising five parts, where all components of the whole system can be set on movable skid. The gas compression system comprises compressor (1), gas-water separator (2), oil mist separator (3), gas buffer tank (4), front pressure regulator (5), and flow meter (6), and the precise filtering system comprises first precise absorber (7) and second precise absorber (8).    USE - The biogas membrane device is used for synchronous separation and purification of methane and carbon dioxide (claimed).    ADVANTAGE - The convenient-to-use device can produce biogas having methane content of 98%. The separated carbon dioxide is improved to more than 95%.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the biogas membrane device.    Compressor (1)    Gas-water separator (2)    Oil mist separator (3)    Gas buffer tank (4)    Front pressure regulator (5)    Flow meter (6)    Precise absorbers (7,8)    Temperature control heating device (9)    Membrane separation control device (10)
NOVELTY - The device has main portion (1) such as hollow cavity structure comprising feed area (11), reaction area (12) and exhaust area (13). The baffle plates (121,131) are located between feed area and reaction area and between reaction area and exhaust area. The reaction area is divided into an upper cavity (122), a middle cavity (123) and a lower cavity (124). A clap board (125) is set between upper and middle cavities, to which potassium superoxide reactor (126) is attached. A rotary sealing door is provided on one side of wall of reaction area.    USE - Device for regenerating air using potassium superoxide for use in coal mine for emergency rescue.    ADVANTAGE - The device is simple in structure and convenient to use. The device can be maintained easily without using power. The substance such as carbon dioxide, methane, carbon monoxide, hydrogen sulfide, sulfur dioxide and nitrogen oxide, which is harmful to human can be absorbed effectively. Oxygen can be supplied continuously to closed space.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the device for regenerating air using potassium superoxide.    Main portion (1)    Reaction area (12)    Exhaust area (13)    Baffle plates (121,131)    Cavities (122-124)    Clap board (125)    Potassium superoxide reactor (126)
NOVELTY - Preparation of synergistic industrial marsh gas involves mixing raw material marsh gas, purifying marsh gas, pressurizing raw material gas under pressure of 0.3-1.5 MPa, removing cellulose by supercritical carbon dioxide, and carbon dioxide gas, desulfurizing by desulfurizing device, removing sulfide, putting the desulfurized raw material marsh gas, cooling, performing dehydration treatment, adding synergistic agent to obtain industrial marsh gas, compressing purified marsh gas under pressure of 20-25 MPa, adding mixing agent, and filling synergistic industrial marsh gas in pressure tank.    USE - Preparation of synergistic industrial marsh gas (claimed).    ADVANTAGE - The synergistic industrial marsh gas is manufactured efficiently with excellent with excellent purity.
NOVELTY - Production of biodiesel involves reacting kitchen waste oil and methanol under action of composite catalyst, distilling the unreacted methanol, maintaining the resultant mixture, separating lower layer of catalyst, obtaining crude biodiesel, performing continuous vacuum distillation of the obtained crude biodiesel in a distillation column, collecting distillate at 130-190 degrees C, adding 25-35 %mass hydrogen peroxide solution to the obtained distillate, stirring, reacting, adjusting the pH of the resultant reaction solution to 6-6.5 using sodium carbonate and filtering.    USE - Production of biodiesel (claimed).    ADVANTAGE - The method economically provides biodiesel with high quality, without discharge of sewage.    DETAILED DESCRIPTION - Production of biodiesel involves reacting kitchen waste oil and methanol under action of composite catalyst at 75-85 degrees C 8-10 hours, distilling the unreacted methanol, maintaining the resultant mixture, separating lower layer of catalyst, obtaining crude biodiesel, performing continuous vacuum distillation of the obtained crude biodiesel in a distillation column, collecting distillate at 130-190 degrees C, adding 25-35 %mass hydrogen peroxide solution to the obtained distillate, stirring uniformly, reacting for 10-20 minutes, adjusting the pH of the resultant reaction solution to 6-6.5 using sodium carbonate and filtering to remove impurities. The composite catalyst contains solid superacid and solid base in mass ratio of 1-3:2-3.
NOVELTY - Production of organic fertilizer comprises dewatering and drying livestock excrement (water content of dried livestock and poultry manure is 25-40%), mixing dry livestock and poultry excrement with 0.1-0.2 pt. wt. effective microorganism (EM), adding 50-120 pts. wt. auxiliary material straw, fully and uniformly stirring, fermenting for 30-50 days, crushing, pelletizing and packaging organic fertilizer.    USE - Production of organic fertilizer.    ADVANTAGE - The method is simple, the production cost is low; it does not contain harmful bacteria, it also has low water content, thus, easy to store and use.
NOVELTY - Preparing base fertilizer comprises adding cotton straw, wheat straw, corn straw, rapeseed cake and castor seed cake, drying pollution-free pond mud, dairy manure and pig manure, adding organic fertilizer fermenting agent, inorganic compound fertilizer, iron amino acid chelate, copper amino acid chelate, manganese amino acid chelate, humic acid chelated zinc, humic acid chelated calcium, humic acid chelated magnesium, 0.05% of amino acid waste liquid, nanoselenium plant nutrient agent and raw material.    USE - The method is useful for preparing base fertilizer (claimed), which is useful for Beijing purple sweet potato plant to improve drought resistance.    ADVANTAGE - The base fertilizer provides the Beijing purple sweet potato plant with high yield and disease resistance, and improves the appearance and quality of the purple sweet potato.    DETAILED DESCRIPTION - Preparing base fertilizer comprises adding cotton straw, wheat straw, corn straw, 15% of rapeseed cake and 10% of castor seed cake, drying 5% of pollution-free pond mud, 12% of dairy manure and 16-20% of pig manure, adding 20-24% of organic fertilizer fermenting agent, 2% of inorganic compound fertilizer containing nitrogen, phosphorus and potassium in a ratio of 8:7:10, 9% of iron amino acid chelate, 0.3% of copper amino acid chelate, 0.1% of manganese amino acid chelate, 0.1% of humic acid chelated zinc, 0.05% of humic acid chelated calcium, 0.2% of humic acid chelated magnesium, 0.05% of amino acid waste liquid, 6% of nanoselenium plant nutrient agent and 0.2% of raw material.
NOVELTY - A high mangiferin is prepared by represented by mixing mangiferin, dimethyl carbonate, boric acid and alkali, and subjecting mixture to methylation reaction in the presence of solvent.    USE - Method of preparing a high mangiferin.    ADVANTAGE - The method is simple and low cost, has good reaction selectivity and high yield, is safe and environment-friendly, and can be applied to large-scale production.
NOVELTY - Producing ethanol comprises: roughly grinding a biomass feedstock; cooking roughly ground products on a low-density alkaline conditions; grinding the cooked treatment products; removing water using water removal step and/or drying rollers; enzymatic hydrolysis of water-excluded products and/or dried products produced in the water removal step; and fermentation of hydrolyzate resulting in enzymatic hydrolysis steps using a yeast to produce ethanol.    USE - The method is useful for producing ethanol.    ADVANTAGE - The method provides ethanol in high yield and xylose as byproduct (that can be used as animal feed and fertilizer) by a simple method thus both work procedures and production costs can be reduced and profitability can be greatly improved.
NOVELTY - A liquid manure is manufactured by activated sludge treatment which generates surplus sludge by circulating activated sludge by a system and aerates an organic waste water, solubilization process which extracts surplus sludge generated by activated sludge treatment out of the system, concentrates, destroys and solubilizes cell of sludge, adds ozone gas to generated concentrated surplus sludge and circulating by the system, and fertilizer fermentation process which disinfects solubilized liquid, ferments and cures.    USE - Manufacturing method of liquid manure used for fertilizer and for processing sewage, industrial waste water and excrement.    ADVANTAGE - The liquid manure can be discharged to river as fresh water.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the manufacture of liquid manure. (Drawing includes non-English language text).    Flow volume adjustment tank (1)    Aerator (2)    Sedimentation tank (3)    Sludge thickening tank (4)    Sludge storage tank (5)
NOVELTY - The gasifier (14) has a reactor body comprising an upper part (22) and a lower part (23) into which biomass is introduced through an inlet duct (1) located in top of the upper part. A grid (8) comprises a set of openings through which ash to be evacuated passes. A set of introducing units introduces a gasification agent e.g. air or oxygen, and comprises a diffusion cone (13) for diffusing the agent located at top of an oxidation area of the gasifier, or above the oxidation area. Reactive gas injecting nozzles (19, 29) inject the agent located in the oxidation area of the gasifier.    USE - Co-current fixed bed gasifier for converting biomass into synthesis gas and ash with aid of a gasification agent i.e. reactive gas.    ADVANTAGE - The diffusion cone diffuses the agent located at top of the oxidation area of the gasifier, or above the oxidation area, and the biomass runs out along a wall of the cone during pyrolysis when homogeneous oxidation of tar takes place inside the cone so as to allow drastic reduction in tar concentration of produced gas, thus ensuring minimal tar rate, and obtaining maximum power higher than 500 kW, and hence obtaining synthesis gas with high output and reduced carbon rate in ashes.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for gasifying of biomass using a gasifier.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of a gasifier.    Inlet duct (1)    Grid (8)    Diffusion cone (13)    Gasifier (14)    Reactive gas injecting nozzles (19, 29)    Upper part of reactor body (22)    Lower part of reactor body (23)
NOVELTY - A genetically enhanced cyanobacterium for the production of a first chemical compound, comprising at least one first recombinant gene encoding a first biocatalyst for the production of the first chemical compound, where the gene is under the transcriptional control of a cobalt ion (Co2+) or zinc ion (Zn2+) inducible promoter, is new.    USE - The genetically enhanced cyanobacterium is useful for producing a first chemical compound. The first chemical compound is a biofuel or an organic compound. The biofuel or the organic compound is selected from alkanols, alkanes, polyhydroxyalkanoates (e.g. PHB), fatty acids, fatty acid esters, carboxylic acids (such as amino acids), hydrogen, terpenes and terpenoids, peptides, polyketides, alkaloids, lactams, such as pyrrolidone, alkenes and ethers, such as tetrahydrofuran (THF) or their combination. The first compound is alkanols. The first compound is ethanol (all claimed).    ADVANTAGE - Improved inducible promoters for the transcriptional control of genes for the production of first chemical compounds are provided.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for producing a first chemical compound by (a) culturing the genetically enhanced cyanobacteria above in a culture medium, and (b) inducing the cyanobacteria by adding Co2+, Zn2+, or nickel ion (Ni2+) to the culture medium, the cyanobacteria producing the first chemical compound.
NOVELTY - Crystalline form IV, V, VI, VII, VIII, IX and X of pitavastatin calcium having powder X-ray diffractogram as given in the specification are new.    USE - The crystalline forms of pitavastatin calcium are useful for treating hypercholesterolemia and mixed dyslipidemia No biological data given.    ADVANTAGE - The crystalline forms of pitavastatin calcium are of high purity and are produced in a simple, cost-effective, ecologically friendly, reproducible, scalable, and robust manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for preparation of crystalline forms of pitavastatin calcium, and crystalline form V of pitavastatin calcium.
NOVELTY - The coconut husk charcoal is manufactured using boiler (3) which uses coconut husk as fuel, and high-temperature gas is introduced from outside. The coconut husk charcoal manufacturing apparatus dry-distills coconut husk with self-sustained combustion-type direct heating-type kiln, to obtain coconut husk charcoal. The secondary combustion air is supplied to exhaust gas with unburned combustible content and discharged from spontaneous combustion-type direct heating kiln to burn exhaust gas to obtain high-temperature gas, and high-temperature gas is conveyed and introduced to boiler.    USE - Manufacture of coconut husk charcoal used as biomass fuel.    ADVANTAGE - The method enables economical and efficient manufacture of coconut husk charcoal.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for system (1) for manufacturing coconut husk charcoal.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the system for manufacturing coconut husk charcoal. (Drawing includes non-English language text)    System for manufacturing coconut husk charcoal (1)    Boiler (3)    Hot-gas conveyance and introduction apparatus (5)    Hot gas-introducing portion (7)    Turbine (23)
NOVELTY - Recovering magnesium ammonium phosphate as a fertilizer, comprises adding urease enzyme and magnesium chloride to urine in waterless and water-saving urinals.    USE - The method is useful for toilets and collecting sites of human and animal urine (claimed).    ADVANTAGE - The method: makes use of inexpensive raw materials, thus it is carried out in a simple and low-cost manner without further processing steps to ensure an environmentally friendly fertilizer that has low levels of heavy metal; makes use of the urine, which is an inexhaustible resource with high concentrations of dissolved nutrients and does not contain precipitates of hormones, drug residues and other impurities; and conserves the wastewater treatment plants energy and saves the cost of phosphate elimination (with regard to precipitation of the phosphate in the urine before it reaches to the treatment plant and only residual urine without phosphate reaches the treatment plant).
NOVELTY - Treating an organic waste material in a liquid form comprises subjecting the liquid waste material to a first solid/liquid separation step resulting in a clarified fraction and a concentrated fraction; subjecting the concentrated fraction to anaerobic fermentation in a biogas reactor resulting in a first digestate; subjecting the first digestate and the clarified fraction to an anaerobic fermentation in upflow anaerobic sludge blanket (UASB) reactor resulting in a second digestate; and with preference subjecting the second digestate to ultrafiltration and reverse osmosis.    USE - The method or plant is useful for treating organic waste material in liquid form (claimed).    ADVANTAGE - The biomethanization is an effective and ecologic method for the treatment of organic wastes while producing energy in the form of methane via methanogenic bacteria. The methanation allows treating refuse and waste as diverse as waste material, sewage sludge, animal waste, food-processing industries waste, household waste, and agricultural waste. Specifically, the invention provides economical process and plant for allowing a continuous and efficient treatment of organic waste material in liquid form, improving efficiency of known treatments and reducing the costs associated to these treatments, and for reducing the global processing time of the treatment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is plant for the treatment of an organic waste material in liquid form, comprising a biogas reactor, an ultrafiltration unit and a reverse osmosis unit where the plant further comprises UASB reactor, a first liquid/solid separator to treat the organic waste material before the biogas reactor and means to direct the clarified fraction to the UASB reactor and the concentrated fraction to the biogas reactor.
NOVELTY - The method comprises providing pellets pressed from a biomass, and heat treating the pellets at a temperature of 250-300 degrees C for a time period of 3-16 minutes in a batch wise manner. The pellets: are heated by a tempered flow of air; have a diameter of 4-20 mm and a moisture content of 5-15 wt.%; and are quenched after the heat treatment. The flow of air is strong so that the pellets are placed in motion by the flow of air. The heat treatment is carried out with the flow of air of 6-20 m3 per kilogram of pellets, and is performed in an atmosphere with reduced oxygen content.    USE - The method is useful for refining pellets (claimed) that are useful as a fuel in the form of co-firing in power plants to generate heat or electrical energy.    ADVANTAGE - The pellets exhibit improved service life and high density.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for refining pellets.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic view of a device for refining pellets.    Treatment chamber (14)    Feed line (18)    Blowers (19)    Burner (20)    Inlet. (21)
NOVELTY - Production of ethanol involves contacting a feed stream containing acetic acid and hydrogen at an elevated temperature with a hydrogenating catalyst comprising platinum, tin and secondary noble metal on a support material. The secondary noble metal is chosen from rhodium, palladium, gold and iridium.    USE - Production of ethanol. Uses include but are not limited to fuel e.g. gasoline for motor vehicles e.g. automobiles, boats and piston engine aircraft, toiletry and cosmetic composition, detergents, disinfectants, coatings, inks and pharmaceutical.    ADVANTAGE - The ethanol is efficiently produced with improved selectivity and productivity.
NOVELTY - Production of sugar alcohol from a cellulosic or lignocellulosic biomass, comprises combining the cellulosic or lignocellulosic biomass with a microorganism that converts at least one of the sugars to a sugar alcohol, where the biomass contains one or more sugars, and maintaining the microorganism-biomass combination under conditions that enable the microorganism to convert the sugars to the sugar alcohol.    USE - The method is useful for producing sugar alcohol e.g. erythritol from a cellulosic or lignocellulosic biomass(claimed), which is useful in a food industry.    ADVANTAGE - The method produces sugar alcohol without leaving undesirable chemicals in the resulting product or degrading the sugars in a cost-effective and high yield manner.
NOVELTY - Making a product comprises saccharifying recalcitrance-reduced lignocellulosic biomass, and adding an isomerization agent to the saccharified biomass.    USE - The method is used for making a product selected from ethanol, butanol, butyric acid, acetic acid, acetone, and lactic acid (all claimed).    ADVANTAGE - Method of increasing the efficiency of biomass saccharification is provided. The method includes ways of avoiding feedback inhibition during the production of useful products. The method provides large quantities of products with high purities and of low prices.
NOVELTY - Preparing a catalyst comprises preparing a support including 0.2-30 wt.% of an NU-86 zeolite and 70-99.8 wt.% of a porous inorganic matrix, impregnating the support with at least one solution containing at least one precursor consisting of Group VIII and Group VIB metals, performing aging step, and performing a drying step at a temperature of less than 150 degrees C without a subsequent calcining step.    USE - The method is useful for preparing a catalyst, which is useful for hydrocracking hydrocarbon feedstocks consisting of light diesel fuel obtained from a cracking catalytic unit, atmospheric distillates, vacuum distillates obtained from direct distillation of crude, distillates obtained from desulfurization or fixed-bed hydroconversion processes in fixed bed, atmospheric residues, vacuum residues, de-asphalted oils, paraffin obtained from Fischer-Tropsch process, and feedstocks obtained from hydro-treating and hydroconversion processes of the biomass and sockets (all claimed).    ADVANTAGE - The catalyst can be economically prepared with improved catalytic activity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for hydrocracking hydrocarbon feedstocks using the catalyst comprising performing a hydrocracking process in the presence of hydrogen at a temperature of higher than 200 degrees C, a pressure of higher than 1 MPa, a space velocity of 0.1-20 h-1 and hydrogen quantity such that the ratio of voluminal liter of hydrogen/liter of hydrocarbon is 80-5000 l/l.
NOVELTY - Device (10) comprises a container (20) made of a non-woven nylon fabric, a desiccant, and a gelling agent, where the desiccant and gelling agent are inside the container.    USE - The device is useful for removing moisture from ethanol blended fuel in a fuel tank (claimed).    ADVANTAGE - The device does not allow water into the container, thus preventing the fuel from drying.    DESCRIPTION OF DRAWING(S) - The figure illustrates a perspective view of the device.    Device (10)    Container (20)    Crimped end (30)
NOVELTY - Preparing organic seaweed liquid fertilizer comprises mixing pear rot and kiwi fruit rot to obtain rotten fruit pulp, soaking unbracteolated spurge root, radix sophorae flavescentis and eucalyptus leaf by vinegar, washing the soaked mixture using water to obtain a compositing plant, mixing the rotten fruit pulp and the plant with peat soil, straw ash, overdue milk powder, dry potato residue, rice bran, pu-erh tea dreg, fermenting the above mixture by sealed fermentation to obtain a fermentation material and mixing the obtained material with diammonium phosphate and potassium chloride.    USE - Used as organic seaweed liquid fertilizer.    ADVANTAGE - The method economically prepares organic seaweed liquid fertilizer with enriched nutrient and low toxicity and improved crop drought resistance.    DETAILED DESCRIPTION - Preparing organic seaweed liquid fertilizer comprises: (1) mixing a pear rot (20-25 pts. wt.) and a kiwi fruit rot (10-12 pts. wt.) to obtain a rotten fruit pulp; (2) soaking unbracteolated spurge root (6-8 pts. wt.), radix sophorae flavescentis (8-10 pts. wt.) and a eucalyptus leaf (3-5 pts. wt.) and by a vinegar for 8-10 hours, washing the soaked mixture using water to obtain a compositing plant; (3) mixing the rotten fruit pulp and the compositing plant with peat soil (10-12 pts. wt.), straw ash (10-12 pts. wt.), overdue milk powder (10-12 pts. wt.), dry potato residue (5-7 pts. wt.), rice bran (3-4 pts. wt.), a pu-erh tea dreg (5-8 pts. wt.), fermenting the above mixture for 12-14 days by sealed fermentation to obtain a fermentation material; and (4) mixing the fermentation material with diammonium phosphate (10-12 pts. wt.) and potassium chloride (18-20 pts. wt.) and then grinding to obtain powder, and mixing the obtained powder with alum (1-2 pts. wt.).
NOVELTY - Meropenem crude product is dissolved in an alkali solution at 10-30 degrees C to obtain a saturated solution. Activated carbon is added to the solution, and the solution tallized. The temperature is reduced to -5 degrees C to 10 degrees C and the reaction mixture is filtered to obtain meropenem trihydrate crystal. The alkali solution is aqueous ammonia, sodium carbonate, or sodium bicarbonate, with a concentration of 5.5%.    USE - Preparation of meropenem trihydrate crystal (claimed).    ADVANTAGE - The method solves the problem that meropenem is low in water solubility. The solubility of meropenem in water is 3 g/ml and the solubility of meropenem in alkali solution is up to 30 g/ml or more. The method eliminates the use of organic solvent and ensures that the process is safe and environmentally-friendly. The yield of meropenem is increased to 79%.    DETAILED DESCRIPTION - Meropenem crude product is dissolved in an alkali solution at 10-30 degrees C to obtain a saturated solution. Activated carbon is added to the solution, and the solution is decolorized and filtered. An acid is added to the filtrate to adjust the pH of solution to less than 7, and meropenem is crystallized. The temperature is reduced to -5 degrees C to 10 degrees C and the reaction mixture is filtered to obtain meropenem trihydrate crystal. The alkali solution is aqueous ammonia, sodium carbonate, or sodium bicarbonate, with a concentration of 5.5%. The acid is hydrochloric acid, sulfuric acid, or acetic acid, with a concentration of 10-50%.
NOVELTY - The machine has a furnace body provided with a high temperature fire resistant column, where a side of the furnace body is provided with a combustion chamber, and another side is provided with a de-dusting and purifying chamber. A feeding mechanism is arranged on an upper end of the combustion chamber. An air supply mechanism is set in a middle of the feeding mechanism and the combustion chamber. An oxygen supply mechanism is arranged on an upper end of the de-dusting and purifying chamber. A nozzle is installed on a side of a dust-removing purifying room.    USE - High temperature cracking biomass gasification combustion machine.    ADVANTAGE - The machine can make complete the biomass particle gasification so as to ensure better the combustion effect, and has high heat efficiency, energy-saving and environment-friendly function, simple structure, convenient operation and wide application range.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a high temperature cracking biomass gasification combustion machine.
NOVELTY - The purifier has a shell provided with a fuel gas output pipe, a water inlet pipe and a drain pipe. The shell is connected with a left baffle plate. The shell is divided into a gas inlet cavity and a gas outlet cavity. A bubble cap plate is connected with the left baffle plate. Another bubble cap plate is connected with a right baffle plate.    USE - Biomass gasification gas bubble washing purifier.    ADVANTAGE - The purifier effectively removes biomass gasification fuel gas in a complete manner.
NOVELTY - The absorber has a box body whose two sides are respectively connected with two ends of a fuel gas input pipe and a fuel gas output pipe. An inner cavity of the box body is provided with a left grid plate and a right grid plate. An inner part of the box body is provided with a wire. The box body is connected with an upper side of a feeding port. The feeding port is provided with a cover plate. The cover plate is arranged on a bottom end of the box body. A drain pipe is connected with the inner cavity of the box body.    USE - Biomass gasification fuel gas wire material absorber.    ADVANTAGE - The absorber enables entering biomass gasification gas that is utilized by a fuel gas generating set. The absorber can use waste absorbing material repeatedly so as to save resource. The absorber has wide application range.
NOVELTY - The biomass fuel gas furnace has combustion chamber which is mounted in furnace unit provided with storage bin on top portion. The combustion chamber is provided in fire grate in furnace unit. The feeding storehouse opening is provided with the outer sealing cover. The bottom portion of the furnace gate is provided with an ash outlet. The ash outlet is provided with rotatable disc-shaped ash hopper and ash bucket driving device. The furnace gate is fixed on the ash hopper. The dust hopper wall is provided with ash scraping knife mounted under the furnace unit.    USE - Biomass fuel gas furnace.    ADVANTAGE - The gas generating efficiency of biomass fuel gas furnace can be improved stably with remote automatic control function. Continuous production of the furnace can be ensured with safe operation and low labor intensity.
NOVELTY - The tower has an anode electrical dust removing chamber fixed with a honeycomb anode plate. The honeycomb anode plate is connected with a cathode insulating chamber of a cathode line. A cell anode separator plate is provided with a washing spray disk pipe. An absorbing filling chamber is connected with an air outlet and a bubble-cap desulfurization section part that is connected with a sieve plate desulfurizing agent spray coil pipe. A bubble cap tower plate type wet deodorization section part is connected with a deodorant spray coil pipe.    USE - Rubbish pyrolyzing, coal gas de-sulfurizing, dust-removing, tar-removing and dioxin deodorizing tower.    ADVANTAGE - The tower has high dust removing efficiency, low system resistance and prolonged service life. The tower ensures rubbish pyrolysis gas purifying effect. The tower is easy to maintain.
NOVELTY - The gasification combustion furnace has a furnace portion that is provided with a feeding port and a rotary adjusting plate. The furnace neck and internal furnace are truncated cone-shaped and made of cast iron. Ventilation holes are uniformly formed on the furnace neck and internal furnace. An observing hole is provided outside a furnace door. An adjusting plate is installed below a furnace gate. A storage chamber is set between adjusting plate and furnace gate. An operating rod is extended into the furnace portion.    USE - Gasification combustion furnace for combusting biomass and rubbish in countryside and remote mountainous area.    ADVANTAGE - Complete combustion of combustible gas can be facilitated. Heat efficiency of the gasification combustion furnace can be improved. The gasification combustion furnace is simple in structure and convenient to use and operate.
NOVELTY - The system has a biomass gasification device collecting solar energy. A lower part of the biomass gasification device is arranged with a bracket. A solar energy mirror is arranged on a solar energy mirror bracket that is provided with a tracking control device. The tracking control device controls the solar energy mirror to focus sunshine. The biomass gasification device is arranged on the solar energy mirror bracket. A tracking solar energy photo-thermal converter is connected with the biomass gasification device.    USE - Mobile node array solar biomass gasification system.    ADVANTAGE - The system improves solar energy utilization efficiency.
NOVELTY - Anaerobic digestion treatment system comprises a first starting phase bioreactor, a second activation phase bioreactor, a third decomposition phase bioreactor, a first digestion liquid tank, a second digestion liquid tank, a third digestion liquid tank, a first pump, a second pump, a third pump. Each bioreactor is connected with the digestion liquid tank via multiple liquid connecting pipes. The system further comprises a gas collecting device for collecting gas. The upper end of each bioreactor is provided with a first inlet. The gas collecting device is connected with a second inlet.    USE - The anaerobic digestion treatment system is useful for treating kitchen waste(claimed).    ADVANTAGE - The system: reduces the processing steps; and prevents the accumulation of high salt, volatile fatty acids and ammonia and thus increases the gas production rate.
NOVELTY - The method involves utilizing high temperature thick semi-coke in a primary level gas-solid separator to separate primary gas from solid at a bottom part of a turbulent coupled fluidized bed. High temperature gas and liquid residue is made to flow along downward direction of an entrained flow bed. Temperature of the coupling fluidized bed is increased by high temperature gas to supply heat during gasification process in the fluidized bed. Liquid slag is made to flow toward circulating ash. Water vapor and oxidants are separated from fuel gas by a secondary level gas-solid separator.    USE - Household rubbish coupled fluidized bed through hierarchical pyrolysis gasification method.    DESCRIPTION OF DRAWING(S) - The drawing shows a circuit diagram of a household rubbish coupled fluidized bed.
NOVELTY - Solid fuel comprises 60-80 wt.% of hickory cattail powder and 20-40 wt.% of wooden meal, bamboo meal and/or crop straw powder.    USE - Used as solid fuel.    ADVANTAGE - The solid fuel can be prepared in a simple manner, high stability and reliable product quality, and is eco-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing solid fuel comprising crushing the Camellia fruit nut external total corn into powder with a grinding diameter of 2-6 mm, weighing other raw materials and mixing with the powder, (3) placing the powder into a round molding machine, placing powder into an annular molding particle mechanism and then cooling by counter flow cooling device, and packing the product and then keeping in a damp proof room.
NOVELTY - A liquid fuel oil preparing method involves weighing biological oil, fat and a USY catalyst at mass ratio of the biological oil and fat to the USY catalyst of 50:1-10. The biological oil, fat and the USY catalyst are added to a reaction kettle. The reaction kettle is heated at 400-500 degrees C, and catalytic cracking is performed followed by condensing produced steam to obtain a dark brown liquid product.    USE - Method for preparing liquid fuel oil.    ADVANTAGE - The method enables preparing oil with high yield of higher than 80%, and good service life of USY catalyst.
NOVELTY - The generator has rectangular or circular box portion whose lower portion is arc-shaped and upper portion is set with water pressure tank (4) with cone-shaped bottom (41) and drain pipe (42). The sides of box portion are respectively provided with man hole covers, feeding pipes (5a,5b), air outlet pipes, and stirrers (8a,8b) at upper end, and discharging openings (9a,9b) at lower end. The lower ends of feeding pipes are set lower than drain pipe. The lower portion of box portion is set with fermentation chamber (20). A gas storage chamber (22) is set outside the pressure tank.    USE - Steel structure water pressure type biogas generator used in animal breeding field.    ADVANTAGE - The generator yield can be increased. The environment pollution can be avoided. The energy-saving and environment-friendly generator can be obtained.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the steel structure water pressure type biogas generator.    Water pressure tank (4)    Feeding pipes (5a,5b)    Stirrers (8a,8b)    Discharging openings (9a,9b)    Fermentation chamber (20)    Gas storage chamber (22)    Cone-shaped bottom (41)    Drain pipe (42)
NOVELTY - The hydrogen production system has an oxygen separator (1) and a hydrogen separator (2) that are arranged on upper portion of electrolytic groove (3). A heat exchange pipe (4) is provided inside the oxygen separator and hydrogen separator. An oxygen electrolyte mixed outlet pipe (5) and hydrogen electrolyte mixed outlet pipe (6) are connected on both sides of electrolytic groove. A return pipe (9) and a return pipe (10) are respectively connected on two sides of the electrolytic groove. Return pipes (9,10) are respectively connected to oxygen separator and hydrogen separator.    USE - Water electrolysis hydrogen production system.    ADVANTAGE - The structure of the water electrolysis hydrogen production system is simplified. The generation of fault in water electrolysis hydrogen production system is reduced. Power consumption is reduced. The water electrolysis hydrogen production system can be worked more stably. The water electrolysis hydrogen production system can be maintained more conveniently. The reliability of the water electrolysis hydrogen production system is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the water electrolysis hydrogen production system.    Oxygen separator (1)    Hydrogen separator (2)    Electrolytic groove (3)    Heat exchange pipe (4)    Oxygen electrolyte mixed outlet pipe (5)    Hydrogen electrolyte mixed outlet pipe (6)    Return pipes (9,10)
NOVELTY - The device has a gasification furnace (1) whose gas outlet is connected with a fuel gas pipe of a combustion machine (3). A shrinking port of the combustion machine is connected to a heat exchange chamber (5). An upper part of a combustion nozzle (6) is connected with a hot gas output pipe (4). The combustion machine is composed of a combustion machine shell, an air inlet pipe, a fuel gas nozzle and a machine cylinder that is processed with air holes. An outer wall of the machine shell is equipped with the air inlet pipe. An inner cavity of the gas nozzle is connected with the fuel gas pipe.    USE - Biomass gasification hot air device    ADVANTAGE - The device has wide use, strong practicability and popularization value, and avoids pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass gasification hot air device.    Gasification furnace (1)    Combustion machine (3)    Hot gas output pipe (4)    Heat exchange chamber (5)    Combustion nozzle (6)
NOVELTY - A system for treating domestic garbage comprises reflecting and accumulating device for a solar radiation to a point or a zone, a heating body, a reflection focusing device for focusing sunlight, a solar energy for heating the fluid in the heating body, and a fermenting tank for fermenting domestic garbage.    USE - The system is used for treating domestic garbage (claimed).    ADVANTAGE - The system is used for economical domestic garbage treatment requiring less energy.
NOVELTY - The ecological purifying device has an artificial wet land system that is connected with a pond positioned on an upper portion of an overflow weir water outlet. An adsorption tank is filled with peanut shell. The artificial wet land system is filled with shale hollow brick.    USE - Ecological purifying device for processing biogas liquid used for livestock and poultry.    ADVANTAGE - The water quality can be improved. The purifying ability of the ecological purifying device can be improved.
NOVELTY - The device has gasification unit, carbon monoxide transformation unit, purifying unit, methanol synthesis unit and methanation unit that are connected with one another. A compression unit of methanol synthesis unit is connected with a methanol synthesis reactor. An alcohol divider is connected to purge outlet of methanation unit. The compression unit is connected in parallel with pressure bypass unit. The circulating air outlet of the alcohol divider is provided with a circulating pipe. The inlet of the compression unit is connected with the alcohol divider.    USE - Synthetic methanol and synthetic methane producing device.    ADVANTAGE - The synthetic natural gas carbon monoxide conversion rate and synthetic gas amount are adjusted, thus the production of methanol is enhanced. The surge of the circulating pipe of the synthetic methanol and synthetic methane producing device is prevented by adjusting the synthetic methanol loop recycle ratio. The production cost and the material cost of the synthetic methanol and synthetic methane producing device is reduced.
NOVELTY - Biomass briquette clean production system comprises a biomass briquette device, where the biomass briquette device inlet is connected to feed material outlet via material conveying belt, and the feed material inlet is connected to the material crushing device via conveying belt. The material crushing device inlet is connected with the outlet of the material drying device. The hot air inlet of air distribution chamber is connected with the inlet of the material drying device. The air distribution chamber is connected to biomass briquette combustion equipment. A fan is connected through a pipe.    USE - Used as biomass briquette clean production system.    ADVANTAGE - The system realizes clean discharge of biomass briquette from biomass feedstock, high efficiency and large scale production.
NOVELTY - Laboratory biological carbon carbonization furnace comprises a feeding tank, a heating steel pipe, a resistance wire, a temperature sensor, a shell and a cover. The feeding tank is a hollow steel drum structure with an upper end opening and sealed bottom. The heating steel pipe is an annular barrel-shaped structure with an upper end opening and sealed bottom. The feeding tank is inserted into the heating steel pipe provided with a heating layer. The temperature sensor is arranged between the heating layer and the heat insulating layer. The upper cover is provided with an air outlet channel.    USE - Used as a laboratory biological carbon carbonization furnace.    ADVANTAGE - The furnace is safe, economical and energy-saving, has high preparing efficiency, and satisfies the laboratory research requirements of biological carbon.    DETAILED DESCRIPTION - Laboratory biological carbon carbonization furnace comprises a feeding tank, a heating steel pipe, a resistance wire, a temperature sensor, a shell and a cover. The feeding tank is a hollow steel drum structure with an upper end opening and sealed bottom. The heating steel pipe is an annular barrel-shaped structure with an upper end opening and sealed bottom. The feeding tank is inserted into the heating steel pipe. The heating steel pipe is externally arranged with a heating layer. The heating layer is a heating resistance wire wound with insulating porcelain beads and covered with a heat insulating layer. The temperature sensor is arranged between the heating layer and the heat insulating layer. The upper cover is provided with an air outlet channel. A fixed switch is arranged between the shell and the cover.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the laboratory biological carbon carbonization furnace.
NOVELTY - The system has winnowing device that is connected with a garbage unit. Garbage-crushing device is connected with winnowing device, for receiving the data from separation device to the combustible garbage. Garbage curing device is used for receiving the crushed combustible garbage, and crushing device is connected with the garbage-curing device for recrushing curing of combustible waste. Drying device is connected with secondary crushing device, and hot melting device is connected with the drying device used for drying the burnable garbage hot-melting extruding molding.    USE - System for treating garbage.    ADVANTAGE - Manufacturing cost of the garbage treating system can be reduced. Recycling of waste can be realized, and the utilization rate of waste can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for treating sludge and garbage.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the system for treating garbage. (Drawing includes non-English language text)
NOVELTY - Organic fertilizer is prepared by (a) pre-processing raw materials, (b) turning pre-processed raw materials, (c) fermenting pre-processed raw materials, (d) adding inorganic fertilizer to the fermented material, (e) crushing the obtained product, (f) sieving the crushed product, (g) drying the sieved product, (h) checking quality of the product, and (i) packing the product. In turning and fermentation step, weight ratio of bone residue, organic material, bacterial enzyme and water is 100:(5-70):(1-15):(5-100).    USE - As organic fertilizer (claimed).    ADVANTAGE - The organic fertilizer is rich in nitrogen, phosphorus and potassium elements, provides organic matter for growth of crops, and hence capable of continuously providing outpouring nutrients for crops.    DETAILED DESCRIPTION - Organic fertilizer is prepared by (a) pre-processing raw materials, (b) turning pre-processed raw materials, (c) fermenting pre-processed raw materials, (d) adding inorganic fertilizer to the fermented material, (e) crushing the obtained product, (f) sieving the crushed product, (g) drying the sieved product, (h) checking quality of the product, and (i) packing the product. In turning and fermentation step, weight ratio of bone residue, organic material, bacterial enzyme and water is 100:(5-70):(1-15):(5-100), and the fermentation is performed at 5-55 degrees C for 20-240 hours. In step (d), weight ratio of fermented material and inorganic fertilizer is 100:(0-90). In step (f), the crushed product is sieved using 10-300 mesh size sieves. An independent claim is included for method for preparing the above-mentioned organic fertilizer, which involves performing the above-mentioned method.
NOVELTY - Preparing fertilizer comprises (i) performing sterilization process of fresh wet poultry excrement, (ii) fermenting the poultry excrement, (iii) deodorizing the fermented poultry excrement by adding attapulgite, and forming strong chelate by using attapulgite and poultry excrement nutrients, and (iv) pulverizing the poultry excrement to form granular organic fertilizer.    USE - Used as a fertilizer.    ADVANTAGE - The method utilizes attapulgite and free organic nitrogen, phosphorus and potassium to form strong chelate.
NOVELTY - Fertilizer comprises poultry manure (1-2 wt.%), biological bacterium (0.5-1 wt.%), organic matter (20-40 wt.%), silicon fertilizer (2-5 wt.%), water retention agent (1-2 wt.%) and micro-element comprising calcium (2-5%), magnesium (2-5%), sulfur (2-5%), zinc (0.2-0.5%) and boron (0.1-0.2%).    USE - The fertilizer is useful for repairing soil (claimed).    ADVANTAGE - The fertilizer repairs the soil without deposition of inorganic salt and potassium phosphate thus avoiding hardening of the soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the fertilizer, comprising introducing poultry manure, biological bacterium (14%) and dry biogas fertilizer (30%) with uniform water content (45%) in a sealed fermentation excrement storage tank and then fermenting at 60-65 degrees C for 7-10 days, turning the fermented tank using a front walking type automatic upender for 3 days and then first time fermenting for 3-4 times for every 2 days and second time fermenting at 60-65 degrees C for absorbing organic matter, reducing the temperature to 30 degrees C until water content reaches less than 30%, polishing the finished product at low temperature and then storing in a warehouse.
NOVELTY - A bentazone agent is prepared by performing closed loop washing kettle with organic phase after washing with water, adding activated carbon and dry blowing; adding 32% caustic soda liquid to kettle, and adding tap water to prepare 5-31% alkali; slowly dripping dilute alkali, controlling temperature at 25-60 degrees C, adjusting pH value to 3-11; standing for 2 hours and taking upper layer water phase material frame; transferring water phase kettle, sampling and measuring; concentrating, adding liquid alkali to adjust pH value, adding stabilizing agent, and slowly opening salt water.    USE - Method for preparing bentazone agent (claimed).    ADVANTAGE - The method is environment-friendly, has reduced acid and alkali consumption than conventional method, reduces strong acid wastewater production, and improves quality of product.    DETAILED DESCRIPTION - Bentazone agent is prepared by performing closed loop washing kettle with organic phase after washing with water, adding activated carbon, constant temperature stirring for 30 minutes by plate-and-frame filter to extract, and dry blowing for 30 minutes; adding 32% caustic soda liquid to kettle, and adding tap water to prepare 5-31% alkali; slowly dripping dilute alkali, controlling temperature at 25-60 degrees C, adjusting pH value to 3-11; standing for 2 hours and taking upper layer water phase material frame; transferring water phase kettle, sampling and measuring; concentrating, adding liquid alkali to adjust pH value to 7, adding stabilizing agent, stirring for 1 hour, and slowly opening salt water; and sampling and measuring product content, pumping 2% liquid surfactant, stirring for 30 minutes, and pumping finished product storage tank.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic block diagram illustrating a preparation method of bentazone agent. (Drawing includes non-English language text).
NOVELTY - Production of biodiesel oil comprises: mixing catalyst, raw oil and short chain alcohol, performing biocatalytic reaction in stirred reactor or fixed bed reactor at 32-55 degrees C for 35-40 hours, collecting reaction liquid, carrying out distillation to recover alcohol, reacting, centrifugally separating to obtain 77-89.3 wt.% fatty acid ester; and performing chemical catalytic reaction by adding 2-8 wt.% acid catalyst and methanol and reacting at 60-90 degrees C for 2-8 hours to obtain 97-99 wt.% fatty acid ester. The raw oil is vegetable oil, animal oil or waste cooking oil.    USE - Method for producing biodiesel oil.    ADVANTAGE - The method has convenient operation, low raw material consumption, high conversion rate, low production cost and environment-friendly process.
NOVELTY - Preparing organic fertilizer, comprises collecting tree leaf garbage and then crushing at 80-120 degrees C, uniformly mixing corn and wheat bran to concentrate and then granulating, and drying the granulated mixture, carbonizing branches class garbage with a diameter of 3 cm and then steam activation, crushing and drying the semi-finished products to obtain charcoal, carrying out carbonization and steam activation of the product, pruning the lawn flower generated by the branches and leaves and plant ash and then carbonizing to produce charcoal powder and then mixing animal manure for fermentation.    USE - The method is useful for preparing organic fertilizer (claimed).
NOVELTY - A biological organic fertilizer comprises 80% high-temperature fermentation raw fertilizer, 10% sodium silicate, 3% urea, 2% potassium chloride, 5% calcium and magnesium phosphate, 0.1% carrier rich root growth agent, 0.1% soil conditioner and 0.1% microbial strain.    USE - Biological organic fertilizer.    ADVANTAGE - The fertilizer has high-standard product orientation, high quality and high efficiency, and promotes development of organic agriculture.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing a biological organic fertilizer.
NOVELTY - Ester exchange reaction of natural oil and 1-3C lower alcohol is carried out in catalyst, and fatty acid ester as an ester exchange product and dimaleate are heated under protection of nitrogen in a cycloaddition catalyst at 160-280 degrees C and reacted for 3-12 hours. The reaction product is cooled to 120-240 degrees C, vacuumized, vacuum degree is maintained at more than 750 mm mercury, and distilled under reduced pressure. Lower layer containing glycerin byproduct is obtained. The distillate is the biodiesel oil (fatty acid ester) and the residue is the 22C-cyclic fatty triacid ester.    USE - Manufacture of biodiesel oil and 22C-cyclic fatty triacid ester.    ADVANTAGE - 22C-cyclic fatty triacid ester serving as a chemical product with high additional value is produced using fatty acid ester having two or more double bonds, when the biodiesel oil is prepared, such that the production cost is reduced.    DETAILED DESCRIPTION - Natural oil is decompressed and dehydrated. Ester exchange reaction of natural oil and 1-3C lower alcohol is carried out in the presence of catalyst, and fatty acid ester as an ester exchange product and dimaleate are heated under the protection of nitrogen in the presence of a cycloaddition catalyst at 160-280 degrees C and reacted for 3-12 hours. The reaction product is cooled to 120-240 degrees C, vacuumized, vacuum degree is maintained at more than 750 mm mercury, and distilled under reduced pressure. Lower layer containing glycerin byproduct is obtained. The distillate is the biodiesel oil (fatty acid ester) and the residue is the 22C-cyclic fatty triacid ester. The molar ratio of oil and alcohol is 1:3-1:10. The molar ratio of maleate and linoleate is 0.9-1.1.
NOVELTY - Low-carbon production of water-soluble fertilizer comprises preparing fluorophosphate by removing suspended matter from wet-process phosphoric acid to obtain a slurry, adding 2 wt.% sodium chloride or sodium sulfate, stirring for 40-60 minutes, reacting at 30 degrees C, removing precipitate, washing the precipitate, and drying; removing heavy metals by neutralizing with liquid ammonia, controlling pH at 6, adding 1 wt.% heavy metal remover, stirring at 30 degrees C for 30 minutes, filtering, mixing filtrate with potassium fertilizer, and mixing; and adding 5-10 wt.% seed crystal, and granulating.    USE - Method for the low-carbon production of water-soluble fertilizer (claimed).    ADVANTAGE - The fertilizer is safe and environment-friendly.
NOVELTY - The device has a crystallizing tank (1) that is connected with outlet of a stirring feeding jar and is connected with the outlet of a feeding tank (2). A charging unit is set on the lower portion of a lower discharging centrifuge and is connected with a loading unit. The loading unit is connected with a sealing pipe which is set above the feeding tank. The lower discharging centrifuge is provided with a full-automatic scraper (3). The feeding tank is connected to a vibration fluidized bed (5), to crush the material introduced by the vibration of the vibration fluidized bed.    USE - Device for processing refined acetaminophen.    ADVANTAGE - The production efficiency of the refined acetaminophen processing device can be improved with less manual effort. The occurrence of the pollution during the operation of the refined acetaminophen processing device can be avoided. The cost of the refined acetaminophen processing device can be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for processing refined acetaminophen.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the refined acetaminophen processing device. (Drawing includes non-English language text)    Crystallizing tank (1)    Feeding tank (2)    Full-automatic scraper (3)    Vibration fluidized bed (5)    Stainless steel pipe (6)
NOVELTY - 4-Methyl-1,3-thiazole-5-carbaldehyde is obtained by reacting methyl 3-oxo-butyrate with bromine and ethanol, reacting obtained 2-amino-4-methyl-thiazole-5-carboxylic acid methyl ester with sodium hypophosphite, sodium nitrite, and sulfuric acid, and reacting obtained 4-methyl-thiazole-5-carboxylic acid with potassium borohydride, lithium chloride, sodium hypochlorite, and sodium bromide.    USE - Synthesis of 4-methyl-1,3-thiazole-5-carbaldehyde for use as intermediate of cefditoren pivoxil used in pharmaceuticals.    ADVANTAGE - The method enables simple and environmentally-friendly synthesis of 4-methyl-1,3-thiazole-5-carbaldehyde with high yield.
NOVELTY - An azithromycin is directly crystallized in aqueous phase by taking aqueous solution of azithromycin salt and stirring in container, preparing 0.1-0.5 mol/L of sodium hydroxide solution using 1-4C alkyl alcohol and dropping into aqueous solution of azithromycin salt at 10-50 degrees C while stirring at 50-160 rpm until pH 9-11, cooling to 0-10 degrees C, crystallizing for 0.5-5 hours, filtering, washing obtained white crystal with water, and vacuum drying.    USE - Method for direct crystallization of azithromycin in aqueous phase (claimed).    ADVANTAGE - The method provides azithromycin crystal having good stability, high content, and low content of related substance. It is simple and suitable for industrial operation with high product yield, good quality and reduced energy consumption.
NOVELTY - A fludarabine is synthesized by putting 2-fluoro-9- beta -D-(2',3',5'-di-tri-alkoxy arabinose furan)adenine as raw material, sodium hydroxide and mixed solution of concentrated ammonia water as reagent into solvent; and reacting with glacial acetic acid and filtering to obtain coarse solid through re-crystallizing and decoloring by active carbon to obtain pure fludarabine.    USE - Method for synthesis of fludarabine (claimed).    ADVANTAGE - The method is environment-friendly, and has simple and safe operation, short reaction time and cheap raw material. The product is easy to be purified.
NOVELTY - Bio-organic and inorganic fertilizer is prepared by uniformly mixing organic material, performing fermentation, and then adding 4% trace elements comprising nitrogen, phosphorus and potassium, 0.3% rare earth and 30% or more organic matter, where the organic material comprises fresh chicken manure, 10% modified rare earth, filter mud, trace element and peat.    USE - As bio-organic and inorganic fertilizer.    ADVANTAGE - The preparation method has less investment and simple production process and can be widely used as soon as being mixed by raw materials such as rare earth, common farmers can produce biological organic (completely ripe) fertilizers meeting agriculture and forestry as long as the strains are selected and a production technique is mastered, as the biological organic fertilizer and a chemical fertilizer are separately stored and used as soon as being mixed, smaller influences on the activity of beneficial bacteria are achieved and the integrity of the fertilizer can be preferably developed.
NOVELTY - Royal jelly, honeybee pupae, honey and yeast are mixed and fermented at constant temperature, to obtain material (A). Golden cypress, light-yellow Sophora root and balsam pear are soaked in water, yeast is added and fermented at constant temperature, water is added and boiled, to obtain material (B). Amino acid or humic acid and wormwood are mixed and soaked in water, yeast is added and fermented, water is added to resultant mixture and boiled, to obtain material (C). The material (B) and (C) are mixed, filtered and added to material (A), to obtain plant fertilizer.    USE - Manufacture of plant fertilizer (claimed).    ADVANTAGE - The plant fertilizer is manufactured effectively with reduced amount of water-insoluble substance.    DETAILED DESCRIPTION - Royal jelly, honeybee pupae, honey and yeast are mixed and fermented at constant temperature, to obtain material (A). Golden cypress, light-yellow Sophora root and balsam pear are mixed, soaked in water, yeast is added, fermented at constant temperature, water is added to resultant mixture and boiled, to obtain material (B). Amino acid or humic acid and wormwood are mixed, soaked in water, yeast is added, fermented at constant temperature, water is added to resultant mixture and boiled, to obtain material (C). The material (B) and (C) are mixed, filtered and added to material (A), to obtain plant fertilizer.
NOVELTY - Producing tylosin comprises using tylosin waste to replace organic nitrogen sources of tylosin culture medium.    USE - The method is useful for producing tylosin (claimed).    ADVANTAGE - The method recycles waste to replace part of organic nitrogen source in the culture medium so as to effectively reduce the protein in tylosin waste and produces tylosin in a cost effective manner.
NOVELTY - Device comprises fluorine-silicon separator, an ammonolysis reaction tank, ammonolysis slurry pump and pipelines for connecting each device. The fluorine-silicon separator comprises an upper cylindrical shaped ammonium fluoride separation zone and a lower inverted cone shaped silicon dioxide separation zone. The upper cylindrical shaped structure of the fluorine-silicon separator is connected with the ammonolysis reaction tank and the ammonolysis slurry pump. The bottom inverted cone shaped structure is connected with a centrifuge for separating silicon dioxide via a three-way valve.    USE - The device is useful for separating fluorine and silicon in fluorine-silicon mixture (claimed) and in phosphate fertilizer production enterprises.    ADVANTAGE - The device: ensures simple and stable operation; saves material resources and reduces labor intensity; ensures the production of high purity ammonium fluoride and silicon dioxide, and complete separation of the products; has good screening effect and does not affect the health of the operator; and is environmentally friendly.
NOVELTY - Methane-enriched gas is produced by preparing oxygen-enriched component, performing oxygen-enriched combustion of coal tar using carbonization unit comprising oxygen supply unit and carbonization furnace combustion chamber which has combustion chamber temperature control component e.g. carbon dioxide, methane, hydrogen, carbon monoxide, and/or hydrogen sulfide, performing desulfurization process, purifying with purifying unit to produce desulfurized and purified gas, and performing methanation reaction in the presence of methanation catalyst using methanation unit.    USE - Production of methane-enriched gas for coal carbonization (claimed).    ADVANTAGE - Effective component loss rate is low. Carbon dioxide gas with high purity can be obtained.    DETAILED DESCRIPTION - Methane-enriched gas is produced by preparing oxygen-enriched component, performing oxygen-enriched combustion of coal tar using carbonization unit comprising oxygen supply unit and carbonization furnace combustion chamber which has combustion chamber temperature control component e.g. carbon dioxide (CO2), methane (CH4), hydrogen (H2), carbon monoxide (CO), and/or hydrogen sulfide (H2S), performing desulfurization process, purifying with purifying unit to produce desulfurized and purified gas, performing methanation reaction in the presence of methanation catalyst using methanation unit, wherein sulfur content of methanation catalyst is less than that of raw material gas, and purifying.
NOVELTY - A fertilizer comprises 55-58 wt.% bamboo powder, 29.6-30.1 wt.% sugarcane filter mud, 8.03-9.76 wt.% sugarhouse alcohol waste liquid, 4-4.6 wt.% bioactive material and 0.37-0.54 wt.% bioactive strain, as raw materials. The moisture content of sugarcane filter mud is 60-70%. The sugarhouse alcohol wastewater has Brix of 55 degrees .    USE - Fertilizer is used for Mao bamboo shoots (claimed).    ADVANTAGE - The fertilizer provides high-quality Mao bamboo shoots with high yield.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) production of fertilizer, which involves mixing the raw materials, stirring in a double-shaft stirrer, uniformly stirring, piling with width of 1.2-1.5 m and height of 0.8-1 m in unlimited length pile, carrying out fermentation at 60-65 degrees C for 20-25 days, obtaining biological decomposition of organic fertilizer, applying turning machines for each 3-3.5 days turning once, and bagging obtained bioorganic fertilizer; and    (2) application of fertilizer for Mao bamboo shoots, which involves planting 3-6 years aged bamboo management per acre of 180-200 plant of the bamboo shoot, applying 240-250 kg of fertilizer per acre of bamboo shoots, adding fertilizer with dosage of 100 kg per acre during last ten-days of October, second time adding fertilizer with dosage of 100 kg per acre during mid-February of next year, third time adding fertilizer with dosage of 40-50 kg per acre during last ten-days of May of next year, cultivators ditching, after fertilizing covering soil with 0.1 m tread tightly, and coupling with soil filled surface of ditch which is in rectangular shape with a depth of 0.3-0.4 m.
NOVELTY - Blue algae are subjected to cell disruption to obtain a blue algae disrupted mixed solution. The blue algae disrupted mixed solution is subjected to microbial inoculation fermentation in an anaerobic state to obtain fermentated liquid. The fermentated liquid is deodorized and deslagged to obtain liquid organic fertilizer.    USE - Manufacture of organic fertilizer (claimed).    ADVANTAGE - The environmentally-friendly organic fertilizer is economically manufactured with reduced energy consumption and emission reduction.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fermentation reactor, which has a fermentation tank, an ultrasonic crushing instrument, aeration component provided on the a discharging pipe at bottom of the fermentation tank and having an ultrasonic crushing head provided on the fermentation tank, and ultrasonic generating controller of liquid inlet pipe and vent-pipe provided on the fermentation tank and electrically connected with a aeration assembly having an air blower, and a aeration head connected with the aeration component on the inner wall of the fermentation tank through air blower.
NOVELTY - A Bacillus subtilis G-I strain (CCTCC M 2012287), is new.    USE - The B.subtilis G-I strain is useful for preparing fertilizer used for preventing crops from Fusarium wilt disease (all claimed). The crop is melon.    ADVANTAGE - The fertilizer promotes growth and fruit production of plant, improves root development of plant, and increases commodity yield of crop.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) method for preparing microbial fertilizer, involves (a) inoculating the B.subtilis strain in solid inclined plane, and culturing at 30-35 degrees C for 16-24 hours, (b) inoculating 1000 ml of the culture liquid in first level seed liquid culture medium, and shaking the culture for 16-24 hours at 30-35 degrees C and 200-300 revolutions per minute (rpm), (c) inoculating obtained culture liquid in fermentation tank containing fermentation culture medium, maintaining temperature at 30-35 degrees C for 16-20 hours, maintaining rotation speed at 200-300 rpm, maintaining ventilation rate at 0.5-0.8 cubic meter/minute, and carrying out fermentation culture, (d) changing temperature and air flow condition, when the bacteria spore forming rate reaches 75%, ending fermentation, preparing fermentation liquid, and adding diatomite to the fermentation liquid in the mass ratio of 5:2-5:3, and (e) adding base fertilizer to the obtained mixture, mixing the obtained mixture, air-drying the obtained mixture at 70 degrees C for 3-4 hours, when the moisture content of the mixture reaches 5% or less, drying and crushing the obtained mixture to 100 meshes, and packaging the obtained product; and (2) microbial fertilizer prepared by the above-mentioned method.
NOVELTY - An organic solid waste is mixed, fermented for 7 days or more, decomposed, crushed, and nitrogen, phosphorus and potassium are added. Molasses alcohol waste liquid is added to evaporating container, and surface active agent is added, processed at 80-100 degrees C and vacuum degree of -0.05 to -0.09 MPa, and concentrated for 30-120 minutes. The evaporation is stopped to obtain concentrate, which is pelletized. The pellets are dried to obtain organic fertilizer product. Thus, comprehensive utilization of organic solid waste and molasses alcohol wastewater is enabled.    USE - Comprehensive utilization of organic solid waste and molasses alcohol wastewater.    ADVANTAGE - The organic solid waste and molasses alcohol wastewater are efficiently utilized for preparation of ecological organic fertilizer.    DETAILED DESCRIPTION - An organic solid waste is uniformly mixed, fermented for 7 days or more at temperature of more than 50 degrees C, decomposed, crushed, and nitrogen, phosphorus and potassium are added in amount of 4-15 wt.% and mixed. Molasses alcohol waste liquid is added to evaporating container, and surface active agent is added, processed at 80-100 degrees C and vacuum degree of -0.05 to -0.09 MPa, evaporated and concentrated for 30-120 minutes such that water content is 35-45%. The evaporation is stopped to obtain concentrate, which is pelletized. The pellets are dried to obtain organic fertilizer product. The organic solid waste is livestock and poultry excrement, starch residue, monosodium glutamate factory leftovers and straw. The surface active agent is anionic surfactant, cationic surfactant or non-ionic surfactant having carbon number of 12-32. The addition amount of molasses alcohol waste liquor is 0.2-1.5%. Thus, comprehensive utilization of organic solid waste and molasses alcohol wastewater is enabled.
NOVELTY - Preparing organic fertilizer, involves mixing rotten chicken manure and algal mud in the ratio of 9.3:0.7, fermenting the mixture initially at 50 degrees C or less for 6 days and then fermenting the obtained product at 60 degrees C or less during process completion, where the water content of the organic fertilizer is less than 30%, decomposing the fermented mixture, and packaging product. The mass ratio of chicken manure, organic matter, nitrogen and water in the fertilizer is 98% or more, 45% or more, 2-3% and 25-30%, respectively.    USE - The method is useful for preparing organic fertilizer which is useful for promoting growth of crops e.g. industrial crops and food crops.    ADVANTAGE - The organic fertilizer is rich in beneficial amino acids, and has free amino acid content of 8.4 g/kg.
NOVELTY - A blue-green algae and polluted bottom sediment composite fertilizer is obtained by removing heavy metal in polluted bottom sediment by bioleaching, mixing blue-green algae and bottom sediment, regulating physicochemical property of the mixture of blue-green algae and the bottom sediment to condition needed by growth of aerobic fermentation microorganisms by adding conditioner by characteristics of high water content of the blue-green algae and C/N ratio imbalance, adding nitrogen conserving agent, and performing forced ventilation fermentation in a compost factory for 20 days.    USE - Blue-green algae and polluted bottom sediment composite fertilizer.    ADVANTAGE - The blue-green algae and polluted bottom sediment composite fertilizer is environmentally-friendly. The temperature of the compost is increased to more than 60 degrees C within short time, the high-temperature fermentation period is kept for 15 days, and the compost is transferred in a secondary fermentation zone till the compost is decomposed thoroughly after the high-temperature fermentation period is ended.
NOVELTY - The household anaerobic digester comprises an insulated housing divided into partitions communicating consistently with one another, a fermentation chamber, filling and discharge pipes, water seal for removal of biogas, a boot outlet valve, a casing, a gap resistance heater, and fill valve. The partitions are drilled and installed in a building, and are positioned one above the other. The casing is made of two insulation layers with a gap. Each layer comprises inner and outer heat-insulating layers. The gap resistance heater is distributed over a surface of the inner insulating layer.    USE - Used as a household anaerobic digester.    DETAILED DESCRIPTION - The household anaerobic digester comprises an insulated housing divided into partitions communicating consistently with one another, a fermentation chamber, filling and discharge pipes, water seal for removal of biogas, a boot outlet valve, a casing, a gap resistance heater, and fill valve. The partitions are drilled and installed in a building, and are positioned one above the other. The casing is made of two insulation layers with a gap. Each layer comprises inner and outer heat-insulating layers. The gap resistance heater is distributed over a surface of the inner insulating layer. The fill valve acts as a petal type flexible flat sleeve freely lying on top of the partition. An inner surface of the casing is coated with corrosion polymer coating. The gap between the insulation layers is placed in a temperature sensor. The outside digester is enclosed by a hard shell.
NOVELTY - Bacillus licheniformis A3 BCRC 910522 and Bacillus subtilis H8 BCRC 910523 were isolated from the preparation of agricultural wastes and livestock wastes composts and biofertilizers. Both of them can grow at 25 DEG C and 50 DEG C, solubilize tricalcium phosphate, iron phosphate, aluminum phosphate, hydroxyapatide, Israel rock phosphate, feldspar, illite and kaolinite, and have amylase, cellulase, chitinase, pectinase, protease, lipase, xylanase and keratinase activities. Inoculation of these multi-functional thermo-tolerant phosphate- and potassium-solubilizing microbes into agriculture, livestock, and poultry wastes during biofertilizers preparation increased the biofertilizer temperature, decreased the total organic carbon content and C/N ratio, increased the total nitrogen content and germination rate of alfalfa seed, elevated the soluble phosphate and soluble potassium contents, accelerated the maturity rates, improved the qualities of biofertilizers, and increased the populations of mesophilic and thermo-tolerant phosphate- and potassium-solubilizing microbes during the preparation of composts and biofertilizers. Therefore, the thermo-tolerant multiple-functional phosphate- and potassium-solubilizing microbes B. licheniformis A3 BCRC 910522 and B. subtilis H8 BCRC 910523 are very important in bioresources recycling, agricultural applications, environment protection and prospective for sustainable agriculture.
NOVELTY - Production of a bioliquid or biofuel, comprises: (i) providing a biomass of fungi, preferably yeasts, either deactivated or inactive; (ii) subjecting the biomass to mechanical liquefaction to obtain a solid phase and a first gas phase; (iii) subjecting the first gas phase to condensation to obtain the bioliquid or biofuel and a second gas phase; and (iv) subjecting the bioliquid or biofuel to at least one process of upgrading.    USE - The process is useful for producing a bioliquid or biofuel (claimed).    ADVANTAGE - The process produces biodiesel which finds application as fuel in the transport sector and as combustible in the production of electrical energy and heat. Also, the process is fast and economical.    DETAILED DESCRIPTION - Production of a bioliquid or biofuel, comprises: (i) providing a biomass of fungi, preferably yeasts, either deactivated or inactive; (ii) subjecting the biomass to mechanical liquefaction to obtain a solid phase and a first gas phase; (iii) subjecting the first gas phase to condensation to obtain the bioliquid or biofuel and a second gas phase; and (iv) subjecting the bioliquid or biofuel to at least one process of upgrading to obtain at least one from among: elimination of solid residue, improvement of pH, deoxygenation, increase of calorific power, and decrease of viscosity, obtaining at the end the industrially usable bioliquid or biofuel.
NOVELTY - The gasifier (1) has a gasification furnace (20) which gasifies a fuel (5) and comprises an inner cylinder (23) that introduces the fuel and air in gasification furnace. A fuel supply apparatus (10) supplies a fuel to gasification furnace. A fuel detection unit detects accumulation height of fuel deposited inside the inner cylinder as a level in a furnace. A control apparatus (28) calculates deviation of level target value in furnace and level in furnace and controls fuel supply apparatus so that level in furnace becomes target value in furnace.    USE - Gasifier for gasifying biomass fuel.    ADVANTAGE - The generation of the clinker resulting from ashy fusion can be prevented, while being able to generate little stable gas. The level of fuel in furnace is fluctuated according to the combustion state in furnace. The injected quantity of fuel is controllable to maintain the fuel level suitable for gasification. The generation of tar can be prevented. Since the quantity of the fuel supplied to inner cylinder is controlled, the stable gasification can be attained.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the gasifier. (Drawing includes non-English language text)    Gasifier (1)    Fuel (5)    Fuel supply apparatus (10)    Gasification furnace (20)    Inner cylinder (23)    Control apparatus (28)
NOVELTY - Preparing a diaryl ether, comprises dehydrating an aromatic alcohol compound over a dehydration catalyst, where the dehydration catalyst comprises an oxide of yttrium.    USE - The method is useful for preparing diaryl ether, preferably diphenyl oxide (claimed) which is used as high temperature solvents, as intermediates in preparing flame retardants and surfactants, as components in heat transfer fluids, as high performance lubricants and as intermediates in preparing pyrethroid insecticides.    ADVANTAGE - The method utilizes a yttrium oxide catalyst (claimed) which: is inexpensive and non-radioactive, thus eliminating the safety and environmental issues; and exhibits good selectivity for the desired product with relatively low formation of undesirable byproducts.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing a heat transfer fluid, comprising preparing the diaryl ether by contacting the aromatic alcohol compound with the dehydration catalyst, isolating the diaryl ether from the dehydration catalyst, and mixing the isolated diaryl ether with biphenyl, where the mixture forms a eutectic mixture.
NOVELTY - Production of tetrachloromethane, comprises catalyzing the chlorination of a feedstream comprising partially chlorinated methanes with a free radical catalyst.    USE - The method is useful for producing tetrachloromethane (claimed), which is useful as feedstocks in the synthesis of refrigerants and other commercial products.    ADVANTAGE - The method ensures safe and cost-effective production of tetrachloromethane with high yield and selectivity in an environmentally friendly manner without requiring high temperatures and/or pressures.
NOVELTY - A supported mono-metallic platinum-containing catalyst is obtained by obtaining a platinum-containing organic precursor by extraction of platinum compound from hydrochloric acid solution with trioctylamine solution in toluene, impregnating a carrier with the precursor solution, drying the carrier, and pyrolytically reducing platinum. Glycerol reduction by molecular oxygen is carried out in the presence of the obtained catalyst in alkaline aqueous solution.    USE - Manufacture of lactic acid from glycerol obtained as by-product of biodiesel fuel production process. Uses include but are not limited to food manufacture, pharmaceuticals, cosmetics, and production of biodegradable polylactic acid for medical applications.    ADVANTAGE - The method enables selective and active simple, economical and environmentally-friendly catalyst synthesis for obtaining lactic acid using glycerol oxidation by molecular oxygen in constructively simple equipment in mild conditions. Clean raw materials are not necessary for obtaining catalysts organic precursors (platinum purification from impurity is carried out during extraction). Reuse of platinum-based technological solutions and secondary raw materials is possible. Metal losses are prevented during carrier impregnation and metal reduction. The use of chemical reducing agents is not required, because platinum reduction occurs during the pyrolysis. The method allows modification and optimization of composition of catalysts, structure and properties in wide range for the selective lactic acid obtaining using oxidation of glycerol by molecular oxygen.
NOVELTY - Making a fertilizer, comprises: in a first mixer, mixing an organic sludge with a force to produce a paste; adding acid to the paste to produce an acidic paste in the first mixer; transferring the acidic paste to one of three pressure vessels; blending the paste with ammonium salts in the one pressure vessel; reacting the acidic paste under high atmospheric pressure and temperature within the one pressure vessel; emptying the one pressure vessel into a second mixer; mixing a pH control agent/hardening agent with the paste in the second mixer; and removing water to form a fertilizer.    USE - The method is useful for manufacturing a fertilizer. No biological data given.    ADVANTAGE - The simple and cost-effective method provides fertilizers with improved physical stability, chemical stability and nutrient properties. The fertilizers are environmentally friendly.    DETAILED DESCRIPTION - Manufacturing a fertilizer, comprises: in a first mixer, mixing an organic sludge with a force sufficient to produce a paste; adding acid to the paste to produce an acidic paste in the first mixer; transferring the acidic paste to one of three pressure vessels; blending the acidic paste with ammonium salts in the one pressure vessel; reacting the acidic paste under high atmospheric pressure and temperature within the one pressure vessel; emptying the one pressure vessel into a second mixer; mixing at least one member consisting of a pH control agent or a hardening agent with the reacted paste in the second mixer; and removing water to form a fertilizer, where while a first pressure vessel is filling, a second pressure vessel is reacting, and a third pressure vessel is emptying to create a batch system.
NOVELTY - The equipment has a primary treatment tank (S1) into which the waste water (W0) is introduced. The to-be-processed water (W2) is circulated inside the primary treatment tank. A return pipe (30) is connected to the primary treatment tank. The return pipe is arranged in the front end of the bottom wall vicinity in the primary treatment tank, so that to-be-processed water is made to flow out of the outflow hole formed in the front end side in the sludge (H) deposited in the primary treatment tank.    USE - Equipment such as purification tank for treating industrial waste water.    ADVANTAGE - Since the necessity of the pump for stirring the anaerobic filter bed and to-be-processed water and sludge becomes unnecessary, the manufacturing cost of the waste water treatment equipment is reduced. Since the periodic cleaning of the purification tank is performed efficiently, the waste water treatment equipment is maintained easily.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for wastewater treatment method.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the waste water treatment equipment.    Return pipe (30)    Sludge (H)    Primary treatment tank (S1)    Waste water (W0)    To-be-processed water (W2)
NOVELTY - The system has a denitrifying apparatus (40) that carries out the anaerobic ammonia oxidation treatment of an electron donor and the nitrite nitrogen for ammonia nitrogen as an electron acceptor by the autotrophic denitrifying microorganisms in anaerobic conditions. The nitrite nitrogen is restored to a nitrogen molecule by heterotrophic denitrifying microorganisms. The transfer path (R1) is provided to supply the liquid from which suspensible organic substance is removed by the suspensible organic substance separation apparatus (10) to the denitrifying apparatus.    USE - System for processing suspensible organic matter containing wastewater.    ADVANTAGE - The processing of the suspensible organic matter containing wastewater which reduce leak of nitric acid can be achieved, even if the wastewater containing high concentration suspensible organic substance. The amount of nitric acid and the amount of organic substance of the processing system discharged out of the system can be reduced. The organic substance contained in the digestive liquid of the sludge anaerobic digester can be reduced. The electric power cost for aeration and the chemical cost can be reduced. The denitrifying ability can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for processing method of suspensible organic matter containing wastewater.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the processing system. (Drawing includes non-English language text)    Suspensible organic substance separation apparatus (10)    Sludge anaerobic digester (20)    Nitritation apparatus (30)    Denitrifying apparatus (40)    Transfer path (R1)
NOVELTY - Treating (I) ethanol production byproduct, comprises: (a) providing a wet distillers grain; and (b) contacting the wet distillers grain with a solution containing at least one alpha -hydroxysulfonic acid, thus hydrolyzing the wet distillers grain to produce at least one fermentable sugar containing product.    USE - The method is useful for treating ethanol production byproduct (fermentable sugar containing product) (claimed) which is useful for the production of biofuels or ethanol.    ADVANTAGE - The method: utilizes the alpha -hydroxysulfonic acid that can be easily removed from the product and recycled; and produces significant amounts of glucose in addition to xylose such that a subsequent hydrolysis by other conventional methods (e.g., enzyme hydrolysis) may not be necessary.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for: method (II) for treating ethanol production byproduct, comprising: (a1) providing grain, (b1) grinding the grain to produce ground grain, (c1) treating the ground grain to produce a fermentable sugar mixture, (d1) fermenting the fermentable sugar mixture to produce fermented product containing ethanol, solids and water, (e1) separating the fermented product to produce ethanol and stillage, and (f1) contacting at least a portion of the stillage with a solution containing the alpha -hydroxysulfonic acid thus hydrolyzing the stillage to produce at least one fermentable sugar containing product; or steps (a1)-(e1) as above per se, (f2) separating stillage to produce thin stillage and wet distillers grain, and (g2) contacting at least a portion of the wet distillers grain with the solution.
NOVELTY - Converting lignocellulosic biomass into fuel, comprises: (a) converting lignocellulosic biomass into fuel and producing aqueous waste stream comprising at least one dissolved organic material and at least one dissolved sulfur-containing compound, where aqueous waste stream has sulfur content of more than 400 parts per million by weight (ppmw); and (b) treating aqueous waste stream, where treating comprises anaerobic digestion of mixture (M1) comprising first aqueous feed (10) containing aqueous waste stream and second aqueous feed (12), and mixture (M1) has sulfur content of at most 400 ppmw.    USE - The process is useful for converting lignocellulosic biomass into a fuel.    ADVANTAGE - The process: provides high conversion level of the dissolved organic materials and a high yield of biogas; and facilitates the recycling of aqueous liquid, thus provides improved water footprint of the whole of the process.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a treating step.    First aqueous feed (10)    Second aqueous feed (12)    Reactor (14)    Separator (20)    Aqueous liquid (26)
NOVELTY - Synthesizing functionalized pyrazolidines (I) with enatioselectivity (75-98%) and distereoselctivity (99-100%) via tandem alpha -amination Corey Chaykovsky reaction of aldehydes, comprises reacting an alpha -unsubstituted aldehyde with azodicarboxylates at 0-20 degrees C in presence of L-proline in a solvent to obtain alpha -hydrazino aldehydes, and subjecting the alpha -hydrazino aldehydes to insitu Corey Chaykovsky reaction at -4 degrees C to -6 degrees C.    USE - The method is useful for synthesizing functionalized pyrazolidines (claimed).    ADVANTAGE - The method allows simple and economical synthesis of functionalized pyrazolidines with high yield and excellent enantioselectivity and disterioselectivity in an eco-friendly manner.    DETAILED DESCRIPTION - Synthesizing functionalized pyrazolidines of formula (I) with enatioselectivity (75-98%) and distereoselctivity (99-100%) via tandem alpha -amination Corey Chaykovsky reaction of aldehydes, comprises reacting an alpha -unsubstituted aldehyde with azodicarboxylates at 0-20 degrees C in presence of L-proline in a solvent to obtain alpha -hydrazino aldehydes, and subjecting the alpha -hydrazino aldehydes to insitu Corey Chaykovsky reaction at -4 degrees C to -6 degrees C.    R = 1-10C-cycloalkyl (optionally substituted with halo or -OH), H, halo or optionally branched 1-10C-alkyl, or naphthyl (optionally substituted with halo, OH, nitro, amino, CN, COOH, or CONH2), where aryl is optionally as mono, di or tri substituted by halo, OH, nitro, amino, CN, COOH, CONH2, heteroaryl with N, O and/or S atoms as hetero atoms; and    R1 = tert-butyl, iso-propyl or benzyl groups.
NOVELTY - Method comprises contacting a lignin sample with a lignin depolymerase, and contacting the lignin sample with an auxiliary compound.    USE - The method is useful for depolymerizing lignin.    ADVANTAGE - The method is capable of simply and economically depolymerizing lignin.    DETAILED DESCRIPTION - Method comprises: either contacting a lignin sample with a lignin depolymerase, and contacting the lignin sample with an auxiliary compound; or contacting an auxiliary compound with a sample comprising uncleaved lignin macromolecules, and at least partially cleaved lignin components in intermolecular association with at least a portion of other lignin components or uncleaved lignin macromolecules, where the auxiliary compound dissociates the at least partially cleaved lignin components from the other lignin components or uncleaved lignin macromolecules; or incubating a sample comprising biomass comprising lignin and a polysaccharide comprising cellulose or hemicellulose, with a lignin depolymerase under conditions effective for the lignin depolymerase to digest at least a portion of the lignin, and digesting at least a portion of the cellulose or hemicellulose.
NOVELTY - The method involves forming a partially condensed intermediate stream from over head vapor (30) obtained from an overhead part (26) of a nitrogen stripping column (20) above a rectifying section (22). A condensed fraction (37) is separated from a vapor fraction (80). The vapor fraction is discharged as off gas, where the vapor fraction includes a heating value. A reflux portion (36) of the condensed fraction is allowed into the stripping column starting at a level above the rectifying section. A cooling duty is adjusted to regulate the heating value of the vapor fraction being discharged.    USE - Method for removing nitrogen from a cryogenic hydrocarbon composition.    ADVANTAGE - The method enables regulating the heating value relative to an actual demand for heating power by minimizing any shortage and excess of heating power being delivered.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an apparatus for removing nitrogen from a cryogenic hydrocarbon composition.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a method for removing nitrogen from a cryogenic hydrocarbon composition.    Nitrogen stripping column (20)    Rectifying section (22)    Overhead part (26)    Over head vapor (30)    Reflux portion (36)    Condensed fraction (37)    Vapor fraction (80)    Liquefaction system (100)    Combustion device (220)
NOVELTY - A diphenylamine compound (I) is new, and excludes compound having chemical abstract service (CAS) number of 872296-37-2, compound having CAS number of 1172626-82-2, compound having CAS number of 1172626-81-1, compound having CAS number of 854873-67-9, compound having CAS number of 828921-30-8, compound having CAS number of 154595-53-6 and compound having CAS number of 854873-66-8.    USE - New diphenylamine compound is used as intermediate for medicine and pesticide.    ADVANTAGE - The diphenylamine compound is safely and economically prepared by simple method, with reduced impact on environment.    DETAILED DESCRIPTION - A diphenylamine compound of formula (I) is new, and excludes compound having chemical abstract service (CAS) number of 872296-37-2, compound having CAS number of 1172626-82-2, compound having CAS number of 1172626-81-1, compound having CAS number of 854873-67-9, compound having CAS number of 828921-30-8, compound having CAS number of 154595-53-6 and compound having CAS number of 854873-66-8.    Y'=halo, 1-4C alkyl, 1-4C alkoxy or 1-4C haloalkyl;    n=0-3;    Z=halo, 1-4C alkyl, 1-4C alkoxy, 1-4C haloalkyl, 1-4C alkoxy-(1-4C) alkyl or 1-4C alkoxycarbonyl;and    m=0-5.    Halo does not exist at para-position of nitro group of diphenylamine compound. An INDEPENDENT CLAIM is included for manufacture of diphenylamine compound (I).
NOVELTY - Hydrodesulfurization method by hydrogen byproduct of electric deionization-type water-treatment apparatus involves discharging hydrogen and oxygen which are produced as byproducts in the electric deionization-type water-treatment apparatus in fuel cell system having electric deionization-type water-treatment apparatus, from a line separate from the electric deionization-type water-treatment apparatus, and utilizing effluent water material for hydrogen for hydrodesulfurization of source gas for reformed-gas production.    USE - Hydrodesulfurization method (claimed).    ADVANTAGE - The hydrodesulfurization is economically carried out using the system by simple method.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) hydrodesulfurization system; and    (2) fuel cell system, which has hydrodesulfurization system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view explaining the hydrodesulfurization method. (Drawing includes non-English language text)
NOVELTY - A microorganism (NITE P-1155) capable of producing ethanol, is new. The microorganism produces ethanol using synthesis gas as substrate. The microorganism comprises ribosomal RNA (rRNA) gene exhibiting 95% sequence identity with respect to a 1470 base pair sequence (SEQ ID NO: 1) fully defined in the specification.    USE - The microorganism belonging to genus Clostridium is useful for producing ethanol (all claimed). The ethanol is used as fuel.    ADVANTAGE - The microorganism stably produces ethanol having higher concentration using synthesis gas obtained by gasifying biomass of wood scrap, and suppresses global warming, as it produces ethanol by utilizing carbon dioxide. As the ethanol is generated from biomass, there are no worries of depletion.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing ethanol, which involves culturing the above-mentioned microorganism in the presence of synthesis gas.
NOVELTY - Deoxygenating (M1) a biomass-derived pyrolysis oil involves combining a biomass-derived pyrolysis oil stream that has an initial temperature of greater than or equal to 100 degrees C with heated low-oxygen-pyoil diluent recycle stream to form heated diluted pyoil feed stream that has a feed temperature of greater than or equal to 150 degrees C; and contacting the heated diluted pyoil feed stream with a first deoxygenating catalyst in the presence of hydrogen at first hydroprocessing conditions effective to form a low-oxygen biomass-derived pyrolysis oil effluent.    USE - For deoxygenating biomass-derived pyrolysis oil (claimed) to produce biofuels and low-oxygen biomass-derived pyrolysis oil.    ADVANTAGE - By contacting the deoxygenating catalyst with the heated diluted pyoil feed stream in the presence of hydrogen at the hydroprocessing conditions, the amount of glassy brown polymer or powdery brown char formed on the deoxygenating catalyst is reduced or minimized compared to conventional methods. Therefore, low-oxygen biomass-derived pyrolysis oil can be produced in the hydroprocessing reactor without plugging the deoxygenating catalyst, thus increasing run duration and improving processability of the biomass-derived pyrolysis oil.
NOVELTY - The oxygen-containing gasification agents (7,8) are added to gasification substances (4) in gasification chambers (1,2). The quantity and composition of gasification agents are measured. The partial gasification of substances is performed. The carbon conversion of primary gasification products is limited to 80% based on carbon input of substances. The temperature of gasification chamber (2) is adjusted to preset level so that complete gasification of substance is performed. The desired compositions of raw synthesis gases of secondary gasification product are obtained.    USE - Method for entrained-flow gasification of solid fuels such as coal, petroleum coke, biomass or other carbonaceous dusts.    ADVANTAGE - The gasification efficiency of solid fuels can be improved. The operational safety of gasification reactor can be ensured. The structure and design of the gasification reactor can be simplified. The gasification process can be carried flexibly. The efficient discharge of ash in dry form and/or in the form of melted slag is possible. The deposition of solid material at the wall of the reactor can be reduced. The ignition reliability can be improved. The operation stability of nozzles can be increased. The complexity of the reactor can be reduced. The fuel consumption can be reduced. The collision of solid substances can be avoided.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for gasification reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the gasification reactor.    Gasification chambers (1,2)    Quenching chamber (3)    Gasification substances (4)    Oxygen-containing gasification agents (7,8)    Lining (11)
NOVELTY - The apparatus has an optical block (2) for forming a space in which gas of a detection target is introduced. An infrared ray radiating element (3) radiates infrared rays in the space. A light receiving element (4A) receives the infrared rays radiated outside the space and converts the infrared rays into an electric signal. A signal processing circuit (6) processes the electric signal output from the light receiving element. A package (10) is provided with multiple terminals electrically connected with the signal processing circuit. The optical block is made of metal-material.    USE - Gas component detection apparatus i.e. infrared ray detection-type gas sensor, for detecting concentration of a gas component such as carbon monoxide, carbon dioxide, methane and nitrogen oxide, of a detection target.    ADVANTAGE - The package is provided with the terminals electrically connected with the signal processing circuit, and the optical block is made of the metal-material, so that heat resistant improvement and cost reduction of the apparatus can be effectively achieved.    DETAILED DESCRIPTION - The metal-material is a sheet metal such as aluminum, brass and copper.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of an optical block.'(Drawing includes non-English language text)'    Optical block (2)    Infrared rays radiating element (3)    Light receiving element (4A)    Signal processing circuit (6)    Package (10)
NOVELTY - The apparatus has an optical block (2) for forming a space in which gas of a detection target is introduced. An infrared ray radiating element (3) radiates infrared rays in the space. A light receiving element (4A) receives the infrared rays radiated outside the space and converts the infrared rays into an electric signal. A signal processing circuit (6) processes the electric signal output from the light receiving element. A package (10) is provided with multiple terminals electrically connected with the signal processing circuit. The optical block is made of heat-resisting glass.    USE - Apparatus i.e. infrared ray detection-type gas sensor, for detecting concentration of a gas component in a detection target. Uses include but are not limited to carbon monoxide, carbon dioxide, methane and nitrogen oxide.    ADVANTAGE - The signal processing circuit calculates a gas concentration based on difference of output-signal levels of the light receiving element so as to cancel fluctuation component of the output-signal level of the light receiving element, thus suppressing fall of detection accuracy of a gas density. The optical block is made of heat-resisting glass so as to improve heat resistance performance and reduce manufacturing cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of an optical block.'(Drawing includes non-English language text)'    Optical block (2)    Infrared ray radiating element (3)    Light receiving element (4A)    Signal processing circuit (6)    Package (10)
NOVELTY - The apparatus has a light receiving element for converting infrared rays radiated by an infrared ray radiating element into an electric signal. A signal processing circuit processes the electric signal output from the light receiving element. A package is provided with multiple terminals electrically connected with the signal processing circuit. A socket (310) is detachably connected with a connector part (8) mounted in a wiring board. An electrically-conductive part i.e. contact (81), is electrically connected to the signal processing circuit.    USE - Gas component detection apparatus i.e. infrared ray detection-type gas sensor, for detecting concentration of gas component such as carbon monoxide, carbon dioxide, methane and nitrogen oxide, in a detection target.    ADVANTAGE - The electrically-conductive part is electrically connected to the signal processing circuit, and an optical block of the apparatus is formed with a synthetic resin material, so that heat resistant improvement and cost reduction of the apparatus can be effectively achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view illustrating non-connecting state of a connector part with a socket.'(Drawing includes non-English language text)'    Optical block (2)    Connector part (8)    Rectangular-shaped parallel-piped mailbox (80)    Contact (81)    Socket (310)
NOVELTY - System (100) configured to selectively remove an acid gas from a feed stream (102) to reduce co-absorption of carbon dioxide, comprises an absorber (120) configured to contact at least a portion of the feed stream with a basic absorbent to produce a clean stream (122) substantially depleted of the acid gas, where the absorber is further configured to receive a driver gas that is substantially non-reactive with the basic absorbent, so that co-absorption of carbon dioxide by the basic absorbent is reduced to less than 10% of the carbon dioxide present in the feed stream.    USE - The system is useful for selectively removing acid gas from feed stream to reduce co-absorption of carbon dioxide.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for reducing co-absorption of carbon dioxide from the feed stream, comprising contacting the portion of the feed stream with basic absorbent in absorber to produce the clean stream substantially depleted of acid gas, where the feed stream comprises driver gas that is substantially non-reactive with the basic absorbent, and sufficient to reduce co-absorption of carbon dioxide by the basic absorbent to less than 10% of the carbon dioxide present in the feed stream.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of system configured to selectively remove acid gas from feed stream.    System (100)    Feed stream (102)    Caustic solution (106)    Absorber (120)    Clean stream (122)
NOVELTY - Preparation of a catalyst comprising an iron for catalyzing at least one reaction in a hydrocarbon conversion system, involves: grinding particles comprising iron so substantially all the particles have a maximum dimension no larger than 130 microns; and coating the particles with at least one hydrocarbon to provide the catalyst with improved flowability.    USE - For the preparation of a catalyst comprising an iron for catalyzing at least one reaction in a hydrocarbon conversion system (claimed). The catalyst is used in the hydroconversion of heavy oils, biofuels, and coal liquids.    ADVANTAGE - The slurry catalyst material is hydrophobic and resists clumping. As a result, the material can be easily handled and combined with a hydrocarbon feed to form a slurry before entering a hydroconversion reactor. The advantageous properties allow the use of a relatively inexpensive material that can be easily handled to facilitate forming a slurry for conducting hydroprocessing reactions.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a slurry catalyst system, comprising: an upflow tubular reactor receiving: 1) a hydrocarbon feed comprising compounds having an initial boiling point temperature of at least 340 degrees C; and 2) a slurry catalyst composition comprising at least one compound, and a coating comprising a hydrocarbon having a melting point temperature of not greater than 250 degrees C for improving flowability of the slurry catalyst composition.
NOVELTY - The apparatus (100) has a biomass feedstock manufacture unit i.e. wet grinding mill (111), manufacturing a biomass feedstock (12). A material supply unit pumps the biomass feedstock to a microwave reaction tube (130), and is equipped with a pressure control valve (132). A microwave heating unit heats the feedstock in the reaction tube in temperature range of 120 to 347 degree Celsius with a microwave heating device and manufactures crude biomass thermal decomposition oil. An isolation unit isolates the biomass thermal decomposition oil from the crude biomass thermal decomposition oil.    USE - Apparatus for manufacturing biomass thermal decomposition oil utilized as fuel or industrial material from a biomass. Uses include but are not limited to timber, bamboo material, rice-straw, straw, herb, agricultural-products, seaweed, organic-refuse, domestic-waste, excrement, industrial waste material, agricultural waste material, livestock farming waste material and activated-sludge waste material.    ADVANTAGE - The apparatus allows the oil to be manufactured from various types of biomasses in small quantities, so that high yield industrial continuous production is achieved. The apparatus allows a carbon yield of biomass thermal decomposition oil to be high rate of 80 to 90%. The apparatus allows water to be used as solvent, so that the biomass thermal decomposition oil can be used without drying the biomass of raw material.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for manufacturing biomass thermal decomposition oil.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass thermal decomposition oil manufacturing apparatus.    Biomass feedstock (12)    Biomass thermal decomposition oil manufacturing apparatus (100)    Wet grinding mill (111)    Microwave reaction tube (130)    Pressure control valve (132)
NOVELTY - The filter has a sealing cover that is arranged in a barrel portion. The side wall of barrel portion is provided with material inlet and outlet ports. A basket is arranged inside the barrel portion. The holes are formed at lower end of the basket.    USE - Non-refining filter for filtering bio-diesel from high acidity grease.    ADVANTAGE - The solid slag can be discharged conveniently. The safety of circulating pump can be ensured. The esterification effect of filter can be improved effectively. The stability of production line can be ensured.
NOVELTY - The separator has a cylinder body whose lower side is provided with a welding head. The cylinder body is welded on a cylinder flange. An end of the cylinder body is provided with a stuffing tube. A filler flange is connected with a filler plate through a packing bolt. The filler plate is connected with the stuffing tube. A middle part of the cylinder body is provided with a sewage pipe. The cylinder body is welded with an umbrella cap that is welded on a draft tube. The draft tube is provided with a rectifying cover. An air outlet pipe is fixed on an air outlet flange.    USE - Biomass fuel-gas oil-gas separator.    ADVANTAGE - The separator is simple in structure, easy to assemble and inexpensive, and has high operation efficiency and better purification effect.
NOVELTY - The furnace has an ash discharge port provided with an ash outlet. A lower furnace body is provided with an ash hopper. The ash hopper is provided with the ash discharge port. An auger ash outlet machine is connected with the ash outlet. A furnace body is connected with a flange body. A feeding port is fixed at a lower part of a flashboard.    USE - Biomass gasification furnace.    ADVANTAGE - The furnace is simple in structure and reasonable in design. The furnace ensures high working efficiency and stable and continuous operation and improves production efficiency.
NOVELTY - The furnace has gasification reacting and burning chambers connected with a gasification gas channel. A metal net is arranged in the gasification combustion chamber that is provided with a cavity. An annular-shaped air pipe is arranged in the gasification combustion chamber. An upper half part of the annular-shaped air pipe is provided with an air hole. The annular-shaped air pipe is connected with another annular-shaped air pipe that is connected with a fan. A furnace body is arranged on lower and upper parts of the metal net.    USE - Combined-type composite wall biomass gasification furnace.    ADVANTAGE - The furnace saves fuel source, avoids water discharge problem, removes peculiar smell and ensures aesthetic appearance. The furnace is environment-friendly, easy to operate and convenient and safe to use. The furnace has high thermal efficiency.
NOVELTY - The furnace has a furnace body provided with a blower, a gas conveying pipeline and a gas storage device. An upper part of the furnace body is provided with a feed inlet and an air outlet. A lower part of the furnace body is connected with a tar collector through a gas pipeline that is connected with the gas storage device.    USE - Gasification furnace for use in home.    ADVANTAGE - The furnace has convenient usage and high efficiency. The furnace avoids fire accident, saves energy and ensures better safe performance.
NOVELTY - The furnace has a furnace body whose upper part is provided with a heat-conducting water tank and a fuel gas outlet. The water tank is connected with a water pipe. The furnace body and a water heater are connected with a converter. The converter is provided with an air outlet pipe and an air inlet pipe. The air inlet pipe and the air outlet pipe are respectively connected with a gas outlet and a gas stove head.    USE - Biomass gasification furnace.    ADVANTAGE - The furnace has high heat energy utilization rate, better gasification performance, smoke-free and dust-free, and avoids environment pollution and saves energy.
NOVELTY - The nozzle has a shell connected with a nozzle head. Center of a sealed board is provided with a central pipe. An upper end of the central pipe is extended out to the shell. A top end of the shell is fixed with a three-way joint. An upper end of the three-way joint is fixed with the nozzle head. The central pipe is connected with a solid biomass raw material inlet. A side part of the three-way joint is fixed with an opening that is opened on the sealed board. A lower end of the sealed board is sealed on a sealing plate. A lower end of the sealing plate is provided with through holes.    USE - Biomass gasification process spraying nozzle.    ADVANTAGE - The nozzle improves solid biomass raw material and oxygen mixing effect.
NOVELTY - The furnace has a pressure-bearing steel shell provided with a bearing steel. The bearing steel is provided with a through-hole. A supporting plate is fixed on an upper part of the pressure-bearing steel shell. A combustion chamber is provided with a bearing. A bottom part of the combustion chamber is fixed with the through-hole. A lower part of a descending pipe is sleeved with a lifting pipe. A bottom part of a synthesis gas outlet is provided with a chilling chamber.    USE - Biomass gasification furnace.    ADVANTAGE - The furnace has high gasification efficiency, high raw material processing efficiency and high safety performance. The furnace is convenient to maintain.
NOVELTY - The gun has a back seat connected with an inlet end of a gun body. An outlet end of an insulating connecting piece is connected with a front gun body. A first electrode is extended into the gun body. A second electrode is connected with the front gun body. The back seat is overlapped in the gun body. Gasification chambers generate electric arc. One of the gasification chambers and the plasma electric arc root are fixed with a third electrode through a rod body.    USE - Plasma gasification spray gun.    ADVANTAGE - The gun adopts a gasification raw material for performing gasification reaction to generate carbon monoxide and hydrogen gas.
NOVELTY - The system has a combustible material connected with a feeding device. An automatic collecting device is connected with a slag removing device and a waste gas purifying device. A light emitting system unit is connected with a sorting system unit. The feeding device is connected with a drying chamber. A power generation system unit is connected with the automatic collecting device. A waste gas recycling device is connected with the waste gas purifying device.    USE - Rubbish carbonization pyrolysis gasification generating system.    ADVANTAGE - The system saves renewable resources and avoids wastages and pollution, and has high resource utilization rate.
NOVELTY - The mechanism has a rod portion whose center end is provided with a penetrated through-hole. The rod portion is made of fermented bamboo product.    USE - Bamboo carbon rod mechanism.    ADVANTAGE - The hardness of rod mechanism can be improved effectively. The occurrence of breakage and damage in rod mechanism can be prevented efficiently. The carbon content contained in rod mechanism can be improved. The combustion time of rod mechanism can be improved.
NOVELTY - The plate has a plate main portion which is provided with a plastic electrode frame. The plastic electrode frame is covered on the outer edge of the main portion to form an integral structure.    USE - Water electrolysis hydrogen electrode plate.    ADVANTAGE - The processing precision of the electrode plate is high. The processing period of the electrode plate can be shortened, thus the production efficiency of the electrode plate can be improved. Consumption of steel can be reduced. The appearance of the electrode plate is beautiful.
NOVELTY - Animal feed is prepared using straw and kitchen wastes by crushing straw, drying, then soaking into clean water, and fermenting to prepare straw feed; collecting and crushing kitchen leftovers, and boiling into a reaction kettle at high temperature; adding straw feed into the reaction kettle, then adding edible preservative, rice bran, wheat bran, and corn flour; uniformly stirring the materials in the kettle and cooking at high temperature; and drying the cooked materials, crushing, pouring into a puffing machine, and packaging the finished product.    USE - Method of preparing animal feed using straw and kitchen wastes (claimed).    ADVANTAGE - The method can obtain nutritious animal feed and which does not contain chemical additive.
NOVELTY - Processing printing and dyeing waste water comprises adding seed sludge, glucose and water into an internal circulation anaerobic tank, inoculating the sludge by hydrolysis acidification bacteria and methane bacteria, desizing waste water to hydrolyze pollutant to generate methane and carbon dioxide, introducing the desizing waste water into an aerobic tank, discharging backflow of nitrifying liquid to an anoxic tank, excess sludge to a continuous stirred tank reactor anaerobic digestion tank from an anoxic tank and supernatant liquid in residual sludge to an intermittent hypoxia tank.    USE - The method is useful for discharging printing and dyeing waste water (claimed).    ADVANTAGE - The method economically and eco-friendly discharges printing and dyeing waste water with high processing efficiency, improved settling property, improved COD removal rate and without generation harmful gas.    DETAILED DESCRIPTION - Processing printing and dyeing waste water comprises adding seed sludge, glucose and water (1-3%) into an internal circulation anaerobic tank, inoculating the sludge by hydrolysis acidification bacteria and methane bacteria, desizing waste water to hydrolyze pollutant (70-80%) by methanation reaction to generate methane and carbon dioxide, introducing the desizing waste water into an aerobic tank, discharging backflow of nitrifying liquid to an anoxic tank, excess sludge to a continuous stirred tank reactor (CSTR) anaerobic digestion tank from an anoxic tank and supernatant liquid in residual sludge to an intermittent hypoxia tank by dehydrating water from the sludge by a filter press, where the aerobic water has chemical oxygen demand (COD) of less than 500 mg/l, discharging the sludge by the belt filter press until the water content is 80-90%, treating sludge with fluidity into a boiling furnace through a plunger pump at 950-1050 degrees C, and introducing the sludge obtained from the furnace top to an incinerating device to form ash.
NOVELTY - A biomass fuel gas purification method involves performing dust removal of gas generated by the gasification of a biomass gasification furnace by a dust removal equipment. The gas after dust removal is washed by a washing equipment. The washed gas is dehydrated by a dehydration equipment. The dehydrated gas is decoked by a decoking equipment. The decoked gas is decarbonized by a decarbonization equipment to obtain the biomass fuel gas.    USE - Method for purifying biomass fuel gas.    ADVANTAGE - The prepared biomass fuel gas has low impurity content and high heat value.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biomass fuel gas comprising 35-48 vol.% carbon monoxide, 24-33 vol.% hydrogen, 15-21 vol.% methane, 0-0.01 vol.% oxygen, 2-6 vol.% nitrogen, 2-6 vol.% carbon dioxide, 0.09-0.11 vol.% ethane and 0.009-0.01 vol.% propane, where the content of the tar in the biomass fuel gas is less than 5 per cubic meter, the dust content of the mixture is less than 10 per cubic meter, and the heat value of the biomass gas is 15.5-16.7 MJ per cubic meter.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating a method for purifying biomass fuel gas. '(Drawing includes non-English language text)'
NOVELTY - The non-catalytic partial oxidation furnace has a vertical type container (3) that is connected to a gasification nozzle (2). The gasification nozzle is equipped on an upper sealing head (6). The lower portion of vertical type container is provided with a lower end enclosure (7). The bottom of the vertical type container is provided with a connection opening of waste heat boiler (4). A connecting port and a gasification burner are arranged coaxial to gasification nozzle. The synthesis of ammonia, methanol and synthetic oil are provided for making the iron.    USE - Non-catalytic partial oxidation furnace of hydrocarbon gas, used in large scale device and in industrial application.    ADVANTAGE - The conversion efficiency, service life and refractory lining load of non-catalytic partial oxidation furnace can be improved conveniently.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the non-catalytic partial oxidation furnace of hydrocarbon gas.    Gasification nozzle (2)    Vertical type container (3)    Waste heat boiler (4)    Upper sealing head (6)    Lower end enclosure (7)
NOVELTY - The device has sludge reactor (1) that is provided with water inlet (6) and water outlet (7) at upper end, and sludge discharge port (13) at lower end. Reactor is provided with stirrer (4) and aeration device (5), and filled with magnetic powder (2) and activated sludge (3). Periphery of reactor is provided with magnetic field device which is included with magnetic field detector (8), iron cover (9), power supply (10), transformer (11) and spiral coil (12) wound around outer surface of reactor. Spiral coil is connected with transformer which is connected with power supply.    USE - Processing device of magnetic powder reinforced active sludge from food industry (claimed).    ADVANTAGE - The device operation cost can be reduced. The organic degradation rate cannot be increased.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a sewage treatment method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the sewage processing device.    Sludge reactor (1)    Magnetic powder (2)    Activated sludge (3)    Stirrer (4)    Aeration device (5)    Water inlet (6)    Water outlet (7)    Magnetic field detector (8)    Iron cover (9)    Power supply (10)    Transformer (11)    Spiral coil (12)    Sludge discharge port (13)
NOVELTY - Production of biodiesel by in situ esterification of sewage treatment plant scum comprises filtering scum, precipitating, centrifuging at 3000 revolutions/minute (rpm), oven-drying to obtain dry sludge, adding dry sludge in pure methanol, adding sulfuric acid solution, reacting while stirring at 55-75 degrees C for 24 hours to perform in situ esterification, cooling, adding pure n-hexane, mixing, reacting, centrifuging, discarding solid, extracting, filtering, putting in separatory funnel, collecting upper phase, filtering, adding anhydrous sodium sulfate to filtrate and evaporating.    USE - Production of biodiesel by in situ esterification of sewage treatment plant scum (claimed).    ADVANTAGE - The method solves sewage treatment plant scum disposal problem. The yield of biodiesel is greater than or equal to 20%, where the yield is increased by greater than or equal to 100%.    DETAILED DESCRIPTION - Production of biodiesel by in situ esterification of sewage treatment plant scum comprises filtering scum using 2-mm screen, precipitating for 4 hours, centrifuging at 3000 rpm for 20 minutes, oven-drying at 103 degrees C for 8-10 hours to obtain dry sludge with water content of less than 5%, adding 5 g dry sludge in 100-130 mL pure methanol, adding 3-5 mL of 98% sulfuric acid solution, reacting while stirring at 55-75 degrees C for 24 hours to perform in situ esterification, cooling to room temperature, adding 100-130 mL pure n-hexane, mixing, reacting for 3-5 minutes, centrifuging thrice at 3000 rpm, discarding solid, extracting, filtering, putting in separatory funnel, collecting upper phase of n-hexane, filtering, adding anhydrous sodium sulfate to filtrate, collecting n-hexane and methanol in residue and evaporating to obtain biodiesel.
NOVELTY - A methanol coal-based diesel oil comprises 20-80 volume parts modified methanol and 20-80 volume parts coal-based diesel oil in which modified methanol consists of 20-60 volume parts methanol, 5-10 volume parts ethylene glycol monomethyl ether, 19.8-44.8 volume parts liquid 12-18 carbon containing fatty acids, 14-20 volume parts 4-12 carbon containing saturated alcohols, 1-5 volume parts methyl tert-butyl ether, 0.028 volume part ferrocene, 0.002 volume part benzotriazole, 0.07 volume parts lauric acid butanol and 0.1 volume parts ethanolamine.    USE - A methanol coal-based diesel oil (claimed).    ADVANTAGE - The diesel oil can be produced using simple process at low cost. Content of harmful gas in the tail gas is greatly reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a production of methanol coal-based diesel oil which involves adding modified methanol into reaction kettle at room temperature, adding coal-based diesel oil at rotating speed of 300 plus minus 30 r/min under stirring condition for 5-15 minutes, continuing to stir for 30 minutes at temperature of 50 plus minus 5 degrees C, and cooling to room temperature to obtain the methanol coal-based diesel oil.
