NOVELTY - The method involves generating carbonized material and pyrolysis gas by using pyrolytic-processing carbonaceous raw material. The generated pyrolysis gas by thermal decomposition furnace (1) is introduced into gas treatment equipment (2). A mixture with clinker is discharged from the lower portion of the thermal decomposition furnace. The crushed mixture is cooled, when carbonized material is selected and collected from the mixture discharged from thermal decomposition furnace.    USE - Method for processing carbonaceous raw material e.g. wood type biomass material, construction waste material, coppiced timber material, wood land surplus material, waste plastic material, waste tire material, sewage sludge material, general waste refuse material, paper manufacture waste material, lumber waste material, thinning lumber material, fuelwood forest material, agricultural type biomass material, livestock waste material and fishery type biomass material.    ADVANTAGE - The recovery processing amount of the carbonized material generated by the thermal decomposition furnace can be reduced. The bad effect of the clinker generated by thermal decomposition furnace can be reduced. The crushing efficiency of clinker can be improved. The size reduction and labor effort of the processing apparatus of carbonaceous raw material can be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for processing apparatus of carbonaceous raw material.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the processing apparatus of carbonaceous raw material. (Drawing includes non-English language text)    Thermal decomposition furnace (1)    Gas treatment equipment (2)    Reforming furnace (21)    Dust removal apparatus (25)    Chiller (33)
NOVELTY - Method for preprocessing biomass, involves immersing wood-type biomass in ionic liquid, performing ultrasonic irradiation to the immersed wood-type biomass, and removing the ionic liquid from the wood-type biomass after pre-processing.    USE - The method is useful for preprocessing biomass, preferably lignocellulosic biomass (all claimed) used for producing ethanol which is used as biofuel.    ADVANTAGE - The method improves saccharification reaction of wood-type biomass, without performing heating process.
NOVELTY - Herbal biomass is saccharified by pelletizing herbal biomass, treating pellet with alkali, and saccharifying solid content with enzyme.    USE - A saccharification method of herbal biomass for ethanol manufacture (claimed).    ADVANTAGE - Saccharification yield of hemicellulose and cellulose contained in herbal biomass is improved, and transport cost is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing method of ethanol which involves using herbal biomass, obtaining saccharide component by saccharifying solid content from alkali-treated herbal biomass with enzyme, and converting saccharide into ethanol using yeast.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of the manufacture of ethanol by applying saccharification method. (Drawing includes non-English language text).
NOVELTY - Device comprises processing container (2) for accommodating culture solution (X1) containing microalgae supplied from culture apparatus, nutrient salt addition unit (3) for adding nutrient salt to the culture solution accommodated in the processing container, and oil-component separation unit (4) to separate oil component from the processed liquid obtained by adding the nutrient salt to the culture solution.    USE - The device and method are useful for extracting oil component from microalgae, preferably Botryococcus braunii (all claimed). The oil component is biofuel.    ADVANTAGE - The device repeatedly utilizes culture solution containing microalgae without annihilating microalgae, is cost-effective, and does not produce cytoclasis by heating or pulverization during extraction process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for extracting oil component, involves adding the nutrient solution to the culture solution in the processing container, and separating oil component from the processed liquid.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of device.    Culture solution concentration unit (1)    Processing container (2)    Nutrient salt addition unit (3)    Oil-component separation unit (4)    Culture solution (X1)
NOVELTY - Apparatus comprises processing container (1) for accommodating microalgae, stimulation unit for accelerating external secretion of oil from microalgae, unit for supplying extract which extracts the oil secreted from microalgae to the processing container, first isolation unit for selectively isolating extract containing the oil from the container, and second isolation unit for selectively isolating the oil from the extract containing the oil component isolated by the first isolation unit.    USE - The apparatus is useful for separating oil components from microalgae, preferably Botryococcus braunii (all claimed) for producing biofuel.    ADVANTAGE - The method separates oil components from microalgae without annihilating the microalgae, and is cost-effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for separating oil from microalgae, which involves accelerating external secretion of oil component from microalgae, extracting oil component secreted from the microalgae by an extract, performing first separation process which selectively separates the extract containing oil component, and second separation process which selectively separates oil component from the extract containing the oil component separated by first separation process.    DESCRIPTION OF DRAWING(S) - The drawing shows a system configuration of biofuel manufacturing system. (Drawing includes non-English text).    Processing container (1)    Extract tank (2)    Extract feed pump (3)    Three-way valve (5)    Distillation apparatus (6)
NOVELTY - Preparing lignocellulosic biomass for enzymatic digestion, comprises: (a) providing lignocellulosic biomass; (b) mixing the lignocellulosic biomass with a 1-4% alkaline peroxide solution at a pH of 10-13 to form a slurry; (c) separating the slurry into a solid precipitate and a supernatant; (d) washing the solid precipitate to produce a neutralized solid precipitate; and (e) treating the neutralized solid precipitate with acidic electrolyzed water at a pH of 2-4 or alkaline electrolyzed water at a pH of 8-13 to prepare the lignocellulosic biomass for enzymatic digestion.    USE - The method is useful for preparing lignocellulosic biomass for enzymatic digestion (where: the lignocellulosic biomass is Miscanthus plant material (preferred), switchgrass, cord grass, rye grass, reed canary grass, common reed, wheat straw, barley straw, canola straw, oat straw, corn stover, soybean stover, oat hulls, Sorghum, rice hulls, sugar cane bagasse, corn fiber, distiller's dried grains with solubles, corncobs, pine, willow, aspen, poplar wood, or energy cane; and the enzyme is cellulase) (all claimed), which releases fermentable monosugars (including glucose and xylose), which are useful for biofuel production.    ADVANTAGE - The process: utilizes the hydrogen peroxide, thus improving the monosugar yield (95%); achieves lignocellulosic biomass digestibility of 95%; and is economical.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for hydrolyzing lignocellulosic biomass with an enzyme, comprising: the steps (a)-(e) as above per se to form an electrolyzed water-treated precipitate; and (f) hydrolyzing the electrolyzed water-treated precipitate with an enzyme.
NOVELTY - The system has gasification furnace, and air pre-heater. Crushed and dried biomass is preheated by air pre-heater to generate high temperature gas. Un-reacted residue is collected and fed to returning device. Dust is removed from high temperature gas through cyclone dust remover. High temperature smoke is discharged after air pre-heater and waste heat boiler respectively pre-heats air and generates steam. Biomass raw material is dried.    USE - Biomass gasification generating system.    ADVANTAGE - Since the dust is removed from high temperature gas through cyclone dust remover, wastage of energy can be avoided, and gasification system running stability can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the biomass gasification generating system.
NOVELTY - The photocathode has an anti-reflective density-graded surface without anti-reflective coatings, where the photocathode is fabricated by metal-assisted etching technique and comprises an array of nanowires, an array of nanopores, and hydrogen evolving catalyst such as platinum, nickel, molybdenum, zinc, copper, palladium, gold, iron and sulfur, adapted to reduce overpotential to create hydrogen more than about 100 mV. A buried p-n junction is determined to reduce overpotential to create hydrogen by about 500 mV.    USE - Nanoporous black silicon photocathode for hydrogen production from water splitting half-reaction, used as solar fuels.    ADVANTAGE - The photocathode ensures suppressing reflectance less than about 2 percent over a whole solar spectrum without application of any anti-reflective coatings to reduce over-potential to create hydrogen while promoting hydrogen gas evolution efficiently without sticking to the nonporous black silicon without usage of a surfactant, thus ensuring efficient hydrogen production while controlling effective surface area of the anti-reflective nano structure to optimize the balance between enhanced photo-limiting current and the reduced overpotential.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a device for producing hydrogen from water splitting half-reaction    (2) a method for producing hydrogen from water splitting half-reaction.    DESCRIPTION OF DRAWING(S) - The drawing shows a photograph of a nanostructure and optical reflectance of silicon photocathodes via a cross-sectional scanning electron microscopy image of nanoporous silicon fabricated by one-step metal-assisted etching process.
NOVELTY - Biocellulose aerosol comprises biocellulose powder, medicine composition liquid and/or active component solution, and propellant.    USE - Biocellulose aerosol used for promoting wound healing, continuously keeping the wound wet, protecting the wound, stopping bleeding, and sterilizing.    ADVANTAGE - The biocellulose aerosol is convenient to use and has high utilization rate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biocellulose aerosol comprising drying and crushing biocellulose into fine powder; at low temperature, mixing drug or active ingredients with water or organic solvent to prepare mixed solution or emulsion; at low temperature, adding biocellulose powder into the mixed solution or emulsion to prepare medicine composition liquid or active component solution; stirring uniformly; filling; and injecting propellant.
NOVELTY - Device comprises a crushing machine (1), a mixing machine (2), a sludge tank (3), a drying machine (6), a cooling machine (4) and a rolling molding machine. The first crushing machine and the sludge tank are connected with the mixing machine by a belt conveyor. The mixing machine is connected with the first drying machine by a belt conveyor. The first drying machine through a belt conveyer is connected with cooling machine. The cooling machine is connected with second drying machine by a belt conveyor. The first drying machine and second drying machine are connected with combustion furnace.    USE - The device is useful for producing biomass sludge synthetic carbon.    ADVANTAGE - The device ensures rapid and continuous production process, ensures mechanical operation and greatly improves the production efficiency.    DETAILED DESCRIPTION - Device comprises a crushing machine (1), a mixing machine (2), a sludge tank (3), a drying machine (6), a cooling machine (4) and a rolling molding machine. The first crushing machine and the sludge tank are connected with the mixing machine by a belt conveyor. The mixing machine is connected with the first drying machine by a belt conveyor. The first drying machine through a belt conveyer is connected with the cooling machine. The cooling machine is connected with the second drying machine by a belt conveyor. The first drying machine and the second drying machine are respectively connected with a combustion furnace to provide thermal air stream. The second drying machine is connected to the second crushing machine by a belt conveyor, and the second crushing machine is connected with the rolling molding machine by a belt conveyer.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the device for producing biomass sludge synthetic carbon.    Crushing machine (1)    Mixing machine (2)    Sludge tank (3)    Cooling machine (4)    Rolling molding machine (6)
NOVELTY - Domestic waste gasification furnace comprises a furnace substrate with a through hole arranged in the gasification furnace and used for dividing the gasification furnace into an upper part and a lower part, where the upper part is a gasification chamber, and the lower part is a motor chamber. The gasification chamber is divided into a gasification area and a high temperature area from top to bottom. A furnace wall on the upper part of the gasification area is connected with a feeder and a gas pipeline.    USE - Used as a domestic waste gasification furnace.    ADVANTAGE - The treatment method uses the furnace to achieve highly efficient, economical, energy saving, environmental friendly, renewable and recycling of the domestic waste.    DETAILED DESCRIPTION - Domestic waste gasification furnace comprises a furnace substrate with a through hole arranged in the gasification furnace and used for dividing the gasification furnace into an upper part and a lower part, where the upper part is a gasification chamber, and the lower part is a motor chamber. The gasification chamber is divided into a gasification area and a high temperature area from top to bottom. A furnace wall on the upper part of the gasification area is connected with a feeder and a gas pipeline. Blanking machines as rows are arranged between a cracking area and the high temperature area, and a turner is arranged in the high temperature area. The turner is fixed on a hollow rotary shaft with equal gap, and the hollow rotary shaft is connected with a vortex cylinder turbo in the motor chamber via a through hole in a center of the furnace. The vortex cylinder turbo is driven by the motor and gearbox operation, and the domestic waste gasification furnace further comprises a discharging device connected to the gasification furnace via the through hole of the furnace substrate.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of the domestic waste gasification furnace.
NOVELTY - Organic material rotten fungicide (I), is new, which is the composite microbial flora comprises Actinomycetes, Saccharomycetes, lactic acid bacteria, Bacillus and photosynthetic bacteria, and 0.05-0.1 billions per unit/g of active bacterium, where the Actinomycetes is 40-60%; the dosage form is powder; the particle size of the powder is less than or equal to 0.2 mm; the water content is less than or equal to 20%; the pH value is 5.5-7.5; and the Actinomycetes has liquor flavor.    USE - (I) is useful for producing soil-less culture.    ADVANTAGE - (I) is rapid, convenient, can be prepared with high yield and strong adaptability at a high temperature in a simple manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing (I) .
NOVELTY - The device has a valve which is fixed to base frame. A water atomizing tube is equipped with spraying nozzle (7). A water pump (4) is connected to water tank, so as to discharge water. A water shifter pipe (8) is connected to water shifter pipe (5) and sprays water in front of garbage falling down in conveyor belt (9) for garbage supply.    USE - Water spray device of combustible waste fuel rod manufacture apparatus.    ADVANTAGE - The quality of the combustible waste fuel rod can be enhanced. The combustible waste fuel rod can be manufactured with reduced cost and with simplified process. The durability of the combustible waste fuel rod can be improved effectively. The power consumption of the water spray device can be minimized effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the water spray device of combustible waste fuel rod manufacture apparatus.    Water pump (4)    Water shifter pipes (5,8)    Spraying nozzle (7)    Conveyor belt (9)
NOVELTY - A metal complex containing bidentate ligand and cyclic hydrocarbon compound, is new.    USE - As a catalyst, multi-electron catalyst, dye or as a pH indicator; in electrode comprising triple-junction solar cell or a tandem cell; and for splitting water into oxygen and protons, which are used to prepare hydrogen, a chemical component or carbon based fuel such as methanol, ethanol or formic acid (claimed).    ADVANTAGE - The complex exhibits improved catalytic properties. The complex is used as multi-electron catalyst that catalyzes the water splitting reaction at a high catalytic turnover number and turnover frequency. By using the catalyst the reaction can proceeds with moderate activation energy and low overpotential over wide pH range.    DETAILED DESCRIPTION - A metal complex containing bidentate ligand and cyclic hydrocarbon compound of formula ((BL)-(M')-(Ar')-(X))n+ (A')n- (I), is new.    M' = metal ion;    BL = bidentate ligand having two nitrogen atoms coordinating with a metal ion M';    Ar' = conjugated cyclic hydrocarbon compound (optionally substituted);    X = H2O;    A' = anion;    n = 1-5.    INDEPENDENT CLAIMS are included for the following:    (1) preparation of the compound (I);    (2) electrode linked to the complex (I); and    (3) splitting (M1) water into oxygen and protons by means of electrolysis involving using the complex (I).
NOVELTY - The processor has a display that is provided in left end of upper surface plate. A water inlet (4), an air outlet (5) and a water outlet are connected to de-odorizing tower (18) provided with active carbon outlet. The lower surface of front surface plate is provided with a sealing material outlet. The main frame is internally provided with a reaction cabin (13) which has mixing shaft (19). A material stirring shaft of mixing shaft is provided with a blade. A main plate is separately distributed at ends of blade. One end of blade is shorter than the other end contacted with stirring shaft.    USE - Organic waste processor.    ADVANTAGE - The waste and the decomposing bacteria are put into the reaction cabin of organic waste processor to react uniformly in the continuously stirring and constant-temperature process, thus the organic waste can be converted into the usable organic fertilizer effectively. The secondary pollution to the environment is avoided by the organic waste processor.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the organic waste processor.    Water inlet (4)    Air outlet (5)    Reaction cabin (13)    De-odorizing tower (18)    Mixing shaft (19)
NOVELTY - The gasifier (10) has gasification chamber (20) for gasifying rice husks provided with synthetic gas. The vent (45) of outside chamber (40) is collected through lower portion of grate (30) and ejected with discharging unit (50). The chaff layer installed at lower portion of gasification chamber is supported. The transfer pipe (70) is provided for transferring gas. The hopper (60) is produced between vent and transfer pipe of outside chamber with constant thickness.    USE - Ash discharge structure integrated rice husk gasifier.    ADVANTAGE - Since the hopper is produced between vent and transfer pipe of outside chamber with constant thickness, the occurrence of air inclusion can be prevented. Thus the damage and slag formation can be prevented. The inflow of the unwanted air can be blocked with the configuration of the hopper and the synthetic gas formation can be uniformly maintained.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the ash discharge structure integrated rice husk gasifier.    Rice husk gasifier (10)    Gasification chamber (20)    Grate (30)    Outside chamber (40)    Vent (45)    Discharging unit (50)    Hopper (60)    Transfer pipe (70)
NOVELTY - A non power air composting device has a fermenting chamber whose side wall is provided for feeding a side door (4), a support fermentation room and the fermenting chamber such that a bottom plate is placed away from the ground. A beam bottom plate (11) and a support seat of the fermentation cabin are formed by opening a movable turning plate of the fermenting chamber connected with a side door corresponding to a hinge that is parallel to an extending direction of a hinge ventilation inclined plate far away from an end part of the beam with a certain distance place through gemel.    USE - Non power air composting device for treating perishable organic substance of waste such as domestic garbage and garden garbage with kitchen waste mixture.    ADVANTAGE - The device has compact structure, small floor area, short fermentation period, high treatment efficiency, low energy consumption, and stable technical condition.    DETAILED DESCRIPTION - A non power air composting device has a draught pipe (1), top cover (3), fermenting chamber and a support saddle. A side wall of the fermenting chamber is provided for feeding a side door (4), a support fermentation room and the fermenting chamber such that a bottom plate is placed away from the ground. A beam bottom plate (11) and a support seat of the fermentation cabin are formed by opening a movable turning plate of the fermenting chamber connected with a side door of two adjacent side walls corresponding to a hinge that is parallel to an extending direction of a hinge ventilation inclined plate far away from an end part of the beam with a certain distance place through gemel.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a non power air composting device.    Draught pipe (1)    Top cover (3)    Side door (4)    Beam bottom plate (11)
NOVELTY - An organic waste decomposition process involves adding microorganism, a microorganism carrier and a microorganism activator to organic waste in a processing groove, stirring the organic waste, and supplying air through an air supply device, where the microorganism is chosen from synthetic bacteria from light, Bacillus bacteria, lactic acid bacteria and yeast.    USE - Process for decomposing organic waste.    ADVANTAGE - The process enables decomposing the organic waste in a short time.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an apparatus for decomposing organic waste.
NOVELTY - An organic fertilizer preparation method involves filtering human excrement slag using mesh screen (2-10 cm), and adding auxiliary material to prepare culture medium. A Chrysomya megacephala ovum is inoculated on a surface of the culture medium and cultured for 4-5 days at 25-35 degrees C. A culture material is collected, dried and prepared into organic fertilizer. The auxiliary material is feather powder, meal powder, sawdust and straw powder.    USE - Method for preparing organic fertilizer.    ADVANTAGE - The method enables preparing the organic fertilizer with strong processing ability and low energy consumption in an eco-friendly manner.
NOVELTY - An organic compound fertilizer comprises organic fertilizer, nitric acid, potassium nitrate, magnesium nitrate, ammonium nitrate, monopotassium phosphate, chelated iron, manganous sulfate, zinc sulfate, ammonium molybdate, ferrous sulfate, sodium molybdate, sodium selenite, humic acid, rare earth, filler, auxiliary agent, beneficial microbial colony, urea, plant ash and wheat bran, where the organic fertilizer is effective microorganism group, the auxiliary agent is mixture of duck manure and sheep manure, the beneficial microbial colony is attapulgite, and the filler is talcum powder.    USE - Organic compound fertilizer for cabbage.    ADVANTAGE - The fertilizer improves plant absorption utilization rate and performance of slow release of effective microbial flora through appropriate fermentation processing. The fertilizer is suitable for wide range of regions and all types of soil.    DETAILED DESCRIPTION - An organic compound fertilizer comprises (in weight parts) organic fertilizer (45-60), nitric acid (2-5), potassium nitrate (1-3.5), magnesium nitrate (1-2), ammonium nitrate (3-5), monopotassium phosphate (2-4), chelated iron (2-8), boric acid (3-4), manganous sulfate (1-1.5), zinc sulfate (0.5-1.5), copper sulfate (1-2.5), ammonium molybdate (3-6), potassium chloride (2-7), ferrous sulfate (1-3), sodium molybdate (1.5-4), sodium selenite (1-2), humic acid (3-6), rare earth (5-10), filler (4), auxiliary agent (3-11), beneficial microbial colony (2-5), urea (10-25), plant ash (5-10) and wheat bran (3-6), where the organic fertilizer is effective microorganism group, the auxiliary agent is mixture of duck manure, sheep manure, fermented dairy manure, earthworm and peanut cake, the beneficial microbial colony is attapulgite, and the filler is talcum powder, diatomite and white carbon black.
NOVELTY - A kitchen garbage processor has a long screw rod mechanism that comprises a screw rod cavity. A long screw rod is installed in the screw rod cavity. A motor drives the screw rod to move. An upper part of the screw rod cavity is provided with a blanking port and a feeding port. A lower part of the rod cavity is provided with a solid garbage outlet. A bottom part of the screw rod cavity is a filter structure. A storage device comprises a storage container whose bottom is provided with a heat preservation heater and a temperature sensor.    USE - Kitchen garbage processor.    ADVANTAGE - The processor is simple and convenient to operate and environment-friendly, and effectively realizes garbage recycling process.    DETAILED DESCRIPTION - A kitchen garbage processor has a blanking device, a crushing device and a storage device. The mixing device comprises a long screw rod mechanism and a ferment powder feeding device set above the long screw rod mechanism. The long screw rod mechanism comprises a screw rod cavity. A long screw rod is installed in the screw rod cavity. A motor drives the screw rod to move. An upper part of the screw rod cavity is provided with a blanking port and a feeding port. A lower part of the rod cavity is provided with a solid garbage outlet. A bottom part of the screw rod cavity is a filter structure. The storage device comprises a storage container whose bottom is provided with a heat preservation heater and a temperature sensor.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a kitchen garbage processor.'(Drawing includes non-English language text)'
NOVELTY - A farmyard manure composting method involves crushing (in kg parts) waste old cabbage leaf and root, celery roots (1) and leaves, vegetable seed or leaf (2), asparagus lettuce roots (2) and leaves, sweet potato (0.5), carrot (0.5), weed (30), compound fertilizer (100), and human excrement (10). Dry soil is added to the crushed product followed by uniform mixing. The obtained product is sealed using a plastic film for greater than three days for composting farmyard manure.    USE - Method for composting farmyard manure that is utilized as a farm base fertilizer.    ADVANTAGE - The method enables composting the farmyard manure in a simple and inexpensive manner, and utilizing the easily obtained raw materials. The farmyard manure has high fertilizer efficiency, and can grow seedlings and increase yield of seedlings.
NOVELTY - A rural marsh gas comprehensive utilization system has a raw material production device, a marsh gas ferment device and a marsh gas utilizing device, where the production device comprises a raw material generating apparatus (1). The marsh gas ferment device is provided with a hydraulic biogas pool (3). The marsh gas utilizing device comprises a kitchen (4) that is connected with the hydraulic marsh gas tank through an air guide pipe (36).    USE - Rural marsh gas comprehensive utilization system.    ADVANTAGE - The system is convenient to operate, and saves usage of marsh gas and ensures stable use of marsh gas in the kitchen. The system is reasonable in design and simple in structure, and saves energy and ensures environmental protection. The system is convenient to maintain and safe and reliable to use.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a rural marsh gas comprehensive utilization system.    Raw material generating apparatus (1)    Hydraulic biogas pool (3)    Kitchen (4)    Air guide pipe (36)
NOVELTY - An air distributing device has a ventilation pipe (6) formed with multiple air outlet holes (7). Each air outlet hole is formed corresponding to an air distributing groove (1) of the ventilation pipe. An outer wall of a supporting leg (3) is connected with the air distributing groove. The air distributing groove is filled with an air-permeable layer (4). An aerobic compost bed body (5) is placed to be parallel with the air distributing groove in inverted cone, inverted pyramid or pipe socket shapes.    USE - Air distributing device for use during aerobic composting of viscous organic waste.    ADVANTAGE - The device increases contact area of gas, and the pyramid material outlet holes ensure flow of the gas from the ventilation pipe at high speed to prevent deposition of material blockage, thus improving fertilizer efficiency, and reducing energy consumption through large diffusion, and hence reducing production and operation costs. The device is reasonable in structure, convenient to install and easy to operate.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of an air distributing device in partial section.    Air distributing groove (1)    Supporting leg (3)    Air-permeable layer (4)    Aerobic compost bed body (5)    Ventilation pipe (6)    Air outlet holes (7)
NOVELTY - A composite carbon fiber material comprises a carbon fiber material soaked with epoxy resin. Epoxy resin adhesive is adhered on carbon fiber. The carbon fiber material is cured initially. A high temperature-resistant material is formed on a carbon fiber layer with fireproof brush coating, high temperature heating, and chlorosilane and high-purity hydrogen. The chlorosilane is cracked with hydrogen chloride and silicon carbide. Silicon deposition high temperature-resistant material is formed on a silicon carbide layer with silicon carbide layer polyethylene resin and a bonding waterproof layer.    USE - Composite carbon fiber material for a biogas generating pit.    ADVANTAGE - The material prevents leakage and corrosion, and has prolonged service life. The material is inexpensive, and ensures energy-saving and environment-friendly effects.    DETAILED DESCRIPTION - A composite carbon fiber material comprises a carbon fiber material soaked with epoxy resin for 1-2 hours. Epoxy resin adhesive is adhered on carbon fiber along tension direction for keeping 5 degrees centigrade temperature during soaking process, where the relative humidity is more than 75%. The carbon fiber material is cured initially for 1-2 hours. A high temperature-resistant material is formed on a carbon fiber layer with fireproof brush coating, high temperature heating, and chlorosilane and high-purity hydrogen. The chlorosilane is cracked with hydrogen chloride and silicon carbide. Silicon deposition high temperature-resistant material is formed on a surface of a silicon carbide layer with silicon carbide layer polyethylene resin and a bonding waterproof layer.
NOVELTY - A plant growth regulator synthesizing method involves passing nitrogen or inert gas into a reaction system to protect easily oxidized raw material, carrying out furfural and glycol condensation reaction to water or benzene, and carrying out strong absorbing force balance reaction to a generated product after adding desiccant. Ethylene glycol and catalyst are separated from the generated product in a layering method.    USE - Method for synthesizing a plant growth regulator.    ADVANTAGE - The method enables synthesizing the plant growth regulator with simple operation, low production cost, low energy consumption, high yield, high sensitivity and high quality in an environment friendly manner.
NOVELTY - A special emulsifier preparing method involves dissolving sodium bicarbonate and acetone in warm water to obtain solution-I and dissolving potassium permanganate and hydroquinone in water to obtain solution-II. The solutions I and II are mixed and added with ethanol, which is kept static for use.    USE - Method for preparing special emulsifier.    ADVANTAGE - The method enables preparing special emulsifier with low energy consumption and simple, cost-effective and eco-friendly manner. The alcohol base fuel utilizing emulsifier has high thermal value.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a special emulsifier    (2) a alcohol base fuel    (3) a preparation method for alcohol base fuel.
NOVELTY - Treating artesunate mother liquor comprises: (a) extracting a mother liquor produced from dihydroartemisinin (10 kg) by using trichloromethane for three times; (b) adding succinic anhydride and triethylamine into the mother liquor, allowing to react, neutralizing and filtering; (c) concentrating the filtered reaction solution; (d) adding 20% methanol into the concentrated solvent-free solution, freezing, crystallizing, centrifuging and filtering; (e) refining with 80% methanol, freezing, crystallizing, centrifuging and filtering; and (f) vacuum-drying the refined product, and vacuum-packaging.    USE - The method is useful for treating artesunate mother liquor.    ADVANTAGE - The method adopts trichloromethane extraction and secondary reactions, and hence reduces pollution and waste, and increases the yield.    DETAILED DESCRIPTION - Treating artesunate mother liquor comprises: (a) extracting a mother liquor produced from dihydroartemisinin (10 kg) by using trichloromethane (120 l) for three times; (b) adding succinic anhydride and triethylamine into the mother liquor produced from dihydroartemisinin, allowing to react for 8 minutes at 27 degrees C, neutralizing with glacial acetic acid and filtering; (c) concentrating the filtered reaction solution in a water bath at 55 degrees C, to obtain a solvent-free solution; (d) adding 20% methanol (2 l) into the concentrated solvent-free solution, freezing and crystallizing, centrifuging and filtering to obtain coarse grains; (e) refining the coarse grains with 80% methanol at 65 degrees C to obtain a saturated solution, freezing and crystallizing, centrifuging and filtering; and (f) vacuum-drying the refined product for 2 hours at 55 degrees C, and vacuum-packaging.
NOVELTY - A micro-emulsified diesel oil comprises (in weight parts) biodiesel (90-91), compound emulsifier (1-2), water (9-10), ethanol (3-5) and carboxymethyl cellulose sodium (0.1-0.15).    USE - Micro-emulsified diesel oil.    ADVANTAGE - The oil has better stability, and no layering and breaking phenomenon. The smoke discharge of the oil is reduced by 25-50%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing micro-emulsified diesel oil.
NOVELTY - A bio-cathode microbial fuel cell has a cathode chamber comprising an aerobic cathode chamber and an anoxic cathode chamber, where fillers are filled in an anode chamber and the aerobic and anoxic cathode chambers. A cation exchange membrane is arranged between the anode chamber and the aerobic chamber. An anion exchange membrane is arranged between the anode chamber and the anoxic chamber. Two sides of the membranes are provided with a metal net. Two ends of the net are made to communicate via a guide line. A bottom part of the aerobic cathode chamber is provided with an aerating device.    USE - Bio-cathode microbial fuel cell for generating electricity for treatment of waste water i.e. nitrogen-containing organic waste water (all claimed).    ADVANTAGE - The cell removes nitrogen in an organic substance, and generates large amount of electricity.    DETAILED DESCRIPTION - A bio-cathode microbial fuel cell has a cathode chamber comprising an aerobic cathode chamber and an anoxic cathode chamber, where fillers are filled in an anode chamber, the aerobic and anoxic cathode chambers. Electrogenesis microbial films are loaded on the fillers, and a cation exchange membrane is arranged between the anode chamber and the aerobic chamber. An anion exchange membrane is arranged between the anode chamber and the anoxic chamber. Two sides of the exchange membranes are provided with a current collection metal net. Two ends of the net are made to communicate via a guide line, where a load is arranged on the guide line. A bottom part of the aerobic chamber is provided with an aerating device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of a bio-cathode microbial fuel cell.
NOVELTY - A alcohol-based liquefied gas is produced by mixing (in wt.%) methanol (80-85), ammonia water (0.3-0.35), copper sulfate (0.3-0.5), camphor or camphor powder (0.005-0.01), zinc oxide (0.3-0.5), active carbon (0.03-0.04), peroxyacetic acid 36-48 ml/100 kg, hydrogen peroxide solution 35-24 ml/100 kg, sodium (3-5) g/ 100 kg, potassium permanganate 2-4 g/100 kg, ferrocene 8-12 g/100 kg, benzene 40-60 g/100 kg and gasoline 500-600 ml/100 kg.    USE - Alcohol-based liquefied gas.    ADVANTAGE - The gas has better antiknock effect and high stability, and avoids corrosion effect in an inexpensive manner.
NOVELTY - Producing fuel from biomass, comprises: (a) torrefying biomass material at 80-300 degrees C to form particulated biomass having a mean average particle size of 1-1000 mu m; (b) mixing the particulated biomass with an organic liquid solvent to form a suspension, where the particulated biomass is present in the suspension at 1-40 wt.%; (c) feeding the suspension into a hydropyrolysis reactor; (d) feeding hydrogen into the hydropyrolysis reactor; and (e) converting at least a portion of the particulate biomass of the suspension into bio-oil at least at 300 degrees C, and a pressure of 1-200 atm.    USE - The process is useful for producing fuel form biomass (claimed), where the fuel is useful as gasoline, a feedstock for gasoline blending, diesel fuel, a basis for blending a diesel fuel, jet fuel, a basis for a jet fuel, and a feedstock for the petrochemical industry.    ADVANTAGE - The process: utilizes the torrefying step that enables the biomass material to be physically compatible with, or otherwise efficiently carried by the liquid; utilizes the step of hydropyrolyzing the biomass, thus producing bio-oil with higher heating value, low viscosity, higher chemical stability, and higher energy density; and produces the fuels with lower oxygen content.
NOVELTY - A biomass fuel production apparatus comprises biomass organic substance raw material which is molded into the apparatus to carry out moisture-content in which easy rotation of the flame, which makes air permeability favorable, is made circular.    USE - A biomass fuel production apparatus.    ADVANTAGE - The apparatus can be assembled and installed easily.
NOVELTY - The method involves molding a resin bond material with carbonaceous powder in a separator (2). A pre-forming body is obtained by a molding process. A side main surface of the separator is processes to maintain surface average roughness. The obtained pre-forming body is arranged in a cooling water flow path (4) such that ten-point average roughness is set less than 10 micrometers. A green sheet is obtained by a green-sheet-izing process. A thermosetting resin binding material and dispersing agent is dissolved in organic solvent with phenol resin curing agent to prepare binder resin liquid.    USE - Method for manufacturing a separator for a fuel cell.    ADVANTAGE - The obtained pre-forming body is arranged in the cooling water flow path such that ten-point average roughness is set to less than 10 micrometers so as to increase sealing performance and productivity of the separator.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of a fuel cell.    Polymer film (m)    Separator (2)    Cooling water flow path (4)
NOVELTY - The system (1) has a fuel gas supply part i.e. hydrogen generator (4), supplying fuel gas to a fuel cell (2). An oxidizing agent supply part i.e. air blower (13), supplies oxidizing agent gas to the fuel cell. A supply flow path (14) connects the agent supply part and the fuel cell. A discharge flow path (15) discharges the oxidizing agent gas from the fuel cell. An oxidizing agent supply valve (17) opens and closes the supply flow path. An oxidizing agent exhaust valve (18) opens and closes the discharge flow path. A control part (20) stops supply of the oxidizing agent gas to the fuel cell.    USE - Fuel cell e.g. polymer electrolyte fuel cell and solid oxide fuel cell, system for use in a home and a business field.    ADVANTAGE - The oxidizing agent exhaust valve opens and closes the discharge flow path. The control part stops supply of the oxidizing agent gas to the fuel cell, so that the system can detect failure of the oxidizing agent exhaust valve and the oxidizing agent exhaust valve in a reliable manner, thus improving reliability of the fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a fuel cell system.'(Drawing includes non-English language text)'    Fuel cell system (1)    Fuel cell (2)    Hydrogen generator (4)    Air blower (13)    Supply flow path (14)    Discharge flow path (15)    Oxidizing agent supply valve (17)    Oxidizing agent exhaust valve (18)    Control part (20)
NOVELTY - The method involves sintering anode (20) on support element (10). The sintering of lower surface of anode is carried out before the sintering of upper surface of anode.    USE - Method for manufacturing fuel cell.    ADVANTAGE - The sintering of lower surface of anode is carried out before the sintering of upper surface of anode, so that peeling of the support element from anode can be suppressed.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view illustrating the anode formation process.(Drawing includes non-English language text)    Support element (10)    Hole (11)    Anode (20)    Anode constituent material (21)    Anode pre-sintering portion (22)
NOVELTY - The method involves joining one end of carbon nanotube to polymer electrolyte element. The temperature of catalyst support carbon nanotube is maintained to temperature (T1) lower than the glass transition temperature of ionomer. The gas diffusion layer is pre-heated to temperature (T2) higher than glass transition temperature of ionomer. The other end of carbon nanotube is joined to a gas diffusion layer.    USE - Method for manufacturing fuel cell.    ADVANTAGE - The fall of electro-conductive between catalyst layer and gas diffusion layer can be suppressed effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view illustrating the process for manufacturing fuel cell.(Drawing includes non-English language text)    Temperature (T1,T2)
NOVELTY - Fermented liquor circulation type methane fermentation method, involves adding organic solid waste which comprises light weight foreign matter into raw material tank, supplying fermented liquor, maintaining liquid level, solubilizing the waste material, circulating the waste material, and discharging the waste material.    USE - Fermented liquor circulation type methane fermentation method.    ADVANTAGE - The method has excellent stability.    DETAILED DESCRIPTION - Fermented liquor circulation type methane fermentation method, involves adding organic solid waste which comprises light weight foreign matter into raw material tank (9) comprising movable rake (60) and screw conveyer (70) of surrounding wall penetration at predetermined height, supplying fermented liquor (S) to the raw material tank, maintaining liquid level in predetermined height by circulation which extracts the fermented liquor of a raw material tank in a downward direction and returns the liquor in upwards direction, solubilizing the waste material in the raw material tank which is immersed in a fermented liquor, where the waste material decomposes into biogas, circulating the waste material with the fermented liquor, bringing together the light weight foreign substance which floats on the liquid level of the raw material tank in a screw conveyer by movement of the rake, and discharging the foreign substance. An INDEPENDENT CLAIM is included for fermented liquor circulation type methane fermentation apparatus (1).    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of the fermented liquor circulation type methane fermentation apparatus.    Fermented liquor circulation type methane fermentation apparatus (1)    Crushing apparatus (2)    Raw material hopper (7)    Raw material tank (9)    Movable rake (60)    Screw conveyer (70)    Fermented liquor (S)
NOVELTY - The method involves measuring temperature of gas collected from gap of stored refuse-derived fuel (1), to determine occurrence or non-occurrence of heat generation. The gas sampling openings (7a-7d) are formed in several places of refuse-derived fuel storage apparatus (20), for performing suction collection of gas in gap, and for indicating position of gas sampling opening. The gas sampling is stopped and nitrogen gas is injected into indicated place of heat generation of fuel as coolant gas (9), when the heat generation place of fuel is indicated, to cool the refuse-derived fuel.    USE - Heat-generation monitoring and cooling method of refuse-derived fuel fed to boiler.    ADVANTAGE - The monitoring of heat generation and facilitation of discharge of residual-derived fuel are attained, without inserting an obstruction with respect to discharge of refuse-derived fuel, so that the thermal storage and heat generation of refuse-derived fuel are prevented efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the refuse-derived fuel storage apparatus.    Refuse-derived fuel (1)    Floor surface (2)    Gas sampling pipe (3)    Measurement control apparatus (5)    Side wall (6)    Gas sampling openings (7a-7d)    Coolant gas (9)    Refuse-derived fuel storage apparatus (20)
NOVELTY - A dry distillation system comprises kiln body, where top part of the kiln body is provided with combustible gas outlet. Kiln body is provided with disk type smoke heating tube which is connected with burner on the outside of kiln body. Combustible gas outlet is connected with purifying device via a pipe. Purifying device is connected with the generator set. Disk smoke heating tube is installed in disk groove. Upper part of disk groove is covered with a steel radiating grid. One end of disk smoke heating tube is connected with burner.    USE - Dry distillation system for agricultural and forestry waste charcoal and gas.    ADVANTAGE - The system has high charcoal yield and short making period, and increases temperature of smoke in kiln tube via effective heat exchange of smoke and air. It has high refining temperature and big charcoal density and yield. The dry distilled combustible gas is purified to eliminate harmful substance in the environment. The obtained combustible gas can be used for generating power and heating. Vinegar solution and tar are extracted as raw materials of the other industries. The system does not have pollution in production process and fully utilizes the resources.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating a dry distillation system.
NOVELTY - The furnace has an air guide pipe (2) arranged on a furnace body (1). An end of an oxygen pipe is connected to an inner cavity of the furnace body. A fuel gas processing cylinder (5) is arranged on a side wall of the furnace body. A hanger rod and the oxygen pipe are staggered on the fuel gas processing cylinder. A lower end of an air duct is connected with the fuel gas processing cylinder. An air outlet pipe (6) is arranged on the fuel gas processing cylinder. A gas-water separator (4) is arranged on the air guide pipe.    USE - Biomass gasification furnace for a tar cracking low row efficient opposed purifying device in a home and an industry.    ADVANTAGE - The device ensures stable gasification furnace combustion and satisfies requirements of a user.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a biomass gasification furnace.    Furnace body (1)    Air guide pipe (2)    Gas-water separator (4)    Fuel gas processing cylinder (5)    Air outlet pipe (6)
NOVELTY - An adsorber assembly (10) comprises adsorber (18) and housing (22) extending between inlet and outlet. The housing is configured to communicate a reformate gas through at least a portion of the adsorber. The adsorber includes a material coating chosen from cerium oxide, rare-earth oxide and manganese oxide. The material coating having predetermined thickness is configured to react with hydrogen sulfide throughout the thickness.    USE - Adsorber assembly is used for fuel cell adsorber arrangement used for conditioning reformate gas stream (all claimed).    ADVANTAGE - The absorber assembly has high sintering activity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) fuel cell adsorber arrangement; and    (2) method for conditioning a reformate gas stream.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of fuel cell adsorber arrangement.    Adsorber assembly (10)    Reformer (14)    Adsorber (18)    Housing (22)    Inlet gas stream (26)
NOVELTY - Producing pyrolysis oil product from biomass comprises: subjecting biomass feedstock to thermal treatment in reactor (I) under torrefaction reaction condition to produce torrefied biomass feedstock; pyrolyzing torrefied biomass feedstock in reactor (II) under pyrolysis reaction condition, where torrefaction reaction conditions includes temperature of 180-350 degrees C, pressure of 11-500 psia and residence time of 1 minute to 24 hours and pyrolysis reaction conditions includes temperature of 375-700 degrees C, pressure of 0.1-1000 psia, residence time of 0.1-200 second and has total acid number of 80-200.    USE - The process is useful for producing pyrolysis oil product from biomass, where the biomass is wood, paper, crops, animal or plant fats, biological waste and/or algae (all claimed).    ADVANTAGE - The process provides improved and high quality of pyrolysis oil with reduced acidity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a pyrolysis oil produced by the process.
NOVELTY - Degrading or converting sugar cane trash comprises separating the sugar cane trash from sugar cane and saccharifying the sugar cane trash with an enzyme composition.    USE - The methods are useful for degrading or converting sugar cane trash; producing fermentation product; and for fermenting sugar cane trash (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a method of producing a fermentation product, comprising: (a) harvesting and separating sugar cane trash from sugar cane; (b) pretreating the sugar cane trash; (c) saccharifying the sugar cane trash with an enzyme composition; (d) fermenting the saccharified sugar cane trash with one or more fermenting microorganisms to produce the fermentation product; and (e) recovering the fermentation product from the fermentation; or a method of producing a fermentation product, comprising: (a) saccharifying sugar cane trash with an enzyme composition; (b) fermenting the saccharified sugar cane trash with one or more fermenting microorganisms to produce the fermentation product; and (c) recovering the fermentation product from the fermentation; and    (2) a method of fermenting sugar cane trash, comprising fermenting the sugar cane trash with one or more fermenting microorganisms, where the sugar cane trash is saccharified with an enzyme composition.
NOVELTY - A Myceliophthora thermophila fungal cell, is new. The fungal cell is genetically modified to reduce amount of endogenous glucose and/or cellobiose oxidizing enzyme activity produced by the fungal cell.    USE - The M.thermophila fungal cell is useful for generating fermentable sugar for producing end products including precursor industrial chemical and fuel alcohol chosen from ethanol or butanol (all claimed).    ADVANTAGE - The fungal cell improves yield of the fermentable sugars.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of generating at least one fermentable sugar, which involves contacting cellulose with an enzyme mixture comprising two or more cellulose hydrolyzing enzymes, where at least one of the two or more cellulose hydrolyzing enzymes is produced by the fungal cell.
NOVELTY - Producing gas from a biomaterial comprises: fermenting the biomaterial using anaerobic hydrolysis-fermentation; photofermentating; removing the gas; and maintaining a pH during at least one stage.    USE - The method is useful for producing gas from biomaterial (claimed) or organic wastes, where the gas is hydrogen.    ADVANTAGE - The method: requires abundant and low cost inocula and reactor with minimal size and built-in illumination; utilizes end products as nursery pots and fertilizers, reuses effluent in pulping digested manure, and recycles effluent as fertilizer thus minimizing overall cost; avoids substrate inhibition; allows integrating two-stage process to produce hydrogen while suppressing methanogens and stabilizing wastes and generating additional hydrogen; prevents conversion and consumption of hydrogen and allows concentrating and purifying gas product, thus converting solid waste into energy fuel, nursery pots and addresses current waste-management problems in dairy and food industries; provides hydrogen at economic yield.
NOVELTY - A plug flow type methane anaerobic reactor comprises a reactor body (7) with a cavity (70), where top part of reactor body is provided with a reactor cover plate (11) for sealing the cavity. The cavity of the reactor body is provided with a metal barrel body (3). The inner cavity (32) of metal barrel body is insulated from cavity of reactor body. The side wall of reactor body is provided with a feed port (1), a discharge port (9) and a sampling port (5). The reactor cover plate is provided with a methane outlet (10).    USE - Plug flow type methane anaerobic reactor.    ADVANTAGE - The reactor is featured with thorough anaerobic digestion and high rate of producing methane.    DETAILED DESCRIPTION - A plug flow type methane anaerobic reactor comprises a reactor body (7) with a cavity (70), where top part of reactor body is provided with a reactor cover plate (11) for sealing the cavity. The cavity of the reactor body is provided with a metal barrel body (3). The inner cavity (32) of metal barrel body is insulated from cavity of reactor body. The side wall of reactor body is provided with a feed port (1), a discharge port (9) and a sampling port (5). The reactor cover plate is provided with a methane outlet (10). The bottom part of the reactor body is provided with a drain outlet (6). The feed port, discharge port, sampling port, methane outlet and drain outlet are communicated with the cavity. The cavity of metal barrel body is provided with a heater (4) and a heat detector (12).    DESCRIPTION OF DRAWING(S) - The drawing is a schematic perspective view of the plug flow type methane anaerobic reactor.    Feed port (1)    Metal barrel body (3)    Heater (4)    Sampling port (5)    Drain outlet (6)    Reactor body (7)    Discharge port (9)    Methane outlet (10)    Reactor cover plate (11)    Heat detector (12)    Cavity (32)    Cavity (70)
NOVELTY - The method involves pre-heating air in a gasification furnace, and adding biomass into the gasification furnace and a filter bag dust remover. An organic solvent spray tower is contained with tar, where the spray tower outlet gas temperature is maintained at 150 to 300 degree Celsius. The tar and organic solvent are passed into a fractionating tower, where the organic solvent is bio-diesel and diesel fuel. The obtained tar is passed into an oxidation zone and a reduction zone of the gasification furnace.    USE - Method for gasifying low tar biomass.    ADVANTAGE - The method enables reducing dust in gas concentration, releasing coke tar and improving gasification process so as to obtain high quality clean gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for realizing low tar biomass gasification, comprising a gasification furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic illustration of a low tar biomass gasifying method.
NOVELTY - Producing synthesis gas from biomass comprises: (a) contacting the biomass with oxygen in an amount effective to oxidize the biomass; (b) contacting at least one combustible material with oxygen to oxidize the combustible material; and (c) contacting the oxidized biomass with the hot oxidized gas to heat the biomass to a temperature of at least 900 degrees C, thus producing synthesis gas; and (d) recovering synthesis gas produced in step (c).    USE - The process is useful for producing synthesis gas from biomass (claimed).    ADVANTAGE - The process provides a method of providing heat for producing synthesis gas without consuming a portion of the synthesis gas to provide such heat, thus providing an increased yield of synthesis gas.    DETAILED DESCRIPTION - Producing synthesis gas from biomass comprises: (a) contacting the biomass with oxygen in an amount effective to oxidize the biomass and to heat the biomass to a temperature no greater than 750 degrees C; (b) contacting at least one combustible material with oxygen to oxidize the combustible material and to heat the combustible material to a temperature of at least 1,100 degrees C, thus providing a hot oxidized gas; and (c) contacting the oxidized biomass with the hot oxidized gas to heat the biomass to a temperature of at least 900 degrees C, thus producing synthesis gas; and (d) recovering synthesis gas produced in step (c).
NOVELTY - Producing biodiesel and biodiesel precursor, comprises (a) providing crude oil with a phosphor (more than 10 ppm) and a steryl glycoside (more than 5 ppm); (b) contacting the crude oil from step (a) with at least one adsorbent; and (c) separating the adsorbent from the oil.    USE - The method is useful: for producing biodiesel and biodiesel precursor (claimed), which is useful as a alternative conventional petrochemical diesel fuel; and to remove phosphatides and steryl glycosides before subjecting the oil to a biodiesel production process.    ADVANTAGE - The method is simple, commercially available and less time consuming. The method provides biodiesel and biodiesel precursor with low phosphatide content, high adsorption capacities, high porosity and/or high specific surface, and improved kinetic effects. The method enables the production of biodiesel without further pre- or post treatments regarding the removal of both phosphor and (non-) acylated steryl glycosides.
NOVELTY - The generator (100) has a vapor condenser (106) connected to a pyrolysis chamber (102), and a synthesis gas collection chamber (107) collecting synthesis gas from the condenser. A bio oil collection chamber (108) collects bio oil from the condenser. A biochar collection chamber (111) includes a biochar conveyor (110) to collect biochar dispensed from the pyrolysis chamber. A biochar cooling chamber (109) is in communication with the biochar collection chamber via the conveyor. An auger (101) fragments the flow of biomass before passing the flow of biomass into the pyrolysis chamber.    USE - Biochar generator for use in a vehicle for cultivating and harvesting food crops and forest products.    ADVANTAGE - The generator eliminates need to transport biomass between a harvesting site and a storage site, and between the storage site and a fragmentation site. The generator eliminates need to transport synthesis gas, bio oil and biochar from the site of the pyrolysis reaction to the ultimate site of storage, consumption, refinement or application, thus reducing fuel consumption associated with the transportation of biomass and products from a pyrolysis reaction to the ultimate site.    DETAILED DESCRIPTION - The pyrolysis reaction occurs in the pyrolysis chamber and produces a product selected from a group consisting of vaporized synthesis gas, vaporized bio oil and biochar. An INDEPENDENT CLAIM is also included for a method for using a biochar generator.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biochar generator carried by a vehicle.    Biochar generator (100)    Auger (101)    Pyrolysis chamber (102)    Vapor condenser (106)    Synthesis gas collection chamber (107)    Bio oil collection chamber (108)    Biochar cooling chamber (109)    Biochar conveyor (110)    Biochar collection chamber (111)
NOVELTY - An anaerobic digestion device comprises a waste material collecting device; a pre-processing device; and an anaerobic digestion tank including a feeding port connected with a feeding valve, a gas storage chamber connected to lower opening of feeding valve, a digestion chamber having a stirrer and a manhole, a heating layer covering the digestion chamber, and a liquid storage chamber connected to lower part of digestion chamber and to liquid charging pipe of gas storage chamber.    USE - Anaerobic digestion device used for processing municipal solid waste.    ADVANTAGE - The anaerobic digestion device has simple structure and high gas production rate.    DETAILED DESCRIPTION - An anaerobic digestion device comprises anaerobic digestion tank, pre-processing device, and waste material collecting device. The anaerobic digestion tank includes a feeding port connected with the pre-processing device and with a feeding valve (e.g. hard seal ball valve) having a feed driving device on one side; a gas storage chamber connected to lower opening of feeding valve and having a guide tube connected with the waste material collecting device, a heat supply pipe and a liquid charging pipe; a digestion chamber connected with the gas storage chamber and having a stirrer and a manhole on outer sidewall; a stainless steel heating layer with thickness of 3-5 cm and covering the digestion chamber; and a liquid storage chamber (preferably digestive bacterial liquid storage chamber) connected to lower part of digestion chamber and having a discharging pipe. The lower opening of discharging pipe is connected with an outlet valve (e.g. hard seal ball valve) having a discharge driving device on one side. The liquid storage chamber is connected to the liquid charging pipe through a circulating pump.
NOVELTY - Unpowered self-circulating totally-mixing anaerobic reaction device comprises a tank body. The lower part of the tank body comprises a water distribution pipe and a sludge discharging pipe, and the upper part comprises a water outlet device and a biogas discharging pipe. The bottom of the tank body is conical-shaped. The upper part of the water distribution pipe in the tank body comprises a hyperboloid guide barrel. The upper part of the guide barrel is enclosed by a three-phase separator. The outer side of the guide barrel comprises a water outlet steady flow barrel.    USE - The device is useful for improving gas yield of highly-enriched organic wastewater.    ADVANTAGE - The device: solves the problems of e.g. poor mixing effects of large-scale high-solid materials, high energy consumption, easy blockage and entrainment of discharged water in anaerobic fermentation process; and ensures stable and automatic circulation with high efficiency and energy conservation.    DETAILED DESCRIPTION - Unpowered self-circulating totally-mixing anaerobic reaction device comprises a tank body. The lower part of the tank body comprises a water distribution pipe and a sludge discharging pipe, and the upper part comprises a water outlet device and a biogas discharging pipe. The bottom of the tank body is conical-shaped. The upper part of the water distribution pipe in the tank body comprises a hyperboloid guide barrel. The upper part of the guide barrel is enclosed by a three-phase separator. The outer side of the guide barrel comprises a water outlet steady flow barrel formed with the inner wall of the tank body. The opening of the water outlet steady flow barrel is located at the lower part.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the anaerobic reaction device.
NOVELTY - A wastewater and sludge synchronous biodegradation compound reactor comprises an anoxic tank (1), an anaerobic tank (2), an aerobic tank and a sediment tank (4) connected in series. A stirring device is arranged in the anoxic tank. A sludge backflow inlet is arranged on a top of the anoxic tank. A biocotton filler is filled in the anaerobic tank. Multiple layers of plate-shaped filler (6) is arranged under the spherical filler.    USE - Wastewater and sludge synchronous biodegradation compound reactor.    DETAILED DESCRIPTION - A wastewater and sludge synchronous biodegradation compound reactor comprises an anoxic tank (1), an anaerobic tank (2), an aerobic tank and a sediment tank (4) connected in series. A stirring device is arranged in the anoxic tank. A sludge backflow inlet is arranged on a top of the anoxic tank. A biocotton filler is filled in the anaerobic tank. A perforating aeration pipe is arranged on an inner bottom of the aerobic tank. Spherical filler is suspended on an inner top of the aerobic tank. Multiple layers of plate-shaped filler (6) is arranged under the spherical filler. Naididae is hung on the spherical filler and plate-shaped filler. A sludge backflow outlet is arranged on a bottom of the sediment tank.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of wastewater and sludge synchronous biodegradation compound reactor.    Anoxic pool (1)    Anaerobic pool (2)    Aerobic pool (3)    Sedimentation tank (4)    Spherical filler (5)    Plate-shaped filler (6)    Perforation aeration pipe (7)    Stirring device (8)    Reflux sludge inlet (9)    Inlet water port (19)
NOVELTY - A plasma arc gasification furnace comprises a hearth (1) comprising a preheating chamber (1-1), a coking chamber (1-2), a gasification chamber (1-3), a wall body, a melt filter chamber (1-4), a fuse collecting room, an arc generating electrode, an arc electrode stepping motor and working electrode; and a gasification furnace comprising four partition boards, an electrode connected to the electrode stepping motor, a working gas inlet pipe, a separation plate having four corners set on gas input tube, and a heat insulating wall.    USE - A plasma arc gasification furnace for processing municipal household waste.    ADVANTAGE - The plasma arc gasification furnace has high utilization rate, and high yield of garbage gasification.    DETAILED DESCRIPTION - A plasma arc gasification furnace comprises:    (A) a hearth (1) comprising a preheating chamber (1-1), a coking chamber (1-2), a gasification chamber (1-3), a wall body, a melt filter chamber (1-4), a fuse collecting room, an arc generating electrode, an arc electrode stepping motor and working electrode; and    (B) a gasification furnace comprising four partition boards, an electrode connected to the electrode stepping motor, a working gas inlet pipe, a separation plate having four corners set on gas input tube, and a heat insulating wall.    The hearth is set on the upper part on the input channel, and has an upper pat extending to the gasification furnace along the axial line. The separating plate is provided with groups of air guide hole and an air guide channel. The coking chamber is provided with two mixed gas channel connected to the gasification chamber. The melt filter chamber is provided with a high temperature filter medium having a slag discharge port and slag outlet.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a plasma arc gasification furnace.    Hearth (1)    Preheating chamber (1-1)    Coking chamber (1-2)    Gasification chamber (1-3)    Melt filter chamber (1-4)
NOVELTY - The method involves providing a carbonaceous solid raw material (40) to carbonaceous solid feedstock during pyrolysis. Gaseous constituents are cooled to obtain liquid bio-oil (120) by the carbonaceous solid raw material at temperature range of 400-700 degrees in a pyrolysis reactor (30). A solid material (80) is separated from pyrolysis gas (60) before the cooling of a gaseous component (90) to provide the bio-oil. The pyrolysis reactor is formed with an inlet to provide carbonaceous solid raw materials.    USE - Method for preparing bio-oil from a lignocellulosic raw material.    ADVANTAGE - The method enables an effective unit to control hydrogenation during a deoxygenating process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an arrangement for preparing bio-oil from lignocellulosic raw material.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a method for preparing bio-oil from a lignocellulosic raw material.    Pyrolysis reactor (30)    Carbonaceous solid raw material (40)    Pyrolysis gas (60)    Solid material (80)    Gaseous component (90)    Liquid bio-oil (120)
NOVELTY - The electrode structure has insulating property fastening element that is inserted into combining holes (120,120') formed on the electrode plates formed of titanium, platinum or stainless steel. An insulating property washer (110) is provided with electrode plates. Several through-holes (140) are formed on the electrode plates.    USE - Electrode structure used in industry field, medical field and automobile field.    ADVANTAGE - The hydrogen blister and oxygen bubble can be separated from the electrode plate easily during electrolysis of water, by forming through-holes on the electrode plate. The resistance of the electrode plate can be reduced. The flow of excessive current to the electrode plate can be prevented so that the loss of electric power can be reduced. The heat generation of electrode plate can be improved so that the corrosion of electrode plate can be prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows an exploded perspective view of electrode structure.    Insulating property washer (110)    Combining holes (120,120')    Through-hole (140)    Keen chamfer (150)    Bolt (161a')
NOVELTY - A raw material comprising organic acids produced by anaerobic fermentation of biomass or organic waste is mixed with ketone in presence of catalyst in a single reactor to obtain mixture of hydrocarbon. The water produced during the reaction is removed.    USE - Manufacture of hydrocarbon used as fuel, lube base oil and aromatics.    ADVANTAGE - The hydrocarbon is manufactured efficiently from biomass or organic waste.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the anaerobic fermentation process.
NOVELTY - A liquid combustion catalyst composition contains ionized metal compound having metal ion formed by dissolving metal compound chosen from magnesium, calcium, manganese and zinc, in soluble liquid. The metal ion is chosen from magnesium ion, calcium ion, manganese ion and zinc ion.    USE - Liquid combustion catalyst composition is used for fuel e.g. hydrocarbon fuel, fossil fuel and biomass fuel.    ADVANTAGE - The liquid combustion catalyst composition has excellent thermal efficiency and reduced fuel consumption.
NOVELTY - The apparatus has a pair of oppositely charged electrolysis plates that are supported in the water-holding vessel. A magnet generates a magnetic field with flux lines penetrating through the water contained in the vessel. An acoustic transducer generates acoustic energy for causing cavitations of the water molecules. A source of infrared energy is directed through the water in the vessel. The combined effects of the electrolysis plates, magnetic field, acoustic energy and infrared energy enhances the disassociation of water into hydrogen and oxygen gasses.    USE - Apparatus for enhancing electrolysis of water.    ADVANTAGE - The water is dissociated into hydrogen and oxygen gases in an efficient manner. The combination of acoustic cavitations, molecular vibrational enhancement, and increased magnetic susceptibility reduces energy dissociation requirements associated with water electrolysis, so that the electrolysis process is enhanced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of enhancing electrolysis of water.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of electrolyzer cell.
NOVELTY - Method comprises: accelerating a motive fluid (108) to at least Mach 1 in a reactor and producing a high speed motive fluid; and reacting (200) a feedstock includes lipid material with the high speed motive fluid in the reactor.    USE - The method is useful for producing: biofuels and biolubricants from lipid material, where the biofuels are fatty acid methyl ester and microdiesel biofuel; non-esterified renewable biofuels such as green diesel, green jet fuel, and green gasoline, which is useful in conventional internal combustion engines; and fatty alcohols.    ADVANTAGE - The improved method is safe, environmentally friendly, cost effective, and reduces harmful emissions from combustion engines.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a method-I comprising: reacting a feedstock that includes lipid material with a motive fluid in a first reactor (102) and producing a first effluent material, and reacting the first effluent material in a second reactor (104) and producing a second effluent material, where the first effluent material is fed directly from the first reactor into the second reactor; and    (2) a method-II comprising reacting fatty acid material with a motive fluid in a nozzle reactor and producing a first effluent material, and reacting the first effluent material in a tubular reactor.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of method for producing biofuels and biolubricants.    First reactor (102)    Second reactor (104)    Motive fluid (108)    Reacting the lipid material and the motive fluid (200)    Separating heavy fraction from the effluent material. (204)
NOVELTY - Preparing dronedarone or its salts comprises reacting 5-amino-3-(4-(3-di-n-butylamino-propoxy)benzoyl)-2-n-butylbenzofuran (I) in an organic phase comprising one or more non-polar solvents with methane sulfonyl chloride, without the addition of a base to give dronedarone, which, if desired, can be reacted with an organic or inorganic acid to form a salt of dronedarone.    USE - The process is useful for preparing dronedarone having antiadrenergic and coronary vasodilatory effects. The dronedarone hydrochloride is useful to prevent recurrence of atrial fibrillation or to reduce ventricular rate. No biological data given.    ADVANTAGE - The simple, safe, environmentally friendly and industrially viable process produces dronedarone or its salts, in high yields and high purity, using inexpensive reactants and solvent and without using toxic halogenated solvents.
NOVELTY - Formulating (M1) a fuel composition, comprises: providing a fuel; and forming the fuel composition by adding a polar fluid and an emulsifier to the fuel, where the emulsifier is present in an amount effective for the biodiesel fuel, alcohol, water and emulsifier to form an emulsion, the emulsifier includes an active surfactant mixture of oleic acid and ammonium oleate, and the ratio of oleic acid to ammonium oleate is not greater than 60:40.    USE - The method is useful for formulating a fuel composition which is useful in internal-combustion engines.    ADVANTAGE - The method: is simple and cost effective; and utilizes simple, selective and recyclable materials, thus the method can be used at an industrial scale.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for forming (M2) a polyol fatty acid ester, comprising: providing a polyol having at least three reactive alcohol groups; selecting a fatty acid; protecting all but a preselected one of the reactive alcohol groups on the polyol by reacting all but the preselected one of the reactive alcohol groups with protecting groups, where a single protecting group protects at least one reactive alcohol group; linking the fatty acid to the polyol through an ester linkage by reacting the fatty acid with the preselected one of the reactive alcohol groups; and forming the polyol fatty acid ester by removing the protecting groups, where each of the steps is performed under conditions that would tend not to reduce an unsaturated fatty acid.
NOVELTY - A composite microbial bactericide for degrading kitchen garbage at normal temperature comprises composite thalluses and carriers, where the thalluses are constituted by Lactobacillus acidophilus zsq11 and Saccharomyces sp. zsq13, and the carriers are constituted by broken peanut shells, sand, wood shavings and bran. The composite thalluses occupy the microbial bactericide (5-10 wt.%).    USE - As composite microbial bactericide for degrading kitchen garbage at normal temperature (claimed).    ADVANTAGE - The method of composite microbial bactericide has good ventilation property; has good running effect at normal temperature with the kitchen garbage degradation rate of greater than or equal to 75%; does not require microbial treatment processes such as filtration and dehydration; and has simple treatment steps with stable effect and no environmental pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the composite microbial bactericide involving culturing the Lactobacillus acidophilus zsq11 and the Saccharomyces sp. zsq13; centrifuging to collect thalluses, mixing to obtain the composite thalluses; mixing the broken peanut shells with the sand, the wood shavings and the bran; and mixing the composite thalluses with the carriers to obtain the composite microbial bactericide, where the composite thalluses occupy the microbial bactericide (5-10 wt.%).
NOVELTY - The apparatus has modification unit (16) which generates a hydrogen-containing-gas by reforming reaction using the source gas and water passed the desulfurizer (17). A heater (13) is provided to heat the desulfurizer. The clearance gap is formed in the outer side of the modification unit. The helical form heater is provided along the inner wall of the outer surface of the desulfurizer.    USE - Hydrogen generating apparatus of fuel cell power generating device (claimed).    ADVANTAGE - Since the helical form heater is provided along the inner wall of the outer surface of the desulfurizer, the heat-transferring effect of the heater to the outer surface of the hydrogen generating apparatus can be improved efficiently. The temperature rising property of hydrogen generating apparatus can be improved. The increase of heater temperature can be prevented. The starting time of hydrogen generating apparatus can be reduced. The high durability of the heater can be achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen generating apparatus. (Drawing includes non-English language text)    Air fan (2)    Burner (3)    Heater (13)    Modification unit (16)    Desulfurizer (17)
NOVELTY - A fuel generator has fuel containing hydrogen generated by chemical reaction, and two or more preparations reproducible by reverse reaction. At least two of fuel generators are thermally connected.    USE - Fuel generator is used for secondary battery-type fuel cell system (claimed) for electric vehicle.    ADVANTAGE - The fuel generator has reduced energy supplied from outside.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for secondary battery-type fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows the cross-sectional view of the fuel generator.    Container (8)    Fuel generation component (9)    Contact component (10)
NOVELTY - The system has a feeding device (2) that is provided in the upper portion of straw gasification furnace (1). The straw gasification furnace is connected with a gas purifier (3), a gas conveyer (4) and a gas storage cabinet (5). The bottom surface of gasification furnace is connected with an ash tank (7). The bottom surface of water-through type ash bucket (6) is immersed in the ash bucket.    USE - Automatic gasification furnace system.    ADVANTAGE - The gasification efficiency of system can be improved, and the gasification process can be continuously performed.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of gasification furnace system.    Straw gasification furnace (1)    Feeding device (2)    Gas purifier (3)    Gas conveyer (4)    Gas storage cabinet (5)    Water-through type ash bucket (6)    Ash tank (7)
NOVELTY - The inoculum package powder biomass fuel rod comprises a rod body (1) and an adhesive body (2). The adhesive body is uniformly distributed with a cylindrical rod body. A material of the adhesive body comprises powder. A material of the rod body comprises saw dust or bamboo powder. A weight of the adhesive body is 5% of the rod body weight (8%).    USE - Used as an inoculum package powder biomass fuel rod.    ADVANTAGE - The sterile inoculum package powder biomass fuel rod exhibits simple structure, stable performance and good effect in an economical manner.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of an inoculum package powder biomass fuel rod.    Rod body (1)    Adhesive body. (2)
NOVELTY - The cassava starch biomass fuel rod comprises a rod body (1) having an upper portion, and an adhesive body (2). The adhesive body is uniformly distributed on the upper portion of the rod body. The rod body is cylindrical in shape. A material of the adhesive body comprises cassava flour. A material of the rod body comprises saw dust or bamboo powder. A weight of the adhesive body is 5% of the rod body weight (8%).    USE - Used as a cassava starch biomass fuel rod.    ADVANTAGE - The cassava starch biomass fuel rod exhibits simple structure, stable performance and good effect.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a cassava starch biomass fuel rod.    Rod body (1)    Adhesive body. (2)
NOVELTY - A microorganism electrolysis tank comprises an electrolysis tank housing (6) provided with a cathode/anode exchange film (8) for separating the electrolysis tank housing into an anode chamber (9) and a cathode chamber (7). Each anode chamber and cathode chamber for containing the to-be-treated sewage is provided with an anode (10) and a cathode (5) connected with the external power supply (1).    USE - Tank for carbon dioxide conversion and sewage treatment.    DETAILED DESCRIPTION - A microorganism electrolysis tank comprises an electrolysis tank housing (6) provided with a cathode/anode exchange film (8) for separating the electrolysis tank housing into an anode chamber (9) and a cathode chamber (7). Each anode chamber and cathode chamber for containing the to-be-treated sewage is provided with an anode (10) and a cathode (5) connected with the external power supply (1). A reference electrode for controlling the cathode potential is formed in the cathode chamber. The upper end of the cathode chamber is provided with a cathode product exit. The anode chamber is connected with the cathode chamber by the air conduit.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the microorganism electrolysis tank.    External power supply (1)    Cathode (5)    Electrolysis tank housing (6)    Cathode chamber (7)    Cathode/anode exchange film (8)    Anode chamber (9)    Anode (10)
NOVELTY - A treatment of oily sewage comprises performing electric polarization antiscaling pre-treatment on oily sewage; performing gas-dissolving oxygenation on oily sewage after polarization pre-treatment; making water after gas-dissolving oxygenation pass through centripetal air floatation device; contributing to generation of large particles by separated water solid via micro-whirl; intercepting and removing generated large particles by filtering method, and backwashing; and performing electric polarization treatment on oxygen-dissolving water after filtering.    USE - Method for treatment of oily sewage.    ADVANTAGE - The method has simple flow process, low operation expenses and good treated water quality compared with medicated chemical treatment technique. Pollution for water, oil and environment of the medicated treatment method is avoided.    DETAILED DESCRIPTION - Treatment of oily sewage comprises:    (A) performing electric polarization antiscaling pre-treatment on oily sewage;    (B) performing gas-dissolving oxygenation on oily sewage after polarization pre-treatment;    (C) making water after gas-dissolving oxygenation pass through centripetal air floatation device to perform separation for oil gas and water solid;    (D) contributing to generation of large particles by separated water solid via micro-whirl;    (E) intercepting and removing generated large particles by filtering method, and backwashing intercepted particles to remove particles; and    (F) performing electric polarization treatment on oxygen-dissolving water after filtering to generate more active oxygen substances for performing sterilization and passivation protection on metal surface.
NOVELTY - A microbial agent comprises (wt.%) Cellulomonas flavigena fiber (0.1-20), Cytophaga fermentans fiber (0.5-30), Bacillus pasteurii (0.5-25), B. cereus (5-50), Butyrivibrio fibrisolvens (1-30), and Fusarium sporotrichioides (1-35).    USE - Microbial agent for straw degradation (claimed), and further applied to rice, wheat, and corn.    ADVANTAGE - The agent can accelerate organic substance decomposing speed, thus providing more nutrition for growth of crops, maintaining and improving soil fertility, improving soil organic material content, improving soil physicochemical property, and improving crop yield by more than 5%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing a straw organic fertilizer.
NOVELTY - The generator has a gasification furnace that is sealed with a dust removing tank filled with water at the lower portion. The bottom of the gasification furnace extends into an ash cleaning device. An ash suction end extends into the ash cleaning device and cleans dust.    USE - Biomass fuel gas generator.    ADVANTAGE - The biomass fuel gas generator has simple structure and design, and can continually ensure high efficiency and stability of normal operation, improve the utilization rate and production efficiency of the equipment and reduce the waste of resource.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of biomass fuel gas generator.
NOVELTY - A moving type garbage recycling processing system comprises a garbage can to transfer transportation of the mobile device and process the garbage to the movable device of the garbage processing device.    USE - System for processing, collecting and treating urban household or domestic garbage.    ADVANTAGE - The system can effectively reduce water accumulation of urban waste recovery treatment of logistics transportation cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the moving type garbage recycling processing system.    Ozone generator (1)    Garbage crusher (2)    Garbage separator (3)    Carbonization kettle (4)    Organic outlet (32)
NOVELTY - An additive comprises (in parts weight) surfactant (55-70), glycol-type alcohol (10-15), alcohol compoundable from biomass (15-25), and aqueous ammonia (5.5-8.8).    USE - Additive is used for manufacturing hydrated biofuel (all claimed).    ADVANTAGE - The hydrated biofuel having high conversion efficiency, is efficiently manufactured without affecting the environment.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of additive, which involves mixing and stirring surfactant, glycol-type alcohol and alcohol compoundable from biomass, adding aqueous ammonia, stirring and mixing;    (2) hydrated biofuel, which is obtained by mixing water and the additive with fuel oil, dispersing and solubilizing; and    (3) manufacture of hydrated biofuel, which involves mixing (in parts weight) fuel oil (58-62) and additives (15-20), adding water (18-27) to obtained liquid mixture, stirring, and solubilizing.
NOVELTY - The device has material blending device that is provided with rice shaped material element and material mixing motor. The rice shaped material element is connected with the material mixing motor. The motor is set on the pressing device. A carbon discharging device is provided on the gasification furnace bottom. The gasification furnace is provided with an air outlet portion. The air outlet is orderly connected water washing device. The carbon device and fan are connected with the control cabinet.    USE - Straw direct gasification poly-generation device.    ADVANTAGE - The reliability of the device can be improved. The safety performance of the device can be improved. The gasifying effect of the device can be improved. The straw utilization rate can be increased. The operation cost of the device can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the straw direct gasification poly-generation device.
NOVELTY - The method involves crushing food waste material in the vacuum dry unit. The membrane filter is provided with storage chamber. The membrane filter is washed using the warm water.    USE - Method for deposing food waste material.    ADVANTAGE - The processing of the food waste material can be improved with simple operation.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph showing vapor pressure of water according to temperature and absolute humidity. (Drawing includes non-English language text)
NOVELTY - Production of organic-inorganic environment-friendly compound fertilizer with 48% of nutrient, involves adding efficient bacterial agent (for microbial fermentation) into livestock and poultry excrement straw to perform rapid fermentation, drying and crushing the fermented material, cementing and compounding the organic-inorganic substrate, and producing particle by existing methods.    USE - Production of organic-inorganic compound fertilizer (claimed).    ADVANTAGE - The method produces organic-inorganic environment-friendly compound fertilizer with 48% of nutrient.
NOVELTY - The fertilizer turning machine has machine frame, driving shaft chain wheel (1), over-bridge big shaft, speed reducer chain wheel and lifting shaft chain wheel (8). The change speed gear box (9) provided in the top of the machine frame is provided with a gear.    USE - Organic fertilizer turning machine used in agricultural field.    ADVANTAGE - The organic waste can be processed efficiently with simple structure, high working efficiency and high market popularization value. Energy-saving effect of the fertilizer turning machine can be ensured.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of organic fertilizer turning machine.    Driving shaft chain wheel (1)    Lifting shaft chain wheel (8)    Change speed gear box (9)    Transverse rack (15)    Walking wheel (16)
NOVELTY - The carbonization fuel manufacturing device has carbonizing machine that is provided with supersonic wave treatment tank, and import hopper. The dehydrated sludge is conveyed to rotary kiln through the sewage sludge.    USE - Carbonization fuel manufacturing device.    ADVANTAGE - The organic sewage sludge is reduced and the emission of toxic gas is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the carbonization fuel manufacturing device.(Drawing includes non-English language text)
NOVELTY - The palm pallet is made of deionized water palm crushed material. The coffee waste is mixed with the palm crushed material.    USE - Palm pallet.    ADVANTAGE - The waste is recycled and the cost of the pallet is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical representation illustrating the palm pallet. (Drawing includes non-English language text)
NOVELTY - The method involves coating gold layer on surface of nickel layer on printed circuit board (1). Patterns are formed on copper foil plates through lithographic process.    USE - Direct current plating method for manufacturing micro fuel cell.    ADVANTAGE - Stability and durability are increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view illustrating the direct current plating process for manufacturing micro fuel cell.    Printed circuit board (1)    Hardened photo resist (2)    Etching portion (3)    Gold deposition portion (5)
NOVELTY - A floating biological bed comprises a buoy (1), a fixing rope (2), a steel structural frame (3) and a filler (4). The buoy is fixed on the steel structure frame. The filler is immersed in liquid.    USE - Floating biological bed.    ADVANTAGE - The bed is convenient to repair and easy to replace.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a floating biological bed.    Buoy (1)    Fixing rope (2)    Steel structural frame (3)    Filler (4)
NOVELTY - An aerobic composting ventilation and heat recycling device comprises an evaporator (1), a condenser (2), a water tank (3) and air pipes (4, 5), where one of the air pipes is connected with an aerobic compost stack body air inlet. The blast air pipe and the evaporator are connected with an aerobic compost stack body (6) and an air outlet of the evaporator and the condenser are respectively connected with a compressor (7). An inner medium connecting pipeline is provided with a phase heat exchanger and the condenser is equipped under the water tank.    USE - Device for aerobic composting ventilation and heat recycling.    ADVANTAGE - The device effectively recycles and utilizes discharged air.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an aerobic composting ventilation and heat recycling device.    Evaporator (1)    Condenser (2)    Water tank (3)    Air pipes (4, 5)    Blast air pipe (6)    Compressor (7)
NOVELTY - An environment-friendly energy-saving biological alcohol oil is prepared by mixing (in weight parts) methanol (75-95), emulsifier (0.2-1.0), ferrocene (0.01-0.5) and water (5-25).    USE - Environment-friendly energy-saving biological alcohol oil.    ADVANTAGE - The alcohol oil is high in calorific value, stable in performance, low in volatility, low in condensation point, not easy to ignite, non-explosive and extinguished by water while being ignited accidentally, and has ignition temperature of greater than 200 degrees C without pressure. The alcohol is non-toxic, tasteless, smokeless and dustless, and achieves quality of national primary standard of alcohol based fuels.
NOVELTY - A fuel carbon preparing method involves performing deodorization and sterilization processes by utilizing sludge (70-90%) and biomass vinegar liquid (1-3%) and allowing to stand for 2-3 hours to obtain a processed sludge. Biomass fuel is crushed and sprayed with limestone (1-5%) and allowed to stand for 1-2 hours to obtain the processed biomass fuel. The processed sludge is mixed with the biomass fuel and 0.5 cm of carbon or carbon powder, where the mixture is sterilized at 100-300 degrees C. The obtained product is sieved and shaped to obtain a product.    USE - Method for preparing fuel carbon.    ADVANTAGE - The method enables preparing fuel carbon in a cost-effective and eco-friendly manner.    DETAILED DESCRIPTION - A fuel carbon preparing method involves performing deodorization and sterilization processes by utilizing sludge (70-90%) and biomass vinegar liquid (1-3%) and allowing to stand for 2-3 hours to obtain a processed sludge. Biomass fuel is crushed to obtain particle size of less than 6 mm and sprayed with limestone (1-5%) and allowed to stand for 1-2 hours to obtain the processed biomass fuel. The processed sludge (70-80 weight parts) is mixed with the biomass fuel (16-22 weight parts) and 0.5 cm of carbon or carbon powder (4 to 8 weight parts), where the mixture is sterilized at 100-300 degrees C till the moisture content of the mixture reaches 15-45%. The obtained product is sieved to remove metallic impurity having particle size less than 6 mm and shaped to obtain a product.
NOVELTY - A biomass tar cracking catalyst comprises a transition metal element i.e. cobalt, utilized as an active component, where content of the cobalt is 15 percent of total mass of the catalyst that is chosen from granular calcium oxide, magnesia, biomass pyrolytic carbon or rice husk gasification ash.    USE - Biomass tar cracking catalyst for an industry.    ADVANTAGE - The catalyst has cracking rate of 100 percent, high catalytic activity and simple preparation process.    DESCRIPTION OF DRAWING(S) - The drawing shows a photographic view of a biomass tar cracking catalyst.
NOVELTY - Method for converting agricultural waste into useful product, involves subjecting waste roots, stem, leaves, vegetables and/or fruits to fermentation process.    USE - The method is useful for converting agricultural waste into useful product chosen from methane gas, dimethyl ether and fertilizer (claimed).    ADVANTAGE - The method effectively prevents secondary pollution and completely eliminates and controls pollution and maintains ecological balance by converting waste into useful products.
NOVELTY - A solid waste high-energy quantum water cracking treatment method involves performing full-automatic sorting in deodorized garbage for picking out indispensable wastes. The wastes are sent to a grinder to grind. The indispensable wastes are picked out and sent to a building recycling unit to regenerate resource. High-energy quantum water is cracked and sent to a high-energy quantum water cracking device that refers to a sealing container. The cracking treatment is carried out in a sealed manner using the quantum water. Tail reactant is finally obtained.    USE - Method for performing cracking treatment for solid waste high-energy quantum water.    DETAILED DESCRIPTION - A solid waste high-energy quantum water cracking treatment method involves sterilizing, deodorizing and spraying hydrolytic protease to solid waste. 50-100 ml of hydrolytic protease is added to each cubic meter of solid waste. The hydrolytic protease is diluted and uniformly sprayed on a mixture. A full-automatic sorting is performed in the deodorized garbage for picking out indispensable wastes comprising glass, ceramic and metal and recyclable substances. The wastes are sent to a grinder to grind, so that diameter or length of the waste is shortened by increasing density of the waste. Indispensable wastes comprising glass, ceramic and metal are picked out and sent to a building recycling unit to treat so as to regenerate resource. High-energy quantum water is cracked and sent to a high-energy quantum water cracking device that refers to a sealing container. The cracking treatment is carried out in a sealed manner using the quantum water, where pressure during treatment is 1-1.5 MPa, temperature is at 150-190 degrees C, and time is 30-40 minutes. Tail reactant is finally obtained.
NOVELTY - A flower seedling water manure manufacturing method involves mixing (in kg) cabbage leaf (0.3), celery leaf (0.2), asparagus lettuce roots (0.3), sweet potato (0.2), radish skin (0.1), residual bean dreg (0.2) and water (25). The mixture is crushed using mill to obtain slurry. The slurry is put in a sealed container for three days to obtain manure.    USE - Method for manufacturing flower seedling water manure.    ADVANTAGE - The method enables manufacturing the manure with high beneficial effect.
NOVELTY - A pre-processing unit has a straw forming fuel production machine and an automatic control system.    USE - Pre-processing unit for producing a crop straw forming fuel.    ADVANTAGE - The unit ensures producing crop straw forming fuel with high density. The fuel is easy to store and transport, and does not absorb moisture easily.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a pre-processing unit.
NOVELTY - A waste recycling device has a fermenting anaerobic tank, an aerobic tank, and a gas storage tank for storing the marsh gas. A biogas purification process tank and the anaerobic fermentation tank are respectively connected with the storage device and the aerobic tank. Biogas slurry purifying dealt pool comprises a first treatment tank and a second treatment tank, a third treatment pool and two biogas slurry channels. The first and third treatment tanks are respectively connected with the two biogas slurry channels and the second treatment tank.    USE - Waste recycling device for recycling human droppings, and crop waste residue into the residue, and biogas.    ADVANTAGE - The device has recycling utilization rate, high accuracy, and saves energy, promotes improving household production and living condition, and is an ecological and eco-friendly.    DETAILED DESCRIPTION - A waste recycling device has a fermenting anaerobic tank and an aerobic tank, and a gas storage tank for storing the marsh gas. A biogas purification process tank, the anaerobic fermentation tank is respectively connected with the storage device and the aerobic tank. The biogas slurry purifying dealt pool comprises a first treatment tank and second treatment tank, third treatment pool and two biogas slurry channels. The first and third treatment tanks are respectively connected with the two biogas slurry channels and the second treatment tank. The second treatment tank is located between the first and the third treatment tanks. The first treatment tank, the aerobic tank and the third processing tank are provided with a water outlet.
NOVELTY - A methanol petrol producing method involves injecting methanol raw material, additive and petrol synchronously to a static mixer to obtain the methanol petrol.    USE - Method for producing methanol petrol that is utilized for a vehicle.    ADVANTAGE - The method enables avoiding execution of middle denatured alcohol production process, reducing wastage of raw material, facilitating simple production technique, avoiding the need of a storage tank for storing the methanol petrol and producing methanol petrol according to requirement of a user.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for producing methanol petrol.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a method for producing methanol petrol.'(Drawing includes non-English language text)'
NOVELTY - A biomass particle fuel comprises (in weight parts) sawdust (80-85), sludge (5-10) and waste oil (0.1-1).    USE - Biomass particle fuel for use as a raw material of a brick.    ADVANTAGE - The fuel can be produced at low cost with less energy consumption and without causing environmental pollution. The fuel improves combustion heat value and combustion time of the brick while reducing machine abrasion and residue obtained from the fuel. The residue can be used as natural fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing a biomass particle fuel.
NOVELTY - A theobromine synthesis method involves weighing hydrated callose caffeine to water in mol ratio of 1: 30-40. The caffeine is mixed with water at 110-120 degrees C, reacted for 12-16 hours and cooled and filtered. The filtered caffeine is dissolved by utilizing water, and concentrated sulfuric acid and sodium nitrite are added to the dissolved caffeine at low temperature for deamination process. Power of Hydrogen value is adjusted to neutral. The filtered caffeine is cooled, filtered and washed to obtain theobromine with alkali solution.    USE - Theobromine synthesis method.    ADVANTAGE - The method enables synthesizing theobromine in a short process and environment-friendly manner with high yield and saving energy.
NOVELTY - An organic fertilizer fermentation device has a weathered coal material pile whose lower part is provided with a padding layer.    USE - Device for fermenting an organic fertilizer using weathered coal in a production workshop and factory (all claimed).    ADVANTAGE - The device is simple in structure, and has strong adaptability.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an organic fertilizer fermentation device.
NOVELTY - Preparing 4-methyl-5-ethoxyoxazole comprises e.g. performing cyclization reaction on N-ethoxyoxalyl-alanine ethyl ester by using cyclization-dehydrating agent of phosphorus oxychloride, triethylamine and dimethylformamide, and heating the reaction mixture, then cooling, separating out water layer, adding sodium hydroxide into organic layer and performing alkali hydrolysis, then vacuum extracting it, adding sulfuric acid to adjust pH value, raising temperature and decarboxylating, then extracting it with chloroform, and drying obtained organic layer.    USE - The method is useful for preparing 4-methyl-5-ethoxyoxazole used as intermediate of vitamin B6.    ADVANTAGE - The method: has simple operation, mild reaction condition, few side reactions, and high product yield and purity; does not utilizes toxic toluene; and is suitable for large scale production, and good for health and environment protection.    DETAILED DESCRIPTION - Preparing 4-methyl-5-ethoxyoxazole comprises performing cyclization reaction on N-ethoxyoxalyl-alanine ethyl ester at 40-60 degrees C for 0.5-1 hour by using cyclization-dehydrating agent of phosphorus oxychloride, triethylamine and dimethylformamide, and heating the reaction mixture to 75-100 degrees C for 5-10 hours, then cooling the reaction mixture, separating out water layer, where water layer is treated with an alkali to recycle triethylamine, adding sodium hydroxide into organic layer to adjust pH value to 12-14 and performing alkali hydrolysis, vacuum extracting it with ethanol and water, then adding sulfuric acid to adjust pH value to 2-3, then raising temperature to 65 degrees C and decarboxylating, adjusting pH value of obtained solution to 8-10 by using an alkali, then extracting it with chloroform, drying obtained organic layer with anhydrous sodium sulfate, and performing normal pressure distillation to remove chloroform.
NOVELTY - Sodium hydroxide aqueous solution is added to dimethylamine aqueous solution at 10-20 degrees C in the speed of 1 drop/2 seconds, and carbon disulfide aqueous solution is added. The pH of resultant mixture is adjusted to 8-10, and maintained for 12 hours to obtain thiram sodium hydroxide aqueous solution. The obtained thiram sodium hydroxide aqueous solution is added to membrane electrolytic cell cathode chamber, and electrochemical oxidation is performed. The resultant product is filtered, cleaned using water, dried at 60 degrees C, crushed to obtain thiram raw powder.    USE - Manufacture of thiuram.    ADVANTAGE - The method efficiently provides thiram having high productivity and purity, by simple method with low consumption of energy without affecting the environment.
NOVELTY - A kitchen waste aerobic degradation processing device has a processing tank (3) provided with a rectangular shell. Two ends of a stirring shaft (4) are installed with the processing tank. A stirring rod (5) is mounted on the stirring shaft. A lower air inlet and an air outlet are located on the rectangular shell. An upper air inlet is located between heating layers (13). The stirring shaft, an automatic control box (15) and a stirring motor (6) are connected with the heating layers located in a treatment tank.    USE - Kitchen waste aerobic degradation processing device.    ADVANTAGE - The device processes kitchen waste in a simple manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a kitchen waste aerobic degradation processing device.    Processing tank (3)    Stirring shaft (4)    Stirring rod (5)    Stirring motor (6)    Heating layers (13)    Automatic control box (15)
NOVELTY - An organic fertilizer preparing method involves mixing agricultural waste, humic acid, and animal excrement, and fermenting the mixture. A statically placing process is performed to the fermented material for screening. An auxiliary element is added to the screened material, and the mixture is agitated to obtain organic fertilizer material powder after sieving.    USE - Method for preparing organic fertilizer.    ADVANTAGE - The method enables obtaining the organic fertilizer by fermenting and recycling agriculture waste and animal excrement, thus realizing the recycling development of agriculture in an environmental-friendly and efficient manner.
NOVELTY - An emulsifying methanol fuel comprises (in weight parts) 85-90% of methanol (1000), glycerol (1.5-2.5), dicyclopentadienyl iron (0.025-0.035), xylene (0.1-0.14), ethyl acetate (0.1-0.12), hydrogen peroxide (0.8-1. 2) and petrol (4.5-5.5).    USE - Emulsifying methanol fuel.    ADVANTAGE - The fuel has low production cost, better stability, high safety, better combustion effect and high popularization value.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing emulsifying methanol fuel.
NOVELTY - An environment-friendly biomass particle fuel comprises (in wt.%) wood powder (30-50), straw (30-40) and coal powder (20-30).    USE - Environment-friendly biomass particle fuel.    ADVANTAGE - The fuel is prepared by using waste coal gangue powder, so that the fuel reaches long combustion time and high heat value.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing environment-friendly biomass particle fuel.
NOVELTY - A crude oil bio-enhancing agent comprises (in volume parts) heavy oil enzyme group (0.5-3), isopropyl alcohol (20-60) and diesel oil (40-60), where the heavy oil enzyme group comprises biochemistry dispersing agent and ultra nanoscale heavy oil biochemistry enzyme group, which includes linear alkyl catabolic enzyme and C-C chemical bond breaking enzyme.    USE - Crude oil bio-enhancing agent.    ADVANTAGE - The agent increases quality, flowing property and boiling range of crude oil and improving yield of the crude oil.
NOVELTY - Organic fertilizer comprises (in parts weight): radix isatidis, Artemisia capillaris, pig urine granules, Artemisia argyi folium, calamus, and farmyard manure. The fertilizer is obtained by (a) washing radix isatidis, A.capillaris, pig urine granules, Artemisia argyi folium, and calamus using sodium chloride (NaCl) solution for 2-3 times, (b) drying the washed materials, (c) crushing the dried materials, (d) collecting residue and extract, (e) boiling residue in NaCl (2%) solution for 30-35 minutes, (f) collecting residue and extract.    USE - The organic fertilizer is useful for supplying nutrients to rice crops.    ADVANTAGE - The organic fertilizer is prepared using medicinal herb waste materials and hence the nutrient content is more.    DETAILED DESCRIPTION - Organic fertilizer comprises (in parts weight): radix isatidis (1.5-3), Artemisia capillaris (7-15), pig urine granules (7-15), Artemisia argyi folium (2.5-6), calamus (7-15), and farmyard manure (35-65). The fertilizer is obtained by (a) washing radix isatidis, A.capillaris, pig urine granules, A.argyi folium and calamus using sodium chloride (NaCl) solution for 2-3 times, (b) drying the washed materials, (c) crushing the dried materials, (d) collecting the residue and extract, (e) boiling the residue in NaCl (2%) solution for 30-35 minutes, where weight ratio of the residue to NaCl solution is 1:2-3, (f) collecting the residue and extract again, (g) mixing the obtained extract with the extract obtained in the step (d), (h) mixing the farmyard manure with the obtained residue and stirring uniformly before composting, where the compost surface height is 10-20 cm, and (i) covering the obtained compost using plastic film until the compost decomposes completely.
NOVELTY - A high clean alcohol based fuel oil comprises (in weight parts) dicyclopentadienyl iron (0.03-0.05), coal oil (25-40), methanol (60-75), toluene (1-2), acetone (2-3) and isobutanol (2).    USE - High clean alcohol based fuel oil for an automobile.    ADVANTAGE - The dicyclopentadienyl iron has carbon reducing effect and smoke eliminating and combustion effect. The oil can reduce sulfur content in the fuel and reduce the discharge of harmful substance. The oil reduces the emission of carbon oxides so as to improve the heat value and utilization rate of heat energy. The oil is energy-saving, and has clean and environment-friendly effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing high clean alcohol based fuel oil.
NOVELTY - Low-proportion methanol gasoline additives comprises (in vol.%) ethanol (10-15), isopropyl alcohol (8-15), tertiary butanol (2-5), benzene (5-10), dimethylbenzene (2-5), petroleum ether (5-10), hydrogen peroxide (2-5), 3-ethyltoluene (3-5), isobutyl alcohol (5-10), ethyl ether (3-5), isoamyl alcohol (5-10), and no.120 solvent oil (25-30).    USE - Used as a low proportion methanol gasoline additives.    ADVANTAGE - The additive improves overall performance e.g. anti-phase separation, corrosion resistance, antiknock and antioxidant stability, and water resistant stability.
NOVELTY - Method for preparing fulvic acid liquid fertilizer, humic acid solid fertilizer and marsh gas, involves using biomass type domestic garbage and domestic sewage and apparatus containing catalytic kettle, drying device, crushing device, plant humus device, marsh gas purifier, gas storage tank, bunching device and solid-liquid separating device.    USE - The method is useful for preparing fulvic acid liquid fertilizer, humic acid solid fertilizer and marsh gas.    ADVANTAGE - The method utilizes regenerated resources, is environmentally-friendly and economical, consumes less energy, generates renewable energy source, produces reduced carbon content carbon, and has recycling economy.