NOVELTY - Zeolite biological organic fertilizer comprises: 35-55 pts. wt. zeolite, 35-55 pts. wt. livestock manure, 2 pts. wt. fermented bacteria and 8 pts. wt. conditioner.    USE - A zeolite biological organic fertilizer is used for improving saline-alkali soil (claimed).    ADVANTAGE - The fertilizer is cheap.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of zeolite biological organic fertilizer comprising: selecting zeolite with 10-300 mesh fineness, livestock manure with 50-70 wt.% water content, fermented bacteria and conditioner; balancing nutrients of fertilizer; treating manure by adding enzyme and stacking at 1-1.2 m high, covering with plastic sheet, stirring every 3-5 days until maturity is reached; mixing conditioner urea, diammonium phosphate and decomposed organic fertilizer, crushing into powder, disk pelletizing, adding water; and drying to 15 wt.% water content and packaging.
NOVELTY - A bipolar membrane comprises cathode electrolytic chamber and anode chamber. The electrode of the cathode electrolysis chamber is lead, indium, tin, silver, mercury, iron, cobalt, nickel, zinc, cadmium, platinum, gold, palladium, ruthenium, iridium, rhodium, osmium, gallium, germanium, chromium, antimony, bismuth and/or carbon. The anode chamber is platinum, gold, palladium, ruthenium, rhodium, rhenium, osmium, copper, silver, iron, cobalt, nickel, zinc and/or carbon.    USE - Bipolar membrane.    DETAILED DESCRIPTION - A bipolar membrane comprises with cathode electrolytic chamber and anode chamber. The electrode of the cathode electrolysis chamber is lead, indium, tin, silver, mercury, iron, cobalt, nickel, zinc, cadmium, platinum, gold, palladium, ruthenium, iridium, rhodium, osmium, gallium, germanium, chromium, antimony, bismuth and/or carbon. The catholyte is hydroxide aqueous solution, aqueous sodium carbonate solution or bicarbonate water solution. The anode chamber is platinum, gold, palladium, ruthenium, rhodium, rhenium, osmium, copper, silver, iron, cobalt, nickel, zinc and/or carbon. The anode electrolyte is aqueous solution containing iodine salt and acid.
NOVELTY - Cefprozil is recycled by stirring cefprozil refined mother liquor, cooling, adding dimethyl formamide and acetone, freeze-drying, washing with acetone, vacuum drying, dissolving dried product in a mixed solvent, adding hydrochloric acid to adjust pH value, stirring, adding activated carbon, decolorizing, filtering, washing filter cake with water, drying, adding aqueous ammonia to adjust pH value, stirring, cooling, stirring, filtering, washing filter cake with acetone, and vacuum drying.    USE - Method of recycling cefprozil (claimed).    ADVANTAGE - The method is simple and convenient, reduces processing pressure of sewage treatment, and utilizes solvent that is recyclable.    DETAILED DESCRIPTION - Cefprozil is recycled by stirring cefprozil refined mother liquor at 20-30 degrees C, cooling to - 5 degrees C, adding dimethyl formamide and acetone, freeze-drying at - 5 to - 10 degrees C for 5-6 hours, washing with acetone, vacuum drying at 20-30 degrees C, dissolving dried product in a mixed solvent, adding 15 wt.% hydrochloric acid to adjust pH value to 1-1.5, stirring at 20-30 degrees C for 30 minutes, adding activated carbon, decolorizing for 45 minutes, filtering, washing filter cake with water, drying at 20-30 degrees C, adding aqueous ammonia to adjust pH value to 6.5-6.6, stirring for 60 minutes, cooling to 5 degrees C, stirring for 30 minutes, filtering, washing filter cake with acetone, and vacuum drying at 30 degrees C for 4 hours.
NOVELTY - Livestock fertilizer manufacturing device comprises a grass chopper, a material storage tank, a water storage tank, a water feeding pipe equipped with a drinking-water device, a material transferring pipe, a rotating shaft, a power driving device, a time setter, an excrement pipe equipped with a cleaning brush, a corral main body provided with an urine drainage pipe and a transmission belt, a pressing device equipped with an one-way valve, a methane tank directly connected with the urine drainage pipe, a drying device connected with a crusher, a grinder and a farm fertilizer bag.    USE - Used as a livestock fertilizer manufacturing device.    ADVANTAGE - The fertilizer manufacturing device conveys the excrement into the pressing device and methane tank through the excrement pipe and the urine drainage pipe, where the pressed excrement is dried and crushed and then bagged into farmyard manure which can be stored and sold; and solves the problem of environmental pollution caused by livestock raising in rural areas.
NOVELTY - Drying surplus sludge by anaerobic fermentation, vacuum pre-pressing and freeze drying, is claimed.    USE - The method is useful for drying surplus sludge (claimed).    ADVANTAGE - The method is capable of economically drying the surplus sludge with high efficiency and good drying effect in an environmentally friendly manner.    DESCRIPTION OF DRAWING(S) - The figure shows a flow chart of a method for drying surplus sludge (Drawing includes non-English language text).
NOVELTY - Fresh chicken manure, pig manure, cow manure and sheep manure as main materials, and crop straws as auxiliary materials are provided. Fresh rice bran (wheat bran or corn meal) is mixed with fermenting agent when the fermenting agent is diluted to ensure uniformity. During biochemical reaction, main materials are uniformly mixed with the auxiliary materials, the water content is maintained. Diluted fermenting additive is added to main and auxiliary materials, materials are piled. Turning again is carried out, to obtain organic fertilizer.    USE - Preparation of organic fertilizer (claimed).    ADVANTAGE - The organic fertilizer is efficiently prepared with improved soil environment, and inhibits plant diseases and insect pests, by simple method.    DETAILED DESCRIPTION - 80-90% Fresh chicken manure, pig manure, cow manure and sheep manure as main materials, and 10-15% crop straws (crushed or chopped into small segments) as auxiliary materials are provided. Fresh rice bran (wheat bran or corn meal) is mixed with fermenting agent in the ratio of 5:1 when the fermenting agent is diluted to ensure uniformity. During biochemical reaction, main materials are uniformly mixed with the auxiliary materials, the water content is maintained to 55-60%. 5 kg Diluted fermenting additive is added to every 1000 kg main and auxiliary materials, 4 m3 materials are piled, heights to 70-80 cm and ambient temperature at 15-20 degrees C and tried to raise the temperature when the temperature is too low and started to turn when the material temperature reaches 50-60 degrees C. Turning again is carried out when the compost temperature exceeds 65 degrees C, to obtain organic fertilizer.
NOVELTY - An organic and inorganic compound fertilizer comprises organic fertilizer base materials and inorganic chemical fertilizers. The base materials are prepared through mixing chicken manure with rape seed cakes in dry weight ratio of (1.74-2.21):1 and carrying out composting fermentation for 20 days. The organic and inorganic compound fertilizer is prepared through mixing organic fertilizer base materials with urea, monoammonium phosphate and potassium chloride in dry weight ratio of (12.82-13.69):(2.01-2.07):(1.80-2.15):(2.01-2.56), drying, granulating, sieving and packaging.    USE - Organic and inorganic compound fertilizer for kiwi fruits.    ADVANTAGE - The organic and inorganic compound fertilizer provides comprehensive nutritional needs for the growth of the kiwi fruits, is conducive to improvement of the soil structure and the increase of the fertilizer utilization ratio, such that the yield and quality of the kiwi fruits are improved. The resource utilization of agricultural wastes is realized, and the fertilizer is economically prepared.
NOVELTY - Wickerhamomyces anomalus (I) under a preservation number of CGMCC No. 5975, is new.    USE - (I) is useful for preparing textile fiber (claimed).    ADVANTAGE - The method does not pollute the environment, directly converts waste liquid into organic fertilizer, realizes zero discharge and zero pollution for producing textile fiber with less energy consumption in cost-effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing textile fiber comprising (a) mixing Wickerhamomyces anomalus with water to form yeast liquid, (b) adding the ramie raw material and then cutting in a section, introducing the raw material into a soaking pool for swelling, and (c) adding the hydrophobic solution to soak the prepared bacterial liquid, adding the biodegradable raw material in bacterial liquid and then draining and steam sterilizing to form a fiber bundle and then grinding to make the fiber beam, separating the single fiber and then screening and filtering, and drying the filtered mixture to obtain slurry, fine grinding the fiber and then soaking in warm water and then drying and carding to obtain the product.    DESCRIPTION OF DRAWING(S) - The figure shows a flow chart of a method for preparing textile fiber (Drawing includes non-English language text).
NOVELTY - An earthworm manure organic fertilizer consists of 55-65 parts mass earthworm, 10-20 parts mass straw, 15-25 parts mass vegetable cake, and 0-10 parts mass raw rice husk.    USE - Earthworm manure organic fertilizer for agricultural production.    ADVANTAGE - The earthworm manure organic fertilizer is comprehensive in nutrient, and the contained substances are not needed to be added manually. The earthworm manure organic fertilizer is easily and economically manufactured with high productivity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of earthworm manure organic fertilizer, which involves mixing stacked earthworm, fermented straw, fermented vegetable cake, and stacked raw rice husk, and keeping in dark places and performing air drying, and adjusting clear water to adjust the total water content to 25-30%.
NOVELTY - Rapid solid-liquid separator comprises a left fixing machine frame, a movable box body, a right fixing frame, a cross beam, a sewage inlet pipe, a stainless steel tube, a steel plate, a fixed square flange, a bottom plate, a rib plate, a scraper, a bottom plate, a sealing steel plate, a sewage water inlet pipe, a fixed square flange, a horizontal container, a rapid charging mechanism, a short steel pipe, a movable square flange, a roller, a reinforcing rib, a joint flange, a rubber plate, strip-shaped reinforcing ribs, a fast loading mechanism, a hydraulic cylinder and a large flange.    USE - The separator is useful for treating oil-containing sludge (claimed), and processing oil-containing wastewater.    ADVANTAGE - The separator does not produce secondary pollution, and thus it is environment friendly; and recycles the available resource materials.
NOVELTY - Producing organic fertilizer through barreled fermentation comprises drying and crushing the collected straw, drying the collected excrement of livestock and poultry to obtain dry excrement of livestock, crushing into powder, diluting the microbial inoculum to obtain diluted microbial inoculum, adding straw powder, dry excrement, urea and dilute fermentation microbial inoculum and then uniformly mixing, filling the wet material in the fermentation barrels, covering the ferment barrel cover to ferment, and naturally ventilating cover and then fermenting.    USE - The method is useful for producing organic fertilizer (claimed).    ADVANTAGE - The method allows simple and economical production of the organic fertilizer with rich raw material sources.    DETAILED DESCRIPTION - Producing organic fertilizer through barreled fermentation comprises drying and crushing the collected straw, adding straw powder in a particles of 8-10 mm, drying the collected excrement of livestock and poultry to obtain dry excrement of livestock, crushing into powder, diluting the microbial inoculum to obtain diluted microbial inoculum, adding straw powder (70-75 pts.wt.), dry excrement (25-30 pts.wt.), urea (1.1-2.9 pts.wt.) and dilute fermentation microbial inoculum (0.3 pts.wt.) and then uniformly mixing to obtain mixed material, adding water to the mixed material until the water content reaches to 30-65% to obtain wet material, filling the wet material in the fermentation barrels, covering the ferment barrel cover to ferment, and naturally ventilating cover for 30 minutes to every day and then fermenting time for 10-14 days.
NOVELTY - A butane-containing raw material is reacted in the absence of hydrogen at 0.1-3 MPa, 300-600 degrees C, and liquid hourly space velocity of 01-10 hour-1, in the presence of a butane conversion catalyst. The catalyst comprises 20-85 %mass mesoporous silicon-aluminum zeolite and 15-80 %mass binder, and has an alpha -value of 25-50.    USE - Method of using butane for producing propane used for ethylene cracking raw material, and gasoline (claimed).    ADVANTAGE - The method provides high-octane rating gasoline and efficiently reduces olefin content.
NOVELTY - Green solid state complete compound fertilizer comprises 40-60 pts.wt. of cinerite, 3-8 pts.wt. of lime stones, 8-12 pts.wt. of medical stones, 4-6 pts.wt. of animal protein raw material, 10-15 pts.wt. of vegetable protein raw material, 8-12 pts.wt. of straw, 8-12 pts.wt. of humic acid and 4-6 pts.wt. of saccharomycetes, where the animal protein raw material comprises waste materials, leftovers and bird and fish products and the vegetable protein comprises bean pulp, bran and maize yellow powder.    USE - Used as green solid state complete compound fertilizer.    ADVANTAGE - The fertilizer is simple and cost-effective, and has high content of organic matter, effect of increasing yield and effect of reducing plant disease (80%).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the green solid state complete compound fertilizer, comprising grinding and screening the straws using a 30 mesh screen, mixing the dried animal protein raw material and vegetable protein raw material with the grinded straws, grinding the dried vegetable and animal protein raw materials to 100 meshes, uniformly mixing lime stones and medical stones with the mixture, fermenting the mixture with saccharomycetes in a fermentation tank for 15 days at a first time, fermenting for 5 days at a second time, fermenting for 5 days at a third time, casting in a fermentation process, adding lard oil before the third fermentation, adding cinerite and humic acid with the fermented mixture, drying the mixture, adding the dried mixture with cyrtomium rhizome, fructus toosendan and semen nelumbinis, uniformly mixing and screening the mixture using the 100 mesh screen, and pelleting the screened mixture into 1-4.5 mm to obtain end product, where the bottom and top of the fermentation tank are arranged on an electric heating device and plastic insulating greenhouse, respectively.
NOVELTY - The system has a proton exchange membrane fuel cell which generates electricity power for a water pump (27), a fan and filters. The water pump works to absorb the raw water such as river water and lake water into a water purification unit. The bacteria, virus and other harmful substance are intercepted by the active carbon filter (23) and reverse osmosis membrane filter (25) for carrying out safe drinking water.    USE - Emergency water purifier for purifying river water, lake water, pond water, stream water, well water and sewage water (all claimed) as drinking water and as medical usage water, used in earthquake areas and battle field and construction work area.    ADVANTAGE - The water purifier is device is fast, stable and simple in operation. The weight and volume of the purifier are reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for hydrogen cleaning tank.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of emergency water purifier.    Active carbon filter (23)    Reverse osmosis membrane filter (25)    Raw water inlet (26)    Water pump (27)    Concentrated water outlet (32)
NOVELTY - A sludge synthetic fuel is prepared using 98-10 wt.% of sludge, conditioning agent and combustion improver. The fuel contains sludge (10-90 wt.%), conditioning agent (0.1-6 wt.%), and remainder of combustion improver.    USE - Sludge synthetic fuel.    ADVANTAGE - The low-carbon sludge synthetic fuel having high calorific value is environmentally-friendly and economical.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of sludge synthetic fuel, which involves preparing raw material including sludge, conditioning agent and combustion improver and mixing uniformly, or drying sludge until water content of sludge becomes 75-98% or less than 75%, and then adding conditioning agent and saw dust, and mixing uniformly, or mixing uniformly sludge having water content of 75-98% and conditioning agent, performing mechanical dehydration, drying and dehydrating, and then, mixing with combustion improver.
NOVELTY - An Chinese herb Astragalus mongholicus fertilizer is prepared by combining (wt.%) dry human excrement (19-22), dry pig manure (10-12), chicken manure (16-19), white gourd stem and leaf powder (1-3), eggplant stem and leaf powder (2-4), broad bean straw powder (4-6), cottonseed cake (6-8), potash fertilizer (10-12), calcium superphosphate (8-10), potassium chloride (2-4), Bordeaux mixture (3-5), dimethoate(1-3), and Bayleton (RTM: triazole fungicide) (4-6).    USE - Method of preparing Chinese herb Astragalus mongholicus fertilizer (claimed) used for stimulating growth of Astragalus mongholicus.    ADVANTAGE - The method has low cost, utilizes easy to obtain materials, is simple in steps, and can produce fertilizer that can increase yield of Astragalus mongholicus and can satisfy growth of Astragalus mongholicus.
NOVELTY - The device has plates, gaskets and a cord that are arranged in an enclosure. A cell (3) is formed in the plates, the gaskets and the cord by a power supply (11) with an alternating voltage of 230 Volt and direct voltage of 12 or 24 Volt.    USE - Device for producing combustible gases e.g. hydrogen and oxygen, from water, utilized in industrial and domestic applications.    ADVANTAGE - The device is compact and safe to use, and allows production of combustible gas in an effective manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a compact device.    Cell (3)    Power supply (11)
NOVELTY - Stable and amorphous 5-methyltetrahydrofolate prepared by neutralizing the 5-methyl tetrahydrofolic acid with alkali to fully dissolve in aqueous medium, adding alkaline-earth metal salts or alkaline earth metal salts solution into the neutralized solution, controlling the temperature of the mixed solution to 0-20 degrees C and carrying out ultrasonic treatment to the mixed solution to separate the end product, is claimed.    USE - The stable and amorphous 5-methyl tetrahydrofolate is useful for preparing a pharmaceutical composition or food additive (all claimed).    ADVANTAGE - The amorphous 5-methyl tetrahydrofolate is simple, economic and rapid to prepare with high stability and purity in an environment-friendly manner.    DETAILED DESCRIPTION - Stable and amorphous 5-methyl tetrahydrofolate prepared by firstly neutralizing the 5-methyl tetrahydrofolic acid with alkali to fully dissolve in aqueous medium, adding alkaline-earth metal salts or alkaline earth metal salts solution into the neutralized solution, controlling the temperature of the mixed solution to 0-20 degrees C, and carrying out ultrasonic treatment to the mixed solution to separate the end product, is claimed, where the aqueous medium is the solution of water and salt or the solution of water and the organic solvent, the alkali is the inorganic or organic alkali, the alkali is alkali metal, and the alkaline-earth metal is carbonate, hydrogen carbonate, ammonia, amine, pyridine or piperazine. An INDEPENDENT CLAIM is included for pharmaceutical composition, comprising the amorphous 5-methyl tetrahydrofolate as a main active ingredient and auxiliary material.
NOVELTY - Fructose based biomass is processed with an acid catalyst and quickly pyrolyzed to obtain 5-methylfurfural.    USE - Preparation of 5-methylfurfural.    ADVANTAGE - The method enables easy and economical preparation of 5-methylfurfural at low pyrolysis temperature and time, with high yield. Usage of solvent and high-pressure processing are not required. Acid corrosion and pollution are reduced.
NOVELTY - Organic granular bed soil is obtained by pulverizing granite soil into particles having diameter of 0.001-4 mm, adding acidity controller to the pulverized soil, producing builder agent by expanding and softening rice hulls, mixing and pulverizing the expanded and softened rice hulls and the acidity controlled soil, mixing 40-80 wt.% builder agent, 1-10 wt.% molasses, and 10-55 wt.% organic byproduct fertilizer to obtain pellet having size of 2-8 mm, and mixing 50-90 wt.% obtained pellet and 10-50 wt.% expanded and softened rice hulls to granular bed soil.    USE - As organic granular bed soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for manufacturing the above-mentioned organic granular bed soil, involves performing the above-mentioned steps.
NOVELTY - The center has a fuel cell generator electrically coupled to an information technology (IT) load. The generator provides power to the IT load. A building structure houses the generator and the IT load. An evaporative cooling device uses process exhaust from the generator or IT load to cool the generator or IT load. An energy storage device e.g. battery, is coupled to the IT load and the generator. The energy storage device receives power from the generator and provides power to the IT load. A controller is coupled to the IT load, the generator and the storage device.    USE - Data center.    ADVANTAGE - The center allows a modular fuel cell system enclosure for servicing the system in an easy manner. The center places routinely or high serviced consumable components in a single module so as to reduce amount of time required for service person. The center is designed in vertical orientation, so that natural convection can drive flow through air inlets and filters for reducing and eliminating need for fans. The center can use heat recovery power generators e.g. reciprocating heat engines, Stirling engines, thermoelectric devices and pyroelectric devices, in place of a turbine, so that capture of energy from process exhaust can increase efficiency of center and reduce required power output of the generator.    DETAILED DESCRIPTION - The fuel cell generator is a modular fuel cell based direct current (DC) generator. The IT load is a server, a computer, a router and an IT rack. The cooling device is an absorptive chiller and a turbine driven compression chiller.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a system for creating and operating data centers.    Power supply (102A)    Segments of fuel cells (106A)    DC-to-DC converters (106B)    DC buses (112)    Grid (114)
NOVELTY - Suppressing isomerization of an olefin metathesis product produced in a metathesis reaction comprises: adding an isomerization suppression agent to a mixture that comprises the olefin metathesis product and residual metathesis catalyst from the metathesis reaction under conditions that are sufficient to passivate at least a portion of the residual metathesis catalyst; where the isomerization suppression agent comprises nitric acid.    USE - The methods are useful for suppressing isomerization of an olefin metathesis product produced in a metathesis reaction; for refining a natural oil; and for producing a fuel composition (all claimed).    ADVANTAGE - The methods produce highly improved and environmentally friendly fuel compositions and specialty chemicals from a natural feedstock.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a method of refining a natural oil comprising: providing a feedstock comprising a natural oil; reacting the feedstock in the presence of a metathesis catalyst to form a metathesized product comprising olefins and esters; passivating residual metathesis catalyst with an agent that comprises nitric acid; separating the olefins in the metathesized product from the esters in the metathesized product; and transesterifying the esters in the presence of an alcohol to form a transesterified product and/or hydrogenating the olefins to form a fully or partially saturated hydrogenated product; and    (2) a method of producing a fuel composition comprising: providing a feedstock comprising a natural oil; reacting the feedstock in the presence of a metathesis catalyst to form a metathesized product comprising olefins and esters; passivating residual metathesis catalyst with an agent comprising nitric acid; separating the olefins in the metathesized product from the esters in the metathesized product; and hydrogenating the olefins to form a fuel composition.
NOVELTY - Method for producing cysteine or its derivative, involves reacting O-phosphoserine (OPS) and sulfide with an amino acid sequence of SEQ ID NO: 1 or 2 in presence of O-phosphoserine sulfhydrylase (OPSS) or microorganism expressing the OPSS, to obtain cysteine or its derivative. Sequences not defined here may be found at ftp://ftp.wipo.int/pub/published_pct_sequences/publication.    USE - The method is useful for producing cysteine or its derivative (claimed) used in pharmaceutical for treating bronchial disorder, cosmetic e.g. permanent wave lotion or hair shampoo, or foodstuff as e.g. flavor enhancer.    ADVANTAGE - The method is environmentally-friendly and easy to perform, is suitable for industrial production of cysteine, and provides high yield.
NOVELTY - Desulfurization of liquid fossil fuel involves evaporating selected liquid fossil fuel, treating with hydrogen in fixed bed reactor over a catalyst, where sulfur species are fully/partially converted to volatile sulfur species (3/4S and/or COS), removing formed volatile sulfur species fully or partially and converting the product to syngas in a connected fuel reforming unit and feeding obtained syngas to solid oxide fuel cell system.    USE - Desulfurization of liquid fossil fuel e.g. low-sulfur diesel and gasoline used for fuel cell e.g. solid oxide fuel cell. Uses include but are not limited to alkaline fuel cell, phosphoric acid fuel cell, polymer electrolyte membrane fuel cell, and molten carbonate fuel cell.    ADVANTAGE - The method is carried out efficiently and economically.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for system for desulfurization of liquid fossil fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic structure of system for desulfurization of liquid fossil fuel.    Evaporator (1)    Fixed bed reactor (2)    Adsorber (3)    Fuel-reforming unit (4)    Recycling pump (5)
NOVELTY - The method involves preparing a polymer electrolyte fuel cell (20) having an electrolytic membrane (23), and an anode (24) and a cathode (25). The gas is supplied through the gas flow paths (30P,31P) into the anode and the cathode which are in contact with an electrolytic membrane (23), and. The anode and the cathode are heat-processed by circulating the coolant gas through the gas flow paths.    USE - Method of manufacturing polymer electrolyte fuel cell for use in electric power generation.    ADVANTAGE - The supply of gas is carried out and the heat-processed to the catalyst layers is made easy, since the heat processing portion is hard to make the portion to which coolant gas is easy to be supplied among catalyst layers. Therefore, the flooding of the fuel cell is suppressed efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the heating furnace. (Drawing includes non-English language text)    Fuel cell (20)    Electrolytic membrane (23)    Anode (24)    Cathode (25)    Gas flow paths (30P,31P)
NOVELTY - A biological bacterial liquid tea foliar fertilizer, comprises Rhizobium (0.02-1.8 wt.%), azotobacter (0.03-1.5 wt.%), Bacillus strain (0.02-1.6 wt.%), potassium bacteria (0.02-1 wt.%), phosphorus bacteria (0.03-1.8 wt.%), protein (3-8 wt.%), ethylene (0.1-10 wt.%), nitrogen (2.8-15 wt.%), molybdenum (0.8-6 wt.%), boron (0.6-8 wt.%), and the rest is purified water.    USE - As a biological bacterial liquid tea foliar fertilizer (claimed).    ADVANTAGE - The biological bacterial liquid tea foliar fertilizer promotes crop absorption; provides fast growth; increases crop quality and fertility; increases the yield of crop; increases the strength of the photosynthesis.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the biological bacterial liquid tea foliar fertilizer, involving conveying plant bacterium culture to bacterium culture tank and radiator, cultivating biological bacteria using hot water bath at 20-60 degrees C, ensuring the bacterium culture workshops in indoor temperature at 18-30 degrees C, making the inclined culture of Rhizobium, azotobacter, Bacillus strain, phosphorus bacterial and potassium bacterial, shaking the inclined culture for 24 hours for fermentation; and conveying pipe for three-stage cultivation and fermentation after 24 hours, and then adding ethylene (0.1-15 wt.%), nitrogen (2.8-15 wt.%), molybdenum (0.6-10 wt.%) and boron (0.6-8 wt.%), culturing the mature fungus liquid, and after 24 hours keeping the fertilizer at low temperature environment.
NOVELTY - A microorganism fertilizer comprises microbial inoculum (1-5 wt.%, preferably 3 wt.%), chicken manure (50-70 wt.%, preferably 60 wt.%), wheat bran (4-10 wt.%, preferably 7 wt.%), humic acid (5-10 wt.%, preferably 8 wt.%), where the microbial inoculum is a mixture of Bacillus licheniformis, photosynthetic bacteria, Bacillus subtilis and yeast, and the microbial inoculum is 80-100 hundred million/g.    USE - As a microorganism fertilizer (claimed).    ADVANTAGE - The microorganism fertilizer increases crop yield and quality; reduces crop disease; increases bacteriostasis action of aerobic bacteria; and improves fertilizer effect and thus it is suitable for all kinds of crops.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the microorganism fertilizer, involving taking all the raw materials according to their weight ratio in a stirring device for uniformly stirring; covering mixed material with plastic film and fermenting for 3-6 days; raising the temperature of the material to 55-65 degrees C for the first time and again raising to 55-65 degrees C, fermenting it uniformly and removing toxic gas; putting the fermented material into hammer type crusher for crushing, where the grain size of the crushed material is 1-2 mm; granulating the material using extrusion granulator, and then drying the material in drying cylinder.
NOVELTY - High-potassium green fertilizer comprises wheat straw (50-70 wt.%), phosphorus powder (5-10 wt.%), potassium chloride (7-13 wt.%), ammonia water (10-20 wt.%), and sulfuric acid (8-15 wt.%).    USE - As high-potassium green fertilizer (claimed) for crop.    ADVANTAGE - The high potassium green fertilizer has good effect of inhibiting the virus in the soil (potassium acid-binding agent), can be produces using simple production technique, that is easy to operate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing high-potassium green fertilizer involving: (1) crushing wheat straw in a fermenting tank, adding water to ferment, heating at 50-60 degrees C for 140-150 hours, to form paste; (2) uniformly stirring for 3-4 minutes, where the rotating speed is 2000 revolution per minute (r/min), then adding 90-98% of sulfuric acid and 60-70% of ammonia, and reacting for 10 minutes; (3) adding potassium chloride and phosphorus powder, and uniformly mixing and granulating.
NOVELTY - A sustained-release fertilizer comprises nitrogen stabilizer (5-25 wt.%), biological surfactant (0.1-10 wt.%), biological fermenting composite amino acid (10-50 wt.%), plant growth regulator (0.1-5 wt.%), soil modifying agent (1-25 wt.%) and water.    USE - As sustained-release fertilizer such as urea for crops (claimed).    ADVANTAGE - The sustained-release fertilizer reduces volatilization loss; regulates the growth of plants; promotes plant to loosen soil and increases the absorption of nitrogen, phosphorus, potassium and microelement; improves the nutrient utilization rate and reduces the phosphorus loss; improves the validity of fertilizer; and increases the crop yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the sustained-release fertilizer involving: crushing nitrogen stabilizer, biological surfactant, biological fermenting composite amino acid, plant growth regulator and soil modifying agent into 80 meshes, dissolved in water at 30-80 degrees C, fermenting and uniformly mixing.
NOVELTY - A sustained-release fertilizer comprises nitrogen stabilizer (1-15 wt.%), biological surfactant (0.1-10 wt.%), biological fermenting composite amino acid (10-50 wt.%), metal ion chelating agent (1-20 wt.%), soil modifying agent (1-25 wt.%) and water.    USE - As sustained-release fertilizer for crops (claimed).    ADVANTAGE - The sustained-release fertilizer adsorbs ammonia and reduces volatilization loss; promotes plant to nutrient absorption, improves nutrient utilization rate; improves the phosphorus utilization rate; and increases the crop yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the sustained-release fertilizer involving: crushing nitrogen stabilizer, biological surfactant, biological fermenting composite amino acid, metal ion chelating agent and soil modifying agent into 80 meshes, dissolved in water at 30-80 degrees C, fermenting and uniformly mixing.
NOVELTY - A nitrification inhibitor is prepared by applying biomass carbon to dicyandiamide nitrification inhibitor while heating at 300 degrees C to match peanut straw carbon to dicyandiamide nitrification inhibitor.    USE - As nitrification inhibitor for improving nitrogenous fertilizer utilization rate (all claimed) in farming of crops planting.    ADVANTAGE - The biomass carbon particles are large, insoluble in water, and have density such that they are not easily leached out i.e. inhibit short-term leaching loss. Also biomass carbon has strong adsorption capacity of nitrification inhibitor dicyandiamide. Thus when nitrification inhibitor in which biomass carbon and nitrification inhibitor are matched, is used with nitrogenous fertilizer, prolonged transition of ammonium nitrogen to nitrate nitrogen in nitration reaction is achieved; whereas before mixing biomass carbon and dicyandiamide, dicyandiamide in soil has short residence time, which inhibits effect of chemical fertilizer; thus reduces leaching loss of dicyandiamide, increases dicyandiamide residence time in soil and improves utilization ratio of fertilizer in farming of crops planting. Thus addition of biomass carbon and dicyandiamide more effectively inhibits soil ammonium nitrogen to nitrate nitrogen conversion in reaction. As ammonium nitrogen is easy to be absorbed in soil, nitrogen spraying solution loss is greatly reduced, and ammonium and amide nitrogen utilization rate is improved.
NOVELTY - A metal complex contains polyhydric carboxylic acid compound, metal ion of 2-13 group(s) of periodic table, and 4-11C aliphatic monocarboxylic-acid compound.    USE - Metal complex is used for adsorbent, occlusion material and separation material for separating carbon dioxide, hydrogen, carbon monoxide, oxygen, nitrogen, 1-4C hydrocarbon, noble gas, hydrogen sulfide, ammonia, sulfur oxide, nitrogen oxide, siloxane and organic vapor e.g. methane, ethane, ethylene, propane and propene discharged from gas storage apparatus and gas motor vehicle (all claimed).    ADVANTAGE - The metal complex has water resistance and adsorption performance.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) gas storage apparatus;    (2) gas motor vehicle;    (3) separating method; and    (4) manufacture of metal complex.
NOVELTY - The method involves providing a membrane reactor (100) comprising a fuel cell, a cavity (20), a solid electrolyte membrane separator arranged in the cavity and dividing the cavity into a cathode chamber and an anode chamber. An electrolytic voltage is applied between the cathode and the anode by the fuel cell to decompose the carbon dioxide gas to form expected products. The expected products comprise a hydrogen gas and an oxygen gas. The hydrogen gas and the oxygen gas are feed back to the fuel cell to generate electric power.    USE - Method for electrochemically converting carbon dioxide gas for main anthropogenic cause of climate change, such as the greenhouse effect.    ADVANTAGE - Method for electrochemically converting carbon-dioxide to useful industrial chemicals containing carbon and fuels.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the membrane reactor.    Cavity (20)    Membrane reactor (100)    Cathode inlet (222)    Cathode outlet (224)    Separator (260)
NOVELTY - Method for producing cellulase and pectinase from herbal industrial residue, involves inoculating, and growing Trichoderma reesei strain (MTCC 164) in a medium containing sterilized herbal industrial residue and a moistening agent at a pH of 3-7, incubating the strain at 28-32 degrees C for 24-120 hours, and separating the filtrate by known methods.    USE - The method is useful for producing cellulase and pectinase.    ADVANTAGE - The method environmentally-friendly treats herbal industrial residue, thus is suitable for solid waste management, and economically produces cellulase and pectinase.
NOVELTY - The methane purification and compression filling device has an air-water separator through which a pipeline is connected with a desulfurizing tower. The desulfurizing tower is connected through a pipeline of a high pressure compressor. A marsh gas with a high pressure compressor is respectively connected with a high pressure gas liquid pipe of the separator. The high pressure gas-liquid separator is connected with the carbon dioxide steel bottle with a molecular sieve high pressure dryer.    USE - Methane purification and compression filling device.    ADVANTAGE - The structure of the methane purification and compression filling device is simple. The methane purification and compression filling device is convenient to use. The methane purification and compression filling device can be operated easily.
NOVELTY - Serially combined high temperature heat conducting oil heating reaction kettle comprises a cylindrical kettle body, a cylindrical body sleeve, an electric heater, a discharge pipe and a liquid material inlet. The reaction kettles are serially connected via a guide tube. A heat conducting oil bottom valve is equipped between the cylindrical body sleeve and the guide tube. The upper part of the reaction kettle is equipped with a compressed air inlet opening and an exhaust opening.    USE - The reaction kettle is useful for synthesizing pseudodiosgenin diacetate by ring opening reaction of diosgenin.    ADVANTAGE - The reaction kettle: improves the product conversion rate; reduces the reaction time and cooling time; and saves the electrical energy.
NOVELTY - The device has a catalytic tower connected with a condensing tower and a gasification furnace through a gas-guide tube. The catalytic tower and the condensing tower are connected with a catalytic reforming tower. A water outlet is connected with a sewage treatment tank that is connected with a filter. The gasification furnace and the condensing tower are connected with a combustion unit. A reaction kettle is connected with another condensing tower through the gas-guide tube. The gas-guide tube is connected with the catalytic reforming tower and the combustion unit.    USE - Building rubbish fuel oil refining device.    ADVANTAGE - The device prevents environment from being polluted caused by refining rubbishes.
NOVELTY - The furnace has a fuel tank (1) provided with a barrel body (2) and a cover (3). Bottom of the barrel body is provided with an ignition pipe (5), a protective cover (4) and a first air inlet (10). An upper part of the barrel body is provided with an air outlet (12). A side part of the barrel body is provided with a second air inlet (19). The air outlet is connected with a blower (6) that is connected with the second air inlet. The second air inlet passes through an inclined pipe (15), a cooker (13) and a stove (17).    USE - Biomass carbon gasification furnace.    ADVANTAGE - The furnace utilizes rural biomass waste pyrolysis and oxidation reaction to generate combustible gas in sealed anoxic condition, saves energy and reduces emission, and has economic benefit and social benefit.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass carbon gasification furnace.    Fuel tank (1)    Barrel body (2)    Cover (3)    Protective cover (4)    Ignition pipe (5)    Blower (6)    Air inlets (10, 19)    Air outlet (12)    Cooker (13)    Inclined pipe (15)    Stove (17)
NOVELTY - Preparing biological fertilizer leaven comprises lyophilizing brown spherical solid nitrogen bacteria culture medium, Bacillus megaterium culture medium, Bacillus mucilaginosus culture medium and wet fiber single spore bacteria culture medium having viable cell count of more than 109 ml according a ratio of 1:1:1:1 and then carrying out freeze-drying to obtain frozen-dry powder, mixing 10000 unit of freeze-dry powder with cellulase and then vacuum packaging.    USE - The method is useful for preparing biological fertilizer leaven using dextrose mother liquor (claimed).    ADVANTAGE - The method rapidly prepares the biological fertilizer leaven.
NOVELTY - The device has an ash storage box door (12) arranged at a side wall part of a furnace body (4). A lower end of the ash storage box door and the furnace body are arranged on a transverse inner cavity wall and fixedly connected with a bottom plate (14). A top end of the furnace body is fixedly connected with a rear supporting plate (3a). The furnace body and a side wall part of the ash storage box door are connected with a falling plate guide box (11). A handle (9) is arranged in an ash pushing plate pull rod (3). The ash pushing plate pull rod is arranged on a horizontal line.    USE - Ash-discharging biomass gasification furnace bottom part pull-push device.    ADVANTAGE - The device is simple in structure and convenient to operate. The device can remove dust from a semi-carbonized material and improve continuous working ability of a biomass gasification furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of an ash-discharging biomass gasification furnace bottom part pull-push device in partial section.    Ash pushing plate pull rod (3)    Rear supporting plate (3a)    Furnace body (4)    Handle (9)    Falling plate guide box (11)    Ash storage box door (12)    Bottom plate (14)
NOVELTY - Improving bio-diesel engine performance using naphtha-based modifier, comprises selecting a biological modifier, naphtha and combustion chamber, where the naphtha is optimal solution of diluent, mixing the naphtha with a fuel into the combustion chamber in a volume ratio of 5-30% and at an injection and ignition times of 30? CA and 5 degrees CA, respectively.    USE - The method is useful for improving bio-diesel engine performance (claimed).
NOVELTY - The device has a drying machine provided with a grain inlet and a finished product outlet. The drying machine is fixed to a crusher that is provided with a conveyor. A mixing mechanism is provided with a cake inlet, a straw vinegar dregs inlet and a Chinese trumpet creeper inlet. The conveyor is fixed to a fermentation tank that is provided with a manure inlet, an organic fertilizer fermenting agent inlet, a water inlet and a sterilizing deodorant inlet. The fermenting tank is fixed to an organic fertilizer dewatering machine that is provided with a slurry pump and a pipeline.    USE - Device for producing grain stillage organic fertilizer in a wine product comprehensive utilization field.    ADVANTAGE - The device improves plant drought resistance, dried cold-resistant, root rot resistant ability and soil fertility and avoids hardening of the soil so as to improve quality of agricultural products.
NOVELTY - The device has a grinder provided with a grain inlet, a rape straw inlet, a bran inlet, an edible fungi slag inlet, a monosodium glutamate dreg inlet, an oil inlet and a cake cypress peanut shell inlet. A fermentation tank is provided with a conveyor and an organic fertilizer fermenting agent inlet. A mixing mechanism is provided with a slurry pump and a pipeline. A dewatering device is provided with a water outlet. A granulator is arranged with the conveyor. A drying machine is provided with a product outlet.    USE - Wine lees biological organic fertilizer production device.    ADVANTAGE - The device ensures simple process and better sterilizing performance, saves material resources and realizes sewage waste gas discharging process. The device performs crushing, fermenting, degrading and dehydratation of grain, a canola straw, a chaff, an edible fungi slag, a monosodium glutamate dreg, an oil cake, a peanut shell, an organic fertilizer fermenting agent, a chicken, a duck excrement, cellulose-decomposing bacteria, protein decomposition bacteria, phosphorus bacteria, potassium bacteria, a sterilizing deodorant and an organic raw material by utilizing a crusher, the fermenting tank, a mixer, an organic fertilizer, a de-watering machine, a granulator and a drying device to obtain a finished product.
NOVELTY - The device has a first biological fermentation tank, a second biological fermentation tank, a third biological fermentation tank and a rotary drying tank that are sequentially connected together in series. A packaged solid material discharge hole of a semi-wet disintegrator is connected with a material conveying belt. The material conveying belt is connected with the first biological fermentation tank that is formed with a biological fermentation tank feeding port. The third biological fermentation tank is connected with a rotary drying tank feeding port through the material conveying belt.    USE - Device for producing dregs bio-organic fertilizer by utilizing decoction dregs.    ADVANTAGE - The device is simple in structure and convenient to operate, and reduces production period, production cost and energy consumption rate and improves production efficiency.
NOVELTY - The device has an insulating sealing ring and an insulating shell body provided with a water inlet pipe. A positive electrode plate is provided with the insulating sealing ring. The positive electrode plate and a negative electrode plate are respectively provided with a water inlet hole and an air outlet hole. An upper insulated shell body is connected with a water outlet that passes through an inlet pipe. A lower insulating shell is connected with an air outlet passes through an air inlet pipe.    USE - Hydrogen fuel gas injection device for an engine.    ADVANTAGE - The device has high hydrogen generating rate and simple and compact structure, and occupies less space.
NOVELTY - The machine has a fermentation tank provided with a groove. The groove is linked with vent holes. The groove is formed in a middle part of a rotating shaft. The fermentation tank is fixed on a side wall of a track. The track is fixed with a guide rail. The guide rail is fixed above the rotating shaft and the track. The guide rail is provided with a sliding device. The sliding device is connected with a rotating disk. A pipeline is fixed with a bottom part of the fermentation tank. An outer end of the pipeline is connected with an air supply unit.    USE - Multifunctional multi spiral-type dry fermentation turning machine.    ADVANTAGE - The machine adopts a spiral stirring sheet whose outer side edge can automatically raised along upward direction so as to collect dried yeast fertilizer during turning process, so that production flow of the system is fully automated, thus reducing labor intensity and time consumption.
NOVELTY - The device has a fermentation tank formed with a feeding opening and arranged on ground. A side wall or bottom part of the fermentation tank is formed with a slag discharging port that is matched with a discharging pipe.    USE - Integrated water-pressure gas-collecting anaerobic fermentation device.    ADVANTAGE - The fermenting tank is arranged on the ground so as to reduce volume of the fermentation tank, thus improving organic waste processing efficiency and sewage purifying efficiency and increasing biogas production capacity. The device has high production efficiency. The side wall or bottom part of the fermentation tank is formed with the slag discharging port so as to realize quick and automatic slag discharging process in a convenient manner under action of gravity.
NOVELTY - Synthesis reactor comprises new-type gas distributor, upper cover plate, clapboard, cylinder, cooling pipe, central pipe, upper part cover plate, inner cavity, clapboard, gas collecting chamber, and a central pipe. The upper end of the baffle plate is set in the gas collecting chamber provided with a trumpet-shaped gas distributor.    USE - Reactor used for methanol synthesis.    ADVANTAGE - The reactor has a cooling pipe for raw material gas that is uniformly distributed and high efficiency. The reaction layer has small temperature difference to the radial plane.
NOVELTY - Essential oil, chlorogenic acid, flavone, biopesticide, bioethanol, and melanin are simultaneously extracted from Eupatorium adenophorum by using a squeezing and crushing device, a Maillard reactor, a three-phase separator, and a bioreactor.    USE - Simultaneous extraction of essential oil, chlorogenic acid, flavone, biopesticide, bioethanol, and melanin from Eupatorium adenophorum (claimed).    ADVANTAGE - The method is environmentally-friendly, energy-saving and economical, when compared with chemical single distillation.
NOVELTY - Bacillus subtilis strain W58 (CGMCC No. 5140) is new.    USE - Bacillus subtilis strain W58 comprising microbial inoculum is used for: biological deodorizing; and deodorizing and purifying garbage, domestic sewage, and animal housing air (all claimed).    ADVANTAGE - The bacterial strain has obvious deodorizing and bacteriostatic effect on multiple foul environments. The microbial inoculum has high ammonia average removal rate, hydrogen sulfide average removal rate, and odor concentration uniform removal rate.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for: (1) a microbial inoculum produced by Bacillus subtilis strain W58 as active ingredient; and (2) producing microbial inoculum by Bacillus subtilis strain W58, comprising (i) strain activating, inoculating the Bacillus subtilis strain W58 stored at -20 degrees C on the Lysogeny broth (LB) plating medium, culturing for 20-24 hours at 28-32 degrees C to obtain the activated functional strain, (ii) preparing seed liquid, selecting the single colony, inoculating the activated functional strain into the LB liquid medium, shake culturing for 20-24 hours at 28-34 degrees C to obtain the seed solution, and (iii) fermenting and culturing, inoculating the seed solution obtained in the step (ii) into the fermentation medium according to a volume percentage of 1-10%, culturing for 24-30 hours at 28-34 degrees C and at a rotating speed of 150-200 revolutions/minute to obtain the liquid preparation of the functional strain W58, where the fermentation medium comprises 0.4-0.8% dipotassium hydrogenphosphate, 0.1-0.3% potassium dihydrogenphosphate, 0.1-0.4% sodium chloride, 0.02-0.04% magnesium sulfate heptahydrate, 0.015-0.025% calcium chloride dihydrate, 0.1-0.3% ammonium sulfate, 2-4% sucrose, 1-3% soybean meal and water (balance).
NOVELTY - Aerobic fermentation of compost, comprises (a) preparing a coconut shell activated carbon; and (b) heating the compost at the initial stage of aerobic fermentation, adding livestock manure and the prepared coconut shell activated carbon, and making the fermentation temperature rapidly reach more than 80 degrees C.    USE - The method is useful for aerobic fermentation of compost (claimed).    ADVANTAGE - The method ensures short fermentation time, low energy consumption and low cost.
NOVELTY - Glyphosate microbiological degradation agent, is prepared using raw materials comprising microbiological fermentation mixed solution, straw charcoal powder, turf, dried chicken dung and nitrogen in the weight of 1:5-10:10-5:3-4:1-2. The microbiological fermentation mixed solution is fermentation solution of Bacillus mucilaginosus, B.megaterium, Azotobacter and Streptomyces microflavus in the volume ratio of 2-3:1-1.5:1-1.5:1-2.    USE - The agent is useful for degrading glyphosate which is useful for removing weeds in farmland, and as microbiological fertilizer.    ADVANTAGE - The agent can be prepared cost-effectively and simply, is suitable for large-scale production, and reduces labor cost.
NOVELTY - A multifunctional biomass heat transform device comprises gas channel (1), activating agent or gasification agent inlet, feeding port, feeding sealing device of gear cover, feeding shoveling plate (6), gear, transmission and gear box (8), heat preservation cotton, cylinder angle adjusting bolt (11), temperature measuring device, combustion channel, product channel, discharging sealing device of gear cover, ignition hole, explosion-proof opening, combustion supporting or viewing port and discharge cooler (21).    USE - Multifunctional biomass heat transform device.    ADVANTAGE - The device can be adjusted by changing the inclination angle.    DESCRIPTION OF DRAWING(S) - The drawing shows a structure schematic diagram of multifunctional biomass heat transform device.    Gas channel (1)    Feeding shoveling plate (6)    Gear box (8)    Cylinder angle adjusting bolt (11)    Discharge cooler (21)
NOVELTY - A microbial agent is used for improving alkaline soil.    USE - A microbial agent is used for preparing microbial fertilizer for improving alkaline soil (all claimed).    ADVANTAGE - The fertilizer improves alkaline soil physical and chemical properties, improves soil structure, improves permeability, and improves fertility of soil.
NOVELTY - A ginkgolide A, B or C is separated and purified from Ginkgo biloba leaf extract by dissolving extract in hot water, stirring mechanically or subjecting to ultrasonic treatment, filtering, dissolving the filter cake in hot water and repeating steps for 3-5 times, combining filtrate, concentrating to adjust relative density of filtrate, adding polyamide material, subjecting mixture to a polyamide column, eluting column with water (1-3 times column volume), collecting eluent, decompressing, setting aside, crystallizing using ethanol (1-3 times set aside product quantity), and filtering.    USE - Method of separating and purifying ginkgolide A, B or C from G. biloba leaf extract for medicine or health products (claimed).    ADVANTAGE - The method is simple and short, obtains product having a purity of higher than 90%, is low cost and environment-friendly, and can be applied to industrial production.    DETAILED DESCRIPTION - A ginkgolide A, B or C is separated and purified from Ginkgo biloba leaf extract by dissolving the extract in hot water, stirring mechanically or subjecting to ultrasonic treatment, filtering, dissolving the filter cake in hot water and repeating the above steps for 3-5 times, combining the filtrate, concentrating to adjust relative of the filtrate, adding polyamide material, subjecting mixture to a polyamide column, eluting column with water (1-3 times column volume), collecting the eluent, decompressing and concentrating, setting aside, crystallizing using ethanol (1-3 times set aside product quantity), and filtering.
NOVELTY - The valve has a guide plate formed as an arc-shaped structure. One end of the guide plate is connected with an inner wall of a valve body, and another end is contacted with a bottom of the valve body. A top part of the valve body is opened with an outer side of the guide plate. An outside of a valve body wall is arranged in a rubber plate that is covered on a vent hole.    USE - Bio-mass gasification furnace integrated gas return protecting valve.    ADVANTAGE - The valve is simple in structure and inexpensive, and prevents high temperature air in a chamber, avoids risk of explosion of a gas return flow fan and ensures production safety and personal safety of an operator.
NOVELTY - Processing chicken manure in henhouse, in which the chicken droppings are dropped onto the hollow bottom manure channel of the henhouse, comprises setting filteration ditch at the bottom part, scattering the rice hull to 5 cm thickness to form rice hull layer on the manure channel, and spraying once effective microorganism (EM) bacteria as decomposition bacteria for every 20 days according to 20 chickens/square meter directly onto the chicken manure, when the spray time of EM bacteria reaches more than 4 times, the manure material within the channel is produced into agricultural fertilizer.    USE - The method is useful for processing chicken manure in henhouse (claimed).    ADVANTAGE - The method utilizes a filtration ditch that can effectively filter away less amount of manure waste water; solves the chicken manure fermentation and odor problems by matching rice hull layer and the EM bacteria; produces agricultural fertilizer, which is environmentally friendly; can process the wastes into useful product; and reduces the pollution, and generates additional income.
NOVELTY - Method for preparing nutritious soil, involves mixing fermented Citrus peel residue and shaximiao formation purple soil, spreading the mixture, covering the mixture with a agricultural plastic film, exposing the mixture to sunlight to obtain Citrus peel residue nutritious soil, drying the mixture, pulverizing the mixture, and sieving the pulverized mixture.    USE - The method is useful for preparing nutritious soil (claimed).    ADVANTAGE - The method is simple, economic and environmentally-friendly, provides easy storage of fermented Citrus peel residue, overcomes use of energy consumption, saves resources of grass peat and changes waste into valuable products.    DETAILED DESCRIPTION - Method for preparing nutritious soil, involves mixing 1 pts. wt. fermented Citrus peel residue and 2-4 pts. wt. shaximiao formation purple soil, spreading the mixture, covering the mixture with a agricultural plastic film, exposing the mixture to sunlight in sunny days for 15-25 days to obtain Citrus peel residue nutritious soil, where the soil comprises 7-8 pts. wt. Citrus peel residue, 1.5-2 pts. wt. rice hull, 0.5-1 pts. wt. dry cow dung and 0.2-0.4 pts. wt. fertilizer, and the mixture has pH of 5.6-7, drying the mixture until the water content is 30% or less, pulverizing the mixture, and sieving the mixture to 4 mm.
NOVELTY - An Acinetobacter lwoffii deposited under CGMCC No. 5973, is new.    USE - The Acinetobacter lwoffii is useful for preparing additive cellulose ester film for optical application (claimed).    ADVANTAGE - The method is environment-friendly, where waste liquid is directly transformed into organic fertilizer, thus zero emission and zero pollution are achieved. A biological treating process performs protection to the fibers. Compared with a traditional chemical method, the method has the advantages of being low in producing cost, high in economic benefit, and is capable of saving an energy resource and protecting an environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for preparing additive for cellulose, comprising: (a) bacterial liquid is configured according to Acinetobacter lwoffii mixed with water to form bacterial liquid; (b) raw material processing: the woody raw material after cortex slice, or the herbal raw material cutting section, to cut the raw material into the soaking pool swelling; and (c) preparing the seal coat of fiber, comprising the steps of: mitigating the swelling of the thread raw material crushing and/or grinding, biodegradable, the hydrophobic solution as raw material to soak the prepared bacterial liquid, steam sterilizing: putting the biodegradable raw material from bacteria liquid, draining, steam sterilizing, obtain the fiber: putting the sterilized raw material for the first time period, a fiber bundle, the first time period for the second section grinding fine grinding to make the fiber beam be separated single fiber, screening, filtering after a period of grinding and the slurry after the second fine grinding of the fiber bundle, and then grinding to make it into single fiber, sterilizing: putting the prepared fiber is soaked in warm water, then drying, sterilizing, and grinding: putting the sterilized fiber into cellulose to be as the additive.
NOVELTY - A Pseudomonas fluorescens deposited under CGMCC No. 5974, is new.    USE - The Pseudomonas fluorescens is useful for preparing additive cellulose ester film for optical application (claimed).    ADVANTAGE - The method is completely environment-friendly, because all waste liquid can be directly converted into organic fertilizers. In a biological treatment process, fibers are protected. Compared with the conventional chemical methods, the production cost is low, the economic benefit is high, energy can be saved and pollution is avoided.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for preparing additive for cellulose, comprising: (a) bacterial liquid is configured: the Pseudomonas fluorescens is mixed with water to form bacterial liquid; (b) raw material processing: the woody raw material after cortex slice, or the herbal raw material cutting section, to cut the raw material into the soaking pool swelling; and (c) preparing the seal coat of fiber, comprising mitigating the swelling of the thread raw material crushing and/or grinding, biodegradable, the hydrophobic solution as raw material to soak the prepared bacterial liquid, steam sterilizing: putting the biodegradable raw material from bacteria liquid, draining, steam sterilizing, obtain the fiber: putting the sterilized raw material for the first time period, a fiber bundle, the first time period for the second section grinding fine grinding to make the fiber beam be separated single fiber, screening, filtering after a period of grinding and the slurry after the second fine grinding of the fiber bundle, and then grinding to make it into single fiber, sterilizing: putting the prepared fiber is soaked in warm water, then drying, sterilizing, and grinding: putting the sterilized fiber into cellulose to be as the additive.
NOVELTY - The water replenishing device has a water inlet unit, a water storage unit, a conveying unit, and a producing unit. The water inlet unit is connected with the water storage unit. The water storage unit is connected with the producing unit, through the conveying unit.    USE - Water replenishing device for preparing hydrogen.    ADVANTAGE - The production efficiency of the water replenishing device can be improved. The continuous production by the device can be ensured.
NOVELTY - The hydrogen generating device has an anode plate that is set with a cylindrical cathode plate. The cathode and anode plates are provided with a separating film. An electrolyzing chamber is divided into anode sub cavity and cathode sub cavity. An oxygen collector is set with a sealing cover. An upper end of a fog spray head device is installed on a pole plate. The pole plate is connected by the sealing cover. The oxygen collector is provided with oxygen outlet pipe. A top side is provided with a pressure limiter.    USE - Hydrogen generating device.    ADVANTAGE - The structure of the hydrogen generating device is simple and novel. The production efficiency of the device is high, and the production speed of the device is fast. The purity of the generated hydrogen by the device is high. The energy consumption by the device is reduced. The use of the device is environment-friendly, and the practicability of the device is strong.
NOVELTY - Plasma energy efficient gas stove comprises an alternate current power supply, a battery, a metal water inlet pipe, a water inlet electromagnetic valve, a temperature sensor, a water evaporator, an intelligent controller, a high voltage power supply, a low temperature plasma generator, a flame arrestor, an ejector, a stove, a distributor, an integrated control valve, a micro switch, a metal air inlet pipe, an air inlet electromagnetic valve, an induction needle, an ignition needle, a furnace frame, a bottom shell, a panel, an anti-dirt plate and a furnace frame structure.    USE - Used as plasma energy efficient gas stove.    ADVANTAGE - The stove saves fifty percent of gas and ensures replacement of high and new technology products.
NOVELTY - The method involves treating a wood in a hot reaction zone at temperature of 350-750 degrees Celsius and process pressure of 10-1000 kPa with a retention time of greater than 10 seconds in a continuous or batch arrangement. A pyrolyzed material is treated with a solution to obtain exchange ion of sulfuric acid on ash generated by a burning biochar of a pyrolysis feedstock product.    USE - Raw materials recycled ions treatment method for obtaining fast pyrolysis timber bio-oil.
NOVELTY - A sulfonic acid derivative (I) is new.    USE - Sulfonic acid derivative used as catalyst in esterification or transesterification of fats or oils, such as edible oil, non-edible oil, residual oil, animal fat or their mixtures into biodiesel (all claimed).    ADVANTAGE - The sulfonic acid derivative provides biodiesel in a simple and cost-effective manner by using inexpensive raw materials, such as fats or edible oils. The produced biodiesel efficiently replaces traditional energy sources such as coal, oil or natural gas.    DETAILED DESCRIPTION - The sulfonic acid derivative of formula (I) is new.    Cy1=represents benzene, naphthalene, anthracene or phenanthrene;    R1=independently represents 10-50C alkyl group, which is optionally replaced by R3 group;    R2=independently represents SO3H group;    R3=independently represents halogen;    n=0-4; and    m=1-5.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical representation depicting comparison of conversions achieved by different three catalysts. (Drawing includes non-English language text).
NOVELTY - A fuel producing method involves processing sewage sludge with sorbent in a form of layered aluminosilicate through a halloysite thermolysis process, and generating gases including carbon dioxide and ammonia, and water molecules to obtain finished product.    USE - Method for producing fuel.
NOVELTY - An ester of fatty acids and trimethylolpropane preparation method involves performing transesterification of vegetable fatty acid methyl esters at 80-160 degrees C for 4-10 hours in the presence of a heterogeneous catalyst base of ionic liquid compound, followed by removing distillate containing methanol and processing mixture to obtain finished product.    USE - Method for preparing ester of fatty acids and trimethylolpropane.    DETAILED DESCRIPTION - An ester of fatty acids and trimethylolpropane preparation method involves performing transesterification of vegetable fatty acid methyl esters at 80-160 degrees C for 4-10 hours in the presence of 1-15 cg/g heterogeneous catalyst base of ionic liquid compound of formula (Z-N-R)OH, followed by removing distillate containing methanol and processing mixture to obtain finished product.    Z=organic cation formed from cyclic diamine and/or triamine;and    R=2-8C aliphatic substituent.
NOVELTY - Zirconia nanotubes are formed by anodic oxidation of zirconium metal in an electrolyte comprising a halogen-containing electrolyte.    USE - Manufacture of zirconia nanotubes for use in manufacture of hydrogen (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) zirconia nanotube; and    (2) manufacture of hydrogen.
NOVELTY - The purpose of this invention is to provide a wastewater treatment system. The system is consisted of a wastewater storage tank, a flow regulation tank, several aeration tanks, a sedimentation tank, a wastewater pump, and an aeration pump. The system is suitable for treating sewage water, swine waste, and industrial wastewater containing oxygen demanding organic matters and nutrients. The aeration tanks are filled with oyster shell. The rough surfaces of oyster shells provide stable sites for the growth of microorganisms with excessive density, resulting in an efficient water purification capability. The irregular size and shape of oyster shells, together with tank design and operation control, can create a condition allowing coexistence of aerobic, anaerobic and facultative micro-environments within the tanks, achieving nitrogen removal through simultaneous nitrification- denitrification biochemical reactions. The sedimentation tank is also filled with oyster shells to provide a quiescent settling environment for the efficient removal of wasted sludge. The use of oyster shells in this system provides efficient water purification functions. It also has the benefits of low cost and waste reuse.
NOVELTY - Ethanol is manufactured by mixing pulverized lignocellulosic biomass with water and ethanol solution, producing saccharide from lignocellulosic biomass contained in liquid mixture, performing ethanol fermentation of saccharide to obtain ethanol from saccharide, and distilling fermented liquor. Saccharified liquid supplied to fermentation process is made to contain ethanol by returning part of fermented liquor after completion of fermentation process to saccharification process resulting in ethanol concentration in fermented liquor of 4-15 mass%.    USE - Manufacture of ethanol for bioethanol manufacture.    ADVANTAGE - Distillation load is reduced, manufacturing cost of ethanol is reduced, and proliferation of microorganisms in fermentation process is prevented.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for ethanol manufacturing apparatus comprising mixing tank (1) which mixes pulverized lignocellulosic biomass, water, and ethanol solution, saccharification tank (2) which supplies liquid mixture and obtains saccharide from lignocellulosic biomass, fermenter (3) to which ethanol fermentation of saccharide obtained from saccharification tank is performed, distillation apparatus (4) which distills fermented liquor obtained from fermenter, and return path (8) which returns to mixing tank as ethanol solution which uses from fermenter a part of fermented liquor supplied to distillation tank in mixing tank.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the manufacture of ethanol. (Drawing includes non-English language text).    Mixing tank (1)    Saccharification tank (2)    Fermenter (3)    Distillation apparatus (4)    Return path (8)
NOVELTY - Isolated nucleic acid molecule encoding a chimeric Cel7A polypeptide having a cellulase activity at least 1.5-fold greater than the wild-type Cel7A polypeptide, is new.    USE - The isolated nucleic acid molecule is useful: for degrading cellulose or lignocellulosic biomass; for producing a biofuel from lignocellulosic biomass (all claimed); and as probes and primers for the identification, isolation and/or purification of other nucleic acid molecules.    ADVANTAGE - The nucleic acid molecule exhibits enhanced cellulase activities, can be prepared in simple and cost-effective manner, and has increased stability, solubility, action and biological activity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) an expression vector comprising the nucleic acid molecule; (2) a host cell comprising the expression vector or expressing a recombinant polypeptide encoded by the nucleic acid molecule; (3) an isolated chimeric Cel7A polypeptide encoded by the nucleic acid molecule; (4) an isolated chimeric Cel7A polypeptide comprising domains from Penicillium funiculosum and Trichoderma reesei Cel7A polypeptides, where the chimeric Cel7A polypeptide has a cellulase activity at least 1.5-fold greater than the wild-type Cel7A polypeptide; (5) degrading cellulose or lignocellulosic biomass, comprising contacting the cellulose or lignocellulosic biomass with the isolated chimeric Cel7A polypeptide; and (6) producing a biofuel from lignocellulosic biomass, comprising (a) contacting the lignocellulosic biomass with an enzyme cocktail comprising the isolated chimeric Cel7A polypeptide to generate sugars, and (b) converting the sugars to a biofuel by fermentation.
NOVELTY - Method of generating fuel/fuel blending product involves providing a feed comprising algae-derived biomass from an algae growth environment, recovering fuel/fuel blending product and residual product from the algae-derived biomass, and performing gasification process on at least a portion of the residual product resulting in at least gas phase output stream comprising hydrogen and carbon monoxide and gasification residue stream.    USE - Method of generating fuel/fuel blending product e.g. biofuel (claimed).    ADVANTAGE - The method efficiently and economically generates fuel/fuel blending product, by exchanging input streams or energy between algae processing systems and system for processing non-algal biomass.    DETAILED DESCRIPTION - Method of generating fuel/fuel blending product involves providing a feed comprising algae-derived biomass from an algae growth environment, recovering fuel/fuel blending product and residual product from the algae-derived biomass, performing gasification process on at least a portion of the residual product resulting in at least gas phase output stream comprising hydrogen and carbon monoxide and gasification residue stream, purifying gas phase output stream by removing at least a portion of one or more contaminant compounds different from hydrogen and carbon monoxide and converting at least a portion of the purified gas phase output stream into one or more organic molecules. An INDEPENDENT CLAIM is included for method of generating biofuel.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic structure of system for generating fuel/fuel blending product.    Water stream (101)    Centrifuge (105)    Product stream (106)    Side water stream (107)    Water-storage tank (108)
NOVELTY - The solid oxide fuel cell (100) comprises a current collector (120) with an electrode (111). A cell (110) is provided with another electrode (115) formed with the groove. A supporting portion (123) is formed in the mesh structure, which is formed in the cell accommodating chamber (121). The wave type structure is formed by the cell accommodating chamber. The outer shape of the cell has the groove of the cell, where accommodating chamber is provided. The current collector has a coating layer made up of the manganese cobalt oxide.    USE - Solid oxide fuel cell for producing electricity.    ADVANTAGE - Ensures providing the contact force improvement of the metal current collector. Elastic force improvement is ensured. Coated with the reduction-resistant or the oxidation resistant layer to minimize chrome element volatilization of the metal. Secondary phase formation at the electrode boundary face or the inner surface is prevented.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for producing solid oxide fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the solid oxide fuel cell.    Solid oxide fuel cell (100)    A cell (110)    Electrodes (111,115)    Current collector (120)    Cell accommodating chamber (121)    Supporting portion (123)
NOVELTY - A biogas production system for farms or any facilities that generate animal waste, comprises a biodigester (1), drain (9), heat source (12), filter (16), biogas storage tank (19), and electric generator (23).    USE - The system is used for producing biogas and is used in farms or any facilities that generate animal waste (claimed).    ADVANTAGE - The biogas production system is easy to install, expand and transport, low-cost, and simple. The user can operate the system with basic training and can be maintained without the need for specialized technicians' visit. The system is capable of producing significant quantities of biogas without harm to the environment and with low chance of producing greenhouse gases. The system does not depend on oil and its derivatives. The biogas produced can be used, inter alia, in ovens, water heaters and electric generators.    DETAILED DESCRIPTION - A biogas production system for farms or any facilities that generate animal waste, comprises a biodigester (1) for producing biogas from the organic waste; a drain (9) which receives the treated organic waste from the biodigester; a heat source (12) for heating the waste, the biogas being produced in the biodigester, where the heat source is connected to the digester by a power injector and a hot water discharge current; a filter (16) for removing impurities from the biogas generated from fermenting organic waste in the digester; a biogas storage tank (19) to store the biogas free from impurities; and an electric generator (23) that runs on the biogas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biogas production system.    Biodigester (1)    Drain (9)    Heat source (12)    Filter (16)    Biogas storage tank (19)    Electric generator (23)
NOVELTY - The system (100) has vessel (102) that is provided with inlet to receive waste matter for processing within chamber (104). An outlet (108) is provided for processing waste matter within chamber. The chamber is arranged such that net flow of waste matter is from the inlet (106) towards outlet. An auger arrangement (112) is partially located within chamber. The primary unit (116) of auger arrangement is arranged to propel matter in direction from inlet into chamber and secondary unit (118) of auger arrangement is arranged to act against the flow of waste matter from inlet towards outlet.    USE - Thermal processing system such as pyrolysis and gasification systems for processing waste matter such as biomass, fuel and feedstock to produce synthetic gas.    ADVANTAGE - Since the secondary unit of the auger arrangement is arranged to act against the flow of waste matter from the inlet towards the outlet, the waste matter can be passed through the chamber smoothly without bridging and the compaction of material is avoided. Hence the efficiency of the system is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of operating thermal processing system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the thermal processing system.    Thermal processing system (100)    Vessel (102)    Chamber (104)    Inlet (106)    Outlet (108)    Auger arrangement (112)    Primary unit (116)    Secondary unit (118)
NOVELTY - Removal collection material of phosphorus involves carrying out crystallization of magnesium ammonium phosphate by vegetable porous carbonized material.    USE - Removal collection material of phosphorus used for soil conditioner (claimed).    ADVANTAGE - The method environmentally-friendly enables collection of phosphorus from the waste material by simple process, without reaction control operation (such as adjustment of pH) and special reaction apparatus.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for soil conditioner, which is obtained by carrying out removal collection material of phosphorus and including vegetable porous carbonized material and magnesium ammonium phosphate.
NOVELTY - Treating and recovering green algae by exothermic treatment with calcium oxide delayed reaction, comprises pretreating, exothermic treating and/or post treating green algae to obtain an innovating organic fertilizer and natural mineral product i.e. without chemical product.    USE - The process is useful for treating and recovering green algae, which are useful for destroying large pest and as rodent repellents. The product is useful: in food industry, nanomaterial field, construction field for manufacturing of insulating bricks for partitions with binder, and building lime applications (all claimed), and for agriculture. No biological data given.    ADVANTAGE - The process provides stable green algae, which naturally increases the pH of the soil thus provides improved environment, eliminates risk of fermentation and leachate, and is transported in bulk or packaged in flexible containers and mixed with complementary fertilizer without any risk during spreading for uniform spraying.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the product obtained by the process.
NOVELTY - The fuel cell has housing (101) that is provided to store water such as electrolyte and to receive conducting elements (102). A power supply unit (103) is provided to supply power to conducting element. A gap (104) is formed between level of water and top of housing and conducting element is arranged in housing and is immersed in water such that portion of conducting element is exposed in gap. The housing is provided with outlet (105) positioned to cooperate with gap. A zone is defined by gap for hydrogen collection and onward transmission through outlet.    USE - Multi-electrode plate fuel cell for producing hydrogen from water such as electrolyte.    ADVANTAGE - The design of the fuel cell is more efficient design resulting in improved efficiency for optimum energy input. The current drawn by the fuel cell generator is reduced, so that the production of oxyhydrogen gas with water vapor is increased and leads to increase in the efficiency of the internal combustion engine with reduction in emissions and improved performance. The efficiency of operation of the internal combustion engine can be increased and the emissions of undesirable gases from the internal combustion engine can be reduced.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) apparatus for increasing fuel efficiency of heating boiler; and    (2) method for producing hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fuel cell.    Housing (101)    Conducting element (102)    Power supply unit (103)    Gap (104)    Outlet (105)
NOVELTY - The system has a reactor (2) with a non-conductive conduit (4) for guiding an ionized particle stream having hydrogen cations (22) and oxygen anions (24). Magnets e.g. neodymium magnets, are oriented relative to the velocity of the stream so that cations are separated from anions as the stream moves via a static or dynamic magnetic field. A barrier (6) isolated the cations from the anions. A cooling system cools the cations and the anions to form two molecular combinations after the cations are isolated from the anions. One combination is directed into a conduit of another reactor.    USE - System for extracting a substance e.g. hydrogen, from a molecular combination such as water.    ADVANTAGE - The system extracts the hydrogen in a reliable and cost effective manner, with less number of parts and with reduced environmental costs.    DESCRIPTION OF DRAWING(S) - The drawing shows a simplified block diagram representing a top view cross-section of a substance extracting system.    Reactor (2)    Non-conductive conduit (4)    Barrier (6)    Hydrogen cations (22)    Oxygen anions (24)
NOVELTY - The apparatus (1) has a contact burning gas sensor (10) provided with a bridge circuit. The bridge circuit is provided with a sensor resistance unit (SU), a reference resistor (Ref) and two fixed resistors (R1, R2). A calculation part (31) computes concentration of detection-target gas based on output of the bridge circuit. A control part (33) controls the sensor part. A change-over-switch (SW) selects a sensor resistor among sensor resistors (Sn1, Sn2) when the control part controls a switching-operation of the change-over-switch.    USE - Gas detection apparatus for detecting target gas i.e. combustible gas such as hydrogen gas, methane gas and carbon monoxide gas.    ADVANTAGE - The change-over-switch selects the sensor resistor among the sensor resistors when the control part controls the switching-operation of the change-over-switch so as to control a residual sensor resistor in a non-energized state by selectively using the sensor resistors, so that over-time deteriorating degree of the apparatus can be suppressed when the sensor resistors are used continuously, thus suppressing fall of detection capability of a contact burning gas sensor in an effective manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a circuit block diagram of a gas detection apparatus.'(Drawing includes non-English language text)'    Fixed resistors (R1, R2)    Reference resistor (Ref)    Sensor resistance unit (SU)    Change-over-switch (SW)    Sensor resistors (Sn1, Sn2)    Gas detection apparatus (1)    Contact burning gas sensor (10)    Calculation part (31)    Control part (33)
NOVELTY - Producing methane enriched biogas from organic waste comprises: (a) placing organic waste material into a vessel; (b) removing the non-biodegradable from the resulting mixture; (c) anaerobically digesting the waste material; and (d) separating the gas mixture from solid and liquid mixture; where carbon dioxide is separated by using of capillary module with polyimide membranes and it is achieved the enrichment of methane from the concentrations of 55-85% up to 91-94.4%.    USE - The process or apparatus is useful for producing methane enriched biogas from organic waste, and can be used in both commercial and household systems (all claimed).    ADVANTAGE - The process provides a source of energy, thus reduces the waste materials into an effective fertilizer solution. Recycling waste material produces easily harnessed energy sources, thus magnifying the need in current energy shortage for alternative energy sources (all claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is an apparatus for producing methane enriched biogas from organic waste by the method, where processing a slurry of biodegradable waste materials includes two tanks containing waste material which are connected to allow fluid flow communication between slurry in each tank characterized in that carbon dioxide is separated by using of capillary module with polyimide membranes it was possible to achieve the enrichment of methane from the concentrations of 55-85% up to 91-94.4%.
NOVELTY - The method involves injecting solid fuel like low-class coal, biomass or waste in fluidized-bed gasification apparatus (110) among air, oxygen, or steam. The synthetic gas (130) produced in gasification apparatus is supplied to high temperature secondary reactor (120) by injecting particulate or liquid phase waste (150) in secondary reactor with air or oxygen. The tar contained in synthetic gas is disassembled by putting tar in fire so that 1000 degrees C high temperature is maintained. A synthetic gas removing tar (160) is provided to extract synthetic gas by removing the tar from reactor.    USE - Method for gasification of biomass with high temperature secondary reactor to tar free in synthetic gas.    ADVANTAGE - The unburned carbon containing asher ejected in the fluidized-bed gasification apparatus to the by-product is injected in the high temperature secondary reactor so that the fuel can be recycled. Hence the resource availability rate is enhanced effectively. The ashers are provided to inject solid fuel like low-class coal, biomass or waste in fluidized-bed gasification apparatus among air, oxygen, or steam so that the availability of the synthetic gas is increased. Hence the environment contamination problem can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram illustrating the process for gasification of biomass with high temperature secondary reactor. (Drawing includes non-English language text)    Fluidized-bed gasification apparatus (110)    High temperature reactor (120)    Synthetic gas (130)    Particulate or liquid phase waste (150)    Synthetic gas removing tar (160)
NOVELTY - Method of preparing black konjac dietary fiber solid beverage, involves weighing (in parts weight): black powder (30-60), konjac glucomannan (10-25), xanthan gum (0.01-0.2), xylitol (5-10), acesulfame (0.05-0.25), sucralose (0.02-0.05) and salt (0.3-0.8), mixing the materials uniformly to prepare mixed material, sterilizing the mixture by microwave instantaneous sterilization machine at 80-90 degrees C for 5-8 minutes, and packaging the sterilized mixture to obtain the black konjac dietary fiber solid beverage.    USE - The method is useful for preparing black konjac dietary fiber solid beverage which is used for resisting tumor (claimed).    ADVANTAGE - The black konjac dietary fiber can be prepared simply and easily. The method is environmentally-friendly, has smooth mouth feel, is rich in nutrition and convenient to eat and carry.
NOVELTY - The fabric comprises a chopped fiber needling non-woven soil engineering cloth layer, a modified montmorillonite mineral powder layer and a continuous fiber needle-punched nonwoven soil engineering cloth layer fixed by a needling process.    USE - Ecological restoration fabric for a farmland soil heavy metal and a sewage treatment plant.    ADVANTAGE - The fabric has strong absorbability. The fabric purifies ground water source and poisonous material so as to reduce heavy metal pollution of soil and water. The fabric saves energy and water resources. The fabric is environmental-friendly, simple in structure, convenient to construct and inexpensive.
NOVELTY - The reactor has a reactor unit which is provided with a sewage inlet and a sewage outlet. The lower portion of the reactor unit is provided with a sludge hopper. A baffle plate is provided in the reactor unit. The baffle plate portion is fixed with a guide plate. One of the ends of reactor space is formed with a water channel. The other end of reactor space is provided with a frame. The sewage outlet of reactor unit is connected with the sewage inlet.    USE - Folding bed bio-membrane reactor used for processing sewage in rural areas.    ADVANTAGE - The floor area occupied by the bio-membrane reactor can be reduced. The cost for processing the sewage can be reduced. The processing effect of the reactor can be improved. The self-renewing capacity of the reactor can be improved. The reactor can be maintained easily. The power consumption of the reactor can be reduced. The sewage processing task can be performed automatically, without the manual intervention. The operation cost of the reactor can be reduced.
NOVELTY - The device has control pressure exhaust valve, pressure valve, main control valve for preventing reverse-flow and biogas burning device that are connected in turn by gas guide pipeline. The control pressure exhaust valve is connected with the marsh gas tank by gas guide pipeline. An ignition controller is respectively connected with the two ends of the anti-reflux valve and biogas burning device.    USE - Composite biogas pressure reducing device.    ADVANTAGE - The pressure reducing device is simple in structure, and convenient to use. The rain-proof effect of the pressure reducing device can be improved. The anti-touch on the burning furnace can be improved. The security effect of the pressure reducing device can be improved.
NOVELTY - A high purity thalidomide is prepared by dissolving thalidomide crude product in hot dimethyl sulfoxide or heated mixture of dimethyl sulfoxide and fatty alcohol as a solvent, decoloring by adding activated carbon, filtering while hot, and cooling the filtrate to crystallize.    USE - Method of preparing high purity thalidomide (claimed).    ADVANTAGE - The method is simple and environment-friendly, has high yield, and prepares product having a purity of more than 99.9%.
NOVELTY - A weeding water dispersible granule comprises isoproturon (30-50%), cyhalofop-butyl (5-10%), dispersing agent (4-10%), wetting agent (1-3%), disintegrating agent (3-5%), and carrier (2-3%). The granule further comprises adhesive.    USE - As a weeding water dispersible granule (claimed) which is used as herbicide for controlling weeds and treating rice stem leaf.    ADVANTAGE - The weeding water dispersible granule can be prepared environment-friendly; is easy and safe for transportation; has low dosage and low preparation cost; and provides improved crop safety.
NOVELTY - Preparation of solid catalyst involves mixing aluminum trichloride (100 g), zirconium oxychloride and three cutter chloride and dissolving in water (1000 g), stirring in ice water bath and adding 28% mass fraction aqueous ammonia to pH of 9-10, aging at room temperature for 24 hours, filtering, washing with deionized water until no chloride ion, drying at 110 degrees C for 12 hours, grinding through 100 mesh sieve using ammonium persulfate (0.5 mol/l) impregnated for 12 hours, filtering, washing filter cake until neutral, drying at 110 degrees C for 4 hours, and roasting at 550 degrees C for 5 hours.    USE - For preparation of solid acid catalyst (claimed) for making e.g. bio-diesel fuel.    ADVANTAGE - The catalyst has high activity and stability, uses small dosage, can be applied to high value of raw material oil without causing the deactivated catalyst, effective for making biodiesel having quality, which reaches the national bio-diesel engine fuel, and has good applicability and practical value.
NOVELTY - A Ganoderma lucidum culture medium comprises 45-55 pts. wt. peanut straw, 25-35 pts. wt. cottonseed hull, 8-12 pts. wt. corn powder, 5-7 pts. wt. bran, 1-3 pts. wt. gypsum, 0.8-1.2 pts. wt. lime, and 0.8-1.1 pt. wt. magnesium sulfate. When the cultivation medium is prepared it is added with 1.3-1.5 times water based on total weight of peanut straw and cottonseed hull.    USE - Ganoderma lucidum culture medium.    ADVANTAGE - The culture medium utilizes low cost and easy to obtain raw materials, can produce high yield of Ganoderma lucidum with high quality and strong resistance to infection, and does not cause chemical reagent pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the Ganoderma lucidum culture medium, comprising:    (A) crushing peanut straw into particles, then mixing with cottonseed hull, adding water and uniformly stirring, covering with plastic film and fermenting for 10-14 hours;    (B) after fermentation is finished, removing the plastic thin film, adding corn powder, bran, gypsum, lime, and magnesium sulfate, and uniformly mixing;    (C) putting the mixed material into bag at 1.8-2.2 kg/bag; and    (D) steam sterilizing the material bag at 95-105 degrees C for 18-22 hours, and cooling to normal temperature to obtain the culture medium.
NOVELTY - The workshop has a rotten ferment workshop located on a bottom gap. The rotten ferment workshop is connected with a material pre-processing workshop. A packaging workshop production area is located in the bottom gap. A cooked production packaging plant and the rotten ferment workshop are linked with a movable door.    USE - Organic fertilizer production workshop.    ADVANTAGE - The workshop realizes centralized mechanical process. The workshop achieves decomposing process without bad smell dejecta, so that air pollution is avoided. The workshop is reasonable in design and convenient to operate, and has low energy consumption.
NOVELTY - Plant straw solar energy gasification and waste residue-wastewater collection and utilization device comprises a straw pretreatment material pool and a fermentation tank arranged in a solar energy warm house, an air storage tank and a waste collection device arranged outside the solar energy warm house. The fermentation tank is a cylindrical horizontal type sealed tank, where one end of the tank is made into a manhole, and the lower part of the tank is provided with a tank clearing and draining device. The tank is arranged on a base in the solar energy warm house through a tank landing leg.    USE - Used as a plant straw solar energy gasification and waste residue-wastewater collection and utilization device.    ADVANTAGE - The device drives feeding and discharging process by motor, thus ensures low labor intensity and high production efficiency, utilizes the fermentation tank provided with multiple stirrers to uniformly stir the materials in the tank, and has good gasification effect and high rate of factor of gasification.
NOVELTY - Separating and cooling system comprises a rectifying tower provided with a circulating pipe, a condenser, and a protective layer located outside of the condenser. The upper part of the rectifying tower is provided with an outlet. The outlet is connected with a condenser inlet via a pipeline. The condenser inlet is set on one end of the condenser.    USE - The system is useful for preparing biodiesel oil (claimed).    ADVANTAGE - The system has simple structure and high cooling efficiency, comprises the condenser, which is capable of self-processing, does not require to purchase a complete set of equipment, and is suitable for wide occasions and for indoor use.
NOVELTY - Preparing Cynanchum chinense extract, involves selecting medicinal parts of the Cynanchum plant; extracting the Cynanchum plant using water or ethanol-water mixed solvent; concentrating the solution using concentrated solution, diluting the obtained solution by adding proper amount of water, and filtering the solution to obtain Cynanchum extract; carrying out adsorption of Cynanchum extract, using pretreated macroporous resin or polyamide, then concentrating the mixture, and drying to obtain the finished product.    USE - In the preparation of Cynanchum chinense extract (claimed) which is used in treating inflammation-related diseases.    ADVANTAGE - The Cynanchum extract has improved anti-inflammatory effects. The method of making Cynanchum extract is economic and reasonable; provides high efficiency, low energy consumption; and is easy to realize industrial production. The plant resource and solvents used in the method are convenient to recycle.    DETAILED DESCRIPTION - Preparing Cynanchum chinense extract, involves selecting medicinal parts of the Cynanchum plant; extracting the Cynanchum plant using water or ethanol-water mixed solvent; concentrating the solution using concentrated solution, diluting the obtained solution by adding proper amount of water, and filtering the solution to obtain Cynanchum extract; carrying out adsorption of Cynanchum extract, using pretreated macroporous resin or polyamide, firstly, using 0-20% of water or ethanol for elution, then 40-95% of ethanol for elution, and the 40-95% of ethanol for elution, then concentrating the mixture, and drying to obtain the finished product.
NOVELTY - The device has molecular sieve towers (A,B) which are arranged in parallel and orderly connected with the inlet valves (22,23). The regenerative inlet valves (20,21) are connected with the molecular sieve towers whose bottom is provided with outlet valves (26,27) which are orderly connected in series. The regenerative outlet valves (24,25) are connected with the methanol tank (7) through which the outlet valve pipe passes. The methanol end product pump (19) is connected with the outlet valves of molecular sieve tower by methanol pump (15) connected with the rectification kettle (4).    USE - Device for recovering and purifying biodiesel methanol.    ADVANTAGE - The device consumes less energy for recovering and purifying biodiesel methanol so that high recycling rate of heat energy, high purity and the production process without pollution can be achieved so that the overall efficiency is high.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for recovering and purifying biodiesel methanol.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for recovering and purifying biodiesel methanol. (Drawing includes non-English language text)    Rectification kettle (4)    Methanol tank (7)    Methanol pump (15)    Methanol end product pump (19)    Regenerative inlet valves (20,21)    Inlet valves (22,23)    Regenerative outlet valves (24,25)    Outlet valves (26,27)    Molecular sieve towers (A,B)
NOVELTY - A passivation method of biomass fuel involves uniformly spraying 10-20 wt.% boric acid solution to 5-10 wt.% biomass fuel, stirring uniformly, uniformly spraying 5-15 wt.% silica sol solution to 4-8 wt.% biomass fuel, and uniformly stirring 3 wt.% biomass fuel with quartz particle size of less than or equal to 20 mu m micro-powder into the biomass fuel.    USE - Passivation method of biomass fuel for iron ore sintering (claimed).    ADVANTAGE - Effective reaction surface area of the biomass fuel, micro-hole and gas hole and reaction activity are reduced.
NOVELTY - Purifier comprises 20-25 wt.% of silicon dioxide, 20-25 wt.% of nickel dioxide, 20-25 wt.% of manganese(IV) oxide, 0.1-7 wt.% of ferric oxide, 8-18.5 wt.% of aluminum oxide, 0.1-5 wt.% of zinc oxide and adhesive as raw materials.    USE - The purifier is useful for purifying acetylene propane, liquefied petroleum gas and fluid catalytic cracker gasoline (claimed).    ADVANTAGE - The purifier agent is prepared by simple and cost-effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for purifying acetylene, propane, liquefied petroleum gas and fluid catalytic cracking (FCC) petroleum, comprising introducing acetylene, propane, liquefied petroleum gas and FCC petroleum into a purifying tank, adding a purifying agent into the tank at normal temperature under the normal pressure, saturating sulfur impurities of the mixture in the tank, carrying out external heating process on the purifying tank at 100-600 degrees C, and regenerating the purified agent from the tank using regenerative exhaust at normal pressure gas until the water and sulfur impurity are removed.
NOVELTY - Botanical natural disinfectant comprises 10-25 pts. vol. garlic essential oil, 100 pts. vol. plant essential oil mixture, 190-250 pts. vol. organic solvent, 100-250 pts. vol. surfactant and 900-2500 pts. vol. water.    USE - The disinfectant is useful for preventing hot pepper powdery mildew (claimed).    ADVANTAGE - The disinfectant: comprises refined garlic oil as a fungicide; comprises more than two other plant essential oils as a synergistic agent, thus improving the powdery mildew preventing efficiency; combines plant essential oil and different chemical composition, thus reducing dosage and preventing the mildew although the dosage is low; prevents the generation of resistance; exhibits synergistic effect with the chemical composition having different functional groups; increases the permeability of the chemical composition, thus improving the efficiency of crop persistence; and is derived from natural medicinal plants, thus the composition is non-toxic to human and livestock, and safe to the environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the botanical natural disinfectant, comprising (a) uniformly mixing garlic essential oil and essential oil mixture to obtain mixture I, and dissolving in an organic solvent to obtain mixture II, (b) mixing a surfactant and water to obtain mixture III, and (c) mixing the mixture II with the solvent, and uniformly stirring at 50-80 degrees C at a rotating speed of 1000-4000 revolutions/minute for 10-40 minutes.
NOVELTY - A Pseudomonas fluorescens J61 (CGMCC No. 4705) for producing cyclohexene and phenol, is new.    USE - The P. fluorescens J61 (CGMCC No. 4705) is useful for producing cyclohexene and phenol (claimed).    ADVANTAGE - The bacterial strain can effectively degrade diethylstilbestrol and is environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for producing cyclohexene and phenol by culturing P. fluorescens in Luria Bertani (LB) culture medium comprising diethylstilbestrol at 28-30 degrees C, 180-200 rounds per minute (rpm), and 10-16 hours, where the strain degrades diethylstilbestrol; performing HPLC and detecting the amount of remaining diethylstilbestrol.
NOVELTY - A multifunctional traditional Chinese organic fertilizer comprises 30% rice bran powder, 30% humic acid, 19% plant ash, 10% bone powder, 3% medical stone, 3% Chinese herbal medicine, 2% syrup, 1% yeast, and 2% strain. The strain comprises 20% effective microorganisms (EM) strain, 10% DA-6, and 10% Bacillus subtilis.    USE - A multifunctional traditional Chinese organic fertilizer.    ADVANTAGE - The multifunctional traditional Chinese organic fertilizer is prepared using a simple method, has improved utilization rate, and is safe.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the multifunctional traditional Chinese organic fertilizer, comprising crushing Chinese herbal medicine, rice bran powder, humic acid, plant ash, and bone powder, and filtering using 80-100 mesh screen filter; adding bone powder, syrup, and yeast; uniformly mixing while adding water to a water content of 50-60%; fermenting at 24 times for 48 hours at normal temperature; adding an additive, and adding strain; and granulating at not greater than 80 degrees C, and keeping the humidity at 20-30%.
NOVELTY - Zinc type alkaline resistant water organic fertilizer comprises 220-225 pts. wt. fermented protein, 175-195 pts. wt. humic acid, 10-20 pts. wt. zinc, 25-40 pts. wt. iron, 15-18 pts. wt. cattle and 50-60 pts. wt. water retention agent.    USE - Zinc type alkaline resistant water organic fertilizer.    ADVANTAGE - The fertilizer has heat preservation effect, supplements crop needed microelement, and improves crop yield and quality. The fertilizer solves problem caused by high pH and high salt which results to bad fertility and low nutrient and biological effectiveness.
NOVELTY - Device comprises orderly arranged synthesis device, a refining device and a post-processing device. The synthesis device includes a dissolving kettle connected to an acylation kettle via a filter A, and an acidifying kettle connected to acylation kettle. The refining device includes a de-coloring kettle connected to a crystallizing kettle via filter D and a microporous membrane filter, and the crystallizing kettle connected to filter E. The post-processing device includes vacuum drying tank, crusher and mixer. A solvent tank and a raw material overhead tank are connected to acylation kettle.    USE - The device is useful for producing rebamipide (claimed).    ADVANTAGE - The device is economical and environmentally friendly, and has low energy consumption, hence the prepared product has high yield and good quality.
NOVELTY - Microalgae with high fat content and its accumulation in culture condition, is new.    USE - The microalgae is useful in the production of microalgae biodiesel.    ADVANTAGE - The fat content in the cultured microalgae meets the microalgae biodiesel standards.
NOVELTY - An animal corpse biochemical treatment device comprises a biodegradable tank provided with oxygen supply device and connected with slag car. Upper end of the biodegradable tank is connected with inlet of condenser. The condenser is connected with water filtering device. Air filter device is set on upper end of exhaust pipe. Lower end of the air filtering device is provided with a water discharging device.    USE - An animal corpse biochemical treatment device.    ADVANTAGE - The device is environment-friendly, has no harmful gas and no peculiar smell. Water after degradation can be directly recycled or directly discharged. Residue can be used as fertilizer. Treatment process is simple.
NOVELTY - Bio-diesel oil continuous esterification dehydration reaction device comprises a methanol tank, a heater, a reaction kettle, a dehydrator and a dilute methanol tank. The methanol tank through the heater is connected to the upper part of the reaction kettle. The top part of the reaction kettle is further provided with a stirrer. The dehydrator is provided with a condenser. The inlet to the top part of the reaction kettle is connected with the condenser. The outlet of the condenser is connected with the dilute methanol tank.    USE - Used as a bio-diesel oil continuous esterification dehydration reaction device.    ADVANTAGE - The device can continuously dehydrate, can greatly shorten the reaction time, and improves the production efficiency.
NOVELTY - A ginkgolide is separated and purified by dissolving Ginkgo biloba leaf extract in ethanol or methanol aqueous solution, filtering, drying the filter cake, dissolving in greater than or equal to 10 vol.% methanol, subjecting to reverse phase silica column, eluting with methanol-isopropanol-water having a volume ratio of 23-27:8-12:63-67, combining the bilobalide section eluent, concentrating to obtain dry ginkgolide, re-crystallizing crude ginkgolide, and drying.    USE - Method of separating and purifying a ginkgolide (claimed).    ADVANTAGE - The method is short, obtains product having high purity, reduces equipment cost and energy consumption, and can be applied to industrial production.
NOVELTY - An organic fertilizer comprises 80-90 pts. wt. main material, 10-15 pts. wt. crop straw, 0.1-0.3 pt. wt. fermented auxiliary agent, 2-5 pts. wt. calcined lime, 1-3 pts. wt. fermentation diluted auxiliary material and 5-8 pts. wt. brandy.    USE - Organic fertilizer.    ADVANTAGE - The organic fertilizer inhibits plant diseases and insect pests, and improves soil environment pH value, which is good for growth of crops.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS is included for:    (1) preparing organic fertilizer comprising:(A) uniformly mixing main material and plant straw by stirrer, conducting water testing, requiring 57-62% moisture, to obtain first mixed material; (B) mixing fermentation auxiliary agent and diluted auxiliary material at a ratio of 1:5, mixing temperature is 0-35 degrees C, mixing and storing for 3-12 hours, to obtain secondary mixed material; (C) mixing secondary mixed material and first mixed material, stirring uniformly to obtain third mixture; (D) placing third mixture in fermentation tank, height is 1-1.2 m, inserting thermometer into third mixture to a depth 0.5-0.6 m; (E) starting and turning third mixed material at temperature of 70 degrees C; after 13-15 days stacking height of 1/3, fermenting third mixed material to obtain semi-finished product; (F) adding brandy, calcium oxide, drying to water content of 20% to obtain finished product; packaging and storing; and (G) mixing semi-finished product and finished product at a ratio of 40:100-45:100; and    (2) using organic fertilizer comprising: taking organic fertilizer as base fertilizer, bottom, hole fertilizing ditch, burying; organic fertilizer with single fertilizer, base fertilizer every 667 m2 dosage accounts for 60% of total amount of fertilizer, fertilizer every 667 m2 is 40% of total fertilizer.
NOVELTY - Production system comprises a storage bin, a magnetic separator, a primary crusher, a primary high speed rotating machine, a secondary crusher, a secondary high speed rotating machine, and environment protection hot-blast stove, a waste storage bin, an additive storage bin, a coal slurry storage bin and molding machine. The feeding storage bin, magnetic separator, primary crusher, primary high speed rotating machine, secondary crusher, secondary high speed rotating machine, environment protection hot-blast stove and waste storage bin are sequentially connected via transmission device.    USE - The production system is used in producing regenerative coal by using urban domestic waste and coal slurry (claimed). The regenerative coal is used in all areas of production and livelihood.    ADVANTAGE - The system can reduce the pollution to the environment; changes waste into valuable material; uses coal slurry of coal mine with the domestic waste due to the viscous nature of coal slurry, which has certain calorific value complementary to the waste particles, so that the product is easy to burn, and does not break easily; and is suitable for large scale industrialization.
NOVELTY - Metal surface corrosion resistant coating comprises strontium oxide, silicon oxide and titanium dioxide (SrO-SiO2-TiO2).    USE - Metal surface corrosion resistant coating.    ADVANTAGE - The coating does not contain toxic elements, can obviously improve the metal surface corrosion resistance and biological activity, does not undergo high temperature heat treatment so as to avoid the structure damage, and can be uniformly applied in complex shape and porous surface of basal body.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of metal surface corrosion resistant coating comprising adding water soluble salt of Sr in water under stirring at 5 ml/minute, gradually dropping SiO2 sol at 5 ml/minute, dropwise adding TiO2 sol, stirring for 1-4 hours, and aging for 6-12 hours at 20-25 degrees C to prepare SrO-SiO2-TiO2 sol-gel; cleaning metal, coating with prepared SrO-SiO2-TiO2 sol-gel at 60 mm/minute at 20-25 degrees C for 6-12 hours, drying at 50-150 degrees C for 0.5-4 hours, cooling to room temperature, and conducting hydrothermal treatment at 150-300 degrees C and 0.15-5 MPa for 5-3 hours, and drying at 40-80 degrees C for 0.5-4 hours.
NOVELTY - Use method of farm biogas sludge to prepare granular organic fertilizer, comprises introducing the sludge into a horizontal screw discharging sedimentation centrifuge via a sludge pump for centrifugal dehydration, conveying the resulting centrifugal liquid into a sewage treatment equipment, conveying the sludge cake into a vertical stirrer through shaft-free spiral conveyor, stirring, simultaneously adding pregelatinized starch solution, stirring, conveying into a roller extrusion granulator to obtain granular organic fertilizer wet material, drying by a rotary drum drier, and sieving.    USE - The farm biogas sludge is useful for preparing granular organic fertilizer (claimed).    ADVANTAGE - The method: recycles the nitrogen and phosphorus in the biogas slurry during fertilizer production, thus the sludge does not contain any harmful microorganisms and parasites; does not require anaerobic fermentation process; provides sludge having high nitrogen, phosphorus, organic substances and minerals; and doses not require addition of nitrogen, phosphorus and potassium chemical fertilizers and organic biomass; and is economical.
NOVELTY - Desulfurization water treatment tower comprises a tank body divided into desulfurizing agent containing desulfurization chamber and a water treatment chamber set with an air inlet and an air outlet. The tank wall of the desulfurization chamber is set with a feed port and a discharge port. The water treatment chamber is set below the desulfurization chamber. A drain valve is set at the top or lower part of the water treatment chamber wall. An inclined baffle plate which is net- or hash shaped is set between the desulfurization- and water treatment chamber and provided with a filter screen.    USE - The desulfurization water treatment tower is useful for desulfurizing biogas.    ADVANTAGE - The desulfurization water treatment tower unloads saturated desulfurization agent in a timely manner; does not causes loss of desulfurization agent; has convenient and faster discharging process; has convenient and automatic management and control of continuous feeding and discharging processes; has simple structure; carries out desulfurization in a simple manner; has long service life; carries out desulfurization, dehydration and purification of a variety of sulfur-containing gases.
NOVELTY - Centrifugal biogas dehydration device comprises tank body, an air inlet pipe set on the top of the tank body, an air outlet connecting pipe coaxially set inside the tank body and extends outside the tank body to form an air outlet pipe, and a water outlet set at bottom of tank body. The tank body is a vertically arranged cylindrical body. The diameter of the air outlet pipe and air inlet pipe are less than the radius of the tank. The axis of the air inlet pipe does not intersect with the axis of the tank body, where the distance between the two axes is greater than or equal to the radius of the air inlet pipe.    USE - Used as a centrifugal biogas dehydration device.    ADVANTAGE - The device carried out dehydration process in a simple manner; is economical; and achieves two-grade dehydration requirement.
NOVELTY - Fermenting Aspergillus niger to produce potassium gluconate, involves adding water into starch and starch raw material, adding high temperature resistant alpha -amylase, obtaining liquefied solution, then adding composite glucoamylase, saccharifying, filtrating to obtain glucose solution, fermenting the solution using A.niger P1205X21, feeding potassium hydroxide solution, neutralizing gluconic acid and purifying the potassium gluconate solution to obtain potassium gluconate finished product.    USE - The method is useful for fermenting A.niger for producing potassium gluconate.    ADVANTAGE - The potassium gluconate can be obtained easily and cost-effectively with good quality and less power consumption, avoids formation of waste gas and wastewater and generation of calcium gluconate mother liquor and calcium gluconate waste, and is environmentally-friendly.    DETAILED DESCRIPTION - Method for fermenting Aspergillus niger to produce potassium gluconate, involves adding water into starch and starch raw material, adding high temperature resistant alpha -amylase, obtaining liquefied solution, then adding composite glucoamylase to be saccharified, filtrating to obtain a glucose solution after the saccharification, using A.niger P1205X21 strain with high potassium ion concentration to ferment glucose liquid, feeding an ionic membrane potassium hydroxide solution in the fermenting process, neutralizing gluconic acid to obtain a potassium gluconate solution, and purifying the potassium gluconate solution to obtain a potassium gluconate finished product.
NOVELTY - The device has a container (1) and a vertical transport channel (2) connected to a lower part of an outlet channel (3). A rotor is located in a stirrer (4) and connected to a shaft (5) and a transmission part (6). The transport channel is arranged near a vertical wall of a tank. The stirrer is arranged on an outer side of the container and supported on an auxiliary part (7). An inlet channel (10) is provided on a funnel-shaped part.    USE - Device for mixing municipal sewage sludge and other organic substances in a digester.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a municipal sewage sludge and organic substances mixing device.    Container (1)    Vertical transport channel (2)    Outlet channel (3)    Stirrer (4)    Shaft (5)    Transmission part (6)    Auxiliary part (7)    Inlet channel (10)
NOVELTY - Use of fresh tobacco leaves is claimed, for producing bioorganic fertilizer. The fertilizer is produced by crushing fresh tobacco, mixing auxiliary materials with fresh tobacco leaves, adding biogas slurry and microbial inoculum, mixing uniformly, fermenting the mixture, performing magnetic separation to remove the impurities, drying and crushing the mixed material and packaging the product in plastic film bag.    USE - The fresh tobacco leaves are useful for producing bioorganic fertilizer.    ADVANTAGE - The organic fertilizer can be mass produced and is suitable for fresh tobacco leaves for long period of time.    DETAILED DESCRIPTION - Use of fresh tobacco leaves is claimed, for producing bioorganic fertilizer. The fertilizer is produced by crushing 10 fresh tobacco to block-shaped or strip-shaped using a crusher, mixing auxiliary materials with fresh tobacco leaves (100 parts weight), adding biogas slurry (20-60) and microbial inoculum (0.1-0.3), mixing and stirring uniformly, fermenting the mixture at 40-59 degrees C for 7-9 days (1-2 times), performing magnetic separation to remove the impurities in the mixed material, drying the mixed material until the water content is less than 30%, crushing the mixed material such that the granularity is 30-50 meshes, and packaging the product in plastic film bag.
NOVELTY - An environment-friendly pig fermenting bed comprises upper layer, middle layer and lower layer. The upper layer is 20-30 cm in thickness and prepared by mixing and fermenting 40-50 pts. wt. rice hull powders, 30-40 pts. wt. sawdust, 10-20 pts. wt silkworm excrement, 10-20 pts. wt. bran and 0.2-0.3 pts. wt. enzyme, and controlling water content to 40-45%. The lower layer is 20-30 cm in thickness and prepared by mixing and fermenting 30-40 pts. wt. wine groove, 40-50 pts. wt. loess, 20-30 pts. wt. bagasse and 10-20 pts. wt. corncob, and controlling water content to 30-40%.    USE - Environment-friendly pig fermenting bed (claimed).    ADVANTAGE - The method economically and environmentally-friendly provides pig fermenting bed.    DETAILED DESCRIPTION - An environment-friendly economical pig fermenting bed comprises upper layer, middle layer and lower layer. The upper layer is 20-30 cm in thickness and prepared by mixing and fermenting 40-50 pts. wt. rice hull powders, 30-40 pts. wt. sawdust, 10-20 pts. wt silkworm excrement, 10-20 pts. wt. bran and 0.2-0.3 pts. wt. enzyme, and controlling water content to 40-45%. The middle layer is 10-20 cm in thickness and prepared by mixing and fermenting 30-40 pts. wt. waste material discharged by fermenting bed, 20-30 pts. wt. coconut shell powder, 10-15 pts. wt. modified palygorskite powder, 10-20 pts. wt. plant straw powder and 10-20 pts. wt. cottonseed meals and enzyme, and controlling water content to 20-30%. The lower layer is 20-30 cm in thickness and prepared by mixing and fermenting 30-40 pts. wt. wine groove, 40-50 pts. wt. loess, 20-30 pts. wt. bagasse and 10-20 pts. wt. corncob, and controlling water content to 30-40%.
NOVELTY - Method of producing straw fermented organic fertilizer, involves obtaining crop straw, leaves, grass, sawdust, lees, furfural residue and organic waste, controlling the moisture content of the raw material to 70%, adding bacterial liquid, bean cake or urea, stirring uniformly, closely compressing with plastic cloth, processing at 50-70 degrees C for 24-48 hours, gradually reducing the temperature for two weeks and fermenting the raw material.    USE - The method is useful for producing straw fermented organic fertilizer used for protecting plant diseases and insect pest.    ADVANTAGE - The method is simple and convenient to perform, improves soil environment and pH, and promotes growth of crops.
NOVELTY - 4-(4-Fluoro-phenyl)-3,4,5,6,7,8,9,10-octahydro-1H-cycloocta(b)pyridin-2-one is dissolved in solvent, and substituted sulfonyl chloride and a catalyst are added. The reaction solution is poured into water and solids are filtered. The organic phase is extracted, washed and concentrated to obtain 4-(4-fluoro-phenyl)-3,4,5,6,7,8,9,10-octahydro-1H-cycloocta(b)pyridin-2-sulfonic acid ester. Ethyl piperazine and a catalyst are added to the obtained compound. The reaction solution is poured into cold water, extracted, filtered, and dried to obtain blonanserin.    USE - Synthesis of blonanserin (claimed).    ADVANTAGE - The method enables simple and convenient industrial synthesis of high-purity blonanserin with high selectivity and low toxicity, with easy process control.    DETAILED DESCRIPTION - 4-(4-Fluoro-phenyl)-3,4,5,6,7,8,9,10-octahydro-1H-cycloocta(b)pyridin-2-one (A) is dissolved in a reaction solvent. Substituted sulfonyl chloride or its organic solvent solution is added and stirred. A catalyst is added and the reaction is monitored by thin-layer chromatography to completion. The reaction solution is poured into water and solids are precipitated and filtered. The organic phase is extracted, washed and concentrated to obtain 4-(4-fluoro-phenyl)-3,4,5,6,7,8,9,10-octahydro-1H-cycloocta(b)pyridin-2-sulfonic acid ester (B), which is purified or used directly for the next reaction. The reaction solvent is ether, amine, amide, ester, ketone, halogenated hydrocarbon, nitrile, hydrocarbon, and/or heterocyclic compound. Ethyl piperazine is added to the obtained compound or its organic solvent solution. A catalyst is added and the reaction is monitored by thin-layer chromatography to completion. The reaction solution is poured into cold water, extracted, filtered, and dried to obtain blonanserin having a purity of 99.8%.
NOVELTY - A preparation method of beta -artemether using artemisinin as raw material in reaction kettle comprises adding ethyl alcohol and homogeneous reduction agent potassium borohydride, lithium borohydride or boron hydride.    USE - Method for preparing beta -artemether (claimed).    ADVANTAGE - The beta -artemether contains less 0.2% alpha -artemether, less than 0.1% dihydroartemisinin and less than 0.5% total impurity. The method is simple with low equipment requirement and convenient operation. It has high economical efficiency and low carbon emission.
NOVELTY - The hydrogen and oxygen generator comprises multiple square metal plates interleaved with multiple rubber sheets, where metal plates are positive electrode, negative electrode and neutral metal plates. The metallic plates and rubber sheets are aligned through holes in proximity and parallel to edges of outline, where ends of the metal plates are connected with positive and negative poles of a battery or power generating element. Water circulation holes and gas outlets are connected to a reservoir outlet of gas generator.    USE - Hydrogen and oxygen generator.    ADVANTAGE - The hydrogen and oxygen generator efficiently achieves separation of gases in respective separate reservoirs.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic side view of copper plate that participates in positive electrodes formation.    Copper sheet (1)    Bevel (4)    Holes (7,8,8')    Electrical connection (9)
NOVELTY - A methane gas catalytic combustion agent contains 2.6-3.6 kg liquid catalytic agent added to 100 kg natural gas.    USE - A methane gas catalytic combustion agent (claimed).    ADVANTAGE - Highly efficient catalytic combustion is performed, reaction speed and flame temperature is improved, gas burning speed is increased, ignition temperature is reduced, heat utilization rate of gas is improved, and safety is increased.
NOVELTY - A marguerite nutritional fertilizer comprises (wt.%) tea cake meal (2-4), pricklyash peel powder (6-8), bitter golden thread powder (1-3), medicinal Indian mulberry root powder (2-4), dried duck manure (6-8), dried chicken manure (7-9), dried human excrement (4-6), pumpkin stem and leaf meal (11-13), bean cake meal (9-11), corncob meal (14-16), broad been skin meal (10-12), wheat straw powder (5-7), calcium powder (1-3), validamycin (7-9), thiophanate-methyl (0.1-0.3), rotenone (0.2-0.4), chlorothalonil (0.1-0.3), and ningnanmycin (0.2-0.4).    USE - A marguerite nutritional fertilizer.    ADVANTAGE - The fertilizer is environment-friendly, and improves growth development of plants.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the marguerite nutritional fertilizer comprising mixing raw materials for 200 minutes, crushing, fermenting in a sealed environment for 50 hours, re-stacking, adding human excrement aqueous solution to the material at a ratio of 2:1.2, re-stacking, covering with thick plastic cloth, compacting, fermenting at more than 68 degrees C for 50 hours, re-stacking, adding human excrement aqueous solution to the material at a ratio of 2:1.2, re-stacking, covering with thick plastic cloth, compacting, fermenting for 50 hours, arranging fermented material at a height of 13 inches, width of 8 inches and length of 6 inches, forming into fertilizer blocks, compacting, and packing.
NOVELTY - Bonding agent comprises 50-80 parts by weight (pbw) of carbide slag, 5-10 pbw of fly ash and 10-45 pbw of powdery sludge, where the carbide slag is calcium carbide waste obtained by PVC production method.    USE - The bonding agent is useful for preparing fuel derived from oversize material of garbage (claimed).    ADVANTAGE - The bonding agent can be easily and economically prepared with high quality and strength and reduced energy consumption, increases the forming rate and the drop strength of a product of the fuel, eliminates stench and the production of percolating liquid during fuel production, and improves the storage performance of the garbage-derived fuel.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparing the bonding agent, comprising weighing carbide slag, fly ash and sludge and then mixing in a stirrer for 30 minutes; and    (2) use of bonding agent for preparing fuel derived from oversize material of garbage, where the step of preparing the fuel comprises grinding the oversize material of garbage to obtain garbage broken matter with a particle size of below 5 mm, adjusting the moisture content of the garbage broken matter to 25-30%, mixing the bonding agent with the broken matter according to a weight ratio of 10-100, stirring the mixture to completely mix to obtain a mixture, and extruding the mixture to obtain solid garbage derived fuel.
NOVELTY - A washed nickel substrate used as working electrode and nickel plate used as counter electrode, are electroplated using plating solution containing nickel sulfate, sodium hypophosphite, boric acid and ammonium chloride. The substrate is washed with deionized water to remove residual plating solution and naturally dried to obtain precursor electrode. Ruthenium chloride-n-butanol solution is prepared and coated on the nickel substrate, and dried to obtain nickel-based nickel-ruthenium oxide composite electrode.    USE - Manufacture of hydrogen evolution electrode used for electrocatalytic hydrogen evolution in chlorine-alkali industry, solar water electrolysis and water electrolysis industry.    ADVANTAGE - The hydrogen evolution electrode is manufactured economically.    DETAILED DESCRIPTION - A nickel substrate is mechanically polished to provide metallic luster, and ultrasonically washed with mixed aqueous solution of sodium sulfate (45 g/l), sodium carbonate (45 g/l) and sodium chloride (45 g/l), and absolute ethanol to remove oil. The washed substrate is washed with deionized water and naturally dried in air. The processed substrate is used as working electrode and nickel plate is used as counter electrode, and electroplated using plating solution containing nickel sulfate (20-60 g/l), sodium hypophosphite (20-60 g/l), boric acid (5-20 g/l) and ammonium chloride (2-10 g/l) and having pH of 4, at 20-60 degrees C with average current density of 20-40 mA/cm2. The substrate is washed with deionized water to remove residual plating solution and naturally dried to obtain nickel plated precursor electrode. Ruthenium chloride-n-butanol solution is prepared and coated on the nickel substrate. The coated substrate is dried at 400-500 degrees C for 10-60 minutes and cooled to room temperature to obtain nickel-based nickel-ruthenium oxide composite electrode.
NOVELTY - The aeration tank has anti-gel counter bore provided on bottom surface of aeration head of aeration tank main portion. One side of aeration tank main portion is provided with sewage inlet pipeline, and sewage inlet pipeline is connected to aeration tank main portion through water pump. The primary and secondary portions of water pump are respectively connected to anti-gel counter bore and water inlet. A sewage reflux pump is connected to anti-gel counter bore and filter cloth.    USE - Aeration tank used for sewage treatment of polyvinyl alcohol polymer immobilized microorganism gel.    ADVANTAGE - The sewage treatment efficiency and performance of the aeration tank having simple structure are improved.
NOVELTY - A cellulosic biomass simultaneously hydrolyzes other ingredients except cellulose and lignin to obtain hydrolysate, neutralized, desalted, processed, and filtered using membrane, to obtain monosaccharide solution and non-monosaccharide solution. The monosaccharide solution is fermented, distilled, and separated into ethanol by-product and arabinose solution. The arabinose solution is refined to obtain arabinose product. The non-monosaccharide solution is absorbed using resin. Plant polyphenol, plant flavonoid and oligosaccharide solution by-products are separated.    USE - Production of arabinose.    ADVANTAGE - The method efficiently produces arabinose with highly productive by-products by simple process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for application of cellulosic biomass.
NOVELTY - Phosphorus trichloride and ethanol are continuously mixed and subjected to esterification reaction to generate phosphite ester material liquid. The phosphite ester material liquid and inorganic base, are continuously saponified to generate ammonium phosphite material liquid. The ammonium phosphite material liquid and water-soluble aluminum salt are subjected to double decomposition to generate fosetyl-aluminum slurry. The fosetyl-aluminum slurry is precipitated, separated and dried, to obtain fosetyl aluminum original drug.    USE - Production of fosetyl aluminum original drug.    ADVANTAGE - The environmentally-friendly fosetyl aluminum original drug is economically and easily prepared with reduced side effects by a simple process.
NOVELTY - Heterogenous acid catalyst comprises zinc oxide supported on aluminosilicate zeolite in the weight ratio of 1:2-1:5.    USE - The heterogenous acid catalyst is useful for producing biodiesel from vegetable oils by transesterification of the vegetable oils with alcohol (claimed).    ADVANTAGE - The heterogenous acid catalyst: is very stable and environmental friendly; enables the transesterification to be carried out in a single step and improves the reaction rate within reduced time to increase the conversion efficiency and productivity; and provides simple and easy process for producing biodiesel from vegetable oil.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) preparation of the heterogenous catalyst, comprising coprecipitating zinc and aluminosilicate zeolite by reacting an aqueous solution of zinc nitrate with aluminosilicate zeolite in the molar ratio of 1:2-1:5 at 70-90 degrees C with pH adjustment of the reaction at 7-7.5 with sodium bicarbonate to precipitate zinc on alumina hydrate, filtering out the precipitate, drying the precipitate to 120-130 degrees C and calcining the precipitate at 400-500 degrees C; and    (2) producing biodiesel from vegetable oils in a single step transesterification of the vegetable oils, where the transesterification of the vegetable oil is carried out with an alcohol in the molar ratio of 1:10-1:41.1 at 200-220 degrees C and 35-42 bars pressure in the presence of the catalyst (1-5 wt.% of the vegetable oils).
NOVELTY - Deoxygenating a biomass-derived pyrolysis oil comprises: diluting the biomass-derived pyrolysis oil with a phenolic-containing diluent to form a diluted pyoil-phenolic feed; and contacting the diluted pyoil-phenolic feed with a deoxygenating catalyst in the presence of hydrogen at hydroprocessing conditions effective to form a low-oxygen biomass-derived pyrolysis oil effluent.    USE - The method is useful for deoxygenating a biomass-derived pyrolysis oil (claimed).    ADVANTAGE - The method effectively produces a low-oxygen biomass-derived pyrolysis oil without plugging of the catalyst, thus increasing run duration and improving processibility of the biomass-derived pyrolysis oil.
NOVELTY - Method of removing contaminants from algal oil involves combining sulfuric acid-aqueous solution (18) which has pH of 1 or less with contaminant-containing algal oil (12) at treatment conditions and forming effluent (20) which comprises a treated algal oil phase and contaminants in an acidic aqueous phase and removing acidic aqueous phase from the effluent (20) to form contaminant-depleted algal oil (24). The contaminants comprise metals and/or phosphorus.    USE - Method of removing contaminants from algal oil used for producing biofuels e.g. bio-diesel and bio-jet.    ADVANTAGE - The method efficiently and economically removes contaminants from algal oil.
NOVELTY - The system (1) has a combustor unit (2) for receiving a flow of synthesis gas (syngas) (8) produced by a pyrolysis unit and producing combustion gas (12) from the syngas. A gas dilution chamber (4) is positioned between the combustor unit and a heat exchanger (5) i.e. low pressure heat exchanger, to reduce a temperature of the combustion gas. A residence chamber (3) is positioned between the combustor unit and the gas dilution chamber, where the residence chamber has an inlet (7) and an outlet for the combustion gas.    USE - Energy recovery system for recovering energy from syngas produced by a pyrolysis unit of a waste pyrolyser, a feedstock hopper, a conveyor, a char removal system, and a waste plant in a thermal processing system i.e. waste pyrolysis system (all claimed). Can also be used for a pyrolysis or gasification system.    ADVANTAGE - The system is simp1e, reliable, inexpensive and efficient for small scale purpose. The system avoids the need for gas clean-up, such that the system is financially viable, small scale, de-centralized and pyrolysis-based.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for recovering energy from syngas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an energy recovery system.    Energy recovery system (1)    Combustor unit (2)    Residence chamber (3)    Gas dilution chamber (4)    Heat exchanger (5)    Inlet (7)    Syngas (8)    Combustion gas (12)
NOVELTY - Processing pyrolysis fuel comprises converting biomass to pyrolysis fuel including pyrolysis oil and char particles and resizing a portion of the char particles, where the resized char particles have a largest dimension of less than 5 microns.    USE - The method is useful for processing pyrolysis fuel, which is useful for combustion in a diesel engine (all claimed) such as stationary diesel engines.    ADVANTAGE - The method enables efficient and rapid processing of pyrolysis fuel without the loss of pyrolysis oil thus preventing the damage to the diesel engine during combustion, and increases the yield of the fuel delivered to the engine for a given quantity of biomass by enhancing the heating value of the pyrolysis fuel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for pyrolysis fuel for combustion in a diesel engine comprising the pyrolysis oil and the resized char particles formed from rapid pyrolysis of biomass.
NOVELTY - Forming a low-metal biomass-derived pyrolysis oil, comprises: (a) washing biomass (8) comprising a water-soluble metal component with wash water (44) that is free of water-soluble metals; (b) separating washed biomass (25) and water containing water-soluble metal after washing the biomass; (c) pyrolyzing the washed biomass in a pyrolysis process to form a pyrolysis vapor stream; and (d) condensing a portion of the pyrolysis vapor stream to form a condensate, where the wash water is derived from the washed biomass.    USE - The method is useful for forming a low-metal biomass-derived pyrolysis oil.    ADVANTAGE - The method: utilizes the wash water, which can be effectively recycled and conserved; provides the pyrolysis oil with high yield; and reduces the need for drying the biomass prior to pyrolysis, hence minimizes the energy requirements, as compared to conventional methods.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an apparatus (10) for forming a low-metal biomass-derived pyrolysis oil, comprising: a washing stage for mixing the biomass with the wash water; a biomass dryer (27) for separating the washed biomass and water containing water-soluble metal after washing the biomass; a pyrolysis reactor for pyrolyzing the biomass in the relative absence of molecular oxygen to form a pyrolysis vapor stream; a quenching system comprising a primary condenser and a secondary condenser for condensing a portion of the pyrolysis vapor stream to form a condensate; and a return line connecting the quenching system to the washing stage for providing water derived from the condensate as the wash water.    DESCRIPTION OF DRAWING(S) - The figure shows a block diagram of an apparatus for forming a low-metal biomass-derived pyrolysis oil.    Biomass (8)    Apparatus (10)    Washed biomass (25)    Biomass dryer (27)    Wash water (44)
NOVELTY - The device has a water jacket furnace provided with a smoke circulating spiral steel pipe. A combustion area is provided with a circulating spiral steel pipe at the bottom of a hearth that is arranged with a purifier at the back of the furnace. A smoke inlet of a smoke circulation spiral steel pipe is arranged on the upper part of the hearth. A spiral steel pipe is extended into the lower part of the purifier. A water jacket is connected with a water circulating spiral steel pipe and a furnace cover.    USE - Biomass gasification furnace device.    ADVANTAGE - The device can remove the oil smoke and provide moisture-proof effect for removing harmful substance, thus protecting the environment efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a biomass gasification furnace device.
NOVELTY - Producing butanol and isopropanol, comprises: (a) fermenting a feedstock with Clostridium under conditions amenable to produce butanol; (b) mixing a nontoxic oil with the fermentation mixture to produce an oil-water foam on the surface of the mixture, where the butanol preferentially partitions into the foam; (c) separating at least part of the foam from the fermentation mixture; (d) resolving the foam into an oil phase, an alcohol phase and an aqueous phase; (e) separating the alcohol phase and extracting butanol from the alcohol phase.    USE - The method is useful for producing butanol and isopropanol (claimed), which are useful as flexible fuels and as building blocks to make jet fuel.    ADVANTAGE - The method: utilizes the Clostridium beijerinckii, which is stable in the environment, and produces butanol and isopropanol with only small amounts of ethanol and low or even undetectable amounts of acetone; decreases product recovery costs and complexity; continuously produces the butanol; provides increased production of the butanol and isopropanol; utilizes low cost distillation process; and economically recycles the resultant water.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a Clostridium bacterium of strain Clostridium beijerinckii optinoii, where a representative sample of Clostridium beijerinckii optinoii has been deposited under American type culture collection accession number PTA-11285.
NOVELTY - Converting organic waste material into a cell culture broth or growth media comprises: mixing (102) an organic waste material with one or more solvent under turbulent conditions to create a mixture of liquids and solids; separating (103) the mixture of liquids and solids into a liquid stream and solid stream; and sterilizing (106) the liquid stream, where the cell culture broth or growth media comprises the sterilized liquid stream.    USE - The method is useful for converting organic waste material into a cell culture broth or growth media, which is useful for propagation, culture, fermentation, or maintenance of bacteria, algae, yeast, synthetically derived microorganisms, insect cells, plant cells or mammalian cells, where the organic waste material is plant waste (preferred), bedding, litter, human organic waste, and/or livestock manure (all claimed).    ADVANTAGE - The method allows economic conversion of organic waste material into the cell culture broth or growth media with less energy consumption in an eco-friendly manner thus achieving optimal growth conditions of bacteria, algae, yeast, synthetically derived microorganisms, insect cells, plant cells or mammalian cells.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a cell culture broth or growth media produced by the method; and    (2) a kit comprising the cell culture broth or growth media.    DESCRIPTION OF DRAWING(S) - The figure shows a flowchart of a method for converting organic waste material into a cell culture broth or growth media.    Mixing organic waste material and water (102)    Separating solid and liquid (103)    Chemical analysis of solid byproduct (104)    Chemical analysis of liquid stream (105)    Sterilizing the liquid stream. (106)
NOVELTY - The system has fuel-generating material which generates fuel by chemical reaction. The fuel is regenerated by reverse reaction of chemical reaction. The gas is circulated in the fuel cell with respect to fuel-generating material. The specific fuel cell generates power using fuel gas introduced from external gas supply source (12). The amount of heat generated in second fuel cell performing power generation operation is transmitted to first fuel cell performing an electrolysis operation.    USE - Fuel cell system.    ADVANTAGE - The fuel cell system can be charged efficiently, even when the surplus electric power is generated during production of electric power by transducing fuel gas from exterior.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fuel cell system.(Drawing includes non-English language text)    Combustor (4)    Heat exchanger (10)    Controller (11)    Gas supply source (12)    Water heater (13)
NOVELTY - A fuel generator has fine particles of fuel-generating agent (1) which generates fuel by oxidation reaction with oxidizing gas and can be regenerated by reduction reaction with reducing gas, and a porous component (3). The fine particles of the fuel-generating agent are dispersed and disposed in the interior of the porous component.    USE - Fuel generator is used for secondary battery-type fuel cell system (claimed).    ADVANTAGE - Since aggregation of fine particles of fuel generating agent is prevented, the performance degradation of fuel generator can be suppressed.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) secondary battery-type fuel cell system; and    (2) manufacture of fuel generator.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of secondary battery-type fuel cell system.    Fuel generating agent (1)    Electrolytic membrane (2A)    Fuel electrode (2B)    Oxidizing agent electrode (2C)    Porous component (3)
NOVELTY - The fuel cell system has buffer tank that stores hydrogen gas. The molten carbonate fuel cell (11) generates electricity using hydrogen gas stored in buffer tank. The control unit controls the output of the currently driven power plant using the fuel of the exhaust gas. The drain line (15) ejects the condensed water.    USE - Polymer electrolyte fuel cell system.    ADVANTAGE - Stable electricity is produced by the fuel cell, the load ability is improved and the fuel utilization and energy efficiency can be enhanced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the fuel cell system. (Drawing includes non-English language text)    Molten carbonate fuel cell (11)    Exhaust heat recovery system (12)    Water gas shift reactor (13)    Drain line (15)    Buffer tank (16)
NOVELTY - A recombinant microorganism for producing 3-hydroxypropionaldehyde (3-HPA) and/or 3-hydroxypropionic acid (3-HP) comprising polynucleotide encoding Roseburia inulinivorans derived glycerol dehydratase, is new.    USE - The recombinant microorganism is useful for producing 3-HPA and/or 3-HP (claimed) which is used in biodiesel and chemical industry.    ADVANTAGE - The microorganism cost-effectively provides high yield of 3-HPA and 3-HP.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing 3-HPA and/or 3-HP, which involves culturing the recombinant microorganism in the culture medium containing glycerol and glucose as carbon source.
NOVELTY - Blend polymeric membrane comprises a poly(ethylene glycol) (PEG) containing polymer and a highly permeable polymer comprising polymers of intrinsic microporosity and/or their tetrazole-functionalized polymers.    USE - The membrane is useful: as thin film composite membrane, a sheet, tube, or hollow fibers for separating gases or liquids from natural gas, where the gases comprise (a) at least one of carbon dioxide, oxygen, nitrogen, water vapor, hydrogen sulfide, volatile organic compounds (toluene, xylene or acetone) and helium, (b) a mixture of carbon dioxide and at least one gas of hydrogen, flue gas or natural gas, (c) mixture of olefins and paraffins or iso and normal paraffins or (d) mixture of gases comprising nitrogen and oxygen, carbon dioxide and methane, hydrogen and methane or carbon monoxide, or helium and methane (all claimed); and in purification and adsorption of a particular species in the liquid or gas phase, and petrochemical, refinery, and natural gas industries.    ADVANTAGE - The membrane exhibits high permeance and high selectivity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for separating at least two gases or two liquids comprising contacting the gases or liquids with the membrane.
NOVELTY - Processing a lignocellulosic biomass material, comprises: pretreating a biomass material in the presence of a tertiary polyamide additive, where the biomass material comprises one or more cellulosic components; and subjecting the pretreated biomass material to enzymatic hydrolysis of the one or more cellulosic components to produce a sugar.    USE - The process is useful for processing lignocellulosic biomass material for the preparation fermentable sugar, preferably alcohol, which is useful in/as a biofuel such as biogasoline.    ADVANTAGE - The efficient process provides fermentable sugars using less amount of reagent e.g. enzyme catalyst in a cost effective and less time consuming manner.
NOVELTY - Solid-liquid treatment of a liquid starting substrate, preferably slurry, fermentation residues or sewage sludge, comprises providing at least one filter aid from pulped, cellulosic material, adding the filter aid of the starting substrate depending on the total dry weight of the starting substrate in a predetermined dry matter ratio, pre-compressing the starting substrate with the filter aid to a pourable material, where at least one liquid phase is separated, and the bulk goods are further pressed in the downstream.    USE - The method is useful for solid-liquid treatment of a liquid starting substrate, preferably slurry, fermentation residues or sewage sludge.    ADVANTAGE - The method: produces solid material in increased yield; achieves the filter cake formation in simple manner; and allows repeated pressing, thus it achieves good separation of solid material.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for solid-liquid treatment of the liquid starting substrate, comprising a cylindrical housing (1) in which a worm shaft (2) is mounted, which forms liquid sealed mantel inner wall in the housing, where the housing has a substrate inlet (3) at a first end region and a substrate outlet (4) at a second end region. A substrate conveyance direction is predetermined from substrate inlet to the substrate outlet by the worm shaft. The housing has at least one mantel inner wall formed as a filter surface (7). The filter surface has greater passage diameters towards substrate outlet, and a press-screw separator is at least downstream to the substrate outlet.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic longitudinal sectional view of the device.    Housing (1)    Worm shaft (2)    Substrate inlet (3)    Substrate outlet (4)    Filter surface (7)
NOVELTY - The method involves producing electricity using graphite membrane along with hydrogen, water or solid fuel based on the fuel cells. The continuous production of hydrogen gas is fed into fuel cell chamber, and is produced from carbon monoxide fuel cell power generation. The unburnt fossil fuel remnants are collected, when the combustion is performed through appropriate mechanism. The mixture of carbon monoxide, carbon dioxide and hydrogen gas is liberated so as to produce power.    USE - Method for effective utilization of exhausts of fossil fuel.    ADVANTAGE - The release of greenhouse gases can be reduced. The fuel efficiency of the combustion engine of fuel combustion system can be improved. The burning of fuel can be reused efficiently to achieve maximum level of energy conversion. The mileage of the system can be enhanced. The cost required for generating power can be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a construction method for designing of a special membrane.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fuel combustion system.
NOVELTY - Preparing and processing waste potato in order to produce a new material which is useful for cooking or heating requirements in the home or in small business environments involves mixed a waste potato with sawdust or wood shavings in proportions of approximately 30% sawdust/wood shavings to 70% waste potatoes.    USE - For preparing and processing waste potato in order to produce a new material which is useful for cooking or heating requirements in the home or in small business environments (claimed).    ADVANTAGE - The process reduces the cutting of trees in rural areas. The burning process with this new material produces less smoke than timber with similar moist content. The end product of the process can be stored for long periods of time in dry areas. The preparation process does not require highly technologic equipment, so reducing production costs. Transporting this material is also more cost-efficient reducing the total transport cost up to 40%.
NOVELTY - The method involves sending the feed gas (1,95) or a hydrogen enriched gas (7) to a liquid nitrogen wash column (11). A mixture of nitrogen and hydrogen constituting an ammonia synthesis gas (99) is removed from the liquid nitrogen wash column. The liquid (15) from a bottom of the liquid nitrogen wash column is sent to a top of a stripping column (23). A methane rich liquid (29) is removed from the bottom of the stripping column, as a final product.    USE - Method for co-producing liquid methane and ammonia synthesis gas from feed gas.    ADVANTAGE - The liquid methane and ammonia synthesis gas can be co-produced from the feed gas in efficient manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an apparatus for co-producing liquid methane and ammonia synthesis gas from feed gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the cold box with heat exchangers, columns and closed cooling circuit.    Feed gas (1,95)    Hydrogen enriched gas (7)    Liquid nitrogen wash column (11)    Liquid from bottom of liquid nitrogen wash column (15)    Stripping column (23)    Methane rich liquid (29)    Ammonia synthesis gas (99)
NOVELTY - The device has a bio reactor which is made of flexible plastic film as separator barrier between sea water and media. Sea surface are coupled to an inlet channel open and closed type made of flexible plastic film. A bio gas digestor is made of flexible plastic film as separator between sea water and organic waste matter to be digested to generate methane used as fuel. A floating platform is provided with engine, pumps, sterilization unit, crane, centrifuge and microprocessor.    USE - Device for enabling large scale cell culture to produce enzymes, bio polymers and crop protection chemicals and pharmaceuticals on sea.    ADVANTAGE - The bio gas digestor is made of flexible plastic film as separator between sea water and organic waste matter to be digested to generate methane used as fuel, and the floating platform is provided with engine, pumps, sterilization unit, crane, centrifuge and microprocessor. Thus, the large scale cell culture can be enabled in cost effective manner to produce enzymes, bio polymers and crop protection chemicals and pharmaceuticals on sea.    DESCRIPTION OF DRAWING(S) - The drawing shows a top view of the oil confining and collecting channel with isolator connector.    Sewage (102)    Multi-chambered wall (104)    Plastic sheet (106)
NOVELTY - Process of refining oil while retaining essential ingredients like tocopherol, sterol, phospholipids, and oil soluble vitamins or refining waste (or spent) and acid oil for removal of free fatty acids, comprises removing free fatty acids from oil by treating with macroporous or macro-reticular weak base anion exchange resin at oil/resin ratio of 10 for 5 hours and simultaneously monitoring free fatty acids content of oil which is to be below 0.5 mg potassium hydroxide/g of sample that is to obtain oil substantially lower in free fatty acids (less than 0.25% free fatty acids (FFA)) content.    USE - The process is useful for refining oil, where the refined oil is used for bio-diesel production and not for edible purpose (claimed).    ADVANTAGE - The process: provides refining oil (containing 0.2-90% free fatty acids, while retaining essential ingredients) without the necessity of organic solvents thus simple, easy, efficient and eco-friendly; and recovers isopropyl alcohol and sodium soap of fatty acids that is used in laundries.
NOVELTY - Renewable gas oil derived at least in part from biomass comprises 0-5 wt.% n-paraffins, 0-5 wt.% iso-paraffins, 5-50 wt.% naphthenes, 0-20 wt.% 1-ring naphthenes, 0-30 wt.% 2-ring naphthenes, 5-30 wt.% 3-ring naphthenes, and 30-85 wt.% aromatics.    USE - The renewable gas oil is useful in jet and diesel fuels.    ADVANTAGE - The renewable gas oil: exhibits cold flow properties; is prepared at higher yields in simple and cost-effective manner by using minimum number of reactors; has very high energy density and found in large deposits so transportation to a refinery is far less complicated and costly as compared to handling and transporting raw biomass and, transportation of feedstocks by large pipelines is economical to conventional refineries that cannot be matched by currently envisioned commercial scale biomass refineries.
NOVELTY - Preparing ketose sugar comprises: (a) solubilizing at least one aldose sugar or its aqueous solution or suspension, in an organic solvent; (b) contacting the organic solution with a catalyst to convert the aldose into ketose by isomerization reaction; (c) optionally, drying the obtained sugar solution; and (d) optionally removing the isomerization catalyst by filtration.    USE - The method is useful for preparing ketose sugar. The organic sugar solution is useful for preparing 5-hydroxymethylfurfural (all claimed), which is useful as a raw material to form 2,5-dimethylfuran as a liquid biofuel, and 2,5-furandicarboxylic acid for producing polyesters.    ADVANTAGE - The method produces 5-hydroxymethylfurfural in high yield without using toxic metal catalyst, and in an economical manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing 5-hydroxymethylfurfural, comprising the step (a) as above per se, contacting the organic solution with at least one heterogeneous catalyst or a basic catalyst to convert the aldose into ketose by an isomerization reaction, which is carried out at an atmospheric pressure, at a temperature of 40-70 degrees C for 4-20 hours, drying the obtained sugar mixture at a temperature of less than 70 degrees C under reduced pressure, then removing the catalyst by filtration, optionally adding a solvent or solvent mixture to obtain an organic sugar solution comprising 5-15 wt.%, then adding an acid catalyst such as sulfuric acid or hydrochloric acid to the obtained sugar solution to obtain a pH of 1-2.5, and placing the acidic sugar solution at a temperature of 50-170 degrees C, optionally under reduced pressure to obtain an organic solution of 5-hydroxymethylfurfural, where the basic catalyst comprises calcium hydroxide, sodium hydroxide, potassium hydroxide, magnesium hydroxide or calcium oxide.
NOVELTY - Balanced unleaded fuel composition comprises: 2-12 vol.% of a mixture of isoparaffins having 4C; 51-73 vol.% of alkylate having an initial boiling point of 34.4-93.9 degrees C and a final boiling point of 109-223 degrees C, where the alkylate comprises isoparaffins having 4-13C and 60 vol.% or more of the isoparaffins having 7-8C; 5-15 vol.% of one or more alkanol having 2-4C; and 7-30 vol.% of an aryl component comprising a quantity of one or more alkylated benzene having 7-12C and an amount of a 9C aryl component having a boiling point of 161.7-178 degrees C.    USE - The fuel composition is useful in automotive engines, high performance engines and racing engines.    ADVANTAGE - The fuel composition has higher average torque outputs and/or higher average power outputs, and improves the vehicle acceleration.    DETAILED DESCRIPTION - Balanced unleaded fuel composition comprises: 2-12 vol.% of a mixture of isoparaffins having 4C; 51-73 vol.% of alkylate having an initial boiling point of 34.4-93.9 degrees C and a final boiling point of 109-223 degrees C, where the alkylate comprises isoparaffins having 4-13C and 60 vol.% or more of the isoparaffins having 7-8C; 5-15 vol.% of one or more alkanol having 2-4C; and 7-30 vol.% of an aryl component comprising a quantity of one or more alkylated benzene having 7-12C and an amount of a 9C aryl component having a boiling point of 161.7-178 degrees C, where the 9C aryl component comprises aryl compounds having 8-11C, 50 vol.% or more of the aryl compounds having 9C, and the fuel composition exhibits a pump octane rating of greater than 100, a T50 (maximum) of 104.4 degrees C, and a T90 (maximum) of 165.6 degrees C.
NOVELTY - The system has an inexpensive hydrogen (HHO) gas generator (A) for generating HHO gas by electrolysis of water. A control unit controls injection rate of HHO gas in a suitable quantity according to load condition of alternating current (AC) dynamo (4) with operating condition of an internal combustion engine (1). A complementation unit controls the operation of control unit and HHO gas generator, such that the HHO gas is simultaneously injected into an intake pipe (6) between an air cleaner (2) and a throttle valve (5).    USE - System for improving fuel-consumption in internal combustion engine such as petrol engine and diesel engine mounted in vehicles such as motor vehicle and two-wheeled motor vehicle.    ADVANTAGE - The reduction in fuel consumption by required and sufficient quantity can be achieved, and the generated amount of insufflations is matched according to operation mode, without gas production amount and electrolysis efficiency falling.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the fuel-consumption improvement system.    Internal combustion engine (1)    Air cleaner (2)    AC dynamo (4)    Throttle valve (5)    Intake pipe (6)    HHO gas generator (A)
NOVELTY - Producing ethanol comprises: hydrogenating acetic acid in a first reaction zone in the presence of a catalyst to form a mixture of ethanol and acetic acid; directing the mixture to a second reaction zone to produce an ester feed stream; and reacting at least a portion of the ester feed stream with hydrogen in a third reaction zone to produce ethanol.    USE - The method is useful for producing ethanol (claimed), which is used in fuels, solvents (for toiletry and cosmetic preparations, detergents, disinfectants, coatings, inks and pharmaceuticals), chemical feedstocks, pharmaceutical products, cleansers, sanitizers, hydrogenolysis transport or consumption.    ADVANTAGE - The method: reduces the need for additional acetic acid and/or ethanol; reduces the recycle of ethanol in the hydrogenolysis process; and improves ethanol productivity.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of ethanol production process that directly feeds an organic phase of the esterification product produced by vapor esterification to the hydrogenolysis zone.    Vapor phase reactor (103)    Distillation column (104)    Acetic acid feed (105)    Vaporizer (107)    Vapor sidestream (111)
NOVELTY - An oxygenate additive for an internal combustion engine fuel, comprises: glycerol dimethyl ethers (GDMEs) (0-25 wt.%) and glycerol trimethyl ether (GTME) (75-100 wt.%).    USE - For internal combustion engine fuel selected from diesel fuel, gasoline and aviation turbine fuel, where the diesel fuel is petro-diesel fuel or biodiesel fuel; and as a green solvent or as an antifreezer (claimed).    ADVANTAGE - The process provides high yield of highly methylated glycerol ethers using reduced quantity of dimethyl sulfate; and improves replacement of the glycerol with a mixture obtained by reacting glycerol with methanol in the presence of an acid catalyst at 50-300 degrees C.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a fuel composition comprises the oxygenate additive and an internal combustion engine fuel, where the amount of glycerol dimethyl ether (GDMEs) in the fuel composition does not exceed 25 wt.% based on the total weight of the fuel composition; and    (2) a process of methylation of glycerol with dimethyl sulfate, involving: (a) mixing glycerol with an aqueous solution of alkali hydroxide to form a solution of glycerate; (c) mixing the solution of glycerate with dimethyl sulfate in a reactor to form highly methylated glycerol ethers; and (c) separating the highly methylated glycerol ethers from the resulting solution, where the steps (a) to (c) are conducted at 25-200 degrees C, where the improvement comprises: replacing the glycerol of step (a) with a mixture obtained by reacting glycerol with methanol in the presence of an acid catalyst at 50-300 degrees C.
NOVELTY - A liquid urease inhibitor formulation comprises: (a) a urease inhibitor selected from N-substituted thiophosphoric triamides and N-substituted phosphoric triamides of formula NH2-P((=X)(NH-R1-Y'))-NH2; and (b) a primary solvent selected from dialkyl sulfones of formula R2-S((=O)2)-R3 (II), and polymethylene cyclic sulfones (III), where the urease inhibitor is soluble in the primary solvent.    USE - As liquid urease inhibitor formulation used in urea-based fertilizers and waste containing urea compounds; and for the inhibition of urease hydrolysis of urea in moist soil (claimed).    ADVANTAGE - The formulation enhance the efficiency of urea-based fertilizers by delaying urea hydrolysis in soils and reducing liberation of ammonia into the atmosphere. The formulation give superior performance with unexpected results not previously obtained with other solvent systems.    DETAILED DESCRIPTION - A liquid urease inhibitor formulation for application to urea-based fertilizers and waste containing urea compounds comprises: (a) a urease inhibitor selected from N-substituted thiophosphoric triamides and N-substituted phosphoric triamides of formula NH2-P((=X)(NH-R1-Y'))-NH2; and (b) a primary solvent selected from dialkyl sulfones of formula R2-S((=O)2)-R3 (II), and polymethylene cyclic sulfones of formula (III), where the urease inhibitor is soluble in the primary solvent.    X=O or S;    R=3-6C alkyl, 5-8C cycloalkyl, phenyl (optionally substituted with nitro, amino, alkyl, or halide);    Y'=H, NO2, halide, NH2 or 1-8C alkyl;    R2=1-6C alkyl;    R3=1-6C alkyl;    n=3-6.    An INDEPENDENT CLAIM is included for inhibiting the urease hydrolysis of urea-containing fertilizer or waste, involving applying a liquid urease inhibitor formulation to the urea-containing fertilizer or waste.
NOVELTY - The system has a biomass raw material preprocessing system provided with a generator, a crusher and a conveyor. A marsh gas fermentation system is provided with an anaerobic digester and a stirrer. A waste heat utilizing system is provided with a solar energy heat collector, a gas turbine, a heat exchanger and a silencer. A fuel spraying automatic control system is provided with a purifying device, a stop valve, a pressure tank, an adjusting valve and a fire arrestor. The arrestor is connected with a combustion chamber, a temperature indicating control instrument and the collector.    USE - Multi-functional coupling renewable energy system.
NOVELTY - Integrated gas generation and gas storage combined biogas fermentation device comprises a fermentation tank, a gas storage bag and a binding belt. An upper opening on the upper part of the fermentation tank is provided with a flange disc. The bottom of the gas storage bag can be sleeved on the circular opening of the flange disc. The side upper part of the bag is provided with a biogas outlet hole.    USE - Used as an integrated gas generation and gas storage combined biogas fermentation device.    ADVANTAGE - The device: has good leak tightness; is leakage proof, safe to use and economical; has simple structure and convenient installation; saves the installation time of the biogas storage device; reduces the production cost; enables transportation of larger volume of products with low cost; and has good economic and social benefit.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the integrated gas generation and gas storage combined biogas fermentation device.
NOVELTY - The method involves placing food waste (T) into fermentation room. The zymogen is mixed into food waste. The food waste is stirred. The air (A) supplied from air hole (4b) of air supply apparatus (4) to fermentation room. The temperature of air supplied to fermentation room is increased. The fermentation is accelerated. The power source of heater is cut off. The air of room temperature is supplied into fermentation room. A ventilating passage (8) is washed. The temperature of exhaust gas (G1) is controlled through driving of circulating water pump (11).    USE - Fermentation processing method of organic waste such as food waste in home and restaurant.    ADVANTAGE - The pathogenic bacteria of the food waste is effectively processed by spraying the circulating water. The generation bad smell can be avoided.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a fermentation treating apparatus of organic waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fermentation treating apparatus.    Air supply apparatus (4)    Air hole (4b)    Ventilating passage (8)    Circulating water pump (11)    Air (A)    Exhaust gas (G1)    Food waste (T)
NOVELTY - Thermus thermophilus UTM802 (I) under a preservation number of CGMCC No. 6186, is new.    USE - (I) is useful for composting organic solid waste (claimed), which is useful as fertilizer.    ADVANTAGE - (I) provides the fertilizer with high stability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) high temperature resistant fungicide comprising (I);    (2) preparing the fungicide comprising (a) fermenting and activating (I) to obtain fermentation seed liquid, and fermenting and culturing the seed liquid to obtain fermented bacterial liquid and (b) uniformly mixing the bacterial liquid and the rotten compost, and then drying, crushing and sieving; and    (3) use of (I) or high temperature fungicide for composting organic solid waste.
NOVELTY - Trimetazidine is produced using 2,3,4-trimethoxybenzaldehyde and piperazine as raw material and formic acid as catalyst.    USE - Preparation of trimetazidine (claimed).    ADVANTAGE - The trimetazidine having yield of 83-92% is prepared economically without using lithium aluminum hydride and sodium borohydride, and palladium as catalyst, and is safe.
NOVELTY - Glycocyamine and water are stirred uniformly, nitric acid is dripping, and temperature is controlled to 20-60 degrees C. Dripping is completed in 10 minutes, and heat is preserved for 20 minutes, while stirring, and the reaction solution is cooled. The obtained glycocyamine nitrate white solid is separated out, filtered, and dried. The filtered liquid is recycled as mother liquor.    USE - Preparation of glycocyamine nitrate (claimed).    ADVANTAGE - The method enables economical, environmentally-friendly, simple and quick large-scale industrial preparation of high-quality glycocyamine nitrate with a purity of more than 99%, by using food-grade glycocyamine and chemical-grade nitric acid, with high productivity, a yield of more than 98%, and no by-products. Recrystallization is not required.
NOVELTY - A fertilizer comprises urea, monoammonium phosphate, potash fertilizer, ammonium chloride, borax, zinc sulfate, and filler. The filler is municipal domestic sludge containing not less than 4% nitrogen, phosphorus, and potassium; and not less than 20% organic matter.    USE - A fertilizer used for multi-element long sugarcane (claimed).    ADVANTAGE - The fertilizer has high nutrient content, and adequately supplements sugar cane nutrient required for stem elongation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing a fertilizer, comprising:    (A) fermenting municipal domestic sludge, and sterilizing;    (B) adding ammonium dihydrogen phosphate, potash fertilizer, ammonium chloride, borax, adding zinc sulfate; and    (C) uniformly mixing, crushing, granulating, drying, sieving, and packaging.
NOVELTY - A biological grease hydrogenating method involves selecting biological oil and fat as raw oil. The raw oil is passed with hydrogen into two hydrogenation reactors. The hydrogenation catalyst is loaded in the low temperature-hydrogenation reactors to obtain effluent-I. The effluent is introduced into a high temperature-hydrogenation reactor to obtain effluent-II. The effluent-II is separated under vulcanized state into gas phase and liquid phase. The liquid phase is entered into a fractionating tower to obtain naphtha and diesel oil.    USE - Method for hydrogenating biological grease for producing clean fuel.    ADVANTAGE - The method enables hydrogenating biological grease with stable flow of the biological oil and fat.    DETAILED DESCRIPTION - A biological grease hydrogenating method involves selecting biological oil and fat as raw oil. The raw oil is passed with hydrogen into two hydrogenation reactors. The hydrogenation catalyst is loaded in the low temperature-hydrogenation reactors to obtain effluent-I. The effluent is introduced into a high temperature-hydrogenation reactor to obtain effluent-II. The effluent-II is separated under vulcanized state to obtain gas phase and liquid phase. The liquid phase is entered into a fractionating tower to obtain naphtha and diesel oil followed by supplementing sulfur-containing substances in the reaction materials to maintain the content of hydrogen sulfide in recycle gas, where the low temperature-hydrogenation reactor is operated by employing an upward flowing operation mode of co-current flow gas and liquid flowing upward, and the hydrogenation catalyst comprises an active component selected from tungsten, molybdenum, nickel and cobalt.    DESCRIPTION OF DRAWING(S) - The drawing shows a hydraulic circuit diagram illustrating a method for hydrogenating biological grease.
NOVELTY - Fermentation of organic fertilizer comprises taking medicine slag dry product and crude fiber degrading bacteria, dissolving into aqueous solution, crushing and adjusting water content; prefermenting and processing by adding nitrogen-containing raw material and carrying out aerobic fermentation; adding plant fiber and zeolite powder and mixing uniformly; aerobic fermenting, decomposing organic matter and keeping temperature; adding microbial active strain, crushing, drying and granulating.    USE - Fermentation of organic fertilizer (claimed).    DETAILED DESCRIPTION - Fermentation of organic fertilizer comprises taking medicine slag dry product and 0.1-0.12 wt.% crude fiber degrading bacteria, dissolving into aqueous solution, crushing and adjusting water content to 55-65 wt.%; prefermenting and processing by adding nitrogen-containing raw material and carrying out aerobic fermentation at 55-66 degrees C for 5-8 days; adding plant fiber and zeolite powder and mixing uniformly; aerobic fermenting at 50-60 degrees C for 10-15 days, decomposing organic matter and keeping temperature at 40-50 degrees C; adding 10-15 wt.% microbial active strain, crushing, drying until water content is below 30% and granulating to not greater than 4 mm.
NOVELTY - A duck manure fertilizer comprises premix and fertilizer at 8:92 mass ratio.    USE - A duck manure fertilizer is used for reducing hardening and improving air permeability of soil.    ADVANTAGE - The fertilizer has small toxic side effect.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) composition of fertilizer comprising: 40-55 pts. wt. fresh manure, 10-15 pts. wt. castor, 10-15 pts. wt. colza cake and 5-10 pts. wt. wheat bran; and    (2) composition of premix comprising: 4-5 pts. wt. vitamin B1, 3-4 pts. wt. pantothenic acid, 1-1.5 pts. wt. folic acid, 0.5-1.5 pts. wt. yeast, 1-2 pts. wt. streptomycin and 0.5-0.8 pt. wt. high temperature actinomycetes.
NOVELTY - A compound microbial fertilizer comprises 60-75 wt.% municipal sludge, 10-20 wt.% nitrogenous fertilizer, 5-10 wt.% phosphate fertilizer, 10-20 wt.% potash fertilizer, and 2-5 wt.% Bacillus licheniformis.    USE - A compound microbial fertilizer for crops.    ADVANTAGE - The compound microbial fertilizer has an improved utilization ratio, and promotes the growth of the crops.
NOVELTY - A methanol gasoline comprises 20-40 wt.% gasoline, 40-60 wt.% methanol, 3-5 wt.% cosolvent, and 1-3 wt.% additive.    USE - Methanol gasoline useful as vehicle fuel.    ADVANTAGE - The methanol gasoline can save oil 50%, and reduces pollutant discharge by more than 60%.
NOVELTY - Device comprises an environment-friendly collection bag for collecting waste, a reactor for processing waste and a heating device for heating the reactor. The environment-friendly collection bag is arranged in the reactor. The reactor is arranged on the heating device.    USE - The device is useful for rapidly converting domestic waste into organic fertilizer (claimed).    ADVANTAGE - The device: can convert domestic waste into sterile, odorless powdery organic fertilizer in a short period of time (about an hour) and kill bacteria and control the spread of diseases; produces organic fertilizer, which can substitute chemical fertilizer and hence avoids environment pollution and utilizes land to form virtuous circle; is compact (about 50 cm), light weight, economical and convenient for domestic usage; and ensures tremendous changes in sanitary and health conditions and agricultural fertilizer usage of rural and urban areas.
NOVELTY - Chemical enzymatic catalysis comprises esterifying fatty acid or fatty acid anhydride and 3,7-dimethyl-6-octen-1-ol at 10-80 degrees C and rotating speed of 50-300 revolutions/minute for 1-6 hours in solvent-free system using both biological catalyst and chemical catalyst, where 3,7-dimethyl-6-octen-1-ol: fatty acid mol ratio is 1: 10-1: 1, 3,7-dimethyl-6-octen-1-ol: fatty acid anhydride mol ratio is 1: 10-1: 0.5, biological catalyst: 3,7-dimethyl-6-octen-1-ol mass ratio is 1: 1-1: 60 and chemical catalyst: 3,7-dimethyl-6-octen-1-ol mass ratio is 1: 100-1: 10.    USE - The enzymatic catalysis is used for preparing ester (claimed).    ADVANTAGE - The method is simple, energy-saving, economical and environment-friendly. It has mild reaction conditions and high efficiency.
NOVELTY - Papermaking sludge treatment agent comprises surface active agent (0.95-0.99 wt.%), bio-enzyme (0.01-0.05 wt.%), and water (rest), where the bio-enzyme is cellulase, hemicellulase, pectinase, lipase (10000-30000 IU/g) and laccase in a mass ratio of 1:1:1:1:1, and the surface active agent is polyoxyethylene alkyl phenol ether, fatty alcohol and ethylene oxide condensation product of an alkoxysilane and hexadecyltrimethylammonium bromide according to a mass ratio of 1:1:1.    USE - The agent is useful for treating papermaking sludge (claimed).    ADVANTAGE - The papermaking sludge treatment agent can be economically manufactured with less energy consumption in an environment-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for treating the sludge using treatment agent, comprising introducing papermaking sludge into tank and then concentrating, adding sludge treatment agent (0.05-0.5 wt.%) and then processing at a temperature of 30-40 degrees C and carrying out filter pressing using precipitation.
NOVELTY - Fertilizer comprises 1-6 pts. wt. glutamic acid synergistic agent A or B, 32-62 pts. wt. urea and 32-67 pts. wt. granulating material. The glutamic acid synergistic agent A is 10-30 wt.% sodium glutamate solution. The glutamic acid synergistic agent B contains 5-15 wt.% aqueous sodium hydroxide solution and glutamic acid with a weight ratio 1.8-5.5:1, or 5-15 wt.% potassium hydroxide solution and glutamic acid with a weight ratio 2.5-7.6:1. The granulating material comprises monoammonium phosphate or diammonium phosphate, potassium sulfate or potassium chloride, bentonite and calcium powder.    USE - Used as fertilizer containing glutamic acid synergistic agent.    ADVANTAGE - The fertilizer improves the nutrient utilization rate to 5-10%, promotes the root growth and enhances root activity, and improves the ability of the crops to absorb nutrients; and reduces nutrient loss, avoids secondary pollution, and reduces agricultural production cost. The method is simple, economical, and suitable for industrial production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the fertilizer, comprising (i) preparing solution of glutamic acid synergistic agent A or glutamic acid synergistic agent B; (ii) respectively crushing monoammonium phosphate or diammonium phosphate, potassium sulfate or potassium chloride, bentonite and calcium powder to a particle size of more than 60 meshes, and mixing uniformly in a rotary drum granulator to obtain granulating material; (iii) adding synergistic glutamic acid solution obtained in the step (i) and urea into a urea melting tank, and melting completely at 95-125 degrees C to obtain molten liquid; and (iv) spraying the granulating material and the molten liquid into the rotary drum granulator, granulating, drying, sieving and cooling.
NOVELTY - Preparing monkshood radix aconite total alkaloids extract, involves extracting aqueous solution of aconite radix aconiti by using macroporous absorption resin, washing the impurity with alkaline aqueous solution at pH of 8-10 (preferably at least 5) and ethanol (5-90 vol.%) to elute acidic ethanol-water solution, collecting the eluent, and removing the solvent to obtain the alkaloids extract.    USE - For preparing monkshood radix aconite total alkaloids extract (Claimed) which is used in a medicament as anti-inflammatory agent, and for relieving pain and resisting cold.    ADVANTAGE - The present method provides purified extract which completely removes impurity without losing and damaging the needed biological alkali component, and eluting to adequately corresponding to biological alkali component; has high recovery rate; and thus effectively solves the problem of the traditional method of alkali loss.
NOVELTY - Biomass synthetic oil as fuel comprises 35-65 vol.% methanol and/or ethanol, 15-30 vol.% diisopropyl ether, kerosene, naphtha, solvent oil, gasoline, and/or dimeric linoleic acid, and 20-35 vol.% butanol, octanol, benzene, toluene, and/or xylene. The oil is prepared by adding the above mentioned components into a reaction kettle, and stirring to obtain the finished product.    USE - Used as a biomass synthetic oil.    ADVANTAGE - The synthetic oil is environmentally friendly (claimed); utilizes mainly coal chemical industry product, industrial products or agricultural waste as raw materials; has high heat value; and can be mixed with petroleum-based fuels, and used directly without changes to the engine. The method has simple preparation technique; is simple to operate; is economical; reduces air pollution to the environment by reducing the discharge of tail gas to 40-60%, which is less than petrochemical gasoline emission.
NOVELTY - Manufacturing boric acid from boric magnesium ore involves: crushing boric magnesium ore to 12-14 meshes; adding sulfuric acid; filtering; crystallizing; recycling the mother liquor evaporation, where the evaporated magnesium content is 37-39%; subjecting the prepared slurry to flotation separation using the flotation machine for 35-40 minutes; taking out foam, and returning back acidolysis slot again, into a tank; centrifuging and drying to obtain magnesium sulfate.    USE - For manufacturing boric acid from boric magnesium ore (claimed). The boric acid is used for e.g. glass, ceramics and medicine.    ADVANTAGE - The method uses no added flotation flotation technology; and the method is carried out with low cost, high efficiency, and no pollution.
NOVELTY - A condensed liquid recycle system comprises gas condenser, liquid collector and control valve. The gas condenser is connected with deoxidation/dehydrogenation unit relative to high part of dehydrogenation. Other end of gas condenser is connected to condensation liquid collecting tube and collector. The liquid trap is provided between condenser and gas-liquid separator in height direction. Liquid collecting device is connected with bottom through condensing liquid return pipe and gas-liquid separator.    USE - Condensed liquid recycle system of water electrolysis hydrogen generation.    ADVANTAGE - The system is suitable for other industries gas process similar to process of condensing solution. It solves problem that gas flow generated in low-pressure side condensed liquid cannot flow back to high voltage side of the problem.    DETAILED DESCRIPTION - Condensed liquid recycle system comprises gas condenser, liquid collector and control valve. The gas condenser is connected with deoxidation/dehydrogenation unit relative to high part of dehydrogenation. Other end of gas condenser is connected to condensation liquid collecting tube and collector. The liquid trap is provided between condenser and gas-liquid separator in height direction. Liquid collecting device is connected with bottom through condensing liquid return pipe and gas-liquid separator. Liquid collector and side through pressure compensation pipe are connected with gas-liquid separator. The condensate liquid collecting pipe, condensing liquid return pipe and pressure compensating pipe are respectively provided with control valve.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic flow diagram illustrating a condensed liquid recycle system.
NOVELTY - Artemisia annua is used as raw material to prepare caffeoylquinic acid.    USE - A. annua is used as raw material to prepare caffeoylquinic acid (claimed).    ADVANTAGE - The method changes waste material into valuable material, providing great economic, social, and environmental benefits.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of caffeoylquinic acid using A. annua as raw material comprising extracting the raw material by extracting solvent to obtain caffeoylquinic acid compound extracting solution; solid-liquid separation; and separating and purifying.
NOVELTY - Organic fertilizer comprises 1.8-2 tons human waste or animal manure, 0.3-0.5 tons straw powder or leaves powder, 2.5-4 tons corn meal and 1-1.2 tons microbial inoculum.    USE - The fertilizer is useful for controlling plant diseases and insects.    ADVANTAGE - The fertilizer is prepared by simple and convenient process, improves soil environment and pH value and promotes crop growth.
NOVELTY - Method for preparing organic fertilizer by mixing pig manure with sawdust, involves obtaining pig manure, sawdust and bran powder and waste material, controlling the ratio of carbon and nitrogen, controlling water content of pig manure, stacking the mixture, performing complete composting process at low temperature, medium temperature and high temperature, subjecting mixture to cooling phase, turning the compost, raising the temperature to 60 degrees C for 48 hours, and determining the number of turning based on the maturity level of the material.    USE - The method is useful for preparing organic fertilizer used for controlling diseases and pests.    ADVANTAGE - The method is simple and convenient, and prepares organic fertilizer that improves soil environment and pH and is beneficial to crop growth.    DETAILED DESCRIPTION - Method for preparing organic fertilizer by mixing pig manure with sawdust, involves (a) obtaining 100 kg pig manure, 50 kg sawdust and 50 kg bran powder and waste material, (b) controlling the ratio of carbon and nitrogen at 23-28 and controlling water content of pig manure at 52-68%, (c) providing natural ventilation, stacking the mixture to a height of 1-1.5 m, width of 1.5-3 m and any arbitrary length, (d) performing complete composting process at low temperature, medium temperature and high temperature, subjecting mixture to cooling phase, composting the mixture at 50-60 degrees C, where the highest compost temperature is 70-80 degrees C and in the process, the temperature gradually raises for harmless treatment process, maintaining the compost at 45-65 degrees C for 10 days for killing pathogenic bacteria, eggs and grass seeds, and (e) turning the compost, raising the temperature to 60 degrees C for 48 hours, immediately turning the mixture when the temperature is more than 70 degrees C and determining the number of turning based on the maturity level of the material.
NOVELTY - The method involves forming box (2) by welding steel plates. A heating plate (1) is installed at bottom of fermentation pool and is laid at bottom of fermentation pool flatwise. A top plate (5) and the box are connected with each other by fastening. The ventilating fans and warming lights are installed on the top plate and the warming lights are overhung above the fermentation pool. A temperature control box is installed on one sealing plate (3) and is electrically connected with the power line of the heating plate and the warming lights.    USE - Method for manufacturing a manure fermentation box.    ADVANTAGE - The manufacturing of manure fermentation box is simple, convenient for usage, with high fermentation speed and good fermentation effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the fermentation box.    Heating plate (1)    Box (2)    Sealing plate (3)    Top plate (5)    Air exchange fan (6)
NOVELTY - Artensunate-intermediate dihydroartemisinin is obtained by reducing artemisinin in cyclic ether type solvent of tetrahydrofuran, 1,3-dioxane or 1,4-dioxane, by adding potassium borohydride, lithium borohydride, or zinc borohydride reducing agent.    USE - Production of artensunate-intermediate dihydroartemisinin (claimed).    ADVANTAGE - The method enables simple, economical, environmentally-friendly (low-carbon) and convenient one-pot industrial synthesis of artensunate-intermediate dihydroartemisinin with a product content of more than 99%, without requiring separation and purification, with low equipment requirement.
NOVELTY - A Rheinheimera tangshanensis deposited under CGMCC No. 5972, is new.    USE - The Rheinheimera tangshanensis is useful for preparing additive cellulose ester film for optical application (claimed).    ADVANTAGE - The method is environment-friendly, where waste liquid is directly transformed into organic fertilizer, thus zero emission and zero pollution are achieved. A biological treating process performs protection to the fibers. Compared with a traditional chemical method, the method has the advantages of being low in producing cost, high in economic benefit, and is capable of saving an energy resource and protecting an environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for preparing additive for cellulose comprising: (a) bacterial liquid is configured: the Rheinheimera tangshanensis is mixed with water to form bacterial liquid; (b) raw material processing: the woody raw material after cortex slice, or the herbal raw material cutting section, to cut the raw material into the soaking pool swelling; and (c) preparing the seal coat of fiber, comprising the steps of: mitigating the swelling of the thread raw material crushing and/or grinding, biodegradable, the hydrophobic solution as raw material to soak the prepared bacterial liquid, steam sterilizing: putting the biodegradable raw material from bacteria liquid, draining, steam sterilizing, obtain the fiber: putting the sterilized raw material for the first time period, a fiber bundle, the first time period for the second section grinding fine grinding to make the fiber beam be separated single fiber, screening, filtering after a period of grinding and the slurry after the second fine grinding of the fiber bundle, and then grinding to make it into single fiber, sterilizing: putting the prepared fiber is soaked in warm water, then drying, sterilizing, and grinding: putting the sterilized fiber into cellulose to be as the additive.
NOVELTY - A Bacillus sp. deposited under CGMCC No. 5971, is new.    USE - The Bacillus sp. is useful for preparing additive cellulose ester film for optical application (claimed).    ADVANTAGE - The method is environment-friendly, where waste liquid is directly transformed into organic fertilizer, thus zero emission and zero pollution are achieved. A biological treating process performs protection to the fibers. Compared with a traditional chemical method, the method has the advantages of being low in producing cost, high in economic benefit, and is capable of saving an energy resource and protecting an environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for preparing additive for cellulose, comprising: (a) bacterial liquid is configured: the Bacillus sp. is mixed with water to form bacterial liquid; (b) raw material processing: the woody raw material after cortex slice, or the herbal raw material cutting section, to cut the raw material into the soaking pool swelling; and (c) preparing the seal coat of fiber, comprising mitigating the swelling of the thread raw material crushing and/or grinding, biodegradable, the hydrophobic solution as raw material to soak the prepared bacterial liquid, steam sterilizing: putting the biodegradable raw material from bacteria liquid, draining, steam sterilizing, obtain the fiber: putting the sterilized raw material for the first time period, a fiber bundle, the first time period for the second section grinding fine grinding to make the fiber beam be separated single fiber, screening, filtering after a period of grinding and the slurry after the second fine grinding of the fiber bundle, and then grinding to make it into single fiber, sterilizing: putting the prepared fiber is soaked in warm water, then drying, sterilizing, and grinding: putting the sterilized fiber into cellulose to be as the additive.
NOVELTY - The method involves providing upper portion of fermenting chamber with movable common air outlet. An air channel is connected with outer fan through ventilation opening. A discharging screw conveyor is set with fermentation chamber, moving mechanism, rail and discharging belt machine. The material discharging belt machine is provided with a strip-shaped through hole set on side plates. The bottom rail is provided with a moving mechanism. The track is provided with a deodorizing device in unit fermenting chamber.    USE - Method for processing urban domestic garbage waste in ferment storehouse.    ADVANTAGE - The urban domestic garbage waste can be processed stably, reliably and conveniently.
NOVELTY - Method of preparing biomass fuel using cow dung as raw material, involves (a) obtaining fresh cow dung, and naturally drying the cow dung, (b) mixing the dried dung with microbial inoculum composition, and fermenting the mixture for 10-20 days, where the water content of the fermented product is less than 42%, and the microbial inoculum composition comprises ray fungi, fungi, Bacillus and thermophilic bacteria, and (c) performing enzymolysis, pulverizing the obtained product, sieving and granulating the product, and drying the granules.    USE - The method is useful for preparing biomass fuel (claimed) and in sewage treatment.    ADVANTAGE - The method utilizes the biological activity of the microbial inoculum, reduces viscosity of cow dung and chemical oxygen demand (COD) concentration to 500 mg/l, does not generate impact load of the cow dung, kills harmful microorganism in the cow dung by increasing temperature up to 70 degrees C, gradually enriches the crude fiber content in the fermented product, and improves calorific value to more than 2500 kcal.    DETAILED DESCRIPTION - Method of preparing biomass fuel using cow dung as raw material, involves (a) obtaining fresh cow dung where sectional stacking is adopted, and naturally drying the cow dung, where the water content of the cow dung is reduced to 60-75%, (b) mixing the dried dung with microbial inoculum composition, and fermenting the mixture for 10-20 days, where the water content of the fermented product is less than 42%, and the microbial inoculum composition comprises 20-30 pts. wt. ray fungi, 15-25 pts. wt. fungi, 10-15 pts. wt. Bacillus and 40-50 pts. wt. thermophilic bacteria, and (c) performing enzymolysis of the fermented product, pulverizing the obtained product, sieving the pulverized product, granulating the sieved product, and drying the granules till the water content is less than 30% to obtain biomass fuel.
NOVELTY - Biofertilizer comprises 30-35 pts. wt. crop stalks, 15-20 pts. wt. rape seed cake, 10-12 pts. wt. rice straw, 15-20 pts. wt. livestock and poultry excrement, 1-3 pts. wt. beneficial microorganism mixture, and 22-29 pts. wt. inorganic nitrogen-phosphorus-potassium mixture. The biofertilizer is prepared by adding crop stalks, rape seed cake, rice straw, livestock and poultry excrement and beneficial microorganism mixture into a stirrer, adjusting pH, fermenting the mixture, adding the inorganic nitrogen-phosphorus-potassium mixture, tabletting, drying and packaging obtained product.    USE - As biofertilizer.    ADVANTAGE - The biofertilizer has effects of soil moisturize preservation, cold resistance and warm keeping, soil hardness resistance and harmful bacteria antagonism.    DETAILED DESCRIPTION - Biofertilizer comprises 30-35 pts. wt. crop stalks, 15-20 pts. wt. rape seed cake, 10-12 pts. wt. rice straw, 15-20 pts. wt. livestock and poultry excrement, 1-3 pts. wt. beneficial microorganism mixture, and 22-29 pts. wt. inorganic nitrogen-phosphorus-potassium mixture. The biofertilizer is prepared by adding crop stalks, rape seed cake, rice straw, livestock and poultry excrement and beneficial microorganism mixture into a stirrer, where moisture content is controlled to 25-30%, adjusting pH to 7-8 by acid or alkali in the process of stirring to form a primary semi-finished mixture, fermenting the mixture, adding the inorganic nitrogen-phosphorus-potassium mixture, where moisture content is controlled to 15-20% to form to second semi-finished mixture, and tabletting, drying and packaging obtained product.    An INDEPENDENT CLAIM is included for use method of the above-mentioned biofertilizer, which involves crushing biofertilizer, applying the biofertilizer to the periphery of the soil surface layer or the crop root so as to form a nutrition protection layer after the crops are cultivated or seeded.
NOVELTY - Producing soil conditioner containing porous silicon calcium fertilizer comprises: (A) crushing the potassium feldspar to particles below 100 meshes; (B) adding water, quick lime and foaming agent into the feldspar powder, stirring the mixture into a homogenate; (C) placing the homogenate into a microwave high-temperature and high-pressure reaction kettle or a high-temperature steam reaction kettle; and (D) taking out the material left after reaction, placing material into a dryer, crushing, grinding the dried material and packing.    USE - Method of producing soil conditioner containing porous silicon calcium fertilizer (claimed).    ADVANTAGE - The production has natural raw materials and simple process. It realizes zero emission, thus, environmental pollution is avoided.
NOVELTY - Microwave synthesis of a substituted piperazine compound (I) comprises reacting a substituted aniline and bis(2-chloroethyl)amine hydrochloride at a mole ratio of 1:1-2 in a solvent at a microwave radiation of 50-1000 W for 1-45 minutes; and neutralizing by an alkali.    USE - Method for the microwave synthesis of a substituted piperazine compound (claimed) used for synthesizing antihistamines, antidepressants, antipsychotics, and relieving cough medicine.    ADVANTAGE - The method has an increased reaction speed, shortened reaction time, improved reaction yield, and is energy-saving and environment-friendly.    DETAILED DESCRIPTION - Microwave synthesis of a substituted piperazine compound of formula (I) comprises reacting a optionally substituted aniline of formula (R1-(CH2)m-NH2) and bis(2-chloroethyl)amine hydrochloride at a mole ratio of 1:1-2 in a solvent at a microwave radiation of 50-1000 W for 1-45 minutes; and neutralizing by an alkali.    R1=optionally substituted phenyl, or optionally substituted heterocyclic aryl, where the substituent is 1-6C alkyl, halo (where halo is Cl, Br, or I), nitro, acyl, OH, CN, carbonyl , 1-6C alkoxy, 1-6C alkyl-acyl, 1-6C halogenated-alkyl (where halo is Cl, Br, or I), 1-6C halogenated-alkoxy (where halo is Cl, Br, or I), or 1-6C halogenated alkyl-acyl (where halo is Cl, Br, or I); and    m=0-6.
NOVELTY - The method involves cutting and kneading the raw materials. The straw wires are sieved by spraying the acetic acid. The ends of each steel wire are provided with clamping head. The disk saw blade is provided on the shaft. The raw material is dried and hot-pressed. The wood soaked in the mixed solution of coal tar and anthracene oil is cut, while heating the asphalt in the liquid. The glue containing urea-formaldehyde, melamine, phenolic glue and isocyanate is applied on the raw material. The length of the high carbon steel wire or bamboo is set to specific value.    USE - Method for producing pre-stress straw wood.    ADVANTAGE - The bending strength of the straw wood can be improved. The application range of the straw wood can be improved. The environmental protection can be ensured.
NOVELTY - Method for preparing Chinese herbal medicine production-increasing fertilizer for Eleusine indica, involves using (in wt.%): dry chicken manure (5-7), dry rabbit manure (2-4), dry duck manure (16-20), sawdust (8-12), rapeseed cake powder (10-12), cottonseed cake powder (4-6), rape straw powder (10-14), wheat straw powder (4-6), sesame straw powder (10-14), pumpkin leaf powder (4-8), sweet potato leaf powder (2-4), broad bean shell powder (2-4), wood ash powder (3-5), and carrot leaf powder (6-8).    USE - The method is useful for preparing Chinese herbal medicine production-increasing fertilizer for growing E.indica.    ADVANTAGE - The fertilizer increases soil permeability, water permeability and water retention, does not remain as residue in plant, promotes rapid growth of E.indica with high yield, and reduces hypertrophic reactions in foliage.
NOVELTY - A fuel preparing method involves allowing biological oil to undergo a catalytic cracking deoxidation reaction under heating in the presence of a cracking deoxidation catalyst. The obtained products are mixed with hydrogen followed by allowing a mixture to undergo a catalytic hydrogenation deoxidation reaction under heating in the presence of a hydrogenation deoxidation catalyst.    USE - Method for preparing fuel from biological oil.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a method for preparing fuel.'(Drawing includes non-English language text)'
NOVELTY - Preparing erlotinib intermediate 3-aminophenylacetylene, comprises carrying out Vilsmeier reaction of 3'-nitroacetophenone (I) to obtain (Z)-N-(3-chloro-3-(3-nitrophenyl)allylidene)-N-methylmethanaminium chloride (II), then carrying out hydrolysis of (II) to obtain (Z)-3-chloro-3-(3-nitrophenyl)acrylaldehyde (III), carrying out elimination reaction of (III) to obtain 3-nitrophenylacetylene (IV), and then reducing (IV).    USE - The method is useful for preparing erlotinib intermediate 3-aminophenylacetylene.    ADVANTAGE - The method: improves atom economy; has simple process; and is environment friendly.
NOVELTY - The device has a storage box located at an upper part, and an inner container is located with a furnace body. The inner container is connected with a material storing tank, where height of the inner container is 200 mm. A gas pipe passing through the furnace body is connected with the inner container. A rotating pressing rod passes through the storage box, and is inserted into the furnace body from an upper end of the material storing tank. A feeding hopper door is arranged on a lower end of a feeding hopper.    USE - Multi-functional biomass gasification device.    ADVANTAGE - The device reduces the tar content in the fuel gas, and has gasification stability.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a multi-functional biomass gasification device.
NOVELTY - The furnace has a tapered furnace cover installed on top of a furnace body, and a gas-liquid mixture outlet installed on an upper part of the furnace body, where an air distributor is installed at a bottom part of the furnace. An automatic ignition device is arranged on the furnace body. A lower part of the furnace body is provided with a slag outlet. A valve is arranged on an air pipe. A lower air outlet pipe is connected with a gas collecting tube. The gas collecting tube is connected with an air inlet pipe.    USE - Solid waste cracking furnace.    ADVANTAGE - The furnace is simple in structure, and can effectively utilize the furnace material uniformly and stably.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a solid waste cracking furnace.
NOVELTY - The generator has a generator shell comprising a generator outer shell, an inner and outer shell flange, a shell body, a circular flange and a sealed steam generator. A generator shell body part is connected with a variable diameter cone shell, an opening ring and a top sealing plate. A sealing ring plate outer side is provided with a discharging guide plate, and an outer furnace shell is provided with a group of brackets supporting a furnace body. A side of the generator is connected with a steam outlet pipe.    USE - Household garbage fuel gas generator.    ADVANTAGE - The generator has simple structure, stable operation, low cost and obvious effect. The generator can design the development of totally enclosed device according to a solid waste component and the thermal value. The generator avoids the need to add the auxiliary fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial sectional view of a household garbage fuel gas generator.
NOVELTY - An improved method for drying an organic material using a dryer, involves mixing a relatively dry material with the organic material to produce a mixture; and subjecting the mixture to a drying process in the dryer to produce a granular product, where the organic material is of the type which, if subjected itself to the drying process, would agglomerate. The improvement includes use of the organic material, where the organic material has been previously dried, as the relatively dry material.    USE - For drying an organic material using a dryer; for drying raw sewage sludge; and for producing a fertilizer from an organic material. The product is used as a fuel for a combustion power plant to produce electricity and ash (all claimed).    ADVANTAGE - The drying operation does not suffer from balling, agglomeration and caking and thus operates relatively economically. The drying cycle involves the pasteurization of the material at above 70 degrees C for at least 30 minutes to destroy pathogens, thereby to minimize the need for special handling procedures. The fuel product is capable of self-sustained combustion with negligible hydrocarbon emissions (i.e. combustion efficiency estimated at 99.3% based on char carbon content of the ashes and CO and methane concentrations in the flue gas) in a vibrating grate style stoker and combustor at an above bed combustion temperature of 173 degrees F.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an improved method for producing a fertilizer from an organic material, involving blending an alkaline material with the organic material to produce a blend; and subjecting the blend to a drying process to produce a granular fertilizer product, where the improvement includes use of the ash as the alkaline material.
NOVELTY - A biogas production process involves providing a substrate containing manure, and either a) adding at least one enzyme to the substrate, and then adding the substrate with the enzyme to a biogas digester; or b) adding the substrate to a digester tank and adding enzyme to the tank.    USE - For producing biogas from substrate containing manure such as porcine manure or cattle manure (claimed), useful for producing methanol.    ADVANTAGE - The method enhances methane production; provides environmental benefits; and increases degradability of substrate material making it more accessible for biogas production process leading to a higher yield.
NOVELTY - Controlling unwanted bacteria in a biofuel production process having reaction mediated by bacterial system reactive agents, involves applying to a biomass substrate bacteriophages virulent for at least one strain of the unwanted bacteria.    USE - For controlling unwanted bacteria selected from species from genera such as lactic acid bacteria, including Lactobacillus, Pediococcus, Lactococcus, Enterococcus, Weissella, Leuconostoc, Streptococcus, and Oenococcus, and species from genera such as acetic acid bacteria, including Acetobacter and Gluconobacter in a biofuel production process (claimed).    ADVANTAGE - The process reduces ecological and environmental impact of human activities through the removal of specific microbial contaminations in biofuel production without the use of antibiotics; and provides a green alternative to toxic chemical biocides and antibiotics for controlling problem bacteria in the industrial biofuel production industries.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a composition comprising at least one bacteriophage virulent for unwanted bacteria in a biofuel production process in which biofuel production process which is impeded by unwanted bacteria utilizes bacterial system reactive agents.
NOVELTY - Producing ethanol from whole stillage, comprises: obtaining supply of whole stillage; pre-treating stillage to convert hemicellulose portions of stillage into sugars, where the pre-treating step comprises adding acid to stillage, heating and pressurizing the stillage, holding stillage under pressure and heating, removing pressure and cooling the stillage; adding enzymes to stillage; fermenting the stillage to form beer mixture; distilling beer mixture; and transferring obtained ethanol to ethanol production facility to be combined with ethanol produced by the production facility.    USE - The method is useful for producing ethanol from whole stillage (claimed), where the ethanol is used as fuel or fuel additive.    ADVANTAGE - The method: provides additional ethanol from byproducts, thus increasing the yield; improves the nutritional content and value of the animal feed produced from the byproducts of the process and corn oil recovery; and produces final byproduct that is higher in protein and lower in fiber, hence easier for monogastrics to digest.    DETAILED DESCRIPTION - Producing ethanol from whole stillage, comprises: obtaining a supply of whole stillage from an ethanol production facility; pre-treating the stillage to convert hemicellulose portions of the stillage into sugars, where the pre-treating step comprises adding acid to the stillage to decrease its pH level, heating and pressurizing the stillage, holding the stillage under pressure and heat for a dwell time, removing pressure from the stillage to cause flashing, and cooling the stillage; adding enzymes to the stillage to convert cellulose portions of the stillage into sugars; fermenting the stillage to create a beer mixture; distilling the beer mixture to separate ethanol; and transferring the ethanol from the distilling step to the ethanol production facility to be combined with ethanol produced by the ethanol production facility.
NOVELTY - Producing ethanol from whole stillage, comprises: obtaining a supply of whole stillage from an ethanol production facility and pre-treating to convert hemicellulose portions into sugars; adding enzymes to the whole stillage to convert cellulose portions of the whole stillage into sugars; fermenting the whole stillage; distilling the obtained beer mixture to separate ethanol; and transferring the ethanol to the ethanol production facility.    USE - The process is useful for preparing ethanol, which is used as a gasoline additive or a straight liquid fuel.    ADVANTAGE - The process improves nutritional content and value of the animal feed produced from the byproducts of the process.    DETAILED DESCRIPTION - Producing ethanol from whole stillage, comprises: obtaining a supply of whole stillage from an ethanol production facility; pre-treating the whole stillage to convert hemicellulose portions of the whole stillage into sugars, where the pre-treating step comprises adding acid to the whole stillage to decrease its pH level, heating and pressurizing the whole stillage in a hydroheater where steam is injected to cause cavitation of the whole stillage, holding the whole stillage under pressure and heat for a dwell time, removing pressure from the whole stillage to cause flashing, and cooling the whole stillage; adding enzymes to the whole stillage to convert cellulose portions of the whole stillage into sugars; fermenting the whole stillage to create a beer mixture, distilling the beer mixture to separate ethanol from it; and transferring the ethanol from the distilling step to the ethanol production facility to be combined with ethanol produced by the ethanol production facility.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a process of producing ethanol from byproducts of the ethanol production facility.
NOVELTY - A methane fermentation apparatus has fermenter (2) which accommodates granule-like sludge, and to-be-processed water is introduced into the lower portion, and organic substance in the to-be-processed water is decomposed and biogas containing methane is generated. The fermenter has gas-solid liquid separation portion (7) which separates the biogas, sludge and to-be-processed water in the fermenter, and gas blowing-in portion (9) provided on the gas-solid liquid separation portion, which blow gas into the to-be-processed water and refluxes biogas discharged from the fermenter.    USE - Methane fermentation apparatus (claimed).    ADVANTAGE - The methane fermentation apparatus suppresses the outflow of the sludge from the upper portion of the fermenter.    DETAILED DESCRIPTION - A methane fermentation apparatus has fermenter which accommodates granule-like sludge, to-be-processed water is introduced into the lower portion, sludge is made to carry out counterflow contact by flowing it upwards, organic substance in the to-be-processed water is decomposed and biogas containing methane is generated, and discharges treated water and biogas from the upper portion. The fermenter has gas-solid liquid separation portion which separates the biogas, sludge and to-be-processed water in the fermenter, and gas blowing-in portion provided on the gas-solid liquid separation portion, which blow gas into the to-be-processed water and refluxes biogas discharged from the fermenter.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of the fermenter.    Fermenter (2)    Settler (6)    Gas-solid liquid separation portion (7)    Induction portion (8)    Gas blowing-in portion (9)
NOVELTY - The furnace has a bottom coupling fluidized bed provided with a gas distributor and a discharging pipe. Position of air flow is provided with a feeding port. A grade gas-solid separator is connected with a material returning device and a coupling fluidized bed. The gas-solid separator of a fine particulate ash circulation returning pipe is connected with another grade gas solid separator that is connected with a gas outlet. Size of diameter of a straight pipe is 1.2 to 2. Reactor equivalent diameter is small.    USE - Domestic garbage coupled fluidized bed grading pyrolysis gasification furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a domestic garbage coupled fluidized bed grading pyrolysis gasification furnace.
NOVELTY - A composition comprises bacterial cell that converts crude glycerol or glycerol or a mixture of glycerol and methanol or ethanol, or a mixture of glycerol and methanol or ethanol and matter organic non-glycerol (MONG) and salts, into at least one lipid or hydrocarbon.    USE - As a composition (claimed), useful for producing oils, fuels, and oleochemicals.    ADVANTAGE - The composition produces organic compounds including lipids, oils, or oleochemicals from low cost or waste energy and carbon sources; allows the crude glycerol byproduct of biodiesel production to be converted into additional triacylglycerols and other neutral lipids, which can be in turn converted into additional biodiesel, thus increasing the yield of biodiesel produced from a given initial input of triacylglycerol and other neutral lipid into the biodiesel production process; allows the development of new genetically enhanced strains of microorganisms that can be used to produce and secrete targeted organic compounds including oleochemicals and drop-in liquid fuels, economically in bulk from petroleum or higher plants, directly from low cost or waste energy and carbon sources; and enables low cost synthesis of chemicals and fuels, which can compete on price with petrochemicals and higher-plant derived oleochemicals, and which have a substantially lower price than oleochemicals produced through heterotrophic growth on sugar or microbial phototrophic synthesis.
NOVELTY - Fertilizer comprises mixture of vinegar mash lees, and foodstuff waste material, where moisture content of the mixture is 20% or more.    USE - The fertilizer is useful for cultivating fruits and vegetables.    ADVANTAGE - The fertilizer can be stored for long period of time, improves growth of crops, and decomposes easily without producing new environmental impact, hence reduces decomposition expense.
NOVELTY - A fuel generator has magnetism in an oxidized state and reduced state, and fuel generating agent (1) which generates fuel by oxidation reaction in which motion of the fuel generating agent is restrained by magnetic force.    USE - Fuel generator for fuel cell system (claimed).    ADVANTAGE - Performance degradation of fuel cell apparatus is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the structure of fuel cell system.    Fuel generating agent (1)    Fuel cell apparatus (2)    Magnetic body (3)    Container (4, 5)    Gas distribution channel (6)
NOVELTY - System to convert biomass derived pyrolysis oil (bio-oil) into fuel range hydrocarbons, comprises a bio-oil feedstream comprising pyrolyzed biomass, an aqueous feedstream, a mixer/separator to mix the bio-oil feedstream and the aqueous feedstream and separate the aqueous extract comprising oxygenates, optionally a reactor to stabilize the aqueous oxygenate extract using mild hydrogenation, a hydrogen donor feedstream, and a reactor to react the aqueous extract and hydrogen donor with a catalyst to generate fuel range hydrocarbons.    USE - The system is useful to convert biomass derived pyrolysis oil (bio-oil) into renewable fuel range hydrocarbons comprising light gases, gasoline range hydrocarbons, diesel range hydrocarbons, light oils, vacuum oil, liquid paraffin, jet fuel, naphthenes and/or paraffins (all claimed) for transportation.    ADVANTAGE - The system converts difficult plant materials lignins, cellulose, hemicellulose, fibers, waste products raw biomass into renewable fuels, thus providing a direct source renewable fuels fungible with fuel products produced from nonrenewable sources.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) converting biomass derived pyrolysis (bio-oil) into fuel range hydrocarbons comprising: providing the bio-oil feedstream, mixing the bio-oil feedstream with the aqueous feed-stream, separating the aqueous extract comprising oxygenates from the bio-oil feedstream and aqueous feedstream mixture, optionally reacting the aqueous extract with hydrogen in the presence of the catalyst to generate a stabilized aqueous extract, and reacting the aqueous extract with a hydrogen donor feedstream in the presence of the catalyst to generate fuel range hydrocarbons; and    (2) a renewable fuel range hydrocarbon produced from the biomass derived pyrolysis oil by the method.
NOVELTY - Preparing a copolymer comprises copolymerizing a vinylidene fluoride monomer with a monomer of alpha -trifluoromethacrylic acid or its derivative in the presence of a xanthate or trithiocarbonate compound.    USE - The process is useful for producing a copolymer to produce a block copolymer, where the copolymer and the block polymer are useful for producing a membrane, which is useful in a fuel cell device (all claimed).    ADVANTAGE - The process produces the copolymer with improved diversity, morphology, properties and exceptional versatility, in high yield in a controlled radicalizing copolymerization manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparing a block copolymer comprising reacting a copolymer of the vinylidene fluoride monomer and the monomer of alpha -trifluoromethacrylic acid or its derivative, having a terminal xanthate or trithiocarbonate group, with a comonomer (b1);    (2) the copolymer prepared by the method; and    (3) a block copolymer comprising a block (a) of the copolymer of the vinylidene fluoride monomer and the monomer of alpha -trifluoromethacrylic acid or its derivative and a homopolymer block (b).
NOVELTY - Multiplying Trichoderma strain, comprises sowing a culture medium by a stock suspension of Trichoderma propagules, and culturing Trichoderma in the medium to obtain a primary inoculum, where the medium comprises 25-50 wt.% of wood fibers having an air volume level of 55-90%, and the medium is substantially free from fungal contaminants and having bacterial contaminants of less than or equal to 102 colony forming unit (CFU)/g.    USE - The method is useful for: multiplying Trichoderma strain (claimed); and producing compost, where the Trichoderma is a fungal microorganism, which is useful as a plant biocontrol agents, and for mycoparasitism, antagonism, producing antibiotics, root stimulation, stimulating plant growth by fertilizing mineral solubilization, and stimulating natural defenses of the plants, where the compost is useful as microflora for cleaning substrate of plant culture and improving fertilization of the plant. No biological data given.    ADVANTAGE - The method improves biomass production, and reduces substrate loss for the development of the microorganism.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a compost comprising 0.02-0.5% of secondary inoculum mass.
NOVELTY - A fuel cell (10) e.g. high-temperature fuel cell has a cathode (1) to which oxygen-containing gas (4) is supplied, an anode (2) to which combustible gas (5) is supplied, and gas-permeable layer(s) (6,6a,6b,7,7a,7b) containing binding material(s) (6a) including silicon, sulfur and/or their compound. The oxygen-containing gas is supplied through gas-permeable layer (6). The combustible gas is supplied through gas-permeable layer (7).    USE - Fuel cell e.g. high-temperature fuel cell is used for fuel cell system (claimed).    ADVANTAGE - The economical fuel cell has favorable durability and suppressed short circuit potential.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) fuel cell system;    (2) manufacture of fuel cell; and    (3) impregnating solution used for manufacture of fuel cell and fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawings show cross-sectional view of the fuel cell.    Cathode (1)    Anode (2)    Oxygen-containing gas (4)    Combustible gas (5)    Gas-permeable layer (6,6a,6b,7,7a,7b)
NOVELTY - Hydrothermal carbonization of biomass in a continuous flow, comprises feeding the biomass by a conveyor (3) to at least one reactor (5), in which the biomass is dehydrated and carbonized, removing the carbon slurry emerging through the carbonization from the reactor via at least one outlet, where the carbon slurry is fed to the outlet by a filtering device (8), which is designed for solid separation of larger particles of a defined particle size.    USE - The method is useful for hydrothermal carbonization of biomass.    ADVANTAGE - The method is carried out continuously using structurally simple, space-saving filtering device, and reduces the cost of preliminary sorting, thus it is cost efficient.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for device for hydrothermal carbonization of biomass in continuous flow, comprising a reactor with an outlet for removal of the carbon slurry emerging through the carbonization and a filtering device.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the device for the hydrothermal carbonization of biomass in a single reactor.    Hydrothermal carbonization plant (1)    Conveyor (3)    Reactor (5)    Filtering device (8)    Heat exchanger (10)
NOVELTY - Hydrothermal carbonization of biomass in a flow, comprises: supplying biomass by a conveyor (3) to a pre-heater (4) and heating the biomass; supplying the heated biomass to at least one reactor (5), dehydrating- and carbonizing the biomass; and removing carbon slurry that is emerged through the carbonization, from the reactor. The dehydrate water emerging through the dehydration in the reactor, is removed from the reactor in a liquid state, and the dehydrate water is fed directly to the pre-heater and mixed with the biomass in the pre-heater.    USE - The method is useful for hydrothermal carbonization of biomass in a flow.    ADVANTAGE - The method is easy and inexpensive, and ensures an improved heating of the biomass, and uniform and continuous dehydration- and carbonization inside the reactor.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an apparatus for hydrothermal carbonization of biomass in the flow, comprising a conveyor for conveying the biomass to a pre-heater, in which the biomass is heated; at least one reactor, in which the biomass is dehydrated and carbonized; a removal device for removing dehydrate water emerging through the dehydration. The removal device is connected directly to the pre-heater, via at least one fluid communication.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the apparatus for hydrothermal carbonization of biomass with a single reactor.    Conveyor (3)    Pre-heater (4)    Reactor (5)    Heat exchanger (6)    Filter device (8)
NOVELTY - Cosmetic product comprises (i) a water-in-oil emulsion comprising (a) at least one antiperspirant aluminum salt, (b) at least one water-in-oil emulsifier with a hydrophilic-lipophilic balance (HLB) value of 1.5-6.5, (c) at least one oil-in-water emulsifier or a solubilizer with the HLB value of more than 7-20, preferably 15-17, (d) at least one cosmetic oil, (e) 5-methyl-2-(1-methylethyl) cyclohexyl-N-ethyl oxamate, preferably (1R, 2S, 5R)-5-methyl-2-(1-methylethyl)-cyclohexyl-N-ethyl oxamate, (ii) at least one propellant, and (iii) an aerosol dispensing device.    USE - The cosmetic product is useful as an aerosol spray.    ADVANTAGE - The cosmetic product: exhibits high corrosion resistance; exhibits good skin compatibility, storage stability and effectiveness; provides pleasant, non-sticky feeling on the skin; and provides a long-lasting cooling and refreshing effect on the skin for a period of at least one hour, preferably at least two to four hours after application.    DETAILED DESCRIPTION - Cosmetic product comprises (i) a water-in-oil emulsion comprising (a) at least one antiperspirant aluminum salt, (b) at least one water-in-oil emulsifier having a hydrophilic-lipophilic balance (HLB) value of 1.5-6.5, (c) at least one oil-in-water emulsifier or a solubilizer with the HLB value of more than 7-20, preferably 15-17, (d) at least one cosmetic oil, which is not a fragrance and not an essential oil, (e) 5-methyl-2-(1-methylethyl) cyclohexyl-N-ethyl oxamate, preferably (1R, 2S, 5R)-5-methyl-2-(1-methylethyl)-cyclohexyl-N-ethyl oxamate, (ii) at least one propellant, and (iii) an aerosol dispensing device.
NOVELTY - Racemization of (S)-3-carbamoylmethyl-5-methyl-hexanoic acid (I) involves: a) heating or optionally treating (S)-3-carbamoylmethyl-5-methyl-hexanoic acid with a base at higher temperature; b) treating the solution with an alkali or alkali hydroxide and further acidifying the solution with an acid to obtain (3)-carbamoylmethyl-5-methyl-hexanoic acid racemate (III); and c) isolating the (3)-carbamoylmethyl-5-methyl-hexanoic acid racemate (III).    USE - For racemization of (S)-3-carbamoylmethyl-5-methyl-hexanoic acid (claimed), used in anticonvulsant therapy.    ADVANTAGE - The method avoids the use of hazardous base and solvent to prepare the pregabalin in green, cost effective and environment friendly manner. The pregabalin has analgesic, anti-convulsant, and anxiolytic activity.
NOVELTY - A gas separation membrane (10) comprises a support layer (2) and a separation layer (1) formed on the upper side of the support layer. The separation layer comprises a hydrophilic layer (1a) containing hydrophilic polymer arranged on the opposite side of support layer, and a main separation layer (1b) arranged on support layer side.    USE - Gas separation membrane is used for gas separation membrane module (claimed) used for separating benzene, toluene and xylene contained in gas from thermal power station, cement plant, and iron mill blast furnace.    ADVANTAGE - The gas separation membrane has excellent gas permeability, and high gas-separation selectivity and durability.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of gas separation membrane. (Drawing includes non-English language text)    Separation layer (1)    Hydrophilic layer (1a)    Main separation layer (1b)    Main layer (1c)    Support layer (2)    Gas separation membrane (10)
NOVELTY - The furnace has a furnace seat provided with a dust hopper. A furnace body is connected with a hearth. The hearth is provided with a furnace bridge and a feeding port. The furnace body is fixed on a side of a combustion air channel. The furnace body is connected with a surface of a sealing cover. A smoke channel is connected with a chimney.    USE - Straw gasifying furnace for use in a rural area during cooking and heating processes.    ADVANTAGE - The furnace saves energy and reduces emission of smoke.
NOVELTY - Production of sensing active component having algae inhibiting activity and anti-bacterial activity using barley involves taking overground part of barley at 50-70 degrees C, drying and crushing the barley having particle size of 20-50 mesh, extracting liquid using ethanol (20-80%) at 20-80 degrees C for 5 times, concentrating the liquid and removing solvent, to obtain organic phase, drying, separating, and eluting, to obtain chloroform phase, followed by extracting and eluting, to obtain the component, which is spirulina bioactive inhibitor.    USE - For production of sensing active component having algae inhibiting activity and anti-bacterial activity using barley (claimed), useful for controlling lake base algae bloom.    ADVANTAGE - The method is simple and easy; has low cost; is capable of obtaining high purity algae; and is environment-friendly.    DETAILED DESCRIPTION - Production of sensing active component having algae inhibiting activity and anti-bacterial activity using barley involves taking overground part of barley at 50-70 degrees C, drying and crushing the barley having particle size of 20-50 mesh, extracting liquid using ethanol (20-80%) at 20-80 degrees C for 5 times, each time for 2-6 hours, concentrating the liquid and removing solvent, to obtain organic phase, drying, separating using positive silica column, eluting using dichloromethane and methanol having volume ratio of 19:1, to obtain chloroform phase, condensing the chloroform phase to remove the solvent to obtain the extract; extracting the extract obtained in the above step for separating positive silica column, and eluting, to obtain the component, which is spirulina bioactive inhibitor.
NOVELTY - Production of sensing active component having algae inhibiting activity using ethyl acetate and barley extract involves taking overground part of barley at 50-70 degrees C, drying and crushing barley having particle size of 20-50 mesh, extracting using ethanol (20-80%) at 20-80 degrees C, combining the extraction liquid, concentrating and removing solvent to obtain extract, mixing the obtained extract with water, using ethyl acetate to extract for 2-4 times, to obtain ethyl acetate phase, followed by condensing, extracting, and eluting by using dichloromethane and methanol.    USE - For production of sensing active component having algae inhibiting activity using ethyl acetate and barley extract (claimed), useful for controlling lake base algae bloom.    ADVANTAGE - The method is simple and easy; has low cost; is capable of obtaining high purity algae; and is environment-friendly.    DETAILED DESCRIPTION - Production of sensing active component having algae inhibiting activity using ethyl acetate and barley extract involves taking overground part of barley at 50-70 degrees C, drying and crushing barley having particle size of 20-50 mesh, extracting using ethanol (20-80%) at 20-80 degrees C for 5 times, each time for 2-6 hours, combining the extraction liquid, concentrating and removing solvent to obtain extract, mixing the obtained extract with water, using ethyl acetate to extract for 2-4 times, to obtain ethyl acetate phase, condensing the ethyl acetate phase to remove the solvent to obtain the extract; extracting the obtained extract for separating positive silica column, and eluting by using dichloromethane and methanol having volume ratio of 49:1, to obtain the component, which is spirulina bioactive inhibitor.
NOVELTY - The tank has an overflow area arranged in a bio-membrane filler area and an active sludge area. A biological membrane filling material area is provided with filler. The filler is arranged in a culture. An active sludge area is arranged with a propeller of a multifunctional hydrolyzing acidification regulating tank body. The tank body is connected with a tail end of a water inlet and a sludge inlet.    USE - Multifunctional hydrolysis acidification adjusting tank.    ADVANTAGE - The tank is convenient to use, and has better multifunction and hydrolysis effect, high biodegradability, anti-impact load ability and strong adaptability. The tank performs easy regulation and management, and carries out hydrolysis acidification process.
NOVELTY - The reactor has a reactor main body whose upper part is provided with a flocculating chamber. A guide chamber is arranged with a separating chamber that is arranged with an umbrella cover. An outer side of the flocculating chamber is provided with multiple mud slag concentrated chambers that are arranged between the umbrella cover and the separating chamber. A top part of the reactor main body is formed with a water collecting groove that is matched with an outside of a water outlet pipe.    USE - Sludge circulating reactor for processing industrial organic waste water.    ADVANTAGE - The reactor improves biodegradability of waste water and ensures uniform anaerobic fermentation process, and has high stability.
NOVELTY - The device has a tower body whose top or bottom part is formed with a gas outlet that is matched with a power motor. The tower body is provided with a gas chamber and a power transmission rod that is connected with a drive motor main shaft. The gas chamber is provided with a transmission main shaft that is fixed on an upper part of an impeller-type analyzer. A cabin is formed with a liquid outlet.    USE - Gas removing focus analysis device for a biomass fuel gas industry.    ADVANTAGE - The device improves gas separating efficiency and reduces tar content.
NOVELTY - The device has a raw material collecting tank and an anaerobic fermenting tank that are filled with pyrolysis material. A bottom part of the raw material collecting tank is formed as a conical cylindrical-shaped structure.    USE - Automatic integrated waste two-phase anaerobic fermentation device for use in a kitchen.    ADVANTAGE - The device is inexpensive and environment-friendly, and has high working efficiency, and reduces energy consumption and realizes automatic and circular acidolysis solution adding process.
NOVELTY - The device has a feeding hopper connected with a feeding pipe that is connected with an acidifying tower. The acidifying tower is arranged at a lower part outlet of an anaerobic hydrogen generating tower that is arranged at a lower part outlet of an anaerobic marsh gas tower.    USE - Kitchen waste producing hydrogen and marsh gas device.    ADVANTAGE - The device has high working efficiency, and avoids secondary pollution and enables collecting collect product hydrogen and marsh gas and fermentation liquor to adequately make kitchen waste.
NOVELTY - The system has a marsh gas tank which is connected with a marsh gas pool to generate marsh gas for generating biogas. An electric generator is set with a marsh gas generator and an electric energy is transmitted to an electric equipment of an electric energy output interface. A gas end of a ground source heat pump system is connected with a heating system.    USE - Ecological residential system.    ADVANTAGE - The high energy conversions in the ecological residential system can be realized and the energy waste can be reduced. The energy utilization rate of the residential system can be improved.
NOVELTY - The production equipment is included with a raw material tank, an electric stirrer in the tank, a mixing tank, and a finished product tank. The raw material tank is provided with the electric stirrer. The raw material tank, mixing pump, mixing tank, pressurizing device, and finished product tank are connected through a pipeline.    USE - Bio-diesel fuel additive production equipment.    ADVANTAGE - The labor intensity for producing bio-diesel fuel additive can be reduced. The production efficiency of the bio-diesel fuel additive can be improved while reducing the production period.
NOVELTY - Biomass composite fuel production line comprises a raw coal crusher, a straw grinder, a discharging port of the raw coal crusher and straw grinder connected with a storage hopper of a dosing machine through a bucket of a loading cabin, and an upper hopper of a forced stirrer connected with a dosing machine through a weighing hopper. The upper hopper is connected with a stirring barrel through a lifting device of the stirrer. The stirring barrel is connected with an adjustment tank through a discharging door. The adjustment tank is connected with the storage hopper by an output conveying belt.    USE - Used as a biomass composite fuel production line.    ADVANTAGE - The production line adopts advanced process, has compact structure, occupies small floor area, ensures high ground utilization rate, and is suitable for processing multiple wastes.
NOVELTY - A reusable seedling substrate comprises corn straw leavening, perlite, mushroom dregs and effective microorganism (EM) culture medium, where the corn straw leavening is corn straw, dairy manure or water.    USE - A reusable seedling substrate.    ADVANTAGE - The seedling substrate has low cost and balanced nutrition, and can meet the nutrition requirement of seedling.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of reusable seedling substrate comprising crushing corn straw; mixing with dairy manure and water; fermenting, drying, drip washing and airing to obtain corn straw leavening; uniformly mixing EM stock solution, molasses, and distilled water; regulating pH at 3.5-4.5 to obtain EM culture solution; and uniformly mixing corn straw leavening, perlites and mushroom dregs; and spraying EM culture solution on its surface.
NOVELTY - A plant cultivation matrix comprises 10-30 pts. wt. sawdust, 30-40 pts. wt. livestock manure, 4-6 pts. wt. peat, 10-30 pts. wt. tree bark, 5-15 pts. wt. waste mushroom stick, 3-8 pts. wt. earthworm, 8-12 pts. wt. peanut skin, 5-10 pts. wt. perlite, and 0.001-0.002 pts. wt. Bacillus.    USE - Plant cultivation matrix used for vegetation growth.    ADVANTAGE - The plant cultivation matrix can avoid pollution to the environment, supply stable elements including potassium, organic matter and trace elements, provide vegetation with high survival rate and fast growth speed, and can be used in all four seasons of a year.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the plant cultivation matrix, comprising:    (A) mixing crushed sawdust, livestock manure, peat, tree bark, waste mushroom stick, earthworm, peanut skin, perlite and stacking at 1.5 m by 2.5 m;    (B) turning the material stack while adding water, where water content of material is controlled at 55-65%;    (C) when material temperature reaches 65-70 degrees C, standing for 8-10 days to completely kill harmful microorganism between upper and lower layers, turning while adding water to completely soak the material;    (D) after two weeks, when pH value reaches 6.5 and conductivity reaches 2.2 dS/m, turning while adding water to completely soak the material for the second time;    (E) turning once every three days for 8 times; and    (F) after turning for 10 times, performing physical and chemical index test, when pH value is 4.8-6.5, electric conductivity is 1.5-2.2 dS/m and when nitrogen and chloride concentration is not less than 200 mg/L, ammonium ion is not less than 100 mg/L and nitrogen present as nitrate ion is greater than or equal to 25 mg/L, and stacking for 10-15 days after sieving.