NOVELTY - A biological fuel oil preparing method involves taking loquat seed as crude raw material, mixing with water, filtering impurities and extracting pigment to obtain fuel oil.    USE - Method for preparing biological fuel oil i.e. loquat seed oil.    ADVANTAGE - The method enables improving ecological environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a loquat seed oil extracted from loquat seed.
NOVELTY - A methanol hydroxide heat supply system has a methanol oxidation heater (1) for methanol catalytic oxidation reaction, a methanol evaporator (12), a methanol hydrogen production device (13) and an air pipeline (2) which is arranged outside the heater, where methanol hydrogen is evaporated by the evaporator into methanol steam and hydrogen fuel gas, and the gases are transferred into a fuel gas pipeline. The heater includes a heat conducting oil pipeline (4) connected with a conduction oil heating device (41). The oil heating device is connected to the heater.    USE - Methanol hydroxide heat supply system.    ADVANTAGE - The system is safe to use, reliable and environment-friendly, and has stable control and operation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a methanol hydroxide heat supply system.'(Drawing includes non-English language text)'    Methanol oxidation heater (1)    Air pipeline (2)    Heat conducting oil pipeline (4)    Methanol evaporator (12)    Methanol hydrogen production device (13)    Conduction oil heating device (41)
NOVELTY - Method for preparing fertilizer involves using raw materials (in wt.%) chosen from cottonseed hull powder (16-18), peanut shell powder (6-8), Sorghum cake powder (12-16), corn cob powder (7-9), duck dropping powder (6-10), rabbit dropping powder (9-11), bean shell powder (4-6), broadleaf wood (2-4), wheat bran powder (2-4), corn powder (15-17), wood ash powder (3), bone powder (0.1-0.3), pine needle powder (0.2-0.4), safflower powder (0.2-0.4), folium isatidis powder (0.1-0.3) and Quisqualis powder (5-7).    USE - The fertilizer is useful for providing nutrients to Lilium casa blanca (claimed) and disease resistance, and promoting growth and inducing flowers.    ADVANTAGE - The preparation method is cost-effective and simple, as raw materials are easily available. The fertilizer is rich in nutrient elements, hence enables rapid growth and development and formation of flowers having big size and bright color in Lilium casa blanca.
NOVELTY - Preparation of D-arginine hydrochloride and L-ornithine hydrochloride comprises resoluting DL-arginine using fermentation thallus of recombinant Escherichia coli efficiently expressing L-arginase or its spray dry preparation as enzyme source and DL-arginine as primer; adding generated liquid in hydrochloric acid to convert L-ornithine into L-ornithine monohydrochloride; adding fixed volume ratio of ethanol; resoluting liquid; collecting precipitate to obtain L-ornithine hydrochloride; and purifying D-arginine.    USE - Preparation of D-arginine hydrochloride and L-ornithine hydrochloride.    ADVANTAGE - The method is environment friendly.    DETAILED DESCRIPTION - Preparation of D-arginine hydrochloride and L-ornithine hydrochloride comprises resoluting DL-arginine for producing D-arginine and L-ornithine using fermentation thallus of recombinant Escherichia coli efficiently expressing L-arginase or its spray dry preparation as enzyme source and DL-arginine as primer; adding generated liquid in hydrochloric acid to convert L-ornithine into L-ornithine monohydrochloride; adding fixed volume ratio of ethanol; resoluting liquid; collecting precipitate to obtain L-ornithine hydrochloride; and purifying D-arginine in suspension by adsorbing, eluting, decompressing, condensing and drying by ion exchange resin to obtain D-arginine hydrochloride.
NOVELTY - Process for culturing microalgae of Botryococcus for the production of fat or hydrocarbon, comprises: culturing one or more strains of microalgae of Botryococcus in the dark in the presence of variable or discontinuous light supply, of which the intensity in photon micromoles varies with an amplitude of more than 10 mu mole/m2/s, at a rate of at least once per hour; maintaining the culture over many generations in the presence of a carbon substrate in the culture medium; and harvesting cells loaded with hydrocarbons or lipids.    USE - The process is useful for culturing microalgae of Botryococcus for the production of fat or hydrocarbon, and for the production of biofuel.    ADVANTAGE - The process provides microalgae of Botryococcus with high yield and is simple.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a cultivable microalgae corresponding to one of the strains filed with the Culture collection of Algae and Protozoa (CCAP) comprising strain of Botryococcus sudeticus deposited under NO:CCAP 807/4; a strain of Botryococcus braunii deposited under NO:CCAP 807/5; or a strain of Botryococcus braunii deposited under NO:CCAP 807/6.
NOVELTY - A system comprising a staged treatment of biomass for biogas (157) producing plants, where the staged treatment comprises at least two separate chambers, where the biomass in the first chamber (117) is conditioned by an air and/or a gas stream (119), where dissolved acid gases such as e.g. carbon dioxide (CO2) are stripped off, the biomass is further led to the second chamber (123) and conditioned by an air and/or a gas stream, where basic gases such as e.g. ammonia (NH3) are stripped off from the biomass.    USE - As staged treatment of biomass for biogas producing plants (claimed), where biomass includes manure, industrial waste, straw and organic waste, and is used for production of biogas, as a source for biologic de-nitrification and as a fertilizer on farmland without veterinarian restrictions.    ADVANTAGE - The system is very effective and increases yield, when the mass has a short treatment time in the chamber. The invention ensures a high level of hygiene and decomposition of infectious substance, since some bacteria, viruses and parasites die relatively fast when heated to greater than or equal to 70 degrees C.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a staged treatment of biomass for biogas producing plants, involving conditioning the mass by an air and/or a gas stream, where dissolved acid gases such as e.g. CO2 are stripped off; and conditioning the mass by an air and/or a gas stream, where basic gases such as e.g. NH3 are stripped off from the biomass.    DESCRIPTION OF DRAWING(S) - The figure shows a view of a system.    Reaction tank (103)    Separator (107)    Pipeline (109)    First chamber (117)    Gas stream (119)    Second chamber (123)    Biogas (157)
NOVELTY - The device has a heating gasification furnace (1) provided with a heat exchange chamber. Upper part of a buffer tank (3) is provided with a heat preservation material layer. A heating gasification furnace body is provided with a vertical storage hopper. The heat exchanging chamber is provided with a gas buffer chamber. A flue pipe (105) is arranged on the gas buffer chamber. Bottom part of a combustion chamber is provided with an ignition channel. A standing separation chamber is provided with a clapboard and a biological heavy tar outlet.    USE - Rural resident counter biomass waste resource pyrolysis gasification heating device.    ADVANTAGE - The device ensures that agricultural waste is converted into biological fuel gas, tar, acetic acid and hot water resource for a rural resident area with large production. The device is environment-friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a rural resident counter biomass waste resource pyrolysis gasification heating device.    Heating gasification furnace (1)    High-temperature mixed gas separator (2)    Buffer tank (3)    Flue pipe (105)    Heat exchange water outlet (2022)
NOVELTY - Proposed method consists in grinding organic origin stock elements to nanoparticle radius of not over 100 nm. Liquid-packed ring pumps are used to created rarefied atmosphere deprived of oxygen and containing water vapors. Fuel is minced in said atmosphere. Surface of produced nanoparticles is coated with monolayer of sorbed water molecules. Sorbed water molecules dissociate in rarefied atmosphere into OH radial and atoms of hydrogen or its isotopes. Note here that atoms of hydrogen or its isotopes penetrate into fuel nanoparticles to ne accumulated therein. Produced fuel particles are mixed with ethanol to produce homogeneous mix.    USE - Machine building.    ADVANTAGE - Higher calorific value, pollution-free fuel. 1 cl, 2 dwg, 4 tbl
NOVELTY - Invention relates to feed production and bioenergetics, as well as chemical and petrochemical industries. Proposed method comprises processing initial stock containing hydrocarbons by affecting them by low-temperature plasma of electric discharge with E/N parameters varying from 1 x 10-16 to 20 x 10-16 V x cm2, where E is electric field intensity and N is total concentration of molecules and atoms in plasma, adding catalysts to said raw stock and chemicals changing solution pH and ionic force. Proposed device is built around electric-discharge plasma power supply, fluid component preparation system, gas component preparation system and plasmachemical reactor. Electric-discharge plasma power supply represents source that allows electric discharge firing in continuous or intermittent pulse mode.    USE - Process engineering.    ADVANTAGE - Splitting of long organic molecules in variable treatment conditions. 6 cl, 4 dwg
NOVELTY - Method of manufacturing an organic acid, involves extracting rumen fluid from the ruminant, and reacting the extracted fluid with a cellulose containing waste material.    USE - The method is useful for manufacturing organic acid chosen from acetic acid, propionic acid, and a butyric acid, preferably acetic acid which is used as a raw material for methane fermentation (claimed).    ADVANTAGE - The method improves quality and yield of the raw materials, and is rapid and suitable for industrial production of fuel gas and electricity as end products.
NOVELTY - Formula comprises high synthetic fuel (HDS), low synthetic fuel (LDS) and additives.    USE - The formula is useful: for producing fully synthetic, joint jet and diesel liquid fuel by utilizing biomass, municipal waste, natural gas or coal feed stocks (claimed) which is used universally; to meet joint battlefield use fuel of future or single battlefield fuel strategic requirements; and as ideal rocket fuel.    ADVANTAGE - The formula: utilizing HDS and LDS blend provides jet, rocket and diesel fuel of standard density and low temperature and higher stability and good seal swelling properties thus achieving thermal stability and preventing leaking fuel form jet fuel tank; has highly reproducible properties, freeze points and flash points which permit ignition and sustained combustion at -47 degrees C; provides joint fuel with existent gum, particulate, filtration time, water reaction and separation rating that complies with jet and rocket fuel specifications; is prepared from commercial available fuel stocks or co-processed using currently available chemical processes; allows rapid deployment and logistic enhancement for military and emergency aid environments where various types of equipment can be operated with one fuel; and provides composition of matter for both commercial and military jet and diesel fuels.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method of fuel formulation that results in smoke point, naphthalenes, jet fuel thermal oxidation tester pressure change and thermal stability rating that meets jet and rocket fuel specifications.
NOVELTY - Hydrothermally processing biomass, comprises introducing a biomass feed having a water to biomass ratio of at least 1:1 into a reaction zone, hydrothermally treating the biomass feed under effective hydrothermal treatment conditions to produce a multiphase product, where the multi-phase product includes a solids portion containing at least 80% of the phosphorus content of the biomass feed, and separating the multi-phase product to produce at least a gas phase portion, a liquid hydrocarbon product and the solids portion.    USE - The method is useful for hydrothermally processing a biomass (claimed) for producing hydrocarbon product as distillate fuel.    ADVANTAGE - The method provides biomass without vaporizing water in an economical manner.    DETAILED DESCRIPTION - Hydrothermally processing biomass, comprises: introducing a biomass feed having a water to biomass ratio of at least 1:1 into a reaction zone, where the biomass feed has a phosphorus content, hydrothermally treating the biomass feed under effective hydrothermal treatment conditions to produce a multiphase product, where the multi-phase product includes a solids portion containing at least 80% of the phosphorus content of the biomass feed, and separating the multi-phase product to produce at least a gas phase portion, a liquid hydrocarbon product, and the solids portion; adding a multivalent metal to a biomass feed having a phosphorus content, contacting the biomass feed with water in the presence of the multivalent metal under effective hydrothermal treatment conditions to produce a multi-phase product; or contacting an algae-containing feed having a phosphorus content with water under effective hydrothermal treatment conditions to produce a multi-phase product, and recycling phosphorus from the solids portion to an algae process.
NOVELTY - The apparatus (101) has solid-liquid separator (10) which separates sewage (1) into solid and liquid. Souring tank (20) performs souring of thickened sludge (3) maintained by predetermined temperature. Mixing tank (30) separates fermentation gas contained in mixing water which mixes solid-liquid-separation water (2) and souring treated water (4) processed by souring tank. Methane fermentation processing tank (40) performs methane fermentation treatment of mixing tank exit water (5) from which fermentation gas is separated.    USE - Organic-waste-water processing apparatus for methane fermentation treatment of low concentration organic waste water e.g. sewage. Can also be used in treatment of domestic waste water.    ADVANTAGE - The low concentration organic waste water can be applied to methane fermentation treatment in low water temperature. Thus the electricity cost of installation and sludge-disposal cost can be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for organic-waste-water processing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the organic waste-water processing apparatus.    Sewage (1)    Solid-liquid-separation water (2)    Thickened sludge (3)    Souring treated water (4)    Mixing tank exit water (5)    Solid-liquid separator (10)    Souring tank (20)    Mixing tank (30)    Methane fermentation processing tank (40)    Organic-waste-water processing apparatus (101)
NOVELTY - The system (10) has housing assembly (80) that comprises three internal chambers, upper diving plate (110) and lower dividing plate (108). The upper and lower dividing plates comprise multiple through holes to allow aqueous solution to flow and circulate through three internal chambers. A hydrogen generator (20) comprises outlet (54) and inlet (52) positioned below outlet. The hydrogen generator serves as electrolysis cell to generate oxygen and hydrogen gas with electric current from power source being passed through aqueous solution.    USE - Hydrogen system for internal combustion engine of vehicle. Uses include but are not limited to truck, sport utility vehicle, motorcycle, aircraft and boat.    ADVANTAGE - Since the hydrogen generator serves as electrolysis cell to generate oxygen and hydrogen gas with electric current from power source being passed through aqueous solution, the atomization of fuel with hydrogen gas can be increased so as to achieve more efficient burning in the engine and carbon build-up can be reduced. The polluting carbon emissions as result of the combustion process can be reduced and combustion efficiency can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the hydrogen system.    Hydrogen system (10)    Hydrogen generator (20)    Inlet (52)    Outlet (54)    Housing assembly (80)    Lower dividing plate (108)    Upper dividing plate (110)
NOVELTY - The furnace has a furnace top panel (13) connected with a gasifying chamber corresponding to a furnace opening. A clapboard (16) is provided with a secondary air supply conical hopper (21). A big bottom is supported on the secondary air supply conical hopper in the clapboard. A fire tube (9) is provided with a secondary space that is opened with a round hole. The secondary air supply conical hopper comprises multiple secondary air supply holes (17). A secondary air pipe (19) is connected with a gasification chamber part.    USE - Cooking and warming dual-purpose biomass gasification furnace.    ADVANTAGE - The furnace is wide in fuel adaptability and easy to operate, and occupies less space.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a cooking and warming dual-purpose biomass gasification furnace.    Fire tube (9)    Furnace top panel (13)    Clapboard (16)    Secondary air supply holes (17)    Secondary air pipe (19)    Secondary air supply conical hopper (21)
NOVELTY - Compost fermentation device comprises a compost fermentation device (1) and a biogas fermentation device (2). The compost fermentation device is set with an evaporator (3). The biogas fermentation device is set with a condenser (4). The evaporator and the condenser are respectively connected with a compressor (5) through a pipeline. The evaporator, the condenser and the pipeline are provided with thermal phase transition working fluid.    USE - The device is useful for increasing temperature of biogas fermentation material.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the compost fermentation device for increasing temperature of biogas fermentation material.    Compost fermentation device (1)    Biogas fermentation device (2)    Evaporator (3)    Condenser (4)    Compressor (5)
NOVELTY - The furnace has a lower furnace body provided with a feeding port. An operating hole is formed on an upper furnace body that is provided with an air outlet of an annular channel. A tower-shaped fire grate is arranged at a bottom part of a hearth. A lower end of the grate is inserted into an inner side of a rotating shaft. A grate rotating device is connected with a middle furnace body. Ventilation holes are formed on multiple layers of the fire grate. The upper furnace body is connected with an eccentric wheel that is fixed on an output shaft of a driving device.    USE - Biomass gasification furnace.    ADVANTAGE - The furnace has simple structure and convenient operation, and reduces labor intensity of an operator, and improves combustion efficiency of fuel. The furnace is safe and reliable to use.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial sectional view of a biomass gasification furnace.
NOVELTY - An overlapped biomass electric chemical extracting cogeneration device comprises a sealed furnace body (1) having a combustion unit comprising a combustion chamber (2) having a feeding cavity (3) on its lower part. The feeding cavity having bottom part provided with a feeding rail (31) set with a carbon tank (34). The carbon tank is connected with the feeding track. The combustion unit has a gas collecting pipe connected to the carbon tank and having an air inlet hole. The combustion chamber is at least provided with three processing layer having same height.    USE - An overlapped biomass electric chemical extracting cogeneration device.    ADVANTAGE - The device is automatic and continuous, has high production efficiency and controllable process, can easily separate chemical raw material and flammable substance, and has high coefficient of recovery.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of an overlapped biomass electric chemical extracting cogeneration device.    Sealed furnace body (1)    Combustion chamber (2)    Feeding cavity (3)    Feeding rail (31)    Carbon tank (34)
NOVELTY - The method involves utilizing synthesis gas as a raw material, where reaction temperature of the synthesis gas is 120-300 degrees Celsius, and the synthesis gas is one of biomass gas and waste gas from fossil raw mineral material. Porous diatomite is taken as a catalyst carrier by a microwave to synthetic high efficiency and high quality oil in a liquid-phase medium, where the liquid-phase medium is one of diesel oil and heavy oil. A catalyst and the catalyst carrier are suspended in the liquid medium, where the catalyst is one of manganese iron and cobalt ruthenium.    USE - High quality and high efficiency diesel synthetic method.    ADVANTAGE - The method enables synthesizing high quality and high efficiency diesel in convenient and simple manner with reduced cost, reducing reaction time and energy consumption, thus achieving high transformation ratio. The method enables making a prepared product with high quality. The raw material synthesized gas can be prepared according to biomass raw material, waste raw material and coal and fossil mineral raw material.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a high quality and high efficiency diesel synthetic device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a high quality and high efficiency diesel synthetic device.'(Drawing includes non-English language text)'
NOVELTY - The system has a biomass raw material passing through a spiral feeding machine (1) in a biomass gasification furnace (2) by a cyclone separator (3). The cyclone separator enters into a dust air pre-heater (4). A gas purifier (6) is inserted into an air storage cabinet (8) through a draught fan (7). A fuel gas internal combustion engine (9) is linked with the storage cabinet. A power output shaft (10) drives a generator (11) by utilizing chemical energy of biomass gas. A speed reducer reaches proper rotating speed after driving the spiral feeding machine for making high-density biomass fuel.    USE - High density biomass fuel preparation system.    ADVANTAGE - The system can realize zero-power consumption and local extruding biomass particle, is flexible to operate, and reduces biomass fuel cost.    DETAILED DESCRIPTION - The cyclone separator is a two-stage cyclone separator.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a high density biomass fuel preparation system.    Spiral feeding machine (1)    Biomass gasification furnace (2)    Cyclone separator (3)    Dust air pre-heater (4)    Gas purifier (6)    Draught fan (7)    Air storage cabinet (8)    Fuel gas internal combustion engine (9)    Power output shaft (10)    Generator (11)
NOVELTY - The method involves adopting domestic waste, food waste, municipal sludge, biomass and carbon-containing waste as raw material under air i.e. oxygen, induced by microwave. Steam or water gas or nitrogen replacement gasification furnace is utilized such that water gas is shifted for reaction, and the air is isolated. The raw material is added with catalyst or absorbing material, or not added with catalyst or absorbing material.    USE - High quality and high efficiency water gas transformation method.    ADVANTAGE - The method enables reducing refining cost of subsequent process, so that fischer-tropsch synthesis unit can be prepared with low cost and high quality of fuel oil resource to replace scarce substituted.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a gasification system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a gasification system.'(Drawing includes non-English language text)'
NOVELTY - The method involves discharging water and tar via a PVC connecting pipe connected between a biomass gasification furnace and a gas boiler of the gasification furnace.    USE - Method for processing water and tar in a PVC connecting pipe connected between a biomass gasification furnace and a gas boiler.
NOVELTY - Biomass is hydrolyzed (2) using a catalyst before hydrotreating (3) to produce biodiesel. The produced hydrogenated biodiesel is recycled during the process, and biodiesel is produced.    USE - Manufacture of biodiesel.    ADVANTAGE - The biodiesel has excellent oxidation stability and is manufactured efficiently and economically with reduced greenhouse gas generation.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the biodiesel manufacturing process. (Drawing includes non-English language text)    Biomass (1)    Hydrolysis process (2)    Hydrotreatment process (3)    Hydrothermal process (4)    Hydrogen (AA)
NOVELTY - Converting synthesis gas to an oxygenate, comprises contacting a mixture of hydrogen and carbon monoxide with a transition metal containing, Anderson-type heteropoly compound catalyst under conditions of temperature, pressure and gas hourly space velocity sufficient to convert the mixture to at least one alcohol, where the alcohol contains 1-6 carbon atoms, and the catalyst is (I).    USE - The process is useful for converting synthesis gas to an oxygenate.    DETAILED DESCRIPTION - Converting synthesis gas to an oxygenate, comprises contacting a mixture of hydrogen and carbon monoxide with a transition metal containing, Anderson-type heteropoly compound catalyst under conditions of temperature, pressure and gas hourly space velocity sufficient to convert the mixture to at least one alcohol, where the alcohol contains 1-6 carbon atoms, and the catalyst is of formula ((A)x(M1MoyW6-y)M2) (I).    A = H+, ammonium ion or alkali metal ion;    M1 = at least one of Al, Zn or transition metal including Fe, Ru, Cr, Rh, Cu, Co, Ni, Pd or Ir;    M2 = optional modifier that is at least one metal comprising alkali metal, alkaline earth metal or transition metal including Re, Cr, Pd, Ni, Ir or Co;    x = 3-4; and    y = 0-6.
NOVELTY - The device has a rotary preheat chamber located in a hot flue gas chamber. A rotary dry distillation chamber is located inside a combustion chamber. An end of the distillation chamber is connected to bottom of a middle hopper through a front roller and a screw conveyor. Another end of the distillation chamber is connected to a discharge chamber through a back roller. The distillation chamber carbonizes preheated biomass raw material e.g. livestock manure. A cooling chamber is located below the discharge chamber and cools the biochar formed through an activation reaction.    USE - Device for manufacturing biochar using livestock manure, crop stalks and bagasse.    ADVANTAGE - The device can manufacture the biochar in a cost effective manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a device for manufacturing biochar.
NOVELTY - A fuel cell system consists of modifier having autothermal reforming catalyst which converts fuel gas into reformed gas containing carbon monoxide and hydrogen, and fuel cell using the reformed gas. The catalyst contains 0.05-20 %mass of nickel supported on carrier comprising lanthanum strontium aluminate (I). Partial oxidation reformation is performed by heating with supply of fuel gas and oxygen-containing gas. Autothermal reformation is performed by supplying water and steam reformation is performed by stopping the supply of oxygen-containing gas.    USE - Fuel cell system.    ADVANTAGE - The fuel cell system has improved performance.    DETAILED DESCRIPTION - A fuel cell system consists of modifier having autothermal reforming catalyst which converts fuel gas into reformed gas containing carbon monoxide and hydrogen, and fuel cell using the reformed gas. The catalyst contains 0.05-20 %mass of nickel supported on carrier comprising lanthanum strontium aluminate of formula: La1-xSrxAlO3 (I) obtained by substituting strontium in perovskite type lanthanum aluminate. Partial oxidation reformation is performed by heating with supply of fuel gas and oxygen-containing gas. Autothermal reformation is performed by supplying water and steam reformation is performed by stopping the supply of oxygen-containing gas.    x=0.05-0.3.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic block diagram of the fuel cell system. (Drawing includes non-English language text)    Fuel cell system (1)    Modifier (2)    Fuel cell (3)    Supply portion (4)    Temperature sensors (5,6)
NOVELTY - The unit has a tank main portion (102) that stores biomass (140). A heating unit (108) is used to heat the biomass at 150-250 degrees C and equipped with the heat exchanger tube (106) for indirectly heating the region including the region in which the biomass is stored in the tank main portion in the range of non-carbonizing temperature. The heat exchanger tube is inserted inside the tank main portion. A jacket (109) is set in outer surface of the tank main portion. A water vapor supply unit (110) is used to supply water vapor heated by the jacket.    USE - Storage unit for storing biomass such as coppiced timber, waste material wood, driftwood, grass, waste material, sludge, tire, and fuel for electric power generation system.    ADVANTAGE - Since the heat exchanger tube is used for indirectly heating the region including the region in which the biomass is stored in the tank main portion in the range of non-carbonizing temperature, the biomass can be pulverized effectively and heated efficiently, and the possibility that the biomass stored in the tank main portion can burn can be reduced.    DETAILED DESCRIPTION - The temperature measurement unit (114) is used to detect the temperature of atmosphere region emitting the biomass. The heating unit is controlled by control unit (130) based on detection result. An inert gas supply unit (120) is used to supply inert gas to the region in which the biomass is stored in the tank main portion. An INDEPENDENT CLAIM is included for pre-processing unit.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass storage unit. (Drawing includes non-English language text)    Tank main portion (102)    Heat exchanger tube (106)    Heating unit (108)    Inert gas supply unit (120)    Control unit (130)    Biomass (140)
NOVELTY - The unit has a biomass storage tank (24) which stores biomass (140). A before-storage supply unit supplies biomass to biomass storage tank. An after-storage supply unit supplies the biomass stored in biomass storage tank to pulverization unit. A heating unit (100) heats biomass in before-storage supply unit, biomass storage tank and after-storage supply unit in the range of non-carbonizing temperature. A heat source supplies air heated by cover. The biomass is heated by supplying air heated by heat source inside cover.    USE - Pre-processing unit of electric power generation system.    ADVANTAGE - Since the heating unit heats biomass in before-storage supply unit, biomass storage tank and after-storage supply unit in the range of non-carbonizing temperature, the biomass can be pulverized efficiently and generation of bad influence with respect to the pre-processing apparatus can be reduced. The energy efficiency can be improved.    DETAILED DESCRIPTION - The unit has heating unit that includes cover which covers the outer periphery of conveyance path of biomass. The heating unit heats the biomass at 150-250 degrees C. The temperature detection unit detects the temperature of the atmosphere of terminus vicinity of region which heats the biomass. The biomass and fossil fuel are burned in air or waste gas. The temperature rose is used for the heating unit as heat source. The heating unit is controlled based on the detection result of temperature detection unit, and provided with control portion.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the pre-processing unit. (Drawing includes non-English language text)    Biomass storage tank (24)    Feeder (25)    Heating unit (100)    Piping (108)    Biomass (140)
NOVELTY - Ground oil composite regenerative fuel comprises (pts.wt.) methanol (35-60), ferrocene (0.1-0.8), cosolvent (6-15), biological diesel oil (5-10), aromatic hydrocarbon (5-10), emulsifier (1-5), and oil (24-45). The cosolvent is ethyl acetate, butyl acetate, ethylene glycol methyl ether, ethylene glycol ethyl ether, ethylene glycol butyl ether, diethylene glycol ethyl ether, diethylene glycol butyl ether, propylene glycol methyl ether, propylene glycol ethyl ether, propylene glycol butyl ether, and/or propylene glycol methyl ether.    USE - Ground oil composite regenerative fuel.    ADVANTAGE - The ground oil composite regenerative fuel has high heat value. The methanol and hogwash are regenerative resources, thus lowering production cost and saving non-renewable resources.    DETAILED DESCRIPTION - Ground oil composite regenerative fuel comprises (pts.wt.) methanol (35-60), ferrocene (0.1-0.8), cosolvent (6-15), biological diesel oil (5-10), aromatic hydrocarbon (5-10), emulsifier (1-5), and oil (24-45). The cosolvent is ethyl acetate, butyl acetate, ethylene glycol methyl ether, ethylene glycol ethyl ether, ethylene glycol butyl ether, diethylene glycol ethyl ether, diethylene glycol butyl ether, propylene glycol methyl ether, propylene glycol ethyl ether, propylene glycol butyl ether, propylene glycol methyl ether, dipropylene glycol ethyl ether, and/or propylene glycol butyl ether. The aromatic hydrocarbon is benzene, toluene, or xylene. The emulsifying agent is polyoxyethylene nonyl phenyl ether with polymerization degree of 9-40, octyl phenol polyethenoxy ether, and/or lauryl alcohol polyoxyethylene ether with polymerization degree of 10-40. An INDEPENDENT CLAIM is included for preparation of ground oil composite regenerative fuel by adding ferrocene in methanol; stirring to dissolve; adding auxiliary solvent, biodiesel, aromatic hydrocarbon, emulsifier and oil; mixing; filtering resulting mixed solution; condensing; and drying filtrate.
NOVELTY - A feedstock (A) comprising at least one biomass derived oils and fatty materials, and feedstock (B) comprising at least one biomass derived polyol are contacted with hydrotreated catalyst in presence of hydrogen in a reaction zone under reaction condition sufficient for converting at least one portion of biomass derived oils and fatty materials into diesel fuel range hydrocarbons product, and at least one portion of the biomass derived polyol is converted into gasoline fuel range hydrocarbons product.    USE - Process of co-producing renewable diesel and gasoline.    ADVANTAGE - The process of co-producing renewable diesel and gasoline is enabled.
NOVELTY - A wood pellet producing method involves pulverizing a timber to form wood powder. A selective non-catalytic reducing agent having amino group is projected in the wood powder. The non-catalytic reducing agent having the amino group is compressed in the wood powder. The wood powder including the non-catalytic reducing agent is dried.    USE - Method for producing a wood pellet including a selective non-catalytic reducing agent having amino group.    ADVANTAGE - The method enables adding the non-catalytic reducing agent having the amino group to the wood powder, so that nitrogen oxide, silicon oxide and carbon monoxide generated during combustion of wood are removed, and the produced wood pellet is environment-friendly and economic to utilize.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a method for producing a wood pellet. '(Drawing includes non-English language text)'
NOVELTY - The method involves constructing cushion layer according to shape of building. The cushion layer is oppositely fixed to ecological concrete plate to form a hollow cavity. The concrete plate is made of zeolite, porcelain granule and concrete in the ratio of 30:30:40. The plate is fixed on both sides of concrete panel. The plate is installed in ecological concrete slot provided in the hollow cavity.    USE - Construction method of ecological concrete wall used for sewage treatment in river or lake bang pond.    ADVANTAGE - The cost of the concrete wall is reduced and wall is convenient to maintain.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating construction process of ecological concrete wall.
NOVELTY - Briquette binder, which is prepared by cassava residue, is claimed.    USE - Used as briquette binder.    ADVANTAGE - The method is simple and economical, utilizes easily available raw materials, and provides socioeconomic benefit.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) preparing the briquette binder, comprises: (a) drying cassava residue, crushing by a pulverizer, (b) weighing the cassava dregs after crushing and uniformly mixing with water, and (c) adding sodium hydroxide into the mixture, boiling and stirring to obtain a light yellow viscous substance;    (2) biomass briquette, comprising (in wt.%) briquette binder (15-20) and anthracite (80-85); and    (3) preparing the biomass briquette, comprising: (i) uniformly mixing briquette and anthracite, (ii) extrusion molding in a molding machine, and (iii) drying in an oven at 120-140 degrees C for 2-3 hours.
NOVELTY - The reactor has a pH value and temperature detection device that is provided in the upper end of reactor main portion. A positive pressure protecting device is connected with upper end of material liquid tank. The upper end of central pipe is provided with scum collecting port and scum suction port. A branch pipe is connected with discharge pipe of material liquid tank. A material liquid distributing pipe is connected with material liquid circulating pump. A distributor is connected with inclined anti-filled mouth. The material circulation pump is connected with suction port.    USE - Straw biogas reactor.    ADVANTAGE - The stability of the biogas in the reactor is improved. The production efficiency of the straw biogas reactor is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the straw biogas reactor.
NOVELTY - A carbon dioxide direct absorption method involves absorbing carbon dioxide and sulfur dioxide discharged from a crystal chemical fertilizer plant.    USE - Method for direct absorption of carbon dioxide of crystal chemical fertilizer plant.    ADVANTAGE - The method enables direct absorption of carbon dioxide, thus effectively controlling the pollution and maintaining ecological balance.
NOVELTY - A synthetic biological compound alcohol-based fuel reactor has a synthesis kettle, a separator, a refining kettle, a reaction kettle and an alcohol fuel tank that are connected in series by a pipeline. The synthesis kettle is provided with a grease metering groove, and the refining kettle is provided with a first stirring device. A refining kettle body is set with a measuring tank, and the refining kettle is provided with a second stirring device. The kettle body is set with an additive metering groove, and the reaction kettle is provided with a third stirring device.    USE - Synthetic biological compound alcohol-based fuel reactor.    ADVANTAGE - The reactor has simple structure, reasonable design and convenient operation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a synthetic biological compound alcohol-based fuel reactor.
NOVELTY - Improved method for preparing valsartan, comprises (i) adding (N-(1-valeryl)-N-(4-(2-(5-cyano)phenyl)benzyl)-L-valine) methylvalsartan intermediate oily substance, sodium azide, triethylamine hydrochloride and high-boiling-point ether, (ii) carrying out saponification reaction with sodium hydroxide solution, processing and crystallizing with 37% concentrated hydrochloric acid, dissolving and extracting the reactant with chloroalkane to obtain a valsartan crude product, and (iii) purifying the crude product by dissolving the valsartan crude product with mixed solvent of ester and water.    USE - The method is useful for preparing valsartan in an improved manner.    ADVANTAGE - The method: requires reduced time, and reduced energy consumption; does not cause environmental pollution; and produces valsartan with high yield and high purity.    DETAILED DESCRIPTION - Improved method for preparing valsartan, comprises (i) adding (N-(1-valeryl)-N-(4-(2-(5-cyano)phenyl)benzyl)-L-valine) methylvalsartan intermediate oily substance, sodium azide, triethylamine hydrochloride and high-boiling-point ether, controlling temperature to 160-180 degrees C and reacting for 5-7 hours, and directly cooling to 60-65 degrees , (ii) carrying out saponification reaction under thermal insulation for 5-6 hours at 60-65 degrees C with 3-4% aqueous sodium hydroxide solution, directly processing and crystallizing with 37% concentrated hydrochloric acid, dissolving and extracting the reactant with chloroalkane under vacuum concentration at a temperature not greater than 30 degrees C to obtain a valsartan crude product, and (iii) purifying the valsartan crude product using a mixed solvent of ester and water as a solvent, preferably dissolving the valsartan crude product at 40-45 degrees C, insulating heat and stirring for 5 hours, directly and slowly cooling to 0-5 degrees C, and centrifuging to obtain a high-purify valsartan.
NOVELTY - A plasmid pRC11 having a 48868 base pair sequence (SEQ ID No: 1) fully defined in the specification, is new.    USE - The plasmid pRC11 is useful for preparing genetically engineered bacteria used for degrading halogenated, preferably chlorinated aliphatic hydrocarbons particularly dichloromethane, bromochloromethane, ethylene dichloride or dichloroethene (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) genetically engineered bacteria, comprising the plasmid pRC11; and    (2) use of genetically engineered bacteria for degrading halogenated hydrocarbons.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic representation of plasmids pRC11 and pJP4.
NOVELTY - A biodiesel preparing method involves providing and pre-processing crude raw material to remove impurity. A pre-treated raw material is added to a reaction kettle. Methanol is added to the reaction kettle and pre-processed. The mixture in the reaction kettle is heated for supplementing methanol gas. Mixture of potassium hydroxide and sodium hydroxide are added to reactant and reacted. The methanol is recycled, and glycerol is separated by gravity settling to obtain crude fatty acid methyl ester. The obtained crude fatty acid methyl ester is purified and distilled to obtain biodiesel.    USE - Method for preparing biodiesel with high purity.    DETAILED DESCRIPTION - A biodiesel preparing method involves providing and pre-processing crude raw material to remove impurity. The pre-treated raw material is added to a reaction kettle. Methanol is added to the reaction kettle according to 0.1-2 weight percent of concentrated sulfuric acid and pre-processed at 70-100 degrees C for 30 minutes to 2 hours, where weight ratio of the raw material to the methanol is 1:1-1:20. The mixture in the reaction kettle is heated at 110-130 degrees C under normal pressure for supplementing methanol gas. Supplementation of the methanol gas is stopped under reaction temperature until liquid phase system value is less than 2. Reactant is cooled to 70 degrees C. Mixture of potassium hydroxide and sodium hydroxide are added to the reactant to make power of hydrogen value of the reaction material in the reaction kettle to be 8-9 at 70 to 90 degrees C, and are reacted for 2-3 hours. The methanol is recycled, and glycerol is separated by gravity settling to obtain crude fatty acid methyl ester. The obtained crude fatty acid methyl ester is purified and distilled to obtain biodiesel.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of a method for preparing biodiesel.'(Drawing includes non-English language text)'
NOVELTY - Processing dewatered sludge having water content of 70-85%, involves adding dessicant to the dewatered sludge, and stirring the mixture to obtain mixed sludge having water content of 50-60%, and (b) drying the mixed sludge to obtain dried granular sludge having water content of less than or equal to 45%.    USE - The method is useful for processing dewatered sludge having water content of 70-85%, which is used for preparing organic fertilizer (all claimed).    ADVANTAGE - The method saves energy and resource, and is environmentally-friendly and cost-effective.
NOVELTY - Method for producing fuel ethanol, involves processing starch raw material, adjusting pH of the product using sulfuric acid to 4-4.5, saccharifying the product using alpha -1,4-glucose hydrolase at 50-70 degrees C for 30-60 minutes, cooling the solution to 28-32 degrees C, adding 30-40% of active dry yeast and urea into tank, adding the product into the tank, fermenting the mixture, distilling and dehydrating the fermented product in presence of carbon dioxide, condensing the alcohol steam through degassing section condenser to get crude alcohol, and purifying the alcohol.    USE - The method is useful for producing fuel ethanol.    ADVANTAGE - The method utilizes the resources completely, consumes less energy and enables to produce useful substance from the generated waste gas and waste substances.    DETAILED DESCRIPTION - Method for producing fuel ethanol, involves (a) uniformly stirring starch raw material and alpha -amylase, obtaining the powder residue with dry substance content of 20-34%, pre-heating the product to 70-85 degrees C, adding the product to pre-liquefying tank and stirring uniformly, heating the powder residue to 80-90 degrees C, subjecting the product to low voltage steam spraying and liquefying process, maintaining the product at 100-110 degrees C for 1-2 hours, boiling and curing the product, reducing the temperature of the product to 65-80 degrees C and cooling the product, (b) adjusting pH of the product using sulfuric acid to 4-4.5, saccharifying the product using alpha -1,4-glucose hydrolase at 50-70 degrees C for 30-60 minutes and cooling the solution to 28-32 degrees C, (c) adding 30-40% of active dry yeast and urea into tank, adding the product into the tank, and fermenting the mixture, and (d) distilling and dehydrating the fermented product in presence of carbon dioxide, condensing the alcohol steam through degassing section condenser to get crude alcohol, and purifying the alcohol.
NOVELTY - Method for preparing balsamine nutrient fertilizer, involves using (in wt.%): cake powder (2-6), bean pulp powder (4-6), corn powder (6-8), peanut powder (4-6), sweet potato leaf powder (6-8), chicken manure (8-12), duck manure (7-9), wheat straw powder (9-11), carrot leaf powder (11-13), bone powder (6-8), peanut cake powder (-3), sesame cake powder (3), pumpkin powder (3 to -5), radix aconite (2-4), blue broad leaf plant powder (4-6), radix sophorae flavescentis powder (7-9), Camellia (0.4-0.6), and Coptis (0.4-0.6).    USE - The method is useful for preparing balsamine nutrient fertilizer.    ADVANTAGE - The method prepares fertilizer which is rich in nutrient and easy to cause balsamine flower bud, and overcomes low in yield, blade wilt, falling, small flower and fine root development, slow growth, and rotten plant death.
NOVELTY - A felodipine preparation method involves utilizing 2,3-dichlorobenzaldehyde and methyl acetoacetate as initial raw materials. The raw materials are made to undergo Knoevenagel reaction to obtain 2-(1-(2,3-Dichloro-phenyl)-methylidene)-3-oxo-butyric acid methyl ester. Cyclization with 3-amino-but-2-enoic acid ethyl ester produces felodipine by the Michael reaction.    USE - Method for preparing felodipine.    ADVANTAGE - The method enables preparing the felodipine in short route and short period and simple manner, improving operation safety and reducing environmental pollution and toxicity residue after a treatment process.
NOVELTY - Preparing L-ascorbic acid-2-phosphate sodium includes dissolving L-ascorbic acid and anhydrous calcium chloride into deionized water to form suspension, and controlling the suspension at 0-20 degrees C; dropping sodium hydroxide solution into the suspension, reacting; and filtering the reactant, and drying to obtain the L-ascorbic acid 2-sodium phosphate product.    USE - Method for preparing L-ascorbic acid-2-phosphate sodium (claimed).    ADVANTAGE - The method does not use organic solvent, increases phosphorylation reaction speed, shortens reaction time, simplifies operation procedure, and is safe to the environment.    DETAILED DESCRIPTION - Preparing L-ascorbic acid-2-phosphate sodium comprises:    (A) dissolving L-ascorbic acid and anhydrous calcium chloride into deionized water for 10-60 minutes in a mass ratio of 1:0.05-0.2:1-4 to form suspension, and controlling the suspension at 0-20 degrees C;    (B) dropping sodium hydroxide solution into the suspension, adjusting pH value to 5-9, controlling the suspension at 0-20 degrees C;    (C) adding sodium trimetaphosphate to the suspension processed in the step (B), where the mass ratio of sodium trimetaphosphate to L-ascorbic acid is 0.3-0.8:1, dropping sodium hydroxide solution to adjust the pH to 10-12, reacting for 2-5 hours to obtain a reactant, controlling the reaction at 20-40 degrees C, where the mass ratio of the sodium hydroxide solution to the L-ascorbic acid is 0.5-1.2:1; and    (D) filtering the reactant obtained in step (C) through a nano-filtration membrane, where the entrance of nano-filtration membrane is at 150-180 degrees C, the outlet of the nanofiltration membrane is at 50-70 degrees C, and the filtrate is obtained through filtering by using spray drying machine, where the drying step is carried out at 150-180 degrees C for 20-30 minutes to obtain the L-ascorbic acid 2-sodium phosphate product.
NOVELTY - Method for processing kitchen garbage, involves removing kitchen garbage, crushing the kitchen garbage, mixing the kitchen garbage with straw powder and limestone powder to obtain mixture, sterilizing the mixture, inoculating edible fungi strain into the sterilized mixture, obtaining edible fungi after spawn running and fruiting and recycling waste mushroom stick.    USE - The method is useful for processing kitchen garbage which is used as feed, fuel for normal pressure steam sterilizer, organic fertilizer and culture substrate (claimed).    ADVANTAGE - The mushroom produced by the method is cost-effective and has high yield.
NOVELTY - An organic fertilizer comprises (in parts weight) urea (10-20, preferably 15), potassium salt (15-40, preferably 30), organic material (30-70, preferably 50), humic acid salt (20-40, preferably 30), sulfate (0.3-4, preferably 2), borax (0.1-1, preferably 0.5), water ammonium molybdate (0.01-0.5, preferably 0.3) and nutrient powder (1-15, preferably 1.3).    USE - Organic fertilizer.    ADVANTAGE - The organic fertilizer is environmentally-friendly and economical.
NOVELTY - Additive comprises pulverized coal ash, wheat straw, urea, ammonium nitrate and magnesium chloride.    USE - The additive is useful for processing kitchen waste.    ADVANTAGE - The additive suppresses acidification of the compost, improves microbial activity, and reduces stabilization time. The method is rapid.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of using the above-cited additive, which involves (a) mixing the kitchen waste and grafted soil in the weight ratio of 1:(0.2-5), where the particle size of the mixture is not greater than 5 mm, (b) mixing the additive with the mixture in the weight ratio of 1:(1-6), (c) filling the obtained mixture into the compost reactor, and ventilating the compost reactor from the bottom portion of the reactor at 1-6 l/minutes, and (d) sampling the compost every 12 hours for one day, and turning the piles, where the composting reaction is carried until there is no degradation.
NOVELTY - A vehicle fuel oil comprises (in volume %) methyl alcohol (5-95) and additives (0.3-10.2).    USE - Vehicle fuel oil.    ADVANTAGE - The oil has high octane value, low energy consumption, and reduces discharging of polluted gas and prolongs service life of an automobile when the content of methyl alcohol is high. The oil ensures that the engine of the automobiles is prevented from being corroded and damaged during cold conditions.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing vehicle fuel oil.
NOVELTY - An Aspergillus aculeatus ZJ strain is new.    USE - Aspergillus aculeatus ZJ strain for preparing 5,7,8,4'-tetrahydroxyisoflavone (claimed).    ADVANTAGE - The strain provides strong-specificity and high-transforming-efficiency. The method has moderation condition, green process, simple process and device requirements and good application value.    DETAILED DESCRIPTION - Aspergillus aculeatus ZJ strain (CCTCC M2011264) is new. An INDEPENDENT CLAIM is included for preparing 5,7,8,4'-tetrahydroxyisoflavone which comprises (A) inoculating A. aculeatus ZJ strain to pagoda tree pod powder including genistein or genistin or extraction liquid, and transforming under predetermined condition, and separating and purifying obtained material to obtain 5,7,8,4'-tetrahydroxyisoflavone; (B) adding bacterial yeast of A. aculeatus ZJ to pagodatree pod powder including genistein or genistin or the extraction liquid, and performing biological transformation, separating and purifying obtained material to obtain 5,7,8,4'-tetrahydroxyisoflavone; or (C) adding enzyme liquid or powder obtained from A. aculeatus ZJ to pagodatree pod powder including genistein or genistin or extraction liquid, and performing biological transformation, separating and purifying obtained transformed liquid to obtain 5,7,8,4'-tetrahydroxyisoflavone.
NOVELTY - Biodiesel deodorizer comprises a pre-heater, a deodorizer, a first receiving tank and a second receiving tank, where the deodorizer top and the first receiving tank is connected with the first condenser, and the deodorizer bottom and the second receiving tank is connected to the second condenser. The output port of the preheater is connected to the top of the deodorizer, and the bottom of deodorizer is provided with a steam inlet and steam outlet.    USE - Used as a biodiesel deodorizer.    ADVANTAGE - The biodiesel deodorizer: is portable; is a low temperature wet deodorizer; and decreases the odor gas (aldehydes, ketones, etc.) partial pressure.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of the biodiesel deodorizer.
NOVELTY - Device for preparing fuel oil using waste cottonseed oil and acidified oil comprises a raw material tank (1) which is connected with a reaction tank (2) equipped with a stirrer through a pipeline. The outlet of the reaction tank is connected with a distillation device (3) through the pipeline. The reaction tank is provided with multiple feeding ports and a drain port.    USE - Used as a device for preparing fuel oil using waste cottonseed oil and acidified oil.    ADVANTAGE - The device is simple, convenient to use, and produces high quality product.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of the device for preparing fuel oil using waste cottonseed oil and acidified oil.    Raw material tank (1)    Reaction tank (2)    Distillation device (3)    Heating device (4)
NOVELTY - The solid fuel contains vegetable matter and a binder. Plastic waste is used as a binder the ratio of components in percent by mass is: vegetable matter 60-90 and plastic waste 3-40. Waste paper, wood shavings, grain husks, plant stems and peat can used as the vegetable matter. The fuel is in briquette or granules shape.    USE - Solid fuel for industrial, domestic and municipal purposes using plastic and vegetable waste.    ADVANTAGE - The waste material is used as binder.
NOVELTY - Providing a Bacillus on a surface, comprises: (a) providing Bacillus spores suspended in a liquid consisting essentially of water and at least one organic acid; and (b) applying the liquid to a surface environment either containing ammonia or being capable of generating ammonia, where the ammonia neutralizes the organic acid to enable the Bacillus spores and provide an enabled Bacillus on the surface environment.    USE - The method is useful for providing a Bacillus on a surface which is useful: to deodorize an animal waste which is animal feces and/or animal urine (claimed) (zootechnic applications), as well as agricultural soil or plant material for odor control in areas of high ammonia generation; and in environmental, agricultural, food and feed applications e.g. soil conditioning, antifungal treatment of plants, as a food or feed additive or preservative.    ADVANTAGE - The method utilizes the acid which lowers the pH so that the spores are inhibited from germination and growth, and prevented from spoilage by preventing unwanted microorganisms in the suspension.
NOVELTY - The method involves preparing multiple carbon nanotubes (CNTs) that are aligned vertically to plane of a substrate. An electrode layer is formed by attaching ionomer on surface of the carbon nanotubes on which the electrode catalyst is supported. The electrode layer is placed to face an electrolyte membrane (12) formed of another polymer electrolyte. The electrolyte membrane is bonded to the electrode layer by applying specific pressure between the electrolyte membrane and electrode layer. The substrate layer is removed after the bonding process.    USE - Method of producing fuel cell such as polymer electrolyte fuel cell.    ADVANTAGE - The characteristics of the fuel cell can be improved. The resistance of the fuel cell can be increased. The output efficiency of the cell can be improved. The manufacturing cost of the fuel cell can be increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of fuel cell.    Fuel cell (10)    Electrolyte membrane (12)    Anode electrode (14)    Cathode electrode (16)    Separators (22,26)
NOVELTY - Flowable, organic-based gel, comprises: (a) at least one flowable, organic gel forming ingredient; and (b) an amount of at least one biologically-active ingredient, which is stably and uniformly suspended in gel and is concentrated so as to be present in gel at an amount of 15-45 wt.% of gel, and gel has shear thinning viscosity and a yield value such that (i) the biologically-active ingredient does not redistribute in gel and remains substantially uniform in gel during standing, and (ii) gel is flowing liquid when in contact with aqueous environment of wastewater.    USE - The flowable, organic-based gel is useful for treating wastewater in systems, including septic tanks, cesspools and sewage systems (all claimed).    ADVANTAGE - The flowable, organic-based gel: avoids the utilization of enzyme stabilizer (borate), thus is environmentally friendly and consumer-friendly; can be easily and conveniently used; takes up less shelf space; can be stored in a single container, thus reducing the cost and environmental costs of large container; and provides uniform distribution/suspension of the biologically-active ingredients.    DETAILED DESCRIPTION - Flowable, organic-based gel, comprises: (a) at least one flowable, organic gel forming ingredient; and (b) an amount of at least one biologically-active ingredient, where the biologically-active ingredient is stably and uniformly suspended in the gel and is concentrated so as to be present in the gel at an amount of 15-45 wt.% of the gel, and the gel has a shear thinning viscosity and a yield value such that (i) the biologically-active ingredient does not redistribute in the gel (other than from diffusion effects) and thus remains substantially uniform in the gel during standing or until the force of gravity of buoyancy is applied that exerts a force greater than the yield stress (from yield value), and (ii) the gel is a flowing liquid when in contact with an aqueous environment of the wastewater.
NOVELTY - The device has a main tube whose two ends are provided with inlet and outlet. The main tube is provided with rotatable screw conveyers which are arranged in specific manner such that outward paths and return paths are vertically arranged. Horizontal discharge tubes (22) are attached at appropriate intervals along the lengthwise direction of main tubes. The horizontal discharge tubes are connected to main tube. Vertical tubes (23) are connected to ends of the horizontal tubes along vertical direction. A bottom collection tube is provided horizontally along bottom portion of main tube.    USE - Drying/carbonizing device for drying/carbonizing foodstuff waste materials such as watery organic refuse, sludge of sewage treatment plan, hen droppings and soybean curd residue.    ADVANTAGE - The drying and carbonizing process of foodstuff waste materials can be performed easily.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for drying/carbonizing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of drying/carbonizing device.    Burner (5)    Cylinder (6)    Horizontal discharge tube (22)    Vertical discharge tube (23)    Lower manifold (24)
NOVELTY - The method involves forming an integral molding of a fuel-supply board (101) and a reinforcement part (102). The integral molding is arranged at circumference of the fuel-supply board and the reinforcement part. The fuel-supply board is prepared with the reinforcement part that is provided with a junction part (103). A part and the reinforcement part of an end surface of the fuel-supply board are connected to the junction part. A unit battery is stacked on the fuel-supply board with the reinforcement part.    USE - Method for manufacturing a fuel cell of a portable electronic device.    ADVANTAGE - The method ensures avoiding a fuel leakage of the fuel cell effectively, and avoids deformation of the fuel-supply board effectively. The method reduces thickness of the fuel-supply board for forming a small fuel supply part so as to attain thin and light weight fuel cell.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a top view of a fuel-supply board.    Fuel-supply board (101)    Leading-member (101a)    Branching part (101b)    Reinforcement part (102)    Junction part (103)
NOVELTY - The crude biodiesel flash tower comprises a tower body (1), a rough biological diesel oil feeding tube, a crude biodiesel distribution plate (3), a diesel oil outlet (4), a baffle plate (5), and a low boiling outlet (6). The low-boiling outlet is connected to a vacuum system. An upper part of the distributing plate has a multi-layer shape.    USE - The crude biodiesel flash tower is useful in equipment for biodiesel production.    ADVANTAGE - The crude biodiesel flash tower allows the simple and economical production of the diesel with high quality, reduced energy consumption and vaporizing time and improved flashing effect in a convenient manner.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of crude biodiesel flash tower.    Tower body (1)    Crude biodiesel distribution plate (3)    Diesel oil outlet (4)    Baffle plate (5)    Low-boiling outlet. (6)
NOVELTY - Fats-and-oils (BM) are contacted with a zeolite solid catalyst (80) at 350-380 degrees C, and the obtained gas component is cooled to obtain bio-oil fuel (BF).    USE - Manufacture of bio-oil fuel used in diesel engine.    ADVANTAGE - The method efficiently and economically provides bio-oil without using strong base which accelerates the saponification of fatty acid without affecting the environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for solid acid catalyst, which contains substrate portion containing clay formed in granular form, gravel shape, plate shape or cylinder shape, and zeolite portion which covers the surface.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of manufacturing apparatus of bio-oil.    Destruction distillation portion (10)    Burner portion (20)    Zeolite solid catalyst (80)    Bio-oil fuel (BF)    Fat-and-oil (BM)
NOVELTY - A carbonization furnace comprises a heating combustion chamber which has fuel hole and flow holes on the furnace side wall and is located on the furnace bottom face, a furnace cover which can be opened and closed, flue gas extending near the cover on the upper surface of the heating combustion chamber, and an exhaust gas-emitting pipe separated from the fuel hole. The carbonization furnace has a cylindrical shape. The side wall of the carbonization furnace has a double structure and provides a circulating space (Y) between an outer wall and an inner wall (3a) with small open holes.    USE - A carbonization furnace for manufacture of charcoal and carbonized soil improvement material.    ADVANTAGE - The carbonization furnace carries out carbonization of solid biomass materials efficiently, can be operated easily, and is cheap.    DETAILED DESCRIPTION - A carbonization furnace comprises a heating combustion chamber which has fuel hole and flow holes on the furnace side wall and is located on the furnace bottom face, a furnace cover which can be opened and closed, flue gas extending near the cover on the upper surface of the heating combustion chamber, and an exhaust gas-emitting pipe separated from the fuel hole. The carbonization furnace has a cylindrical shape. The side wall of the carbonization furnace has a double structure and provides a circulating space (Y) between an outer wall and an inner wall (3a) with small open holes. The structure is connected to the heating combustion chamber through a furnace space, the circulating space, and a carbonization furnace bottom face space (Z) between a carbon material mounting grate (5) and the flow hole of the heating combustion chamber side surface.    DESCRIPTION OF DRAWING(S) - The drawing shows a vertical side view of the carbonization furnace taken along line 1B-B.    Inner wall (3a)    Carbon material mounting grate (5)    Ceiling space (X)    Circulating space (Y)    Bottom face space (Z)
NOVELTY - A microorganism belonging to Burkholderia and capable of growing in fat and oil containing culture medium (pH 5-6) and/or fat and oil containing wastewater and degrading the fat and oil, is new.    USE - The microorganism is useful in composition for degrading fats and oils and proteins present in wastewater (claimed), and degrading or removing fats and oils accumulated in grease trap used in restaurants and meat processing industries, and sewage pipes.    ADVANTAGE - The microorganism reduces the fat and oil content in wastewater to less than 50% before processing, as the microorganism has proliferation ability and high lipolytic activity in acidic conditions which is the actual condition in grease traps, and hence prevents problems (e.g. generation of offensive odor and insect pest problems) associated with excess accumulation of fats and oils. The microorganism can be handled easily and is more suitable to mass culture as compared to Candida.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) microbial composition comprising one or several lipolytic microorganisms; and    (2) method for processing fat and oil containing wastewater, involves reducing fats and oils in fat and oil containing wastewater at pH 5-6 (acidic condition) using the microbial composition.
NOVELTY - The method is carried out by extracting empty fruit bunch fibers from the waste. This product is then processed using a blade mill, then treated with a weak solution of hydrochloric acid in a flow reactor and then with hot water in a flow reactor. The product formed is treated with diluted enzyme solution and then dried at 100-120 degrees C. The dried material is crushed in the continuous flow mill with shearing action. The crushed product is then treated with a complex of enzymes and the carbohydrate part of the waste is hydrolyzed. The solid deposit is separated after hydrolysis to 65-70 percent hydrocarbon conversion. Pallets are then formed from the solid deposit by hot extrusion. When treating the product with diluted enzyme solution it is subjected to ultrasonic force at a frequency of 17.5-44 kHz and power of 0.2-2 Wt/cm3.    USE - For using lignocellulosic wastes from palm oil production to produced liquid and solid fuel.    ADVANTAGE - The process is ecologically friendly and uses empty fruit bunch fibers.
NOVELTY - Producing (M1) an organic soil amendment comprises: producing an initial extract from a compost by soaking the compost in water; mixing the initial extract with additional water and re-circulating the mixture; aerating the mixture; and introducing additives and beneficial fungi to the mixture.    USE - The method is useful for producing an organic soil amendment (claimed) which is useful to suppress plant diseases, insects and fungi by enhancing the growth of the plants, crops, trees, shrubs or ornamental lawns.    ADVANTAGE - The method: provides organic soil amendment which is safe and facilitates the plants to more effectively utilize the nutrition that is already present in the surrounding soil; utilizes less amount of chemical fertilizers and petroleum products; and utilizes living beneficial microorganisms which are stronger and last longer, and thus reduces the number of applications required per year.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) the organic soil amendment produced the method (M1);    (2) applying (M2) an organic soil amendment, comprising: diluting organic soil amendment containing a live aerobic culture of beneficial microorganisms with water; and aerating the diluted organic soil amendment to maintain the live beneficial microorganisms in aerobic state; and    (3) an organic soil amendment (A1) comprising: a live aerobic culture of beneficial microorganisms, containing beneficial bacteria and fungi; and additives and plant extracts.
NOVELTY - A water electrolysis system (100) comprises water electrolysis apparatus (12) for electrolyzing water to generate oxygen and hydrogen having pressure higher than pressure of oxygen, low-pressure gas-liquid separator (14) to separate oxygen and water that are received from anode of water electrolysis apparatus and supply separated water to water electrolysis apparatus in a circulating manner, high-pressure gas-liquid separator (22) to separate hydrogen received from cathode of water electrolysis apparatus and permeation water permeated from anode, and water pipe (24).    USE - A water electrolysis system (claimed).    ADVANTAGE - Water removal from generated high-pressure hydrogen allows economical use of water, and adjusting amount of water discharged from tank unit is unnecessary.    DETAILED DESCRIPTION - A water electrolysis system (100) comprises water electrolysis apparatus (12) for electrolyzing water to generate oxygen and hydrogen having pressure higher than pressure of oxygen, low-pressure gas-liquid separator (14) to separate oxygen and water that are received from anode of water electrolysis apparatus and supply separated water to water electrolysis apparatus in a circulating manner, high-pressure gas-liquid separator (22) to separate hydrogen received from cathode of water electrolysis apparatus and permeation water permeated from anode, water pipe (24) that connects high-pressure and low-pressure gas-liquid separators and returns water from high-pressure gas-liquid separator to low-pressure gas-liquid separator, and decompression water supply device (26) arranged at the water pipe for decompressing water discharged from high-pressure gas-liquid separator.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a water electrolysis system.    Water electrolysis apparatus (12)    Low-pressure gas-liquid separator (14)    High-pressure gas-liquid separator (22)    Water pipe (24)    Water electrolysis system (100)
NOVELTY - Method of producing fatty acid ester product, involves (a) contacting a reactant feedstock with at least one immobilized lipolytic enzyme on a carrier to obtain a reaction mixture comprising the fatty acid ester product, (b) adding a liquid preparation comprising at least one lipolytic enzyme to the at least one immobilized lipolytic enzyme, and (c) separating the reaction mixture from the immobilized lipolytic enzyme, where step (b) may be performed before, during and/or after step (a).    USE - The method is useful for producing fatty acid ester product, preferably biodiesel and fat hardstock e.g. margarine (claimed).    ADVANTAGE - The method is cost-effective, environmentally-friendly, desirable and suitable for commercial scale biodiesel production, enables to extend life of immobilized lipolytic enzyme, and has reduced number of process steps.
NOVELTY - Fermentation process for production of organic compound, involves: (a) incubation of components comprising polysaccharides with a phage receptor protein in an aqueous medium, and (b) fermentation of the mixture of step (a) to the organic compound, where the organic compound consists of carbon, hydrogen and oxygen atoms only.    USE - As fermentation process for production of organic compound, where the organic compound is alcohol (preferably ethanol or butanol), lipid (preferably triacylglycerol, glycolipid, sterol, sterol ester, cartenoid, xanthophyll or fatty acid, in particularly free fatty acid, unsaturated fatty acid, polyunsaturated fatty acid or ester of a fatty acid), and biofuel (preferably bioethanol, biobutanol or biodiesel) (all claimed).    ADVANTAGE - The fermentation process offers a wide range of possibilities of producing organic compounds from renewable resources such as biomass. The fermentation process provides excellent efficiency and environmental sustainability at low cost.
NOVELTY - Solid biomass (AA) containing water is contacted with ammonia gas (BB) under a pressure higher than atmospheric pressure, and ammonia gas is dissolved in water in solid biomass. Contacted solid biomass and ammonia gas are pressure-reduced at the contact process at a pressure lower than the pressure during contact process. Ammonia gas dissolved in water is vaporized, separated from solid biomass, and recovered.    USE - Saccharification preprocessing of solid biomass used for producing bioethanol fuel.    ADVANTAGE - The method minimizes energy consumption required for additional heating, and is economical. Efficient saccharification preprocessing of solid biomass can be carried out stably by a simple and easy process.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) saccharification preprocessor (1) consisting of an ammonia-gas contact portion (10), a pressure-reduction portion (20), and an ammonia-gas separation portion (30); and    (2) saccharification of solid biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the schematic structure of the saccharification preprocessor of solid biomass. (Drawing includes non-English language text)    Saccharification preprocessor (1)    Ammonia-gas contact portion (10)    Pressure-reduction portion (20)    Ammonia-gas separation portion (30)    Solid biomass (AA)    Ammonia gas (BB)    Heating (FF)
NOVELTY - The equipment (1) has a reaction tank (10) with to-be-treated water that is brought into contact with microbial aggregates in bottom (100) of tank and discharged from top as treated water. A gas bubble-separating screen (11) contacts microbial aggregates with attached gas bubbles and the separates the gas bubbles. A gas bubble-collecting tube (12) collects and guides separated gas bubbles to vicinity of liquid surface in reaction tank. A side surface screen (13) separates the liquid phase at top of reaction tank into microbial aggregates and treated water.    USE - Waste water treatment equipment of upward flow anaerobic sludge-blanket (UASB) system.    ADVANTAGE - Since the gas bubble-collecting tube collects and guides the separated gas bubbles to vicinity of liquid surface in reaction tank, the efficient solid gas separation and solid liquid can be performed. The residence time of to-be-processed water can be shortened.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the waste water treatment equipment.    Waste water treatment equipment (1)    Reaction tank (10)    Gas bubble-collecting tube (12)    Side surface screen (13)    Tank bottom (100)
NOVELTY - Dewatered cake of sewage sludge and waste liquid containing phenol are mixed to obtain cake for distribution. The obtained cake is added to a storage tank (6) through distribution path (5,8) for pumping, and then transferred to a cement manufacturing apparatus in order to use as raw material or fuel of cement. Thus, sewage sludge is processed.    USE - Processing method of sewage sludge.    ADVANTAGE - The method efficiently and economically processes the sewage sludge without using industrial water. The generation of odor gas such as methyl mercaptan, hydrogen and ammonia from cake for distribution is suppressed. Swelling of cake in the storage tank is suppressed. The waste liquid used during processing of sewage sludge does not contain chlorine and heavy metal.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of processing system for processing method of sewage sludge. (Drawing includes non-English language text)    Vehicle (1)    Pumps (4,7)    Distribution path for pumping (5,8)    Storage tank (6)    Drying apparatus (9)
NOVELTY - The equipment (10) has aerobic tank (20) that processes to-be-processed water aerobically with an activated sludge. A membrane unit (34) performs membrane separation of activated sludge. The activated-sludge density of secondary aerobic tank (30) is set higher than that of primary aerobic tank. A circulation line (37) is provided to circulate digestive fluid from secondary aerobic tank more upstream than primary aerobic tank. The primary aerobic tank is attached to micro-bubble aeration unit (108) to supply micro-bubble in tank.    USE - Activated-sludge process equipment.    ADVANTAGE - Since the circulation line circulates digestive fluid from secondary aerobic tank, more upstream than primary aerobic tank whose activated-sludge density is set lesser than that of secondary aerobic tank, the oxygen supply of the aeration unit can be obtained efficiently, so that the amount of the aerations can be reduced effectively, and the operation motive power required for the aeration unit can be reduced effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for processing activated-sludge.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the activated-sludge process equipment.    Activated-sludge process equipment (10)    Activated sludges (20,30)    Membrane unit (34)    Circulation line (37)    Micro-bubble aeration unit (108)
NOVELTY - The apparatus (100) has two hydrolyzing electrode planes (11,12) to which light (52,54) is irradiated to decompose water (60). The hydrolyzing electrode planes that generated oxygen (21) and hydrogen (31) are accommodated in oxygen generation cell (20) and hydrogen generation cell (30), respectively. A photolysis element (10) is arranged with respect to horizontal surface. The oxygen and hydrogen generation cells forms water-flow path for distributing water towards upper side from lower side.    USE - Hydrolyzing apparatus.    ADVANTAGE - Since the retention of the oxygen and hydrogen in the oxygen generation cell, and hydrogen generation cell, respectively, are suppressed, the decomposition efficiency of the water is increased.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of generating oxygen and hydrogen from water using hydrolyzing apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the hydrolyzing apparatus.    Photolysis element (10)    Hydrolyzing electrode planes (11,12)    Oxygen generation cell (20)    Oxygen (21)    Hydrogen generation cell (30)    Hydrogen (31)    Lights (52,54)    Water (60)    Hydrolyzing apparatus (100)
NOVELTY - A membrane electrode assembly (MEA) is formed by coating a catalyst layer (13) on the surface of a polymer electrolyte membrane (14). An uneven structure having a preset width (16), pitch (15) and height (17) is formed in the MEA by pressing the MEA heated to glass transition temperature of polymer electrolyte membrane between a metal mold (11) and a mold receptacle (18).    USE - Membrane electrode assembly manufacturing method for fuel cell e.g. polymer electrolyte fuel cell.    ADVANTAGE - The uneven structure is formed in the MEA in the state of maintaining a uniform interface structure between the polymer electrolyte membrane and catalyst layer. The electric power generation characteristic of fuel cell is improved by improving current-voltage output characteristic by setting the pitch and width of uneven structure of membrane electrode assembly appropriately. The water repellent process film is provided to the surface of the mold and the mold receptacle for enabling easier separation of mold and mold receptacle from the membrane electrode assembly after the hot pressing operation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the uneven catalyst layer formation method.    Metal mold (11)    Water repellent film (12)    Catalyst layer (13)    Polymer electrolyte membrane (14)    Pitch (15)    Width (16)    Height (17)    Mold receptacle (18)
NOVELTY - Catalytic partial oxidation with in-situ coke removal comprises: (a) feeding a hydrocarbon fuel into a reactor; (b) feeding an oxidant into the reactor; (d) varying the feed of hydrocarbon fuel, or the feed of oxidant, or both feeds to the reactor to produce a fuel-lean feed ratio of hydrocarbon fuel to oxidant; (e) maintaining the fuel-lean feed ratio for a fuel-lean cycle-time sufficient; and (f) varying the feed of hydrocarbon fuel, or the feed of oxidant, or both feeds to the reactor so as to provide a fuel-rich feed ratio in the manner of steps (a) and (b).    USE - The process is useful for catalytic partial oxidation with in-situ coke removal (claimed).    ADVANTAGE - The invention provides improved method of coke removal during operation of catalytic partial oxidation process for reforming hydrocarbon fuel to form partially-oxidized reaction product, preferably, a useable gaseous hydrogen fuel.    DETAILED DESCRIPTION - Catalytic partial oxidation with in-situ coke removal comprises: (a) feeding a hydrocarbon fuel into a reactor; (b) feeding an oxidant into the reactor, the hydrocarbon fuel and oxidant being fed in a fuel-rich feed ratio; (c) contacting the hydrocarbon fuel and oxidant with a catalyst in the reactor for a fuel-rich cycle-time sufficient to produce at least one partially-oxidized reaction product; (d) varying the feed of hydrocarbon fuel, or the feed of oxidant, or both feeds to the reactor to produce a fuel-lean feed ratio of hydrocarbon fuel to oxidant; (e) maintaining the fuel-lean feed ratio for a fuel-lean cycle-time sufficient to reduce coke deposits while maintaining a substantially constant yield of partially-oxidized reaction product; and (f) varying the feed of hydrocarbon fuel, or the feed of oxidant, or both feeds to the reactor so as to provide a fuel-rich feed ratio in the manner of steps (a) and (b); and reiterating process steps (c) through (f).
NOVELTY - Agent in particulate form comprises iron oxide and/or iron oxide hydroxide, where: the agent comprises an average trace element comprising less than or equal to 80 ppm of arsenic, less than or equal to 50 ppm of lead and less than or equal to 1 ppm of mercury, and has a residual moisture content of 0-30 wt.% and a bulk density of 0.4-2 g/cm3; and at least 50 wt.% of the agent has a particle size of greater than 0.5 mm.    USE - The agent is useful: for removing hydrogen sulfide, inorganic or organic sulfide from liquid or gas medium, preferably biogas; and in biogas digesters. The mixture is useful as fertilizer (all claimed). No biological data given.    ADVANTAGE - The agent exhibits high adsorption capacity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a mixture comprising biomass and the agent.
NOVELTY - Biphenyl benzyl ether marker compound, is new.    USE - The biphenyl benzyl ether marker compound is useful for marking petroleum hydrocarbon, biodiesel fuel or ethanol fuel (claimed).    DETAILED DESCRIPTION - Biphenyl benzyl ether marker compound of formula (I), is new.    G=at least one substituent selected from 1-12C alkyl and 1-12C alkoxy.    An INDEPENDENT CLAIM is a method for marking a petroleum hydrocarbon, biodiesel fuel or ethanol fuel comprising adding at least one biphenyl benzyl ether marker compound of formula (I) to the petroleum hydrocarbon, biodiesel fuel or ethanol fuel.
NOVELTY - An overground methane tank capable of adjusting methane pressure, comprises a gas storage kettle (1), and a fermentation tank (6) with a material inlet (2), a material outlet (3), a gas outlet (4) and a water outlet (5), where the gas storage kettle and fermentation tank is of a split structure, and both are interconnected by a gas pipe (7), and the upper end of the gas storage kettle is provided with a gas exhaust port (11), and lower end of the gas storage kettle is placed in a water tank (8).    USE - As overground methane tank (claimed) for marsh gas production.    ADVANTAGE - The methane tank employing the gas storage kettle and the fermentation tank of the split structure is capable of adjusting the methane pressure in the gas storage kettle and to keep balance between the methane pressure and the atmosphere pressure. The methane tank is adaptable for large-scale production; and is simple in the structure, very environment-friendly and convenient for use.    DESCRIPTION OF DRAWING(S) - The figure shows diagram of the marsh gas tank.    Gas storage kettle (1)    Material inlet (2)    Material outlet (3)    Gas outlet (4)    Water outlet (5)    Fermentation tank (6)    Gas pipe (7)    Water tank (8)
NOVELTY - A microbe is separated by using bean dregs, tofu wastewater, and soybean flour as the selective culture medium; and inoculating the strain in the liquid culture medium to ferment at 100-160 rpm at 20-35 degrees C for 1-3 days to separate out the strain.    USE - Method for separation of microbe for purifying tofu wastewater (claimed).    ADVANTAGE - The method provides convenient operation, high efficiency, good selectivity, and low cost. It lays a foundation for quickly processing the tofu wastewater using the biological process.    DETAILED DESCRIPTION - Separation of microbe for purifying tofu wastewater involves adding 700-900 ml tofu wastewater to 400-600 g bean dregs, stirring, and filtering the solution, collecting the filter liquid, adding 2-4 g soybean flour and controlling the volume to 1000 ml, adjusting the pH value to the neutral, and sterilizing the solution at 120 degrees C for 20 minutes to obtain a liquid culture medium. A solid culture medium is prepared by adding 17-18 g/liter agar to the liquid culture medium, dissolving, and sterilizing to obtain flat plate culture medium. Compost fertilizer or soil is diluted using 10-times dilution method. The compost fertilizer is diluted to a dilution degree of 105-107. The diluents are coated to the flat plate culture medium. The liquid is cultivated at 20-35 degrees C for 24-48 hours. The strain with larger bacterial colony on the flat plate culture medium is selected to perform the separation purification. It is inoculated in the liquid culture medium to ferment at 100-160 rpm at 20-35 degrees C for 1-3 days to separate out the strain with the quick growth speed. After the fermentation, the quantity of the microbes in each ml of fermentation liquid is greater than 105 strains.
NOVELTY - An ozone oil is used for treating plant infection disease. The ozone oil is coated on the plant having disease until new tissue is generated.    USE - An ozone oil for treating plant infection disease.    ADVANTAGE - The ozone oil does not leave residue, and is toxic-free and environment-friendly.
NOVELTY - A marsh gas fermentation tank automatically control temperature device comprises a fermentation tank (13), heating device (14), temperature control sensor (12), temperature controller (11), water pump (16), water tank (5), and a marsh gas generator (1), where the fermentation tank is equipped with a temperature sensor that directly extends into a connection control to the middle fermentation tank. The temperature control sensing switch of the temperature controller is connected with a power supply wire that is connected with water pump by the inductive switch control and power cord (10).    USE - As marsh gas fermentation tank automatically control temperature device (claimed) used for methane fermentation.    ADVANTAGE - The device is environment-friendly, has simple structure and reasonable design, needs small investment, is set with automatic control, has low operation cost and good effect, and it saves energy and reduces heat discharge.    DESCRIPTION OF DRAWING(S) - The figure shows a view of new-type biogas fermenting tank automatic temperature control device.    Marsh gas generator (1)    Power cord (10)    Temperature controller (11)    Temperature control sensor (12)    Fermentation tank (13)    Heating device (14)
NOVELTY - The combination has a central drive device (5) arranged on a middle part of a beam (15). A tail pipe (1) is extended toward a bottom part of a sedimentation tank (7). A dredge body is provided with an underwater scraping rake part (10) that is fixed with a scraping plate (9). The underwater scraping rake part is arranged below a center part of a drive device (5). An end of a mud pump (8) is connected between the drive device and the scraping rake part. Another end of the mud pump is connected with a mud discharging pipe (2) through a connecting device (12).    USE - Central rotating-type mud scraper and suction dredge combination.    ADVANTAGE - The combination ensures normal operation of a peripheral transmission pulley and improves sludge fluidity and biochemical processing efficiency without changing condition of a current slot.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a central rotating-type mud scraper and suction dredge combination.    Tail pipe (1)    Mud discharging pipe (2)    Central drive device (5)    Sedimentation tank (7)    Mud pump (8)    Scraping plate (9)    Underwater scraping rake part (10)    Connecting device (12)    Beam (15)
NOVELTY - Cultivating a microalgae capable of heterotrophic growth, comprises incubating the microalgae under a heterotrophic growth condition for a period of time sufficient to allow the microalgae to grow, where the heterotrophic growth condition comprises a media comprising a fruit wastewater, and light.    USE - The method is useful for cultivating a microalgae (capable of heterotrophic growth) to produce materials (a polysaccharide, a pigment, a lipid, or a hydrocarbon), and processed materials including a fuel, biodiesel, jet fuel, a cosmetic, a pharmaceutical agent, a surfactant, a renewable diesel (all claimed), biopetroleum, carotenoids, and biopolymers.    ADVANTAGE - The method utilizes wastewater from dried fruit/fruit juice industries and wineries, thus: increasing the growth rate of the microalgae compared to microalgae that is grown utilizing non-fruit waste water carbon source; providing a cost-effective and environmentally friendly solution for wastewater from dried fruit and wine industries; and providing a low cost sugar source which can be used for economic production of the microalgal products.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a bioreactor system, comprising: a bioreactor; a culture media comprising a fruit wastewater carbon source, where the culture media is located inside the bioreactor; the microalgae located in the culture media; and a light source operatively coupled to the bioreactor; and    (2) a culture for cultivating the microalgae, comprising the microalgae placed under a heterotrophic growth condition for a period of time sufficient to allow the microalgae to grow.
NOVELTY - A hydrogen generator system comprises a hydrogen generator (10) formed of stainless steel and having an electrical power supply including a fluctuations switch to provide a non-continuous current supply to the generator. The generator comprises a hydrogen outlet in fluid communication with an engine air intake part of a vehicle, and a reaction chamber (32) in fluid communication via a filler (20) with a water header tank. The chamber includes an internal baffle(s) (24), and restraining baffles (23) that support the internal baffles in a correct alignment and separation.    USE - A hydrogen generator system for a light or heavy commercial vehicle (claimed).    ADVANTAGE - The hydrogen generator system is highly safe, portable, robust, reliable, easy to install in an engine, simple to use and maintain, and that does not interfere with day-to-day running of the engine or affect any existing engine management system. It incorporates a safety device to ensure that the hydrogen generator does not overheat.    DESCRIPTION OF DRAWING(S) - The drawing is cross-sectional view of the hydrogen generator system.    Hydrogen generator (10)    Filler (20)    Restraining baffles (23)    Internal baffle (24)    Reaction chamber (32)
NOVELTY - Water is initially allowed to pass through an ion exchange resin, and 100 special weights of water which generate at least one tourmaline, and rock containing 65-76 wt.% of silicon dioxide containing liparite or granite, is allowed to pass through behind previously, and then 0.5 wt.% or more of magnesium powder are added into container (60), and heated at 30 degrees C by heating unit, to obtain hydrogen.    USE - Manufacture of hydrogen used as fuel gas.    ADVANTAGE - The method economically provides hydrogen without using any metals.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of apparatus for generating hydrogen.    Container (60)    Main component (62)    Interconnecting passageway (64)    Opening-closing valve (68)    Barometer (70)
NOVELTY - Use of rape methyl ester as fuel additive in an engine, is claimed, where the engine runs on an ethanol-based fuel and has a motor oil additive in the form of a dispersant, the engine works according to the diesel principle and the rape methyl ester prevents formation of sticky precipitates.    USE - The rape methyl ester is useful as fuel additive in an engine, which runs on ethanol-based fuel, to prevent formation of sticky precipitates.    ADVANTAGE - The rape methyl ester minimizes precipitation of oil additives in the fuel system of an ethanol engine and works even in cold climates.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a fuel additive composition containing rape methyl ester and bis-(2-hydroxyethyl)-oleyl amine in a weight ratio of 3:1-1:1.
NOVELTY - A system (S1) for separation of mixtures of gases or liquids comprises: a pre-membrane unit (113), a primary membrane unit (121) and a secondary membrane unit (135). The pre-membrane comprises a membrane with selectivity at least higher than 20, and the primary membrane comprises at least one glassy polymer. A liquid or gas mixture is separated into a retentate stream (126) and a permeate stream (128) by each of the pre-membrane unit, primary membrane unit and secondary membrane unit in sequence.    USE - For separation of mixtures of gases or liquids (claimed), useful in the separation of component gases from the mixtures comprising carbon dioxide/methane, or hydrogen/methane, or to remove carbon dioxide from the natural gas.    ADVANTAGE - The system uses high performance polybenzoxazole polymer and cross-linked polybenzoxazole polymer membranes that have easy processability, high selectivity, high permeability, high thermal stability, and high resistance to solvent swelling, plasticization and hydrocarbon contaminants. The multi-stage membrane system can reduce inter-stage compression cost, increase product recovery and product purity for gas, vapor, and liquid separations. It can also save the cost compared to the system using all the high cost polybenzoxazole membranes or cross-linked polybenzoxazole membranes.    DESCRIPTION OF DRAWING(S) - The figure shows a multi-stage membrane system.    Pre-membrane unit (113)    Primary membrane unit (121)    Retentate stream (126)    Permeate stream (128)    Secondary membrane unit (135)
NOVELTY - A composite microbial inoculum comprises (pts. wt.): Serratia plymuthica (ACCC 01503) fermentation liquid (12-20), Sphingomonas trueperi (ATCC 12417) fermentation liquid (17-25), and Alcaligenes sp. (DSM 2625) fermentation liquid (50-63). Fermentation liquid effective viable count is more than 109/mL.    USE - Composite microbial inoculum for reducing ammonia release and protecting nitrogen of cow manure.    ADVANTAGE - The microbial inoculum can greatly reduce bacteria release quantity of ammonia in compost process and effectively improves content of the nitrogen element in the fertilizer.
NOVELTY - Ecological cultivation system comprises chicken, goose cultivation, maggot and earthworm breeding box, finless eel cultivating tank and biogas residue, marsh gas pool; where the finless eel cultivation box is provided with grape planting frame; the biogas residue, marsh gas pool is connected to the grape planting frame around the pipeline; the goose breeding cage is provided with a first transmission belt transmission chicken goose excrement, the maggot and earthworm cultivating tank and biogas residue.    USE - As an ecological cultivation system.    ADVANTAGE - The ecological cultivation system is more effective; reduces the human in bad environment in work time; has good market development prospect; reduces the discharge of pollutant, and realizes low carbon environment-friendly.    DETAILED DESCRIPTION - Ecological cultivation system comprises chicken, goose cultivation, maggot and earthworm breeding box, finless eel cultivating tank and biogas residue, marsh gas pool; where the finless eel cultivation box is provided with grape planting frame; the biogas residue, marsh gas pool is connected to the grape planting frame around the pipeline; the goose breeding cage is provided with a first transmission belt transmission chicken goose excrement, the maggot and earthworm cultivating tank and biogas residue; marsh gas pool is located between the first transmission belt around, the maggot and earthworm breeding box between the biogas residue; marsh gas pool is provided with transmission fly maggot and earthworm excrement fermentation of the second transmission belt maggot and earthworm dejecta ferment.
NOVELTY - An ecological purification channel comprises feeding zone (2) comprising front end and tail end, and exhalant region (5). Exhalant region comprises end water outlet pipe. Series of multi-stage purification area (3) is provided between feeding zone and exhalant region. Trench bottom is gradually reduced and connected in hierarchical drop form between each grade purifying area collecting recycling well (4). Purifying region is provided with partition wall, water flow is formed wall part or opening on lower stream.    USE - Ecological purification channel for collecting, purifying and recycling of sewage.    ADVANTAGE - The purification channel has high treatment efficiency, low energy consumption, small floor space, convenient management, flexible arrangement, and landscape effect.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating and ecological purification channel.    Feeding zone (2)    Multi-stage purification area (3)    Purifying area collecting recycling well (4)    Exhalant region (5)
NOVELTY - Sealed-type sludge composting continuous fermentation processing device comprises a stander and a fermentation cylinder installed on the stander, a feeding chamber and a discharging chamber installed at two ends of the fermentation cylinder, and a control system. The fermentation cylinder is connected to a power device for driving the fermentation cylinder to overturn around axial direction.    USE - Used as a sealed-type sludge composting continuous fermentation processing device.    ADVANTAGE - The device is simple, environmental-friendly and suitable for sludge composting which produces high quality fertilizer in short processing time; and reduces sludge.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the sealed-type sludge composting continuous fermentation processing device.
NOVELTY - An indoor anaerobic digestion renewable energy device for organic wastes comprises hydrolysis acid production pool (1), gas production pool (2) and gas storage device (3), where hydrolysis and gas production pools are independent closed structures; the middle upper part of sidewall of hydrolysis acid production pool which is advantaged to gas production pool is provided with acid liquid pump (16), and normally closed outlet (164) is connected with gas production pool; and fixed-pressure one-way gas guide pipe (20) on the top of gas production pool is connected with gas storage device.    USE - As an indoor anaerobic digestion renewable energy device for organic wastes (claimed).    ADVANTAGE - The device is simply and compactly structured; is convenient to operate; has high gas production efficiency; is free of other auxiliary energy and suitable for placing in the room; saves the large amount of water resources for drainage; prevents the damage about the environment in the drainage process; and generates certain energy for life.    DESCRIPTION OF DRAWING(S) - The figure shows a sectional view of indoor anaerobic digestion renewable energy device.    Hydrolysis acid production pool (1)    Gas production pool (2)    Gas storage device (3)    Acid liquid pump (16)    Fixed-pressure one-way gas guide pipe (20)    Closed outlet (164)
NOVELTY - Treating food residues comprises (i) washing food residue in a clear water cell, filtering by a screen and collecting the filtered food residue in a reaction kettle; (ii) sterilizing at 120-150 degrees C for 40 to 45 minutes; (iii) cooling the sterilized food residue in the reaction kettle; and (iv) shearing and cutting the cooled food residue, adding plant ash and quicklime to adjust the acidity of the food residue, then adding straws of 2-2.5 cm, adding lactate complex enzyme strain or Lactobacillus, heating, recovering to room temperature and peracetic fermenting for 20-24 hours.    USE - The method is useful for treating food residues.    DETAILED DESCRIPTION - Treating food residues comprises (i) washing food residue in a clear water cell, filtering by a screen and collecting the filtered food residue in a reaction kettle; (ii) sterilizing at 120-150 degrees C for 40 to 45 minutes; (iii) cooling the sterilized food residue in the reaction kettle; and (iv) shearing and cutting the cooled food residue, adding plant ash and quicklime to adjust the acidity of the food residue, then adding straws of 2-2.5 cm, adding lactate complex enzyme strain or Lactobacillus (0.5-1.5%) and yeast, heating at 65-70 degrees C for 4 hours, recovering to room temperature and peracetic fermenting for 20-24 hours.
NOVELTY - The device (100) has a PV cell element (120) that is provided to convert a portion of received solar energy into electrical energy. The PV cell element is provided to pass another portion of the solar energy. An electrolysis compartment (140) is provided with an aqueous electrolyte (142). The aqueous electrolyte is positioned to receive the other portion of the solar energy passing through the PV cell element. The electrolysis compartment is provided with electrodes (144,146) that are electrically connected to receive the electrical energy produced by the PV cell element.    USE - Photovoltaic electrolysis device.    ADVANTAGE - The overall conversation efficiency can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for photovoltaic (PV) electrolysis method.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of the photovoltaic electrolysis device. (Drawing includes non-English language text)    Photovoltaic electrolysis device (100)    PV cell element (120)    Electrolysis compartment (140)    Aqueous electrolyte (142)    Electrodes (144,146)
NOVELTY - The cell has anodes and cathodes that are provided with graphite. A cell cavity is provided by which water flown through cell is made to contact with anodes and cathodes simultaneously, so as to produce electrolytic reaction in water without using metallic components.    USE - Non-metallic electrolysis cell for producing electrolysis in water.    ADVANTAGE - The accumulation of excess amount of hydrogen gas from electrolysis in the cell can be facilitated. The performance of electrolysis cell can be improved effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows the perspective view of the electrolysis cell.    Cell units (9,11)    Power supply (10)    Cell design (12)
NOVELTY - Substituted diamide compounds (A) are new.    USE - (A) are useful for manufacturing (B1), preferably (B2) (claimed), where (B2) is useful as an anticonvulsive drug. No biological data given.    ADVANTAGE - (A) are prepared with improved yield and purity in an industrial, economical and environmentally friendly manner.    DETAILED DESCRIPTION - Substituted diamide compounds of formula (R2-O-CH=CH((-C(=O)-NH-CH2-R1)(-NH-C(=O)-R3))) (A) are new.    R1 = an aryl; and    R2, R3 = an optionally substituted alkyl.    INDEPENDENT CLAIMS are included for:    (1) the preparation of (A); and    (2) manufacturing substantially optically pure diamide compounds of formula (R2-O-CH2-CH((-C(=O)-NH-CH2-R1)(-NH-C(=O)-R3))) (B1), comprising catalytic asymmetric hydrogenation of (A).
NOVELTY - The apparatus has a photoelectric conversion unit (2) that is provided with light receiving surface and back surface. The electrical potential difference occurs between two zones on back surface so that zones are electrically connected with electrolysis electrodes (7,8) when photoelectric conversion unit receives light. A hydrogen generation unit generates the hydrogen and oxygen generation unit generates oxygen from electrolyte solution using the electromotive force, when two electrolysis electrodes contact with the electrolyte solution.    USE - Apparatus for producing hydrogen at home, hydrogen station and large-scale hydrogen production factory.    ADVANTAGE - Since the electrical potential difference occurs between two zones on back surface can be made large, the light reception amount can be increased, the light receiving surface of the photoelectric conversion unit can be reduced and the manufacturing cost can be reduced. Since electrically conductive distance between photoelectric conversion unit and electrolysis electrodes can be made small, the internal resistance can be small. Since hydrogen generation unit and the oxygen generation unit are formed on the back surface of the photoelectric conversion unit, the absorption and scattering of incident light can be prevented, the quantity of incident light can be improved and the optical efficiency can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for hydrogen production method.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the hydrogen production apparatus.    Board (1)    Photoelectric conversion unit (2)    Electrolysis electrodes (7,8)    Insulation unit (11)    Top plate (14)
NOVELTY - The apparatus has an electrode pair which is provided with a hydrogen electrode (102) and a charging/discharging oxygen electrode (103). A partition (104) is provided between hydrogen electrode and charging/discharging oxygen electrode. A tank (105) is provided with electrode pair, partition and electrolyte aqueous solution (106). The hydrogen foam (107) is generated by electrolyzing the electrolyte aqueous solution by electrode pair. The charging/discharging capacity of the oxygen electrode is 10-10000 more than that of hydrogen electrode.    USE - Hydrogen production apparatus.    ADVANTAGE - The response of the system is excellent with respect to fluctuation of input electric power by a renewable energy, so that hydrogen production apparatus can be operated reliably.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the cell of the hydrogen production apparatus. (Drawing includes non-English language text)    Hydrogen electrode (102)    Oxygen electrode (103)    Partition (104)    Tank (105)    Electrolyte aqueous solution (106)    Hydrogen foam (107)
NOVELTY - A hybrid particles-containing composition contains active ingredient for absorption of carbon dioxide and active ingredient for water gas shift reaction catalyst.    USE - Composition is used for slurry composition for manufacturing hybrid particles used for fluidized-bed adsorption-enhanced water gas shift reaction process (all claimed) in integrated coal gasification combined cycle generation, fuel cell and coal liquefaction.    ADVANTAGE - The hybrid particles in the composition have excellent packing density, abrasion resistance, carbon monoxide conversion rate, carbon dioxide absorption characteristics and regeneration characteristics. The hybrid particles are economically manufactured, with high yield.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) slurry composition, which contains solid material comprising hybrid particles-containing composition and a solvent;    (2) manufacture of hybrid particles; and    (3) fluidized-bed adsorption-enhanced water gas shift reaction process.    DESCRIPTION OF DRAWING(S) - The drawing shows the flowchart of manufacture of the hybrid particles. (Drawing includes non-English language text)    Preparation of slurry (10)    Preparation of primary integrated particles (20)    Dry-baking primary integrated particles (30)
NOVELTY - Curable polymer having an ethylene oxide content above 50 wt.% comprises a backbone, pendant, and following side chains (a) and (b): (a) side chains which comprise a poly(ethylene oxide) group and are free from ethylenically unsaturated groups; and (b) side chains which comprise an ethylenically unsaturated group; where the mole ratio of side chains (b):(a) is from 0.001 to 0.95.    USE - The curable polymer is useful for preparing membrane, composite membrane, gas separation cartridge, and gas separation module for separating feed gas containing target gas into gas stream rich in the target gas and gas stream depleted in the target gas. The membrane is useful for separating a mixture comprising polar gas or vapor and non-polar gas or vapor (all claimed).    ADVANTAGE - The invention provides membranes capable of discriminating between gases and having even better fluxes. The membranes can be produced efficiently at high speeds using toxicologically and environmentally acceptable liquids (particularly water).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a process for preparing a membrane comprising curing the polymer;    (2) a membrane comprising the cured polymer;    (3) a composite membrane comprising a porous support and a non-porous membrane in contact with the porous support;    (4) a gas separation cartridge comprising the membrane; and    (5) a gas separation module for separating a feed gas containing a target gas into a gas stream rich in the target gas and a gas stream depleted in the target gas, comprising a housing and the cartridge.
NOVELTY - A papermaking white clay is used as pH buffering agent and inorganic nutrient substance of hydrogen and for mixing with kitchen waste and dewatered sludge of sewage plant to produce hydrogen by biological fermentation.    USE - Papermaking white clay for producing hydrogen (claimed).    ADVANTAGE - The method is simple in operation and low in cost, is capable of reducing the pollution of the papermaking white clay, increases stability and hydrogen production rate of up to 112.39 ml/g volatile solid, and increases hydrogen activity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing hydrogen which comprises:    (A) mixing the dewatered sludge in the sewage plant, the papermaking white clay and the kitchen waste;    (B) adding into the fermenting bottle;    (C) adding water and adjusting the solid content to 5-10 wt.%; sealing; and producing hydrogen by fermenting at 50-53 degrees C.
NOVELTY - The method involves providing an electric power feeding casing in both sides of an electrolytic membrane. An anode side generates oxygen by applying electrolytic voltage between the electric power feeding casings while cathode side generating hydrogen. Application of the electrolytic voltage is stopped (S2) to electric power feeding casings. A high-pressure water electrolzer is cooled (S3) in the state of the stopping electrolytic voltage by applying medium for cooling in the high-pressure water electrolyzer. The cathode side is pressure-reduced (S4).    USE - Shutdown method of high-pressure water electrolyzer for generating hydrogen gas used as fuel gas for fuel cell.    ADVANTAGE - The amount of hydrogen leaked to the anode side can be reduced. The deterioration of the catalyst electrode can be prevented after shutdown. The favorable water electrolysis process can be performed.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating the shutdown process of high-pressure water electrolyzer.(Drawing includes non-English language text)    Step for stopping application of electrolytic voltage (S2)    Step for cooling water electrolyzer (S3)    Step for pressure-reducing cathode side (S4)    Step for stopping cooling process of high-pressure water electrolysis mechanism (S6)
NOVELTY - The method involves setting pressure of the back pressure valve (24). The pressure of the back pressure valve is less than the hydrogen filling pressure of fuel cell vehicle (48). The voltage of the high pressure water electrolyzer (14) is raised, when the desired pressure of the hydrogen is raised above the predetermined pressure. The hydrogen is filled in the fuel cell vehicle.    USE - Method for operating high pressure water electrolysis system of fuel cell vehicle such as car.    ADVANTAGE - The energy consumption of the fuel cell vehicle can be reduced. The hydrogen filling operation of the fuel cell vehicle can be performed efficiently. The loss of energy can be reduced, by decreasing the pressure of hydrogen. The efficiency of the high pressure water electrolysis system can be optimized. The size of the adsorption column can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view illustrating the high pressure water electrolysis system. (Drawing includes non-English language text)    High pressure water electrolysis system (10)    High pressure water electrolyzer (14)    Water suction apparatus (20)    Back pressure valve (24)    Fuel cell vehicle (48)
NOVELTY - The method involves setting lowest pressure of adsorption apparatus (20) obtained from adsorption capacity to the setting pressure of back pressure valve (24). The history of hydrogen filling pressure of the hydrogen filling apparatus is stored, when the hydrogen filling apparatus is filled with hydrogen. The residual adsorption capacity of adsorption apparatus is computed from the history of hydrogen filling pressure of the hydrogen filling apparatus. The setting pressure of back pressure valve is set again, based on the residual adsorption capacity.    USE - Method for operating high-pressure water electrolysis system for fuel cell vehicle.    ADVANTAGE - Since the setting pressure of back pressure valve is set again based on the residual adsorption capacity, the loss of energy due to pressure reduction of hydrogen can be reduced at the time of hydrogen filling. Thus the efficiency of the high-pressure water electrolysis system can be improved. Hence the efficient and economical hydrogen filling operation can be performed.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view illustrating the operation of high-pressure water electrolysis system. (Drawing includes non-English language text)    High-pressure water electrolysis system (10)    Adsorption apparatus (20)    Back pressure valve (24)    Fuel cell vehicle (48)    Controller (50)
NOVELTY - Production of hydrogen from hydrocarbon involves generating hydrogen by reacting sulfur compound of aqueous alkali solution with water, and reducing sulfur compound oxidized by hydrocarbon compound which optionally contains oxygen.    USE - Production of hydrogen from hydrocarbon used for purifying petroleum and fuel for fuel cell used for generating electric power.    ADVANTAGE - The method efficiently and economically provides hydrogen from hydrocarbon without generating carbon monoxide as byproduct.
NOVELTY - A sulfur-tolerant catalyst composition comprises molybdenum disulfide (MoS2) catalyst having total carbon monoxide (CO) conversion in synthesis gas methanation of 75-80%.    USE - Sulfur-tolerant catalyst composition.    ADVANTAGE - The composition creates more active MoS2 catalyst that can be tested in fixed bed unit and with high activity for synthesis gas methanation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a preparation of sulfur-tolerant catalyst comprises processing decomposition of ammonium tetrathiomolybdate in organic solvent in presence of solution comprising solvent and promoter, under gaseous pressure, and producing MoS2 catalyst.    DESCRIPTION OF DRAWING(S) - The drawing is a graph showing the carbon monoxide conversion of molybdenum disulfide catalyst under greater than 2000 psig.
NOVELTY - System for producing hydrogen, comprises: a reactor (410) including a reaction channel adapted to receive a reaction stream (222) including a mixture of supercritical water and a hydrocarbon fuel (111); and a catalyst positioned in the reaction channel so that a product stream (412) containing hydrogen is produced by a reaction in the reaction channel when the mixture is exposed to the catalyst, where the catalyst contains a catalytically active metal and a promoter in a metal format comprising of potassium, sodium, rubidium, lithium, cesium, beryllium, magnesium, calcium, strontium or barium.    USE - The system is useful for producing hydrogen.    ADVANTAGE - The system: is simple; provides high purity hydrogen; and reduces generation of byproduct (i.e. carbon dioxide).    DESCRIPTION OF DRAWING(S) - The figure shows a flow diagram illustrating a system for hydrogen production.    Hydrocarbon fuel (111)    Reaction stream (222)    Heat exchanger (310)    Reactor (410)    Product stream (412)
NOVELTY - Preparation of organic fertilizer, involves uniformly mixing livestock excrement, crushed corn straw and bacterial strain HM for fermentation.    USE - The method is useful for preparing organic fertilizer used for crops.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for organic fertilizer, which comprises (in %): livestock excrement (87), crushed corn straw (13) and bacterial strain HM (2 kg).
NOVELTY - The processor has mixing device that is provided with ferment powder feeding device which is set above a long screw rod mechanism. The long screw rod mechanism has screw rod that is installed in upper screw rod cavity. An upper portion of the screw rod cavity is provided with a blanking port and a feeding port and lower portion is provided with a solid rubbish outlet. A storage device has storage container whose bottom is provided with heat preservation heater and temperature sensor. A deodorizing device is provided with activated carbon filter in exhaust passage.    USE - Processor for kitchen rubbish.    ADVANTAGE - The hydrolyzing and fermenting process can be improved. The kitchen rubbish can be converted into organic fertilizer. The processor is provided with simple operation and rubbish can be recycled easily.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the processor for kitchen rubbish. (Drawing includes non-English language text)
NOVELTY - The system has fermentation unit that ferments a sample reduction for predetermined time. A screening device selects a foreign substance included in the sample reduction in which fermentation is completed. A transfer conveyor transfers the sample reduction selected with the screening device to molding unit. The molding unit agitates the sample reduction and molds the sample reduction. A dryer unit dries livestock urine derived fuel in which the molding is completed. A packout section wraps the dried livestock urine derived fuel.    USE - System for manufacturing solid fuel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for manufacturing solid fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a block flow diagram illustrating system for manufacturing solid fuel. (Drawing includes non-English language text)
NOVELTY - The apparatus has anaerobic absorption promotion unit (200) which diversifies flow of flowing organic sludge according to spiral shape rising fluid path (133) by drawing out gas existing in gas collection domain and re-supplying again to anaerobic absorption unit. A flow control valve (330) for controlling flow of fluid along chimney passage (310) is connected in gas collection domain with spiral shape rising fluid path and chimney passage.    USE - Apparatus for processing organic sludge.    ADVANTAGE - The yield of biogas is improved by enhancing the mixing efficiency of the anaerobic microorganism. Hydrolysis and acid fermentation efficiency is increased while reaction time is shortened.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the apparatus for processing organic sludge.    Spiral shape rising fluid path (133)    Anaerobic absorption promotion unit (200)    Flow control valve (300)    Chimney passage (310)    Flow control valve (330)
NOVELTY - Rectifying biodiesel by acid catalyzed reaction, comprises reacting methanol with an acid catalyst and grease raw materials to obtain the product.    USE - The method is useful for rectifying biodiesel by acid catalyzed reaction.    ADVANTAGE - The method reduces the energy consumption, and shortens the reaction time.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the device for rectifying biodiesel.
NOVELTY - A polymer containing acrylamide group-containing repeating unit (I), is new.    USE - New polymer is used for gas-storage material for storing hydrogen, methane and carbon dioxide (all claimed).    ADVANTAGE - The gas-storage material using the polymer has excellent gas-storage property.    DETAILED DESCRIPTION - A polymer containing acrylamide group-containing repeating unit of formula: -(CH2-C(-R)(-C(=O)-NH-R1))n- (I), is new.    n=15-1800;    R=H or methyl;    R'=X, -Y'-NHC(=O)-X, -X-Y'-NHC(=O)-X, -X-Y'-NHC(=O)-Y'-NHC(=O)-X or -X-Y'-NHC(=O)-Y'-NHC(=O)-Y'-NHC(=O)-X;    X=-Z-R";    Y'=1-10C alkylene;    Z=6-20C arylene;and    R"=linear or branched 1-20C hydrocarbyl or linear or branched 10-20C perfluorohydrocarbyl.
NOVELTY - The bioprocessor has an air inlet that is arranged on end face on of a rotary drum and sleeved with a screen with aperture of less than 10 mm. A discharge door and an exhaust fan are arranged on other end face of drum. Air inlet of an exhaust fan is provided with a screen with aperture of less than 5 mm. An opening-closing feed inlet is arranged near circumferential surface of end face of air inlet. The exhaust fan is externally connected with an air filter. Rollers are supported on bottom of rotary drum and the lower supporting device and rotated by a drive device.    USE - Drum-type hermitia illucens bioprocessor for treating biomass waste used as organic fertilizer.    ADVANTAGE - The treatment efficiency for treating biomass waste is increased by utilizing the drum-type hermitia illucens bioprocessor. Biomass waste can be treated in 3-5 days, and the treatment residues are dried to prevent bad smell and used as organic fertilizer. The bioprocessor is convenient to operate, the need for manual operation is not required, closed treatment can reduce the diffusion of the bad smell and convenient to maintain.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the hermitia illucens bioprocessor.
NOVELTY - The system has an organic waste conveying device (1) that is connected with an anaerobic dry fermentation device (2) so that the organic waste enters into dry fermentation device through organic waste conveying device. Dry fermentation device is connected with a slag conveying device (5) and earthworm bioreactor (6). Earthworm excrement material separating system (7) separates a biogas residue from a fresh earthworm generated in earthworm bioreactor. A feed processing device (8) converts the separated biogas residue and fresh earthworm.    USE - Integrated production system of marsh gas and biological organic fertilizer.    ADVANTAGE - The organic waste is recycled and the biological organic fertilizer is produced efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the integrated production system of marsh gas and biological organic fertilizer. (Drawing includes non-English language text)    Organic waste conveying device (1)    Anaerobic dry fermentation device (2)    Slag conveying device (5)    Earthworm bioreactor (6)    Earthworm excrement material separating system (7)    Feed processing device (8)
NOVELTY - A Hypoxylon DPZ-SYz-36 (CGMCC 4872), is new.    USE - The Hypoxylon DPZ-SYz-36 is useful for producing cellulase and preparing bio-fertilizer for degrading organic matter (claimed). The cellulase is useful for degrading cellulose present in root of Rhizophora stylosa.
NOVELTY - The method involves allowing solid excrement of livestock and poultry with dry mass concentration of more than 15% to enter into fermentation device directly for producing biogas. Organic fertilizer is produced using fermentation residue.    USE - Method for producing marsh gas and organic fertilizer by dry fermentation of livestock and poultry excrement.    ADVANTAGE - Organic fertilizer can be obtained with high efficiency.
NOVELTY - Method of producing marsh gas, involves (a) adding 80% water to domestic sewage to dilute the sludge until water content of the sludge reaches 93-94%, heating the sludge at 37 degrees C, and adding the hot sludge to anaerobic reactor for performing anaerobic reaction for 20 days to produce marsh gas, or (b) adding 20% water and wheat corn straw in ratio of 1:15 to marinating tank of the anaerobic reactor, subjecting the mixture to anaerobic reaction at 37 degrees C for 40 days to produce marsh gas.    USE - The method is useful for producing marsh gas and bio-organic fertilizer.    ADVANTAGE - The method avoids secondary pollution, and manual addition of urea, overcomes problems of vehicle-mounted transportation, and requires small area for storage.
NOVELTY - A biological diesel esterification reaction device manufacturing method involves connecting an upper part gas outlet pipe to an esterification kettle (1) with an air bubble trap (2). A fan (6) is made of a lower methanol rectifying tower head side inlet. A methanol rectifying tower bottom box is directly connected with a rectifying kettle (3). A methanol rectifying tower (4) is directly connected with a condenser (5). Methanol gas is passed into the esterification kettle through the fan during biologic diesel oil methyl esterification reaction.    USE - Method for manufacturing a biological diesel esterification reaction device.    ADVANTAGE - The method enables utilizing heat of methanol steam during esterification reaction, recycling methanol to gas phase, reducing gasified heat loss and improving heat energy utilization ratio and saving industrial cooling water to reduce condensing process of the methanol to save energy consumption and reduce cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biological diesel esterification reaction device.    Esterification kettle (1)    Air bubble trap (2)    Rectifying kettle (3)    Methanol rectifying tower (4)    Condenser (5)    Fan (6)
NOVELTY - A bio-organic fertilizer producing method involves processing horse manure through black soldier fly, and crushing the horse manure to thickness of 1-5mm. The crushed horse manure is added with auxiliary materials such as feather powder, meat and bone meal, and spray-dried blood cells to obtain compost. Eggs of the black soldier flies are inoculated on a surface of the obtained compost and cultured at 25-35 degrees C for 20-30 days. The cultured compost is collected and dried to obtain bio-organic fertilizer.    USE - Method for producing bio-organic fertilizer.    ADVANTAGE - The method enables producing the bio-organic fertilizer with strong processing ability and less energy consumption in an eco-friendly manner. The method enables utilizing the horse manure for preparing the bio-organic fertilizer, thus converting waste into valuable products.
NOVELTY - An organic fertilizer preparing method involves crushing horse dung at a thickness of 1-5 mm, and adding auxiliary material to obtain a culture medium. Housefly ovum is inoculated on a surface of the culture medium and cultured at 25-35 degrees C for 4-5 days. The culture medium is collected and dried to obtain an organic fertilizer, where the auxiliary material is feather powder, meat, bone meal and blood albumen powder.    USE - Method for preparing an organic fertilizer and a biological protein (claimed).    ADVANTAGE - The method enables preparing the organic fertilizer in an environment-friendly manner with strong processing capability and low energy consumption.
NOVELTY - A microbial photoelectrochemical system has an electrolytic tank (1) and an ion exchange film (6) arranged in the electrolytic tank. The electrolytic tank is divided into an anode chamber (7) and a cathode chamber (8), which is internally filled with sewage including organic pollutant and electrolytic solution, respectively. The anode chamber and the cathode chamber are separately provided with an anode (2) and an optical cathode (4), which are connected to a resistor (3) by threads. One side of the optical cathode is provided with a fully light transmitting quartz glass window (5).    USE - Microbial photoelectrochemical system for use in electricity production, hydrogen generation and sewage treatment.    DETAILED DESCRIPTION - A microbial photoelectrochemical system has an electrolytic tank and an ion exchange film arranged in the electrolytic tank. The electrolytic tank is divided into an anode chamber and a cathode chamber, which is internally filled with sewage including organic pollutant and electrolytic solution, respectively. The anode chamber and the cathode chamber are separately provided with an anode and an optical cathode, which are connected to the resistor by threads. One side of the optical cathode is provided with a fully light transmitting quartz glass window. The anode comprises an electricity-generating microbe and an anode substrate. The optical cathode is made of semiconductor material with sunlight response.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a microbial photoelectrochemical system.    Electrolytic tank (1)    Anode (2)    Resistor (3)    Optical cathode (4)    Light transmitting quartz glass window (5)    Ion exchange film (6)    Anode chamber (7)    Cathode chamber (8)
NOVELTY - Preparing adenine, comprises (i) reacting 9H-purin-6-yl acetate and superfluous phosphorus oxychloride under catalysis of N,N-dimethylaniline and then performing post-treatment to obtain 6-chloropurine, and (ii) aerating ammonia gas to aqueous solution of 6-chloropurine until reaching saturation in a high pressure kettle, then closing the reaction kettle and warming to 120-140 degrees C for complete reaction, regulating pH value of reaction solution to 7-8, then cooling to separate crude product of adenine, refining the crude product by using water, and decoloring it by using activated carbon.    USE - The method is useful for preparing adenine.    ADVANTAGE - The method: has high production efficiency, high product yield and purity, and low production cost; and has less waste gas, waste water and waste residue.
NOVELTY - Preparing lapatinib intermediate compound comprises (a) performing reflux reaction on substituted 4-(benzyloxy)-3-chloroaniline compound (I) and 4-chloro-6-iodo-quinazoline in isopropanol, (b) preparing palladium catalyst, (c) mixing the product obtained in step (a), palladium catalyst, 5-formyl-2-furan boronic acid and potassium carbonate in a first organic solvent, and (d) mixing the product obtained in step (c), an organic alkali and 2-aminoethylmethylsulfone hydrochloride in a second organic solvent, and reacting to obtain lapatinib intermediate or its analogues.    USE - The method is useful for preparing lapatinib intermediate compound.    ADVANTAGE - The method uses non-homogeneous phase palladium catalyst, which can be easily recycled, thus it saves the raw material and it is environment-friendly.    DETAILED DESCRIPTION - Preparing lapatinib intermediate compound comprises (a) performing reflux reaction on substituted 4-(benzyloxy)-3-chloroaniline compound of formula (I) and 4-chloro-6-iodo-quinazoline in isopropanol, (b) mixing kieselguhr, stannous chloride, trifluoroacetic acid, hydrogenchloropalladate and polyvinylpyrrolidone in water, heating the mixture to 100-150 degrees C and reacting to obtain palladium catalyst, (c) mixing the product obtained in step (a), palladium catalyst, 5-formyl-2-furan boronic acid and potassium carbonate in a first organic solvent, where the reaction temperature is 70-90 degrees C, and (d) mixing the product obtained in step (c), an organic alkali and 2-aminoethylmethylsulfone hydrochloride in a second organic solvent, and reacting to obtain lapatinib intermediate or its analogues.    R = methyl, halo, ester group or cyano group.
NOVELTY - Two phase reaction method for improving efficiency of biomass fuel prepared using grass, involves fermenting grass in acid production hydrolysis reactor, obtaining acid, and subjecting undigested or undecomposed residues to fermentation to obtain methane.    USE - The method is useful for improving efficiency of biomass fuel (claimed).    ADVANTAGE - The method improves utilization rate of raw materials, and reduces detention time of the whole reaction so as to improve the reaction efficiency of the hydrolysis phase and the reactor volume. The method does not perform solid-liquid separation process and thus produces methane continuously.
NOVELTY - The method involves desulfurizing and dewatering biogas in the storage tank. The biogas with multiple components is obtained. The main components include biogas and carbon-dioxide. The biogas and carbon-dioxide are separated by the purifying device.    USE - Biogas fertilizer compounding method.    ADVANTAGE - The heating efficiency of the process can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biogas fertilizer compounding method.
NOVELTY - Preparation of biogas (cellulose product), involves adding inert solid particles to liquid culture medium.    USE - The method is useful for preparing biogas (cellulose product).    ADVANTAGE - The suspended inert solid particles provide energy needed for microbial growth and thus improves the cellulose production. The biogas has improved density, mechanical property and quality.
NOVELTY - A kitchen garbage aerobic ferment disposing device has a fertilizer chamber (1) provided with an aeration tank (4) and a filtrate. The aeration tank is located at a compost cabin. A bottom part of the aeration tank is covered with a ventilation plate. A penetrating fluid circulating system is provided with a percolate and a percolate water distribution pipe. A percolate collecting device is arranged on the aeration tank. A penetrating fluid water distribution pipe is arranged in the compost cabin and connected to the percolate collecting device through a corrosion sewage pump.    USE - Kitchen garbage aerobic ferment disposing device.    ADVANTAGE - The device is inexpensive, environment-friendly and easy to process and control, and occupies small space.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a kitchen garbage aerobic ferment disposing device.    Fertilizer chamber (1)    Aeration tank (4)    Leachate collecting pool (6)
NOVELTY - Composition comprises (in parts weight): fly ash (1-2), decomposed straw (2-4), perlite (2-4) and diatomite (1-2).    USE - The composition is useful for controlling soil nematodes (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing the above-mentioned composition, which involves (a) sieving fly ash and shell powder using 60 mesh size to obtain particles of size less than 0.25 mm, (b) cutting the straw into 2-3 cm, adding water and straw decomposition agent (0.05-0.15 wt.%) or chicken manure (10-15 wt.%) to the straw to obtain decomposed straw, (c) uniformly mixing the particles obtained in step (a), decomposed straw and perlite to obtain components and piling the components, and (d) fermenting the components for 20-30 days.
NOVELTY - A sludge utilizing method involves taking sludge from bottom part of a biogas pool, where solid content in the sludge is about 10%. The sludge is directly used as farmland fertilizer, grain fertilizer and granule fertilizer, and packed and sold.    USE - Method for utilizing sludge in biogas pool.    ADVANTAGE - The method enables improving internal hole structure of coal, coal gasification reaction and transformation rate of carbon and reducing residual carbon in ash. The method enables improving utilization rate of marsh gas tank sludge, thus increasing income and reducing sludge pollution.
NOVELTY - Environment-friendly household insecticidal composition, is prepared using (in parts weight): raw materials chosen from Celastrus angulatus (5), neem (7), foaming agent (3), Aconitum (2), Stemona (3), Achyranthes (3), herba scutellariae barbatae (5), Perilla (3), Eucalyptus (5), Geranium (5), rosemary (2), onion (3), small white plant (5).    USE - The composition is useful for controlling and killing household insects including cockroach, mosquito, fly, flea, bug, mite, and ticks.    ADVANTAGE - The composition is pure plant preparation, non-toxic and environmentally-friendly, and does not have any stimulary function with respect to human, and discharge any pollutant in the production process.
NOVELTY - A ligustilide is prepared by mixing Angelica oil and Ligusticum wallichii oil, subjecting to vacuum fractionation at 100-110 (preferably 105-110) degrees C, flow speed of 0.5-5 (preferably 1-2) ml/minute and pressure of 5-100 (preferably 5-50) Pa, pre-heating obtained product at 40-45 degrees C, and subjecting to molecular distillation at 70-90 (preferably 80-85) degrees C, rotation speed of 50-500 (preferably 80-350) revolutions/minute and pressure of 0.1-10 (preferably 0.1-5) Pa.    USE - Method of preparing a ligustilide.    ADVANTAGE - The method prepares product having a purity of 93.2-98.8%, and does not utilized solvent thus making the method environment-friendly.
NOVELTY - A biogas type anaerobic digestion device has biogas backflow main pipe (10), anaerobic digestion pool body (1) and a gas return main pipe placed in an air displacement pump (18), where the biogas backflow main pipe extends downward from two opposite sides of a horizontal methane backflow main pipe. Perforated exhaust branch pipe ends of a resistor (7) are connected with an automatic open valve (8). A valve (15) is provided in an end gas discharge tube (14).    USE - Biogas type anaerobic digestion device for mud of pool body.    ADVANTAGE - The device has high processing efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biogas type anaerobic digestion device.    Anaerobic digestion pool body (1)    Resistor (7)    Automatic open valve (8)    Biogas backflow main pipe (10)    End gas discharge tube (14)    Valve (15)    Air displacement pump (18)
NOVELTY - Preparation of nutrient fertilizer for Jasminum floridum, involves using (in wt.%): plant ash powder (6-8), wheat straw powder (7-9), cake flour (4-6), broomcorn cake powder (11-13), sunflower seed powder (8-12), corn stigma (8-10), honeysuckle powder (11-13), peanut shell powder (6-8), chicken manure (4-6), rabbit manure (4-6), broadleaf wooden material (11-13), bone powder (-3), pine needle powder (4-6), Coptis powder (0.2-0.4), Camellia (0.2-0.4), green Chinese onion powder (0.1-0.3), and pepper powder (0.1-0.3).    USE - The method is useful for preparing J.floridum nutrient fertilizer.    ADVANTAGE - The prepared fertilizer is rich in nutrients, inexpensive and prepared by simple process using easy available raw material, promotes rapid growth of J.floridum, and provides disease resistance.
NOVELTY - Preparation of Hippeastrum vittatum nutrient fertilizer, involves using (in wt.%): rapeseed powder (8-12), yellow bean cake powder (19-21), broomcorn (7-9), corn core powder (6-8), barley straw powder (2-6), rice straw powder (4-6), chicken manure powder (9-11), bone meal (11-15), mushroom powder (3), milk powder (3), peanut powder (2-4), towel gourd powder (3), corn powder (2-4), dung (3), honeysuckle powder (7-9), pine needle powder (0.2-0.4), Camellia (0.2-0.4), semen plantaginis (0.1-0.3) and safflower (0.1-0.3).    USE - The method is useful for preparing H.vittatum nutrient fertilizer.    ADVANTAGE - The prepared fertilizer is rich in nutrients, and overcomes problems of low yield, low economic value, small bud, slow growth and susceptibility to diseases and withers.
NOVELTY - Preparation of Camellia nutrient fertilizer, involves using (in wt.%): manure (7-9), chicken manure (6-8), rapeseed cake powder (11-13), cottonseed powder (4-6), mushroom powder (13-15), broomcorn cake powder (2-4), milk powder (1-3), soybean protein powder (18-22), broad-leaf bean powder (1-3), safflower (1-3), honeysuckle powder (1-3), bone powder (11-15), wheat bran powder (2-4), pine powder (5-7), radix aconite powder (0.2-0.4), rhizoma curculiginis (0.1-0.3), Lotus powder (0.2-0.4), and Perilla powder (0.1-0.3).    USE - The method is useful for preparing Camellia nutrient fertilizer.    ADVANTAGE - The prepared fertilizer is rich in nutrients, inexpensive and prepared by simple process using easy available raw material, promotes rapid growth of Camellia, provides disease resistance, and improves brightness of Camellia flower.
NOVELTY - Method for preparing carnation nutrient fertilizer, involves using raw materials chosen from (in wt.%): dried dairy manure (14-18), dried duck manure (4-6), pumpkin stem leaf powder (2-4), towel gourd stem leaf powder (12-16), bone powder (18-20), soybean (3), broomcorn (10-12), plant straw powder (10-12), corn core powder (8-10), mud (2-6), Morinda officinalis powder (0.2-0.4), Coptis powder (0.2-0.4), stramonium (0.1-0.3), fumitory (0.1-3), and radix aconiti powder (4-6).    USE - The method is useful for preparing carnation nutrient fertilizer (claimed).    ADVANTAGE - The fertilizer is cost-effective, can be prepared simply, promotes growth of carnation with good disease resistance property, and produces large and beautiful flowers.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the carnation nutrient fertilizer, which involves (a) mixing the above-mentioned materials, placing the mixture in a stirrer and stirring for 120 minutes, (b) crushing mixture (2%), and transferring to fermenting tank and turning piles, (c) adding human excrement water to the fermenting mixture in a weight ratio of 1:0.5 during pile turning, (d) placing fermented nutrient fertilizer in a molding box to obtain nutrient fertilizer blocks with height, width and length of 15, 10 and 8 cm respectively, where the nutrient fertilizer blocks are tight, sturdy, and not easy to be crushed by hands.
NOVELTY - Preparation of 15- alpha hydroxylated D-ethylgonendione comprises fermenting with Penicillium raistrickii (ATCC 10490); and adding D-ethylgonendione substrate for biotransformation, where the biotransformation system comprises an ionic liquid phase and a buffer solution phase at a volume ratio of 0.25-1.25:1.    USE - Method for the preparation of 15- alpha hydroxylated D-ethylgonendione (claimed).    ADVANTAGE - The method does not require an organic solvent thus reducing usage of organic solvents which severely damages the environment. It has mild reaction condition, simple transformation apparatus, is inexpensive, and reduces environment pollution.
NOVELTY - An organic fertilizer is prepared by fermenting garden wastes having water content of 50-60% and comprising tree branches, grass clippings and/or fallen leaves; and adding auxiliary materials comprising fermentation agent, sediment, peat, kitchen wastes and urea.    USE - Organic fertilizer.    ADVANTAGE - The fertilizer has complete nutrient component. Preparation method is simple, recycles waste and protects the environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fertilizer by preprocessing collected garden wastes until grain diameter of 3-10 mm, and uniformly mixing; adding (wt.%) fermentation agent (0.1-0.2, preferably 0.2), sediment (0.2-0.4, preferably 0.4), peat (0.2-0.4, preferably 0.4), kitchen wastes (0.3-0.5, preferably 0.5) and urea (1-2, preferably 1); uniformly mixing and piling until bottom width is 120-200 (preferably 150) cm, length is 50 cm and height of rectangular pile body is 50-80 (preferably 70) cm; regularly measuring temperature, and turning and stirring once a day when the temperature reaches 50-60 degrees C; and aging for 1-2 weeks.
NOVELTY - Diaryl pyridine is synthesized by reacting 3-benzyl-5-(2-hydroxyethyl)-4-methylthiazolium chloride catalyst, triethylamine, and epichlorohydrin in solvent; adding substituted aldehyde, heating and stirring at 50-100 degrees C for 20-40 minutes or microwave irradiating at frequency of 150-500 Hz for 5-15 minutes; adding ammonium acetate with uniform stirring; heating and stirring the reaction system at 50-100 degrees C for 20-40 minutes or microwave irradiating at frequency of 150-500 Hz for 5-15 minutes; and evaporating the solvent, recrystallizing solid using ethanol to obtain the diaryl pyridine.    USE - Method for synthesizing diaryl pyridine (claimed).    ADVANTAGE - The method has short reaction time, reduced energy consumption, and improved efficiency. It utilizes non-toxic and environment friendly catalyst.    DETAILED DESCRIPTION - Synthesis of diaryl pyridine comprises:    (A) adding (pts.wt.) 3-benzyl-5-(2-hydroxyethyl)-4-methylthiazolium chloride catalyst (1-2), triethylamine (1-2), and epichlorohydrin (100-200) in solvent in a container, and stirring at normal temperature to react;    (B) adding substituted aldehyde (200-400), heating and stirring at 50-100 degrees C for 20-40 minutes or microwave irradiating at frequency of 150-500 Hz for 5-15 minutes;    (C) adding ammonium acetate (100-200) with uniform stirring;    (D) heating and stirring the reaction system at 50-100 degrees C for 20-40 minutes or microwave irradiating at frequency of 150-500 Hz for 5-15 minutes; and    (E) evaporating the solvent, and recrystallizing solid using ethanol to obtain the diaryl pyridine.
NOVELTY - A household biogas furnace combustion unit comprises ten square river sewage heating glass (1), a gas pipe (2), a domestic gas furnace (3) and an electronic switch (4).    USE - Household biogas furnace combustion unit for use in urban river sewage.    ADVANTAGE - The combustion unit reduces natural disasters.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a household biogas furnace combustion unit.    Square river sewage heating glass (1)    Gas pipe (2)    Domestic gas furnace (3)    Electronic switch (4)
NOVELTY - Method for preparing culture material for snow lotus, involves using components (in wt.%) bean cake powder (3-9), peanut cake powder (30-40), peanut stem and leaf powder (6-18), broomcorn (10-20), silkworm powder (10-12), dry sugarcane (2-6), corn powder (5-15), tuckahoe (0.5-1), bone powder (0.5-1), hawthorn powder (0.5-1), lotus powder (2-6) and vitamin (0.5-1).    USE - The method is useful for preparing culture material used as organic fertilizer for snow lotus.    ADVANTAGE - The method is simple and easy to perform, and cost-effective. The culture material generates beneficial microorganisms during growth of snow lotus.
NOVELTY - Preparing fertilizer for cultivating crown daisy Chrysanthemum, involves using (in wt.%) dried rabbit manure (10-14), dried chicken manure (10-16), plant ash (12-18), cotton powder (6-8), colza cake powder (6-10), wheat straw powder (2-6), peanut stem leaves powder (15-25), balsam pear stem leaves powder (1-3), Angelica (2-4), Perilla powder (1-3), cypress (3-5), pine needle powder (1-3), semen cassiae powder (2-4), tuckahoe (1-3), and Cordyceps (2-4).    USE - Preparing fertilizer for cultivating crown daisy Chrysanthemum.    ADVANTAGE - The method is cost-effective, easy and simple, improves quality and growth of Chrysanthemum, and prevents Chrysanthemum from disease. The cultivated Chrysanthemum has fresh taste and rich nutrition.
NOVELTY - Long-acting microbial organic fertilizer, comprises (in parts weight): animal manure (418-550), hardwood leaf powder (98-150), beanstalk (58-85) corn (48-80), grass carbon powder (78-90), bean powder (40-60), calcium magnesium phosphate (70-100), gypsum powder (15-30), hydrated product (6-8), fast fermenting composite microbial inoculum (3-6), humic acid (40-60 l), brown sugar (4-6), wood ginger powder (2-4), white crane Ganoderma lucidum powder (2-4), quis quails (1-3) and purified water (180-310).    USE - The long-acting microbial organic fertilizer is useful for continuous cropping of melon plant, ginseng, American ginseng, and Chinese medicinal plant.    ADVANTAGE - The fertilizer improves activity of the beneficial microorganism, stress resistance of the plant and soil physicochemical property, inhibits harmful microorganism in soil, degrades the farm chemical residue in soil and other harmful substance, balances soil nutrient, after fertilizing, and increases quality standard of the organic products.
NOVELTY - Method of preparing culturing material of Pleurotus geesteranus, involves using (in wt.%): dry duck manure (45-55), corncob (4-12), rice husk meal (3-9), broadleaf wooden meal (4-12), gourd leaf powder (3-9), balsam pear leaf powder (8-12), bagasse powder (3-11), cucumber stem leaf powder (1-3), edible salt (0.5-1), rape root powder (0.5-1), safflower (0.5-1), and bone powder (0.5-1).    USE - The method is useful for preparing culturing material of P.geesteranus.    ADVANTAGE - The method is simple, improves amount of beneficial microorganism in the ingredients, and promotes growth of P.geesteranus. The cultured product has big end, increased weight, rapid growth rate, and is tender, delicious and nutritious.
NOVELTY - Preparation of nutrient fertilizer, involves using (in wt.%): Atractylodes rhizome (7-9), radix aconiti powder (6-8), monkshood powder (2-4), semen plantaginis (4-6), peanut cake powder (11-12), towel gourd leaf powder (11-13), rabbit manure (7-9), soybean straw powder (6-9), taro leaf powder (7-9), cotton powder (6-8), plant ash (8-10), bone powder (1-3), milk powder (1-3), pine needle powder (2-4), licorice powder (5-7), sesame powder (0.2-0.4), sugar powder (0.2 to -0.4%), onion powder (0.1 to -0.3) and tea powder (0.1-0.3).    USE - The method is useful for preparing nutrient fertilizer for promoting growth of tulip.    ADVANTAGE - The fertilizer improves yield of tulip flowers, develops fine roots of tulip, has improved economic value, enables rapid growth of tulip, and prevents death of tulip plants caused by multiple diseases. The fertilization for several times is prevented.
NOVELTY - Preparing Cedrela sinensis culturing fertilizer, involves using (in wt.%): dry pig manure (6-10), sheep manure (14-16), cottonseed powder (4 to -6), soybean cake powder (12-16), vegetable cake straw powder (13-15), wood ash powder (10-12), soybean straw powder (2-4), barley straw powder (2 to -6), mulberry leaf powder (8-12), tea (1-3), Ganoderma (2-4), medlar (2-4), Chinese (1-3), Houttuynia cordata (1-3), Morinda officinalis powder (1-3), radix paeoniae alba (1-3).    USE - The method is useful for preparing fertilizer for planting C.sinensis for preventing yellowing of leaves and leaf spot.    ADVANTAGE - The fertilizer overcomes shortage of nutrition, can be easily absorbed by plant, and improves resistance of plant with respect to diseases and insect.
NOVELTY - A fish protein preparation method involves heating fish processing waste for 1-3 hours at 85-100 degrees C. The heated fish processing waste is cooled, and the pH of the cooled product is adjusted to 7-8. The pH adjusted product is enzymolysed by adding protease to obtain enzymolysis liquid. The obtained enzymolysis liquid is cooled to room temperature. pH of the cooled product is adjusted to 3.5-4.5 and the product is subjected to acid hydrolysis at 90-105 degrees C. Residues are removed from the product by filtration, and the pH is adjusted to 4.5-5.5 to obtain fish protein.    USE - Method for preparing fish protein.    ADVANTAGE - The method enables preparing fish protein under mild reaction condition in a simple, safe and eco-friendly manner.
NOVELTY - The method involves forming an unevenness pattern on a surface of an electrode support. A molding frame is provided with a stamp pattern corresponding to the unevenness pattern. The electrode support is connected with the molding frame. The electrode support is made of a ceramic material. A solid electrolyte layer is formed on the surface of the electrode support. An anode is fixed to a side of the electrode support. An interconnector is fixed to another side of the electrode support. A relief portion is provided with multiple unit cells.    USE - Method for manufacturing a flat pipe-type fuel cell unit.    ADVANTAGE - The method ensures secure air passage to the interconnector.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow chart illustrating a flat pipe-type fuel cell unit manufacturing method.'(Drawing includes non-English language text)'
NOVELTY - The apparatus has a main body provided with a drain gutter to discharge water. A separation film is installed at an inner part of the main body. An inlet port is provided with a lower part of the main body to flow reaction gas. Moisture falls down from the upper and lower parts of the main body. An opening and closing unit is provided with a two-way valve to open/close the upper and lower parts of the main body. A connection line block is connected with the two-way valve that is made of a suspended material. Multiple plates are arranged between an air-outlet and a separation film.    USE - Automatic gas-liquid separating drain apparatus for a fuel cell generation system in a home.    ADVANTAGE - The apparatus prevents a connection line block and the drain gutter from generated vibration, moisture and noise during process. The apparatus improves power generation capacity and efficiency of a fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an automatic gas-liquid separating drain apparatus.
NOVELTY - The method comprises synthesizing a composition comprising a perovskite, applying the composition on an electrolyte support to form an anode, applying nickel oxide (0.1-5 wt.%) to the composition on the anode, utilizing a dry-pressing method to form the electrolyte support, and operating the anode as a cathode. The composition is synthesized by a microwave-assisted combustion method and synthesized with a metal precursor.    USE - The method is useful for fabricating a solid oxide fuel cell.    ADVANTAGE - The method is capable of simply and rapidly fabricating the solid oxide fuel cell at high operating temperature with high density and stability and improved electrical conductivity in a convenient manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a solid oxide fuel cell.
NOVELTY - A transmission power amount database (DB) server (160) detects and stores transmission power amount transmitted to electric power system (130) from fuel cell stack. A receiving power quantity DB server (170) detects and stores receiving power quantity received from electric power system. An electric energy comparison server (180) compares transmission power amount stored in transmission power amount DB server and receiving power quantity stored in receiving power quantity DB server, such that the electric energy produced from fuel cell stack is supplied directly.    USE - Fuel cell power generation system for domestic and industrial applications.    ADVANTAGE - The power generation efficiency of the fuel cell can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the fuel cell power generation system. (Drawing includes non-English language text)    Fuel cell power generation system (100)    Electric power system (130)    Transmission power amount DB server (160)    Receiving power quantity DB server (170)    Electric energy comparison server (180)
NOVELTY - Carbon-containing wastes first undergo anaerobic fermentation, after which the obtained fermented residue is mixed with filler, moulded and subjected to thermal decomposition in a reducing medium without access to oxygen at temperature 300-1050 degrees C. The filler used is solid combustible carbon-containing materials. The mixture is moulded by rolling with addition of long-fibre carbon-containing materials during the rolling process.    USE - Chemistry.    ADVANTAGE - Invention increases the efficiency of the process of processing carbon-containing wastes. 3 cl, 1 ex
NOVELTY - The method involves granulating biomass by the volume reduction device (4) whose dehydration of biomass is performed. The granulated biomass is injected to a boiler as a fuel. A pressure roller is positioned at center portion of dies. The granulated biomass is conveyed to the installation location of boiler with a mobile vehicle (1).    USE - Method for utilizing biomass of manure.    ADVANTAGE - The biomass containing moisture contents can be utilized effectively. The transport cost for conveying biomass fuel to the installation location of granulator can be reduced. The efficiency and operability for utilizing biomass of manure can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows the conceptual diagram illustrating the process for utilizing biomass of manure.    Mobile vehicle (1)    Hook roll container (3)    Volume reduction device (4)    Process target object (5)    Conveyance (6)
NOVELTY - The device has a heat evaporator installed on a heat storage heat exchange tank body. An interface and an over-heat evaporator are connected with a solar light condensing device, a tube array or a coil pipe evaporator, a heat exchanger and a power generating unit. A heat evaporator is fixed in the heat storage heat exchange tank body. A biomass gasification furnace is provided with a combustion chamber, a fuel gas nozzle and an air outlet. The air outlet is connected with a biomass storage bag and an air pre-heater.    USE - Fused salt storage device for storing solar energy, biomass gasification complementary energy and gas thermal energy.    ADVANTAGE - The device can store the solar energy, biomass gasification complementary energy and the gas thermal energy in a controllable and continuous manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic circuit diagram of a fused salt storage device for storing solar energy, biomass gasification complementary energy and gas thermal energy.
NOVELTY - The furnace has a furnace body whose high temperature area is arranged with a cracking pipe. An end of the cracking pipe is connected with an input pipe channel. Another end of the cracking pipe is connected with an output pipe. The cracking pipe is paved with a catalyst, where gas enters into the cracking pipe from an input pipe. The catalyst is nickel-base catalyst, natural mineral catalyst or alkali metal-based catalyst. An output pipeline of a three-way valve is connected with a cracking tube passage. An emptying pipe is hung on the three-way valve.    USE - Biomass gasification furnace.    ADVANTAGE - The furnace improves tar cracking processing efficiency, effectively reduces contents of tar in biomass gas during biomass gas preparation and avoids generation of pollution to an environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing biomass fuel gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a biomass gasification furnace.
NOVELTY - The furnace has a furnace body whose top is provided with a rubbish feed inlet and a pyrolysis gas outlet. A lower part of the furnace body is fixed with a furnace wall air inlet pipe and a furnace wall air inlet hole. A bottom part of the furnace body is fixed with a fire grate and a bottom air inlet pipe. A top part of the furnace body is equipped with a central air inlet pipe i.e. single air inlet tube. The central air inlet pipe is located at the air inlet hole. An upper end pipe wall of the central air inlet pipe is provided with double-row central air inlet holes.    USE - Middle gas supply type rubbish gasification furnace.    ADVANTAGE - The single air inlet tube ensures rubbish pyrolysis and gasification when an inner wall part of the furnace body can obtain enough air so as to design larger diameter of refuse gasification furnace for rubbish treatment of large amount of rubbish processing capability.    DESCRIPTION OF DRAWING(S) - The drawing shows a front partial sectional view of a middle gas supply type rubbish gasification furnace.
NOVELTY - The method involves crushing agriculture and forestry waste processing granular. A granular material is provided into a cracking furnace, and ignition heating is performed by a microwave heating source in the cracking furnace. The material is not completely in combustion condition with air, and combustible gas is generated by a thermal cracking reaction. Cooling processing is conveyed to a storage tank, where thermal-cracking reaction temperature is 300 degrees centigrade to 700 degrees centigrade.    USE - Agricultural and forestry waste pyrolysis method.    ADVANTAGE - The method enables generating the vacuum pump gas by the negative pressure air, and makes the material to partially combustion condition with air, thus improving fuel gas efficiency and production capacity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an agricultural and forestry waste pyrolysis device comprising a cracking furnace body.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an agricultural and forestry waste pyrolysis device.
NOVELTY - The device has a carbon tank arranged at a bottom part of a furnace body. An outer wall of the furnace body is equipped with a carbon collecting device for regenerating activated carbon. A carbon collecting pool is connected to the collecting device for regenerating the activated carbon in the carbon tank via a water outlet pipe with a mud pump. The carbon collecting pool is connected to the carbon tank via a water pipe. The carbon collecting pool is formed as a hopper arranged on an inner wall of a fire grate of the furnace body.    USE - Straw gasification furnace carbon discharging device.    ADVANTAGE - The device ensures that a bottom part of the furnace body is utilized to collect carbon dust and carbon ash so as to discharge carbon via the outer wall of the furnace body and ensure better carbon sealing effect so as to improve discharging process of gas generated by combustion process. The device can realize continuous straw gasification to discharge ash and carbon in a better manner. The device avoids influencing the furnace body and ensures stable performance in an inexpensive manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a straw gasification furnace carbon discharging device.
NOVELTY - The boiler has a threaded smoke pipe (6) arranged on an upper end of a boiler body (1). An upper boiler cylinder (8) is connected with water cooling fire grate and a boiler smoke gas outlet (19). A separating belt (11) is provided with a gasifying burning device (3). The gasifying burning device is arranged on the boiler body and provided with a gas nozzle. A heat resistant cast fixing fire grate (10) is arranged on a bottom part of the boiler body. A down-sucking type biomass gas generating chamber is formed between the upper boiler cylinder and the water cooling fire grate.    USE - Down suction-type biomass formed fuel gasified boiler.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a down suction-type biomass formed fuel gasified boiler.    Boiler body (1)    Gasifying burning device (3)    Threaded smoke pipe (6)    Upper boiler cylinder (8)    Heat resistant cast fixing fire grate (10)    Separating belt (11)    Boiler smoke gas outlet (19)
NOVELTY - Complex decolorizing agent comprises (in wt.%) zinc oxide (80-95) and sodium carbonate (5-20).    USE - The complex decolorizing agent is useful for decolorizing waste oil for preparing biodiesel.    ADVANTAGE - The decolorizing agent: decolorizes waste oil, which has lower acid value and dehydration effect; and is economical, simple to prepare, easy to use and can be recycled.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) preparing the complex decolorizing agent, comprising weighing zinc oxide and sodium carbonate, and adding a small amount of water to dissolve into a paste, heating at 120-150 degrees C for 3-5 hours, cooling to room temperature and crushing into powder;    (2) decolorizing waste oil for preparing biodiesel, comprising decolorizing dark biodiesel prepared from waste oil by using the complex decolorizing agent to obtain light-colored biodiesel; and    (3) reclaiming and reusing the complex decolorizing agent, comprising using the complex decolorizing agent and adding water, and separating an oil layer, drying at 120-150 degrees C for 3-5 hours and reusing.
NOVELTY - The apparatus has air introduction tube (6) that is arranged on the side surface of a process chamber (2). A magnetic action element (4) is provided with a positioned magnet, so that north-pole and south-poles are faced at a perpendicular direction. A heat insulating material layer (4b) is provided to cover the magnet and paramagnetic plate-shaped object (4c) which is provided to adjoin to the positioned magnet, so that magnetic induction is performed with magnet.    USE - Thermal decomposition apparatus for incinerating industrial waste materials such as waste plastic, scrap wood, organic refuse, used paper and adhesive sludge.    ADVANTAGE - Since oxygen is concentratively supplied to the bottom portion of the process chamber in which waste material is located abundantly, waste material can be burned efficiently. The combustion efficiency of the waste material can be increased. The fuel oil cost can be reduced in the case of incineration of the waste material, and the process cost can also be reduced. The generation of the dioxin can be suppressed. The cheap thermal decomposition apparatus can be provided and the installation cost of the apparatus can also be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional views of the thermal decomposition apparatus.    Process chamber (2)    Magnetic action element (4)    Heat insulating material layer (4b)    Paramagnetic plate-shaped object (4c)    Air introduction tube (6)
NOVELTY - The method involves heating a portion of the thermally buffered hydrogen-producing fuel processing system (12) to a thermally buffered temperature range. The portion of the thermally buffered hydrogen-producing fuel processing system is maintained in the thermally buffered temperature range during a period of inactivity. The non-oxidizing gas stream is supplied to the separation assembly during the period of inactivity.    USE - Method for maintaining hydrogen permeability in thermally buffered hydrogen-producing fuel processing system.    ADVANTAGE - The hydrogen-selective elements are maintained effectively during periods of inactivity to the hydrogen-processing and fuel cell industries.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of thermally buffered hydrogen-producing fuel processing system.    Consuming assembly (10)    Hydrogen-producing fuel processing system (12)    Mixed gas stream (20)    Energy consuming device (46)    Power system (56)
NOVELTY - The system has an interface for system settings. A reversible sensor i.e. radio wave receiver, is formed of an actuator. A first microcontroller comprising configurable input-outputs is interconnected with reversible components (105, 107) by an input-output power amplification stage. Second and third microcontrollers are provided with respective safety functions and energy control functions. A data base stores parameters of the components. A fuel cell (106) produces, stores and supplies energy and raw materials in the form of gas.    USE - Security system for connecting with reversible components e.g. motor, for opening and closing a rotary door and reversible loudspeaker utilized as a siren, for producing energy.    ADVANTAGE - The system is compatible with sustainable development and provides security objectives using the reversible components according to environmental context and security scenario set.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for producing energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a reversible safety system connected to a loudspeaker and microphone, and connected to a motor for opening a rotary door. '(Drawing includes non-English language text)'    Reversible components (105, 107)    Fuel cell (106)    Input power stages (109, 110)    Tank (111)    Water tank (112)
NOVELTY - Preparing biologic diesel by catalysis of rare earth oxide mesoporous material, involves adding vegetable plant oil and methanol or ethanol to a high pressure kettle, in which the mass ratio of vegetable plant oil to methanol or ethanol is 0.2 to 2:1; adding rare earth oxide mesoporous material amount is plant oil 1 (20%), at 60-240 degrees C mechanically stirring for ester exchange reaction for 1-5 hours; filtering after reaction, separating rare earth oxide mesoporous catalyst to heat, transferring solution to liquid separating funnel, to give rough biodiesel, and byproduct glycerol.    USE - For preparing biologic diesel (claimed), especially biological diesel oil.    ADVANTAGE - The method has simple production technique, high catalytic activity, and the catalyst can be repeatedly used, convenient post-treatment, no industrial waste water.    DETAILED DESCRIPTION - Preparing biologic diesel by catalysis of rare earth oxide mesoporous material, where vegetable oil is used as raw material to react with methanol or ethanol, adding a certain amount of catalyst to obtain biodiesel by esterification and ester exchange, involves adding vegetable plant oil and methanol or ethanol to a high pressure kettle, in which the mass ratio of vegetable plant oil to methanol or ethanol is 0.2 to 2:1; adding rare earth oxide mesoporous material amount is plant oil 1 (20%), at 60-240 degrees C mechanically stirring for ester exchange reaction for 1-5 hours; filtering after the reaction, separating the rare earth oxide mesoporous catalyst to heat; a liquid phase methanol or ethanol by distillation; transferring the solution to a liquid separating funnel, standing, the upper layer is rough biodiesel, the lower layer is byproduct glycerol.
NOVELTY - The method involves utilizing glycerin received from biodiesel production, cassava starch and water. The glycerin is added as additive agents or plasticizers alloy for obtaining a solution or dispersion. A warm solution of water and starch is stirred and cooled in Petri dishes.    USE - Method for producing biofilm from glycerin residual coming from biodiesel production.    ADVANTAGE - The method involves utilizing glycerin received from biodiesel production, cassava starch and water, and hence ensures cost-effective production of biodegradable products of high aggregate value.
NOVELTY - The furnace has an annular water tank arranged on a furnace wall of a hearth and a furnace body (6). An upper part of the annular water tank is provided with a water inlet (82). A lower part of the annular water tank is provided with a water outlet (81). The hearth is provided with a sealed furnace cover. An upper part of the furnace body is provided with the sealed furnace cover from the hearth (3). A hearth cover is provided with an upper cavity. A lower end of the furnace body is provided with a lower cavity. A side part of the lower cavity is connected with a blower (10) of an air inlet.    USE - Environment-friendly energy-saving straw gasification furnace.    ADVANTAGE - The furnace is simple in structure, convenient to use, environment-friendly, and saves energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of an environment-friendly energy-saving straw gasification furnace.    Hearth (3)    Furnace body (6)    Blower (10)    Water outlet (81)    Water inlet (82)
NOVELTY - The method involves diverting purified raw biogas (2) via adsorbers (A1-A4) made of adsorber resin in an adsorption phase in ambient pressure. The raw gas is regenerated in a regeneration phase of the adsorbers using flushing gas (7) e.g. air, at a temperature and the pressure. The biogas is purified before a separation process of carbon dioxide, desulfurized and dried. Minor components are removed, and a flushing process of the adsorbers is implemented with the biogas for avoiding contamination in the biogas at beginning of the adsorption phase and controlled by valves (V1-V4) and sensors.    USE - Method for separation of carbon dioxide from purified raw biogas i.e. methane, in a biogas system.    ADVANTAGE - The method enables complete regeneration of adsorber materials and moderately reduces energy expenditure for regeneration, thus separating carbon dioxide from the purified raw biogas in an economical manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for separation of carbon dioxide in a biogas system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a device for separation of carbon dioxide from purified raw biogas in a biogas system.    Adsorbers (A1-A4)    Blowers (G1, G2)    Valves (V1-V4)    Heat exchangers (WT1, WT2)    Purified raw biogas (2)    Flushing gas (7)
NOVELTY - An organic waste composter (101) comprises a vertically orientated processing vessel having a tank (1) with at least one heating unit, a stirring mechanism (8), an unit for injection of air for composting waste, a waste inlet and a waste overflow (6).    USE - As vertically orientated organic waste composter for compacting organic waste (claimed).    ADVANTAGE - The heating units reduce the time required for the composite dry and wet waste material to reach the optimum composting temperature; and maintain the composite material at an appropriate temperature to ensure safe decomposition of the waste material in a predetermined timescale. The organic waste composter prevents the growth of harmful microorganisms such as pathogens, under strict legislation; improves process of composting; obviate or mitigate the problem of non standard size particles entering the processing vessel as well as ensuring there are no blockages to the flow of waste material during the ongoing composting process.    DESCRIPTION OF DRAWING(S) - The figure shows a front elevation sectional view of the organic waste composter.    Tank (1)    Waste overflow (6)    Pipe work (7)    Stirring mechanism (8)    Organic waste composter (101)
NOVELTY - The device has anaerobic reaction furnace that is provided as vertical furnace main portion. A section reaction chamber of the furnace main portion is provided with inlet extended in reaction chamber. A gathering room is provided with an air outlet connected to gas inlet.    USE - Device for generating combustible gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for generating combustible gas.
NOVELTY - A gas treatment system comprises a circuit for creating a pulsed electric field between electrodes (110) and for applying a reference voltage to shield portions. Dielectric sections and electrodes are arranged so that a greater portion of overall energy density of a corona discharge within the discharge chambers is due to the surface-streamers.    USE - A system for the treatment of a gas (claimed).    ADVANTAGE - The system reduces requirements and complexity for a circuit providing power to device.    DETAILED DESCRIPTION - A gas treatment system comprises a gas inlet (114) for receiving the gas prior to treatment; dielectric sections defining discharge chambers (102) coupled to the gas inlet; two electrodes disposed in the chambers; electrically conductive shield portions positioned between adjacent ones of the discharge chambers; a gas outlet coupled to the discharge chambers; and a circuit in communication with the shield portions and electrodes in the discharge chambers. The circuit is configured for creating a pulsed electric field between the electrodes and for applying a reference voltage to the shield portions. Dielectric sections and electrodes are arranged so that a greater portion of overall energy density of a corona discharge within the discharge chambers is due to the surface-streamers.    DESCRIPTION OF DRAWING(S) - The drawing is a top side view of surface-streamer based plasma reactor.    Discharge chambers (102)    Lateral side portion (108)    Electrodes (110)    Cathode electrode (112)    Inlet (114)
NOVELTY - A reducing energy-saving device system of an ocean vessel comprises micro processing sub-system, a waste gas collecting system and wastewater collecting and utilizing system. The micro processing system is composed of multiple tubular photobioreactors (4) arranged on top layer ship deck, where one end of each photobioreactor is connected with micro injection interface (1), and the other end is connected with micro discharge interface (5).    USE - A reducing energy-saving device system of ocean vessel for processing micro-algae.    ADVANTAGE - The system has energy saving effect.    DETAILED DESCRIPTION - A reducing energy-saving device system of an ocean vessel comprises micro processing sub-system, a waste gas collecting system and wastewater collecting and utilizing system. The micro processing system is composed of multiple tubular photobioreactors (4) arranged on top layer ship deck, where one end of each photobioreactor is connected with micro injection interface (1) which is further connected with the outlet of the other subsystems and a washing pipe, and the other end is connected with micro discharge interface (5). The waste gas collecting system comprises power device, two waste gas outlets, a cooling tower, a washing tower, a waste gas collecting tank, a pipeline fan, optical bioreactor, permeable membrane, and reverse-osmosis filtering film. The wastewater collecting and utilizing system comprises domestic sewage pipe, pre-treating device, wastewater storage chamber, wastewater delivery pump, and wastewater gravity cabinet.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating the reducing energy-saving device system.    Micro injection interface (1)    Photobioreactors (4)    Micro discharge interface (5)
NOVELTY - A fully enclosed sludge continuous aerobic composting system using solar energy comprises a premixing device connected with a fully enclosed horizontal continuous fermenting device by a delivering device. The fermenting device is arranged in a solar fermenting tent, and provided with an air outlet external fan and a gas purifying device. An intelligent control system is included for controlling various parts. The gas purifying device comprises a cyclone dust remover and a biodeodorizer which are sequentially connected.    USE - A fully enclosed sludge continuous aerobic composting system using solar energy.    ADVANTAGE - The system can remarkably reduce odor and dust pollution generated from sludge composting process, improve oxygen supply condition during fermenting, effectively accelerate speed of fermenting material and quality of fertilizer, and save energy. It can also realize intelligent control of work status. The produced half-finished product is sold as commercial fertilizer after being aged and processed, thus realizing sludge decrement, hazard-free treatment and recycle.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating the fully enclosed sludge continuous aerobic composting system using solar energy.
NOVELTY - The device has a feeding device (2) that is connected with the feeding port of dry distillation reactor (1). A discharging device (4) is connected with the output port of dry distillation reactor. A carbon material collecting device (15) is connected with the input end of gas output device (7) connected with the inner cavity of the dry distillation reactor. The output end of the gas output device is connected with a gas processing device (6) which supplies oxygen to combustion chamber (10).    USE - Biomass distilling device for household rubbish, medical rubbish, and sludge.    ADVANTAGE - The biomass can be transformed into electric energy by the biomass distilling device efficiently. The energy substance of the biomass distilling device can be circulated and recycled efficiently. The speed of the dry distillation reactor is improved, thus the combustible gas, oil and carbon can be generated by the biomass distilling device effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass distilling device. (Drawing includes non-English language text)    Dry distillation reactor (1)    Feeding device (2)    Discharging device (4)    Gas processing device (6)    Gas output device (7)    Combustion chamber (10)    Carbon material collecting device (15)
NOVELTY - The device has a valve that is connected with a feeding pump (1) via a conveying pipeline. A quick-opening filter (2) and the feed pipe (3) are connected to the feeding pump. A spiral nozzle (4) is provided in the feeding pipe. A spiral channel is provided in the feeding pump.    USE - Biodiesel flash tower feeding device.    ADVANTAGE - The vaporization time of the biodiesel flash tower feeding device can be reduced. The efficiency, operability, reliability and usability of the biodiesel flash tower feeding device can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the biodiesel flash tower feeding device.    Feeding pump (1)    Quick-opening filter (2)    Feed pipe (3)    Spiral nozzle (4)    Flash (5)
NOVELTY - Fermenting pool padding material comprising rape seed stalk, sawdust and effective microorganisms (EM) raw liquid prepared by crushing rape seed stalk into particle of 5 mmx 5 mm; adding sawdust (60%), EM stock solution (39.8-39.9) and water (0.2%), uniformly stirring and controlling the humidity to 48-50%, is claimed.    USE - Used as a fermenting pool padding material.    ADVANTAGE - The padding material: increases the pig disease resistance ability when applied to the pig shed excrement pool; saves labor and materials; does not discharge any pollutants in the shed; and can be converted into high-quality organic fertilizer after using.
NOVELTY - Manufacturing a padding formulation using corn straw (2) and saw dust (3) by fermentation of effective micro organism (EM)-liquid, comprises crushing the corn straw to have a dimension of 2-3 cm, immersing 60% of sawdust in EM stock solution (39.8-39.9%), adding 0.1-0.2% of the resulting solution in the corn straw and then uniformly stirring, and maintaining the humidity at 50-52%.    USE - The method is useful for manufacturing padding formulation (claimed).    ADVANTAGE - The method is capable of manufacturing padding formulation with improved quality, pig disease resistance, and reduced labor and energy pollutant in a simple manner. The padding formulation can be converted into high-quality organic fertilizer.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of manufacturing a padding formulation.    Corn straw (2)    Sawdust (3)    Water (5)    Fermentation tank (6)    Excrement pool. (7)    Sawdust (3)    Water (5)    Fermentation tank (6)    Excrement pool. (7)
NOVELTY - The apparatus has a methane fermentation tank (1) that generates the treated water containing biogas and organic substance. An aerobic treatment tank (2) generates the treated water containing nitrogen component. A solid-liquid separation mechanism (3) separates the treated water containing solid component and nitrogen component. A denitrification and desulfurization apparatus (4) performs the denitrification and desulfurization process and produces the biogas. A measuring device detects the amount of nitrogen components and the amount of phosphorus components.    USE - Water treatment apparatus for organic waste water.    ADVANTAGE - The operating cost of the water treatment apparatus can be reduced. The growth of the plant can be increased, since the hydrogen sulfide in the liquid fertilizer is oxidized.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the water treatment apparatus. (Drawing includes non-English language text)    Methane fermentation tank (1)    Aerobic treatment tank (2)    Solid-liquid separation mechanism (3)    Denitrification and desulfurization apparatus (4)    Pipe (101)
NOVELTY - A hydrogen-producing catalyst is obtained by supporting composition containing cerium oxide, alumina, platinum group metal, and alkaline-earth metal compound whose specific surface area is 50 m2/g or more to honey-comb support. The content of cerium oxide is 20-150 g/L per unit volume of catalyst (mass per 1 liter of catalyst).    USE - Catalyst is used for producing hydrogen (claimed) for polymer electrolyte fuel cell and solid oxide fuel cell.    ADVANTAGE - The catalyst has excellent catalytic activity for long period of time, heat resistance and durability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of hydrogen-producing catalyst; and    (2) production of hydrogen, which involves reforming hydrocarbon compound and sulfur-containing compound in presence of the catalyst.
NOVELTY - The device has a regulating pool connected to an integrated fermentation tank. The integrated fermentation tank is connected with a feeding tank through a pipe. An inlet is formed between a branch fermentation tank and the regulating pool. An upper end of the integrated fermentation tank and the branch fermentation tank are connected with a biogas pool through an outlet. A gas pipe is connected with the integrated fermentation tank and the branch fermentation tank.    USE - Biogas fermentation device.    ADVANTAGE - The device is simple in structure. The device improves quality of produced marsh gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a biogas fermentation device.
NOVELTY - Municipal initial rainwater pollutant spiral in-situ purifying device comprises overflowing distributing well, which is connected with normal water opening and respectively provided with rainwater detention chambers at its two sides. The overflowing distributing well is connected with the rainwater detention chamber. It is provided with an adjustable overflow weir and water retention chamber inside suspension biological filler balls. The overflowing distributing well inner wall has a spiral shape.    USE - Municipal initial rainwater pollutant spiral in-situ purifying device.    ADVANTAGE - The device reduces the input of primary rainwater pollutants to the river; and can remove more than 75% of the primary rainwater pollutants and biodegradable waste.    DETAILED DESCRIPTION - Municipal initial rainwater pollutant spiral in-situ purifying device comprises overflowing distributing well, which is connected with normal water opening and respectively provided with rainwater detention chambers at its two sides. The overflowing distributing well is connected with the rainwater detention chamber. It is provided with an adjustable overflow weir and water retention chamber inside suspension biological filler balls. The overflowing distributing well inner wall has a spiral shape. The rainwater detention chambers have six layers and labyrinth intestinal tract. It has upper part, which is designed into bending pipe around the overflowing distributing well.
NOVELTY - Magnesium soluble salt solution is neutralized using alkali, washed, mixed with salt solution of aluminum sol and rare-earth metal, dried, pulverized, calcined, pelletized, molded and roasted to obtain methane synthesis catalyst carrier.    USE - Preparation of methane synthesis catalyst carrier used for preparing gene delivery carrier.    ADVANTAGE - The method efficiently provides methane synthesis catalyst carrier having excellent hydrothermal stability.
NOVELTY - Integrated treatment of fermentation type pharmaceutical wastewater, involves after pre-processing the wastewater, orderly flowing through both separating internal circulation anaerobic reactor and compound A/0 for biological treatment, and then obtaining the processed water through outlet.    USE - Integrated treatment of fermentation type pharmaceutical wastewater.    ADVANTAGE - The integrated treatment method has removing rate of COD in wastewater up to 99%, removal rate of ammonia nitrogen of 90%, and at the same time can produce economic value of marsh gas product. The method has low treatment cost, high load reactor, is easy to control, and requires small occupied area.
NOVELTY - The system has an anaerobic reactor that is connected with a solid-liquid mixing device whose biogas outlet is connected with a low temperature condensing device while residue outlet is connected with a drying device. A concentrated solution outlet of the condensing device is connected with the drying device. A heat exchanging pipe is arranged in the anaerobic reactor. The water inlet end of heat exchanging pipe is connected with a water outlet pipe of the biogas generator while water outlet end is connected with low temperature condensing device.    USE - System for treating pig manure and breeding wastewater.    ADVANTAGE - The pig manure and breeding wastewater treatment system provides environment-friendly pig manure and featured with high efficiency and convenient operation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for treating pig manure and breeding wastewater.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the pig manure and breeding wastewater treatment system. (Drawing includes non-English language text)
NOVELTY - The method involves catering garbage with less than 8% of oil and conveying garbage to a garbage separating device for crushing and segmentation. The garbage is crushed to obtain slurry. The obtained slurry is pre-processed and sent to an anaerobic digestion device. 8-12% of solid content in mixed material is stirred and mixed in the anaerobic digestion device for anaerobic digestion.    USE - Anaerobic processing method for food residue and sludge.    ADVANTAGE - The anaerobic processing method can process food waste without classification, requires simple technical equipment and resource, reduces heat consumption and power consumption and satisfies the city food garbage source classification. The food waste is separated without using oil-water separation, and the biodegradable waste is directly mixed to produce marsh gas and sludge.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for anaerobic processing system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the anaerobic processing system.
NOVELTY - A municipal sludge biological fermentation process involves dehydrating sludge water and stacking the water. Attapulgite and fly ash are mixed with stacked material and transferred to aerobic fermentation tank. Microbial inoculum is added to the aerobic fermentation tank and fermented by supplying oxygen and activating beneficial bacterium. Biological deodorization process is carried out in the fermented mixture, and the fermented mixture is dried in a roller drier, palletized, granulated and dried. The dried granular sludge is sieved and packed to obtain finished product.    USE - Municipal sludge biological-fermentation process.    ADVANTAGE - The method enables processing municipal sludge in a simple, cost-effective and eco-friendly manner.    DETAILED DESCRIPTION - A municipal sludge biological fermentation process involves dehydrating sludge water (60-70%) using a sludge dewatering device stacking the water. Attapulgite (10-20 wt.%) and fly ash (15-20 wt.%) are mixed with the stacked mixture, and transferred into aerobic fermentation tank. The microbial inoculum (0.2-0.5 wt.%) is added to the aerobic fermentation tank at 40-70 degrees C and fermented for 5-7 days, by supplying oxygen and activating beneficial bacterium. Biological deodorization process is carried out on the fermented mixture and the mixture is dried in a roller drier, palletized and granulated. The particle size of granule is controlled to 1-5 mm, and dried in the roller drier at 120-150 degrees C until the water content is less than or equal to 10%. The dried granular sludge is sieved, and packed to obtain finished product.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating a method for municipal sludge biological-fermentation.'(Drawing includes non-English language text)'
NOVELTY - Flora construction method, involves collecting reservoir oil production well liquid sample or pollution caused by original active sludge sample, adding anaerobic hydrocarbon culture medium in the liquid sample or active sludge sample, and adding sample in the culture medium.    USE - Flora construction method.    ADVANTAGE - The method is environmentally-friendly and simple.
NOVELTY - Organic fertilizer is obtained by using (in parts weight): Amorpha fruticosa (10-30), Polygonum (3-10), maifan stone (5-15), coal (5-15), farmyard manure (35-60) and ammonium bicarbonate (1-5), cutting A.fruticosa flower, washing Polygonum, drying, extracting, collecting juice and residue and processing residue to obtain extract liquid, uniformly mixing ammonium carbonate, coal and maifan stone, adding farmyard manure, A.fruticosa flowers and residue, composting, spraying extract liquid and covering with plastic film.    USE - The organic fertilizer is useful for supplying nutrient elements to vegetable yielding plants (claimed).    ADVANTAGE - The organic fertilizer enables effective utilization of wastes and is safe, as it is low-carbon fertilizer.    DETAILED DESCRIPTION - Organic fertilizer is obtained by (a) using raw materials (in parts weight) chosen from Amorpha fruticosa (10-30), Polygonum (3-10), maifan stone (5-15), coal (5-15), farmyard manure (35-60) and ammonium bicarbonate (1-5), (b) cutting dried red flower of A.fruticosa in withered state, washing Polygonum with water for 2-3 times, drying, extracting, collecting juice and residue, boiling the residue for 20-25 minutes in water, where weight ratio of the residue and water is 1:2-3, separating and collecting juice and residue after boiling, boiling the juice to obtain Polygonum extract liquid, (c) uniformly mixing ammonium carbonate, coal and maifan stone for at least 40 minutes, (d) adding the farmyard manure, dried cut flowers of A.fruticosa, residue obtained in step (b) to obtain mixture, subjecting mixture to composting up to height of 10-15 cm, spraying Polygonum extract liquid on surface of the compost and covering the compost with plastic film.
NOVELTY - Organic soybean fertilizer comprises (in parts weight): hemlock (2-10), humus (10-20), soybean straw (10-30), and farmyard manure (25-60). The fertilizer is prepared by cutting soybean straw and hemlock and exposing to sun, mixing with humus and farmyard manure, stirring uniformly, composting the mixture, covering using plastic film and sealing the product.    USE - Organic soybean fertilizer.    ADVANTAGE - The organic fertilizer is prepared by a method that converts waste material into valuable products, and rich in nutrition required for soybeans.
NOVELTY - Additive comprises waste oil which is a generated by-product obtained from process of refining biodiesel stock oil, and wastewater which is a mixture of effluent. The waste oil is obtained from biomass.    USE - The additive is useful for producing emulsified fuel (claimed).    ADVANTAGE - The emulsified fuel has improved combustion efficiency, and excellent stability and phase stability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for emulsified fuel, which comprises above-mentioned additive and heavy oil.
NOVELTY - A biological organic fertilizer production device comprises a first fermentation tank (1), a second fermentation tank (2), a dryer (3), a crusher (4), and a flat granulator (5). The first fermentation tank is provided with a livestock manure inlet (6), a fiber decomposition bacteria inlet, a hemicellulose decomposition bacteria inlet, a protein decomposition bacteria inlet, and an organic phosphorus decomposing bacteria inlet. The second fermentation tank is provided with an ammonification bacteria inlet, a light and bacteria inlet, a yeast inlet, and an actinomycete inlet.    USE - Biological organic fertilizer production device.    ADVANTAGE - The device has simple structure, low equipment investment, and convenient operation.    DETAILED DESCRIPTION - A biological organic fertilizer production device comprises a first fermentation tank (1), a second fermentation tank (2), a dryer (3), a crusher (4), and a flat granulator (5). The first fermentation tank is provided with a livestock manure inlet (6), a fiber decomposition bacteria inlet, a hemicellulose decomposition bacteria inlet, a protein decomposition bacteria inlet, and an organic phosphorus decomposing bacteria inlet. The first fermentation tank is connected to the second fermentation tank via a conveyor. The second fermentation tank is provided with an ammonification bacteria inlet, a light and bacteria inlet, a yeast inlet, and an actinomycete inlet. The second fermentation tank is set between the dryer and the conveyer. The dryer is provided with a steam inlet (17), and is connected to the crusher via a conveyor. The crusher is connected to the flat granulator via a conveyor, and is provided with a product outlet (20).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the biological organic fertilizer production device.    Fermentation tanks (1, 2)    Dryer (3)    Crusher (4)    Flat granulator (5)    Livestock manure inlet (6)    Steam inlet (17)    Product outlet (20)
NOVELTY - An organic fertilizer comprises (wt.%) animal excrement (40-60), biomass carbon (10-35), biomass extract (5-15), and rice bran cake (10-20). The animal excrement is excrement of chicken, duck, goose, pig, horse, sheep and/or cattle.    USE - Organic fertilizer.    ADVANTAGE - The organic fertilizer saves water, reduces emission, adjusts soil acidity, improves microbiological environment of soil, and realizes resource utilization of low-carbon waste.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of organic fertilizer by adding zymophyte agent (1.5-2.5 kg/ton raw materials) to raw materials, uniformly mixing, stacking, and fermenting for 20-25 days, while regularly turning over and supplying oxygen at 55-65% relative humidity and 55-60 degrees C.
NOVELTY - An ecological fertilizer comprises organic material (3-20%) and sulfur-based compound fertilizer. The ecological fertilizer is prepared by fermenting livestock manure, drying and crushing into powder; and adding compound fertilizer.    USE - Ecological fertilizer used for field crops, fruit trees, and urban greening trees and flowers.    ADVANTAGE - The ecological fertilizer has high nutrient content, does not harden, and reduces environmental pollution by converting urban and rural wastes into useful product.
NOVELTY - Slow-release organic microbial fertilizer particles comprise spherical urea particles covered with, from inside to outside, organic layer, carrier layer and coated shell.    USE - Slow-release organic microbial fertilizer particles.    ADVANTAGE - The fertilizer particles have improved utilization rate.
NOVELTY - An herbicide composition comprises fluroxypyr or its ester and flumetsulam.    USE - Herbicide composition in form of wettable powder or water dispersible agent (claimed) used for controlling broadleaf weeds in corn and wheat fields.    ADVANTAGE - The composition has simple preparation, is safe and environmental-friendly, delays herbicide resistance, reduces dosage of active ingredients, and can completely and rapidly remove the weeds without polluting the environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation method of the herbicide composition, comprising uniformly mixing fluroxypyr or its ester, flumetsulam and additive in a double helix conical mixer, performing supermicro crushing with air current to obtain powder composition; or pelletizing the super micropowder in a granulator, and drying to obtain granular composition.
NOVELTY - Treating and processing domestic sewage and waste comprises providing slag water-collecting front end, grey water treatment unit, and decompressed black collecting front end, and decompressed black collecting pipe system, decompressed black collecting terminal, black transfer units and organic fertilizer factory. The method includes introducing grey water into slag water treatment unit. The discharging or recycling steps are processed according to water quality at collecting front, excrement, kitchen garbage pollution and little washing water collecting section.    USE - Method for treating and processing domestic sewage and waste (claimed) for organic fertilizer.    ADVANTAGE - The waste materials are converted into useful products.    DETAILED DESCRIPTION - Treating and processing domestic sewage and waste comprises providing slag water-collecting front end, grey water treatment unit, and decompressed black collecting front end, and decompressed black collecting pipe system, decompressed black collecting terminal, black transfer units and organic fertilizer factory. The method includes introducing grey water into slag water treatment unit. The discharging or recycling steps are processed according to water quality at collecting front, excrement, kitchen garbage pollution and little washing water collecting section. The decompressed black collecting pipe system is connected to black collecting terminal and further connected into organic fertilizer factory by black transfer unit.
NOVELTY - Synthesis of betulic acid comprises inoculating Cunninghamella blakesleeana (AS 3.910) to sterilized culture solution to obtain pre-culture system; adding betulin solution with surface active agent to obtain betulin with concentration of 0.01-0.1 g/l; converting at 25-30 degrees C for 2-6 days to obtain conversion liquid; and separating and purifying to obtain betulinic acid.    USE - Synthesis of betulic acid.    ADVANTAGE - The method has simple technique, mild reaction condition, short production period, high yield, environment-friendly performance, and provides high rate of betulic acid.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a process for synthesizing betulic acid (Drawing includes non-English language text).
NOVELTY - Production of organic fertilizer involves drying crop straw, introducing dried crop straw and livestock excrement (0.5-5 times of crop straw weight) with bacteria (preferably effective microorganism bacterial solution having viable count of 1x 1010/ml, 0.01-0.2 vol.%, based on straw volume) into a biogas digester, adding water, anaerobically fermenting (preferably for 10-15 days), pumping supernatant to material storage pool, and continuously adding crop straw and livestock excrement to the remaining material in the digester after fermentation period. The straw is cut into 5-10 cm sections.    USE - Method for producing organic fertilizer (claimed).    ADVANTAGE - The organic fertilizer improves soil fertility; reduces fertilizer dosage; and not only saves cost and protects the environment, but also increases production yield.
NOVELTY - The method involves baking an electrode constituent material which is arranged on a metal support body (10) and electrolyte laminated constitution material (31) arranged on the electrode constituent material. The temperature of the electrolyte laminated constitution material, the temperature of the electrode constituent material, and the temperature of the metal support body is set low by adjusting the baking temperature of electrode constituent material.    USE - Manufacturing method for fuel cell.    ADVANTAGE - Suppresses oxidation of metal support body and electrode to permit precise suppression of the film thickening of the electrolyte layer since the temperature of the electrolyte laminated constitution material, the temperature of the electrode constituent material, and the temperature of the metal support body is set low by adjusting the baking temperature of electrode constituent material. Exhibits excellent in environmental viewpoint and while exhibiting high energy efficiency by baking an electrode constituent material which is arranged on a metal support body and electrolyte laminated constitution material arranged on the electrode constituent material.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the manufacturing method for the fuel cell. (Drawing includes non-English Language text).    Metal support body (10)    Anode (20)    Anode constituent material (21)    Electrolyte layer (30)    Electrolyte laminated constitution material (31)
NOVELTY - The cluster typed oil production complex has a biomass supplying unit (BB) to supply biomass. The methane-fermentation (CC) ferments the biomass supplied . The gas-liquefaction apparatus (EE) produces gas-liquefaction oil from methane gas.An oil refinery (HH) has an acceptance installation to receive gas-liquefaction oil from the movement transport unit loading the gas-liquefaction oil produced with the gas-liquefaction apparatus of the cluster. A refiner refines the gas-liquefaction oil received by the acceptance installation, and manufactures a product.    USE - Cluster typed oil production complex to produce gas-liquefaction oil.    ADVANTAGE - The gas-liquefaction apparatus is very cheap. The liquefied gas-liquefaction oil can be conveyed to a petroleum refinery by suitable cost of transport using normal movement transport unit, such as a tank lorry and a tanker, and can produce various primary petroleum products and a secondary petroleum product. The gas-liquefaction oil which can refund capital-investment expense sufficiently is produced and profits are gained.The digestive liquid which contains the phosphorus made by methane fermentation of biomass, nitrogen, etc. can be used as a fertilizer for greening of a desert etc.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the cluster typed oil production complex. (Drawing includes non-english language text)    Cluster A (AA)    Biomass supplying unit (BB)    Methane-fermentation (CC)    Gas-liquefaction apparatus (EE)    Oil refinery (HH)
NOVELTY - The system has outlet tube (3) to guide methane gas generated by methane fermentation tank to methane gas separation portion (10) with processed material. The processed material insertion opening (9) is provided in methane gas separation portion of upper portion of return pipe (4). The air supplying apparatus (21) connects methane gas separation portion with methane gas piping (25b) to supply methane gas. The blowing-in pipe (24) is provided in tank to blow-in methane gas in tank. The methane gas extraction portion (23) is provided in methane gas piping.    USE - System for purifying methane fermentation for use during sewage work in office. Can also be used in small-scale sake production place ad restaurant.    ADVANTAGE - The process liquid can be circulated smoothly and ferment of the methane can be performed efficiently. The cost of the methane fermentation purifying system can be reduced since the structure of the system can be simplified. The methane gas with high concentration can be achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the methane fermentation purifying system.    Outlet pipe (3)    Return pipe (4)    Processed material insertion opening (9)    Methane gas separation portion (10)    Air supplying apparatus (21)    Methane gas extraction portion (23)    Blowing-in pipe (24)    Methane gas piping (25b)
NOVELTY - The manufacturing method comprises providing a support for a fuel cell, and forming an interconnecting member layer including metal-glass and interconnecting unit cells on the support. The glass is barium oxide (25-30 wt.%)-silicon oxide (15-25 wt.%) based glass. The metal-glass has 25-75 wt.% of metal and 75-25 wt.% of glass. The interconnecting member layer: is formed of slurry, a sheet, a powder, a mesh and/or foam; is composed of layers; and is coated by a wet coating method that is screen printing method and/or dip coating method.    USE - The method is useful for manufacturing a fuel cell such as a solid oxide fuel cell, a cylindrical fuel cell, a flat tubular fuel cell, a flat fuel cell (all claimed), a polymer electrolyte membrane fuel cell, a direct methanol fuel cell, a molten carbonate fuel cell, a phosphoric-acid fuel cell and an alkali fuel cell.    ADVANTAGE - The method is capable of simply, efficiently, economically and reliably manufacturing the large capacity fuel cell in an environmentally friendly manner with high durability and stability, improved chemical resistance and mechanical strength, excellent electrical conductivity and increased output and low-resistance characteristics.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a fuel cell.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic cross-sectional view of a unit cell of a fuel cell.    First electrode (10)    Second electrode (20)    Interconnecting members (31, 32)    Electrolyte layer. (50)
NOVELTY - The method involves connecting side edges (3, 4) of a contour (2) of an electrode (1) with each other by a connection section (5). The side edges are produced by respective sections. The connection section is provided with a linear region (5a) and a bent region (5b) between the side edges, and produced with the sections. The bent region is provided with a circular gradient and an opening angle (7) of approximately 45 degrees. The bent region is tangentially passed into one of the side edges (4). The other side edge is cut by the linear region in an angle of approximately 45 degrees.    USE - Method for manufacturing an electrode for an electrochemical cell (claimed) i.e. fuel cell, of an electrochemical energy storage device for storing energy in a motorvehicle and a power plant. Can also be used for a primary battery and a secondary battery.    ADVANTAGE - The connection section is provided with the linear region and the bent region between the side edges, thus avoiding cutting of edges or edge sections of the electrode in an acute angle, and avoiding formation of sharp edged corners at the electrode. The method reduces mechanical and thermal stresses of the electrode in a region of the connection section and risk of damage of an adjacent enclosure in a region of the connection section, thus increasing life span of the electrochemical cell with the electrode.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an electrode comprising a contour with side edges.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a part of a contour of an electrode in a region of a connection section between side edges of an electrode.    Electrode (1)    Contour (2)    Side edges (3, 4)    Connection section (5)    Linear region (5a)    Bent region (5b)    Opening angle (7)
NOVELTY - The method involves forming a pore in a metal foam supporter. Complementary goods i.e. paraffin phosphorus material, are in-flowed in the pore of the metal foam supporter. A junction layer is formed in the metal foam supporter. An end cell of a fuel anode is laminated with the junction layer. The junction layer is sintered between the metal foam supporter and the fuel anode.    USE - Method for manufacturing a solid oxide fuel cell.    ADVANTAGE - The method enables improving mechanical strength and porosity property, preventing the solid oxide fuel cell from damage and reducing weight of the solid oxide fuel cell.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a solid oxide fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a solid oxide fuel cell.
NOVELTY - The burner (1) has burner front portion (2) whose opening (3) is connected to central passage way (5) and single central opening (4) is connected to annular passage way (6). A hollow portion (9) is arranged inside downstream portion of central passage way. The hollow portion is fluidly connected with annular passage way for passing oxygen containing gas through connecting conduits (14). An opening (11) of hollow portion is connected with single central opening. The discharge opening (17) of connecting conduits is positioned in the diverging portion of hollow portion.    USE - Burner used for gasification of solid fuel e.g. coal, petroleum coke or biomass (all claimed).    ADVANTAGE - The erosion of the burner can be prevented. The complexity design of the burner can be reduced. The heat flux to the burner front can be greatly decreased. The service life of the burner can be prolonged.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for manufacturing mixture of hydrogen and carbon monoxide.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the burner.    Burner (1)    Burner front portion (2)    Opening (3)    Single central opening (4)    Central passage way (5)    Annular passage way (6)    Hollow portion (9)    Opening of hollow portion (11)    Connecting conduits (14)    Discharge opening of connecting conduits (17)
NOVELTY - A hydrogen producing catalyst comprises catalyst composition containing alumina, cerium-nickel even density mixed oxide, platinum group metal and basic compound which is carried to a honeycomb carrier in which basic compound is element chosen from magnesium, calcium, strontium, barium, yttrium, lanthanum, praseodymium and neodymium.    USE - Hydrogen-producing catalyst for hydrogen production (claimed), and fuel cells e.g. polymer electrolyte fuel cell or solid oxide fuel cell.    ADVANTAGE - The catalyst has long-term durability and can reforming-react at low temperature even when fuel cell system contains sulfur compound, and poisoning deterioration with sulfur containing compound can be suppressed.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) manufacture of hydrogen-producing catalyst involving carrying the catalyst composition formed by containing alumina, cerium-nickel even density mixed oxide, platinum group metal and basic provision compound to honeycomb carrier, and coating the slurry obtained by mixing and wet-grinding alumina and cerium-nickel series even density mixed oxide to honeycomb carrier; and    (2) hydrogen production involving using hydrocarbon compound in which fuel contains sulfur containing compound and reforming reaction of fuel using the hydrogen-producing catalyst.
NOVELTY - The system has control apparatus (70) that operates aluminum addition apparatus (50) and hydro-generated apparatus (60) based on temperature and water quantity data which are detected by temperature detection unit (20) and water quantity unit (22) in reaction container (10). The hydrogen is generated by reacting aluminum, water or organic solvent mixing water within the reaction container. The reaction heat of aluminum and water at the time of hydrogen production in reaction container is utilized as a heat source by exchanging warm air by heat exchange medium (34).    USE - Thermal system for motor vehicle and electric vehicle.    ADVANTAGE - The reaction heat of aluminum and water at the time of hydrogen production can be utilized as a heat source of electric vehicle. The energy efficiency of the thermal system can be raised at low cost, to reduce environmental impact.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the thermal system. (Drawing includes non-English text language)    Reaction container (10)    Temperature detection unit (20)    Water quantity unit (22)    Heat exchange medium (34)    Aluminum addition apparatus (50)    Hydro-generated apparatus (60)    Control apparatus (70)
NOVELTY - A bio-oil is pre-processed by molecular distillation separation at 200 degrees C and pressure of 10-1800 Pa, to obtain biological oil light fraction, medium fraction and heavy fraction. The light fraction and alcohol in volume ratio of 1:10-1:1 are reacted at 80-120 degrees C under at normal pressure for 0.5-1.5 hours and subjected to catalytic esterification reaction in presence of solid acid catalyst to obtain ester.    USE - Biological grading of light fraction fuel.    ADVANTAGE - The method enables efficient biological grading of light fraction fuel. The corrosion of manufacturing equipment is suppressed.
NOVELTY - Biomass carbon has a density of 1.1-1.4 g/cc, fixed carbon content of 75-90%, volatile matter content of 5-15%, and calorific value of 25-32 MJ/kg.    USE - Biomass carbon is used as substitute of partial fossil fuel in iron ore sintering (claimed).    ADVANTAGE - Biomass carbon reduces the emission of carbon oxides, sulfur oxides, and nitrogen oxides during sintering.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparation of biomass carbon, which involves adding middle-temperature asphalt (1-5 wt.%) to biomass, uniformly mixing, heating biomass by two-stage carbonization at 400-450 degrees C for low-temperature carbonization, and heating biomass at 500-700 degrees C for high-temperature carbonization; and    (2) use of biomass carbon as substitute of partial fossil fuel in iron ore sintering.
NOVELTY - An emulsified diesel oil producing method involves adding biomass additive (5-10%) into diesel oil (70-85%), stirring at normal temperature and 800-1200 rpm, adding water (15-20%), stirring at 800-1200 rpm for 10-20 minutes and mixing solution to intensive clear to obtain emulsified diesel oil.    USE - Method for producing emulsified diesel oil for use in renewable energy source field.    ADVANTAGE - The method enables producing emulsified diesel oil with high stability, less sulfur content and better combustion property. The emulsified diesel oil is eco-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing biomass additive.
NOVELTY - The chamber has a focusing part arranged at an inner side of a primary gasification zone. A flattening part is provided with a hole flat turning arm. A coke is provided with two groups of stirring rods. A cylinder head of a hydraulic pressure pushing device is connected with a speed reducing motor that is connected with an output end of a decelerating motor. Three plasma torches are arranged on a gas purifying area and formed with an angle of 120 degree or 45 degree with ground. An automatic feeding device is arranged on a top part of the primary gasification zone.    USE - Side suction-type plasma rubbish gasification reaction chamber.    ADVANTAGE - The chamber utilizes rubbish heat gas and the plasma torches to remove waste residue, improve gas purification rate and gas yield and reduce investment cost and operation cost, and has better gas purification effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a gasification reaction chamber rubbish purifying method.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a side suction-type plasma rubbish gasification reaction chamber.
NOVELTY - Producing ethanol involves (a) adding microbial liquid and mixed enzyme to active sludge, (b) adding the active sludge including microbial liquid with mixed enzyme to fermentation tank and carrying out fermentation at 25-32 degrees C for 48-80 hours to obtain fermented liquid, and (c) adding the fermented liquid to distillation tank, and collecting the distilled liquid.    USE - The method is useful for producing ethanol which is used as fuel (claimed).    ADVANTAGE - The method is environmentally-friendly, as it uses waste materials as raw materials.    DETAILED DESCRIPTION - Method for producing ethanol involves (a) adding microbial liquid (2-5%) and mixed enzyme (0.1-0.6%) to active sludge, where microbial liquid comprises Bacillus licheniformis, B.megaterium, B.subtilis, Lactobacillus plantarum, L.delbrueckii ssp. bulgaricus, Saccharomyces cerevisiae and Pichia fermentans, and the mixed enzyme comprises amylase, cellulase, lipase, protease, pectinase and glucoamylase, (b) adding the active sludge including microbial liquid with mixed enzyme to fermentation tank and carrying out fermentation at 25-32 degrees C for 48-80 hours to obtain fermented liquid, and (c) adding the fermented liquid to distillation tank, and collecting the distilled liquid.
NOVELTY - A dry organic fertilizer is prepared by adjusting water content of papermaking mixed sludge; mixing the sludge in fermenting chamber high temperature anaerobic fermentation, where reaction gas generated through a special system device for recycling and purifying; providing anaerobic fermentation reaction material, out of ferment storehouse, and drying; crushing and sieving to obtain fermenting material powder; and preparing the powder material for preparing organic fertilizer by mixing, and pelletizing.    USE - Method for the preparation of dry organic fertilizer (claimed).    ADVANTAGE - The method improves the dry high temperature anaerobic fermentation technique and economic benefit cycle, saves energy, and protects environment.
NOVELTY - Fertilizer manufacturing involves mixing and fermenting organic waste and earthworm excrement soil.    USE - Method for manufacturing fertilizer (claimed).    ADVANTAGE - The fertilizer manufacturing method enables to produce improved production of the fertilizer.