NOVELTY - Producing organic fertilizer using sewage sludge, comprises using urban sewage sludge through primary processing, using a horizontal type fermentation cylinder, adopting natural ventilation, forced ventilation and intermittent forced ventilation as three types of ventilation method, fermenting the sludge in the cylinder for 4-5 days, controlling the temperature in the cylinder to 55-75 degrees C until the moisture content of the sludge is reduced from 70% to 40%, extruding the sewage sludge by an extruder, and pelleting to obtain granular organic fertilizer.    USE - The method is useful for producing organic fertilizer using sewage sludge (claimed).    DETAILED DESCRIPTION - Producing organic fertilizer using sewage sludge, comprises using urban sewage sludge through primary processing, using a horizontal type fermentation cylinder having a cylinder length of 10-12 m, an inner diameter of 1-1.2 m and a rotation speed of 0.03 r/rain, adopting natural ventilation, forced ventilation and intermittent forced ventilation as three types of ventilation method, fermenting the sludge in the cylinder for 4-5 days, controlling the temperature in the cylinder to 55-75 degrees C until the moisture content of the sludge is reduced from 70% to 40%, extruding the sewage sludge by an extruder, and pelleting to obtain granular organic fertilizer.
NOVELTY - An organic fertilizer comprises 60-65 wt.% plant straw, 20-22 wt.% edible fungi residue, 14-16 wt.% rapeseed or soybean cake, 5 wt.% calcium-magnesium phosphate fertilizer, and 1 wt.% thermophilic cellulose decomposing bacteria. The plant straw has water content of 30-35%. The edible fungi residue is straw mushroom or needle mushroom culture waste residue. The thermophilic cellulose decomposing bacteria comprise Bacillus subtilis, Cellulomonas flavigena, Bacillus licheniformis, or Cellulomonas cartae.    USE - Organic fertilizer.    DETAILED DESCRIPTION - An organic fertilizer comprises 60-65 wt.% plant straw, 20-22 wt.% edible fungi residue, 14-16 wt.% rapeseed or soybean cake, 5 wt.% calcium-magnesium phosphate fertilizer, and 1 wt.% thermophilic cellulose decomposing bacteria. The plant straw has water content of 30-35%. The rapeseed or soybean cake is a by-product after rapeseed or soybean pressing method for extracting fat. The edible fungi residue is straw mushroom or needle mushroom culture waste residue. The calcium-magnesium phosphate comprises 12% phosphorus, calcium, magnesium, and phosphorus and 10% microelement. The thermophilic cellulose decomposing bacteria comprise Bacillus subtilis, Cellulomonas flavigena, Bacillus licheniformis, Cellulomonas cartae, Aspergillus versicolor, or Trichoderma viride.
NOVELTY - Circulating water using device comprises reservoir, a water feeding pump, a refining pulping machine, slurry storage tank, slurry pump, slurry valve, a stirring tank, a valve switch, slurry pump and slurry pumping pipe, a heavy metal ion removing and anaerobic fermentation device, a slurry machine, a filter press, an outlet pipe, a water return pipe joint, a water return pipe, a small tank, and a water pump. The reservoir via the water pump is connected with the refining pulping machine and slurry storage tank. The slurry pump is connected to refining pulping machine and slurry storage tank.    USE - The circulating water using device is used in household waste fertilizer production.    ADVANTAGE - The device does not cause secondary pollution, can save water to avoid waste of water resource, reduces the fertilizer cost, and increases the economic benefit of enterprises.
NOVELTY - The marsh gas generating device includes a value-added cavity containing sewage (1). The chamber body is provided with a discharging mechanism (2), a sewage input mechanism (4), an air inlet flushing mechanism (5), and a sewage water level (6) to control the discharging mechanism. The sewage water level to control the discharging mechanism is lower than the opening in the cavity.    USE - Sewage automatic deslagging marsh gas generating device. Can be used for processing domestic sewage to generate marsh gas.    ADVANTAGE - Water source pollution is reduced since sewage treatment is harmless and value added. Processing cost is low and automation degree is high.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic cross-sectional view of the sewage automatic deslagging marsh gas generating device.    Value-added cavity containing sewage (1)    Discharging mechanism (2)    Sewage input mechanism (4)    Air inlet flushing mechanism (5)    Sewage water level (6)
NOVELTY - A hydrogenation method involves selecting biological oil and fat as raw oil. The raw oil is passed with hydrogen at two hydrogenation reactors under the condition of hydrogenation operations followed by loading hydrogenation catalysts in the hydrogenation reactors. The raw oil and hydrogen is passed through a low temperature-hydrogenation reactor operated utilizing an upward flowing operation mode of co-current flow gas and liquid flowing upward to obtain effluent. The effluent is passed into a high temperature-hydrogenation reactor.    USE - Hydrogenation method for producing high-quality motor fuels.    ADVANTAGE - The method enables producing high-quality motor fuels with stable flow of the biological oil and fat.    DETAILED DESCRIPTION - A hydrogenation method involves selecting biological oil and fat as raw oil. The raw oil is passed with hydrogen at two hydrogenation reactors under the condition of hydrogenation operations followed by loading hydrogenation catalysts in the hydrogenation reactors. The raw oil and hydrogen is passed through a low temperature-hydrogenation reactor operated utilizing an upward flowing operation mode of co-current flow gas and liquid flowing upward to obtain effluent. The effluent is passed into a high temperature-hydrogenation reactor under the reaction condition, followed by separating hydrogenation reaction effluents from the high temperature-hydrogenation reactor into gas phase and liquid phase, where the hydrogenation catalysts comprise active components comprising reduced noble metal or reduced non-noble metal and the liquid phase is transferred into fractionating tower to obtain naphtha and diesel oil.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a hydrogenation method for producing high-quality motor fuels.
NOVELTY - A bio-oil-diesel blend hydrogenation method involves adopting fixed bed reactor, supplying straight-run diesel oil and/or secondary processing diesel oil into a hydrogenation reactor, filling catalyst bed layer with non-noble metal vulcanized state hydro-refining catalyst. The method further involves discharging biological oil from the reactor, mixing oil and hydrogen, transporting into hydrogenation reactor-II, filling catalyst bed layer with reduced noble metal catalyst, separating gas-liquid material from reactor-II to obtain liquid phase and fractionating tower to obtain a diesel fraction.    USE - Method for hydrogenating bio-oil-diesel blend.    ADVANTAGE - The method enables hydrogenating bio-oil-diesel blend in a stable and effective manner.    DETAILED DESCRIPTION - A bio-oil-diesel blend hydrogenation method involves adopting fixed bed reactor, supplying straight-run diesel oil and/or secondary processing diesel oil as raw material into a hydrogenation reactor from a top portion of reactor-I, filling catalyst bed layer in the hydrogenation reactor-I with a non-noble metal vulcanized state hydro-refining catalyst. The method further involves discharging biological oil from bottom portion of the reactor, mixing oil and hydrogen, transporting into hydrogenation reactor-II, filling catalyst bed layer of the reactor-II with reduced noble metal catalyst, and separating gas-liquid material from the reactor-II to obtain liquid phase and fractionating tower to obtain diesel fraction.
NOVELTY - Method (M1) for producing lactones (I) or their open chain forms (IX), involves performing enzymatic oxidation of lactols (II), aldehydes (III), or diols (IV).    USE - The method is useful for producing lactones which is used for synthesizing statins chosen from atorvastatin, rosuvastatin (all claimed), cerivastatin, pitavastatin, fluvastatin, and pravastatin.    ADVANTAGE - The method produces lactones with excellent stereochemical purity, and utilizes simple, less aggressive and environmentally-friendly agents.    DETAILED DESCRIPTION - Method for producing lactones of formula (I) or their open chain forms of formula (IX), involves performing enzymatic oxidation of lactols of formula (II), aldehydes of formula (III), or diols of formula (IV).    X=-H, 1-6C alkyl, 6-14C aryl, -Cl, -Br, -I, -SH, -SR1, -NH2, -NHR1, -CH2NHR1, -CH2R2, -N3, -OTs, -OMs, or -OAc;    R=-H or hydroxy protecting group;    R1=1-4C alkyl or ?C(O)OCH2Ph;    R2= group of formula (a) or (b);and    R3=-H, 1-6C alkyl, or 6-14C aryl.    INDEPENDENT CLAIMS are included for the following:    (1) method (M2) for producing (4R,6S)-6-(chloromethyl)-4-hydroxytetrahydro-2H-pyran-2-one or its open chain form (3R,5S)-6-chloro-3,5-dihydroxyhexanoic acid, involves enzymatic oxidation of (4R,6S)-6-(chloromethyl)tetrahydro-2H-pyran-2,4-diol; and    (2) crystalline lactol having an X-ray diffraction pattern of containing two or more peaks at 8.6, 17.3, 19.6, 22.8, 25.6, 26.1, 32.3, 38.1, and 42.4 plus minus 0.2 degrees 2- theta (2 theta ).
NOVELTY - A Jatropha curcas biological refined aviation fuel, where unsaponifiable matter in refined oil content is less than or equal to 0.2%, metal ion content is less than or equal to 10 ppm, phosphorus content is less than or equal to 3 ppm, acid value is not less than 5 mg KOH/g, water content is less than or equal to 1000 ppm, and appearance is clear and transparent.    USE - J. curcas biological refined aviation fuel.    ADVANTAGE - The crude oil or processed by conventional method J. curcas oil physical and chemical index: appearance color and luster is clear and transparent, phosphorus content is not less than 500 ppm, calcium content is not less than 16 ppm, magnesium content is not less than 8 ppm, iron content is less than or equal to 3 ppm and acid value is not less than 6 mg KOH/g, water content is less than or equal to 1000 ppm and insoluble impurity content is less than or equal to 0.2%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing biological aviation fuel comprising:(A) removing insoluble impurity by filtering or processing based on conventional method, heating J. curcas oil to 30-95 degrees C, adding 0.5-10% adsorbent and 0.1-1% acid adjusting agent based on oil total weight, and stirring for 15-50 minutes, then filtering; and (B) heating refined J. curcas oil to 40-80 degrees C, adding 0.5-6% chelating agent monoethanolamine (MEA), fully mixing for 30-60 minutes, centrifugal separating and removing chelating agent MEA, vacuum dehydrating and drying.
NOVELTY - Preparing glycoside IA from bitter figwort comprises extracting bitter figwort using methanol or ethanol and then heating in a microwave, decompressing the mixture and then concentrating, extracting the obtained product by hot water, dispersing the extract through a macroporous absorption resin column and then eluting with ethanol, collecting the ethanol eluent and then decoloring, concentrating the ethanol eluent and then drying, adding active carbon and then heating and stirring, filtering the stirred mixture, and decoloring liquid to decompress and recycle ethanol and then drying.    USE - The method is useful for preparing glycoside IA from bitter figwort (claimed).    ADVANTAGE - The method simply provides the glycoside IA with high purity (greater than 95%) in a rapid manner.    DETAILED DESCRIPTION - Preparing glycoside IA from bitter figwort comprises extracting bitter figwort using methanol or ethanol and then heating in a microwave, decompressing the mixture and then concentrating to obtain the extract, extracting the obtained product by hot water, dispersing the extract through a macroporous absorption resin column and then eluting with ethanol (60-90%), collecting the ethanol eluent and then decoloring, concentrating the ethanol eluent and then drying, adding active carbon and then heating and stirring, filtering the stirred mixture, decoloring liquid to decompress and recycle ethanol and then drying to obtain crude product, and separating the crude product and then purifying in high speed counter current chromatography.
NOVELTY - Bioorganic fertilizer comprises 80-85 pts. wt. animal manure, 4-5 pts. wt. straw powder, 10-15 pts. wt. coal, 0.15-0.20 pts. wt. microbial inoculum, 20-30 pts. wt. urea, 16-20 pts .wt. potassium sulfate, 20-24 pts. wt. calcium magnesium phosphate and 18-20 pts. wt. humic acid.    USE - As bioorganic fertilizer.    ADVANTAGE - The product has improved quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the above bioorganic fertilizer, which involves (a) uniformly mixing animal manure, straw powder and coal, where the animal manure is livestock and poultry manure, (b) spraying microbial inoculum to the above mixture, (c) fermenting the obtained mixture (1-2 times) for 25-20 days, (d) drying, crushing and sieving the fermented mixture and (e) adding urea, potassium sulfate, calcium magnesium phosphate and humic acid to the sieved mixture obtained in step (d), and granulating and drying the obtained product.
NOVELTY - Insecticidal microemulsion comprises 1-20 %mass chlorpyrifos, 5-60 %mass organic solvent, 5-25 %mass cosolvent, 3-8 %mass emulsifier, 5-25 %mass antifreeze agents and water (remainder).    USE - As insecticidal microemulsion (claimed).    ADVANTAGE - The insecticidal microemulsion is stable and environmentally-friendly, and promotes dilution and permeation of insecticides.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the above-mentioned insecticidal microemulsion, which involves (a) adding chlorpyrifos and lufenuron to organic solvent, (b) adding cosolvent to the obtained solution and adding emulsifier to the solution, (c) uniformly stirring the solution at a speed of 50-90 revolutions per minute, (d) uniformly mixing water with the stirred solution for 10-30 minutes to obtain uniform transparent microemulsion, and (e) uniformly mixing the obtained microemulsion with the antifreeze agents.
NOVELTY - Comprehensive utilization of sludge comprises fermenting the sludge with bacteria, where the bacteria are mixed bacteria (yeast, bacteria and fungi) according to a ratio of 100:2:2, uniformly mixing the inoculated sludge and then stirring, fermenting the stirred mixture at an initial temperature of 27-37 degrees C and then at 35-45 degrees C for 2 days, mixing fly maggot and then cultivating and breeding at room temperature of 25-35 degrees C for 6-7 days, and separating the fly maggot from the sludge and then processing at a temperature of 20 degrees C for 15 days.    USE - The method is useful for comprehensive utilization of sludge (claimed).    ADVANTAGE - The method realizes the reduction of sludge quantization in the environment with high stability.
NOVELTY - A shaddock sticky rice special fertilizer comprises 63-66 wt.% sugarcane filter mud, 19.5-21 wt.% wood residue, 9.3-11 wt.% factory alcohol waste liquid, 3.7-4.6 wt.% active base material and 0.37-0.55 wt.% active strain. Water content of filter mud is 60-70%. Alcohol factory waste liquid brix is 55 degrees .    USE - Shaddock sticky rice special fertilizer.    ADVANTAGE - The fertilizer solves sticky rice planting low yield and fruit quality problems.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing sticky rice shaddock special fertilizer which comprises mixing above raw materials in double-shaft stirrer and fully and uniformly stirring; and fermenting stack to 60-65 degrees C for 21-28 days, and turning every 3-4 days to obtain desired fertilizer.
NOVELTY - Azabicyclo(4.3.0)nonene-acyl halide intermediates (I) i.e. N-chlorocarbonyl-8-azabicyclo(4.3.0)nonene and N-bromocarbonyl-8-azabicyclo(4.3.0)nonene are new.    USE - (I) are useful for treating diabetes mellitus (claimed).    ADVANTAGE - The preparation method: has mild reaction condition, simple operation, and high product yield; utilizes cheap and easily available raw materials; has no toxic and harmful reagents; and is suitable for large scale production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparation of (I).
NOVELTY - The discharging device has sludge inlet pipe (1), pulse air cans (2), pulse component (3), pipe (4), sludge outlet pipe (5), air inlet pipe (6), and fixing bracket (8). The sludge inlet pipe is welded on the pulse air cans. The one end of the pulse component is connected with the sludge inlet pipe, while the other end is connected with pipe. The sludge outlet pipe is welded on the pulse air cans. The air inlet pipe is welded on the pulse air cans. The upper portion of outer side of the fixing bracket is welded on the pulse air cans.    USE - Pulse gas stripping sludge discharge device used for clarification tank, biochemical reaction pond, and sludge discharging pool.    ADVANTAGE - The pulse gas stripping sludge discharge device is simple in structure, easy to maintain, easy to operate, high in stability, and high in durability. The occurrence of blockage can be prevented. The consumption of energy can be saved. The discharge amount can be adjusted at random manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the pulse gas stripping sludge discharge device.    Sludge inlet pipe (1)    Pulse air can (2)    Pulse component (3)    Pipe (4)    Sludge outlet pipe (5)    Air inlet pipe (6)    Fixing bracket (8)
NOVELTY - Manufacturing fertilizer turner, involves welding the steel rectangular frame, where the rectangular frame of the upper and lower sides are provided with table set with engine box, the lower side of fixed drive door track is set with a walking wheel, the walking wheel is pressed on the wall of the two sides of the fertilizer trough, the welding beam is equipped in the middle of the rectangular frame, the bracket is inverted V-shaped, the end of the bracket shaft is connected with turning wheel, and the upper part is welded on the bracket motor.    USE - The method is useful for manufacturing fertilizer turner.    ADVANTAGE - The method is simple and cost-effective.    DETAILED DESCRIPTION - Method for manufacturing fertilizer turner, involves welding the steel rectangular frame, where the rectangular frame of the upper and lower sides are provided with table set with engine box, the lower side of fixed drive door track is set with a walking wheel, the walking wheel is pressed on the wall of the two sides of the fertilizer trough, the welding beam is equipped in the middle of the rectangular frame, the bracket is inverted V-shaped, the end of the bracket shaft is connected with turning wheel, the upper part is welded on the bracket motor, a motor is set with motor and connected with the turning wheel belt transmission connection, an engine box is mounted on the upper part of the operating platform, the operating platform and the engine box are provided with an engine, and a motor for driving the walking wheel along the track.
NOVELTY - Fertilizer turner comprises a cross beam and a side table, where the beam is provided with a motor, the motor is provided with a motor lower part of the cross beam provided with a bracket, the bracket is inverted V-shaped, the end part of the bracket is provided with a turning wheel, and the turning wheel is connected with a motor belt in transmission manner.    USE - Fertilizer turner.    ADVANTAGE - The device has simple structure, and is cost-effective.
NOVELTY - The device has drying chamber that is surrounded by walls made of toughened transparent glass. The drying chamber has sludge recycling spreading device connected with ground source heat pump of the geothermal coil pipe. The material outlet of drying chamber and crushing chamber is connected with stirrer. The stirrer is connected with the punch through the spiral conveying device.    USE - Device for producing fuel rod by mixing papermaking sludge and biomass.    ADVANTAGE - The waste resource produced during production of fuel rod is recycled effectively, so that the environment protection is achieved. The manufacturing of device for producing fuel rod is performed at low cost. The simple and convenient operation of the device is performed for large-scale industrial production.
NOVELTY - A bifunctional catalyst comprises alkaline earth metal oxide-supported copper oxide.    USE - Bifunctional catalyst used for manufacturing high cetane number biodiesel (claimed).    ADVANTAGE - The bifunctional catalyst produces biodiesel with low carbon content and excellent low temperature fluidity and stability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of the bifunctional catalyst, which involves mixing copper oxide precursor and alkaline earth metal oxide, adding ammonia solution, diluting the mixture to obtain copper oxide precursor loaded with alkaline earth metal oxide, and calcining the precursor; and    (2) manufacture of biodiesel, which involves carrying out catalytic ester interchange reaction and hydrogenation of unsaturated oil in the presence of the bifunctional catalyst to obtain biodiesel.
NOVELTY - Amino acid fertilizer comprises 1-2 pts. wt. enzymes and bacteria, 20-30 pts. wt. livestock manure, 50-70 pts. wt. Artemisia annua dregs, where the bacteria is comprises Bacillus subtilis RB and commercial bacterial enzyme, and the Bacillus subtilis RB is preserved in China general microorganism culture preservation management center with the preservation number CGMCG NO.6268.    USE - Used as an amino acid fertilizer.    ADVANTAGE - The fertilizer is rich in nutrients, realizes changing of waste into useful product, and has high quality, thus suitable in agriculture and forestry.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the amino acid fertilizer, comprising mixing enzymes and bacteria, livestock manure and Artemisia annua residue according their proportion, performing open type aerobic solid state fermenting at 60-70 degrees C for 6-7 days, and the transmitting into a drying system, crushing, granulating and sieving.
NOVELTY - Composition comprises 5-50 wt.% Solidago canadensis extract, 1-70 wt.% fungicide agent and other fillers (balance amount). The Solidago canadensis extract is prepared by completely soaking Solidago canadensis plant by adding absolute methanol at 25-30 degrees C, filtering, subjecting to vacuum drying, and concentrating the filtrate to remove methanol, obtaining a concentrated material, and drying the concentrated material to obtain the Solidago canadensis extract. The fungicide agent is carbendazim, thiophanate-methyl, flusilazole or chlorothalonil.    USE - The composition is useful for preventing and treating fungal diseases of crops.    ADVANTAGE - The composition utilizes the fungicidal and chemical fungicidal activity of Solidago canadensis extract, and thus it exhibits synergist effect; and reduces the utilization rate of chemical fungicides, and thus it facilitates pollution-free agricultural production; and comprising Solidago canadensis exhibits comprehensive preventing and controlling effect.    DETAILED DESCRIPTION - Composition comprises 5-50 wt.% Solidago canadensis extract, 1-70 wt.% fungicide agent and other fillers (balance amount). The Solidago canadensis extract is prepared by completely soaking Solidago canadensis plant by adding absolute methanol at 25-30 degrees C, filtering, subjecting to vacuum drying, and concentrating the filtrate to remove methanol, obtaining a concentrated material, and drying the concentrated material to obtain the Solidago canadensis extract. The fungicide agent is carbendazim, thiophanate-methyl, flusilazole or chlorothalonil. The other fillers are carriers used for preparing aqueous composition, powdered composition or oily composition of pesticide.
NOVELTY - Reaction tank (1) of a plant for the hydrothermal carbonization of biomass (3), is claimed, where the reaction tank of a plant encloses a reaction space with a unit for feeding a biomass and for supplying a steam (5), and the supplying unit comprises at least one injection nozzle, which is configured for swirling the biomass using inflowing vapor and arranged in a ground-level turbulence area of the reaction space.    USE - The reaction tank of a plant is useful for the hydrothermal carbonization of biomass (claimed).    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic perspective view of a plant for the hydrothermal carbonization of biomass.    Reaction tank (1)    Preheating tank (2)    Biomass (3)    Stream (5)    Steam pump. (6)
NOVELTY - Apparatus for hydrothermal carbonization of solid or liquid biomass, comprises at least one preheating device, a reactor, and an after-treatment device. The preheating device is at least one separate-, closed preheating tank (30), which is connected with at least one separate-, closed reactor, preferably a reaction tank (40) that is emptied into at least one separate-, closed buffer tank (50) for the after-treatment of slurries formed from the biomass. A slurry pump is arranged between the closed pre-heating tank and the closed reaction tank.    USE - The apparatus is useful for hydrothermal carbonization of solid or liquid biomass.    ADVANTAGE - The device allows an easy-, time saving- and inexpensive hydrothermal carbonization of the biomass.    DETAILED DESCRIPTION - Apparatus for hydrothermal carbonization of solid or liquid biomass, comprises at least one preheating device, a reactor, and an after-treatment device. The preheating device is at least one separate-, closed preheating tank (30), which is connected with at least one separate-, closed reactor, preferably a reaction tank (40) that is emptied into at least one separate-, closed buffer tank (50) for the after-treatment of slurries formed from the biomass. A slurry pump is arranged between the closed pre-heating tank and the closed reaction tank, for conveying the slurry from the preheating tank into the reaction tank.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic perspective view of the apparatus for hydrothermal carbonization both solid and liquid biomass.    Feed tank (10)    Feed funnel (20)    Preheating tank (30)    Reaction tank (40)    Buffer tank (50)
NOVELTY - The process comprises producing a mixture of oxide particles (16) having mixed conductivity and nickel-aluminum composite oxide particles, cobalt-aluminum composite oxide particles or composite oxide particles composed of a nickel-aluminum composite oxide and a cobalt-aluminum composite oxide, superposing a layer of the mixture on a surface of a solid electrolyte and sintering the mixture layer, and reducing the resultant sinter at a temperature of 800-1000 degrees C.    USE - The process is useful for producing a fuel electrode for a solid oxide electrochemical cell (claimed) such as a solid oxide fuel cell and a solid electrolyte high-temperature steam electrolysis cell.    ADVANTAGE - The process allows economical production of the electrode with high catalytic activity and durability thus improving power generation efficiency, stability, output density and performance of the fuel cell.    DETAILED DESCRIPTION - The process comprises producing a mixture of oxide particles (16) having mixed conductivity and nickel-aluminum composite oxide particles, cobalt-aluminum composite oxide particles or composite oxide particles composed of a nickel-aluminum composite oxide and a cobalt-aluminum composite oxide, superposing a layer of the mixture on a surface of a solid electrolyte and sintering the mixture layer, and reducing the resultant sinter at a temperature of 800-1000 degrees C. The oxide particles having mixed conductivity are mixed with the nickel-aluminum composite oxide particles, cobalt-aluminum composite oxide particles, or composite oxide particles composed of a nickel-aluminum composite oxide and a cobalt-aluminum composite oxide, in a weight ratio of 50:50-95:5.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic sectional view of a structure of a solid oxide fuel cell.    Solid electrolyte plate (11)    Fuel electrode material (12)    Air electrode material (13)    Current collector (14)    Oxide particles. (16)
NOVELTY - Producing biofuel from tobacco biomass, comprises: extracting oil from the tobacco biomass with a polar organic solvent selected from methyl acetate and ethyl acetate, removing the polar organic solvent, transesterifying the extracted oil, and separating the biofuel from the products of the transesterification step.    USE - The method is useful for producing biofuel from tobacco biomass (claimed).    ADVANTAGE - Excellent yields of biofuel based on the weight of the biomass are obtained using the method.
NOVELTY - The method involves heating of ashes to vitrification temperature by a set of burners using air as oxidant, where the air is enriched with oxygen or purified syngas (6) from a gasification unit (1), or biogas (23), or natural gas (24). The flue gases produced by the burners during combustion of the ashes are evacuated, and the ashes are cooled in a vitrification chamber (26). The ashes are directed towards the gasification unit at one or more points of the gasification unit having a gas treatment unit (14) upstream of the gasification unit.    USE - Method for vitrification of ashes produced by a gasification process or pyrogasification.    ADVANTAGE - The method allows the ashes to be recovered in vitreous form with great stability and very weak potential to leach salt out of initial contaminants.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the method for vitrification of ashes produced by a gasification process or pyrogasification.'(Drawing includes non-English language text)'    Gasification unit (1)    Purified syngas (6)    Gas treatment unit (14)    Biogas (23)    Natural gas (24)    Vitrification chamber (26)
NOVELTY - The method involves introducing a volume of gas into a collection chamber (14), where the volume of gas is exposed to a side of hydrogen permeable membrane (22), and hydrogen gas within the volume of gas is permeated through the membrane and out of the chamber to produce lower partial pressure of the hydrogen gas in the chamber and increased partial pressure of contaminant gas with the chamber. Pressure within the chamber is measured. The pressure within the collection chamber is converted to a reading indicative of the contaminant gas present in the volume of gas.    USE - Method for testing contaminant levels in a volume of gas containing hydrogen gas and contaminant gas e.g. hydrocarbon and water vapor, to obtain ultra pure hydrogen that is utilized during manufacturing a fuel cell. Can also be used for manufacturing electronic microprocessors.    ADVANTAGE - The method enables concentrating contaminants in the sample of hydrogen gas analyzed by a mass spectrometer so that extremely low levels of contamination can be accurately detected, thus enabling a person to better track when an ultra pure hydrogen generation system is beginning to fail.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a gas collection system.    Gas collection chamber (14)    Hydrogen permeable membrane (22)    Extraction port (24)    Computer controller (32)    Mass spectrometer (34)
NOVELTY - The reactor system has a chamber that is formed between hollow cathode (11) and anode (5). The plasma gas and/or electric arc are generated in the chamber. The working gas (4) is passed through electric arc forming region (20) to generate plasma gas. The plasma gas is mixed with carbonaceous material and carrier gas as feedstock. The mixed gas is passed into chamber through hollow passage of hollow cathode within or nearby highest temperature region of chamber so as to perform pyrolysis of carbonaceous material and gasphase reaction of the volatiles.    USE - Multi-stage plasma reactor system with hollow cathodes for cracking carbonaceous material such as coal, coal tar, coal direct liquefaction residue, heavy crude residuum, char, petroleum coke, tar sand, shale oil, carbonaceous industrial wastes or tailings, biomass, synthetic plastic, synthetic polymer, spent tire, municipal solid waste, bitumen (all claimed).    ADVANTAGE - The temperature and heating rate of the carbonaceous material can be enhanced. The carbonaceous material can release more volatiles that can cause production of more cracked products by realization of fast and efficient thermal transfer to the carbonaceous material. The energy wastage can be prevented and over concentration of thermal emission is avoided in reaction tube. The hollow cathodes and anodes are prevented from overheating as portion of outer surface of hollow cathode and anode is cooled by recycling cooling medium. The generated cracked products are quenched instantaneously before exiting last one reaction tubes so as to prevent the cracked products obtained in gas phase reaction from decomposing. The higher energy efficiency can be achieved and the yield of cracked product can be maximized.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the three-stage plasma reactor system.    Working gas (4)    Anode (5)    Cathode (11)    Insulator (15)    Forming region (20)
NOVELTY - Composting pressmud comprises (a) culturing thermophilic and mesophilic bacteria in a nutrient medium comprising jaggery, to yield a microbial composition having a pH value of 4.2-5.2 and a temperature of 300-400 degrees C, and (b) providing the microbial composition to sugarcane pressmud.    USE - The method is useful for compositing sugarcane pressmud (claimed) and coirpith, tomato pulp or mango pulp.    ADVANTAGE - The method is capable of effectively, economically and eco-friendly composting the sugarcane pressmud.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a compost prepared using the microbial composition.
NOVELTY - A sustainable chemical process of reduction of 4-methoxy-2-nitroaniline to 4-methoxy benzene-1,2-diamine, involves carrying out a neutral reaction medium and inherent recycling of the neutral reaction medium in several cycles, each of the cycle has a reaction sequence and a extraction and layer separation sequence, where the extraction and layer separation sequence follows the green reaction sequence.    USE - For the reduction of 4-methoxy-2-nitroaniline to 4-methoxy benzene-1,2-diamine (claimed).    ADVANTAGE - The process is an environmentally friendly (green) process that overcomes the problem of generation of large quantities of liquid waste resulting from the conventional processes of reduction; reduces undesirable side reactions leading to organic and inorganic side products formation by the virtue of chemo-selectivity and region-selectivity which results in purer product formation; possibly makes large number of mother liquor recycles; has surprisingly low levels of organic compounds and are thus ireen in nature; does not require any acidic liquid effluent treatment facility or elaborate solid waste disposal facility; is not constrained in respect of plant location, in that it doesn't necessarily have to be carried out in industrial areas; the inorganic by-product is non-sticky, which makes their handling easier and simpler than conventional processes; is highly recyclable; is carried out at milder acid concentrations and at atmospheric pressure, which makes it safer; is inherently safe due to the safe levels of the process parameters such as pressure, temperature, pH, concentrations of reaction components, and various reaction agents, this reduces the risk of injuries to the personnel and damage to the process plant; and it saves energy and therefore results in the process economy.
NOVELTY - The system has pre-reformer (40) that carries out pre-reformation before carrying out steam reforming of natural gas. A carbon dioxide recovery apparatus (50) recovers carbon dioxides from waste gas. An air-preheat apparatus (60) pre-heats combustion air supplied to steam reformer (10). The self balance of energy in whole system is carried out using heat recovery from waste gas and reformed gas, and combination heat in methanol synthesis tower (20), gasoline combining tower (30), pre-reformer, carbon dioxide recovery apparatus and air-preheat apparatus.    USE - System for manufacturing gasoline or dimethyl ether via methanol from natural gas.    ADVANTAGE - The gasoline can be used effectively without discarding effectively the exothermic energy at the time of manufacturing gasoline or dimethyl ether via methanol from natural gas. The production amount of gasoline can be increased, as the supply amount of methanol is increased. The exothermic energy in the gasoline combining tower can be increased according to the increase in production amount.    DETAILED DESCRIPTION - The system has steam reformer that carries out steam reforming of natural gas, and produces reformed gas. The methanol synthesis tower combines methanol with reformed gas. The gasoline combining tower combines gasoline or dimethyl ether with methanol. An INDEPENDENT CLAIM is included for a method for manufacturing gasoline or dimethyl ether via methanol from natural gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the system for manufacturing gasoline via methanol from natural gas.    Steam reformer (10)    Methanol synthesis tower (20)    Gasoline combining tower (30)    Pre-reformer (40)    Carbon dioxide recovery apparatus (50)    Air-preheat apparatus (60)
NOVELTY - A waste material of pruned branches or mowed grass is pulverized. Leaf or grass is removed from ground waste material.    USE - Method of processing waste material for use as fuel for combustion apparatus.    ADVANTAGE - The method enables rapid processing of waste material. The thermal efficiency of waste material is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the combustion apparatus. (Drawing includes non-English language text)    Combustion apparatus (10)    Fuel-supply channel (11)    Combustion chamber (12)    Heat exchanger (13)    Air supply path (14)
NOVELTY - A renewable jet fuel derived at least in part from biomass comprises: n-paraffins (0-10 wt.%), iso-paraffins (5-20 wt.%), naphthenes (15-95 wt.%), 1-ring naphthenes (5-50 wt.%), 2-ring naphthenes (0-50 wt.%), 3-ring naphthenes (0-10 wt.%), and aromatics (0-25 wt.%).    USE - As renewable jet fuel derived from biomass (claimed).    ADVANTAGE - The renewable jet fuel has a freeze point of less than -40?F; and a flashpoint of greater than 100?F. The jet fuel is a drop in jet fuel that meets all specifications for Jet A and JP-8. As these fuels are derived from biomass with an expected 50% reduction in greenhouse gas emissions compared to petroleum-derived fuels, production of these fuels will earn credits under the Renewable Fuel Standard 2 (RFS2) of the US Energy Independence and Security Act of 2007 and therefore have value in addition to their basic value as fuels or other commodities. Each fraction of these biofuels from distillation is fungible and relatively easily sold to customers for value. These fuels allow production of fungible renewable fuel products that are stable, functional, and equivalent to current fuel products used. The fuels have properties that are equivalent to or superior to fuel products on the market today. The fuels have a distributed range of paraffins, iso-paraffins, naphthenes, and aromatics. Unlike ethanol and other alcohol based fuels, these renewable fuels have a high heat of combustion and deliver equivalent energy to that of traditionally purified hydrocarbons. The naphthenes help the biomass derived hydrocarbons meet product specifications for jet and diesel while really helping cold flow properties.
NOVELTY - Renewable diesel fuel derived at least in part from biomass comprises 0-10 wt.% of n-paraffins, 5-20 wt.% of iso-paraffins, 15-95 wt.% of naphthenes, 5-50 wt.% of 1-ring naphthenes, 5-50 wt.% of 2-ring naphthenes, 0-15 wt.% of 3-ring naphthenes, and 0-25 wt.% of aromatics.    USE - Used as renewable diesel fuel.
NOVELTY - At least one portion of vegetable organic substance-containing raw material is subjected to fluidized-bed carbonization using air as fluidization gas. A fixed bed or moving bed is integrated in a portion of carbonization process, in flow carbonization furnace (1), and carbonization time is extended. The residence time of fluidized bed (5) is shortened which is less than the residence time which the carbonized material smoke emission of flow carbonization layer requires. Thus, the flow carbonization of vegetable organic substance-containing raw material is carried out.    USE - Flow carbonization of vegetable organic substance-containing raw material e.g. pruned branch leaf, disaster debris and agriculture-and-forestry industrial waste.    ADVANTAGE - The method enables efficient, economical and safe flow carbonization of vegetable organic substance-containing raw material. The size of carbonization furnace, power consumption of air blower and expense of raw material grinding and drying are reduced.    DETAILED DESCRIPTION - At least one portion of vegetable organic substance-containing raw material is subjected to fluidized-bed carbonization at 280-630 degrees C using air as fluidization gas. A fixed bed or moving bed driven by low-temperature long time from fluidized bed is integrated in a portion of carbonization process, in flow carbonization furnace, and the carbonization time is extended. The residence time of fluidized bed is shortened which is less than the residence time which the carbonized material smoke emission of flow carbonization layer requires. Thus, the flow carbonization of vegetable organic substance-containing raw material is carried out.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the apparatus for flow carbonization of vegetable organic substance-containing raw material.    Carbonization furnace (1)    Fluidized bed (5)    Heat insulating material (9)    Cyclone (13)    Bag filter (18)
NOVELTY - Preparing oxidation-stabilized biodiesel comprises reacting at least one natural oil with at least one 2-tert-butyl-4-methyl-phenol compound (I) and subsequently transesterifying the natural oil in the presence of methanol and/or ethanol.    USE - The oxidation-stabilized biodiesel is useful as fuel (claimed).    ADVANTAGE - The process provides biodiesel with high oxidation and storage stability; and can be prepared in high yield without any by-products.    DETAILED DESCRIPTION - Preparing oxidation-stabilized biodiesel comprises reacting at least one natural oil with at least one 2-tert-butyl-4-methyl-phenol compound of formula (I) and subsequently transesterifying the natural oil in the presence of methanol and/or ethanol.    R = (3-tert-butyl-2-hydroxy-5-methyl-phenyl)methyl or tert-butyl (preferred).
NOVELTY - The method comprises diverting a part of water (E1) produced by a fuel cell to a treatment tank containing a saturation reagent, and mixing a flow of the treated water from the treatment tank with an undiverted flow of water (E3) to obtain water (E5) with a desired mineralization and/or pH.    USE - The method is useful for remineralizing and correcting a pH of water produced by a fuel cell in an aircraft (claimed) such as passenger aircraft, where the remineralized water is used for passengers consumption and food sanitation in the aircraft.    ADVANTAGE - The method is capable of remineralizing and correcting the pH of water in the treatment tank without requiring a high exposure time in a compact manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for implementing a method for remineralizing and correcting a pH of water.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic sectional view of a first mode of realization of a device for remineralizing and correcting a pH of water.    First tank spreader (100)    Conduit (120)    Water (E1)    Undiverted flow of water (E3)    Produced water. (E5)
NOVELTY - Stabilized biodiesel obtained by doping at least one natural oil with at least one 2-tert-butyl-4-methyl-phenol compound (I) and subsequently transesterifying the natural oil in the presence of methanol and/or ethanol, is claimed.    USE - The stabilized biodiesel is useful as fuel (claimed).    ADVANTAGE - The stabilized biodiesel: exhibits improved oxidation and storage stability; and can be prepared in high yield without any byproducts.    DETAILED DESCRIPTION - Stabilized biodiesel obtained by doping at least one natural oil with at least one 2-tert-butyl-4-methyl-phenol compound of formula (I) and subsequently transesterifying the natural oil in the presence of methanol and/or ethanol, is claimed.    R = (3-tert-butyl-2-hydroxy-5-methyl-phenyl)methyl or tert-butyl (preferred).
NOVELTY - Producing biomethane obtained from hydrocarbon charge comprises: gasificating (201) the charge to produce a synthesis gas in a gasification reactor; purifying (204) the synthesis gas of the biomass in a purification unit; methanating (206) the purified synthesis gas in a methanation reactor; and implementing specification (207) of the obtained gas mixture to obtain biomethane, where, during the step of specification, at least a flow composed of excess carbon monoxide is recycled (208) to the gasification reactor.    USE - The method is useful for producing biomethane (claimed) from biomass including wood residues such as chips, sawdust and bark, plant residues such as peels, seeds, stems, cereals and wheat, agricultural sector residues, agroalimentary waste such as grease and slaughterhouse waste, animal wastes such as manure, and human waste (drainage) and marine algae.    ADVANTAGE - The method produces biomethane in high yield and high purity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for producing biomethane comprising the gasification reactor, the purification unit, the methanation reactor and means for setting specifications of the gas mixture obtained in the step of methanation of synthesis gas.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a process for producing biomethane.    Gasificating charge (201)    Purifying synthesis gas (204)    Methanating purified synthesis gas (206)    Implementing specification (207)    Recycling excess carbon monoxide. (208)
NOVELTY - An organic fertilizer comprises household garbage as raw material and corn.    USE - Organic fertilizer.    ADVANTAGE - The organic fertilizer is prepared in an eco-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing organic fertilizer which involves crushing and drying raw material, adding water, stirring uniformly, heating to 40 degrees C, warming, raising temperature to 60-70 degrees C for 10-12 days, decomposing resultant product for 3-5 days, pelleting, polishing and drying to obtain finished product.
NOVELTY - The system has a reaction tank body provided with a thermal insulating sleeve. A drive unit is provided with a heating device. A multi-functional reaction tank is arranged on a top cover of a cylinder body that is divided into an additive feeding port a liquid discharge opening port. The liquid discharge opening port is arranged at a bottom part of the multi-functional reaction tank. An upper end of the cylinder body is installed with an air inlet pipe and an air outlet pipe.    USE - Household waste/mud and water recycling and treating system.    ADVANTAGE - The system recycles waste or mud and water to produce a solid waste liquid fuel and makes solid waste liquid fuel temperature to reach 800 to 1000 degrees or 1000 to 1500 degrees, and is inexpensive and environment-friendly.
NOVELTY - The system has a septic tank and a homogeneous tank connected with an anaerobic fermenting device. The anaerobic fermenting device is provided with an anaerobic up flow blanket filter (UBF) composite reactor. The anaerobic fermenting device is respectively connected with a sedimentation tank, a marsh gas purifying device and marsh gas generating device.    USE - Marsh gas engineering biogas excrement processing system.    ADVANTAGE - The system avoids environment pollution, and has economic and social benefits.
NOVELTY - A biomass powder fuel preparation method involves utilizing peony bean pod and seed coat under mechanical process.    USE - Method for preparing biomass powder fuel.    ADVANTAGE - The method enables preparing biomass powder fuel with reduced energy consumption and better economic benefit and social benefit in a simple manner.
NOVELTY - The controller has a blower control circuit provided with a controllable silicon and a photo-electric isolation chip. An electromagnetic valve control circuit is provided with the photo-electric isolation chip, a relay and a keyboard module. A state indicating module and an alarm module are connected with a single chip. A blower is connected with the blower control circuit and a domestic biomass gasification furnace that is connected with the electromagnetic valve control circuit.    USE - House-hold intelligent biomass ignition gasification furnace controller.    ADVANTAGE - The controller is convenient to operate, and realizes biomass ignition gasification process in an effective manner.
NOVELTY - Straw marsh gas fermentation floating shell breaking device comprises a material liquid return-flow system and a stirring system, where the material liquid return-flow system comprises a drain groove, a liquid circulating pipe and negative pressure outlet port. The drain groove and the liquid circulating pipe are connected, and the negative pressure outlet port and the liquid circulation pipe are connected via a straight pipe. The stirring system comprises a fixed support, motor and transmission rod connected to a stirring blade. The motor is fixed by the fixing frame.    USE - Used as a straw marsh gas fermentation floating shell breaking device.
NOVELTY - A biomass granular fuel is obtained by crushing 40-65 %mass straws and 20-40 %mass corncobs into powder, uniformly mixing powder with 10-25 %mass coal dust, 1-6 %mass yellow mud and 0.1-1 %mass water, drying, compressing, screening, cooling and packaging.    USE - Biomass granular fuel (claimed).    ADVANTAGE - The biomass granular fuel has high calorific value, low melting point and excellent permeability. The utilization rate of heat energy of biomass granular fuel is improved. The biomass granular fuel is completely combusted.
NOVELTY - A biomass raw material is pulverized primarily to obtain coarse material. The coarse material is pulverized secondarily to obtain fine material. Coal powder and/or additives are mixed evenly with fine material to obtain hardened raw material. The hardened raw material is subjected to solid-molding process to obtain molded fuel. Thus, biomass solid molded fuel is processed.    USE - Processing of biomass solid molded fuel (claimed).    ADVANTAGE - The biomass solid molded fuel is stably processed with high productivity, reduced energy consumption, and high degree of automation.
NOVELTY - Biodiesel oil has fatty acid methyl ester content of more than 63%, a glycerol monofatty acid ester content of less than 25%, a diglyceride fatty acid ester content of less than 10%, and a triglyceride fatty acid ester content of less than 2%.    USE - Biodiesel oil is used for coal floatation.    ADVANTAGE - The biodiesel oil uses waste oil, which reduces production cost of flotation agent and provides nontoxic and safe biodiesel oil having excellent biodegradability. The biodiesel oil is environmentally-friendly and efficient.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biodiesel oil, which involves esterifying waste oil as raw material to obtain biodiesel oil by catalyzing using a mesoporous solid superacid catalyst. Methanol and waste oil are stirred in an intermittent reaction kettle in a molar ratio of 10-20:1, and 5-10% solid superacid catalyst is added. The contents are reacted at 120-200 degrees C and 0.1-6.5 MPa for 5-3 hours, the catalyst is filtered, and the reaction mixture is allowed to stand and layered. The upper solution and catalyst are added to reaction kettle, and water is added and reacted at 150-200 degrees C and 0.5-4 MPa for 0.5-1 hour. The catalyst is filtered, and the mixture is allowed to stand and layered. The upper liquid is obtained as biodiesel.
NOVELTY - An organic fertilizer comprises 32.12-34.6 wt.% biological carbon, 62.83-64.12 wt.% fermented organic substance, and 2.28-5.05 wt.% trace element.    USE - Organic fertilizer used for crops.    ADVANTAGE - The organic fertilizer has improved fertilizer utilization rate and improved absorption of trace elements on crops, reduces tobacco planting area ambient pressure, and enhances crop yield and quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the organic fertilizer, comprising preparing biological carbon by putting flue-cured tobacco straw into a vacuum carbonization kiln, heating, carbonizing and calcining at 400-800 degrees C for 4-6 hours, then cooling, drying, and crushing to particle diameter of 0.5-0.8 mm; mixing the biological carbon with fermented organic substance and trace element, and blending at negative pressure; and granulating mixture by drum granulator at material temperature of 60-65 degrees C, and discharging fertilizer having diameter of 2-3 mm and drying to water content of 3% to obtain finished fertilizer product.
NOVELTY - A fermented biological fertilizer comprises 50-70 wt.% wheat bran, 6-18 wt.% black humic acid, 4-7 wt.% humic acid, 4-8 wt.% fulvic acid, and 16-20 wt.% ulmic acid.    USE - Fermented biological fertilizer used for promoting plant growth and improving soil condition.    ADVANTAGE - The biological fertilizer is environmental-friendly, can improve autoimmune mechanism of plant and inhibit bacterial growth in the soil, provides nitrogen source to ensure enough and not excessive nitrogen supply. Further, the wheat bran in the fertilizer can bond the components together, so that when the fertilizer is applied to the soil, the nitrogen-containing material is slowly released and not lost to pollute water and the soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the biological fertilizer, comprising adding fermentation bacteria into a bran to culture, then cooling and drying cultured bran till water content is 8-11% at normal temperature; mixing the raw materials according to ratio and adjusting pH value of mixture to 7-7.2; and putting mixture in a culture box, at controlled temperature of culture box of 50-60 degrees C, ventilating with right amount of oxygen and fermenting for 50-70 hours in shade, and drying, checking quality and packaging.
NOVELTY - A bioparticle fuel is prepared by slicing the combustible raw material, crushing the combustible raw material to 1-30 meshes, drying the resultant crushed raw material in a drying machine to humidity of less than 15%, pressing to obtain particles, cooling the obtained particles in a cooling tank, screening to diameter of 0.5-2 mm, and packaging the resultant material.    USE - Bioparticle fuel (claimed).    ADVANTAGE - The bioparticle fuel is economically and safely prepared in a short period of time, with reduced environmental pollution.
NOVELTY - Urine resource and energy processing device comprises an urine storage tank, a photobioreactor, a biogas fermentation device and a gas storage tank. The urine storage tank is connected with the photobioreactor, which in turn is connected with a biogas fermentation tank. The biogas slurry outlet of the biogas fermentation tank is connected with the photobioreactor. The biogas outlet of the biogas fermentation tank is connected with the gas storage tank.    USE - Used as an urine resource and energy processing device.    ADVANTAGE - The device can simultaneously process waste and generate energy, is simple in structure, economical and easy to manufacture and install, and can transform urine, manure and other waste materials into energy and resource.
NOVELTY - A traditional Chinese medicine material plant disinfectant solution is prepared by dissolving 5-10 g borneol into 10-15 ml ethanol; adding 10-15 g alum and 5-8 g iodine into 10-20 ml water to dissolve, and adding obtained solution to the borneol ethanol solution to obtain mixed solution; and adding 75-90 g Angelica, 70-90 g mint, 100-120 g radix arnebiae seu lithospermi, 100-120 g Gentiana scabra and 120-140 g herba schizonepetae into 2000 ml water to boil, distilling, and adding the distillate to the mixed solution.    USE - Method of preparing traditional Chinese medicine material plant disinfectant solution (claimed) used for preventing and treating tomato downy mildew and cucumber rot disease.    ADVANTAGE - The method can obtain disinfectant solution that is non-toxic and safe to human and livestock, does no harm to plants, and has no wastewater discharge. Further, the ecological environment is protected and the cost is greatly lowered than biological pesticide.
NOVELTY - Biological organic fertilizer is produced using water sediments by carrying out solid-liquid separation on water sediments to obtain material II; preparing a strain for production of organic fertilizer by microbial screening and purifying and using strain as seed, and preparing a biological agent by aerobic fermentation; mixing the material II with crop straws, and carrying out aerobic fermentation; and sterilizing, drying and crushing aerobic fermentation product and adjusting carbon-nitrogen ratio, and then adding the biological agent.    USE - Method of producing biological organic fertilizer using water sediments (claimed).    ADVANTAGE - The method utilizes water sediments excavated from lake and wetland to produce the fertilizer, so that internal water source pollution can be treated and water body and the ecological environment can be recovered. Thus, resources are efficiently utilized.
NOVELTY - Producing straw fermentation bio-additive by solid fermentation comprises split charging the solid medium in wide-mouth bottles after uniformly mixing, where the solid medium comprises water, bean pulp powder, wheat bran powder, sucrose, and urea; inoculating the mixed cultivated liquid strain; and static fermenting.    USE - The method is used for producing straw fermentation bio-additive. The bio-additive is used for water purification by rapidly reducing the nitrite content and pH value in water (all claimed).    ADVANTAGE - The preparation method above is low cost, and provides straw fermentation bio-additive with improved quality and effectiveness.    DETAILED DESCRIPTION - Producing straw fermentation bio-additive by solid fermentation comprises (a) split charging the solid medium in wide-mouth bottles after uniformly mixing; sterilizing for 15-20 minutes at 121 degrees C, where the solid medium comprises water, bean pulp powder, wheat bran powder, sucrose, and urea at a ratio of 400:200:200:10:5; (b) inoculating the mixed cultivated liquid strain according to 10-20% of bacterium amount; static fermenting for 48-72 hours in constant temperature incubator at 35 degrees C; and (c) naturally airing for 5 days at 20-35 degrees C; the microbial content can reach to 700 x 108 per gram; the liquid strain is straw fermentation bioadditive.
NOVELTY - A hydrotreating method involves selecting biological oil and fat as raw oil. The raw oil and hydrogen pass through two reduced hydrogenation catalyst layers, where the raw oil and hydrogen are introduced into bottom of a reactor. Effluent after the reaction from top of the reactor is discharged, and the effluent after the reaction into a gas phase and a liquid phase is separated. The gas phase is used circularly, and the liquid phase is introduced into a fractionating tower to obtain naphtha, diesel oil and unconverted oil.    USE - Hydrotreating method for producing motor fuels.    ADVANTAGE - The method enables guaranteeing that a hydrogenation apparatus of the biological oil and fat runs stably in long period.    DETAILED DESCRIPTION - A hydrotreating method involves selecting biological oil and fat as raw oil. The raw oil and hydrogen pass through two reduced hydrogenation catalyst layers, which have increased content of a hydrogenation active component in sequence, where the raw oil and hydrogen are introduced into bottom of a reactor, and pass through the reduced hydrogenation catalyst layer with low content of the hydrogenation active component and through the reduced hydrogenation catalyst layer with high content of the hydrogenation active component. Effluent after the reaction from the top of the reactor is discharged, and the effluent after the reaction into a gas phase and a liquid phase is separated. The gas phase is used circularly, and the liquid phase is introduced into a fractionating tower for fractionation to obtain naphtha, diesel oil and unconverted oil, where the diesel oil and/or partial of the unconverted oil are returned to the reaction system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a hydrotreating method for producing motor fuels. '(Drawing includes non-English language text)'
NOVELTY - A hydrogenation method involves selecting biological oil and fat as raw oil. The raw oil and hydrogen are successively passed through reduced hydrogenation catalyst layers that have increasing content of a hydrogenation active component in sequence. The reaction materials are passed through the reduced hydrogenation catalyst layer with low or high content of the hydrogenation active component. The hydrogenation reaction products are separated, and sulfur-containing substances are supplemented in the reaction material flow to maintain the content of hydrogen sulfide in circulation gas.    USE - Hydrogenation method for producing motor fuel.    DETAILED DESCRIPTION - A hydrogenation method involves selecting biological oil and fat as raw oil. The raw oil and hydrogen are successively passed through reduced hydrogenation catalyst layers that have increasing content of a hydrogenation active component in sequence, where the raw oil and hydrogen are introduced from the bottom of a reactor. The reaction materials are passed through the reduced hydrogenation catalyst layer with low or high content of the hydrogenation active component, where the hydrogenation active component is sulfide, tungsten, molybdenum, nickel and cobalt. The hydrogenation reaction products are separated, and sulfur-containing substances are supplemented in the reaction material flow to maintain the content of hydrogen sulfide in circulation gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a hydrogenation apparatus for producing motor fuel.
NOVELTY - Biomass pyrolysis system comprises a raw material storage bin, a crushing device, a drying device, dust-removing and desulfurizing device, a draught fan, a chimney, combustible gas tank storage tank, oil storage tank, wood vinegar purification device, an oil-water separating device, an oil-gas separating device, rotary pyrolysis furnace and charcoal storage bin. The material storage bin is connected with the crushing device, which is connected with the drying device. The drying device is connected with the dust-removing and desulfurizing device. The furnace is connected with the drying device.    USE - Used as biomass pyrolysis system.    ADVANTAGE - The device: performs carbonization process with high efficiency of biomass; is capable of continuous feeding and continuous discharging; produces carbon with high rate in short period of time; improves the working environment; achieves industrial production; and consumes low energy.
NOVELTY - Preparation of solid alkali catalyst for biological diesel production, involves: adding mixed solution of calcium nitrate tetrahydrate and aluminum nitrate nonahydrate into distilled water, adding alkali precipitator to the mixed solution and reacting at a certain water bath temperature and magnetic force; filtering the reaction liquid, washing until the filtrate is neutral, and drying to obtain white material; and protecting the white material form nitrogen for a certain temperature to obtain calcium-aluminum composite oxide as solid base catalyst.    USE - In preparation of solid alkali catalyst for biological diesel production (claimed).    ADVANTAGE - The method provides solid alkali catalyst having high specific surface area and strong alkaline strength, has conversion rate of preparing biological diesel oil of more than 95%, and can be used for many times.
NOVELTY - Producing microbial fertilizer comprises mixing bran, corn flour and rice bran, dissolving corn steep liquor, urea, ammonium sulfate, potassium dihydrogen phosphate and magnesium sulfate in water, uniformly mixing with the bran, corn flour and rice bran mixture, controlling the water content to be 60-65%, mixing uniformly, passing steam, cooling to obtain culture medium, inoculating 5 strain seed liquids, where the inoculation amount of each strain is 5%, paving bamboo curtain, sterilizing, stacking to a thickness of 4-6 cm, fermenting, and drying until the water content is below 10%.    USE - The method is useful for producing microbial fertilizer (claimed).    ADVANTAGE - The fertilizer: has low dosage of 0.10.2%; increases the yield of crops; improves the quality of crops; increases crop nutrition; reduces harmful components; resists plant diseases and insect pests; increases the soil fertility; and reduces environmental pollution.    DETAILED DESCRIPTION - Producing microbial fertilizer comprises mixing bran, corn flour and rice bran in a ratio of 80:10:10, dissolving 2% corn steep liquor, 2% urea, 1% ammonium sulfate, 0.1% potassium dihydrogen phosphate, and 0.05% magnesium sulfate in water, uniformly mixing with the bran, corn flour and rice bran mixture, controlling the water content to be 60-65%, mixing uniformly, passing normal atmospheric steam for 1 hour, cooling to 30 degrees C to obtain solid culture medium, inoculating 5 strain seed liquid, where the inoculation quantity of each strain is 5%, uniformly mixing, paving bamboo curtain, sterilizing, stacking to a thickness of 4-6 cm, fermenting for 56-60 hours at 30-32 degrees C, and drying at 45 degrees C until the water content is below 10%.
NOVELTY - The device has a feeding device and a rotary cracking furnace connected with a gas-solid separator. The gas-solid separator is connected with a rectifying tower. The rectifying tower is connected with a built-in condenser. The condenser is connected with another condenser. The latter condenser is connected with a receiving tank. A combustible gas liquid seal tank is connected with the receiving tank and a tail gas combustion device. The tail gas combustion device is connected with the rotary cracking furnace.    USE - Organic wastes cracking and fractionating device.
NOVELTY - Soil infiltration bed process method involves paving an anaerobic groove on artificial soil in which the cross section of anaerobic groove is trapezoidal, filling gravels in the anaerobic groove, paving a water dissipating pipe and punched on the anaerobic groove, paving a layer of cultivated soil on the artificial soil, cultivating a herbaceous plant on the surface of earth, charging the rural domestic waste into the soil infiltration bed through the water dissipating pipe under the power-free condition, and collecting the treated discharged water by the collector pipe.    USE - Soil infiltration bed process method used for treating rural domestic sewage.    ADVANTAGE - The method enables microbial activity in the infiltration region.    DETAILED DESCRIPTION - Soil infiltration bed process method involves surrounding infiltration bed by clay, paving a layer of high-density ethylene film around the bed, paving collector pipe and punched at the bottom of the infiltration bed, paving a layer of gravels around the collector pipe, paving a layer of artificial soil on a frozen earth layer and infiltrating by spraying water for 24 hours, paving an anaerobic groove on the artificial soil in which the cross section of anaerobic groove is trapezoidal, filling gravels in the anaerobic groove, paving a water dissipating pipe and punched on the anaerobic groove, paving a layer of cultivated soil on the artificial soil, cultivating a herbaceous plant on the surface of earth, charging the rural domestic waste into the soil infiltration bed through the water dissipating pipe under the power-free condition, and collecting the treated discharged water by the collector pipe.
NOVELTY - Organic cultivation method, involves at a rice filling stage, utilizing organic fertilizer thoroughly decomposed by fermentation to perform topdressing, placing the organic fertilizer in snakeskin bags according to the quantity of 10 kg per square meters, placing the organic fertilizer at water inlets of rice fields when water is fed to the rice fields, and naturally letting flowing water (to bring the organic fertilizer into the fields).    USE - The organic cultivation method is useful for improving thousand grain weight of rice (claimed).
NOVELTY - Separating alpha -linolenic acid from flaxseed oil comprises placing organic flaxseed into a ultrasonic wave pipe and then extracting at a normal pressure and a temperature of 8-38 degrees C or 25-45 degrees C for 10-30 minutes or 30 minutes to 1 hour and separating alpha -linolenic acid, vitamin E and lignan.    USE - The method is useful for separating alpha -linolenic acid from flaxseed oil (claimed).    ADVANTAGE - The method enables simple separation of alpha -linolenic acid from flaxseed oil with high purity and without chemical residue in a safe manner.
NOVELTY - Biomass particles are mixed with a heat carrier in reactor (I) to form premix (I), which is stirred to obtain solid-liquid mixture (I). Mixture (I) is separated to obtain liquid (I) and a solid. The solid is mixed with heat carrier in reactor (II) to form premix (II). Premix (II) is stirred to form solid-liquid mixture (II). Mixture (II) is separated to obtain liquid (II). Liquids (I,II) are distilled separately or as mixed liquid to obtain a biomass liquid fuel. The biomass particles contain cellulose, hemicellulose and/or lignin.    USE - Production of biomass liquid fuel (claimed).    ADVANTAGE - The method enables production of biomass liquid fuel with high conversion rate, under mild conditions.    DETAILED DESCRIPTION - Biomass particles are mixed with a heat carrier in reactor (I) to form premix (I), which is stirred to obtain solid-liquid mixture (I). Mixture (I) is separated to obtain liquid (I) and a solid. The solid is mixed with heat carrier in reactor (II) to form premix (II). Premix (II) is stirred to form solid-liquid mixture (II). Mixture (II) is separated to obtain liquid (II). Liquids (I,II) are distilled separately or as mixed liquid to obtain a biomass liquid fuel. The biomass particles contain cellulose, hemicellulose and/or lignin. The heat carrier is an organic liquid at 250-350 degrees C and normal pressure, and has a heat capacity of greater than 1.5 kJ/kg degrees C.
NOVELTY - Jatropha bio-jet fuel oil comprises less than 500 ppm phosphorus, less than 16 ppm calcium, less than 8 ppm magnesium, less than 3 ppm iron, and less than 1000 ppm water. It has clear and transparent appearance and color, has acid value of less than 6 mg potassium hydroxide (KOH)/g.    USE - Jatropha bio-jet fuel oil.    ADVANTAGE - The fuel oil has low acid value and moisture content, high quality, low temperature protein denaturation, more reserve active substance. The resulting seed cake has improved nutritional value and high comprehensive utilization. It has simple, easy, and controllable preparation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of Jatropha bio-jet fuel oil by classifying seed endosperm of Jatropha curcas; drying at less than 90 degrees C until water content is 4-10%; cooling at 40 degrees C; shelling; crushing; sorting; controlling shell rate at more than 98% to obtain 2-10% shell; adjusting pH of J. curcas seed at 7-8; adding deionized water until water content is 10-15%; maintaining seed surface at 60-80 degrees C and 12-80 kPa for 40-70 minutes; drying at 90 degrees C until water content is 3-7%; adding dried seed in double-screw cold pressing machine; and pressing at 50-70 degrees C under controlled oil temperature at not greater than 60 degrees C and cake outlet temperature at not greater than 80 degrees C.
NOVELTY - Preparing biomass fuel, comprises (1) preprocessing a plant fiber by diluted acid to produce furfural plant fiber and its derivative, adjusting a pH value of the furfural plant fiber using alkali, carrying out enzymolysis using cellulose to produce sugar, (2) culturing furfural degrading bacterium in an inclined surface of a liquid culture medium, and centrifuging and collecting cell precipitate, and (3) adding the dilute acid-cellulose in the enzymolysis sugar solution to configure growth factor of the furfural degrading bacterium in the liquid culture medium.    USE - The method is useful for preparing biomass fuel using furfural degradation.    ADVANTAGE - The method economically and eco-friendly prepares the biomass fuel with improved degradation efficiency.    DETAILED DESCRIPTION - Preparing biomass fuel using furfural degradation, comprises (1) preprocessing a plant fiber by diluted acid to produce furfural plant fiber and its derivatives, adjusting a pH value of the furfural plant fiber using alkali, carrying out enzymolysis using cellulose to produce sugar, (2) culturing furfural degrading bacterium in an inclined surface of a liquid culture medium, and centrifuging and collecting cell precipitate, (3) adding the dilute acid-cellulose in the enzymolysis sugar solution containing inorganic salt to configure growth factor of the furfural degrading bacterium in the liquid culture medium, inoculating the obtained furfural degrading bacteria and Saccharomyces cerevisiae having weight ratio of 1:2-5 in the liquid culture medium to prepare biomass fuel and degrade furfural.
NOVELTY - A methanol synthesis vehicle cleaning gasoline is prepared from clean gasoline including 15-25 wt.% methanol, 10-20 wt.% hydrogenated 9C aromatic hydrocarbon, 3-5 wt.% isopropyl ether, 3-6 wt.% petroleum ether, 2-4 wt.% synergistic stabilizer, 0.05-1 wt.% antioxidant anti-adhesive agent, and 0.05-1 wt.% national standard gasoline.    USE - A methanol synthesis vehicle cleaning gasoline.    ADVANTAGE - The gasoline does not need to do any modification of an automobile engine, and can save energy and reduces harmful exhaust.
NOVELTY - A methanol gasoline speed solvent comprises aromatic ketone, alkaryl ether and alicyclic alcohol at wt. ratio of 1:1-0.7:2-3.5.    USE - Methanol gasoline speed solvent.    ADVANTAGE - The solvent improves gasoline and methanol compatibility without risk of stratification.
NOVELTY - A lead-free fuel oil solvent comprises 2-4 wt.% methanol and 96-9 8 wt.% gasoline additive.    USE - Fuel oil solvent.    ADVANTAGE - The solvent has reduced cost, improves quality of original product, reduces oil consumption by 15-20%, reduces total harmful gas of exhaust gas exhaust by more than 60% compared with common gasoline, and is energy-saving and environment-friendly.
NOVELTY - Biomass coal forming system comprises biomass input system, conveyer belt system, blast and predicting optimizing control module; biomass input system connected with transmission belt system provided with modifying agent control unit, provided with heating system between conveyer belt system and blast furnace, predicting optimization control module through signal line and biomass input system, conveyer belt system, heating system, modifying agent control unit, connected with blast furnace.    USE - Biomass coal forming system.    ADVANTAGE - The system greatly improves heat efficiency by 30-50%, has reduced control system, and reduces dust slag discharge.    DESCRIPTION OF DRAWING(S) - The drawing shows a plan view of the biomass coal forming system.
NOVELTY - A sludge synthetic fuel comprises 10-90 wt.% sludge, 1-81 wt.% combustion improver, and the rest is heat value improving agent.    USE - Sludge synthetic fuel.    ADVANTAGE - The sludge synthetic fuel has high heat value, low cost, and excellent combustion condition and environmental performance. The addition of coal powder can further improve sludge heat value.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing sludge synthetic fuel comprising mixing sludge, combustion improver, heat value improving agent according to proportion in any order successively or at the same time; or carrying out mechanical dehydration from sludge water content of 75-98% to less than 75% water content, then adding combustion improver, heat value promoting agent according to proportion, mixing uniformly; or drying and dehydrating or dehydrating sludge water content of 75-98% with combustion improver and heat value improving agent and mixing uniformly according to proportion.
NOVELTY - Preparation of biological oil from algal cell comprises crushing algal cell, centrifuging, performing first stage liquid-liquid extraction using n-hexane-ethyl acetate mixed organic solvent, collecting aqueous phase and organic phase, performing second stage liquid-liquid extraction of aqueous phase using solvent, collecting aqueous phase and organic phase, performing third stage liquid-liquid extraction of aqueous phase using solvent, collecting aqueous phase and organic phase, combining collected organic phase and vacuum-evaporating to remove solvent.    USE - The biological oil is used for preparing biodiesel (claimed).    ADVANTAGE - The biodiesel produced from the biological oil meets the national GB/T20828-2007 diesel engine fuel biodiesel for blending with biodiesel (BD100) standard.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biodiesel from algal cell biological oil comprising adding 2 mol/L methanol-potassium hydroxide solution into algal cell biological oil at oil to solution mass ratio of 1:10-20, esterifying while stirring at 2800 revolutions/minute for 2 minutes and standing to obtain layers, where the upper layer is the biodiesel.
NOVELTY - A solid alkali catalytic film comprises ceramic membrane as carrier, load-type hydrotalcite and hydrotalcite-like solid base as active component and is prepared by in situ growth method. The ceramic film is composed of support and separation membrane coated on support. The separation membrane is made of alpha -alumina, titania, zirconia and silicon carbide, and has aperture size of 0.01-10 mu m. The load-type hydrotalcite is loaded using potassium fluoride, sodium fluoride, sodium carbide, potassium carbide, zinc fluoride and/or alkaline-earth metal.    USE - Solid alkali catalytic film is used for catalytic membrane reactor for producing biodiesel.    ADVANTAGE - The solid alkali catalytic film has high durability and catalytic activity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of solid alkali catalytic film, which involves preparing hydrotalcite precursor salt solution containing hydrotalcite having metal ion concentration of 0.1-0.4M, immersing ceramic membrane in the solution, heating at 60-100 degrees C, cooling, removing the ceramic membrane, washing until neutral, calcining and cooling.
NOVELTY - Method for preparing biopesticide using kitchen waste, involves (a) steaming and boiling kitchen waste, sterilizing the kitchen waste, separating oil from the kitchen waste, pressing and stewing the kitchen waste, crushing the kitchen waste to obtain residue and oil-water mixture, processing the residue and oil-water mixture to obtain biodiesel, liquid and chemical raw material, concentrating the liquid, and sterilizing the concentrated liquid at high temperature, and (b) adding bacterial strain to the sterilized liquid, and fermenting the mixture.    USE - The method is useful for preparing biopesticide using kitchen waste (claimed).    DETAILED DESCRIPTION - Method for preparing biopesticide using kitchen waste, involves (a) processing kitchen waste by steaming and boiling kitchen waste, sterilizing the kitchen waste, separating oil from the kitchen waste, pressing the kitchen waste, stewing the kitchen waste, crushing the kitchen waste to obtain residue and oil-water mixture, processing the residue and oil-water mixture, using the residue as insect feed, mechanically separating oil-water mixture with horizontal three-phase separator to obtain oil, liquid and residue, combining the residue with the obtained residue of the step (b), then mechanically separating oil-water mixture with the horizontal three-phase separator to obtain biodiesel, liquid and chemical raw material, concentrating the liquid, and sterilizing at high temperature, and (b) preparing biopesticide by adding bacterial strain to the sterilized liquid, and fermenting the mixture, where the strain includes Bacillus thuringiensis.
NOVELTY - Amino acid is produced from kitchen waste by pressing and steaming kitchen waste material to obtain slag and oil-water mixture, mechanically separating oil slag using horizontal 3-phase separator to obtain grease, separating with vertical oil-water separator to obtain bio-oil as biological diesel oil and chemical raw material, cooking liquor to high concentration, hydrolyzing protein into amino acid by adding protein hydrolase in cooking liquor and adding hydrochloric acid, and sterilizing amino acid concentrated liquor.    USE - Amino acid production from kitchen waste (claimed).    ADVANTAGE - Energy consumption is low, and process is environment-friendly.
NOVELTY - Preparation of a polyaniline loaded sulfuric acid solid acid catalyst comprises dropwise adding ammonium persulfate solution in sulfuric acid to obtain an aniline sulfate solution, low-temperature stirring, standing, filtering, washing the solid with acetone, and drying.    USE - Method for the preparation of a polyaniline loaded sulfuric acid solid acid catalyst used in preparing biodiesel oil from waste cooking oil (claimed).    ADVANTAGE - The method is simple, uses easily obtained raw material, has short reaction time, and achieves high product yield and high catalyst activity. The catalyst can be used repeatedly for many times, and does not need neutralizing and washing. The catalytic activity is not changed. The method does not generate waste acid and waste alkali, does not corrode the device, prevents environment pollution, has convenient processing, and is inexpensive.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a polyaniline loaded sulfuric acid solid acid catalyst; and    (2) preparing biodiesel by carrying out ester exchange reaction of polyaniline loaded sulfuric acid solid acid catalyst, waste cooking oil, and methanol at 70-85 degrees C for 3-6 hours; centrifuging to separate catalyst; separating, and evaporating methanol to obtain glycerin as lower layer and crude biological diesel oil as upper layer; and decompressing and distilling methanol, where the mass ratio of waste cooking oil and methanol is 1:0.25-0.45, the catalyst dosage is 0.25-0.4% of raw material total weight.
NOVELTY - Preparing 2'-deoxyuridine by chemical-bio-enzyme combined method comprises using 2'-deoxyuridine crystallization induced asymmetric transformation method to obtain single (alpha) configuration nucleoside medicine intermediate 2-deoxy-alpha-D-1-phosphoric acid; using the intermediate substrate; and adding uracil to obtain uridine phosphorylase under biotransformation.    USE - The method is used for preparing 2'-deoxyuridine by chemical-bio-enzyme combined method (claimed).    ADVANTAGE - The method above provides 2'-deoxyuridine with high yield, is highly-efficient and environment-friendly, and has high specificity, high conversion rate, and mild reaction condition.
NOVELTY - Microbial organic fertilizer comprises 60-66 parts urea, 53-70 parts calcium superphosphate, 45-50 parts potassium sulfate, 480-525 parts animal manure, 30-40 parts Bacillus subtilis solution, and 0.03-0.11 parts inorganic fertilizer additive.    USE - The microbial organic fertilizer is useful for preventing and/or treating southern blight of H.cordata (claimed).    ADVANTAGE - The microbial organic fertilizer is rich in nutrition, meets growth needs of H.cordata, improves yield and quality of H.cordata and soil fertility, reduces environmental pollution, and has improved pertinence and specificity of fertilizer in use and wide application prospect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing microbial organic fertilizer, which involves taking the livestock and poultry manure, crushing the mixture, fermenting the crushed mixture, adding urea, calcium superphosphate, potassium sulfate, B.subtilis solution, and inorganic fertilizer additive to the poultry mixture, and extruding and granulating the mixture.
NOVELTY - Method for producing organic fertilizer using pig manure and straws, involves preparing raw materials, adding and mixing bacteria, composting and fermenting the mixture, and checking and finishing the product.    USE - The method is useful for producing organic fertilizer using pig manure and straws (claimed).    ADVANTAGE - The method simply and feasibly converts lot of crop straws into beneficial products, is suitable for popularization in rural areas, and effectively improves farmland soil structure and soil biological activity.
NOVELTY - Organic fertilizer comprises 1000-1200 kg raw vegetables, 5-8 kg probiotic liquid, 10-15 kg bean cakes and 10-15 kg urea.    USE - The organic fertilizer is useful for controlling diseases and pests and improving crop growth.    ADVANTAGE - The organic fertilizer is prepared simply and conveniently, and improves environment and pH value of soil.
NOVELTY - Biological agent comprises 32 wt.% Rhodococcus sp., 20 wt.% Bacillus subtilis, 10 wt.% Pesudomonas aeruginosa, 10 wt.% Saccharomyces cerevisiae, 10 wt.% nitrosobacteria, 8 wt.% Bacillus megaterium, 5 wt.% Aspergillus niger and 5 wt.% Paracoccus denitrificans.    USE - The agent is useful for treating industrial sewage (claimed).    ADVANTAGE - The biological agent has synergistic agent, and degrades macromolecular toxic and harmful substances which are hardly degraded, such as phenols, aromatic hydrocarbons, ammonia nitrogen and phosphorus and hence has unique effect of processing high-concentration organic sewage and high-ammonia nitrogen sewage which are hardly processed by existing activated sludge process.
NOVELTY - Anaerobic hydrolysis reaction of sludge of sewage treatment plant is carried out in anaerobic pool, and introduced into aeration tank for aerobic reaction. Material is processed in denitrification reaction tank, and then further processed to reach water quality standard. Water is supplied to municipal sewage pipe system, and then returned to anaerobic tank. Processes are repeated, and active sludge is produced during processing. Active sludge is used as fertilizer, building material and soil modifying agent. Thus, processing of sludge of sewage treatment plant is enabled.    USE - Processing of sludge of sewage treatment plant.    ADVANTAGE - The sludge is efficiently and economically processed without affecting the environment.
NOVELTY - Preparing high purity sclareolide, comprises performing aldol condensation of beta-ionone to obtain acetaldehyde, hydrogenating and condensing the acetaldehyde to obtain alkene nitrile, hydrolyzing the alkene nitrile to obtain tert-butyl 1-methyl-1-(isopropylphenyl)ethyl peroxide, cyclizing obtained tert-butyl 1-methyl-1-(isopropylphenyl)ethyl peroxide at low temperature to obtain sclareolide, and distilling and purifying obtained product to get high purity sclareolide.    USE - The process is useful for preparing sclareolide (claimed), which is useful in fields of medical, pharmaceutical, food, perfume and cosmetics.    ADVANTAGE - The process allows simple and economical preparation of the sclareolide with high purity (98%) and improved yield (more than 100 ton) in an eco-friendly manner.
NOVELTY - Double-sided coating composite electrode electrolysis tank comprises titanium metal substrate with surface that is attached with a chlorine electrode layer by thermal decomposition process, and other surface attached with a hydrogen electrode layer by plating technique.    USE - Double-sided coating composite electrode electrolysis tank.    ADVANTAGE - The electrolytic tank has simple structure, increased resistance, and long service life, and saves the material.
NOVELTY - Preparation of biomass city waste gas comprises providing two sets of furnace sections of the same structure, where two furnace sections are adjacent parallel to each other and vertical to the ground, each furnace section is provided with a valve connected to gas pipeline and double-layer fire grate and upper fire grate is residual carbon fire grate; and steam heating to prepare pure oxygen or oxygen-enriched air as gasification agent, and gasification and cracking the residual reaction heat generated raw material gas and furnace gas at high temperature.    USE - Preparation of biomass city waste gas (claimed).    ADVANTAGE - The method does not use external heat source for high temperature cracking of biomass.    DETAILED DESCRIPTION - Preparation of biomass city waste gas comprises:    (A) providing two sets of furnace sections of the same structure, where two furnace sections are adjacent to each other and parallel vertical to the ground, each furnace section is provided with a valve connected to gas pipeline and double-layer fire grate, upper fire grate is residual carbon fire grate, the lower layer of gas manufacturing furnace is provided with refractory heat storage section, the upper part of the furnace section has air outlet filter, two control valves of the gas pipe are respectively connected with the lower part of the lower furnace from the gas blower outlet, the biomass waste is continuously or intermittently provided as raw material from the furnace top; and    (B) steam heating to prepare pure oxygen or oxygen-enriched air as gasification agent, and gasification and cracking the residual reaction heat generated raw material gas and furnace gas from furnace bottom at high temperature i.e. 950-1050 degrees C.
NOVELTY - Production of active carbon and gas using Eupatorium adenophorum comprises drying E. adenophorum; heating to 500-700 degrees C at 10-50 degrees C/minute to carbonize for 1-3 hours; crushing the carbonized material to 30-50 mesh; heating to 620-700 degrees C at 30-45 degrees C/minute; maintaining temperature for 5-10 minutes; heating to 900-1000 degrees C at 10 plus minus 5 degrees C/minute; activating by charging carbon dioxide to obtain active carbon product and gas; cooling the active carbon product to room temperature under air isolation protection; and drying.    USE - Production of active carbon and gas using E. adenophorum (claimed), where gas is used as fuel gas.    ADVANTAGE - The method provides active carbon having iodine adsorption capacity that reaches the national level I standard and good adsorption performance; and gas having calorific value of 11000-13000 KJ/m3 and main components of acetylene (C2H2), H2, CH4, and carbon monoxide. It has short activation period; provides no pollution; realizes high resource comprehensive utilization; achieves high value-added products; and fully uses E. adenophorum for converting into biomass energy product.    DETAILED DESCRIPTION - Production of active carbon and gas using E. adenophorum comprises drying E. adenophorum; heating to 500-700 degrees C at 10-50 degrees C/minute to carbonize for 1-3 hours; crushing the carbonized material to 30-50 mesh; heating to 620-700 degrees C at 30-45 degrees C/minute; maintaining temperature for 5-10 minutes; heating to 900-1000 degrees C at 10 plus minus 5 degrees C/minute; activating by charging carbon dioxide for 60-150 minutes at 50-90 L/kg.minute to obtain active carbon product and gas; cooling the active carbon product to room temperature under air isolation protection; and drying at 100-120 degrees C for 2-3 hours to obtain the active carbon product.
NOVELTY - The processing device has a centrifugal solid-liquid separation unit (7) that is connected with a liquid outlet of a pressurizing water tank (3). The pressurizing water tank is connected with inlet of an oil-water separating unit. The separating barrel, oil pipe and oil outlet pipe of oil-water separating unit are connected with oil pump connected with inlet end of air outlet pipe. A waste water outlet is connected with separating barrel through water pump. A sediment outlet is located at bottom of separating barrel and is connected to opening of a garbage barrel (4).    USE - Food garbage processing device.    ADVANTAGE - The pressure in the water system can be reduced effectively and the energy utilization rate can be increased efficiently so that the protection to the environment can be ensured favorably.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the food garbage processing device.    Pouring pool (1)    Food grinder (2)    Pressurizing water tank (3)    Garbage barrel (4)    Centrifugal solid-liquid separation unit (7)
NOVELTY - Butan-1-amine, hypophosphorous acid and acetone are reacted to obtain butafosfan.    USE - Preparation of butafosfan used as metabolic accelerator.    ADVANTAGE - The method enables economical preparation of butafosfan with yield of 90%, without environmental pollution.
NOVELTY - The equipment has a material tank (1) of waste cooking oil, which is connected with dehydration vacuum oil-filter (2). The dehydration vacuum oil-filter is connected with transition tank (3) connected with reaction portion (4). The drug feeding device is installed on the reaction portion. The heater (7) and temperature sensor (8) are connected with controller (9).    USE - Equipment for transforming waste cooking oil to biodiesel.    ADVANTAGE - Continuous production of biodiesel can be ensured with high production efficiency and simple manufacturing process.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of equipment for transforming waste cooking oil to biodiesel.    Material tank (1)    Dehydration vacuum oil-filter (2)    Transition tank (3)    Reaction portion (4)    Heater (7)    Temperature sensor (8)    Controller (9)
NOVELTY - A continuous aerobic fast carbonization process of crop straw comprises drying after cutting straw, putting the carbonizing reactor and performing carbonization reaction, cooling, and carbon discharging at lower than 80 degrees C. The ratio of feeding speed and rate of carbon discharging is 2.5-5:1 kg/hour. Carbonizing reaction is carried out at 350-550 degrees C and - 8 to - 1 KPa for 20-40 minutes.    USE - Continuous aerobic fast carbonization process of crop straw.    ADVANTAGE - The process has 50% reduction of energy consumption as compared with traditional technology, realizes continuous industrial production, and has high production efficiency. Charring period is shortened to 0.5-1 hour.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating a continuous aerobic fast carbonization process of crop straw.
NOVELTY - A hydrogen chloride gas is prepared from hydrochloric acid solution by preparing extracting agent using neutral phosphorus organic material of amino acids as complexing agent, and mixing and stirring, a volume fraction of the complexing agent and diluting agent being 10-100%; extracting hydrochloric acid aqueous solution (0.02-50%) under normal temperature and normal pressure condition, and separating extracting agent to obtain extracting agent; and dehydrating the extracting agent phase by hot air bubble or rectification method, and releasing hydrogen chloride gas by multistage distillation.    USE - Method for preparing hydrogen chloride gas from the hydrochloric acid solution (claimed).    ADVANTAGE - The method is simple and uses extracting agent that can be easily separated from the organic phase.
NOVELTY - Preparation of titanium tungsten powder for forming selective catalytic reduction (SCR) denitration catalyst involves preparing titanium pigment with sulfuric acid using metatitanic acid as raw material, pulping, dispersing, filtering, cutting it into blocks, calcining and crushing to prepare the titanium-tungsten powder.    USE - In the preparation of titanium tungsten powder used for forming selective catalytic reduction (SCR) denitration catalyst (claimed). The powder is also used in coating, paint, paper, rubber, food, medicine and so on.    ADVANTAGE - Compared with the existing technology, the method forms powder having high flue gas denitration efficiency. The product and the technique are reliable. The product is stable, has improved quality, relatively lows cost, and greatly reduces manufacturing cost of denitration catalyst. The method is environment-friendly. The price of the metatitanic acid is low and is widely available thereby reducing production cost. The production process causes little pollution to the environment and at the same time improves technology content of normal titanium pigment, promotes industry upgrading, and widens the industrial chain of environmental protection.
NOVELTY - Variable-frequency-vacuum microwave pre-treatment of alcohol fuel raw material, comprises: (a) drying matrix powder in an oven at 60-80 degrees C to constant weight, and crushing the dried matrix powder into powder; (b) adding distilled water into the powder to obtain a mixture, where the solid-to-liquid ratio is 1:(5-20); (c) carrying out vacuum microwave treatment of the mixture in a microwave processor at 70-80 degrees C, under the absolute pressure of 0.3-0.7 atm for once with a time interval of 1-2 minutes, and processing for 5 times for 1-2 minutes (each time) to complete the pre-processing.    USE - The method is useful for variable-frequency-vacuum microwave pre-treatment of alcohol fuel raw material.    ADVANTAGE - The method solves the problem of high cost involved in the existing alcohol fuel raw material microwave pretreatment method, and produces an intermediate product with high inhibitory action on cellulase and Saccharomyces cerevisiae, which affects the glucose conversion rate and ethanol yield.    DETAILED DESCRIPTION - Variable-frequency-vacuum microwave pre-treatment of alcohol fuel raw material, comprises: (a) drying matrix powder in an oven at 60-80 degrees C to constant weight, and crushing the dried matrix powder (5-10 g) into powder of particles less than 40 meshes; (b) adding distilled water into the powder to obtain a mixture of distilled water and the powder, where the solid-to-liquid ratio is 1:(5-20); and (c) carrying out vacuum microwave treatment of the mixture in a microwave processor at 70-80 degrees C under the absolute pressure of 0.3-0.7 atm for once with a time interval of 1-2 minutes, and processing for 5 times for 1-2 minutes (each time) to complete the pre-processing of alcohol fuel raw material.
NOVELTY - Synthesizing dutasteride intermediate (I) comprises dissolving (4aR,4bS,6aS,7S,9aS,9bS)-4a,6a-dimethyl-2-oxo-tetradecahydro-1H-indeno(5,4-f)quinoline-7-carboxylic acid (2,5-bis-trifluoromethyl-phenyl)-amide in an organic solvent, stirring mixture and slowly adding sodium cyanoborohydride as reducing agent, carrying out hydrogenation reaction, extracting organic layer using dichloromethane, drying organic layer using anhydrous magnesium sulfate and then filtering.    USE - (I) is useful for treating prostatic hyperplasia.    ADVANTAGE - The process provides (I) with high yield in an eco-friendly manner.    DETAILED DESCRIPTION - Synthesizing dutasteride intermediate (I) comprises dissolving (4aR,4bS,6aS,7S,9aS,9bS)-4a,6a-dimethyl-2-oxo-tetradecahydro-1H-indeno(5,4-f)quinoline-7-carboxylic acid (2,5-bis-trifluoromethyl-phenyl)-amide in an organic solvent and then adjusting pH value to 2 using 2 mole/l of aqueous hydrogen chloride, stirring the mixture at room temperature and slowly adding sodium cyanoborohydride as reducing agent, carrying out hydrogenation reaction for 1 hours and then adjusting the pH value to 8 using sodium hydroxide solution (10%), extracting organic layer using dichloromethane, drying the organic layer using anhydrous magnesium sulfate and then filtering, reducing pressure of the filtrate and then steaming to obtain coarse product, (2) adding the coarse product into a recrystallizing agent and then recrystallizing to obtain refined product of (I) and analyzing the purity of refined product of (I) with a high performance liquid chromatography.
NOVELTY - Invention relates to complex waste water treatment. The system comprises a waste water mechanical treatment unit having a grid, a sand trap, a fat trap and a settling tank. The system has a biological treatment unit consisting of an aeration tan, a methane tank, a settling tank, sludge beds and apparatus for producing biogas, a fat trap having a reinforced-concrete housing, having the shape of a parallelepiped having a slanted bottom with vertical walls on top of which a detachable cover is mounted. Under the top cover there is a detachable lower cover for conducting preventive maintenance or eliminating emergency situations in case of discharge emissions. One of the vertical walls adjoins a box for regenerating the fat trap with hot water or steam or a mechanical means if the pipe for realising waste water into the drainage is clogged. A pipe for feeding waste water lies opposite the box on the vertical wall. An inlet opening for releasing waste water lies on the bottom part of the housing, next to an emergency valve for drainage if the inlet opening is clogged. Vibrators whose outputs are connected to a control unit are mounted on one of the vertical walls and the bottom of the housing.    USE - Chemistry.    ADVANTAGE - High quality and efficiency of treating waste water.2 dwg
NOVELTY - Biomass is pulverized (S1) to cellulose microfibrils and thermally decomposed (S2) by heat-resistant cellulase at 50 degrees C or more to obtain cellulose nanofiber. The aspect-ratio and crystallinity degree are controlled by adjusting heating temperature, heating time, or enzyme concentration.    USE - Manufacture of cellulose nanofiber. Uses include but are not limited to reinforcement of polymers, transparent materials, membrane filters, coating agents, and foodstuffs.    ADVANTAGE - The method enables simple manufacture of cellulose nanofiber with efficient enzyme reaction, and easy and precise adjustment of aspect ratio and crystallinity degree. The obtained nanofiber is tasteless, odorless and avirulent, and has excellent water-retention property, oil-maintenance property, texture, shape stability, and diet property.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of the manufacturing method of cellulose nanofiber. (Drawing includes non-English language text)    Pulverization process (S1)    Thermal decomposition process (S2)
NOVELTY - A hydrogen generating apparatus (1) comprises material supply source which supplies raw material containing hydrocarbon compound, hydrogen generator (2) which generates fuel gas which contains hydrogen from raw material, isolation side discharge port which is connected to supply side discharge port (11), splitter which isolates harmful component to hydrogen generator to be removed out of raw material, 1st material supply path which connects material supply source and raw material supply port, and 2nd material supply path which connects supply side discharge port and hydrogen generator.    USE - Hydrogen generating apparatus used as fuel cell system for producing electric power.    ADVANTAGE - To-be-removed components, such as sulfur compound contained in the raw material, are separable by simple structure.    DETAILED DESCRIPTION - A hydrogen generating apparatus (1) comprises material supply source which supplies raw material containing hydrocarbon compound, hydrogen generator (2) which generates fuel gas which contains hydrogen from raw material, isolation side discharge port which is connected to supply side discharge port (11) which discharges raw material from supply side flow path, raw material supply port distributes, and isolation side flow path in which component isolated from raw material to be removed circulates, splitter which isolates harmful component to hydrogen generator to be removed out of raw material, 1st material supply path which connects material supply source and raw material supply port, and 2nd material supply path which connects supply side discharge port and hydrogen generator.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the hydrogen generating apparatus.    Hydrogen generating apparatus (1)    Hydrogen generator (2)    Source gas supply source (3)    Source gas supply port (4)    Supply side discharge port (11)
NOVELTY - The fuel cell system has fuel generating agent (1) which generates fuel by oxidation reaction, and a fuel cell apparatus (2) which produces electric power by reaction with the fuel supplied from the oxidizing agent containing oxygen. A safety mechanism (7) prevents gas from being supplied to the fuel generating agent because shape change member (6) deforms with temperature. The fuel cell apparatus is a solid oxide fuel cell.    USE - Fuel cell system, e.g. secondary battery type fuel cell system.    ADVANTAGE - Improves the security since the thermal runaway and ignition of fuel generation agent can be prevented. Prevents the gas supply to a fuel generating agent since a safety mechanism functions when a shape change member becomes more than predetermined temperature.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fuel cell system.    Fuel generating agent (1)    Fuel cell apparatus (2)    Gas distribution channel (5)    Shape change member (6)    Safety mechanism (7)
NOVELTY - The fuel cell system has a battery (14) for supplying power to the portable electronic device (10) when the device is in a stand-by mode. A fuel cell element (12) includes two fuel cells. The primary fuel cell is activated and the secondary fuel cell is turned off when the portable electronic device is in stand-by mode. A processor (26) is configured to sense environmental condition surrounding the secondary fuel cell and to activate fuel cell based on sensed environmental condition. The heat generated by primary fuel cell is conveyed to secondary fuel cell.    USE - Fuel cell system for portable electronic device such as smart phone and portable computer (all claimed) such as tablet computer and laptop computer. Can also be used in cellular phone, MPEG audio layer-3 music player, remote control, electronic navigation devices such as global positioning system devices, portable DVD player and personal digital assistant.    ADVANTAGE - One fuel cell can act as a heater for the other fuel cells in the set of fuel cells to maintain a minimum ambient temperature surrounding the set of fuel cells. Thus the fuel cells can be operated under desired operating conditions when power is required. The inefficiency can be reduced and the reliability can be improved. The time required for the start-up of fuel cells can be reduced.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a portable electronic device; and    (2) a method of improving fuel cell recovery time.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the portable electronic device.    Portable electronic device (10)    Fuel cell element (12)    Hybrid battery (14)    Fuel tank (16)    Processor (26)
NOVELTY - The hydrogen production apparatus has a conductive deionization surface within a field line of an electric field source, and an electric conductor connected to conductive deionization surface and adapted to discharge charge built up due to attracted ions at the conductive deionization surface. An electric field source is electrically isolated from the water by insulation layer while hydrogen is produced on conductive deionization surface positioned within the water.    USE - Production apparatus used for sorting ions during production of hydrogen gas from water.    ADVANTAGE - Improves extraction of hydrogen from water by preventing free ions from reconnecting and forming water molecules by providing the electric conductor which discharges charge built-up.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a production method of hydrogen from water.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram illustrating the arrangement of paired electric field sources used for producing hydrogen from water.
NOVELTY - The system (200) has a primary gas source (216) providing primary gas to an ion source chamber (206). A co-gas source (220) provides co-gas to the ion source chamber. A primary gas module (218) controls primary gas. A co-gas module (222) controls the co-gas. A control system (201) selects the co-gas as a function of the selected primary gas. The primary and co-gas modules comprise high pressure identifiers or sub-atmospheric identifiers as defined by a pressure reading device. The co-gas module releases the co-gas from co-gas sources into the ion source chamber.    USE - Ion implantation system for use in semiconductor device fabrication process to selectively implant dopant into semiconductor and/or wafer material.    ADVANTAGE - The system improves performance and extends lifetime of an ion source, so that selection, delivery, optimization and control of the flow rate of the co-gas into the ion source chamber are automatically controlled.    DETAILED DESCRIPTION - The co-gas source is a fluorine-containing co-gas source. The primary gas source comprises boron trifluoride, germanium tetrafluoride, phosphorus trifluoride, silicon tetrafluoride, carbon dioxide, carbon monoxide, phosphine, arsine, or methane. The co-gas source comprises hydrogen, fluorine, or inert/noble gas. An INDEPENDENT CLAIM is also included for a method for improving performance of an ion implantation system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of an ion implantation system.    Ion implantation system (200)    Control system (201)    Ion source chamber (206)    Primary gas source (216)    Primary gas module (218)    Co-gas source (220)    Co-gas module (222)
NOVELTY - The device comprises a reactor (5) having a reactor wall, in which the biomass is dehydrated and carbonized, where the reactor comprises a coating on an entire inner side of the reactor wall in sections. The coating prevents the biomass from adhering. The reactor further comprises a heat exchanger (6), which is formed for a passage of flue gases or water vapor and comprises the coating. Elements contained in the reactor comprise coating. A preheating device (4) having a wall is provided for heating the biomass supplied to the reactor.    USE - The device is useful for the hydrothermal carbonization of biomass (claimed), where: the biomass is animal biomass and plant biomass such as green waste, wood chips, plants and plant residues, straw, silage, residues from agriculture, paper and sewage sludge; and the hydrothermal carbonization is an exothermic reaction.    ADVANTAGE - The device allows economical hydrothermal carbonization of the biomass thus effectively preventing the adhesion of biomass or intermediate products.    DETAILED DESCRIPTION - The device comprises a reactor (5) having a reactor wall, in which the biomass is dehydrated and carbonized, where the reactor comprises a coating on an entire inner side of the reactor wall in sections. The coating prevents the biomass from adhering. The reactor further comprises a heat exchanger (6), which is formed for a passage of flue gases or water vapor and comprises the coating. Elements contained in the reactor comprise coating. A preheating device (4) having a wall is provided for heating the biomass supplied to the reactor, and comprises, in sections, a coating that prevents adhesion of the biomass to the wall of the preheating device and has a layer thickness of 15-20 mu m.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic view of a device for the hydrothermal carbonization of biomass.    Conveying device (3)    Preheating device (4)    Reactor (5)    Heat exchanger (6)    Filter device. (8)
NOVELTY - A controlled-release fertilizer comprises fertilizer particles encapsulated in biodegradable polyurethane obtained from reaction between polyisocyanate and isocyanate-reactive component, which is formed by polyol and methyl ester derivative of natural oil, in the presence of an amine catalyst.    USE - As a controlled-release fertilizer such as chemical fertilizer or bio-fertilizer containing oil palm biomass, and palm oil mill effluent (claimed).    ADVANTAGE - The controlled-release fertilizer has improved abrasion resistance to avoid agglomeration and has efficient slow release of the plant nutrients; has superior hydrophobic qualities by acquiring high content of natural oil polyol in the polyurethane coating; and does not produce unpleasant odor and promote dust accumulation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing a controlled-release fertilizer involving preheating fertilizer particles at 60-105 degrees C; and coating the preheated fertilizer particles to form polyurethane-coated fertilizer particles.
NOVELTY - Use of ozone for removing residual phytosanitary molecules contained in plant seeds, is claimed.    USE - The ozone is useful for removing residual phytosanitary molecules contained in plant seeds, which are wheat, corn or rapeseed, where the treated seeds are useful in the preparation of biogas by fermentation (all claimed).    ADVANTAGE - The ozone easily and economically removes residual phytosanitary molecules contained in plant seeds thus increasing the production of biogas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the treatment of plant seeds contaminated by the residual phytosanitary molecules comprising (a) providing plant seeds contaminated by residual phytosanitary molecules, (b) adjusting the moisture content of the contaminated plant seeds to a rate of at least 10% and at most 21% with respect to the dry material, (c) contacting the ozone and the contaminated plant seeds with each other and (d) removing the residual ozone.
NOVELTY - A purification process (P1) of isolating biobutanol, involves: removing biobutanol from a fermentation broth using at least one separation process to phase separate a concentrated organic layer which includes biobutanol; dewatering the concentrated biobutanol and removing acid components with a saturated or near-saturated aqueous salt solution; chemically drying the biobutanol with at least one absorbent; and distilling the biobutanol to produce a purified biobutanol product.    USE - For purification process of isolating biobutanol (claimed). The biobutanol is useful in preparing biobutene that is useful in making diesel and jet fuels and biolubricants.    ADVANTAGE - The process produces purified biobutanol product containing at least 97% (preferably at least 98%, especially at least 99%) pure 1-butanol. The process leads to an increase in production yield; simplifies the equipment; uses lower energy in the purification process; and concurrently eliminates acidic components. This process greatly reduces distillation energy and losses for the final purification of butanol (normal or iso-). The process allows for generation of sufficiently pure biobutanol (greater than 97%) for use in a subsequent chemical process.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a purified biobutanol product obtained from the process (P1); and    (2) a system that isolates biobutanol, comprising: a fermentation vessel that removes biobutanol from a fermentation using a separation system that yields an organic layer of concentrated biobutanol; a dehydrating device that dewaters a the concentrated biobutanol and removes acid components with a saturated or near-saturated aqueous salt solution; a chemical drying device that dries the biobutanol with at least one absorbent; and a distilling system that separates undesired components from the biobutanol to produce a purified biobutanol product.
NOVELTY - A support comprises carbonization material obtained by performing carbonization of raw material containing organic substance and metal. The metal exhibits catalytic activity with respect to the methanation of carbon monoxide.    USE - Support is used for metal-supported catalyst used in methanation reaction apparatus for performing methanation of carbon monoxide (all claimed).    ADVANTAGE - The methanation of carbon monoxide is efficiently performed using the support.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) metal-supported catalyst;    (2) methanation reaction apparatus; and    (3) methanation of carbon monoxide.
NOVELTY - The method involves creating electrolytic fluid (20) containing purified hydrogen gas (80), and placing an anode (40) and a cathode (30) in electrical contact with the fluid. A potential difference or voltage between the anode and the cathode is created by a direct current (DC) power supply, where production of hydrogen is caused by electrolysis. A vibrational mode of the fluid is determined. Radiation emitted by a laser (70) is matched to the vibrational mode. The radiation is applied to the fluid, where hydrogen is produced at an increased rate over the electrolysis alone.    USE - Method for increasing hydrogen production by electrolysis through electrolytic solution containing hydrogen in a reaction vessel within a hydrogen generation system and a test system or test fixture.    ADVANTAGE - The method enables producing large amount of hydrogen in a rapid and efficient manner.    DETAILED DESCRIPTION - The laser is an erbium-doped yttrium aluminum garnet laser. The electrolytic fluid is water and an elemental salt i.e. Epsom salt. An INDEPENDENT CLAIM is also included for a device for production hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a test fixture.    Electrolytic fluid (20)    Cathode (30)    Anode (40)    Laser (70)    Purified hydrogen gas (80)
NOVELTY - The aggregate comprises normal direct current (DC) power unit and electrolysis cell. The electrolysis oxygen mixed with air, is used as oxidizer for combustion engine. A connection line is provided between motor tube and gas line that is secured with solenoid valves which are opened only when power is supplied. The valves are connected to each other through a circuit which is only closed, so the current flows only when the engine is switched to gas mode. The feed hoses are made of silicone.    USE - Electrolysis-hydrogen aggregate, for engine of motor vehicle e.g. passenger car.    ADVANTAGE - The combustion of fuel can be carried out completely. The engine is environmentally friendly and efficient. The engine can be repaired easily. The components can be protected against highly aggressive electrolysis ozone, since electrolysis oxygen is introduced into engine unit. The release of pollutants except ozone can be prevented, since penetration of electrolytes into electrolysis cell is eliminated.
NOVELTY - The test gas connectors (30.0-30.3) connect the test gas containers (11-16) to a pressure reduction valve (45.1). A first main pipe (201) supplies calibration gas to first container. A second main pipe (202) supplies zero-point gas to second container. The second pipe is connected to a compressor (71) for introducing ambient air. A test chamber device (58.1) is formed for receiving the calibration gas and/or the zero-point gas and is connected to the pipes such that the calibration gas in first pipe and the zero-point gas in second pipe are fed time-sequentially in a row.    USE - Gas admission device for testing operability and calibration of gas measuring instruments used for measuring gases such as methane, oxygen, carbon monoxide, or hydrogen sulfide.    ADVANTAGE - The measurement of gas concentration can be carried out efficiently with high precision, in a faster manner and at low cost, while enabling for testing of large amount of gases.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for performing evaluation of predetermined concentration of test gas in measurement gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic circuit diagram of the gas admission device.    Test gas containers (11-16)    Test gas connectors (30.0-30.3)    Pressure reduction valve (45.1)    Test chamber device (58.1)    Compressor (71)    Main pipes (201,202)
NOVELTY - The fermenting apparatus has a vertical-type fermenting portion (10) that is attached with and input hopper (20) and is provided with the four side walls. The air pipe is arranged on the wall. The timber door is formed in one side wall of the vertical-type fermenting portion. The vertical-type fermenting portion satisfies the carbon-nitrogen ratio and driving condition of the aerobic fermentation.    USE - Apparatus for fermentation of organic waste and food waste.    ADVANTAGE - The damage of the hose can be prevented. The moisture absorption effect in timber can be improved. The blockage of the air supply nozzle can be prevented. The air-supply can be performed smoothly.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the apparatus for fermentation of organic waste.    Vertical-type fermenting portion (10)    Input hopper (20)    Blower (30)    Wood wall side (200)    Air distribution high-tension hose (300)
NOVELTY - The hydrogen generator has a pellet strip which is provided with a flexible carrier (20) with several pellets (22). Each pellet is provided with a hydrogen containing material which releases hydrogen gas, when it is heated. A feed system is provided to feed the pellet strip to sequentially position the pellets in proximity to a heater (16), such that the heater heats the proximal pellet to release hydrogen gas. The pellet strip is wound on a reel (18).    USE - Hydrogen generator for fuel cell system (claimed).    ADVANTAGE - The total volume of hydrogen gas produced per unit of mass can be increased efficiently. The release of hydrogen gas from the hydrogen containing material is controlled, in order to provide hydrogen on needed basis. Thus, the internal pressure within the hydrogen generator can be reduced effectively. The hydrogen generator can be operated at desired maximum temperature. The portions of hydrogen generator can be replaced efficiently, after the hydrogen containing materials is consumed. The long term durability and reliability of the hydrogen generator can be improved efficiently. The hydrogen generator can be manufactured easily with low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the hydrogen generating cartridge.    Cartridge (10)    Heater (16)    Reel (18)    Carrier (20)    Pellets (22)
NOVELTY - A hydropyrolysis catalyst (100) comprises a support and an active metal component. The catalyst is an eggshell-type catalyst having active metal component located in the outer portion of support.    USE - Hydropyrolysis catalyst is used for converting biomass to products (claimed) e.g. gasoline, diesel fuel and jet fuel.    ADVANTAGE - The biomass is efficiently converted, using the hydropyrolysis catalyst.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for process for converting biomass to products, which involves contacting biomass with hydrogen in presence of fluidized bed of hydropyrolysis catalyst in reactor vessel under hydropyrolysis conditions and removing products and char from the reactor vessel.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the equipment for hydropyrolysis process.    Catalyst (100)    Surface (110)    Biomass feed line (120)    Hydrogen feed line (122)    Cyclone (130)
NOVELTY - A Penaeus vannamei fertilizer comprises: 70-80 wt.% diatomaceous earth, 10-22 wt.% compost duck manure, 3-10 wt.% calcium phosphate, 2-5 wt.% potassium dihydrogen phosphate, 0.5-5 wt.% calcium carbonate, 0.02-0.35 wt.% zinc sulfate, 0.04-0.7 wt.% manganese sulfate, 0.02-2 wt.% manganese chloride, 0.1-0.6 wt.% copper, 0.1-0.7 wt.% ferrous sulfate heptahydrate, 0.02-0.2 wt.% ammonium and 0.02-0.35 wt.% boron ions.    USE - A Penaeus vannamei fertilizer.
NOVELTY - A low-temperature-resistant Lactobacillus plantarum CCZZ1 strain, which is collected at China General Microbiological Culture Collection Center with an address of Institute of Microbiology, Chinese Academy of Sciences, No. 3, Court 1, West Beichen Road, Chaoyang District, Beijing. The strain has a collection number of CGMCC NO. 6078, with collection date of May 3, 2012, is new.    USE - The low-temperature-resistant Lactobacillus plantarum CCZZ1 strain is useful for modulating silage (claimed).    ADVANTAGE - The low-temperature-resistant Lactobacillus plantarum CCZZ1 strain is glucose-homofermentative, and is acid-resisting. It has high growth speed and wide reproductive temperature range. With the strain, under a low-temperature or normal-temperature environment, silage fermentation quality can be substantially improved.
NOVELTY - Guanidinopropionic acid and water are uniformly stirred and nitric acid is dripped. The temperature is controlled at 20-40 degrees C and dripping is completed in 10 minutes. Heat is preserved for 20 minutes, while continuously stirring. The reaction mixture is cooled, and the separated out solid is filtered and dried to obtain guanidinopropionic acid nitrate. The filtered liquid is recycled as mother liquor.    USE - Preparation of guanidinopropionic acid nitrate (claimed).    ADVANTAGE - The method enables economical, environmentally-friendly, simple and quick industrial preparation of high-quality guanidinopropionic acid nitrate with a purity of more than 99%, by using food-grade guanidinopropionic acid and chemical-grade nitric acid, with high productivity, a yield of more than 98%, and no by-products. Recrystallization is not required.
NOVELTY - Producing organic fertilizer by using original red soil and agricultural waste, comprises: crushing natural red soil, taking rice straw or wheat straw, sorghum and corn straw, piling up the red soil in the middle, cultivating red soil at the periphery to form an elliptical shape, covering the rice straws or wheat straws, and finally using residual red soil to cover; burning to enable the red soil to be changed to be brown, uniformly stirring burned red soil and the burned plant ash, moving into the room, pouring night soil every two days, stirring and piling for two and half months.    USE - The method is useful for producing organic fertilizer by using original red soil and agricultural waste (claimed).    DETAILED DESCRIPTION - Producing organic fertilizer by using original red soil and agricultural waste, comprises: crushing 30 pts. wt. natural red soil, taking 3 pts. wt. rice straw or wheat straw, sorghum and corn straw, piling up the red soil in the middle, firstly burning hay stacks tied up by the rice straws, cultivating red soil at the periphery to form an elliptical shape, covering the rice straws or wheat straws, and finally using residual red soil to cover; burning for 24 hours to enable the red soil to be changed to be brown, uniformly stirring burned red soil and the burned plant ash, moving the mixture into the room, pouring night soil or excrement of pig, chicken and duck while moving until the mixture is wet, piling up together after uniformly stirring, and then pouring 2 pts. wt. night soil every two days, stirring and piling up together until the operation is continuously performed for two and half months.
NOVELTY - The device has an electrolytic vessel (110) which stores electrolyte solution and several set of electrodes with electric corrosion-proof property. An airtight lid (120) seals the upper-end opening portion of electrolytic vessel. An electrolyzer (100) electrolyzes the electrolyte solution and generates HHO gas by sending electric current between anode and cathode of each electrode using a power supply device (300). A current control apparatus (200) controls electric current sent between anode and cathode of each electrode to predetermined electric current value.    USE - HHO gas generation device installed in combustion apparatus and fuel supply apparatus of internal combustion engine mounted in two-wheeled motor vehicle (all claimed). Can also be used in transporting apparatus such as bus, truck, diesel train, boat and ship, construction apparatuses such as crane and shovel car, domestic use boiler, business use boiler, thermal power station and incinerator.    ADVANTAGE - The electrolysis can be accelerated and HHO gas can be generated stably and efficiently. The current control apparatus controls electric current sent between anode and cathode of each electrode, hence the safety can be ensured. The sodium carbonate and sodium hydrogen carbonate can be attained efficiently at lower cost. The simplified structure can be achieved. The electrolyte solution heats the sodium carbonate aqueous solution and sodium hydrogen carbonate aqueous solution, hence carbonic acid content can be removed reliably. The removal of carbonic acid content can be realized.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the HHO gas generation device. (Drawing includes non-English language text)    Electrolyzer (100)    Electrolytic vessel (110)    Airtight lid (120)    Current control apparatus (200)    Power supply device (300)
NOVELTY - A marsh gas tank comprises a multiple of disconnected single marsh gas tanks. Each single biogas tank is provided with marsh gas outlet and inlet. Marsh gas control valve is set at the gas outlet. The gas outlet is connected to marsh gas collecting device.    USE - A marsh gas tank.    ADVANTAGE - The tank makes use of the long marsh gas fermentation period and uses multiple single marsh gas tanks so that it can recycled. It increases capability of the excrement treatment to satisfy the demand of production and life.
NOVELTY - The system has power generation equipment (1) which is provided with a turbine and a hydrolyzing photocatalyst hydrogen production installation (2). The hydrolyzing photocatalyst hydrogen production installation is provided for manufacturing hydrogen. The manufactured hydrogen is supplied to the power generation equipment. A sea water desalination installation is provided for discharging vapor from the power generation equipment which is used as a heat source for manufacturing freshwater and is supplied to the hydrolyzing photocatalyst manufacturing equipment.    USE - High efficiency power generation system.    ADVANTAGE - Since the hydrogen manufactured by the hydrolyzing photocatalyst hydrogen production installation is supplied to the power generation equipment, the efficiency of power generation equipment can be improved effectively. The fresh water can be generated efficiently.    DETAILED DESCRIPTION - The hydrolyzing photocatalyst hydrogen production installation has a separation mechanism which separates hydrogen and oxygen. The electrode type hydrolyzing photocatalyst water manufacturing equipment is provided. The power generation equipment performs thermal power generation. The combined cycle thermopower plant is provided in the high efficiency power generation system and is comprised of a gas turbine and steam turbine for fuel and hydrogen gas respectively. The gas turbine is provided for the fuel and hydrogen gas.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the high efficiency power generation system. (Drawing includes non-English language text)    Power generation equipment (1)    Hydrolyzing photocatalyst hydrogen production installation (2)
NOVELTY - Converting residual carbon dioxide (CO2) in oil reservoirs after CO2 flooding into methane (CH4) comprises screening CO2 flooding oil reservoirs which are suitable for the method; detecting hydrogenogens and methanogens of inner sources in the CO2 flooding oil reservoirs; screening nutritional systems of the hydrogenogens and the methanogens of the inner sources and/or outer sources according to a target oil reservoir; and after closing CO2 flooding oil reservoirs for 6 to 12 months, opening a well to produce CH4.    USE - The method is useful for converting residual CO2 in oil reservoirs after CO2 flooding into CH4 (claimed); and for oil reservoirs which meet the oil reservoir condition of the method in the CO2 flooding oil reservoirs.    ADVANTAGE - By using the method, an input-output ratio is more than 1:3.0, and the volume content of the methane in output gas is more than 90.0%. The method has the advantages of cleanness and environment friendliness, and can be widely applied to the field of tertiary oil recovery.    DETAILED DESCRIPTION - Converting residual carbon dioxide (CO2) in oil reservoirs after CO2 flooding into methane (CH4) comprises screening CO2 flooding oil reservoirs which are suitable for the method; detecting hydrogenogens and methanogens of inner sources in the CO2 flooding oil reservoirs; screening nutritional systems of the hydrogenogens and the methanogens of the inner sources and/or outer sources according to a target oil reservoir, where screening nitrogen sources and phosphorus sources are mainly screened in the nutritional systems; injecting the screened nutritional systems of the hydrogenogens and the methanogens into the CO2 flooding oil reservoirs; and after closing CO2 flooding oil reservoirs for 6 to 12 months, opening a well to produce CH4.
NOVELTY - Method for manufacturing chicken manure, involves (a) mixing 50-55 parts fresh chicken manure, 10-15 parts corn flour, 10-15 parts wheat flour and 5-10 parts wheat bran uniformly in a stirrer, (b) preparing premix by stirring 4-5 parts brown sugar, 3-4 parts lime, 1-1.5 parts dinoflagellate, 1-2 parts yeast, 1-2 parts lactic acid bacteria and 0.5-0.8 parts Thermoactinomyces uniformly, (c) mixing the products obtained in step (a) and (b), and (d) stacking products for anaerobic fermentation at 45-60 degrees C for 25-35 days, and obtaining chicken manure.    USE - The method is useful for manufacturing chicken manure (claimed) which is used for providing disease resistance to plants.    ADVANTAGE - The method is simple, cost-effective and causes reduced side effect. The chicken manure can decompose nitrates and secondary salts formed by chemical manure residues in soil, and thus improves crop yield.
NOVELTY - Method for manufacturing duck manure, involves (a) mixing 40-55 parts fresh duck manure, 10-15 parts castor cakes, 10-15 parts colza cakes and 5-10 parts wheat bran uniformly in a stirrer, (b) preparing premix by stirring 4-5 parts vitamin B1, 3-4 parts pantothenic acid, 1-1.5 parts folic acid, 0.5-1.5 parts yeast, 1-2 parts streptomycin and 0.5-0.8 parts Thermoactinomyces uniformly, (c) mixing the products obtained in step (a) and (b) and (d) stacking products for anaerobic fermentation at 45-60 degrees C for 25-35 days, and obtaining duck manure.    USE - The method is useful for manufacturing duck manure (claimed) which is used for providing disease resistance to plants.    ADVANTAGE - The method is simple, cost-effective and causes reduced side effect. The duck manure can decompose nitrates and secondary salts formed by chemical manure residues in soil, and thus improves crop yield.
NOVELTY - Use of artificial wetland plant biomass resource for preparing marsh gas fuel, is claimed.    USE - The artificial wetland plant biomass resource is useful for preparing marsh gas fuel (claimed).    ADVANTAGE - The artificial wetland plant biomass resource exhibits improved applicability, good purification effect and stability and better quality in an economical manner.
NOVELTY - USR fermentation comprises taking pig manure, pre-treating sewage in processing tank, processing after acidification, carrying out acidification hydrolysis, precipitating in sedimentation tank, adjusting metering tank, fermenting in anaerobic fermentation tank, filtering fermentation to generate biogas, biogas residue and biogas slurry, taking biogas residue organic fertilizer, taking biogas slurry stored in biogas tank, passing marsh gas through condensing water and entering into gas storage cabinet.    USE - Method of USR fermentation (claimed).    ADVANTAGE - The method promotes coordinated development of biological and ecological environment, energy and economic benefit, increases circulation factor, prolongs biological chain and chain, and improves the living and ecological environment.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the USR fermentation.
NOVELTY - Preparation of chondrocyte-derived waste fuel involves: providing a fibrous sludge; adding microorganism bacteria and a bulking agent; dopping microbial fermentation promoter in a predetermined ratio, with the fiber in the sludge and mixing uniformly, and fermenting to form a solid waste fuel. The fermentation time is 3-30 (preferably 7-20) days. The water content of the solid waste fuel is less than 50%.    USE - For preparation of chondrocyte-derived waste fuel (claimed), which is useful for the boiler or incinerator combustion furnace.    ADVANTAGE - The process is carried out using reduced energy consumption. The manufacturing cost is low; and mass production is high.
NOVELTY - The device has a reactor (1) which is provided with a magnetic stirrer (10). The reactor is divided into mutually independent photo-catalytic primary battery (5) and light catalytic hydrogen production tank (6). The photo-catalytic primary battery and hydrogen production tank are provided with several pairs of photo-catalysis electrodes. The photo-catalytic electrode pairs are connected in series to form a loop. The photo-catalytic primary battery is provided with a sub-hydrogen tank.    USE - Device for producing hydrogen from photoelectric degradation organic pollutant based on visible light driving.    ADVANTAGE - The hydrogen can be produced efficiently. The hydrogen production cost can be reduced, as the production efficiency is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing hydrogen from photoelectric degradation organic pollutant.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen producing device. (Drawing includes non-English language text)    Reactor (1)    Photo-catalytic primary battery (5)    Hydrogen production tank (6)    Hydrogen collecting unit (9)    Magnetic stirrer (10)
NOVELTY - A chondrocyte-derived fuel in cement kiln joint disposal mineralized waste is manufactured by screening a mineralized waste to remove rotten soil organic fine material, separating using mechanical or manual sorting step of screened and processed combustible garbage, naturally drying the combustible garbage to remove the residual water, crushing dried combustible garbage, and uniformly mixing and forming crushed and processed combustible garbage and coal and alkaline additive in extrusion molding to obtain refuse derived fuel.    USE - Manufacture of chondrocyte-derived fuel in cement kiln joint disposal mineralized waste (claimed).    ADVANTAGE - Land resource is saved, building garbage is reduced, and energy consumption is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of the preparation of chondrocyte-derived fuel in cement kiln joint disposal mineralized waste. (Drawing includes non-English language text).
NOVELTY - Aldose reductase inhibitor fidarestat is prepared by performing addition reaction of p-fluorophenol and N-phenylmaleimide in organic solvent e.g. chloroform, dichloromethane, ethyl acetate, toluene, benzene, acetone, acetonitrile, methanol, ethanol and/or acetone under alkali catalysis of oxo-Michael addition reaction to obtain 1-phenyl-3-(4-phenoxy)-2,5-pyrrolidine diketone, wherein alkali agent is amine, octylamine, cyclopentylamine, dodecyl dimethyl tert.-amine, hexadecyl dimethyl tert.-amine, dimethyl tert.-amine, tetramethylammonium hydroxide, pyridine, and/or triethylamine.    USE - Preparation of aldose reductase inhibitor fidarestat (claimed).    ADVANTAGE - Preparation method is low cost, features high yield and simple and safe operations, has relatively mild reaction conditions, and is environment-friendly and suitable for large-scale preparation.    DETAILED DESCRIPTION - Aldose reductase inhibitor fidarestat is prepared by performing addition reaction of p-fluorophenol of formula (II) and N-phenylmaleimide of formula (III) in organic solvent e.g. chloroform, dichloromethane, ethyl acetate, toluene, benzene, acetone, acetonitrile, methanol, ethanol and/or acetone under alkali catalysis of oxo-Michael addition reaction to obtain 1-phenyl-3-(4-phenoxy)-2,5-pyrrolidine diketone of formula (IV), wherein alkali agent is amine, octylamine, cyclopentylamine, dodecyl dimethyl tert.-amine, hexadecyl dimethyl tert.-amine, dimethyl tert.-amine, tetramethylammonium hydroxide, pyridine, triethylamine, sodium carbonate, sodium bicarbonate, and/or sodium hydroxide..
NOVELTY - Special fertilizer comprises 65-80 wt.% fermented animal waste, 10-20 wt.% humic acid, 5-10 wt.% potassium sulfate, 5-10 wt.% clay and 2-3 wt.% magnesium, iron, boron and zinc.    USE - As special fertilizer for greenhouse vegetables and fruit trees.    ADVANTAGE - The fertilizer has complete nutrient element and hence improves soil fertility and product quality and enhances disease and insect resistance of the greenhouse vegetables and fruit trees.
NOVELTY - A pemetrexed intermediate is prepared by performing aluminum trichloride-catalyzed Friedel-Crafts alkylation on benzene and 4-halo-1-butanol to obtain 4-phenyl-1-butanol (II), performing Friedel-Crafts acylation on component II to obtain 4-(4-alkoxycarbonyl phenyl)-1-butanol (III), oxidizing component III to obtain 4-(4-alkoxycarbonyl phenyl)-1-butyraldehyde (IV), performing bromine substitution on component IV to obtain 4-(3-bromo-4-oxo-butyl)benzoic acid methyl ester (V), and reacting component V with 2,4-diamino-6-hydroxypyrimidine (VI).    USE - Preparation of pemetrexed intermediate (claimed).    ADVANTAGE - Preparation method is simple with high reaction efficiency, convenient and easy to operate, stable, low cost, and environment-friendly.    DETAILED DESCRIPTION - A pemetrexed intermediate is prepared by performing aluminum trichloride-catalyzed Friedel-Crafts alkylation on benzene and 4-halo-1-butanol to obtain 4-phenyl-1-butanol (II), performing Friedel-Crafts acylation on component II to obtain 4-(4-alkoxycarbonyl phenyl)-1-butanol (III), oxidizing component III to obtain 4-(4-alkoxycarbonyl phenyl)-1-butyraldehyde (IV), performing bromine substitution on component IV to obtain 4-(3-bromo-4-oxo-butyl)benzoic acid methyl ester (V), reacting component V with 2,4-diamino-6-hydroxypyrimidine (VI) to obtain 4-(2-(2-amino-4,7-dihydro-4-oxo-1H-pyrrolo(2,3-d)pyrimidin-5-yl)ethyl) benzoate (VII), and hydrolyzing component VII. Pemetrexed is 4-(2-(2-amino-4,7-dihydro-4-oxo-1H-pyrrolo(2,3-d)pyrimidin-5-yl)ethyl) benzoic acid of formula (I)..
NOVELTY - Method for preparing silicon-containing organic fertilizer, involves mixing 200-300 kg plant ash, 500-600 kg excrement or humus, 3-5 kg corn flour and 1-1.2 kg fermenting agent, fermenting the mixture for 5-7 days in fermentation tank, adding 10-20 kg silicon dioxide into the mixture, stirring mixture uniformly, extruding mixture into strips using extruder, cutting the strips, granulating the cut strips using disk granulator, drying the granules, and packaging the product using packaging machine, where the content of the product is 50 kg/per bag.    USE - The method is useful for preparing silicon-containing organic fertilizer (claimed).    ADVANTAGE - The method is simple and convenient, and prepares fertilizer that is rich in silicon element, thus solves the problem of shortage of silicon-containing organic fertilizer and improves soil environment, thus enables to improve growth of crops.
NOVELTY - The method involves adding raw material oil and lipase catalyst into enzyme catalysis reactor (R-1). The material after enzyme catalytic reaction is provided into heat exchanger (E-1) by pump. The methanol is removed by stream of flash evaporator (F-1). The low carbon alcohol is provided to alcohol refining rectification tower (D-2). The fatty acid methyl ester is pumped into purifying rectifying tower (D-1). The top stream is provided into reservoir tank. The fatty acid methyl ester rectification purification stream is passed through flow divider.    USE - Method for generating low energy consumption biological diesel oil.    ADVANTAGE - The low energy consumption diesel oil can be produced effectively. The low carbon alcohol can be recovered.    DETAILED DESCRIPTION - The method involves removing glycerin in material flow centrifuge. The acid reaction process is performed from centrifuge to device-acidification reactor (R-2). The sodium carbonate is added into neutralization reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the process for generating low energy consumption biological diesel oil. (Drawing includes non-English language text)    Purifying rectifying tower (D-1)    Alcohol refining rectification tower (D-2)    Heat exchanger (E-1)    Flash evaporator (F-1)    Enzyme catalysis reactor (R-1)    Device-acidification reactor (R-2)
NOVELTY - The pool has a marsh gas tank (2) that is buried underground. A bearing wall (1) is arranged for supporting marsh gas tank. The marsh gas tank is provided with smoke channel (3) two sides of the top are respectively provided with soot blowing gun (4). A stirrer (8) is provided at the middle shaft of marsh gas tank. The inlet of smoke channel is provided with smoke channel inlet adjusting valve (9) and smoke channel outlet adjusting valve (10). A boiler chimney (6) is provided at the outlet of smoke channel.    USE - Energy saving biomass biogas pool.    ADVANTAGE - The biomass biogas pool has simple structure, convenient maintenance, and improves the efficiency of the boiler. The discharging of boiler chimney dust into the atmosphere can be prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of the energy saving biomass biogas pool.    Bearing wall (1)    Marsh gas tank (2)    Smoke channel (3)    Soot blowing gun (4)    Boiler chimney (6)    Stirrer (8)    Smoke channel inlet adjusting valve (9)    Smoke channel outlet adjusting valve (10)
NOVELTY - Composite flora comprises Bacillus with CGMCC NO. 5971, Rheinheimera tangshanensis with CGMCC NO. 5972, and Pseudomonas fluorescens with CGMCC NO. 5974.    USE - The composite flora is useful in biological bacterial liquid pulping application; and for paper-making using bacterial liquid (all claimed).    ADVANTAGE - The paperboards made by the bio-bacterial solution pulping method reach AA or above level; and the waste liquid produced in pulp making can be recycled or changed into methane which is a kind of energy or organic fertilizers, so energy can be saved and environment pollution is avoided.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for paper-making using bacterial liquid comprising bacterial liquid is configured: the compound flora is configured to composite bacteria water solution; raw material processing: the woody raw material after cortex slice, or the herbal raw material cutting section, to cut the raw material into the soaking pool swelling; mitigating the swelling of the thread raw material crushing and/or grinding, biodegradable, the hydrophobic solution as raw material to soak the prepared bacterial liquid, steam sterilizing: putting the biodegradable raw material from bacteria liquid, draining, steam sterilizing, grinding: putting the sterilized raw material for a period of roughly grinding slurry to form fiber bundle, fine grinding: putting the first section grinding slurry for the second section thin grinding slurry, to make the fiber beam be separated single fiber, slurry screening: screening, filtering after a period of grinding slurry and the second slurry fine grinding slurry of the fiber bundle, and then grinding to make it into single fiber, latency, and washing.
NOVELTY - An organic fertilizer fermentation drying shed deodorizing device comprises a suction pipe, gas-liquid separating tower, exhaust fan, deodorizing tower, circulating pool, circulating pump and water seal. Each fermentation field is set with 2-4 plastic air suction pipes drilled with small holes. The ozone from the fermentation field enters the gas-liquid separating tower. The gas-liquid separating tower is set with detachable flow baffle plates, plastic filler and stainless steel silk screen layers. The devices are connected into one by a pipe.    USE - An organic fertilizer fermentation drying shed deodorizing device is used in recovering organic matter in ozone as liquid fertilizer.    ADVANTAGE - The device has simple and reasonable structure, convenient operation, and good liquid phase separation to obtain good odor deodorization.
NOVELTY - Producing natural insecticide compound fraction extracted from gingko leaf or gingko episperm, comprises processing activated charcoal by extracting gingko leaf or gingko episperm using low class alcohol and fractioning it by non-polar solvent, removing generated impurities, adding and extracting non-polar solvent, adding methyl ethyl ketone that is a low class ketone or in low class ketone to activated charcoal, agitating the mixture, and removing impurities to obtain fraction of natural insecticide compound.    USE - The method is useful for producing natural insecticide compound fraction extracted from gingko leaf or gingko episperm (claimed), where the natural insecticide compound fraction is useful for killing pest. Tests details are described but no results given.    ADVANTAGE - The natural insecticide compound fraction can prevent the abuse of synthetic insecticide and affect the human body or the environment.    DETAILED DESCRIPTION - Producing natural insecticide compound fraction extracted from gingko leaf or gingko episperm, comprises processing activated charcoal by extracting gingko leaf or gingko episperm using low class alcohol and fractioning it by non-polar solvent, where organic solvent extract is produced in a solution phase to make 30 plus minus 5% of coextract finely pulverized by lower class alcohol solution, removing generated impurities, adding and extracting non-polar solvent for 20-40 times, where non-polar solvent is hexane, chloroform and ethyl acetate, adding methyl ethyl ketone that is a low class ketone or in low class ketone to activated charcoal, agitating the mixture at a room temperature for 60-90 minutes, and removing impurities to obtain fraction of natural insecticide compound.
NOVELTY - Dysosma versipellis is crushed, ethanol is added to crushed dysosma, resultant mixture is added in microwave extracting device, microwave extraction process is carried out for 2-4 times. Obtained extracts are combined, filtered, and resultant ethanol is concentrated. Obtained concentrated ethanol is added into polyamide chromatography column, and elution process is carried out using methylene dichloride-methanol mixed solvent as eluent, and resultant solvent is recovered. Acetone is added to resultant product, crystallized, washed and dried, to obtain podophyllotoxin.    USE - Extraction of podophyllotoxin (claimed).    ADVANTAGE - The method enables economical extraction of podophyllotoxin with purity of 99%, and reduced solvent consumption, energy consumption and pollution, by simple process.    DETAILED DESCRIPTION - Dysosma versipellis is crushed, 80-90 %mass ethanol is added to crushed dysosma in the volume ratio of 15-20 times, resultant mixture is added in microwave extracting device, microwave extraction process is carried out at 300-600 W for 2-4 times, in which each extraction process is carried out for 5-20 minutes. Obtained extracts are combined, filtered, decompressed and ethanol is recycled and concentrated. Obtained concentrated ethanol is added to macroporous adsorption resin column, adsorption process is carried out using 50-70% ethanol in volume ratio of 3-8 times as eluent, resultant ethanol is decompressed, recycled and concentrated. Obtained concentrated ethanol is added into polyamide chromatography column, elution process is carried out using methylene dichloride-methanol mixed solvent as eluent, and resultant solvent is recovered under reduced pressure. Acetone is added to resultant product, crystallized, resultant product is washed and dried, to obtain podophyllotoxin. The ratio of methylene dichloride and methanol in the mixed solvent is 4:1.
NOVELTY - Method for harmless biotreatment of Tilapia mossambica, involves digging pits in sites, stacking T.mossambica corpses in the pit, mixing dry yeast with Lactobacillus to form complex bactericide, mixing complex bactericide with water, splashing the mixture on surface of corpse stack, coating a plastic thin film on the surface of the corpse stack, backfilling and compacting the stack by soil to ferment, digging away a soil layer and collecting fermentation liquor and solid residue in the pit to be taken as organic fertilizer.    USE - The method is useful for harmless biotreatment of T.mossambica for producing organic fertilizer.    ADVANTAGE - The method enables thorough degradation of organic matters into inorganic nutrients capable of being absorbed and used by plants, as anaerobic compound microorganisms are directionally added into the T.mossambica corpses and anaerobic fermentation is performed in sealed space, and eliminates harmful organisms in animal body such as parasite, as the method provides high temperature and anoxic environment during fermentation.    DETAILED DESCRIPTION - Method for harmless biotreatment of Tilapia mossambica, involves (a) selecting sites and digging pit in the sites, (b) stacking Tilapia mossambica corpses in the pit in a concentrated way, (c) mixing high-activity dry yeast with Lactobacillus to form a complex bactericide, (d) mixing the complex bactericide with water, evenly stirring the mixture, evenly splashing the mixture to the surface of corpse stack, coating a plastic thin film on the surface of the corpse stack and backfilling and compacting the stack by soil to ferment, and (e) digging away a soil layer and collecting fermentation liquor and solid residue in the pit to be taken as organic fertilizer.
NOVELTY - A nitrogen-containing compound (I) or (II) is new.    USE - Nitrogen-containing compound is used as halogen-free amine antibacterial agent.    ADVANTAGE - The nitrogen-containing compound is efficiently prepared with high yield, and excellent antibacterial property without polluting the environment, by simple method.    DETAILED DESCRIPTION - A nitrogen-containing compound of formula (I) or (II) is new.    X1,X2=substituents chosen from chloro or bromo, or hydroxymethyl;and    X3=chloro or bromo.    An INDEPENDENT CLAIM is included for preparation of nitrogen-containing compound.
NOVELTY - Preparation of psoralen and isopsoralen involves refluxing fructus psoraleae extract, concentrating, obtaining concentrated solution, adding acid to the obtained concentrated solution, heating, hydrolysis, feeding the resultant hydrolyzate into a macroporous adsorption resin column, eluting with water to remove impurities, then eluting with more than 50% aqueous solution of ethanol as eluent, collecting ethanol eluent, concentrating or drying, and obtaining psoralen and isopsoralen.    USE - Preparation of psoralen and isopsoralen (claimed).    ADVANTAGE - The method provides psoralen and isopsoralen with high yield, by a simple process in a short period of time, without environmental pollution.    DETAILED DESCRIPTION - Preparation of psoralen and isopsoralen involves refluxing fructus psoraleae extract, concentrating, obtaining concentrated solution, adding acid to the obtained concentrated solution, heating, hydrolysis, feeding the resultant hydrolyzate into a macroporous adsorption resin column, eluting with water to remove impurities, then eluting with more than 50% aqueous solution of ethanol as eluent, collecting ethanol eluent, concentrating or drying, and obtaining psoralen and isopsoralen or alternatively purifying the hydrolyzate in a silica gel column, eluting with organic solvent, collection psoralen fractions and isopsoralen fractions, removing solvent and obtaining psoralen and isopsoralen.
NOVELTY - The method involves homogenizing and concentrating dried tobacco leaf (10-20% w/v) by using proteolytic enzymes, preferably subtilisin (0.1-0.3% w/v). The reaction is performed at 50-60 degrees C with extraction time of 90-150 minutes at pH 8-9.5.    USE - Method for obtaining protein extracts from leaves of tobacco by enzymatic hydrolysis in a bioreactor, and used as fertilizer for crops by direct application to soil or by foliar fertigation, and used as protein supplement for use in food for animals (all claimed).
NOVELTY - Breeding maggot and earthworm involves fermenting kitchen garbage in anaerobic condition, regulating pH of the garbage, crushing the garbage, filtering and dewatering the garbage to obtain residue, adding animal excrement and/or straw powder, adding the mixture to a culture dish, adding fly eggs, maintaining the dish at 30-35 degrees C and humidity 50-70%, separating maggots, repeatedly performing the above breeding process until only fibrous material remains in the residues, and adding the residue to earthworm breeding base to breed earthworms.    USE - The method is useful for breeding maggots used as high protein feed, and earthworms using kitchen garbage (claimed).    ADVANTAGE - The method utilizes kitchen garbage at high efficiency as compared to composting method, eliminates soil pollution, reduces air pollution and achieves recycling of the garbage.    DETAILED DESCRIPTION - Breeding maggot and earthworm involves fermenting kitchen garbage in anaerobic condition, regulating pH of the fermented garbage to 5-8, crushing the garbage, filtering and dewatering the garbage to obtain residue, adding 30-50% animal excrement and/or straw powder to the residue, adding the mixture to a maggot culture dish, layering the mixture to 5-10 cm thickness, adding fly eggs, maintaining the dish at 30-35 degrees C and humidity of 50-70% such that the eggs hatch and grow into larvae and then maggots, separating maggots, repeatedly performing the above breeding process until only fibrous material remains in the residues, and adding the residue to earthworm breeding base to breed earthworms.
NOVELTY - Phosphorus oxychloride and 2-p-ethoxy-anilino-4-nitrobenzoic acid are mixed in molar ratio of 2:1 and reacted at 70-120 degrees C for 0.5-2 hours, to obtain 6-nitro-9-chloro-2-ethoxyacridine. The 6-nitro-9-chloro-2-ethoxyacridine is added to polar aprotic solvent to dissolve, polyhydric aliphatic alcohol and activating reagent which is phosphorus oxychloride are added, then adding ammonia source is added at -10 degrees C to 20 degrees C, and heated up to 80-180 degrees C for 1-7 hours, to obtain 6-nitro-9-amino-2-ethoxy-acridine.    USE - Preparation of ethacridine lactate intermediate.    ADVANTAGE - The ethacridine lactate intermediate is economically prepared with high yield, by a simple and safe process. The preparation process is environmentally-friendly.
NOVELTY - Chlorpyrifos is synthesized by putting trichloroacetyl chloride, acrylonitrile, o-dichlorobenzene, and copper(I) chloride (CuCl) catalyst into reactor, increasing temperature, refluxing, guiding dry hydrochloric acid (HCl) gas into reactor, refluxing for 8-10 hours, removing low-boiling-point substance, adding aqueous alkali in feed, reacting for 2-3 hours at 55-65 degrees C, filtering, obtaining crude product after cooling to 5-25 degrees C, adding crude product into reactor containing water, catalyst, and alkali, increasing temperature, refluxing for 3-4 hours, separating out solvent, and precipitating.    USE - Synthesis of chlorpyrifos (claimed).    ADVANTAGE - Method is easy to perform, produces high yield, reduces environment pollution, and guarantees sustainable development.    DETAILED DESCRIPTION - Chlorpyrifos is synthesized by putting trichloroacetyl chloride, acrylonitrile, o-dichlorobenzene, and copper(I) chloride (CuCl) catalyst into reactor, increasing temperature, refluxing, guiding dry hydrochloric acid (HCl) gas into reactor, refluxing for 8-10 hours, removing low-boiling-point substance, adding aqueous alkali in feed, reacting for 2-3 hours at 55-65 degrees C, filtering, obtaining crude product after cooling to 5-25 degrees C, adding crude product into reactor containing water, catalyst, and alkali, increasing temperature, refluxing for 3-4 hours, separating out solvent, precipitating crystal in aqueous phase, centrifuging to obtain wet trichloropyridine-hexoxyl potassium, drying to obtain dried trichloropyridine-hexoxyl potassium product, putting trichloropyridine-hexoxyl potassium into reactor, adding water, boric acid, and catalyst, stirring and heating to 75-80 degrees C, maintaining pH at 9-10, dripping ethyl chloride, maintaining for 3-5 hours, performing phase-splitting to separate oil phase, adding absolute ethyl alcohol into oil phase, recrystallizing, filtering, and air-drying.
NOVELTY - N,N-dihydroxymethylglycine and dimethyl phosphite are polymerized, to produce glyphosate methyl ester. The obtained reaction solution is acidolyzed using hydrochloric acid, to produce glyphosate and methylal. The obtained liquid is cooled and then esterified using 35% of hydrochloric acid for 1.5-2.5 hours at 50-115 degrees C. The obtained solution is distilled at normal pressure to remove methylal and methanol low-boiling-point substance. The obtained solution is distilled at 115 degrees C for 0.5-1.5 hour at 0.085 MPa to remove extra acid and finish hydrolysis, to obtain glyphosate.    USE - Manufacture of glyphosate used for potassium fertilizer.    ADVANTAGE - The method enables economical and environmentally-friendly manufacture of glyphosate in short period. The manufacturing process saves energy.    DETAILED DESCRIPTION - Glycine and polyformaldehyde are subjected to addition reaction using methanol solvent in presence of potassium hydroxide catalyst, to produce N,N-dihydroxymethylglycine. The N,N-dihydroxymethylglycine and dimethyl phosphite are subjected to polymerization reaction to produce glyphosate methyl ester. The obtained reaction solution is acidolyzed using hydrochloric acid, to produce glyphosate and methylal. The obtained liquid is cooled and then esterified using 35% of hydrochloric acid (3.3-3.5 mol) for 1.5-2.5 hours at 50-115 degrees C. The obtained solution is distilled for 45 minutes to 1 hour at normal pressure to remove methylal and methanol low-boiling-point substance. The obtained solution is distilled at 115 degrees C for 0.5-1.5 hour at 0.085 MPa to remove extra acid and finish hydrolysis, to obtain glyphosate.
NOVELTY - Ruthenium-based ammonia synthesis catalyst (I) having ruthenium-ammonia complex as precursor, is new.    USE - Used as ruthenium-based ammonia synthesis catalyst having ruthenium-ammonia complex as precursor.    ADVANTAGE - The catalyst has high performance and low cost. The preparation method: is simple and short in preparation time; has high production efficiency; and is energy-saving, environment-friendly, and suitable for large scale production.    DETAILED DESCRIPTION - Ruthenium-based ammonia synthesis catalyst of formula ((RuL+M1+M2)/AC, (M1-(RuL+M1+M2))/AC, ((RuL+M1+M2)-M1)/AC, or ((RuL+M1+M2)-M2-M1)/AC) (I) having ruthenium-ammonia complex as precursor, is new.    RuL = water-soluble ruthenium complex obtained by reacting ruthenium potassium with ammonia;    M1 = barium nitrate, barium acetate, magnesium nitrate, ammonium nitrate, aluminum nitrate and/or zirconium nitrate;    M2 = alkali metal e.g. sodium, potassium, rubidium and cesium, and/or nitrates, acetates, hydroxides or oxides of rare earth metals; and    AC = carrier, which is activated carbon or graphitized activated carbon.    An INDEPENDENT CLAIM is also included for preparation of (I).
NOVELTY - The present invention is related to a lignocellulose pretreatment method using white-rod fungus to selectively remove lignin. The present invention is characterized in that a semi-solid culturing method is used to inoculate the white-rod fungus Perenniporia tephropora capable of selectively decomposing lignin without decomposing cellulose into the agricultural waste or grass weed. Through the pretreatment of the white-rod fungus, the present invention can effectively reduce the lignin amount to increase the effect of the agricultural waste or grass weed to be decomposed by other cellulases to produce carbohydrate or is advantageous to use the residual cellulose as the raw material in paper making, alcohol production or the animal feedstuff.
NOVELTY - A processing system of organic wastewater has precipitation separation apparatus which collects organic wastewater and performs precipitation separation of high water content solid, transfer unit of high water content solid, volume reduction device which carries out dry reducing treatment of high water content solid, stirring unit, and injection unit for low oxygen superheated steam.    USE - Processing system of organic wastewater used in food-processing factory and supermarkets.    ADVANTAGE - Chemical agent is not required, and obtained dry organic refuse can be reused as soil improvement agent, biofuel processing, and raw material for compost.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the processing system. (Drawing includes non-English language text).    Office (1)    Filter apparatus (2)    Aeration treatment apparatus (3)    Precipitation separation apparatus (10)    Vacuum pump (13)
NOVELTY - Lactone is manufactured by contacting cycloalkene derivative and aluminosilicate and performing molecule cyclization.    USE - Manufacture of lactone for flavoring, pharmaceutical, or agrochemical.    ADVANTAGE - Bicyclic lactone can be selectively produced. Environmental impact of lactone manufacturing method is small.    DETAILED DESCRIPTION - Lactone of formula (2) is manufactured by contacting cycloalkene derivative of formula (1) and aluminosilicate and performing molecule cyclization.    ring A=cycloalkene ring which has 1 or 2 -C=C- unsaturated bond;    R1, R2=H or 1-5C alkyl group; and    ring B=cycloalkene ring which has cycloalkyl ring or 1 -C=C- unsaturated bond which is reaction residue of ring A.
NOVELTY - Producing soil enhancing substrate, comprises processing digestate obtained from biogas plants, mixing or contacting the digestate or liquid fraction of the digestate with at least one magnesium ion source and at least one phosphate ion- and/or hydrogen phosphate ion source, and optionally removing water from the substrate.    USE - The processed digestate is useful as terra preta-like substrate, fertilizer, or soil enhancer (all claimed).    ADVANTAGE - The method: produces the soil enhancing substrate in a cost-efficient manner; and reduces organic and inorganic components in extracted water. The soil enhancing substrate improves the ion storage and exchange capacity of soils.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for the soil enhancing substrate produced by the above method.
NOVELTY - Functional unlimited culture medium having a natural biocomposite inducer, comprises: (a) plant biomass with high levels of copper, vitamins and trace minerals; and (b) a natural inducer, which is plant vinegar.    USE - The functional unlimited culture medium or process is useful for culturing cell (claimed); and for obtaining biocomposites.    ADVANTAGE - The medium provides natural components that are inexpensive and nontoxic. It provides optimum conditions for cell culture and obtaining biocomposites without the addition of toxic substances, or synthetic or supplements. Biocomposites are achieved in short time compared to conventional crops at higher concentrations.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a functional unlimited culture medium having a natural biocomposite inducer, comprising: (a) cereal mixture incorporating a quantity of copper that does not exceed a concentration millimolar, especially vitamin B complex in at least micromolar concentrations and trace minerals in a concentration not exceeding millimolar; and (b) natural inducer, which is a vinegar Bambusoideae refined pharmaceutical grade;    (2) a culture process comprising carrying out cell growth in the medium; and    (3) a product obtained by the process.
NOVELTY - Lanthanum nitrate hexahydrate and chromium nitrate nonahydrate as starting material are subjected to hydrothermal treatment using sodium hydroxide as precipitant at 100-250 degrees C for 8-32 hours, to obtain spherical-shaped lanthanum chromate nanopowder with a particle diameter of 100-300 nm. The molar ratio of lanthanum and chromium in lanthanum nitrate hexahydrate and chromium nitrate nonahydrate is 0.8-1.3.    USE - Synthesis of lanthanum chromate nanopowder used for solid oxide fuel cell connector.    ADVANTAGE - The method provides lanthanum chromate nanopowder having excellent conductivity.
NOVELTY - The apparatus has an oil pressure relief valve controlling flow of fluid pressure generated in a hydraulic chamber. The hydraulic chamber is provided with an oil pressure generation piston. A hydrogen pressure control valve controls flow of the hydrogen pressure ejected to a cylinder part. The hydraulic chamber supplies brake oil to a wheel cylinder. A hydraulic conversion control unit controls pressure of the brake oil. A hydraulic braking part is fixed with the hydraulic conversion control unit. The cylinder part is connected with the oil pressure generation piston.    USE - Breaking pressure generating device for a fuel cell automobile.    ADVANTAGE - The device controls brake pressure at a hydrogen storage tank, reduces electric consumption, increases brake pressure rapidly and rising speed of brake pressure.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a breaking pressure generating device.'(Drawing includes non-English language text)'
NOVELTY - Treating (M1) biomass involves (i) treating the biomass with first hot water stream in temperature (T1) in the range of 100-170 degrees C to release minerals, (ii) treating the biomass with second hot water stream in temperature (T2) in the range of 140-200 degrees C to release hemicellulosic fraction, and (iii) treating obtained biomass matrix with third hot water stream in temperature (T3) in the range of 200-300 degrees C to torrefy the biomass to produce high energy solid product.    USE - For treating biomass which is useful in mineral product, hemicellulosic product, and high energy solid fuel product (claimed).    ADVANTAGE - The method is done in a concentrated way. The different treatment steps are carried out in the same reactor or chamber, which saves energy and time. Both the end product and the by-products are of good quality and useful and can be easily recovered. No flushing of the reactor for example with gas between the steps is required. No extra chemicals are required, such as acids or catalysts. This makes the method both simple and economic. The end product is a commercially viable biofuel fully compatible with fossil coal cofireable in existing boilers or coal power plants. Preferably the end product is hydrophobic mass. No dry torrefaction is required. This helps maintaining the hemicellulose fraction which would otherwise be burnt and lost in the dry torrefaction.
NOVELTY - The apparatus has a rotatable tube (5) having an inlet for receiving unprocessed biomass, an outlet for discharging processed biomass. A microwave generator applies electromagnetic energy to the rotatable tube containing biomass. A waveguide (9) associated with the microwave generator, introduces electromagnetic energy to the rotatable tube. The waveguide is adapted such that the electromagnetic energy introduced by the waveguide into and through the rotatable tube travels in a direction generally parallel to the longitudinal axis of the rotatable tube.    USE - Apparatus for processing biomass such as plant material, used for producing bio-oil for use as fuel for vehicle, activated carbon and/or recarburizer carbon used for manufacturing steel and for sugar industry, agricultural field, for inhibiting methane emissions from certain stock, and nut-coke (all claimed) used as fuel and as reducing agent in smelting iron ore in blast furnace.    ADVANTAGE - The biomass such as plants can be processed and converted into bio-oil, activated carbon and/or recarburizer carbon, and nut-coke in an energy efficient manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a method for processing biomass;    (2) a method of producing bio-oil from biomass;    (3) a bio-oil; and    (4) an activated carbon and/or recarburizer carbon.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the biomass processing apparatus.    Rotatable tube (5)    Waveguide (9)    Inlet end of housing (15)    Infeed hopper (23)    Auger (24)
NOVELTY - Producing (M1) triacylglycerides from renewable biomass, comprises culturing xylose-fermenting Rhodococcus bacterial cells.    USE - The method is useful for producing triacylglycerides from renewable biomass comprising xylose, xylan and/or xylose polymer (claimed).    ADVANTAGE - The method provides at least 40%, preferably at least 60% of the bacterial cell dry weight of triacylglycerides, during stationary phase of growth of the population of bacterial cells (claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for: (1) culturing (M1) Rhodococcus bacterial cells, comprising culturing, in culture medium supplemented with xylose, Rhodococcus bacterial cells that metabolize xylose for a time sufficient for the bacterial cells to produce triacylglycerides; (2) a culture medium produced by the method (M1); (3) a Rhodococcus bacterial cell that metabolizes xylose; (4) a cell population comprising the bacterial cell; (5) preparing a high concentration saccharified corn stover solution, comprising combining alkali with lignocellulose material, heating, purifying, drying, and grinding the material to obtain a fibrous powder, combining the fibrous powder with acid, hemicellulose, exoglucanase, endoglucanase, and beta -glucosidase to form a suspension having a pH of 3-7 and incubating the suspension at 20-70 degrees C; (6) a xylose-fermenting bacterial cell designated MITXM-61, deposited with the ATCC patent depository on October 26, 2011 having deposit number PTA-12196; and (7) a bacterial cell, or a mutated bacterial cell produced from the xylose-fermenting bacterial cell.
NOVELTY - Manufacture of hydrogen gas and hydrochloric acid gas involves electrolyzing water containing saline, separating hydrochloric acid gas and hydrogen gas based on specific gravity difference, and collecting.    USE - Manufacture of hydrogen gas and hydrochloric acid gas (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for drainage treatment method.
NOVELTY - Topical composition comprises at least a blue algae extract and at least one alpha hydroxy acid or its salts in combination with at least an excipient.    USE - The composition is useful: for preventing and/or treating aging signs of an organism, preferably skin, cutaneous and/or mucous membranes, affections of oral mucous membrane, and keratinous materials, preferably skin of body or face, lips, nails, hair, lashes and/or mucous membranes, for producing vascular endothelial growth factor for skin revascularization, elastin fibers, collagen and hyaluronic acid; and as an antioxidant (all claimed). Tests details are described but no results given.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the composition comprising obtaining blue algae biomass, which is harvested after a culture period of 10-20 days under conditions of temperature and luminance, washing and crushing the biomass, separating an aqueous fraction from the crushed biomass by centrifugation or filtration to obtain the blue algae extract, adding the alpha hydroxy acid or its salt and maltodextrin to the obtained solution, adjusting a pH of the solution to 6.5 using 0.1N sodium hydroxide, and eliminating water from the obtained solution by a process, preferably freeze-drying process, atomization or drying in a ventilated oven at low temperature.
NOVELTY - Removing acidic compounds contained in a gaseous effluent comprises absorption of the acidic compounds by contacting the gaseous effluent with an absorbent solution comprising water and at least one diamine compound (Q) comprising bis(amino-3-propyl)ether compounds (I) or (amino-2-ethyl)-(amino-3-propyl) ether compounds (II).    USE - The process is useful for removing acidic compounds contained in a gaseous effluent comprising natural gas, synthesis gases, flue gases, refinery gases, acid gases obtained from an amine unit, gases obtained from a unit of reduction in tail of Claus process, biomass fermentation gas, gases of cement factory, or smoke of incinerator, and for selective removal of hydrogen sulfide compared to carbon dioxide from a gaseous effluent comprising hydrogen sulfide and carbon dioxide (all claimed).    ADVANTAGE - The process selectively eliminates the acidic compounds contained in a gaseous effluent with low energy consumption and low operating costs.    DETAILED DESCRIPTION - Removing acidic compounds contained in a gaseous effluent comprises absorption of the acidic compounds by contacting the gaseous effluent with an absorbent solution comprising water and at least one diamine compound (Q) comprising bis(amino-3-propyl)ether compounds of formula (R-N(R)-(CH2)3-O-(CH2)3-N(R)-R) (I) or (amino-2-ethyl)-(amino-3-propyl) ether compounds of formula (R-N(R)-(CH2)2-O-(CH2)3-N(R)-R) (II).    R = CH3 or CH3CH2.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a process for removing acidic compounds contained in a gaseous effluent.    Regeneration column (C2)    Heat exchanger (E1)    Gaseous effluent (1)    Acidic compounds (2, 3)    Absorbent solution. (4)
NOVELTY - Method for controlling an oviposition of an insect, preferably cabbage fly, involves applying repellent produced by microorganisms.    USE - The method is useful for controlling oviposition of an insect, preferably cabbage fly (claimed), and developing a combined smell-free solid insect repellent fertilizer for organic farming of cabbage and other crops of the Brassica including cabbage, cauliflower, broccoli, Brussels sprouts and kale.    ADVANTAGE - The method increases farmers crop yield by stimulating the cabbage growth and reducing crop losses by the cabbage root fly.
NOVELTY - The system has a condensed water tank (6) storing condensed water condensed by heat exchange in a heat exchanger structure (50). A fuel gas is generated by reforming source gas using the condensed water stored by the condensed water tank as modification water. A control apparatus (19) operates an air supply part i.e. air blower (20), and makes the condensed water to flow through an off-gas path (29a, 29b) in thawing mode at time of starting the system. Air operates the heat exchanger structure, and is made to flow through condensed water tank by heat exchange with hot storage water.    USE - Fuel cell system for modifying a raw material i.e. hydrocarbon, by steam reforming and producing electric power with generated fuel.    ADVANTAGE - The system operates the air supply part and makes the condensed water to flow through the off-gas path at thawing mode at the time of starting of the system, so that the air, which operates the heat exchanger structure, is made to flow through the condensed water tank and heated by heat exchange with the hot water storage water, thus thawing frozen modification water utilized for steam reforming without applying cost by components addition.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for controlling a fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a fuel cell apparatus.'(Drawing includes non-English language text)'    Condensed water tank (6)    Control apparatus (19)    Air blower (20)    Off-gas paths (29a, 29b)    Heat exchanger structure (50)
NOVELTY - A temporary lavatory comprises toilet transit shed (3) with toilet bowl (3a) at closed space top-plate part of a fermenter (2) which accommodates decomposition promotion substance (S), stirring unit (4) which mixes and stirs excretion that falls from toilet bowl to decomposition promotion substance which contains ripe compost of cattle feces, pig feces, hen droppings, straw, fallen leaves and organic refuse, air supply unit which supplies air from exterior with respect to upward space of decomposition promotion substance, and air discharge unit which discharges air from upward space outside.    USE - A temporary lavatory (claimed).    ADVANTAGE - The lavatory can be used for a long time without the need for ladling and generating odor.    DESCRIPTION OF DRAWING(S) - The drawing shows a longitudinal cross-sectional view of the temporary lavatory.    Fermenter (2)    Toilet transit shed (3)    Toilet bowl (3a)    Stirring unit (4)    Decomposition promotion substance (S)
NOVELTY - A host cell comprising (a) a first membrane-bound protein or peptide bound directly or indirectly to an electrocatalyst molecule, (b) enzymes capable of synthesizing a biologically derived compound, and (c) optionally a second protein or peptide bound to the electrocatalyst molecule, is new. The first protein or peptide is bound to the second protein or peptide.    USE - The host cell is useful for producing biologically derived compound. The biologically derived compound is an alkane, alcohol, fatty acid, ester, or isoprenoid (all claimed). Can also be used in biofeul production.    ADVANTAGE - The host cell has capability for autotrophic growth, is amenable to metabolic engineering and expresses metabolic pathway that supports significant carbon flux. The method utilizes pyridine donors as building block for ligand design, as they support water-stable and water-soluble complexes with reasonable reduction potentials based on strong s-donor/mild p-acceptor properties, inexpensive catalysts containing accessible earth-abundant metal centers that are soluble and stable in microbial growth media, and integrated microbial-electrocatalytic system for efficient conversion of carbon dioxide and hydrogen to one or more biologically derived compounds, and maintains benefits of microbial processes, preferably low environmental impact and scalability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing a biologically derived compound, which involves (a) culturing host cell in a suitable medium, and hence the biologically derived compound is produced, and (b) optionally isolating the biologically derived compound.
NOVELTY - Achieving high biomass thermo-chemical conversion to liquid fuels, comprises (a) decomposing biomass to create one or more volatile hydrocarbons and a carbonaceous solid, (b) catalytically upgrading (23) the volatile hydrocarbons to liquid fuels, (c) gasifying the output carbonaceous solid to produce synthesis gas, and (d) catalytically upgrading the synthesis gas to a fuel or a fuel precursor.    USE - The method is useful for achieving high biomass thermo-chemical conversion to liquid fuels such as gasoline, gasoline components, jet fuel, diesel, naphtha, oxygenate fuels, higher mixed alcohols, dimethyl ether, methane, light gas oil, ammonia or vacuum gas oil (all claimed).    ADVANTAGE - The method recycles water and carbon dioxide produced in the fuel production process thus increasing efficiency of biomass conversion.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a system for achieving high biomass thermo-chemical conversion to liquid fuels comprising the steps (a)-(d) as above per se.    DESCRIPTION OF DRAWING(S) - The figure shows a block diagram of a method for achieving high biomass thermo-chemical conversion to liquid fuels.    Thermo chemical process (20)    Catalytic upgrading the volatile hydrocarbons to liquid fuels (23)    Liquid fuel and chemicals (25)    Syngas generation (27)    Fuel separation process. (32)
NOVELTY - Producing ethanol, comprises: esterifying acetic acid and ethanol in first reaction zone to give vapor phase esterification product having ethyl acetate, ethanol, water and acetic acid; separating at least a portion of the product in first column to get first distillate of ethyl acetate, ethanol, and water, and first residue of acetic acid; biphasically separating at least a portion of distillate in decanter (120) into organic phase with ethyl acetate and aqueous phase with ethanol and water; and reacting at least a portion of organic phase with hydrogen in second reaction zone to get ethanol.    USE - The method is useful for producing ethanol (claimed) that is used as e.g. fuel, blend for other fuels (gasoline), solvents for toiletry, chemical feedstocks (e.g. vinegar), sanitizers, hydrogen transport or consumption.    ADVANTAGE - The method: forms minor amounts of impurities; utilizes acetic acid that is cost effective, thus providing cost effective ester, simplifying the esterification system and allowing minimal ethyl acetate separation; utilizes minimal amount of water, thus reducing number of distillation columns and separation capital for ethanol recovery; and avoids recycling ethanol through hydrogenolysis reactor that leads to capacity restraints and additional capital costs, thus providing commercially feasible scale for producing ethanol and improving recovery.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic diagram of ethanol production that directly feeds the organic phase of the esterification product produced by vapor esterification to the hydrogenolysis zone.    Esterification zone (101)    Vaporizer (107)    Decanter (120)    Recovery column (131)    Hydrogenolysis reactor (140)
NOVELTY - The method involves purifying waste water in rainwater spacer, so as to produce purified water for electrolysis and for drinking. The solar energy is converted into electrical energy by photovoltaic system. The purified water is split into hydrogen and oxygen by electrolysis. The hydrogen is compressed by hydrogen compressor and stored in a hydrogen tank, at sun-rich months. The electric power is produced by stored hydrogen and supplied at low weather-related days. The electrical energy is fed to city power plant so to supply electric power based on computer controlled program.    USE - Water and solar energy based method of producing and supplying electric power to estate and automobile (all claimed) e.g. car. Can also be used in supply of electric power to commercial/industrial area such as office, school and building.    ADVANTAGE - The electric power can be supplied reliably based on different energy resources. The energy resources can be utilized efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating the water and solar energy based process of producing and supplying electric power. (Drawing includes non-English language text)
NOVELTY - The device has a main body provided with a water pipe, a solar battery board, a floating head, a storage battery, a motor speed reducer, a rotating shaft and an impeller. A water outlet pipe is fixed on an upper plane of a water lifting pipe. An output shaft of the motor speed reducer is coaxially connected with the rotating shaft. The water pipe is fixed with a telescopic rod. An upper end of the telescopic rod is hinged on the solar battery board. The water lifting pipe is symmetrically fixed with the storage battery.    USE - Solar energy river sewage purification device.    ADVANTAGE - The device adopts a solar panel for absorbing solar power and charging up the storage battery to drive a motor and the impeller to rotate so as to pump lower sewage from a watercourse to a surface layer through a water lifting pump, so that the sewage is fully in contact with oxygen in air to increase oxygen content in the sewage, thus enhancing activity of aerobic micro-organisms in the sewage, quickly propagating the aerobic micro-organisms and quickly decomposing organic nutrient substances in a river, and hence realizing self-purification and zero-emission function in an effective manner.
NOVELTY - A biomass gasification pyrolysis furnace comprises furnace body and tower. The furnace body comprises cuboid bricks. The lower part of furnace is provided with smoke channel which is connected to tower. The four side-openings of furnace body are provided with U-shaped water sealing tank. The water tank is provided with circular sealing cover and sealing groove. The lower part of furnace body is built with bricks with 30-50 mm gap. The tower is a sealed metal cylinder with metal hollow tubes. The metal tube is welded to cold water pipe at upper end, and to hot water pipe at other end.    USE - A biomass gasification pyrolysis furnace.    ADVANTAGE - The furnace has small volume, small investment and high efficiency. It is convenient to use for any occasion.
NOVELTY - The anaerobic reactor has a warming heating pipe whose two ends of the inlet and outlet are respectively installed with a water inlet pump. A water pump is set with a solar energy heat collecting device. The lower port is connected with pre-treatment tank. A pipeline is connected to the underground embedded with biogas residue biogas liquid tank.    USE - Anaerobic reactor.    ADVANTAGE - The anaerobic reactor has compact structure, reasonable design and low cost. The stability of the anaerobic reactor can be improved be improved.
NOVELTY - Microbial deodorizing inoculant comprises Pichia jadinii yeast strain preserved in China microorganism bacterial strain preservation management committee common microorganism center under preservation number of CGMCC No.5982 and Saccharomyces cerevisiae yeast strain preserved in China microorganism bacterial strain preservation management committee common microorganism center under preservation number of CGMCC No. 5984.    USE - The microbial deodorizing inoculant is useful for treating livestock and poultry excrement (claimed), and is useful for deodorizing a public toilet.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a method for preparing microbial deodorizing inoculant, comprising activating Pichia jadinii yeast strain and Saccharomyces cerevisiae yeast strain into yeast extract peptone dextrose (YPD) solid slant culture medium, inoculating obtained product into an inoculants liquid culture medium and culturing for 24 hours, adjusting the bacteria content of two strains to 108 colony-forming unit (cfu)/ml, and combining the bacterial liquids to obtain liquid microbial deodorizing inoculant; and    (2) an use of microbial deodorizing inoculant for treating livestock and poultry excrement.
NOVELTY - A residential house drainage recovery fertilizer-preparing device comprises a residential house main body, a poultry house, ground ferment cultivating bed and planting bed space. One end of the poultry house is connected with the house and the other end is connected with drainage recovery device.    USE - A residential house drainage recovery fertilizer-preparing device.    ADVANTAGE - The device rationally utilizes agricultural waste to produce fertilizer and plant nutrient solution. It not only reduces space for placing waste and environmental pollution, but also saves overhead required to purchase fertilizer.
NOVELTY - The system has cheap soft sheets that are linked into a large-area leakage-proof cover curtain (12) for covering a large amount of garbage (11) in a low cylinder wall (4). The soft sheet of the cover covers on the outer wall of the inner ring (10) of the garbage. The cover curtain is provided with a rigid long-tubular chimney pipe having one port 0.3 m higher than the garbage. A bolt (16) is provided to pass through the soft sheet. The upper portion of an external distribution nut (13) is screwed.    USE - Soft sheet cover-curtain type garbage swamping system.    ADVANTAGE - The method for producing energy by wastes is simplified effectively. The large pressure uniform ridging is formed efficiently to strengthen the pressure seal and to avoid pollution. The manufacturing cost of the soft sheet cover-curtain type garbage swamping system is cheaper.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the soft sheet cover-curtain type garbage swamping system.    Low cylinder wall (4)    Inner ring (10)    Garbage (11)    Large-area leakage-proof cover curtain (12)    External distribution nut (13)    Bolt (16)
NOVELTY - The heat ventilation system comprises a ground source heat pump system whose tail end of a pipeline is connected with a biogas pool to convey heat for increasing the temperature of the biogas pool. The pipeline of the ground source heat pump system is connected with a photo-thermal system. A tail end of the ground source heat pump is provided with a warming disk pipe and a capillary pipe. The warming disk pipe is arranged on a bottom part of the biogas pool. The capillary pipe is placed on a pool wall of the biogas pool.    USE - Used as a heat ventilation system.    ADVANTAGE - The heat ventilation system avoids influence of weather and energy waste.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a method for warming biogas pool; and    (2) a biogas pool.    DESCRIPTION OF DRAWING(S) - The figure shows a flow chart of a heat ventilation system (Drawing includes non-English language text).
NOVELTY - The reactor has an air returning system that conveys secondary air to blast system. A film closed system is matched with fermentation tank for sealing organic wastes in fermentation groove. An air supply pipe is connected with fermentation tank and fan respectively. One end of air return pipe of air returning system is connected to the fermentation groove. The other end of the air return pipe is connected with blower and waste gas discharge pipe. A valve is provided in the waste gas discharge pipe which is connected with air supply pipe and fan of air blowing system respectively.    USE - Solid organic waste aerobic fermentation reactor.    ADVANTAGE - The temperature of the solid organic waste is raised by the solid organic waste aerobic fermentation reactor quickly. The solid organic waste heat utilization rate of the aerobic fermentation reactor is improved. The odor sealed environment effect is ensured by the aerobic fermentation reactor.
NOVELTY - The pool structure has a supporting case (1), a heat preservation layer (2), a soft film (3), biogas tank, an upper plate, a cover (6), an air outlet pipe (7), a raw material inlet (8), a force opening pressure air pump, a heat pipe (9) and a storage bag. The soft film is provided on the biogas tank with the supporting case. The pool structure main portion is arranged between a radiator (12) and marsh gas tank (4) and is connected to a compression pump.    USE - High-efficient marsh gas pool structure.    ADVANTAGE - The pool structure main portion is arranged between a radiator and marsh gas tank, hence safety can be ensured. The light weight, high efficiency and heat preservation effect can be improved effectively. The simplified structure can be achieved. The cost can be reduced. The structure can be transported conveniently.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the high-efficient marsh gas pool structure.    Supporting case (1)    Heat preservation layer (2)    Soft film (3)    Marsh gas tank (4)    Cover (6)    Air outlet pipe (7)    Raw material inlet (8)    Heat pipe (9)    Radiator (12)
NOVELTY - The reactor has several upper baffled plates that are arranged on the top of the reactor and lower baffled plates are arranged on the bottom of the reactor. The upper baffled plates and the lower baffled plates are all arranged vertically, tow ends of the reactor are respectively provided with a water inlet pipe and a water outlet pipe. The upper and lower baffled plates separate the reactor into six compartments along the water flow direction.    USE - Separating type anaerobic baffled reactor.    ADVANTAGE - The acid production and methane production are achieved in different compartments so that acid production and methane production are separated physically.
NOVELTY - A biogas digester stirring apparatus comprises an ejector, a high-pressure water supply facility and a water pipe connected with the ejector and the high-pressure water supply facility. The ejector is arranged in biogas digester feed liquid for ejecting high-pressure water to carry out jet agitation for the feed liquid.    USE - Biogas digester stirring apparatus.    ADVANTAGE - Position of the ejector in the biogas digester is adjustable. The stirring apparatus can uniformly and fully stir the feed liquid, improving testa chipping effect and ensuring the biogas digester gas production rate through adjusting the position of the ejector.
NOVELTY - Method for preparing ethanol using urban domestic garbage, involves subjecting household garbage to enzymatic hydrolyzing process, and fermenting the hydrolyzed product using Saccharomyces cerevisiae.    USE - The method is useful for preparing ethanol using urban domestic garbage (claimed).
NOVELTY - A biological medical fertilizer comprises elemental fertilizer and biological protein.    USE - Biological medical fertilizer for rice, tomato, apple, pepper and crops.    ADVANTAGE - The fertilizer has high suspension rate, good dispersibility, has strengthened ability to resist disease of crops. It effectively supplements trace elements to meet crop nutrient demand, is safe to the environment, human and animal, and has no toxic residue and small dosage. The fertilizer also increases yield rate to more than 5%.
NOVELTY - Distilled water is added with amoxicillin in three-mouth bottle, heated in water bath, stirred and dissolved, to obtain suspension. Sodium salt powder and amoxicillin are added, sodium salt powder is slowly added, and filtered to remove the solid impurity. Filtrate is provided in the crystallizer and stirred. Entrainer is added to azeotropic distillation, entrainer is additionally added, and crystallizer liquid is continuously added. Azeotropic distillation is performed, cooled, crystallized, filtered, washed and dried, to obtain amoxicillin sodium crystal.    USE - Preparation of amoxicillin sodium crystal (claimed).    ADVANTAGE - The amoxicillin sodium crystal is economically prepared with high purity, and excellent liquidity and stability without polluting the environment.    DETAILED DESCRIPTION - Distilled water is added with amoxicillin in the mass ratio of 100:10-25 in the three-mouth bottle, heated in water bath at 25-45 degrees C, stirred and dissolved completely, to obtain suspension. The sodium salt powder and amoxicillin are added in the molar ratio of 0.3-1:1, sodium salt powder is slowly added until the solution is clear, and then filtered to remove the solid impurity. The filtrate is provided in the crystallizer, heated in water bath at 30-50 degrees C and stirred. Entrainer is added to the azeotropic distillation, vacuum degree is maintained to 0.05-5 MPa, entrainer is additionally added for 2-3 times, and crystallizer liquid level not changed is continuously added. The content of the water in the crystallizer is gradually reduced to the solution in the crystallizer water quality content of 5-15%, azeotropic distillation is performed under reduced pressure, and cooling and crystallizing are controlled. The final temperature is controlled at 10 degrees C, temperature in the crystallizer is not changed continuously, stirred for 20 minutes to 1.5 hours, then filtered, washed and dried, to obtain amoxicillin sodium crystal.
NOVELTY - Ecological organic fertilizer comprises base material and nutrient solution in a mass ratio of (800-1200):1. The base material comprises 0-90 pts. wt. pig manure, 0-6 pts. wt. chicken manure, 0-8 pts. wt. bean dregs, 0-4 pts. wt. wheat bran, 0-3 pts. wt. sugar, 0-2 pts. wt. lees, 0-19 pts. wt. beer lees, and 0-4 pts. wt. corn powder (where the amount of raw materials is more than zero and not simultaneously zero). The nutrient solution comprises complex strain and water. The complex strain comprises e.g. lactic acid bacteria, Bacillus subtilis and Lactobacillus plantarum.    USE - Used as an ecological organic fertilizer.    ADVANTAGE - The fertilizer: efficiently improves physical, chemical and biological properties of soil and cures soil, comprises green manure, which enhances the fertilizing and buffering capacity of soil; is rich in organic matter and various nutrient elements, and hence provides essential nutrition to crops; promotes crop growth and improves the quality of agricultural products; and can be easily absorbed by crops and hence has improved utilization rate.    DETAILED DESCRIPTION - Ecological organic fertilizer comprises base material and nutrient solution in a mass ratio of (800-1200):1. The base material comprises 0-90 pts. wt. pig manure, 0-6 pts. wt. chicken manure, 0-8 pts. wt. bean dregs, 0-4 pts. wt. wheat bran, 0-3 pts. wt. sugar, 0-2 pts. wt. lees, 0-19 pts. wt. beer lees, and 0-4 pts. wt. corn powder (where the amount of raw materials is more than zero and not simultaneously zero). The nutrient solution comprises complex strain and water. The complex strain comprises lactic acid bacteria, yeast, photosynthetic bacteria, Gram-positive actinomycetes bacteria, fermentative filamentous bacteria, Bacillus subtilis, Bacillus natto, Lactobacillus plantarum, Bacillus licheniformis, highly active enzymes and growth factors in a mass ratio of (2-3):(3-4):(1-2):(1-2):(1-2):(1-2):(1-2):(1-2):(1-2):(1-2):(1-2).
NOVELTY - Spiral-type in situ purification device comprises a rainwater collecting port connected with an overflow distribution well. Both the sides of the overflow distribution well are provided with a rainwater retention chamber. The overflow distribution well is connected with the rainwater retention chamber by a water pipe. The overflow distribution well is provided with an adjustable overflow weir. The rainwater retention chamber is placed in suspension of biological filler ball. The inner wall of the overflow distribution well is provided with a spiral shaped body.    USE - The spiral-type in situ purification device useful for treating municipal polluted rainwater (claimed).    ADVANTAGE - The purification device ensures removal of more than 75% particulate biodegradable organic matter in the rainwater; reduces pollution of river by rainwater; improves the quality of the rainwater; and reduces ecological pollution.    DETAILED DESCRIPTION - Spiral-type in situ purification device comprises a rainwater collecting port connected with an overflow distribution well. Both the sides of the overflow distribution well are provided with a rainwater retention chamber. The overflow distribution well is connected with the rainwater retention chamber by a water pipe. The overflow distribution well is provided with an adjustable overflow weir. The rainwater retention chamber is placed in suspension of biological filler ball. The inner wall of the overflow distribution well is provided with a spiral shaped body. The rainwater retention chamber is provided with six layers, which together forms a labyrinth intestinal type structure. The upper part of the rainwater retention chamber is designed to form a bending pipe and the rainwater retention chamber surrounds the overflow distribution well.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the spiral-type in situ purification device for treating municipal polluted rainwater.
NOVELTY - A freckle removing facial mask contains 8-15 g, preferably 10 g white batryticatus silkworm, 8-15 g, preferably 10 g Rhizoma typhonii, 8-15 g, preferably 10 g Radix angelicae, 8-15 g, preferably 10 g Rhizoma kaempferiae, 8-15 g, preferably 10 g borax, 10-20 g, preferably 16 g gypsum, 10-20 g, preferably 16 g talc, 5-10 g, preferably 7 g clove and 1-5 g, preferably 7 g borneol.    USE - Facial mask is used for removing freckle.    ADVANTAGE - The facial mask is environmentally-friendly and efficiently removes dark spots.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparation of freckle-removing facial mask, which involves mixing raw materials with distilled water; and    (2) usage method of freckle-removing facial mask, which involves preparing the film back into paste with distilled water, uniformly coating on the face, removing after 15-20 minutes, and then cleaning face with clean water.
NOVELTY - Betaine is dispersed in water, nitric acid is added, the temperature is controlled to 20-60 degrees C, preserve heat for 20 minutes, stirred at less than 65 degrees C, and water is vacuum removed, cooled to less than 10 degrees C. The obtained solids are precipitated, filtrated, and dried, to obtain betaine nitrate. The precipitated solid is collected as liquid mother liquor and used in the production cycle.    USE - Preparation of betaine nitrate (claimed).    ADVANTAGE - The Preparation of high-quality betaine nitrate is economically and efficiently prepared with high productivity by a simple and environmentally-friendly process in a short period of time.
NOVELTY - Preparing bio-fuel process inhibitor by degrading acid hydrolysis plant fiber comprises (a) preprocessing the plant fiber with a solution containing furfural and its derivative, adjusting pH value with alkali; (b) culturing a strain capable of producing laccase and cellulose, centrifuging and collecting the fermentation liquid, salting out and dialysis to obtain laccase-cellulase enzyme; and (c) enzymolyzing.    USE - The method is used for preparing bio-fuel process inhibitor by degrading acid hydrolysis plant fiber (claimed).    ADVANTAGE - The method above has simple steps and allows large-scale production.
NOVELTY - The device has several sludge fermentation devices which are connected with several sludge fermentation devices for ventilation of sludge fermentation device for oxygen ventilation device. The ventilation device is connected with a fan, and is provided with multiple temperature sensors in the sludge fermentation device. The temperature sensor is provided to collect the temperature data and to control the temperature of sludge fermentation devices. The temperature control device is connected with the ventilation device.    USE - Sludge treatment device.    ADVANTAGE - The temperature control device controls the temperature parameter of sludge fermentation device by temperature sensor, and the ventilating device is provided for ventilating and cooling the sludge fermentation device, so that stable sludge fermentation device is provided to ensure the quality of the organic fertilizer.
NOVELTY - A biomass and oil shale low-temperature hot carbonization pyrolyzing furnace comprises combustion chamber arranged in carbonization chamber connected with raw material preheating chamber having heat collector.    USE - Biomass and oil shale low-temperature hot carbonization pyrolyzing furnace.    ADVANTAGE - The furnace produces high calorific value coal from biomass and oil shale. When using the furnace, the process is continuous and has high recovery rate.
NOVELTY - Organic fertilizer is prepared by spreading silkworm feces, mixing grenadine syrup, lactic acid bacteria and yeast to obtain fermentation liquid, spraying the fermentation liquid on spread silkworm feces, again spreading a layer of silkworm feces, again uniformly spraying the fermentation liquid on spread silkworm feces, covering a film on the silkworm feces, incubating the silkworm feces, adding phosphorus and potassium to the silkworm feces to obtain mixture, and pelletizing, drying and packing the mixture to obtain finished product.    USE - The organic fertilizer is useful for stimulating endogenous hormone secretion of plants.    ADVANTAGE - The fertilizer is environmentally-friendly, avoids the need of nitrogenous fertilizer for prompting growth, has excellent quality, and enhances the tillering capacity of plant cells.    DETAILED DESCRIPTION - Organic fertilizer is prepared by spreading silkworm feces to a height of 10-15 cm, mixing 10 wt.% grenadine syrup, lactic acid bacteria and yeast in the proportion of (250-350):(40-60):1, obtaining fermentation liquid after uniformly stirring the grenadine syrup, lactic acid bacteria and yeast, uniformly spraying the fermentation liquid on the spread silkworm feces until the silkworm feces are wet through exactly, again spreading a layer of silkworm feces to a height of 10-15 cm, again uniformly spraying the fermentation liquid on spread silkworm feces until the silkworm feces are wet through exactly, covering a film on the silkworm feces, incubating the silkworm feces for 15-30 days, again covering the silkworm feces with a film for 10-15 days, adding phosphorus and potassium to the silkworm feces, in a ratio of 100:(3-6):(1-4) to obtain mixture, and pelletizing, drying and packing the mixture to obtain finished product.
NOVELTY - The composting device has a fermenting tank (1) whose is covered by cement. A spiral stirrer (4) powered by a motor (6) is arranged in the vertical inner wall of the fermentation tank. A gas path system is fixed in the bottom of the fermenting tank and connected with a heat circulation pipeline (3). A solar energy water heater (5) is connected with a thermal cycle pipeline system through a water pump for circulating hot water. A three-way valve switch is connected with the solar energy water heater. The gas path system is connected with a fan.    USE - Organic agriculture waste composting device used in rural northern region.    ADVANTAGE - The fermentation time of organic agriculture waste can be reduced. The fermentation temperature of the composting device can be improved. The efficiency of compost fertilizer can be improved. The organic waste composting device is combined with extract from corn fermentation product of cellulose to improve the compositing efficiency and to reduce the composting time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for composting organic agriculture waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the organic agriculture waste composting device.    Fermenting tank (1)    Heat circulation pipeline (3)    Spiral stirrer (4)    Solar energy water heater (5)    Motor (6)
NOVELTY - The turner has control chamber (2) which is located on the machine frame (1). The sides of movable device (3) are provided with a transmission device (4), lifting device (5) and turning device (6). A motor (7) is provided to transmit power to a speed reducer (8). A stirring paddle (11) is provided with paddle arms (11-1). The machine frame is installed on the left and right sides of bracket (12). The bracket is equipped with a blocking plate.    USE - Material turner.    ADVANTAGE - The service life of the turner can be improved effectively. The scattering of material from the fermenter to the back sides can be prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the material turner.    Machine frame (1)    Control chamber (2)    Movable device (3)    Transmission device (4)    Lifting device (5)    Turning device (6)    Motor (7)    Seed reducer (8)    Stirring paddle (11)    Paddle arms (11-1)    Bracket (12)
NOVELTY - A fertilizer automatic production line system comprises a raw material storage tank, a spiral feeder, a discharging port, a weighing sensor of a static measuring bin, a belt transmission and lifting material loading machine, a bottom discharging opening of the static measuring bin, a mixing stirrer, a discharge hole, a vibration screening machine, a spiral conveyor, a bucket elevator, a granulator, and an automatic quantitative packing machine.    USE - A fertilizer automatic production line system.    ADVANTAGE - The system achieves feeding accuracy and automatic batching, and avoids pollution.
NOVELTY - A concentrated liquid fertilizer comprises beer yeast, acetobacter, and Lactobacillus acidophilus prepared by microbial fermentation, where the fermentation culture medium comprises 1-10% potato, 2-15% brown sugar, 1-2% peptone, 0.01-0.2% sulfuric acid, 0.01-0.2% manganese sulfate, 0.01-1% potassium, 1-2% sodium chloride, and 69.6-96.8% water.    USE - The concentrated liquid fertilizer is used for promoting growth of plants.    ADVANTAGE - The concentrated liquid fertilizer strengthens and effectively promotes the progress of the crops in various physiological process, improves and promotes photosynthesis, and effectively transports organic matter so as to increase the yield and improve quality of plants.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for preparing the concentrated liquid fertilizer by preparing beer yeast, acetobacter and L. acidophilus, inoculating and fermenting, and heat treatment to sterilize.
NOVELTY - Preparing biological fertilizers from corn soaking liquid, involves concentrating corn soaking liquid, adding filtered mud and alkali to the concentrated corn soaking liquid for performing neutralization, adding the corn soaking liquid to mixed pre-fermentation device, adding filter mud and fiber residue to fermentation device, inoculating biological strain to anaerobic fermentation device, and drying product, granulating dried product, cooling the granulated product, and sieving the cooled product.    USE - The method is useful for preparing biological fertilizers from corn soaking liquid (claimed).    ADVANTAGE - The method reduces environmental pollution and environmental pressure. Nutrition and irrigation requirements of local farmers are met.    DETAILED DESCRIPTION - Method for preparing biological fertilizers from corn soaking liquid, involves concentrating corn soaking liquid, adding filtered mud and alkali to the concentrated corn soaking liquid for performing neutralization, regulating the pH of the solution to 5-6, adding the corn soaking liquid to pre-fermentation device, adding filter mud and fiber residue to fermentation device, where pre-fermentation is carried out after uniformly mixing corn soaking liquid, filter mud and fiber residue, inoculating biological strain to anaerobic fermentation device, where the fermentation is carried out at 28-30 degrees C, and fermented products are added with ingredients, and drying product, granulating dried product, cooling the granulated product, and sieving the cooled product.
NOVELTY - The barrel comprises a support (1), a cross beam (9), a clamp seat (2) and the fermentation barrel main unit (7). The barrel main unit is provided with multiple temperature control probes (5). The cross beam is provided with a temperature control box (8). The bottom portion of the barrel main unit is provided with a wire outlet. The temperature control probe is connected with the temperature control box through the data wire (4). The data processing module is connected with the battery box and the display screen.    USE - Barrel for fermentation of animal excrement, straw and other waste for preparing fertilizer.    ADVANTAGE - The structure of the barrel is simplified. The barrel is convenient to use. The fermentation temperature can be monitored effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of using fermentation barrel.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fermentation barrel.    Support (1)    Clamp seat (2)    Data wire (4)    Temperature control probe (5)    Fermentation barrel main unit (7)    Temperature control box (8)    Cross beam (9)
NOVELTY - Complex fertilizer comprises an organic fertilizer and an inorganic fertilizer and prepared by fermenting and mixing organic and inorganic fertilizers and pelletizing. The organic fertilizer is fermented and deodorized livestock manure with rice hull or straw. The inorganic fertilizer is urea, ammonium phosphate, potassium chloride and/or potassium sulfate.    USE - Used as a complex fertilizer.    ADVANTAGE - The fertilizer has simple processing method, comprises the required nutrients, improves soil hardening, and promotes stable and high agricultural yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the complex fertilizer comprising: (i) mixing livestock manure, rice hull and straw (organic fertilizer raw material), composting and fermenting, and drying; and (ii) adding urea, ammonium phosphate, potassium chloride and potassium sulfate (inorganic fertilizer), mixing and stirring, heating to 90-100 degrees C, granulating and drying in a rotary drum, cooling, and sieving to obtain the finished product.
NOVELTY - Fertilizer composition comprises 80-92 wt.% composted duck manure, 3-10 wt.% calcium superphosphate, 1-5 wt.% potassium dihydrogen phosphate, 1-2 wt.% dipotassium phosphate, 0.5-5 wt.% calcium carbonate, 0.02-0.5 wt.% zinc sulfate, 0.04-1 wt.% manganese sulfate, 0.1-0.6 wt.% copper sulfate, 0.5-1 wt.% magnesium sulfate, 0.1-0.7 wt.% ferrous sulfate heptahydrate, 0.02-0.2 wt.% ammonium molybdate, 0.02-0.35 wt.% boric acid, 0.01-0.3 wt.% citric acid and 0.3-0.5 wt.% Melosira.    USE - The fertilizer composition is useful for farming pearl oyster.    ADVANTAGE - The composition has sufficient organic nutrients and micronutrients, and rapidly supplements organic residues needed by pearl oyster and nitrogen, phosphorus, potassium and various trace elements needed by phytoplankton and zooplankton.
NOVELTY - The device has a granulating device that is connected with a drying device. The drying device is connected with a collecting device through a transmission device. The transmission device is provided with a baffle plate. The inner baffle plate is provided with a cooling device.    USE - Organic fertilizer production device.    ADVANTAGE - The device avoids the damage of conveyor belt. The service life and the production efficiency of the conveyor belt can be improved be improved.
NOVELTY - The organic fertilizer fermenting machine has a fermentation cylinder that is set on a base. A motor is electrically connected with an electric control box. The motor is provided with a rotating shaft. The rotating shaft passes through the middle portion of fermentation cylinder. The motor drives the rotating shaft to rotate. An air purifier located at the upper portion of the fermentation cylinder. A microwave electromagnetic heater is located at the two ends of an outer wall of the fermentation cylinder.    USE - Organic fertilizer fermenting machine.    ADVANTAGE - The machine has high efficiency, saves energy, strong adaptability and strong practicability.
NOVELTY - Microwave cracking biomass continuous production device comprises a carbide furnace shell, and conveyor belt installed in the carbide furnace shell. The furnace carbon shell is divided into microwave dry distillation cracking chamber and cooling chamber. The microwave dry distillation cracking chamber is divided into micro-positive pressure section, pre-heating section, middle-temperature area, and micro high temperature dry distillation section. The microwave dry distillation cracking chamber is installed in the shell with a microwave wire.    USE - Microwave distillation cracking biomass continuous production device.    ADVANTAGE - The device improves the charcoal yield, and saves heat energy.
NOVELTY - Preparing functionalized heterobicyclic compound (Ia), comprises (a) reacting 1,2-diamine compound (I) with 1,2-diketone compound (II) in the presence of surfactant as a catalyst in aqueous medium, and (b) obtaining (Ia) from reaction mixture of step (a).    USE - The process is useful for preparing functionalized heterobicyclic compound which is a quinoxaline derivative or a heterocyclic pyrazine derivative (all claimed).    ADVANTAGE - The process: provides (Ia) at an improved yield of 79-98% (claimed); utilizes water as a solvent rather than volatile/toxic organic solvents, and biocompatible, nontoxic, cheap and easily available surfactants as a micellar catalyst instead of toxic or/and costly catalysts i.e. protic acid, metal Lewis acid, organocatalyst or ionic liquid; eliminates additional agent; minimizes the side product formation; and is a short reaction time, and one-pot, single step, simple workup procedure, hence potentially more economical.    DETAILED DESCRIPTION - Preparing functionalized heterobicyclic compound of formula (Ia), comprises (a) reacting 1,2-diamine compound of formula (I) with 1,2-diketone compound of formula (R1a-C(=O)-C(=O)-R2a) (II) in the presence of surfactant as a catalyst in aqueous medium, and (b) obtaining (Ia) from reaction mixture of step (a).    R1a, R2a = aryl, heteroaryl (both optionally substituted by either electron donating or electron withdrawing groups) or alkyl;    R4a = H, alkyl, electron donating substituent or electron withdrawing substituent;    R3a (if present) = H, alkyl, electron donating substituent or electron withdrawing substituent, where the electron donating substituent is alkyl, alkoxy, OH or N,N-dimethylamino, and the electron withdrawing substituent is nitro, CN, CF3, halo or alkoxycarbonyl (preferably alkyl is CH3 and alkoxy is OCH3); and    X1a = C, N or two N-atoms at 5th and 7th positions.
NOVELTY - Extracting remangilone A, comprises (i) crushing Physena madagascariensis leaves to crude powder, carrying out supercritical fluid extraction in an extracting kettle, pumping carbon dioxide and cosolvent, and collecting the extract, (ii) dissolving the extract in methanol, drying sample, placing in a high pressure silica gel column chromatography, using dichloromethane-acetone solvent system for gradient elution, collecting remangilone A fraction, vacuum extracting, concentrating, cooling and crystallizing to obtain crude crystal, and (iii) re-crystallizing with hexane-diethyl ether.    USE - The method is useful for extracting remangilone A.    ADVANTAGE - The method has simple extraction process; is suitable for large-scale production; consumes less energy; reduces pollution; and has environmentally friendly production techniques.    DETAILED DESCRIPTION - Extracting remangilone A, comprises (i) crushing Physena madagascariensis leaves into crude powder, carrying out supercritical fluid extraction in an extracting kettle, pumping carbon dioxide and cosolvent into the extraction tank, where the extracting pressure is 25-45 MPa, the extracting temperature is 42-55 degrees C, the extracting time is 1-3 hours, analyzing pressure is 7. 5-9 MPa, analyzing temperature is 30-38 degrees C, and collecting the extract, (ii) dissolving the obtained extract in methanol, drying sample, placing in a high pressure silica gel column chromatography for purification, using dichloromethane-acetone solvent system for gradient elution, collecting remangilone A fraction, vacuum extracting and concentrating, cooling and crystallizing to obtain crude crystal, and (iii) re-crystallizing the crude crystal with hexane-diethyl ether to obtain the product.
NOVELTY - A kitchen garbage rotating fertilizer machine comprises shell provided with a kitchen garbage feeding opening, a filtrate recovery port and an organic fertilizer outlet. The shell is provided with a crushing mold, a conveying system, a stirring module, a filtrate recycling mold and an organic fertilizer processing module. The filtrate recycling module is connected with filtrate recycling port. The stirring module through the conveying system is connected with organic fertilizer outlet.    USE - Kitchen garbage rotating fertilizer machine.    ADVANTAGE - The machine has simple structure, modular integration, convenient to assemble, quick processing, and small floor area.
NOVELTY - Aminocyclopropane-1-carboxylate (ACC) deaminase producing alfalfa Pseudomonas preserved in china general microbiological culture collection center in Chaoyang district Beijing west, Beichen road, No.3 yard on june 26, 2012 under preservation number of 6294, is new.    USE - The ACC deaminase producing alfalfa Pseudomonas is useful as microbial fertilizer for culturing plants (claimed).    ADVANTAGE - The ACC deaminase producing alfalfa Pseudomonas promotes plant growth and improves yield and stress resistance of the plants.
NOVELTY - A composite microbial inoculum comprises Candida tropicalis (CCTCC No. AY92045), Streptomyces microflavus (CICC23626), and Bacillus licheniformis (CCTCC No. M207093).    USE - The composite microbial inoculum is used in a biological organic fertilizer and in producing fruits and vegetable plants with disease resistance, such as gray mold disease resistance (all claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a biological organic fertilizer prepared according to the following method: the pig manure and straw are mixed according to the weight ratio of 1.8-2.5:1, adjusting the water content to 28-35%, turning when the stack temperature is 75-80 degrees C, and adding water, turning for 2-5 times so as to keep compost water content, the stack is turned when the stack temperature is reduced to 42-46 degrees C, access composite microbial inoculum, regulating water content is 45-50%, when the stack temperature reaches 48 degrees C, fermenting for 3-5 days to obtain organic fertilizer, where the composite microbial inoculum comprises C. tropicalis (CCTCC No. AY92045), S. microflavus (CICC23626), and B. licheniformis (CCTCC No. M207093) at a ratio of 1-10:0.1-1:0.1-1.
NOVELTY - Preparation of decoquinate, comprises adding aniline-diazonium salt solution into methanol solution of ortho-ethoxyphenol in dropwise, and reacting to obtain aniline coupled product, reducing the aniline coupled product with sodium dithionite to obtain 3-ethoxy-4-hydroxyaniline, carrying out thermal condensation of 3-ethoxy-4-hydroxyaniline with diethyl ethoxymethylenemalonate, adding bromodecane and carrying out etherification, subjecting obtained product to high-temperature cyclization to obtain decoquinate crude product, then recrystallizing the crude product, centrifuging and drying.    USE - The method is useful for preparing decoquinate.    ADVANTAGE - The method: utilizes easily available raw materials; has moderate technical conditions, safe and simple operation, high conversion rate, and stable product quality; and is clean and environment-friendly.
NOVELTY - The processing unit has an opening and closing cover that is attached to a recycling apparatus for fermenting the organic waste. An outer blower (F2) arranged in a base frame (10), is connected to an odor removing apparatus through an air pipe (P3). The odor removing apparatus is connected between a reactor (30) and a ventilation fan through other air pipe. An air shower equipment (63) of an air preheating unit (60) is arranged inside the reactor. The net elements are separately installed in a zig-zag type vertical bulkhead portion of the odor removing apparatus.    USE - Organic waste recycling and processing unit.    ADVANTAGE - The leakage of condensed water from condensed water collecting unit can be prevented reliably, since net elements are separately installed in the zig-zag type vertical bulkhead portion of the odor removing apparatus. The reaction speed and operating efficiency of reactor can be improved effectively. The polluted condensed water can be collected effectively in the condensed water collecting unit. The occurrence of odor from organic waste can be removed utterly. The fermentation efficiency of organic waste recycling and processing unit can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the organic waste recycling and processing unit.    Base frame (10)    Reactor (30)    Air preheating unit (60)    Air shower equipment (63)    Outer blower (F2)    Air pipe (P3)
NOVELTY - Purifying rubber seed oil to produce biodiesel fuel, comprises: measuring amount of rubber seed oil and ethanol in mole ratio of methanol/rubber seed oil of 5/1-10/1; introducing them into a treatment apparatus equipped with an impeller and a methanol vapor condensation system and maintaining a stable agitation; transferring the mixture to a precipitating device to perform the phase precipitation; and fractionally discharging in the known conventional manner so as to separately obtain layers of clean rubber seed oil and the abundant methanol layer out of the impurity residual adhesive layer.    USE - The method is useful for purifying rubber seed oil by ethanol for the production of biodiesel fuel.    DETAILED DESCRIPTION - Purifying rubber seed oil by ethanol for the production of biodiesel fuel, comprises: measuring amount of rubber seed oil to be treated; measuring the amount of ethanol to be used in the mole ratio of methanol/rubber seed oil of 5/1-10/1; introducing the measured rubber seed oil and ethanol into a treatment apparatus equipped with an impeller and a methanol vapor condensation system and maintaining a stable agitation at a temperature for 20-40 minutes; transferring the mixture to a precipitating device for performing the phase precipitation in a time period of 30-150 minutes; and fractionally discharging in the known conventional manner so as to separately obtain layers of clean rubber seed oil and the abundant methanol layer out of the impurity residual adhesive layer.
NOVELTY - The device has moving wheel (13) that is firmly installed in order to roll in both sides of the arbor. The lid (12) is installed so that the rear end (12a) is fixed by a hinge onto the upper portion of the main portion (11). The control unit (27) drives and controls so that the microbial fermentation solution is emitted from the injection nozzle (23) within the main portion for fixed time. The detection sensor (26) senses opening and closing of the lid of pump (25).    USE - Injection device of microorganism fermentation liquid for food garbage.    ADVANTAGE - The food garbage can be decomposed easily and the food waste can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the injection device of microorganism fermentation liquid for food garbage.    Main portion (11)    Lid (12)    Rear end (12a)    Moving wheel (13)    Injection nozzle (23)    Pump (25)    Detection sensor (26)    Control unit (27)
NOVELTY - Fermented organic fertilizer comprises 1-1.5 tons rapeseed cakes, 115-180 kg auxiliary materials, 1-1.2 kg fermenting agent and 5-10 kg corn meal.    USE - The fermented organic fertilizer useful for controlling diseases and pests.    ADVANTAGE - The organic fertilizer is simple and convenient to prepare, and improves soil environment and pH value, which is beneficial to crop growth.
NOVELTY - Compact type fertilizer granulator comprises a machine main portion and a feeding port, where the machine main portion is further provided with a compaction belt and rotating shaft, the compaction rotating shaft is pressing shaft and connected with the machine main portion, the compaction belt is covered on the two compaction rotating shafts, the outside of the bottom of the machine main portion is provided with a lower motor, where a pressing type rotating shaft is connected with the lower part of the motor through the belt transmission.    USE - Compact type fertilizer granulator.    ADVANTAGE - The device has simple structure, is convenient to use, and reduces the fertilizer production cost.
NOVELTY - Method for producing organic fertilizer, involves (a) crushing straw into 200-250 meshes, (b) stirring poultry excrement and straw, adding lime powder to adjust the pH value to 7-8, adding probiotics and uniformly stirring the components, (c) turning the mixture and maintaining the moisture content of 65-70%, and (d) granulating the mixture, fermenting the granulated mixture, drying the fermented product and packaging the dried product.    USE - The method is useful for producing organic fertilizer for controlling plant diseases and insect pests.    ADVANTAGE - The method is simple and convenient, and produces organic fertilizer that improves soil environment and pH, thus improves crop growth.
NOVELTY - Silicon-containing organic fertilizer, comprises 10-20 kg silicon dioxide, 200-300 kg plant ash, 500-600 kg excrement or humus, 3-5 kg corn flour, and 1-1.2 fermenting agent in one ton.    USE - As silicon-containing organic fertilizer.    ADVANTAGE - The organic fertilizer can be prepared simply and conveniently, improves soil environment, thus improves the growth of crops, and is rich in silicon elements, thus solves the problem of shortage of silicon-containing organic fertilizers.
NOVELTY - Composite flora comprises Bacillus stored with CGMCC NO. 5971, Rheinheimera tangshanensis stored with CGMCC NO. 5972, Acinetobacter lwoffii stored with CGMCC NO. 5973, Pseudomonas fluorescens stored with CGMCC NO. 5974 and Wickerhamomyces anomalus stored with CGMCC NO. 5975.    USE - The composite flora is useful for preparing additive cellulose ester film for optical application (claimed).    ADVANTAGE - The method is environment-friendly; and the waste liquid is directly transformed into organic fertilizer, thus zero release and zero pollution are achieved. The biological process performs protection to the fibers. Compared with traditional chemical method, the method has the advantages of low producing cost, high economic benefit, and capabilities of saving the energy and protecting the environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for preparing additive for cellulose, comprising bacterial liquid is configured: the composite flora is configured to composite bacteria water solution; raw material processing: the woody raw material after cortex slice, or the herbal raw material cutting section, to cut the raw material into the soaking pool swelling; preparing seal coat of fiber, comprising mitigating the swelling of the thread raw material, crushing and/or grinding, steam sterilizing: putting the biodegradable raw material from bacteria liquid, draining, steam sterilizing, obtain the fiber: putting the sterilized raw material for the first time period, a fiber bundle, the first time period for the second section grinding fine, grinding to make the fiber beam be separated single fiber, screening, filtering after a period of grinding and the slurry after the second fine grinding of the fiber bundle, and then grinding to make it into single fiber, sterilizing: putting the prepared fiber soaked in warm water, then drying, sterilizing, and grinding: putting the sterilized fiber into cellulose to be as the additive.
NOVELTY - A Wickerhamomyces anomalus deposited under CGMCC No. 5975, is new.    USE - The Wickerhamomyces anomalus is useful in bio-bacterial liquid pulping application; and for paper-making (all claimed).    ADVANTAGE - The paperboards made by the bio-bacterial liquid pulping method reach AA or above level; and the waste liquid produced in pulp making can be recycled or changed into methane which is a kind of energy or organic fertilizers, so energy can be saved and environment pollution is avoided.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for paper-making using bacterial liquid, comprising: (a) configuring bacterial liquid: using Wickerhamomyces anomalus with water to form bacterial liquid; (b) raw material processing: the woody raw material after cortex slice, or the herbal raw material cutting section, to cut the raw material into the soaking pool swelling; and (c) mitigating the swelling of the thread raw material crushing and/or grinding, biodegradable, the hydrophobic solution as raw material to soak the prepared bacterial liquid, steam sterilizing: putting the biodegradable raw material from bacteria liquid, draining, steam sterilizing, grinding: putting the sterilized raw material for a period of roughly grinding slurry to form fiber bundle, fine grinding: putting the first section grinding slurry for the second section thin grinding slurry, to make the fiber beam be separated single fiber, slurry screening: screening, filtering after a period of grinding slurry and the second slurry fine grinding slurry of the fiber bundle, and then grinding to make it into single fiber, latency, and washing: putting the prepared paper pulp is soaked in the warm water, for preparing.
NOVELTY - Compound bacteria comprise Bacillus stored with a number of CGMCC No. 5971, Rheinheimera tangshanensis stored with a number of CGMCC No. 5972, Pseudomonas fluorescens stored with a number of CGMCC No. 5974, and Wickerhamomyces anomalus stored with a number of CGMCC No. 5975.    USE - The compound bacteria are useful for preparing textile fiber (claimed).    ADVANTAGE - The method is environment-friendly, where waste liquid is directly transformed into organic fertilizer, and thus zero emission and zero pollution are achieved. A biological treating process performs protection to the fibers. Compared with a traditional chemical method, the method has the advantages of being low in producing cost, high in economic benefit, and is capable of saving an energy resource and protecting an environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for preparing textile fiber comprising configuring the bacterial liquid: the compound bacteria are configured to composite bacteria water solution; (b) raw material treatment: the ramie raw material cutting section, and the raw material is put into the soaking pool of swelling; and (c) preparing seal coat of fiber, comprising biodegradable, the hydrophobic solution as raw material to soak the prepared bacterial liquid, steam sterilizing: putting the biodegradable raw material from bacteria liquid, draining, steam sterilizing, obtain the fiber: putting the sterilized raw material for the first time period, a fiber bundle, the first time period for the second section grinding fine grinding to make the fiber beam be separated single fiber, screening, filtering after a period of grinding and the slurry after the second fine grinding of the fiber bundle, and then grinding to make it into single fiber, drying, carding: putting the prepared fiber is soaked in warm water, and then and drying for preparing textile fiber.
NOVELTY - A Bacillus sp. deposited under CGMCC No. 5971, is new.    USE - The Bacillus sp. is useful for preparing textile fiber (claimed).    ADVANTAGE - The method is environment-friendly, where waste liquid is directly transformed into organic fertilizer, thus zero emission and zero pollution are achieved. A biological treating process performs protection to the fibers. Compared with a traditional chemical method, the method has the advantages of being low in producing cost, high in economic benefit, and is capable of saving an energy resource and protecting an environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for preparing textile fiber, comprising configuring the bacterial liquid: the Bacillus sp. is mixed with water to form bacterial liquid; (b) raw material treatment: the ramie raw material cutting section, and the raw material is put into the soaking pool of swelling; and (c) preparing the seal coat of fiber, comprising biodegradable, the hydrophobic solution as raw material to soak the prepared bacterial liquid, steam sterilizing: putting the biodegradable raw material from bacteria liquid, draining, steam sterilizing, obtain the fiber: putting the sterilized raw material for the first time period, a fiber bundle, the first time period for the second section grinding fine grinding to make the fiber beam be separated single fiber, screening, filtering after a period of grinding and the slurry after the second fine grinding of the fiber bundle, and then grinding to make it into single fiber, drying, carding: putting the prepared fiber is soaked in warm water, and then drying, and carding, used for preparing textile fiber.
NOVELTY - Method for preparing light matrix using Eupatorium adenophorum, involves (a) crushing E.adenophorum straw, mixing crushed straw with fertilizer and corrosion accelerating agent, adding water, uniformly stirring the mixture, and adjusting the water content, and (b) stacking the mixed materials, fermenting mixed materials, spreading the obtained mixture, and drying material until water content reaches 20-40%, when performing fermentation, turning mixture one time for every 4 days.    USE - The method is useful for preparing light matrix (all claimed) which is used for plant cultivation.    DETAILED DESCRIPTION - Method for preparing light matrix using Eupatorium adenophorum, involves (a) crushing E.adenophorum straw into the length of 1 cm, mixing crushed straw with fertilizer and corrosion accelerating agent, adding water, uniformly stirring the mixture, and adjusting the water content of mixed material to 60-65%, and (b) stacking the mixed materials in a width of 1.5-2 m and height of 1-1.2 m, fermenting mixed materials at 60-70 degrees C for 7-15 days, spreading the obtained mixture when the stack temperature is reduced to less than greater than or equal to 40 degrees C, and drying material until water content reaches 20-40%, when performing fermentation, turning mixture one time for every 4 days.