NOVELTY - The system has a heating type biomass gasification furnace (1) that is installed in a chamber. An infrared stove head is connected with a biomass fuel stove. A water heater is placed on the wall. A tap water inlet pipe (12), oil-water tank and warm water heater (15) are respectively equipped with heating hot water control valve (16) and are arranged in the pipes, heater (17), radiating heating sheet (18).    USE - Biochemical energy-integrated device system.    ADVANTAGE - An improved non-energy biochemical energy-integrated device system is obtained. The combustion effect is good. The device is safe and reliable, energy-saving and environment-friendly. The device has no toxicity and harm.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of biochemical energy-integrated device system.    Heating type biomass gasification furnace (1)    Tap water inlet pipe (12)    Warm water heater (15)    Hot water control valve (16)    Heater (17)    Radiating heating sheet (18)
NOVELTY - A recombinant microorganism capable of producing butanol, and which is constructed by transferring a foreign gene that encodes an enzyme having both alcohol/aldehyde dehydrogenase and butanol dehydrogenase activity into a host organism that produces butyric acid as a metabolic product, is new.    USE - For producing butanol from glucose; for producing butanol from a monosaccharide, oligosaccharide, or polysaccharide (claimed); and for producing biofuels.    ADVANTAGE - The recombinant microorganism is capable of producing butanol at a titer greater than 10 g/l and a yield greater than 0.3 g/g substrate. The microorganism exhibits improved properties (e.g. the ability to produce new or greater quantities of an intracellular metabolite, improve the flux of a metabolite down a desired pathway, and reduce the production of undesirable by-products).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) producing butanol involving culturing the recombinant microorganism in a culture medium containing glucose, and collecting butanol from its culture;    (2) new vector containing the DNA sequence of pMAD72, or pMAD22;    (3) a microbial host transformed by the vector;    (4) metabolically engineering (M1) a microorganism capable of producing butanol from a substrate involving obtaining a microbial host capable of naturally producing butyric acid, and transferring a foreign gene that encodes an enzyme having both alcohol/aldehyde dehydrogenase and butanol hydrogenase activity into the microbial host.
NOVELTY - (R)-3-Benzyloxyamino-4-(2,4,5-trifluoro-phenyl)-butyric acid compound (IV) or its amine salt is new.    USE - (IV) is useful as key intermediate for the synthesis of sitagliptin (claimed), which is useful for improving glycemic control in patients with type-2 diabetes mellitus. No biological data given.    ADVANTAGE - (IV) is capable of easily synthesizing sitagliptin with improved yield, purity, solubility, and stability in a reproducible, robust, economical and environmentally friendly manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparing tert-butylamine salt of (IV), comprising (a) reacting (IV) with an azodicarboxylate, and a phosphine to form (4R)-1-(benzyloxy)-4-(2,4,5-trifluorobenzyl)azetidine-2-one compound (V), (b) reacting (V) with a base or an acid to form a reaction mass, (c) adding the tert-butyl amine to the reaction mass of (b), and (d) isolating (IV) as tert-butylamine salt;    (2) preparing amine salt of (IV), comprising (a1) reacting (IV) with azodicarboxylate, phosphine and a solvent to form (V), (b1) reacting (V) with base or acid to form reaction mass, (c1) adding the amine to the reaction mass of step (b1), and (d1) isolating (IV) as a salt; and    (3) preparing sitagliptin or its salt, comprising reacting amine salt of (IV) with 3-trifluoromethyl-5,6,7,8-tetrahydro-1H-(1,2,4)triazolo(4,3-a)pyrazine compound (III) or its salt to form a (R)-3-benzyloxy amino-1-(3-trifluoromethyl-1,5,6,8-tetrahydro-(1,2,4)triazolo(4,3-a)pyrazin-7-yl)-4-(2,4,5-trifluoro-phenyl)-butan-1-one compound (II), and debenzylating (II).
NOVELTY - A cellulose biomass is subjected to saccharification decomposition process by making the slurry of cellulose biomass to a supercritical state or a subcritical state. The saccharified liquid is alcoholically fermented, distilled, and concentrated, to obtain ethanol. The flash vaporization of the slurry after saccharification decomposition is carried out within a flash tank (3) such that decomposition temperature reaches 150-200 degrees C, and the residence time of the slurry after the saccharification decomposition in flash tank (3) is made into 3 minutes or less.    USE - Production of ethanol used as fuel for motor vehicles.    ADVANTAGE - The method efficiently and economically provides ethanol by preventing excessive decomposition and caramelization of saccharides.    DETAILED DESCRIPTION - A cellulose biomass is subjected to saccharification decomposition process by making the slurry of cellulose biomass to a supercritical state or a subcritical state. The saccharified liquid is alcoholically fermented, distilled, and concentrated, to obtain ethanol. The flash vaporization of the slurry after saccharification decomposition is carried out within a flash tank (3) such that decomposition temperature reaches 150-200 degrees C, and the residence time of the slurry after the saccharification decomposition in flash tank (3) is made into 3 minutes or less. The flash vaporization of the slurry after the saccharification decomposition taken out from flash tank (3) is carried out within flash tank (11) such that the decomposition reaches 100-120 degrees C. The flash vapor generated from the flash tank (3) is utilized as heat source of the saccharification decomposition process or the distillation process.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic structure explaining the production of ethanol. (Drawing includes non-English language text)    Hot water reactor (1)    Path (2)    Flash tanks (3,11)    Saccharified liquid (4)    Steam line (5)
NOVELTY - The method involves operating hydraulic cylinder-type pressurizing reactor (1a) and hydraulic cylinder-type steam compressor (5a). The surplus hydraulic pressure is recovered as compression power for hydraulic cylinder-type steam compressor, when breakdown of cellulosic biomass is completed. Flash steam produced from slurry containing broken down substances is supplied to hydraulic cylinder-type steam compressor.    USE - Method for breaking down cellulosic biomass for manufacturing ethanol used as motor fuel.    ADVANTAGE - The compression power is reduced by recovering surplus pressure when reducing reactor pressure. The thermal efficiency is improved by recovering latent heat through cyclic use of flash steam.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus for breaking down cellulosic biomass has hydraulic cylinder-type steam compressor that performs superheated steam supply to hydraulic cylinder-type pressurizing reactor. The oil pressure return path of reactor and oil pressure chamber (2a) of compressor are connected for recovering oil pressure of oil pressure chamber of reactor. The oil pressure path is provided with alternative pathway having air chamber. The pressure accumulation setting values of air chamber is varied sequentially. A steam generation apparatus is connected to flash tank. Air/nitrogen supply apparatus is connected to flash tank using steam line.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydraulic cylinder-type steam compressor and hydraulic cylinder-type pressurizing reactor. (Drawing includes non-English language text)    Hydraulic cylinder-type pressurizing reactor (1a)    Oil pressure chamber (2a)    Hydraulic cylinder (3a)    Reaction chamber (4a)    Hydraulic cylinder-type steam compressor (5a)
NOVELTY - Purifying an aqueous solution derived from lignocellulosic biomass containing at least (a) dissolved sugars and/or their sugar oligomers, (b) lignin derived fragments, and (c) optional suspended solids, comprises mixing at least one precipitating agent into the aqueous solution to form a precipitate, and separating at least some of the precipitate from the aqueous solution.    USE - The process is useful for purifying an aqueous solution derived from lignocellulosic biomass.    ADVANTAGE - The simple and cost effective process removes poisoning components from the streams without significant influence on the loss of material.
NOVELTY - A catalyst substance or carbon particle, and primary electrolyte are dispersed in solvent to obtain catalyst ink. The obtained catalyst ink is dried, to obtain catalyst substance. The catalyst substance embedded with primary polymer electrolyte, carbon particles and secondary polymer electrolyte are dispersed in secondary solvent, to obtain secondary catalyst ink. The obtained secondary catalyst ink is coated on base material chosen from gas diffusion layer, transfer sheet and polymer electrolyte membrane, to form electrode catalyst layer.    USE - Manufacture of fuel cell electrode catalyst layer used for membrane electrode assembly for polymer electrolyte fuel cell (all claimed) used as power supply for household appliances.    ADVANTAGE - The method provides fuel cell electrode catalyst layer having excellent proton conductivity. The polymer electrolyte fuel cell using fuel cell electrode catalyst layer has excellent output characteristics.    DETAILED DESCRIPTION - A catalyst substance or carbon particle, and primary electrolyte are dispersed in solvent to obtain catalyst ink. The obtained catalyst ink is dried, to obtain catalyst substance. The catalyst substance embedded with primary polymer electrolyte, carbon particles and secondary polymer electrolyte are dispersed in secondary solvent, to obtain secondary catalyst ink. The obtained secondary catalyst ink is coated on base material chosen from gas diffusion layer, transfer sheet and polymer electrolyte membrane, to form electrode catalyst layer. The ratio of the dielectric constant of the primary solvent and secondary solvent is 1.2-25:1, at 20 degrees C. INDEPENDENT CLAIMS are included for the following:    (1) membrane electrode assembly; and    (2) polymer electrolyte fuel cell.
NOVELTY - Liquefying a hydrocarbon rich fraction (1, 1') comprising methane, hydrogen and nitrogen, comprises carrying out permeative separation of the hydrogen, before liquefying the hydrocarbon-rich fraction.    USE - The method is useful for liquefying a hydrocarbon-rich fraction comprising methane, hydrogen and nitrogen.    ADVANTAGE - The method: comprises separating hydrogen before liquefaction and thus it requires less energy and is cost effective; and optimizes standard liquefaction process that is relevant to liquefaction system.    DESCRIPTION OF DRAWING(S) - The drawings 1 and 2 show schematic process flows for liquefying the hydrocarbon-rich fraction.    Hydrocarbon-rich fraction (1, 1')    Hydrogen-rich fraction (2)    Fuel recycle gas fraction (6)    Nitrogen-rich fraction (7)    Mixture of condensed hydrogen, condensed fuel recycle gas fraction and/or the condensed nitrogen-rich fraction (8)
NOVELTY - The method involves performing compression (A) of a feed fraction (1) and subjecting to nitrogen separation (B). A nitrogen-containing fraction (5) is split by nitrogen separation and subjected to a cryogenic adsorptive cleaning process (E). The cryogenic adsorptive cleaning process is adapted in such a manner that the nitrogen-containing fraction is cooled and adsorptive product is purified at a temperature of less than 80 K. The purification of the nitrogen-containing fraction is realized by a pressure swing adsorption, vacuum pressure swing adsorption and/or thermal swing adsorption.    USE - Method for extracting of liquid helium from feed fraction containing helium, nitrogen and methane and/or oxygen in a liquid helium trailer.    ADVANTAGE - The nitrogen-containing fraction is split by nitrogen separation and subjected to the cryogenic adsorptive cleaning process, thus easily extracting the liquid helium from the feed fraction containing helium, nitrogen and methane and/or oxygen with hazardous components, without any danger of explosion, and extracting highly pure liquid nitrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic flow diagram illustrating the steps involved in a method for extracting liquid helium from feed fraction containing helium, nitrogen and methane and/or oxygen.    Process of compression of feed fraction (A)    Nitrogen separation process (B)    Cryogenic adsorptive cleaning process (E)    Feed fraction (1)    Nitrogen-containing fraction (5)
NOVELTY - Recovery of carbon dioxide to methane, comprises reacting carbon dioxide with hydrogen to form methane and water in a free radical reaction, where hydrogen gas is dissolved in supercritical carbon dioxide at a ratio of 2:1, and the reaction is initiated with hydrogen peroxide and optionally oxygen gas at ratio of 1:0-1:1, and microwaves provide energy for the free racial initiation.    USE - The process is useful for recovery of carbon dioxide to methane.    ADVANTAGE - The process is carried out at lower temperature and pressure, in less complicated reactor, and utilizes the reactants in near liquid phase, hence it is simple, safe and economical.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for system for recovery of carbon dioxide to methane, comprising a geometric facility providing energy for electrolysis of water to oxygen gas and hydrogen gas, where the oxygen gas is used for free radical initiation and hydrogen gas is used as the reactant hydrogen gas in the process.    DESCRIPTION OF DRAWING(S) - The figure shows a flow chart overview of the system for recovery of carbon dioxide to methane.
NOVELTY - Composition comprises (a) biomass, (b) an ionic liquid, (c) water, and (d) salt comprising kosmotropic anion chosen from phosphate, hydrogen phosphate, sulfate, ethyl sulfate, borate, bromide, chloride, acetate, formate, citrate, and their mixtures.    USE - The composition is useful for pretreating biomass (all claimed).    ADVANTAGE - The method can be performed inexpensively by utilizing reduced amount of energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of pretreating biomass, which involves (a) combining the biomass with an ionic liquid to form a first composition, (b) heating the first composition to form a pretreated biomass composition, (c) contacting a salt comprising a kosmotropic anion in an aqueous solution with the pretreated biomass composition to form an aqueous phase, an ionic liquid phase, and precipitated solids, where the aqueous phase comprises 0-2 wt.% of the ionic liquid, and (d) separating the aqueous phase, the ionic liquid phase, and the precipitated solids.
NOVELTY - Method (I) of producing biofuel (12) from cellulosic feedstock (14), comprises: converting cellulose from the feedstock into lipids; converting lignin from the feedstock into ringed hydrocarbons (74); and processing the lipids and ringed hydrocarbons into biofuel.    USE - The method is useful for producing biofuel (as a surrogate for jet fuel) from cellulosic feedstock including agricultural residues e.g. corn stover, saw dust, rice hulls, distiller grains and straws, energy crops grown specifically for their biomass e.g. grasses, sweet sorghum and fast growing trees, and waste products of paper, e.g. recycled newspaper, paper mill sludges, pulp mill waste and sorted municipal solid waste, and/or green wastes e.g. leaves, grass clippings, shrimp wastes, vegetable and fruit wastes.    ADVANTAGE - The method is simple to implement, easy to use, and comparatively cost effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a system comprising means for pre-treating the cellulosic feedstock to facilitate further treatment of cellulose and lignin on it, first means for converting the cellulose into sugars, second means for (66) converting the sugars into lipids, third means for converting the lignin into ringed hydrocarbons, and means for processing the lipids and ringed hydrocarbons into biofuel.    DESCRIPTION OF DRAWING(S) - The figure shows an operational flow chart of the biofuel production method.    Producing biofuel (12)    Pre-treating the cellulosic feedstock (26)    Converting sugar into lipid (66)    Processing the lipids into straight chain paraffins and esters (70)    Converting lignin from the feedstock into ringed hydrocarbons (74)
NOVELTY - A laboratory sample reserving and storing method comprises (A) detection sampling, and (B) performing sample capsulation. The step (A) comprises using one-off head of full automatic enzyme, increasing sampling procedure, performing enzyme detection, and reserving hole position and plasma upper box-plate detection sampling hole. About 96 hole remaining sampling box uses bar code mark. The special storing box according to left sample box size distinguishes location to ensure the left sample position is unique.    USE - Laboratory sample reserving and storing method.    ADVANTAGE - The method increases a sampling procedure. It effectively prevents evaporation, thus sample cross contamination is avoided. When need starting sample review, the sample can be taken out, and does not influence other sample. Sample reserving is more fast and convenient. The method also ensures sampling sample quality, and is scientific and reasonable.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method using geotechnical filter bag for landfill processing municipal sludge which comprises reserving hole position and plasma on box detecting plate position corresponding to test sample at the same time of sampling.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating (Drawing includes non-English language texts)
NOVELTY - The method involves flowing waste water via an electrolysis cell (22) coupled to an electrical grid (18) that receives power from an intermittent power source (20). The electrolysis cell is biased to form hydrogen when power availability on the grid is above an upper threshold. The hydrogen is distributed to a set of fuel cells (30, 32). Current and potable water are drawn from the fuel cells when the power availability is below a lower threshold. Anode off gas from the electrolysis cell is pressurized and readmitted into a portion of waste water not converted to the potable water.    USE - Method for converting waste water e.g. storm-drain outflow, treated sewage, and untreated sewage (all claimed), received from municipal area, residential area, and/or commercial area, into potable water.    ADVANTAGE - The method enables converting the waste water into the portable water in an efficient and economical manner using energy from the intermittent energy sources.    DETAILED DESCRIPTION - The intermittent power source is a solar power source, a wind power source, a wave power source and a tidal power source. An INDEPENDENT CLAIM is also included for a water-treatment system comprising an electrolysis cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a water-treatment system for converting waste water into potable water.    Water treatment system (10)    Electrical grid (18)    Intermittent power source (20)    Electrolysis cell (22)    Hydrogen-storage reservoir (28)    Fuel cells (30, 32)
NOVELTY - Biological drying of municipal domestic sludge, comprises (i) mixing the municipal domestic sludge with the organic filling auxiliary material; (ii) obtaining the fermentation materials; (iii) carrying out aerobic fermentation; (iv) carrying out the first time turning over and mixing treatment for the fermentation materials and the second time turning over and mixing treatment for the fermentation materials, then carrying out the turning over and mixing treatment for once every 8-24 hours; and (v) obtaining the product when water content of fermentation materials is reduced to 30 wt.% below.    USE - The method is useful for biological drying of municipal domestic sludge.    ADVANTAGE - The method reduces the dosage of the organic filling auxiliary material; reduces the water content of the sludge to 30 wt.% below in 7-9 days; and is simple, quick and economical.    DETAILED DESCRIPTION - Biological drying of municipal domestic sludge, comprises (i) mixing the municipal domestic sludge with the organic filling auxiliary material in a ratio of 1:0.1-0.6 uniformly; (ii) introducing the aerobic fermenting agent in the mixture to obtain the fermentation materials; (iii) stacking the fermentation materials to the strip fermentation buttress for aerobic fermentation; (iv) carrying out the first time turning over and mixing treatment for the fermentation materials when the temperature of the fermentation materials increases to 38-42 degrees C, carrying out the second time turning over and mixing treatment for the fermentation materials when the temperature of the fermentation materials increases to 60-75 degrees C, then carrying out the turning over and mixing treatment for once every 8-24 hours; and (v) obtaining the product when the water content of the fermentation materials is reduced to 30 wt.% below.
NOVELTY - A p-(4-hydroxy-o-tolylazo)benzenesulfonic acid or its salt is subjected to catalytic reduction in presence of hydrogen and a transition metal catalyst to obtain 4-amino-m-cresol.    USE - Manufacture of 4-amino-m-cresol. Uses include but are not limited to resin, dye, antioxidant, agrochemical and pharmaceuticals.    ADVANTAGE - The 4-amino-m-cresol having high purity is economically manufactured with high yield by simple method, without environmental pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for recovery of sulfanilic acid, which involves recovering of sulfanilic acid from the filtrate.
NOVELTY - A hydrogen gas manufacturing apparatus (10A) has a portion (1A) for manufacturing liquid mixture of water glycogen, which mixes water-containing liquid and powder-form glycogen, and a hydrogen gas manufacturing portion (2A) for heating and vaporizing liquid mixture, reacting, and producing hydrogen gas. The hydrogen gas manufacturing portion has a heating steam portion for heating and vaporizing the liquid mixture, and a reaction portion for reacting vaporized mixture and generating hydrogen gas. The water-containing liquid is fermented ethanol.    USE - Apparatus used for manufacturing hydrogen gas used for fuel cell.    ADVANTAGE - The apparatus efficiently and economically enables to produce hydrogen with reduced power consumption and without discharging carbon dioxide.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of manufacturing apparatus of hydrogen gas. (Drawing includes non-English language text)    Portion for manufacturing liquid mixture (1A)    Hydrogen gas manufacturing portion (2A)    Hydrogen gas manufacturing apparatus (10A)
NOVELTY - Producing hydrogen by electrolysis of an aqueous electrolyte and/or an electrolyte contained alcohols comprises feeding an element of group IV to the electrolyte.    USE - The method is useful for producing hydrogen by electrolysis of an aqueous electrolyte and/or an electrolyte contained alcohols.    ADVANTAGE - The method has good controllability and produces high yield of hydrogen.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) producing silane, preferably also with the aid of one of the hydrogen generating method comprising subjecting a silicon or a silicon compound containing electrolyte to electrolysis; and    (2) hydrogen and/or silane production process by using monovalent hydroxide as an electrolyte for the electrolysis
NOVELTY - Producing alcohol involves performing Guerbet reaction in gas phase and at total pressure of less than 1 atmosphere, using at least one raw material alcohol.    USE - For producing alcohol (claimed) useful as chemical industrial raw material or high octane fuel.    ADVANTAGE - The method increases the yield of Guerbet alcohols and reduces the production cost.
NOVELTY - A hydrogen storage alloy has composition (I) containing cobalt, iron, manganese, titanium, vanadium and zirconium.    USE - Hydrogen storage alloy used for heat storage, heat pump, hydrogen purification, isotope separation, secondary battery and fuel cell of cars.    ADVANTAGE - The hydrogen storage alloy has excellent hydrogen absorption/desorption property, hydrogen storage capacity and does not produce harmful polluted gases.    DETAILED DESCRIPTION - A hydrogen storage alloy has composition of formula: CouFevMnwTixVyZrz, where u, w are 0.5-2.0, v, x are 0.5-2.5, y, z are 0.4-3.0. The content of cobalt is 9.0-28.6 and the remaining contents are 14.3-18.2, or the content of iron is 9.0-33.3 and remaining contents are 13.3-18.2, or the content of manganese is 9.0-28.6 and the remaining contents are 14.3-18.2, or the content of titanium is 9.0-33.3 and remaining contents are 13.3-18.2, or the content of vanadium is 9.0-33.3 and the remaining contents are 13.3-18.2, or the content of zirconium is 7.5-37.5 and the remaining contents are 12.5-18.5.
NOVELTY - A composite metal sulfide-containing photocatalyst is synthesized by mixing and heating copper(I) sulfide (Cu2S), silver sulfide (Ag2S), zinc sulfide (ZnS), and germanium disulfide (GeS2) so that molar ratio (Cu2S:Ag2S:ZnS:GeS2) becomes x:(1-x):((100+y)/100):((100+y)/100), where x=0.5-1 and y=5-30.    USE - A synthesis of composite metal sulfide-containing photocatalyst for photocatalyst electrode used for hydrogen generating apparatus (all claimed).    ADVANTAGE - A composite metal sulfide-containing photocatalyst is efficiently synthesized, and hydrogen is effectively generated.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a photocatalyst electrode containing the photocatalyst consists of composite metal sulfide represented by empirical formula Cu((800x)/(400+3y))Ag((800-800x)/(400+3y))Zn((400+4y)/(400+3y))Ge((400+4y)/(400+3y))S4 (1) and exhibiting p-type semiconductor characteristic; and    (2) a hydrogen generating apparatus which contains the photocatalyst electrode and a counter electrode, applies external bias below the theoretical decomposition voltage of water between the photocatalyst electrode and the counter electrode, and decomposes water and produces hydrogen on the photocatalyst electrode surface by light irradiation.    x = 0.5-1; and    y = 5-30.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph of capacitance voltage (CV) measurement results. (Drawing includes non-English language text).
(PT105275-A1)   NOVELTY - The method involves utilizing production line controlled by an electronic control unit, where a mixing system provides homogeneous mixture of biomass pulp. A mechanical compression system is provided for reducing moisture content, where an extruder is provided with a cutting blade system.    USE - Method for producing blocks, pellets and granules from vegetable waste, particularly olive pulp and cork powder.    ADVANTAGE - The method produces the blocks, pellets and granules on industrial scale.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a plant for industrial production of blocks, pellets and granules from vegetable waste.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of the installation.    System (5)    Production lines (5,6,8,9,14)    Mechanical compression system (6)    Extrusion system (7)    Electronic control unit (15)
NOVELTY - A CLIMAX-VMT strain of Myceliophthora thermophila whose preservation number is CGMCC No. 5134, is new.    USE - The strain is useful for treating agricultural organic solid waste (claimed).    ADVANTAGE - The strain CLIMAX-VMT of M. thermophila has obvious rapid fermentation of fermented sausage of heating and decomposing cellulose, and does not have toxicity and harm to human and domestic animal. Also, the strain has no antagonism to the most low thermophiles, and namely has good generality and the compatibility with the other strain with good effect.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a microbial inoculum containing the strain; and    (2) use of the strain in the agricultural organic solid waste treatment.
NOVELTY - Method for processing wastewater containing soluble protein, involves mixing wastewater and protein separation agent, maintaining the mixture, and carrying out solid-liquid separation process of the mixture to obtain solid product and liquid product, where the protein separation agent comprises alginic acid salt, chitosan, starch and gelatin.    USE - The method is useful for processing wastewater, and separating soluble proteins and insoluble solid. The wastewater is wastewater which is generated in fermentation process for producing alcohol.    ADVANTAGE - The method is cost-effective, and enables recovery of soluble protein and insoluble solid with light color and excellent quality.
NOVELTY - Aescin extract preparation and purification comprises weighing aescin extract in water to dissolve; adjusting pH at 1-4 by acid solution; adding 1-2 times of n-butyl alcohol for 2 times; combining extraction liquid; washing by alkaline solution until neutral; decompressing and recycling the solvent; drying by microwave irradiation until water content is less than 2%; adjusting microwave power to keep the material temperature at 35-55 degrees C; obtaining white aescin powder; packing; and sealing.    USE - Aescin extract preparation and purification (claimed).    ADVANTAGE - The method is simple and environmentally friendly; and has high production efficiency.
NOVELTY - The method involves arranging settling tank, alimentary canal, fermenting room, and compound fermenting chamber sequentially in aeration pool of the sewage tank. The polysilicon material and aerobic fermentation microbial material are prepared to solar heat collecting system. The aerobic fermentation microbial material is mixed in fermentation room to magnetize the raw sludge.    USE - Method for dehydrating sludge during sewage treatment plant.    ADVANTAGE - The sludge can be dehydrated at low cost during sewage treatment plant.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view illustrating sludge dehydrating process.
NOVELTY - A carbon-preparing device is manufactured using a heat furnace hollow blade vaporization reactor and a hollow blade carbonization reactor, connected with a heat conducting oil pipeline and a tail gas channel. Sludge is stirred continuously by heating, the tail gas simultaneously reacting in the moving sludge. The middle section carries out sludge organic matter curing melting and mixing polymerization to form organic colloid. The back section carries out carbonization reaction of sludge fiber and organic colloid to form high-molecular organic carbon.    USE - Manufacture of device used for preparing carbon by carbonization treatment of sludge at low temperature.    DETAILED DESCRIPTION - A carbon-preparing device is manufactured using a heat furnace hollow blade vaporization reactor and a hollow blade carbonization reactor, connected with a heat conducting oil pipeline and a tail gas channel. The work temperature is less than 270 degrees C. Sludge is stirred continuously by heating, the tail gas simultaneously reacting in the moving sludge. Sludge water is converted into steam. The middle section carries out sludge organic matter curing melting and mixing polymerization to form organic colloid. The back section carries out carbonization reaction of sludge fiber and organic colloid to form high-molecular organic carbon. Sludge is carbonized to form carbon. Each ton of sludge (water content is less than 80%) is made into 70 kcal of high-molecular organic carbon. One-off energy combustion boiler is replaced for sludge carbonization process in the production process. Organic carbon is produced by burning slag (24-60 kg). The high-frequency coil for producing 0.1 m3 of slag brick for construction, and a charring municipal sludge device for shortcut nitrification of sludge treatment and disposal are provided.
NOVELTY - Saprophytic bacteria culture medium comprises (in parts weight): beef extract (0.11-0.12), peptone (0.8-0.9), sodium chloride (0.8-0.9), glucose (0.19-0.2), deionized water (97.83-97.85), and 10% concentrated sulfuric acid (0.29-0.3).    USE - The saprophytic bacteria culture medium is useful for treating sewage wastewater (claimed) and detecting bacteria in wastewater.    ADVANTAGE - The culture medium detects bacteria conveniently and rapidly with excellent sensitivity, and accuracy.
NOVELTY - Preparing natural antibacterial peptide products of insects comprises: selecting Tenebrio molitor, housefly and Bactrocera dorsalis insects as raw materials, preparing a raw material slurry using phosphate buffer solution, heating, centrifuging to extract the supernatant, purifying by passing the supernatant through a membrane filter of 30 kDa and 10 kDa, passing the liquid through the cation exchange column chromatography, desalting the combined sample of cation exchange column, intercepting through the film membrane, collecting the permeate liquid and spray drying.    USE - The antibacterial peptide product of insects is useful as pharmaceutical raw materials, food, fruit and vegetable preservatives, feed additives and skin care products (claimed).    ADVANTAGE - The method is simple, rapid and environment-friendly.    DETAILED DESCRIPTION - Preparing natural antibacterial peptide product of insects comprises: (i) selecting Tenebrio molitor, housefly and Bactrocera dorsalis insects as raw materials, (ii) preparing raw material slurry using phosphate buffer solution, heating at 100 degrees C in a boiling water bath and centrifuging for 10 minutes to extract the supernatant, (iii) passing the supernatant through a membrane filter by tangential flow fractionation, intercepting the supernatant through a 30 kDa film and purifying by intercepting through film package of 10 kDa, (iv) passing the liquid through a cation exchange column, collecting and combining the obtained sample, (v) desalting the combined sample of cation exchange column and intercepting through 5 kDa film membrane and collecting the permeate liquid, and (vi) spray drying the liquid to obtain the product.
NOVELTY - Method for producing acetic acid, involves fermenting active sludge under anaerobic condition and adding l-3 g/l of lactose to the fermentation medium on eleventh day of fermentation.    USE - The method is useful for producing acetic acid.    ADVANTAGE - The method is environmentally-friendly as the waste materials contained in the sludge are easily degradable, and produces large amount of acetic acid of 8.87 g/l.
NOVELTY - Starch raw material powder is mixed with water to obtain a starch slurry. The starch slurry is mixed with portion (I) of amylase to obtain a mixture. The mixture is primarily injected with steam (I) at 80-100 degrees C to obtain a primary emulsion. The primary emulsion is injected with steam (II) at 120-150 degrees C to obtain a secondary emulsion. The secondary emulsion is flashed and cooled, mixed with portion (II) of amylase, and enzymolyzed.    USE - Processing of starch raw material e.g. corn, tuber, wheat and/or broomcorn used in preparation of citric acid (all claimed).    ADVANTAGE - The method reduces digestible energy (DE) value and shortens citric acid fermentation period.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of citric acid, which involves fermenting processed starch raw material in the presence of Aspergillus niger.
NOVELTY - The device has a urea melting tank that is respectively connected with a lower and upper end of pipe. An upper end of urea melting tank is provided with an oil pump. A lower end of connecting pipeline is provided in a heat-conducting oil boiler. An oil tank is connected with an oil return pipe and oil delivery pipe. The oil delivery pipe is provided with an oil pump in urea melting tank. The oil tank is provided between the connecting pipes. The oil tank and a low-position oil groove are provided with an exhaust pipe.    USE - Oil recycling device for heating and melting urea.    ADVANTAGE - The energy utilization rate of recycling device can be improved. The wastage of water resource and environment pollution can be avoided. The urea can be heated and melted automatically.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the oil recycling device.
NOVELTY - The treatment device has a gas inlet device and a gas outlet device that are arranged on upper and lower parts of a low temperature plasma reaction chamber and connected with a gas inlet and a gas outlet of the plasma reaction chamber that is formed with a honeycomb shaped longitudinal reaction cavity. The gas outlet device is connected with a photo-catalysis device. A center part of the reaction cavity is provided with a longitudinal corona line. A side face of the plasma reaction chamber is provided with an air supply port. An insulating ceramic layer is formed on the air supply port.    USE - Waste gas treatment device.    ADVANTAGE - The device is simple in structure, and is provided with a flow guiding plate for balancing airflow speed and improving treatment effect. The device is convenient to install, repair and maintain, and occupies less floor space. The insulating ceramic layer ensures better safety.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a waste gas treatment method.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a waste gas treatment device.
NOVELTY - The furnace has a furnace body provided with a furnace bridge that is divided into upper and lower cavities. The furnace bridge is formed as a reaction chamber. A top part of the reaction chamber is provided with a gathering chamber, a drying section and an anaerobic combustion reaction area. A cylindrical is extended into the reaction chamber. An upper end of a feeding connection purifier is provided with an air pump that is connected with a gas pipe. A hollow tube is provided with multiple oxygen supplementing holes. An ash cavity is provided with a slag outlet.    USE - Carbon monoxide combustible gas generating anaerobic reaction furnace.    ADVANTAGE - The furnace utilizes carbon monoxide combustible gas during an anaerobic combustion reaction, and has high productivity. The furnace avoids pollution to environment.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a carbon monoxide combustible gas generating anaerobic reaction furnace.
NOVELTY - The device has an outer sleeve horizontally arranged at a bottom end of a straw gasification furnace. Outer circles of upper and lower parts of the outer sleeve are formed with carbon discharging openings. An outer circle of an inner sleeve is formed in a zero clearance rolling sleeve. The zero clearance rolling sleeve is sleeved on the outer sleeve in a collecting opening corresponding to the carbon discharging openings, where diameter of the collecting opening is not less than the diameter of the carbon discharging openings. The inner sleeve is driven by a driving motor.    USE - Straw gasification furnace double layer sleeve-type rotary carbon discharging device.    ADVANTAGE - The zero clearance rolling sleeve is sleeved on the outer sleeve so as to discharge the straw carbon through the collecting opening and carbon discharge openings, thus ensuring continuous discharging of ash and carbon without air tightness from the straw gasification furnace and improving discharging of gas generated during combustion. The device ensures that performance of the straw gasification furnace is stable and unaffected by biomass carbon. The device is inexpensive.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a straw gasification furnace double layer sleeve-type rotary carbon discharging device.
NOVELTY - Solid fuel is prepared using sawdust from wood processing plant by making collected sawdust into ball or pressing into group having diameter of 10-150 mm, and then drying naturally; packaging the processed sawdust material into a distillation tank to carry out destructive distillation using solar or wind energy which is transformed to electric energy as heat source; after finishing carbonization, removing heat source to naturally cool the material in the distillation tank at lower than 60 degrees C; and collecting solid material in the distillation tank to obtain a high quality solid fuel.    USE - Method of preparing solid fuel using sawdust from wood processing plant (claimed).    ADVANTAGE - The method can develop a way for resource utilization of sawdust material and uses renewable solar energy and wind energy as heat source, which is an environment-friendly green process. The obtained solid fuel has carbon content of more than 80 wt.% and sulfur content of less than 0.015 wt.%.    DETAILED DESCRIPTION - Preparation of solid fuel using sawdust from wood processing plant comprises:    (A) pre-processing collected sawdust by making into ball or pressing into group having diameter of 10-150 mm, and then drying naturally;    (B) packaging the processed sawdust material into a distillation tank to carry out destructive distillation using solar or wind energy which is transformed to electric energy as heat source, when gas flow meter arranged outside of tank displays less than or equal to 10% of peak value of gas volume flow rate, finishing carbonization;    (C) removing heat source to naturally cool the material in the distillation tank at lower than 60 degrees C; and    (D) opening distillation discharging port, and collecting the solid material in the distillation tank to obtain a high quality solid fuel.
NOVELTY - The fuel cell (100) has anode-side and cathode-side diffused layers (226,227) arranged such that an anode-side high-elasticity portion (Aah) and a cathode-side high-elasticity portion (Ach) overlap when seen from the lamination direction of the diffused layers with respect to a membrane electrode assembly (210). An anode-side low-elasticity portion (Aas) and a cathode-side low-elasticity portion (Acs) do not overlap when seen from the lamination direction of the diffused layers with respect to the membrane electrode assembly.    USE - Fuel cell for generating electric power.    ADVANTAGE - Allows use of components which differ in Young's modulus and thickness, thus suppressing failure of membrane electrode assembly. Increases electric power generation efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic sectional views of a fuel cell.    Fuel cell (100)    Membrane electrode assembly (210)    Anode-side and cathode-side diffused layers (226,227)    Anode-side high-elasticity portion (Aah)    Anode-side low-elasticity portion (Aas)    Cathode-side high-elasticity portion (Ach)    Cathode-side low-elasticity portion (Acs)
NOVELTY - A renewable energy mixed use system has solar power generation device installed on the ground, biomass cultivation apparatus installed in the underground of the solar power generation device, and methane fermentation tank which methane-ferments the biomass grown with the biomass cultivation apparatus.    USE - A renewable energy mixed use system.    ADVANTAGE - Decline in the efficiency of photoelectric conversion of solar power generation device is prevented, and total amount of renewable energy obtained from a unit area is increased.    DETAILED DESCRIPTION - A renewable energy mixed use system has solar power generation device installed on the ground, biomass cultivation apparatus installed in the underground of the solar power generation device, and methane fermentation tank which methane-ferments the biomass grown with the biomass cultivation apparatus. While using the thermal effluent used for cooling the light-receiving surface of the solar power generation device as a heat source of a methane fermentation tank, organic waste including the biomass grown with the biomass cultivation apparatus in the methane fermentation tank are methane-fermented.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the renewable energy mixed used system. (Drawing includes non-English language text).    Pump (1)    Water supply piping (2)    Thermal effluent supply piping (3, 4, 5)    Piping (6)    Solar power generation device (10)    Thermal effluent collection tank (20)
NOVELTY - Filtering vinasse obtained during bioethanol production, comprises alkalizing vinasse with lime milk (A), which is a solution or suspension of calcium hydroxide with upto a pH of at least 12; introducing carbon dioxide gas into the alkalized vinasse, where a large part of the lime milk is converted into calcium carbonate and the pH value is reduced to 8-8.5; filtering the carbonated vinasse to remove the solids; eliminating remaining dissolved substances with ion exchangers; and/or evaporating the greater portion of residual water in the vinasse in a single- or multi-stage evaporation plant.    USE - The method is useful for filtering vinasse obtained during bioethanol production.    ADVANTAGE - The method: is simple and economic; carries out the filtration in the ion exchangers without damaging the ion exchange resins in an irreversible manner; and avoids the formation of hard coatings on heat transfer surfaces.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic flow diagram for filtering the vinasse.    Alkalization step (A)    First carbonation step (C1)    Second carbonation step (C2)    First filtration step (F1)    Second filtration step (F2)
NOVELTY - The method involves producing two electrode ink mixtures comprising different compositions. The electrode ink mixtures are deposited on a substrate, so as to form electrode layers (15) on the substrate. The electrode layers are combined to form a combined electrode layer, so that average level of property of combined electrode layer changes over the substrate.    USE - Method for manufacturing fuel cell electrode (claimed) for use in vehicle.    ADVANTAGE - The fuel cell electrode with gradated properties can be manufactured reliably. The durability of the fuel cell electrode even over different environmental temperatures can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell electrode.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view illustrating the manufacturing process of fuel cell electrode.    Gas diffusion medium (10)    Electrode layer (15)
NOVELTY - The system has a collection line (96) placed adjacent to an outlet (17) of a retort (14) for receiving charcoal from the retort, where the line comprises a collection auger (94) with a flighted portion (98). A delivery line comprising a flighted delivery auger (104) is connected to the collection line. A transfer zone (102) is defined by a space between a downstream end of the flighted portion and an upstream end of the flighted delivery auger. The collection auger collects and delivers the charcoal to form a plug at the zone for blocking biogas from the retort from entering the delivery line.    USE - Charcoal reactor system for converting organic feed i.e. saw dust, to charcoal and biogas. Can also be used for converting wood waste, agricultural waste or organic material that is burned to produce heat energy.    ADVANTAGE - The system enables a condenser and collection tanks to condense undesirable moisture from the biogas to produce clean syngas so as to prevent explosion hazard, and continuously produces the charcoal and biogas by pyrolysis of the organic feed.    DESCRIPTION OF DRAWING(S) - The drawing shows a rear view of a delivery assembly of a charcoal reactor system.    Retort (14)    Outlet of retort (17)    Collection auger (94)    Collection line (96)    Flighted portion (98)    Transfer zone (102)    Flighted delivery auger (104)
NOVELTY - The method involves injecting fuel and oxidant inside a gassifier chamber. The gassifier chamber is arranged close to a plasma torch (5). The fuel is a combination of natural gas, syngas, butane, propane, pentane, ethane and other gaseous fuel. The fuel and oxidant are directed directly to a plasma stream. The natural gas is injected into the plasma stream.    USE - Method for augmenting heat energy in plasma gassifier.    ADVANTAGE - Since the fuel delivered into the gassifier chamber is directed towards the plasma discharge of the electrically operated plasma torch, heat energy of about 21% is obtained, and the electrical consumption of the plasma torch is reduced and the electrical energy is easily converted into plasma heat energy. The fuel/air ratio can be determined in stoichiometric terms so as to enhance control over the emission of syngas at syngas line.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for enhanced plasma gassifier arrangement of gassifier chamber.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the plasma gassifier.    Municipal solid waste (1)    Shredder (2)    Natural gas injection port (3)    Plasma torch (5)    Output slag (7)
NOVELTY - The biodegradable mortar comprises a mixture of agricultural plaster, earth, clay or sand, water, dormant bacteria and sugar, preferably glucose. The dormant bacteria is Nitrosomonas and Nitrobacter.    USE - Biodegradable mortar for producing artifacts and for use in fitness and weight are as a material encapsulated in wheels for bicycles, treadmills, weights, rings, knee pads and general fitness equipment.    ADVANTAGE - The biodegradable mortar is environmentally friendly by using with biological activators and reusable following disposal and generates future reuse of the mixture after scrapping fitness components.
NOVELTY - A Bacillus subtilis strain 104-1-3-1 (NITE P-680) and its induced strain capable of producing thrombolytic enzyme having decomposing activity with respect to waste material, is new.    USE - The B.subtilis strain 104-1-3-1 (NITE P-680) is useful for decomposing waste materials including jellyfishes, fish, plankton, and toxin (claimed), fishery waste materials, marine waste material unintentionally captured especially in seaside industries including power station, and waste material of fresh water-type living organism.    ADVANTAGE - The strain decomposes waste materials simply, cost-effectively and rapidly without using vast place, electrical or heat energy, and suppresses putrefactive smell at time of decomposition.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) thrombolytic enzyme produced by above-mentioned strain; and    (2) method of the processing the waste material, involves subjecting the waste material to decomposition process catalyzed by thrombolytic enzyme.
NOVELTY - The method involves forming a precision film by performing plastic process in a cathode supported solid oxide fuel cell. An inter connector coating process is carried out on a coating face of the cathode supported solid oxide fuel cell at temperature of 600 to 800 degrees centigrade. The plastic process is carried out at the temperature of 850 to 900 degrees centigrade.    USE - Method for coating inter connector material of cathode supported solid oxide fuel cell.    ADVANTAGE - The method enables improving the inter connector coating process and providing better de-intercalation effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an apparatus for processing reduction reaction of a cathode supported solid oxide fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of an apparatus for processing reduction reaction of a cathode supported solid oxide fuel cell.
NOVELTY - Manufacturing regenerated fuel by using urban sewage treatment plant sludge includes pre-treating raw material, uniformly mixing sludge, plant straw and/or traditional Chinese medicine waste residue using a horizontal stirrer; drying and sterilizing the mixture in roller drier such that the material has water content of 40-50% and particle diameter of 2-10 mm; and sending the material to solar and geothermal greenhouse for further drying, sterilizing, drying for 24-48 hours such that water content of the material is 8-15%.    USE - A method for manufacturing regenerated fuel by using urban sewage treatment plant sludge.    ADVANTAGE - The method is simple and easy to operate, convenient to popularize and apply, uses solar energy as heat source, can greatly save energy consumption in the process and reduce production cost.
NOVELTY - Method for utilizing surplus sludge, involves adding and stirring quicklime to the surplus sludge produced by activated sludge method, removing moisture content from the mixture as calcium hydroxide, producing dry organic substance, and utilizing the substance as biofuel.    USE - The method is useful for utilizing surplus sludge for producing biofuel which is used in thermal station.    ADVANTAGE - The method more efficiently removes moisture content from sludge and produces biofuel without impairment of energy and production of odor.
NOVELTY - The system has an electrode plate assembly (5) that is provided with series of plates having cathode plate, anode plate and inner plates which are arranged in parallel. The plates are mounted in lower portion of electrolyzer vessel (3). The voltage is applied across cathode and anode plates through electrode plate assembly, to dissociate water into constituent hydrogen and oxygen gases. An air injector (9) is arranged in water return line of electrolyzer vessel to inject air in water flow for causing air bubbling in water supplied between and around electrode plate assembly.    USE - System for enhancing hydrogen-oxygen gas for internal combustion engines in vehicles.    ADVANTAGE - The electrode plate assembly can produce sufficient hydrogen gas by using low amount of electrical power. The chemical agents are not required to be added to the electrolyte water for boosting electrolyte conductivity or dissociation performance. The hydrogen gas dissociated from oxygen gas can be maintained in stable condition by an electromagnetic coil assembly which separates hydrogen gas from oxygen gas. The fuel usage in vehicle engine and carbon exhaust can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the system for enhancing electrolyzed hydrogen gas.    Electrolyzer vessel (3)    Plate assembly (5)    Water circulation line (7)    Air injector (9)    Water return port (10)
NOVELTY - Method for storing granular sludge, involves (a) storing sludge discharged through water outlet of an anaerobic ammonium oxidation reactor in a sealed container, filling inert gas for maintaining the sealed container in an anaerobic condition, and maintaining the container at normal temperature and pH of 7-9, (b) adding nutrient solution comprising ammonia and nitride for every 3-15 days to the container, and (c) adding fresh granular sludge to the container every 3-18 days, where the addition amount of sludge is 0.1-0.5% of the volume of container.    USE - The method is useful for storing granular sludge (claimed).    ADVANTAGE - The method maintains activity of anaerobic ammonium oxidation bacteria by supplementing growth factors at regular intervals through addition of fresh sludge, and hence the sludge can be stored for long period of time. The method enables denitrification at a higher rate in short period of time. The nutrient solution is added at long intervals and thus frequent disturbance of stored sludge is avoided.    DETAILED DESCRIPTION - Method for storing granular sludge, involves (a) storing sludge discharged through water outlet of an anaerobic ammonium oxidation reactor in a sealed container, filling inert gas for maintaining the sealed container in an anaerobic condition, and maintaining the container at normal temperature and pH of 7-9, (b) adding nutrient solution comprising ammonia and nitride for every 3-15 days to the container, and ensuring that the concentration of ammonia nitrogen and nitride in the sealed container is 14-98 mg/l, where the amount of nutrient solution added each time is 1-50% of the volume of container, and (c) adding fresh granular sludge to the container every 3-18 days, where the addition amount of sludge is 0.1-0.5% of the volume of container. The volume ratio of sludge to water is 1:0.6-1.4. The molar ratio of ammonia to nitride in the nutrient solution is 1:0.8-1.3.
NOVELTY - An additive comprises fatty alcohol, aliphatic ether, aliphatic ester, fatty acid, aliphatic amine and emulsifier. The fatty alcohol is isopropanol, propanol, pentanol, isoamylol and/or n-butanol. The aliphatic ether is ethylene glycol propyl ether and/or ethylene glycol monobutyl ether. The aliphatic ester is butyl acetate, n-amyl acetate and/or isoamyl acetate. The fatty acid is oleic acid and/or naphthenic acid. The aliphatic amine is dimethylamine and/or diethylamine. The phenol emulsifier is octyl phenol ethoxylate (OP-15) emulsifier and/or octyl phenol ethoxylate (OP-20) emulsifier.    USE - Additive for improving anti-phase separating performance and heat value of methanol petrol.    ADVANTAGE - The additive has better low-temperature anti-phase separation and water-phase separation properties.    DETAILED DESCRIPTION - An additive comprises (in wt.%) fatty alcohol (35-45), aliphatic ether (10-20), aliphatic ester (15-30), fatty acid (5-15), aliphatic amine (1-5) and octyl phenol emulsifier (0.1-3). The fatty alcohol is isopropanol, propanol, pentanol, isoamylol and/or n-butanol. The aliphatic ether is ethylene glycol propyl ether and/or ethylene glycol monobutyl ether. The aliphatic ester is butyl acetate, n-amyl acetate and/or isoamyl acetate. The fatty acid is oleic acid and/or naphthenic acid. The aliphatic amine is dimethylamine and/or diethylamine. The octyl phenol emulsifier is octyl phenol ethoxylate (OP-15) emulsifier and/or octyl phenol ethoxylate (OP-20) emulsifier.
NOVELTY - A greenhouse warming fuel comprises (in weight parts) straw (30-50), methanol (10-20), sulfonamides (5-10) and ethanol (1-3).    USE - Greenhouse warming fuel.    ADVANTAGE - The greenhouse warming fuel is effective and economical.
NOVELTY - The device has discharging plug board that is located on one side of rubbish pool wall, and flashboard set above a feeding port. The movable baffle is provided to push the rubbish into a rubbish pool. A pebble layer is provided as filtrate collecting pipe.    USE - Sewage treatment device for pig farm.
NOVELTY - The method involves analyzing the concentration of sulfate and phosphate in the sample of petroleum hydrocarbon anaerobic biodegradation system. The sulfate and phosphate are supplemented in the petroleum hydrocarbon anaerobic degradation system, to adjust the sulfate concentration and phosphate concentration in the petroleum hydrocarbon anaerobic biodegradable system. The methane is obtained by adjusting the sulfate concentration and phosphate concentration in the petroleum hydrocarbon anaerobic biodegradable system.    USE - Method for controlling production rate of methane.    ADVANTAGE - The reaction rate for petroleum can be improved. The production rate of methane can be controlled easily.
NOVELTY - The method involves processing biomass raw material by pre-processing system. The processed raw material is sent to the compressed air purifier for collecting the waste heat. The collected waste heat is reused by the anaerobic fermentation tank.    USE - Method for producing biological natural gas for use in vehicle.    ADVANTAGE - The heat utilization efficiency can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus for producing biological natural gas for use in vehicle.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the apparatus for producing biological natural gas for use in vehicle. (Drawing includes non-English language text)
NOVELTY - A filamentous Penicillium sp. HDSF3 (CGMCC No: 5029) capable of degrading lignocellulose in forest litter, is new.    USE - The filamentous Penicillium sp. HDSF3 is useful for degrading lignocellulose in forest litter.    ADVANTAGE - The filamentous Penicillium sp. is environmentally-friendly, degrades lignocellulose high efficiently and protects forest at improved level.
NOVELTY - The method involves collecting, sorting and crushing organic solid waste for anaerobic fermentation. The organic waste is processed to carry out solid-liquid separation process. The liquid raw material is separated for anaerobic fermentation to produce biogas. The prepared biomass fuel is collected. The solid raw material is separated for anaerobic fermentation to produce biogas. The prepared biomass fuel is collected. The fermentation is continued to produce biogas, after processing raw materials. The biological fuel gas is collected by generating residual liquid.    USE - Method for preparing biological fuel gas by using organic solid waste.    ADVANTAGE - The treatment effect of harmless organic waste can be improved reliably.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for device for preparing biological fuel gas by using organic solid waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for preparing biological fuel gas by using organic solid waste.
NOVELTY - The method involves separating organic wastes from the water content. The solid material and liquid content are pre-heated in the respective reactors to produce the biological fuel gas. The biological fuel gas collected from reactors is purified to discharge the residues from biological fuel gas.    USE - Method for producing biological fuel gas.    ADVANTAGE - The biological fuel gas can be produced effectively. The power consumption of biological fuel gas producing device can be reduced. The environment can be protected from pollution caused by discharge of biological fuel gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for device for producing biological fuel gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the process for producing biological fuel gas.
NOVELTY - Treating wastewater of fermented alcohol production, comprises (i) performing high temperature contact type anaerobic fermentation to produce alcohol wastewater; (ii) centrifugally separating alcohol to obtain sludge and clear fluid; (iii) anaerobically fermenting by an upward-flow anaerobic sludge bed (UASB); (iv) carrying out separation of anaerobically fermented wastewater by a three phase separator to obtain methane, deposited sludge, and clear fluid; (v) aerobically fermenting, depositing after fermenting, and separating clear fluid; and (vi) processing alcohol.    USE - The method is useful for treating wastewater of fermented alcohol production.    ADVANTAGE - The method saves energy and water by comprehensive utilization of resources, utilizes natural resources and secondary energy, and reduces wastes and pollutants discharge.    DETAILED DESCRIPTION - Treating wastewater of fermented alcohol production, comprises (i) performing high temperature contact type anaerobic fermentation to produce alcohol wastewater, where the fermentation temperature is 55-60 degrees C, and the fermentation time is 8-10 days; (ii) centrifugally separating alcohol, and obtaining a sludge and a clear fluid; (iii) performing upward-flow anaerobic sludge bed (UASB) anaerobic fermentation at 36-38 degrees C on the separated clear liquid medium of the step (ii); (iv) carrying out separation of anaerobically fermented wastewater by a three phase separator to obtain methane, deposited sludge, and clear fluid; (v) aerobically fermenting the clear liquid of the step (iv) in a sequencing batch reactor (SBR) under room temperature, and then depositing after fermenting, and separating the clear fluid; and (vi) processing alcohol in the separated clear fluid of the step (v).
NOVELTY - Production of ethanol from cassava residue, involves (a) pre-hydrolyzing starch, cellulose and hemicellulose in cassava residue, (b) regulating temperature of the pre-hydrolyzed residue to 32-44 degrees C, (c) adding Saccharomyces cerevisiae FE-B strain to the residue, and (d) hydrolyzing and fermenting the residue simultaneously.    USE - The method is useful for producing ethanol from cassava residue, which is useful as fuel.    ADVANTAGE - The method enables saccharification of starch at high temperature and hence the process is simplified, energy consumption is reduced (thus cost is reduced), and fuel efficiency of the produced ethanol is enhanced.
NOVELTY - Method for producing ethanol fuel, involves using Canna edulis ker as raw material, and cellulose.    USE - The method is useful for producing ethanol fuel.    ADVANTAGE - The method is simple to perform, cost-effective and suitable for industrial production, and reduces fermentation time.
NOVELTY - The detecting ball has a gas sensor that is selected from methane sensor, carbon monoxide sensor, carbon dioxide sensor, oxygen sensor, sulfureted hydrogen sensor, and arranged in the case. A data processing device is electrically connected with the gas sensor. A wireless transmitting module is electrically connected with the data processing device and lithium battery. A protective cover made of silica gel, rubber or acrylic is separated and distributed with suckers for damping on the outer surface. Several vent holes are formed to the gas sensor.    USE - Wireless detecting ball for detecting gas concentration in disaster area used for mine rescue.    ADVANTAGE - The gas concentration in disaster area can be detected.    DESCRIPTION OF DRAWING(S) - The drawing shows the exploded perspective view of the wireless detecting ball.
NOVELTY - Household garbage machine comprises shell, ferment roller, removable organic fertilizer box, ozone device, speed-variable electric motor box, bracket, and feeding plate. The left upper part of the shell is provided with a hopper. The left lower part of the shell is provided with a lower water inlet. The ferment roller, removable organic fertilizer box, ozone device, and bracket set are provided in the shell. The fermentation roller comprises bearing. The ferment roller is provided on the bracket through the bearing. The ferment roller is provided with a stirring partition.    USE - Household garbage machine.    ADVANTAGE - Compared with the prior art, the machine has garbage automatic sorting and processing functions, so that stirring device is not damaged by hard materials; has sterilizing function; achieves waste recycling; and saves energy.    DETAILED DESCRIPTION - Household garbage machine comprises shell, ferment roller, removable organic fertilizer box, ozone device, speed-variable electric motor box, bracket, and feeding plate. The left upper part of the shell is provided with a hopper. The left lower part of the shell is provided with a lower water inlet. The ferment roller, removable organic fertilizer box, ozone device, and bracket set are provided in the shell. The fermentation roller comprises bearing. The ferment roller is provided on the bracket through the bearing. The variable speed motor drives the ferment roller through gear box. The ferment roller is provided with a stirring partition. The feeding plate is provided below the feed hopper and fixedly connected with the bracket.
NOVELTY - The furnace has a hearth whose bottom part is provided with a raw material pre-heating zone, a raw material pyrolysis area, a reduction area and a high temperature cracking area that are equipped with a temperature control device. A steam inlet main pipe is provided with a vertical branch pipe. A bottom end of the branch pipe is inserted into the hearth and the reduction area. The bottom end of the branch pipeline is provided with a spraying device. A steam input total pipeline is connected with a steam electric boiler.    USE - Steam spray straw gasification furnace.    ADVANTAGE - The furnace uses high pressure steam as gasification agent, improves heat value, and has high production efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a steam spray straw gasification furnace.
NOVELTY - The device has a scraping carbon frame provided with a quenching ring of a gasification furnace bottom. Multiple carbon scraping shafts i.e. hollow water cooling pipes, are horizontally supported on the carbon scraping frame. Ends of multiple carbon scraping shafts are connected with multiple driving wheels. Multiple driving gears are meshed with a drive gear that is connected with a driving motor. Multiple scraping carbon shafts are located on a shaft in the carbon frame that is axially provided with scraping carbon along a working spindle.    USE - Straw gasification furnace carbon scraping device.    ADVANTAGE - The device utilizes multi-cable and the carbon scraping wing of the carbon scraping rotating shaft to drive the carbon scraping gasification furnace by the driving motor. The device has simple structure, better carbon discharging effect, high production efficiency, stable service performance to ensure burning-gasifying room of biomass and high utilization rate of product, and is better for a gasification furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a straw gasification furnace carbon scraping device.
NOVELTY - The furnace has a carbon scraping plate and a support tube. A support plate is wound on the support tube. The upper drawing plate is in rotated state.    USE - Straw gasification furnace.    ADVANTAGE - The structure of the furnace can be realized. The cost of the furnace can be reduced. The efficiency of the furnace can be improved. The performance of furnace is improved stably. The utilization rate can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the straw gasification furnace.
NOVELTY - Microbial fuel cell (100) comprises: a cation exchange membrane (102) defining an anode chamber; an anode (106) positioned in the anode chamber; a cathode (114) in contact with an exterior of the cation exchange membrane; and a restrictor (122) in contact with the cation exchange membrane and defining an opening through which water flows into or out of the anode chamber.    USE - The microbial fuel cell useful for generating electricity for powering the electrically powered devices (claimed) in remote locations and/or deep water settings.    ADVANTAGE - The microbial fuel cell is: capable of generating electricity in the absence of an external power source; and of low-cost, low-maintenance source of continuous electricity for the electrically powered devices.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) an apparatus comprising a buoy, and the microbial fuel cell coupled to the buoy; and    (2) generating electricity for powering the electrically powered device, comprising positioning the buoy in a body of water, and powering the electrically powered device with electricity generated by the microbial fuel cell.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the floating microbial fuel cell.    Microbial fuel cell (100)    Cation exchange membrane (102)    Anode (106)    Cathode (114)    Restrictor (122)
NOVELTY - Biomass pyrolyzing furnace comprises a furnace shell, a furnace tube, a steam discharge pipe, an air inlet pipe and a condensing tower. The furnace tube is set in the furnace shell with a multi-mesh furnace tube. A multi-layer separated from an exhaust chamber is provided between the inner surface of the furnace tube and furnace shell. The inner surface of the furnace shell is provided with multilevel ring sheet clapboard. The furnace tube, the inner wall of the furnace shell, and the ring sheet clapboard form the exhaust chambers. Each exhaust chamber is connected with the condensing tower.    USE - The biomass pyrolyzing furnace is useful for continuous production of charcoal and wood tar.    ADVANTAGE - The furnace is energy-saving, has rapid pyrolyzing rate and hence reduces time, produces wood tar with high quality and high yield, and the operation saves labor.    DETAILED DESCRIPTION - Biomass pyrolyzing furnace comprises a furnace shell, a furnace tube, a steam discharge pipe, an air inlet pipe and a condensing tower. The furnace tube is set in the furnace shell with a multi-mesh furnace tube. A multi-layer separated from an exhaust chamber is provided between the inner surface of the furnace tube and furnace shell. The inner surface of the furnace shell is provided with multilevel ring sheet clapboard. The furnace tube, the inner wall of the furnace shell, and the ring sheet clapboard form the exhaust chambers. Each exhaust chamber is connected with the condensing tower inlet by an exhaust pipe. One side of the air inlet pipe is set on one surface of the furnace shell corresponding to the exhaust pipe, and the outlet of the condensing tower is provided with a draught fan.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the biomass pyrolyzing furnace for continuous production of charcoal and wood tar.
NOVELTY - The device has a gasified gas outlet arranged on an upper part of a shell (5). An air outlet comprises a horizontal gasification gas outlet pipe that is linked with a tapered pipe (9). An exhaust pipe (10) is linked with a clapboard, a lower pipe and a circulating pipe (8). The circulating pipe is arranged at a lower part of the furnace body. An end of a U-shaped liquid seal pipe is linked with a liquid sealing pipe. Another end of the U-shaped liquid seal pipe is linked with a tar cracking pipe (3). The tar cracking pipe comprises an air return vertical pipe body center (4) of a shell.    USE - Biomass gasification tar separating cycling cracking transforming device.    ADVANTAGE - The device realizes gasification gas cycling removing tar and improves purification of gasification gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a cutaway partial sectional view of a biomass gasification tar separating cycling cracking transforming device.    Tar cracking pipe (3)    Air return vertical pipe body center (4)    Furnace body (5)    Circulating pipe (8)    Tapered pipe (9)    Exhaust pipe (10)
NOVELTY - The system has hydrogen generator (2) that performs steam reforming reaction of source gas and supplies produced hydrogen containing gas to anode (1a) of fuel cell (1). The oxidizing agent gas supply apparatus (3) supplies oxidizing agent gas to cathode (1b). The burner (4) produces combustion exhaust gas for combustion to supply heat required for steam reforming reaction to hydrogen generator. The combustion exhaust gas supply structure (5) supplies combustion exhaust gas having carbon monoxide or nitrogen oxide to cathode of fuel cell during starting operation.    USE - Fuel cell system used for moving object e.g. electric vehicle.    ADVANTAGE - Since the combustion exhaust gas supply structure supplies combustion exhaust gas produced by burner to cathode of fuel cell at the time of starting operation, the deterioration of the polymer electrolyte membrane of fuel cell driven by simple structure under the low humidity conditions can be prevented. Thus the polymer electrolyte membrane can be moistened suitably. The durability of the catalyst layer of the anode and the cathode can be ensured.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for operating fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the fuel cell system. (Drawing includes non-English language text)    Fuel cell (1)    Anode (1a)    Cathode (1b)    Hydrogen generator (2)    Oxidizing agent gas supply apparatus (3)    Burner (4)    Combustion exhaust gas supply structure (5)
NOVELTY - Biodiesel fuel is obtained by purifying crude biodiesel fuel obtained by transesterification of waste edible oil, after removal of impurities carried out as follows. An impurity-removal agent by-product glycerol, which is a transesterification by-product, is stir-mixed with raw material waste edible oil. The obtained mixture is left still for 3 hours or more for gravity separation and the impurity-removal agent is gravity-separated.    USE - Manufacture of biodiesel fuel for diesel engines.    ADVANTAGE - The method reduces burden of final filtration process, enables economical and efficient manufacture of biodiesel fuel with high stability, and reliably removes temperature-dependent animal-fat-and-oil impurities.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biodiesel fuel manufacturing apparatus.    Biodiesel fuel manufacturing apparatus (1)    Reaction tank (2)    Impurity-removal-agent supply system (4)    Waste-glycerol recovery system (5)    Biodiesel fuel recovery system (9)
NOVELTY - Treating waste, involves (a) providing waste to treatment site, (b) treating waste to provide organic rich waste fraction, (c) encapsulating organic rich waste fraction in a treatment cell, (d) allowing organic rich waste fraction to undergo anaerobic digestion within cell for predetermined period of time, (e) recirculating leachate and/or extracting biogas produced from anaerobic digestion, (f) opening treatment cell and removing treated waste after predetermined period, and (g) optionally repeating steps (a)-(f) with new waste.    USE - The method is useful for treating waste including municipal solid waste (MSW), commercial and industrial (C and I) waste, agricultural waste, forestry waste and waste from food processing units (claimed) for producing biogas.    ADVANTAGE - The method is rapid, improves yield of biogas, enables to recycle the MSW derived organics, prevents entry of leachate into ground, and can capture any gas formed in anaerobic digestion process in the cell.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) apparatus for performing above-mentioned method; and    (2) treatment facility for treating waste.
NOVELTY - The composter comprises semi-cylindrical enclosure geometry at bottom (la), where the enclosure is opened at its top with a lid (2). The composter comprises a ventilation part (7), brake (6) and a gas forced ventilation element (3b), where a set-axis motor is located inside the enclosure. A cross-renewal system is provided that is comprised of the ventilation element (3b). A loading and unloading system is comprised of guides that are fixed to a casing or a gear mechanism crown-pinion type.    USE - Composter for aquaculture animal by-product waste (claimed).    ADVANTAGE - The composter is good device to clean, safe and efficient treatment of small amounts of waste, which is generated by normal mortality in aquaculture facilities.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the aquaculture animal by-product composter.    Lid (2)    Gas forced ventilation element (3b)    Ventilation element (3b)    Brake (6)    Ventilation part (7)    Bottom (la)
NOVELTY - A post-service processing of a semicrystalline bioplastic, involves thermally annealing the semicrystalline bioplastic to increase degree of crystallinity in the semicrystalline bioplastic; and anaerobically biodegrading the thermally annealed semicrystalline bioplastic.    USE - As post-service processing of a semicrystalline bioplastic, used in soil landfills, digester, or fermentation compost facility (claimed); used to modify the micro-scale morphology of semicrystalline bioplastic.    ADVANTAGE - The present method creates defects/voids in the crystalline bioplastics; modifies the semicrystalline morphology of the semicrystalline bioplastic; increases lamellae thickness in the semicrystalline bioplastic; facilitates penetration of microbial enzymes or fluids, e.g. water, resulting in faster breakup of the material during biodegradation. Through such controlled thermal treatment of semicrystalline bioplastic materials, their out-of-service break-down in landfills or anaerobic digesters is improved, thus making these materials suitable for high-end and durable applications. Applications include environment-friendly packaging, green building materials, structural materials, and biocomposite materials.
NOVELTY - The furnace has a sleeve (1) placed between a first bevel gear (2) and a flange (7), where the first bevel gear and an upper end of a compressing screw rod (8) are fixedly connected. A second bevel gear (4) is fixedly connected with one end of a rocker shaft (6), where another end of the shaft is connected with a rocker (10). The first and second bevel gears are matched with each other. The second bevel gear on the shaft is installed with a rear part of a bearing (26) that is fixed on a bearing seat on a furnace cover. A connecting rod shaft (11) is fixed below a small furnace tooth (19).    USE - Household straw gasification furnace.    ADVANTAGE - The furnace is convenient to operate, ideal and stable in effect, can improve thermal efficiency, and lays the foundation for the automation.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a household straw gasification furnace.    Sleeve (1)    Bevel gears (2, 4)    Rocker shaft (6)    Flange (7)    Compressing screw rod (8)    Rocker (10)    Connecting rod shaft (11)    Small furnace tooth (19)    Bearing (26)
NOVELTY - The furnace has an inlet opened on a furnace body (3). An upper part (2) of the furnace body is fixed around an inlet chamber (6) and provided with a suction port (1). A lower end of the furnace body is located in a lower chamber (5). The lower chamber is provided with a lower suction inlet (4).    USE - Composite suction-type straw gasification furnace.    ADVANTAGE - The furnace reduces waste gas emission, and improves production rate.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a composite suction-type straw gasification furnace.    Suction port (1)    Furnace body upper part (2)    Furnace body (3)    Lower suction inlet (4)    Lower chamber (5)    Inlet chamber (6)
NOVELTY - The furnace has a furnace casing (1) that is provided with a furnace liner (2). The furnace liner on the sealing end cover is provided with an upper end cover (3). The upper end cover is provided with an axial-flow fan (4). The side wall of the furnace casing is provided with the protection gas pipe (5) with exhaust pipe (6) and atomizing cooling pipe in the furnace liner. The furnace inner liner is provided with basket (7).    USE - Biomass energy air dry furnace.    ADVANTAGE - The problem related to the bad heat transfer effect and low heat efficiency, high energy consumption and pollution to the environment can be solved effectively. The furnace with simple structure can be provided at low cost and operated conveniently.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass energy air dry furnace.    Furnace casing (1)    Furnace liner (2)    Upper end cover (3)    Axial-flow fan (4)    Protection gas pipe (5)    Exhaust pipe (6)    Basket (7)
NOVELTY - The device has a two stage pyrolysis reactor (2) and a local product gas strand comprising heat exchangers (4, 13), so that thermal energy required for pyrolysis is directed or not directed from product gas produced in a gasifier (8) i.e. stationary fluidized bed gasifier. A two-stroke ignition beam motor (30) acts as an internal combustion engine and comprises separate injectors for highly compressed synthesis gas and ignition oil from wash oil, pyrolysis oil, tar and combustion air. The highly compressed synthesis gas is injected through the separate injectors into the ignition beam motor.    USE - Device for producing synthesis gas as combustible gas for an internal combustion engine.    ADVANTAGE - The device produces clean and tar-free combustible gases and prevents environmental impact by disposal of problem substances such as chicken muck.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of components of a device for producing synthesis gas as combustible gas for an internal combustion engine.    Fuel voltage (1)    Two stage pyrolysis reactor (2)    Heat exchangers (4, 13)    Gasifier (8)    Two-stroke ignition beam motor (30)
NOVELTY - The gasifier includes a carburetor for producing fuel gas from the biomass, and a filter element (3) such as a filter candle made of stainless steel non-woven fiber through which the fuel gas from the gasifier is conducted. The stainless steel fiber is manufactured by the sintering process. A stainless steel mesh is formed around the stainless steel fiber. A filter element is arranged on a supporting basket.    USE - Gasifier e.g. fixed bed gasifier of biomass, used in combined heat and power station.    ADVANTAGE - Less sensitive filtering effect is provided by the filter element of the gasifier, since the filter element is made up of stainless steel non-woven fabric which reduces mechanical loads and local temperature fluctuations. The filter element comprises a highly effective filtering surface with small space requirement. The filter element is highly stable against mechanical deformation. Penetration of surrounding air into the gasifier is prevented, so that the deflagrations of the device can be obviated effectively. Automatic operation of the device is enabled.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for operating method of biomass gasifier.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of the filter used in the gasifier.    Filter (1)    Filter element (3)    Clean gas side (4)    Ball valve (6)    Gas line (8)
NOVELTY - The device has measuring device with wireless data transmission, data acquisition and evaluation device. The reaction vessel (1) is rotatably driven about first axis, such that parameters such as frequency of rotation, direction of rotation, and rotation speed are variable during operation of the apparatus, and recorded data of reaction vessel is wirelessly transmitted to a data acquisition device.    USE - Device for performing biological degradation test of benzo(a)pyrene (BAP) in aqueous system such as sludge, waste and compost with more solid contents or soil samples (all claimed) using closed reaction vessel under aerobic, anoxic and anaerobic conditions for cell culture, .    ADVANTAGE - The gentle agitation of test material in reaction vessel is performed efficiently, by adjustment of rotation speed of reaction vessel.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the device for performing biological degradation test of BAP.    Reaction vessel (1)    Gearwheels (4)    Rollers (5)    Electromotor (9)    Gearbox (13)
NOVELTY - The method involves supplying hydrogen gas and air to a fuel cell (20) of a fuel cell stack (12) for generating electricity using the fuel cell. The supply of hydrogen gas is stopped while supplying the air into the fuel cell for generating electricity, when shutting down of the fuel cell is detected. The generation of electricity by the fuel cell is stopped when the pressure of hydrogen gas is decreased to a preset lower limit value with respect to actually measured anode pressure value.    USE - Method for shutting down of system of fuel cell e.g. fixed polymer electrolyte fuel cell used in fuel cell vehicle e.g. fuel cell automobile.    ADVANTAGE - The size and cost for producing fuel cell system can be reduced significantly. The damage to the polymer electrolyte membrane can be prevented effectively and deterioration of the fuel cell stack can be suppressed reliably.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fuel cell system. (Drawing includes non-English language text)    Fuel cell system (10)    Fuel cell stack (12)    Regulation/control device (18)    Fuel cell (20)    Polymer electrolyte membrane (22)
NOVELTY - An organic fertilizer is produced by adding heat resistant microbe which can survive under high temperature of 80-90 degrees C to organic materials (2), heating organic materials to high temperature of 80-90 degrees C by zymosis of heat resistant microbe, and setting organic materials as organic fertilizer.    USE - Production of organic fertilizer for crops.    ADVANTAGE - The pest-repellence effect is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the production method of organic fertilizer. (Drawing includes non-English language text).    Organic materials (2)    Air supply pipe (16)    Blowing hole (16a)    Gas return pipe (21)    Heat exchanger (31)
NOVELTY - A sewage ecological treatment and microbial fuel cell power generation structure comprises artificial wetland main body comprising thick gravel layer (1), conductive filler layer (2), insulating filler layer (3), top conductive material layer (4) and wetland plants (5); mass flow controller (MFC) system comprising anode electrode, cathode electrode and external wire connected to cathode and the anode; and anode comprising lower conductive filler layer of artificial wetland, and cathode comprising top conductive material layer of artificial wetland.    USE - Sewage ecological treatment and microbial fuel cell power generation structure.    DETAILED DESCRIPTION - A sewage ecological treatment and microbial fuel cell power generation structure comprises artificial wetland main body comprising thick gravel layer (1), conductive filler layer (2), insulating filler layer (3), top conductive material layer (4) and wetland plants (5); thick gravel layer arranged on bottom, conductive filler layer arranged in anaerobic zone of thick gravel layer; insulating filler layer arranged between conductive filler layer and top conductive material layer; wetland plants fixed in insulating filler layer, root of wetland plants penetrating lower conductive filler layer as growth of the plants; MFC system comprising anode electrode, cathode electrode and external wire connected to cathode and the anode; anode comprising lower conductive filler layer of artificial wetland, and cathode comprising top conductive material layer of artificial wetland; and one part of the top conductive material layer soaked in water, and other part exposed in air to form air cathode.    DESCRIPTION OF DRAWING(S) - The drawing shows an isometric view of the sewage ecological treatment and microbial fuel cell power generation structure.    Thick gravel layer (1)    Conductive filler layer (2)    Insulating filler layer (3)    Top conductive material layer (4)    Wetland plants (5)
NOVELTY - Methane tank comprises a supporting shell, an insulating layer, a soft film, an upper plate, a cover, an air outlet pipe, a raw material inlet, a high pressure air pump, a heat conducting pipe and a soft membrane biogas tank main body with a supporting shell, which is set between a radiator, a marsh gas tank and a stove with a compression pump and a storage tank.    USE - Used as a methane tank.    ADVANTAGE - The tank has simple structure, and it is economical and light in weight with high efficiency, heat preservation and convenient transportation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the methane tank.
NOVELTY - Producing (M1) gas from biomass involves digestion of manure in at least one fermentation device, where at least a part of the fermentation heat is recovered by shifting thermal energy from a subsequent liquefaction of the gas in a coupled liquefaction device to the fermentation device.    USE - For producing gas from biomass in a dairy farm (claimed).    ADVANTAGE - The method provides combination of small scale biogas liquefaction device with a small scale biogas fermentation device in a very cost-effective manner; is more effective and less lossy compared to the know biomass combined heat and power systems; and provides an integrated energy system for a farmery which effectively uses the animal waste incurred at the farmery.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for device for the production of biogas from a biomass feed stock for conducting the method including at least one fermentation reactor, at least a gas liquefaction device (5) coupled to the reactor and units for transfer of rejected heat from liquefaction of gas into the reactor.    DESCRIPTION OF DRAWING(S) - The figure shows combined fermenting and biogas liquefaction system implemented into a farmery.    Cattle farm (1)    Manure fermenter (2)    Gas heater (3)    Heat mixing device (4)    Liquefaction device (5)    Heat storage (6)    Heat pump (7)    Milk cooling device (8)
NOVELTY - Methanol and hydrogen production oxidation heating system comprises a methanol catalytic oxidation heater (1), a methanol evaporator (12), a methanol hydrogen production device (13), and a methanol oxidation heater air pipeline (2). The methanol evaporator produces hydrogen mixed combustible by combustible gas pipeline (3). The outside of the methanol oxidation heater is provided with heat conducting oil pipeline provided with oil heating device. The heating conducting oil heating device is connected to methanol oxidation heater by conducting oil pipeline in heated methanol reaction system.    USE - Used as a methanol and hydrogen production oxidation heating system.    ADVANTAGE - The system is environmental-friendly, stable and safe.    DETAILED DESCRIPTION - Methanol and hydrogen production oxidation heating system comprises a methanol catalytic oxidation heater (1), a methanol evaporator (12), a methanol hydrogen production device (13), and a methanol oxidation heater air pipeline (2). The methanol evaporator produces hydrogen mixed combustible material by the combustible gas pipeline (3). The outside of the methanol oxidation heater is provided with heat conducting oil pipeline provided with oil heating device. The heating conducting oil heating device is connected to the methanol oxidation heater by conducting oil pipeline within the heated methanol reaction system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the methanol and hydrogen production oxidation heating system.    Methanol catalytic oxidation heater (1)    Methanol oxidation heater air pipeline (2)    Combustible gas pipeline (3)    Methanol evaporator (12)    Methanol hydrogen production device (13)
NOVELTY - An organic wastewater processing apparatus (101) comprises methane fermentation processing tank (10) which performs methane fermentation treatment of organic wastewater (1), reaction tank (20) which performs aerobic-organic process of methane-fermentation-treated water (2), solid-liquid separator which separates liquid mixture (3) in reaction tank into solid and liquid, cover part in methane fermentation processing tank which prevents dissolved methane from diffusing in air, and supply part which supplies methane-fermentation-treated water to reaction tank.    USE - An organic wastewater processing apparatus for sewage and industrial wastewater.    ADVANTAGE - Methane-fermentation-treated water is processed easily without diffusing methane gas in air, therefore contributing to global-warming countermeasure.    DETAILED DESCRIPTION - An organic wastewater processing apparatus (101) comprises methane fermentation processing tank (10) which performs methane fermentation treatment of organic wastewater (1), reaction tank (20) which performs aerobic-organic process of methane-fermentation-treated water (2), solid-liquid separator which separates liquid mixture (3) in reaction tank into solid and liquid, cover part in methane fermentation processing tank which prevents dissolved methane from diffusing in air, and supply part which supplies methane-fermentation-treated water to reaction tank, maintaining the state in which dissolved methane is prevented from being diffused in air. An INDEPENDENT CLAIM is included for organic wastewater processing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of an organic wastewater processing apparatus. (Drawing includes non-English language text).    Organic waste water (1)    Methane-fermentation-treated water (2)    Liquid mixture (3)    Methane fermentation processing tank (10)    Reaction tank (20)
NOVELTY - Disclosed are ((E)-5-(4-substituted phenyl)-1,1-bis(methylthio)penta-1,4-dien-3-ones of formula (3), where R1, R2 and R3 are selected from the group consisting of OMe, OCH2Ph, Cl, F, NO2, triazolyl and imidazolyl. The compounds prepared are useful as antileishmanial agent and have shown excellent in vitro results and in vivo tests carried out with hamster models. The synthesis of these compounds is simple, economically feasible, environmentally-friendly and easily processable. Image 0/0
NOVELTY - Disclosed are terpenyl pyrazolidines/pyrazoles of formula (A), where R1, R2, R3 and R4 are selected from the group consisting of OMe, OCH2Ph, Cl, F, and NO2, and the dotted lines indicate the presence of single bond or double bond. The compounds prepared are useful as antileishmanial agents and compounds have shown excellent in vitro/in vivo results. The synthesis of these compounds is simple, economically feasible, environmentally-friendly and easily processable. Image 0/0
NOVELTY - Biofuel is obtained from sesame deoiled cake by thermal pyrolysis. The maximum yield of 58.51% of fuel oil (by weight) was obtained at a temperature of 550 degrees C. This pyrolytic oil is blended with diesel up to 30%, which is used in single cylinder C.I diesel engine. The performance of single cylinder C.I diesel engine is found better with respect to brake specific energy consumption, brake thermal efficiency and emission point of view. It is concluded that up to 30% blending of sesame deoiled cake pyrolytic oil in diesel gives better or comparable performance than that of diesel. Image 0/0
NOVELTY - A monomer (m1) comprising one or more aromatic moieties and at least two amino groups is contacted with formaldehyde or source of methylene, to obtain polymer. Each amino group of monomer (m1) is attached to aromatic moiety.    USE - Formation of polymer e.g. polymeric quaternary ammonium cationic polymer used for fiber, microporous material, adsorbent material, optical sensor, proton exchange membrane for fuel cell, manufacturing catalyst, catalytic material, ion-exchange resin, anion-exchange membrane and separation membrane (all claimed) for separation of carbon dioxide from methane, carbon dioxide from hydrogen, carbon dioxide from nitrogen and oxygen from nitrogen.    ADVANTAGE - The method enables efficient formation of polymer.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) separation membrane;    (2) manufacture of catalyst, which involves contacting metal having catalytic activity with polymer;    (3) catalyst, which comprises polymer and catalytic metal ligated to polymer; and    (4) catalytic material, which has negatively-charged catalyst and polymer.
NOVELTY - Improved grain milling process for the production of ethanol by fermentation, comprises: (a) grinding a whole grain; (b) forming a slurry with water (18) of the ground whole grain; adding one or more enzymes to the slurry with heating to liquefy fermentable components of the ground whole grain and produce a mash (24); (c) separating out an oil product stream (28) from the mash; (d) adding an enzyme (22) to the deoiled mash to form a fermentation medium for producing ethanol; and (e) fermenting the fermentation medium in the presence of yeast and one or more added enzymes.    USE - The process is useful for the production of ethanol. The oil product stream is useful as an animal feed for producing biodiesel (claimed). The ethanol is useful as fuel additive.    DETAILED DESCRIPTION - Improved grain milling process for the production of ethanol by fermentation, comprises: (a) grinding a whole grain, (b) forming a slurry with water of the ground whole grain, (c) adding one or more enzymes to the slurry with heating to liquefy fermentable components of the ground whole grain and produce a mash, (d) separating out an oil product stream from the mash, (e) adding an enzyme to the deoiled mash to form a fermentation medium for producing ethanol and (f) fermenting the fermentation medium in the presence of yeast and one or more added enzymes; or carrying out the steps (a), (b) and (c) as above per se; adding an enzyme to the mash to form a fermentation medium for producing ethanol; separating out an oil product stream from the fermentation medium; and fermenting the deoiled fermentation medium in the presence of yeast and one or more added enzymes.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of improved grain milling process for producing ethanol.    Ground corn stream (16)    Water (18)    Enzyme (22)    Mash (24)    Oil product stream. (28)
NOVELTY - A solid fuel is obtained by compression molding mixture of wood fragment (A) with size of 1-50 mm, paper fragment (B) with size of 1-50 mm, binder (C1), form retaining agent (C2), and calorie augmentation agent (D). The total amount of the components (A,B) is 15-45 parts weight with respect to 100 parts weight of the mixture. The weight ratio of the components (A,B) is 20:80-80:20. The total amount of the components (C-1,C-2,D) is 55-85 parts weight.    USE - Solid fuel used for thermal power generation (claimed).    ADVANTAGE - The solid fuel does not produce toxic gas or residue after combustion.
NOVELTY - Method of producing product, involves growing algae in a medium containing biocide and adjuvant, where the biocide and the adjuvant control grazer population, harvesting the algae, and producing the product from the harvested algae.    USE - The method is useful for producing product chosen from biofuel, nutraceutical and pharmaceutical product (all claimed), agar, alginic acid, carrageenan, fuels, alkenes, lubricants, sulfur or sulfuric acid, bulk tar, asphalt, petroleum coke, paraffin wax, aromatic petrochemicals, food, fertilizer, bioplastics, dyes, colorants and chemical feedstock.    ADVANTAGE - The methoprene is non-toxic to humans and animals as it rapidly degrades in sunlight.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) aquaculture medium for promoting algae growth comprising 0.01-5% of biocide and 0.01-5% of surfactant; and    (2) open pond aquaculture system for producing biofuel, comprising algae with chlorophyll concentration of at least 300 mu g/l, biocide for controlling grazer population, and adjuvant for increasing the biocide's ability to control the grazer population.
NOVELTY - Cellulose hydrolyzing composition comprises a material containing cellulose and lignin, an aqueous solution comprising a divalent metal that increases enzymatic cellulose hydrolysis as compared to enzymatic cellulose hydrolysis in the absence of such a divalent metal, and a cellulase.    USE - The composition is useful: for cellulose hydrolysis for the production of biofuel (all claimed) including alcohols (e.g. ethanol, methanol, propanol, and butanol), solvents (acetone), and their blends.    ADVANTAGE - The composition: reduces or eliminates inhibitive processes in enzymatic hydrolysis of lignocelluloses by preventing non-productive adsorption of enzymes onto compounds in enzyme and lignocellulose substrate; and utilizes divalent metal, which allows elimination of substrate washing, thus saving water or reducing enzyme loading while achieving excellent enzymatic saccharification, and thus cost effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for cellulose hydrolysis, comprising (a) providing a cellulose hydrolyzing composition, and (b) treating the cellulose hydrolyzing composition under conditions which hydrolyze cellulose, thus hydrolyzing the cellulose in the material.
NOVELTY - A hydrogen generating apparatus comprises cylindrical inner pipe (3), cylindrical outer pipe (2) with helical groove part (20) arranged coaxially on outer side of inner pipe and depressed in direction of inner pipe, catalyst layer (24) arranged to cylindrical space (27) formed between inner and outer pipes, heater (6, 25) arranged on helical groove part of outer pipe and heats catalyst layer, and heat insulating material (19, 26) arranged on outer side of outer pipe, wherein outer periphery position (6A) of heater is below outer-diameter position (2A) of outer pipe.    USE - A hydrogen generating apparatus for catalytic reaction apparatuses and fuel cell system.    ADVANTAGE - Heat release is reduced, heat conduction is improved, hydrogen generation time is shortened, and thermal efficiency and electric power generation efficiency are improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional diagram of the principal part of a hydrogen generating apparatus. (Drawing includes non-English language text).    Cylindrical outer pipe (2)    Cylindrical inner pipe (3)    Heater (6, 25)    Heat insulating material (19, 26)    Helical groove part (20)
NOVELTY - A hydrogen generating apparatus has a modification portion (4A) for reacting a hydrocarbon raw material and water vapor, and producing a hydrogen-containing gas, and an evaporation portion (12) for evaporating water and supplying to modification portion. The evaporation portion has an evaporation passage provided in annular ring portion between inner cylinder (13) and outer cylinder (14), and a deformation unit for changing cross sectional shape of evaporation passage (16) in vicinity, provided inside the passage.    USE - Apparatus for generating hydrogen used for fuel cell power generating device.    ADVANTAGE - The hydrogen generating apparatus has simple structure. The obstruction of evaporation portion by precipitation of silica is prevented, even the apparatus is installed in area using water with high silica component concentration for long period of time.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of hydrogen generating apparatus. (Drawing includes non-English language text)    Modification portion (4A)    Evaporation portion (12)    Inner cylinder (13)    Outer cylinder (14)    Evaporation passage (16)
NOVELTY - A hydrogen generating apparatus comprises modification part (1) which produces hydrogen-containing reformed gas for steam reforming reaction with source gas and water vapor and selective-oxidation part (3) which reduces carbon monoxide (CO) in reformed gas with air from selective-oxidation air supply apparatus (6), wherein hydrogen generating apparatus produces more 1st air quantity from selective-oxidation air supply apparatus in starting process before total operating hour or total operation time of hydrogen generating apparatus exceeds 1st predetermined time and a fixed number of times.    USE - A hydrogen generating apparatus for fuel cell system (claimed), combustor, turbines, and engines.    ADVANTAGE - Favorable temperature of catalyst is achieved, and CO in generated gas is reduced stably.    DETAILED DESCRIPTION - A hydrogen generating apparatus comprises modification part (1) which produces hydrogen-containing reformed gas for steam reforming reaction with source gas and water vapor and selective-oxidation part (3) which reduces carbon monoxide (CO) in reformed gas with air from selective-oxidation air supply apparatus (6), wherein hydrogen generating apparatus produces more 1st air quantity from selective-oxidation air supply apparatus in starting process before total operating hour or total operation time of hydrogen generating apparatus exceeds 1st predetermined time and a fixed number of times. After 1st predetermined time or 1st fixed number of time, control part (10) sets more 2nd air quantity than 1st air quantity. An INDEPENDENT CLAIM is included for fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a hydrogen generating apparatus. (Drawing includes non-English language text).    Modification part (1)    Selective-oxidation part (3)    Selective-oxidation air supply apparatus (6)    Control part (10)    Modification temperature detection part (11)
NOVELTY - The electrolyzer (10) has a cathode side separator (36) which is arranged facing towards the cathode side electric power feeding portion (42) and the water is electrolyzed where the pressure of hydrogen is higher than the generated oxygen. A plate unit (44) is laminated by cathode side electric power feeding portion. An elastic unit is arranged between the plate unit and cathode side separator. The load is provided to plate unit at the lamination direction. A porous conductor is molded integrally by thermal spraying through the plate.    USE - High-pressure water electrolyzer.    ADVANTAGE - The need for the parallel-accuracy management can be avoided significantly so that the load can be equalized by the elastic unit. Since the management of parallel accuracy can be simplified, the simplified operation can be attained easily and the cost can be reduced. Since the cathode side electric power feeding portion and plate unit are integrated, the contact resistance can be suppressed and the number of components can be reduced easily.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of the unit cell.    High-pressure water electrolyzer (10)    Anode side separator (34)    Cathode side separator (36)    Cathode side electric power feeding portion (42)    Plate unit (44)
NOVELTY - A fuel cell comprises fuel generation component (1) equipped with discharge surface for discharging fuel of fuel generation component and supply surface to which fuel of fuel electrode is supplied, electrolytic membrane (2), fuel electrode (3), oxidizing agent electrode (4), and fuel cell unit pinchingly supported between fuel electrode and oxidizing agent electrode.    USE - Fuel cell used as solid oxide fuel cell.    ADVANTAGE - The fuel cell has high fuel efficiency and simple structure.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the fuel cell.    Fuel generation component (1)    Electrolytic membrane (2)    Fuel electrode (3)    Oxidizing agent electrode (4)    Separator (5)
NOVELTY - A tilt capable kitchen waste biochemical treatment device comprises a roller support frame comprising a front supporting part and a back support part; a roller supporting frame having a capability to tilt at an angle of 90-180 degrees , a feeding position and a discharging position; a roller set on the front and back support part, and having a working opening, a holding part, an opening cover and a rotating center shaft; and a driving control module for controlling rotating and stopping of the roller.    USE - A tilt capable kitchen waste biochemical treatment device.    ADVANTAGE - The device has simple and convenient design, and is kitchen splash-proof.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a tilt capable kitchen waste biochemical treatment device.
NOVELTY - The cooling medium is water with two coolers each connected to a water inlet and outlet pipe and a condenser. The upper pipe has a water pump for the liquid storage tank and an air outlet pipe. The gas pipe and gas cooler are connected by pipe to the gas-liquid separating tank with a single-connection return pipe. A liquid return pipe and a liquid storage tank with valve of the gas-liquid separating tank have a pressure sensor connected to the control system. The gas-liquid separating tank passes through the air inlet of the flame arrester and flame outlet.    USE - Automated double water-cooled hydrogen-oxygen generator for various industrial purposes.    DETAILED DESCRIPTION - The control system is connected to all these components. The flame outlet comprises an upper filtering tank and a liquid storage tank with a filter electrolyte between tanks. The filter is provided with a liquid filling pipe. An electrolyte filter tank is connected to the liquid storage tank by pipeline with valve and pump. Each group of electrolytic cells and cooler is connected through pipeline in series. The electrolyte filter tank is between the cooler and liquid storage tanks. The cooling medium is water with two coolers each connected to a water inlet and outlet pipe and a condenser. The upper pipe is provided with a water pump for the liquid storage tank and is equipped with an air outlet pipe. The gas pipe and gas cooler are connected by pipe to the gas-liquid separating tank with a single-connection return pipe. A liquid return pipe and a liquid storage tank with valve of the gas-liquid separating tank are provided with a pressure sensor connected to the control system. The gas-liquid separating tank passes through the air inlet of the flame arrester and flame outlet.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram of the water-cooled hydrogen-oxygen generator.