NOVELTY - Composting method of residual sludge in urban sewage treatment plants, involves mixing residual sludge of urban sewage treatment plants with chicken manure, adding attapulgite, adjusting mass ratio of carbon and nitrogen in the mixture, adjusting the initial water content, adding the mixture into a reactor tank for composting process in the static forced ventilation method, and obtaining sludge composting product used as afforesting substance for scenery plants, stock growing and urban afforesting after 28-32 days.    USE - The composting method is useful for residual sludge in urban sewage treatment plants (claimed).    ADVANTAGE - The composting method has effects of inactivating and fixing heavy metal such as lead and cadmium, so that the potential ecology toxicity is reduced or eliminated, thus the residual sludge of urban sewage treatment plants is less harmful.    DETAILED DESCRIPTION - Composting method of residual sludge in urban sewage treatment plants, involves mixing residual sludge of urban sewage treatment plants in which the water content is 80-86% with chicken manure in ratio of 2-3:1, adding attapulgite in the ratio of 5% according to the overall mass of the residual sludge and the chicken manure to obtain mixture, adjusting the mass ratio of carbon and nitrogen in the mixture to 28-31:1, adjusting the initial water content to 58-62%, adding the mixture into a reactor tank for composting process in the static forced ventilation method, where the air throughput is 10-40 m3/hour.t, and obtaining sludge composting product used as afforesting substance for scenery plants, stock growing and urban afforesting after 28-32 days, where the attapulgite serves as a heavy metal fixing agent.
NOVELTY - Method for removing steroid estrogen from poultry excrement composted fertilizer, involves obtaining composted fertilizer which is prepared by treating poultry excrement by conventional composting method, where the composting method involves adjusting water weight content in composted fertilizer, transferring to sealed container, composting, inoculating bacterium agent, adding straw, adjusting water content of composted fertilizer mixture, composting, transferring the fertilizer to the sealed container, fertilizing, and controlling composting temperature.    USE - The method is useful for removing steroid estrogen from poultry excrement composted fertilizer (claimed).    DETAILED DESCRIPTION - Method for removing steroid estrogen from poultry excrement composted fertilizer, involves obtaining composted fertilizer which is prepared by treating poultry excrement by the conventional composting method, where the composting method involves (a) adjusting the water weight content in the composted fertilizer to 50-60%, transferring into a sealed container, and composting at room temperature, (b) inoculating a microorganism bacterium agent capable of degrading steroid estrogen in the obtained composted fertilizer, and adding straw and uniformly mixing to obtain composted fertilizer mixture, adjusting the water content of the composted fertilizer mixture to 40-50%, adjusting pH to 5.5-6, stacking the mixture on ground to form composted fertilizer, and composting for 14-40 days, and (c) transferring the composted fertilizer obtained in the step (b) to the sealed container and fertilizing, controlling the composting temperature in the sealed container in the fermentation process to greater than or equal to 45 degrees C, and controlling the fermentation time to 6-8 days.
NOVELTY - The biocomposter has a reservoir arranged in an upper part of a mantle that is located in an external water jacket. A lower part of an internal water jacket is arranged on bottom of a tank whose inner side is placed with a rotor shaft that is mounted at top of an upper flat scraper that is evenly spaced on circumference of the rotor shaft. A central part is arranged at bottom of the rotor shaft that is mounted on a support frame. A shelf is mounted on a rear fan. A reducer box is locked to a drive system. An electric motor is connected with a lower part of a regulator.    USE - Biocomposter.
NOVELTY - Dried and crushed cortex dictamni is added into subcritical extraction kettle, and polar organic solvent is added at 80-120 degrees C and pressure of 0.2-1 MPa. Dynamic extraction of the mixture is carried out for 30-80 minutes, and the extracting solution is decompressed and recycled to obtain concentrated liquid. The concentrated liquid is purified with macro-porous absorption resin using 60.0 vol.% ethanol solution to elute. The eluent is concentrated and dried, and extracted 2-3 times with petroleum ether. The obtained extract is collected to obtain fraxinellone.    USE - Extraction of fraxinellone from cortex dictamni (claimed).    ADVANTAGE - The extraction process is carried out efficiency and easily with reduced energy consumption.
NOVELTY - Separation and purification of natamycin comprises taking natamycin fermentation liquid; adding oxalic acid to adjust the pH; adding potassium ferrocyanide and zinc sulfate; stirring; adding sodium polyacrylate; controlling the temperature and processing time; filtering by van-type pressure filter to obtain clear and transparent filtrate; carrying out ultrafiltration; carrying out nanofiltration; separating out white crystal; and vacuum drying to obtain natamycin white crystal powder having purity of 95.0%.    USE - Separation and purification of natamycin (claimed).    ADVANTAGE - The method can save the extraction cost; reduces environmental pollution and energy consumption; is simple and suitable for industrial production; and has high yield ( greater than or equal to 65%), high purity (dry basis content of greater than or equal to 95%), and low cost.
NOVELTY - Complex biological agent comprises Lactobacillus species with a preservation number CGMCC NO: 5983, Streptococcus thermophilus with a preservation number CGMCC NO: 5985 and orange peel extract solution.    USE - The complex biological agent is useful for deodorizing public toilets (claimed) and livestock and poultry excrements.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for: (1) preparing liquid complex biological agent, comprising activating Lactobacillus species and Streptococcus thermophilus in DeMan Rogosa and Sharpe (MRS) solid culture medium, inoculating to liquid culture medium and culturing for 24 hours, adjusting the bacterial content of both the strains to 109 colony forming units/ml respectively, mixing the two bacterial solutions to obtain the liquid microbial deodorization agent, adding orange peel extract solution accounting for 0.02-0.05% (vol./vol.) and mixing uniformly; (2) preparing solid complex biological agent, comprising adding liquid complex biological agent to an adsorbent, where the weight of the adsorbent is 1 kg/l of the liquid complex biological agent, stirring and mixing uniformly, drying for 20-24 hours at 40 degrees C in a constant temperature incubator until the moisture content is 15-20% to obtain the dried complex biological agent, adding 5 g accelerator to each kg of the dried complex biological agent, and stirring uniformly; and (3) use method of the liquid complex biological agent, comprising directly spraying the liquid agent on public toilet excrement, toilet environment or a septic tank; and solid complex biological agent, comprising uniformly mixing the solid agent with physiological saline, activating for 3-5 hours at 30 degrees C and then scattering on the public toilet excrement or the septic tank.
NOVELTY - Deodorizing composition comprises (in %): ethanol (95-98), perfume (3), 5-chloro-(2,4-dichlorophenoxy)phenol, ((2R)-2,5,7,8-tetramethyl-2-((4R,8R)-4,8,12-trimethylsilyl)-chromium-6-yl)acetate, propane, butane, tocoferol acetate (0.03-0.06) and triclosan (0.04-0.06).    USE - The deodorizing composition is useful for jackets, shoes and socks, helmets, car air conditioner and veil for preventing dandruff (all claimed), and as cleanser, freshener and odor remover. The composition is in the form of aerosol.    ADVANTAGE - The composition is environmentally-friendly and provides antibacterial and antioxidant effects.
NOVELTY - The gas pool generating device has a marsh gas generating tank (3) that is equipped with a homogenizing pump. The cylindrical marsh gas generating tank is provided with an air outlet. The air outlet channel is connected with an air supply pipe (9) to generate marsh gas output. The marsh gas generating tank is provided with column hangers to generate the marsh gas. The column is provided with a discharging port of biogas slurry and biogas residue.    USE - Columnar solid marsh gas pool generating device for use in e.g. urban construction, development of agriculture and rural economy development.    ADVANTAGE - The device has high fermentation efficiency, low investment cost, low using cost, long service life, safety and performance. The multilayer body of the device overlaps small floor area, and degree of automation controlled by solenoid valve is high.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic perspective diagram of the structure of the columnar marsh gas pool generating device.    Material homogenizing tower (2)    Marsh gas generating tank (3)    Biogas slurry pipe (5)    Air outlet channel (9)    Air supply pipe (9)
NOVELTY - A carbonyl group-containing compound (I) is dissolved into the mixed solution of diethyl ether and ethanol mixed solution under the protection of nitrogen, and cooled at -30 degrees C to -15 degrees C by a conventional refrigerator. Ether solution of diethyl methoxy boron alkyl (50 %mass) is added, stirred uniformly at -30 degrees C to -15 degrees C, and cyano sodium borohydride or potassium borohydride is added for 1-4 hours, and heat is preserved for 4-6 hours, to obtain hydroxyl group-containing compound (II).    USE - Preparation of hydroxyl group-containing compound used as statin intermediate by chiral reduction.    ADVANTAGE - The hydroxyl group-containing compound is economically prepared with reduced emission.    DETAILED DESCRIPTION - A carbonyl group-containing compound of formula (I) is dissolved into the mixed solution of diethyl ether and ethanol mixed solution under the protection of nitrogen, and cooled at -30 degrees C to -15 degrees C by a conventional refrigerator. Ether solution of diethyl methoxy boron alkyl (50 %mass) is added, stirred uniformly at -30 degrees C to -15 degrees C, and cyano sodium borohydride or potassium borohydride is added for 1-4 hours, and heat is preserved for 4-6 hours, to obtain hydroxyl group-containing compound of formula (II). The weight ratio of ether solution of diethyl methoxy boron alkyl and carbonyl group-containing compound is 0.8-1.2:1. The weight ratio of sodium cyanoborohydride or potassium borohydride and carbonyl group-containing compound is 0.2-0.5:1.    X=CN or Cl.
NOVELTY - An organic solvent as diluent is added to vitamin B1 as starting material, esterified using phosphoric acid and phosphorus pentoxide as esterification reagent, hydrolyzed, alkali metal salt is added to neutralize phosphoric acid, crystallized, and dried to obtain vitamin B1 phosphomonoester.    USE - Synthesis of vitamin B1 phosphomonoester.    ADVANTAGE - The method efficiently and economically produces vitamin B1 phosphomonoester without environmental pollution, and reduces solid waste residue, by simple process.
NOVELTY - Extracting tylosin, comprises preprocessing tylosin fermentation broth, and obtaining tylosin filtrate, and then extracting, re-extracting, decolorizing, and filtrating, crystallizing, aging, subjecting to water washing, and vacuumizing the tylosin filtrate to obtain the product.    USE - The method is useful for extracting tylosin.    ADVANTAGE - The method produces intermediate tylosin whose solubility meets the quality standards of Chinese Veterinary Pharmacopoeia; has mild production conditions, simple operation procedures, low production cost, and high working efficiency; is safe and reliable in production process; reduces the loss of organic solvent; and saves energy consumption.
NOVELTY - Tanshinone derivative (I) or its salt is new.    USE - For treating tumor (claimed) such as papillary carcinoma, adenocarcinoma, adenocarcinoma, basal cell carcinoma, fat sarcoma.    ADVANTAGE - The compound is prepared by simple and environmental friendly method.    DETAILED DESCRIPTION - Tanshinone derivative of formula (I) or its salt is new.    R1-R4=chloro, bromo, iodo, fluoro, methoxy, allyloxy, amino, 1-4C alkyl mono-substituted amino, 1-4C dialkylsubstituted amino, optionally 1-4C alkyl substituted phenylamino, optionally 1-4C alkyl substituted alkyl substituted benzylamino, 1-morpholinyl, piperidyl, acetamido, N-carbamido, N-thiocarbamido, guanidyl, nitro, trifluoromethyl, cyano, acetyl, 1-4C alkylsulfonyl, aminosulfonyl, 1-4C alkylamino, allylaminosulfonyl, morpholin-1-ylsulfonyl or piperidin-1-ylsulfonyl.    An INDEPENDENT CLAIM is included for preparation of compound (I).
NOVELTY - The solid fuel lighting device (10) comprises a receptacle (15) provided with two compartments. The former compartment contains solid fuel. A material lighter (40) is provided, which is placed in the receptacle. The material lighter is selected from paper, paperboard, cardboard, cotton, burlap or cellulose material. The receptacle is made is paper, paperboard, cardboard or fabric.    USE - Device for use in a kit (Claimed) for lighting solid fuel, such as coal, wood and briquettes compressing cellulosic material.    ADVANTAGE - The solid fuel lighting device is simple and improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a kit comprises element burners.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the solid fuel lighting device.    Solid fuel lighting device (10)    Receptacle (15)    Material lighter (40)    Paperboard (50)    Element burners (60)
NOVELTY - Jatropha oil as raw material (AA), methanol (BB) and potassium hydroxide are mixed and stirred (CC) with respect to 100 parts mass of Jatropha oil, and transesterification process (S1) is carried out, to obtain fatty acid alkyl ester. The obtained fatty acid alkyl ester is processed, to obtain biodiesel fuel (NN).    USE - Manufacture of biodiesel fuel used for diesel engine.    ADVANTAGE - The method provides biodiesel fuel with high yield, and without pretreatment even when the raw material contains free fatty acid in high concentration.    DETAILED DESCRIPTION - n Parts mass Jatropha oil as raw material (AA), (25-28)x 2n parts mass methanol (BB) and 1.1+(0.20-0.25)x n parts mass potassium hydroxide are mixed and stirred (CC) with respect to 100 parts mass of Jatropha oil, and transesterification process (S1) is carried out, to obtain fatty acid alkyl ester. The obtained fatty acid alkyl ester is processed, to obtain biodiesel fuel (NN).    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of manufacturing biodiesel fuel. (Drawing includes non-English language text)    Raw material (AA)    Methanol (BB)    Mixing and stirring (CC)    Static mixer (DD)    Biodiesel fuel (NN)    Transesterification process (S1)
NOVELTY - Degrading a plant biomass sample so as to release fermentable sugars, comprises mixing, with the biomass sample, a plant degrading cock tail comprising at least one cell extract that comprises an active plant degrading compound recombinantly expressed in cells from which the cell extract is derived. The cell extract comprises beta -mannanase.    USE - The method is useful for degrading a plant biomass sample so as to release fermentable sugars, where the plant biomass sample comprises grain and/or grain residues, sugar beet, sugar cane, grasses, wood-based biomass (preferred), fruits and/or fruit waste residues and the plant biomass is switchgrass, sawdust or otherwise processed wood, sugar cane, citrus peel or sugar beet (all claimed), where the converted biomass is useful in biofuels, such as cellulosic ethanol.    ADVANTAGE - The method utilizes the plant crude extract without purification for lignocellulosic biomass hydrolysis thus the process is cost effective.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a plant-degrading cocktail for degrading a plant biomass, comprising at least two recombinantly expressed plant degrading enzymes and ribulose-1,5-bisphosphate carboxylase oxygenase (rubisco), and optionally, expansin;    (2) a plant degrading enzyme cocktail for digesting a wood-based biomass sample comprising plant expressed beta -mannanase and optionally, in addition, cellulase, beta glucosidase, xylanase, alpha amylase, amyloglucosidase, pectin lyase, swollenin and pectate lyase, and/or an amount of rubisco; and    (3) producing a plant biomass degrading material comprising producing at least one plant comprising chloroplasts that express beta -mannanase, harvesting the plant and processing the plant to produce plant degrading material suitable for mixing with and degrading a biomass sample.
NOVELTY - Fertilizer comprises granules for producing ethylene, where the granules are coated with precursor of ethylene and biological-origin resin.    USE - Fertilizer used for enhancing growth of crops.    ADVANTAGE - The fertilizer produces ethylene stably over a long period of time, and the rate of degradation of ethylene by soil microbe is suppressed. The fertilizer is prepared easily with reducing production cost.
NOVELTY - The gasifier has a biomass supply unit (5) that supplies a biomass (4) from a biomass supply port (15). A water steam supply unit (7) supplies a water steam (6) from biomass supply port with biomass. A control unit (8) controls the inside temperature of a gasification reactor (1), such that the temperature between the generated gas discharge ports (13) reaches 1000 degree C or more from the biomass supply port, and the temperature between the biomass supply port and the gasifying agent supply port (14) becomes below in the hemisphere temperature of ash of the biomass.    USE - Gasifier for gasifying biomass of grass and tree, paper garbage.    ADVANTAGE - The tar in the generated gas is reduced significantly, such that the fusion of the ashes within the gasification reactor can be prevented. The generated gas and liquid fuel can be manufactured efficiently. The running cost can be reduced significantly.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the gasifier.    Gasification reactor (1)    Biomass (4)    Biomass supply unit (5)    Water steam (6)    Water steam supply unit (7)    Control unit (8)    Gas discharge port (13)    Gasifying agent supply port (14)    Biomass supply port (15)
NOVELTY - Method for sterilizing organic fertilizer involves culturing Actinomyces and filamentous fungi to culture medium in culture room under environment of dry-form of collection site, mixing produced spore with flour to obtain microbial mixture, mixing the microbial mixture with 9-11 wt.% organic fertilizers such as manure and stable manure and sequentially germinating spore of each microbe in an organic fertilizer, and suppressing reproduction of bacteria, such as Escherichia coli.    USE - The method is useful for sterilizing organic fertilizer (claimed).    ADVANTAGE - The method enables to suppress reproduction of harmful microorganisms in an organic fertilizer, utilizes flour having moderate gap such that microbe can easily adheres and form habitation interval between Actinomyces and filamentous fungi, and prevents disease in crops and damage of human by harmful microbe adhering to the crops. When the organic fertilizer is applied to plants, nutrition rotten plant and permanent rotten plant can be able to increase in soil, and promotes soil fertility.    DETAILED DESCRIPTION - Method for sterilizing organic fertilizer involves culturing Actinomyces and filamentous fungi to culture medium in culture room under environment of dry-form of collection site, where the culture medium is impregnated with liquid mixture of sodium nitrate, phosphoric acid potash, and sporogenous lactic acid bacteria which is collected from topsoil, such as bamboo thicket, mixing produced spore with flour to obtain microbial mixture, mixing the microbial mixture with 9-11 wt.% organic fertilizers such as manure and stable manure and sequentially germinating spore of each microbe in an organic fertilizer and breeding microbe, and suppressing reproduction of bacteria, such as Escherichia coli.
NOVELTY - An agricultural composition contains fermented liquor consisting of microorganisms from conifer chips pressurized steaming liquid as active ingredient.    USE - Agricultural composition for nitrate-nitrogen reducing agent, crop growth stimulant, and excrement fermentation promoter (all claimed).    ADVANTAGE - Nitrate content can be reduced, putrefaction of ginger in storage is prevented, harvest yield is improved, growth of crops is accelerated, and livestock excrement decomposition is accelerated.
NOVELTY - Micro-algae Pseudochoricystis ellipsoidea 5P strain with hydrocarbon producing ability is new.    USE - Micro-algae Pseudochoricystis ellipsoidea 5P strain for manufacturing hydrocarbons and acyl glyceride (all claimed) used as alternative fuel source.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) manufacturing method of hydrocarbon which involves culturing micro-algae of and extracting produced hydrocarbon; and    (2) manufacturing method of acyl glyceride which involves culturing micro-algae and collecting produced acyl glyceride from the culture.
NOVELTY - Method for culturing algae, involves culturing algae having hydrocarbon producing ability in culture medium to which salt is added, where optical density of the culture medium is adjusted to 1/2 of optical density which shows saturated state.    USE - The method is useful for culturing algae, which are used for producing hydrocarbons. The algae are algae which inhabit in freshwater, preferably Pseudochoricystis ellipsoidea N1 strain (all claimed). The hydrocarbons are used as raw material for biofuel.    ADVANTAGE - The method increases production of hydrocarbon based on lipogenesis per algae cell.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing hydrocarbons, which involves culturing the algae and obtaining hydrocarbons from the cultured algae.
NOVELTY - The present invention provides a method of producing activated carbon from lignocellulosic material such as coconut shell. The method comprises the removal of accessible glucose units from the cellulose polysaccharides of the material prior to activation. The activated carbon material produced according to the method of the invention has a pore structure that is rich in micropores and mesopores. The material is suitable for use in tobacco smoke filtration, for example, in smoking article filters.
NOVELTY - Producing amino acid liquid fertilizer, comprises performing leather scraper concatenation step to crush the leather scraper, mixing the crushed leather scrap and peptizing agent, dissociating and liquefying the mixture with warm water, transferring the liquid solution to a fermenter, fermenting and degrading the solution in the fermenter, and adding fertilizer additive to the fermenter.    USE - The method is useful for producing amino acid liquid fertilizer (claimed).    DESCRIPTION OF DRAWING(S) - The diagram shows a flowchart of a method for manufacturing amino acid liquid fertilizer (Drawing includes non-English language text).
NOVELTY - The method involves drying the raw material from waste plant material until moisture content of between 12-18%, and separating or screening the raw material from vegetable waste to obtain sawdust. The sawdust is homogenized by grinding to obtain a product having particle size of 3 to 5 mm. The sawdust is decanted, and then calcium carbonate or bicarbonate is added into the decanted sawdust to obtain a mixture. The mixture is pelletized, and then pelletized mixture is cooled to obtain pellets.    USE - Method for obtaining pellets used as fuel for household boilers (all claimed).
NOVELTY - Compressed fuel comprises: 40-60 wt.% of a lavender stem of which 95 wt.% has a diameter of 0.3 mm to 2.5 cm; and 20-30 wt.% of coniferous tree sawdust, where the fuel has a water content of 5-15 wt.%.    USE - Used as a compressed fuel.    ADVANTAGE - The compressed fuel can be stored for long time without risk of degradation/rotting due to microorganisms, insects or parasites and moisture, and is easy and safe to handle and for transport.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing a fuel comprising crushing the lavender stem particles, mixing the crushed particles with the coniferous tree sawdust to obtain a mixture having a water content of 12-23 wt.%, compressing the mixture to obtain a compressed mixture and drying the compressed mixture to obtain the fuel.
NOVELTY - Raw material oil containing fatty acid alkylester and hydrogen gas are contacted under hydrogen pressure of 1 MPa or less in presence of catalyst supported on porous metal oxide carrier containing metallic element(s) chosen from group 9 or group 10, and group 6 element, to obtain fuel oil having n-paraffin and/or isoparaffin as main component. The weight ratio of the group 6 elements to the metal elements contained in the catalyst is 1 or less in conversion of a metal.    USE - Manufacture of fuel oil used as aeronautical navigation fuel oil based on ASTM D 7566, biodiesel fuel for aircraft.    ADVANTAGE - The high quality and environmentally-friendly fuel oil is manufactured by economical method with high yield.
NOVELTY - An isolated variant of a parent glycoside hydrolase, comprising a substitution at a position corresponding to position 373 of a defined sequence of 513 amino acids (SEQ ID NO: 2), given in the specification, where the variant comprises an amino acid sequence that has at least 90% sequence identity to SEQ ID NO: 2, and where the variant has glycoside hydrolase activity, is new.    USE - The variant of a parent glycoside hydrolase is used in a detergent composition, and for degrading cellulose-and hemicellulose-containing biomass (all claimed); producing monosaccharides, disaccharides, and polysaccharides; treating textiles as biopolishing agents and for reducing fuzz, pilling, texture modification, and stonewashing; wood processing for biopulping or debarking, paper manufacturing for fiber modification, bleaching, and reduction of refining energy costs, whitewater treatment, important to wastewater recycling, lignocellulosic fiber recycling such as de-inking and secondary fiber processing, and wood residue utilization.    ADVANTAGE - The glycoside hydrolase variants have improved properties including altered temperature-dependent activity profiles, thermostability, pH activity, pH stability, substrate specificity, product specificity, and chemical stability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a method for obtaining the variant above;    (2) a detergent composition comprising the variant above and a surfactant; and    (3) a method for degrading cellulose-and hemicellulose-containing biomass by treating the biomass with a variant above and recovering the degraded biomass.
NOVELTY - N-Substituted 2-(acetylamino)-N'-benzyl-3-methoxypropanamide compounds that are enantiomerically and diastereomerically pure or as mixture with the corresponding enantiomer or diastereomer, are new.    USE - For preparation of (R)-lacosamide (claimed) which is useful as anticonvulsant drug for treatment of epileptic seizures.    ADVANTAGE - The compounds provide intermediate compounds (I) for preparing (R)-lacosamide, where the preparation can be carried out easily by using commercially available compounds, which are simple and environmentally compatible reagents and solvents, such as acetic acid, methoxyacetaldehyde, benzyl isonitrile, as well as their chiral amines and salts, while affording high overall yields and good purity of the products.    DETAILED DESCRIPTION - N-Substituted 2-(acetylamino)-N'-benzyl-3-methoxypropanamide compound of formula (I) that is enantiomerically and diastereomerically pure or as mixture with the corresponding enantiomer or diastereomer, is new.    R1=allyl, tert-butyl, diphenylmethyl, triphenylmethyl, or aryl-methyl group (substituted by group R') of formula (ia) or (ib);    Ar=phenyl (optionally substituted by 1-3 groups selected from 1-4C alkyl, 1-4C alkoxy, halo, or nitro);    R'=H, or 1-4C alkyl;or    R' as 2-4C alkyl+Ar=aromatic or partially unsaturated 6-10C bicyclic group.    INDEPENDENT CLAIMS are included for the following:    (1) process for preparing the compound (I); and    (2) process for preparing (R)-lacosamide involving: removing the group R1 in the compound (I) with a reagent, optionally in a solvent.
NOVELTY - A lignocellulosic fibrous composite, comprises: at least one solvent; and a dried lignocellulosic fiber, where the dried lignocellulosic fiber has been processed by ruminant digestion and anaerobic digestion.    USE - As lignocellulosic fibrous composites (Claimed), used in dairy bedding, horse bedding, cat bedding, small animal bedding, filler material, fertilizer and/or fertilizer base material, and biocompatible absorbent.    ADVANTAGE - The fibrous composites have longer stall life (i.e. utilization time), reduce store, farm and/or stall management costs, reduce cleaning costs, reduce material disposal costs, reduce veterinary costs relative to commercially available composites. The fibrous composites are a direct result of the conversion of waste material to a resource which is biodegradable, compostable, and sustainable with respect to biological systems. The composite is free flowing and non-pelletized.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the lignocellulosic fibrous composite, involving: providing excrement from an animal which has undergone ruminant digestion; introducing the excrement into an anaerobic digester; modifying the excrement to a first wet product; and drying the first wet product to, in turn, generate a lignocellulosic fibrous composite.
NOVELTY - Making epigallocatechin gallate (EGCg) stabilized, gold nanoparticles, comprises mixing (24) a solution of EGCg as a reducing agent with an aqueous solution containing gold salts, and permitting reaction of the gold salts, in the absence of any other reducing agent, to form stabilized, biocompatible gold nanoparticles.    USE - The EGCg stabilized, gold nanoparticles are useful: in a medical therapeutic formulation for a therapy (all claimed) of hyperthermia and targeted prostate cancer; as therapeutic agents, sensors, electronic materials and coatings on biological and non-biological surfaces; in biological imaging for the diagnosis of various diseases; and as X-ray enhancers in X-ray therapy of diseases such as cancer. Tests details are described but no results given.    ADVANTAGE - The EGCg stabilized, gold nanoparticles can be fabricated, via a simple room temperature method, with high reactivity and biocompatibility and reduced toxicity in an environmentally friendly manner and without using harsh chemicals, and exhibits high affinity for cancer cells/tissue.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) the gold nanoparticle stabilized with a material coating of EGCg;    (2) a medical therapeutic formulation comprising the gold nanoparticles;    (3) a method of therapy comprising introducing the stabilized gold nanoparticles into a human or animal subject and conducting gold nanoparticle enhanced therapy; and    (4) a sensing method comprising introducing the stabilized gold nanoparticles into the human or animal subject and conducting gold nanoparticle enhanced imaging.    DESCRIPTION OF DRAWING(S) - The figure shows a flow chart of a method for making stabilized, gold nanoparticles.    Providing an aqueous solution containing gold salts (20)    Adding EGCg in the aqueous solution (22)    Mixing aqueous solution with EGCg in deionized water (24)    Collecting stabilized, gold nanoparticles. (26)
NOVELTY - Removing (M1) excess phosphorus from poultry litter rich in phosphorus content, comprises: contacting broiler litter with an extractant solution containing at least one extractant agent consisting of sodium sulfate or potassium sulfate; leaving the broiler litter in contact with the extractant solution for a sufficient time to allow a desired amount of phosphorus to be removed from the broiler litter; and separating the broiler litter and the extractant solution to obtain phosphorus-depleted broiler litter.    USE - The method is useful for removing excess phosphorus from poultry litter rich in phosphorus content and to obtain phosphorus-depleted broiler litter which is used in augmenting crop soil (all claimed), where the removed phosphorus can be further for other purposes such as in formulation of plant food.    ADVANTAGE - The method removes the phosphorus from poultry litter while maintaining its general stability for crop soli augmentation.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) disposing (M2) of poultry litter rich in phosphorus content, comprising removing a desired amount of phosphorus from the phosphorus rich poultry litter utilizing the method (M1) and mixing the phosphorus-depleted poultry litter obtained with crop soil; and    (2) augmenting crop soil, comprising mixing crop soil with the phosphorus-depleted poultry litter obtained by the method (M1).
NOVELTY - Plant activator composition comprises nitrogen-containing polysaccharide, charcoal powder with particle size of 5 mm or less, and compost, where the compost comprises Actinomyces fermented hen droppings, Actinomyces fermented fish meal, and Actinomyces fermented rice bran.    USE - The plant activator composition is useful supplementing nutrient to crops, preventing against disease with respect to crops, and particularly performing greenhouse cultivation, where the plant activator is only immersed in water, which can improve water quality, create water suitable for reformation of soil, replenishment of a nutrient, and can improve quality of soil by dispersing the water in soil.    ADVANTAGE - The plant activator composition is added only with water until active ingredients are dispersed in water, such that the water can be applied uniformly to soil without performing special operation.
NOVELTY - Producing medicine from a Cannabis plant, involves extracting cannabinoids from the Cannabis plant by performing a reflux process through evaporating, optionally heating and condensing the Cannabis plant, or performing an ultrasonic extraction with ultrasonic waves to produce refluxed or extracted cannabinoids, and infusing refluxed or extracted cannabinoids with glycerin or honey.    USE - The method is useful for producing medicine from Cannabis plant (claimed) used to treat pain and various medical conditions.    ADVANTAGE - The method avoids toxic and harmful by-products in the tinctures, creates doses that are easily used for self-titration for medical patients, and does not use carbon dioxide, remove delta (1)-tetrahydrocannabinol, concentrate by extracting, and use chromatographic fractioning. The method overcomes the problems in the existing technology including addition of unwanted toxins and solvents, low yields of the active compound and production of undesirable active ingredient.
NOVELTY - The method involves heating the sludge for a predetermined amount of time to a temperature sufficient to enable hydrolysis of the sludge to begin. The sludge is heated for a second predetermined period of time to increase the temperature and enable pasteurization of the sludge to occur. The temperature of the sludge is allowed decrease. The sludge is held at decreased temperature for a third predetermined period of time to enable hydrolysis of the sludge to occur. The sludge is transferred to an anaerobic digester.    USE - Method for treating sludge such as solid waste from waste-water treatment.    ADVANTAGE - The pathogen content of the sludge can be reduced. The biogas production can be increased. The amount of volatile solids destruction can be increased. The heat balance of the process can be efficient. The heating is carried out using low grade heat recovered from the combined heat and power (CHP) engine to ensure energy efficiency. The carbon footprint can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating the method for treating sludge.
NOVELTY - A collection device comprises a fermenting device, an ammoniation process system, an ammoniation treatment system, an ammonia liquid conveying pump, and an ammonia gas absorbing groove.    USE - A collection device for collecting loss ammonia in fertilizer (claimed).    ADVANTAGE - The device has a simple structure, and realizes compost in the loss of ammonia gas.
NOVELTY - The system has a feeding storage bin, a magnetic separator, a primary crusher, a first grade high speed rotating machine, secondary crusher, secondary high speed rotating machine, an environment protection hot blast stove and a garbage storage bin which are connected in turn through the transmission device. The garbage storage bin, additive storage bin and the coal storage bin are connected with a forming machine.    USE - System for producing regenerative coal using municipal wastes and coal slime, used in coal mine production.    ADVANTAGE - The municipal solid waste can be treated effectively, so as to reduce the pollution to the environment. The waste can be recycled effectively. The durability of the regenerative coal producing system can be extended, as the damage of the regenerative coal producing system can be prevented effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing regenerative coal using municipal wastes and coal slime.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating the regenerative coal producing process. (Drawing includes non-English language text)
NOVELTY - The hydrogen generator (1) has a reaction unit (5) that mixes a hydrogen-producing solution and a hydrogen-producing stimulation solution. A hydrogen-producing solution supply flow channel (7) introduces the hydrogen-producing solution into the reaction unit. A reaction promotion solution supply flow channel (8) introduces the reaction promotion solution into the reaction unit. A mixing flow path mixes the hydrogen-producing solution extruded by the force of volume expansion in a merging reaction flow path and the reaction promotion solution.    USE - Hydrogen generator for fuel cell (claimed).    ADVANTAGE - The reactivity of the hydrogen-producing solution and reaction promotion solution can be enhanced so that the hydrogen of required amount can be generated effectively and exactly without requiring the large-scale mechanism. The pH of the aqueous solution can be changed rapidly so that the hydrogen producing controllability can be improved efficiently.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the hydrogen generator.    Hydrogen generator (1)    Reaction unit (5)    Hydrogen-producing solution supply flow channel (7)    Reaction promotion solution supply flow channel (8)    Hydrogen consumption apparatus (14)
NOVELTY - Producing a volatile biomass product, comprises: subjecting biomass (50) to sequential or concurrent ramps of temperature and pressure shocks; and selectively collecting at least one group of volatile compounds as it is released from the biomass.    USE - The method is useful for producing: a volatile biomass product or a group of volatile compounds including lipids, furans, hydrocarbons or hydrocarbon fragments or synthesis gas; and biofuel (all claimed), diesel, gasoline or jet fuel.    ADVANTAGE - The method utilizes: temperature ramps and pressure shocks, hence provides the volatile biomass product in high yield; and the supercritical fluids that improve heat transfer and accelerate reaction rates, hence it is efficient, as compared to conventional methods.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a system for converting biomass to biofuel, comprising: means for applying pressure shocks to biomass; means for applying temperature ramps to the biomass; and means for collecting the group of volatile components as it is released from the biomass.    DESCRIPTION OF DRAWING(S) - The figure shows a flow diagram of biomass conversion to char with subsequent reaction in a reactor.    Biomass (50)    Reaction chambers (51)    Residual char (52)    Biomass fractionation reactor (60)
NOVELTY - Humidification condition of moisture in fuel cell stack (40) is controlled and reformate gas containing moisture is passed through carbon monoxide remover (30) which is at temperature more than evaporation temperature of moisture, to operate fuel cell.    USE - Method of fuel cell operation (claimed).    ADVANTAGE - The fuel cell is operated economically and efficiently without using separate membrane humidifier.    DESCRIPTION OF DRAWING(S) - The drawing shows configuration view of fuel cell system.    Reformer (10)    Carbon monoxide remover (30)    Fuel cell stack (40)    Primary heat exchanger (50)    Controller (70)
NOVELTY - The arrangement has an exhaust gas system (24) for connecting a combustion chamber of a cylinder of an internal combustion piston engine by an exhaust valve (23) to atmosphere via a turbine section (28-2) of a turbo charger unit. A fuel processing unit (34) i.e. oxidation catalyst unit, oxidizes fuel material in exhaust gas of the engine. A flow path (32) is provided in the exhaust gas system in vicinity of the exhaust valve of the cylinder at a side opposite to the chamber. The processing unit is arranged into the flow path to receive and process fuel material in the exhaust gas.    USE - Arrangement for reducing slip of fuel material i.e. methane, to atmosphere in an internal combustion piston engine e.g. gas operated piston engine such as dual-fuel (DF) engine, gas diesel engine and externally ignited gas engine.    ADVANTAGE - The arrangement facilitates effective handling of unburned fuel material. The arrangement allows concentration of methane to be made high, thus increasing temperature in the oxidation catalyst unit and improving reduction of the fuel material slip. The oxidation catalyst unit is small in size so as to consume less space. The oxidation catalyst unit can be placed off the engine and easily bypassed. The arrangement allows post combustion oxidation to be arranged in a feasible manner. The arrangement improves fuel flexibility, and can be operated in an efficient manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a method for reducing fuel material slip to atmosphere in an internal combustion piston engine    (2) a cylinder head for an internal combustion piston engine.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a cylinder head of an internal combustion piston engine.    Exhaust valve (23)    Exhaust gas system (24)    Turbine section (28-2)    Flow path (32)    Fuel processing unit (34)
NOVELTY - The method involves preparing a chromium metal film on a substrate, which is made of silicon or glass. A photo-resist layer is coated on a surface of the metal film. A photo-etching and developing processes are carried out for the photo-resist layer to form a required electrode pattern. The electrode pattern is placed in chromium etching solution for etching to obtain an electrode of needed shape. The electrode is placed in a high temperature furnace for heat processing. The electrode is carbonized by loaded metal catalyst, and a carbon electrode is obtained.    USE - Method for manufacturing a micro-membranous fuel cell electrode.    ADVANTAGE - The electrode is carbonized by the loaded metal catalyst, and the carbon electrode is obtained, so that catalytic performance and chemical reaction speed are improved. The method enables manufacturing the micro-membranous fuel cell electrode in simple operation steps.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a micro-membranous fuel cell electrode.
NOVELTY - A carbonization furnace comprises hearth and dry distillation kettle, where gap between dry distillation kettle and hearth comprises flue of combustion chamber. The hearth is provided inside furnace chamber. Bottom of dry distillation kettle includes kettle cover provided with dry distillation of fin material and inner fin shape which is freely pick-and-place. The distillation kettle is provided with outer wall of outer fin gas channel structure.    USE - Carbonization furnace for carbonization production of wood raw material (claimed) such as tree wood, hard wood, bamboo, agricultural and forestry waste raw material.    ADVANTAGE - The furnace provides uniform heating to wood raw material, thus avoiding half cooked, improves heat exchange efficiency, reduces fuel consumption, reduces heating time and stabilizes charcoal. It has simple structure.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for use of carbonization furnace to carbonize wood raw material which comprises putting carbonized wood raw material, sorting and removing impurities, cutting to length of less than 30 cm and less than 60 cm2 of small blocks, sieving wood raw material for drying and dehydrating; controlling water content to less than 20%, where dehydration of wood raw material is provided on material frame; and integrating material into dry distillation kettle, carbonizing at 500-700 degrees C for 3-6 hours.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating a carbonization furnace.
NOVELTY - A carbonization furnace comprises hearth provided in dry distillation kettle. A gap between dry distillation kettle and hearth is provided with combustion chamber. Bottom of dry distillation kettle comprises kettle cover and kettle body. Distillation kettle is provided with outer wall of outer fin gas channel structure.    USE - Carbonization furnace for carbonization production of wood raw material (claimed), which is fruit tree wood, wood hard, bamboo, agricultural or forestry waste raw material.    ADVANTAGE - The furnace provides uniform heating to wood raw material, thus avoiding half cooked, improves heat exchange efficiency, reduces fuel consumption, reduces heating time and improves and stabilizes charcoal.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for use of the carbonization furnace to carbonize wood raw material which comprises putting carbonized wood raw material, sorting and removing impurities, cutting length to less than 30 cm and less than 60 cm2 of small blocks, and sieving wood raw material for drying and dehydrating; and controlling water content to less than 20%, performing dehydration of wood raw material on material frame and integrating material into dry distillation kettle; and carbonizing with high temperature flue gas at 500-700 degrees C for 3 hours.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating a carbonization furnace.
NOVELTY - Sewage treatment device comprises a processing device provided with a feeding and discharging device. The bottom is provided with a drain valve of processing device. The processing device is provided with an external circulation control device and a dosing device. The feeding device comprises a liquid level controller set on inner cavity of the processing device. The processing device is respectively connected with inner cavity of feeding pipe and discharging pipe. The feeding pipe and the discharging pipe are respectively provided with a feeding pump and a discharging pump.    USE - Sewage treatment device.    ADVANTAGE - The device is environment-friendly, has convenient operation, saves labor force, and improves the mixing effect of strain in the processing device, which improves the sewage processing by an external circulating air outlet.
NOVELTY - A dust-removing biomass pyrolysis crucible furnace comprises orderly connected biomass pyrolysis chamber (8), dust removing device (12) and crucible furnace (19). The inlet of dust removing device is connected at one end to pyrolysis chamber. The outlet end is connected through the crater (15) to crucible furnace.    USE - A dust-removing biomass pyrolysis crucible furnace.    ADVANTAGE - The device improves cracking efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of dust-removing biomass pyrolysis crucible furnace.    Biomass pyrolysis chamber (8)    Dust removing device (12)    Crater (15)    Crucible furnace (19)
NOVELTY - Processing of oil field oil-containing sewage comprises putting oil-containing sewage in two-stage biological contact oxidation treatment biochemical pool; filtering liquid, such that at all levels of biological contact oxidation, biochemical pool under bottom aeration, uses Bacillus adsorbed hydrophilic fiber filler; and controlling gas and oily wastewater aeration volume ratio at (20-30):1, biochemical pool pH at 6-9.5, carbon, nitrogen, and phosphorus ratio of 100:5:1, dissolved oxygen of not less than 4 mg/l, and process environment temperature at 15-40 degrees C.    USE - Processing of oil field oil-containing sewage.    ADVANTAGE - The method can thoroughly remove end product of sewage system that is not completely removed within residual emulsified oil. It effectively improves efficiency of biological treatment systems, and reduces sewage biochemical system residence time from more than 12 hours to 8 hours.    DETAILED DESCRIPTION - Processing of oil field oil-containing sewage comprises putting oil-containing sewage in two-stage biological contact oxidation treatment biochemical pool; filtering liquid, such that at all levels of biological contact oxidation, biochemical pool under bottom aeration, uses Bacillus adsorbed hydrophilic fiber filler; and controlling gas and oily wastewater aeration volume ratio at (20-30):1, biochemical pool pH at 6-9.5, carbon, nitrogen, and phosphorus ratio of 100:5:1, dissolved oxygen of not less than 4 mg/l, and process environment temperature at 15-40 degrees C. The Bacillus is Bacillus (CGMCC 5135), Bacillus (CGMCC 5136), or Bacillus (CGMCC 5137).
NOVELTY - Method for performing energy induction technology, involves extracting organic liquid from plant, mixing organic liquid, fertilizer additive, microbial leaven, chemical raw material, organic raw material and functional bacteria, performing high temperature aerobic fermentation to the above-mentioned mixture, and decomposing the fermented mixture.    USE - The method is useful for performing energy induction technology which is useful for preparing organic and biological fertilizer (claimed).
NOVELTY - Producing ethanol involves: establishing an atmosphere containing a methanol forming catalyst and an ethanol forming catalyst; injecting syngas into the atmosphere at a temperature and for a time to produce methanol; and contacting the produced methanol with additional syngas at a temperature and for a time to produce ethanol.    USE - For producing ethanol (claimed).    ADVANTAGE - The present method is carried out using two catalysts, one for purely methanol production, and another for purely ethanol production. The system integrates methanol with ethanol production, thereby resulting in less energy usage. In the system, the end point production of ethanol is irreversible, and no heat is added to the system after the heated syngas is fed to the atmosphere. The irreversibility continues to drive the conversion of syngas past the intermediate production of methanol to arrive at ethanol. The methanol homologation catalyst is co-introduced with methanol catalyst in the same oil phase. Thus, providing one reaction venue or phase and as such obviating the need for the just formed methanol to transfer from a first liquid phase (containing the methanol-producing catalyst) to a second phase that contains homologation catalyst.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an integrated system for producing methanol and ethanol from syngas comprising: an atmosphere isolated from the ambient environment; a first catalyst to produce methanol from syngas, where the first catalyst resides in the atmosphere; a second catalyst to produce ethanol from methanol and syngas, where the second catalyst resides in the atmosphere; a unit for introducing syngas to the atmosphere; and a protocol for separating ethanol from the atmosphere.
NOVELTY - The gas purifier (105) has a collection tank (107) and a purification inlet (106) for supplying a two-phase fluid into the collection tank. A sprinkler (109) is adapted to distribute washing liquid onto several washing dishes (108). A recondenser (111) is provided with a heat exchanger in which a refrigerating fluid is circulated. A purification outlet (112) is adapted to convey a flow of gas to-be-purified through multiple washing dishes and the recondenser. The washing dishes are shaped such that the accumulation of washing liquid is allowed.    USE - Gas purifier for purifying gas such as oxygen and hydrogen gas produced by electrolytic generator (claimed) from electrolyte contaminants. Uses include but are not limited to thermal treatment, oxy-cutting, braze welding, glass and crystal processing, sintering and thermal treatment furnace, cooling of medium-power alternator.    ADVANTAGE - The purifier is provided with compact dimension, thus the electrolytic generator with the simple and economical system structure can be obtained. The reliability can be improved, the number of components can be reduced and the manufacturing cost can be reduced. The electrolytic generator with purifier is conveniently enclosed within a confined space, thus the system components can be protected, and the operational safety can be maintained. The need for frequent service to refill or handle the electrolyte can be avoided.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) electrolytic generator of oxygen and hydrogen gas; and    (2) a method for purifying oxygen and hydrogen gas produced in electrolytic dissociation cell of electrolytic generator.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the electrolytic generator comprising the purifier.    Gas purifier (105)    Purification inlet (106)    Collection tank (107)    Washing dish (108)    Sprinkler (109)    Recondenser (111)    Purification outlet (112)
NOVELTY - Organic waste source separation treatment system comprises an organic waste source separation system, an organic waste conveying system, an organic waste automatic packaging system and an organic waste treatment system. The separation system and conveying system are connected. The conveying system and automatic packaging system are connected. The packaging system adopts chemical fiber filter bag for packaging organic waste and filtrate, and respectively conveys to the treatment system.    USE - Used as an organic waste source separation treatment system.    ADVANTAGE - The system serves as kitchen waste conveying pipeline in providing convenience to resident, thus the kitchen waste can be transported, avoids the mixed pollution caused by kitchen waste and other domestic waste, and ensures maximized recycling of the other materials; and saves water and energy when installed in toilets, and ensures that feces and urine are conveyed and discharged separately.
NOVELTY - A device comprises combustion furnace (1) having at least one wall set in cracking furnace (2), fuel gas pipe (4), combustion-supporting gas pipe (5) and ignition device (6). The cracking furnace has feeding port (7), sealing gate (8) and gas-collecting pipe (9).    USE - The device is used for producing synthesis gas for preparing fermentable reducing sugar from biomass (claimed).    ADVANTAGE - The method has high conversion rate and does not produce tar, dioxin and other harmful gases.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the production of synthesis gas from biomass comprising heating furnace to 900-1200 degrees C, adding biomass through feeding port (7) into cracking furnace (2), closing sealing gate (8), performing anaerobic pyrolysis at high temperature and collecting synthesis gas comprising carbon monoxide, methane and hydrogen gas through gas-collecting pipe (5).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the device.    Combustion furnace (1)    Cracking furnace (2)    Fuel gas pipe (4)    Combustion-supporting gas pipe (5)    Ignition device (6)    Feeding port (7)    Sealing gate (8)    Gas-collecting pipe (9)
NOVELTY - A sludge synthetic fuel comprises 40-60 wt.% sludge, 1-10 wt.% straw, 10-30 wt.% pulverized coal, and 10-35 wt.% combustion improver. The fuel has a combustion value of 4000-5000 kcal.    USE - Sludge synthetic fuel is used in combustion furnace.    ADVANTAGE - The sludge synthetic fuel can be prepared with high sludge processing capacity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of sludge synthetic fuel, which involves adding sludge into a sludge storage hopper, adding biochemical treatment additive into a biochemical treatment additive bin, mixing the added materials in a mixer through a conveyor, deodorizing and sterilizing sludge, transferring materials to a curing mixer through a conveyor, adding solidifying additive, curing sludge while biochemically treating, processing the material in a waste-gas absorbing tower, adding straw, pulverized coal, and combustion improver, mixing in a synthetic mixer, crushing the obtained fuel, dewatering to a water content of 20%, and conveying to a forming machine.
NOVELTY - Mineralization of garbage from organic waste water using multiphase method involves: adding organic waste water in the electrolytic slot; then adding hydrogen peroxide (H2O2) solution in waste water, where the electrolytic slot contains anode electrode and cathode electrode, where anode electrode is iron electrode, and cathode electrode is graphite electrode; flowing current in the whole process, while continuously stirring; after the reaction is finished, settling, and separating the waste from discharged water.    USE - For mineralization of garbage from organic waste water using multiphase method (claimed).    ADVANTAGE - The method uses iron electrode in the electrolytic oxidation which save electric energy; has good electrolysis and microbial degradation property; and has strong adaptability, strong processing ability, and strengthens treatment effect.
NOVELTY - The method involves processing biomass and waste as a raw material from a furnace top into a gas-producing furnace. High temperature combustion gas is sent to inside the gas-manufacturing furnace and a steam manifold. Mixing gas is injected into a furnace outlet pipe that passes through a drying layer. The furnace is provided with a material layer from top to bottom. A cracking layer is provided with a residual carbon on a furnace grate. An original furnace grate is provided with carbon and water vapor to generate water gas reaction.    USE - Gas producing method.    ADVANTAGE - The method enables avoiding the need of an external heat source for high temperature cracking biomass and utilizing municipal waste for producing coal gas, and preventing mixing of gas with raw material.    DESCRIPTION OF DRAWING(S) - The drawing shows a circuit diagram illustrating a gas producing method. '(Drawing includes non-English language text)'
NOVELTY - The hopper has a wedge plate guide box (7) connected with a feeding port cover (1). A storage hopper body (2) is connected with a lower end of a sliding plate (4) that is passed through a gasification furnace wall (8) extending into a biomass gasification fuel gas interlayer inner container. The gasification furnace wall is connected with the storage hopper body and equipped with the wedge plate guide box. A wedge-shaped plate (5) is inserted in a wedge plate groove (3). A handle (6) is fixedly connected with surface at an upper end of a wedge-shaped insert plate.    USE - Biomass gasification furnace feeding hopper.    ADVANTAGE - The hopper has better sealing property, simple and convenient operation, simple structure and wide application range, and avoids long-term impeding during development of a gasification furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a biomass gasification furnace feeding hopper.    Feeding port cover (1)    Storage hopper body (2)    Wedge plate groove (3)    Sliding plate (4)    Wedge-shaped plate (5)    Handle (6)    Wedge plate guide box (7)    Gasification furnace wall (8)
NOVELTY - The method involves crushing biomass to obtain a granular material. The granular material is sent to a cracking furnace. Oxidation-reduction reaction and cracking reaction are carried out at the same time by forming electric arc ignition with pure oxygen. Combustible gas to be purified is cooled by an oil absorption tower and a condenser. The separated gas is cleaned by washing the gas and conveying the gas to a gas storage tank. Mixed liquid is separated out by an oil skimmer to remove water and sent to the furnace.    USE - Method for preparing biomass thermal cracking gas by utilizing solid organic waste.    ADVANTAGE - The method enables utilizing pure oxygen combustion-supporting heating technology to avoid the need of large amount of nitrogen so as to improve producing gas heat value. The method enables preparing the gas in a reasonable manner, allowing continuous charging and discharging of the gas and improving production capability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biomass thermal cracking gas preparing device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a biomass thermal cracking gas preparing method.
NOVELTY - Preparing jionoside-A1 from purple Rehmannia, comprises taking Rehmannia root and then crushing, adding 5-10 times of water and then extracting, filtering the extracting solution using ultra filtration membrane and nano-filtration membrane, adding ethyl acetate to the filtrate to extract, concentrating the extracted liquid by aluminum oxide column, separating the concentrated solution, taking chloroform-methanol-normal butanol-water as solvent system, where the upper phase is fixed phase and the lower phase is mobile phase and then steam drying.    USE - The method is useful for preparing jionoside-A1 from purple Rehmannia (claimed).    ADVANTAGE - The method uses membrane separation and high speed counter-current chromatography separation technology to prepare jionoside-A1 with high yield and low pollution.    DETAILED DESCRIPTION - Preparing jionoside-A1 from purple Rehmannia, comprises taking Rehmannia root and then crushing, adding 5-10 times of water and then extracting at 60-75 degrees C, filtering the extracting solution using ultra filtration membrane and nano-filtration membrane, adding ethyl acetate to the filtrate to extract, concentrating the extracted liquid by aluminum oxide column, separating the concentrated solution by high speed counter-current chromatography and taking chloroform-methanol-normal butanol-water as solvent system, where the upper phase is fixed phase and the lower phase is mobile phase and then steam drying.
NOVELTY - Manufacture of oil in water (O/W) emulsified composition involves preparing O/W emulsification portion by emulsifying oil phase (A) containing 12-26C higher aliphatic alcohol and oil component, and aqueous phase containing anionic surfactant which can form ( alpha )-gel with component (A), alkylene-oxide derivative (I), and water at 80 degrees C or more, and cooling by mixing and stirring emulsification portion (excluding aqueous phase (second aqueous phase)) at 10-35 degrees C. The content of alkylene-oxide derivative in the emulsification portion is 1-30 %mass.    USE - Manufacture of O/W emulsified composition. Uses include but are not limited to milky lotion, cream, massage cream, cleansing cream, essence, body cream, hair cream, conditioner, rinse, sun screen, cleansing and makeup remover, foundation, pharmaceutical and quasi-drug.    ADVANTAGE - The method economically and efficiently provides O/W emulsified composition with reduced impact on environmental pollution, by simple process.    DETAILED DESCRIPTION - Manufacture of O/W emulsified composition involves preparing O/W emulsification portion by emulsifying oil phase (A) containing 12-26C higher aliphatic alcohol and oil component, and aqueous phase containing anionic surfactant which can form ( alpha )-gel with component (A), alkylene-oxide derivative of formula: R1O-((AO)m(EO)n)-R2 (I), and water at 80 degrees C or more, cooling by mixing and stirring emulsification portion (excluding aqueous phase (second aqueous phase)) at 10-35 degrees C. The content of alkylene-oxide derivative in the emulsification portion is 1-30 %mass. The ratio of oxyalkylene group with respect to the sum total of 3-4 oxyalkylene group and oxyethylene group is 20-80 wt.%.    AO=3-4C oxyalkylene;    EO=oxyethylene;    m,n=average added mole numbers of oxyalkylene group and oxyethylene group of 1-70;    A=3-4C oxyalkylene group and oxyethylene group;and    R1,R2=1-4C alkyl.
NOVELTY - Pre-processing biomass by using vacuum hydro-thermal method comprises (a) cutting and crushing biomass raw material; (b) degassing treatment with pre-treated water or de-ionized water; (c) adding water to the biomass material in the reaction kettle; (d) adjusting the mass ratio of the biomass and water from 1:10 to 1:50, mixing them uniformly; (e) putting high pressure in the kettle; (f) when the temperature of the reaction kettle reaches 150-230 degrees C, keeping for 1-30 minutes; and (g) where the temperature of the reaction kettle is less than 50 degrees C, taking out the material.    USE - The method is used for pre-processing biomass. The pre-processed biomass is useful producing sugar, ethanol, butanol, animal feed, or fertilizer (all claimed).    ADVANTAGE - The method above reduces the probability of side reaction caused by the hydro-thermal pre-processing process due to the presence of oxygen; enhances the treatment effect; no potential inhibiting effect to the subsequent use of the inhibitor; and requires low concentration of materials.
NOVELTY - Synthesizing diacerein (III), comprises (a) oxidizing 1,8-dihydroxy-3-hydroxymethyl-anthraquinone (I) in a presence of reaction solvent, (b) adding catalyst and hydrogen peroxide solution to the oxidized solution and then refluxing at 80 degrees C for 1-5 hours to obtain 4,5-dihydroxy-9,10-dioxo-9,10-dihydro-anthracene-2-carboxylic acid (II) and (c) acetylating (II).    USE - The process is useful for synthesizing (III) (claimed).    ADVANTAGE - The process: avoids the traditional chromium-containing oxidant; and provides (III) with mild reaction condition and improved quality, in cost-effective and environmental-friendly-manner.
NOVELTY - Multinutrient plant fermented fertilizer is prepared by adding 20 parts poultry and livestock manure, 20 parts plant oil residue, 1 part fermenting agent and 1 part sulfur powder into fermentation tank, adding water, uniformly stirring mixture, sealing fermentation tank, fermenting the mixture for 150-200 days when the fermentation tank does not exhaust gas when the fermentation process is finished, removing seal of the fermenting tank, and filtering and extracting concentrated solution.    USE - The multinutrient plant fermented fertilizer is useful for planting flowers, vegetables, fruits, melons and grains.    ADVANTAGE - The fertilizer is rich in biological active substances and comprehensive in nutrient, enhances stress tolerance and the disease and pest resistance of crops after the fermentation fertilizer is applied, converts bacteria such as nitrogen-fixing bacteria, phosphate solubilizing bacteria and potassium solubilizing bacteria in fertilizer to nutrient substances in soil to be used by the crops, improves quality of agricultural products, and promotes yield increase and income increase of crops.
NOVELTY - The electrode plate has main portion which is provided with metal main electrode plate (2) and plastic electrode frame (1) such as enhanced polysulfone electrode frame, reinforced polyether ether ketone electrode frame, or enhanced polyphenylene sulphide electrode frame. The plastic electrode frame is provided on the outer edge of main electrode plate. The metal main electrode plate is provided with air holes (3). A nickel plate is embedded to the main electrode plate.    USE - Hydrogen electrode plate.    ADVANTAGE - The processing precision of electrode plate can be improved. The processing time of electrode plate can be shortened. The production efficiency of electrode plate can be improved. The consumption of steel can be reduced. The external appearance of electrode plate can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a manufacturing method of hydrogen electrode plate.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the of hydrogen electrode plate.    Plastic electrode frame (1)    Metal main electrode plate (2)    Air hole (3)
NOVELTY - Preparing biological selenium-enriched fertilizer involves culturing multiple kinds of microbes having specific functions to obtain mass of selenium-enriched living cells; and fermenting the composite culture substance of multiple probiotics under the anaerobic condition to obtain a mass of selenium enriched multi-strain fermentation product.    USE - For preparing biological selenium-enriched fertilizer (claimed) for increasing selenium containing nutrient of crops through leaf fertilization and improving the quality of farm product crops such as melon and vegetable, leaf vegetable, tobacco, tea, fruit trees, soybean.    ADVANTAGE - The method prepares fertilizer is safe and reliable to human, livestock, plant and soil, has no toxicity and harm; has no side effect and pollution to the environment; effective in little dosage; is convenient to application; improves the stress resistance, improves yield of crop.
NOVELTY - Rhizosphere regulating agent is prepared by mixing raw materials comprising 4-5 pts. wt. sulfur, 5-7 pts. wt. nitrogen fertilizer, 4-5 pts. wt. phosphate fertilizer, and 4-5 pts. wt. potash fertilizer.    USE - The rhizosphere regulating agent is useful for promoting phytoremediation of cadmium-contaminated soil in plant (claimed), and carrying out the remediation of the cadmium-contaminated soil on one hand and carrying out normal agricultural production activities on the other hand.    ADVANTAGE - The agent has excellent stability, is environmentally-friendly, simple, cost-effective and convenient to popularize.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for use method of rhizosphere regulating agent for promoting phytoremediation of cadmium-contaminated soil in plant, which involves planting high cadmium accumulation rapeseed variety on cadmium-contaminated soil, where every hectare is fertilized with 200-400 kg rhizosphere regulating agent.
NOVELTY - Organic fertilizer comprises 1.6-1.8 tons pig manure, 4-6 kg probiotic liquid, 2-5 kg corn meal, 8-10 kg sawdust and 50-75 kg distiller's grains, where the organic fertilizer is prepared by fermenting pig manure.    USE - The organic fertilizer is useful for controlling diseases and pests.    ADVANTAGE - The organic fertilizer is simple and convenient to prepare and improves soil environment and pH value, which promotes growth of crops.
NOVELTY - Preparing organic fertilizer, involves mixing and stirring the main material and plant straw, extracting using water to obtain primary mixed material, mixing and stirring the fermentation auxiliary agent and diluting agent auxiliary material to obtain secondary mixed material, mixing the primary and secondary mixed material uniformly to obtain third mixed material, placing the mixture in fermentation tank and fermenting to obtain semi-finished product, adding calcium oxide, drying, packaging and storing the product.    USE - The method is useful for producing organic fertilizer used for preventing insect pest and plant diseases.    ADVANTAGE - The method is simple and convenient to perform. The produced organic fertilizer improves soil environment with suitable pH and promotes the growth of crops.    DETAILED DESCRIPTION - Method of preparing organic fertilizer, involves mixing and stirring the main material and plant straw with double horizontal shafts, extracting using water at 57-62 degrees C to obtain primary mixed material, mixing and stirring the fermentation auxiliary agent and diluting agent auxiliary material at 0-35 degrees C for 3-12 hours to obtain secondary mixed material, mixing the primary and secondary mixed material uniformly to obtain third mixed material, placing the mixture in a fermentation tank and fermenting at 70 degrees C for 13-15 days to obtain semi-finished product, adding calcium oxide, drying until the water content is reduced to 20% to obtain the finished product, and packaging and storing the product.
NOVELTY - Synthesis of pregnenolone acetate involves: adding sisal saponin, glacial acetic acid and acetic anhydride having weight ratio of 1:0.5 to 1.5:1.5 into pressure kettle, sealing the kettle, vacuumizing, preserving temperature and reacting for 2 hours, cooling, discharging; diluting with methylene dichloride for 2-4 parts by weight (pts.wt.), then adding water (0.1-0.2 pts.wt.), stirring, adding halogenated diimide oxidant (0.2-1 pts.wt.), cooling, adding water, stirring and discharging; and adding the material liquid to ethanol, heating, cooling, filtering and drying.    USE - For synthesis of pregnenolone acetate (claimed).    ADVANTAGE - The method uses the halogenated diimide type material as oxidant; has mild reaction condition, little side reaction and harmful by-product; can effectively reduce the pollution to the environment; as the crown ether phase transfer catalyst, improves the reaction efficiency and reduces the cost; and is suitable for large-scale industrial production.    DETAILED DESCRIPTION - Synthesis of pregnenolone acetate involves: adding sisal saponin, glacial acetic acid and acetic anhydride having weight ratio of 1:0.5 to 1.5:1.5 into pressure kettle, sealing the kettle, vacuumizing, opening the electric heating, where the temperature is raised to 195-205 degrees C, preserving temperature and reacting for 2 hours, cooling, discharging; diluting with methylene dichloride for 2-4 parts by weight (pts.wt.), then adding water (0.1-0.2 pts.wt.), stirring, slowly adding halogenated diimide oxidant (0.2-1 pts.wt.), cooling, adding water, stirring, standing and layering, washing by water, decompressing and concentrating, discharging; and adding the material liquid to ethanol, heating and dissolving, cooling, filtering and drying to obtain the product.
NOVELTY - A highly efficient composite additive comprises 10-15 wt.% isopropyl alcohol, 40-70 wt.% isooctanol, 2-10 wt.% methyl t-butyl ether, 2-10 wt.% tetrahydrofuran, 5-15 wt.% dimethylbenzene, 0.2-0.5 wt.% metal corrosion inhibitor, 0.1-0.4 wt.% rubber swelling inhibitor, 3-10 wt.% dispersant, 0.5-2 wt.% antiwear lubricant and 0.05-0.3 wt.% antioxidant.    USE - Highly efficient composite additive of methanol gasoline.    ADVANTAGE - The highly efficient composite additive produces stable and safe methanol gasoline.
NOVELTY - A Pseudomonas fluorescens deposited under CGMCC No. 5974, is new.    USE - The Pseudomonas fluorescens is useful for preparing textile fiber (claimed).    ADVANTAGE - The method is completely environment-friendly, because all waste liquid can be directly converted into organic fertilizers. In a biological treatment process, fibers are protected. Compared with the conventional chemical methods, the method has the advantages that the production cost is low, the economic benefit is high, energy can be saved and pollution is avoided.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for preparing textile fiber comprising: (a) preparing the bacteria liquid: the Pseudomonas fluorescens is mixed with water to form bacterial liquid; (b) raw material treatment: the ramie raw material cutting section, and the raw material is put into the soaking pool of swelling; and (c) preparing the seal coat of fiber, comprising the steps of: biodegradable, the hydrophobic solution as raw material to soak the prepared bacterial liquid, steam sterilizing: putting the biodegradable raw material from bacteria liquid, draining, steam sterilizing, obtain the fiber: putting the sterilized raw material for the first time period, a fiber bundle, the first time period for the second section grinding, fine grinding to make the fiber beam be separated single fiber, screening, filtering after a period of grinding and the slurry after the second fine grinding of the fiber bundle, and then grinding to make it into single fiber, drying, carding: putting the prepared fiber is soaked in warm water, and then drying for preparing textile fiber.
NOVELTY - Pre-processing for anaerobic fermentation of kitchen waste comprises: (a) transferring the kitchen waste into a receiving bucket of a receiving and conveying system, and then conveying to a crushing and separating system; (b) separating hard substances from the kitchen waste by virtue of a crushing and separating integrated machine in the crushing and separating system; and (c) conveying the pulped waste buffered in step (b) into a sand removing system, and separating the heavy substances, and then feeding into an anaerobic fermentation device.    USE - The method is useful for pre-processing for anaerobic fermentation of kitchen waste (claimed).    ADVANTAGE - The pre-processing method is short in technological process, high in processing efficiency, capable of effectively removing various impurities which bring influence to the anaerobic fermentation system and able to sort the organic waste from the kitchen waste to the maximum.    DETAILED DESCRIPTION - Pre-processing for anaerobic fermentation of kitchen waste comprises: (a) transferring the kitchen waste into a receiving bucket of a receiving and conveying system, and then conveying to a crushing and separating system by virtue of a longitudinal shaftless screw conveyor, a transverse shaftless screw conveyor and a lifting screw conveyor which are arranged at the bottom of the receiving bucket; (b) separating hard substances from the kitchen waste by virtue of a crushing and separating integrated machine in the crushing and separating system, and processing the kitchen waste to obtain pulped waste, and then buffering the pulped waste in a buffering tank of the system; and (c) conveying the pulped waste buffered in step (b) into a sand removing system, and separating the heavy substances, and then feeding into an anaerobic fermentation device.
NOVELTY - Preparing D-arginine comprises preparing L-arginine at 20%, distilled water at 57%, 3,4-dimethylphenylformaldehyde at 3%, wet Streptococcus faecium at 9%, sodium hydroxide aqueous solution at 5% and trichloroacetic acid at 6% as raw materials to obtain the finished product.    USE - The method is useful for preparing D-arginine (claimed).    ADVANTAGE - The method as simple processes and a low cost, does not produce pollution in production, is convenient for volume production and realizes good product quality. Compared with the traditional method, the method has the advantages of mild reaction conditions, low reaction temperature and good product quality.
NOVELTY - Invention relates to the field of agriculture, in particular, to veterinary medicine, and can be used for disinfection of manure. The method provides the application into the manure of mixture of microorganisms Bacillus stearothermophilus, Bacillus subtilis, Bacillus brevis and Bacillus coagulans with subsequent exposition additionaly to the mixture of microorganisms the Streptococcus thermophylus is added. For a mixture the microorganisms are used in a concentration of 1.5-2 million microbial cells in 1 ml. The volume ratio in the mixture of Bacillus stearothermophilus, Bacillus subtilis, Bacillus brevis, Bacillus coagulans and Streptococcus thermophilus constitute 1.0:0.8-1.2:0.8-1.2:0.8-1.2:0.8 -1.2, respectively. The resulting mixture is added to the manure at a volume ratio of 0.01:1-1.5 with subsequent exposition at a temperature of 56 degrees -62 degrees C for 3-4 days.    USE - Agriculture.    ADVANTAGE - Invention provides acceleration and simplification of the method of disinfection of manure.3 ex
NOVELTY - The device has a collecting device (1) which is provided with a cover plate (2) having a probe (3). A baffle plate (4) is provided with a garbage conveyer belt (5). A crushing mechanism (6) is connected with the outlet of pump (7) which is connected with the outlet of steam heater (8). An oil-solid separator (9) is provided with a collecting tank (10) having a feeding mechanism (13).    USE - Device for separating oil-water fin kitchen garbage.    ADVANTAGE - The generation of waste gas and waste liquid can be prevented and the pollution can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of device for separating oil-water.    Collecting device (1)    Cover plate (2)    Probe (3)    Baffle plate (4)    Garbage conveyer belt (5)    Crushing mechanism (6)    Pump (7)    Steam heater (8)    Oil-solid separator (9)    Collecting tank (10)    Feeding mechanism (13)
NOVELTY - Preparing straw-based organic fertilizer, involves triturating natural laterite and haulm or wheat, broomcorn, straw of corn, mountain grass or combustible garbage, boiling the laterite, stirring the boiled laterite and plant ash, moving indoors, moving and irrigating the night soil or pig manure, chicken manure and duck manure to be wet, stacking after evenly stirring, irrigating two burdens of the night soil every two days, stacking after overturning, and placing after continuous 75 days to be used, and fermenting, and carrying out microbial decomposition.    USE - The method is useful for preparing straw-based organic fertilizer.    DETAILED DESCRIPTION - Method for preparing straw-based organic fertilizer, involves triturating 1500 kg natural laterite and 1500 kg haulm or wheat, broomcorn, straw of corn, mountain grass or combustible garbage, boiling the laterite (to be brown by grass or garbage), stirring the boiled laterite and plant ash, moving indoors, moving and irrigating the night soil or pig manure, chicken manure and duck manure to be wet, stacking after evenly stirring, irrigating two burdens of the night soil every two days, stacking after overturning, and placing for 15 days after continuous 75 days to be used, and fermenting by 90 days of bubbling, and carrying out microbial decomposition, and hence the brown muck is changed into black brown, where the nitrogen content of the straw-based organic fertilizer is 5.6%, phosphorus pentoxide content of the straw-based organic fertilizer is 1.3%, and potassium oxide content of the straw-based organic fertilizer is 1.8%, pH of the straw-based organic fertilizer is 7.5, and straw-based organic fertilizer comprises raw materials comprising 1500 kg natural laterite, 150 kg haulm, straw and garbage, proper quantity of plant ash, and several night soil or pig manure, chicken manure and duck manure.
NOVELTY - Bacterial strain, preferably Bacillus amyloliquefaciens under a preservation number of PS57H ICGMCCNo. 6089, is new.    USE - The bacterial strain, preferably Bacillus amyloliquefaciens is useful for decomposing soil soluble phosphorus including inorganic phosphorus containing calcium phosphate, phosphorite and phosphorus iron (all claimed), which is useful as fertilizer.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) phosphorus decomposing microbial inoculum, comprising Bacillus amyloliquefaciens, fermentation liquid or solid microbial inoculum fermentation liquid; (2) the construction of Bacillus amyloliquefaciens; (3) a method for obtaining the fermentation solution of Bacillus amyloliquefaciens comprising mixing glucose (10 g), ammonium sulfate (0. 5 g), yeast powder (0.5 g), sodium chloride (0.3 g), potassium chloride (0.3 g), magnesium sulfate (0.3 g), ferrous sulfate (0.03 g), manganese sulfate (0.03 g), calcium phosphate (5 g), distilled water (1000 ml) to prepare inorganic phosphorus bacteria liquid culture medium having a pH of 7-7.5, and sterilizing inorganic phosphorus bacteria liquid culture medium at 115 degrees C for 30 minutes degrees centigrade, and (2) inoculating Bacillus amyloliquefaciens to inorganic phosphorus of bacteria liquid culture medium according to the proportion of 5% and then shaking speed of 180-200 revolution per minutes and cultivating for 20-24 hours to obtain PS57H1 zymotic fluid; and (4) preparing efficient phosphorus-decomposing microbial inoculum comprising sterilizing PS57H1 fermentation liquor, the grass peat and light calcium carbonate according to weight ratio of 1:4:0.04 at high temperature and uniformly stirring the sterilized material using stirrer and then crushing.
NOVELTY - Hydrogen preparation device comprises four cylindrical electrolytic cells connected together in series and have top areas respectively provided with strip-shaped spray device. Each cylindrical electrolytic cell is provided with cylindrical electrode plate, positive and negative electrodes as air outlet pipeline, cooling tank, and pressure pump, which is connected with gas-water separating tank. The gas-water separating tank and cylindrical electrolytic slots are respectively connected with liquid discharging valve, sewage filter valve, water inlet, and water level switch.    USE - Hydrogen preparation device.    ADVANTAGE - The hydrogen preparation device has simple structure, improved production rate, high energy conversion rate, small volume and light weight, high production efficiency, provides low cost hydrogen production, improves automation level, safe, reliable, and convenient to use.
NOVELTY - Preparing irbesartan, comprises carrying out alkylation reaction on 2-n-butyl-1,3-diaza-spiro(4,4)non-1-en-4-one hydrochloride and 2-cyano-4'-biphenyl with non-polar solvent under the effect of inorganic alkali and phase transfer catalyst to obtain 2-3-((2'-cyano-1'-biphenyl-4-yl)methyl)-1,3(4,4)-1-4-ketone (sic), adding 2-3-((2'-cyano-1'-biphenyl-4-yl)methyl)-1,3(4,4)-1-4-ketone (sic) with diazoimido compound, and carrying out cyclization reaction of the mixture in a polar solvent under the action of cyclization catalyst.    USE - The method is useful for preparing irbesartan (claimed).    ADVANTAGE - The method allows simple and economical preparation of the irbesartan with high yield in a convenient and eco-friendly manner. The method is suitable for industrial production.
NOVELTY - Producing Hypsizygus marmoreus using strain, comprises mixing 20-35 wt.% of sawdust, 25-40 wt.% of corncob, 10-20 wt.% of rice bran, 15-25 wt.% of bran and 1-2 wt.% of lime with water to form a seed culture medium and adding into 1100 ml of primary bottle, inoculating strain in the medium, cooling and culturing the culture medium and mixing with 63-65 wt.% water to form culture medium, inoculating into the medium into cultivated bacteria and cooling, and scratching strain from the medium after standard breeding.    USE - The method is useful for producing Hypsizygus marmoreus (claimed).    ADVANTAGE - The method provides Hypsizygus marmoreus in an environment-friendly and simple manner.    DETAILED DESCRIPTION - Producing Hypsizygus marmoreus using strain, comprises mixing 20-35 wt.% of sawdust, 25-40 wt.% of corncob, 10-20 wt.% of rice bran, 15-25 wt.% of bran and 1-2 wt.% of lime with water to form a seed culture medium with water content of 61-63 wt.%, adding the medium into 1100 ml of primary bottle after sterilizing a liquid plastic bottle, inoculating strain in the medium, cooling and culturing the culture medium at room temperature, keeping the culture medium into the culture chamber at 21-23 degrees C under controlled condition, mixing 10-15 wt.% of sawdust, 10-20 wt.% of corncob, 30-50 wt.% of cotton, 10-20 wt.% of rice bran, 10-20 wt.% of bran, 3-5 wt.% of corn powder and 1-2 wt.% calcium oxide with 63-65 wt.% water to form culture medium, adding the medium into culture bottle after sterilizing a liquid plastic bottle, inoculating the medium into cultivated bacteria and cooling at room temperature, keeping the culture medium into the culture chamber to cultivate at 21-23?0C with air humidity of 60-80%, culturing the strain for 60-80 days, and scratching strain from the medium after standard breeding for 25-26 days, where the chamber has carbon dioxide concentration of 3000-5000 parts per million (ppm) and air humidity of 60-80%.
NOVELTY - The method involves fractionating crude product into a light component and a heavy component. Direct hydrogenation refining reaction is performed on light component. Heavy component is connected with reaction zone structure of catalytic distillation column. Catalytic agent such as aluminium oxide is filled in catalytic distillation tower. Hydrogenation refining or re-mixing reaction is performed with waste plastic oil. Hydrogenated refined distillate oil at normal pressure is fed to distillation tower and separated into petrol and diesel oil distillate according to temperature.    USE - Method for refining biomass material to produce petrol and diesel oil.    ADVANTAGE - The conversion rate and selectivity of reaction series for balancing reaction can be improved. The coking amount can be reduced. Energy can be saved. The service life of the catalyst can be increased. The refining process can be performed effectively and investment cost can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the process for refining biomass material to produce petrol and diesel oil. (Drawing includes non-English language text)
NOVELTY - The generator has a refuse bin whose lower port is provided with cradle. A water cavity (4) is provided in upper portion of casing (2). An upper smoke cavity (8) is defined by upper end plate of combustion chamber. A lower smoke cavity is defined by cylindrical wall of ash bin. An inner fire tube (6) is arranged in upper smoke cavity. The upper and lower ends of outer fire tube (5) are respectively connected with upper end plate of lower smoke cavity and wall of upper smoke cavity. A connection tube is arranged between lower smoke cavity and high-pressure gas tank.    USE - Combustible refuse gas generator.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the combustible refuse gas generator.    Casing (2)    Water cavity (4)    Outer fire tube (5)    Inner fire tube (6)    Upper smoke cavity (8)
NOVELTY - The purifying system has primary purifier and secondary purifier that are communicated with each other. The primary purifier is provided with one cylindrical case (2) and a baffle plate (3). The baffle plate is welded on one side of the inner wall of the cylindrical case and is inclined at 10-20 degrees. Secondary purifier is provided with other cylindrical case (5) and a filtering device. The interior of the filtering device is provided with two mesh-hole type filtering plates (8) and one absorption material (9).    USE - Purifying system for biomass gasification furnace.    ADVANTAGE - The purifying system is good purifying effect, easy to dismount and replace, and low in cost and can be popularized to a large scale.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the purifying system.    Fuel gas inlet (1)    Cylindrical cases (2,5)    Baffle plate (3)    Mesh-hole type filtering plate (8)    Absorption material (9)
NOVELTY - The method involves adding water and coagulant in a sewage treatment dispensing tank. A water adding operation is stopped when a water level is high. An electromagnetic valve is opened. Supernatant fluid is dispensed into a suction pipe. Bottom solid particles are sucked into the suction tube. The particles are stirred via the stirring tube in a plastic centrifugal pump. Sewage treatment coagulant is stirred in a uniform manner. Another electromagnetic valve is opened to disperse liquid medicine. The liquid medicine is conveyed to a sewage treatment equipment.    USE - Method for stirring and dispensing dual-port dual-feeding pump-circulating-type liquid medicine.    ADVANTAGE - The method enables conveying liquid medicine to a unit of the sewage treatment equipment via a metering pump outlet pipe in an effective manner, realizing low equipment investment and simple structure and avoiding blockage for preventing pump overload and realizing easy maintenance and replacement.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a dual-port dual-feeding pump-circulating-type liquid medicine stirring and dispensing method.
NOVELTY - A polyphenol phytotoxicity reducing method involves utilizing mineral component, which is an antidote for transformation of a plant phenolic compound.    USE - Method for reducing polyphenol phytotoxicity released in biological degradation process of lignin and cellulose after composting process.    ADVANTAGE - The method enables reducing polyphenol phytotoxicity with reduced time of maturation of compost, reduced labor force and energy associated with composting process, and increased capacity and profitability.
NOVELTY - The vitamin D2 analog precursor production involves reacting Inhoffen-Lythgoe diol (II) with iodine, imidazole and triphenylphosphine in tetrahydrofuran by protection of secondary alcohol to give a compound (III) The obtained compound is reacted with diphenylphosphine followed by oxidation to give a phosphine compound (IV). The obtained phosphine compound is reacted with aldehyde (V) in a polar solvent at or below -70 degrees C in basic medium to give compound (VI). The obtained compound is reacted with a base in a polar solvent at 0 degrees C to form trans compound (VII).    USE - Method for producing precursor of vitamin D2 analog of formula (I), or their salts or active form used in pharmaceutical industry and foodstuffs.    ADVANTAGE - The method efficiently provides vitamin D2 analog in a simple and eco-friendly manner without using hazardous and toxic reagents, such as amalgam sodium and mercury.    DETAILED DESCRIPTION - The vitamin D2 analog precursor production involves reacting Inhoffen-Lythgoe diol of formula (II) with iodine, imidazole and triphenylphosphine in tetrahydrofuran by protection of secondary alcohol to give a compound of formula (III). The obtained compound is reacted with diphenylphosphine followed by oxidation to give a phosphine compound of formula (IV). The obtained phosphine compound is reacted with aldehyde of formula (V) in a polar solvent at or below -70 degrees C in basic medium to give compound of formula (VI). The obtained compound is reacted with a base in a polar solvent at 0 degrees C to form trans compound of formula (VII). The obtained compound is deprotected to form trans configuration diol of formula (VIII). The formed trans configuration diol is oxidized to obtain the desired compound of formula (I).    R1 and R2=an alcohol protecting group.
NOVELTY - A crude glycerol treating method involves treating crude glycerol from biodiesel distillation after dehydration and alkalinity followed by mixing crude glycerol obtained from vacuum distillation with water or diluting 20-30% crude glycerol obtained from the dehydration process in a distillate to obtain a mixture. The mixture is stirred continuously and cooled to 30-90 degrees C. The cooled mixture is subjected to centrifugation to finish treating the crude glycerol.    USE - Method for treating crude glycerol from biodiesel production.
NOVELTY - The device has air supply device, a carbon dioxide air supply device, a low press, and comprehensive tower. The air supply device and carbon dioxide gas supply device are respectively connected with a low press which is connected to carbonization tower. The carbonization tower is connected with the comprehensive tower.    USE - Carbonizing device for producing methane gas.    ADVANTAGE - The copper sleeve loss of the separated gas is reduced. The environmental pollution is prevented. The nitrogen consumption is reduced.
NOVELTY - The coconut shell material comprises biomass, fibers and plant. The material is burned by using oxygen to produce carbon dioxide.    USE - Coconut shell material for producing energy.    ADVANTAGE - The coconut shell material is burned for producing energy in an eco-friendly manner.
NOVELTY - Improving erythromycin fermentation titer and promoting erythromycin A generation comprises fermenting seed culture of red Streptomyces in a fermentation tank containing erythromycin fermentation culture medium, and controlling the biomass concentration, ventilation ratio, fermentation tank pressure, fermentation temperature, stirring speed, pH and edible oil concentration in fermentation liquid, where erythromycin fermentation culture medium contains betaine, edible oil and microelements, and a surfactant Tween-20 (RTM: Polyoxyethylene (20) is added in fermentation process.    USE - The method is useful for improving erythromycin fermentation titer and promoting erythromycin A generation.    ADVANTAGE - The method creates good environment for synthesizing erythromycin, and reduces production cost.
NOVELTY - Vertical pond photo bioreactor comprises a translucent reactor chamber of generally flat surface having a rectangular cross-sectional profile with an inner surface covered by multiple elevated fins, flexible thin sleeve for containing an algal solution.    USE - The vertical pond photo bioreactor is used in producing biomass and chemical intermediates which is used in producing fuels, chemicals and pharmaceutical agent.    ADVANTAGE - The bioreactor utilizes low-cost disposable sleeve eliminating need for maintenance or clean-up and low-cost air or water jacket for controlling algal solution temperature.    DETAILED DESCRIPTION - Vertical pond photo bioreactor comprises a translucent reactor chamber of generally flat surface having a rectangular cross-sectional profile with an inner surface covered by multiple elevated fins, flexible thin sleeve for containing an algal solution, where the sleeve being at least partially translucent, the sleeve is sleeve for insertion inside reactor chamber, the sleeve thickness and perimeter is configured for the sleeve to rest over tips of fins inside bioreactor, and low-cost conditioning, such as heating or cooling of the algal solution is achieved by displacing conditioning fluid in the space created between fins and the sleeve outer surface.
NOVELTY - Separating mixture of norfloxacin and chlorine piperazine acid, involves adding water to mixture containing norfloxacin (10-20%) and chloro piperazine acid to obtain a slurry, where the weight ratio of the chloro piperazine acid to piperazine acid mixture is 1-2:1; 2) adding acid solution (10-30 mass%) to achieve a pH of 5-5.5 and then filtering to form filtrate comprising chloro piperazine acid and a filter cake; adding alkali solution (2-5 mass%) to filter cake to achieve a pH of 7-8, and then filtering to obtain filtrate and filter cake containing norfloxacin.    USE - For separating method of norfloxacin and chlorine piperazine acid (claimed), used as antibacterial medicine used for tonsillitis, urinary tract infection, biliary tract infection, gastrointestinal tract infection's treatment.    ADVANTAGE - Recycling and separating technique is simple. The operation cost is low; there is no pollution to the environment and the method is capable of recycling the fluorine piperazine acid. The piperazine acid has high purity.    DETAILED DESCRIPTION - Separating mixture of norfloxacin and chlorine piperazine acid, involves adding water to mixture containing norfloxacin (10-20%) and chloro piperazine acid to obtain a slurry, where the weight ratio of the chloro piperazine acid to piperazine acid mixture is 1-2:1; adding acid solution (10-30 mass%) to achieve a pH of 5-5.5 and then filtering to form filtrate comprising chloro piperazine acid and a filter cake; adding alkali solution (2-5 mass%) to filter cake to achieve a pH of 7-8, and then filtering to obtain filtrate and filter cake containing norfloxacin. The acid solution is formic acid or acetic acid solution. The alkali solution is sodium hydroxide, potassium hydroxide solution or ammonia water.
NOVELTY - An efficient leavening agent for livestock manure, comprises microbial strain component comprising 15-25% of Streptococcus faecalis, 10-20% of Enterococcus faecium producing lactic acid, 2-8% of Sporotrichum, 3-8% of Streptomycete, 5-15% of Saccharomycetes, 5-15% of Sphingobacterium multivorum, 5-15% of Bacillus laterosporus, and 5-15% of Bacillus natto; and carrier component comprising 10-20% of kieselguhr.    USE - The efficient leavening agent is useful for livestock manure (claimed).    ADVANTAGE - The leavening agent is made of all kinds of feed grade high-density and highly dynamic lactic acid bacteria, other fermented cultures and carrier kieselguhr. It can rapidly ferments livestock manure into odorless matters with aroma and sour flavor, and then accumulatedly ferments into completely harmless product, wipes out pathogenic bacteria thoroughly, where the product is applicable as feed for livestock and fish.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a fermentation method of leavening agent comprising: (a), preparing the leavening agent and wheat bran and/or corn according to mass ratio of 1-1.2:10-12 into culture premixing agent; (b) uniformly mixing the culture premixing agent and livestock manure according to mass ratio of 1-1.5:200-300, preparing into livestock manure mixed materials, controlling the water content of mixed materials at 40-70 wt.%, loosely stacking the mixed materials, sealing and fermenting; (c) fermenting the sealed mixed materials, making the mixed materials rise above fermenting tank, controlling fermenting time at 3-25 days.
NOVELTY - Producing combustion fuel mixture, comprises mixing cashew nut shell (4500 kcal/kg) with coal, drying cashew nut shell, and controlling grain size of the nut shell to fixed size.    USE - The method is useful for producing combustion fuel mixture (claimed)    ADVANTAGE - The method is capable of economically and energy efficiently producing the fuel mixture with good fuel combustibility and without environmental pollution.
NOVELTY - Converting a cellulosic material into a bio-oil comprises (a) contacting the cellulosic material with a liquid solvent (104) in an inert atmosphere at a reaction temperature of 260-400 degrees C to produce a product mixture (108), (b) separating a middle fraction (120) from the product mixture to produce a product mixture middle fraction, and (c) recycling a first volume part of the product mixture middle fraction to be used as part of the liquid solvent and a second volume part of the product mixture middle fraction to produce the bio-oil.    USE - The process is useful for converting the cellulosic material into the bio-oil (claimed), where the cellulosic material comprises agricultural wastes such as corn stover, soybean stover, corn cobs, rice straw, rice hulls, oat hulls, corn fiber or cereal straws including wheat, barley, rye and oat straw or grasses, forestry products including wood and wood-related materials such as sawdust, waste paper or sugar processing residues such as bagasse and/or beet pulp, where the bio-oil is useful in engine of a transportation vehicle.    ADVANTAGE - The process ensures economic conversion of cellulose material without requiring large quantities of solvent.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a process for converting a cellulosic material into a bio-oil.    Product mixture (108)    Solid-liquid separator (110)    Removing top fraction (118)    Separating middle fraction (120)    Removing bottom fraction. (122)
NOVELTY - The system has a retention tank (22) receiving biomass slurry discharged through a bottom outlet (20) of a pre-treatment reactor vessel (12), where the tank receives recovered wash liquid to dilute the slurry in the tank with the liquid and discharge diluted biomass slurry. A drain device has a biomass slurry inlet receiving the discharged slurry from the tank, a solids outlet to discharge concentrated biomass slurry and a liquid drain to discharge liquid extracted from the slurry. The liquid drain is in fluid communication with the tank such that the discharged liquid flows to the tank.    USE - System for washing processed biomass i.e. cellulosic biomass, and removing dissolved solids e.g. five carbon sugars (C5) and six carbon sugars (C6), from the biomass.    ADVANTAGE - The biomass is washed and dewatered to extract dissolved hemi-cellulose to separate the C5 sugars in the biomass from other sugars e.g. C6, in the biomass after pre-hydrolysis process.    DETAILED DESCRIPTION - The drain device is an inclined solids passage. INDEPENDENT CLAIMS are also included for the following:    (1) a system for processing biomass    (2) an apparatus for washing processed biomass and removing dissolved solids from the biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram representing a process for extracting hemi cellulosic components from biomass and reducing dissolved solids content of biomass following pre-hydrolysis.    Pre-treatment reactor vessel (12)    Liquor (16)    Bottom outlet (20)    Retention tanks (22, 34, 42)    Fresh wash liquid (24)
NOVELTY - This invention relates to a method of preparing the waste-derived fuel, comprising the following steps: providing the fibrous peat; adding the microbial organism, the leavening agent and the microbial fermentation promoter by a predetermined ratio to form a mixture, followed by doping and well mixing; and carrying out fermentation on the well mixed mixture and fibrous peat for a period of time, thereby forming the solid waste fuel.
NOVELTY - Organic fertilizer is obtained by mixing placenta and organic materials suitable for plants, preferably vegetables.    USE - The fertilizer is useful for improving plant growth by nourishing soil with micronutrients.    ADVANTAGE - The fertilizer produces vegetable with high quality, provides efficacy immediately and for long period as it decomposes slowly, can be easily absorbed by plants, improves taste and suppresses offensive odor of vegetables, and produces vegetable that contains no harmful materials.
NOVELTY - The method involves connecting a fuel cell stack (201) with an external load using a power circuit unit for obtaining electric power. A control part is utilized to perform maintenance correction of driving state by setting and monitoring driving condition of an attached equipment containing a reactive-gas supply part and the power circuit unit. Oxidizing agent gas is supplied to the fuel cell stack in continuous electric power generation. Reducible gas i.e. hydrogen, is contained in the fuel stack. The oxidizing agent gas is humidified within a humidifier.    USE - Method for operating a solid polymer electrolyte type fuel cell system.    ADVANTAGE - The method enables preventing active deterioration of electrode catalyst and stabilizing catalyst over long period of time, thus improving battery characteristic of a fuel cell system and lifetime of the fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a solid polymer electrolyte type fuel cell system.    Fuel cell stack (201)    Fuel generator (203)    Combustion part (204)    Cooling water pump (205)    Fuel gas discharge valve (207)
NOVELTY - Converting energy stored in phytoplankton into mechanical, electrical and/or thermal energy, comprises producing carbon dioxide from phytoplankton, and using produced carbon dioxide for culturing phytoplankton.    USE - The method and the combined device are useful for converting energy stored in phytoplankton into mechanical, electrical and/or thermal energy. (all claimed).    ADVANTAGE - The method converts energy without releasing carbon dioxide into the atmosphere and is environmentally friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a combined device for converting energy stored in phytoplankton into mechanical, electrical and/or thermal energy, comprising (i) a device for producing biomass, where phytoplankton is subjected with carbon dioxide, (ii) a device for gasifying biomass obtained in step (a), (iii) a device for combusting the gas obtained in step (b), and for converting the thermal energy obtained during combustion, into mechanical and/or electrical energy, (iv) a device for oxidizing exhaust gases obtained in step (c), (v) a device for separating carbon dioxide obtained in step (d), and (vi) a device for transferring carbon dioxide obtained in step (e) into the apparatus (i).    DESCRIPTION OF DRAWING(S) - The figure shows a schematic flow diagram of the method and the device.    Greenhouse (i)    Gas engine (iii)    Oxidation catalyst (iv)    Extraction device (v)    Pipe (vi)
NOVELTY - The method comprises adding hydrogel to waste edible oils or fats (0.1-1 wt.%) present in liquid form, mixing the hydrogel with the oils or fats for a dwell time of 5-15 minutes to obtain a mixture, and filtrating the mixture with the separation of the hydrogel and the polyolefin from the oils or fats. The waste edible oils or fats are pretreated or not pretreated, water-degummed or partially degummed, neutralized or partially neutralized, dehydrated and/or partially dewatered. The mixing step is performed by stirring in a container or on a mixing chamber provided with a mixing device.    USE - The method is useful for separating polyolefins from waste edible oils or fats to produce biodiesel (all claimed) such as biosynthetic fuel, where: the oils are rapeseed oils; and the edible oils and fats are useful in home, restaurants, fast food restaurants, and food processing industry.    ADVANTAGE - The method allows simple and effective separation of the polyolefins from the oils or fats with less consumption of energy thus providing economical production of the biodiesel with high quality in an environmentally-friendly manner.    DETAILED DESCRIPTION - The method comprises adding hydrogel to waste edible oils or fats (0.1-1 wt.%) present in liquid form, mixing the hydrogel with the waste edible oils or fats for a dwell time of 5-15 minutes to obtain a mixture, and filtrating the mixture with the separation of the hydrogel and the polyolefin from the waste edible oils or fats. The waste edible oils or fats are pretreated or not pretreated, water-degummed or partially degummed, neutralized or partially neutralized, dehydrated and/or partially dewatered. The mixing step is performed by stirring in a container or on a mixing chamber provided with a mixing device. The steps of adding, mixing and filtrating are carried out at a temperature of 50-90 degrees C. The filtrating step is performed using an inorganic or organic filter with or without precoating.
NOVELTY - Activated sludge treatment process of wastewater, involves adding Streptomyces and Actinomyces to wastewater, and performing wastewater treatment.    USE - The activated sludge treatment process, agent or equipment are useful for treating wastewater (all claimed). The wastewater is water discharged from kitchen, hospital, research laboratory, or sewage.    ADVANTAGE - The process removes offensive odor caused by hydrogen sulfide, mercapten, cadaverine and acetic acid, and pathogens contained in wastewater, solves the problem of sanitation, and enables settleability of sludge during treatment process.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) Agent comprising Streptomyces and Actinomyces; and (2) Equipment has holding portion that contains the above-mentioned agent.
NOVELTY - Constructed wetland treatment system comprises multi-grade stepped artificial wetland, where each stage is filled with aquatic plant filler. The artificial wetland is divided into four groups, each group is divided into stages, and the first stage constructed wetland is directly connected with the other two groups of artificial wetland.    USE - Constructed wetland treatment system used processing mountain city methane discharge sewage.    ADVANTAGE - The system reduces the height of multilevel type artificial wetland, and effectively controls the generation and discharge of methane.
NOVELTY - The device has a dielectric barrier discharge device provided with a cylindrical reaction vessel, an air inlet, an air outlet, an inner electrode and a cylindrical reaction container. A side wall of the cylindrical reaction vessel is fixed with an insulating shell. A dielectric layer is arranged on the insulating shell. An outer electrode and the inner electrode are respectively connected with two poles of a power supply. The cylindrical reaction vessel is provided with a sintered metal fiber beam.    USE - Waste gas treating plasma catalytic device.    ADVANTAGE - The device adopts a sintered metal fiber bundle catalyst in the dielectric barrier discharge device so as to reduce energy consumption and improve volatile organic compound degradation in waste gas.
NOVELTY - Preparing fermentation fertilizer, comprises mixing effective microorganisms (EM) bacteria solution (0.01-1 pts.wt.) with water (100 pts.wt.) and phosphoric acid at a temperature of 28-35 degrees C for 1-5 minutes, maintaining the mixture at a temperature of 7-12 degrees C, mixing 50 pts.wt. of EM bacteria solution with 100 pts.wt. of compost in which phosphoric acid and potassium are mixed, and fermenting the mixture at a temperature of 28-35 degrees C for 1-5 minutes.    USE - The method is useful for preparing fertilizer that is useful for fertilizing crops including Ipomoea batatas , rice plant, potatoes, apple, edible roots, garlic, Sesame and platycodon grandiflorum (all claimed). No biological data given.    ADVANTAGE - The fertilizer enhances quality and the yield of the crops.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fertilizing the fertilizer comprising mixing fructose (0.1-2 pts.wt.) and EM fungus garden bacteria (10-30 pts.wt.) in water 100 (pts.wt.) at a temperature of 28-35 for 1-5 minutes, fermenting the EM bacteria solution in which the phosphoric acid and potassium are mixed, in an anaerobic condition, at a temperature of 23-30 degrees C for 10-30 minutes, mixing bacteria solution (50 pts.wt.) with compost (100 pts.wt.) including phosphoric acid (P) (30-50 wt.%) and potassium (K) (50-70 wt.%), adding water (100 pts.wt.) into the mixture, and keeping the mixture at a temperature of 7-12 degrees C.
NOVELTY - A pyrolysis device comprises pyrolyzing reactor (1), fluidized bed reactor (2), moving bed filter device (3) and heat exchange device (4). Light tar is produced by using solid fuel to generate pyrolysis gas, carrying out gasification of garbage fuel for pyrolysis, producing pyrolyzing tar heavy component in the condensation of solid fuel at 500-900 degrees C and filtering and removing pyrolysis oil product carried in ash to obtain semi-coke product.    USE - Pyrolysis device used for producing light tar.    ADVANTAGE - The device is good for improving light tar yield, heat efficiency and for removing product oil of ash.    DESCRIPTION OF DRAWING(S) - The drawing shows a sketch map of pyrolysis device (Drawing includes non-English text).    Pyrolyzing reactor (1)    Fluidized bed reactor (2)    Moving bed filter device (3)    Heat exchange device (4)    Condensing separating device (5)
NOVELTY - A hydrogen producing apparatus (1) comprises hydrogen producing solution chamber (2) which stores hydrogen producing solution, reaction container (3) for storing reaction promoting solution which produces hydrogen by mixing with hydrogen producing solution, reaction part (4) which mixes hydrogen producing solution and reaction promoting solution, and reaction flow path which has greater than or equal to 2 opening parts in perpendicular up-down direction. Reaction part is immersed in reaction promoting solution.    USE - A hydrogen producing apparatus for fuel cell (claimed).    ADVANTAGE - The hydrogen producing apparatus can produce hydrogen of required amount, without requiring large-scale mechanism. Fuel loss of the fuel cell containing the hydrogen producing apparatus can be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the hydrogen producing apparatus.    Hydrogen producing apparatus (1)    Hydrogen producing solution chamber (2)    Reaction container (3)    Reaction part (4)    Liquid feeding pipe (5)
NOVELTY - The alkaline fuel cell system has a gas-liquid separator (18) which separates liquid and gas in exhausted fuel discharged from anode pole of alkaline fuel cell. A fuel waste gas recovery line returns (19) the gas separated by the gas-liquid separator to a fuel tank (12). A water recovery tank (21) stores the liquid separated by the gas-liquid separator. A control unit (29) controls the temperature of a stack (11) during steady electric power generation to a temperature that is lower than the boiling point of the liquid fuel and higher than the boiling point of the fuel.    USE - Alkaline fuel cell system, e.g., methanol type fuel cell system, for generating liquid fuel.    ADVANTAGE - The alkaline fuel cell system can be driven continuously without the fuel tank overflowing during long term, and without reducing electric power generation efficiency since the control unit controls the temperature of the stack during steady electric power generation to a temperature that is lower than the boiling point of the liquid fuel and higher than the boiling point of the fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the methanol type fuel cell system.    Stack (11)    Fuel tank (12)    Gas-liquid separator (18)    Fuel waste gas recovery line returns (19)    Water recovery tank (21)    Control unit (29)
NOVELTY - The fuel cell power generation system has a grid connection relay (33) which is linked with the system (20), and is released at the time of a system power failure. A storage battery (38) is used as the power supply for the self-supporting generating-mode stop process of the fuel cell. The generating-mode stop process for stopping fuel cell is performed using the electric power electrically stored by the storage battery, when the control unit of the fuel cell receives the stop request of the self-supporting generating mode.    USE - Fuel cell power generation system used for domestic cogeneration system.    ADVANTAGE - The stop process of the generating-mode of the fuel cell can be performed using the electric power electrically stored by the storage battery when the stop request of self-supporting generating mode is received, while the fuel cell is performing the self-supporting generating mode at the time of system power failure. Thus the deterioration of the fuel cell can be avoided. The fuel cell can be restarted using the electric power of storage battery, when the storage battery has sufficient electric power for restarting fuel cell. Thus the fuel cell can be restarted even at the time of system power failure.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the fuel cell power generation system. (Drawing includes non-English language text)    Fuel cell main portion (1)    Power conditioner (3)    System (20)    Grid connection relay (33)    Storage battery (38)
NOVELTY - Additive comprises hydrogen producing bacteria, where the activity of the hydrogen producing bacteria is maintained, and glycolipid which suppresses the activity of hydrogen utilizing bacteria, or glycolipid containing yeast fermentation liquid.    USE - The additive or method is useful for producing hydrogen using microorganism (all claimed), where hydrogen is used as new energy source. The additive is in the form of liquid, water-soluble powder, powder, granule, water-dispersible powder, emulsion, flowable concentrate, or microcapsule.    ADVANTAGE - The method suppresses the proliferation of the hydrogen-utilizing bacteria without performing heat treatment, does not inhibit proliferation of hydrogen producing bacteria without repeating the cycle, replaces raw material in a short time, provides rapid proliferation rate of hydrogen producing bacteria, fastens production of hydrogen before activation of hydrogen-utilizing bacteria, inactivates hydrogen-utilizing bacteria by heating, is cost-effective, and performs hydrogen fermentation which utilizes biomass as raw material.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of producing hydrogen, which involves adding the above-mentioned additive in methane fermentation anaerobic fermenter which is supplied with organic substance, or in microbial fuel cell, maintaining the activity of hydrogen producing bacteria, and suppressing the activity of hydrogen-utilizing bacteria, preferably methanogenic bacteria.
NOVELTY - The method involves contacting the fuel to an oxidation catalyst so as to oxidize the fuel and generate heat. The oxidized fuel is warmed with the heat, while simultaneously warming a reforming catalyst with the heat. The oxidized fuel is reacted with steam using reforming catalyst. The oxidation catalyst and reforming catalyst are supported on a single contiguous substrate made of cordierite, iron chromium aluminum alloy, mullite, alumina and aluminum titanate. The fluid flow throughout volume of substrate and from exterior to interior of substrate is facilitated.    USE - Method for reforming fuel such as petroleum-derived fuel, bio-derived fuel, synthetic fuel and methane (all claimed).    ADVANTAGE - The catalyst function in autothermal and partial oxidation reformer-based processors can be improved. The catalyst life in autothermal and partial oxidation reformer-based processors can be increased vastly. The different catalysts are heated to the optimum operating temperature to concomitantly facilitate chemical conversions. The fluid communication can be established between the temperature zones. The rapid oxidation reactions that produce hotspots on the catalyst surface leading to deactivation can be avoided.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a catalyst system encapsulated by housing.    Housing (11)    Upstream portion (14)    Downstream portion (16)
NOVELTY - A heating furnace (1a-1c) comprises heating unit (4a-4d) which is arranged in a housing (5), injects organic waste inside and heats the container for carbonization processes (2a-2e) which can maintain airtight condition, and the container which carbonizes internal organic waste.    USE - Heating furnace for organic waste carbonization processes.    ADVANTAGE - Carbonized material is recycled as soil improvement material and water-quality-improvement material, and adsorbed without odor and harmful gas leaking outside. Carbonization volume of organic waste is greatly reduced by simple installation, low cost and short time.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial notch side surface schematic view of the heating furnace for organic waste carbonization processes.    Heating furnace (1a-1c)    Container for carbonization processes (2a-2e)    Conveying unit (3)    Heating unit (4a-4d)    Housing (5)
NOVELTY - A catalytic cracking catalyst comprises 2 or more types of metal oxides of groups 2A or 4A, VIII, and 3B.    USE - Catalytic cracking catalyst is used for catalytic cracking of fats and oils during preparation of biodiesel fuel (claimed).    ADVANTAGE - The catalytic cracking catalyst efficiently provides biodiesel fuel having low high-molecular-weight component content and acid value, and high fluidity, and has excellent durability and high productivity, and can be manufactured economically. The cracked oil formed using the catalytic cracking catalyst is rich in light oil fraction, and has excellent quality, and low oxygen-containing compound content. The catalytic cracking catalyst forms high yield of degradation product with reduced residues.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of catalytic cracking catalyst, which involves mixing dolomite, mixture containing hydrotalcite, oxide(s) of magnesium, calcium, iron and zirconium and aluminate of alkali metal, molding obtained mixture to particulate form with particle size of 0.05-10 mm, granular form or pellet form, and baking at 350-800 degrees C; and    (2) biodiesel fuel, which is obtained by contacting catalytic cracking catalyst with fat and oil containing biomass in a reaction container, and heating at 350-475 degrees C. The biodiesel fuel has acid value of less than 0.5 mg potassium hydroxide/g and 20C or more organic compound content of 15 wt.% or less.
NOVELTY - Apparatus (10) comprises a deposition part (11), which deposits an organic raw material. An air supply unit (14) is provided to supply air to the organic raw material, where the air supply unit is provided in the deposition part through an air supplying opening (15) from downward direction. A suction unit has a flush-mounting part (20), where a suction opening is embedded inside of the organic raw material, and air is suck in the organic raw material from the suction opening.    USE - Apparatus for fermenting organic raw material (claimed).    ADVANTAGE - The apparatus ensures fully ventilated fermentation process, particularly aerobic fermentation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for performing organic raw material fermentation process, which involves:    (A) embedding a suction opening with flush-mounting part that suck air to inside of organic raw material deposited on a deposition part; and    (B) performing gas flowing process in the organic raw material from the suction opening in air supply state when air is supplied from downward direction by an air supply unit, which is provided in the deposition part with respect to the organic raw material.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a compost manufacturing apparatus. (Drawing includes non-English language text).    Apparatus (10)    Deposition part (11)    Air supply unit (14)    Air supplying opening (15)    Flush-mounting part (20)
NOVELTY - Producing ethanol and concentrated stillage from a fermented product involves flashing the fermented product in an evaporator to produce an ethanol-laden vapor, water vapor, and stillage, where the evaporator is a thermally accelerating evaporator having an upper distribution section with internal expansion nozzle and a tubenest located beneath the distribution section; feeding the ethanol-laden vapor and water vapor to a distilling assembly; and evaporating water from the stillage using a thermally accelerating evaporator to reduce the water content of the stillage.    USE - For producing ethanol and concentrated stillage from a fermented product (claimed), which is used as a biofuel additive for gasoline and for other purposes.    ADVANTAGE - The process provides significant energy savings over conventional bioethanol production and evaporation system by using the energy (vapor) that drives distillation process; and produces high quality ethanol and concentrated stillage.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) an ethanol production system (S1) comprising pre-flash stage that flashes a fermented liquid to form an ethanol-laden vapor and ethanol-free liquid; distillation stage that distils ethanol from the ethanol-laden vapor; and post-flash stage that removes water from the ethanol-free liquid to provide a concentrated stillage; and    (2) an ethanol production system (S2) comprising: a distillation stage that distills ethanol from a fermented liquid and that discharges stillage; evaporation stage that dewaters stillage from the distillation stage; at least one preheater, associated with the evaporation stage, which provides heated vapor to the evaporation stage and further provides heat to the fermented liquid before the fermented liquid is input to the distillation stage.
NOVELTY - Preparation of an alkyl compound or its mixture involves: preparing a ketene; reacting the ketene in a self-addition reaction to form a diketene; and hydrogenating the diketene in the presence of a metal catalyst to form the alkyl compound or its mixtures.    USE - For preparation of an alkyl compound or its mixture (selected from 4C alcohol such as butanol such as 1-butanol and 2-butanol) which is purified to produce fuel (all claimed); as industrial chemicals from syngas and biomass; as fuels for transportation, industrial chemicals that produce polymers, plastics, pharmaceuticals, paints and other important chemicals.    ADVANTAGE - The method synthesize fuels and chemicals from non-petroleum sources such as biomass, coal and natural gas. The synthetic manufacture of fuels and chemicals e.g. alcohols and alkanes with at least 4C, provides potential for higher energy fuels that are readily compatible with existing automotive and transportation infrastructure.    DETAILED DESCRIPTION - Preparation of an alkyl compound or its mixture involves: preparing a ketene of the formula R1-C(R2)=C=O (I); reacting the ketene (I) in a self-addition reaction to form a diketene of formula (II); and hydrogenating the diketene (II) in the presence of a metal catalyst to form the alkyl compound or its mixtures. An INDEPENDENT CLAIM is included for a fuel composition comprising the alkane compounds prepared by the method.
NOVELTY - The gasification device has a tank case is provided with an air internal combustion chamber and inner cavity heat-resisting layer. The heat insulating layer is provided with a gas storage chamber whose inner ring with several air holes. The air outlet joint is provided with the upper portion of the gas storage chamber and lower portion is provided with a water outlet.    USE - Biomass fuel gasification device.    ADVANTAGE - The reliability of the biomass fuel gasification device can be improved.
NOVELTY - A plant oil degrading bacteria with Pseudomonas species (JNS01 strain) and which is preserved in China Centre for Type Culture Collection, and with preservation number of CCTCC NO: M2012021 is new.    USE - In ternary oil extraction sewage treatment (claimed).    ADVANTAGE - The oil degrading bacteria when used for sewage treatment, provides as high as 1800 mg/L in concentration, pH value of polyacrylamide of 10.5 alkaline solution to develop, can be reduced to 25 mg/L of the crude oil content in the extraction liquid after JNS01 treatment, and the degradation rate can reach 92%.
NOVELTY - Burning method of straw comprises reducing water content of straw below 40% and carrying out combustion in high temperature ceramic grid oxygen-free furnace; starting negative ion generator; igniting in oxygen-free furnace for 0.25-1 hour at above 400 degrees C and recycling furnace dust and carbon oil. Straw is wheat rod, straw rod, maize, potato, oil plants, cotton and/or sugar cane.    USE - Burning straw.    ADVANTAGE - The method reduces pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the combustion device.
NOVELTY - Extracting total coumarin from traditional Chinese medicine common cnidium fruit, involves crushing common cnidium fruit, adding ethanol, extracting, combining the extracts, filtering and concentrating the extracting solution, adding 80% of ethanol solution, collecting liquid, then passing through nanofiltration membrane and concentrating to obtain the concentrated liquid, centrifuging the liquid at high speed, decompressing and concentrating the liquid, and spray-drying to obtain fructus cnidii total coumarin at room temperature.    USE - The method is used for extracting total coumarin from traditional Chinese medicine common cnidium fruit.    ADVANTAGE - The method is simple, environmentally-friendly and cost-effective, produces coumarin with high purity, and prevents formation of solvent residue.    DETAILED DESCRIPTION - Method for extracting total coumarin from traditional Chinese medicine common cnidium fruit, involves obtaining traditional Chinese medicine common cnidium fruit, crushing, sieving through 20-40 meshes sieve to obtain fructus cnidii powder, adding 8-10 times of 80-95% ethanol, dipping and extracting for 2-3 times, combining the extracts, filtering and concentrating the extracting solution, adding 80% of ethanol solution, collecting liquid, then passing through nanofiltration membrane and concentrating to obtain the concentrated liquid, centrifuging the liquid at high speed, decompressing and concentrating the liquid, and spray-drying to obtain fructus cnidii total coumarin at room temperature.
NOVELTY - A culturing and separating device comprises a sludge-water mixed liquid storage tank (1) connected to a water pump and provided with a stirrer (8), a larvae culturing device (3) provided with a heating device and an aeration device, a larvae separator (6), a water discharging valve (4) connected to the larvae separator, an exhaust valve connected to larvae separator, and a stopping screen installed on upper part of the larvae culturing device.    USE - A culturing and separating device for sludge decrement of larvae.    ADVANTAGE - The device has reduces sludge quantity.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a culturing and separating device.    Sludge-water mixed liquid storage tank (1)    Larvae culturing device (3)    Water discharging valve (4)    Larvae separator (6)    Stirrer (8)
NOVELTY - An energy conversion device containing heterojunction semiconductor comprising semiconductors (A,B) joined and two-dimensional hole gas reservoir formed in the joining interface of semiconductor (A). The semiconductor (B) has thickness of 30 nm or less.    USE - Energy conversion device used in oxidation-reduction apparatus used for manufacturing oxidation-reduction component chosen from compound containing carbon such as alcohol, hydrogen and oxygen (all claimed).    ADVANTAGE - The energy conversion device has high efficiency even when a metal pattern is not formed on the semiconductor surface.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of oxidation-reduction component.    DESCRIPTION OF DRAWING(S) - The drawing shows the structure of energy conversion device. (Drawing includes non-English language text)
NOVELTY - The electrolyzer cell (EC) has a hydrogen separation chamber that is deployed with a level sensing device to detect the level of electrolyte such that if a low level of electrolyte is detected, a water pump is activated to inject water into the hydrogen separating chamber at a pre-determined flow rate. An oxygen separation chamber has an oxygen connecting line (CLO) for connection to the bottom of the cell, and a valve to vent accumulated oxygen as a by-product at a preset rate to prevent excessive flow of the electrolyte into the cell via connecting line.    USE - Electrolyzer cell for generating ultra high pressure hydrogen.    ADVANTAGE - Enables provision of an improved electrolyzer apparatus that provides improved control over the cell-pressure balance and separator liquid level in an electrolyzer for producing high pressure hydrogen. Enables provision of a unique configuration that allows effective balancing of the cell-pressure.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a method for controlling cell pressure balance and separator liquid level in an electrolyzer cell; and    (2) a passive circulation process in an electrolyzer cell.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of a system in which electrolyzer cells are connected in parallel to the common separation chambers for oxygen and hydrogen collection.    Anode (A)    Cathode (C)    Oxygen connecting line (CLO)    Electrolyzer cell (EC)    Electrolyte chamber (EL)
NOVELTY - An electrolysis cell has anode chamber and a cathode chamber provided on both sides of solid electrolytic membrane (4) between an anode plate (3) and a cathode plate (2), and porous current collector (5) arranged on the anode chamber and each cathode chamber. The metal coating chosen from coating of electroconductive carbon film, metal carbide film, and metal oxycarbide film on the main surface of porous current collector and/or surface which connects the porous current collector of anode plate and cathode plate is adhered.    USE - Electrolysis cell is used for hydrogen oxygen generator (claimed).    ADVANTAGE - The electrolysis cell is economical, and has excellent corrosion resistance, and low contact resistance, and suppressed electrode surfaces.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of electrolysis cell.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of electrolysis cell.    Cathode plate (2)    Anode plate (3)    Solid electrolytic membrane (4)    Porous current collector (5)
NOVELTY - Removing acidic compounds contained in a gaseous effluent comprises absorption of the acidic compounds by contacting the gaseous effluent with an absorbent solution comprising water and at least one nitrogenous compound (Q) comprising di-(hydroxyalkyl)-monoamine compounds (I) or (II).    USE - The process is useful for removing acidic compounds contained in a gaseous effluent comprising natural gas, synthesis gases, flue gases, refinery gases, acid gases obtained from an amine unit, gases obtained from a unit of reduction in tail of Claus process, biomass fermentation gas, gases of cement factory, or smoke of incinerator, and for selective removal of hydrogen sulfide compared to carbon dioxide from a gaseous effluent comprising hydrogen sulfide and carbon dioxide (all claimed).    ADVANTAGE - The process selectively eliminates the acidic compounds contained in a gaseous effluent with low energy consumption and low operating costs.    DETAILED DESCRIPTION - Removing acidic compounds contained in a gaseous effluent comprises absorption of the acidic compounds by contacting the gaseous effluent with an absorbent solution comprising water and at least one nitrogenous compound (Q) comprising di-(hydroxyalkyl)-monoamine compounds of formula (R1-CH(OH)-C(R2)(R3)-NH-C(R4)(R5)-CH(OH)-R6) (I) or (R8-CH(OH)-CH(R10)-N(R7)-CH(R11)-CH(OH)-R9) (II).    R1-R6, R8-R11 = H or 1-4C-alkyl, where at least two of R2-R5 are 1-4C-alkyl, at least one of R8 and R9 is 1-4C-alkyl, and at least one of R10 and R11 is 1-4C-alkyl; and    R7 = 1-4C-alkyl.
NOVELTY - A rural straw marsh gas pool comprises a fermenting tank having a feeding pool, a water pressure discharging tank, an air outlet, and a discharge hole connected with an artificial strong reflux liquid.    USE - A rural straw marsh gas pool.    ADVANTAGE - The rural straw marsh gas pool is environment-friendly.
NOVELTY - The furnace has a furnace inner container (6) fixed with a furnace head (5). An outer side of the furnace inner container is covered with a furnace outer container (4). A fuel chamber (12) is arranged in the furnace inner container. A circulation chamber (13) is arranged between the furnace outer container and the furnace inner container. The furnace outer container is provided with an output pipe (14) and an exhaust pipe (17). A purifying device is arranged between the furnace inner and outer containers. The purifying device is filled with wooden meal, straw powder or straw.    USE - Straw gasification furnace.    ADVANTAGE - The furnace adopts dual-filtering design to achieve heat insulation effect during combustion process such that combustion gas attains high-temperature phase and strengthening phase in a dual-circulation mode, so that high-temperature crack biomass gas tar is dissolved and returned to a bottom part of the furnace and formed into furnace ash after performing burning and diluting process to obtain ash without dust pollution. The furnace utilizes a dust returning path for tar filter effect and achieves tar recovery so as to realize environment-friendly effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a straw gasification furnace.    Furnace outer container (4)    Furnace head (5)    Furnace inner container (6)    Fuel chamber (12)    Circulation chamber (13)    Output pipe (14)    Exhaust pipe (17)
NOVELTY - Aqueous manure composition comprises 80-92 wt.% decomposed 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 ions, 0.04-0.70 wt.% manganese ions, 0.1-0.6 wt.% copper ions, 0.1-0.7 wt.% divalent iron ions, 0.02-0.2 wt.% molybdenum ions, 0.02-0.35 wt.% boron ions and 0.5-1 wt.% nitzschia.    USE - The aqueous manure composition is useful for breeding phytoplankton, zooplankton and pearl mussel.    ADVANTAGE - The composition is rich in organic nutrients, nitrogen, phosphorus, potassium and trace elements, has high compatibility, and can rapidly supplement small molecular organic molecules required by phytoplankton, zooplankton and pearl mussel.
NOVELTY - Domestic waste and sewage treatment system, in which the domestic sewage waste and excrement are filled into a sedimentation processing device, comprises a two-stage sedimentation processing device, in which the primary sedimentation processing device is a closed primary sedimentation tank provided with a sealing cover and an exhaust pipe. The exhaust pipe is set with a filter. The urinal and water tank is connected with the primary sedimentation tank inlet via water pipe. A waste crushing machine is connected with the water pipe.    USE - Used as a domestic waste and sewage treatment system.    ADVANTAGE - The system utilizes waste crushing machine to crush household waste together with the waste water, and conveys into sedimentation tank after aerobic treatment, which is then fermented into fertilizer, and finally discharging the waste water after precipitation filtration.
NOVELTY - The tank has gas storage fermentation chamber and a water pressure chamber that are vertically provided with a discharging pipe. The water pressure chamber is connected with a biogas storage chamber. A biogas slurry conveyer pipe is connected with water pressure chamber and air storage fermentation chamber arranged below the vertical discharge pipe. The water pressure chamber is connected with U-shaped connecting pipe that is connected with the water pressure chamber. The connecting pipe is connected with the upper portion of the gas storage fermentation chamber.    USE - Return-flow type marsh gas tank.    ADVANTAGE - The return-flow type marsh gas tank can efficiently remove the floating residue incrustation, such that use and management can be convenient ensured.
NOVELTY - A garbage processing system comprises garbage collecting system and conversion system. The garbage collecting system comprises a garbage can and garbage transportation vehicle. The garbage can comprises a solid garbage and liquid garbage barrel. The solid fertilizer processing system comprises a solid fertilizer multi-level packing auger, multi-stage crushing and fermenting device and cross layout, and packaging device. The liquid fertilizer processing system comprises liquid garbage barrel, heating fermentation device and liquid fertilizer packaging device.    USE - A system for processing garbage fertilizer.    ADVANTAGE - The system minimizes waste pollution, avoids the decomposition of harmful odor, and promotes healthy development of the environment.
NOVELTY - Invention relates to biotechnology and agriculture. The composition for producing vermicompost consists of wood processing wastes and chicken manure. The wood processing wastes used are pine bark ground to particle size of 1-2 mm, with the following ratio of components, wt %: pine bark - 25, chicken manure -75.    USE - Chemistry.    ADVANTAGE - Adding pine bark to the chicken manure enables decontamination of the substrate for subsequent vermicomposting, optimises pH of the mixture to a neutral medium and enables faster processing of the substrate by worms.2 tbl
NOVELTY - A Serratia marcescens subspecies marcescens FXWNJ2D strain deposited as CCTCC M2012261, is new.    USE - The S.marcescens is useful as biofertilizer for promoting growth of Chinese sweetgum.
NOVELTY - Producing a solidification auxiliary fuel comprises selecting food waste in a selector, crushing the selected food waste through a crusher to 10-20 mm, injecting the crushed food waste into centrifugal type dehydrator having a moisture content of 40% to dehydrate the food waste, pulverizing the dehydrated food waste to 3-5 mm, pulverizing red clay to 100 meshes, pulverizing peat to 100 meshes, mixing corn chip and sawdust to form first a mixture, adding activated chemicals to the first mixture to form a second compound, and injecting the second compound into a pellet extruder to extrude.    USE - The method is useful for producing a solidification auxiliary fuel (claimed).    ADVANTAGE - The method allows efficient and economical production of the solidification auxiliary fuel with high safety.    DETAILED DESCRIPTION - Producing a solidification auxiliary fuel comprises selecting food waste in a selector, crushing the selected food waste through a crusher to 10-20 mm, injecting the crushed food waste into centrifugal type dehydrator having a moisture content of 40% to dehydrate the food waste, pulverizing the dehydrated food waste to 3-5 mm, pulverizing red clay to 100 meshes, pulverizing peat to 100 meshes, mixing corn chip and sawdust to form a first mixture, adding activated chemicals to the first mixture to form a second compound (70-90 wt.%), injecting the second compound into a pellet extruder to extrude, transferring the second compound to a transfer conveyor to solidifies the extruded compound, then cutting, and drying the compound using hot air at a temperature of 80-100 degrees C in a hot-air blower.    DESCRIPTION OF DRAWING(S) - The figure shows a flow chart of a method for producing fuel (Drawing includes non-English language text).
NOVELTY - Producing a solidification auxiliary fuel comprises selecting food waste in a selector, crushing the selected food waste through a crusher to 10-20 mm, injecting the crushed food waste into centrifugal type dehydrator having a moisture content of 40% to dehydrate the food waste, pulverizing the dehydrated food waste to 3-5 mm, pulverizing waste lime to 100 meshes, pulverizing waste coal to 100 meshes, mixing corn chip and sawdust to form a first mixture, adding activated chemicals to the first mixture to form a second compound, and injecting the second compound into a pellet extruder.    USE - The method is useful for producing a solidification auxiliary fuel (claimed).    ADVANTAGE - The method allows efficient and economical production of the solidification auxiliary fuel in an environmental friendly manner with high safety.    DETAILED DESCRIPTION - Producing a solidification auxiliary fuel comprises selecting food waste in a selector, crushing the selected food waste through a crusher to 10-20 mm, injecting the crushed food waste into centrifugal type dehydrator having a moisture content of 40% to dehydrate the food waste, pulverizing the dehydrated food waste to 3-5 mm, pulverizing waste lime to 100 meshes, pulverizing waste coal to 100 meshes, mixing corn chip and sawdust to form a first mixture, adding activated chemicals to the first mixture to form a second compound (70-90 wt.%), injecting the second compound into a pellet extruder to extrude, transferring the second compound to a transfer conveyor to solidifies the extruded compound, then cutting, and drying the compound using a fan at a room temperature.    DESCRIPTION OF DRAWING(S) - The figure shows a flow chart of a method for producing fuel (Drawing includes non-English language text).
NOVELTY - Producing a solidification auxiliary fuel comprises selecting food waste in a selector, crushing the selected food waste through a crusher to 10-20 mm, injecting the crushed food waste into centrifugal type dehydrator having a moisture content of 40% to dehydrate the food waste, pulverizing the dehydrated food waste to 3-5 mm, pulverizing red clay to 100 meshes, pulverizing peat to 100 meshes, mixing corn chip and sawdust to form first a mixture, adding activated chemicals to the first mixture to form a second compound, and injecting the second compound into a pellet extruder to extrude.    USE - The method is useful for producing a solidification auxiliary fuel (claimed).    ADVANTAGE - The method is capable of efficiently and economically producing the solidification auxiliary fuel with high safety and quality.    DETAILED DESCRIPTION - Producing a solidification auxiliary fuel comprises selecting food waste in a selector, crushing the selected food waste through a crusher to 10-20 mm, injecting the crushed food waste into centrifugal type dehydrator having a moisture content of 40% to dehydrate the food waste, pulverizing the dehydrated food waste to 3-5 mm, pulverizing red clay to 100 meshes, pulverizing peat to 100 meshes, mixing corn chip and sawdust to form a first mixture, adding activated chemicals to the first mixture to form a second compound (70-90 wt.%), injecting the second compound into a pellet extruder to extrude, transferring the second compound to a transfer conveyor to solidifies the extruded compound, then cutting, and drying the compound using hot air at a temperature of 80-100 degrees C in a hot-air blower.    DESCRIPTION OF DRAWING(S) - The figure shows a flow chart of a method for producing fuel (Drawing includes non-English language text).
NOVELTY - Method for fermenting methane, involves inoculating methane inoculum in primary and secondary fermentation device, adding 10-40 wt.% raw material to primary fermentation device, subjecting the raw material to fractional heating at 25-35 degrees C, performing anaerobic fermentation to the mixture for 2-8 days, adding the remaining raw materials to the second fermentation device, mixing the fermented material obtained from primary fermentation device with secondary fermentation device, and continuously performing anaerobic fermentation for 4-15 days.    USE - The method is useful for fermenting methane (claimed).    ADVANTAGE - The method has improved heat efficiency and improves fermentation efficiency of the methane.
NOVELTY - The apparatus has a sorting equipment (10) connected with a container (30) through a stack part (20). Natural substances are provided with cellulose, textiles and plastics. A homogenization dispensing device (40) is equipped with an addition device (41), a grinder (50) and a press unit (60).    USE - Apparatus for producing fuels from natural substances.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of an apparatus for producing fuels from natural substances.    Sorting equipment (10)    Stack part (20)    Container (30)    Homogenization dispensing device (40)    Addition device (41)    Grinder (50)    Press unit (60)
NOVELTY - Producing hydrogen and methane involves performing hydrolysis of biological waste material in a reactor under mesophilic conditions in presence of organic acid at pH4-5 for three days at 30-40 degrees C. Methanogenesis is performed in another reactor. The gaseous effluent is separated and supernatant is obtained from the reactor.    USE - Method for producing hydrogen and methane.    ADVANTAGE - The method enables to produce hydrogen and methane in a stable manner.
NOVELTY - Preparing 16 alpha -hydroxy prednisolone, comprises carrying out dehydration reaction of prednisolone in the presence of 5,5'-methylenebis(2-dodecylbenzenesulfonic acid) gemini surfactant to generate double-bond containing compound, adding aqueous hydrogen peroxide solution, reacting, adding water and carrying out hydrolysis reaction.    USE - The method is useful for preparing 16 alpha -hydroxy prednisolone.    ADVANTAGE - The method utilizes gemini surfactant and catalyst, which can be recycled and repeatedly used; is simple, economical, practical and environmentally friendly; and has convenient post-treatment, and high yield (more than 85%) and efficiency.
NOVELTY - Denitration adsorbent comprises humate as a carrier and nano titanium dioxide as a catalyst in a mass ratio of (1:0.1)-(1-0.5).    USE - Used as a denitration adsorbent.    ADVANTAGE - The denitration method produces nitrogen-rich humic acid, which can be used as fertilizer to achieve environmental protection and resource utilization.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) preparing the denitration adsorbent, comprising (a) selecting humate as carrier and anatase type nano titanium dioxide as catalyst, mixing, adding water, and thoroughly stirring, (b) granulating the mixture of humate and nano titanium dioxide in a granulator to prepare into particle, and (c) drying the prepared particle using a drying device to obtain the adsorbent; and    (2) a denitration method of the adsorbent, comprising adding the adsorbent into a photocatalytic reaction device, inletting nitrogen oxide-containing exhaust gas, and removing out the adsorbent after complete reaction.
NOVELTY - The device has liquid-phase mixed refrigerant inlet which is connected with liquid cooling box. A throttle valve is connected with a refrigerant return passage cooling tank. A gas-phase refrigerant inlet is connected with gas channel cooling box. A mixed gas inlet is connected with the cooling box. A flash tank is provided with a methane-rich stream mixing inlet, a gas phase outlet and bottom liquid phase outlet. The liquid phase outlet of cold flash tank is connected with the other throttle valve that is connected to one end of resistor.    USE - Device for producing throttle flash dehydrogenation gas, nitrogen, carbon monoxide and liquefied natural gas.    ADVANTAGE - The simple process can be achieved, and the operation stability can be attained. The cost of the device can be reduced, and the consumption of energy can be reduced.
NOVELTY - A low-carbon methanol gasoline compound additive comprises 1-5 pts.wt. latent solvent, 2-3 pts.wt. heat-value improving agent, 0.5-2 corrosion inhibitor and 0.5-1 pts.wt. antioxidant.    USE - Low-carbon methanol gasoline compound additive.    ADVANTAGE - The low-carbon methanol gasoline compound additive has excellent performance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of low-carbon methanol gasoline compound additive, which involves adding auxiliary solvent and heat value improving agent in a sealed container, stirring at 20-50 degrees C for 5 minutes, and then adding corrosion inhibitor, stirring for 5 minutes, adding antioxidant, and stirring for 3 minutes.
NOVELTY - An anhydrous methanol and grease are added to the floatation groove of flotation machine, and machine is started. Alkaline catalyst is added into high speed, and machine air inlet valve is started. The amount of air inlet is adjusted, and reacted to air inlet valve and stirrer. The lower glycerol is discharged from discharging port, and upper layer is stirred and washed at the bottom of the floatation groove. Water is added, and lower water is discharged from discharging port, to obtain biological diesel oil.    USE - Production of biological diesel oil.    ADVANTAGE - The biological diesel oil is efficiently produced, by simple method.    DETAILED DESCRIPTION - An anhydrous methanol and grease are added in the molar ratio of 20:1-100:1, added to the floatation groove of flotation machine, and machine is started. An alkaline catalyst is added into the high speed in the flotation groove to stir for 10 minutes, and machine air inlet valve is started. The amount of air inlet is adjusted to 0.1-0.4 m3/hour, reacted at 30-60 degrees C for 5-30 hours to air inlet valve and a stirrer, and standard for 5-20 hours. The lower glycerol is discharged from the discharging port, rough biological diesel oil of IV is added in water, and upper layer is continuously stirred and washed at the bottom of the floatation groove. Water is added, then standard for 5-10 hours, and lower water is discharged from discharging port, to obtain biological diesel oil. The upper layer is biodiesel product.
NOVELTY - A bupropion hydrochloride is prepared by using m-benzoyl chloride as initial raw material, and reacting with 2-methyl malonic acid diester in non-proton solvent in alkaline environment to obtain chlorine-containing intermediate; hydrolyzing and removing carboxyl from the intermediate under acidic condition to obtain propan-1-one; brominating the propan-1-one to prepare alpha -bromo-m-benzene acetone; reacting alpha -bromo-m-benzene acetone with tert-butylamine under the function of proton capturing agent to prepare bupropion; and reacting bupropion with hydrochloric acid.    USE - Method for preparation of bupropion hydrochloride (claimed).    ADVANTAGE - The method is simple and easy, has less side reaction, improves reaction yield, and reduces production cost simultaneously with reducing pollution to the environment.    DETAILED DESCRIPTION - Preparation of bupropion hydrochloride comprises using m-benzoyl chloride as initial raw material, and reacting with 2-methyl malonic acid diester in non-proton solvent in an alkaline environment to obtain chlorine-containing intermediate of formula (V); hydrolyzing and removing carboxyl from the intermediate (V) under acidic condition to obtain propan-1-one; brominating the propan-1-one to prepare alpha -bromo-m-benzene acetone; reacting the alpha -bromo-m-benzene acetone with tert-butylamine under the function of proton capturing agent to prepare bupropion; and reacting bupropion with hydrochloric acid to obtain bupropion hydrochloride.    R1=Me or Et.    An INDEPENDENT CLAIM is included for use of compound (V) in the preparation of bupropion hydrochloride.
NOVELTY - The method involves providing an organic nature waste in a wet sludge, where organic nature waste is combined with chopped polyolefins and subjected to a live steam heat treatment process. Obtained mixture is enriched by adding a calcium aluminum silicate and aluminum. Coal sludge of relatively biomass is formed from straw or sawdust.    USE - Method for preparing biofuel from sewage.
NOVELTY - Preparation of 3,6-dichlorosalicylic acid involves drying and roasting 2,5-dichlorophenol and inorganic alkali, mixing, transferring the resultant mixture to a reactor, decompressing, dehydrating, introducing carbon dioxide gas into a reactor, performing carboxylation reaction, obtaining reaction mixture, adding water to dissolved the obtained reaction mixture, adding acid, filtering, washing by water, and drying.    USE - Preparation of 3,6-dichlorosalicylic acid (claimed).    ADVANTAGE - The method economically provides 3,6-dichlorosalicylic acid having high yield and quality, by a simple process with reduced usage amount of solvent and catalyst.
NOVELTY - Preparation of isooctyl salicylate involves adding salicylic acid and isooctanol in mass ratio of 1:2-5 into a reactor, adding 1.5-5.5 %mass acid catalyst, stirring, heating at 150-200 degrees C, refluxing, reacting for 10 hour, cooling the resultant reaction mixture at room temperature, filtering the catalyst from the resultant mixture, washing using hot water and saturated sodium carbonate, drying under anhydrous magnesium sulfate, filtering, decompressing, distilling, and recycling the residual solvent.    USE - Preparation of isooctyl salicylate (claimed).    ADVANTAGE - The method economically provides isooctyl salicylate having high purity. The isooctyl salicylate is environmentally-friendly.
NOVELTY - A biofuel comprises: a diesel fuel; a plant oil or its derivative; an alcohol viscosity reducer; and a surfactant not greater than 1 vol.%/vol.%, where the biofuel exists as a clear, stable microemulsion at -10 degrees C to 70 degrees C and has a kinematic viscosity of less than 6 cSt at 37.8 degrees C.    USE - As biofuel (claimed).    ADVANTAGE - The biofuel exists as a clear, stable microemulsion at -10 degrees C to 70 degrees C. The use of mixture of alcohols contributes characteristics of viscosity reduction and energy content, to the fuel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for making the biofuel, involving mixing the diesel fuel, the plant oil, the alcohol viscosity reducer, and the surfactant in an amount such that the surfactant constitutes less than 1 vol.%/vol.% of the biofuel, where the biofuel exists as a clear, stable microemulsion at -10 degrees C to 70 degrees C.
NOVELTY - Converting a cellulosic material, comprises: a liquefaction step to produce a final liquefied product, where the liquefaction step comprises contacting a cellulosic material with a liquid solvent at greater than or equal to 200 degrees C, or contacting a cellulosic material with a liquid solvent at greater than or equal to 100 degrees C in the presence of a catalyst; and a catalytic cracking step to produce at least one cracked product, where the catalytic cracking step comprises contacting at least part of the final liquefied product with a fluidized catalytic cracking catalyst at greater than or equal to 400 degrees C.    USE - The method is useful for converting a cellulosic material for producing product fraction and hydrotreated product fraction that are useful in a biofuel components for producing biofuel (all claimed), where the biofuel is used in a transportation vehicle.    ADVANTAGE - The method: minimizes coking; is less critical; utilizes the liquefaction step that liquefies not only the cellulose but also the lignin and hemicellulose; has improved operability; and is economic.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a biofuel component (b1) comprising at least one product fraction or any product derived from the product fraction;    (2) a biofuel component (b2) comprising at least one hydrotreated product fraction or any product derived from the hydrotreated product fraction; and    (3) producing a biofuel, comprising blending the biofuel component (b1) or (b2) with at least one other component to produce a biofuel.
NOVELTY - Co-culture composition comprises: a first population of mutant lignocellulolytic cells, where the mutant cells comprise a mutation in one or more beta -glucosidase genes; and a second population of fermentative microorganisms.    USE - The composition is useful for producing a commodity chemical from lignocellulosic biomass, where the commodity chemical is a biofuel consisting of an alcohol, ethanol, propanol, isopropanol, acetone, butanol, isobutanol, 2-methyl-1-butanol, 3-methyl-1-butanol, phenylethanol, a fatty alcohol, isopentenol, an aldehyde, acetylaldehyde, propionaldehyde, butryaldehyde, isobutyraldehyde, 2-methyl-1-butanal, 3-methyl-1-butanal, phenylacetaldehyde, a fatty aldehyde, a hydrocarbon, an alkane, an alkene, an isoprenoids, a fatty acid, a wax ester, an ethyl ester and/or hydrogen.    ADVANTAGE - The composition is capable of degrading cellulose efficiently while producing biofuels at high yields.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing a commodity chemical from lignocellulosic biomass, comprising: (a) providing a fermentation broth that comprises the co-culture composition; (b) contacting lignocellulosic biomass with the fermentation broth; and (c) incubating the fermentation broth and lignocellulosic biomass under conditions sufficient for the co-culture composition to produce a commodity chemical from the lignocellulosic biomass.
NOVELTY - A method, comprises: contacting an oil producing cell with an herbicide in an effective amount to promote secretion of oil by the cell and collecting the oil from the oil producing cell.    USE - The methods are useful for preparing a biofuel; for collecting oil from an oil producing cell; and for reducing toxin secretion in an algae (all claimed).    ADVANTAGE - The methods effectively enhance secretion of oils from oil producing cells.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a syngas comprising a gaseous mixture of hydrogen and carbon monoxide produced from an oil producing cell contacted with a sulfonylurea;    (2) a biodiesel comprising a liquid diesel fuel produced from an oil producing cell contacted with a sulfonylurea;    (3) an oil comprising a mixture of at least 90% hydrocarbon and lipids of intermediate polarity where the oil mixture is substantially free or beta -carotene and chlorophyll;    (4) a method comprising contacting an oil producing cell with an herbicide in an effective amount to promote secretion from the cells of recoverable oil in excess of 1 mg/l accumulated; and    (5) a method for reducing toxin secretion in an algae, comprising contacting an algae with a fatty acid metabolism inhibitor in an effective amount to reduce toxin production.
NOVELTY - Method for producing succinic acid, involves (a) converting an organic raw material into succinic acid in an aqueous medium in the presence of a microorganism or its processed product, and (b) collecting the succinic acid. The step (a) involves (i) adjusting the concentration of a succinic acid alkali metal salt in the aqueous medium to 80 mM or more, and (ii) adding ammonia and/or an ammonium salt to the aqueous medium.    USE - The method is useful for producing succinic acid for preparing polymer (all claimed) including polyester and polyamide. The succinic acid is used as synthetic raw material of foodstuff, pharmaceutical and other chemical products, and in food additive and cosmetics.    ADVANTAGE - The method yields high concentration of succinic acid, improves succinic acid productivity, overcomes the problem of depletion of fossil fuel resources, is cost-effective and environmentally-friendly, recovers succinic acid with high purity from the medium by existing method, and consumes less time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing succinic acid containing polymer, which involves producing succinic acid by the above-mentioned method, and polymerizing the obtained succinic acid.
NOVELTY - Device (1) for extracting energy from biomass, comprises a pyrolysis device (3) for obtaining a process gas from the biomass, a cogeneration plant (11) for the extraction of heat energy and/or electrical energy from at least one portion of the process gas, a separation device (9) for depositing methane from the process gas, and a device for supplying remaining residual gas after the separation of methane from the process gas to a cogeneration plant for extraction of energy.    USE - The device is useful for extracting energy from biomass.    ADVANTAGE - The device ensures improved utilization of biomass, the filters are temperature stable and are easily cleanable, and allows low-air or air-free transport of the biomass.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for extracting energy from biomass, comprising (i) obtaining process gas from biomass by the pyrolysis- or gasification device, (ii) obtaining heat and electric energy from at least one portion of the process gas by the cogeneration plant, (iii) separating methane from the process gas by a separation device, and (iv) supplying residual gas to the cogeneration plant for the extraction of energy after the deposition of methane from the process gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of a device.    Device (1)    Pyrolysis device (3)    Reactor (4)    Separation device (9)    Cogeneration plant (11)
NOVELTY - Separation process (11) of biomass which is to be subsequently fed to a biogas plant (20) for generating biogas, comprises providing biomass to be processed and adding at least one activator to the biomass, which leads to biochemical treatment of the biomass, where an acetic acid forming-activator is added as at least one activator.    USE - The method is useful for generating biogas from the prepared biomass in a biogas plant. The living acetic acid bacteria and living yeast are useful for processing biomass which is to be supplied to the biogas plant for the generation of biogas (all claimed).    ADVANTAGE - The method allows complete degradation of biomass for generating biogas and extracts a high proportion of methane from the processed biomass.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) use of the method for generating biogas from the processed biomass in a biogas plant; and    (2) an agent for processing biomass, comprising at least two components, of which a first component includes living acetic acid bacteria, and the second component is acetic acid, sugar, alcohol or water.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the process flow of the biomass separation process.    Separation process (11)    Biogas plant (20)    First container space (22)    Second container space (24)    Third container space (26)
NOVELTY - The device has a submersible agitator (1) immersed and operated in the interior of a container. Pivoting levers (4, 8) are associated with hinge elements (6b, 6c) for height adjustment of the agitating device. A bearing bracket is arranged in the interior of the container for receiving the pivoting lever, and a supply line is arranged in a container wall (3) in a gas-and liquid-tight manner, where the supply line is provided in a protective tube that is connected with the pivoting levers by a holder.    USE - Mixing device for mixing and fermenting a renewable raw material e.g. corn, grass and liquid manure, in a container in a biogas plant.    ADVANTAGE - The mixing device can be made available with low investment cost. The device allows free-hanging and fluttering, and reduces a distance from a pivot point to reduce emergent forces and moments. The device allows time-or event-driven automation of a mixing process with preselectable positions both in height and in angle coaxial with an axis of the agitator, and prevents formation of dead zones reliably in the container while permitting cost-effective production.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic side sectional view of a mixing device.    Submersible agitator (1)    Gas hood (2)    Container wall (3)    Pivoting levers (4, 8)    Hinge elements (6b, 6c)
NOVELTY - An apparatus has high-pressure boiler in which electrolysis of electrochemical water is performed at pressure above atmospheric pressure.    USE - Apparatus is used for producing hydrogen and oxygen.    ADVANTAGE - The production of hydrogen and oxygen is efficiently using the apparatus.
NOVELTY - The fuel cell system has a current sensor (34) which detects the electric current generated in fuel cell stack (40). The pressure sensors (31-33) are arranged on the piping for supplying the fuel gas containing hydrogen to the fuel cell stack. A control unit (70) is configured to detect the detection error of the pressure sensors based on the output difference of the pressure sensor before and after the predetermined time and based on the electric current generated in the fuel cell stack.    USE - Fuel cell system.    ADVANTAGE - The fuel cell system can detect the error of the pressure sensor appropriately. The cost of the fuel cell system can be reduced.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) an error detection method of pressure sensor; and    (2) a correction method of pressure sensor.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the fuel cell system. (Drawing includes non-English language text)    High pressure sensor (31)    Medium pressure sensor (32)    Low pressure sensor (33)    Current sensor (34)    Fuel cell stack (40)    Control part (70)
NOVELTY - Vegetable bio-pellet is obtained by mixing pressed extracts of Vernicia cordata during wood pellet preparation.    USE - As vegetable bio-pellet.    ADVANTAGE - The vegetable bio-pellet has stable feed rate and improved quality than existing wood pellet, provides higher calorific value and energy, is prepared cost-effectively, and does not require cutting trees of V.cordata.
NOVELTY - A pure culture of mutant strain of C. acetobutylicum, MTCC 5587 which has increased tolerance to butanol as compared to wild strain.    USE - For producing butanol (claimed).    ADVANTAGE - The mutant strain has butanol tolerance of 1.5-3.5, preferably 3.5)% as compared to wild strain, has butanol tolerance that was associated with increased membrane saturated fatty acid content of 4-5% as compared to wild type, has butanol tolerance that was associated with increased tolerance to toxic compounds such as Rhodamine 6G as compared to the wild type; provides yield of butanol is upto 19 g/L at 15 L scale with jatropha seed cake hydrolysate; provides yield of butanol is up to 18 g/L with banana stem hydrolysate at 50 ml scale; and provides yield of butanol is up to 14.3 g/L with jatropha seed cake hydrolysate at 50 ml scale.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparation of mutant strain of C. acetobutylicum, MTCC 5587 involves performing chemical mutagenesis of C. acetobutylicum ATCC 4259;    (2) a continuous and efficient process (M1) of production of high yield of butanol from pretreated biomass using mutant strain of C. acetobutylicum, MTCC 5587 with enhanced butanol tolerance.
NOVELTY - 13-nitro-2,3,5,6,8,9-hexahydro-1,4,7,10-benzotetraoxacyclododecine-12-carbonitrile (A), 13-amino-2,3,5,6,8,9-hexahydro-1,4,7,10-benzotetraoxacyclododecine-12-carbonitrile (B) or benzotetraoxacyclododecine compound (I), is new.    USE - Benzotetraoxacyclododecine compound is useful for manufacturing icotinib and its hydrochloride (all claimed) useful as medicine.    ADVANTAGE - The icotinib is economically manufactured without affecting environment by without using phosphoryl chloride.    DETAILED DESCRIPTION - 13-nitro-2,3,5,6,8,9-hexahydro-1,4,7,10-benzotetraoxacyclododecine-12-carbonitrile (A), 13-amino-2,3,5,6,8,9-hexahydro-1,4,7,10-benzotetraoxacyclododecine-12-carbonitrile (B) or benzotetraoxacyclododecine compound of formula (I), is new.    R1,R2=methyl, ethyl, propyl or isopropyl;and    or R1+R2+N=3-7 membered ring.    INDEPENDENT CLAIMS are included for the following:    (1) manufacture of benzotetraoxacyclododecine compound (I);    (2) manufacture of icotinib, which involves reacting compound (I) and 3-aminophenylacetylene in organic acid; and    (3) manufacture of icotinib hydrochloride, which involves dissolving icotinib in lower alcohol, feeding into hydrogen chloride gas or hydrogen chloride solution under stirring, after terminate reaction, and filtering.
NOVELTY - The apparatus (100) has modifier (1) which generates hydrogen-containing-gas by reforming reaction using raw material. Distributor (3) is set to supply fuel to combustion chamber. Burner-port case (5) is provided, so that distributor's outer periphery is covered. Inside of distributor is penetrated and electrode (6) is set for performing flame detection and ignition. One portion of electrode is arranged in downstream rather than the air ejection port located in most downstream hole in extending direction of the electrode with respect to combustion chamber.    USE - Hydrogen generating apparatus used for fuel cell system (claimed).    ADVANTAGE - The electrode for flame detectability can be improved effectively. The carbon monoxide in the hydrogen-containing-gas generated with the modifier can be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen generating apparatus. (Drawing includes non-English language text)    Modifier (1)    Distributor (3)    Burner-port case (5)    Electrode (6)    Hydrogen generating apparatus (100)
NOVELTY - A solid oxide fuel cell consists of solid electrolyte layer (11) having oxygen ion conductivity, fuel electrode (12) containing oxide ceramic particles (121) formed by dispersion support of metal particles (122) formed in the main surface of solid electrolyte layer, and air electrode (13) formed in the other side of the electrolyte layer. A modified layer (17) containing oxide ceramic particles (131) formed by dispersion support of metal particles (132) is provided through collector (15).    USE - Solid oxide fuel cell used as electric power generation system.    ADVANTAGE - The solid oxide fuel cell has excellent modification efficiency of hydrocarbon type gas to hydrogen gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of the solid oxide fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic block diagram of the solid oxide fuel cell.    Solid electrolyte layer (11)    Fuel electrode (12)    Air electrode (13)    Collector (15)    Modified layer (17)    Oxide ceramic particles (121,131)    Metal particles (122,132)
NOVELTY - Analyzing fuel for biodiesel content, comprises converting at least a portion of any methyl esters present in a fuel sample to the corresponding free acid, reacting the free acid with a strong acid to protonate the free acid, solubilizing the protonated free acid in a non-polar fluid and measuring the protonated free acid in tire non-polar fluid to determine the concentration of methyl esters in tire fuel.    USE - The method is useful for analyzing fuel for biodiesel content (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a test kit for analyzing fuel for biodiesel content, comprising a sampling device for taking an accurately sized fuel sample, a heating device for converting at least a portion of any methyl esters present in a fuel sample to the corresponding free acid, at least one ampule containing a strong base and/or an alcoholic solvent to help improve the rate of the conversion, a strong acid to help protonate the free acid, and a non-polar fluid to help solubilize the protonated free acid.
NOVELTY - Supercritical extraction of magnolol comprises ultra-micro crushing Magnolia officinalis leaf into powder with 40 meshes, drying the powder for 2-4 hours, introducing carbon dioxide liquid in an extraction kettle and then adding the powder, where the flow rate of the carbon dioxide liquid is 25-35 kg/ hour, controlling a pressure in the extraction kettle to 23-28 MPa, separating the product using a separating kettle at a pressure of 5-8 MPa and then heating at 35-42 degrees C for 4-6 hours and then drying.    USE - The method is useful for supercritical extraction of magnolol (claimed).    ADVANTAGE - The method enables simple and economical extraction of the magnolol with high extraction rate (greater than 90%), good quality and less energy consumption and without solvent residue in an eco-friendly manner.
NOVELTY - Matrix is prepared using 30-50 pts. wt. farmyard manure, 20-35 pts. wt. sawdust, 15-28 pts. wt. cake fertilizer, 15-25 pts. wt. humic acid, and 0.13-0.22 pts. wt. Bacillus subtilis.    USE - The matrix is useful for planting strawberry (claimed).    ADVANTAGE - The matrix contains large amount of organic substances and beneficial flora, which effectively control the soil acidity and alkalinity, enables to cultivate strawberry safely for long period of time, and improve quality and yield of strawberry.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the matrix, which involves uniformly mixing farmyard manure, sawdust, cake fertilizer and humic acid, inoculating B.subtilis to the obtained mixture, fermenting the obtained mixture at 15-25 degrees C for 7-9 days, sealing the obtained mixture, sterilizing the obtained product at 45-60 degrees C, and drying and packaging the obtained product.
NOVELTY - An alcohol-ether gasoline comprises 20-40 wt.%, preferably 30 wt.% gasoline, 40-60 wt.%, preferably 40 wt.% methanol, 2-6 wt.%, preferably 4 wt.% dimethyl ether, 10-30 wt.%, preferably 20 wt.% naphtha, 3-5 wt.%, preferably 4 wt.% latent solvent, and 1-3 wt.%, preferably 2 wt.% additive.    USE - Alcohol-ether gasoline is used for vehicles.    ADVANTAGE - The alcohol-ether gasoline is energy-saving and environmentally-friendly (reduces pollution by more than 60%), can be used directly as fuel for vehicles, and saves oil consumption by 50%.
NOVELTY - Fertilizer composition comprises 80-92 wt.% decomposed chicken manure, 3-10 wt.% calcium superphosphate, 1-5 wt.% potassium dihydrogen phosphate, 0.5-5 wt.% calcium carbonate, 0.02-0.5 wt.% zinc sulfate, 0.04-0.7 wt.% manganese sulfate, 0.1-0.6 wt.% copper sulfate, 0.5-1 wt.% magnesium sulfate, 0.1-0.7 wt.% ferrous sulfate heptahydrate, 0.02-0.2 wt.% ammonium molybdate, 0.02-0.35 wt.% boric acid, and 0.5-1 wt.% Pinnularia.    USE - The composition is useful for culturing pearl mussel by supplementing organic debris needed by pearl mussel, and nitrogen, potassium, and phosphate and variety of trace elements needed by phytoplankton and zooplankton.    ADVANTAGE - The fertilizer composition has sufficient organic nutrients and trace element, and reasonable compatibility and rapidly supplements organic debris.
NOVELTY - Fertilizer composition comprises 80-92 wt.% composted duck 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, 0.02-0.2 wt.% manganese chloride, 0.1-0.6 wt.% copper sulfate, 0.1-0.7 wt.% ferrous sulfate heptahydrate, 0.02-0.2 wt.% ammonium molybdate, 0.02-0.35 wt.% boron, and 0.5-1 wt.% Cyclotella.    USE - The fertilizer composition is useful for farming pearl oyster.    ADVANTAGE - The composition has sufficient organic nutrients and micronutrients, and rapidly supplements organic residues needed by pearl oyster, and nitrogen, phosphorus, potassium and various trace elements needed by phytoplankton and zooplankton.
NOVELTY - Recycling and regenerating the active carbon to produce aspirin comprises discharging the waste active carbon from refining tank using salicylic acid and then filtering using filter, performing regeneration using multifunctional filter, and returning the salicylic acid into refining tank.    USE - The method is useful for recycling and regenerating the active carbon to produce aspirin (claimed).    ADVANTAGE - The method is capable of economically recycling and regenerating the active carbon with less energy consumption.
NOVELTY - A fuel composition comprises a mixture of 1-10 pts.wt. biodiesel and remainder of ethanol.    USE - Fuel composition.
NOVELTY - A rotten livestock excrement organic fertilizer is produced by providing livestock excrement and straw at wt. ratio of 5.5-8:1-2, dehydrating, drying and crushing until grain diameter is 0.5-2.5 mm; and mixing the mixture and decomposing inoculant agent at 7500-12000:1-2, mixing adding water until water content is 30-32% and fermenting at high temperature under 50-55 degrees C for 5-7 days, and preparing powder or granular formulation organic fertilizer.    USE - Method for production of rotten livestock excrement organic fertilizer (claimed).    ADVANTAGE - The fertilizer solves problem of livestock manure to environment and realizes harmlessness. Fermentation is carried out at high temperature in a short time.
NOVELTY - High-concentration level-pressure type automatic-deslagging biogas generation tank comprises pressure tank, horizontal biogas fermentation tank and gas holder tank, where the pressure tank is provided with sand sediment tank and stirrer, the outlet of the pool is horizontal marsh gas fermenting tank, the slope ratio of the bottom of a fermentation tank is 1:4-6, the bottom of the tank is provided with a heating device, and the top of the front section of the fermentation tank is equipped with an isolating wall.    USE - The high-concentration level-pressure type automatic-deslagging biogas generation tank is useful for producing biogas which is used as fertilizer.    ADVANTAGE - The tank provides gas yield of more than 2 cubic meter, and fermentation yield of 5 or more times. The tank is horizontally constructed underground so as to be good for heat preservation, consumes less energy and ensures normal operation in north winter, can realize automatic feeding and automatic slag discharging, and has low operation cost.    DETAILED DESCRIPTION - High-concentration level-pressure type automatic-deslagging biogas generation tank comprises pressure tank, horizontal biogas fermentation tank and gas holder tank, where the pressure tank is provided with sand sediment tank and stirrer, the outlet of the pool is closed horizontal marsh gas fermenting tank, the slope ratio of the bottom of a fermentation tank is 1:4-6, the bottom of the tank is provided with a heating device, the top of the front section of the fermentation tank is equipped with an isolating wall, the rear portion of the fermentation tank is provided with a baffle wall, the rear portion of the fermentation tank is connected into the gas-holder tank through the baffle wall, the tank is provided with gas holder, the gas-holder tank is connected with slag storage tank through a baffle opening and a baffle channel and biogas pipeline on the fermentation tank cover is led into the gas holder.
NOVELTY - A composite microorganism fertilizer comprises 80-85 wt.% sugar filter mud, 1-2 wt.% orange water, 10-15 wt.% tobacco powder, 4-8 wt.% medical stone, 1-2 wt.% rhizome of Rehmannia, 1-2 wt.% solid nitrogen-phosphorus-potassium strain, and 3-5 wt.% bentonite.    USE - Composite microorganism fertilizer.    ADVANTAGE - The method is simple, easy, energy-saving, and environment-friendly. The fertilizer has high efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of composite microorganism fertilizer which comprises:    (A) weighing raw materials, and mixing at 40-60 revolutions/minute (rpm);    (B) putting mixed raw materials into fermentation tank, fermenting at 30 degrees C, increasing temperature everyday until it is 70 degrees C, stopping increase of temperature, and fermenting for 10 days;    (C) performing enzymolysis to the fermented material into rotary drum granulator, where pressure is 120-150 Pa and rotation speed is 100-200 rpm;    (D) drying and prilling at 135-145 degrees C for 20-25 minutes; and    (E) sieving at rotation speed of 50-100 rpm to obtain finished product.
NOVELTY - A dye-stable furnace fuel composition comprises mineral oil component having effective boiling point of 160-380 degrees C, biocomponent fuel component comprising 1-5C alkyl esterified acid from rapeseed oil, canola oil, soybean oil, coconut oil, sunflower oil, palm oil, palm kernel oil, peanut oil, linseed oil, tall oil, corn oil, castor oil, jatropha oil, jojoba oil, olive oil, flaxseed oil, camelina oil, safflower oil, babassu oil, tallow oil, rice bran oil, and/or yellow grease, 0.5-5 mg/kg azo dye components, and 50 vppm or less tert-butyl-functionalized hydroquinone antioxidant component.    USE - Dye-stable furnace fuel composition (claimed).    ADVANTAGE - The dye-stable furnace fuel composition has improved dye stability.    DETAILED DESCRIPTION - A dye-stable furnace fuel composition comprises a mineral oil component having effective boiling point of 160-380 degrees C, biocomponent fuel component comprising 1-5C alkyl esterified acid from rapeseed oil, canola oil, soybean oil, coconut oil, sunflower oil, palm oil, palm kernel oil, peanut oil, linseed oil, tall oil, corn oil, castor oil, jatropha oil, jojoba oil, olive oil, flaxseed oil, camelina oil, safflower oil, babassu oil, tallow oil, rice bran oil, and/or yellow grease, 0.5-5 mg/kg azo dye components, and 50 vppm or less tert-butyl-functionalized hydroquinone antioxidant component. The volume ratio of mineral oil component and biocomponent fuel component is 99:1-1:9. The fuel composition exhibits increased dye stability, with respect to fuel composition having similar mineral oil and biocomponent fuel components and identical azo dye component(s), but having a different or no antioxidant component.
NOVELTY - A sanitation vehicle fuel comprises 40-73 wt.% gasoline component oil, 10-40 wt.% methanol, 8-15 wt.% isopropyl alcohol, and 8-10 wt.% anti-corrosive combustion-supporting agent which is composed of 9-11 wt.% antioxidant, 5-7 wt.% swelling agent, 58-62 wt.% accelerant, 10-14 wt.% antistatic agent, 4-6 wt.% anti-knock agent and 5-7 wt.% metal passivator.    USE - Fuel used for sanitation vehicle.    ADVANTAGE - Methanol heat value is low, engine motor force performance is improved, swelling and corrosion are prevented, and is safer and reliable.
NOVELTY - A refuse derivative fuel is prepared by sieving treated domestic garbage, removing inorganic non-combustible domestic garbage, crushing using crusher after automatically sorting household waste, adding 5-20 wt.% garbage and coal and 5-10 wt.% alkaline additive to household garbage, stirring and uniformly mixing, drying mixture of domestic garbage, coal and additive by forced ventilation so that water content is reduced to 20%, and extruding and forming using forming device.    USE - Preparation of refuse derivative fuel for cement kiln joint treatment.    ADVANTAGE - Land resource is saved, pollution by garbage is removed and the fuel has low cost and high quality.    DETAILED DESCRIPTION - A refuse derivative fuel is prepared by sieving treated domestic garbage, removing inorganic non-combustible domestic garbage, crushing using crusher after automatically sorting household waste, adding 5 wt.% coal and 10 wt.% alkaline additive to household garbage, stirring and uniformly mixing, drying mixture of domestic garbage, coal and additive by forced ventilation so that water content is reduced to 20%, and extruding and forming using forming device.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of the preparation of derived fuel in cement kiln joint disposal waste. (Drawing includes non-English language text).
NOVELTY - An urban sewage treatment plant sludge fuel treatment technology involves carrying out chemical conditioning of sludge by adding and stirring 3.5-4 g high molecular flocculating agent and 4-4.5 g surfactant, adding 100-130 g dispersing agent per 1 kg sludge dispersing agent, carrying radiation conditioning of sludge by sending sludge to microwave radiation at 600 W for 250-300 s, filter pressing dehydration the sludge into filter press with 0.8 MPa limit pressure for 30-45 min in which cake water content is less than or equal to 50%, pelleting after dehydration, and microwave heating until water content is 5-10%.    USE - Urban sewage treatment plant sludge fuel treatment technology (claimed).    ADVANTAGE - Energy consumption is reduced, processing time is shortened, and mechanical dewatering performance of sludge is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the urban sewage treatment plant sludge fuel treatment technology. (Drawing includes non-English language text).
NOVELTY - Biological organic fertilizer comprises 80-90 wt.% fermented chicken manure, 5-10 wt.% humic acid, 4-10 wt.% clay, 2 million/kg active beneficial bacteria, and 1-2 wt.% microelements.    USE - Used as a biological organic fertilizer.    ADVANTAGE - The fertilizer has complete nutritional elements, and improves soil fertility, crop quality, and plant resistance against insects and diseases.
NOVELTY - A rhizosphere control agent contains weathered coal nitro humic acid, nitrogen fertilizer, phosphate fertilizer, and potash fertilizer. Weight ratio weathered coal nitro humic acid:nitrogen fertilizer:phosphate fertilizer:potash fertilizer is 25-26:5-7:4-5:4-5.    USE - A rhizosphere control agent for soil contaminated with heavy metal (claimed).    ADVANTAGE - Biological effectiveness of cadmium in soil and plant restoration efficiency of rhizosphere control agent are improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for application of rhizosphere control agent to soil contaminated with heavy metal.
NOVELTY - Crushing bucket comprises a loader mechanical arm detachably mounted on a bucket shell. The front end of the bucket shell is provided with a shovel feed opening. A partition wall is arranged in the inner cavity of the bucket shell. The inner cavity of the partition wall of the bucket shell is divided into two cavities. One cavity is located at the front end and the other cavity is located at the rear end. The rear end cavity of the bucket shell is provided with a material outlet. The composting material first enters into the front end cavity from the shovel feed opening.    USE - Used as a crushing bucket.    ADVANTAGE - The crushing bucket is set with a loading vehicle for controlling moisture content of the materials to 20-70% during transport; ensures homogeneous mixing and crushing, and the mixed materials can be used for pre-composting; and ensures convenient composting and reduces the composting cost.
NOVELTY - A yield increasing fertilizer is prepared by mixing 4-6 wt.% sheep manure, 4-6 wt.% dry donkey manure, 14-18 wt.% bean cake, 12-16 wt.% broomcorn cake, 6-8 wt.% wheat straw powder, 2-4 wt.% peanut stem and leaf powder, 4-6 wt.% melon powder, 2-6 wt.% wheat straw powder, 4-6 wt.% corn core powder, 12-14 wt.% Lotus leaf powder, 8-10 wt.% straw powder, 2-4 wt.% potassium fertilizer, 3-5 wt.% potassium fertilizer, 1-3 wt.% trichlorfon, and 4-6 wt.% epoxy resin.    USE - Method of preparing a yield increasing fertilizer (claimed).    ADVANTAGE - The method increases yield; and improves growth speed, disease resistance capability, and insect and pest resistance of root.
NOVELTY - A biogas production system comprises a fermentation tank, steam-water separator, desulfurizing tower, gas holder and biogas boiler. Biogas air outlet valve is provided between the fermentation tank and the steam-water separator. First gas inlet valve is provided between the steam-water separator and the desulfurizing tower. Second gas inlet valve is provided between the desulfurizing tower and the gas holder. Fan is provided between the gas holder and the biogas boiler. Water outlet pipeline of the biogas boiler is provided with a circulating pump for conveying water to heat exchanger.    USE - Biogas production system.    ADVANTAGE - The system can automatically control the fermentation tank temperature, ensure the temperature desired to bacterial fermentation, and increase the gas yield.
NOVELTY - Production of synthesis gas involves dividing a hydrocarbon -containing feed into hydrocarbon feed (a) and hydrocarbon feed (b), subjecting hydrocarbon feed (100) (a) to catalytic partial oxidation, yielding reaction product (a) comprising hydrogen, carbon monoxide and carbon dioxide, and subjecting hydrocarbon feed (b) to steam reforming (5) followed by a water gas shift reaction, yielding reaction product (b), combining reaction products (a) and (b), yielding a synthesis gas for methanol synthesis. The reaction product (a) comprises less than 10% carbon dioxide on dry basis.    USE - Production of synthesis gas used for producing methanol.    ADVANTAGE - The method provides synthesis gas with improved energy efficiency.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) production of methanol, which involves using synthesis gas; and    (2) method for adapting methanol plant, which involves adding catalytic partial oxidation unit in parallel with a steam reforming unit.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the reformer with a pre-reforming section.    Autothermal reformer (2)    Steam reformer (5)    Pre-reformer (11)    Natural gas feed (100)    Desulfurized feed (120)
NOVELTY - A catalyst comprises mixed catalyst fine particle with nickel (Ni) metal particle as main catalyst metal particle and iron (Fe) particle or manganese dioxide (MnO2) particle as adjuvant particle and porous material consisting of metal oxide as support.    USE - A catalyst for biomass gasification (claimed).    ADVANTAGE - Catalyst has excellent durability during biomass gasification process and high modification activity.
NOVELTY - Ethyl 4-methyl-pyridine-2-carboxylate is catalytically oxidized using phosphomolybdic acid to obtain ethyl 4-methyl-1-oxy-pyridine-2-carboxylate. The obtained compound is reduced using methanol or ethanol as solvent, to obtain ethyl 4-methyl-piperidine-2-carboxylate hydrochloride.    USE - Preparation of ethyl 4-methyl-piperidine-2-carboxylate hydrochloride (claimed).    ADVANTAGE - The method enables simple and environmentally-friendly industrial preparation of ethyl 4-methyl-piperidine-2-carboxylate hydrochloride under mild reaction conditions, with increased catalytic activity, reduced usage of oxidant, and high yield, safety, product purity, and product quality.
NOVELTY - Multicompartment device comprises: a first compartment including a dyeing composition (a) comprising one or more oxidation dyes and one or more alkaline agents; a second compartment including a composition (b) comprising one or more oxidizing agents; and one or more self-foaming agents having at least one of the compositions (a) and/or (b).    USE - The device is useful for dyeing keratinous fibers (claimed) such as hair dyeing.    ADVANTAGE - The device: provides improved colorings, preferably in terms of strength, chromaticity and/or resistance and minimizes maintenance problem of the dyeing; and does not require specific tools (e.g. brush).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a self-foaming dyeing composition for keratinous fibers comprising the oxidation dyes, the alkaline agents, the self-foaming agents and a hydrogen peroxide; and    (2) a method for dyeing keratinous fibers, comprising applying the self-foaming dyeing composition to the fibers during a sufficient exposure time to obtain the expansion of the composition and to develop the desired coloration.
NOVELTY - Method for preparing fermented pig manure organic fertilizer, involves (a) taking 1.6 tons pig manure with moisture controlled at 40%, uniformly mixing 5 kg probiotic liquid and 2-3 kg corn meal and crushing mixture, (b) mixing 8-10 kg sawdust and 50-75 kg vinasse, (c) stacking the mixtures to form strip-type piles and (d) decomposing raw materials in the piles for 5-7 days.    USE - The method is useful for preparing fermented pig manure organic fertilizer (claimed), which is used for controlling plant disease and insect pests.    ADVANTAGE - The method enables to prepare fermented pig manure organic fertilizer improves soil environment and pH value and is beneficial to crop growth.    DETAILED DESCRIPTION - Method for preparing fermented pig manure organic fertilizer, involves (a) taking 1.6 tons pig manure with moisture controlled at 40%, as raw material, uniformly mixing 5 kg probiotic liquid and 2-3 kg corn meal and crushing mixture, (b) mixing 8-10 kg sawdust and 50-75 kg vinasse, (c) stacking the mixtures to form strip-type piles with width of 2 m, height of 0.5 m and unlimited length, where the strip-type piles are covered with old sack pieces or straw mats, and temperature of the piles are raised to 50 degrees C within 24 hours, and above 60 degrees C and even 70 degrees C within 48 hours, and (d) completely decomposing raw materials in the piles for 5-7 days in spring, summer and autumn, where the stinks are disappear and all the pathogenic bacteria such as Pseudomonas putida, eggs and grass seeds in the raw materials are killed.
NOVELTY - Organic fertilizer obtained using lees, comprises vinasse, excrement and straw in a weight ratio of 35-40:35-40:70-80.    USE - As organic fertilizer obtained using lees.    ADVANTAGE - The fertilizer is environmentally-friendly and cost-effective, and can be produced simply.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing organic fertilizer obtained using lees, which involves mixing grain and mixed manure for natural fermentation, drying until the water content is 5-10%, crushing the materials, placing in fermentation tank, fermenting at 100 degrees C for 15-20 days, drying the fermented product until the water content is 5-10%, crushing the dried mixture, and sieving the particles to diameter of 1-10 mm.
NOVELTY - Method of preparing chicken manure organic fertilizer, involves obtaining chicken manure, straw powder or leaf powder, corn and fermentation microbial inoculum, placing chicken manure in fermentation tank and fermenting at high temperature for 5-7 days, mixing with straw powder or leaf powder and corn flour, stirring the combined ingredients, again carrying out aerobic fermentation at 50 degrees C for 24 hours, and at 60-70 degrees C for 48 hours.    USE - The method is useful for preparing 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 - Fertilizer comprises urea, ammonium sulfate, methylene urea, acetic acid, benzyl ammonium chloride, compound amino acid, dicyandiamide and titanium dioxide in a weight ratio of 3-40:1-20:2-30:10-20:5-10:2-10:5-15:0.1-5.    USE - As fertilizer.    ADVANTAGE - The fertilizer is environmentally-friendly and cost-effective, increases yield of crops, can be prepared simply and easily, and enhances nutritional value of the agricultural products.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing nitrogenous fertilizer, which involves mixing the components uniformly, drying, crushing into powder, uniformly stirring, adding the powder into pelleting machine at 70-85 degrees C to form extrudate, cutting the extrudate into granules, granulating, drying and sieving using 10-15 meshes sieve to obtain the particulate material.
NOVELTY - Fermented organic fertilizer comprises 20-30 pts. wt. poultry excrement, 40-50 pts. wt. crop straw, 2-6 pts. wt. lime powder and 1.5-15 pts. wt. probiotics.    USE - The fermented organic fertilizer is useful for preventing plant diseases by controlling insects and pest.    ADVANTAGE - The fermented organic fertilizer improves pH of soil and is suitable for growth of crops.
NOVELTY - Bacterial flora, preferably Bacillus sp. under a preservation number of CGMCC No. 5971, Rheinheimera tangshanensis under a preservation number of CGMCC No. 5972, and Wickerhamomyces anomalus under a preservation number of CGMCC No. 5975, is new.    USE - The bacterial flora is useful for making paper (claimed).    ADVANTAGE - The bacterial flora produces the paper more than the grade AA level with less energy consumption. The pulping process of the waste liquid can be recycled or converted into marsh gas or organic fertilizer hence eco-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for making paper comprising mixing bacterial flora with water to form bacterial liquid, where the weight ratio of the Bacillus sp., Rheinheimera tangshanensis and Wickerhamomyces anomalus is 1-3:1-3:2-3, (b) adding the woody raw material after cortex slice or herbal raw material and then cutting in a section, introducing the raw material into a soaking pool for swelling, and (c) adding the hydrophobic solution as raw material to soak the prepared bacterial liquid, adding the biodegradable raw material in bacterial liquid and then draining and steam sterilizing to form a fiber bundle and then grinding to make the fiber beam, separating the single fiber and then screening and filtering, and drying the filtered mixture to obtain slurry, fine grinding the slurry to obtain the paper pulp and then soaking in warm water.    DESCRIPTION OF DRAWING(S) - The figure shows a flow chart of a method for making paper using bacterial flora (Drawing includes non-English language text).
NOVELTY - Rheinheimera tangshanensis (I) under a preservation number of CGMCC No. 5972, is new.    USE - (I) is useful for making paper (claimed).    ADVANTAGE - (I) produces the paper more than the grade AA level with less energy consumption. The pulping process of the waste liquid can be recycled or converted into marsh gas or organic fertilizer hence eco-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for making paper comprising (a) mixing Rheinheimera tangshanensis with water to form bacterial liquid, (b) adding the woody raw material after cortex slice, or herbal raw material and then cutting in a section, and putting the raw material into a soaking pool and then swelling, and (c) adding the hydrophobic solution as raw material to soak the prepared bacterial liquid, adding the biodegradable raw material in bacterial liquid and then draining and steam sterilizing to form a fiber bundle and then grinding to make the fiber beam, separating the single fiber and then screening and filtering, and drying the filtered mixture to obtain slurry, fine grinding the slurry to obtain the paper pulp and then soaking in warm water.    DESCRIPTION OF DRAWING(S) - The figure shows a flow chart of a method for making paper using Rheinheimera tangshanensis (Drawing includes non-English language text).
NOVELTY - Device comprises a feeding port set on a fermentation processing chamber and a discharge hole is connected with a drying storage chamber. The fermentation processing chamber comprises a multiple parallel horizontal straight air outlet pipes. Each of the air outlet pipes is provided with a stirring screw driven by a motor. The end of the fermentation cavity is connected with the discharge hole connected with the feeding port.    USE - The device is useful for fermentative treatment of organic waste (claimed).    ADVANTAGE - The device: processes organic waste into fertilizer for plants, which is easy to store and does not cause bad odor; and is suitable for processing household, restaurant, hotel and other occasion wastes.
NOVELTY - The system has an air distribution plate fixed with a fluidized bed gasification unit. The fluidized bed gasification unit is connected with a water film dust remover. A spraying tower, a turbulence tower, a separator and a static coke catching device are fixed with a wet dust-removing coke unit. A dust-removing unit is connected with a draught fan. An anti-explosion water seal, an air-water seal, an air storage cabinet and an internal combustion generating unit are connected with the wet dust-removing coke unit.    USE - Fluidized bed biomass gasification system.    ADVANTAGE - The system has high efficiency and high temperature gas-solid separation function. The system meets working requirements of an internal combustion generator unit. The system absorbs biomass fluidized bed gasification so as to ensure stability of air flow in a fluidized bed gasification furnace. The system can convert biomass energy into electrical energy in an efficient manner.
NOVELTY - Producing methanol, comprises: providing a divided electrochemical cell comprising an anode in a first cell compartment and a cathode electrode in a second cell compartment that also contains a catalyst (at least one of a substituted or unsubstituted aromatic heterocyclic amine), where both compartments contain an aqueous solution of an electrolyte; providing carbon dioxide from an existing source into the second cell compartment; and electrochemically or photoelectrochemically reducing the carbon dioxide in the second cell compartment to produce methanol.    USE - The method is useful for producing methanol (claimed) which is used as: a feedstock for synthetic hydrocarbons, polymers, biopolymers and proteins, which can be used for animal feed or human consumption; and an energy storage and transportation material.    ADVANTAGE - The method: is environmentally-friendly, simple and economic, since it utilizes any available source of carbon dioxide thus reducing atmospheric carbon dioxide and mitigating global warming; does not require extra reactants, such as a hydrogen source; and provides methanol which is a convenient energy storage medium, which allows convenient and safe storage and handling and can be a readily transported and dispensed fuel for methanol fuel cells.
NOVELTY - A composting of agricultural waste treatment system was developed. It included a crusher with dehydrator, a rotary kiln-type main fermentation machine, and a secondary vertical-type fermentation machine. First, the crusher with dehydrator was used to crush and dehydrate the agricultural waste, let the agricultural waste became a scrap and low moisture content of the organic fertilizer substrate materials. Then, the substrate materials were conveying into a rotary kiln-type main fermentation machine for bacterial inoculation and stir thoroughly mixed fermentation. Finally, the secondary vertical-type fermentation machine, it had seal, insulation and ventilation, mixing and drainage functions, was used to the second fermentation, let the substrate materials became a maturity organic composting. This system had a series of complete fermentation of agricultural waste composting.
NOVELTY - The method involves collecting the urine of livestock and poultry and carrying out solid-liquid separation. The farm manure is collected in a grit chamber and plant straw powder is mixed with the straw manure by a hoisting machine. The solid-liquid separated farm manure is fermented. The fermented manure is recycled, and is entered into marsh gas pool. The fermented manure is dried to form solid fertilizer. The granular material in the solid fertilizer is separated, and the fertilizer is packaged in a bag.    USE - Livestock and poultry farm manure recycling method.    ADVANTAGE - The recycling efficiency is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating the livestock and poultry farm manure recycling process. (Drawing includes non-English language text)
NOVELTY - Preparing organic ammonia water involves evenly mixing 50 kg fresh cow dung, 50 g soybean meal and 5 kg calcined gypsum powder, stirring and sealing the mixture, maintaining the mixture at less than 25 degrees C for three days and adding water which is three times more than weight of the mixture.    USE - The method is useful for preparing organic ammonia water used as fertilizer.    ADVANTAGE - The fertilizer efficiency of the organic ammonia water is higher than ammonia water.
NOVELTY - The method involves mixing vegetable oil and/or animal oil with hydrogen into a hydrogenation refining reactor, carrying out hydrogenation saturation and hydrogenation deoxidization reaction in presence of hydrogenation refining catalyst. A hydrogenation refining reaction product is placed on the hydrogenation cracking reactor above a gas-liquid separator. Gas-liquid separation is carried out on a tower plate. The refined oil and hydrogen flow is uniformly spread on a hydrogenation cracking catalyst bed layer.    USE - Naphtha biological resource preparation method.    ADVANTAGE - The method enables reducing inner and outer pressure difference by using the gas-liquid separator, decreasing wall thickness, reducing device investment and operation cost, preventing ammonia and water vapor in the refined product from being entered into the cracking catalyst bed layer and ensuring cracking catalyst activity.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a naphtha biological resource preparation method.
NOVELTY - The method involves mixing hydrogen into a hydrogenation refining reactor, and carrying out hydrogenation refining reaction. The hydrogenation refining reaction product is entered into the hydrogenation refining reactor above a gas-liquid separator. A gas-liquid separation is carried out for transferring refined oil on a tower plate. The refined oil and hydrogen flow are uniformly distributed on the tower plate by hydride-waxing catalyst bed layer. The obtained oil is formed in the tower to obtain a diesel product.    USE - Biological diesel oil preparing method.    ADVANTAGE - The method enables ensuring high cetane value, low sulfur content and low solidifying point.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a biological diesel oil preparing method.
NOVELTY - The method involves entering fresh oil feeding and refining diesel oil into a mixing tank and fully dissolving hydrogen discharging excessive hydrogen. The saturated dissolved hydrogen is fed into liquid phase hydrogenation reactor to carry out hydrogenation refining reaction. The hydrogenation refining reaction effluent decompressed by a pressure reducing valve is entered into a high temperature and low pressure flash evaporation tank to obtain gas phase and liquid phase. Hydrogen and hydrogen sulfide are separated to obtain biodiesel product.    USE - Diesel oil liquid phase hydrogenation method.    ADVANTAGE - The method enables reducing heavy fraction of content of hydrogen, avoiding circulating enrichment of hydrogen sulfide, and reducing liquid phase circulation amount of circulating pump investment and operation energy consumption.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a diesel oil liquid phase hydrogenation method.
NOVELTY - The method involves dividing solution into two parts, and recycling one of the parts in a mixing tank through a circulating pump for continuous reaction. The other part is entered into an oxidization desulphurization reactor to perform oxidation reaction. A biodiesel product is obtained after separating and flashing a light diesel fraction. The product is entered into a gas-liquid separator to obtain an ultra-low sulfur diesel product. A liquid phase hydrogenation reactor used catalyst is VIB and/or VIII group metal, aluminum oxide or silicon-containing aluminum oxide.    USE - Diesel oil deep desulfurization combined method.    ADVANTAGE - The method enables making full use of hydrodesulfurization and oxidation, reducing operation cost and energy consumption, and performing diesel oil deep desulfurization to produce clean diesel oil.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a diesel oil deep desulfurization combined method.
NOVELTY - The system has a biomass feeding device comprising a calcium oxide feeding device whose discharge end is connected to a generator, and another discharging end is connected to a fluidized bed reactor. An input end of the fluidized bed reactor is connected with the generator, and an output end of the bed reactor is connected with a gas-solid separator. The bed reactor is provided with a heat exchanger for gasification of a product. A gasification generating device comprises a boiler, a fan and a gasification agent generator, where the gas-solid separator is a cyclone separator.    USE - Biomass high temperature gasification system.    ADVANTAGE - The system has high gasification efficiency, low energy consumption and high quality generated gas, and is inexpensive.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biomass high temperature gasification method    DESCRIPTION OF DRAWING(S) - The drawing shows a partial sectional view of a biomass high temperature gasification system.
NOVELTY - The machine has machine case which is provided with the walking wheel that is set with crusher. The mixing unit and fermentation tank are set with conveying element. The conveying element is connected with the transmission mechanism connected with the machine case. The fermentation tank is connected with the discharge port.    USE - Movable organic fertilizer combined processing machine.    ADVANTAGE - The reduction of organic waste pollution, environment-friendly green agriculture, strong processing ability, and low equipment investment can be improved effectively.
NOVELTY - An organic fertilizer-producing device comprises fermenter, organic fertilizer crusher, fermenting tank, inorganic fertilizer crusher, and mixing machine. Fermenter is provided with chicken manure inlet, bacteria inlet, phosphorus bacteria inlet, potassium inlet, and ammonification bacteria inlet. Yeast fermentation groove is provided with conveyor. Organic fertilizer crusher is provided with monosodium glutamate leftovers inlet, and polluted river mud inlet. Inorganic fertilizer crusher is provided with urea inlet, calcium superphosphate inlet and potassium sulfate inlet.    USE - Device for producing watermelon tenement special biological organic fertilizer.    ADVANTAGE - The device provides complete fermentation and thorough sterilization, and is convenient to use. The prepared fertilizer contains abundant biological organic material, nitrogen, phosphorus, potassium and middle microelement chelate and agrochemical.
NOVELTY - Treating organic wastewater by recycling synthesis gas, comprises introducing the wastewater by a high pressure pump into a preheater (7) and into a supercritical gasification device, dividing a first portion of the preheater into the gasification device by a compressor (2), entering the water into an outlet of the device into a high pressure gas-liquid separator (6) by a heat exchanger (5), and recycling the synthesis gas using the gas-liquid separator and entering into a bottom of a fluid heater and oxygen into a supercritical water oxidation reactor (4).    USE - The method is useful for treating organic wastewater by recycling synthesis gas (claimed).    ADVANTAGE - The method is capable of efficiently treating the high concentration organic wastewater with less effort.    DETAILED DESCRIPTION - Treating organic wastewater by recycling synthesis gas, comprises introducing the organic waste water by a high pressure pump into a preheater (7) and into a supercritical gasification device, dividing a first portion of the preheater into the supercritical gasification device by a compressor (2), entering the water into an outlet of the supercritical gasification device into a high pressure gas-liquid separator (6) by a heat exchanger (5), recycling the synthesis gas such as hydrogen, carbon monoxide and methane using a high pressure gas-liquid separator and entering into a bottom of a fluid heater and oxygen into a supercritical water oxidation reactor (4), where the fluid reactor comprises a cooler, and a back pressure valve.    DESCRIPTION OF DRAWING(S) - The diagram shows a flow chart of a method for treating organic wastewater.    Compressor (2)    Supercritical water oxidation reactor (4)    Heat exchanger (5)    High pressure gas-liquid separator (6)    Preheater. (7)
NOVELTY - The method involves mixing vegetable oil or long-chain fatty acid and a solvent, where the vegetable oil comprises a soybean oil, palm oil, cotton seed oil, peanut oil, sunflower seed oil, rapeseed oil, rice bran oil, corn oil, castor oil, tallow oil, stillingia oil, coptis wood oil, tung oil, tree skin oil, fructus ligustri lucidi oil, olive oil, hemp oil and air chestnut flax oil. The fatty acid is oleic acid, palmitic acid, stearic acid, linoleic acid and linseed acid. The mixed solution is added with hydrogenation catalyst. The temperature is reduced to obtain the long chain alkane.    USE - Method for catalyzing vegetable oil that is utilized for diesel application.    ADVANTAGE - The method enables catalyzing the vegetable oil in a simple, convenient and cost effective manner. The vegetable oil can be repeatedly used, and is directly used for diesel application.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical illustration of a method for catalyzing plant oil composed of Ruthenium based catalyst and long chain fatty acid. '(Drawing includes non-English language text)'
NOVELTY - The furnace has a large cover (2) comprising a large furnace cover body, core and an inner cover. A core protection cover is fixed on the inner cover and the core. A mounting cavity is equipped between the core and the inner cover. The core protection cover is formed between mounting cavities. The core is provided with an edge and a core body that is provided with multiple through-holes. A body (1) is provided with a sealing ring. The mounting cavities are provided with a tar filter device (5). A feeding port is provided with a sealing cover (6).    USE - Straw gasification furnace.    ADVANTAGE - The furnace is environment-friendly when producing the tar.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a straw gasification furnace.    Body (1)    Large cover (2)    Tar filter device (5)    Sealing cover (6)
NOVELTY - The structure has a hearth (11) connected to a drying area, cracking area and oxidation and reduction area. An inner wall of the hearth in the oxidation area bulges inwards. The cracking area is smaller than the reduction area of inner diameter of a hearth structure.    USE - Down-sucking type biomass fuel gasification stove hearth structure.    ADVANTAGE - The inner wall of the hearth on a part corresponding to oxidation can be bulged inwardly so that inner diameter of the cracking region is formed lesser than inner diameter of reduction region so as to ensure oxidation zone the temperature of cracking section and reducing section, thus improving carbon monoxide gas production effect in the reduction zone.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a down-sucking type biomass fuel gasification stove hearth structure in partial section.    Hearth (11)
NOVELTY - The structure has a hearth (11) provided with a fire grate gasification furnace (13), and an air outlet pipe (2) connected with a gasifying furnace body (1). The air outlet pipe is connected with an air outlet cavity (12), and a spray washing mechanism (5) is connected with a carbon monoxide gas filtering mechanism (4) that is provided with an air inducing mechanism (3). The filtering mechanism is arranged on a gas-water separating mechanism (6). The air inducing mechanism comprises a frame (31), a motor (32) and transmission wheels (33, 34).    USE - Biomass fuel gasification furnace structure.    ADVANTAGE - The structure can guarantee bleed stable, and can avoid intermittent air supply.    DESCRIPTION OF DRAWING(S) - The drawing shows a front perspective view of a biomass fuel gasification furnace structure in partial section.    Gasifying furnace body (1)    Air outlet pipe (2)    Air inducing mechanism (3)    Carbon monoxide gas filtering mechanism (4)    Spray washing mechanism (5)    Gas-water separating mechanism (6)    Hearth (11)    Air outlet cavity (12)    Fire grate gasification furnace (13)    Frame (31)    Motor (32)    Transmission wheels (33, 34)
NOVELTY - The structure has an air outlet pipe (2) connected with a gasification furnace body (1), and an air feeding mechanism (3) connected with a carbon monoxide gas filtering mechanism (4). A material expanding mechanism (8) comprises a motor (81). A transmission wheel (83) is fixed on a final stage power output shaft of a material expanding speed reducer (82). A material plate shaft (861) is extended to an upper end of a top plate (15). One end of a transmission belt (85) is sleeved on the transmission wheel, and another end of the belt is connected with another transmission wheel (84).    USE - Improved down-sucking type biomass fuel gasification furnace structure.    ADVANTAGE - The structure ensures efficient furnace feeding by the feeding mechanism and reduces labor intensity.    DETAILED DESCRIPTION - The transmission wheels are chain wheels,and the transmission belt is a transmission chain.    DESCRIPTION OF DRAWING(S) - The drawing shows a front perspective and partial sectional combinational view of an improved down-sucking type biomass fuel gasification furnace structure.    Gasification furnace body (1)    Air outlet pipe (2)    Air feeding mechanism (3)    Carbon monoxide gas filtering mechanism (4)    Material expanding mechanism (8)    Top plate (15)    Motor (81)    Material expanding speed reducer (82)    Transmission wheels (83, 84)    Transmission belt (85)    Material plate shaft (861)
NOVELTY - The furnace has a hearth (11) sealed to a top plate (15) of a gasification furnace body (1). The hearth is linked with a biomass fuel feeding mechanism (7). The top plate is connected with a feeding interface (151). The feeding mechanism is connected with the feeding interface. The feeding mechanism is provided with a feeding motor (71), three driving wheels (72, 73, 74), a lifting chain (75), a lifting box (76), a hopper (77) and two transmission belts (78, 79). The feeding motor is fixed on the top plate.    USE - Automatic feeding biomass fuel gasification furnace.    ADVANTAGE - The feeding mechanism is matched with the feeding interface, so that the furnace can be automated to reduce working intensity of a worker.    DESCRIPTION OF DRAWING(S) - The drawing shows a front perspective view of an automatic feeding biomass fuel gasification furnace in partial section.    Gasification furnace body (1)    Biomass fuel feeding mechanism (7)    Hearth (11)    Top plate (15)    Feeding motor (71)    , Driving wheels (72, 73, 74)    Lifting chain (75)    Lifting box (76)    Hopper (77)    Transmission belts (78, 79)    Feeding interface (151)
NOVELTY - The furnace has a furnace body (1) fixed on a water-sealed dust collecting tank (14), and a fire grate (13) used for driving a rotary fire grate driving mechanism assembly (9). One end of a transmission belt (94) is sleeved on a transmission wheel (92), and another end of the belt is connected with another transmission wheel (93). A gear shaft (961) is rotatably fixed on a water sealing dust collecting pool bottom plate (141). A speed reducer (95) and a grate driving shaft (98) are located in the dust collecting tank.    USE - Down-sucking type biomass fuel gasification furnace.    ADVANTAGE - The furnace does not need manual cleaning ash, and reduces labor intensity.    DESCRIPTION OF DRAWING(S) - The drawing shows a front perspective view of a down-sucking type biomass fuel gasification furnace in partial section.    Furnace body (1)    Rotary fire grate driving mechanism assembly (9)    Fire grate (13)    Water-sealed dust collecting tank (14)    Transmission wheels (92, 93)    Transmission belt (94)    Speed reducer (95)    Grate driving shaft (98)    Water sealing dust collecting pool bottom plate (141)    Gear shaft (961)
NOVELTY - Sludge processing device comprises a spiral feeding chamber, a spiral feeding machine, an integrated processing kettle, a storage hopper, a spiral discharging machine, crusher, feed inlet, packing auger, granulation plate with meshes, stirring shaft with stirring blades, extrusion chamber, feeding chamber, mixing chamber, material outlet and integrated processing kettle discharge hole. The spiral feeding chamber is equipped with spiral packing auger. The spiral feeding chamber and crusher are connected with feed inlet. The crusher discharging port is connected with the spiral feeding machine.    USE - Used as a sludge processing device.    ADVANTAGE - The device has compact structure, good operational stability and reliability, and ensures environment-friendly processing process.
NOVELTY - An organic fertilizer production device comprises liquid material container and transparent upper cover. Opening of the container is sealed to define inner space of liquid material and container. A gas inlet is provided on wall of upper part of upper cover. Production gas is supplied to inner space, where liquid inlet is provided on wall of upper part of upper cover. An illumination device is irradiated toward liquid material in inner space. A heating device is provided on cover of upper or outer surface, inner surface of wall of container or outer surface or wall in inner space of container.    USE - Organic fertilizer production device.    ADVANTAGE - The device has simple structure.
NOVELTY - The machine has truss whose lower portion is provided with a walking wheel. Lifting device is fixed on truss, when two sections of turning frame are set in straight line state under top baffle plate. Lifting hanging hook of chain end is hung on one section of turning frame. Chain plate fixed harrow is fixed on truss of turning driving motor connected with chain plate driven by chain wheel. Truss is provided with temperature measuring device connected with screw rod sleeved with nut. Temperature sensor provided in lower end of probe is connected with data line.    USE - Compost turning machine.
NOVELTY - The device has storage chamber which is connected with the hydrolyzing pond through the chain. The hydrolyzing pond is connected with the solid-liquid separator, sunshine shed, and straw pyrolysis digestion nano element. The raw material tank is connected with the anaerobic fermentation tank through the liquid material pipe. The anaerobic fermentation tank is connected with the biogas slurry pool and module type sewage treatment element.    USE - Straw comprehensive utilization processing device.    ADVANTAGE - The simple structure, convenient operation, saving energy, and utilization rate can be improved effectively.
NOVELTY - An excrement and water separator comprises separating tank and collecting device. Top and bottom of separating tank are respectively provided with water inlet and outlet. Upper part of separation box is provided with at least two filter plate. The upper part of each filter plates forms filter layer. One end of filter layer is connected to collecting device and the other end is provided with pushing device. Filtering layer and collecting device are provided between gate.    USE - Excrement and water separator.    ADVANTAGE - The separator reduces water source environment pollution and feces.
NOVELTY - The system (100) has fermenters (140,150) that dry the food waste and produce the fermented feed respectively. A condensation bath (170) condenses the high quality water ejected from the fermenter. A flocculation basin (180) administers the coagulant to condensed water. A high speed precipitator precipitates the administered coagulant and sludge. A reverse osmosis membrane tub (210) filters the filtered water ejected from the activated carbon tub (200) and concentrates the sludge ejected from the high speed precipitator.    USE - System for producing fermented compost and liquefied fertilizer.    ADVANTAGE - The fermented compost and liquefied fertilizer can be produced efficiently. The high quality organic fermented feed can be cohered using the food waste. The release of contamination in environment can be prevented.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing fermented compost and liquefied fertilizer.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the system for producing fermented feed, fermented compost and liquefied fertilizer. (Drawing includes non-English language text)    System for producing fermented feed, fermented compost and liquefied fertilizer (100)    Fermenters (140,150)    Condensation bath (170)    Flocculation basin (180)    Activated carbon tub (200)    Reverse osmosis membrane tub (210)
NOVELTY - The apparatus has a moisture condenser (300) which lowers moisture contained in the food gas generated during fermentation process of food waste in a food fermentation tub (100). A refrigerant circulation pipe (340) is provided for circulating the refrigerant to the food gas passing through a tube (323) installed at the inside in the fermentation tub. The temperature sensors are used for sensing the temperature of refrigerant flowing through the tube when the temperature of food gas ejected through a food gas exhaust port (332) is higher than fixed reference temperature.    USE - Food garbage disposal apparatus used in home and restaurant.    ADVANTAGE - The dehumidification efficiency of the contained moisture in food gas generated in the food fermentation tub can be increased effectively. The installation and maintenance task of the moisture condenser can be facilitated without increasing fabrication cost of the moisture condenser. The operating time, susceptibility and power consumption of the refrigerant circulation pipe can be reduced and the durability of the refrigerant circulation pipe can be improved effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the food garbage disposal apparatus.    Fermentation tub (100)    Heater (200)    Moisture condenser (300)    Tube (323)    Food gas exhaust port (332)    Condensate outlet (333)    Refrigerant circulation pipe (340)
NOVELTY - The gasify biomass fuel system comprises a reactor (1) with moving bed having parallel streams or down draft, where the reactor is provided with a grill (2) for supporting biomass of ashes falling from gasification process. The grill is mounted vertically inside a chamber (3) of the reactor, which is intended for reducing products from oxidation zone (4). The also controls enlargement or reduction of the chamber to maintain substantially constant temperature and gas output speed. The reactor includes a pyrolysis zone (6) provided with a conical configuration.    USE - Gasify biomass fuel system.    ADVANTAGE - The gasify biomass fuel system comprises a reactor with moving bed having parallel streams or down draft, where the reactor is provided with a grill for supporting biomass of ashes falling from gasification process, and thus simply adjusts volume reduction process of chamber according to need, removes tars obtained from final gas without causing yield losses, and allows to maintain constant fuel reactivity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method performing biomass gasification.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic longitudinal sectional view of reactor.    Reactor (1)    Grill (2)    Chamber (3)    Oxidation zone (4)    Pyrolysis zone (6)
NOVELTY - An alcohol-based liquid fuel comprises (wt.%) a polyethylene wax, water (70-98), ethanol (0.1-28), acetone (5.5-8.5), and combustion-supporting additive (0.05-2). The liquid fuel comprises the polyethylene wax on a surface layer, paraffin oil, carbon dioxide at an upper part in the cylinder.    USE - An alcohol-based liquid fuel for a gas-liquid flame retardant cylinder (claimed).    ADVANTAGE - The liquid fuel has improved flash point, has an explosion-proof effect, and is safe to use and transport.
NOVELTY - A hydrogen-oxygen generating device used for vehicle oil-saving comprises a water electrolysis device comprising a container provided with anode plate and cathode plate. More than one lifting baffle plates, which comprise at least one gap control baffle plate, are provided between the anode plate and the cathode plate. A gap is kept between the bottom gap control baffle plate and the internal bottom of the stirring vessel bottom, where height of the gap is 0.2-30 mm.    USE - Hydrogen-oxygen generating device used for vehicle oil-saving.    ADVANTAGE - The lifting baffle plate controls the speed of the electrolytic reaction to generate the hydrogen and oxygen to the air inlet of the automobile engine such that part of fuel oil is replaced to obtain oil-saving effect under the condition of the same power output.
NOVELTY - The apparatus has a first screw conveyor (9) that is installed at the central axis of a cold room lean (18) and is rotated in opposite direction of a second screw conveyor (10). The second screw conveyor is installed at the central axis of middle temperature cylinder (19) and is rotated in opposite direction to third screw conveyor (12). The third screw conveyor is installed at the central axis of the hot house lean (20). The outlet (22) is formed on middle temperature cylinder to transfer the workpiece.    USE - Apparatus for multi-stage drying and carbonizing waste material such as domestic waste and industrial waste e.g. sewage sludge, food waste, waste plastic film, lungs pet bottle and livestock excretion waste.    ADVANTAGE - The waste material can be dried and carbonized efficiently. The processing time of the waste can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the apparatus for multi-stage drying and carbonizing waste.    Screw conveyors (9,10,12)    Cold room lean (18)    Middle temperature cylinder (19)    Hot house lean (20)    Outlet (22)
NOVELTY - An ionized water burner comprises glass cylinder, sponge, shell, electric wire, metal bar, cover, hydrogen outlet, oxygen outlet, lighter, glass baffle plate, transformer, switch, water outlet hole and water level display. Sponge is provided between cylinder and shell. Wire is connected with switch and transformer and passes through shell. Clapboard divides glass tank into two parts. The two sides of cover are respectively provided with hydrogen outlet and oxygen outlet. Hydrogen outlet opening is provided with lighter. Surface of shell is provided with water outlet hole.    USE - Ionized water burner.
NOVELTY - A straw anaerobic fermentation tank feeding and discharging device comprises a liquid inlet pipe, a feeding mechanism, and a discharging port. A feeding auger feeding port is located on the outer part of the anaerobic fermentation tank, and connected with the discharge hole of the feeding machine. The feeding auger is inclined downwards. The feeding auger discharging port extends into the upper part of the anaerobic fermentation tank.    USE - Straw anaerobic fermentation tank feeding and discharging device.    ADVANTAGE - The device realizes separate conveying of solid-liquid fermentation raw materials to avoid blockage problem, and has stable and reliable operation.
NOVELTY - The fermentation tank has cylindrical portion whose height is less than half of the diameter of the cross section of the tank. The ratio of the diameter of the cross section and height is set to predetermined value. The tank is provided with maize straw and waste water mixture.    USE - Fermentation tank.    ADVANTAGE - The straw anaerobic digestion is performed reliably.
NOVELTY - A hydrophilic slow release fertilizer comprises (parts by weight): wood flour (10-90, preferably 20-80), starch (100), acrylic acid or its derivative (10-70, preferably 20-60), polymerization catalyst (0.5-2, preferably 1-1.5), and chain extender (1-20, preferably 2-15).    USE - As a hydrophilic slow release fertilizer used as carrier, where the fertilizer is nitrogen, phosphorus and potassium fertilizer, preferably urea, ammonium nitrate, potassium sulfate (claimed).    ADVANTAGE - The fertilizer improves plant growth; and is environmental friendly fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the fertilizer involving mixing wood powder, starch, additive, catalyst and chain extender in the reaction container; adding water, stirring, at 40-90 degrees C, for 5-4 hours to obtain the gel carrier; and concentrating the gel carrier in water solution for 10 days to obtain slow release fertilizer product.
NOVELTY - The method involves obtaining sludge reflux to a sample set, and obtaining data for reducing dimension number. A genetic algorithm-support vector regression (GA-SVR) hybrid algorithm is utilized to predict sludge. A control model of a sludge return-flow system is formed. Sludge reflux data is obtained by a sensor and a transducer. A selecting front covariance matrix is arranged according to a descending order to obtain a characteristic value and feature vector reconstruction matrix.    USE - Method for predicting principal component analysis (PCA) genetic algorithm-support vector regression (GA-SVR) sludge reflux quantity.    ADVANTAGE - The method effectively increases prediction precision with fast velocity of convergence and operation speed.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a principal component analysis genetic algorithm-support vector regression sludge reflux quantity predicting method. '(Drawing includes non-English language text)'
NOVELTY - Soil water retention agent comprises water hyacinth fragment, where the agent is prepared by screening, cleaning, drying and crushing the fragment hyacinth from water hyacinth.    USE - The soil water retention agent is useful as fertilizer (claimed).    ADVANTAGE - The soil water retention agent: is completely biodegradable and has no soil pollution; improves soil water content; and has strong water absorption property.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for use of soil water retention agent as fertilizer, where the application method comprises (a) planting the hyacinth fragment filled in ditch, (b) watering the planted fragment and then spraying fertilizer (50-70%) in the soil filled in the ditch, and (c) filling soil in a groove, sowing or transplanting and then spraying fertilizer (30-50%).
NOVELTY - The chamber has a hearth (2) that is arranged in a furnace main portion (1), and is provided with a tangential feeding port in upper end and a cooling air conveying pipe (7) in lower end. A dust cleaning door (8) is arranged in the surface of hearth. Two air inlets (9,10) are set on the outer wall of the upper end of the furnace main portion, and are connected with one end of inner wall of hearth. The other end of the hearth is connected with a cooling layer vent-pipe (11). The inner diameter of a furnace cover is larger than the diameter of furnace main portion and the hearth.    USE - Biomass fuel cracking chamber.    ADVANTAGE - The biomass fuel cracking efficiency of the cracking chamber can be improved, by reducing the discharge of smoke, so that the pollution to the environment can be prevented. The utilization rate of the biomass fuel cracking chamber can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass cracking chamber.    Furnace main portion (1)    Hearth (2)    Cooling air conveying pipe (7)    Dust cleaning door (8)    Air inlets (9,10)    Cooling layer vent-pipe (11)
NOVELTY - Procyanidine plant raw material or its extract, and tea polyphenol (5-100%) are added to an acid aqueous solution with a concentration of 1-20 wt.%, to prepare a 10-200 g/L mixed solution. The solution is reacted for 0.5-5 hours at 40-100 degrees C. The solution left after the reaction is absorbed using a polymeric adsorbent, washed with distilled water to remove impurities and then using 30-80 vol.% ethanol solution for elution. The eluant is concentrated and dried to obtain oligomeric proanthocyanidin.    USE - Preparation of oligomeric proanthocyanidin for use in foodstuffs, healthcare foods, drugs, cosmetics, daily chemicals, and animal feeds.    ADVANTAGE - The method provides high oligomeric proanthocyanidin content, low average degree of polymerization, high water solubility, and high recovery rate, and is environmentally-friendly, efficient, simple, convenient, economical, and suitable for large-scale industrial production.
NOVELTY - The method involves removing dusts from muncipal waste by a mechanical separation process, where the muncipal waste is sorted, crushed and dried to ensure mechanical segregation of small and medium waste fractions with size not less than 120 mm. The waste fractions are selected manually by a non-flammable material for recycling the harmful remaining waste by a magnetic separation process. Residual iron waste is crushed and dried in a gaseous medium for obtaining alternative fuel that are stored in a harvested container cargo.    USE - Method for obtaining alternative fuel from municipal waste.
NOVELTY - The method involves drying and packaging a base material i.e. municipal sewage sludge, in a pellet press (105) to form a cylinder whose diameter is specified in mms. The base material is dried to obtain granules with a fraction from 1 to 5 mm. The granules and worm pellets (103A, 103B) are moved to a screw feeder. The worm pellets are exposed to UV radiation that is originated from UV lamps (104A, 105B). The UV lamps are located above the screw feeder. The granules are subjected to a radiation dose of 3.6 watts per square meter for three seconds, where the granules are provided to the press.    USE - Method for producing fuel pellets.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram illustrating a method for producing fuel pellets.'(Drawing includes non-English language text)'    Worm pellets (103A, 103B)    UV lamps (104A, 105B)    Pellet press (105)
NOVELTY - The device has a fermentation chamber formed in a thermal ring, which is attached to a top cover. A bottom part of the thermal ring is hermetically embedded in a liquid annulus part, which is formed in a bottom cover. A truncated pyramid shaped container is mounted in an interior of the fermentation chamber. The container is arranged at a bottom part and an open top part. Side walls are provided with an openwork unit.    USE - Device for generating biogas from solid agricultural wastes i.e. manure.