NOVELTY - A gas comprising carbon dioxide is exposed to an aqueous material comprising hydroxide ions and water, and having pH of 8.5 or above, and at least a portion of carbon dioxide is dissolved in the aqueous material. The aqueous material is subjected to an electrical potential in an electrochemical cell, and at least a portion of the hydroxide ions is oxidized to water. The electrical energy requirement for releasing the dissolved carbon dioxide is less than about 350 KJ/mole of carbon dioxide. At least a portion of the dissolved carbon dioxide is released.    USE - Method for generating carbon dioxide used for photo-bioreactors for cultivation of biomass for production of biofuel.    ADVANTAGE - The carbon dioxide is generated at high yield.    DETAILED DESCRIPTION - A gas comprising carbon dioxide is exposed to an aqueous material comprising hydroxide ions and more than 20% of water, and having pH of 8.5 or above, and at least a portion of carbon dioxide is dissolved in the aqueous material. The aqueous material comprising the dissolved carbon dioxide is subjected to an electrical potential in an electrochemical cell, and at least a portion of the hydroxide ions is oxidized to water. The electrochemical cell has a primary electrochemical half-cell, a secondary electrochemical half-cell, and a proton exchange membrane. The electrochemical cell has an electrical energy requirement for releasing the dissolved carbon dioxide as a gas. The electrical energy requirement for releasing the dissolved carbon dioxide is less than about 350 KJ/mole of carbon dioxide. At least a portion of the dissolved carbon dioxide is released.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of carbon dioxide absorber and absorbent regeneration module based on hydrogen concentration electrochemical mechanism.    Absorber (112)    Carbon dioxide bearing stream (114)    Scrubbed gas (115)    Anode half cell (130)    Cathode (162)
NOVELTY - Extracting pork blood protein peptide comprises (a) conducting quarantine inspection of fresh pork blood, cooking, mincing cooked blood block, adding purified water and uniformly stirring; (b) heating, adjusting pH, adding alkaline protease and Flavourzyme (RTM: Protease from Aspergillus oryzae), incubating, maintaining pH of reaction mixture, performing enzymolysis, and heating enzymatic hydrolyzate; (c) adding food grade powdered active carbon, stirring, filtering and removing the active carbon; (d) separating filter liquid, desalting and concentrating; and (e) drying.    USE - The peptide is useful in health care products, food and drugs.    ADVANTAGE - The method produces a highly safe product in a short production cycle, and is economical and environmental-friendly.    DETAILED DESCRIPTION - Extracting pork blood protein peptide, comprises: (a) conducting quarantine inspection of fresh pork blood and providing as a raw material, cooking at 95-98 degrees C for 30-35 minutes, mincing cooked blood block using a mincing machine, adding purified water 5-6 times the weight of raw material and uniformly stirring; (b) heating upto 50-55 degrees C, adjusting pH to 7.8-8.3 by using a food grade sodium hydroxide, adding 1-2% of alkaline protease (20 U/mg) and flavourzyme (0.5-1%) based on the weight of raw material respectively, incubating at 50-55 degrees C, allowing to react for 4-5 hours, maintaining a stable pH of reaction mixture, performing enzymolysis, heating enzymatic hydrolysate at 90-95 degrees C for 10-15 minutes to deactivate the enzymes; (c) adding 1.5-2% of food grade powdered active carbon of the weight of pork blood in the enzymatic hydrolysate to decolor, stirring for 1-1.5 hours, filtering and removing the active carbon to obtain a filter liquid; (d) separating the filter liquid via a nanofiltration membrane separating device; desalting and concentrating; and (e) drying the concentrated liquid.
NOVELTY - The electrolyzer has electrode board (102) which is arranged in electrolytic vessel (100). Electrode board (104) is arranged opposite to electrode board (102). Alternating voltage of high frequency is applied between two electrode boards by voltage control unit (130). Anode plates (106a-106d) for electrolysis are arranged in electrolytic vessel. Cathode plates (108a-108d) for electrolysis are arranged facing the anode plates. Electric current is applied between anode plates and cathode plates by voltage control unit (140).    USE - Electrolyzer for generating hydrogen and oxygen mixed gas supplied for transporting apparatus such as aircraft, boat, ship and other motor vehicles.    ADVANTAGE - The electrolyzer can excellently work in low electric power property without producing noise. Hydrogen and oxygen mixed gas is easily generated with sufficient quantity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for generation method of hydrogen and oxygen mixed gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the electrolyzer for generating oxygen and hydrogen mixed gas.    Electrolytic vessel (100)    Electrode boards (102,104)    Vlotage control units (130,140)    Anode plates for electrolysis (160a-160d)    Cathode plates for electrolysis (18a-180d)
NOVELTY - The unit has porous current collection component in which the porous main portion is included with electroconductive metal powder. Metallic bond is formed between metal powder and plate-shaped base material.    USE - Unit of electrolysis cell for hydrogen manufacturing apparatus (claimed).    ADVANTAGE - Since the current collection component is composed of porous main portion, the spherical metal powders are coupled three dimensionally. Since effective interfacial area becomes large, the reduction of contact resistance is attained and production of hydrogen is improved. Unnecessary surface treatment of gold plating in the hydrogen generation apparatus is avoided. The problem arises in the supply characteristics of alcohol, and in the discharge characteristic of hydrogen generated can be avoided.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for hydrogen manufacturing apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen manufacturing apparatus. (Drawing includes non-English language text)    Porous collector at hydrogan generation side (1)    Porous collector of methanol aqueous solution supply side (2)    Solid polymer electrolyte membrane (3)    Catalyst electrode layer of methanol aqueous solution supply side (4)    Catalyst electrode layer at hydrogen generation side (5)
NOVELTY - Recovering (M1) potassium from waste waters for growing microbes, plants and algae involves: collecting waste waters with potassium content; and/or separating the potassium content from waste waters in a usable form in combination with the separation of several remaining contaminants in a usable form by means of a separation process, where the separated potassium content in combination with the remaining contaminants defines a potash.    USE - For recovering potassium from waste waters for growing microbes, plants and algae (which is useful as food, bio-fuels, and as fertilizer on land crops), and also the recovered potassium is used as fertilizer in agriculture, hydroculture, and aquaculture. Also useful for recovery of oil from wells.    ADVANTAGE - The method addresses the use of waste waters in general and particularly produced water from oil and gas wells in assisting our nation's path to sustainability through expanded use of wastewaters, and produced water from oil and gas wells. Generating a supply of potassium hydroxide from waste waters at or near points of use and with the complete use of the spent potassium hydroxides as fertilizer, following its use in water purification, the net costs of potassium use, including savings in cost of disposal of spent regeneration brine, can be driven down. As a result, both the ecological cost and monetary cost of disposal of the wastes from use of sodium hydroxide are avoided.
NOVELTY - System comprises: at least a hydrogen generator (41); a liquid used by the hydrogen generator to produce hydrogen; and a ceramic (11) that emits infrared at wavelengths covering at least a portion of 3-20 micrometers range, where the infrared emitting ceramic is disposed in contact with or at proximity of the liquid so that the liquid can be excited by the infrared before or during the production of hydrogen.    USE - The system is useful for achieving efficient production of hydrogen (claimed).    ADVANTAGE - The system: is simple; and uses infrared excited electrolyte solution in the hydrogen generator which helps reduce the energy consumption, lowers operating voltage and thus reduces cost of the production of hydrogen.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic illustration of the system with an infrared emitting ceramic immersed in electrolyte solution of a fuel cell.    Infrared emitting ceramic (11)    Anode (21)    Cathode (22)    Liquid electrolyte (32)    Hydrogen generator (41)
NOVELTY - The system has a gas flux measurement tube comprising a flattened outer portion extending longitudinally along the length of the tube. A set of gas collection openings is formed along the length of the flattened outer portion of the tube so as to provide gaseous communication from outside of the tube to the inside of the tube for collecting gas for analysis. A semi permeable membrane covers the openings to allow gas to enter the tube while preventing undesirable fluids and solids entering the tube. A gas analyzer (14) i.e. infrared gas analyzer, analyses the collected gas.    USE - Gas flux measurement system for measuring carbon dioxide flux emitted from soil respiration from grasslands or densely vegetated croplands into the atmosphere. Can also be used for measuring methane and nitrous oxides, and for monitoring small area root and stem gas respiration, respiration from liquid surfaces such as river, lake and ocean surfaces and for monitoring gas flux under snow.    ADVANTAGE - The system provides accurate gas flux measurements that reflect the true natural state of the environment in an economical manner without disturbing or removing the vegetation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for measuring gas flux.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a gas flux measurement system.    Gas analyzer (14)    Closed loop gas flow lines (28-1-28-n)    Flushing unit (40)    Valves (48-50, 54)    Open loop gas flow line (52)
NOVELTY - A photocatalytic semiconductor layer (102) and conductive substrate (101) are provided on semiconductor electrode (120). A counter electrode (103) is electrically connected to semiconductor electrode. An electrolyte (106) is provided in housing (105) to maintain respective electrodes. The through-holes (131,132) are formed in electrodes at corresponding position. A slit shape communicating hole (130) is provided in through-hole and connected with regions (122,123). An isometric ion-exchange film (140) is arranged in communicating hole, to cover communicating hole.    USE - Device for generating hydrogen to fuel cell, used in energy system.    ADVANTAGE - As the structure of hydrogen generation device is simplified, the manufacturing cost of the hydrogen generation device can be reduced. The space of hydrogen generation device can be reduced. Since the photocatalytic semiconductor layer of electrode and sufficient ion for each surface of electrode are supplied, decline in hydrogen-producing efficiency can be suppressed. The freedom degree of hydrogen generation device can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the hydrogen generation device.    Conductive substrate (101)    Photocatalytic semiconductor layer (102)    Counter electrode (103)    Housing (105)    Electrolyte (106)    Semiconductor electrode (120)    Slit shape communicating hole (130)    Isometric ion-exchange film (140)
NOVELTY - Enzymolysis of household waste and reinforcing dark fermentative hydrogen production, comprises (i) dehydrating sludge in urban sewage, placing under anaerobic condition, placing in a fermentation bottle, sealing, performing heat treatment, adding glucose, shaking uniformly, sealing, cultivating and acclimatizing, domesticating and inoculating; (ii) saccharifying the household waste, adding alpha -amylase for enzymolysis, adding glucose amylase; and (iii) combining saccharified household waste and seed sludge, adding water, shaking uniformly, sealing and carrying anaerobic fermentation.    USE - The method is useful hydrogen production.    ADVANTAGE - The method is simple, reduces the fermentation time, improves the hydrogen production rate and is economical.    DETAILED DESCRIPTION - Enzymolysis of household waste and reinforcing dark fermentative hydrogen production, comprises (i) dehydrating sludge in urban sewage after removing the impurity, placing under anaerobic condition for 10 to 20 days, placing in a fermentation bottle, sealing, performing heat treatment, adding glucose and peptone, shaking uniformly, sealing, cultivating and acclimatizing at 50-53 degrees C, domesticating the sludge without producing gas and inoculating; (ii) saccharifying the household waste by heating at 70-80 degrees C, then adding alpha -amylase for enzymolysis, after enzymolysis reducing the temperature to 60 degrees C and adding glucose amylase; and (iii) combining saccharified household waste and seed sludge into the fermentation bottle, adding water to control the solid content at 5-10wt.%, shaking uniformly, sealing, carrying anaerobic fermentation and generating hydrogen at 50 -53 degrees C.
NOVELTY - The device has a pyrolyzing reaction kettle whose lower end is provided with a microwave heating device and gas heating device. An air outlet of the pyrolyzing reaction kettle is connected with a lower end of a gas-solid separator. An air outlet of a voltage stabilizer is connected with a rectifying tower through a pipeline. A top part of the rectifying tower is linked to a condenser. An upper end of a gas-liquid separator is connected with a gas combustion device by the pipeline. The gas-liquid separator is connected with a lower end of a diesel tank.    USE - Biomass raw material direct steam manufacturing device for refining biological diesel oil system of an automobile ship.    ADVANTAGE - The device saves material resources. The device is safe and environment-friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a biomass raw material direct steam manufacturing device.
NOVELTY - The system has a compressor that is connected with the pipeline. A control valve is connected with the de-coloring tank. A gear pump is connected with the flow meter. A filter tank is connected with the finished product tank. The finished product tank is connected with the vacuum buffer tank. A control valve is connected with the vacuum pump.    USE - Impurity removal system used for de-coloring biomass diesel used as fuel of vehicle.    ADVANTAGE - The standard impurities in the biomass diesel can be removed easily, since the filter tank is connected with the finished product tank. Hence de-coloring of the biomass diesel can be achieved and the requirement of the vehicle fuel can be satisfied.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the impurity removal system.
NOVELTY - A nitrogen-containing compound (I), is new.    USE - New nitrogen-containing compound is used for agent for promoting generation of natural gas hydrate and manufacturing natural gas hydrate (all claimed).    ADVANTAGE - The nitrogen-containing compound has excellent natural gas hydrate generation characteristics and gas storage capacity.    DETAILED DESCRIPTION - A nitrogen-containing compound of formula (I), is new.    R1,R2=1-30C alkyl optionally having unsaturated bonds or aromatic ring optionally substituted by fluoro;    M=alkali metal;and    n=0-8.    INDEPENDENT CLAIMS are included for the following:    (1) manufacture of nitrogen-containing compound (I); and    (2) preparation of natural gas hydrate, which involves injecting natural gas to aqueous solution containing nitrogen-containing compound (I) and hydrating mixture.
NOVELTY - Pipelines are conditioned by filling pipeline or its portion with a first aqueous composition including first effective amount of metal ion formate salt, and pressurizing pipeline to test pressure. The first effective amount is sufficient to reduce gas hydrate formation and/or to reduce freezing point of the aqueous composition to a sub-freezing point temperature.    USE - Method for conditioning pipelines.    ADVANTAGE - The metal formate salt solutions have low viscosity, have high density, have low metals corrosivity, are non-volatile, have low solubility in hydrocarbons, are readily biodegradable, have low toxicity, are non-hazardous, have low environmental impact, have freezing point depression property forming water/formate eutectic point mixtures, and have water-structuring and water activity modification property.
NOVELTY - The system has a Fourier transform infrared spectrometer whose infrared light source is provided with sample tanks for transmitting a light signal, where the Fourier transform infrared spectrometer is connected with the sample tanks and a mounting part of a rechargeable battery detector for receiving reflection signal light. An air pump and the Fourier transform infrared spectrometer are supported by a computer control outlet of a multi-reflection sample cell. The Fourier transform infrared spectrometer is arranged between an infrared light source and a light outlet path.    USE - Greenhouse gas measuring system.    ADVANTAGE - The system ensures that the Fourier transform infrared spectrograph measures infrared spectrum, analyzes measured gas and improves measuring precision of carbon dioxide, nitrous oxide and methane greenhouse gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a greenhouse gas measuring method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a greenhouse gas measuring system.'(Drawing includes non-English language text)'
NOVELTY - The device has an inlet switch valve (8) provided with a gasification gas inlet (9). A gasification tar purifier (7) is connected with the inlet switch valve that is connected to an inlet of another gasification tar purifier (14). An outlet switching valve (2) is provided with the latter gasification tar purifier. A compressor is provided with a gasification gas outlet (1). A switching valve (13) is connected with an air pump (12). An oil tar purifier main body is fixed with a lower part of a vibration generator (4). A biomass conductive carbon unit (6) is provided with a graphite electrode.    USE - Biomass conductive carbon forced discharge gasified tar removing device.    ADVANTAGE - The device improves tar removing efficiency, reduces energy consumption and pollution discharge and increases perception of a gas purifying/gasifying process.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a biomass conductive carbon forced discharge gasified tar removing device.    Gasification gas outlet (1)    Outlet switching valve (2)    Vibration generator (4)    Biomass conductive carbon unit (6)    Gasification tar purifiers (7, 14)    Inlet switch valve (8)    Gasification gas inlet (9)    Air pump (12)    Switching valve (13)
NOVELTY - The method involves collecting food waste in crusher (100). The food waster wrapped up in a vacuum with crusher is crushed. The crushed food waste is ejected to inner housing through vent (113). The moisture in the ejected food waste is dried by injecting air through drain hole (133) which is connected to the outer housing (130).    USE - Recycling method of food waste.    ADVANTAGE - The salinity and percentage of water content modulation of the food waste can be facilitated effectively. The generation of the bad smell can be suppressed. The processing efficiency of the food waste can be improved effectively. The moisture of the food waste is dried stably. The food waste can be recycled effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross sectional view of the food waste recycling system.    Crusher (100)    Vent (113)    Outer housing (130)    Drain hole (133)    Drying port (190)
NOVELTY - The method involves mixing obtained gas with purified material, and forming a gas-liquid mixture. The gas-liquid separation is pre-formed on the gas-liquid mixture in the gas-liquid separator. The separated gas phase material stream is transmitted to the downside of the nitrogen washing tower.    USE - Method for performing gas cryogenic separation liquefaction of coal gas.    ADVANTAGE - The gas cryogenic separation liquefaction can be performed efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view explaining the process of performing gas cryogenic separation liquefaction of coal gas. (Drawing includes non-English language text)
NOVELTY - The system has electrolytic cell (1) which is connected with power supply control device (4). A hydrogen cooling structure (5) is connected with hydrogen liquid separating structure (7) that is connected with electrolytic cell. A hydrogen tank (9) is connected with oxygen liquid separating structure (8) and oxygen tank (11). A base rubber plate is provided with flow guide slot. An end plate is provided with power connecting contact. An isolating film is arranged on motherboard.    USE - Water electrolysis system.    ADVANTAGE - The electric energy of the water electrolysis system can be saved efficiently.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for water electrolysis method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of water electrolysis system. (Drawing includes non-English language text)    Electrolytic cell (1)    Power supply control device (4)    Hydrogen cooling structure (5)    Hydrogen liquid separating structure (7)    Oxygen liquid separating structure (8)    Hydrogen tank (9)    Oxygen tank (11)
NOVELTY - The system has a disaster gas parameter look-ahead detection subsystem comprising a remote detection probe, an emitting device i.e. pneumatic emitter, and a display receiving device. A battery component and a control component are equipped in an outer housing. A multi-parameter sensor component sends measured signals to the control component and the display receiving device by wireless transmission. A gas sensor detects methane, carbon monoxide, carbon dioxide and oxygen. The outer housing comprises a battery storage.    USE - Remote detection system for use at a coal mine disaster area environment.    ADVANTAGE - The system is simple in structure, convenient to use and quick in information collection speed. The system enables a rescuer to quickly perform look-ahead detection to light, an image and a disaster gas parameter.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a remote detection system.'(Drawing includes non-English language text)'
NOVELTY - A method for producing hydrogen involves passing hydrogen producing raw material and water into a special ultrasonic device to form nanometer sized material; passing fixed amount of the resulting mixture and nanocompound material into a secondary special ultrasonic device; decomposing and extracting hydrogen and oxygen; passing hydrogen and oxygen through hydrogen pipe and oxygen pipe into a hydrogen and oxygen storage containers. The hydrogen is then fed into notch of internal combustion engine.    USE - For producing hydrogen used for generating electricity particularly for powering internal combustion engine of e.g. vehicles.    ADVANTAGE - The method enables green and clean production of hydrogen which in turn is used to generate electricity, and this serves as an alternative to petrochemical energy hence helping in development of the national economy and preserving the environment. The method has a lost cost, is energy saving and results in zero pollution discharge of carbon dioxide or carbide.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for super power 1.5 thousand kilowatt-hour nano-rare earth generator used to produce hydrogen, comprising a nano-rare earth type stator of a nano-rare earth magnetic rotor, with protection level and structure, as per international company standard 1 type.
NOVELTY - Soft straw, wheat straw and rice hull are crushed under high pressure and high temperature, to obtain rod-type solid material. The obtained rod-type solid material is placed in straw gasification furnace, such that partial combustion of straw is carried out. Generated heat energy carbonizes other straw to obtain carbonized straw containing carbon (40-60 wt.% of dry weight of straw). Obtained carbonized straw is crushed by converter using 800-1000 degrees C steam into granules, to activate pore-formation, then obtained granules are rinsed, dried, and milled, to form activated carbon.    USE - Straw carbonizing method.    ADVANTAGE - The straw carbonizing method is uniformly and economically performed with reduced abrasion to device. The product formed using the method has high carbon density and calorific value, and reduced defective rate.
NOVELTY - The system has a multi-gas detection pipeline connected with a control system and a host and provided with a carbon monoxide (CO) detecting pipe, a carbon dioxide pipeline and an oxygen pipeline. A flow meter and the CO detecting pipeline are provided with a three-way valve and a CO calibration port and connected with a CO probe. Methane (CH4) gas is passed into a pipeline that is provided with a three-way valve and a CH4 calibration port. Oxygen (O2) is passed via the pipeline and provided with an O2 calibration port and connected with an O2 probe.    USE - Explosionproof high temperature environment air detection alarm system.    ADVANTAGE - The system maintains 120 degrees centigrade temperature environment gas after finishing extracting, filtering, cooling and dehydrating processes. The system can reduce gas temperature to normal temperature when four different gas probes solve temperature tolerance problems.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of an explosionproof high temperature environment air detection alarm system. '(Drawing includes non-English language text)'
NOVELTY - The absorption tower (100) has a main unit (110) of hollow barrel. An outlet gas pipe (130) in which the biogas is flowed is formed in one side of the main unit. A filler (140) absorbing the adsorption target is provided in the biogas while forming inside the main unit. The gas gathering tubes (150,160,180) are formed on the main unit. The outlet gas pipe allowing the biogas to pass through is formed in the other side of the main unit to discharge the biogas.    USE - Absorption tower for biogas refining system (claimed).    ADVANTAGE - The component of the biogas can be analyzed easily. The replace period of the filler can be determined efficiently with reduced maintenance cost.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) biogas refining system; and    (2) management method of filler for absorption tower.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of biogas refining system. (Drawing includes non-English language text)    Absorption tower (100)    Main unit (110)    Outlet gas pipe (130)    Filler (140)    Gas gathering tubes (150,160,180)
NOVELTY - The method involves producing several floating sample boxes. The floating boxes are connected by fixing rope is set on water surface, and through hole in box is sealed by soft stopper. The gas in floating sample box is extracted by water cylinder with vacuum bottle as background sample, and sampling time of each box along water flow is recorded. The background sample is collected for each floating sample box. The sample with specific primer of carbondioxide, methane and nitrogen are measured. The greenhouse gas discharge rate of water cylinder is calculated.    USE - Method for measuring temperature of gas in water chamber.    ADVANTAGE - The flowing water chamber is convenient, quick and accurate to collect the greenhouse gas.
NOVELTY - The reactor has drum (2) that is provided with rotating shaft (3). The heating cylinder (1) is fixed on the outer side of drum on rotating shaft, temperature controller (8) and heating cylinder. The oil collecting cylinder is set on heating cylinder. The circulation pump (19) is connected with spray head (13).    USE - Rotating type biomass cracking reactor.    ADVANTAGE - The cracking temperature is reduced by 100-150 degrees C.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the rotating type biomass cracking reactor.(Drawing includes non-English text)    Heating cylinder (1)    Drum (2)    Rotating shaft (3)    Temperature controller (8)    Spray head (13)    Circulation pump (19)
NOVELTY - Preparing catalyst for catalyzing hydrocracking of bio-oil, comprises (i) adding a binder to kaolin ore powder to a prepare plastic solid, drying and roasting the solid to prepare a carrier; and (ii) dipping the carrier obtained in step (i) in a solution containing VI B group metal elements and VIII group metal elements, drying and roasting to obtain a catalyst loaded on the carrier, where metal oxide is taken as active ingredient. The mass percentage content of metal oxide of VI B group metal elements in the catalyst is 4-12% and content of metal oxide of VIII group metal elements is 2-4%.    USE - The catalyst is useful for catalyzing hydrocracking of biomass liquefied oil to improve quality of liquefied oil.    ADVANTAGE - The method is simple and produces a catalyst, which performs hydrocracking and processing of oil to obtain processed bio-oil, where the processed biomass oil has increased hydrogen content, increased heat value, and decreased oxygen content, sulfur content and nitrogen content.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a catalyst prepared by above mentioned method.
NOVELTY - The system has a waste heat boiler that is provided with a heat exchanging pipeline. The heat exchange pipeline is provided with a gas inlet and a gas outlet. An air outlet is connected with a pyrolysis gas pipeline. A waste heat boiler is connected to a heating device through the pyrolysis gas pipeline. An activation device is provided for activating the pyrolysis of biomass carbon residue in the biomass pyrolysis furnace.    USE - Double active carbon production system.    ADVANTAGE - The quality of the active carbon product is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of double active carbon production system.
NOVELTY - Device for preparing modified methanol for vehicle comprises methanol modified material pre-mixing device, methanol storage tank, oil storage tank, combining mixing tank, high pressure air pump and thermostatic water supplying system. The methanol modified material pre-mixing device comprises methanol storage vat and four high speed separation mixers. A methanol modified pre-mixing electromagnetic valve is provided between storage vat and mixers. The high speed separation mixer outlet is connected with the combining mixing tank via modified pre-mixing material adding electromagnetic valve.    USE - The device is useful for mixing various organic and inorganic raw materials.    ADVANTAGE - The device can provide deep processing synthesis under constant temperature conditions, thus producing stable and high quality products.    DETAILED DESCRIPTION - Device for preparing modified methanol for vehicle comprises methanol modified material pre-mixing device, methanol storage tank, oil storage tank, combining mixing tank, high pressure air pump and thermostatic water supplying system. The methanol modified material pre-mixing device comprises methanol storage vat and four high speed separation mixers. A methanol modified pre-mixing electromagnetic valve is provided between storage vat and the mixers. The high speed separation mixer outlet is connected with the combining mixing tank via modified pre-mixing material adding electromagnetic valve. The methanol storage tank and oil storage tank are connected with the combining mixing tank.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the device for preparing modified methanol for vehicle.
NOVELTY - The method involves heating dried biomass material at temperature of 350-450 degrees c. The microwave pyrolysis processing of biomass material is performed at low temperature so as to generate large amount of combustible pyrolysis gas product and solid-phase product. The primary cooling process and decoking dust removing process of combustible pyrolysis gas product are performed. The phase products are separated from rectifying tower so as to form gas-phase product. The primary and secondary heat preservation decoking process of liquid phase product is performed.    USE - Processing method for biomass microwave cracking circulation.    ADVANTAGE - The manufacturing cost of processing device of biomass microwave cracking circulation is reduced. The processing device of biomass microwave cracking circulation can be efficiently utilized.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for processing device of biomass microwave cracking circulation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of processing device of biomass microwave cracking circulation.
NOVELTY - The ball has a protective cover that is made of silica gel, rubber or acrylon is installed in the housing. A data processing device is electrically connected with gas sensor. A wireless sending module is electrically connected with data processing device and lithium battery. The outer surface of split type protective cover is provided with shock absorption suction plate. Several air vents are arranged on the position close to the gas sensor such as methane sensor, carbon oxide sensor, oxygen sensor and sulfureted hydrogen sensor.    USE - Wireless sensing ball for sensing disaster area.    ADVANTAGE - The concentration of environmental parameters such as methane (CH4), carbon dioxide (CO2), carbon monoxide (CO) and oxygen (O2) in the danger area can be sensed easily. The sensed data can be sent effectively to wireless receiving host machine.    DESCRIPTION OF DRAWING(S) - The drawing shows an exploded perspective view of the wireless sensing ball.
NOVELTY - Preparing mixed liquid fuel using biomass, comprises performing catalytic reaction by passing biomass synthetic gas into a reactor filled with catalyst, obtaining a mixture of liquid hydrocarbon and alcohol, dehydrating to obtain the product, where the catalyst is iron-copper-zinc-aluminum-potassium catalyst.    USE - The method is useful for preparing mixed liquid fuel.    ADVANTAGE - The method is economical; involves simple steps; increases the yield; and is suitable for large scale production.
NOVELTY - The method involves selecting kitchen waste after removing bulk material. The raw material concentration is adjusted by adding anaerobic active sludge into methane tank. The mixed raw material is placed into a reactor for synchronizing biogas fermentation and oil separation. The rest waste water is returned to the raw material for adjusting solid mass concentration of the raw material.    USE - Method for separating oil and recycling biogas from kitchen waste.    ADVANTAGE - The process for separating oil and recycling biogas from kitchen waste can be simplified at low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biogas fermenting and coupling oil separating device.    DESCRIPTION OF DRAWING(S) - The drawing shows the block flow diagram illustrating the process for separating oil and recycling biogas from kitchen waste. (Drawing includes non-English language text)
NOVELTY - Synchronous denitrification and dephosphorization of sewage comprises taking anaerobic active sludge as strain source; screening target strain using iron for autotrophic denitrification; pre-treating bio-chemically treated sewage in aerobic nitrifying tank; oxidizing organic matter, organic nitrogen and ammonia nitrogen; leading sewage into denitrification tank; adding iron and denitrification bacteria; operating denitrification pool; continuously stirring; and removing iron phosphate deposit and suspended solid to finish sewage treatment.    USE - Synchronous denitrification and dephosphorization of sewage.    ADVANTAGE - The method introduces elemental iron as electron donor, nitrate as electron acceptor, and combines biological denitrification and chemical dephosphorization, thus realizing synchronous denitrification and dephosphorization.    DETAILED DESCRIPTION - Synchronous denitrification and dephosphorization of sewage comprises taking anaerobic active sludge as strain source; screening target strain using iron for autotrophic denitrification; pre-treating bio-chemically treated sewage in aerobic nitrifying tank; oxidizing organic matter, organic nitrogen and ammonia nitrogen; leading sewage into denitrification tank in which mixed solution is under anaerobic condition; adding iron and denitrification bacteria; intermittently operating denitrification pool during initial operation; continuously stirring when denitrification operation is stable; and setting sedimentation tank behind denitrification pool to remove iron phosphate deposit and suspended solid to finish sewage treatment.
NOVELTY - Preparation of ethanol-diesel emulsifier comprises using grease waste discharged, boiling by wet method to extract grease, reacting grease and methanol to generate fatty acid methyl ester with potassium hydroxide (KOH), and reacting with diethanol amine with KOH to generate diethanolamide type ethanol-diesel emulsifier.    USE - Method for preparing ethanol-diesel emulsifier (claimed).    ADVANTAGE - The emulsifier is clear, has stable performance, and low cost.
NOVELTY - The system has a high-sensitivity gas sense organ, and a chemical absorption device connected through a pipeline. A sample water collector collects redundant sample water that flows into a bulkhead. Sample gas is entered into a gaseous hydrocarbon detection device. An analog-to-digital converter converts a voltage signal into a digital electric signal on a personal computer (PC) after collecting the voltage signal via a chromatogram software. The digital signal is transmitted by a transmitter to a ship, a data real-time display and a storage through an optical cable.    USE - Seawater methane concentration in-situ detection system.    ADVANTAGE - The system can realize submarine in directly detecting methane concentration and provide accurate data, and has high precision and low disturbance.    DETAILED DESCRIPTION - The high-sensitivity gas sense organ is made of tin aluminum as a doping agent, platinum, palladium di chlorine metal oxide semiconductor grain. The system adopts an interference gas purifying aerator that is filled with calcium chloride, alumina, or silica gel.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a seawater methane concentration in-situ detection system.'(Drawing includes non-English language text)'
NOVELTY - Erythroculter ilishaeformis is organically and ecologically cultivated at hilly mountain pool by selecting breeding pool (8 acres) having a water outlet, a bottom flat, silt, pre-determined water depth, oxygen generator and a water pump; fermenting chicken manure; dissolving brown sugar in warm boiled water; pouring effective microorganisms original dew bacteria; seeding E. ilishaeformis; spraying with water; and feeding microorganisms original dew bacteria for 3-4 times/day and brown sugar for 2 times/day.    USE - Method of organic ecological cultivation of E. ilishaeformis at hilly mountain pool.    ADVANTAGE - The method has high efficiency and yield, and is purely organic.    DETAILED DESCRIPTION - E. ilishaeformis is organically and ecologically cultivated at hilly mountain pool by selecting breeding pool (8 acres) having a water outlet, a bottom flat, silt, pre-determined water depth, oxygen generator and a water pump; fermenting chicken manure; dissolving brown sugar in warm boiled water; pouring effective microorganisms original dew bacteria; seeding E. ilishaeformis; spraying with water; feeding microorganisms original dew bacteria for 3-4 times/day and brown sugar for 2 times/day; cultivating for 9 months; transporting to a bigger breeding pool (25 acres) having same set-up with the previous breeding pool; cultivating for 5-6 months; feeding calcium (6 kg/100 mu) during noon during cultivating period; feeding effective microorganisms original dew bacteria for 3-4 times/day during cultivation period; and harvesting.
NOVELTY - Preparation of organic humus, involves pulverizing fresh Camellia and fresh oleander leaves, stirring the mixture uniformly, paving the pulverized materials on ground with thickness of 10-20 cm, diluting fermentation strain, adding pure nitrogen and diluted fermentation strain over the spreaded mixture, adding the mixture into fermentation pool, stacking the mixture, covering the mixture using plastic cloth, composting the mixture for 25-60 days, and naturally drying the product.    USE - The method is useful for preparing organic humus as garden ground cover, and soilless culture matrix (all claimed).    ADVANTAGE - The organic humus has rich nutrition, is environmentally-friendly and cost-effective, can be prepared simply, contains stable raw material source, and low cost, and overcomes problems of forestry waste pollution.    DETAILED DESCRIPTION - Preparation of organic humus, involves (a) pulverizing fresh Camellia having water content of 75-80% and fresh oleander leaves, stirring the mixture uniformly, measuring total carbon content in the mixture by potassium dichromate method, and total nitrogen content by micro-Kjeldahl method, where the ratio of carbon content to nitrogen content is 25-30:1 as standard, and calculating the content of pure nitrogen, (b) paving the pulverized materials on ground with thickness of 10-20 cm, diluting fermentation strain, and adding pure nitrogen and diluted fermentation strain over the spreaded mixture, (c) repeating the step (b), adding the mixture into fermentation pool, stacking the mixture, covering the mixture using plastic cloth, composting the mixture for 25-60 days, and during composting, turning the pile when the temperature reaches 62-64 degrees C, and (d) stopping fermentation, and naturally drying the product.
NOVELTY - Hydrophobic oxygen generating agent comprises plant particles and vermiculite mixture in the weight ratio of 1:1-1.3.    USE - The hydrophobic oxygen generating agent is useful for processing and composting sludge.    ADVANTAGE - The compost has increased permeability and improved fertilizer effect, and can be recycled repeatedly. The vermiculite and clinker can be separated easily. The method can be performed uniformly, and cost-effectively, reduces crushing process of saw dust or straw, and saves labor cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of using the agent, which involves adding sulfur oxygen generating agent, mixture of plant particles and vermiculite in the sludge, adding clinker to the mixture, blending the mixture to obtain thermophilic composite as ferment induction flora, where initial water content of the mixture is 60-70%, diluting the composite in the sludge pipe, adding wooden meal and vermiculite into mixing machine, stirring the mixture, inoculating microbe into the mixture, spraying the mixture uniformly, stirring the mixture uniformly, pouring the mixture into a fermentation tank to stack heaps, composting the mixture for 18-20 days, preferably 10-13 days at 55 degrees C, where turning frequency is 10-30 minutes every 8-12 hours, continuously repeating the process for 10-13 days after stirring the mixture, detecting coliform in the sludge, where the amount of coliform in the sludge is reduced to less than 30 MPN/100 gDM, inactivating roundworm, sieving the sludge, and separating vermiculite particles from the clinker.
NOVELTY - The device has a storage battery utilized to supply power for a vehicle. A voltage transformer is utilized to convert direct current into alternating current. A high-voltage electrode is placed in a medium tube and coaxial with a grounding pole. The grounding pole is tightly and coaxially attached to an outer wall of the medium tube. A dielectric barrier is discharged between the medium tube and the high voltage electrode to generate plasma.    USE - Plasma generating device for purifying nitric oxide in automobile tail gas. Can also be used for purifying nitric oxide in boat tail gas and waste gas of a factory.    ADVANTAGE - The device has wide application range, high reliability and strong portability, and is inexpensive and convenient to maintain. The device ensures safety and occupies less space.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a plasma generating device.'(Drawing includes non-English language text)'
NOVELTY - A fully automatic biomass pyrolysis and gasification device comprises a heating furnace (1) having a flue gas residual heat utilization device; a dry distillation kettle (2) set on the heating furnace; a sintering flue device (3); a gas explosion-proof device (4); a tar pyroligneous liquor separating device (5) connected to the dry distillation kettle; and a desulfurizing and dust-removing device connected to the tar pyroligneous liquor separating device.    USE - A fully automatic biomass pyrolysis and gasification device.    ADVANTAGE - The device produces biomass gas having improved quality, and ensures safe production.    DETAILED DESCRIPTION - A fully automatic biomass pyrolysis and gasification device comprises:    (A) a heating furnace (1) having a flue gas residual heat utilization device;    (B) a dry distillation kettle (2) set on the heating furnace;    (C) a sintering flue device (3);    (D) a gas explosion-proof device (4);    (E) a tar pyroligneous liquor separating device (5) connected to the dry distillation kettle;    (F) a desulfurizing and dust-removing device connected to the tar pyroligneous liquor separating device;    (G) a dewatering device connected to the desulfurizing and dust-removing device;    (H) a gas conveying device;    (I) a gas filtering device;    (J) a spraying water washing device;    (K) a plate-type dehydrating device;    (L) a safety water seal arrangement;    (M) a fuel gas leakage detecting device; and    (N) a full-automatic control device.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a fully automatic biomass pyrolysis and gasification device.    Heating furnace (1)    Dry distillation kettle (2)    Sintering flue device (3)    Explosion-proof device (4)    Tar pyroligneous liquor separating device (5)
NOVELTY - A straw carbon gas making device comprises first grade, second grade and third grade condensing filters; a draught fan; a collector; an air outlet; an inner and outer carbonizing pool connected to the condensing filters, and connected to the collector at one end and connected to the draught fan at the other end; and a pure gas outlet connected to the draught fan.    USE - A straw carbon gas making device.    ADVANTAGE - The device reduces carbon gas making cost and labor intensity, and improves the comprehensive utilization method of grass straw and working environment.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a straw carbon gas making device.
NOVELTY - The device has a feeder connected with a gasification furnace. A water washing device is connected with the gasification furnace by a dehydrating device. The dehydrating device is connected with a decoking device and a gas discharging device. The gas discharging device is connected with an acid removing device by a connecting pipe. The decoking device is connected with a safe water sealing device. A high temperature resistant heat-insulated material is arranged on a gasification furnace body. A combustion chamber is arranged on an upper part of a main reaction section part.    USE - Biomass oxidation gasification device.    ADVANTAGE - The device improves biomass gasification efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass oxidation gasification device.
NOVELTY - The gasification plant has a biomass unit which is provided to subject biomass to gasification in a down-flow gasifier and a generation unit is provided to generate gas flow through gasifier. A filter unit (8) is provided to remove particulate material from gas flow in gasifier. The filter unit has a chamber that is divided into an inlet zone (23) and an outlet zone (24) by divider plate that supports multiple hollow ceramic filter candles (20), where each ceramic filter candle is provided with gas-permeable steel fiber filter pad (30) in downstream side.    USE - Gasification plant for processing biomass such as straw, bagasse, agricultural waste, waste paper and wood.    ADVANTAGE - The ceramic filter candle is provided with gas-permeable steel fiber filter pad, so that particulate material at the outer surface is blown off and the separated carbon charcoal can be efficiently provided.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross sectional view of gasification plant.    Filter unit (8)    Ceramic filter candle (20)    Inlet zone (23)    Outlet zone (24)    Steel mesh filter pad (30)
NOVELTY - Treating sludge (1), comprises providing at least two electrodes (2) by which an electric field is generated, where the electric field is provided such that water, which is present in the sludge is electrolyzed and hydroxyl radicals are produced.    USE - The method is useful for treating sludge.    ADVANTAGE - The method carries out both dewatering and disinfection of the sludge and also removes heavy metals.    DESCRIPTION OF DRAWING(S) - The drawings 1 and 2 show a schematic representation of an electrochemical treatment of the sludge, preferably bio-sludge and an arrangement of electrodes in an alternating polarization in the form of rakes, respectively.    Sludge (1)    Electrodes (2)    Anode (3)    Cathode (4)    Flow region (8)
NOVELTY - The system (10) acquires electric charge produced, when reflected inside temperature is below reference temperature, and generating fuel cell (20), by electric charge acquisition unit (916). A presumed reaction heat amount which is induced by applying electric charge is calculated. The driving condition at time of generating fuel cell including condition regarding circulation of coolant is determined, from calculated presumed reaction heat amount. The fuel cell is generated according to determined driving condition.    USE - Fuel cell system used in motor vehicle. Can also be used in power supply system of residence or plant, and electric machine apparatus.    ADVANTAGE - The deterioration of the cell can be suppressed, as the inside temperature of the cell can be raised rapidly by the fuel cell system. Since the raise values of the inside temperature required in order to switch the driving condition of the fuel cell to another driving condition is notified outside, the convenience of the system can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of controlling fuel cell system used in motor vehicle.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the fuel cell system. (Drawing includes non-English language text)    Fuel cell system (10)    Fuel cell (20)    Hydrogen supply unit (30)    Air supply unit (50)    Electric charge acquisition unit (916)
NOVELTY - The solid oxide fuel cell has a base material (1) which is formed with electrolyte (202). A first cell (10) has a fuel electrode and an air electrode which are arranged at predetermined intervals on the base material. A second cell (20) has fuel electrode and air electrode which are arranged at predetermined intervals on the electrolyte. The electrolyte is arranged on the insulating layer (201) which is positioned on the base material. The second cell is arranged between the adjoining first cells.    USE - Solid oxide fuel cell for producing electric power.    ADVANTAGE - Obtains high electric power generation output, prevents short circuit, and prevents fall of battery performance since the electrolyte is arranged on the insulating layer which is positioned on the base material while the second cell is arranged between the adjoining first cells.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a connection structure for solid oxide fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the solid oxide fuel cell.    Base material (1)    First cell (10)    Second cell (20)    Insulating layer (201)    Electrolyte (202)
NOVELTY - The burner has a furnace body provided with a boiler water outlet. A water outlet and a water inlet are connected with a water tank. A combustion device comprises a combustion chamber and a gasification reaction chamber. The combustion chamber is connected with a heating pipe that is arranged in the water tank. An automatic temperature control system comprises a temperature sensor. The temperature sensor is connected with a fan of the gasification reaction chamber. An automatic cleaning system is fixed at bottom of the gasification reaction chamber.    USE - Fully automatic burner for a biomass gasification boiler.    ADVANTAGE - The burner has high heat utilization rate and high frequency igniter. The burner utilizes waste as an organic fertilizer, avoids environment pollution and ensures safety.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a fully automatic burner.
NOVELTY - The invention relates to a process for preparing biofuel for Diesel-type engines. According to the invention, the process consists of the transesterification of soy oil with 14...17% methyl alcohol as related to the volume of oil, and sodium hydroxide dissolved in ethyl alcohol, at a temperature of 58...62 degrees C, for 55...65 min, followed by the separation of raw glycerine and alkaline water, next the resulting product is dried and filtered, to result purified biodiesel fuel.
NOVELTY - Treating a feed containing bio-oil, comprises dispersing the feed containing bio-oil in a hydrocarbon type liquid with the aid of a dispersing agent, subjecting the dispersion so obtained to a hydro-reforming step with hydrogen under pressure in the presence of at least one transition metal catalyst and separating the effluent from the hydro-reforming step in an aqueous phase and at least one organic phase containing partially upgraded bio-oil and hydrocarbon type liquid.    USE - The method is useful for treating a feed containing bio-oil by converting liquefied biomass to liquid hydrocarbon biofuels (motor-grade liquid biofuels).    ADVANTAGE - The method: efficiently converts bio-oil to high value hydrocarbon products; minimizes hydrogen consumption; stabilizes the bio-oil so it can be hydrotreated in a refinery without the risk of coke formation that leads to catalyst deactivation and/or reactor plugging; accommodates wide range of biomass-derived liquids, and biomass pyrolysis liquids, that have wide ranges of viscosity, water content and degree of polymerization depending on the feedstock and pyrolysis process; can be implemented with existing reactor technologies; utilizes low-cost and long-lived catalyst; maximize reaction kinetics to reduce required reactor volumes and associated capital and operating costs and maximize throughput/productivity; reduces capital and operating costs by utilizing operating conditions as mild as possible; and provides products which are free of water, thus decreasing the corrosiveness of the product.
NOVELTY - The device has a jig part arranged between an upper plate and a lower plate of a hot press unit. A membrane electrode assembly (MEA) is guided to a lamination position through the plates. A MEA absorbing body is equipped on the lower plate of the hot press unit. A gas diffusion layer (GDL) absorbing body is equipped on an opposite side of the hot press unit. Two gas diffusion layers are arranged on the laminated position. A transport unit is provided in the MEA. A recessed part is arranged on the MEA. A fixing groove is formed on the GDL absorbing body.    USE - Fuel cell manufacturing device.    ADVANTAGE - The device ensures better effect and improves performance and quality of a fuel cell.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a fuel cell manufacturing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a top view of a fuel cell manufacturing device.
NOVELTY - An energy storage and conversion system comprises a first module for blending a first amount of hydrogen generated from electrolysis of water using renewable energy and a second amount of hydrogen extracted from cellulosic plant residue to create an amount of blended hydrogen; a second module for synthesizing anhydrous ammonia using the blended hydrogen from the first module; and a third module for converting anhydrous ammonia to electrical energy.    USE - Energy storage and conversion system.    ADVANTAGE - The system can provide hybrid hub that caters important zero-low carbon products for key industries worldwide. Distributed hybrid hub power generation and green product synthesis sites enhance and stabilize the power grid, provide new energy-dense renewable fuels, open a zero-carbon path for global fertilizer production, create advanced fuels for transportation, and provide high purity products for advanced electronics, all from renewable sources.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of a conceptual design of a fully integrated hybrid hub system.
NOVELTY - The device comprises a feed apparatus (2) for feeding biomaterial to a pressure pipe (3), in which a plunger (4) is guided in such a way that the plunger can be moved back and forth against a pressure lock (5) to the combustion or carburetor chamber (1). The plunger is moved back and forth against the pressure lock, to form a compressed plug (6) comprised of biomaterial, which is sealed against the combustion chamber and periodically advanced towards the combustion chamber.    USE - Device for introducing biomaterial into combustion or carburetor chamber.    ADVANTAGE - A simple, secured and inexpensive device for the fitful introduction of compacted biomaterial in the combustion or carburetor chamber is provided. Pure oxygen is used for the gasification process. Hence the gasification efficiency of the gasifier is improved, and wastage of heat energy can be prevented. The compaction of fuel and pressure lock function is achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the device for introducing biomaterial into combustion or carburetor chamber.    Combustion or carburetor chamber (1)    Feed apparatus (2)    Pressure pipe (3)    Plunger (4)    Pressure lock (5)    Compressed plug (6)
NOVELTY - The device has a raw gas outlet (20) for cooled raw gas released from clinker, and an immersion pipe (3) with a lower section that is formed as a gas distributor bell jar (12) at a coolant bath (14), where the jar is radially extended. The bell jar is formed by a cone-shaped cover surface with a cross-section that is extended downward. The cover surface comprises gas passage openings (12'), which are distributed over circumference of the bell jar. Dimensions of the gas passage openings increase with immersion depth at the coolant bath.    USE - Device for cooling clinker-containing hot gas flow and for separating clinker from the hot gas flow of an entrained flow gasifier system (claimed) of a biomass gasifier.    ADVANTAGE - The dimensions of the gas passage openings increase with the immersion depth at the coolant bath, thus ensuring approximately constant separation of slag and constant gas cooling even during volumetric flow fluctuations of hot gas flow, and hence providing raw gas with quality independent of the amount of gas to large extent.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic side sectional view of a device for immersion quenching of hot gas flow.    Immersion pipe (3)    Gas distributor bell jar (12)    Gas passage openings (12')    Coolant bath (14)    Raw gas outlet (20)
NOVELTY - Torrefaction of biomass, preferably dried digestate in a biogas plant with a cogeneration plant, a combustion engine and digestate drying, comprises introducing digestate after drying into a torrefaction device, heating the dried digestate in the absence of air for few minutes to 300 degrees C, heating the torrefaction device with at least a part of the heat energy from the exhaust gases (11) of internal combustion engine, and using the torrefied digestate emerging from the torrefaction device as fuel.    USE - The method is useful for torrefaction of biomass.    ADVANTAGE - The method provides high-quality fuel from the dried digestate of biogas plant in a cost efficient manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for the device for carrying out the above mentioned method, comprising at least a double-walled, preferably cylindrical tube with driven, preferably concentric rotating screw (2) for conveying the material, where (a) the tube is closed at the axial ends, (b) the tube has at least three openings on the outside, in which a closable opening is present for the material input, a closable opening is present for the material discharge, and an opening is present for the emission of gas, (c) the tube has at least two double casings, in which the outer casing of one double casing (5) has at least two openings comprising an opening for the introduction of the exhaust gases of the combustion engine and an opening for the outlet of the exhaust gas, and (d) the outer casing of the other double casing has at least an inlet (9) and an outlet (10) for a cooling medium.    DESCRIPTION OF DRAWING(S) - The figure 1 shows a schematic representation of the device, preferably constructed as a screw reactor.    Screw (2)    Double casing (5)    Inlet (9)    Outlet (10)    Exhaust gases (11)
NOVELTY - The device has a crushing device (35) for crushing biomasses, and a grinding device (2) for grinding solid fuel. A mixing device mixes the crushed biomasses and the ground solid fuel and provided before lock hoppers (19a, 19b). A dust collector (5) has an input connected with the crushing and grinding devices and a solid-output connected with an input of a container (17). Gas recirculation circuits (8, 11-13) are connected with a gas output of the dust collector and a gas supply line of the crushing and grinding devices. The hoppers have an input connected with an output of the container.    USE - Device for simultaneous processing of solid fuel e.g. petroleum coke, tar and brown or hard coal, and biomasses to produce a mixture.    ADVANTAGE - The design of the device eliminates the need of pre-treatment stages for the biomass, enables simultaneous processing of the solid fuel and biomasses in an efficient manner and achieves optimal mixing ratio of components of a gasification mixture with simple machine effort and optimal utilization of the mixture for gasification while avoiding risk of damage of walls of a gasifier by aggressive gases e.g. hydrochloric acid and hydrosulfuric acid.    DETAILED DESCRIPTION - The container is designed as the mixing device. The crushing device is designed as a granulator or an impact crusher. An INDEPENDENT CLAIM is also included for a method for simultaneous processing of solid fuel and biomasses to produce a mixture.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a device for simultaneous processing of solid fuel and biomasses.    Grinding device (2)    Dust collector (5)    Gas recirculation circuits (8, 11-13)    Container (17)    Lock hoppers (19a, 19b)    Crushing device (35)
NOVELTY - The system has a housing (166), a rotor (216) which is located in the housing and a curved passage (220) is located between the rotor and the housing. An inlet (160) and an outlet (162) are coupled to the curved passage. A solid feed guide (222) is extended across the curved passage and a thermal control path (214) is extended through a portion of the solid feed pump (10).    USE - Thermal management system for solid feed pump used in production of chemicals, fertilizers, substitute natural gas, transportation fuels or hydrogen.    ADVANTAGE - The thermal management system prolongs the life of the components of the solid feed pump so that the downtime of the overall system is reduced and cheaper metals is used in the solid feed pump due to the reduction in heat and active clearance control is provided for critical components of the pump and dew point condensation and gas leakages are prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross sectional view of solid feed pump.    Solid feed pump (10)    Inlet (160)    Outlet (162)    Thermal control path (214)    Rotor (216)    Curved passage (220)    Solid feed guide (222)
NOVELTY - Pig manure treatment system comprises solid-liquid mixing device, medium-temperature anaerobic reactor, desulfurizing device, gas storing device, marsh gas generator, medium-temperature anaerobic reactor, and solid-liquid separating device, which is connected with an outlet of low temperature vacuum concentration device. The biogas outlet of solid-liquid separating device is connected with drying device. The concentrated liquid exit of low temperature vacuum concentration device is connected with the drying device. The medium-temperature anaerobic reactor is provided with heat exchange tube.    USE - Pig manure treatment system.    ADVANTAGE - The system provides no environmental pollution; and has high efficiency and convenient operation.    DETAILED DESCRIPTION - Pig manure treatment system comprises solid-liquid mixing device, medium-temperature anaerobic reactor, desulfurizing device, gas storing device, marsh gas generator, medium-temperature anaerobic reactor, and solid-liquid separating device, which is connected with an outlet of low temperature vacuum concentration device. The biogas outlet of solid-liquid separating device is connected with drying device. The concentrated liquid exit of low temperature vacuum concentration device is connected with the drying device. The medium-temperature anaerobic reactor is provided with heat exchange tube. Water inlet end of the heat exchange tube is connected with water pipe of marsh gas generator. The water outlet end of heat exchange tube is connected with low temperature vacuum concentration device.
NOVELTY - A campus biological resource methane gas producing system comprises toilet sewage pipes of teaching building, dormitory building toilet draining pipeline, bathroom toilet drainage pipeline, canteen toilet sewage pipes, cafeteria food waste drain outlet pipe, sewage drains outlet pipe, and biogas digester port pipeline connected to pressurized gas station pipeline.    USE - Campus biological resource methane gas producing system.    ADVANTAGE - The system can realize comprehensive utilization of resource by changing waste into valuable while saving resource.
NOVELTY - The industrial equipment comprises a vertical reactor sealed on both ends with double peripheral wall comprising thermal insulation. A heating system is also arranged at bottom of the reactor, where an upper outlet is provided for releasing hot gases. A vertical shaft is designed with paddles, which is connected to a motor system.    USE - Industrial equipment for production of alternative fuels from solid waste.
NOVELTY - Method (M1) for fermenting and collecting biomass of heterotrophic microalgae of Schizochytrium species, is disclosed.    USE - The method (M1) is useful for fermenting and collecting biomass of heterotrophic microalgae of Schizochytrium species. The method (M2) is useful for producing biodiesel from biomass. The method (M3) is useful for producing such long-chain unsaturated fatty acids including docosahexaenoic acid (DHA), and diphenylamine (DPA) which is used in functional food for humans and domestic animals (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method (M2) for producing biodiesel from biomass, involves using food plants or oil plants; and    (2) method (M3) for producing such long-chain unsaturated fatty acids including docosahexaenoic acid (DHA), and diphenylamine (DPA) which is used in functional food for humans and domestic animals.
NOVELTY - The apparatus has an input part connected to a fermentation treatment tank that is connected to a cooling unit. A circulating pipe circulates mixed air in the fermentation treatment tank. Inner temperature of the fermentation treatment tank is about 30 to 90 degree centigrade. Condensed water is removed from the fermentation treatment tank. A fermentor is arranged on the fermentation treatment tank. A partition wall is arranged on the fermentor. A stirring unit is combined with the fermentor, and a driving unit is connected to a controller.    USE - Noxious and malodorous gas preventing type food waste disposal apparatus.    ADVANTAGE - The apparatus is environment-friendly, simple in structure and inexpensive. The apparatus prevents generation of noxious and malodorous gas from the fermentation treatment tank.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a noxious and malodorous gas preventing type food waste disposal apparatus.
NOVELTY - The method involves decomposing a hot water vapor obtained at a water vapor heating process (A) by electrolysis into hydrogen and oxygen during water vapor electrolysis process (B). The sensible heats from hydrogen and oxygen which are obtained at water vapor electrolysis process are collected during hydrogen and oxygen sensible-heat collection process (C1,C2). Hydrogen and oxygen which are obtained during water vapor electrolysis process, and sensible heat collected by sensible heat collection process is utilized (G1,G2) by an iron making process.    USE - Method of manufacturing and utilizing hydrogen and oxygen in iron mill for steel making process.    ADVANTAGE - Since the low grade water vapor which is generated in an iron mill is used for manufacturing and utilizing hydrogen and oxygen, the clean hydrogen and oxygen can be manufactured at low cost, and it can contribute to the carbon dioxide reduction and the cost reduction in an iron making process by using hydrogen and oxygen which were manufactured in an iron mill.    DESCRIPTION OF DRAWING(S) - The drawing shows the block flow diagram illustrating the process of manufacturing and utilizing hydrogen and oxygen. (Drawing includes non-English language text)    Step to perform water vapor heating process (A)    Step to perform water vapor electrolysis process (B)    Step to perform oxygen sensible heat collection process (C1)    Step to perform hydrogen sensible heat collection process (C2)    Step to utilize oxygen (G1)    Step to utilize hydrogen (G2)
NOVELTY - The method involves computing permeated water matter flow volume and oxygen flow volume which are discharged from high pressure water electrolyzer (12). The dilution flow volume for permeated water matter and dilution flow volume for oxygen are computed based on permeated water matter flow volume and oxygen flow volume. The dilution flow volume for permeated water matter and dilution flow volume for oxygen are compared, the direction with much flow volume is selected as dilution air flow volume and the dilution air is supplied in gas-liquid separation apparatus (16).    USE - Method for operating water electrolysis system for generating hydrogen and oxygen.    ADVANTAGE - Since the dilution air of the optimum amount is supplied based on the permeated water matter flow volume and oxygen flow volume which are actually discharged from the high-pressure water electrolyzer, the dilution process of permeated water matter and oxygen can be performed efficiently and reliably. The blower is not driven with the fixed output corresponding to maximum hydrogen concentration, so that supply of excess dilution air can be suppressed. The blower is controlled efficiently and reduction of the power consumption of the blower and reduction of noise can be achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the operating method of water electrolysis system. (Drawing includes non-English language text)    Water electrolysis system (10)    High-pressure water electrolyzer (12)    Water circulation apparatus (14)    Gas-liquid separation apparatus (16)    Blower (86)
NOVELTY - The furnace has a burner that supplies heat to a carbonizing chamber. A carbonizing auger is arranged in the carbonizing chamber. The carbonizing auger is provided with feeding and discharging opening portions. Several air guide pipes are provided to guide the combustible gas to the outer portion of the carbonizing chamber formed on the auger wall of the carbonizing auger.    USE - Straw carbonization furnace.    ADVANTAGE - The energy utilization rate of straw carbonization furnace can be improved effectively. The energy consumption of straw carbonization furnace can be reduced. The straw carbonization furnace can be operated efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the straw carbonization furnace.
NOVELTY - A reformation and hydrogen purification system comprises a reformer (102) including a vaporizer coil configured to vaporize a feedstock, and an annular reactor filled with a reforming catalyst reactive with the vaporized feedstock to generate a reformate; a hydrogen purifier (104) configured to produce purified hydrogen and a raffinate from the reformate; an accumulation tank (162) configured to receive the purified hydrogen; and a reduction return line configured to route the purified hydrogen from the accumulation tank to the hydrogen purifier.    USE - Used as a reformation and hydrogen purification system (claimed).    DETAILED DESCRIPTION - A reformation and hydrogen purification system comprises a reformer (102) including a vaporizer coil configured to vaporize a feedstock, and an annular reactor at least partially surrounding the vaporizer coil and filled with a reforming catalyst reactive with the vaporized feedstock to generate a reformate; a hydrogen purifier (104) disposed externally to the reformer and configured to produce purified hydrogen and a raffinate from the reformate; an accumulation tank (162) configured to receive the purified hydrogen; and a reduction return line configured to route the purified hydrogen from the accumulation tank to the hydrogen purifier to provide a reducing atmosphere for one or more surfaces of the hydrogen purifier.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the reformation and hydrogen purification system.    Reformer (102)    Hydrogen purifier (104)    Controller (106)    Heater block (108)    Accumulation tank (162)
NOVELTY - Seawater (7) is electrolyzed, anodic electrolyzed water (7a) and cathodic electrolyzed water (7b) which are generated from the electrolysis of seawater are separated from each other, the pH of the anodic electrolyzed water is adjusted by adding alkaline agent and then carbon dioxide gas is blown into the cathodic electrolyzed water to fix the carbon dioxide gas as carbonate. The pH-adjusted anodic electrolyzed water and the carbonate-fixed cathodic electrolyzed water are joined together and pH is adjusted to pH of seawater to discharge.    USE - Carbon dioxide fixation method.    ADVANTAGE - The method is efficiently carried out.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for carbon dioxide gas-fixing device.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view explaining the carbon dioxide fixation method. (Drawing includes non-English language text)    Electrolytic vessel (1)    Processing tanks (2,3)    Seawater (7)    Anodic electrolyzed water (7a)    Cathodic electrolyzed water (7b)
NOVELTY - An electrolyte composition of matter comprises an aqueous solvent; at least one inorganic salt dissolved in the solvent; and at least one organic acid or its salt, where the acid is soluble in the aqueous solvent and present in a concentration sufficient to support cavitation-assisted electrolytic combustion.    USE - For generating hydrogen gas from water and a hydrocarbon feedstock (claimed) useful in fuel cell.    ADVANTAGE - The matter maximizes the volume and mass of hydrogen produced, and minimizes the energy input, thus minimizing cost of operation; produces hydrogen from water and returning water back to its original form; and generates hydrogen from water in-situ wherever it is needed, thus eliminates the need of dangerous, costly, and hazardous storage and transport issues.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for generating hydrogen gas from water and a hydrocarbon feedstock, involving providing a high-temperature electron-rich aqueous environment, where water is dissociated for reaction with the feedstock and the hydrocarbon is converted to hydrogen gas and carbon dioxide; or creating cavitation within and supplying an external source of electrons to an aqueous electrolyte solution containing a hydrocarbon feedstock thereby producing hydrogen gas and carbon dioxide.
NOVELTY - Production of microalgae biofuel, involves performing fluid storage step which stores fluid including microalgae in culture tub placed in plant indoor and having circulation flow path, consecutively circulating fluid to circulation flow path, controlling the internal space temperature value of the culture tub to internal space temperature value of the plant indoor, and separating the microalgae and microalgae biofuel by fluid separation.    USE - Production of microalgae biofuel.
NOVELTY - The method involves creating a system unifying and standardizing garbage operation of standardizing net. The standardizing net is divided into garbage feed, humus and common garbage according to request. The garbage is classified and collected in bag. The box of full mark of garbage is labeled and sent to garbage sorting center. The garbage is sorted and processed in the garbage sorting center.    USE - Method for processing garbage.    ADVANTAGE - The garbage processing method classifies the garbage for garbage treatment and recycles the garbage for reuse.
NOVELTY - The wetland has a wetland tank whose inner wall is stacked with multiple particles. Filler is arranged in wetland bed portion. The bed portion is planted with vegetable.    USE - Artificial wetland for treatment of rural domestic sewage.    ADVANTAGE - The artificial wetland has simple structure, low cost and wide application range.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the artificial wetland.
NOVELTY - The system has adjusting tank (2) provided with lattice well (1). The adjusting tank is connected with sewage treatment device (4) through sewage lifting pump (3). Sewage treatment device is connected with sludge tank (5) and middle water tank (6). Sludge tank is provided with sludge pump and sludge dewatering machine (8). Middle water tank is connected with pressure pump (9) which is set in sludge tank. Pressure pump is connected with mechanical filter (10) which is connected with biological active carbon tower (11) and backwater reservoir (12).    USE - Integrated domestic sewage treatment system.    ADVANTAGE - The sewage processing can be performed by simple technique. The operation cost can be reduced. The water quality and the removal rate of organic substance can be improved. The static sedimentation effect can be improved. The denitriding and removal of phosphorus can be performed easily.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the integrated domestic sewage treatment system. (Drawing includes non-English language text)    Lattice well (1)    Adjusting tank (2)    Sewage lifting pump (3)    Sewage treatment device (4)    Sludge tank (5)    Middle water tank (6)    Sludge dewatering machine (8)    Pressure pump (9)    Mechanical filter (10)    Biological active carbon tower (11)    Backwater reservoir (12)
NOVELTY - The device has gas liquid solid three phase separator that is placed on upper portion of water tank (1.12). A synchronous denitrification reaction vulcanizing tank wall is provided with annular baffle board (1.7). An anaerobic producing methane pool internal wall is provided with annular baffle board (2.13). The aerobic reaction zone is placed at bottom aeration head (4.6) an containing space is filled with biological filler mass. The upper portion of water tank is provided with drain pipe.    USE - Device for performing synchronous biological denitrifying, devulcanizing, and autotroph denitrifying treatment of pharmaceutical waste water.    ADVANTAGE - The structure of waste water treatment device can be simplified so that cost can be reduced. The production efficiency pf water treatment process can be improved efficiently.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for performing synchronous biological denitrifying, devulcanizing, and autotroph denitrifying treatment of pharmaceutical waste water.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view illustrating the device for performing synchronous biological denitrifying, devulcanizing, and autotroph denitrifying treatment of pharmaceutical waste water.    Water pipe (1.1)    Water tank (1.12)    Annular baffle boards (1.7,2.13)    Methane discharging pipe (2.9)    Bottom aeration head (4.6)
NOVELTY - The method involves performing anaerobic fermentation process. Residual nitrogen and phosphorus compound in water is removed. Purified water is entered into biological filter pool.    USE - Method for treating artificial wetland sewage from rural area.    ADVANTAGE - The operation efficiency and treatment efficiency are increased while operation cost is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for system for treating artificial wetland sewage from rural area.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the system for treating artificial wetland sewage from rural area.
NOVELTY - The fibre-composite film bioreactor (5) has reactor (14) that is connected with water distribution box (1). A water inlet pump and a flow meter (4) are connected with a hollow fibre component (8). A water outlet pump (10)pumps the water. An aeration head (6) is arranged on the bottom. An air pump in the reactor and the air flow meter (9) are connected with liquid level meter (3). The top of the pipe (13) is set at the bottom of the reactor.    USE - Fibre-composite film bioreactor of pig farm waste water treatment device.    ADVANTAGE - The fibre-composite film bioreactor has good decontamination effect and secondary pollution can be avoided.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic structural view of the fibre-composite film bioreactor. (Drawing includes non-English language text)    Water distribution box (1)    Liquid level meter (3)    Flow meter (4)    Aeration head (6)    Fibre component (8)    Air flow meter (9)    Water outlet pump (10)    Pipe (13)    Reactor (14)
NOVELTY - The device has amorphous solar battery component (1) that is connected with direct current-direct current (DC-DC) voltage stabilizing module (2) whose output end is connected with current limiting resistor (3). The current limiting resistor is connected with voltage regulating resistor (5). The voltage regulator tube (6) and J-FET pipe (7) are connected with the amplifier (8). The J-FET pipe is connected with an earth pin.    USE - Hydrogen device.    ADVANTAGE - The effect of hydrogen can be ensured, to realize the purpose of manufacturing solar hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the hydrogen device.    Amorphous solar battery component (1)    DC-DC voltage stabilizing module (2)    Current limiting resistor (3)    Voltage regulating resistor (5)    Voltage regulator tube (6)    J-FET pipe (7)    Amplifier (8)
NOVELTY - The device has electrolysis tank that produces hydrogen and oxygen. The processed hydrogen and oxygen are filled in a gas adjustable balance device (20) which is provided with hydrogen gas cavity (6) and oxygen gas cavity (7) by a film sheet (1). The hydrogen gas cavity is provided with hydrogen inlet (8) and hydrogen outlet (4). The oxygen gas cavity is provided with oxygen inlet (9) and oxygen outlet (5). A bump (10) is provided on the inner wall of the oxygen gas cavity.    USE - Device for producing hydrogen.    ADVANTAGE - The structure of the hydrogen producing device can be greatly simplified. The operation reliability of the hydrogen producing device can be improved.The manufacturing cost of the hydrogen producing device can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of the hydrogen producing device.    Film sheet (1)    Hydrogen outlet (4)    Oxygen outlet (5)    Hydrogen gas cavity (6)    Oxygen gas cavity (7)    Hydrogen inlet (8)    Oxygen inlet (9)    Bump (10)    Gas adjustable balance device (20)
NOVELTY - The gas balancing device (20) has a hollow cavity that is divided into hydrogen gas cavity (6) and oxygen gas cavity (7) by a film sheet (1). The hydrogen gas cavity is provided with hydrogen outlet (4) and hydrogen inlet (8). The oxygen gas cavity is provided with oxygen outlet (5) and oxygen inlet (9). A lug boss (10) is provided on the inner wall of the oxygen gas cavity.    USE - Gas balancing device.    ADVANTAGE - The size of the gas balancing device can be simplified. The pressure balancing effect of the gas balancing device can be improved with balanced spped. The operation reliability of the gas balancing device can be improved. The manufacturing cost of the gas balancing device can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of the gas balancing device.    Film sheet (1)    Hydrogen outlet (4)    Oxygen outlet (5)    Hydrogen gas cavity (6)    Oxygen gas cavity (7)    Hydrogen inlet (8)    Oxygen inlet (9)    Lug boss (10)    Gas balancing device (20)
NOVELTY - The system has a power unit (3) that includes solar generating device (31) and kinetic energy emitting device (32). A rotating unit (4) is provided with rotating shaft (41) for driving kinetic energy emitting device. A hydrogen and oxygen generating unit (5) is provided with a bottle for holding an electrolyte of electrolytic cell. A combustion unit (6) is provided with furnace base (61) which uses hydrogen and oxygen mixed gas to generate heat source gas for heating the flow space (22) in air filtering device to generate ascending air stream, so as to drive a fan (42) to rotate.    USE - Composite power generation system.    ADVANTAGE - The power generating efficiency of the composite power generation system is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the composite power generation system.    Power unit (3)    Rotating unit (4)    Hydrogen and oxygen generating unit (5)    Combustion unit (6)    Flow space (22)    Solar generating device (31)    Kinetic energy emitting device (32)    Rotating shaft (41)    Fan (42)    Furnace base (61)
NOVELTY - The device has outer panel and panel that are tightly connected with each other by clamping the metal plate. A metal frame and metal plate are fixed integrally. The adjacent metal plate is connected with leakage-proof, so that the metal plate, the metal frame and the other metal board hermetically sealed. The electrode plate and the metal are formed between electrolytic baths. The metal plates provide voltage for electrolysis.    USE - Hydrogen electrolysis device.    ADVANTAGE - Since the electrolytic process heat is conducted to the outside of the electrolytic cell by metal frame, the electrolytic efficiency is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows an exploded perspective view of the hydrogen electrolysis device.
NOVELTY - The device has an alloy electrolysis cylinder and titanium platinum electrode. The alloy electrolysis cylinder is comprised with an upper cylinder and a lower cylinder. The titanium platinum electrode is fixedly connected with the cylinder. The upper cylinder and lower cylinder is fixed to a lock. The anode titanium platinum electrode is connected with the inserting type cathode cylinder.    USE - Electrolytic device.    ADVANTAGE - The gas pollution emission can be effectively reduced. The engine power, energy-saving effect and the technical performance can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the electrolytic device.
NOVELTY - Reformer comprises a base (1) in hollow cylindrical form, cylindrical column provided with spiral channel (2), cylinder present on outer surface provided with two ends connected with a spiral feeding pipe (3), inlet and outlet of discharge pipe (4), and feed inlet (31) located at discharge hole (41).    USE - The reformer is useful for decomposing methanol and dimethyl ether for producing carbon monoxide and mixed gas of hydrogen or methane which is used as fuel in industrial burner and appliances.    ADVANTAGE - The device is simple in structure, inexpensive and convenient to operate, and consumes less energy.    DESCRIPTION OF DRAWING(S) - The drawing shows three-dimensional image of the reformer.    Base (1)    Spiral channel (2)    Feeding pipe (3)    Discharge pipe (4)    Feed inlet (31)    Discharge hole (41)
NOVELTY - Nicotinic acid is reacted with dimethyl carbonate in presence of potassium carbonate catalyst, filtered to remove potassium carbonate and other insoluble substances, and decompressed and concentrated to remove the solvent and dimethyl carbonate. The residual solid is dissolved by using hydrochloric acid, and then decompressed to remove solvent, residual solid is dissolved by using anhydrous methanol, filtered, filtrate is concentrated and separated and filtering, to obtain solid. The obtained solid is recrystallized by using ethanol, to obtain trigonelline hydrochloride.    USE - Synthesis of trigonelline hydrochloride.    ADVANTAGE - The method efficiently provides trigonelline hydrochloride without polluting the environment, by simple method.    DETAILED DESCRIPTION - Nicotinic acid is reacted with dimethyl carbonate in presence of potassium carbonate catalyst, filtered to remove potassium carbonate and other insoluble substances, and decompressed and concentrated to remove solvent and dimethyl carbonate. The residual solid is dissolved by using hydrochloric acid (4 mol/L) and pH value is adjusted to 2-3, and then decompressed to remove solvent, residual solid is dissolved by using anhydrous methanol, filtered to remove insoluble substances, filtrate is concentrated and separated and filtering, to obtain solid. The obtained solid is recrystallized by using ethanol, to obtain trigonelline hydrochloride. The molar ratio of nicotinic acid and dimethyl carbonate is 1:1-1:10. The molar ratio of nicotinic acid and potassium carbonate is 1:1-1:5.
NOVELTY - Dry degumming of biodiesel raw material from waste oil, comprises: (i) adding waste oil into a reaction kettle, heating, stirring, evaporating raw material oil until water bubbles are dehydrated on reservoir surface; (ii) cooling dehydrated oil, mixing, adding complex acid of concentrated phosphoric acid and citric acid, removing phospholipids to obtain large granular flocculation; (iii) adding degumming absorbent to raw material oil in the kettle, stirring; and (iv) introducing raw material oil into a filter press, and obtaining filtrate to produce biodiesel raw material.    USE - The method is useful for dry degumming of biodiesel raw material from waste oil.    ADVANTAGE - The method is simple, economical and environmental-friendly; and has high product yield and consumes less energy.    DETAILED DESCRIPTION - Dry degumming of biodiesel raw material from waste oil, comprises: (i) adding waste oil into a reaction kettle, heating at 100-120 degrees C, controlling vacuum degree to 0.075-0.098 MPa, stirring at 100-120 revolutions/minute, evaporating the raw material oil for 30-60 minutes until water bubbles are dehydrated on oil reservoir surface; (ii) cooling dehydrated oil to 95-99 degrees C, rapidly mixing, adding concentrated phosphoric acid and citric acid in a ratio of 2:1 to oil (0.2-1 wt.%), reducing stirring speed to 50-60 revolutions/minute, raising reaction temperature to 100-120 degrees C, reacting for 50-90 minutes, removing phospholipids to obtain large granular flocculation; (iii) adding degumming absorbent (0.5-2 wt.%) to the raw material oil in the reaction kettle, controlling vacuum degree to 0.080-0.098 MPa, at 110-130 degrees C, stirring at 50-70 revolutions/minute for 30-60 minutes; and (iv) introducing raw material oil into a filter press, controlling oil temperature at 70-90 degrees C and a pressure of 0.15-0.45 MPa, and obtaining filtrate after filter pressing to produce biodiesel raw material.
NOVELTY - Device for reducing methanol gasoline saturated vapor pressure comprises a normal pressure fractionating tower with a water bath heating jacket for the basic gasoline in the fractionating tower to produce low boiling point fraction and high boiling point fraction. A gasoline tank is connected to lower part of the fractionating tower through a pipeline for conveying the basal gasoline into the fractionating tower. A water tank is connected to fractionating tower with water bath heating jacket through a circulating pump to form water circulating system.    USE - Used as a device for reducing methanol gasoline saturated vapor pressure.    DETAILED DESCRIPTION - Device for reducing methanol gasoline saturated vapor pressure comprises a normal pressure fractionating tower with a water bath heating jacket for the basic gasoline in the fractionating tower to produce low boiling point fraction and high boiling point fraction. A gasoline tank is connected to lower part of the fractionating tower through a pipeline for conveying the basal gasoline into the fractionating tower. A water tank is connected to fractionating tower with water bath heating jacket through a circulating pump to form water circulating system, and passing heat energy to fractionating tower. A solar heating device is connected to the water tank for heating water medium. A condenser is connected to the top of the fractionating tower for cooling low boiling point distillate, and the cooled low boiling point fraction is stored in the low boiling point fractionate storage tank. A methanol gasoline mixing device is connected to storage tank for collecting high boiling point fractionate from the fractionating tower end, mixing with low proportion methanol gasoline, and conveying the methanol gasoline product.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of the device for reducing methanol gasoline saturated vapor pressure.
NOVELTY - An efficient and reusable natural bone waste based heterogeneous mesoporous catalyst with substantial basicity and surface area and having proper pore size distribution, comprising calcined natural waste animal, particularly chicken bones comprising tricalcium phosphate (TCP, beta-Ca3(PO4)2) as the active phase and a method of manufacturing the same, which when advantageously deployed as a transesterification catalyst in the fuel grade biodiesel synthetic process favors fuel grade biodiesel production from pre-treated (waste)/wild/unrefined vegetable oils with acid number (AN) below 0.5 together with monohydric alcohols. Image 0/0
NOVELTY - Producing mixed higher alcohol blend, comprises: providing an aqueous alcohol stream including mixed lower and higher alcohols (110); removing the lower alcohols from the aqueous alcohol stream, resulting in a total weight of C4+ alcohols greater than or equal to total weight of 3C alcohols in the resultant aqueous alcohol stream (120); and extracting the C3+ higher alcohols from the resultant alcohol stream with a solvent (130).    USE - The process is useful for producing mixed higher alcohol blend, which is used as a fuel comprising automotive fuel.    ADVANTAGE - The process: utilizes less energy during exothermic reaction to drive downstream distillation columns in a cascade mechanism, thus provides a low energy process; does not require separation energy in initial distillation stage prior to extraction, thus allows for overall lower energy separation process; is self contained both composition-wise with regard to specific alcohols and energy-wise; provides 99% of C3 alcohol, less than 1% of C3 alcohol-free aqueous raffinate and less than 0.2 wt.% water content; prevents phase separation behavior, thus results in gasoline-alcohol mixture that is resistant to loss of alcohol in presence of water; and provides simple distillation process for alcohols separation.    DESCRIPTION OF DRAWING(S) - The figure illustrates method of producing mixed higher alcohol blend.    Providing an aqueous alcohol stream including mixed lower and higher alcohols (110)    Removing the lower alcohols and optionally, isopropanol from the aqueous alcohol stream, resulting in a total weight of C4+ alcohols greater than or equal to total weight of 3C alcohols in the resultant aqueous alcohol stream (120)    Extracting the C3+ higher alcohols from the resultant alcohol stream with a solvent (130)
NOVELTY - Treating input coal involves treating the coal in pyrolysis step to form coal char, where the pyrolysis step includes heating coal in absence of oxygen to remove volatile material from coal; treating the volatile material evolved from coal in pyrolysis step to separate volatile material into gases and liquids, where the liquids contain condensed volatile material; directing portion of liquids to coal char, and mixing the returned portion of liquids with coal char, thus returning some of volatile material to coal char; and optionally mixing biomass material with coal char.    USE - For treating input coal (claimed).    ADVANTAGE - The return of liquids to coal char increases volatile content of coal char by 2-10 (preferably 3-6)%. The biomass material has high volatile content, where the addition of biomass material to coal char increases volatile content of coal char by 2-15%. The volatile content of biomass is at least 50% of biomass material. The process improves heating quality and removes certain undesirable constituents of input coal. The addition of biomass material to coal char increases the volatile content of coal char to provide enhanced coal product. The process enables undesirable constituents to be removed from coal, and biomass to be added to coal. The biomass fuel sources have many beneficial characteristics, including reducing greenhouse gas emissions and other pollutants, and improving combustion due to relatively high volatile content of biomass fuels. Further, certain constituents in input coal, such as mercury and sulfur, can be removed from coal while still maintaining suitable levels of volatile material in coal for processing in power generation application. Also, the process generates synthetic crude oil for refining into transportation fuels.
NOVELTY - The reactor has a liquid-cooled cooling screen (3) limiting a gasification chamber (8) and arranged within a pressure cladding (5). The cooling screen comprises a cooling system that acts according to a principle of transpiration refrigeration. The cooling screen comprises a porous layer (6) in which medium is injected by lines aligned on the gasification chamber for realizing transpiration refrigeration. The lines terminate in the porous layer. The porous layer is divided into various heights of the cooling screen into segments of different porosities.    USE - Reactor for gasification of ashless or ash-poor fuel e.g. hydrocarbonaceous gas, organic matter, ash-poor coal, coke, biomass and fractions of waste and residual substances (all claimed) at temperatures upto 1900 degree Celsius and pressures up to 10 mega Pascal.    ADVANTAGE - The cooling screen comprises the cooling system that acts according to the principle of transpiration refrigeration, thus reducing quantities of heat exhausted over the cooling screen and providing cooling screen technology for fuel with small or no ash portion to make an alternative technology with similar small thermal inertia for the fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of an air flow carburetor.    Raw gas stream (1)    Liquid-cooled cooling screen (3)    Pressure cladding (5)    Porous layer (6)    Gasification chamber (8)
NOVELTY - The reactor has a fluid-cooled cooling screen (3) arranged with a pressure shell (5) and limiting a reaction and/or heating gas space (8). Nozzle pins are arranged between windings of the cooling screen and energized by distribution systems i.e. annular pipes (4.1, 4.2). Medium e.g. gas or vapor or water, is directly injected into the space through the nozzle pins. A fire-proof ramming mass (6) is attached on a side of the cooling screen, where the side is turned toward the gasification space. The annular pipes are individually realized to height of the cooling screen.    USE - Reactor i.e. entrained gasifier, for gasification of ashless or ash-poor fuel i.e. hydrocarbonaceous gas, utilized as fractions of petroleum refining or thermal treatment of organic matters ash-poor coals, coke, biomasses and fractions of waste and residual substances (all claimed). Can also be used for refinery and chemical residues such as heavy oils, bitumens, tars and petrol coke and pyrolysis coke.    ADVANTAGE - The cooling screen is used even for fuel with very reduced or small ash proportion, thus providing an entrained gasifier with reduced thermal inertia for the fuel, and preventing gas fixed heat transition from a reaction interior space into an inner wall of reaction space confinement of the entrained gasifier.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an entrained gasifier with a cooling screen and coolant direct injection.    Fluid-cooled cooling screen (3)    Annular pipes (4.1, 4.2)    Pressure shell (5)    Fire-proof ramming mass (6)    Reaction and/or heating gas space (8)
NOVELTY - The solid oxide fuel cell (1) has a second detection unit (111a) which senses a demand power according to an input from a fuel cell controller. An inverter controller (111) is configured to control an inverter (54) independently of a fuel cell controller (110) to extract an electric current from a fuel cell module (2) based on the sensed demand power.    USE - Solid oxide fuel cell for generating variable electric power according to demand power.    ADVANTAGE - Eliminates the need for performing a high-speed control of fuel cell module, and allows simple, efficient, and high-speed control of the inverter.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic block diagram of a solid oxide fuel cell. (Drawing includes non-English language text).    Solid oxide fuel cell (1)    Fuel cell module (2)    Inverter (54)    Fuel cell controller (110)    Inverter controller (111)    Second detection unit (111a)
NOVELTY - The fuel cell (1) has electric current detection unit that detects real extraction electric current that is taken out from fuel cell module (2). A control unit is provided to control the fuel flow volume adjustment unit (38) to reduce the fuel supply amount after the reduction of extraction possible electric current value so that reduction of extraction possible electric current value is tracked. The extraction possible electric current value is made to increase with the electric current raise change rate, when demand power begins is increased in predetermined state.    USE - Solid oxide fuel cell for generating variable electric power.    ADVANTAGE - The extraction possible electric current value can be made to increase quickly and trackability with respect to the change of demand power can be improved by making the operation of the fuel cell module stable.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the solid oxide fuel cell. (Drawing includes non-English language text)    Solid oxide fuel cell (1)    Fuel cell module (2)    Combustion chamber (18)    Fuel flow volume adjustment unit (38)    Control box (52)
NOVELTY - Use of a catalyst system comprising a transesterification catalyst comprising alkali metal- or alkaline earth metal-alkoxides or alkali metal hydroxides, and at least one activator different from the transesterification catalyst, comprising salt-like compounds, titanates or non-salt-like compounds having a density of at least 0.9 g/ml, for catalyzing transesterification reactions, is claimed.    USE - The catalyst system is useful for catalyzing transesterification reactions and preparing fatty acid alkyl esters, which are useful as a component of biodiesel (all claimed).    ADVANTAGE - The catalyst system accelerates the separation of the phases, which facilitates the work-up considerably and increases the space-time yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing fatty acid alkyl esters, comprising transesterifying at least one mono-, di- or triglyceride in the presence of at least one monohydric alcohol.
NOVELTY - The furnace has a furnace body (6) provided with a feeding device (3) and an ash cleaning device (5), where the furnace body is connected with a fuel chamber and a furnace cavity. A feeding port (2) of the fuel chamber is completely sealed to avoid returning smoke. An upper part of the furnace body is connected with a water tank. An inner side of the water tank is connected with a water tank separating plate that is inclined downward. Heat is returned to an end part of the water tank to repeatedly utilize the heat and to improve heat absorbing efficiency of the water tank.    USE - Biomass gasification furnace.    ADVANTAGE - The furnace utilizes biomass fuel to generate combustion gas for daily use, and is clean, environment-friendly and energy-saving.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a biomass gasification furnace.    Opening (1)    Feeding port (2)    Feeding device (3)    Ash cleaning device (5)    Furnace body (6)
NOVELTY - The furnace has a furnace core (2) located in a furnace body (1) that is connected with a chimney (3) and a lower part dust hopper (4). The furnace core is provided with inner and outer walls to form an annular chamber (6). An upper part of the inner wall is provided with a through hole (2a). The annular chamber is opened with a vent hole. A side wall of the furnace body is provided with a material inlet (8). A bottom part of the furnace core is provided with a stirring mechanism. The stirring mechanism is provided with a stirring rod, a stirring bar and a fixed support bar.    USE - Biomass gasification furnace.    ADVANTAGE - The furnace is simple in structure and design and environment-friendly, and avoids discharge of black smoke, saves fuel and energy and prevents fire accident.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a biomass gasification furnace.    Furnace body (1)    Furnace core (2)    Through hole (2a)    Chimney (3)    Lower part dust hopper (4)    Annular chamber (6)    Material inlet (8)
NOVELTY - Treating animal waste, comprises applying quebracho tannins onto animal waste to elicit at least one effect comprising (a) reducing total gas emissions, (b) reducing hydrogen sulfide emissions, (c) reducing methane emissions, (d) reducing populations of anaerobic sulfate reducing bacteria, and (e) reducing the metabolic activity of anaerobic sulfate reducing bacteria.    USE - The method is useful for treating animal waste including feces and fecal waste containing materials, and urine, where the animal waste is substantially solid, and the animal waste is from swine, bovine, fowl, equine, caprine, ovine, feline, canine, rodentia, leporids, mustelids and zoo animals (all claimed).    ADVANTAGE - The method is cost effective and environmentally friendly. The method reduces offensive odors generated from animal wastes.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for reducing odor emissions from animal waste comprising combining quebracho tannins with animal litter, and applying the litter in the locus of an animal to receive animal waste discharged.
NOVELTY - The gasifier has a combustion chamber provided with an inner cavity and an air outlet. The combustion chamber is connected with a feed pipe. An inner wall of the feed pipe is tangent to an inner wall of the combustion chamber. The combustion chamber is provided with a through hole and connected with a steam pipe. An inner wall of the through hole is tangent to the inner wall of the combustion chamber. A steam is tangentially fed into the combustion chamber by the through hole and gasified with reactant generated by biomass fuel combustion to obtain heat biomass fuel gas.    USE - Biomass cyclone air-steam gasifier.    ADVANTAGE - The gasifier ensures that the gasified biomass fuel gas has higher heat value for about 1800 to 2000 Kcal/N m3, which is improved by 30 to 40 percent and output rate improved by 20 percent.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a biomass cyclone air-steam gasifier in partial section.
NOVELTY - The gasifier has a combustion chamber connected with a steam pipeline. A high temperature vapor input is inserted into the combustion chamber that passes through the steam pipeline, and generates gasification reaction with reactant. An inlet of the steam pipeline is connected with a steam distributor. The steam distributor distributes a steam to each steam pipeline quantificationally. The steam distributor is formed as a structured pipeline. Each steam pipeline is provided with a stop valve and a pressure gauge.    USE - Biomass air-steam gasifier.    ADVANTAGE - The gasifier ensures gasifying biomass fuel pyrogenation after burning, and is utilized for gasifying a biomass gas heat value so as to improve heat value by 30-40 percentages. The gasifier ensures that gas yield is increased by 20 percent.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial sectional view of a biomass air-steam gasifier.
NOVELTY - The method involves performing purifying biomass fuel gas during gasification reaction. Redundant gas pressure is dispersed. Discharged unburned fuel is correspondingly measured. Air in a combustion chamber is provided with a biomass gasifier. Biomass fuel reactant is burned in temperature of 750 to 1000 degrees centigrade under normal pressure or pressure condition. 0.2 to 120 to 160 degrees centigrade of a steam and the biomass fuel reactant of 0.8 MPa is added during the gasification reaction, and the biomass fuel gas is produced.    USE - Biomass air-steam gasification method.    ADVANTAGE - The method enables introducing biomass fuel pyrolysis reaction generated by the steam and preparing biomass fuel gas heat value, so that the heat value is improved by 30-40 percent and gas yield is increased by 20 percent.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic illustration of a biomass air-steam gasification method.
NOVELTY - The method involves aerating air to a combustion room of a biomass gasifier to burn steam/biomass fuel under micro-normal pressure for producing reactant, where temperature in the biomass gasifier reaches up to 750 to 1000. The reactant is utilized in a gasification reaction process. Biomass fuel gas is generated after the gasification reaction process, where mass ratio of the steam/biomass fuel is about 0 to 1.5 and air equivalence ratio of the steam/biomass fuel is about 0.19 to 0.27. Dolomite, olivine and two aluminum oxides are added as catalyst in the gasification reaction process.    USE - Biomass air-steam gasification method.    ADVANTAGE - The method enables generating a biomass fuel pyrolysis reaction process by increasing steam during the gasification reaction process, thus improving a biomass fuel gas heat value by 30-40 percent and gas yield by 20 percent.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic illustration of a biomass air-steam gasification method.
NOVELTY - The system has a hoisting machine discharging biomass fuel. A storage bin stores and conditions the biomass fuel. A spiral conveyor quantitatively conveys the biomass fuel. A gasifier prepares composition material gas. A cyclone separator separates biomass gas mixed with unburned particle and impurity. A device releases over-voltage of the biomass gas. A blower is connected with an air gasifier. A combustion chamber of the gasifier is connected with a steam boiler via a steam pipeline. The biomass fuel is injected into the combustion chamber through the steam pipeline.    USE - Biomass air-vapor gasification system for a vehicle (claimed).    ADVANTAGE - The system improves biomass heat values by 30 to 40 percent and gas yield rate by 20 percent.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass air-vapor gasification system.
NOVELTY - The device has a heat preservation layer whose outer surface layer is coated with a layer cylinder. An outer cylinder and an insulating layer form a cooling chamber, where a wall of the insulating layer includes a feeding port. The feeding port is connected with a combustion chamber. The insulating layer is provided with a through hole, where the through-hole is connected with the combustion chamber. A steam input passes to the combustion chamber from the through hole, and is mixed with biomass material to burn pyrolysis and reacted with gasification reaction to generate biomass gas.    USE - Biomass water-cooled air-steam gasifying device.    ADVANTAGE - The device improves a heat value by 30 percent to 40 percent and gas yield to about 20 percent.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a biomass water-cooled air-steam gasifying device.
NOVELTY - The unit has an electrode support stand accommodated with rhombic-shaped part. Anode and cathode ray parts are provided with a gap. A saw blade is provided with a needle bed. The cathode ray part is connected to a rhombic electrode. Inner side of an aluminum wire netting is provided with a voltage output beam by anode and cathode rays. A plasma production power module is provided with a direct current (DC) voltage at an input power voltage of 6 volts and output voltage of 8 kilovolts. Width of the electrode support stand is 6 cm. Length of the electrode support stand is 1 cm.    USE - Gad-cross hair low temperature plasma reaction unit for an air purifier.    ADVANTAGE - The unit has low power consumption, and is convenient to use. The unit reduces production cost, and improves productivity. The unit reduces outdoor air, wastage of energy and poisonous gas of the air purifier.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a gad-cross hair low temperature plasma reaction unit.
NOVELTY - Converting microbial lipids from an oleaginous microbial biomass into fatty acid alcohol esters without prior extraction of the lipids from the biomass, comprises contacting an acid catalyst, an alcohol, and an oleaginous microbial biomass containing microbial lipids under sufficient conditions and for a sufficient period of time for in situ transesterification of at least some microbial lipids to their corresponding fatty acid alcohol ester.    USE - The method is useful for producing biodiesel fuel or fatty acid alcohol ester component (claimed).    ADVANTAGE - The method provides biodiesel fuel or fatty acid alcohol ester components with improved purity, quality and reproducibility.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a biodiesel fuel or its fatty acid alcohol ester component produced by the method.
NOVELTY - Preparing repaglinide or its salt, comprises reacting (S)-3-methyl-1-(2-piperidinophenyl)-1-butylamine or its salt with a protected carboxylic acid in the presence of a dehydrating agent and a suitable solvent to produce pure acid compound (II) or its salt, and deprotecting obtained (II) to obtain 2-(3-ethoxy-4-formyl-phenyl)-N-((S)-3-methyl-1-(2-piperidin-1-yl-phenyl)-butyl)-acetamide compound (I) or its salt, where the dehydrating agent is boric acid and/or a boric acid derivative.    USE - The repaglinide is useful in the management of type 2 diabetes mellitus.    ADVANTAGE - The process provides repaglinide with high yield and purity (99%) in an economical, non-hazardous and environmentally friendly manner.    DETAILED DESCRIPTION - Preparing repaglinide or its salt, comprises reacting (S)-3-methyl-1-(2-piperidinophenyl)-1-butylamine or its salt with a protected carboxylic acid in the presence of a dehydrating agent and a suitable solvent to produce pure acid compound of formula (II) or its salt, and deprotecting obtained (II) to obtain 2-(3-ethoxy-4-formyl-phenyl)-N-((S)-3-methyl-1-(2-piperidin-1-yl-phenyl)-butyl)-acetamide compound of formula (I) or its salt, where the dehydrating agent is boric acid and/or a boric acid derivative.    R = methyl, ethyl (preferred), tert-butyl, benzyl, p-nitrobenzyl, or p-methoxybenzyl.