NOVELTY - Liquid organic fertilizer formulations obtained by mixing of liquid organic fertilizer formulations made from human urine (30-40%), fish meal (3-4%), flour (2-3%), molasses (7-10%) and starter bacteria (20-25%), diluting the mixture with coconut water solvent (35-40%), where liquid organic fertilizer is obtained by stirring mixture of human urine, flour fish, rice flour, molasses and starter bacteria in the fermenter; checking temperature every time; measuring temperature every day; stirring once every 2 days; checking pH; and checking visible air bubbles that occur in a mixture.    USE - As liquid organic fertilizer formulations for plants (claimed).    ADVANTAGE - The formulation meets quality requirements; and enables to grow plant rapidly and is low in cost.    DETAILED DESCRIPTION - Liquid organic fertilizer formulations obtained by mixing of liquid organic fertilizer formulations made from human urine (30-40%), fish meal (3-4%), flour (2-3%), molasses (7-10%) and starter bacteria (20-25%), diluting the mixture with coconut water solvent (35-40%), where liquid organic fertilizer is obtained by stirring the mixture of human urine, flour fish, rice flour, molasses and starter bacteria in the fermenter (reactor) to mix homogeneously; checking temperature of the mixture every time; measuring the temperature every day; stirring the mixture once every 2 days; checking the pH; checking visible air bubbles that occur in the mixture; where when no air bubbles and temperature is stable, then fermentation occurs for 14 to 17 days, and the final liquid organic fertilizer contains (in a volume of 1 liter): nitrogen, potassium chloride (P2O5), potassium oxide (K2O), sulfate, iron (Fe), boron (B), cobalt (Co), copper (Cu), calcium (Ca), magnesium (Mg), manganese (Mn), molybdenum (Mo), zinc (Zn), and organic carbon.
NOVELTY - The infrared gas analyzer has a laser drive circuit connected to laser and intensity modulation circuit to tune laser. An optical system is connected with one end of laser whose other end is connected with infrared detector having main and reference detectors. The light emitted by laser is divided into two beams and transmitted to main and reference detectors. A data collection and display circuit is connected with phase-locked amplification circuit to display measured gas concentration.    USE - TDLAS WMS based infrared gas analyzer used for measuring concentration of hydrogen chloride, methane, carbon monoxide, carbon dioxide and water vapor in gas.    ADVANTAGE - The measuring efficiency and accuracy of the TDLAS WMS based infrared gas analyzer can be improved.
NOVELTY - The system comprises a garbage pre-processing unit (5), a micro-organism electrolytic cell (1) and a microbe fuel cell. The air outlet is set in micro-organism electrolytic cell vertical to spiral conveying device (10). The cathode of the electrolytic pool is located to encircle the pool wall. A spiral conveying device is provided with multiple anodes. The microbiological fuel cell is composed of an anode chamber and a cathode chamber of the double-chamber structure. The exchange films are separated by a proton.    USE - Hydrogen capturing system for treating kitchen garbage.    ADVANTAGE - The kitchen waste resource utilization can be improved effectively while recovering energy by using microorganism fuel battery. The clean energy hydrogen can be generated. The kitchen garbage can be treated effectively by using the system. The environment-friendly hydrogen capturing system can be obtained.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen capturing system for treating kitchen garbage.    Electrolytic cell (1)    Proton exchange membrane (2)    Garbage pre-processing unit (5)    Annular gas collecting port (9)    Spiral conveying device (10)
NOVELTY - Improving sludge anaerobic digestion, comprises performing semi-continuous anaerobic digestion process on the sludge and then introducing into a digestion tank, extracting digestion liquid from the digestion tank when the accumulated gas volume is reached to 70-90%, adding water soluble hydroxide to carry out cracking process, and adjusting the pH value of the solution to 7-8 after flowing into the digestion tank or directly into the digestion tank.    USE - The method is useful for improving anaerobic digestion of sludge (claimed).    ADVANTAGE - The method increases the sludge organic matter degradation rate, and improves the gas production rate of biogas through anaerobic digestion.
NOVELTY - Method for producing eco-friendly biofertilizer containing yogurt, involves mixing yogurt, dry-yeast, sugar, fermented soybeans, adding the mixture to warm water at 35-40 degrees C, fermenting the obtained mixture at 35-40 degrees C for 7-10 days, and adding and mixing cool water with the fermented product.    USE - The method is useful for producing eco-friendly biofertilizer containing yogurt (claimed).    ADVANTAGE - The method produces biofertilizer that does not contaminate the environment, and does not produce bad smell.
NOVELTY - Separation of triglyceride and free fatty acid contained in mixture of triglyceride and free fatty acid involves contacting mixture of triglyceride and free fatty acid contained in vegetable oil, acid oil, animal fat, recycled vegetable oil and fatty acid of raw palm oil with low-boiling aliphatic solvent and water under vigorous stirring.    USE - Separation of triglyceride and free fatty acid used for fuel for power generation plant and automobile.    ADVANTAGE - The renewable fuel is economically manufactured using the triglyceride and free fatty acid.
NOVELTY - Composter organic material placement equipment in rainwater catchment wells, where water can be drained from the top to spread out through the wall, essentially consists of a hollow shell (1), a handle sleeve, reinforced wellhead, funnel (5), filter cover (3) and a filter perforated base (2), where the hollow shell as a composter that comes up the wall sleeve on top of it and underneath is covered with a filter base, upper lip hollow shell is placed at the bottom of a wellhead amplifier (4), and a funnel above the wellhead amplifier which is locked to the filter cover.    USE - Used as composter organic material placement equipment in rainwater catchment wells.    ADVANTAGE - The composter organic material placement equipment reduces the cost of absorbing wells and the volume of organic material before being transported out of the yard.    DESCRIPTION OF DRAWING(S) - The figure shows an isometric view of the part of the composter infiltration wells.    Hollow shell (1)    Filter perforated base (2)    Filter cover (3)    Wellhead amplifier (4)    Funnel (5)
NOVELTY - The reactor (1) has a flexible bag (2) for collecting liquid biological material (3). The organic material is subjected to a fermentation process to obtain gas (4). A gas line (5) is connected with an electrical generator for discharging the gas. The bag is formed with an input part (7) for supplying the biological material into the bag. An output part (8) is utilized for removing the organic material from the bag. The input part and the output part are separated from each other. A heat exchanger is provided with the bag to warm up the material when the material is inserted into the bag.    USE - Biogas reactor.    ADVANTAGE - The flexible bag is large in size, so that the bag absorbs and carries large amount of organic material. The design of the bag avoids producing gas in a continuous manner and enables refreshing the biological material in the reactor. The reactor is simple to manufacture and avoids unwanted discharge of the gas. The reactor is provided with an insulation board that is simple to manufacture. The bag's support is improved by placing the bag against a part of circumference of a well. The reactor avoids increasing pressure using a pressure relief valve.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for manufacturing a biogas reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a biogas reactor.    Biogas reactor (1)    Flexible bag (2)    Liquid biological material (3)    Gas (4)    Gas line (5)    Input part (7)    Output part (8)
NOVELTY - Urea coated activated charcoal (UAA), is claimed, where the coated urea is present at 10-30 parts by weight.    USE - The UAA is useful as fertilizer and for increasing microbial populations such as Pseudomonas, Serratia, Sphaerotilus natans, Bacillus, Azotobacter, and Azospirrillium (claimed). No biological data given.    ADVANTAGE - The UAA is non-volatile, not easily vaporizable and leachable, and binds to pesticide residues, hence is eco-friendly and economical (saves up to 50% of cost of fertilizer usage).
NOVELTY - Method for producing chitin from shrimp waste using protease enzyme papain, involves washing and drying shrimp shells, demineralizing shrimp shells by soaking the washed shells in a solution of strong acid, washing the demineralized shell with water to neutralize the shells, drying the shells using oven or dryer cabinet for 8-12 hours, grinding the shell to a particle size of 20 meshes, subjecting the shells to deproteinization by soaking the shell in a solution of protease enzymes, filtering the solution and drying the obtained chitin.    USE - The method is useful for producing chitin from shrimp waste (claimed), used as base material for manufacturing chitosan used in food, biotechnology, cosmetics, health and agricultural industries.    ADVANTAGE - The method is simple, cost-effective and environmentally-friendly, requires less energy as heating process is not required, and employs enzymatic deproteination that is highly specific. The produced chitin is nontoxic and biodegradable, and has high molecular weight, high absorption capacity, bacteriostatic or fungicidal activity.    DETAILED DESCRIPTION - Method for producing chitin from shrimp waste using protease enzyme papain, involves (a) washing and drying shrimp shells in drying oven at 50 degrees C for 8-12 hours, (b) demineralizing shrimp shells by soaking the washed shells in a solution of strong acid, preferably hydrochloric acid at 75 degrees C for 4 hours, (c) washing the demineralized shell with water to neutralize the shells and drying the shells using oven or dryer cabinet for 8-12 hours, (d) grinding the shell to a particle size of 20 meshes, (e) subjecting the shells to deproteinization by soaking the shell in a solution of protease enzymes (15 weight/volume%), and (f) filtering the solution and drying the obtained chitin using an oven or dryer cabinet for 8-12 hours.
NOVELTY - Making flour pury of waste-mulberry pupae, using a waste or byproducts of spinning silk thread, includes selecting a pupae, cleaning, steaming, grinding, mixing the pupae with flour, drying and smoothing.    USE - The process is useful for making flour pury of waste-mulberry pupae (claimed), which is useful as a as food and medicine supplements. No biological data given.    ADVANTAGE - The process makes the waste-mulberry pupae in a simple, cost effective and eco-friendly manner.
NOVELTY - Making liquid organic fertilizer sludge material, comprises decomposing material with decomposer (stardec), extracting and pyrolyzing pulp fecal sludge.    USE - The method is useful for making liquid organic fertilizer sludge fecal material, which is useful for organic agricultural products.    ADVANTAGE - The liquid organic fertilizer products is free of Salmonellaand Escherichia coli hence it is safe and eco-friendly.
NOVELTY - Process for producing bioethanol gel using natural thickener for household fuel, involves (a) dissolving natural thickener in water, (b) stirring the solution to completely dissolve natural thickener in water, (c) mixing the natural thickener solution with bioethanol to obtain homogenous and clear bioethanol gel, and (d) stirring the mixture such that natural thickener solution is perfectly mixed with bioethanol and produces clear and homogenous gel having good parameter values.    USE - The process is useful for producing bioethanol gel, which is used as alternative fuel for household.    ADVANTAGE - The process produces bioethanol gel that is environmentally-friendly, biodegradable, and easy to handle, pack and store, does not spill, flow and evaporate, has high calorific value and low combustion residues, and replaces kerosene.
NOVELTY - Making ozonide biodiesel with special antifreeze specification from palm oil comprises using two-stage reactions including transesterification and ozonation in a fixed bed reactor.    USE - The method is useful for making ozonide biodiesel.    ADVANTAGE - The ozonide biodiesel produced by the method does not freeze easily.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for the ozonide biodiesel.
NOVELTY - The microbial consortium is obtained by agitating effluent in a single digestion unit, which comprises a single operational phase (anaerobic digestion).    USE - Microbial consortium for optimizing conversion of organic substrates.    ADVANTAGE - The microbial consortium efficiently inhibits recalcitrant or toxic substances that are represented in industrial effluents such as oil mills, and directly converts substrate in anti-agricultural and biofuel without using any dilution actions with water.
NOVELTY - Tool for bio-conversion of organic wastes into solid and liquid fertilizer using household kitchen mold, is claimed.    USE - The tool is useful for bio-conversion of organic wastes into solid and liquid fertilizer using household kitchen mold (claimed).    ADVANTAGE - The tool is small so it takes up little space and can be placed in the kitchen. The tool can be easily handled by any adult including domestic helpers. The method avoids the need for reversal of organic matter during the composting process. The tool converts organic wastes into solid and liquid fertilizer without causing a foul odor using a very simple procedure.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) mushrooms including fungus that occurs naturally or results from selection with high degradation ability; and    (2) a method comprising selection of the remaining organic material, chopping, laying pieces of organic material to form a uniform layer, and closing the layer of organic material with husk fuel, which is done every time with obtained remnants of organic materials, and every day continuously until finally the top compartment is fully charged, without reversal of organic matter during the composting process, in which liquid organic fertilizer can be harvested every day and solid organic fertilizer is harvested once for two weeks.
NOVELTY - Zoledronic acid is prepared by taking iminazole as raw material, performing N-alkylation and acidic hydrolysis on iminazole and ethyl chloroacetate in presence of phase transfer catalyst, reacting with phosphorus trichloride or phosphorus oxychloride in presence of 85% phosphoric acid and acidic catalyst under homogeneous phase state, hydrolyzing under acidic condition, and recrystallizing by distilled water.    USE - Preparation of zoledronic acid (claimed).    ADVANTAGE - Preparation of zoledronic acid avoids use of chlorobenzene which is harmful to human body and environment, simplifies operation, and has mild reaction conditions, low production cost, and high efficiency.
NOVELTY - A lignocellulosic material hydrolyzing method involves hydrolyzing a raw material such as straw, hay, silage corn or whole maize plant, to obtain a hydrolyzed product. The hydrolyzed product is ground and expanded to obtain a mixture followed by evaporating resultant mixture of water by causing a disruption of plant cell wall structure and treating resulting mash with an enzyme or sugar cellulose to obtain sweet mash. The sweet mash is cooled to yeast form at 32 degrees C after completing decomposition of cellulose. The cooled mash is subjected to alcoholic fermentation to obtain a finished product.    USE - Method for hydrolyzing lignocellulosic material for processing straw, hay, corn silage, whole crop corn and other similar materials.
NOVELTY - Preparation of dapoxetine, comprises e.g. carrying out carboxylation of acetophenone to obtain 3-oxo-3-phenylpropanoic acid (II), esterifying (II) to obtain methyl 3-oxo-3-phenylpropanoate (III), reacting (III) with hydroxylamine, then reducing and protecting with tert-butoxycarbonyl group, and performing condensation of obtained compound to obtain tert-butyl 3-(naphthalen-1-yloxy)-1-phenylpropylcarbamate (VII), then carrying out methylation of (VII) to obtain N,N-dimethyl-3-(naphthalen-1-yloxy)-1-phenylpropan-1-amine (VIII), and carrying out chiral resolution of (VIII).    USE - The method is useful for preparing dapoxetine.    ADVANTAGE - The method: does not use toxic and harmful reagent, and thus it reduces three wastes discharge; has simple operation, and improved product yield; is environment-friendly, and is suitable for large scale production.    DETAILED DESCRIPTION - Preparation of dapoxetine, comprises carrying out carboxylation of acetophenone to obtain 3-oxo-3-phenylpropanoic acid (II), carrying out esterification of (II) to obtain methyl 3-oxo-3-phenylpropanoate (III), reacting (III) with hydroxylamine to obtain (Z)-methyl 3-(hydroxyimino)-3-phenylpropanoate (IV), then reducing (IV) to obtain 3-amino-3-phenylpropan-1-ol (V), protecting (V) with tert-butoxycarbonyl (Boc) group to obtain tert-butyl 3-hydroxy-1-phenylpropylcarbamate (VI), performing condensation of (VI) to obtain tert-butyl 3-(naphthalen-1-yloxy)-1-phenylpropylcarbamate (VII), then carrying out methylation of (VII) to obtain N,N-dimethyl-3-(naphthalen-1-yloxy)-1-phenylpropan-1-amine (VIII), and carrying out chiral resolution of (VIII).
NOVELTY - Recovering para-toluenesulfonyl chloride from production wastewater of sulfonylurea herbicides, comprises adding acid to a solution containing tosylate to be acidized, performing decolorizing treatment, removing water, dissolving obtained para-toluenesulfonic acid in a polar solvent, and adding an acyl chlorination reagent at a certain temperature to react to obtain the paratoluenesulfonyl chloride.    USE - The method is useful for recovering para-toluenesulfonyl chloride from production wastewater of sulfonylurea herbicides.    ADVANTAGE - The method ensures economic recovery of the para-toluenesulfonyl chloride from production waste water on a large scale with high purity (more than 98%) and yield, and reduces Chemical Oxygen Demand content of the waste water.
NOVELTY - Separating an aqueous substrate into a concentrate and filtrate in a biogas plant (1), comprises filtering a liquid to be filtered from the substrate in a filter (7) having a substrate side (9) and a filtrate side (10), where filtering is carried out from the substrate side in the filtrate side. The pressure on the filtrate side is varied up to pressure equalization between the substrate- and the filtrate side.    USE - The method is useful for separating an aqueous substrate into a concentrate and filtrate in a biogas plant.    ADVANTAGE - The method allows separation of higher energetic solids from the substrate and balances the equilibrium of forces between the substrate and filtrate stream.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biogas plant for carrying out above mentioned method, comprising at least one biogas reactor (2), which comprises a filter, where a substrate line is arranged between the biogas reactor and filter, and a concentrate line is arranged between the filter and biogas reactor.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the method for separating aqueous substrate.    Biogas plant (1)    Biogas reactor (2)    Filter (7)    Substrate side (9)    Filtrate side (10)
NOVELTY - Thickener (1) for removing an aqueous portion of a thickened substrate by a warm or hot gas as a drying gas (7), which flows through drying gas together with the substrate in a thickening chamber (2) of the thickener, is claimed. The substrate is provided with an accelerating pump (15), through which the substrate can be inserted in the ventilated thickening chamber by at least one distributor device with drying air.    USE - The thickener is useful for removing an aqueous portion of a thickened substrate by a warm or hot gas as a drying gas, which flows through drying gas together with the substrate in a thickening chamber of the thickener, and for thickening manure or digestate from biogas plants or sewage sludge (claimed).    ADVANTAGE - The thickener ensures uniform drying in an economical manner, and utilizes waste heat and thus it is energy-efficient.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic side view of a thickener. (Drawing includes non-English language text).    Thickener (1)    Thickening chamber (2)    Drying gas (7)    Baffle plate (14)    Accelerating pump (15)
NOVELTY - Drive shaft (4) comprises areas for holding at least one stirring element (5), where the drive shaft is at least a hollow shaft and has a polygonal profile in cross-section of the same thickness.    USE - The polygonal profile is useful for the drive shaft which is used for a mixer (1) of biogas plants and for receiving stirring element (all claimed).    ADVANTAGE - The drive shaft distributes the resistance-moments of mixer symmetrically around the perimeter, and enables a positive drive shaft-hub connection, thus it ensures a permanent rotation.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic partial cross sectional view of a stirred tank exhibiting the use of mixer with the drive shaft.    Mixer (1)    Drive shaft (4)    Fixing elements (10)    Inner wall (11)    Outer wall (12)
NOVELTY - Preparing polypeptide containing L-glutamate, L-alanine, L-tyrosine and L-lysine by using circular dichroism as a guidance tool, comprises: polymerizing N-carboxyanhydride (NCA) derivatives of protected L-glutamate, L-alanine, optionally protected L-tyrosine, and protected L-lysine; optionally treating with acidic resin in suitable solvent; treating with base in suitable solvent with a suitable moisture content; adjusting pH by adding acetic acid; and isolating glatiramer acetate.    USE - The process is useful for preparing polypeptide containing L-glutamate, L-alanine, L-tyrosine and L-lysine by using circular dichroism as a guidance tool (claimed), where the polypeptide is used in treating multiple sclerosis. No biological data given.    ADVANTAGE - The process: is simple and easy to handle, operate and isolate in large scales production; utilizes acidic resin which is less hazardous and easy to handle and exhibits a better separation from the reaction mixture to any other reagents which are hydrogen bromide, or sulfuric acid for cleavage of the protected groups.
NOVELTY - Wastewater treatment equipment (1) has support tank (2) provided with microorganisms immobilization support, activated sludge tank (3), sedimentation tank (4), return-sludge line (5) which returns the sludge made to settle by the sedimentation tank to the activated sludge tank, and sand separator which carries out filtration of living organism in supernatant water separated by the sedimentation tank.    USE - The wastewater treatment equipment is useful for biochemically processing wastewater containing soluble organic substance, and purifying wastewater under aerobic conditions (all claimed) using microorganisms, preferably protozoa.    ADVANTAGE - The equipment stably provides high quality treated water, solves the problem of load fluctuation, utilizes microorganism with excellent biological activity, has excellent biological treatment property, and is reliable to use.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of wastewater treatment equipment useful for biochemically processing wastewater containing soluble organic substance, and purifying wastewater under aerobic condition.    Wastewater treatment equipment (1)    Support tank (2)    Activated sludge tank (3)    Sedimentation tank (4)    Return-sludge line (5)
NOVELTY - Biomass fuel in form of mixed particles is obtained by processing pruning branches and leaves of weed, tree and shrub of all biomass plant such as bamboo, sliver, bamboo grass and ivy into biomass, drying the biomass, pulverizing one portion of obtained product which is cause for bulkiness of biomass, and eliminating bulk component.    USE - Biomass fuel in form of mixed particles (claimed).    ADVANTAGE - The biomass fuel is economically prepared by simple method.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) biomass charcoal, which is obtained by carbonizing the biomass; and    (2) fine coal and powder mixing charcoal, which are pulverized to obtain the biomass charcoal.
NOVELTY - Biorefining comprises providing woody biomass, processing the woody biomass to provide a component streams, and producing derivative products from the component streams.    USE - The biorefining method is useful for producing value-added, biobased chemical products from the component streams from woody biomass.    ADVANTAGE - The method is simple and cost-effective.
NOVELTY - Method (M1) for biorefining, comprises: (a) providing agricultural biomass (10); (b) processing the agricultural biomass to provide many component streams; and (c) producing derivative products from the component streams.    USE - The method is useful for biorefining the agricultural biomass to produce derivative products comprising at least one of commodity chemicals, fine chemicals and specialty chemicals (all claimed).    ADVANTAGE - The method: facilitates recovering and recycling of chemicals; produces the energy by utilizing the waste product of the biomass (claimed), hence it is cost effective, and is easy to implement and use; and minimizes the production of waste product, as compared to conventional methods.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method (M2) for biorefining, comprising: the step (a) as above per se; processing the agricultural biomass to provide the component streams resulting in at least one waste product; and utilizing the waste product to produce energy.    DESCRIPTION OF DRAWING(S) - The figure shows a flow diagram representing the method of biorefining.    Agricultural biomass (10)    Mechanical processing (12)    Chemical processing (14)    Cellulose (26)    Lignin (34)
NOVELTY - Biorefining (M1) comprises: (a) providing cultivated plant biomass (10); (b) processing the cultivated plant biomass to provide many component streams; and (c) producing derivative products from the component streams.    USE - The method is useful for biorefining biomass to produce: derivative products comprising at least one of commodity chemicals, fine chemicals, or specialty chemicals; and energy comprising heat or power (all claimed).    ADVANTAGE - The method: minimizes waste product generation by generating many component streams which can be reused; and utilizes fewer chemicals by recovering at least 90% of the chemicals used in the process, thus are cost effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for biorefining, comprising: (a) as above per se; processing the cultivated plant biomass to provide many component streams resulting in at least one waste product; and utilizing the waste product to produce energy.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of the method of biorefining.    Cultivated plant biomass (10)    Mechanical processing (12)    Cellulose (26)    Lignin (34)    Hemicellulose (36)
NOVELTY - Method (M1) for biorefining, comprises: (a) providing a biomass (10); (b) processing the biomass to provide many component streams; and (c) producing derivative products from the component streams.    USE - The method is useful for biorefining the biomass to produce derivative products comprising at least one of commodity chemicals, fine chemicals or specialty chemicals (all claimed).    ADVANTAGE - The method: facilitates recovering and recycling of chemicals; produces the energy by utilizing the waste product of the biomass (claimed), hence it is cost effective, and is easy to implement and use; and minimizes the production of waste product, as compared to conventional methods.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method (M2) for biorefining, comprising: the step (a) as above per se; processing the biomass to provide component streams resulting in at least one waste product; and utilizing the waste product to produce energy.    DESCRIPTION OF DRAWING(S) - The figure illustrates a flow diagram for the biorefining method.    Biomass (10)    Mechanical processing (12)    Cellulose (26)    Lignin (34)    Hemicellulose (36)
NOVELTY - Method for producing biodiesel, involves using microalgae, preferably Oscillatoria sejongensis KNUA009 (KCTC 12034BP).    USE - The method is useful for producing biodiesel.    ADVANTAGE - The method enables to mass produce biodiesel rapidly.
NOVELTY - Compost depot device comprises mounting frame, trolley, fermentation composting tank, stirring unit, and wooden roof unit. The mounting frame is provided with trolley which is installed at the upper portion of the fermentation composting tank. The fermentation composting tank is provided to store organic waste. The stirring unit is provided at the bottom of the trolley for stirring organic waste. The wooden roof unit is provided at the one side of tank wall of the fermentation composting tank.    USE - The device is useful for composting and fermenting livestock farming excretion.    ADVANTAGE - The device is easy, economic and less labor intensive, and improves processing of organic waste material and compost.
NOVELTY - A hydrogen generation device comprises electrolyte layer (21), photocatalyst anode (22) which is formed on 1 side of electrolyte layer and contains photocatalyst particle (24), electronic conductor (25), and proton conductor (26), and hydrogen generation cathode (23) formed on another side of electrolyte layer. Electrolyte layer is used as solid polymer electrolyte membrane with proton conductivity.    USE - A hydrogen generation device for hydrogen production installation (claimed).    ADVANTAGE - Conduction of protons is effectively stimulated, therefore enabling efficient hydrogen production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for hydrogen production installation which is installed adjacent to power generation equipment for generating water vapor and contains hydrogen generation device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the electrode which is the principal part of the hydrogen generation device. (Drawing includes non-English language text).    Electrolyte layer (21)    Photocatalyst anode (22)    Hydrogen generation cathode (23)    Photocatalyst particle (24)    Electronic conductor (25)    Proton conductor (26)
NOVELTY - Method of preparing organic fertilizer, involves mixing sludge, peat, chicken manure and bean cake in a ratio of 5:1:2:1 to obtain powdered fertilizer, where the powdered fertilizer comprises 300 g/kg organic matter, 30 g/kg nitrogen, 20510 g/kg phosphorus and 2020 g/kg potassium.    USE - The method is useful for preparing organic fertilizer (claimed) which is used in rice plant, wheat plant and vegetables.    ADVANTAGE - The method processes large amount of sludge, provides high yield of plants, and changes the waste into treasure.
NOVELTY - The mold has a bio-degradable waste crusher, a waste conveying pipe, a blow-off pipe, a submersible pump and a diving pump that are connected with a planting system and a marsh gas tank through an irrigation pipeline. The diving pump is provided with a timer. The waste conveying pipe, the bio-degradable waste crusher and a bio-gas pool are connected with each other. The waste conveying pipe conveys bio-degradable waste to the bio-degradable waste crusher. The crushed bio-degradable waste is filled in the bio-gas pool. A drain pipe is connected with a waste water treatment system.    USE - Building window structure mold.    ADVANTAGE - The mold is environment-friendly, and can recycle bio-degradable resource, and reduces bio-degradable resource wastage.
NOVELTY - The oil tank temperature control system comprises an oil tank (14), a disk pipe, a pneumatic valve (15), a distributed control system (DCS) (11) and a steam coil pipe (13). The steam coil pipe is set with the oil tank. A steam outlet of the steam coil pipe is connected with a steam inlet pipe. The steam coil pipe is provided with a valve. The DCS control system is set with the oil tank and the pneumatic valve. The oil tank is provided with a temperature sensor (12). The steam coil pipe is stainless steel pipe.    USE - The oil tank temperature control system is useful in biodiesel production technology.    ADVANTAGE - The system controls the temperature at stable state during production of biodiesel to avoid pipeline blockage of the subsequent section, and has long service life.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of an oil tank temperature control system.    Distributed control system (11)    Temperature sensor (12)    Steam coil pipe (13)    Oil tank (14)    Pneumatic valve. (15)
NOVELTY - Watermelon tray matrix comprises decomposed pig manure, peat and vermiculite at ratio of 6:3:1, respectively. The tray matrix is prepared by adding, mixing and stirring with 2-3 kg of potassium sulfate compound fertilizer and 0.15-0.25 kg Effective Microorganisms.    USE - Watermelon tray matrix used for grafting seedling.    ADVANTAGE - The method uses low cost which improves economic benefit, saves land, produces high survival rate with excellent propagation and convenient transportation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the use method of watermelon tray matrix comprising preparing before seedling: preparing seedling growth, seeding, seedling bed management after sowing, seedling transplanting, seedling management (front survival of management and management and survival), controlling and removing lateral bud and customizing seeding seedling for 30-35 days.
NOVELTY - An organic fertilizer comprises livestock manure, shale, agricultural waste, leaves and municipal solid waste through yeast fermentation process. The yeast is Saccharomyces cerevisiae. The organic fertilizer further comprises 20-50% yeast, 1-2% brown sugar and 10-15% water.    USE - Organic fertilizer used to overcome soil compaction, inhibit disease and insect pest and expel activity of harmful bacteria (all claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of organic fertilizer comprising carrying out yeast fermentation to obtain expanded second generation bacteria on the crushed raw materials for 3-4 days and air drying or drying to obtain product.
NOVELTY - A method of producing organic fertilizer comprises spreading a layer of animal excrement and/or biogas slurry on the ground to form first layer; spreading a layer of crushed straw to form second layer; spreading a layer of animal excrement and/or biogas slurry on the straw to form third layer; and overlapping one layer to another. Biogas slurry comprises brown sugar and Effective Microorganisms (EM) solution.    USE - Method of producing organic fertilizer.    ADVANTAGE - The fertilizer has simple production process, low cost and excellent fertilizing effect.    DETAILED DESCRIPTION - A method of producing organic fertilizer comprises spreading a layer of animal excrement and/or biogas slurry on the ground to form first layer; spreading a layer of crushed straw to form second layer; spreading a layer of animal excrement and/or biogas slurry on the straw to form third layer; and overlapping one layer to another. Biogas slurry comprises brown sugar and Effective Microorganisms (EM) solution. The slurry is prepared by setting uniform flow of mixed liquid biogas solution with brown sugar at ratio of 200:1-2:1, carrying out fermentation for 1-15 days to red or white mycelium, keeping it wet and repeatedly pouring biogas liquid every 5-10 days, screening, drying, crushing and packing.
NOVELTY - Conversion of naturally occurring fats, glycerides, or oils to anionic surfactants and esters, involves trans-esterifying the glycerides with an alcohol; reacting the esters with an arylalkyl sulfonic acid; neutralizing the resulting sulfonic acid; and separating the resulting anionic surfactant from the un-reacted, unsaturated salts or esters.    USE - For converting naturally occurring fats, glycerides, or oils into anionic surfactants and esters (claimed) which are used in a variety of applications including in enhanced oil recovery, paper and pulp processing, mining, metal treating, adhesives, coatings, pesticide formulations, herbicide formulations, and fungicide formulations, and used as biodiesel fuel.    ADVANTAGE - The anionic surfactants and esters formed by the method reduces the amount of energy for cultivating, harvesting and converting agricultural crops into alcohol and esters, and for protecting from diseases.
NOVELTY - Nutrient fertilizer for Chinese herbal medicine selfheal comprises corn core powder (10-14%), bean cake powder (8-10%), broomcorn cake (4-6%), compound fertilizer (10-12%), wheat bran (6-8%), chicken (18-20%), dried goose manure (11-15%), wheat straw powder (2-4%), rapeseed straw powder (4-6%), oxalic acid (4-6%), procymidone (3-5%), bacteria (1-3%), and heavy calcium powder (1-3%).    USE - As a nutrient fertilizer for Chinese herbal medicine selfheal (claimed).    ADVANTAGE - The nutrient fertilizer has low cost. The preparation method is simple. The large amount of organic fertilizer produced by the nutrient fertilizer provides fast growth according to the self-heal. The nutrient fertilizer increases the yield; improves the ability to resist plant disease; and has no pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing nutrient fertilizer of Chinese herbal medicine selfheal involving combining the powders, putting them into the stirrer for stirring for 130 minutes, taking out and putting into a crusher to crush having particle size of 80 meshes, and then placing them in the mixer to stir for 130 minutes, pouring into a fermenting tank; adding to the stacked compact ferment, sewage water in 1:15 parts ratio and fermenting for 35 hours; turning lower layer over the upper layer; turning inner layer to the outer layer; again adding sewage water in a 1:15 proportion; compacting, stacking and fermenting for 35 hours; and putting into a 15 high, 15 wide and 10 long blocks to obtain the nutrient fertilizer.
NOVELTY - Transforming kitchen garbage into fertilizer, comprising mixing livestock manure, crop straw and kitchen garbage to obtain the mixture, and fermenting the mixture to obtain the fertilizer.    USE - The method is useful for transforming kitchen garbage into fertilizer (claimed).    ADVANTAGE - The method is capable of transforming the kitchen garbage into fertilizer with less energy consumption in an effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fertilizer prepared by method, where the fertilizer has a: germination index of more than 80%; electrical conductivity of 4 mS.cm-1; E4/E6 ratio of 3-6; water-soluble carbon (WSC) content of 4 g/kg; and carbon-nitrogen (CN) ratio of 10.5-13.5.
NOVELTY - A fertilizer comprises 5-10 wt.% nano-concentrated enzyme and 90-95% organic fertilizer. The nano-concentrated enzyme comprises 2-4 wt.% carbon, 1-3 wt.% silicon, 20-40 wt.% protease, 30-40 wt.% lignin, 20-40 wt.% soil enzyme, and 1-3 wt.% Bacillus subtilis.    USE - A fertilizer.    ADVANTAGE - The nano-concentrated enzyme enhances the absorption of fertilizer, improves the utilization ratio of fertilizer, increases bio-enzyme acting time in the soil, and improves utilization rate of the organic fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the fertilizer, comprising mixing an organic fertilizer and nano-concentrated enzyme including carbon, silicon, protease, lignin, soil, and B. subtilis; and extruding, granulating, and drying.
NOVELTY - Synthesizing vitamin E nicotinate comprises adding nicotinic acid into an organic solvent, adding triphosgene and tocopherol, adding (in dropwise) triethylamine, continuing the reaction to completion, adding water and rinsing, separating out organic solvent phase, washing organic solvent phase using sodium bicarbonate aqueous solution, vacuum recovering organic solvent to obtain a crude product, and refining the crude product to obtain the final product.    USE - The method is useful for synthesizing vitamin E nicotinate.    ADVANTAGE - The method: achieves crude product yield of about 95% and pure product yield of more than 90%; has simple operation process and high conversion rate and selectivity; ensures convenient recycling of the used solvent and auxiliary materials; utilizes easily available raw materials; is economical and environmentally friendly; reduces water emissions and three-waste pollution; and is suitable for industrial production.
NOVELTY - A gallic acid is prepared by orderly adding deionized water, 3.5-12 mass% hydrochloric acid and 8-123 mass% tannin-containing biomass into high-pressure reaction kettle, stirring, heating to 105-140 degrees C, and hydrolyzing for 0.5-6 hours; cooling product after crystallization solid-liquid separation, dissolving solid phase by hot water, decoloring by active carbon, recrystallizing, and vacuum drying to obtain gallic product; combining mother liquor, recycling hydrochloric acid through distillation and myrrh nutgall acid, and recycling hydrochloric acid for hydrolysis reaction.    USE - Method for preparing of gallic acid (claimed).    ADVANTAGE - The method is green and environmental, has high product yield rate and purity. It is also suitable for industrial production. The hydrochloric acid catalyst is recycled and does not produce wastewater.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating a preparation of gallic acid. (Drawing includes non-English language text).
NOVELTY - (E)-Ethyl 3-(5-(1-acetoxy-2-oxoethyl)-2,2-dimethyl-1,3-dioxolan-4-yl)acrylate (I) is new.    USE - (I) is useful for treating avian influenza (claimed).    ADVANTAGE - (I) has simple, economical and environmentally friendly preparation method with an average yield of 40%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing (I).
NOVELTY - A rice transplanting and seedling matrix comprises 20-100 pts.wt. crop processing residue or waste, and 0-80 pts.wt. crop straw. It is prepared by uniformly stirring crop processing residue or waste and crop straw; adding water; stacking, and covering using agricultural film; and increasing the temperature, naturally fermenting for 10-20 days, and fully curing.    USE - A rice transplanting and seedling matrix for rice transplanter (claimed).    ADVANTAGE - The rice transplanting and seedling matrix is inexpensive.
NOVELTY - Biological sludge is used to produce sludge dewatering granulator comprising dilute sludge washing process, organic rare sludge concentration and dehydration process and organic mud pelleting process. The dilute sludge washing process involves adding ferric trichloride agent, washing in dilute sludge, removing heavy metal and sand, and retaining for biological organic rare sludge concentrating and dehydrating, granulating, and obtaining produced organic fertilizer.    USE - Biological sludge used to produce sludge dewatering granulator (claimed).    ADVANTAGE - The method is simple, and environment-friendly.    DETAILED DESCRIPTION - Biological sludge is used to produce sludge dewatering granulator comprising dilute sludge washing process, organic rare sludge concentration and dehydration process and organic mud pelleting process. The dilute sludge washing process involves adding ferric trichloride agent, washing in dilute sludge, removing heavy metal and sand, and retaining for biological organic rare sludge concentrating and dehydrating, granulating, and obtaining produced organic fertilizer. The organic rare sludge concentrating and dehydrating the mud cake and organic granulation process comprises using screw extrusion sludge deep dehydration machine, concentrating, dewatering and pelletizing process for biological organic rare sludge, using screw extrusion type sludge dewatering machine, and utilizing machine bracket with sludge concentrating and dehydrating mechanism and granulating mechanism. The sludge concentrating and dehydrating mechanism comprises filter cylinder, screw rod and power transmission mechanism; and organic rare sludge flow into filter cartridge from filter cylinder at one end of organic rare sludge inlet, and screw rod and filter cylinder from filter cylinder mud extruded to other end.
NOVELTY - Alcohol-based fuel contains 80-85% methanol or ethanol as liquid fuel raw material, 2% additive as catalyst, and less than or equal to 18% water. Alcohol-based fuel is manufactured by mixing additive, alcohol, and water, stirring uniformly, leaving to stand for 4 hours, and sampling.    USE - Alcohol-based fuel used in hotel, restaurant, factory, school, and household.    ADVANTAGE - Alcohol-based fuel exhibits high heating value and high stability and is environmentally friendly and safe to use.
NOVELTY - The system has a filter (30) that is equipped with the exhaust frame to absorbing the organic waste flowed from reservoirs (10a,10b). A solid-liquid separator (40) separates the solid from liquid with the solubility organic compound (L) hydrolyzed in filter. An anaerobic digestion tub (50) stores the anaerobic digestion liquid form the separator. A gas holder (60) stores the biogas generated from the hydrolyzed liquid.    USE - System for producing biogas e.g. methane gas from livestock excretion, food waste and organic waste of animal and plant.    ADVANTAGE - The various concentrations of organic wastes can be hydrolyzed effectively. The moisture content in the organic waste can be hydrolyzed through the cyclic supply of the anaerobic digestion liquid. The biogas production efficiency of the system can be improved with high reliability.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the system for producing biogas. (Drawing includes non-English language text)    Reservoirs (10a,10b)    Filter (30)    Solid-liquid separator (40)    Anaerobic digestion tub (50)    Gas holder (60)    Solubility organic compound (L)
NOVELTY - The apparatus (2) has a hydrodesulfurizer (3) which removes the sulfur compound in a raw material and a heater (4) which heats hydrodesulfurizer. Hydrodesulfurizer is provided on the outer periphery of heater. Hydrodesulfurizer is equipped with several blocks (31) divided in circumferential direction so that the raw material passed through the inside of the block moves to next block. The hydrodesulfurizer is configured so that adjacent blocks communicate with each other and the directions of raw material flowing through adjacent blocks are opposite to each other.    USE - Hydrodesulfurization apparatus for hydrogen generating apparatus of fuel cell system (all claimed).    ADVANTAGE - Since the directions of the raw material flowing through the adjacent blocks are opposite to each other, the fall of catalyst temperature can be suppressed. Thus the utilization efficiency of the hydrodesulfurization catalyst can be improved. The flow path length can be shortened and the manufacture process can be simplified.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a hydrogen generating apparatus; and    (2) a fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows the perspective view and sectional view of the hydrodesulfurization apparatus. (Drawing includes non-English language text)    Hydrodesulfurization apparatus (2)    Hydrodesulfurizer (3)    Heater (4)    Blocks (31)    Communicating hole (302)
NOVELTY - The detector has a light guide (3) which induces light from a light emission unit (1) to a light-receiving unit (2) through a detection space (3a) for determining the state of preset gas. The light guide comprises a concave ellipse shaped reflective surface (6) which reflects the light radiated to inner surface of detection space. The focus position (P1) of light emission unit arranges opposingly to focus position (P2) of light-receiving unit, so that reflective surface makes long axis along straight line defined by light emission unit and light-receiving unit.    USE - Detector such as infrared type gas detector, for detecting kind of gases such as carbon monoxide and methane gases, for detecting concentration of carbon monoxide and methane gases, and for detecting smoke and dust contained in carbon monoxide and methane gases.    ADVANTAGE - The focus position of light emission unit arranges opposingly to focus position of light-receiving unit, so that reflective surface makes long axis along straight line defined by light emission unit and light-receiving unit, such that the correct transmittance -wavelength characteristic can be exhibited efficiently. The signal to noise ratio can be improved reliably. The reflection of the light in reflecting surface can be minimized.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the detector.    Light emission unit (1)    Light-receiving unit (2)    Light guide (3)    Detection space (3a)    Concave ellipse shaped reflective surface (6)    Focus positions (P1,P2)
NOVELTY - A catalyst composition comprises 85-95 wt.% porous support, 1-10 wt.% Group III A or VA elements, 1-20 wt.% Group VI B elements, and 0.01-10 wt.% Group VIII B elements.    USE - For conversion of vegetable oils to hydrocarbon products in the diesel boiling range (claimed).    ADVANTAGE - The process provides an improved catalyst and process for conversion of vegetable oils to diesel at high temperatures and high hydrogen pressures. The catalyst is efficient in full conversion of vegetable oils, and is able to retain the catalyst activity for longer durations and the products meet all requisite specifications to use as transportation fuels. The obtained hydrocarbon products have high cetane number, better fuel properties in the range of diesel and can be easily blended with diesel pool in various proportions.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparing a catalyst composition involving drying the porous support at 350-550 degrees C for four hours; depositing Group III A or VA elements and drying at room temperature for one hour; impregnating Group VIB elements and drying for ten to fourteen hours at 100-120 degrees C; impregnating Group VIIIB elements; drying at 90-110 degrees C for ten to fourteen hour; and calcining at 400-540 degrees C for four hours;    (2) process (p2) for conversion of vegetable oils to hydrocarbon products in the diesel boiling range using the catalyst composition or discarded refinery spent hydro-treating catalyst;    (3) hydrocarbon products in the diesel boiling range obtained using the catalyst composition.
NOVELTY - Treating industrial sewage using biological microbial inoculum comprising Rhodococcus sp. (25 wt.%), Bacillus subtilis (20 wt.%), copper green Pseudomonas (15 wt.%), Saccharomyces cerevisiae (10 wt.%), Nitrosomonas (10 wt.%), Bacillus megaterium (10 wt.%), Aspergillus niger (5%) and Paracoccus (5 wt.%), is claimed.    USE - The method is useful for treating industrial sewage using biological microbial inoculum (claimed), where the sewage includes high-concentration organic sewage and high ammonia-nitrogen waste water.    ADVANTAGE - The method ensures good degradation effect of toxic and harmful substances such as phenol, ammonia nitrogen and phosphorus.
NOVELTY - The machine has fermentation tank (51) that is provided with a feeding port (511) connected with a pressing device (30) of slag outlet (391) that is connected with the fermentation tank. The fermentation tank is provided with a temperature sensor that is connected with a heater and a temperature automatic control system. The heater is installed in the fermentation tank. A stirrer (52) is comprised of a second driver and a stirring screw propeller that is extended into the fermentation tank installed on the outside of the second driver.    USE - kitchen garbage recycling automatic processing machine in restaurant.    ADVANTAGE - The machine is featured with small volume, and can greatly shorten the composting time and improve the processing efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for automatically processing recycling of kitchen garbage.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the kitchen garbage recycling automatic processing machine.    Pressing device (30)    Fermentation tank (51)    Stirrer (52)    Slag outlet (391)    Feeding port (511)
NOVELTY - Bacterial strain, preferably Lactobacillus plantarum under a preservation number of CGMCC 6193, is new.    USE - The bacterial strain is useful for producing calcium lactate by fermenting cane molasses (claimed).    ADVANTAGE - The method produces calcium lactate with stable property in a simple culture medium and large scale fermentation. The cane molasses as carbon source used in the method can greatly reduce the production cost and realizes reclamation of the waste, it has important significance in effective utilization of resource and environmental protection.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing calcium lactate by fermenting cane molasses, comprising introducing the strain in culture medium at 30-50 degrees C and a pH value of 2-8, where the culture medium is Murashige and Skoog (MS) medium and yeast extract (YE) medium, and then fermenting using cane molasses (5-20%) as carbon source and carrying anaerobic fermentation at a speed of 10-200 revolutions per minute and a time of 20-240 hours.
NOVELTY - An anaerobic digester comprises: (a) a covered cylindrical tank; (b) in interior wall dividing the cylindrical tank into a ring shaped outer portion and a cylindrical inner portion; and (c) a passageway between the outer portion and the inner portion.    USE - The anaerobic digester and process are useful for digesting a substrate (all claimed); and for treating a high solids, stackable feedstock.    ADVANTAGE - The anaerobic digester is time efficient and can be operated in a thermophilic temperature range.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a process comprising: (a) feeding a substrate into a raceway; (b) partially digesting the substrate in the raceway; (c) transferring partially digested substrate from the raceway to a mixing tank; and (d) further digesting the partially digested substrate in the mixing tank.
NOVELTY - The apparatus (100) has a hydrogenation desulfurizer (1) that removes sulfur compounds in raw material. A reformer (2) generates hydrogen-containing gas by using raw material. A raw material supplier (3) supplies raw material to reformer. The ON/OFF valve (5) and pressure detector (6) are provided to recycle flow path (4). An abnormality detector (7) is arranged for detecting occlusion abnormality of recycle flow path on basis of detected pressure when raw material is supplied to reformer in a state where ON/OFF valve is closed.    USE - Hydrogen generating apparatus of fuel cell system.    ADVANTAGE - The abnormality in occlusion of the recycle flow path can be easily detected.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an operating method of hydrogen generating apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the hydrogen generating apparatus.    Hydrogenation desulfurizer (1)    Reformer (2)    Raw material supplier (3)    Recycle flow path (4)    ON/OFF valve (5)    Pressure detector (6)    Abnormality detector (7)    Hydrogen generating apparatus (100)
NOVELTY - Agricultural waste composting pre-treatment equipments system were developed, that consist of a sequence sets of a feed conveyor, a crusher with dehydrator and an output conveyor. First, to use the feed conveyor of agricultural waste to transport and screening treatment, followed to use the crusher with dehydrator of agricultural waste go for crush and dehydration, so that fragmentation of agricultural waste became into a size of less than 5 to 7 cm and moisture content below 60%wb of the organic fertilizer substrate materials, then re-use the output conveyor sent those organic fertilizer substrate materials into a rotary kiln-type main fermentation machine and a secondary vertical-type fermentation machine to go for fermentation operation. Let those organic fertilizer substrate materials could carry out follow-up of fermentation treatment, consistent and effective completion of agricultural waste treatment processes.
NOVELTY - A secondary vertical-type fermentation machine for composting of agricultural waste was developed. The system has a closed hollow chamber fermentation tank, a mixing device within the fermentation tank, an air blower pipe connected to the fermentation tank, and the temperature sensor and pH sensor located in the tank.. The invention utilized sealed with insulation and ventilation, mixing and drainage functions of secondary vertical-type fermentation machine, capable mixed pre-treatment of organic substrate and fermentation bacteria by appropriate ratio. Created a favorable environment for the growth of fermenting bacteria fermentation conditions, to ensure that the fermenting conduct of maturity, so that agricultural wastes could be efficiently decomposed into organic compost. And in the process, no odor, with a deep industry value in use.
NOVELTY - 1-(2-Benzyloxy-phenyl)-2-(3-methoxy-phenyl)-ethanol is dehydrated in the presence of acid dehydrating agent to obtain 1-(benzyloxy)-2-((Z)-2-(3-methoxyphenyl)vinyl)benzene. The obtained dehydrated compound is used to prepare sarpogrelate hydrochloride.    USE - Manufacture of sarpogrelate hydrochloride (claimed).    ADVANTAGE - The sarpogrelate hydrochloride with purity of more than 99% is manufacture with low energy consumption, reduced pollution, under mild reaction conditions and with high conversion rate and improved productivity.
NOVELTY - The bioreactor has a main body arranged with two flat plates (6) in parallel and vertical manners. A rectangular groove is formed between two sealing regions (1). Outer sides of upper and lower ends of one of the flat plates are provided with an air inlet (2) and an air outlet. The air inlet and the air outlet are respectively connected with two sealing regions that are respectively connected with a water outlet and a water inlet port. A flat membrane (5) and one of the sealing regions are fixed on a side of a layer of an active bio-film.    USE - Flat membrane bioreactor.    ADVANTAGE - The bioreactor avoids direct contact between waste gas and circulation active biological liquid so as to realize control residence time of a gas phase and a liquid phase. The bioreactor is convenient to use, and reduces secondary pollution.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a volatile organic waste gas purifying method    (2) a flat membrane bioreactor constructing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a flat membrane bioreactor.'(Drawing includes non-English language text)'    Sealing regions (1)    Air inlet (2)    Flat membrane (5)    Flat plates (6)
NOVELTY - Compound fertilizer is prepared by (a) immersing waste concrete in potassium solution, drying the obtained waste concrete, repeating the immersing step, drying the obtained concrete, making the concrete to absorb potassium fertilizer, and drying the concrete to obtain potassium-containing concrete, (b) mixing biogas fermentation product and diatomaceous earth slurry, and obtaining sticky mixture, and (c) adding the potassium-containing concrete to the sticky mixture, stirring the obtained mixture, and drying the obtained product to obtain finished product.    USE - The fertilizer is useful for sweet potato.    ADVANTAGE - The compound fertilizer contains large amount of nitrogen, phosphorus and potassium, and suitable quantity of amino acid, enzyme, amide, cytokinin and beneficial biological bacteria, provides complete nutritional components for sweet potato, and improves soil condition. The sweet potato cultivated using the compound fertilizer, has higher content of trace nutritional components and can meet dietary standard of modern people.    DETAILED DESCRIPTION - Compound fertilizer is prepared by (a) immersing waste concrete having particle size of 1-3 mm in potassium solution, drying the obtained waste concrete, repeating the immersing step, drying the obtained concrete, making the concrete to absorb potassium fertilizer, and drying the concrete to obtain potassium-containing concrete, (b) mixing biogas fermentation product and diatomaceous earth slurry, and obtaining sticky mixture, and (c) adding the potassium-containing concrete to the sticky mixture, stirring the obtained mixture, and drying the obtained product to obtain finished product, where the weight ratio of waste concrete, biogas fermentation product, diatomaceous earth slurry and potassium in the fertilizer.
NOVELTY - Polygonum cuspidatum raw material is placed in a steam stripper and frangula emodin is extracted using steam. Polygonum cuspidatum is contacted with steam, emodin is sublimated or volatilized, and the vapors are condensed and cooled to obtain a liquid at 40-90 degrees C. Liquefied emodin is layered in a separation tank, the upper layer is returned to the separation tank, and emodin the middle-lower layer is recrystallized and purified to obtain pure emodin.    USE - Extraction of emodin from Polygonum cuspidatum (claimed).    ADVANTAGE - The method is simple, economical and environmentally-friendly.
NOVELTY - The heater (1) has a hearth (11) provided with computer-executable instructions. A top plate (15) feeds biomass fuel to a feed mechanism to the hearth. The top plate is pivoted with a floating cover (152). An upper part of the top plate is provided with a signal collector (153) that is connected with the floating cover. The signal collector is provided with travel switches, micro switches, position proximity switches or Hall sensing element.    USE - Biomass fuel gasification heater for heating a cooker.    ADVANTAGE - The feeding mechanism stops working according to the signal collector so as to avoid climbing to the top of the body monitor feeding condition of the workers.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a biomass fuel gasification heater for heating a cooker.    Biomass fuel gasification heater (1)    Hearth (11)    Top plate (15)    Floating cover (152)    Signal collector (153)
NOVELTY - Composition comprises 65-75 wt.% of livestock manure, 10-25 wt.% of agricultural waste material, 1-10 wt.% of organic acid additive and 0.1-1 wt.% of strain, where the nitrogen ratio of the livestock manure and agricultural waste material is in the range of 24-32, and the water content is 48-65 wt.%.    USE - The composition is useful for planting blueberry (claimed) and as organic fertilizer.    ADVANTAGE - The composition prevents soil hardening, increases permeable performance and organic matter content of the soil, and promotes root growth.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing composition comprising adding livestock manure and agricultural waste material into fermentation groove for first day, adding yeast strain according to the proportion, turning the material using turning mechanism in the groove at a temperature of more than 65 degrees C, turning the sequence of material in third and fourth days and then fermenting at a temperature of 55-75 degrees C for 15-30 days, reducing the temperature, carrying out the ripening, adding the organic acid additive and then turning for 1-2 times after two weeks to two months, reducing the temperature to less than 45 degrees C, sieving the material to less than 30%, drying the material with water content of less than 30% and then crushing and sieving to remove impurity.
NOVELTY - Synthesizing biodiesel comprises plasticizing starfish lungs at high temperature, and reacting plasticized starfish lungs with alcohol to produce fatty acid.    USE - The method is useful for synthesizing biodiesel (claimed), which is useful as a heterogeneous system solid catalyzer.    ADVANTAGE - The biodiesel is simple to produce, and has increased yield.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic view of a batch synthesizer.
NOVELTY - The device has an oil-water separator provided with a water outlet and an oil outlet. The oil outlet is connected with a catalytic reforming tower that is connected with the water outlet and a sewage treatment pool. The sewage treatment pool is connected with a catalytic reforming tower through a gas-guide tube. The gas-guide tube is connected with a secondary condensing tower through the oil-water separator. A reaction kettle burning device unit is connected with the secondary condensing tower through the gas-guide tube of a combustion device unit.    USE - Organic urban waste fuel oil refining device.    ADVANTAGE - The device is simple in structure, convenient to use, and reducing the burden of urban waste.
NOVELTY - The device has a device main body provided with a pre-processing system, a primary gasification chamber, a secondary gasification chamber, a secondary de-acidifying system, a dust removing system and a synthesis gas utilization device. The secondary gasification chamber is fixedly connected with a plasma torch system.    USE - Plasma technology based household rubbish processing system integrated device for use in an internal combustion engine power generation field.    ADVANTAGE - The device reduces manual operation, realizes biomass fuel recycling effect and ensures better environmental protection, and has wide application range.
NOVELTY - Method for producing neoagarotetraose and neoagarohexaose, involves (a) reacting agarase derived from Streptomyces coelicolor with agarose or agar, or (b) obtaining extracellular agarase (DagA) protein encoded by S.coelicolor derived dagA gene comprising a 2397 base pair sequence (SEQ ID NO: 2) fully defined in the specification, and reacting the DagA protein with the agarose or agar.    USE - The method is useful for producing neoagarotetraose and neoagarohexaose (all claimed) used in foods, cosmetics and pharmaceuticals.    ADVANTAGE - The method enables efficient production of the neoagarotetraose and neoagarohexaose under optimum conditions, and obtained neoagarotetraose and neoagarohexaose are safe with respect to human body, as the neoagarotetraose and neoagarohexaose are produced by enzymatic method and not chemical method, hence the production method is environmentally-friendly also.
NOVELTY - Leaves and stems of corn, tobacco and Sorghum are crushed, sieved and heat-distilled. Water, methanol, and yeast powder are added to obtain a black or dark brown viscous liquid, which is reacted in reactor (I). The liquid is transferred to reactor (II), and sulfur, oxygen and nitrogen are added. The product is transferred to reactor (III) and sodium is added to produce sodium peroxide. The liquid is precipitated to obtain bio-gasoline upper layer, biodiesel as layer (II), small amount of wastewater as layer (III), and impurities as layer (IV).    USE - Mixed manufacture of green bio-gasoline and diesel oil (claimed).    ADVANTAGE - The method is simple, quick, economical and environmentally-friendly.    DETAILED DESCRIPTION - Corn, tobacco and Sorghum are planted at 4000-5000 trees/acre to a height of 80-100 cm. The plants are harvested before flowering and sealed tightly in a double-layer bag. The leaves and stems of all plants are crushed and sieved in a ratio of 1:1:1, and heat-distilled. Water, methanol, and yeast powder are added and temperature is controlled to 20-80 degrees C to obtain a black or dark brown viscous liquid with density slightly smaller than water, with no fixed melting point and boiling point. The liquid is supplied to 2-ton reactor (I) and reacted for 12 hours at 10 atm, stirring for 30 minutes after heating. The liquid is transferred to reactor (II) and reacted for 24 hours with addition of 1-5 kg sulfur, oxygen, and nitrogen. The product is transferred to reactor (III) and 97 g/l sodium is added. Sodium is reacted with oxygen to produce sodium peroxide. The liquid is precipitated to obtain bio-gasoline as upper layer, biodiesel as layer (II), small amount of wastewater as layer (III), and impurities as layer (IV).
NOVELTY - A sawdust particle fuel has sawdust, adhesive, and combustion improver, with weight ratio of 1000:5-6:3-4.    USE - A sawdust particle fuel (claimed).    ADVANTAGE - The manufacturing method is simple, and the obtained wood particle fuel has high flash point, low ash content and improved heat value and combustion rate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation method of sawdust particle fuel which involves (1) crushing wood after drying, and sieving using 4-20 meshes screen to obtain raw material, (2) mixing with adhesive and combustion improver according to weight ratio 1000:5-6:3-4 to obtain mixed material, and (3) granulating by extruding mixed material into granular fuel.
NOVELTY - A vehicle hydrogen machine comprises hydrogen generating unit, electrolysis water machine, filtering device, gas filter and vehicle storage battery generating unit for providing electric power. The hydrogen generating unit is provided with electrolysis chamber having electrolyte inlet that is connected with water storage unit which is fixed with positive polar plate and negative electrode plate. The negative electrode plate is provided with at least one voltage-dividing electrode adjacent the electrolysis sheet. The cell sheet is provided with gas barrier membrane.    USE - Vehicle hydrogen machine.    ADVANTAGE - The membrane can set proportion of hydrogen and oxygen according to the need so as to reach the best combustion-supporting effect, or to drain all the oxygen generated so as to avoid the interference of oxygen sensor. It is capable of controlling the injection for spraying oil so as to achieve the purpose of saving energy. The machine saves occupying space and pipeline, and is more beautiful.
NOVELTY - The device comprises a fan having blades for driving the rotor to cut the magnetic induction coil to generate an electromotive force in the stator output electric energy to generate the electric energy to the rectifying filter circuit. The boosted direct current power is sent to the electrolytic cell, which is used for electrolysis of water.    USE - Wind power water electrolysis device.    ADVANTAGE - The device is simple in structure and convenient in operation. The electric energy consumed can be reduced. The environmental protection of the device can be ensured.
NOVELTY - The solar electrolysis device has a solar photovoltaic plate that converts the solar energy into an electric energy. A rectifying filter circuit generates the direct current, and provides to a voltage booster circuit. The voltage booster circuit boosts the direct current power to an electrolytic cell which is provided for electrolysis of water. A rechargeable battery cell is provided for storing redundant electric energy.    USE - Solar electrolysis device.    ADVANTAGE - Since the voltage booster circuit boosts the direct current power to an electrolytic cell which is provided for electrolysis of water, the electric energy of solar electrolysis device can be reduced. The environmental protection function of solar electrolysis device can be improved. The structure of solar electrolysis device can be simplified. The solar electrolysis device can be operated conveniently.
NOVELTY - The hydroxide generator has a main machine that is provided with an outer shell and a reactor. The outer shell is connected with the reactor, and is filled with an electrolyte. The side wall of outer shell is provided with an annular pipe.    USE - Hydroxide generator.    ADVANTAGE - The heat generated by the electrolyte can be quickly discharged to the outside through the side wall of outer shell, so that the radiating effect of hydroxide generator can be improved. The occupied space and volume of hydroxide generator can be reduced, as the annular pipe is integrally made with the outer shell. Thus, the manufacturing process of hydroxide generator can be simplified. The manufacturing cost of hydroxide generator can be reduced. The hydroxide generator can be maintained conveniently and the structure of hydroxide generator can be simplified.
NOVELTY - Solar energy driven device comprises a reactor (4), a hydrogen collecting device (10) and a light source, and further comprises a solar energy battery (1). The reactor is provided with at least one reaction tank including at least one of photocatalytic electrode to pass through the solar battery power supply at the bottom of the reaction tank. The photocatalytic electrode is provided with a magnetic force stirrer (7).    USE - As solar energy driven device which is useful for photocatalysis degradation of organic pollutant to form hydrogen (claimed), where the organic pollutant include aromatic compounds and alcohols.    ADVANTAGE - The device is simple and compact equipment; easily controls various parameters; effectively utilizes photovoltaic cell system; does not need external power supply; reduces the energy consumption; and greatly improves the quantum efficiency and pollutant degradation rate of light.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for using solar energy driven device for producing hydrogen involving: subjecting waste water containing organic pollutant into reaction tank containing a visible light response type anode (5), hydrogen-producing electrode as cathode (6), and solar cell to provide voltage; irradiating the anode; magnetic force stirring the waste water in the reaction tank; and collecting the generated hydrogen.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of solar energy driven device.    Solar battery (1)    Storage battery (3)    Reactor (4)    Anode (5)    Cathode (6)    Magnetic force stirrer (7)    Anode lead (9)    Hydrogen collecting device (10)
NOVELTY - The device has a thermal-pressurized destructor mounted on a common frame that is connected with a dosing tank. A septic tank is provided with a combined heat and power generating device. The dosing tank is arranged in a lower part of a hatch.    USE - Micro-biogas producing device for small and medium-sized farms to produce electricity and heat.
NOVELTY - The bioreactor has a stand provided with a shell that is made of a light rays permeable material. A coating part is made of glass, plexiglass or ethylene tetra-fluoro ethylene foil that is provided with a spherical cap that is connected with a rim that is attached tightly to an inner side of a base that is connected with a bowl. A base is vertically mounted on a nozzle that is provided with slots. The nozzle is rotatably mounted with a drive. Outflow slits are arranged radially relative to center of the nozzle. A cup shell is connected with a reflector.    USE - Photo bioreactor for biomass production of algae.
NOVELTY - The reactor has a refrigerator positioned on a magnetic stirrer and coupled via a piston pump. An upper end of a reaction chamber is interconnected to an electro valve by a pipe to dispense tap water. The reaction chamber is provided with a pipe for discharging purified liquid with a peristaltic pump. A sensor of an upper liquid level sensor body and a conduit are utilized for evacuating excess sludge. The conduit is equipped with a solenoid valve, which is interconnected with a time controller. A programmable logic controller is utilized to control elements.    USE - Culture oxygen reactor for reacting granular activated sludge for biological wastewater treatment.
NOVELTY - The method involves heating pyrolysis gas with liquid at temperatures of 350-600 degrees Celsius at normal pressure about 1 bar in a pyrolysis reactor (4), where the pyrolysis gas is dissipated via a gas neck (6). Oxygen is added in an inert medium during heating to solidify the liquid at temperatures below 100 degrees Celsius. Biomass is deposited on a liquid surface through an auger (3) that is sucked down into the liquid with a stirrer (5).    USE - Pyrolysis gas producing method.    ADVANTAGE - The method ensures processing the transfer of energy to the biomass in a controlled oxygen-free environment with high energy transfer, high heat transfer capacity, short process and minimal particles in the gas phase.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a pyrolysis reactor.    Auger (3)    Pyrolysis reactor (4)    Stirrer (5)    Gas neck (6)
NOVELTY - Invention relates to agriculture. The method of processing dung wastes of pig-breeding complexes, which involves feeding phosphogypsum into a dung storage container and obtaining liquid decontaminated fertiliser, wherein phosphogypsum with pH 3.0-3.5 is added to liquid pig manure and humus is added 2-3 days after the sharp foul smell disappears. All components are taken in a defined ratio. The material is then mixed until a homogeneous mass is obtained and the substrate is held for 1-2 months.    USE - Chemistry.    ADVANTAGE - Invention enables to obtain liquid decontaminated fertiliser while reducing labour input and power consumption. 1 ex
NOVELTY - Invention relates to a method of producing 4-thioureidoiminomethyl pyridinium perchlorate, having high tuberculostatic activity by reacting 4-pyridinoaldehyde, perchloric acid and thiosemicarbazide in an aqueous medium, wherein thiosemicarbazide is added to the obtained 4-pyridine aldehyde perchlorate (concentration of 28-46%) in molar ratio 4-pyridine aldehyde: thiosemicarbazide: perchloric acid of 1:1:1.05. The technical result is a novel simple, practically feasible and ecologically clean single-reactor method of producing pharmacopoeial 4-thioureidoiminomethyl pyridinium perchlorate (PERCHLOZONE(R)).    USE - Chemistry.    ADVANTAGE - Process does not require power consumption, additional heating or cooling. 3 cl, 7 ex
NOVELTY - Biological organic fertilizer produced by chicken manure with water content of less than 30%, is claimed, where the chicken manure comprises cellulose-decomposing bacteria (0.3-0.5%), semi-decomposing bacteria (0.3-0.5%), protein decomposition bacteria (0.4%), organic phosphorus decomposing bacteria (0.3%), ammonifier (0.5%), photophosphorylation bacteria (0.3%), yeast (1%) and actinomycete (0.2%).    USE - The biological organic fertilizer is useful for crops such as food crops, commercial crops, vegetable crops, and melon and fruit crops.    ADVANTAGE - The biological organic fertilizer improves yield and quality of the agricultural products, and can be produced with high safety and without toxicity and environmental pollution.
NOVELTY - Coated slow-release fertilizer comprises 1-10 wt.% of hydroxymethyl cellulose, 5-15 wt.% of starch, 0.5-2 wt.% of composite catalyst, 0.1-0.5 wt.% of sodium sulfite, 10-30 wt.% of borax, 1-10 wt.% of polyacrylamide, 0.1-1 wt.% of hydrogen peroxide, 0.1-0.5 wt.% of sodium hydroxide, 0.1-0.5 wt.% of acid, 1-5 wt.% of gelatine and 52-58 wt.% of deionized water.    USE - Used as coated slow-release fertilizer.    ADVANTAGE - The coated slow-release fertilizer can prepared in an environment friendly manner, and does not pollute the soil and environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the coated slow-release fertilizer comprising adding the deionized water with the starch, uniformly stirring the mixture, adding hydrogen peroxide the mixture and reacting for 40 minutes, adding composite catalyst to the mixture, placing the mixture in ice for 30 minutes, raising the temperature to 65 degrees C, then oxidation reacting the mixture for 1.5 hours to obtain a reaction liquid, adding sodium sulfite in the reaction liquid, adding borax and carboxymethyl cellulose, stirring uniformly the solution, heating the solution at 80 degrees C for 40 minutes to make paste, adding sodium hydroxide into the reaction liquid and heating the liquid at 90 degrees C for 30 minutes to make paste, adding polyacrylamide to the reaction solution at 90 degrees C and reacting for 10 hours, adding hydrochloric acid in the reaction liquid, and regulating the pH value of the solution adjusted to 7-7.5 to obtain the final product.
NOVELTY - Producing biofuels involves utilizing byproducts obtained during production of bioethanol, sugar beet or other raw materials and then carbon dioxide is recovered by cultivating algae. Seeds oil is also utilized for producing biofuels, and feedstock are also utilized for performing pyrolysis for producing biofuels.    USE - Method for producing biofuels from bioethanol and byproducts obtained during production of bioethanol.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an industrial plant for producing biofuels.
NOVELTY - Reactor system has (i) a reactor (104) having an enclosed area comprising a catalyst slurry (106), an inlet for introducing biomass feed stream into the reactor, an inlet for introducing hydrogen gas to the reactor, cooling coils for controlling the temperature of the reactor to a target value and an outlet for the hydrocarbon product slurry, (ii) a heater to heat at least one of the biomass feed or the hydrogen gas before entering the reactor, and (iii) a separation device for separating catalyst slurry from hydrocarbon product present in the hydrocarbon product slurry.    USE - The reactor system is useful for producing hydrocarbons from biomass.    ADVANTAGE - The reactor system cost-effectively produces hydrocarbons with high concentration of even carbon number paraffins by single-step hydrogenation/hydrogenolysis of biological feedstock, and reduces thermal decarboxylation and consequent co-production of odd number paraffins.    DETAILED DESCRIPTION - Reactor system has (i) a reactor (104) having an enclosed area comprising a catalyst slurry (106), an inlet for introducing biomass feed stream into the reactor, an inlet for introducing hydrogen gas to the reactor, cooling coils for controlling the temperature of the reactor to a target value and an outlet for the hydrocarbon product slurry, (ii) a heater to heat at least one of the biomass feed or the hydrogen gas before entering the reactor, and (iii) a separation device for separating catalyst slurry from hydrocarbon product present in the hydrocarbon product slurry, where the hydrocarbons are produced from the biomass at the target temperature in the presence of the hydrogen gas and the catalyst slurry.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of reactor system producing hydrocarbons from biomass.    Pump (102)    Pressurized liquid stream (103)    Reactor (104)    Catalyst slurry (106)    Vapor product (107)    Air cooler (108)    Separator drum (110)
NOVELTY - Diesel fuel composition comprises a basic diesel and additives, where the basic diesel is composed of biodiesel, and the additive is an amide compound containing at least one phenolic hydroxy group and nitrogen-containing saturated heterocyclic group.    USE - Used as diesel fuel composition.    ADVANTAGE - The diesel fuel composition; utilizes pure biodiesel or biodiesel-containing diesel fuel as basic diesel; and has good oxidation stability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for improving oxidation stability of biodiesel, comprising adding the additive into biodiesel-containing basic diesel, where the additive is amide compound containing at least one phenolic hydroxy group and nitrogen-containing saturated heterocyclic group.
NOVELTY - An organic fertilizer, obtained by preparing a mixture of fertilizer base material, an organic conditioning agent and an estrogen degrading agent (1-5 wt.%), where the volume ratio of polypropylene resin to organic conditioner is 1:1-2.    USE - As organic fertilizer (claimed).    ADVANTAGE - The organic fertilizer is completely biodegradable, and improves the safety of the organic fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for composting method of estrogen in a degradation of livestock and poultry excrement, involving preparing fertilizer base material and organic conditioning agent according to 1:1-2 volume ratio of mixing, 2) adding the fertilizer base material 5% and the mixture of organic conditioning agent is 1-5% of total weight. The estrogen degradation oxidant, adequately mixing uniformly, carrying out composting, 3) composting stage, the ventilation control the stack temperature is not greater than 40 degrees C, and is maintained for at least 3 days, and then the ventilation, the stack temperature rise and is kept for 50-70 degrees C for at least 5-7 days, then increased ventilation, the stack temperature is reduced to 30-40 degrees C, and keeping stack temperature 3 days completely estrogen degradation, and then stacking the stack, 4) the stacking humidity is kept at 40% to 50% of prepared rhizome of rehmannia, 1-2 months.
NOVELTY - Method for sampling sugar, involves (a) preparing algal biomass, (b) pre-treating the algal biomass using ionic liquid, and (c) hydrolyzing the pre-treated biomass using acid catalyst.    USE - The method is useful for sampling sugar.
NOVELTY - Extracting flavonoids from camphor tree leaves, comprises (i) drying camphor leaves and immersing in ethanol, extracting alcohol-soluble substances by reflux heating, and filtering to obtain camphor tree leaf tincture; (ii) heating and distilling the tincture to recover ethanol, and obtaining camphor tree leaf extract; (iii) adding petroleum ether to the camphor tree leaf extract and stirring, and filtering to obtain filtrate and crude flavonoids; and (iv) drying crude flavonoids to obtain the finished product.    USE - The method is useful for extracting flavonoids from camphor tree leaves.    ADVANTAGE - The method: utilizes the industrial ethanol to extract flavonoids from the dried camphor tree leaves; is simple and suitable for industrial production; has low equipment requirement, high efficiency of extracting flavonoids, utilizes wide variety of camphor tree leaves source, and fully utilizes the resources, and reduces the flavonoids production cost.
NOVELTY - The system has lithium bromide heat absorption pump that is provided with condenser. The fractionating columns are provided to fractionate propylene. The bottom of primary fractionating column is provided with outlet through which distillate is flowed out. The outlet is interlinked with propane gas cooler through propane distillate pump. The lower portion of propane evaporation tank is connected with propane evaporation tank pump. A propane auxiliary condenser for fractionating propylene propane is connected with lower portion of primary fractionating column.    USE - Propylene-propane fractionation system used in oil refining industry.    ADVANTAGE - The waste heat resource can be effectively used and energy saving effect of the system is improved. The profit of the industry is improved and environmental protection is improved.
NOVELTY - Invention relates to recycling wood-plant wastes and peat and can be used in producing ecologically clean biofuels in form of active briquettes and granules (pellets) for industrial and domestic needs. The solid biofuel based on wood-plant components and/or peat additionally contains a combustion catalyst, with the following ratio of components, wt %: combustion catalyst 0.001-10; crushed wood-plant component and/or peat 100. The wood-plant components used are wood shavings, wood chips, bark, straw, chaff, seed husks, mill cake, stalks and leaves, waste paper, and the combustion catalyst is in form of inorganic derivatives of group I-II and VI-VIII metals.    USE - Chemistry.    ADVANTAGE - Obtaining ecologically clean biofuel. 3 cl, 2 tbl
NOVELTY - Mobile modular system for exploiting the energy from forest residues, at source, by generating liquid biofuel, comprises a drying unit; a pyrolysis unit; a condensation unit; a biofuel storage unit and a non-condensable gas storage unit; a fluidized bed gas preparation unit; an air preparation unit for the drying unit; a circulation and recycling system in operational communication with each one of the units; and a mechanical disassembly means.    USE - The mobile modular system is useful for exploiting the energy from forest residues, at source, by generating liquid biofuel (claimed).    ADVANTAGE - The mobile modular system is capable of removing forest residues and can access difficult terrain with high production capacity. It is profitable and environment-friendly.    DETAILED DESCRIPTION - Mobile modular system for exploiting the energy from forest residues, at source, by generating liquid biofuel, comprises a drying unit; a pyrolysis unit; a condensation unit; a biofuel storage unit and a non-condensable gas storage unit; a fluidized bed gas preparation unit; an air preparation unit for the drying unit; a circulation and recycling system in operational communication with each one of the units; and a mechanical disassembly means which enables the system selectively to adopt a transport configuration and an operating configuration; in which the system and each one of the components are mounted on at least one land vehicle; and in which also, in the transport configuration, the components are arranged in transport position; and, in the operating configuration, the components are operationally connected via a connection means to the circulation and recycling system, and all the elements are in operational position.
NOVELTY - A low sugar biomass apparatus comprises lignin decomposition apparatus (1) which decomposes lignin in cellulose biomass using ammonia, ammonia supply unit (3), recovery unit which recovers ammonia and lignin decomposition products in lignin decomposition apparatus, enzymatic-decomposition apparatus (4) which decomposes residue in lignin decomposition apparatus using an enzyme, and solid-acid-catalyst decomposition apparatus (5) which decomposes the decomposition product of enzymatic-decomposition apparatus into monosaccharide using solid acid catalyst.    USE - Low sugar biomass apparatus used for ethanol manufacturing apparatus (claimed).    ADVANTAGE - Biomass is decomposed into monosaccharide without degrading the solid acid catalyst while removing the lignin and improving the yield of monosaccharide.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an ethanol manufacturing apparatus (A).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the ethanol manufacturing-plant A. (Drawing includes non-English language text).    Lignin decomposition apparatus (1)    Pressurized hot water supply apparatus (2)    Ammonia supply unit (3)    Enzymatic-decomposition apparatus (4)    Solid-acid-catalyst decomposition apparatus (5)
NOVELTY - An air-pole-material of solid oxide fuel cell comprises material containing lanthanum-strontium manganate and cerium oxide.    USE - Air-pole-material used for manufacturing solid oxide fuel cell (claimed).    ADVANTAGE - Solid oxide fuel cell is manufactured efficiently. Mechanical strength and power generation characteristic are favorable.    DETAILED DESCRIPTION - An air-pole-material of solid oxide fuel cell comprises material containing lanthanum-strontium manganate of formula LaxSr1-xMnO3 and cerium oxide.    x=0-1.    INDEPENDENT CLAIMS are included for:    (1) solid oxide fuel cell comprising fuel electrode, solid electrolyte which is yttria stabilized zirconia (YSZ) and air electrode which is in contact with solid electrode without containing lanthanum zirconate (La2Zr2O7) or having 2nd order reaction phase in solid electrolyte interface including the lanthanum-strontium manganate; and    (2) manufacture of solid oxide fuel cell which involves baking and carrying out co-sintering of laminated body containing air-pole-material layer and solid electrolyte material layer.
NOVELTY - Preparing liquid fuel and chemical intermediates from biomass-derived oxygenated hydrocarbons, comprises reacting in a single reactor an aqueous solution of a biomass-derived, water-soluble oxygenated hydrocarbon reactant, in the presence of a catalyst comprising a metal e.g. chromium, manganese, iron, cobalt, nickel and copper, at a temperature, and a pressure, and for a time sufficient to yield a self-separating, three-phase product stream comprising a vapor phase, an organic phase comprising linear or cyclic mono-oxygenated hydrocarbons, and an aqueous phase.    USE - The method is useful for: preparing liquid fuel and chemical intermediates from biomass-derived oxygenated hydrocarbons; and producing liquid-phase organic compounds via catalytic processing of aqueous-phase biomass.    ADVANTAGE - The improved method is simple and more economical, and does not require multiple reactors and separation/purification steps between reactors.    DETAILED DESCRIPTION - Preparing liquid fuel and chemical intermediates from biomass-derived oxygenated hydrocarbons, comprises reacting in a single reactor an aqueous solution of a biomass-derived, water-soluble oxygenated hydrocarbon reactant, in the presence of a catalyst comprising a metal consisting of chromium, manganese, iron, cobalt, nickel, copper, molybdenum, technetium, ruthenium, rhodium, palladium, silver, tungsten, rhenium, osmium, iridium, platinum or gold, at a temperature, and a pressure, and for a time sufficient to yield a self-separating, three-phase product stream comprising a vapor phase, an organic phase comprising linear or cyclic mono-oxygenated hydrocarbons, and an aqueous phase.
NOVELTY - Carbonization system comprises drying machine (1) which dries waste material type biomass (2) to obtain made dry biomass (3), carbonization furnace (4) which heats and carbonizes dry biomass and produces carbonized material (5) and dry distilled gas (6), combustion furnace (11) which burns the dry distilled gas from the carbonization furnace, and produces combustion exhaust gas (13), and cooling mechanism for cooling introduced water vapor (9) or water into the carbonized material discharged from the carbonization furnace.    USE - The carbonization system is useful for processing waste material type biomass such as dewatered sludge and used for producing fuel.    ADVANTAGE - The carbonization system does not generate spontaneous ignition and an unpleasant odor.    DETAILED DESCRIPTION - Carbonization system comprises drying machine (1) which dries waste material type biomass (2) to obtain made dry biomass (3), carbonization furnace (4) which heats and carbonizes dry biomass and produces carbonized material (5) and dry distilled gas (6), combustion furnace (11) which burns the dry distilled gas from the carbonization furnace, and produces combustion exhaust gas (13), cooling mechanism for cooling introduced water vapor (9) or water into the carbonized material discharged from the carbonization furnace, where the carbonization system utilizes combustion exhaust gas which burned the dry distilled gas from carbonized waste material type biomass and emitted at the time of carbonization as heat source.    DESCRIPTION OF DRAWING(S) - The drawing shows explanatory drawing of the carbonization system.    Drying machine (1)    Waste material type biomass (2)    Dry biomass (3)    Carbonization furnace (4)    Carbonized material (5)
NOVELTY - The generator has a power source that provides electrical power to an electrolysis cell (13) provided with positive and negative electrode plates. The positive and negative electrode plates are respectively connected to positive and negative electrode support rods. A connecting unit is provided for electrically connecting support rods to power source. A fluid conduit unit is provided for conveying liquid electrolyte from reservoir (18) to electrolysis chamber, and for conveying hydrogen and oxygen gases from chamber. A cooling unit is provided for maintaining a constant temperature.    USE - Hydrogen generator for supplementing fuel in internal combustion engine.    ADVANTAGE - The fuel efficiency and performance of the internal combustion engine can be improved. The water can be effectively decomposed into hydrogen and oxygen. The O-ring is located on the surface of heat sink to prevent the moisture entering into the generator.    DESCRIPTION OF DRAWING(S) - The drawing shows an exploded perspective view of the hydrogen and oxygen generating assembly.    Housing (11)    Electrolysis cell (13)    Electronic regulator compartment (16)    Reservoir (18)    Cap (20)
NOVELTY - The 1-((2S)-2-benzyl-4-(1H-imidazol-1-yl)-4-oxobutanoyl)-1H-imidazole, (3aR,7aS)-octahydro-1H-isoindole and hydrogen chloride are reacted to obtain (S)-2-benzyl-1-imidazol-1-yl-4-(3aR,7aS)-octahydro-isoindol-2-yl-butan-1,4-dione. The (S)-2-benzyl-1-imidazol-1-yl-4-(3aR,7aS)-octahydro-isoindol-2-yl-butan-1,4-dione and mitiglinide alkali metal salt are reacted to obtain carbonyl group-containing compound (I). The carbonyl group-containing compound (I) is reacted with basic compound, or amine salt to obtain mitiglinide calcium salt.    USE - Manufacture of mitiglinide calcium salt used as diabetes drug.    ADVANTAGE - The mitiglinide calcium salt with high purity is efficiently manufactured with high yield by simple method within short period of time, without environmental pollution.    DETAILED DESCRIPTION - An imidazole group is introduced to 1C and 4C position of (2S)-2-benzylsuccinic acid to obtain 1-((2S)-2-benzyl-4-(1H-imidazol-1-yl)-4-oxobutanoyl)-1H-imidazole. The 1-((2S)-2-benzyl-4-(1H-imidazol-1-yl)-4-oxobutanoyl)-1H-imidazole, (3aR,7aS)-octahydro-1H-isoindole and hydrogen chloride are reacted to obtain (S)-2-benzyl-1-imidazol-1-yl-4-(3aR,7aS)-octahydro-isoindol-2-yl-butan-1,4-dione. The (S)-2-benzyl-1-imidazol-1-yl-4-(3aR,7aS)-octahydro-isoindol-2-yl-butan-1,4-dione and mitiglinide alkali metal salt are reacted to obtain carbonyl group-containing compound of formula (I). The carbonyl group-containing compound (I) is reacted with basic compound, or amine salt to obtain mitiglinide calcium salt.    A=alkali metal or NR1R2R3;    R1-R3=H, or 1-10C alkyl;and    or R1-R3+N=5-membered to 7-membered aliphatic heterocyclic ring or heterocyclic aromatic ring.    An INDEPENDENT CLAIM is included for (S)-2-benzyl-1-imidazol-1-yl-4-(3aR,7aS)-octahydro-isoindol-2-yl-butan-1,4-dione.
NOVELTY - Preparing composite biological bacteria fertilizer using multiple microorganisms, involves making functional strains by culturing microbes in aerobic culture, culturing probiotic strains by culturing microbes using deeply standing anaerobic culture method, and forming selenium-containing culture medium, and obtaining largest amount of living cells and metabolic products, where deodorized and harmlessly treated living sludge is taken as carrier.    USE - For preparing composite biological bacteria fertilizer (claimed).    ADVANTAGE - The obtained fertilizer has effectively stabilizing application effect; and properly selects treated living sludge as carrier, thus reduces cost and protects ecological environment.    DETAILED DESCRIPTION - Preparing composite biological bacteria fertilizer using multiple microorganisms, involves making functional strains by independently or dually culturing microbes having physiological property of fixing nitrogen, degrading phosphorus, degrading potassium, resisting insects, resisting diseases, and stimulating growth in the aerobic culture; culturing probiotic strains by culturing microbes using deeply standing anaerobic culture method, where the microbes are capable of producing multiple active enzymes and secondary metabolic products in biological activity, such as organic acid, small molecule peptide, vitamins and oligosaccharide substance; forming selenium-containing culture medium by using soy hydrolysate (10-50 g), peptone (4-10 g), sucrose (16-24 g), potassium hydrogen phosphate (KH2PO4) (3-8 g), magnesium sulfate (MgSO4) (1-6 g), selenium (10-100 parts per million) and water (1 liter); and obtaining largest amount of living cells and metabolic products using aerobic culture and anaerobic culture according to the physiological characteristics of strains, where deodorized and harmlessly treated living sludge is taken as carrier.
NOVELTY - Preparing composite microorganism fertilizer involves selecting culture medium formulation and culture condition of control and design according to the physiological characteristics of the strain are adopted the growth speed and different period, nutrient, microorganism at same environment; performing co-cultivation and concentration process to obtain high-concentration composite microorganism bacterial liquid; and adding active material with organic carrier to obtain composite microorganism fertilizer.    USE - For preparing composite microorganism fertilizer useful for improving crop nutrition, stress resistance, quality and yield of crop (claimed).    ADVANTAGE - The method prepares has improved production efficiency, and is greatly saves the production cost; prepares fertilizer that changes dressing fertilizer fundamentally caused by the negative, prevents fertilizer damage, injury and excessive dressing fertilizer caused by environment pollution; adjusts crop physiological process of strengthening the ability of plant immunity and having drought resistance and cold resistance, lodging, cropping, anti-dead, prevents plant diseases and insect pests.    DETAILED DESCRIPTION - Preparing composite microorganism fertilizer involves selecting culture medium formulation and culture condition of control and design according to the physiological characteristics of the strain are adopted the growth speed and different period, nutrient, microorganism such as Bacillus, lactic acid bacteria, yeast, acetic acid bacteria, nitrogen fixing bacteria, rhizobium at same environment; performing co-cultivation and concentration process to obtain high-concentration composite microorganism bacterial liquid; and adding active material such as organic acids, vitamins and solid nitrogen, phosphorus, potassium, with organic carrier such as humus soil, grass carbon, weathered coal to obtain composite microorganism fertilizer.
NOVELTY - A biological diesel oil comprises Cornus walteri as raw material.    USE - Biological diesel oil for fuel of diesel motor vehicle, turbine and turbine installation and aviation.    ADVANTAGE - The diesel oil has good quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a production of biological diesel oil which involves extracting plant hair oil and carrying out esterification reaction of C. walteri fruit into biodiesel.
NOVELTY - A device for efficiently producing methane comprises a rotatable methane forming container placed on conveyable base seat and provided with a rotary shaft and a cavity opening. Inner cavity of the container forms a methane generating chamber and provided with a double-spiral blade or a multi-spiral blade. The inner cavity opening is connected with flange cover. The flange cover has flange pipe and inner pipe. Second double-spiral blade naturally jointed with the first double-spiral blade is connected between inner wall surface of the flange pipe and outer wall surface of the inner pipe.    USE - Device for efficiently producing methane.    ADVANTAGE - Automatic feeding and discharging are realized by the forward/reverse rotation of spiral blades. Gas production speed is fast, and efficiency is high.
NOVELTY - A high purity potent composite alcohol group fuel comprises alcohol group which is composed of alcohol base main material which is distilled crude methanol, additive and alkaline pure water in 8:1:1 weight ratio.    USE - High purity potent composite alcohol group fuel for industrial and kitchen use.    ADVANTAGE - The fuel has stable performance, great value, low cost, no oil smoke and residual liquid and can be completely burned.
NOVELTY - Processing ultrasonic reaction of biomass refining technology, comprises (i) taking oil and alcohol in a molar ratio of 1:(1-40); (ii) dissolving a basic catalyst in the alcohol to obtain catalyst/alcohol mixed solution; (iii) adding the oil into an ultrasonic reaction container, starting a heater, and at the same time activating the ultrasonic vibration mechanism; (iv) using ultrasonic vibration, adding the catalyst/alcohol mixed solution into oil, heating, and carrying out esterification reaction to obtain a reaction product; and (v) separating the reaction product to obtain biodiesel.    USE - The method is useful for processing ultrasonic reaction of biomass refining technology.    ADVANTAGE - The method: utilizes ultrasonic physical vibration wave, which not only shortens the esterification reaction time, but also reduces the consumed energy of the reaction and production cost.    DETAILED DESCRIPTION - Processing ultrasonic reaction of biomass refining technology, comprises (i) taking oil and alcohol in a molar ratio of 1:(1-40); (ii) dissolving a basic catalyst in the alcohol to obtain catalyst/alcohol mixed solution, where the weight of the basic catalyst is 0.1-5% of the oil weight; (iii) adding the oil into an ultrasonic reaction container, starting a heater, and at the same time activating the ultrasonic vibration mechanism; (iv) using ultrasonic vibration, adding the catalyst/alcohol mixed solution into oil, heating at 20-100 degrees C, and carrying out esterification reaction to obtain a reaction product; and (v) separating the reaction product to obtain biodiesel.
NOVELTY - A nanometer carbon radical organic fertilizer comprises sulfate and organic fertilizer, where the fertilizer is fermented by antibiotic bacteria. The organic fertilizer is the fertilizer stack, make compost, or manure.    USE - As a nanometer carbon radical organic fertilizer (claimed, useful for treatment of plant disease including apple rot disease, sweet potato black spot disease, sclerotinia rot, rotten of seedling, and cotton in a hydrocarbon.    ADVANTAGE - The fertilizer is pollution-free organic fertilizer; promotes development of root system; and increases nutrient absorption and fast growth.
NOVELTY - A marsh gas collecting-generating system includes marsh gas pre-processing system having a dewatering tank and a desulfurization tank. Marsh gas collecting holes on top of garbage fermentation storehouse and sewage fermentation pool are connected with the dewatering tank. Drainage ditch is arranged at the bottom of the garbage fermentation storehouse and connected with the sewage fermentation pool. The desulfurization tank is connected with a water condensing tank that is connected with a marsh gas cabinet. The desulfurization tank is further connected with marsh gas generating set.    USE - Marsh gas collecting-generating system.    ADVANTAGE - The system can effectively utilize the marsh gas in the garbage, and reduces pollution caused by the garbage in the environment. Marsh gas utilization rate is enhanced and the energy waste is reduced.
NOVELTY - The solvent type whistle ultrasonic emulsifier has an upper inlet (1) and an outlet (7) that are arranged at ends of a shell. A resonance (5) is positioned in a middle portion of the shell. The ends of the shell are provided with a spring. The resonance and a reed (4) are integrated by a cover (6) is fixed on the shell. The plant oil and water-alcohol mixed solution are provided into an ultrasonic emulsifier casing to emulsify by a pressure pump.    USE - Solvent type whistle ultrasonic emulsifier for processing vegetable oil for diesel engine.    ADVANTAGE - The occurrences of environment pollution can be reduced. The structure of the ultrasonic emulsifier can be simplified and can be operated safely and reliably. The raw material usage can be reduced. The cost required for production of the ultrasonic emulsifier can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the whistle ultrasonic emulsifier. (Drawing includes non-English language text)    Upper inlet (1)    Reed (4)    Resonance (5)    Cover (6)    Outlet (7)
NOVELTY - Poultry anaerobic waste liquid ecological circulation process comprises anaerobic waste liquid passing through nitrogen (N), phosphorus (P) and chemical oxygen demand (CODCr) unit, absorbing heavy metal ion in absorbing water, entering into feed plant processing unit to feed plant to be absorbed, decomposing pollutant in anaerobic waste liquid, and producing feed plant growth for livestock and poultry feed.    USE - Method of poultry anaerobic waste liquid ecological circulation (claimed).    ADVANTAGE - The method has low cost of sewage treatment, and has zero pollution discharge.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the poultry anaerobic waste liquid ecological circulation process.
NOVELTY - The stove has a hearth (11) provided with a fire grate (13) at a bottom part. A water sealing dust collecting pool is located at a lower part of a body (1) corresponding to the fire grate, a water-sealed dust collecting tank (14) and the hearth.    USE - Biomass fuel gasification stove.    ADVANTAGE - The lower part of the body and the water-sealed dust collecting pool are connected to the lower part of the fire grate, so that the water seal is fixed for plugging water in a tan and the fire grate is connected with the body, thus preventing potential safety hazard.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a biomass fuel gasification stove in partial section.    Body (1)    Hearth (11)    Fire grate (13)    Water-sealed dust collecting tank (14)
NOVELTY - The sampler has an air cylinder provided with an upper cover and fixed with a piston via a bolt and a nut. The upper cover is connected with a base, a charging opening stop valve and an inflation cavity pressure gauge and formed with a nitrogen gas containing cavity. The nitrogen gas containing cavity is matched with the base. The base is equipped with a working cavity pressure gauge and an air inlet check valve that are matched with the nitrogen gas containing cavity.    USE - Self-piston type high-pressure balanced natural gas sampler.    ADVANTAGE - The sampler is simple in structure and convenient to operate and carry, and has high reliability, and improves gas detecting accuracy.
NOVELTY - A extreme thermophilic bacteria i.e. Calditerricola yamamurae strain UTM801 (CGMCC No. 6185), is new.    USE - The C.yamamurae is used in compost seed which is used for organic solid waste treatment (all claimed).    ADVANTAGE - The C.yamamurae enables effective organic solid waste treatment and recycling of energy. The compost seed significantly simplifies compost management, improves processing efficiency of the compost, shortens period of composting process and reduces compost processing cost.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) compost seed comprising the above-mentioned C.yamamurae; (2) method for preparing the above-mentioned compost seed, involves preparing fermented seed liquid of the C.yamamurae, and uniformly mixing the fermented seed liquid with compost material in presence adsorption agent, fermenting obtained mixture, drying and sieving fermented product; and (3) use of the above-mentioned compost seed in organic solid waste treatment.
NOVELTY - The device has raw material emulsion portion which is provided with a high speed cutting emulsifying machine. A gasification reaction portion is provided with a reaction kettle that is connected with the output port of emulsion solution input pipeline. A pre-heater is connected with a quartz tube gasification reactor that is arranged at the inlet of fluid dynamic type ultrasonic atomizing nozzle. A floater flow meter is connected to the ultrasonic atomizing nozzle. A drying tower is connected to high grade synthetic gas outlet.    USE - Device for preparing high grade synthesis gas by mixing bio-oil and hydrocarbon-containing raw material.    ADVANTAGE - The discharge of organic waste can be reduced effectively.
NOVELTY - A low-freezing biodiesel combined fuel comprise ethyl levulinate, methylfuroate, dibutyl carbonate, methyl oleate, solubilizing additive and flash point improver.    USE - A low-freezing biodiesel combined fuel.    ADVANTAGE - The fuel is prepared from biomass materials, simple in preparation technology, easy in separation and purification, and pollution-free in production process. It is low in cost, and environment-friendly and reproducible. The method of preparation can realize continuous operation with high preparation efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of low-freezing biodiesel combined fuel comprising (A) performing acid hydrolysis reaction to biomass raw material to obtain furfural and levulinic acid; (B) taking levulinic acid and ethanol to supercritical esterification reaction to obtain levulinic acid ethyl ester; (C) performing oxidation reaction between furfural and oxygen to obtain furoic; (D) reacting furoic with methanol to supercritical esterification reaction to obtain fatty acid methyl ester furfural; (E) performing ester exchange reaction to dimethyl carbonate and butanol to obtain dibutyl ester carbonate; and (F) mixing levulinic acid ethyl ester, acid methyl ester, carbonic acid butyl ester, methyl oleate, cosolvent and flash point improving agent to obtain low condensation bio-diesel fuel.
NOVELTY - Synthesizing vinpocetine comprises reacting (41S,12S,13aS)-methyl 13a-ethyl-12-hydroxy-2,3,41,5,6,12,13,13a-octahydro-1H-indolo(3,2,1-ij)pyrido(3,2,1-de)(1,5)naphthyridine-12-carboxylate with polyphosphoric acid/toluene, and reacting the (41S,13aS)-methyl 13a-ethyl-2,3,41,5,6,13a-hexahydro-1H-indolo(3,2,1-ij)pyrido(3,2,1-de)(1,5)naphthyridine-12-carboxylate with sodium ethoxide/ethyl alcohol for 12 hours to give (41S,12S,13aS)-methyl 13a-ethyl-12-hydroxy-2,3,41,5,6,12,13,13a-octahydro-1H-indolo(3,2,1-ij)pyrido(3,2,1-de)(1,5)naphthyridine-12-carboxylate.    USE - The vinpocetine is useful for treating ischemic brain disease, hypertension, cerebral arteriosclerosis, cerebral ischemia, cerebral vasospasm, cerebral artery, cerebral embolism, cerebral thrombosis, vertigo, aphasia and Meniere~s syndrome, and improving vision and memory.    ADVANTAGE - The method is capable of synthesizing the vinpocetine with high purity (99.5%) and less energy consumption in an environmentally friendly manner.    DETAILED DESCRIPTION - Synthesizing vinpocetine comprises reacting (41S,12S,13aS)-methyl 13a-ethyl-12-hydroxy-2,3,41,5,6,12,13,13a-octahydro-1H-indolo(3,2,1-ij)pyrido(3,2,1-de)(1,5)naphthyridine-12-carboxylate with polyphosphoric acid/toluene for 8 hours to give (41S,13aS)-methyl 13a-ethyl-2,3,41,5,6,13a-hexahydro-1H-indolo(3,2,1-ij)pyrido(3,2,1-de)(1,5)naphthyridine-12-carboxylate, and reacting the (41S,13aS)-methyl 13a-ethyl-2,3,41,5,6,13a-hexahydro-1H-indolo(3,2,1-ij)pyrido(3,2,1-de)(1,5)naphthyridine-12-carboxylate with sodium ethoxide/ethyl alcohol for 12 hours to give (41S,12S,13aS)-methyl 13a-ethyl-12-hydroxy-2,3,41,5,6,12,13,13a-octahydro-1H-indolo(3,2,1-ij)pyrido(3,2,1-de)(1,5)naphthyridine-12-carboxylate.
NOVELTY - A liquid manure of biomass is prepared by 1st process (S1) which obtains microorganisms carrying diatom shale which makes diatom shale carrying microorganisms, and 2nd process (S2) which obtains liquid product which stirs the mixture which contains microorganisms carrying diatom shale, biomass and water and passes through disintegration of biomass by the microorganisms.    USE - Preparation of liquid manure of biomass for liquid manure and microorganisms carrier (all claimed).    ADVANTAGE - Radioactive substance from biomass is removed or reduced.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) liquid manure comprising the liquid product obtained by 2nd process (S2); and    (2) microorganisms carrier comprising diatom shale which is dried after making diatom shale carry a microorganism-containing liquid.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the preparation of liquid manure of biomass. (Drawing includes non-English language text).    1st process (S1)    2nd process (S2)    3rd process (S3)
NOVELTY - A manufacturing machine of biomass fuel comprises basic structure which processes biomass fuel by performing dry carbonization of biomass centering on weeds.    USE - A manufacturing machine of biomass fuel (claimed).    ADVANTAGE - Production of biomass fuel is low cost, and manufacturing machine of biomass fuel is self-sufficient such that fuel and electric power produced are also consumed by the machine.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional diagram of a boiler part.    Combustion furnace (1)    Steam pipe (2)    Water tank (3)    Dry carbonization drum (4)    Heating chamber (5)
NOVELTY - A fuel cell module comprises a first electrode layer (30); an electrolytic layer (40) arranged on first electrode layer; a second electrode layer (60) arranged on electrolytic layer; and inter-connectors (50a), where at least one of the inter-connectors has first face contacting first electrode layer, second face opposing first face, and third and fourth faces connecting first face to second face, respectively, where at least a portion of inter-connectors also contacts electrolytic layer, where a length of first face of inter-connectors is 20-80% of a length of second face.    USE - As a fuel cell module having inter-connectors (claimed) used in solid oxide fuel cell for generating electrical energy.    ADVANTAGE - The fuel cell module improves a contact structure of the inter-connectors to prevent gas leaks, and improves the performance and the durability of the unit cell.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing a fuel cell module, involving forming a first electrode layer; laminating an electrolytic layer onto the first electrode layer; laminating a second electrode layer onto the electrolytic layer; and attaching inter-connectors, where a portion of the inter-connectors also contacts the electrolytic layer.    DESCRIPTION OF DRAWING(S) - The figure shows a sectional view of thickness direction schematically showing a unit cell structure of a solid oxide fuel cell (SOFC) module.    Unit cell (1)    First electrode layer (30)    Electrolytic layer (40)    Inter-connectors (50a)    Second electrode layer (60)
NOVELTY - The cell (1) has a porous central diaphragm (30) whose surfaces (32, 35) are in contact with an electrolyte (20) and a cathode (50). The electrolyte has material conducting M ions and the diaphragm has material conducting both M and N ions. Rectilinear channels (52) pass through the cathode and connected to the diaphragm and a free surface of the cathode. Minimum size of a cross-section of one of the channels is larger than 20 micrometers so as to enable a product i.e. water, from reaction of the ions to be discharged from the diaphragm to outside the cell through the channels.    USE - Fuel cell e.g. mixed conduction membrane fuel cell, for producing electric energy for stationary applications. Can also be used for long term onboard applications e.g. car.    ADVANTAGE - The minimum size of the cross-section of one of the channels is larger than 20 micrometers so as to enable the product resulting from reaction of the ions to be discharged from the diaphragm to outside the cell through the channels in an efficient manner, thus increasing power density of the fuel cell. The electrolyte and the central membrane are manufactured by using single operation e.g. sintering, so as to simplify manufacturing of the fuel cell and improve mechanical resistance and durability of the assembly.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic front sectional view of a fuel cell.    Fuel cell (1)    Electrolyte (20)    Porous central diaphragm (30)    Surfaces of porous central diaphragm (32, 35)    Cathode (50)    Rectilinear channels (52)
NOVELTY - Producing hydrocarbon compounds comprises: (a) generating power using a renewable energy generator; (b) cultivating, harvesting and drying algal biomass; and (c) generating hydrocarbon compounds from the algal biomass, where step (b) and/or step (c) utilize the power generated by the renewable energy generator.    USE - The method is useful for producing hydrocarbon compounds, and for generating biofuels, biodiesel, kerosene or naptha. The renewable energy source is useful for producing desalinated water, preferably by multi-effect desalination or reverse osmosis (all claimed).    ADVANTAGE - In producing hydrocarbon compounds, the main advantage algae have over other crops is its greater efficiency in using sunlight and consuming carbon dioxide (CO2) for photosynthesis, which results in much greater productivity per km2.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a plant for producing hydrocarbon compounds comprising a renewable energy generator; an algal biomass cultivator; an algal biomass harvester; an algal biomass dryer; and unit for generating hydrocarbon compounds from the algal biomass, in which the algal biomass cultivator, the algal biomass harvester, the algal biomass dryer and/or the unit for generating hydrocarbon compounds are arranged to utilize power generated by the renewable energy generator.