NOVELTY - Isolated polypeptide having xylose reductase activity but negligible arabinose activity, where the polypeptide has at least 60% identity to the amino acid sequence of SEQ ID No.2 or SEQ ID No.4, is new, where Sequences not defined here may be found at ftp://ftp.wipo.int/pub/published_pct_sequences/publication .    USE - The polypeptide, the nucleotide sequence, the vector and the host cell are useful for the production of fuels, bulk chemicals and platform chemicals from lignocellulosic feedstock (claimed), where chemicals are ethanol, butanol, isobutanol, lactate, 1,4-diacids (succinate, fumaric, malic), glycerol, sorbitol, mannitol, L-ascorbic acid, xylitol, hydrogen gas, 2,5-furan dicarboxylic acid, 3-hydroxy propionic acid, aspartic acid, glutaric acid, glutamic acid, itaconic acid, levulinic acid, and 3-hydroxybutyrolactone, fatty acids, fatty-derived molecules, isoprenoids, isoprenoid-derived molecules, alkanes, isopentanol and isoamylacetate.    ADVANTAGE - The polypeptide has the ability to reduce a number of compounds. The polypeptide improves xylose and/or arabinose conversion in host cells and host cell harbouring one or both of the enzymes/polypeptides. The polypeptide has minimized/negligible activity towards arabinose. The polypeptides enable a more efficient utilization of xylose and/or arabinose, which results in higher yield and/or productivity of the specific product (gram product per gram substrate), which is achieved due to reduction of by-product formation, such as arabitol formation.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a nucleotide sequence encoding the polypeptide;    (2) a vector comprising the nucleotide sequence; and    (3) a host cell comprising the nucleotide sequence or the vector.
NOVELTY - Acidification of manure by using acidic transportable flow of an anaerobic digestion device and/or a flow of sulfuric and/or sulfurous acid from a device that removes hydrogen sulfide gas from biogas, comprises: retrieving at least a part of the flow that is in any phase of a digestion process and/or a part of the flow, from the device and/or retrieving sulfuric and/or sulfurous acid from the device that removes hydrogen sulfide gas from biogas from the anaerobic digestion device by chemical and/or biological oxidation to sulfuric acid; and transporting the acidic flows to the manure.    USE - The method is useful for the acidification of manure by using acidic transportable flow of an anaerobic digestion device and/or a flow of sulfuric and/or sulfurous acid from a device that removes hydrogen sulfide gas from biogas.    ADVANTAGE - The method significantly reduces emissions of methane gas and ammonia gas from the manure. In the method: the part of ammonia that would be emitted as a gas is stored as a nitrogen mineral in the digested manure for use as fertilizer; and the manure has a pH value that is more preferable for digestion processes.
NOVELTY - The hybrid hydrogen oxygen (HHO) generator or electrically controlled electrolyzer comprises an electrically conductive stainless steel or metal grid composite plate. The generator is controlled by an increased voltage and variable current intensity, and produces an optimal amount of HHO.    USE - The hybrid hydrogen oxygen generator or electrically controlled electrolyzer is useful for internal combustion engines.    ADVANTAGE - The hybrid hydrogen oxygen generator or electrically controlled electrolyzer saves the fuel such as diesel and petrol in the combustion engines with high efficiency and without any environmental impacts.
NOVELTY - Gasification catalyst of lignin, is obtained by adding high surface area graphite to ruthenium metal to obtain graphite carrying ruthenium catalyst.    USE - The gasification catalyst is useful for converting lignin into fuel gas (claimed) e.g. methane and hydrogen.    ADVANTAGE - The gasification catalyst has high selectivity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for preparing the gasification catalyst, involves impregnating graphite in ruthenium salt water solution, drying the solution to evaporate water, and reducing ruthenium salt under hydrogen air flow atmosphere; and    (2) fuel gasification method of lignin, involves converting lignin (main component of wood type biomass) in supercritical water into fuel gas using the graphite carrying ruthenium catalyst.
NOVELTY - An optical hydrolyzable-electrode (100) comprises collector electrode (10), p-type semiconductor (20), zinc sulfide as n-type semiconductor (30) and reaction co-catalyst (40), in order. The p-type semiconductor is copper, gallium and/or chalcogen element.    USE - Electrode is used for optical hydrolyzing for optical water-splitting reaction used for producing hydrogen.    ADVANTAGE - The electrode is manufactured efficiently without using indium metal.    DETAILED DESCRIPTION - An optical hydrolyzable-electrode comprises collector electrode, p-type semiconductor, n-type semiconductor and reaction co-catalyst, in order. The p-type semiconductor is copper, gallium and/or chalcogen element. The ratio of content of gallium to copper in p-type semiconductor is calculated by formula: 2+3v, where v is 0.5-2. The ratio of content of chalcogen element to content of copper is calculated by formula: 2+3v. INDEPENDENT CLAIMS are included for the following:    (1) manufacture of optical-hydrolyzable electrode; and    (2) hydrolyzing method of electrode, which involves immersing electrode in electrolyte solution and then irradiating using light.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic structure of electrode.    Collector electrode (10)    P-type semiconductor (20)    N-type semiconductor (30)    Reaction co-catalyst (40)    Electrode (100)
NOVELTY - An electrode is obtained by depositing a platinum group metal on a conductive substrate by carrying out electrolysis using an electroconductive base material (2) as a cathode, platinum group metal as an anode (3), and an inorganic acid aqueous solution as electrolyte solution (4).    USE - Manufacture of electrode (claimed) for use in production of hydrogen used as fuel in fuel cells.    ADVANTAGE - The method enables economical manufacture of electrodes having excellent hydrogen-production catalytic activity (hydrogen overvoltage is low), without requiring waste-liquid processing like plating method. The usage amount of platinum group metal is reduced. The method is not complicated as a thermal decomposition method.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for electrode.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the electrolyzer.    Electrolyzer (1)    Electroconductive base material (2)    Anode (3)    Electrolyte solution (4)    Direct current power supply (5)
NOVELTY - The apparatus (50) has a modifier which is provided for producing reformed gas containing hydrogen with water and raw material. A carbon monoxide reduction device is heated with heat of the reformed gas for producing fuel gas. A combustion-air passage (23) is provided for connecting combustor (8) and combustion-air supply device (22). A cooling passage (24) is arranged on the outer periphery of the carbon monoxide reduction device, so as to achieve heat exchange between the carbon monoxide reduction device and air supplied by the combustion-air supply device.    USE - Hydrogen generating apparatus used in fuel cell system (claimed) e.g. PEM fuel cell system for domestic application.    ADVANTAGE - The carbon monoxide reduction device is heated with the heat of the reformed gas, so as to reduce carbon monoxide in the reformed gas. The temperature of the carbon monoxide reduction device can be maintained at predetermined temperature. The heat balance of the hydrogen generating apparatus can be controlled easily. The operation of the hydrogen generating apparatus can be maintained stably.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the hydrogen generating apparatus.    Combustor (8)    Combustion-air supply device (22)    Combustion-air passage (23)    Cooling passage (24)    Hydrogen generating apparatus (50)
NOVELTY - Composition (I) comprises: at least one phenolic antioxidant (at least 22 (preferably 15) wt.%); at least one metal chelating compound (at least 0.5 wt.%); and at least one solvent comprising at least one compound of glycols, glycol ethers, glycol ether ester compounds, 1-25C monofunctional alcohols, 1-25C esters, 3-14C ketones, 2-10C amides, 2-10C ethers, and nitro compounds, where the phenolic antioxidant and the metal chelating compound are dissolved in the solvent.    USE - (I) is useful for increasing the oxidative stability of at least one fatty acid or ester of fatty acid, which is biodiesel (all claimed). (I) is useful in food and fuel industries.    ADVANTAGE - (I) is readily miscible in biodiesel. (I) is stable at cold temperatures (e.g. -25 degrees F for 7 days).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a method comprising dissolving the metal chelating compound in a first solvent to form a first solution, and combining the phenolic antioxidant with the first solution to form (I);    (2) a composition (II) comprising 0.001-5 wt.% of an antioxidant composition, where the antioxidant composition is (I), and at least one fatty acid or ester of fatty acid;    (3) a composition comprising at least one burnable fuel source, and a biodiesel composition, where the biodiesel composition is (II); and    (4) a method for increasing the oxidative stability of the fatty acid or ester of fatty acid, comprising combining the fatty acid or ester of fatty acid with (I).
NOVELTY - The gas sensor has an electrode pin (5) which supports a detecting element (7) and a compensation element (8). A mount base (2) fixes the electrode pin. A heat shield board (1a) insulates the detecting element and the compensation element. A cap (1) covers the detecting element and the compensation element and is fixed to the mount base. The heat shield board is fixed to the cap.    USE - Gas sensor used for monitoring of various gas leakages such as carbon monoxide (CO) gas, hydrogen (H2) gas and methane (CH4) gas.    ADVANTAGE - In the gas sensor the heat generated with the heater coil and the detecting element is thermally radiated from a heat shield board to a cap side so that excellent thermal radiation characteristic and the fall of a sensor output can be suppressed. Since the heat shield board can be formed integrally, and there are few factors to which a yield falls the manufacturing cost of the gas sensor can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a front sectional drawing of the gas sensor.    Cap (1)    Heat shield board (1a)    Mount base (2)    Electrode pin (5)    Detecting element (7)    Compensation element (8)
NOVELTY - A desulfurizing agent comprises material which is zeolite of porous inorganic oxide in which mean pore diameter of desulfurizing agent is a size which does not capture unsaturated hydrocarbon type odorant while capturing sulfur compound.    USE - Desulfurizing agent for desulfurizing apparatus and desulfurization process (claimed) used in industry, agriculture, fishing, energy industry, airline industry and space industry.    ADVANTAGE - The removal of sulfur compound in hydrocarbon containing gas is stable, and the adsorption of unsaturated hydrocarbon type odorant is reduced.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) desulfurizing apparatus (100) comprising desulfurizer (114) which is filled with desulfurizing agent, carbonyl sulfide (COS) converter which converts COS in hydrogen containing gas into a hydrogen sulfide in the upstream of the desulfurizer, and metal type desulfurizer which adsorbs hydrogen sulfide in hydrogen containing gas;    (2) hydrogen production system which manufactures hydrogen containing gas by making hydrogen containing gas desulfurized by desulfurizing apparatus with modification catalyst; and    (3) desulfurization process involving desulfurization step which desulfurizes hydrocarbon containing gas by making hydrocarbon containing gas contact the desulfurizing agent with material which is zeolite of porous inorganic oxide.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the modification of the desulfurizer and the desulfurizing apparatus.    Desulfurizing apparatus (100)    Cylinder (111)    Pressure reduction valve (112)    Flow meter (113)    Desulfurizer (114)
NOVELTY - An adsorbent contains copper-containing organometallic complex (I).    USE - Adsorbent is used for adsorbing and discharging methane (claimed) in methane gas collection apparatus.    ADVANTAGE - The adsorbent has excellent methane gas adsorption capability, and efficiently recovers methane gas from methane gas collection apparatus.    DETAILED DESCRIPTION - An adsorbent contains copper-containing organometallic complex of formula: (Cu2(pyridine-3,5-dicarboxylato)2)n (I). The adsorbent is capable of adsorbing and discharging methane gas reversibly. An INDEPENDENT CLAIM is included for usage of organometallic complex.
NOVELTY - A production device of biomass carbon has a stirring device provided with a material inlet at outer shell, a biological carbon discharge port, and a smoke gas outlet. A material inlet and a flue gas outlet are arranged on the upper portion of the outer shell. Carbon discharging opening is provided at the lower portion of the outer shell. The outer shell is divided into 5 layers having holes. The stirring device comprises a stirring shaft, stirring arm and several teeth formed in the arm of the lower portion of the stirring shaft.    USE - Production device of biomass carbon.    ADVANTAGE - The production device of biomass carbon has simple structure and lightweight.
NOVELTY - The device has shell which is provided with feeding port. The one end of the screw rod is connected with the screw motor. The lower portion of the shell is provided with a solid waste collecting tank and a liquid collecting box along the pushing direction of push rod. The liquid waste collecting box is communicated with the bottom of screw cavity. The cavity is provided with powder box with screw opening upwards. The outlet of powder box is provided with pushing screw ferment switch.    USE - Device for crushing and fermenting kitchen waste.    ADVANTAGE - The pushing screw can be provided with the stirring effect so as to ensure the complete mixing of the yeast powder and waste material in efficient manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the device for crushing and fermenting kitchen waste.
NOVELTY - The pool extractor has a motor and a speed reducer that are fixed on a frame. A power transmission is fixed on the output shaft of a speed reducer. An upper end of a connecting rod is hinged with a follower frame. The two ends of the follower are provided with a roller. The follower is fixed on a machine frame and is moved up and down in a guide rail groove. An upper end face of the basket shaped piston is fixed on a frame. The lower end face of the cylinder barrel is fixedly connected on the connecting end of the flange and the lower end of the cylinder by a flange three-way pipe.    USE - Electric-type marsh gas pool extractor.    ADVANTAGE - The reliability of the gas pool extractor can be improved and the working efficiency can be improved. The operation of the marsh gas pool extractor is convenient.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of electric-type marsh gas pool extractor.
NOVELTY - The tube has a venturi tube main portion in which diameter of exit and entrance is increased. The neck whose diameter is small is formed inside the middle portion. A bubble pipe is equipped in inlet side of venturi tube portion. A micro bubble generator is connected to bubble pipe and generates the micro bubble. The generated micro bubble is supplied to the inlet side of venturi tube main portion.    USE - Venturi tube for sludge treatment apparatus.    ADVANTAGE - The cavitations is raised in sludge treatment, such that the pressure of sludge is dropped effectively in venturi tube less than saturated vapor pressure of dissolved gas. The small-capacity pump is used by destroying pressure gradient of extent. The pressure loss in venturi tube and energy loss can be reduced effectively. The digestion efficiency of sludge by microorganism is improved efficiently. The sludge treatment efficiency is increased and the production of biogas can be improved reliably. Hence the cost of sewage treatment can be reduced effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for equipment for treating sludge in venturi tube.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the sewage treatment apparatus. (Drawing includes non-English language text)    Sludge treatment (10)    Sludge transfer pipe (101)    Sludge circulating pipe (102)    Inlet valve (104)    Digestion tank circulating pipe (120)
NOVELTY - An ammonia decomposing system comprises shell (5) equipped with fluid tank (6) connected with reaction tank (7), driving shaft connected with fluid tank and pump (1) of reaction tank, and pressure switch (2).    USE - An ammonia decomposing system used for hydrogen producing system device of fuel cell system device (claimed).    ADVANTAGE - The system provides stable hydrogen output, thus allowing fuel cell system device to generate stable voltage and power, and having service life reaching more than 4000 hours.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a fuel cell system device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of ammonia decomposing system.    Pump (1)    Switch (2)    Shell (5)    Fluid tank (6)    Reaction tank (7)
NOVELTY - An electrolytic hydrogen producing method of polycrystalline silicon comprises electrolyzing alkaline solution to obtain crude hydrogen and oxygen; deoxidizing, dewatering and drying the crude hydrogen using a purifying device to obtain hydrogen having a purity of 99.999% and to obtain oxygen having a purity of 99%; recycling the purified oxygen; diluting to obtain oxygen-enriched air having oxygen content of 21-25%; and subjecting to oxygen enriched combustion.    USE - An electrolytic hydrogen producing method of polycrystalline silicon.    ADVANTAGE - The method recycles by-products, does not discharge by-product thus saving reducing and saving energy, and reduces manufacturing cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an oxygen recycling system which comprises an oxygen buffer tank, a pressure adjusting sub-assembly connected to the oxygen buffer tank, a pressure stabilizing sub-assembly connected to the outlet of the oxygen buffer tank, an oxygen mixer located on the outlet of the pressure stabilizing sub-assembly, a blast blower for inputting the air in the oxygen mixer to mix with the oxygen, and a concentration adjusting sub-assembly connected to the oxygen mixer to adjust the concentration of the oxygen in the oxygen mixer.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of an electrolytic hydrogen producing method of polycrystalline silicon. Drawing includes non-English language text.
NOVELTY - The device has a mark gas observing device provided with a folded air chamber, mark gas measuring device, pressure maintaining valve, high pressure hose, pressure gauge, flow meter and an one-way stop valve. A marked gas collecting measuring device is provided for measuring collected mark gas and flow rate of the inert gas to detect gas pressure of coal bed permeability. A sealing medium device is connected with the one-way stop valve. A mark gas injection device is formed with a sealing release air chamber    USE - Test device for fast measuring coal mine permeability.    ADVANTAGE - The device utilizes coal seam water injection technology to provide strong technical support.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for fast measuring coal mine permeability.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a test device for fast measuring coal mine permeability.
NOVELTY - A solar three-supplying system of heat, electric and gas comprises solar light concentrating module converting solar light into heat energy, solar energy hot water power generation water heating module generating electric by utilizing temperature difference and generate warm water, gas generation module generating hydrogen, and solar temperature difference generating hot water module set on solar light concentrating module.    USE - Solar three-supplying system of heat, electric and gas (claimed).    ADVANTAGE - The system has high solar energy utilization efficiency and low cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a plan view of the solar three-supplying system of heat, electric and gas.    Reflector (4)    Glass tube (14)    Thermoelectric cell (17)    Second insulating heat conductive material (18)    Stainless steel tube (19)
NOVELTY - Preparation of dibasic alcohol from wood fiber biomass comprises crushing wood fiber biomass; adding alkaline solution, acid solution, or water; preprocessing; enzyme hydrolyzing; decoloring the filtered saccharification solution; conducting ion exchange to remove foreign materials and concentrating; adding catalyst having hydrogenation activity to the concentrated saccharification solution in the presence of hydrogen at pH 8-14 and 130-250 degrees C to perform hydrogenation reaction; separating the catalyst; and distilling the product to obtain multiple dibasic alcohols having 2-6C.    USE - The method is for preparation of dibasic alcohol i.e. dibasic alcohol having 2-6C from wood fiber biomass (claimed), useful for producing unsaturated polyester resin, polyurethane, fuel additive surfactant, emulsifier, and locomotive antifreeze solution.    ADVANTAGE - Because the monosaccharide, soluble polysaccharide, and degradation product are reacted, the method achieves greatly improved efficiency and controllability. The product can be separated and used separately to directly produce end products without deep separation.
NOVELTY - De-oil wastewater of kitchen garbage is used by filtering de-oil wastewater of the kitchen garbage to remove impurity with large particles; diluting filtrate with water; adding corn flour, monopotassium phosphate and magnesium sulfate; stirring to obtain a suspension; sterilizing at high pressure vapor and normal pressure vapor; cooling; adding calcium peroxide powder; subjecting to aseptic environment; adding edible fungi strain; culturing; vibrating; culturing in dark environment; loading obtained suspension to industrial fermentation device; sterilizing; and cooling.    USE - Method of using de-oil wastewater of kitchen garbage.    ADVANTAGE - The method prepares product having strong activity, has high yield, and is simple.    DETAILED DESCRIPTION - De-oil wastewater of kitchen garbage is used by:    (A) filtering de-oil wastewater of the kitchen garbage using filter having an aperture of 1-1.5 mm to remove impurity with large particles, and diluting filtrate with water until the solid content of the filtrate is 2-4%;    (B) adding (wt.%) corn flour (2-4), monopotassium phosphate (1-3) and magnesium sulfate (0.2-0.3);    (C) stirring to obtain a suspension, sterilizing at 100 degrees C and high pressure vapor for 4-8 hours, cooling to less than 30 degrees C, adding calcium peroxide powder (0.05-0.1), subjecting to aseptic environment, and adding edible fungi strain (5-10 wt.%);    (D) culturing for 48 hours, vibrating at a speed of 80-120 revolutions/minute, culturing in dark environment at 23-28 degrees C for 5-10 days, and loading obtained suspension to industrial fermentation device; and    (E) sterilizing at 100 degrees C and high pressure vapor for 4-8 hours, cooling, inoculating liquid strain under sterile condition, introducing aseptic air, and culturing for 5-10 days.
NOVELTY - Device for desulfurization of biogas comprises an air inlet pipe, a valve, desulfurization bottle and a pressure gauge. The inlet of the desulfurization bottle is connected with a suspended porous pipe. The porous pipe transversely stretches into the desulfurization cavity. The porous pipe is densely distributed with small holes, whose aperture is less than the small ferric oxide particles.    USE - The device is useful for desulfurization of biogas.    ADVANTAGE - The device comprises the porous pipe, which expands the outlet channel area of gas and performs desulfurization of water content accumulated at the lower side of the suspended porous pipe, and does not easily submerge the porous pipe surrounding the iron oxide particles.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the device for desulfurization of biogas.
NOVELTY - Multi-slot vehicle-mounted machine comprises cell, electrode plate, electrolytic tank with electrode which is connected to vehicular power supply of hydrogen-oxygen outlet, electrolytic cell which is set into several independent grooved body which is equipped with multiple electrode plates having multiple electrode sheets, electrode board which is electrically connected with electrode, and hydrogen gas outlet of tank body which is placed outside of cell from hydrogen gas.    USE - Multi-slot vehicle-mounted machine.    ADVANTAGE - Multi-slot vehicle-mounted machine provides required working temperature, oxygen reduction rate, small voltage fluctuation, thus generated current is stable.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram of multi-slot vehicle-mounted machine.
NOVELTY - Fast pyrolysis ablative type composite set comprises pipeline connected with ablation furnace, crude purifier, crude ion separation tower, water cooling and separating tower, gas desulfurizer, and precision purifier. The water cooling and separating tower and crude ion separation tower separating outlet are connected with gas-liquid separator for separating biomass tar and pyroligneous material.    USE - Fast pyrolysis ablative type composite set.    ADVANTAGE - The composite set improves the quality of biomass gas; increases gas yield; and provides valuable by-products such as wood vinegar.
NOVELTY - Two-stage hydrogenation device comprises a hydrogenation reactor, a feeding mixer and a feeding heater. The hydrogenation reactor comprises first stage and second stage hydrogenation reactor. The inlet of first stage and the second stage hydrogenation reactor are connected to a feeding mixer. The outlet of the hydrogenation reactor is connected to the reflux tank via a discharging cooler. The reflux pump outlet is connected to a reflux pump inlet. The reflux pump outlet is connected in parallel to feeding heater and second feeding mixer. The feeding heater is connected to first feeding mixer.    USE - Used as a two-stage hydrogenation device.    ADVANTAGE - The device avoids the deep hydrodesulfurization of 1,3-butadiene, reduces the operation cycle, prolongs service life of catalyst and utilizes raw materials which has great adaptability.    DETAILED DESCRIPTION - Two-stage hydrogenation device comprises hydrogenation reactor, feeding mixer and feeding heater. The hydrogenation reactor comprises a first stage hydrogenation reactor and a second stage hydrogenation reactor. The first stage hydrogenation reactor and the inlet of the second stage hydrogenation reactor are connected to a feeding mixer. The outlet of the hydrogenation reactor is connected to the reflux tank via a discharging cooler. The reflux pump outlet is connected to a reflux pump inlet. The reflux pump outlet is connected in parallel to the feeding heater and second feeding mixer. The feeding heater is connected to first feeding mixer. A pipeline is set between the feeding heater and the first feeding mixer. The pipeline between the reflux pump and the second feeding mixer is connected in parallel to the carbon material feed tube.    DESCRIPTION OF DRAWING(S) - The drawing illustrates a schematic representation of the two-stage hydrogenation device.
NOVELTY - The invention relates to a pyrolysis plant employed to obtain a synthesis gas. According to the invention, the plant comprises one or several fluidized bed pyrolysis and gasification furnaces (4) comprising some pyrolysis chambers (8) and gasification chambers (5) provided with an ash discharge system (9), some combustion chambers (14) and some post-combustion chambers (16), a biomass supply system (1) and a system (2) for recovering and recycling the smoke resulting from the post-combustion of the synthesis gas and from a smoke flue (23), possibly mixed with fresh air, which are introduced in the pyrolysis and gasification process.
NOVELTY - The system (10) has a posimetric pump (18) to increase pressure of a feedstock (12) to provide a pressurized feedstock. A fixed bed gasifier (52) is used to gasify the pressurized feedstock, where the fixed bed gasifier comprises an enclosure, a feedstock inlet to receive the pressurized feedstock and an agent inlet to receive a gasification agent (55) e.g. steam (56). A syngas outlet is used to output syngas e.g. ammonia. An ash outlet is used to output ash. A fixed bed supports the pressurized feedstock while allowing flow of the agent through the pressurized feedstock.    USE - System for pressurizing and delivering solid feedstock e.g. biomass such as wood chips, rice hulls, corn stalks, municipal solid waste and industrial waste, to a fixed bed reactor e.g. fixed bed gasifier, fixed bed boiler, or fixed bed combustion system (all claimed) to generate energy.    ADVANTAGE - The posimetric pump is used to pressurize and meter pressurize feedstock to fixed bed reactors and elevate the pressure in the reactors so as to increase the production capacity of normally small scale fixed bed reactors. The system includes a heater to control the moisture content of the feedstock to improve the performance of the feedstock such as fuel, and multiple feedstocks are transferred to the fixed bed reactor in a controlled manner to adjust a heating value, so that the moisture content of the mixture of feedstock is controlled.    DETAILED DESCRIPTION - The agent inlet comprises an oxidant inlet and a steam inlet.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a system for pressuring a mixed fuel feedstock for a fixed bed gasifier and using a gasification product in a combustion engine for generating electrical power.    System for pressurizing and delivering solid feedstock (10)    Feedstock (12)    Posimetric pump (18)    Fixed bed gasifier (52)    Gasification agent (55)    Steam (56)
NOVELTY - The system (10) has a gas-impermeable barrier (26) that divides interior portion of housing (20) into high and low-pressure chambers (22,24). The housing is filled with hydrogen gas, and an electrical-energy-generating mechanism operates between charge and discharge conditions. A storage device is placed in high-pressure chamber, when hydrogen molecules are converted to hydrogen ions by generating mechanism. The storage device is placed in low-pressure chamber, when the electric current is passed through the gas-impermeable and electrical-energy-generating mechanism.    USE - Electrochemical conversion system such as Johnson Ambient-heat engine.    ADVANTAGE - Since the hydrogen-storage medium increases the amount of hydrogen that can be stored at given pressure in given volume, the amount of electronic charge produced is increased. Since the heat is absorbed in the high-pressure chamber, the engine facilitates heat transfer between the chambers to minimize the amount of heat transferred to the environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for generating electrical energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the electrochemical conversion system.    Electrochemical conversion system (10)    Housing (20)    High-pressure chamber (22)    Low-pressure chamber (24)    Gas-impermeable barrier (26)
NOVELTY - A biomass resource is heated with superheated steam, and the oil component in biomass resource is vaporized. The biomass residue is heated and carbonized, after vaporization process with superheated steam. The processing of biomass resources is carried out continuously within one processing tank.    USE - Processing of biomass resource e.g. Jatropha seeds, and used for forming biomass oil (claimed) for forming biodiesel oil and edible oil. The carbonized material generated during processing of biomass resource is used for molecular sieve, catalyst carrier and adsorbent.    ADVANTAGE - The method enables efficient and economical processing of biomass resource within short period of time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus for processing biomass resource.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the apparatus for processing biomass resource.    Boiler (10)    Heater (11)    Cooler (12)    Filter apparatus (13)    Waste gas processing apparatus (15)
NOVELTY - The fuel cell (1) has a cathode (14) and an anode (13) which are arranged in a container (11). A pump (20), arranged adjacent to the anode, produces an electro-osmotic flow (E) in the anode. A power supply (27) applies a voltage to the electrodes (21,22) of the pump. The electrodes are opposingly arranged and spaced from each other.    USE - Fuel cell for producing electric power.    ADVANTAGE - Accelerates the supply of fuel e.g. glucose to the anode, and removes a reaction product, thus improving electric power generation efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic block diagram of a fuel cell.    Fuel cell (1)    Container (11)    Anode (13)    Cathode (14)    Pump (20)    Electrodes (21,22)    Power supply (27)    Electro-osmotic flow (E)
NOVELTY - A Desmodesmus pleiomorphus strain SUHL0708 (green alga, FERM P-21960), is new. Fatty-acid type hydrocarbon can be accumulated in alga portion using nitrogen-containing culture solution (40 mg/l or more).    USE - The D.pleiomorphus strain SUHL0708 is useful for preparing lipid, and in biomass fuel extract and biomass feedstock (all claimed). The lipid is used in foodstuff and chemical industry.    ADVANTAGE - The green alga enables inexpensive and simple preparation of lipid.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) method of preparing lipid, involves culturing the D.pleiomorphus strain SUHL0708; (2) dried alga portion obtained by drying the above-cited green alga; and (3) biomass fuel extract and biomass feedstock comprising purified green alga.
NOVELTY - An apparatus (102) consists of container which contains aqueous electrolyte solution (160) containing hydrogen, electrodes in contact with the solution, acoustic transducer (140) per cathode capable of causing cavitation in solution and transmitting along cathodic axis, power supply (110) which supplies power to the electrodes and transducer, wave form generator for imposing wave or other function on transducer, and gas-liquid separation and capturing device. The electrodes are cylindrical cathode (130) and cylindrical hollow anode (132) capable of accommodating the cathode.    USE - Apparatus used in system for producing hydrogen used for generating electricity (claimed).    DETAILED DESCRIPTION - An apparatus consists of container which contains aqueous electrolyte solution containing hydrogen, electrodes in contact with the solution, acoustic transducer per cathode capable of causing cavitation in solution and transmitting along cathodic axis, power supply which supplies power to the electrodes and transducer, wave form generator for imposing wave or other function on the power to the transducer, and gas-liquid separation and capturing device. The electrodes are cylindrical cathode and cylindrical hollow anode capable of accommodating the cathode. The cathode is located along the central axis of the hollow anode. An INDEPENDENT CLAIM is included for system for generating electricity, which consists of the apparatus, electrical generator, fuel cell and hydrogen-burning internal combustion engine.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of the system used for generating hydrogen.    Apparatus (102)    Power supply (110)    Cathode (130)    Anode (132)    Transducer (140)    Aqueous electrolyte solution (160)
NOVELTY - The apparatus has a weight measurement unit (201) that measures the weight of a measurement object. An oscillation frequency calculating unit (204) calculates the frequency component currently emphasized in output signal of weight measurement unit. A weight calculating unit (205) calculates the metal weight of measurement object using the data of calculated frequency component and the data of spring constant of weight measurement unit. An oxidation-state identification unit (206) identifies the metal oxidation state using the data of calculated metal weight.    USE - Metal oxidation-state detection apparatus for fuel cell apparatus (claimed) used as motive power source of moving object.    ADVANTAGE - Since the weight calculating unit calculates the metal weight of measurement object using the data of calculated frequency component and data of spring constant of weight measurement unit, the metal oxidation state can be detected correctly. The fuel residual amount of fuel cell apparatus can be grasped correctly. Thus, the convenience of fuel cell apparatus can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fuel cell apparatus. (Drawing includes non-English language text)    Fuel cell apparatus (1)    Weight measurement unit (201)    Oscillation frequency calculating unit (204)    Weight calculating unit (205)    Oxidation-state identification unit (206)
NOVELTY - Producing methane in a photobioreactor, comprises supplying carbon dioxide and oxygen to photosynthetically active microorganisms, preferably algae or bacteria, separating glycolate secreted from the photosynthetically active microorganisms using a membrane, and converting glycolate that is used as a substrate, into carbon dioxide and methane under anaerobic conditions by methanogenic microorganisms.    USE - The device or the photosynthetically active microorganisms are useful for producing methane (claimed).    ADVANTAGE - The method: exhibits improved efficiency; produces methane with enhanced yield; and does not require nitrogen or phosphorus compounds as nutrients.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a device for carrying out the above method, comprising (i) an aerobic compartment containing a carrier material for the cultivation of photosynthetically active microorganisms and a gas inlet and gas outlet, which are mounted such that the gas flows through the carrier material, and (ii) an anaerobic compartment with a gas outlet, where the anaerobic compartment is separated from the aerobic compartment by a membrane; and    (2) the photosynthetically active microorganisms, where (a) the glycolate dehydrogenase is partially inactivated, (b) the ribulose-1,5-bisphosphate carboxylase/oxygenase and/or the glycolate-phosphate phosphatase is over-expressed, and/or (c) the expression of the glycolate transporter is increased in the cytoplasmic membrane and/or the membrane of chloroplasts.
NOVELTY - A hydrogen generating apparatus (100) comprises modifier (1) which generates hydrogen-containing-gas by reforming reaction using a raw material, ammonia-removal device (4) which removes ammonia by making water absorb ammonia in the hydrogen-containing-gas emitted from the modifier, and carbon monoxide removal device (5) which removes carbon monoxide in hydrogen-containing-gas emitted from ammonia-removal device by oxidation reaction.    USE - Hydrogen generating apparatus for fuel cell system (claimed).    ADVANTAGE - Decline in the carbon monoxide removal efficiency in carbon monoxide removal device can be suppressed and the carbon monoxide concentration and ammonia in the hydrogen-containing-gas can be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the schematic structure of the hydrogen generating apparatus. (Drawing includes non-English language text).    Modifier (1)    Combustor (2)    Ammonia-removal device (4)    Carbon monoxide removal device (5)    Hydrogen generating apparatus (100)
NOVELTY - Centralized gas supplying system of biomass carbonization, gas, oil and liquid co-production, comprises a double-purpose fixed combustion furnace, a relay type movable dry distillation kettle, a cooling and purification system and an air storage tank of a power transmission and a distribution system. The movable dry distillation kettle is movably set on the double-purpose fixed combustion furnace. The movable dry distillation kettle is connected with the cooling and purification system via a pipe. The cooling and purification system is connected with power transmission and distribution system.    USE - Used as a centralized gas supply system of biomass carbonization, gas, oil and liquid co-production.    ADVANTAGE - The device: can continuously carry out operation; comprises in-built heat source; does not require large gas storage cabinet to be installed, thus has low equipment utilization and engineering investment; does not discharge sewage during the production process; saves energy and is ecofriendly.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the.
NOVELTY - Material having at least one dimension of 10 nm-1000 mu m and at least one metal-organic framework (MOF) covalently bound to the material, is claimed.    USE - The material is useful for absorbing a gas or liquid (claimed) including toxic chemicals.    ADVANTAGE - The material is capable of efficiently and selectively absorbing a gas or liquid such as toxic chemicals. The material exhibits enhanced methane permeability and extends the half-life of the attached compound.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) absorbing a gas or liquid, comprising exposing the material to a mixture comprising at least one gas or liquid, where the material selectively absorbs the gas or liquid; and    (2) a method-I of making MOF-modified materials, comprising providing the material, and exposing the material to a mixture of MOF precursors, under conditions resulting in the formation of at least one material.
NOVELTY - Fuel composition (I) comprises: dimethyl ether; and a 2C or larger alcohol or a 2C or larger hydrocarbon.    USE - (I) is useful in consumer, industrial and transportation applications. (I) is useful for providing an energy source during camping, hiking, backpacking, long-distance cycling, or other outdoor activities. (I) is useful as a source of heat for raising a local temperature for a user, such as for warming up a room or a piece of equipment (e.g. a heating mantle), for heating up or cooking a liquid or solid substance for consumption, or other purposes, and for a stationary cooking stove or a portable camping stove; and as a source of light for lighting up a room, a trail, or a camping site; as a source of power for a hand-held pump or a personal water-purification device for camping and as a transportation fuel or fuel additive for a vehicle combustion chamber.    ADVANTAGE - (I) can produced substantially from renewable resources, such as biomass, to provide green fuel composition.
NOVELTY - The system has an air storage tank (4) is connected with a desulphurization tower (5) with a dust remover (6). The dust remover is connected with a pressurizing device (7) that sends specific amount of gas into a fuel gas generator (8). The fuel gas generator is connected with an electric arc plasma power supply (9). The smoke generated by the generator is accessed to a smoke type cold water machine (10). The smoke type cold water machine outputs the cooling water to circulately cool the electric arc plasma (2).    USE - System for processing solid waste energy based on electric arc plasma.    ADVANTAGE - The system can be manufactured with simple structure at low cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a bloc diagram of the System for processing solid waste energy. (Drawing includes non-English language text)    Electric arc plasma (2)    Air storage tank (4)    Desulphurization tower (5)    Dust remover (6)    Pressurizing device (7)    Fuel gas generator (8)    Electric arc plasma power supply (9)    Smoke type cold water machine (10)
NOVELTY - The reactor has anoxic tank that is provided with stirring device and sludge reflux inlet. The anaerobic tank is filled with biochemical cotton filler. The bottom of aerobic tank is provided with through hole aeration pipe and aerobic pool suspension spherical filler. The lower spherical filler layer is provided with multiple plate filler, spherical filler and plate-like filler hanging load earthworm. The bottom of sedimentation tank is provided with sludge reflux outlet.    USE - Biodegradable type reactor for use during wastewater sludge treatment.    ADVANTAGE - The degradation wastewater sludge is improved. The sewage treatment and sludge reduction can be performed effectively, so that sludge processing cost can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of biodegradable type reactor.
NOVELTY - Fresh cow dung waste of different shapes is processed in dry-wet separator, compressed and charred in a charring furnace. The compressed product is carbonized in a carbonization furnace at 450-600 degrees C for 8-10 hours, and clean coke is produced.    USE - Manufacture of clean coke used as fuel for boiler in steel industries.    ADVANTAGE - Clean coke is efficiently manufactured at high yield without affecting the environment.
NOVELTY - The device has a marsh gas waste transfer device and a marsh gas waste sedimentation tank that are connected together. A marsh gas waste precipitation pool and a marsh gas waste rough filtering pool are formed integrally. The marsh gas waste rough filtering pool and fine filtering pools are connected together. A marsh gas fine filter tank is connected to dropping water pool that is connected with the branch pipe and drip irrigation.    USE - Waste marsh gas treatment device used for drip irrigation.    ADVANTAGE - The device can uniformly fertilize the marsh gas waste in the farmland so that the efficiency of the drip irrigation can be improved and the pollution to rural environments can be avoided by coupling the fertilizer.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the waste marsh gas treatment device. (Drawing includes non-English language text)
NOVELTY - The tank has a split-type storage tank (1) and a fermenting pool (6) that are communicated through an air pipe (7). The upper end of the gas storage tank is provided with a vent (11) and the lower end is placed in a water pool (8). The bottom portion of the gas storage tank is communicated with the water pool.    USE - Methane tank used for adjusting methane pressure.    ADVANTAGE - The imbalance in the atmospheric pressure can be avoided and utilized for mass production. The methane tank can be designed in simple structure.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing method of methane tank.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the methane tank.    Storage tank (1)    Air outlet (4)    Fermenting pool (6)    Air pipe (7)    Water pool (8)    Vent (11)
NOVELTY - The reactor has a convey belt driven wheel (14) that supports the frame of the conveyer belt (18) passed through the cavity (13). An infrared temperature sensor (9) monitors temperature change of the material. The conveying belt (15) conveys speed of monitoring regulation and temperature regulation.    USE - Pre-treating reactor.    ADVANTAGE - The continuous pre-treated biomass can be realized. The special preprocessing requirement of biomass can be satisfied. The normal pressing for continuous preprocessing biomass can be realized. The energy consumption of the reactor can be reduced. The speed of the reactor can be improved. The pre-processing cost of the reactor can be greatly reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the pre-treating reactor.    Infrared temperature sensor (9)    Cavity (13)    Convey belt driven wheel (14)    Conveying belt (15)    Conveyer belt (18)
NOVELTY - The device has side wall portion that is provided with garbage input pin. An anaerobic reaction tank is connected with marsh gas output pipe and waste discharging pipe. A hand wheel is connected with a stirring impeller extending in the anaerobic reaction tank. An outer side wall surface of movable air chamber is provided with edge of internal channel. The movable air chamber is connected with the top cavity of the anaerobic reaction tank, and is provided with a locating guide device for lifting air chamber.    USE - Biological garbage treatment device.    ADVANTAGE - The device is simple in structure, so that manufacturing cost can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biological garbage treatment device.
NOVELTY - The device has a synthetic gas outlet connection pipeline device which is connected with a pipeline of a synthetic gas cooling condensing device (43) among a reaction kettle (1). The pipelines of the synthetic gas cooling condensing device are connected with a thermal cracking liquid collecting box (37). The pipeline of in-condensed gas pipeline device is connected with a gas burner. The reaction kettle is sealed in a heat insulating chamber (10).    USE - Device for biomass thermal cracking for agriculture and forestry.    ADVANTAGE - The device for biomass thermal cracking is safe and convenient. The need for the accurate monitoring of the device can be avoided.    DESCRIPTION OF DRAWING(S) - The drawing shows a cut away view of the device biomass thermal cracking.    Reaction kettle (1)    Heat insulating chamber (10)    Gas outlet (26)    Thermal cracking liquid collecting box (37)    Synthetic gas cooling condensing device (43)
NOVELTY - The device has an opened rectangular container (1) whose bottom is inclined with respect to a plane. A flue (2), vent hole (6) and air ducts (3) are set along the bottom of the container. The container is provided with air channels (4) and air draft passage (5).    USE - Biomass cracking device.    ADVANTAGE - The cracking effect and cracking rate are improved. Energy is saved efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the biomass cracking device.    Container (1)    Flue (2)    Air duct (3)    Air channel (4)    Air draft passage (5)    Vent hole (6)
NOVELTY - The device has several circulating pumps (1,2,3) that are provided at outside the tank portion (9). The inner annular tubes (13,14,15) are provided at inner wall of the tank portion from top to bottom. A jet assembly is centrally provided at bottom of tank portion. The output ends of circulating pumps are connected with jet assembly and inner annular tubes. A balance tube (7) and outlet upper tube are respectively induced from upper portion of side wall of tank portion. The balance tube and outlet upper tube (6) are simultaneously connected with an inducing tube (5).    USE - Rotary anaerobic fermentation device for processing municipal solid waste-gas.    ADVANTAGE - The device has low manufacturing cost and is easy to install and saves energy consumption.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the rotary anaerobic fermentation device. (Drawing includes non-English language text)    Circulating pumps (1,2,3)    Inducing tube (5)    Outlet upper tube (6)    Balance tube (7)    Tank portion (9)    Inner annular tubes (13,14,15)
NOVELTY - Biomass solid fuel molding machine, comprises machine frame (6), feeding table (1), spiral juicer (9), and extrusion molding machine. The spiral juicer is provided with a pressure flow guiding sleeve.    USE - Biomass solid fuel molding machine.    ADVANTAGE - The biomass solid fuel molding machine improves biomass solid fuel dehydration rate, extrusion density, high solidification density and heat value, reduces labor, and compactly molds fuel, has excellent durability and is convenient to use. The molded product is easy to store and environmentally-friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows perspective view of biomass solid fuel molding machine.    Feeding table (1)    Molding frame (6)    Spiral juicer (9)    Extrusion molding machine (12)    Belt (19)    Second projecting barrel (22)
NOVELTY - The slot has a hydrogen side pole frame (1) that is provided on pole plate (3). A pole plate is formed on oxygen-side electrode (4). A sealing pad (2) is provided between the hydrogen side pole frame and pole plate.    USE - Electrolytic slot.    ADVANTAGE - The weight of the pole frame can be reduced so that the weight of the electrolytic slot can be reduced. The electrolytic slot can be assembled effectively. The cost of electrolytic slot can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the electrolytic slot.    Hydrogen side pole frame (1)    Sealing pad (2)    Pole plate (3)    Oxygen-side electrode (4)
NOVELTY - The tank has several earthworm composite reactors (3) provided with a through hole (2) at side wall. A flashboard is provided between each earthworm composite reactor. A slide way (4) is provided between clapboard (9) with holes and the earthworm composite reactor. A lower end of the clapboard is fixed with a percolate recycling inclined plane. A percolate recycling groove (7) is fixed with the percolate recycling inclined plane.    USE - Earthworm composite reaction tank used in home.    ADVANTAGE - The discharge of waste, earthworm fertilizer and percolation liquid is reduced so that the environmental consciousness of the family member is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the earthworm composite reaction tank.    Through hole provided in earthworm composite reactor (2)    Earthworm composite reactor (3)    Slide way (4)    Percolate recycling groove (7)    Clapboard (9)
NOVELTY - A processing device comprises kneading device, sealing reaction tank, oval pre-soaking pool, circulating coupling fermentation tank, two sections of biological aerobic processor, anaerobic digester and desulfurization tower which are orderly connected. The circulating coupling fermentation tank is provided with solid fermentation reactor and two gas circulators.    USE - Processing device used for combined dry-wet fermentation of waste straw (claimed).    ADVANTAGE - The processing device can safely and efficiently recycle and treat domestic waste straw or kitchen garbage. It is economical and eliminates the need for sorting and crushing waste straw, thus greatly reducing the operational cost. It does not generate secondary pollution and is configured to prevent the spread of bacteria and virus, thus making it environment-friendly and enabling good ecological cycle.
NOVELTY - The system has a ventilation pipe which is connected with a rotor flowmeter. The rotor flowmeter is connected with an aeration pump. The aeration pump is connected with a relay switch through a wire. The wind chamber is mounted on the bottom portion of the ventilation pipe.    USE - Controlled composting system for removing polycyclic aromatic hydrocarbon residue in soil.    ADVANTAGE - The polycyclic aromatic hydrocarbon from the polluted soil can be removed effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for removing polycyclic aromatic hydrocarbon residue in soil.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the controlled composting system.
NOVELTY - The device has a micro-controller connected to an oxygen data acquisition module, a hydrogen sulfide data acquisition module, a methane data acquisition module and a carbon monoxide data acquisition module through an input circuit. An oxygen sensor, a hydrogen sulfide sensor, a methane sensor and a carbon monoxide sensor are respectively connected to the oxygen data acquisition module, the hydrogen sulfide data acquisition module, the methane data acquisition module and the carbon monoxide data acquisition module. A shell (1) is arranged with a panel (6).    USE - Multiple gas measuring device for use in mining field, transportation field, and storage and logistics field.    ADVANTAGE - The device has high detection precision, wide application range, simple structure, small volume and high portability.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a multiple gas measuring device.    Shell (1)    Buzzer window (2)    Sensor window (3)    Key (5)    Panel (6)
NOVELTY - Disclosed is a process for production of biodiesel from acid oil, where the acid oil is contacted with an alcohol in countercurrent manner in the presence of an acid catalyst for esterification. Esterification is followed by saponification and then transesterification of triglycerides, by an alcohol in the presence of an alkaline catalyst. In the overall process, fatty acid from acid oil is contacted with alcohol in multiple countercurrent steps, where between two steps, organic and aqueous acid phases are separated by phase separation. Esterification of the fatty acids in the acid oil with alcohol in countercurrent manner and intensified by hydrodynamic cavitation has increased the efficiency of process to such extent that ratio of alcohol to free fatty acid of acid oil has considerably been reduced. Image 0/0
NOVELTY - Cover plate, which prevents hollow fire in a hollow carburetor compartment of a wood gasification boiler, is claimed.    USE - The cover plate is useful for preventing hollow fire in a hollow carburetor compartment of a wood gasification boiler.    ADVANTAGE - The cover plate: ensures uniform utilization of the surface area of the carburetor compartment; exhibits strength, which prevents its self destruction, and reduced smoke emission, reduced pollutant emission and reduced particulate emission during the prevention of fire; and improves the efficiency degree of the boiler.    DESCRIPTION OF DRAWING(S) - The figure 1 and 2 show a schematic representation of the top view and the side view of the cover plate respectively.
NOVELTY - Organic waste is carbonized by reduced pressure drying of microorganisms, heating organic waste in pressure reduction environment, forming dry organic substance, condensing moisture content evaporated from organic waste, mixing condensed water and gas including odor produced during reduced-pressure-drying process, and cooling with cooling water. During carbonization process, combustible gas is produced while heating dry organic substance in low-oxygen environment, and organic carbonized material is formed.    USE - A carbonization method of organic waste, such as waste material from agriculture and fishery, foodstuff residue, and organic refuse from general household.    ADVANTAGE - Carbonization method uses little fuel consumption, preventing spread of organic waste odor.    DETAILED DESCRIPTION - Organic waste is carbonized by reduced pressure drying of microorganisms, heating organic waste in pressure reduction environment, forming dry organic substance, condensing moisture content evaporated from organic waste, mixing condensed water and gas including odor produced during reduced-pressure-drying process, and cooling with cooling water. During carbonization process, combustible gas is produced while heating dry organic substance in low-oxygen environment, and organic carbonized material is formed. Combustion process burns combustible gas produced from dry organic substance during carbonization process as a fuel for heating in reduced-pressure-drying process or carbonization process. An INDEPENDENT CLAIM is included for carbonization plant of organic waste (1).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a carbonization plant of organic waste. (Drawing includes non-English language text).    Carbonization plant of organic waste (1)    Pressure reduction fermentation drying apparatus (3)    Ring-die-type granulator (4)    Carbonization apparatus (5)
NOVELTY - Fermenter (1), which is designed in gas-tight manner, comprises a base (3) and a liquid-permeable supporting device (4) for supporting and/or receiving the biomass (2) introduced into the fermenter. The fermenter is sealed gas-tight manner by the interaction of at least one base with a non-load bearing shell (5) of the fermenter construction, which is mounted such that the biomass introduced into the fermenter is supported only at the base and the support device. The base has drainage system arranged away from side of the support device, from which the biomass is introduced.    USE - The fermenter is useful for fermenting biomass.    ADVANTAGE - The fermenter is easily expandable, and provides favorable fermenting conditions.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic sectional view of the fermenter.    Fermenter (1)    Biomass (2)    Base (3)    Supporting device (4)    Shell (5)
NOVELTY - The system has a hydrogen generator provided with a reaction kettle upper cover (1), a shell (2), a seal pad, an interior air outlet joint, a seal ring, a limit pressing sheet, a screw plug, an air transporting pipe, a pressure releasing valve, a water filter, a spiral pipe, a filter, ball valves, an exterior hydrogen interface, a pressure adjusting valve, a flame arrester and a flow meter. The generator is connected with a polymer hydrogen fuel cell generating system unit via a fuel cell air inlet solenoid valve and a relay.    USE - Polymer hydrogen fuel cell system.    ADVANTAGE - The system can be carried and used conveniently. The fuel cell can generate the electric energy that is adjusted by the self-automatic adjusting device and a direct current (DC)-DC convertor and stored in the storage battery. The electric energy can be used in the universal serial bus (USB) output mode and alternating current 220V output mode.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a polymer hydrogen fuel cell system.'(Drawing includes non-English language text)'    Reaction kettle upper cover (1)    Shell (2)
NOVELTY - The method involves registering substances into a reactor (3). Waste products are melted, cracked and discharged. Combustible light liquid is condensed by gas-phase after execution of cracking of the waste products, where the produced light liquid is stored. Organic residues are cracked and dried in a reactor space. A heating medium (6.3) is made to flow into a heating jacket (6.1) in counter flow to material flow, where the jacket surrounds the reactor. Fuel is obtained from solid plastic mixtures and lignocelluloses mixtures in form of fuel oil (7.1), combustible gases (7.13) and coke (5.9).    USE - Method for treating organic highly loaded substance e.g. wood chip, lignocelluloses biomass and recycled household waste, into fuel oil, combustible gases and coke, utilized for a stationary diesel engine for producing electrical power. Can also be used in organic chemical- and pharma industries.    ADVANTAGE - The method enables avoiding secondary reactions in gas flow by creation of vacuum in the reactor, thus avoiding loss of quality in pyrolysis oil. The method enables allowing the flow of heating medium into the heating jacket in the counter flow to the material flow, so that optimum heat entry into a fusion property can be ensured.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for carrying out a method for treating organic highly loaded substances.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a reactor and a condensation system for entry of substances.    Reactor (3)    Coke (5.9)    Heating jacket (6.1)    Heating medium (6.3)    Fuel oil (7.1)    Combustible gases (7.13)
NOVELTY - Hydrotreatment of a vegetal biomass comprises (a) subjecting the vegetal biomass to a hydrotreatment in a first reactor, where the hydrotreatment comprises contacting the vegetal biomass in an aqueous medium and a metal oxide, a mixed metal oxide, or a metal-metalloid oxide catalyst comprising at least 35 wt.% of metal oxide, mixed metal oxide, or metal-metalloid oxide relative to the total weight of the catalyst, with hydrogen at a pressure of 10-400 bar and at a temperature of 50-300 degrees C, and the metal oxide, a mixed metal oxide, or a metal-metalloid oxide catalyst comprises nickel.    USE - The process is useful for hydrotreatment of a vegetal biomass. The catalyst is useful for the hydrogenation or hydrodeoxygenation of organic materials, hydrogenation of pyrolyzed organic materials, and preparation of biofuels (all claimed) such as bioethanol, biodiesel and various biogases.    ADVANTAGE - The process is capable of hydrotreating a vegetal biomass in an economic manner with high yield. The process provides better treatment for biomass from vegetal sources which are easier to carry in a shorter time, and less severe conditions, prevents the polymerization of the biomass by catalyst and less methanation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for metal oxide, mixed metal oxide or metal-metalloid oxide catalyst obtainable by a process comprising (1) mixing hydrated metal oxides a ammonia aqueous solution, (2) adding a solution of a 1-6C alkyl silicate in a 1-6C alkyl alcohol, (3) impregnating with zirconium (IV) dinitrate oxidehydrate and lanthanum (III) nitrate hexahydrate in water, (4) drying the obtained product, and (5) calcining the product obtained in (4) at 350-900 degrees C.
NOVELTY - Producing a fuel or fuel precursor from lipid-containing biomass comprises heating an aqueous slurry comprising lipid containing biomass and water in a pressure vessel at a temperature of about 200 degrees C to about 350 degrees C in the presence of a metal base to produce a solid phase comprising one or more precipitated metal soaps and an aqueous phase, and separating the solid phase from the aqueous phase, and heating the solid phase to the decomposition temperature of the one or more metal soaps.    USE - The method is useful for producing fuel or fuel precursor from lipid-containing biomass. The ethyl benzene or styrene obtained from the mixture produced by the method is useful for manufacturing polystyrene of biological origin. The dialkylated or polyalkylated pyrazines obtained from the mixture produced by the method is useful for manufacturing precursors of condensation polymers of biological origin by oxidation of pyrazine dicarboxylic acids or pyrazine polycarboxylic acids or anhydrides (all claimed).    ADVANTAGE - The invention provides method of processing hydrothermally lipid containing biomass such as algal biomass in the presence of certain metal bases such that following the hydrolysis of lipids, the lipid acids form insoluble soaps, while nitrogenous and oxygenated materials remain dissolved in the aqueous phase, thus making it easier to separate and purify the different classes of chemicals and also significantly preventing cross-reactions between different classes of materials, thus obtaining better yields of each class of useful chemicals, particularly nitrogen heterocyclic materials and liquid fuel or liquid fuel precursors that are essentially free of nitrogenous contaminants.
NOVELTY - The method involves making (STP1) original sludge foaming under reduced pressure by entraining the foaming gas in vacuum concentration process. The high temperature vapor is blown off at high speed into the working fluid in vacuum formation process. The thickened sludge and high temperature vapor are contacted to obtain solubilization sludge in solubilization process. Solubilization sludge is retained and deaerated to obtain deaeration sludge. The deaerated sludge is methane fermented on anaerobic condition to obtain digested sludge in methane fermentation process.    USE - method for disposing sludge such as activated sludge, first precipitated sludge, surplus sludge, coagulation sludge, purification tank sludge and organic sludge.    ADVANTAGE - The efficiency of methane fermentation of highly concentrated sludge is effectively and reliably improved. The exploitation of energy is solved by simple and compact structure of sludge disposal system. The method can be implemented for processing the activated sludge, first precipitated sludge, surplus sludge, coagulation sludge, purification tank sludge and organic sludge.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for sludge disposal system.    DESCRIPTION OF DRAWING(S) - The drawing shows a floe chart illustrating the sludge disposal method. (Drawing includes non-English language text)    Step for making original sludge foaming under reduced pressure (STP1)    Step for vacuum formation process (STP2)    Step for solubilization process (STP3)    Step for solid gas separation process (STP4)    Step for performing methane fermentation process (STP5)
NOVELTY - Fibrous biomass is crushed, dried and granulated. The granulated material is heat-press-molded into a hollow cylinder and then carbonized, to obtain a carbonized material.    USE - Manufacture of carbonized material for use as combustion improver in waste-material melting furnace (claimed).    ADVANTAGE - The method enables manufacture of carbonized material having excellent strength and high density for use as an alternative of coke used as heat-of-fusion source of waste material. The usage amount of coke and discharge of carbon dioxide derived from fossil fuel are reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the manufacturing equipment of carbonized material. (Drawing includes non-English language text)    Press (15)    Conveyor (16)    Cutter (17)    Drying furnace (18)    Rotary dryer (19)    Molding machine (25)
NOVELTY - Producing oil by using yeast, comprises utilizing at least one yeast strain comprising Pseudozyma as a working microorganism to produce the oil.    USE - The method is useful for producing oil, which is useful for manufacturing bio-diesel oil (all claimed).    ADVANTAGE - The method produces oil at high yield rate. The oil produced by the yeast strain is less easily oxidized.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an oil generation system, comprising a carbon source, and at least one yeast strain comprising Pseudozyma that is reacted with the carbon source to produce oil.
NOVELTY - The mold has a molding slot formed with an intaglio part corresponding to thickness of a gasket. A rubber is injected in an inner side of the gasket. A projection part is protruded along a longitudinal direction of the molding slot. A metal support part is combined with a gear. A locking protrusion portion is formed on a plane of the projection part.    USE - Fuel cell gasket manufacturing mold.    ADVANTAGE - The mold reduces assembling time and increases a sealing function, thus improving durability of the gasket.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross sectional view of a fuel cell gasket manufacturing mold.
NOVELTY - Pluggable universal composter comprises stainless steel with multiple corner angles (10) and multiple connecting elements (20).    USE - Used as a pluggable universal composter.    ADVANTAGE - The composter: does not require screwing; is easy to mount; and has high durability.    DESCRIPTION OF DRAWING(S) - The figure 1 shows a schematic representation of the pluggable universal composter.    Corner angle (10)    Connecting element (20)
NOVELTY - Agent comprising natural occurring organic acids, obtained gently from acid derivative-containing natural products by Green Chemistry, is claimed.    USE - The agent is useful in biofood products including flavors and natural/bio-cosmetics.    ADVANTAGE - The agent is composed of naturally occurring organic acids obtained from acid derivative-containing natural products by Green Chemistry.
NOVELTY - A Klebsiella strain having the capability to produce 1,3-propanediol, which assimilate a glycerol and produce hydrogen gas, is new.    USE - The Klebsiella strain is useful for producing hydrogen and 1,3-propanediol, and for processing biodiesel waste liquid (all claimed).    ADVANTAGE - The Klebsiella strain can be used for efficiently processing biodiesel waste liquid.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a method for producing hydrogen by using the strain above by making a glycerol into a substrate;    (2) a method for producing 1,3-propanediol by using the strain above by making a glycerol into a substrate; and    (3) a method for processing biodiesel waste liquid by using the strain above to decompose the glycerol contained in a biodiesel waste liquid.
NOVELTY - Manufacture of solid fuel involves grinding mixture of coal and palm kernel shell in a vertical roller mill (4) with roller pressure of 5.8-10.5 kg/cm2.    USE - Manufacture of solid fuel.    ADVANTAGE - The method efficiently and economically provides solid fuel by consuming reduced amount of energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for vertical roller mill.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view explaining the manufacture of solid fuel. (Drawing includes non-English language text)    Raw material hopper (1)    Raw material belt feeder (2)    Vertical roller mill (4)    External circulation system (5)    Dust collector (6)
NOVELTY - A hydrogen-purification apparatus (100) comprises a reforming catalyst (5a) which reduces the content of carbon monoxide in hydrogen-containing gas by reforming reaction, and a methanation catalyst (6a) which reduces content of carbon monoxide in hydrogen-containing gas which has passed reforming catalyst. The reforming catalyst and methanation catalyst are structured such that heat exchanges through first dividing wall (8) and hydrogen-containing gas passing reforming catalyst flows in opposite direction from hydrogen-containing gas passing methanation catalyst.    USE - Apparatus is used for purifying hydrogen used for fuel cell for generating electric power.    ADVANTAGE - The apparatus efficiently purifies hydrogen by reducing temperature gradient of upstream and downstream of methanation catalyst and improving methanation catalyst property of carbon monoxide.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic structure of hydrogen-purification apparatus. (Drawing includes non-English language text)    Transformer (5)    Conversion catalyst (5a)    Carbon monoxide removal device (6)    Methanation catalyst (6a)    Hydrogen-purification apparatus (100)
NOVELTY - The system has hydrogen-producing portion in which hydrogen is generated by oxidation reaction with water, and reproduced by reductive reaction with hydrogen. An electric power generation/electrolysis portion has electric power generation unit that produces electric power by using hydrogen as fuel, and electrolysis unit in which water is electrolyzed to generate hydrogen. The hydrogen-producing portion is provided with several hydrogen generators (1), and temperature control portion in which the temperature of hydrogen generators is separately controlled.    USE - Secondary battery type fuel cell system of electric vehicle.    ADVANTAGE - The temperature control portion can control the temperature of hydrogen generators separately, so that the secondary battery type fuel cell system with high energy efficiency can be achieved. The number of heat cycles of hydrogen generator does not increase, such that the useless heating can be prevented. Hence the durability of hydrogen generator is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the secondary battery type fuel cell system. (Drawing includes non-English language text)    Hydrogen generator (1)    Heater (2)    Temperature sensor (3)    Residual amount sensor (4)    Controller (8)
NOVELTY - Method of processing glycerol and sewage surplus sludge, involves subjecting the glycerol and sewage surplus sludge to anerobic fermentation process to obtain decomposition product of glycerol and reduced solid content of sewage surplus sludge, respectively, where the glycerol is obtained as byproduct while reacting alkali catalyst with alkyl ester of the fatty acid in manufacture of biodiesel fuel using vegetable oil and primary alcohol as raw material.    USE - The method is useful for processing glycerol which is used as raw material for preparing pharmaceutical, cosmetics and soap.    ADVANTAGE - The method consumes organic substance contained in sewage surplus sludge by anaerobic fermentation and hence is easy to recycle the solid substance. The method is cost-effective as the solid substance can be decomposed completely without applying electrical energy.
NOVELTY - A pair of electrode is provided in a reactor, and very short pulse of rise time is intermittently applied with high voltage which makes hydrogen separable from hydrogen-containing compound existing into two poles and which does not generate a glow discharge or arc discharge between electrodes. Hydrogen is produced from hydrogen-containing compound in the formed electric field.    USE - Manufacture of hydrogen in hydrogen producing apparatus used in automotive fuel electric power generating apparatus for motor vehicles (claimed).    ADVANTAGE - The hydrogen is efficiently and economically produced using the hydrogen production apparatus.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for hydrogen producing apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of automotive fuel electric power generating apparatus. (Drawing includes non-English language text)
NOVELTY - Complete combustion of liquid fuel comprises: supplying oxygen gas and liquid fuel; electrostatically atomizing the fuel; evaporating the atomized liquid fuel; and reacting the evaporated liquid fuel with oxygen in contact with a catalyst (930).    USE - The process is useful for producing heat, hydrogen and olefins (claimed) which are used in bio-refinery technologies.    ADVANTAGE - The process: is continuous, utilizes a single apparatus with a single reactor which is multi-functional that can operate in multiple modes of reforming, bio-refinery and combustion; provides optimal heat production at the fuel/oxygen equivalence ratio of less than 1, 1-2.5 or greater than 2.5; and produces hydrogen which enables fuel reformation for hydrogen fuel power generation, and produces olefin which enables production of synthetic jet-fuels.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a multi-functional compact fuel converter (900) apparatus comprising: a reactor (920); a continuous supply of fuel to the reactor; a continuous supply of oxygen to the reactor; an electrostatic atomized fuel injection device (960) located in the reactor; a pre-heat region in the reactor having sufficient temperature and length to fully vaporize the atomized liquid fuel; a grounded mesh (950) screen located below the fuel injection device and connected to it; a source of heat for vaporization of atomized liquid fuel; a fuel-oxidizer mixing region in the reactor; and a catalyst on a foam support.    DESCRIPTION OF DRAWING(S) - The figure shows a multi-functional fuel converter.    Converter (900)    Reactor (920)    Catalyst (930)    Grounded mesh (950)    Fuel injection device (960)
NOVELTY - Device (1) for producing energy carriers from biological material, comprises at least one heating module (2) for heating the biological material, and at least one subsequent degassing module (4) in a transport direction of the biological material to the heating module for discharging the resulting gases. The degassing module comprises at least one, preferably many tubes for transport of the biological material. The biological material is fed within the tubes, and walls of the tubes comprises many openings for discharging resulting gases.    USE - The device is useful for producing energy carriers from biological material.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a plant for producing fuels from biological material with the device, a means for producing pressed bodies from biological material, and a supply device for supplying the pressed biological material to the device; and    (2) producing fuels from biological material comprising heating the biological material using at least one heating module, and discharging the resulting gases using at least one subsequent degassing module in the transport direction of the biological material, where (a) the biological material supplied in the absence of oxygen is transported in one, preferably many tubes through the heating module, (b) the biological material undergoes heating and the resulting gas leaves through the opening into the subsequent degassing module arranged at the heating module into the walls of the tubes and is discharged during the transport of the biological material.    DESCRIPTION OF DRAWING(S) - The figure 1 shows a spatial representation of the device.    Device (1)    Heating module (2)    Degassing module (4)    Outlet connection (14)    Heating mantle (16)
NOVELTY - Preparing alcohol from a liquid alcohol/hydrocarbon mixture comprises: (a) providing the mixture; (b) adding and mixing a polar organic compound as phase separating auxiliaries; (c) performing phase separation to obtain a hydrocarbon-rich first liquid phase and an alcohol-rich second liquid phase; (d) feeding the second liquid phase to a thermal separation method to obtain a third alcohol-enriched liquid phase and a fourth phase separation auxiliaries-enriched liquid phase; and (e) discharging the third liquid phase and recovering the alcohol from the third liquid phase.    USE - The process is useful for preparing alcohol from liquid alcohol/hydrocarbon mixture.    ADVANTAGE - The process is carried out in simple and an efficient manner.    DETAILED DESCRIPTION - Preparing alcohol from a liquid alcohol/hydrocarbon mixture comprises: (a) providing the alcohol/hydrocarbon mixture; (b) adding and mixing a polar organic compound as a phase separating auxiliaries, whose boiling point differ significantly from the boiling point of the alcohol; (c) performing phase separation to obtain a hydrocarbon-rich first liquid phase and an alcohol-rich second liquid phase, which are enriched at the phase separation auxiliaries; (d) feeding the second liquid phase to a thermal separation method to obtain a third alcohol-enriched liquid phase and a fourth phase separation auxiliaries-enriched liquid phase; and (e) discharging the third liquid phase and recovering the alcohol from the third liquid phase.
NOVELTY - The ammonia-/hydrogen plant comprises a motor driven combustion air-ventilator (3) and a motor driven flue gas-ventilator (3'). The driven motor is equipped with two drive ends for the respective ventilator. A steam turbine (5) is connected to the drive shaft via a gear box (7). An individual shaft section is connected via coupling elements (4). The motor with a shaft output is provided in an arrangement of the motor/combustion air-ventilator/flue gas-ventilator/turbine.    USE - Used as ammonia-/hydrogen plant.    ADVANTAGE - The ammonia-/hydrogen plant can be economically manufactured with less energy, effort and reduced size.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic view of an ammonia-/hydrogen plant. asteriskasteriskLISTPasteriskasterisk(3) Combustion air-ventilator #(3') Flue gas-ventilator #(4) Coupling elements #(5) Steam turbine #(7) Gear box.asteriskasterisk/LISTPasteriskasterisk
NOVELTY - Inclusion compound with a matrix of a silicate-based dried gel, in which an inorganic hydride is embedded, is new.    USE - The inclusion compound or inclusion compound-containing composition is useful as a hydrogenating agent or hydrogen former and for energy production (claimed).    ADVANTAGE - The inclusion compound is stable at air for long time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of the inclusion compound.
NOVELTY - Porous polymer films, preferably polymer electrolyte membranes based on polymers containing multivalent, hetero-aromatic rings with one or two rings containing nitrogen atoms, have a porosity based on film volume of 2-90%, an average pore diameter of 0.5 mu m to maximum 20% of the film thickness at 20?0C and 1000 hPa, with the condition that the porous polymer films are soluble in N, N-dimethylacetamide (0-20 wt.%) in relative to its polymer content at 130 degrees C and 1000 hPa.    USE - The polymer electrolyte membrane is useful for producing membrane-electrode-units for fuel cells or electrolysis cells and as a semipermeable membrane for the separation of liquids and gases (all claimed).    ADVANTAGE - The porous polymer films: exhibit properties that include improved chemical resistance and improved porosity, improved proton conductivity, thus the films provide an improved electrical performance with improved mechanical stability and durability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) producing the porous polymer film, preferably polymer electrolyte membranes comprising (i) preparing a mixture comprising polymers containing multivalent, hetero-aromatic rings with one or two ring containing nitrogen atoms, polar aprotic solvent, pore-forming agents, optionally bridging reagents and optionally further substances, (ii) coating the resultant mixture on a support, (iii) removing the polar aprotic solvent completely or partially and (4) cross linking the polymer film obtained in the step (iii), with the condition that depending on the type of pore-forming agent in step (iii) and/or after the step (iv) the polar aprotic solvent is removed completely or partially and doping with a strong acid; and    (2) membrane-electrode-units comprising at least one electrode and at least the polymer electrolyte membrane.
NOVELTY - The apparatus (23) has an electrode (8) that is electrically connected with a rear surface of a photoelectric conversion element and an electrode (7) that is electrically connected with a light-receiving surface of a photoelectric conversion element. The electrodes are immersed in the water in a flow path. The water is electrolyzed due to the electromotive force produced during the light receiving process of the photoelectric conversion element such that the hydrogen gas and the oxygen gas are generated from water.    USE - Water electrolysis apparatus.    ADVANTAGE - The hydrogen gas and the oxygen gas can be generated efficiently using the electromotive force produced during the light receiving process of the photoelectric conversion element.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the water electrolysis apparatus.    Electrodes (7,8)    Electro-conductive portion (10)    Partition portion (13)    Gas discharge port (19)    Water electrolysis apparatus (23)
NOVELTY - The dust removing system has a biomass gasification furnace (5) whose exhaust port is connected with a cyclone dust collector (1). A flue exhaust pipe of a first smoke dust collector and an outlet nozzle of a second exhaust gas pipe are connected with a tubular dust cooler (2). A second smoke exhaust pipe of tubular dust cooler connects with a third smoke exhaust pipe of a de-dusting cooling tower (3) and enters into de-dusting cooling tower. The de-dusting cooling tower has a third smoke exhaust pipe that is connected with a foam-fourth gas exhaust pipe (4).    USE - Dust removing system of biomass gasification furnace.    ADVANTAGE - The dust removing system is featured with simple structure, good dust removing effect, low operation cost and so on.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic structural view of the dust removing system of biomass gasification furnace.    Cyclone dust collector (1)    Tubular dust cooler (2)    De-dusting cooling tower (3)    Foam-fourth gas exhaust pipe (4)    Biomass gasification furnace (5)
NOVELTY - The device has an upper conveying belt and lower conveying belt that are fixedly provided with uniformly distributed vacuum heat tube (3). A stirrer (6) respectively connected with condensation water drain valve, gas outlet valve and a waste water drain valve. An upper portion of stir drying storehouse is provided with a gas outlet and a conveying drying storehouse (7) is provided with a gas outlet and drying chamber. A condenser (10) of gas outlet is connected with condensation water collecting container and gas purifying device.    USE - Sludge drying device for garbage landfill methane gas power generation.    ADVANTAGE - The sludge drying device having reasonable structure and that improves operating efficiency can be provided. The utilization rate of sludge drying device can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the sludge drying device.    Motor (1)    Vacuum heat tube (3)    Stirrer (6)    Conveying drying storehouse (7)    Condenser (10)
NOVELTY - The self-generating biomass gasification furnace has a power generation device (1) connected with a power storage device (2). The circuit connecting end of an ignition device (3) is connected with power storage device. An ignition end of the ignition device is connected to the furnace housing (7). The furnace housing is connected with a multi-level tar filter device (8). A purity measuring and exhaust device (9) is connected with the tar filter device. The control circuit of a blast device (5) is connected with the power storage device.    USE - Self-generating biomass gasification furnace.    ADVANTAGE - The problem of the ignition when there is no external power supply is avoided. The simple and convenient ignition device is obtained, and the fast ignition is achieved. The furnace gas is tested by the pure exhaust device. The smoke and tar blocking are eliminated.    DESCRIPTION OF DRAWING(S) - The drawing shows a structural view of the self-generating biomass gasification furnace.    Power generation device (1)    Power storage device (2)    Ignition device (3)    Blast device (5)    Furnace housing (7)    Multi-level tar filter device (8)    Purity measuring and exhaust device (9)
NOVELTY - One end of an air outlet of a-shaped pipe fitting is connected with a 360 degrees steering pipe (15), second end is connected with streamline of a secondary oxygen pipe (13), and third end is connected to a blower (12). The other end of oxygen pipe is connected with a number of pipe fitting. The other two ends of pipe are respectively connected with an air outlet pipe (6). A stove head (10) is connected with air outlet pipe. The streamline on secondary oxygen supplying pipe are equipped with an air outlet pipe valve (7), a secondary valve (8), an air inlet pipe (5) and a purifying device (14).    USE - Plateau biomass gasification furnace.    ADVANTAGE - The combustion rate of the biomass gasification furnace is improved with single gasification fuel. Thus the secondary oxygen supply can be realized with increased combustion quality and combustion-supporting.    DESCRIPTION OF DRAWING(S) - The drawing shows a structural view of the plateau biomass gasification furnace.    Air inlet pipe (5)    Air outlet pipe (6)    Air outlet pipe valve (7)    Secondary valve (8)    Stove head (10)    Blower (12)    Secondary oxygen pipe (13)    Purifying device (14)    Steering pipe (15)
NOVELTY - The fuel cell system has a solid oxide fuel cell (12) supplied with fuel and air for producing electric power and an exhaust gas of high temperature. A reformer (13) is provided for generating hydrogen, where the hydrogen containing the carbon monoxide is cooled in a heat exchanger (11). The hydrogen is outputted from the heat exchanger by a transformer (15). The hydrogen supplied from the transformer is cooled in another heat exchanger (14) and a polymer electrolyte fuel cell (17), where the hydrogen is outputted with air for producing electric power.    USE - Fuel cell system.    ADVANTAGE - The hydrogen supplied from the transformer is cooled in a heat exchanger and a polymer electrolyte fuel cell, where the hydrogen is outputted with air for producing electric power, and thus ensures efficient and improved fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a multi-stage fuel cell system. (Drawing includes non-English language text).    Heat exchangers (11,14,16)    Solid oxide fuel cell (12)    Reformer (13)    Polymer electrolyte fuel cell (17)
NOVELTY - The method involves dropping straw in gasification furnace (18). The straw is uniformly pressed on upper portion of the gasification furnace. The gas is generated by burning the straw. The straw is cooled after passing the gas through labyrinth spraying device (35). The thickness of anoxic burning layer in the gasification furnace is controlled. The material pressing machine is raised when continuously operating the gasification furnace, so as to operate carbon scraping mechanism. The straw carbon is discharged from the bottom of the gasification furnace.    USE - Method for preparing straw carbon by direct-gasification of straw.    ADVANTAGE - The straw carbon can be prepared using simple and efficient process. The reliability of the preparation process can be improved. The safety can be ensured during preparation process. The cost required for preparing straw carbon can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the straw gasification device.    Hopper (1)    Feeding motor (3)    Pushing plate (5)    Gasification furnace (18)    Labyrinth spraying device (35)
NOVELTY - The device has a rice shape material structure that is connected with a material mixing motor on a pressing device in a lower horizontal rotating state. A carbon discharging device is positioned at the bottom portion of a gasification furnace. The gasification furnace is provided with an air outlet unit that is connected with water washing device, a fan, the water-sealing and filtering device and a gas storage cabinet. A feeding motor, a pushing motor, a pressing motor, a regenerating motor, a carbon discharging device and the fan are connected with a control cabinet.    USE - Poly-generation device for gasifying straw.    ADVANTAGE - The reliability of the poly-generation device is increased. The safety of the poly-generation device is ensured. The preparation process of poly-generation device is simplified. The gasifying effect of the poly-generation device is improved. The straw utilization effect of the poly-generation device is improved. The operating cost of the poly-generation cost is reduced. The straw can be directly gasified.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation method of poly-generation device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of poly-generation device.
NOVELTY - The furnace has furnace cover that is located at upper end of furnace main portion. Upper furnace grate of furnace grid is fixed on lower thermal cracking area flange. Gas discharge area is connected with screw of two flanges on lower portion of thermal cracking area. Lower furnace grate is provided with sealing ring. Water jacket layer is provided with and connected with water inlet and water outlet, whose lower portion is filled with sealed liquid. Gas discharge end of flange area is set in lower portion of opening of outlet while vent is set at upper portion.    USE - Cracking reaction furnace of biomass fuel.    ADVANTAGE - The gas discharge can be uniformed and stabilized. The application range of the reaction furnace can be widened.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the cracking reaction furnace.
NOVELTY - The tower has a box portion that is provided with a feeding system. A primary auger feeding hopper (88) is welded with a back cover plate (87) which is connected with an outer seal cylinder (85) and an inner seal cylinder (86). A water sealing cover (84) is connected with the outer seal cylinder. A control valve (79) is connected with a secondary feeding auger hopper (80) which is equipped with a material level display instrument (81). A box (41) is equipped with a separating box pressure sensor (42), and provided with a discharging plate (40).    USE - Biomass dry distillation tower.    ADVANTAGE - Since the biomass fuel is heated in large area, the biomass carbon, tar, wood acetic acid and biomass fuel gas can be decomposed effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass dry distillation tower.    Discharging plate (40)    Box (41)    Separating box pressure sensor (42)    Control valve (79)    Secondary feeding auger hopper (80)    Material level display instrument (81)    Water sealing cover (84)    Outer seal cylinder (85)    Inner seal cylinder (86)    Back cover plate (87)    Primary auger feeding hopper (88)
NOVELTY - The device has liquid outlet that is arranged at side of lower portion of spray type condenser and is connected with inlet of oil pump. Liquid inlet is located at top portion of condenser. Cooling water inlet and cooling water outlet of condenser are extended to outer portion of main portion. A liquid product outlet is arranged at bottom portion of condenser. Condensing section is arranged in upper portion of condenser. Heat exchange section is arranged in lower portion of condenser. A non-condensed gas outlet is arranged at other side of lower portion of condenser.    USE - Classification type condensing device used in coal and biomass pyrolysis device.    ADVANTAGE - High temperature pyrolysis steam can be generated, since the heat exchange section is arranged in the lower portion of the condenser. Hence the coal and biomass pyrolysis device can be cooled easily. The pyrolytic liquid products can be classified easily in the condensing process.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the condensing device.
NOVELTY - A water inlet pipe (17) is connected with a water preheating pipe coil (21). The water preheating pipe coil is located in a flue (25) of smoke outlet (18). A steam generating pipe coil (22) is connected with water pre-heating pipe coil. An organic garbage carbonization furnace exhaust pipe (2) is connected with a steam turbine generator (4). The steam generator and exhaust pipe (5) are connected with gas liquid separator exhaust pipe. A gas-liquid separator (11) is connected to steam generator (16) by fuel gas pipe (13).    USE - Superheated steam carbonization furnace for processing organic waste.    ADVANTAGE - The efficiency and operability of the carbonization furnace can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the carbonization furnace.    Organic garbage carbonization furnace exhaust pipe (2)    Steam turbine generator (4)    Exhaust pipe (5)    Gas-liquid separator (11)    Fuel gas pipe (13)    Steam generator (16)    Water inlet pipe (17)    Smoke outlet (18)    Water preheating pipe coil (21)    Steam generating pipe coil (22)    Flue (25)
NOVELTY - The system has spiral flow reactor that is equipped with electric heating device. The electric heating device (4) is provided with insulating layer (5). The spiral flow reactor (3) is connected with grain discharge valve (6). The grain discharge valve is connected with granule collector (7). The granule collector is connected with solid particle circulate pipe (8).    USE - Reactor system.    ADVANTAGE - The yield of the bio-oil is improved, the reaction time is shortened and heating rate is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the reactor system.    Spiral flow reactor (3)    Electric heating device (4)    Insulating layer (5)    Grain discharge valve (6)    Granule collector (7)    Solid particle circulate pipe (8)
NOVELTY - An ecological purifying ditch comprises front and terminal ends having water feeding region and water discharging region. A rear end of the water discharging region is connected with a water discharging pipe. A multi-level purifying region is connected between the water feeding and water discharging regions in series. A height of the ditch bottom gradually reduces to be connected in a graded water decreasing manner. A collected water reusing well is arranged among each purifying region.    USE - Ecological purifying ditch for sewage.    ADVANTAGE - The ditch has high treatment efficiency, low operation energy consumption, small area, convenient management, and flexible arrangement.    DETAILED DESCRIPTION - Ecological purifying ditch comprises front and terminal ends having water feeding region and water discharging region. A rear end of the water discharging region is connected with a water discharging pipe. A multi-level purifying region is connected between the water feeding and water discharging regions in series. A height of the ditch bottom gradually reduces to be connected in a graded water decreasing manner. A collected water reusing well is arranged among each purifying region. Each purifying region has gravel filler and plant. A grain size of the gravel in purifying region is gradually reduced from front part to rear part along the ecological purifying ditch. The purifying region has partition wall. Water flow is divided into upper and lower folded flows via the holes on upper or bottom part of the partition wall.
NOVELTY - The method involves crushing plant waste straw, branch, fruit shell, leaf in agriculture and forestry for a biomass fuel block. A biomass fuel block forming machine is utilized for extruding and shaping a material. The biomass fuel block is extruded with circular or polygon shapes. The biomass fuel block is gasified into a pyrolysis gasification furnace and provide large amount of combustible gas. The combustible gas is transported to a tank through a gas pipeline. The combustible gas is replaced by petroleum natural gas that is supplied to a cell and a park.    USE - Method for producing a plant waste manufacturing biomass fuel block gasification air supply system.    ADVANTAGE - The method ensures easy storage, high heat value, easy burning, gasification of combustion-supporting gas and reducing investment cost, floor area, processing period, running cost, and avoids slag in biomass fuel block. The method enables replacing resources to fossil fuel gas in large area for providing gas and achieving national policy of energy conservation and emission reduction.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of a plant waste manufacturing biomass fuel block gasification air supply system producing method.
NOVELTY - Producing L-carnitine tartrate, comprises precipitating L-carnitine tartrate from a reaction mixture comprising L-carnitine and tartaric acid, where the reaction mixture is dissolved in ethanol having a water content of less than 5 wt.%.    USE - The process is useful for producing of L-carnitine tartrate.    ADVANTAGE - The process: is energy-efficient; avoids high and low temperatures; requires relatively low amounts of reactants, solvents (which can be recycled and reused in the process); yields L-carnitine tartrate and L-carnitine content in high amounts; and is relatively simple and the reactants are readily available.
NOVELTY - The method involves increasing contact area between fuel cell separating board (200) and electrode assembly. The laser is irradiated on the surface of fuel cell separating board and multiple groove portions (201) which are formed on fuel cell separating board.    USE - Processing method of fuel cell separating board.    ADVANTAGE - The size and depth of fuel cell separating board can be controlled. Hence the current collecting ratio of fuel cell separating board is improved efficiently. The uniform quality heat of fuel cell separating board can be improved reliably.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view illustrating the processing method of fuel cell separating board. (Drawing includes non-English language text)    Stage (40)    Fuel cell separating board (200)    Groove portion (201)
NOVELTY - A recombinant microorganism (A1) comprising at least one DNA molecule encoding a polypeptide that catalyzes a substrate to product conversion selected from: (a) pyruvate to acetolactate, (b) acetolactate to 2,3-dihydroxyisovalerate, (c) 2,3-dihydroxyisovalerate to isobutyraldehyde, and (d) isobutyraldehyde to isobutanol, is new. The at least one DNA molecule is heterologous to the microorganism and the microorganism produces isobutanol.    USE - For producing isobutanol or 2-butanol from pyruvate (claimed), isobutanol or 2-butanol are useful as biofuels and as commodity chemicals.    ADVANTAGE - The recombinant microorganisms provide the isobutanol while circumventing the need for the dihydroxyacid dehydratase (DHAD) and 2-keto-acid decarboxylase (KIVD) enzymes. The microorganisms produce isobutanol or 2-butanol most economically and with high yields.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) producing (M1) isobutanol involving: (i) providing the recombinant microorganism (A1) comprising an isobutanol producing metabolic pathway, and (ii) cultivating the microorganism in a culture medium containing a feedstock providing a carbon source until the isobutanol is produced;    (2) new recombinant microorganism (B1) comprising at least one DNA molecule encoding a polypeptide that catalyzes a substrate to product conversion selected from: (a1) pyruvate to acetolactate, (b1) acetolactate to 2,3-dihydroxy-2-methylbutanoic acid, (c1) 2,3-dihydroxy-2-methylbutanoic acid to 2-butanone, and (d1) 2-butanone to 2-butanol, where the at least one DNA molecule is heterologous to the microorganism and the microorganism produces 2-butanol; and    (3) producing (M2) 2-butanol involving: (i) providing the recombinant microorganism (B1) comprising a 2-butanol producing metabolic pathway, and (ii) cultivating the microorganism in a culture medium containing a feedstock providing a carbon source until the isobutanol is produced.
NOVELTY - Product comprises microorganisms, organic substance degradation enzyme, vitamin and several minerals, where the product is made from fiber disposable toiletry material.    USE - The product is useful for microbiological wastewater treatment.    ADVANTAGE - The product does not generate offensive odor chosen from hydrogen, ammonia and sulfide, as pineapple enzyme is used and does not produce clogging of the tank.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of microbiological wastewater treatment, which involves introducing wastewater containing the toiletry material into biological sewage disposal tank, and decomposing the product in the tank.
NOVELTY - A recombinant Myceliophthera thermophilus lignocellulose degradation enzyme, given in the specification (Table 1 or Table 2), where the enzyme is selected from a glycohydrolase, an esterase, an oxidase, and an oxidoreductase, is new.    USE - The recombinant M. thermophilus lignocellulose degradation enzyme, composition, and method are useful for degrading a cellulosic biomass (claimed).    ADVANTAGE - The recombinant M. thermophilus lignocellulose degradation enzyme and method efficiently degrade a cellulosic biomass.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) an isolated nucleic acid encoding a polypeptide;    (2) a recombinant vector comprising the isolated nucleic acid, where the nucleic acid is operably linked to a promoter;    (3) a host cell comprising the recombinant vector;    (4) a method of producing the lignocellulose degradation enzyme, comprising culturing the cell that comprises the recombinant vector under conditions in which the enzyme is produced;    (5) a method for degrading a cellulosic biomass, comprising contacting the cellulosic biomass with a composition comprising the recombinant lignocellulose degradation enzyme, or a recombinant lignocellulose degradation enzyme having an amino acid sequence selected from SEQ ID NO: 180-720, all even sequences only; or selected from SEQ ID NOS: 12-178, all even numbers only, sequences not defined here may be found at ftp://ftp.wipo.int/pub/published_pct_sequences/publication; and    (6) a composition comprising a cellulase and a recombinant cellulase and a recombinant lignocellulose degradation enzyme.
NOVELTY - Saccharification of lignocellulosic biomass involves contacting lignocellulosic biomass with any one type of microorganism, preferably Streptomyces-derived recombinant protein comprising an amino acid sequence of any one of 8 (318-1019) amino acid sequences (SEQ ID NOs: 2-16) (even numbers) all fully defined in the specification with lignocellulosic biomass saccharogenic amylase.    USE - The method is useful for saccharification of lignocellulosic biomass (claimed), e.g. bamboo, woody plant and sawdust for producing bioethanol.    ADVANTAGE - The method improves saccharification of lignocellulosic biomass, as Actinomyces-derived saccharogenic amylase is added to commercially available cellulase.
NOVELTY - A hydrogen generator (1) consists of a modifier (3) which produces a hydrogen-containing gas by reforming a source gas and steam, a heat exchanger (5) for heat-exchanging between hydrogen-containing gas sent from the modifier, and mixed gas of source gas and steam, and a hydrodesulfurizer (6) which removes sulfur compound contained in the source gas. The hydrodesulfurizer is arranged such that the exterior of heat exchanger is heated by hydrogen-containing gas during or after passage.    USE - Hydrogen generator is used in fuel cell systems (claimed).    ADVANTAGE - The hydrogen generator enables easy generation of hydrogen-containing gas, and carries out hydrodesulfurization at suitable temperature.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen generator. (Drawing includes non-English language text)    Hydrogen generator (1)    Modifier (3)    Combustor (4)    Heat exchanger (5)    Hydrodesulfurizer (6)
NOVELTY - The waste heat generated during the electrolysis of water (1) is stored, and the heat energy is converted into electrical energy by steam turbine process. The temperature level of the waste heat is raised by the heat pump process which is performed in two stages. The hydrogen (3) and/or oxygen (4) generated by the electrolysis is utilized in a fuel cell to produce electric current (18).    USE - Method for producing hydrogen used in fuel cell (claimed), by electrolysis of water.    ADVANTAGE - Hydrogen gas can be produced more economically by the electrolysis process. The heat energy of stored waste heat is converted into electrical energy which is efficiently delivered to the public. The compressor can be driven favorably by an electric drive, and compaction of the production device is achieved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production device of hydrogen by electrolysis of water.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the production device of hydrogen.    Electrolyzer (E)    Water (1)    Hydrogen (3)    Oxygen (4)    Electric current (18)
NOVELTY - The fuel cell includes a fuel gas flow channel (11) which extends along the inner side of a plane parallel to the main surface of a support substrate (10). The inflow port and outflow port of the fuel gas flow channel are formed in one of the short sides of the support substrate.    USE - Fuel cell for generating electricity.    ADVANTAGE - Prevents deformation of the support substrate when the support substrate receives an external force. Suppresses formation of cracks in a solid electrolytic membrane resulting from stress concentration, thus preventing deterioration of the gas-seal function of the solid electrolytic membrane.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of a portion of a fuel cell.    Support substrate (10)    Fuel gas flow channel (11)    Fuel electrode (20)    Interconnector (30)    Solid electrolytic membrane (40)
NOVELTY - The apparatus (10) has a hydrogen discharge communicating hole (50) that is extended in lamination direction of unit cell (12) to connect the hydrogen flow path. A sealing element (78d) is provided in outer side of hydrogen discharge communicating hole in anode side separator (34). The water passage portion (60) is provided in outer side of hydrogen discharge communicating hole and to circulate water provided in the anode side separator. The cathode side separator (36) is provided with sealing element (70d) in outer side of hydrogen discharge communicating hole.    USE - Water electrolysis apparatus used for manufacturing hydrogen gas.    ADVANTAGE - Since the water passage portion circulated the water in the outer side of sealing element, the drying of outside portion of the sealing element can be prevented. The whole electrolytic membrane can be maintained in wet condition and the film thicknesses of the electrolytic membrane do not differ partially at the time of varying contact pressure even if it is at the low pressure time. The damage to the sealing element can be prevented by varying the thickness of the electrolytic membrane.    DESCRIPTION OF DRAWING(S) - The drawing shows an exploded perspective view of the water electrolysis apparatus.    Water electrolysis apparatus (10)    Unit cell (12)    Anode side separator (34)    Cathode side separator (36)    Hydrogen discharge communicating hole (50)    Water passage portion (60)    Sealing element (70d,78d)
NOVELTY - A visible light response-type photocatalyst is barium-bismuth-indium complex oxide (I).    USE - Visible light response-type photocatalyst is used for hydrogen generation device used in energy system (all claimed). Uses include but are not limited to methanol synthesis, deodorizing device, air purification apparatus, antibacterial film, antifouling film, super hydrophilic film, anti-fog film, and water purification device.    ADVANTAGE - The visible light response-type photocatalyst utilizes light of long-wavelength region (more than 640 nm), for hydrolyzing or organic-material decomposition and has improved utilization efficiency of sunlight.    DETAILED DESCRIPTION - A visible light response-type photocatalyst is barium-bismuth-indium complex oxide of formula: BaBi1-xInxO3 (I), where x is more than 0 and less than 0.3, preferably 0.25 or less and 0.1 or more. INDEPENDENT CLAIMS are included for the following:    (1) hydrogen generation device, which has a casing (73) to accommodate visible light response-type photocatalyst in contact with electrolyte solution (74) containing water. Water is decomposed by irradiation of light to the visible light response-type photocatalyst and hydrogen gas is generated; and    (2) energy system, which is provided with a line which supplies the hydrogen generated in the hydrogen generation device to a fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of hydrogen generation device.    Photoelectrode (70)    Counter electrode (71)    External circuit (72)    Casing (73)    Electrolyte solution (74)
NOVELTY - The method involves generating gaseous hydrogen in an electrolyzer (1). The gaseous hydrogen is transported to the metal hydride store at a maximum pressure of at least 1 MPa. A pressure adjusting device (11) is provided for reducing the maximum pressure. The maximum pressure is reduced to a minimum pressure by use of the pressure adjusting device. A metal hydride store (13) is fed with the gaseous hydrogen at the minimum pressure. The maximum pressure of the gaseous hydrogen is generated in the electrolyzer incorporates a polymer electrolyte membrane (PEM) (4).    USE - Method for charging metal hydride hydrogen store for fuel cell.    ADVANTAGE - The condition of the hydrogen before reaching pressure adjusting device is under a higher pressure than needed for the charging and so keeping the water content nearby zero so as to reduce volume.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for device for generating and storing hydrogen gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram illustrating a device for generating and storing hydrogen gas.    Electrolyzer (1)    Cathode compartment (2)    PEM (4)    Pressure adjusting device (11)    Metal hydride store (13)
NOVELTY - Integrated management and recycling of domestic garbage landfill comprise recycling and reusing methane generated by the garbage landfill; processing the garbage landfill leachate using self-purification processing method; and performing ecological restoration to the garbage landfill surface.    USE - Method for integrated management and recycling of domestic garbage landfill (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a system for integrated management and recycling of domestic garbage landfill comprising:    (A) a methane processing system recycling and reusing to the methane generated by the garbage landfill;    (B) a leachate processing system processing to the garbage landfill leachate using the self-purification processing method; and    (C) a surface ecological restoration system performing ecological restoration to the garbage landfill surface.
NOVELTY - Device for synthesizing alcohol-based synthetic fuels comprises methanol raw material conveying system, a solvent conveying system, carbon-12 raw material conveying systems comprising a fuel synthesis system, a self-circulating mixing system, a synthetic fuel conveying system and a finished product tank. The methanol conveying system, the solvent conveying system, and carbon-12 conveying systems are parallely connected with the inlet of the self-circulating mixing system. The outlet of the self-circulating mixing system is connected with the inlet of the fuel conveying system.    USE - The device is useful for synthesizing alcohol-based synthetic fuels.    ADVANTAGE - The device: is simple, has short process flow, has high degree of online monitoring and automation; carries out production process without raw material consumption; and does not discharge solid, liquid and gaseous wastes, thus is ecofriendly.    DETAILED DESCRIPTION - Device for synthesizing alcohol-based synthetic fuels comprises a methanol raw material conveying system, a solvent raw material conveying system, carbon-12 raw material conveying systems comprising a fuel synthesis system, a self-circulating mixing system, a synthetic fuel conveying system and a finished product tank. The methanol raw material conveying system, the solvent raw material conveying system, and carbon-12 raw material conveying systems are parallely connected with the inlet of the self-circulating mixing system. The outlet of the self-circulating mixing system is connected with the inlet of the fuel conveying system. The outlet of the synthesized fuel conveying system is connected with the inlet of finished product tank.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the device for synthesizing alcohol-based synthetic fuels.
NOVELTY - Device for producing, promoting production, stabilization and/or maintaining an emulsion formation of oil and water, comprises an object with capillary openings e.g. membrane or micro porous filter, for introducing the water and oil emulsion and an object for applying voltage causing an electro osmotic flow of at least parts of the emulsion via the capillaries.    USE - The device is useful for preparing water-in-oil emulsion, which is used as a fuel e.g. diesel/heavy fuel oil, gasoline, including aviation fuel, bio oil as vegetable oil or biodiesel (claimed).    ADVANTAGE - The device: is used with freely available degassed water, which increases the emulsion capacity; promotes the flow rate and achieves a very fine, trouble-free mixing with simultaneous stable electrical alignment of the ions and the adjacent hydrated molecules, due to effect of electro-osmosis.
NOVELTY - The furnace an air outlet pipe (2) connected with a gasification furnace body (1), an air outlet cavity and a guiding mechanism (3), where the guiding mechanism is connected with a carbon monoxide gas filtering mechanism (4). The carbon monoxide gas filtering mechanism is connected with a gas water separating mechanism (6). The guiding mechanism is connected with a fog washing mechanism (5). A lower part of the gasification furnace body is provided with a water sealing dust collecting tank (14) and a water seal dust collecting tank.    USE - Downdraft biomass fuel gasification furnace.    ADVANTAGE - The furnace has better adequately purity to carbon dioxide gas so as to prevent backfire by explosion of the gasification furnace body.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a downdraft biomass fuel gasification furnace in partial section.    Gasification furnace body (1)    Air outlet pipe (2)    Guiding mechanism (3)    Carbon monoxide gas filtering mechanism (4)    Fog washing mechanism (5)    Gas water separating mechanism (6)    Water sealing dust collecting tank (14)
NOVELTY - The furnace has a power generation device (1) connected with a power storage device (2). A circuit connecting end of an ignition device (3) is connected with the power storage device. An igniting end of the ignition device is connected with a furnace body (7). The furnace body is connected with a multi-level tar filter device (8). A purity measuring and exhaust device (9) is connected with the multi-level tar filter device. A control circuit of a blast device (5) is connected with the power storage device. The multi-level tar filter device is provided with a tar filter tank (81).    USE - Self-generating biomass gasification furnace.    ADVANTAGE - The furnace avoids non-external power supply ignition problem. The furnace is simple and convenient to use. The ignition device realizes quick ignition in an easy manner. The furnace ensures pure exhaust device testing process so as to improve purity of furnace gas and eliminate smoke and tar, thus effectively avoiding tar blocking in a pipeline.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a self-generating biomass gasification furnace.    Power generation device (1)    Power storage device (2)    Ignition device (3)    Blast device (5)    Furnace body (7)    Multi-level tar filter device (8)    Purity measuring and exhaust device (9)    Tar filter tank (81)
NOVELTY - The furnace has a furnace body whose upper part is equipped with a smoke vent opening. A lower end of the furnace body is fixed on a furnace seat. A cylindrical furnace core is arranged in the furnace body and provided with an annular interlayer air passage and a circular upper plate. The upper plate is provided with a fan-shaped opening port, which is connected with a cylindrical clapboard central hole. A lower end of the core is provided with a furnace bridge. A lower part of the bridge is provided with a bowl shaped lower disk, which is provided with a push-pull type movable air door plate.    USE - High-efficiency smokeless coal, firewood, straw and liquefied fuel gas burning furnace for use during cooking or heating process in a home and a hotel.    ADVANTAGE - The furnace is simple in structure and easy to operate, has better burning effect without smoke dust and tar, and avoids the need for utilizing an external connection pipeline and a filter while burning liquefied gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a high-efficiency smokeless coal, firewood, straw and liquefied fuel gas burning furnace.
NOVELTY - The method (M100) involves increasing a contact area between a fuel cell separating board and an electrode assembly. The laser is irradiated (S10) in the fuel cell separating board. The grooves are formed on the surface of the fuel cell separating board so that the electric-discharge machining of the fuel cell separating board is performed (S20).    USE - Processing method of fuel cell separating board.    ADVANTAGE - The surface area of the fuel cell separating board is increased even if the surface strength of the fuel cell separating board is not degraded. The current collecting ratio of the fuel cell separating board is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating processing method of fuel cell separating board. (Drawing includes non-English language text)    Method for processing fuel cell seperating board (M100)    Step for irradiating laser in fuel cell separating board (S10)    Step for performing electric-discharge machining of fuel cell separating board (S20)
NOVELTY - Method for preparing liquid fertilizer, involves separating water from organic waste sludge and subjecting the water to low aeration treatment.    USE - The method is useful for preparing liquid fertilizer from organic waste, preferably livestock barn.    ADVANTAGE - The fertilizer is cost-effective, odorless and suitable for nurturing plant growth, can be prepared simply and improves water-permeability of soil.
NOVELTY - Humus-containing case comprises combination of expanded polystyrene case with two covers.    USE - The humus-containing case is useful for adiabatic biodegradation plastic planter for greening desert (claimed) for environmental biomass formation.    ADVANTAGE - The humus-containing case is cost-effective, can be used for long period of time, and produced in large quantities, maintains circulation of ecosystem, and prevents desertification at every corner of earth without requiring excess raw materials.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for adiabatic biodegradation plastic planter for greening desert, which comprises the humus-containing case, where the root of the plastic planter prevents dryness of desert as water retention property is maintained by humus. The planter is buried in desert, and trees are planted to perform natural decomposition. The ground surface of the planter is covered with dead leaves or straw, and prevents evaporation of moisture content. Urine is applied when the soil appears to be dry, where caution is required as excess application of urine can damage growth of plant.
NOVELTY - System for collecting waste edible oil at base for every area, and processing, solidifying and molding oil into pellet form biomass fuel, and selling fuel pellet, is claimed.    USE - The system is useful for converting waste edible oil into pellet form biomass fuel (claimed) used for heating in public facilities including school of cold region, hospital and retirement home, and for cooking in household, center for providing meals and restaurant.    ADVANTAGE - The system has improved moldability and produces biomass fuel having high combustion efficiency. The system enables to process waste edible oil into energy resource in a simple manner, and stable supply of the resource, as it is not influenced by natural conditions like sunlight.
NOVELTY - Degradation of recalcitrant organic compounds present in industrial effluents using a two-step system comprises using manganese peroxidase (MnP) or versatile peroxidase (VP), chelating agents, manganese (II) and hydrogen peroxide in stirred reactors for the generation of oxidative species of manganese (III); separating outlet of enzymatic reactor into two streams, using an ultrafiltration membrane; and recovering manganese by a reverse osmosis device which returns same to the enzymatic reactor.    USE - The method is useful for degradation of recalcitrant organic compounds present in industrial effluents using two-step system (claimed).    ADVANTAGE - The method stabilizes and optimizes the catalytic action of enzymes.    DETAILED DESCRIPTION - Degradation of recalcitrant organic compounds present in industrial effluents using a two-step system comprises using manganese peroxidase (MnP) or versatile peroxidase (VP), chelating agents, manganese (II) and hydrogen peroxide in stirred reactors for the generation of oxidative species of manganese (III); separating outlet of enzymatic reactor into two streams, using an ultrafiltration membrane, where one stream, containing the enzyme(s) (MnP or VP and/or glucose oxidase (GOD)), is returned to the enzymatic reactor (step I), while the second stream, containing the oxidative species of manganese (III), is introduced into the degradation reactor (step II) in which the degradation of the recalcitrant compounds takes place in stirred reactors; and recovering manganese by a reverse osmosis device which returns same to the enzymatic reactor (step I).
NOVELTY - A bio-oil having oxygen content of 15-50 wt.% is separated into a light fraction and a heavy fraction. The mid-boiling point of heavy fraction is 100 degrees C or more than the mid-boiling point of light fraction. The portion of light fraction is hydrotreated to obtain hydrotreated light fraction.    USE - Production of renewable fuel e.g. gasoline and diesel.    ADVANTAGE - The method enables efficient production of renewable fuel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for system for producing bio-oil.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the biomass conversion system.    Biomass source (12)    Biomass feed system (14)    Solid separator (20)    Regenerator (24)    Cracker (54)
NOVELTY - Treating (10) hydrogen recycle gas in a process for converting bio-renewable feedstock into green diesel fuel, comprises either: (14) providing sponge oil, and (16) contacting the hydrogen recycle gas with the sponge oil (16); or removing light hydrocarbons from the hydrogen recycle gas by contacting the hydrogen recycle gas with a sponge oil, where the light hydrocarbons is absorbed in the sponge oil to produce purified recycle gas and propane rich sponge oil; separating the light hydrocarbons from the propane-rich sponge oil; and recovering the light hydrocarbons.    USE - The method is useful for treating hydrogen recycle gas in a process for converting bio-renewable feedstock into green diesel fuel (claimed), which can be used as a substitute for the diesel fuel produced from crude oil.    ADVANTAGE - The method and system saves energy, and reduces the heat exchange area and the amount of fresh hydrogen gas required.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a system for converting bio-renewable feedstock into green diesel fuel in the presence of a deoxygenation catalyst, comprising: a treating reactor configured to convert bio-renewable feedstock into a reaction product; a separator configured to separate the reaction product into a liquid product comprising a hydrocarbon fraction and hydrogen recycle gas; and a contact drum configured to contact sponge oil with the hydrogen recycle gas to produce purified recycle gas and a propane-rich sponge oil.    DESCRIPTION OF DRAWING(S) - The figure shows a flow diagram of a method for treating hydrogen recycle gas in a process for converting bio-renewable feedstock into green diesel fuel.    Treating hydrogen recycle gas in a process for converting bio-renewable feedstock into green diesel fuel (10)    Producing hydrogen recycle gas (12)    Providing sponge oil (14)    Contacting sponge oil with hydrogen recycle gas (16)
NOVELTY - Removing oxygen from a biologically derived oil, comprises contacting a feed (2)comprising a biologically derived oil comprising fatty acids and/or fatty acid esters having an initial oxygen content with a catalyst comprising a metal titanate, thus resulting in a product having a final oxygen content less than the initial oxygen content of the feed.    USE - The process is useful for removing oxygen from a biologically derived oil for the production of biofuels, which is useful as transportation fuel.    ADVANTAGE - The process is economical and does not require the addition of hydrogen.    DETAILED DESCRIPTION - Removing oxygen from a biologically derived oil, comprises contacting a feed comprising a biologically derived oil comprising fatty acids and/or fatty acid esters having an initial oxygen content with a catalyst comprising a metal titanate of formula (MTiO3) thus resulting in a product having a final oxygen content less than the initial oxygen content of the feed.    M = metal having a valence of 2+.    DESCRIPTION OF DRAWING(S) - The figure shows a flow diagram of a process for removing oxygen from biologically derived oil.    Feed (2)    Fixed bed reactor (4)    Treated product stream (8)    Condenser (10)    Effluent cooling water. (14)
NOVELTY - Device (1) comprises: a drying device (4) for drying the biomass; a feeding device (3) for feeding the biomass to the drying device; a discharge device (10) for discharging the dried biomass from the drying device; a mixing device (11) for supplying additives and/or products of the biomass and for mixing the additives and/or products with the biomass.    USE - The device is useful for processing and refining the biomass, preferably residues from a biogas plant, and for producing fertilizers.    ADVANTAGE - The device: exhibits simple design; has mixing device, which allows good mixing of the additives and/or products with the biomass; and produces the fertilizer in simple manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for fertilizer comprising the biomass, preferably fermentation residues from a biogas plant, and additives and/or products, where the fertilizer is produced by drying the biomass, feeding the additives and/or products and mixing additives and/or products with the biomass, or produced by passing ammonia from the waste air by an ammonia scrubber and feeding an acid, base and/or liquor.    DESCRIPTION OF DRAWING(S) - The figures 1 and 2 show a schematic top view of the device and a side view of the device. The figure 3 shows a schematic perspective view of the drying device of the device, which is designed as a drum dryer.    Device (1)    Feeding device (3)    Drying device (4)    Discharge device (10)    Mixing device (11)
NOVELTY - A hydrogen is produced by making working electrode and counter electrode contact culture solution (4) containing electron-acceptor substance (3), microorganisms (2) and organic substance (5), oxidizing reduced form of electron-acceptor substance produced by electron transport reaction of microorganisms with working electrode by giving electrical potential difference between working electrode and counter electrode, culturing microorganisms, decomposing organic substance into microorganisms, and collecting hydrogen generated from counter electrode.    USE - Production of hydrogen.    ADVANTAGE - The versatility of hydrogen production method using microorganisms is significantly improved.    DETAILED DESCRIPTION - A hydrogen is produced by making working electrode and counter electrode contact culture solution (4) containing electron-acceptor substance (3) as electron acceptor of microorganisms (2), microorganisms and organic substance (5) which may be assimilated by microorganisms, oxidizing reduced form of electron-acceptor substance produced by electron transport reaction of microorganisms with working electrode by giving electrical potential difference between working electrode and counter electrode, culturing microorganisms, decomposing organic substance into microorganisms, and collecting hydrogen generated from counter electrode. An INDEPENDENT CLAIM is included for a hydrogen production apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the hydrogen production method.    Hydrogen production apparatus (1)    Microorganisms (2)    Electron-acceptor substance (3)    Culture solution (4)    Organic substance (5)
NOVELTY - The device has a gasification unit having pyrolysis gasification furnaces, a pair of reaction chamber and towers that are connected with each other through an air channel. A torch portion of the pyrolysis gasification furnace is provided with an explosion-proof device.    USE - Garbage processing device.    ADVANTAGE - The garbage processing device can be operated effectively. The garbage processing device is environment-friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the garbage processing device.
NOVELTY - Water electrolysis cell comprises proton-conductive porous electrolyte (GG), electrode (anode (EE) and cathode (CC)) which comprises a water-repellent material and joined on both surfaces of the porous electrolyte, respectively, and unit to supply water to porous electrolyte. The other side of the joint surface with the porous electrolyte of anode or cathode comprises oxygen gas or hydrogen gas in the gaseous phase.    USE - The water electrolysis cell is useful as fuel cell in electric vehicle and hydrogen fuel cell in car for producing hydrogen and oxygen in gas phase.    ADVANTAGE - The water electrolysis cell comprises electrolytic membrane having strong mechanical strength and water-repellant material which blocks permeation of water and allows gas to pass, pressurize the porous electrolyte, consume low power, and can be manufactured easily.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of water electrolysis cell. (Drawing includes non-English language text)    Feed water (AA)    Sealing agent (BB)    Cathode (CC)    Cathode chamber (DD)    Anode (EE)    Anode chamber (FF)    Porous electrolyte (GG)
NOVELTY - The system (10) has a pump apparatus (100) that is positioned near a depressurization piping (88a). A pressure detection apparatus (150) detects the primary side pressure and secondary side pressure of pump apparatus. A control apparatus (18) is provided for controlling the pump apparatus and supplying the hydrogen to a secondary side portion of pump apparatus from a primary side portion of pump apparatus on detecting that the secondary side pressure of pump apparatus is more than the primary side pressure of pump apparatus.    USE - Water electrolysis system.    ADVANTAGE - The damage caused to a sealing element of water electrolysis system at the time of the depressurization of water electrolysis system is prevented. The discard of hydrogen in sealing element of water electrolysis system is prevented. The manufacturing cost of the water electrolysis system is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for depressurization method of water electrolysis system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of water electrolysis system. (Drawing includes non-English language text)    Water electrolysis system (10)    Control apparatus (18)    Depressurization piping (88a)    Pump apparatus (100)    Pressure detection apparatus (150)
NOVELTY - Treating molecular sieve particles comprising the treated molecular sieve particles dispersed in a crosslinked polymer continuous phase, comprises: selecting molecular sieve particles suitable for use in a mixed matrix membrane; and polymerizing a polymer which is compatible with the polymer to be employed in the mixed matrix membrane in the presence of the molecular sieve particles to obtain treated molecular sieve particles.    USE - The method is useful for treating molecular sieve particles which are used in mixed matrix membrane (claimed) for gas separations.    ADVANTAGE - The method provides the molecular sieve particles with enhanced permeability and selectivity properties.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a mixed matrix membrane for separating carbon dioxide and methane, comprising a crosslinked polymer continuous phase and treated molecular sieve particles dispersed in the continuous phase, where the membrane have a carbon dioxide/methane ideal selectivity of at least 5% higher at 65 psia and 35 degrees C than a comparable membrane with untreated molecular sieve particles.
NOVELTY - Hydrogen generation device (100), comprises: a tank (110) containing a reaction solution; a porous structure (120) with a solid reactant (60a) distributed in it; and a guide structure (130) connected with the tank, where the guide structure is adapted to guide the reaction solution in the tank to the porous structure, such that the reaction solution reacts with the solid reactant to generate hydrogen.    USE - The hydrogen generation device is useful in a fuel cell (claimed), to generate electricity.    ADVANTAGE - The hydrogen generation device enhances the generation efficiency of hydrogen.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a hydrogen generation method, comprising: providing a porous structure with the solid reactant distributed in the porous structure; and guiding a reaction solution to the porous structure such that the solid reactant reacts with the reaction solution to generate hydrogen.    DESCRIPTION OF DRAWING(S) - The figure illustrates a hydrogen generation device.    Solid reactant (60a)    Hydrogen generation device (100)    Tank (110)    Porous structure (120)    Guide structure (130)
NOVELTY - The processor has a crushing device (30) arranged on a lower part of a feeding device (20). Another feeding device (60) is arranged on a stirring container (50). A stirring blade device is provided with a stirring blade (41), a stirring shaft (43) and a stirring motor (45). The stirring motor drives the stirring shaft. The stirring container is arranged on the crushing device, where the stirring container is arranged on a bottom surface of a filter leaf (51). A heating device (70) is arranged on a processor, and a storage device (90) is arranged on the stirring container.    USE - Kitchen rubbish processor.    ADVANTAGE - The processor ensures stirring kitchen solid rubbish in a container by realizing a heating under dual function to continuously and quickly perform hydrolyzing and fermenting process. The processor realizes complete hydrolysis treatment of kitchen rubbish with environment-friendly and convenient processing technique.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a kitchen rubbish processor.    Feeding devices (20, 60)    Crushing device (30)    Stirring blade (41)    Stirring shaft (43)    Stirring motor (45)    Stirring container (50)    Filter leaf (51)    Heating device (70)    Storage device (90)
NOVELTY - A vehicle-mounted ultra-small hydrogen generator comprises ultra-small reactor for vehicle-mounted thermal decomposition which decomposes acetylene as starting material into hydrogen and carbon at less than or equal to 500 degrees C.    USE - A vehicle-mounted ultra-small hydrogen generator.    ADVANTAGE - The generator can produce a lot of hydrogen economically.
NOVELTY - The container has liquid inlet tube (11) that introduces liquid in container main portion (21). An inlet (14) is provided with float (13) which is connected with inflexible tube (6a) through flexible tube (5a). One end of flexible tube (5b) is connected with inflexible pipe (6b), and the other end of flexible tube is provided with a water-intake port (8). The liquid in container main portion is sucked through liquid discharge pipe (12). The water supplied to the hydrogen-producing material is accommodated by container main portion.    USE - Liquid container of hydrogen production apparatus used for fuel cell system (both claimed) used for motor vehicle.    ADVANTAGE - The liquid container can supply the liquid stably, even if the container is inclined in any direction. The container can be used stably for a long term. The malfunction of the fuel cell due to the supplied water content can be prevented. Fuel cell with favorable battery performance can be obtained.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) hydrogen production apparatus; and    (2) fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the liquid container.    Flexible tubes (5a,5b)    Inflexible tubes (6a,6b)    Water-intake port (8)    Cover portion (10)    Liquid inlet tube (11)    Liquid discharge pipe (12)    Float (13)    Inlet (14)    Container main portion (21)
NOVELTY - Utilization of carbon dioxide in biogas comprises removing impurity and crushing biomass raw material; adjusting pH of raw material liquid at 7; fermenting treated raw material to obtain mixing gas of carbon dioxide (CO2) and methane; transporting mixing gas to biological reactor using CO2 of mixing gas as carbon source and energy needed for algae growth in illuminating biological reactor; recycling electric energy by microorganism fuel cell system; and illuminating biological reactor and microorganism fuel cell to reduce CO2 content in bio-gas.    USE - Utilization of carbon dioxide in biogas.    ADVANTAGE - The method increases energy conversion efficiency of whole system.    DETAILED DESCRIPTION - Utilization of carbon dioxide in biogas comprises removing impurity and crushing biomass raw material; adjusting pH of raw material liquid at 7; fermenting treated raw material to obtain mixing gas of carbon dioxide (CO2) and methane; transporting mixing gas to biological reactor using CO2 as carbon source and energy needed for algae growth in illuminating biological reactor; configuring microorganism fuel device; recycling electric energy by microorganism fuel cell system composed of biological anode attached to external circuit and air cathode; and illuminating biological reactor and microorganism fuel cell to reduce CO2 content in bio-gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a process for utilizing carbon dioxide in biogas (Drawing includes non-English language text).
NOVELTY - Biogas is prepared by (1) adding white rot fungi into brewery anaerobic sludge to obtain a fundamental fermentation sludge, fermenting for 8 hours at normal temperature; (2) mixing with plant straw, tannery sludge and water to form a fermentation substrate; (3) mixing up the fermentation substrate and charging it into a fermentation device, performing dry anaerobic fermentation at normal temperature, and collecting the biogas generated in the fermentation process.    USE - Method for preparing biogas (claimed).    ADVANTAGE - The method is convenient to operate, can improve the activity of anaerobic sludge, enables complete degradation of straw, has good biogas generating effect, and realizes effective utilization of biomass resources.
NOVELTY - Gas cooling and drying device provided below the ground comprises air inlet pipe, air outlet pipe, and condensed water collecting device. The air inlet pipe and air outlet pipe are inclined pipes. The condensed water collecting device comprises condensed water collecting tube, which is provided at the air inlet and outlet pipes.    USE - Gas cooling and drying device used for cooling and drying biogas fermentation tank of methane.    ADVANTAGE - The device allows for further purification of methane; and has simple structure, low cost, convenient installation, and good maintenance.
NOVELTY - Preparing biogas comprises pre-treating mushroom bran of edible mushroom by removing impurities, drying, crushing, adding microbial agent to obtain a mixture with 50-60% water, sealing, performing anaerobic fermentation for 2-3 days, mixing the mushroom bran and cow dung, adding to a fermentation tank, controlling methane fermenting temperature at 30-40 degrees C and pool capacity of the fermentation tank at 70-80%, and carrying out biogas fermentation for 25-45 days, where per mL composite microbial agent contains 2x 109 Bacillus subtilis and 1x 109 Lactobacillus plantarum.    USE - Method for the preparation of a biogas (claimed).    ADVANTAGE - The method prevents environment pollution problem caused by waste fungi residue.
NOVELTY - Anaerobic fermentation of straw comprises utilizing a nitrogen product deoxidized in a deoxidizing reactor utilizing air as an initial nitrogen source; inoculating photosynthetic bacteria in an organic wastewater, lighting, and culturing in the nitrogen atmosphere, centrifugally separating the cultured liquid, and taking a supernatant liquor comprising an organic nitrogen product; and inactivating the organic nitrogen product, and adding in a straw anaerobic fermentation process using 400-800 mL organic nitrogen product for every 100 g straw.    USE - Method for anaerobic fermentation of straw (claimed).    ADVANTAGE - The method re-utilizes the organic wastewater and avoids pollution caused by directly discharging the organic wastewater to the environment.
NOVELTY - Preparation of a methane comprises pre-treating food waste, municipal sludge, and municipal excrement to obtain materials with particle diameters of lesser than 20-25 mm; conveying to a homogenizing tank, uniformly mixing and degrading part of a suspension substance, and reducing the particle diameters of the solid materials to lesser than 20-25 mm to obtain a fermentation substrate with a solid content of 8-12%; and conveying to an anaerobic fermentation tank, carrying out anaerobic fermentation by continuous fermentation, medium temperature anaerobic fermentation, and jet flow type mixing.    USE - Method for the preparation of methane (claimed).    ADVANTAGE - The method achieves complete material fermentation and high yield.
NOVELTY - Pretreating (M1) a solid biomass for pyrolysis, involves contacting the solid biomass with an inorganic material present in an effective amount for increasing pyrolysis yield of an organic liquid product.    USE - For pretreating a solid biomass for pyrolysis (claimed), or for fast pyrolysis to liquids.    ADVANTAGE - The method maximizes the amount of condensable biocrude vapors released from pyrolysis of solid biomass, which represents a clear economic and process advantage over existing methods and systems; pretreats a biomass material that allow biomass conversion via pyrolysis to result in higher yields of organic liquids (e.g. bio-oil); and also provides bio-oil of improved quality.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) producing (M2) an organic liquid product from a solid biomass, involving: (a) contacting the solid biomass with an inorganic material present in an effective amount for increasing pyrolysis yield of an organic liquid product; and (b) subjecting the solid biomass to a pyrolysis reaction in the presence of the inorganic material to produce the organic liquid product, where the inorganic material is selected from aluminum sulfate, ammonium hydroxide, magnesium hydroxide; and    (2) composition for pyrolysis comprising a solid biomass and an inorganic material, where at least a portion of inorganic material is accessible to at least a portion of solid biomass.
NOVELTY - The invention relates to a process and an installation for post treating residual urban muds in order to obtain a compost to be used as agricultural fertilizer. According to the invention, the process consists in that it is carried out in aeration conditions, by ensuring an amount of oxygen necessary for composting, while monitoring the functional parameters concerning the composting of urban muds in admixture with vegetable waste in a mass ratio ranging from 1:1 to 4: 1 for 30...60 days wherein a stage of aerobic mesophilic fermentation takes place at a temperature of 25...40 degrees C which consists in increasing the number of bacteria; a thermophilic stage at a temperature of 45...60 degrees C in which the present bacteria, fungi and actinomycetes decompose the cellulose, lignin and other resisting organic substances, the maximum temperature being necessarily to be maintained at least one day in order to ensure the destruction of pathogens and organic contaminants; the last stage being the ageing when temperatures are lowered and some oxidative biological processes are continued and stabilized transforming the degraded organic substrate into humus. The installation claimed by the invention consists of an aeration subassembly (A) which ensures the amount of oxygen necessary in a subassembly (B) for composting and a subassembly (C) for monitoring which measures and records the functional parameters of the process for treating the urban muds.
NOVELTY - The invention relates to a process for preparing a fuel for internal combustion engines. According to the invention, the process consists in separating the cellulose fractions by autohydrolysis with steam under a pressure of 50...70 barr, catalyzed by acid at a pH value of 2...4, a temperature of 190...220 degrees C, after which the hemicellulose-containing liquid phase is separated and the glucidic fractions contained in the solid phase are hydrolyzed by impregnation, in two stages, with diluted sulphuric acid in a concentration of 2% and 15%, respectively, the liquid glucidic phases resulting from autohydrolysis and the two hydrolysis stages being then subjected to fermentation for 36...96 h with Saccharomyces cerevisiae, at a pH value of 4...6 and a temperature of 30...40 degrees C, thereby resulting a bioethanol fuel.
NOVELTY - The invention relates to a component for a furnace fuel composition and to a composition including said component. The claimed component is prepared by the esterification of industrial olefin with glycerine at a mass ratio oleine:glycerine of 0.5...4:1 in the presence of metal oxide catalyst at a temperature of 120...250 degrees C and a pressure of 20...760 mmHg for 2...10 h, the resulting product having an acidity index of 2...40 mg KOH/g, a hydroxyl number of 140...320 mg KOH/g, a caloric power of 6,000...8,000 cal/g. The claimed composition comprises the biorenewable component and fossil fuel for furnace at a molar ratio of 0.02...0.9:1 with a caloric power of 5,500...10,100 cal/l.
NOVELTY - The present invention relates to a process for preparing simultaneously a biofuel and some tensides. According to the invention, the process consists in the transesterification of triglycerides from dehydrated fatty materials with aliphatic amine in a ratio of 2...4%, with methanol in a ratio of 12.5....16% and with guanidinium carbonate in a ratio of 0.09...0.15% as catalyst, by stirring for 3...6 h at a temperature of 67...75 degrees C, followed by the removal by distillation of a methanol complex with large content of amines and the separation after settling of the raw glycerine from the ester fraction, which is subjected to high vacuum distillation in descending film, in a first step at a temperature of 152...162 degrees C separating the fatty acid methyl esters in a ratio of 66.6...74% by weight in comparison with the fatty material, and in a second stage at a temperature of 200...216 degrees C , wherefrom there are separated the monoglycerides of fatty acids in a ratio of 18.85...23.55% by weight in comparison with the fatty material.
NOVELTY - The invention relates to a process for decomposing organic materials from solid waste. According to the invention, the process consists in treating the residual organic material in the presence of a catalyst consisting of a reduced metal selected from Ni, Cu, Zn, Fe, Pd, Ti applied onto a carrier, in a reactor under a pressure of at least 50 at, at a temperature of 250...500 degrees C, there taking place the decomposition of the organic material while producing methane, carbon dioxide, hydrogen and C2...C9 hydrocarbons, from the gaseous mixture there being recovered the hydrogen, the remainder of the gas mixture, which presents a high energetic value, being used as fuel.
NOVELTY - The method involves forming (S1) carbon layer in a base-material surface by the gaseous phase forming process. An intermediate layer is formed (S2) between base materials and carbon layer by heat-processing. The intermediate layer is provided with titanium carbide.    USE - Method for manufacturing titanium made fuel cell separator.    ADVANTAGE - The adhesiveness of the base material and the carbon layer is improved. The excellent separator can be manufactured for high electrical conductivity and durability.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of manufacturing process of the fuel cell. (Drawing includes non-English language text)    Step for removing passive-state coat (S0)    Step for forming carbon layer in base-material surface (S1)    Step for forming intermediate layer (S2)
NOVELTY - The method involves forming a mixed layer of a base-material surface (S1), which contains metal powder and carbon powder. The metal powder is formed in the base material. A rolling part is used to roll a base material (S2). A heat treatment part is heated at temperature of about 500-950 degree Celsius in nonoxidizing atmosphere (S3). A test body is interposed by a carbon cloth. Voltage is added to the carbon cloth and measured by a voltmeter. The mixed layer is formed in a single side of the base material.    USE - Method for manufacturing a fuel cell separator.    ADVANTAGE - The method enables maintaining high electric conductivity for a long time and improving adhesiveness of the mixed layer.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating a method for manufacturing a fuel cell separator.'(Drawing includes non-English language text)'    Step for forming mixed layer of a base-material surface (S1)    Step for rolling the base material (S2)    Step for heating heat treatment part at specific degree Celsius in nonoxidizing atmosphere (S3)
NOVELTY - The machine has furnace that is provided with continuous discharge port. The purified gas outlet is connected with smoke discharge port by four-way pipe. The upper portion of main structure is connected with odorizing secondary purification chamber. A box is connected with air inlet of fuel gas generator. The fuel gas dividing room bottom of odorizing secondary purification chamber is provided with multiple distributing valves. The distributing valve is divided by the dividing valve through gas pipe.    USE - Straw gas heat source machine.    ADVANTAGE - The energy consumption of straw gas heat source machine can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the straw gas heat source machine.
NOVELTY - The ternary fuel composition comprises 20-80 wt.% of biodiesel, preferably ethyl or methyl ester, 10-60 wt.% of plant oil and 10-50 wt.% lower alcohols.    USE - Ternary fuel composition for feeding diesel-cycle motors.    ADVANTAGE - The ternary fuel composition is natural, non-toxic, and biodegradable, ensures excellent technical performance, and provides complete burning of fuel, low pollutant emissions and reduced internal impurity deposit formation on internal surface of motors.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical representation depicting thermal efficiency of the ternary fuel composition. (Drawing includes non-English language text).
NOVELTY - Conversion of biomass into a biomass product, which is suitable for use as a fuel, where the biomass is of plant origin and microorganisms naturally occurring in the biomass, comprises preparing a slurry by dispersing the biomass comprising the naturally occurring microorganisms in an aqueous liquid, maintaining the slurry at conditions suitable for aerobic digestion by the microorganisms to obtain a slurry comprising the biomass product as a dispersed solid phase, and recovering the biomass product comprises washing using water as a washing liquid and drying the biomass product.    USE - The biomass product is useful as a fuel (claimed), starting material in an anaerobic digestion for the production of methane gas and as a filler material for plastics, concrete or bitumen, or for making board material for building purposes.    ADVANTAGE - The process is easy to handle, environmentally friendly, convenient for outdoor storage and economical. The process provides an improved yield of biomass product. The biomass product has a high caloric value. The biomass extract has a remarkable stability and may be stored for extended periods of time, such as weeks or months.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a combustion process comprising preparing a slurry by dispersing a biomass in an aqueous liquid, where the biomass is of plant origin and microorganisms naturally occurring in the biomass, maintaining the slurry at conditions suitable for aerobic digestion by the microorganisms to obtain a slurry comprising a biomass product as a dispersed solid phase, recovering the biomass product from the slurry comprising washing using water as a washing liquid, and combusting the biomass product.
NOVELTY - A solid fuel is obtained by heating shells after pressing kernel oil from seed of fruit of palm. The solid fuel (based on dry weight) contains fixed carbon content of 22-60 %mass, volatile material content of 30-66 %mass, ash content of 3-6 %mass, moisture content of 6 %mass or less and gross calorific value of 20-30 MJ/kg.    USE - Solid fuel is used in heat-use installation e.g. blast furnace, powdered coal burning boiler, rotary kiln of cement clinker manufacturing equipment, calcination furnace of cement clinker manufacturing equipment, waste furnace of iron-manufacture installation, and blast furnace.    ADVANTAGE - The solid fuel has excellent combustion efficiency and grindability. The solid fuel does not disperse in air, thus safe and environmentally-friendly.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of solid fuel, which involves supplying the shell after pressing kernel oil from seed of fruit of palm to heating unit, and heating at 240-350 degrees C; and    (2) manufacturing apparatus of solid fuel, which has heating unit capable of heating shell, supply unit capable of supplying shell with respect to heating unit, and heating unit.
NOVELTY - Water or heavy water is subjected to mechanochemical reaction in presence of a catalyst metal to obtain hydrogen or deuterium.    USE - Manufacture of hydrogen or deuterium used for hydrogenating or deuterating organic compound e.g. polychlorinated biphenyl (all claimed), manufacture of ammonia, aniline, nylon 66, and hydrochloric acid, and as reducing agent and fuel for internal combustion engine of car and rocket.    ADVANTAGE - The method efficiently provides hydrogen or deuterium by simple method without using expensive reagent and special catalyst. The drug containing deuterated organic compound, has high efficacy.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of deuterated organic compound, which involves performing mechanochemical reaction of organic compound, and water or heavy water in presence of catalyst metal; and    (2) dehalogenation method of halogen-containing organic compound, which involves performing mechanochemical reaction of organic compound having halogen, and water or heavy water in presence of catalyst metal.
NOVELTY - A catalyst comprising a material resulting from a process of: precipitating a nickel/aluminum (Ni/Al) layered double hydroxide at 1-100 degrees C; aging the Ni/Al layered double hydroxide at 1-100 degrees C for 1-24 hours; isolating the Ni/Al layered double hydroxide following aging; and treating the Ni/Al layered double hydroxide under a reducing atmosphere at 250-800 degrees C for 0.5-12 hours, is new.    USE - As catalyst (claimed) useful in the conversion of triglycerides and fatty acids including, those constituting vegetable oils, algal oils, and animal fats, to hydrocarbon fuels.    ADVANTAGE - The catalyst consists of highly porous NiO-Al2O3 which contains small Ni nanoparticles dispersed over the external and internal surface (pores) of the mixed oxide particles. The process allows for good dispersion of metallic Ni nanoparticles even at high nickel loading (i.e. Ni loading greater than or equal to 30%). The mixed oxide catalyst resulting from the process exhibits good mechanical properties and catalytic activity. The catalyst can be readily regenerated by heating without any damage to the underlying matrix. The mixed oxide catalyst of nickel and aluminum, is relatively easy and inexpensive to produce but provides performance similar to performance exhibited by more expensive palladium and platinum catalysts.    DETAILED DESCRIPTION - A catalyst comprising a material resulting from a process of: precipitating a nickel/aluminum (Ni/Al) layered double hydroxide at 1-100 degrees C where the Ni/Al layered double hydroxide is of formula (NixAly(OH)2)(CO3)y/2.mH2O; aging the Ni/Al layered double hydroxide at 1-100 degrees C for 1-24 hours; isolating the Ni/Al layered double hydroxide following aging; and treating the Ni/Al layered double hydroxide under a reducing atmosphere at 250-800 degrees C for 0.5-12 hours, is new.    x+y=1;    m=0.5.
NOVELTY - The spaces (14,15) are formed in a plastic material separation wall (11). A polymer electrolyte membrane (13) is arranged parallel to the separation wall. The anode (21) and cathode (22) are provided in a front-tip element connected with the polymer electrolyte membrane. A connection element is exposed to the side surface of the separation wall. A liquid introducing unit is connected to the space. A liquid discharge unit is connected to the space (15). An electrolysis cell (10) is arranged on anode and cathode, when the hydrogen gas is generated in the space.    USE - Apparatus for generating hydrogen gas in solar cell module (claimed).    ADVANTAGE - The structure of apparatus for generating hydrogen gas can be simplified. The voltage difference between the maximum output voltage of solar cell module and the electrolytic voltage in the hydrogen gas generation apparatus can be eliminated. The component reduction, size reduction and weight reduction of the apparatus for generating hydrogen gas can be attained. The electrical energy conversion efficiency of the solar cell module can be improved.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) drive method of hydrogen gas generation apparatus;    (2) electric power generation and hydrogen gas generation apparatus; and    (3) drive method of electric power generation and hydrogen gas generation apparatus.    DESCRIPTION OF DRAWING(S) - The drawings show the sectional views of the apparatus for generating hydrogen gas. (Drawing includes non-English language text)    Electrolysis cell (10)    Plastic material separation wall (11)    Polymer electrolyte membrane (13)    Spaces (14,15)    Anode (21)    Cathode (22)
NOVELTY - The apparatus has a hydrogen gas generation unit (10) that is provided with several electrolysis cells separated by a separation-wall (12) containing a portion (51) in one end of heat-transport unit (50). A solar cell (40) is attached to solar cell attaching unit (53) provided with a portion (52) in other end of heat-transport unit. The heat generated by the solar cell is transferred to the electrolysis cell from the separation-wall through the solar cell attaching unit. A polymer electrolyte membrane made of fluorine resin is arranged in parallel with separation-wall.    USE - Electric power generation and hydrogen gas generation apparatus.    ADVANTAGE - Since the heat generated by the solar cell is transferred to the electrolysis cell from the separation-wall, the hydrogen gas generation raw material can be heated easily, and the raise of the temperature of solar cell can be suppressed. The energy released and discarded as remaining heat is converted into electrical energy, thus the energy utilization efficiency and hydrogen conversion efficiency of the electric power generation and hydrogen gas generation apparatus are improved. The need of incidental equipment in the hydrogen generation apparatus is eliminated, thus the manufacturing cost of the hydrogen generation apparatus is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a conceptual diagram of electric power generation and hydrogen gas generation apparatus. (Drawing includes non-English language text)    Hydrogen gas generation unit (10)    Separation-wall (12)    Solar cell (40)    Heat-transport unit (50)    Portions of heat-transport unit (51,52)    Solar cell attaching unit (53)
NOVELTY - The system (10) has valve apparatus (26) that is connected to drain piping (24) which discharges water from a gas-liquid separation apparatus (22). A detector (150) judges whether clogging of water is produced in the valve apparatus. An ultrasonic vibrator (104) is driven to clean water passage in pressure-reduction valve (98) when clogging of water in valve apparatus is judged by the detector.    USE - Water electrolysis system used for manufacturing hydrogen gas.    ADVANTAGE - Since ultrasonic vibrator is driven to clean water passage in pressure-reduction valve when clogging of water in valve apparatus is judged by detector, cleaning of valve apparatus is made easy. The operational efficiency of the water electrolysis system is improved and smooth and reliable waste water treatment can be performed.    DETAILED DESCRIPTION - An independent claim is included for operation method of water electrolysis system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the water electrolysis system. (Drawing includes non-English language text)    Water electrolysis system (10)    Gas-liquid separation apparatus (22)    Drain piping (24)    Valve apparatus (26)    Pressure-reduction valve (98)    Ultrasonic vibrator (104)    Detector (150)
NOVELTY - The gasifier has a combustion chamber whose inner cavity is provided with an air outlet. The combustion chamber is connected with a feeding pipe. The combustion chamber is formed with a through-hole and connected with a steam pipeline. The through-hole is provided with two steam outlet ports that are located on different positions in the combustion chamber. A steam distributor is connected with a steam pipe that is provided with a stop valve. The steam pipeline is provided with a flow meter and a pressure gauge.    USE - Biomass cyclone air-steam gasifier.    ADVANTAGE - The gasifier improves gasification reaction according to biomass gas heat value, and improves yield efficiency by 20 percent.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a biomass cyclone air-steam gasifier.
NOVELTY - The gasifier has a combustion chamber connected with three steam pipelines, where each steam pipeline is provided with an outlet at different positions. A water inlet valve of the steam pipeline is connected with a steam distributor. The steam pipeline is provided with a stop valve and/or pressure gauge, and a pressure reducing valve and/or a flow meter and/or pressure gauge. An inner cavity of the combustion chamber is cylindrical in shape.    USE - Biomass air-steam gasifier.    ADVANTAGE - The gasifier improves heat about 30-40 percent, and increases gas yield by 20 percent.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a biomass air-steam gasifier.
NOVELTY - Processing mushroom waste culture medium, involves spin-drying the waste culture medium produced after mushroom cultivation, squeezing juice from the dried medium to obtain culture solution, culturing yeast in the culture solution, isolating microbial cell from the cultured yeast, cleaning the dried waste culture medium, regulating the moisture content of the spin-dried waste culture medium, and obtaining regenerated culture-medium material.    USE - The method is useful for processing mushroom waste culture medium for obtaining base material for fertilizer, and combustion base material of recycle solid fuel.    ADVANTAGE - The method enables recycling of mushroom waste culture medium cost-effectively, purification of culture medium easily, and rapid heat sterilization of fossil fuels.    DETAILED DESCRIPTION - Method of processing mushroom waste culture medium, involves (a) spin-drying the waste culture medium produced after mushroom cultivation, (b) squeezing juice from the dried medium, and sterilizing obtained juice by heat to obtain culture solution, (c) culturing yeast in the culture solution, propagating and isolating microbial cell from the cultured yeast that is floating in the upper surface of the culture solution, (d) cleaning the dried waste culture medium, (e) repeating above-mentioned steps (a) and (b) to obtain squeezing juice, (f) regulating the moisture content of the spin-dried waste culture medium, and (g) obtaining regenerated culture-medium material.
NOVELTY - Method of manufacturing devulcanizing/desulfurizing agent, involves mixing acidic solution containing nickel and basic solution containing molybdenum, allowing the mixture to react, and producing a coprecipitate at 50-90 degrees C, where the pH of the solution after mixing is 6-8, the nickel is derived from nickel sulfate and the acid solution is prepared at pH of 3-4.    USE - The method is useful for devulcanizing agent for hydrocarbons used for desulfurization for producing hydrogen for fuel cell.    ADVANTAGE - The agent has improved lifetime, and break time.
NOVELTY - A metal complex comprises metal ion(s) chosen from group II and group VII-XII, an organic ligand having tetra-carboxy di-imido skeleton in which bidentate coordination is possible, and a dicarboxylic acid compound (I).    USE - Metal complex is used for absorbent and occlusion material for absorbing and occluding carbon dioxide, hydrogen, carbon monoxide, oxygen, nitrogen, 1-4C hydrocarbon, noble gas hydrogen sulfide, ammonia, sulfur oxide, nitrogen oxide, siloxane, water vapor and organic vapor, and separating material for separating carbon dioxide, hydrogen, carbon monoxide, oxygen, nitrogen, 1-4C hydrocarbon, noble gas hydrogen sulfide, ammonia, sulfur oxide, nitrogen oxide, siloxane, water vapor and organic vapor, or methane and carbon dioxide, ethylene and carbon dioxide, hydrogen and carbon dioxide, nitrogen and carbon dioxide, air and methane, methane and ethane, ethylene and ethane, ethylene and acetylene, ethane and propane, propane and propene, and methane, ethane and propane (all claimed).    ADVANTAGE - The metal complex has excellent gas-adsorption performance, gas occlusion capacity and gas-separation performance.    DETAILED DESCRIPTION - A metal complex comprises metal ion(s) chosen from group II and group VII-XII, an organic ligand having tetra-carboxy di-imido skeleton in which bidentate coordination is possible, and a dicarboxylic acid compound of formula (I).    R1-R4=H, optionally substituted alkyl, alkoxy, optionally substituted formyl, acyloxy, alkoxycarbonyl, nitro, cyano, amino, monoalkyl amino, dialkylamino, acylamino or halo;and    R1+R2 or R3+R4=alkylene or alkadienylene (both optionally substituted).    When R1-R4 are H, then R1 and R3, or R2 and R4 is not halogen. An INDEPENDENT CLAIM is included for manufacture of metal complex, which involves reacting dicarboxylic acid compound (I), organic ligand in which bidentate coordination is possible and metal ion chosen from group II and group VII-XII in presence of a solvent.
NOVELTY - The device (1) has filter column set at upper portion provided with sewage inlet for collecting dirt liquid portion of metal frame (2). The drawer container (12) is arranged along flow path, and is provided with outlet opening (38) at bottom portion to form filter material (36) corresponding to filter block. The drawer containers are extended parallel along transverse direction to path and are stacked on top portion, so the dirt in liquid portion is orderly crossed. Drawer container is slid out to remove and replace filtering block when being saturated.    USE - Device for obtaining biological quantity from organic dirt.    ADVANTAGE - Since the drawer container is slid out to remove and replace the filtering block when being saturated, the changing of height position of the drawer container can be realized effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for obtaining biological quantity from organic dirt.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device of obtaining biological quantity from organic dirt.    Biological quantity obtaining device (1)    Metal frame (2)    Drawer container (12)    Filter material (36)    Outlet opening (38)
NOVELTY - The method involves molding a sheet lamination flat type pre-form for a fuel cell carbon complex separator through an injection molding process. A compression molding machine is a pre-form shaped over melting point of a binder, so that a wave plate type flow path is formed. The compression molding machine is cooled by less than the melting point of the binder. An extrusion process is applied by using a T-die, where an adhesive application line is made as a compression mold for molding a manifold and a gasket groove.    USE - Method for manufacturing a fuel cell carbon complex separator of a fuel cell (claimed).    ADVANTAGE - The method enables inducing pressure molding and material charge according to flow path location and molding pressure accordingly, so that intensity of the separator is improved, thus achieving uniform sheet lamination.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic illustration of a method for manufacturing a fuel cell carbon complex separator of a fuel cell.'(Drawing includes non-English language text)'
NOVELTY - Method for extracting total iridoid glycoside from herba hedyotis diffusae, involves (a) crushing herba hedyotis diffusae into crude powder, extracting the crude powder using ethanol in a supercritical extraction tank, and collecting the extract, (b) extracting the extract with 5-6 volumes of ethanol repeatedly, and concentrating the extract, and (c) treating the concentrate with macroporous adsorption resin, eluting with ethanol, collecting eluent, concentrating and filtering the eluent with a membrane, and vacuum-drying to obtain total iridoid glycoside.    USE - The method is useful for extracting total iridoid glycoside from herba hedyotis diffusae.    ADVANTAGE - The method does not use harmful reagents, is environmentally-friendly as it does not cause pollution, and can be easily industrialized.    DETAILED DESCRIPTION - Method for extracting total iridoid glycoside from herba hedyotis diffusae, involves (a) crushing whole herba hedyotis diffusae into crude powder, adding the crude powder into a supercritical extraction tank, extracting the crude powder using ethanol as entrainer, and collecting the extract, (b) adding the extract into a Soxhlet extractor, extracting with 5-6 volumes of ethanol for 3-6 hours repeatedly, and concentrating the extract until the alcohol smell vanishes, and (c) treating the concentrate with macroporous adsorption resin, eluting with 0-10% ethanol and 30-80% ethanol, collecting eluent, concentrating and filtering the eluent with a membrane, and vacuum-drying to obtain total iridoid glycoside.
NOVELTY - The device has a spiral rod and a bin cover that are linked together via a spiral structure. Surfaces of a steel bin housing and a mesh steel bin are coated with oil-unattached paint. A head part of the rod is provided with a round-shaped stainless steel cake. The rod is utilized for compressing and dehydrating kitchen rubbish. A waste oil collecting tank collects waste oil after reaching an oil guiding port. A pedal-type water outlet is opened for discharging sewage when sewage flows out. A disk-type screw head is utilized for extruding and dehydrating the rubbish via rotating the spiral rod.    USE - Kitchen rubbish pre-processing device for use during ethanol production and aerobic or anaerobic fermentation.    ADVANTAGE - The device utilizes a re-usable geotextile bag for separating oily water from the kitchen rubbish that is conveniently separated into solid rubbish in a simple manner. The device is simple in structure and convenient to operate, and saves energy and dehydrates the kitchen rubbish in an effective manner. The device utilizes kitchen rubbish resources during ethanol production and aerobic or anaerobic fermentation.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a kitchen rubbish pre-processing device.
NOVELTY - A garbage percolate processing method comprises using environment mineral material, agricultural straw, composite flocculating agent to remove heavy metal and suspended material and chemical oxygen demand in garbage leachate; removing ammonia nitrogen by anaerobic-aerobic biological method for salt bittern and environmental mineral material advanced treatment; and performing composite artificial wetland processing, and standard-reaching column recycling process.    USE - Garbage percolate processing method.    ADVANTAGE - The method has low cost and low energy consumption and has no three wastes discharge. The garbage percolate waste is changed into useful products. Garbage produced by incineration power plant can be used as the fuel.
NOVELTY - Solar rectifying device comprises a crude slide storage tank and a rectifying tower. The crude slide storage tank is connected to a solar heat-collecting evaporator inlet. The outlet of the solar heat-collecting evaporator is connected with a vapor-liquid separating inlet, and the vapor-liquid separating outlet is connected with the rectifying tower inlet.    USE - Used as a solar rectifying device.    ADVANTAGE - The device is economical and environmental friendly; has simple structure, and convenient operation and saves energy; and promotes the yield of ethanol.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the solar rectifying device.
NOVELTY - A self sustaining and combined dual biomethanation system to produce biogas and manure, is disclosed. The system for biomethanation process comprises two or more different biogas reactors using mixed and/or multiple solid biomass as feed. The leachates generated through the displaceable percolating container proximally placed inside the solid digester are utilized by recirculating the leachates produced, thereby ensuring optimum biogas generation with significant reduction in the size of the methane digesters. Image 0/0
NOVELTY - Recycling of livestock manure involves collecting livestock manure from dairy industrial area, performing desulfurization and deodorization by plasma reactor in small-scale plant, storing produced hydrogen as energy of storage battery in liquid state, and restoring to area.    USE - Recycling of livestock manure.    ADVANTAGE - The increase in efficiency of required energy and scale of installation and reduction of cost are attained.
NOVELTY - Photobioreactor system for obtaining biotechnology products comprises a binary culture made up of a combination of a prototrophic organism and a heterotrophic organism, where photobioreactor has a chamber with a height to diameter ration greater than two, an integrated heat sink and an artificial lighting system comprised of light emitting diodes (LEDs) arranged in a spaced configuration.    USE - The photobioreactor system is useful for obtaining biotechnology products. The system and methods are useful for simultaneously generating algal biomass carotenoids and reducing nutrient loads in starch wastewater; and for producing biofuel (all claimed).    ADVANTAGE - The improvement in the invention leads to significant savings in energy consumption and allows for the design of photobioreactors of any desired shape. The invention also allows for the use of a variety of types of waste materials to be used as the organic starting material.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a method for simultaneously generating algal biomass carotenoids and reducing nutrient loads in starch wastewater comprising incubating nutrient loads with a co-culture of at least two heterogenous organisms in a closed photobioreactor system bioreactor; and    (2) a method for producing a biofuel comprising incubating a co-culture of a methane-oxidizing phototrophic microorganism and a heterotrophic microorganism in a controlled illuminated environment containing a mineral medium sparged by methane (CH4).
NOVELTY - The furnace has a furnace body provided with a cylindrical furnace core that is provided with an air passage i.e. annular interlayer. The furnace body and the furnace core are arranged under an air channel of the annular interlayer that is provided with upper and lower air channels. An upper box is installed inside an upper wind passage that is connected through an air box. The furnace core is provided with an upper plate. An opening port is connected with a clapboard central hole. A lower disk is provided with a push-pull type movable air door.    USE - Smokeless firewood furnace for use in a house and a hotel to cook or heat foods.    ADVANTAGE - The furnace has better burning effect, simple structure and easy operation, and can use coal, firewood, straw and combustible waste as fuel. The furnace avoids generation of smoke and dust.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a smokeless firewood furnace.
NOVELTY - The fuel cell has a desulfurization unit (200) and a water supply part for supplying water to the to the desulfurization unit. A fuel generating unit (400) and a fuel pre-processing unit (500) are also provided.    USE - Fuel cell for steam power station.    ADVANTAGE - The fuel cell has desulfurization unit and water supply part for supplying water to desulfurization unit, and fuel generating unit and fuel pre-processing unit are also provided, and thus the fuel cell is simple and improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of fuel cell. (Drawing includes non-English language text).    Fuel supply part (100)    Desulfurization unit (200)    Fuel generating unit (400)    Fuel pre-processing unit (500)    Fuel cell stack (600)
NOVELTY - Method used for treating palm oil mill effluents (POME), involves treating the palm oil mill effluents with concentrated butyrate; introducing the treated palm oil mill effluents into reaction tank (11) with loading rate of at least 1.5 g COD/L/d and hydraulic retention time of at least 4 days; and providing microorganism biomass at the reaction tank so that anaerobic degradation of palm oil mill effluents treated with butyrate can be performed.    USE - For treating palm oil mill effluents (POME) (claimed).    ADVANTAGE - The anaerobic degradation of palm oil mill effluents appear as efficient treatment since there are up to 99.4% palm oil mill effluents have been degraded at COD loading rate of 1.5-4.8 g COD/L/d and hydraulic retention time of 7.2 days. Furthermore, approximately 20.17 L/day biogas with 70-80% methane contents is obtained throughout the treatment operation. The method enhances the performance of existing anaerobic degradation based palm oil mill effluent treatment so that the start-up period and hydraulic retention time can be reduced. The method optimizes the production of methane throughout the anaerobic degradation based palm oil mill effluent treatment.    DESCRIPTION OF DRAWING(S) - The figure shows view of upflow anaerobic sludge blanket reactor (UASBR) system.    UASBR system (10)    Reaction tank (11)    Holding tank (12)    Peristaltic pump (13)    Biogas collector (14)    Baffle (15)    Biogas separator (16)    Methane gas holder (17)    Biogas pipe (18)    Sampling port (19)    pH and temperature indicator (20)    Sodium bicarbonate dosing tank (21)    Pressure controller (22)    Hot water tank (23)    Liquid splitter (25)    Water jacket (26)
NOVELTY - The device for heating a liquid obtained from the decomposition of an organic material, comprises a cylindrical body used as an outer envelope and closed by a lid (3) equipped with hatches and allowing the loading and evacuation of the material, a tank (2) present inside the cylinder (1) and connected to a water circuit by two pipelines (12), and a pivoting claw for stirring the decomposed material to perform the decomposition process by facilitating the arrival of oxygen. A sliding plate is provided at the cylindrical space to control the discharge of the decomposed material.    USE - The device is useful in a garden for heating a liquid obtained from the decomposition of an organic material.    ADVANTAGE - The device ensures uniform and continuous heating of the liquid obtained from the decomposition of the organic material in a highly ecological manner.    DETAILED DESCRIPTION - The device for heating a liquid obtained from the decomposition of an organic material, comprises a cylindrical body used as an outer envelope and closed by a lid (3) equipped with hatches and allowing the loading and evacuation of the material, a tank (2) present inside the cylinder (1) and connected to a water circuit by two pipelines (12), and a pivoting claw for stirring the decomposed material to perform the decomposition process by facilitating the arrival of oxygen. A sliding plate is provided at the cylindrical space to control the discharge of the decomposed material. Air vents are provided at the bottom of the cylindrical body. The pivoting claw is rotated using a crank. Two doors (4) are located in the lower part of the cylindrical body to allow the recovery of the material after decomposition.    DESCRIPTION OF DRAWING(S) - The figure shows a cross-sectional view of a device for heating a liquid obtained from the decomposition of an organic material.    Cylinder (1)    Tank (2)    Lid (3)    Two doors (4)    Two grids (6)    Two pipelines. (12)
NOVELTY - A desulfurizing agent contains (in %mass) nickel (50-95), molybdenum (0.5-25), calcium (0.1-3) by oxide conversion, and an inorganic oxide.    USE - Desulfurizing agent for desulfurizing hydrocarbon (claimed) e.g. kerosene, jet fuel, naphtha, gasoline, liquefied petroleum gas and natural gas, for reforming raw material for manufacture of hydrogen used in fuel cell used as power supply for motor vehicles and industries.    ADVANTAGE - The desulfurizing agent is economical. The sulfur content in hydrocarbon is efficiently removed to low concentration of ppb level, using desulfurizing agent having high durability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for desulfurization of hydrocarbon, which involves reducing sulfur content of hydrocarbon to 50 mass ppb or less using the desulfurizing agent, at 0-400 degrees C, pressure of 0.1 MPa or more, and liquid space velocity of 0.01-100 hour-1.
NOVELTY - A hydrogen generating apparatus consists of a hydrogen generator provided with a modifier and a transformer, and a material supply device. The modifier reform-reacts a raw material and produces a hydrogen-containing gas. The transformer has a shift catalyst which reduces carbon monoxide in the hydrogen-containing gas by shift reaction. The material supply device supplies raw material to the modifier. The raw material flowing into the transformer is circulated in the hydrogen generator during starting.    USE - Hydrogen generating apparatus is used for fuel cell systems (claimed).    ADVANTAGE - The hydrogen generating apparatus suppresses performance degradation of shift catalyst during starting.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) fuel cell system; and    (2) operating method of hydrogen generating apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen generating apparatus.    Material supply device (1)    Modifier (6)    Transformer (8)    Hydrogen generating apparatus (100)    Hydrogen generator (100A)
NOVELTY - Device for crushing and fermenting kitchen waste comprises shell, pushing screw rod and screw rod motor (4), where shell is provided with feeding port (1), one end of screw rod is connected with screw motor, pushing screw (5); lower part of shell is provided with solid waste collecting tank (10) and liquid collecting box (8), solid waste collecting tank is set at bottom of pushing screw propulsion at pushing direction and connected with screw rod cavity, the cavity is provided with ferment powder box with screw opening upwards and outlet provided with pushing screw ferment switch.    USE - As device for crushing and fermenting kitchen waste (claimed).    ADVANTAGE - The input amount of yeast powder provides effective ratio for hydrolyzing effect. The solid waste collecting tank and liquid waste collecting box are arranged along the pushing direction of the pushing rod, so as to realize the separation between solid and liquid waste in the process of pushing. Also, the pushing action of the screw provides a stirring effect so as to ensure complete mixing of the yeast powder and waste material.    DESCRIPTION OF DRAWING(S) - The figure shows a view of kitchen device.    Feeding port (1)    Set cover (2)    Powder box (3)    Screw rod motor (4)    Pushing screw (5)    Liquid waste collecting box (8)    Temperature heating device (9)    Solid waste collecting box (10)    Ferment powder box motor (11)    Box switch (15)
NOVELTY - Household hydraulic biogas pool comprises an anaerobic fermenting tank which is set with a fabric wall on one side. The fabric wall of the anaerobic fermenting tank and the wall of a distributing pool are set in a sedimentation area. The upper part of a liquid storage tank is set near fabric wall. The liquid storage tank is provided with an aerobic pool. The side part of aerobic pool is provided with an overflow hole. The aerobic pool is equipped with a feeding pipe. A fabric tube is connected to anaerobic fermenting tank. The opening of feeding pipe in aerobic pool is set with filter holes.    USE - Used as a household hydraulic biogas pool.    ADVANTAGE - The device has the provision of automatic flushing, automatic sedimentation, automatic breaking of shell, automatic clearing of shell, automatic cyclic stirring, and self-suction feeding; and does not require power.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the household hydraulic biogas pool.
NOVELTY - Extracting liquid fuel from waste sewage comprises collecting sewage and placing in a water cellar, then placing oil plant in the cellar with sewage, performing soaking-fermentation, precipitating the fermented liquid, and separating by filtration to obtain organic liquid of raw liquid i.e. liquid fuel, and adding combustion improver (30-50%).    USE - The method is useful for extracting liquid fuel from waste sewage.    ADVANTAGE - The method is simple, utilizes rich resources of sewage and produces rich energy source, and it reduces carbon emission, thus it is environment-friendly.
NOVELTY - The device has a current loop compensator for calculating voltage loop feedback gain and current loop feedback gain of direct current (DC)/DC converter when output voltage (Vo) and output current (ILf) of the DC/DC converter are inputted and for providing calculated control variable i.e. DC/DC converter phase shift angle or step-up duty ratio, to the DC/DC converter by performing phase shift method in a transformer mode.    USE - Dual-loop control device for DC/DC converter of a grid-connection type fuel cell generating system.    ADVANTAGE - The device minimizes frequency electric current ripple in a grid-connection type fuel cell generation system by providing the control variable and by avoiding insertion of ultra capacitors, so that volume and unit cost of the fuel cell generation system are reduced. The device stabilizes the output and availability ratio increase of a fuel cell by minimizing the low frequency electric current ripple.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for controlling a dual-loop control device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a dual loop control device.    Output current (ILf)    Output voltage (Vo)
NOVELTY - Fuel cell comprises fuel supply portion for supplying formic acid to fuel, reformer for converting fuel to hydrogen formic acid using microorganism capable of producing hydrogen from the formic acid, where the reformer is connected to the fuel supply portion, carbon dioxide removal portion for removing carbon dioxide generated by formic acid, air supplying portion for supplying external air to fuel cell stack portion, and fuel cell stack portion capable of producing electricity from the air supplied by reformer by redox reaction.    USE - The fuel cell is useful for producing electricity.    ADVANTAGE - The cell produces electricity with high power density without generating carbon monoxide, and can be operated even at low temperature.
NOVELTY - Town people excrement dry fermentation biogas tank comprises reaction tank body, feeding port, cover plate, gas guide tube, discharge hole, pressure gauge, and temperature detector. The reaction tank body is provided with feeding port and pressure gauge. The cover plate is provided at the top of the feeding port. It is provided with gas guide tube. The discharge hole is provided at the side wall of the reaction tank body. The reaction tank body is provided with temperature detector.    USE - Town people excrement dry fermentation biogas tank.    ADVANTAGE - The biogas tank fully utilizes urban human waste and plant straw to prepare biogas; avoids environmental pollution; has no loss and simple structure; and is convenient to maintain. The generated biogas residue can be provided for agricultural use.
NOVELTY - A sludge containing siloxane compound and an organic component, is aerated, and aeration gas is produced. The resultant sludge is digested to obtain digestion gas.    USE - Manufacture of digestion gas used as fuel for working of gas engine and gas turbine of generator.    ADVANTAGE - The method efficiently and economically provides digestion gas without affecting the environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production apparatus of digestion gas (1), which has an aerator (20) capable of aerating the sludge by aeration gas, and digester (30) which digests the sludge after aeration, and produces digestion gas.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of production apparatus of digestion gas. (Drawing includes non-English language text)    Production apparatus of digestion gas (1)    Aerator (20)    Heating apparatus (22)    Digester (30)    Stirring apparatus (32)    Water-removal device (50)    Combustion furnace (60)
NOVELTY - Apparatus (1) comprises granule tank (21) having granule filled layer which is filled with granule containing acid production microbe and methane producer, rotating shaft extended along upward up-ward direction of the granule tank, stirring apparatus (22) which stirs water in lower portion of the granule filled layer and is equipped along circumferential direction of the rotating shaft, stirring region (23) where water is stirred by the circumferential direction, and upward flow region (24) through which water flows with upward flow above the stirring region.    USE - The apparatus and anaerobic method are useful for processing organic water containing wastewater (claimed).    ADVANTAGE - The apparatus decomposes organic substances simply and completely.    DETAILED DESCRIPTION - Apparatus (1) comprises granule tank (21) having granule filled layer which is filled with granule containing acid production microbe and methane producer, rotating shaft extended along upward up-ward direction of the granule tank, stirring apparatus (22) which stirs water in lower portion of the granule filled layer and is equipped along circumferential direction of the rotating shaft, stirring region (23) where water is stirred by the circumferential direction, and upward flow region (24) through which water flows with upward flow above the stirring region. Organic water containing wastewater is supplied in the granule tank through lower portion.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of apparatus.    Apparatus (1)    Granule tank (21)    Stirring apparatus (22)    Stirring region (23)    Upward flow region (24)
NOVELTY - The apparatus (1) has heating combustion chamber (14) that is enclosed by the inner side partition wall (5) and provided to burn a fuel for the heating of the fluid bed reaction tank (3). A waste gas supply-flow channel is provided to connect the upper end side of the heating combustion chamber and the upper end side of the waste gas channel (16). A waste gas exit (17) is connected with waste gas channel provided in the lower end side of the furnace outer wall (2). The heating combustion chamber is raised to the waste gas channel through waste gas supply-flow channel.    USE - Apparatus for supplying gas of fluid bed for fluidizing grain such as sand, alumina and gas raw material e.g. wood chip. Can also be used in forest-products waste material biomass, agricultural waste biomass, foodstuff waste material biomass and waste plastic.    ADVANTAGE - The fluidized-bed-gasification apparatus can reduce the heating amount required for a gasification reaction. The thermal radiation from the fluid bed reaction tank to the inside of air can be suppressed effectively. The improvement in energy reduction and the economical efficiency can be achieved effectively. The thermal radiation from a fluid bed reaction tank to the inside of air can be effectively suppressed according to the heat insulation effect obtained by interposing a waste gas channel between a fluid bed reaction tank and the air outside a furnace. The fluid bed reaction tank can be heated efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the fluidized-bed-gasification apparatus. (Drawing includes non-English language text)    Fluidized-bed-gasification apparatus (1)    Furnace outer wall (2)    Fluid bed reaction tank (3)    Inner side partition wall (5)    Heating combustion chamber (14)    Waste gas channel (16)    Waste gas exit (17)
NOVELTY - The evaluation involves computing a membrane water diffusion coefficient and an electro-endosmosis coefficient based on a membrane moisture content. The gradient of the membrane moisture content used for a diffusion water movement calculation is calculated based on the difference of the respective membrane moisture contents of small regions arranged adjacently in a film thickness direction.    USE - Evaluation of inter-pole water movement in fuel cell for generating electric power.    ADVANTAGE - Increases the accuracy of estimation and evaluation of water movement in the film thickness direction of solid polymer membrane.    DESCRIPTION OF DRAWING(S) - The drawing shows the flowchart of an inter-pole water movement evaluation. (Drawing includes non-English language text).
NOVELTY - The fuel cell has a flat section column (120) which forms a reactive gas flow path by having a predetermined gap between the surfaces of the electrode in a predetermined direction. The communicating hole column (110) and the flat section column are arranged by turns. The flat section (S) provides a level difference (D) between adjacent flat sections while being connected.    USE - Fuel cell, e.g., sold polymer form fuel cell, for generating electric power.    ADVANTAGE - Improves draining ability of generated water since the flat section provides a level difference between adjacent flat sections while being connected.. Suppresses flooding by improving draining ability.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the flow-path formation section.    Flow-path formation section (40)    Communicating hole column (110)    Flat section column (120)    Level difference (D)    Flat section (S)
NOVELTY - The furnace has a furnace body (1) whose outside part is connected with a hot water tank (2) and a fire-proof part (4). A side of the furnace body is provided with an air outlet pipe (7) and an air inlet pipe (11).    USE - Rural rubbish combustion gas furnace.    ADVANTAGE - The furnace ensures providing the inlet and outlet pipes with an air outlet valve, and integrates a fan body with the air outlet pipe.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a rural rubbish combustion gas furnace.    Furnace body (1)    Hot water tank (2)    Fire-proof part (4)    Air outlet pipe (7)    Air inlet pipe (11)
NOVELTY - The furnace has a biomass pretreatment part provided with a drying machine, a crusher, a collecting box and a powder feeder. A pre-heating chamber is provided with a material inlet. A gas purifying part is provided with a gas-solid separating device, a gas purifying device and a fan. A circulating cooling system is provided with a circulating cooling tank and a circulating water pump. The cooling tank and the water pump are connected with each other to form a water circulation structure. Gas stored in an air storage tank is filtered and purified under driving function of the fan.    USE - Plasma ultra-turbulence thermal cracking biomass material gasification furnace.    ADVANTAGE - The furnace has high production efficiency and better system stability, and avoids harmful substance content.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a plasma ultra-turbulence thermal cracking biomass material gasification furnace.
NOVELTY - The burner has a vertical cylinder type gasification burner body with an insulating layer and a lower cylinder part, where upper part of the burner body is provided with plant straw and sealed with water via an opening cover. An inner cylinder near a cylinder bottom part is provided with a grate. A bottom cylinder part and an upper part of a cylinder wall of the grate are provided with an ash outlet and an air inlet. A smoke pipe is equipped with a smoke discharging valve with a gasification gas control valve arranged on a transverse pipe located between the smoke pipe and an input pipe.    USE - Plant straw gasification combustion burner.    ADVANTAGE - The burner is simple in design and structure with better gasifying effect, and ensures that a gas stove realizes high gas purity with convenient usage and prolonged service life. The burner realizes better lifting speed of input initial gasification process.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a plant straw gasification combustion burner.
NOVELTY - The furnace has an air pump connected with a gas pipe nozzle (3). A furnace body (1) outer wall is inclined to an inner furnace body of a filter box (5), which is connected with an upper part of the furnace body outer wall. A bottom part of the furnace body is provided with an air outlet box (9) and a tray frame (10). The tray frame is provided with an exhaust pipe (7) inclined toward the furnace body. An air outlet pipe (6) is arranged on the filter box. The air outlet pipe is connected with a cooking stove (8). The filter box is filled with a filtering material i.e. corn core.    USE - Biomass gasification furnace.    ADVANTAGE - The furnace has easy processing tar water vapor, and burns material continuously, so as to ensure high yield.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a biomass gasification furnace.    Furnace body (1)    Gas pipe nozzle (3)    Filter box (5)    Air outlet pipe (6)    Exhaust pipe (7)    Cooking stove (8)    Air outlet box (9)    Tray frame (10)
NOVELTY - Plant comprises a high pressure pump (1) formed for shattered material, which leads into one high pressure hydrolyser (2) for pressures of 3.5 MPa, which is formed in a closed space and contains a heater (3) at its entrance for the material, and is provided with an inner screw for regulating the material transport, and an expansion turnstile connected to the high pressure hydrolyser, which opens into an expansion vessel (6) having a vapor cast (7).    USE - The plant is useful for processing a significant amount of phytomass-containing materials by continuous pressure hydrolysis and subsequent expansion of the hydrolyzate.    ADVANTAGE - The plant is simple and processes the phytomass-containing material by large variability of parameters.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic block diagram of the plant for processing a significant amount of phytomass-containing material.    High pressure pump (1)    High pressure hydrolyser (2)    Heater (3)    Expansion vessel (6)    Vapor cast (7)
NOVELTY - An oil generation system, comprises a saccharide or carbon source; and a working microorganism reacting with the saccharide or carbon source to produce an oil, where the working microorganism has a genus being a Cystofilobasidium.    USE - The oil generation system is used for producing an oil (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for producing an oil, by utilizing an oil-generating microorganism to produce the oil, where the oil-generating microorganism has a genus being a Cystofilobasidium.
NOVELTY - Composition, comprises a polypeptide having cellulolytic enhancing activity and a dioxy compound, where the combination of the polypeptide having cellulolytic enhancing activity and the dioxy compound enhances hydrolysis of a cellulosic material by a cellulolytic enzyme.    USE - The composition is useful for: producing a fermentation product; and fermenting the saccharified cellulosic material (claimed) to fermentable sugars and converting the fermentable sugars to substances including fuel, potable ethanol, and/or fermentation products (acids, alcohols, ketones or gases).    ADVANTAGE - The composition utilizes polypeptide which exhibits enhanced cellulolytic activity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) degrading or converting a cellulosic material, comprising treating the cellulosic material with an enzyme composition in the presence of the polypeptide having cellulolytic enhancing activity and the dioxy compound, where the combination of the polypeptide having cellulolytic enhancing activity and the dioxy compound enhances hydrolysis of the cellulosic material by the enzyme composition;    (2) producing a fermentation product, comprising saccharifying a cellulosic material with the enzyme composition in the presence of the polypeptide having cellulolytic enhancing activity and the dioxy compound, fermenting the saccharified cellulosic material with at least one fermenting microorganism to produce the fermentation product and recovering the fermentation product from the fermentation; and    (3) fermenting a cellulosic material, comprising fermenting the cellulosic material with at least one fermenting microorganism, where the cellulosic material is saccharified with the enzyme composition in the presence of the polypeptide having cellulolytic enhancing activity and the dioxy compound.
NOVELTY - A block-shaped biomass fuel is obtained using byproduct waste material derived from naturally grown plants or artificial plants, as a raw material, and processing the raw material.    USE - Block-shaped biomass fuel for biomass pellet fuel used as fuel in combustion apparatus (all claimed) for manufacture of bioethanol and biodiesel, and fuel for agricultural heater, domestic heater and industrial heater.    ADVANTAGE - The block-shaped biomass fuel is economically manufactured without affecting environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biomass pellet fuel, which is obtained by processing the biomass fuel.
NOVELTY - A to-be-processed object containing organic substance is subjected to methane fermentation treatment on anaerobic conditions to produce biogas containing methane gas and carbon dioxide gas. To-be-processed object contains 50-500 mass parts of paper waste with respect to 100 mass parts of organic waste as dry mass.    USE - A methane fermentation processing method for biogas production (claimed).    ADVANTAGE - Inhibition of methane fermentation is suppressed, methane fermentation advances smoothly, and biogas is emitted quantitatively.
NOVELTY - Agent comprises monohydrocalcite which is obtained by precipitating mixture having aqueous solution of soluble carbonate or carbonate and aqueous solution containing magnesium and calcium ion in a ratio of 0.3 or more.    USE - The agent is useful for recovering phosphorus from wastewater and producing phosphate fertilizer (all claimed).    ADVANTAGE - The phosphorus recovery agent is recyclable as phosphate fertilizer and enables suppression of eutrophication in lakes and marshes.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) phosphate fertilizer obtained by recovering phosphorus from the wastewater using the above-cited agent; and    (2) method of purification of wastewater, involves contacting the phosphorus recovering agent with phosphorus or/and calcium phosphate containing wastewater for adsorption.
NOVELTY - The sensor (100) has a porous electrode layer (110) permeable to predetermined gas, and a dielectric layer (120) limited at the porous electrode layer. The dielectric layer is provided with a material that differs from silicon dioxide and silicon nitride, and a rear electrode (150) is made of metal or semiconductor material and bordered at the dielectric layer at a side, which lies opposite to the electrode layer. The dielectric layer is manufactured using atomic-layer-deposition-process, where material of the dielectric layer is doped with doping material.    USE - Field effect gas sensor i.e. gas-sensitive chemical FET, for use in a gas detector (claimed) for detecting sensitivity and selectivity of gas.    ADVANTAGE - The sensor is designed such that sensitivity and selectivity of gas are detected in a fast and efficient manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a method for detecting gas at a field effect gas sensor    (2) a computer program product comprising a set of instructions for performing the method for detecting gas at the field effect gas sensor    (3) a method for manufacturing the field effect gas sensor.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of a sensor structure as a gas-sensitive FET.'(Drawing includes non-English language text)'    Field effect gas sensor (100)    Porous electrode layer (110)    Dielectric layer (120)    Rear electrode (150)    Source region (160)
NOVELTY - The grate has a lower layer fire grate unit fixed at a lower end of a fireproof material gasification reacting chamber. A pour ladder model is provided with multiple ladder type stainless steel racks. Ends of the steel racks are fixedly linked together to form an upper fire grate ring. A movable upper layer fire grate unit is linked with a hydraulic power device and lower layer fire grate ladder type stainless steel racks. The power device is automatically controlled by a programmable logic controller (PLC) system that drives the upper grate unit at frequency of about less than 200 times/min.    USE - Coke ash dreg page-discharged vibration extrusion fire grate for use during biomass gasification reaction process.    ADVANTAGE - The grate ensures the coke ash dreg page-discharged vibration extrusion process to enable continuous biomass gasification reaction process and continuous power generation process.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial sectional view of a coke ash dreg page-discharged vibration extrusion fire grate.
NOVELTY - The device has a gas pipeline connected with a gasification reaction chamber, a steam heating device and a steam buffering tank. The gasification reaction chamber is provided with an automatic feeding device, an automatic ignition device, a primary gasification area and a plasma reaction area. A cylinder head of a hydraulic pressure pushing device is connected with a speed reducing motor. An output end of the speed reducing motor is connected with a central shaft, where a central line of an output shaft of cylinder head is overlapped with a central line of a gasification zone.    USE - Plasma rubbish carbon dioxide gasification device.    ADVANTAGE - The device is simple in structure and inexpensive, and has high energy efficiency and reduced power consumption. The device can effectively remove harmful substances for volume reduction ratio to change waste into valuable.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a rubbish carbon dioxide gasification method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a plasma rubbish carbon dioxide gasification device.'(Drawing includes non-English language text)'
NOVELTY - The equipment has a gas reaction chamber whose gas outlet pipe is connected to a steam heat exchanger of a gas feeding pipeline, a gasification reaction chamber and a steam heat exchange chamber through a gas conveying pipe. An inner and outer double-cyclone heat exchange dust and cooling tower is provided with an automatic discharging device. The automatic discharging device is provided with a ball valve, a storage bin and a low material level detector. The storage bin is arranged on a two-level ball valve arranged between a high and low position level detector and the storage bin.    USE - Biomass gasification equipment for use in a fuel gas generating set.    ADVANTAGE - The equipment is scientific and environment-friendly with rational structure design, high automation degree and stable gasification reaction control. The equipment has high gasification efficiency, high strength and high heat value, and is suitable for large area to be popularized and applied. The equipment ensures continuous and stable power generation in a fuel gas generating set.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biomass gasification technique using a carbon dioxide gasification process.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a biomass gasification equipment.'(Drawing includes non-English language text)'
NOVELTY - The chamber has a slag discharging passage connected with a ball valve that is provided with a storage bin and a low material level detector, where the ball valve is arranged between a high and low position level detector and the storage bin. A secondary gasification zone of a mixing gas outlet pipeline is connected to a steam heat exchanger of a gas feeding pipeline and a gasification area of an air inlet pipe by a gas conveying pipe. A steam buffer tank and an air buffer tank are connected with the steam heat exchanger and an air pre-heating device of an air outlet pipeline.    USE - Lower suction type biomass gasification reaction chamber for use in continuous and stable power generation of a fuel gas generating set.    ADVANTAGE - The chamber is environment-friendly and rational in structure and design. The chamber has high automation degree, stable gasification reaction control, high gasification efficiency and high heat value.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a reaction chamber biomass gasification method.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a lower suction type biomass gasification reaction chamber.
NOVELTY - The device has a pyrolysis hearth arranged on an upper stage of an interior part and provided with a feeding device. A bottom part of a gasification hearth on a lower stage is provided with a mixed gas inlet. An upper end of a columnar or square shaped reaction furnace is provided with a smoke outlet. The smoke outlet is connected with a cyclone separator. An outer side of the reaction furnace is provided with a temperature control device corresponding to the pyrolysis hearth on the upper stage, the gasification hearth on the lower stage and a nickel-containing catalyst bed layer.    USE - Gasification device for producing synthetic gas by a three-stage biomass pyrolysis and gasification process.    ADVANTAGE - The device simplifies a synthetic gas preparation experimental system, improves gasification furnace gas yield and synthetic gas quality and reduces tar content level in gas. The device is simple in structure and environment-friendly, and has convenient temperature control function and continuous operation, and saves energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a gasification device for producing synthetic gas by a three-stage biomass pyrolysis and gasification process in partial section.'(Drawing includes non-English language text)'
NOVELTY - Manufacturing ethanol from synthesis gas consisting of the gas phase, comprises reacting carbon monoxide with hydrogen to produce ethanol and carbon dioxide, where the reaction is conducted in the presence of a catalyst comprising a mixture of copper chromite catalyst, copper zinc oxide catalyst, and promoted activated carbon catalyst, and operated at a reaction temperature of 250-350 degrees C and a pressure of 1-20 atm.    USE - The method is useful for manufacturing ethanol from synthesis gas consisting of the gas phase.    ADVANTAGE - The method: provides high yields of product; is designed to operate under mild conditions; directly provides absolute alcohol; and ensures a dependable and robust method. Utility costs are minimized by the relatively high conversions.
NOVELTY - The furnace has a combustion furnace unit provided with a furnace shell. An end of a distribution unit is connected with a combustion furnace port. Another end of the distribution unit is connected with a bottom part of the combustion furnace unit. A fan is connected to the distribution unit. The fan and an upper part of the distribution unit are provided with a lower valve. A pipe is connected with an end of a left side part of the combustion furnace unit. An end shell is provided with a slag outlet arranged at the bottom part of the combustion furnace unit.    USE - Single-cylinder straw gasification furnace.    ADVANTAGE - The furnace adopts simple integrated structures so as to realize convenient utilization with reduced smoke and tar.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a single-cylinder straw gasification furnace.
NOVELTY - Preparing S-2-hydroxy-3-methoxy-3,3-diphenyl propionic acid (I), comprises: (a) reacting benzophenone with methyl chloroacetate to give 3,3-diphenyl-oxirane-2-carboxylic acid methyl ester (II); (b) reacting (II) with p-toluene sulfonic acid to give 2-hydroxy-3-methoxy-3,3-diphenyl-propionic acid methyl ester (III); (c) hydrolyzing (III) with sodium hydroxide to give 2-hydroxy-3-methoxy-3,3-diphenyl-propionic acid (IV); and (d) resolving (IV) by reacting it with (S)-(-)p-nitro phenyl ethyl amine dissolved in methyl tert-butyl ether to give (I).    USE - (I) is useful for the synthesis of pharmaceutical grade ambrisentan, which is useful for treating pulmonary artery hypertension. No biological data given.    ADVANTAGE - The process provides (I) with improved yield, chemical purity (more than 99.8%), and chiral purity (more than 99.9%) in an industrial and environmentally friendly manner.
NOVELTY - Process for converting pyrolysis oil to a hydrocarbon fuel involves: (a) reacting pyrolysis oil with a feed comprising alcohol species in a reactor to form a product mixture containing an alcoholysis product; and (b) contacting the alcoholysis product with a hydrotreating catalyst in the presence of hydrogen in a reaction zone under reaction conditions to convert at least a portion of the alcoholysis product into at least one fuel range hydrocarbon product.    USE - For converting pyrolysis oil to a hydrocarbon fuel (claimed) used in boilers, gas turbines and diesel engines.    ADVANTAGE - The process provides straightforward methodology to prepare upgradable pyrolysis oil via alcoholysis. The water in pyrolysis oil promotes hydrolysis and cracking of different pyrolysis oil components. Direct alcoholysis of pyrolysis oil results in lower concentration of acidic species (lower total acid number, or total acid number (TAN)), thereby increasing the pH of the oil. The alcoholysis of pyrolysis oil significantly reduces the molecular weight average of pyrolysis oil components. The latter is key for upgradability, as heavy molecular weight species in pyrolysis oil promote char formation and coke deposition during catalytic upgrading to hydrocarbons, seriously hindering upgrading viability. The process uses well-established hydrotreating technology for oxygen removal and hydrocarbon production. The biofuel products produced by the process are 100% fungible with conventional transportation fuels.
NOVELTY - Biological diesel continuous ester exchange production device, comprises a stirring kettle, a first material pump (3), a plug flow reactor, separator (6), a buffer tank (8), a second material pump (9), a static mixer (10) and two-stage piston flow reactor comprising a first end which is connected to the stirring kettle and an other end which is connected on the second material pump and the static mixer of the pipeline, where the pipeline is connected with alkali methanol is kettle.    USE - Used as a biological diesel continuous ester exchange production device.    ADVANTAGE - The device: has compact structure, strong generality and simple control, realizes the normal pressure; reduces the triglyceride content in the biodiesel; and improves the product quality.    DESCRIPTION OF DRAWING(S) - The figure shows the biological diesel continuous ester exchange device.    First material pump (3)    Separator (6)    Buffer tank (8)    Second material pump (9)    Static mixer (10)
NOVELTY - Membrane electrode assembly preparation involves depositing thin films of 20-70 mu m thickness on a polymer membrane having functions as a gas separator, an electrical insulator and a conductor of hydrogen ions. The membrane surface is treated through chemically for cleaning and activation protonation of the membrane. An electro-catalytic ink is sprayed on sides of the membrane to generate porous electrodes.    USE - Method for preparing membrane electrode assembly for manufacturing fuel cell.
NOVELTY - Firewood briquetting machine comprises a briquetting machine and a crushing machine, and further composed of a feed port, a crusher, a stirrer, a briquetting press and a discharge port. The firewood is crushed and molded by a stirring machine, crushing machine and briquetting machine. The fuel blocks are prepared by adding firewood via the feed port, crushing using crusher, mixing with water using a stirrer to obtain crushed material sludge, and molding into high-density material blocks by using briquetting press molds to obtain fuel blocks, which are regularly molded from the discharge port.    USE - The fuel block produced from machine is useful in: all stoves, which is suitable for rural areas, towns, and at home for heating, and cooking; and boiler and straw power plant.    ADVANTAGE - The machine solves traditional wood burning manner, and also the security problems; simplifies the stacking of firewood; and is suitable for large-scale production.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the firewood briquetting machine.
NOVELTY - Method for producing cell and liposoluble substance, involves culturing cell capable of producing liposoluble substance in a broth, partitioning the cohered cell without damage, extracting the liposoluble substance using extraction solvent, obtaining fractionated cell and liposoluble substance-solvent complex, and dissolving the liposoluble substance.    USE - The method and device are useful for producing cell and liposoluble substance, which are used as drug, health promoting food, biofuel and protein hydrolysates.    ADVANTAGE - The method is inexpensive and enables high yield of product.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for device which comprises culture tub (10) for culturing the cell, solvent bath (20) for storing the liposoluble substance extraction solvent, mixed unit (30) for mixing the liposoluble substance extraction solvent and cell, flocculation basin (40) comprising ultrasound resonance field generator (41) for applying the ultrasound resonance field in the mixed unit, fraction tub (50), accommodation unit (80) for accommodating the fractionated cell from the fraction tub, and accommodation unit (90) for accommodating the liposoluble substance-solvent partitioned from the fraction tub.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of device.    First peristaltic pump (2)    Second peristaltic pump (3)    Third peristaltic pump (4)    Culture tub (10)    Solvent bath (20)    Mixed unit (30)    Vibration milling apparatus (31)    Stirrer (32)    Flocculation basin (40)    Ultrasound resonance field generator (41)    Ultrasonic generator (43)    Ultrasonic oscillator (44)    Reflective film (45)    Fraction tub (50)    Cell-cycle line (60)    Accommodation units (80,90)
NOVELTY - Waste flow anaerobic digester (100) comprises digesting reaction chamber (1), feeding pipe, discharging pipe and gas discharging pipe, several stirrers, and control mechanism arranged along the front and back of the digestion reaction chamber, mixer placed between adjacent stirrer and stirring paddle, heat insulation device for heating and providing stable heat and maintaining the temperature to the digestion reaction chamber connected to the mixer, and more agitators that alternating rotate under control of the control mechanism.    USE - The waste flow anaerobic digester is useful for processing e.g. household organic garbage, garden garbage, animal waste, food waste, kitchen residue, animal slaughtering waste, municipal sludge and sideline products.    ADVANTAGE - The waste flow anaerobic digester has low production cost and high energy recovering efficiency.    DETAILED DESCRIPTION - Waste flow anaerobic digester (100) comprises digesting reaction chamber (1), feeding pipe, discharging pipe and gas discharging pipe, several stirrers, and control mechanism arranged along the front and back of the digestion reaction chamber (where each stirrer comprises motor, stirring shaft and stirring paddle, motor drives the stirring shaft, and stirring paddle is fixed or equipped in the end of the stirring shaft and the digestion reaction chamber), mixer placed between adjacent stirrer and stirring paddle, heat insulation device for heating and providing stable heat and maintaining the temperature of the digestion reaction chamber, connected to the mixer, and more agitators that alternating rotate under control of the control mechanism.    DESCRIPTION OF DRAWING(S) - The drawing a schematic view of waste flow anaerobic digester.    Digesting reaction chamber (1)    External vacuum system (6)    Discharge tube (12)    Discharging vacuum tank (61)    Vacuum generator (62)    Sludge dewatering device (64)    Sludge reflux device (65)    Flow anaerobic digester (100)
NOVELTY - Biomass energy anaerobic fermentation tank comprises at least one bottom modular tank and at least one layer of assembly tank body. The assembly tank body comprises several tank walls assembling plates and connecting piece for connecting tank wall assembling plates. Mounting parts are arranged at upper, lower, left and right sides of tank wall assembling plates. The assembly tank body is connected to modular tank by tank wall assembling plates via connecting piece.    USE - Biomass energy anaerobic fermentation tank.    ADVANTAGE - The biomass energy anaerobic fermentation tank is integrated with corrosion resistance and thermal insulation. It is convenient to transport and easy to assemble.    DETAILED DESCRIPTION - The tank wall assembling plates are arc-shaped plates. The mounting part is flange with through hole. The connecting piece is bolt or screw. The left and right flanges of tank wall assembling plates are connected with corresponding flange of adjacent tank wall assembling plate to form layer of assembly tank body. The layers of assembly tank bodies are integrally connected on vertical direction by mounting parts of upper side and lower side of tank wall assembling plate and mounting part of adjacent assembly tank body via connecting piece. Each layer of assembly tank body comprises connecting piece.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of biomass energy anaerobic fermentation tank.
NOVELTY - An anaerobic sewage purification tower comprises a tower body (1), a water distributor (2), sludge bed (3), collecting hood (4), circulating inner cylinder (5) and gas-liquid separator (6). Lower part of the purification tower is sewage anaerobic digestion reaction zone, circulation in cylinder and the tower body is sludge zone (8). The cylinder is detachably mounted. Gas enters the circulating inner cylinder in the fermenting liquid internal circulation.    USE - An anaerobic sewage purification tower used for processing and purifying farm organic wastewater.    ADVANTAGE - The device overcomes the flow tunnel methane pool and mixed gas are mixing, long staying time, low volume organic load, large volume, low removing rate, and difficult post treatment.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating the anaerobic sewage purification tower.    Tower body (1)    Water distributor (2)    Sludge bed (3)    Collecting hood (4)    Cylinder (5)    Gas-liquid separator (6)    Sludge zone (8)
NOVELTY - A biogas raw material feeding device comprises a waste removing device, a container comprising greater than or equal to 2 receptacle connectors, and a cable.    USE - A biogas raw material feeding device.    ADVANTAGE - The feeding device has convenient biogas raw material feeding and waste material out, and improves rural environmental sanitation.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a biogas raw material feeding device.
NOVELTY - A biogas pool comprises sealing strip where its middle is connected two sides of the round structure. Circular structure is symmetrical fin-shaped structure. The lower half part of sealing strip circular structure is pressed to marsh gas tank joint surface, while half part is clamped in methane tank flat joint surface. The sealing strip fin of two sides of fin structure is clamped between two jointing plane of methane tank.    USE - Biogas pool for fin-shaped sealing strip.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating a biogas pool.
NOVELTY - A biogas pool stirring filter comprises stirring shaft, impeller and detachable slag filter screen. The residue filter screen is welded with center of the bottom of the shaft sleeve. The top end periphery through the fastening bolt and wall of marsh gas pool are fixed on outer wall. Stirring shaft passes through filter screen residue of shaft sleeve. The top end and tail end through two bearings and is rotatably connected with cover of marsh gas tank and methane tank bottom. Detaching impeller is installed at lower end of stirring shaft. Each impeller is connected with stirring shaft.    USE - Biogas pool stirring filter.    ADVANTAGE - The filter has simple structure, convenient operation, low cost, and wide application. It prevents tank material layering and precipitation.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating a biogas pool stirring filter.
NOVELTY - A biomass energy straw comprehensive utilization of solar energy and marsh system comprises marsh gas generating unit, biogas storage unit and biogas storage distribution unit. The gas generating unit is connected to green storage bunker together, feeding machine, vacuum tank, and fermentation tank. The fermentation tank is further connected with hot water boiler and biogas storage unit. The fermentation tank is connected with biogas storage unit, gas-water separator, desulfurizing tank dispensing unit.    USE - Biomass energy straw comprehensive utilization of solar energy and marsh system.    ADVANTAGE - The system has wide source of raw material, marsh gas fermentation fast starting, high yield, and stable production.
NOVELTY - A residue salvaging machine comprises bracket, winch and grab bucket, where the winch is fixed on the bracket. The grab bucket is connected to the winch. The winch is electrical or manual. The grab bucket comprises handle and a clamp. The clamp can be opened and closed. Length of the grab bucket is greater than 1 m.    USE - Residue dragging machine for household methane tank.    ADVANTAGE - The dragging machine solves problem that vacuum and centrifugal device cannot extract straw containing fused slag. It has low cost and light weight, is safe, has high work efficiency, and can use two phase power.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating a residue dragging machine.
NOVELTY - The device has a condensation and cooling gas unit including a set of heat exchangers, deethanizer and demethanizer, and a steaming off section supplied with an extension pump for supplying bottom products in the deethanizer. A strengthening section performs methane fraction of average pressure, helium concentrate obtaining unit and a set of connecting conduits. A line for performing methane fraction of the average pressure at an output from reinforcement section of the demethanizer is connected by an intermediate wall of a stage and supplied with a locking accessory.    USE - Hydrocarbon gas low-temperature separating device.
NOVELTY - Combined metering and dosing sewage treatment device comprises a storage gallipot (1), less flow dosing pump (3) and a rotameter (4), where the tap water pipe network of the storage gallipot is set with dosing hole (5). The storage gallipot and the less flow dosing pump are connected. The less flow dosing pump is in turn connected to the rotameter, and the rotameter is connected to the dosing point (6).    USE - Used as a combined metering and dosing sewage treatment device.    ADVANTAGE - The device: reduces the investment cost and the operation cost of sewage treatment station; is suitable for treating sewage with low flow rate; reduces medicine consumption, and the cost; and prevents unsatisfactory sewage treatment effect caused by insufficient medicine feeding.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of the combined metering and dosing sewage treatment device.    Storage gallipot (1)    Less flow dosing pump (3)    Rotameter (4)    Dosing hole (5)    Dosing point (6)
NOVELTY - The invention can be used to produce electric power and heat energy at agricultural enterprises, logging sites and public utility sites. The gas power plant contains from the following components installed in series: the gas generator 1, cyclonic separator 2, gas-water heat exchange unit 3, scrubber 4 and power generator 18 with gas engines 10, 11 and exhaust heat boiler 12. The exhaust heat boiler 12 is connected in series with the gas-water heat exchange by the heat carrier flowing circuit. Furthermore, the scrubber 4 water outlet is connected with the inlet through a decanting tank 5and an air heating unit 8. Between the air heating unit 8 and the water inlet of the scrubber 4 there are anaerobic filters 6, 7 and a water cooling unit - a heat pump evaporator 9 comprising a compressor 14 with a gas engine, a condensator-water heater 13 and a thermal regulation valve 15.    USE - Electric engineering.    ADVANTAGE - Improved generator gas quality and reduced environmental pollution. 1 dwg
NOVELTY - The apparatus (20) has a rotatable anode (44) including channels in an active face. A gap (46) is formed between a cathode (42) and the anode. The liquid inlet port (34) is located in the vessel wall for the inflow of water or aqueous solution into the reaction vessel. The water or aqueous solution and the gases produced in the reaction vessel are sent out through an output port (72). The titanium dioxide coating is coated on the anode and the cathode. The hydrogen gas is separated from the gases generated by generation portion.    USE - Electrolytic cell apparatus for producing gases from water or aqueous solution.    ADVANTAGE - The gases can be produced efficiently from water or aqueous solution by electrolysis process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing gases from water or aqueous solution.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the electrolytic cell apparatus.    Electrolytic cell apparatus (20)    Liquid inlet port (34)    Cathode (42)    Rotatable anode (44)    Gap (46)    Output port (72)
NOVELTY - The system (10) has dust removal apparatus (14) which removes the dust in the biomass gasifying gas (13) obtained by a biomass gasifier. Desulfurizing-apparatus (15) removes the sulfur-oxide component in dust-removed biomass gasifying gas. Pre-reforming reactor (16) reforms the coal tar fractions in the biomass gasifying gas after the desulfurization. Vapor supply unit (18) supplies vapor (17) to the upstream side of reactor. Natural gas supply unit (20) supplies the natural gas to the upstream flow side of the desulfurizing-apparatus or pre-reforming reactor.    USE - Biomass gasification gas-purification system used in methanol production system (claimed) to obtain clean gas raw material for use in manufacture of liquid fuel and alcohol.    ADVANTAGE - The methanation reaction is inhibited by transducing the natural gas and water vapor, when reforming the coal tar fractions in biomass gasifying gas with high carbon dioxide component concentration. By suppressing thermal runaway of the reforming reactor, the gas purification of stable biomass gasifying gas can be performed. The gas by which the coal tar fractions are removed can perform stable methanol synthesis, without degrading methanol synthesis catalyst.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) methanol production system;    (2) biomass gasification gas-purification method; and    (3) methanol production method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the biomass gasification gas-purification system. (Drawing includes non-English language text)    Biomass gasification gas-purification system (10)    Biomass gasifying gas (13)    Dust removal apparatus (14)    Desulfurizing-apparatus (15)    Pre-reforming reactor (16)    Vapor (17)    Vapor supply unit (18)    Natural gas supply unit (20)
NOVELTY - The system (10A) has dust removal equipment (14) that filters soot and dust in biomass gasification gas (13) obtained through gasification of biomass by using biomass gasification furnace. Desulfurization equipment (15) is configured to remove sulfur oxide components in filtered biomass gasification gas. Pre-reforming reactors (16A-16C) are provided for pre-reforming catalysts for reforming tar components in biomass gasification gas after desulfurization, and coolers (17A,17B) are located between pre-reforming reactors for cooling the reformed gas.    USE - Biomass gasification gas-purification system used during manufacturing of liquid fuel such as alcohol e.g. methanol.    ADVANTAGE - The methanation reaction can be inhibited during biomass gas purification, while reforming the coal tar fractions in biomass gasifying gas with high carbon monoxide component concentration. The gas purification of stable biomass gasifying gas can be performed by suppressing thermal runaway of reforming reactor.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) methanol production system;    (2) biomass gas-purification method; and    (3) methanol production method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the biomass gas purification system. (Drawing includes non-English language text)    Biomass gas purification system (10A)    Biomass gasification gas (13)    Dust removal equipment (14)    Desulfurization equipment (15)    Pre-reforming reactors (16A-16C)    Coolers (17A,17B)
NOVELTY - The bio-energetic complex comprises a methane-tank with coil pipe, which is located in a geometric center of methane-tank, a heat insulation unit, a screw mixer, loading and unloading branch pipes, conduits for supply of biogas, a gas holder, a solar collector with a tank-storage battery, a screw intermixing device, a boiler for heating the biomass with a wind-power installation with a thermal electrical heater, which in the absence of solar radiation supports in the methane-tank at a temperature of 47-55 degrees C and with built-in conduit of reverse supply of heat-transfer agent.    USE - Used as a bio-energetic complex.    DETAILED DESCRIPTION - The bio-energetic complex comprises a methane-tank with coil pipe, which is located in a geometric center of methane-tank, a heat insulation unit, a screw mixer, loading and unloading branch pipes, conduits for supply of biogas, a gas holder, a solar collector with a tank-storage battery, a screw intermixing device, a boiler for heating the biomass with a wind-power installation with a thermal electrical heater, which in the absence of solar radiation supports in the methane-tank at a temperature of 47-55 degrees C and with built-in conduit of reverse supply of heat-transfer agent. The methane-tank has a coil pipe of heating of biomass, which is located in the geometric center of methane-tank.
NOVELTY - The device has cylindrical container which is equipped with feedstock loading unit. A mixing unit is placed in upper portion of reactor. An aluminum methyl made tubular shaft is located in mixing unit. A cylindrical barrel is provided with flanges. A scraping device is connected with screw device. A generation unit is arranged to generate acoustic pulses having frequency within the range of 5-70 pulsation per minute in pulsation chamber.    USE - Pulsating device for delignificating cellulose-containing plant feedstock.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for operating pulsating device.
NOVELTY - A saccharification method of wood type biomass involves reducing crystallinity degree of cellulose by pulverizing wood type biomass, carrying out alkali oxidation treatment of obtained fine powder fraction, and saccharifying solid content with enzyme.    USE - A saccharification method of wood type biomass.    ADVANTAGE - The saccharification method of wood type biomass has high yield, and is low cost and efficient.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a manufacturing method of ethanol involving reducing crystallinity degree of cellulose by pulverizing wood type biomass, carrying out alkali oxidation treatment of obtained fine powder fraction, saccharifying solid content with enzyme, and obtaining ethanol as saccharide component.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of system which performs pulverization process. (Drawing includes non-English language text).
NOVELTY - Bark compost is manufacture by mixing water purifying cake with bark.    USE - Manufacturing method of bark compost for soil improvement material and plant growth culture medium (claimed).    ADVANTAGE - Manufacture efficiency is high, manufacturing cost is reduced, and culture efficiency is raised.
NOVELTY - A carbide material manufacturing plant consists of carbonization furnace (20) of rotary kiln type which thermally decomposes biomass and produces carbide material and pyrolysis gas, partial combustion reactor (70) which burns the pyrolysis gas, and produces partial combustion gas, heating jacket (22) for heating the carbonization furnace, combustion furnace (30) which burns the partial combustion gas and partial combustion gas flow path (91) which connects the partial combustion reactor and combustion furnace via heating jacket.    USE - Plant for manufacturing carbide material.    ADVANTAGE - The carbide material manufacturing plant reduces the usage amount of supplementary fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the plant for manufacturing carbide material. (Drawing includes non-English language text)    Carbonization furnace (20)    Heating jacket (22)    Combustion furnace (30)    Partial combustion reactor (70)    Partial combustion gas flow path (91)
NOVELTY - Producing fuel and fuel additives comprises: (a) reacting biomass with an oxidizing agent to produce unoxidized aromatic and/or phenolic compounds and 1-6C carboxylic acids; (b) separating the unoxidized aromatic and/or phenolic compounds from carboxylic acids; and (c) anaerobically fermenting the carboxylic acids in the presence of an anaerobic bacterium in its solventogenesis phase to produce a solvent having short chain, linear and branched, saturated and unsaturated alcohols and non-fermentable carboxylic acids.    USE - The process is useful for the production of fuel and fuel additives (claimed) that are useful in vegetable oil, animal fat and recycled grease for diesel engine and boiler fuels.    ADVANTAGE - The process provides straight vegetable oil and/or grease having similar viscosities, cloud points and fuel consumption rates as conventional petroleum diesel fuel.
NOVELTY - The system has a hoisting machine and a storage bin utilized for storing biomass fuel. A conveying belt is arranged to the storage bin. A spiral conveyor is utilized for quantitatively conveying the biomass fuel. An air gasifier is utilized for preparing composition material gas. A cyclone separator is utilized for separating biomass gas. A voltage releasing device is utilized for releasing over-voltage of the biomass gas. A blower is utilized to the air gasifier. A combustion chamber is connected with a steam boiler via a steam pipeline.    USE - Biomass air-steam gasification system.    ADVANTAGE - The gasifier is provided with a steam pipeline, so that steam in gasification reaction gasifies biomass fuel pyrogenation after burning and gasifying the biomass gas, thus improving 30-40 percent of heat value and increasing 20 percent of gas yield.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass air-steam gasification system.
NOVELTY - The biomass air-steam gasifier has an outer surface layer that is coated with an insulating layer. The insulating layer is provided with hollow cylindrical combustion chamber of outer cylinder. A cooling chamber for filling cooling wall heat preservation layer is provided to feeding port. The insulating layer is provided on one input portion of water through hole.    USE - Biomass air-steam gasifier.    ADVANTAGE - The biomass fuel pyrogenation process can be gasified. The heat value of the biomass gas can be improved by 30-40%. The gas yield can be increased by 20%.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the biomass air-steam gasifier.
NOVELTY - A waste disposal system includes a gasification process for obtaining gas containing hydrogen and carbon dioxide, and a residue from a waste material, and a methanol production process for synthesizing methanol from a portion of or all carbon dioxide and hydrogen.    USE - Waste disposal system. Uses include but are not limited to garbage, scrap wood, coppiced timber, wood chips, paper garbage, fiber garbage, plastic garbage, sewage garbage, excrement, livestock farming waste material, waste oil, rubber tire, black liquor, and waste molasses.    ADVANTAGE - The waste disposal system reduces environmental burden.
NOVELTY - A hydrogen generating apparatus (2) has a modifier (4) for producing hydrogen-containing gas by reforming reaction using a source gas, a source gas supply device (13) for supplying source gas to modifier, a methanation device (6) for reducing carbon monoxide contained in hydrogen-containing gas by methanation reaction, and a controller (11) for reducing supply amount of source gas to modifier such that the supply device is controlled and production amount of hydrogen-containing gas is reduced, when temperature of methanation device is increased.    USE - Hydrogen generating apparatus used in fuel cell system (claimed) and chemical processing plant.    ADVANTAGE - The hydrogen generating apparatus enables to produce hydrogen with high purity. The temperature raise of methanation device is suppressed, since emitted heat amount accompanying methanation reaction is reduced. The fuel cell system having the hydrogen generating apparatus has improved charging and discharging characteristics.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of hydrogen generating apparatus. (Drawing includes non-English language text)    Hydrogen generating apparatus (2)    Modifier (4)    Methanation device (6)    Controller (11)    Source gas supply device (13)
NOVELTY - The device has a belt conveyer that is located in the spiral feeding machine box. The bottom of the spiral feeding machine box is connected with the spiral feeding machine. A gasification furnace bucket (78) has several gasification furnaces. A gasification furnace on the barrel seals the top plate. A gasification cylinder (74) is connected with the upper portion of the outer barrel. A tower-shaped grate (72) is ventilated and hydraulic station (68) and ash pan driving hydraulic rod (71) acts on the hearth teeth (69).    USE - Boiler heating device for tobacco stalk gasification.    ADVANTAGE - The device uses the liquefied natural gas cold energy efficiently and avoids the smoke pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a structural schematic view of the boiler heating device.    Spiral feeding machine (1)    Spiral feeding machine box (2)    Belt conveyer (11)    Hydraulic station (68)    Hearth teeth (69)    Ash pan driving hydraulic rod (71)    Grate (72)    Gasification cylinder (74)    Gasification furnace bucket (78)
NOVELTY - Denatured fuel ethanol composition, comprises: an ethanol composition containing ethanol (at least 92 wt.%) and isopropanol (95-850 weight parts per million (wppm)); and fuel denaturant (at least 1.96 vol.%).    USE - The composition is useful for blending with gasoline or diesel fuel which is used commercially (all claimed) as motor fuels.    ADVANTAGE - The composition: comprises minor amounts of organic impurities, and thus is highly pure; and can be produced with out the use of petrochemical feed stocks, and fermentation techniques.    DESCRIPTION OF DRAWING(S) - The figure illustrates a schematic representation of a hydrogenation system.    Hydrogenation system (100)    Reaction zone (101)    Distillation zone (102)    Reactor (103)    Hydrogen feed line (104)
NOVELTY - Ethanol/fuel blend composition comprises: an ethanol composition comprising at least 92 wt.% of ethanol, and 95-850 weight parts per million (wppm) of isopropanol; and a fuel.    USE - The ethanol/fuel blend composition is useful as fuel in motor vehicles, such as automobiles, boats and small piston engine aircrafts.    ADVANTAGE - The ethanol/fuel blend composition is free of more than 6C alcohols, lead and heavy metals. The ethanol/fuel blend composition is prepared without using any petrochemical feed stocks, and fermentation techniques in an economical manner.
NOVELTY - A hydrogen generator includes a cascade of at least two electrolytic cells (1, 17). Each cell comprises a membrane (14) electrode assembly incorporating a solid polymer electrolyte polarized to generate hydrogen from water at a cathode and oxygen at an anode. Any water (2) entrained in or carried over with the hydrogen produced in the first cell is the only significant feedstock for each successive electrolytic cell.    USE - A hydrogen generator.    ADVANTAGE - The hydrogen generator enables electrochemically produced hydrogen to be dried efficiently, and eliminates the need for condensate removal.    DETAILED DESCRIPTION - A hydrogen generator comprises a cascade of at least two electrolytic cells (1, 17). Each cell comprises a membrane (14) electrode assembly incorporating a solid polymer electrolyte polarized to generate hydrogen from water at a cathode and oxygen at an anode. The membrane electrode of a first cell is partially exposed on one or both sides to a supply of liquid water and the hydrogen produced in this cell contacts the cathode surfaces of each successive electrolytic cell. Any water (2) entrained in or carried over with the hydrogen produced in the first cell is the only significant feedstock for each successive electrolytic cell. INDEPENDENT CLAIMS are included for:    (1) a method of generating dry hydrogen by electrolysis of water in a cascade of at least two electrolytic cells; and    (2) a method of operating a hydrogen generator, where two cells share a common chamber enclosing the respective electrodes and electrode surfaces of the same polarity face each other.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen generator.    Electrolytic cells (1, 17)    Water (2)    Leads (7, 8)    Enclosure (11)    Membrane (14)
NOVELTY - The device has a primary crushing machine provided with a grinding disk for primary grinding and crushing organic rubbish. The grinding disk is located in a crushing cavity. A biochemical processor is provided with a control circuit board (14), a speed reducing motor (13) and a filter screen (27). A stirrer is connected with the speed reducing motor via a transmission chain (16). The filter screen is provided with a ceramic grinding ball (22). An inner barrel (11) is provided with rubbish feeding ports (23, 24) and a cleaning port (25).    USE - Complete organic rubbish biochemical treatment device for use in a kitchen.    ADVANTAGE - The device performs primary biochemical rubbish crushing via grinding in the biochemical processor for processing the organic rubbish so as to save biochemical treatment time, improve processing effect and avoid accumulating frequent organic rubbish in the kitchen. The device avoids blocking of a water pipeline with rubbish and pollution so as to achieve standard rubbish discharge.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a complete organic rubbish biochemical treatment device in partial section.    Inner barrel (11)    Speed reducing motor (13)    Control circuit board (14)    Transmission chain (16)    Ceramic grinding ball (22)    Rubbish feeding ports (23, 24)    Cleaning port (25)    Filter screen (27)
NOVELTY - Producing methane from non-gaseous fuels, comprises initially gasifying fuel, preferably an entrained flow gasification at a pressure of 10 MPa and 1750 degrees C, cooling the hot gasification raw gas by direct contact with hot water and also quenching and saturating with water vapor, where the steam is used as a temperature moderator in one of the cooling/quenching of combined carbon monoxide conversion and methanation step.    USE - The method is useful for producing methane from non-gaseous fuels.    ADVANTAGE - The method has simple temperature limitation and heat dissipation.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the production of methane from non-gaseous fuels.
NOVELTY - An iron composite material is immersed in waste liquid containing phosphorus produced by methane fermentation of an organic waste, and phosphorus is precipitated and removed as iron phosphate. A suspension of iron phosphate is contacted with biogas containing hydrogen sulfide produced by methane fermentation, hydrogen sulfide in biogas is removed as iron sulfide. The produced phosphoric acid solution is reacted with calcium hydroxide and/or magnesium hydroxide and recovered as water-soluble phosphate.    USE - Recovery of phosphorus in waste liquid and purification of biogas from methane fermentation of organic waste e.g. agricultural waste, forestry waste, and waste materials from livestock farming.    ADVANTAGE - The method efficiently removes hydrogen sulfide contained in biogas and recovers phosphorus as phosphate, which can be used for fertilizers.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of the recovery method of phosphorus and purification of biogas. (Drawing includes non-English language text)
NOVELTY - Acrylonitrile, sulfuric acid and isobutylene are reacted and 2-methylpropane sulfonic acid acrylamide is separated from the reaction liquid. N-tert-butyl acrylamide in the reaction liquid is purified and collected after recovering N-tert-butyl acrylamide as crude crystals and collecting the crystals by sublimation.    USE - Manufacture of N-tert-butyl acrylamide used for cosmetics, print material and medical application.    ADVANTAGE - The N-tert-butyl acrylamide having stable color during preservation, high purity is manufactured economically and efficiently without using organic solvent such as methanol.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for sublimation purification apparatus, which consists of melting tank (1) and sublimation collection tower (8).    DESCRIPTION OF DRAWING(S) - The drawing shows the structure of the sublimation purification apparatus.    Melting tank (1)    Oil bath (2)    Nitrogen gas inlet tube (3)    Addition water inlet tube (4)    Sublimation collection tower (8)
NOVELTY - Enzymatic acylation method comprises contacting a compound having at least one function comprising amine, alcohol or thiol functions, at least one microorganism having an acyl transfer activity and/or an acyl transfer enzyme, and at least one acylphosphonate donor (I), and recovering the compound including at least one acyl function comprising the amine, alcohol or thiol functions.    USE - The enzymatic acylation method is useful for the production of organic compounds, preferably active substances, pharmaceutical intermediates and intermediate compounds for the flavor industry, perfumes and convenience products.    ADVANTAGE - The method is environmentally friendly and carried out in an inexpensive manner. The method does not require the use of harmful compounds, odorous and/or nucleophiles.    DETAILED DESCRIPTION - Enzymatic acylation method comprises contacting at least one compound having at least one function comprising amine, alcohol or thiol functions, at least one microorganism having an acyl transfer activity and/or an acyl transfer enzyme, and at least one acylphosphonate donor of formula (R-C(=O)-P(=X)(Y1)(Z)) (I), and recovering the compound including at least one acyl function comprising the amine, alcohol or thiol functions.    R = alkyl, alkene, alkyne, aryl, aralkyl, -OR1a, -SR1a or -NR1aR1b;    R1a, R1b = alkyl, alkene, alkyne, aryl or aralkyl (all optionally substituted), or H;    X = O or S;    Y1, Z = -OR1, -OR2, -SR1, -SR2, -NR11R21 or -NR12R22; and    R1, R2, R11, R12, R21, R22 = alkyl, alkene, alkyne, aryl or aralkyl (all optionally substituted).
NOVELTY - Catalytic hydrogenation involves performing catalytic hydrogenolysis reactions of hydroxy cycloalkane-derived substrates, such as menthol and isopulegol. A catalytic system consists of a physical mixture of heterogeneous hydrogenation catalysts, acidic heterogeneous catalysts and acid-supported metal hydrogenation catalysts, is also used. The used hydrogenation catalysts include noble metals from groups VI, VII, VIII, IX and X of the periodic table of the elements.    USE - Method for catalytic hydrogenation of hydroxy cycloalkanes for producing biofuel compositions for use in aviation industry, for propulsion jet engines and turbo motor powered aircraft and for use as filler in composition of aviation kerosene (claimed).    ADVANTAGE - The method produces the biofuel compositions increased energy density and reduced freezing point, which allows small volume of fuel tank and better performance of aircraft at high altitudes.
NOVELTY - Intensive large scale dairy cow dung compressed high density fuel comprises a compressed fuel obtained by compressing fresh dairy cow dung through a compressor into different shapes, drying by using a dryer at 100 degrees C until the water content is less than 12%, and separating by a dry-wet separator.    USE - Used as an intensive large scale dairy cow dung compressed high density fuel.    ADVANTAGE - The fuel: prevents the problem of pollution caused by the cattle industry on the environment; provides a new energy resource and manure resource; and conserves land and human resources.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the cow dung compressed fuel, comprising: (i) separating the cow dung by the dry-wet separator; (ii) compressing the cow dung by passing into a compressor; (iii) transferring the compressed product into the drier, drying at 100 degrees C, until the water content is less than 12% to obtain a cow dung compressed fuel.
NOVELTY - System has a floating unit, which is connected to cylinder. A raft is installed inside the floating unit, and a pump is provided for filling water inside the tank. A recovery unit is provided for the recovery of gas, which is formed inside the tank.    USE - System for recovery of methane obtained from organic compounds.    ADVANTAGE - The system enables to recovery methane in an efficient manner.
NOVELTY - Composting garden wastes using chemical composting agent is accelerated by pulverizing the garden wastes; adding water till the water content is 40-60%, then adding chemical composting agent (10-60 kg/ton garden wastes) and stirring uniformly, and then standing for 12-24 hours; and adding urea (8-12 kg/ton) and microbial strain (5-10 kg/ton) and composting for 24-34 days.    USE - Method for accelerating composting garden wastes using chemical composting agent (claimed).    ADVANTAGE - The method can solve the problem on garden wastes that are difficult to degrade and have long composting time. It is capable of removing lignin in the lignocelluloses and partly breaks the chemical bond between the lignin and the lignocelluloses so as to accelerate the composting of garden wastes.
NOVELTY - A biomass energy burner comprises combustion chamber provided at one side feeding port and main air inlet, where other side is open air outlet. The bottom of firebox is provided with carbon outlet. The combustion chamber of each side wall of air outlet is surrounded with distribution chamber. The combustion chamber is connected with air outlet of the annular. External portion is connected with one end of the ring wall. Carbon discharging pitch of helical blade is provided with carbon packing. The carbon discharging carbon along direction gradually decreases from top to bottom.    USE - Biomass energy burner for combustion chamber extension.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating a biomass energy burner.
NOVELTY - A rotary continuous carbonization furnace comprises furnace body (1) and fuel inlet, where furnace body is opposite to side wall of fuel . Flue gas flue is provided with gate (22). A combustion chamber is connected to furnace gate. The combustion chamber has high temperature hot air through smoke flue. The furnace utilizes afterheat of biomass boiler as heat source. The gate is made of refractory material made of the gate.    USE - Rotary continuous carbonization furnace.    ADVANTAGE - The furnace improves biomass boiler heat efficiency. It can achieve low carbon discharge and is environment-friendly. The heat energy is recycled without burning medium.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating a rotary continuous carbonization furnace.    Furnace body (1)    Gate (22)
NOVELTY - A roller-type aerobic fermentation device comprises a bracket and a shell arranged on the bracket. The shell is divided into upper and lower shells hinged by a fastening piece. A porous roller is horizontally arranged in the shell. Two ends of porous roller are connected with two ends of lower shell by a roller shaft. A roller handle is fixed connected on one end of roller shaft. A stirring blade shaft is axially and fixedly connected on inner side of porous roller. A water outlet pipe is arranged below the lower shell. A heater is arranged between inner side of shell and porous roller.    USE - Aerobic fermentation device used for treating kitchen waste for cultivating flowers and vegetables.    ADVANTAGE - The device is convenient to use, has simple structure, and enables quick fermentation and decomposition of kitchen waste.
NOVELTY - The system has a furnace body whose upper part is provided with a feeding mechanism and a gas washing tower. A middle part of the furnace body is provided with a fire grate. A bottom part of the furnace body is provided with a stirring blade, an air device and a slag pipe. The fire grate and the stirring blade are driven by a power shaft. A middle part of the fire grate is provided with multiple layers. A screw is provided with a slit that is equipped to the power shaft along axial direction. The power shaft is fixed at a furnace section.    USE - Biomass rubbish cracking furnace system.    ADVANTAGE - The system avoids oil formation condition, simplifies oil-gas separation process and improves sewage cracking process efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a biomass rubbish cracking furnace system.
NOVELTY - The container has a structure which is equipped with the stirring component attached to the inside of container main case (1). A steering-wheel (5) is attached to exterior of the container main case. The stirring component is provided with stirring shaft (4) rotated in response to rotation of the steering-wheel. The stirring component is provided with stirring blade (2) in the vertical direction with respect to the longitudinal direction of stirring shaft, and stirring blade is provided with the protrusion portion (3).    USE - Container for aerobically processing organic refuses by stimulating decomposition and preventing putrefaction of organic refuse using active microorganisms for promoting soil fungus and fermentation.    ADVANTAGE - The effect of taking in air is increased and aerobic decomposition force is improved. The effect of stimulating decomposition and reducing the capacity of the organic refuse is increased. The putrefaction of the organic refuse is prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the organic-refuse processing container. (Drawing includes non-English language text)    Container main case (1)    Stirring blade (2)    Protrusion portion (3)    Stirring shaft (4)    Steering-wheel (5)
NOVELTY - System comprises a livestock production facility for generating livestock output from their consumption of feed and water, an algae production facility located proximate to the livestock production facility, where the algae production facility comprises a reaction chamber for growing algae cells using livestock output, and a conduit providing fluid connection between the livestock production facility and the algae production facility.    USE - The system is useful for producing algae cells for processing biofuel (claimed).    ADVANTAGE - The system is convenient to use.    DETAILED DESCRIPTION - System comprises a livestock production facility for generating livestock output from their consumption of feed and water, an algae production facility located proximate to the livestock production facility, where the algae production facility comprises a reaction chamber for growing algae cells using livestock output, and a conduit providing fluid connection between the livestock production facility and the algae production facility, where the conduit defining a passageway comprises an input port through which livestock output is received from the livestock production facility and an output port through which livestock output is discharged into the reaction chamber. An INDEPENDENT CLAIM is included for method of producing algae cells.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of system.
NOVELTY - Anaerobic digestion method, involves performing biological treatment by fixed bed using living organism adhesion carrier which comprises a spherical porous portion, and circulating the processed sludge using carrier in the fixed bed, where the processed sludge is evenly distributed without circulating the carrier, without blocking the fixed layer.    USE - Anaerobic digestion method.    DETAILED DESCRIPTION - Anaerobic digestion method of wastewater or sludge, involves performing biological treatment by fixed bed (20) using living organism adhesion carrier (22) which comprises a spherical porous portion, and circulating the processed sludge using carrier in the fixed bed, where the processed sludge is evenly distributed without circulating the carrier, without blocking the fixed layer (28). The wastewater comprises 5000 mg/l or more of precipitated sludge. The wastewater is obtained from sewage or waste liquid precipitation processes. The sludge comprises livestock waste sludge or suspended solids. The sludge is supplied to the fixed bed, and is sampled from an upper layer of the fixed bed. The sampled processed sludge is supplied to a fixed layer in the adhesion carrier, which is provided in the lower layer of the fixed bed (20). The carrier comprises spherical porous portions with an average diameter of 4 mm or more.    DESCRIPTION OF DRAWING(S) - The drawing shows block diagram of digester used for anaerobic digestion method. (Drawing includes non-English language text)    Digester (10)    Fixed bed (20)    Processing tank (21)    Adhesion carrier (22)    Fixed layer (28)
NOVELTY - Alcoholic fermentation yeast, preferably Saccharomyces having tolerance to limonene, is new.    USE - The alcoholic fermentation yeast, preferably Saccharomyces is useful for producing ethanol (claimed) which is used as liquefied fuel.    ADVANTAGE - The yeast has excellent high temperature resistance, fermentability and stability, and produces ethanol cost-effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of manufacturing ethanol, which involves using the above-mentioned yeast.
NOVELTY - The method involves mixing a biomass liquefaction reaction and a solvent, where biomass is a plant seed, straw, trees, pasture, rice hull, bagasse, sawdust, wooden meal or seaweed. Reaction temperature is controlled at 180-450 degrees centigrade. A liquefied product is obtained after finishing the reaction. The liquefied product in water is extracted and separated a soluble organic product. The liquefied product is obtained by extracting and washing a separated organic soluble product. A mixture of the water and an oxygen-containing organic solvent are remained in a solid product.    USE - High pressure liquefied biomass carbon preparing method.    ADVANTAGE - The method ensures heat value of coal to be utilized as substitute of natural coal.
NOVELTY - The furnace has a furnace body (1) whose side is connected with an air outlet of a combustion gas channel (2). An upper end of the furnace body is provided with a feeding port (5). The feeding port is connected with a sealing cover (6). A lower part of the furnace body is equipped with a fuel isolated plate (7) and a water collector (8). A lower part of a front end of the collector is provided with a furnace door (9). The lower part of the furnace body is connected with an ash plate. The water collector is provided with a water outlet.    USE - Gas furnace for burning straw.    ADVANTAGE - The furnace can sufficiently burn straw.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a gas furnace.    Furnace body (1)    Combustion gas channel (2)    Feeding port (5)    Sealing cover (6)    Fuel isolated plate (7)    Water collector (8)    Furnace door (9)
NOVELTY - The device has a gasification process unit provided with a front gasification stage and a back gasification stage. A front biomass coke gasification phase unit and a biomass material are arranged in the gasification process unit. A gasification phase unit of the biomass material is connected with an up-draft gasification process unit. The gasification phase unit is connected with an upper part of a gasification device and a gasification reaction device. A primary gasification agent inlet is connected with a secondary gasification agent inlet.    USE - Biomass mixed gasification device.    ADVANTAGE - The device performs lower absorbing type gasification process and up-draft gasification so as to easily control a gas component. The device has strong load adaptability, stable operation, strong scale amplifying capacity, wide range of applications and high work efficiency. The device generates and supplies heat by electricity.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a biomass mixed gasification device. '(Drawing includes non-English language text)'
NOVELTY - The furnace has a furnace body (11) provided with a furnace material support (14) divided into a gas chamber and an air inlet chamber. A furnace inner container (12) is arranged in a gas generating chamber. An outer wall includes an air inlet of a furnace cover (3) vertically placed in an annular groove sealed by a sealing liquid (9). A blanking device is provided with a connecting rod head (7), a main rod (8) and a main rod locating shaft (10). The connecting rod head is connected on the furnace cover through a bolt (6) and sealed by a sealing gasket (4), a nut (5) and the furnace cover.    USE - Straw gasification furnace.    ADVANTAGE - The furnace is compact, and has reasonable design, simple structure, convenient use and better sealing performance. The furnace ensures continuity of gas generated by combustion reaction of a cavity, and has improved practicability.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial sectional view of a straw gasification furnace.    Furnace cover (3)    Sealing gasket (4)    Nut (5)    Bolt (6)    Connecting rod head (7)    Main rod (8)    Sealing liquid (9)    Main rod locating shaft (10)    Furnace body (11)    Furnace inner container (12)    Furnace material support (14)
NOVELTY - The furnace has a secondary catalytic cracking field (12) located around a lower part of a burning chamber. A secondary catalyzing cracking zone (5) and the catalytic cracking field are provided with a catalyst inlet (4) and a catalyst outlet (3). The cracking zone is provided with a wire net (8). The secondary catalyzing cracking zone is provided with a fuel gas outlet. A purifying device is connected with the gas outlet through a heat exchanger (19) of a heat exchange pipe. Another heat exchange pipe of the heat exchanger is connected with an air inlet combustion chamber (20).    USE - Secondary catalytic cracking biomass gasification furnace.    ADVANTAGE - The furnace ensures that the catalytic cracking of biomass fuel gas is divided into two steps and maintains temperature during catalytic cracking. The furnace ensures that a catalytic cracking chamber is scientifically designed for realizing adequate gas and catalyst supply. The furnace has high heat utilization rate, and enables a water jacket to cool the gas and utilizes waste heat to save energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a secondary catalytic cracking biomass gasification furnace.    Catalyst outlet (3)    Catalyst inlet (4)    Secondary catalyzing cracking zone (5)    Wire net (8)    Secondary catalytic cracking field (12)    Heat exchanger (19)    Air inlet combustion chamber (20)
NOVELTY - The device has a container (1) whose bottom part is provided with two vertical pipes (2, 4) that are respectively connected with an air inlet pipe (3) and an air outlet pipe (5). The vertical pipes are connected together by multiple bent pipes (6). The vertical pipes are connected with a lower end of an impurity tube (7).    USE - Biomass gas cooling device.    ADVANTAGE - The device has simple structure and better separating effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a biomass gas cooling device.    Container (1)    Vertical pipes (2, 4)    Air inlet pipe (3)    Air outlet pipe (5)    Bent pipes (6)    Impurity tube (7)
NOVELTY - A Bacillus-genus bacteria THU-H0024 strain (FERM P-21946) which is a microorganism which shows organic waste decomposition, is new.    USE - The Bacillus-genus bacteria THU-H0024 strain and methods are useful for decomposing organic waste; and for manufacturing compost (all claimed).    ADVANTAGE - The strain can efficiently decompose organic waste in a short time and produces less odor.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a method of decomposing organic waste comprising mixing the microorganisms with organic waste, and is heat-retained at the temperature of 37-75 degrees C; and    (2) a method of manufacturing compost comprising mixing the microorganisms with organic waste, and is heat-retained at the temperature of 37-75 degrees C.
NOVELTY - Method for manufacturing liquid manure, involves separating liquid from fermented organic waste residue, evaporating moisture content from the separated liquid, fractionating undiluted solution concentrated at the evaporation process to obtain potassium fraction and nitrogen-phosphorus fraction, and evaporating moisture content of each fractions.    USE - The method is useful for manufacturing liquid manure which is used as fertilizer for promoting plant growth.    ADVANTAGE - The manure is highly nutritious. The method is cost-effective, and can be performed using residue obtained after fermenting organic waste and producing biogas.
NOVELTY - The pelletized onion shell produced in large quantities during the classification process of onion is used as fuel of heating system. The shell is crushed and divided at the onion classification process using the crusher (16). The combustion air is generated by air heater (26) that uses the warm air generated by primary warm air generation unit.    USE - Heating system used in facility (claimed) of classification of onion during production.    ADVANTAGE - The operation cost of the onion classification facility is reduced efficiently, as the onion shell produced in large quantities during the classification process of onion is used as the fuel for operation of onion classification facility.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) onion classification facility; and    (2) working method of onion classification facility, which involves using shell pellet produced by granulator (20) as fuel for primary warm air generation apparatus for operation of heating system. The shell pellet is stocked in the stage at which the system is not operated.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the heating system.    Crusher (16)    Granulator (20)    Storage tank (21)    Carbonization furnace (22)    Air heater (26)
NOVELTY - A system for the manufacturing of a soil conditioner comprises a gaseous hydrocarbon source which is fed to plasma cracking unit (5), where the produced carbon (6) is fed to a circular vortex air flow material grinder (4) and the plasma carbon is mixed with a substrate (1) to produce a carbon enriched soil conditioner.    USE - For manufacturing of a soil conditioner (claimed).    ADVANTAGE - The present system is used to manufacture a soil conditioner by easily scaleable method which is used both in an industrial scale and at the individual farm. The system is produced inexpensively and thus become economically viable also in small scale facilities.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacturing (m1) of soil conditioner involving plasma cracking of a gaseous hydrocarbon source, mixing the produced carbon with a substrate, and grinding the mixture and optionally drying, where the mixing, grinding and drying is performed simultaneously; and    (2) a soil conditioner produced by the method (m1).    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a system for the manufacturing of a soil conditioner.    Substrate (1)    Circular vortex air flow material grinder (4)    Plasma cracking unit (5)    Carbon (6)
NOVELTY - The method involves calculating energy, sewage treatment, drugs emission factors and activity level of greenhouse gas emissions by fixed amount of greenhouse gases and carbon footprint, where the fixed amount of greenhouse gases is equal to trees cleared factor multiplied with activity level of greenhouse gas fixed amount, and the carbon footprint is equal to different between the greenhouse gas emissions and the fixed amount of greenhouse gases.    USE - Metering method for sewage treatment plant carbon footprint.    ADVANTAGE - The method enables metering the sewage treatment plant carbon footprint in a better manner in water plant, an urban sewage treatment plant and an industrial waste water processing system.
NOVELTY - Improved plant for the electrolytic decomposition of water, where water is introduced into a coulometer equipped with positive and negative electrodes; an electric current (DC) is passed from one cathode to another, the water, hydrogen and oxygen are separated and recovered in the electrolysis process, where improvements because they get their water from streams or water bodies existing without affecting the water for urban use or draw water from groundwater, and which includes the step of treating water to remove foreign matter, before submitting to the process of electrolysis.    USE - The improved plant is useful for the electrolytic decomposition of water (claimed).    ADVANTAGE - The improved plant does not use treated water from the water mains.
NOVELTY - Producing algal medium chain length fatty acids or hydrocarbons, comprises: culturing a first algal strain that produces a first medium chain length fatty acid subset; and extracting oil from the first algal strain to produce a medium chain length combination, where the medium chain length combination comprises carbon chain length C10, C12, C14 and C16 fatty acids or hydrocarbons, and the oil is enriched for C16 fatty acids such that greater than 50% of the fatty acids in the oil are C16 fatty acids.    USE - The method is useful for producing algal medium chain length fatty acids or hydrocarbons. The method is useful for producing a hydrocarbon fraction, such as isolated medium chain length hydrocarbon fraction, preferably kerosene (all claimed).    ADVANTAGE - The method provides large amounts of algal medium chain length fatty acids or hydrocarbons.    DETAILED DESCRIPTION - Producing algal medium chain length fatty acids or hydrocarbons, comprises: culturing a first algal strain that produces a first medium chain length fatty acid subset, where at least 50% of the fatty acids in the subset are of a chain length of C16, and the culturing is conducted under conditions suitable to promote the production of the first medium chain length fatty acid subset; and extracting oil from the first algal strain to produce a medium chain length combination, where the medium chain length combination comprises carbon chain length C10, C12, C14 and C16 fatty acids or hydrocarbons, and the oil is enriched for C16 fatty acids such that greater than 50% of the fatty acids in the oil are C16 fatty acids. An INDEPENDENT CLAIM is included for a composition comprising Nannochloropsis strain LRB-AZ 0202.2 deposited at ATCC Deposit Number PTA-11049 and/or Nannochloropsis strain LRB-AZ 0202.3 deposited at ATCC Deposit Number PTA-11050.
NOVELTY - The water disposal plant (10) has operation control system (221) which controls the dispersion transfer process of water in anaerobic tank (310). A nitrification liquid carrier pump (333c) is provided for allowing flow of nitrification liquid to anoxic chamber (320). An operation control system (412) is provided for processing water introduced into the indoor portion in water storage tank (410). A sludge catchment apparatus is provided for collecting the precipitated sludge such that sludge drawing pump (445) releases the sludge to the outside.    USE - Biochemical waste water disposal plant.    ADVANTAGE - The effectiveness of the waste water disposal process can be improved by removing phosphorus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of biochemical waste water disposal plant. (Drawing includes non-English language text)    Water disposal plant (10)    Operation control system (221)    Anaerobic tank (310)    Anoxic chamber (320)    Nitrification liquid carrier pump (333c)    Water storage tank (410)    Operation control system (412)    Sludge drawing pump (445)
NOVELTY - Method for using flammable plant powder as fuel firing ceramic grain, involves using fuel combustible plant powder.    USE - The method is for using flammable plant powder as fuel firing ceramic grain. The flammable plant powder is chaff powder (bran powder of 80 meshes), sawdust powder (sawmilling powder of 120 meshes), or straw powder (all claimed). The method is useful for producing ceramic used for modern building, sculpture and other fields.    ADVANTAGE - The method produces ceramic with energy saving, heat preservation, light weight and corrosion effects. Compared with the existing method, the method saves energy, reduces discharge of pollutant, has high surface intensity, and high puffing degree.
NOVELTY - The device has machine main portion, inlet and lift cover. The machine main portion is provided with upper and lower cavities. The upper cavity is solid kitchen garbage storage cavity. The lower cavity is liquid kitchen garbage storage cavity. Filter device is arranged between solid and liquid kitchen garbage storage cavities. Blowing heating device is arranged above opening of solid kitchen garbage storage cavity. Solid garbage storage cavity is arranged at bottom portion of liquid kitchen garbage storage cavity.    USE - Kitchen garbage fermentation device.    ADVANTAGE - Since the solid garbage storage cavity is arranged at bottom portion of liquid kitchen garbage storage cavity, separation of the solid kitchen garbage and liquid kitchen garbage can be realized easily, due to which fermentation, and decomposition are performed effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of the kitchen garbage fermentation device.
NOVELTY - The method involves forming adopting agricultural waste unit by using sawdust, straw, rice husk and a peanut shell. Rice bran is uniformly mixed with bran solid ammonium chloride, and fermentation material is filtered. The sawdust is uniformly mixed with water to form cushion material water. The cushion material water is kept at 40 to 50 percentages in stirring process.    USE - Pollution-free livestock home constructing method.    ADVANTAGE - The method enables improving anti-stress capability and immunologic function and reducing morbidity and poultry death rate.
NOVELTY - A reformer (10) consists of a carrier (14) having a substrate (32) containing iron-chromium-aluminum type alloy, and a support layer containing an alumina precipitate precipitated from the surface of the substrate in needle shape. A modification catalyst is supported on the support layer.    USE - Reformer is used for producing hydrogen from raw fuel containing hydrocarbon as main component.    ADVANTAGE - The reformer has excellent reformation efficiency with respect to raw fuel. The substrate has excellent thermal conductivity (which prevents heat spots and heat distribution, and homogenizes the temperature of modification catalyst) and thermal-impact durability. The carrier can be preheated efficiently. The support layer is firmly supported with respect to the substrate. The precipitate provides a large amount of corrugation, which increases the specific surface area. A suitable quantity of modification catalyst can be supported over a long period of time, maintaining excellent dispersibility. The support layer also improves the oxidation resistance of substrate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of reformer, which involves heat-processing a substrate in an oxidizing atmosphere at a temperature more than the temperature at which alumina precipitates and less than the melting point of substrate, forming a support layer to obtain a carrier, and supporting the modification catalyst.    DESCRIPTION OF DRAWING(S) - The drawing shows a longitudinal schematic cross-sectional view of the reformer. (Drawing includes non-English language text)    Reformer (10)    Carrier (14)    Heat insulating material (20)    Supply device (26)    Substrate (32)
NOVELTY - The method involves spirally wounding CF in sheet form for building a cylinder. The thin CF pipe (10) is provided with outer diameter smaller than internal diameter of wide CF pipe (9). The wide CF pipe and thin CF pipe are immersed in sodium chloride aqueous solution (8). The thin pipe is used as cathode and applied with direct current voltage, when wide pipe is used as anode such that chlorine and hydrogen are generated. The sodium hydroxide is generated in the cathode side even if wide pipe is used as cathode and thin pipe is used as anode.    USE - Electrolysis method of sodium chloride aqueous solution.    ADVANTAGE - The surface area of pipes can be increased with improved electrolysis efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of electrolyzer.    Sodium chloride aqueous solution (8)    Wide CF pipe (9)    Thin CF pipe (10)
NOVELTY - Extraction of indigenous microorganism from sludge comprises adding normal saline after mixing the dewatered sludge with decomposed sludge; taking the filtrate after vibrating and filtering to obtain mixed extracting liquid of indigenous microorganism; processing enrichment culture by enrichment culture liquid; and obtaining the indigenous microorganism from the enrichment as fermentation agent, where moisture content of dewatered sludge is 50-65 wt.%.    USE - Extraction of sludge indigenous microorganism for use as fermentation agent in compost sludge for static forced ventilation and fermentation (claimed).    ADVANTAGE - The method has wide sources and easy culture operation and composting environment adaptation; can quickly start the compost fermentation even if the environmental temperature is low, improving the composting efficiency and reducing the cost; and achieves stable composting parameters.
NOVELTY - A household garbage and sewage comprehensive processing system comprises a circulating gasification dry distillation incinerator, a heat exchanger, a secondary combustion chamber connected to the heat exchanger and to the incinerator through exhaust gas outlet, a smoke dust-removing device, a chimney, an anaerobic reaction tower having an energy-saving anaerobic pulse generator, an energy-saving anaerobic pulse generator, a liquid inlet, a sewage inlet connected to the anaerobic reaction tower, a methane, and an aerobic pool having water outlet.    USE - A household garbage and sewage comprehensive processing system for rural small town.    ADVANTAGE - The system can comprehensively recycle garbage and sewage.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a household garbage and sewage comprehensive processing system.
NOVELTY - A food wastewater recycling device comprises an electric flocculating reaction mechanism comprising an electrolytic flocculation reactor, a direct current pulse power supply, a feed hopper, and an electrode plate set on inner wall of the electrolytic flocculation reactor and connected to direct current pulse power supply; a fermentation mechanism comprising a fermentation tank, a storage tank and stirrer set at bottom of fermentation tank, and an air pump comprising a diaphragm pump and a centrifugal solid-liquid separator; and a transmission separating mechanism.    USE - A food wastewater recycling device.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a food wastewater recycling device.
NOVELTY - Hydroisomerization catalyst comprises: a catalytic material comprising a molecular sieve comprising a pre-loaded platinum group metal; and a matrix component, where the catalytic material and the matrix component are processed together to form the hydroisomerization catalyst.    USE - The hydroisomerization catalyst is useful for processing a bio-based feed into biodiesel fuel (claimed).    ADVANTAGE - The hydroisomerization catalyst exhibits high activity and thus provides the diesel fuel with excellent yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for making a biofuel, comprising: providing a source of paraffins derived from a bio-based feed; and contacting the hydrodeoxygenated bio-based feed with the hydroisomerization catalyst, to yield the biofuel.
NOVELTY - Fire substance/agent obtained by pressing hay and stiorin under the action of heat and cutting into pieces, after cooling or mixing hay and stiorin in a ratio of 1:1, is claimed.    USE - The fire substance/agent is useful for producing heat and energy (claimed), and in incinerators for heating of homes, buildings or in large combustion plants.    ADVANTAGE - The fire substance/agent produces heat and energy in an improved manner compared to the conventional fuels.
NOVELTY - A sewage treatment unit comprises a separation tank (2) which separates wastewater (1) into solid and liquid, concentrator (8) which concentrates separated sludge (4) from the separation tank, and a transfer installation which transfers concentrated liquid (10) discharged from the concentrator to a biological reactor (6) which carries out aerobic treatment of wastewater.    USE - A sewage treatment unit for processing organic substances in wastewater.    ADVANTAGE - Organic substances contained in sludge are collected in high yield, and nitrogen and phosphorus removal by microorganisms is carried out stably.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the sewage treatment unit.    Wastewater (1)    Separation tank (2)    Separated sludge (4)    Biological reactor (6)    Concentrator (8)
NOVELTY - The method involves arranging a fuel cell main body (120) between metal interconnectors (111, 112). A fuel gas flow channel (113) and an air flow path (114) are arranged between the interconnectors. Reaction of a solid electrolyte layer (122) is prevented by a reaction barrier layer (123). A frame (130) is connected to a separator (132) of the fuel cell main body. A main surface of a porous collector is connected by pressurizing the interconnectors. A fixing part fixes multiple sets of the fuel cell main body.    USE - Method for manufacturing a fuel cell stack.    ADVANTAGE - The main surface of the porous collector is connected by pressurizing the interconnectors, and the fixing part fixes multiple sets of the fuel cell main body, thus reducing the contact resistance between the fuel cell main body and the collector, and preventing the crack of the fuel cell main body.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a fuel cell.    Metal interconnectors (111, 112)    Fuel gas flow channel (113)    Air flow path (114)    Fuel cell main body (120)    Solid electrolyte layer (122)    Reaction barrier layer (123)    Frame (130)    Separator (132)
NOVELTY - A manufacturing method of biodiesel fuel oil involves transesterifying alcohol and raw material fat-and-oil, carrying out layer separation of reaction liquid, and contacting with cation exchange resin after contacting obtained light liquid with adsorption agent.    USE - A manufacturing method of biodiesel fuel oil.    ADVANTAGE - The method reduces carbon residue in biodiesel fuel oil.
NOVELTY - Producing a fuel composition from a feedstock which comprises biomass and/or municipal solid waste (MSW) involves pyrolyzing the feedstock in the presence of a transition metal, using microwave energy, so that the level of oxygen in at least one product of the pyrolysis is reduced.    USE - For producing a fuel composition from feedstock which comprises biomass and/or municipal solid waste (claimed).    ADVANTAGE - The method provides pyrolysis feedstock that contains a pre-determined amount of oxygen before pyrolysis, and after pyrolysis, the amount of oxygen has been reduced by at least 50% of the amount before pyrolysis.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a system for producing a fuel composition from a feedstock material comprising at least one of biomass and municipal solid waste (MSW), comprising: a pyrolysis reactor, adapted to accept a feedstock of biomass and/or MSW, and to convert the feedstock to pyrolysis products; a microwave source adapted to supply microwave energy to the pyrolysis reactor; a transition metal supply unit in communication with the pyrolysis reactor, to supply a selected amount of transition metal during pyrolysis; and at least one upgrading unit in communication with the pyrolysis reactor, to convert at least one of the pyrolysis products to a liquid fuel composition.
NOVELTY - The continuous or discontinuous integrated system for recycling and recovering energy from municipal solid waste and waste fractions such as plastic, organic-biodegradable, glass, paper, metals and other waste recycling activities, is claimed.    USE - The continuous or discontinuous integrated system for recycling and recovering energy from municipal solid waste and waste fractions such as plastic, organic-biodegradable, glass, paper, metals and other waste recycling activities (all claimed), and for biodegradable fraction treatment to get compost, plastic, glass, raw materials, paper and ferrous and non-ferrous metals.    ADVANTAGE - The continuous or discontinuous integrated system is capable of simply, rapidly, effectively and economically recycling and recovering energy from the municipal solid waste in an environmentally friendly manner with high throughput and reduced water consumption.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic view of a continuous or discontinuous integrated system.
NOVELTY - Catalytic hydrogenation involves reacting biomass through catalytic hydrogenation by using supported hydrogenation catalysts. The reaction is performed at 70-250 degrees C during stirring speed of 100-1000 revolutions per minute for 1-48 hours. The hydrogenation catalyst includes noble metals selected from groups VI-X of the periodic table of the elements, preferably nickel, platinum, palladium, ruthenium, molybdenum, cobalt, tungsten or their combinations.    USE - Method for producing p-menthane used as aviation biofuel, industrial solvent, auxiliary of synthesis processes and intermediate for fine chemicals, agrochemicals and drugs (all claimed).    ADVANTAGE - The method produces the p-menthane through single-step process by using hydrogenation catalyst with improved conversion and selectivity.
NOVELTY - Recovering pure cellulose from a cellulose-containing sludge, comprises treating a sludge cellulose source under conditions permitting dissolution of non-cellulose material and suspension of the cellulose, where the dissolution conditions do not alter cellulose morphology.    USE - The process is useful for recovering pure cellulose from cellulose-containing sludge. The nano crystalline cellulose is useful in material applications including foams, films for paper reinforcement and packaging, medical applications (e.g. tissue engineering), food thickening and lubricants.    ADVANTAGE - The energy effective process is cost effective and economical.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a process-I for preparing nano crystalline cellulose from cellulose sludge source, comprises (e) treating a sludge cellulose source to separate pure cellulose, (f) causing preferential degradation of cellulose amorphous domains while maintaining intact the cellulose crystalline domains, (g) isolating the crystalline domains and (h) optionally dispersing the obtained product to obtain NCC;    (2) pure cellulose obtained by the process; and    (3) nano crystalline cellulose obtainable by the process.
NOVELTY - The box has a fermenting tank that is provided with a feeding port, a discharging port and an exhaust port. The fermentation tank is provided with a stirring shaft. Stirring teeth is provided on the stirring shaft of a stirring device. The lower portion of fermentation tank is provided with a waste liquid collecting tank. The lower portion of waste liquid collecting tank is provided with a drain pipe.    USE - Processing box of household organic garbage placed in indoor or outdoor.    ADVANTAGE - The requirement of space for processing box can be reduced. The operation process of processing box can be simplified. The processing efficiency and treatment effect of box can be improved. The energy consumption of processing box can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the processing box of household organic garbage.
NOVELTY - Combustion analyzer comprises combustion chamber for receiving a sample for combustion to form combustion products, target gas sensor for sensing in the combustion products a target gas characteristic of incomplete combustion of the sample and generating signal indicative of incomplete combustion, and valve disposed upstream of the target gas sensor and switchable between first valve position for directing combustion products to the target gas sensor and second valve position for directing combustion products to waste line.    USE - The combustion analyzer is useful for combustion analyzing sample (claimed) in chemical, refinery, hydrocarbon, petrochemical, and food and beverage industries for analyzing solid, high-viscosity liquid or gaseous samples. Can also be used for analyzing refinery products chosen from gasoline, diesel and liquefied pressurized gas (LPG).    ADVANTAGE - The analyzer prevents soot formation, and is easy to maintain and cost-effective. The contamination of components of combustion products processing unit and target gas sensor is reduced.    DETAILED DESCRIPTION - Combustion analyzer comprises combustion chamber for receiving a sample for combustion to form combustion products, target gas sensor for sensing in the combustion products a target gas characteristic of incomplete combustion of the sample and generating signal indicative of incomplete combustion, and valve disposed upstream of the target gas sensor and switchable between first valve position for directing combustion products to the target gas sensor and second valve position for directing combustion products to waste line, where the valve is arranged to switch from its first position to its second position in response to the signal indicative of incomplete combustion. An INDEPENDENT CLAIM is included for method for combustion analyzing a sample in combustion analyzer.
NOVELTY - The device has rubbish landfill reactor and methane production reactor that are respectively connected with solar heating device. The rubbish landfill reactor and methane production reactor are provided with cylinder portion, insulating layer and heating pipe. A heating pipe outlet of the methane production reactor is connected with inlet of the solar heating device.    USE - Processing device for rural household rubbish.    ADVANTAGE - By using solar heating device, efficiency of the domestic rubbish stabilization and methane production reactor can be improved and yield is increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the processing device for rural household rubbish.
NOVELTY - A visible-light-response type photocatalyst (11) comprises tantalum-niobium nitride and has a maximum light absorption wavelength of 620-1008 nm.    USE - Visible-light-response type photocatalyst is useful for hydrolysis in hydrogen generators (all claimed). Can also be used in deodorizing devices, air purification apparatus, antibacterial films, stain-resistant films, super-hydrophilic films, anti-fogging films, and water purification devices.    ADVANTAGE - The visible-light-response type photocatalyst enables decomposition of water using light of wavelength 620 nm or more.    DETAILED DESCRIPTION - A visible-light-response type photocatalyst comprise tantalum-niobium nitride of formula: (TaxNb1-x)3N5 (x is 0 or more and less than 1, preferably greater than 0.13 and less than 1), and has a maximum light absorption wavelength of 620-1008 nm. INDEPENDENT CLAIMS are included for the following:    (1) hydrogen generator (1) which consists of a housing (15) which accommodates the visible-light-response type photocatalyst and an electrolyte solution (16) containing water and contacting the photocatalyst, and which decomposes water by irradiation of light to the photocatalyst to generate hydrogen; and    (2) hydrolysis method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen generator. (Drawing includes non-English language text)    Hydrogen generator (1)    Visible-light-response type photocatalyst (11)    Substrate (12)    Housing (15)    Electrolyte solution (16)
NOVELTY - Nitrogen-hydrogen mixture production for ammonia synthesis includes natural gas and carbon monoxide conversion and subsequent synthesis gas purification. During synthesis gas purification the removal of methane and argon is combined with the excess nitrogen condensation by methane and argon absorbtion by condensing excess nitrogen in the absorber-condenser vertical pipes in a counter flow with the purified synthesis gas that flows through the pipes from the bottom to the top. The inter-pipe space is cooled by throttling the condensate. The absorber-condenser pipes are provided with internal ribs ensuring condensate flow turbulization. The condensate collected as the absorber-condenser still liquid contains excess nitrogen liquid fraction enriched with methane and argon with hydrogen. Pure quality argon and liquefied methane is obtained from excess nitrogen fraction by rectifying the still liquid.    USE - In chemical industry for production on stoichiometric nitrogen-hydrogen mixture for ammonia synthesis.    ADVANTAGE - The content of argon and methane in the synthesis gas is reduced to 0.03 percent by volume and less. The synthesis ammonia pressure is reduced from 300 to 160-180 atmospheres, thus increasing the purification efficiency whilst ensuring complete extraction of inert admixtures. The ammonia production energy consumption is reduced and production of quality argon is ensured.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for    (A) Plant for synthesis gas purification from methane and argon and removal of excess of nitrogen to form stoichiometric nitrogen-hydrogen mixture
NOVELTY - Bioprocessing carbon-containing materials, comprises combining a feedstock comprising a cellulosic or lignocellulosic material and/or a saccharified cellulosic or lignocellulosic material, with a microorganism and a food-based nutrient source to form a mixture, where the microorganism utilizes the feedstock to produce a product or intermediate.    USE - The method is useful for bioprocessing carbon-containing materials to produce an intermediate or product, which is used as fuels (all claimed), energy, foods for human or animal consumption or materials.    ADVANTAGE - The method: utilizes low cost materials or waste material as the food-based nutrient source, thus enhancing efficiency of the bioprocess; and provides product, which is easily store, handle, and manufactured.    DESCRIPTION OF DRAWING(S) - The figure shows a flow diagram illustrating conversion of a feedstock to ethanol via production of a glucose solution.    Optionally mechanically treating the feedstock (110)    Recalcitrance (112)    Saccharifying the feedstock to form a sugar solution (114)    Optionally transporting the sugar solution to a manufacturing plant (116)    Product (118)
NOVELTY - Producing renewable fuel range hydrocarbon comprises: providing a fluid feed stream comprising at least one fatty material comprising triglycerides, diglycerides, monoglycerides or free fatty acids; providing a hydrocracking catalyst comprising a group VIII metal and a group VIB metal on an acidic support; and contacting the fluid feed stream with the catalyst under conditions sufficient for converting at least a portion of the fatty material into at least one member comprising 3-30C hydrocarbons.    USE - The process is useful for producing renewable fuel range hydrocarbon.    ADVANTAGE - The process: provides hydrocarbon-containing diesel product compounds exhibiting improved cold flow properties when compared with the diesel products of conventional hydrotreating processes; and yields significant quantities of 3-30C hydrocarbon compounds for improving the cetane rating of diesel fuel.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a renewable fuel range hydrocarbon produced by the above process; and    (2) a system comprising: the fluid feed stream comprising at least one fatty material; the hydrocracking catalyst; and a reactor for reacting the fluid feed stream with the catalyst conditions sufficient for converting at least a portion of the fatty material into at least one member comprising 3-30C hydrocarbons.
NOVELTY - Process of fractionation of animal by-product comprises: (a) grinding animal by-product to obtain particles having a size of 0.1-100 mm; (b) contacting the material with water at a temperature of 20-85 degrees C; (c) separating the solid phase and liquid phase from the mixture at a temperature of 20-85 degrees C; (d) decanting the liquid phase obtained in step (c); and (e) cooling and separating the aqueous and fatty phase obtained after the step (d).    USE - The protein solution is useful to prepare foods for pets, food paste and flavoring formulas. The fatty material is useful to prepare food for pets, biofuels such as biodiesel, soaps, detergents, lubricants, or paints. The protein-mineral aggregates are useful for the manufacture of bone glue, or as a source of calcium, nitrogen and phosphorus in a fertilizer (all claimed).    ADVANTAGE - The process is cost effective and rapid, and allows an excellent fat extraction by simply using water.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for protein solution obtained by the method, containing 1-20 wt.% of dry extract comprising: 75-95 wt.% of protein; 1-10 wt.% of fat, and 0.5-3 wt.% of minerals; 0.1-5 wt.% of sulfated glycosaminoglycans; and 0.01-1 wt.% of hyaluronic acid.
NOVELTY - Converting carbonaceous material into fuel bases comprises: (a) liquefying the carbonaceous material in the presence of hydrogen in at least one reactor containing a supported catalyst in a boiling bed; and (b) liquefying a part of the effluent obtained in the step (a) in the presence of hydrogen in at least one reactor containing a supported catalyst in bubbling bed and operating at a temperature of at least 10 degrees C higher than that of the step (a), where the process comprises producing hydrogen using at least one non-fossil resources.    USE - The process is useful for converting carbonaceous material.    ADVANTAGE - The process converting carbonaceous material with high yield.    DETAILED DESCRIPTION - Converting carbonaceous material into fuel bases comprises: (a) liquefying the carbonaceous material in the presence of hydrogen in at least one reactor containing a supported catalyst in a boiling bed; and (b) liquefying a part of the effluent obtained in the step (a) in the presence of hydrogen in at least one reactor containing a supported catalyst in bubbling bed and operating at a temperature of at least 10 degrees C higher than that of the step (a), where the process comprises producing hydrogen using at least one non-fossil resources, and the produced hydrogen is at least partially or totally introduced into at least one of liquefaction steps.
NOVELTY - An aromatic compound (I) is made to react with 4-acetyl butyric acid (II) in presence of solid acid catalyst to obtain cyclohexanone (III).    USE - Manufacture of cyclohexanone used as intermediate and raw material of pharmaceuticals and agrochemicals.    ADVANTAGE - The method efficiently provides cyclohexanone at high yield by safe process within a short period of time, and enables recovery of solid acid catalyst by simple process, without generating toxic wastes and polluting the environment.    DETAILED DESCRIPTION - An aromatic compound of formula: RH (I) is made to react with 4-acetyl butyric acid of formula: CH3COCH2CH2CH2CO2H (II), in which hydrogen atoms of methylene group is optionally substituted by the group which is not involved in the reaction, in presence of solid acid catalyst to obtain cyclohexanone of formula (III).    R=monovalent hydrocarbyl ring system or heterocyclic aromatic organic group, where a portion of hydrocarbyl rings and heterocyclic hydrogen atoms are optionally substituted by the group which is not involved in the reaction.
NOVELTY - The system has fresh mass airflow (MAF) sensors estimating fresh mass flow combined with exhaust oxygen measurements. An exhaust oxygen sensor measures exhaust oxygen in an internal combustion engine. An engine speed sensor measures engine speed. An engine torque sensor measures engine torque, where the sensors are used to estimate biodiesel blend ratio marked by solid circles. The engine includes power cylinders (1), an intake air throttle (2), a charge air cooler (3), an exhaust gas recirculation (EGR) valve (4), EGR cooler (5), a compressor (6) and a variable geometry turbine (7).    USE - Biodiesel estimation system for an internal combustion engine.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an internal combustion engine.    Power cylinders (1)    Intake air throttle (2)    Charge air cooler (3)    EGR valve (4)    EGR cooler (5)    Compressor (6)    Variable geometry turbine (7)
NOVELTY - Conveying type discharging device for straw fiber material feed, comprises a material injection cylinder piston (1), first piston (2), second piston (3), power cylinder (4), suction one-way valve (5), and discharge valve.    USE - Conveying type discharging device for straw fiber material feed.    ADVANTAGE - The device is simple in structure, durable and convenient to use.    DETAILED DESCRIPTION - Conveying type discharging device for straw fiber material feed, comprises a material injection cylinder piston (1), first piston (2), second piston (3), power cylinder (4), suction one-way valve (5), and discharge valve. The first piston is contained in the cylinder piston. The second piston is contained in the power cylinder. The first piston and second piston are connected through a connecting bar. The power cylinder is respectively provided with a first pressure and second pressure pipe. The first pressure and second pressure pipe are located on different sides of the second piston. The second piston reciprocates motion to realize feeding and deslagging raw material. The suction valve and discharge valve are respectively connected with the cylinder piston.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of the device.    Cylinder piston (1)    First piston (2)    Second piston (3)    Power cylinder (4)    Suction one-way valve (5)
NOVELTY - Biogas anaerobic fermentation tank (1) has marsh gas anaerobic fermentation tank horizontally set with three phase separation device (3).    USE - The anaerobic fermentation tank is useful for producing biogas by processing dairy manure.    ADVANTAGE - The tank has simple structure and convenient construction. The tank effectively prevents material crust, as it has steel structure grid design, does not need power in the production of biogas and avoids slag at liquid surface crust. The device effectively separates solid, liquid and gas and improves yield, as three phase separation device is present.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic representation of biogas anaerobic fermentation tank.    Biogas anaerobic fermentation tank (1)    Biogas outlet (2)    Three phase separation device (3)    Material inlet (4)    Overflow port (6)
NOVELTY - The tank has upper shell (1) and lower shell (3) that is provided with observing port (1a). An observation window (6) is mounted on upper shell of the observation port and provided with biogas output pipe (6a) and pressing nozzle (6b). One end of pressing pipe (8) is inserted in pressing pipe while other end of pressing pipe is connected with pressure pump (9). A groove (4) is arranged on upper shell. The upper port of water pressure tube (5) is connected with discharging box. The feeding cylinder (3b) with round shape lower end opening is connected to intersection of upper shell.    USE - Methane tank for feeding glass fiber reinforced plastic.    ADVANTAGE - The glass fiber reinforced plastic marsh can be fed conveniently as the feeding cylinder with round shape lower end opening is connected to intersection point of upper shell.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the methane tank.    Shell (1,3)    Observing port (1a)    Feeding cylinder (3b)    Groove (4)    Water pressure tube (5)    Observation window (6)    Biogas output pipe (6a)    Pressing nozzle (6b)    Pressing pipe (8)    Pressure pump (9)
NOVELTY - The device has a tank main portion (4) that is provided with a blade (10). The font end of the motor (1) is provided with stirring shaft (13). The sealing seat (3) is connected to the tank main portion through a shaft joint (2). The stirring shaft is connected to front and back end of the two stirring semi-shaft (16) and is mounted on the bracket through bearing seat (11).The front end of the displacement pump (1) is connected with the feeding port (14) while back end is connected with the top of the collecting cover (5).    USE - Dry fermentation biogas device for straw/solid organic waste treatment device.    ADVANTAGE - Since the front end of the displacement pump is connected with the feeding port while back end is connected with the top of the collecting cover, the installation is easy, so that more energy is saved and the production is high. The occurrence of environment pollution can be avoided.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the dry fermentation biogas device. (Drawing includes non-English language text)    Motor (1)    Shaft joint (2)    Sealing seat (3)    Tank main portion (4)    Collecting cover (5)    Blade (10)    Bearing seat (11)    Stirring shaft (13)    Feeding port (14)    Stirring semi-shaft (16)
NOVELTY - A dry etching agent comprises 1,3,3,3-tetrafluoropropene, additive gas, and an inert gas.    USE - Dry etching agent is used for etching silicon-type material (claimed) during manufacture of semiconductor.    ADVANTAGE - The dry etching agent has reduced impact on global environment, wide process window, and can accommodate without a special substrate-exciting operation, and responds to a process which requires reduced side etch ratio and a high aspect ratio.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for dry etching method, which involves selectively etching silicon-type material chosen from silicon dioxide, silicon nitride, polycrystalline silicon, amorphous silicon, and silicon carbide, using plasma gas obtained by plasmifying the dry etching agent.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the test equipment for etching using the dry etching agent. (Drawing includes non-English language text)    Chamber (1)    Pressure gauge (2)    Lower electrode (4)    Upper electrode (5)    Specimen (8)
NOVELTY - Purifying biogas using a biogas purifier comprises adding a desulfurizer into a permeable membrane bag, placing the bag in first (1) and second purification cylinders (2), measuring the atmospheric pressure in the biogas purifier using a real-time pressure gauge, closing a valve (3a) and opening an air outlet at relatively low pressure to enable a small amount of biogas to pass through the desulfurizer for the first time, opening the valve and an outlet port (2c) and closing the air outlet (1c) at relatively high pressure to enable large amount of biogas pass through the desulfurizer.    USE - The method is useful for purifying biogas using a biogas purifier.    ADVANTAGE - The method: is convenient, saves energy and raw material; and replaces the desulfurizer rapidly with high desulfurization efficiency.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of the biogas purifier.    First purification cylinder (1)    Air outlet (1c)    Second purification cylinder (2)    Outlet port (2c)    Valve (3a)
NOVELTY - Bio-desulfurization unit of a biogas project comprises a shell, a gas inlet pipe, a gas outlet pipe, a return pipe, a spraying pipe, a filler layer, a nutrient fluid layer, an air inlet pipe and a waste liquor tube. The filler layer is located in the shell is a webby filler attached to the biological filler. The nutrient fluid layer is arranged in the shell. The return pipe connected with circumfluence pump and the lower end is opened in nutrient fluid layer surface, and upper end of the spraying pipe. The spraying pipe is at the top of the shell and opening at the top of the filler layer.    USE - Used as a bio-desulfurization unit of a biogas project.    ADVANTAGE - The device: is simple in structure, convenient to operate, safe, reliable; and has high processing efficiency.    DETAILED DESCRIPTION - Bio-desulfurization unit of a biogas project comprises a shell, a gas inlet pipe, a gas outlet pipe, a return pipe, a spraying pipe, a filler layer, a nutrient fluid layer, an air inlet pipe and a waste liquor tube. The filler layer is located in the shell is a webby filler attached to the biological filler. The nutrient fluid layer is the filler layer in the shell. The return pipe is connected with the circumfluence pump and the lower end is opened in the nutrient fluid layer surface, and the upper end of the link spraying pipe. The spraying pipe is at the top of the shell and opening at the top of the filler layer. The gas inlet pipe and the air inlet pipe between the filler layer and the nutrient solution layer at the lower end of the shell, and the air heating and humidifying process from the air inlet pipe into the shell.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the bio-desulfurization unit of a biogas project.
NOVELTY - Automated discharging biogas desulfurization device comprises a vertically arranged reverse cone tank body (4). The middle part of the tank body is horizontally fixed with a hoop (6) and a support. The support comprises four supporting legs (7) and a beam (18) is horizontally set between the two adjacent supporting legs. The hoop is symmetrically fixed with two horizontal rotating shafts. The open ends of the rotating shafts are fixed on the two cross beams by bearings (8). The middle part of the support is used for fixing the tank body to a braking device.    USE - Used as an automated discharging biogas desulfurization device.    ADVANTAGE - The device reduces the labor intensity, and improves the production efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the automated discharging biogas desulfurization device.    Tank body (4)    Hoop (6)    Supporting legs (7)    Bearings (8)    Beam (18)
NOVELTY - An urban residential area biogas pool comprises crushed garbage inlet (7), urine feeding port (5), discharging opening (10) and biogas outlet pipe (9) of marsh gas tank body (1). The biogas tank body is provided with at least two methane tank body buried underground well. The axial size is at least 2 times of radial size. Urine feeding port is connected with tank.    USE - Urban residential area biogas pool for urban environment construction.    ADVANTAGE - The biogas pool has enlarged capacity, saves land, household garbage and excrement. The cell is stable and continuous. It ensures stable gas. The residue is environment-friendly and is a harmless organic fertilizer.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating an urban residential area biogas pool.    Tank body (1)    Urine feeding port (5)    Garbage inlet (7)    Biogas outlet pipe (9)    Discharging opening (10)
NOVELTY - Anaerobic biogas power generation engineering equipment comprises pulp slurry collecting tank (1), anaerobic reactor (2), reaction power box (3), and wet gas storage tank (4) which are sequentially connected through pipelines. The pulp slurry collecting tank is divided into adjusting tank (6) and feed tank (7) by a partition plate provided with a grid (8). The anaerobic reactor is connected to a biogas tank (5) through a pipeline.    USE - Anaerobic biogas power generation engineering equipment.    ADVANTAGE - The anaerobic biogas power generation engineering equipment has simple structure and can effectively utilize biogas resources, such as waste straw and wood pulp, for power generation.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating the anaerobic biogas power generation engineering equipment.    Pulp slurry collecting tank (1)    Anaerobic reactor (2)    Reaction power box (3)    Wet gas storage tank (4)    Biogas tank (5)    Adjusting tank (6)    Feed tank (7)    Grid (8)
NOVELTY - A combined biogas fermenting tank feeding system comprises a feeding port (1) provided with hopper (2); a group of roller wheels (3) disposed at the lower end of the hopper; a pipeline (4) connecting the material inlet and material outlet; and a packing auger (6) provided with discharge port (7). The tail end of the packing auger is provided with motor (8).    USE - Combined biogas fermenting tank feeding system.    ADVANTAGE - The combined biogas fermenting tank feeding system has reasonable design and high degree of mechanization; can speed up pre-processing of the biogas raw material; reduces labor intensity; improves the efficiency of the fermentation base material; and ensures the production efficiency. The whole feeding system can be mounted on the trolley frame (10) and can be moved easily, thus satisfying the need for the fermentation base multipoint feeding process.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating the combined biogas tank feeding system.    Feeding port (1)    Hopper (2)    Roller wheels (3)    Pipeline (4)    Packing auger (6)    Discharge port (7)    Motor (8)    Trolley frame (10)
NOVELTY - The movable plant has protective side railings that are provided with stairs. A table is positioned near a heating assembly that is supported by a bench. A peripheral suction pump and a gear pump are provided with a control panel. Multiple support structures are connected to poly vinyl chloride tubes. Multiple nozzles are provided for removing the glycerol.    USE - Movable plant for production of biodiesel.    ADVANTAGE - The movable plant has protective side railings that are provided with stairs, where a table is positioned near a heating assembly that is supported by a bench, and thus ensures efficient and convenient plant.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a biodiesel movable plant.
NOVELTY - The device has an inlet pipe (1) arranged in a lower tank body (8). A ceramic filling layer (2) is located at an upper part of the lower tank body. A liquid baffle plate is arranged in an upper tank body (7). A tail gas outlet portion (3) is arranged at a top portion of the upper tank body. A bottom outlet portion (4) is arranged at a bottom portion of the lower tank body. A discharge opening portion (6) and a manhole (5) are arranged in the ceramic filling layer. The inlet pipe is connected to a buffer. The tail gas outlet portion is connected to a vacuum system.    USE - Rectifying oil, coke and tail gas separation device for producing biological diesel.    ADVANTAGE - The device has high vacuum degree and efficient and steady operation.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a rectifying oil, coke and tail gas separation device.    Inlet pipe (1)    Ceramic filling layer (2)    Tail gas outlet portion (3)    Bottom outlet portion (4)    Manhole (5)    Discharge opening portion (6)    Upper tank body (7)    Lower tank body (8)
NOVELTY - The generator has a gasification furnace provided with a sealed dedusting pool that is charged with water. An outlet is formed at a bottom part of a lower furnace body and extended to the dedusting pool. An inside part of the dedusting pool is provided with a dust cleaning device. A dust sucking end part of the dust cleaning device is extended to a bottom part of the dedusting pool. A dust outlet is extended to the dedusting pool. The gasification furnace comprises multiple fire grates that are connected with a rotary shaft. A grate support is connected with a grate rotating device.    USE - Biomass fuel gas generator.    ADVANTAGE - The generator has simple structure and rational design, and guarantees normal running of dust cleaning device with high efficiency and stability, increases utilization rate and production efficiency and avoids resource wastage.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of a biomass fuel gas generator.
NOVELTY - Hydrogen-generating material comprises many metal particles consisting of aluminum and/or its alloy, and many modifier particles with an average particle size of less than 25 nm being mixed with the metal particles, where the modifier particles comprise titanium dioxide particles.    USE - The material is useful for generating hydrogen (claimed).    ADVANTAGE - The material is suitable: for generating hydrogen in a simple and cost-effective manner; for providing products that are free of carbon such as carbon monoxide or carbon dioxide, hence safe to human and environment; and for recycling by-products, such as aluminum hydroxide or aluminum oxide for further treatments.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing hydrogen, comprising mixing the metal particles with the modifier particles to generate a hydrogen-generating material, and reacting the hydrogen-generating material with water to generate products comprising hydrogen.
NOVELTY - Producing (M1) phase stable, reduced acid biomass-derived pyrolysis oil involves providing a biomass-derived pyrolysis oil having determined water content not greater than 30 wt.%; and mixing a base with the biomass-derived pyrolysis oil.    USE - For producing phase stable, reduced acid biomass-derived pyrolysis oil from water-containing biomass-derived pyrolysis oil (claimed), used as a fuel and biofuel.    ADVANTAGE - The method provides phase stable, reduced acid biomass-derived pyrolysis oil having a water content of not greater than 30 wt.% that is homogenous, with an acidity (as measured by pH) reduced from that of conventional biomass-derived pyrolysis oil. The energy density of the phase stable, reduced acid biomass-derived pyrolysis oil is higher than that of conventional biomass-derived pyrolysis oil. The increased pH, phase homogeneity, and higher energy density of the phase stable, reduced acid biomass-derived pyrolysis oil produced improve its suitability as a fuel and biofuel.
NOVELTY - The method involves generating specific amount of hydrogen/oxygen based on two conditions. An electrolyte is composed of a specific mixture of distilled water and Potassium hydroxide (KOH). A cell following the specifications is produced. The system is shut down effectively by the sensor, if the water level reach the level of the sensor.    USE - Method for producing stable cell in hydrogen/oxygen generator apparatus.    ADVANTAGE - The Bubbler can purify the hydrogen/oxygen gas and protect the internal combustion engine in case of backfiring.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the electrolyte level sensor.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the cell.    Solid container (11)    Top cover (12)    Negative connector (13)    Positive connector (14)    Electrolyte Level Sensor (15)
NOVELTY - The system has a dehydrator connected with a filtrate pool via a pipeline. A separator is connected with an iron collector, a mechanical sorting machine and a manual sorting platform inorganic glass. A fluid bed gasification oven is utilized for discharging a furnace refractory lining. An inner ring slot and an outer ring slot are connected with a slurry pump. A slag pump is connected with a ball mill via a residual reflowing pipe. A gas purification system is connected with a fuel gas inlet. A gas scrubber of the gas purification system is connected with a gas blower air inlet.    USE - Large-scale rubbish gasification treatment and energy recycling system.    ADVANTAGE - The system improves utilization development rate, and has energy-saving function. The rubbish is processed by single process to save cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a big scale rubbish gasification treatment and energy recycling system.
NOVELTY - Waste water treatment system, comprises: a basin for holding water; nitrifying and denitrifying bacteria; macroalgae; and a biobed having at least one layer and is constructed of materials selected to allow pH adjustments for enabling bacterial and algal growth, in which biobed de-nitrification and nitrification bacterial processes are separated, where oxygen produced by algae is used by the nitrifying bacteria, and water is provided continuously to the biobed at an inlet and exits the system downstream after having gone through the biobed.    USE - The system is useful for: treating waste water (claimed); cleaning nitrogen, phosphorus and biochemical oxygen demand in water; cultivating algae; and producing biogas.    ADVANTAGE - The waste water treatment system: decreases the need for energy and chemicals, thus is cost effective; exhibits high flexibility for construction on site; and produces biomass efficiently.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for treating waste water, comprising providing the waste water treatment system, and harvesting algae from the biobed.
NOVELTY - A biomass processing apparatus (1) comprises mixing tank (2) which mixes fermentation residue of biomass and biomass, processing tank (3, 3A-3C) where mixture is injected and performs dry-type methane fermentation of mixture, heating apparatus (4) which heats inside of processing tank, biogas collection unit (5) which collects biogas produced from mixture during dry-type methane fermentation, composting unit (6) which composts fermentation residue after passing through processing tank, and discharge unit (7) which emits composted fermentation residue from processing tank.    USE - A biomass processing apparatus (claimed).    ADVANTAGE - Biomass is easily processed, biogas collection is performed efficiently, and installation space of processing tank reduces installation cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional diagram of a biogas processing apparatus.    Biomass processing apparatus (1)    Mixing tank (2)    Processing tank (3, 3A-3C)    Heating apparatus (4)    Biogas collection unit (5)
NOVELTY - The combustion gas generator (1) has 3asteriskn electrodes and spacers (4) arranged alternating with the electrodes, where n is a natural number greater than or equal to 3. The electrodes are grouped into a floating electrode group which does not require grounding and voltage application, a first electrode group to which a positive voltage or a negative voltage is applied, and a second electrode group to which a voltage of polarity different from the voltage applied to the first electrode group is applied.    USE - Combustion gas generator for use in e.g. motor vehicle to generate combustion gas containing oxygen gas and hydrogen gas.    ADVANTAGE - Reduces number of electrical connections since floating electrode group does not require grounding and voltage application and is instead electrically charged when voltage is applied to first and second electrode groups, thus reducing distance between electrodes and voltage applied to electrodes. All electrodes are utilized effectively, suppressing heat generation and corrosion of electrode. Hydrogen gas and oxygen gas can be generated efficiently.    DESCRIPTION OF DRAWING(S) - The drawing is a front view which shows the combustion gas generator.    Combustion gas generator (1)    Electrolytic vessel (2)    Spacers (4)    Bolt shank (9)    Electrolytic solution tank (12)
NOVELTY - A method (M1) of production of a biofuel involves co-culturing polysaccharide-producing photosynthetic microorganisms with polysaccharide-consuming, biofuel-producing, non-photosynthetic microorganisms to produce a biofuel.    USE - For production of biofuel such as alcohol (including ethanol, propanol and butanol), alkene, alkane, lipid or polysaccharide (claimed).    ADVANTAGE - The method shows high productivity of the biofuel.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a method (M2) of production of lipid involving co-culturing a lipid-producing, photosynthetic microorganism with a solvent-producing, non-photosynthetic microorganism, where the lipid is soluble in the solvent;    (2) a co-culture (C1) of photosynthetic microorganisms and non-photosynthetic organisms where the photosynthetic microorganisms produce polysaccharide and the non-photosynthetic microorganisms consume the produced polysaccharide and produce a biofuel;    (3) a co-culture (C2) of lipid-producing, photosynthetic microorganisms and solvent-producing, non-photosynthetic microorganisms, where the lipid is soluble in the solvent; and    (4) a composition (C3) comprising an oil and an alcohol.
NOVELTY - Deoxygenating treated biomass-derived pyrolysis oil, involves: exposing the treated biomass-derived pyrolysis oil to a catalyst having a neutral catalyst support.    USE - For deoxygenating treated biomass-derived pyrolysis oil (claimed).    ADVANTAGE - The low oxygen biomass-derived pyrolysis oil produced in the method has significantly less oxygen and water, making it more suitable for use and processing as a biofuel. In addition, the plugging that occurs with conventional deoxygenation is substantially prevented, providing for longer run times and improved processibility of the biomass-derived pyrolysis oil.
NOVELTY - Heterogeneous enzyme catalyst, which is in the form of a honeycomb monolith made of a silica matrix, where the monolith is free of micropores and comprises macropores having an average size (dA) of 1-100 mu m and mesopores having an average size of 2-50 nm, the macropores are interconnected, and in which the inner surface of the macropores is functionalized by a coupling agent comprising silanes on which an enzyme is fixed, through covalent or electrostatic bonding, is new.    USE - The heterogeneous enzyme catalyst is useful for the production of chemical reactions catalyzed in heterogeneous phase in continuous flow, where the enzyme is a lipase, to catalyze the hydrolysis of fatty acid triglycerides, esterification reactions of an acid and an alcohol, transesterification reactions of an ester and an alcohol, inter-esterification reactions of two esters or transfer reactions of an acetyl group of an ester on amine or thiol; for synthesizing butyloleate, for hydrolyzing the glycerolinoleic ester derivatives for producing soaps or detergents, for transesterification reaction of fatty acid triglycerides by an alcohol, such reactions are involved in the synthesis of biodiesel at low viscosity (all claimed).    ADVANTAGE - The preparation of the catalyst is simple and cost effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of the heterogeneous enzyme catalyst.
NOVELTY - Purifying a gaseous stream comprising methane, comprises: passing the gaseous stream including methane through a column that is packed with an adsorbent material; maintaining the column at an adsorption temperature, where the adsorption temperature is a temperature at which an amount of methane is retained in the column, while impurities in the gaseous stream are released from the column; and subsequently heating the column to a desorption temperature, where the desorption temperature is a temperature at which the retained methane is released from the column.    USE - The method is useful for purifying a gaseous stream comprising methane (claimed), during the production of methyl iodide.    ADVANTAGE - The method: eliminates the need of liquid nitrogen to retain methane for synthesis purification; can conduct the process at room temperature (based on the chemical and physical properties of the sorbent); removes methane from the column by simple heating; and alleviates serious risks to personnel arising from handling cryogenic materials.    DESCRIPTION OF DRAWING(S) - The figure shows a process flow employing a chemical trap.    Chemical trap (5)    Heating mantle (6)    Particle accelerator (12)    Hydrogen supply tank (13)    Methane oven (14)
NOVELTY - An apparatus having a tank (21) comprising electrolyte solution (15), a working electrode (11) containing boron compound chosen from strontium hexaboride, calcium hexaboride, barium hexaboride, lanthanum hexaboride and cerium hexaboride, and a counter electrode (13) containing metal is prepared. The carbon dioxide in electrolyte solution is reduced by applying negative voltage and positive voltage to working electrode and counter electrode, respectively.    USE - Reduction of carbon dioxide used for generating methane, ethylene, ethane and formic acid (all claimed).    ADVANTAGE - The method enables efficient reduction of carbon dioxide.    DETAILED DESCRIPTION - An apparatus having a tank comprising electrolyte solution, a working electrode containing boron compound chosen from strontium hexaboride, calcium hexaboride, barium hexaboride, lanthanum hexaboride and cerium hexaboride, and a counter electrode containing metal is prepared. The boron compound touches the electrolyte solution. The metal touches the electrolyte solution. The electrolyte solution contains carbon dioxide. The carbon dioxide in electrolyte solution is reduced by applying negative voltage and positive voltage to working electrode and counter electrode, respectively.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the apparatus for reducing carbon dioxide.    Working electrode (11)    Counter electrode (13)    Electrolyte solution (15)    Solid electrolytic membrane (16)    Tank (21)
NOVELTY - An apparatus having a tank (21) comprising electrolyte solution (15), a working electrode (11) containing boron, and a counter electrode (13) containing metal is prepared. The boron compound touches the electrolyte solution. The metal touches the electrolyte solution. The electrolyte solution contains carbon dioxide. The carbon dioxide in electrolyte solution is reduced by applying negative voltage and positive voltage to working electrode and counter electrode, respectively.    USE - Reduction of carbon dioxide used for generating methane, ethylene, ethane and formic acid (all claimed).    ADVANTAGE - The method enables efficient reduction of carbon dioxide.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the apparatus for reducing carbon dioxide.    Working electrode (11)    Counter electrode (13)    Electrolyte solution (15)    Solid electrolytic membrane (16)    Tank (21)
NOVELTY - The device (100) has a reaction chamber (120) for reacting hydrogenated polysilanes with water. A supply line device (112) supplies a reagent into the reaction chamber. Dissipation devices (122-124) dissipate the hydrogen to a fuel cell (150) during reaction process, where the hydrogenated polysilanes are selected from a group consisting of powders, granules, balls, cubes, pellets or porous pieces. The reaction chamber comprises metal catalysts, and is provided with basic medium i.e. alkaline medium. A water storage container (110) provides water to the supply line device.    USE - Fuel cell supply device for use as an emergency system to produce hydrogen to operate a fuel cell i.e. polymer electrolyte membrane fuel cell, in an aircraft (all claimed).    ADVANTAGE - The device ensures simple and safe hydrogen supply of the fuel cell in the aircraft.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for producing hydrogen for a fuel cell in an aircraft.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a fuel cell supply device for producing hydrogen.    Fuel cell supply device (100)    Water storage container (110)    Supply line device (112)    Reaction chamber (120)    Dissipation devices (122-124)    Fuel cell (150)
NOVELTY - 1,5-Diketone is obtained by reacting an aromatic compound with glutaric acid (in which some hydrogen atoms of methylene group are optionally substituted by group not involved in reaction) or dihydro-2H-pyran-2,6(3H)-dione in the presence of a solid acid catalyst.    USE - Manufacture of 1,5-diketone (claimed) useful as raw material of various chemicals. Uses include but are not limited to pharmaceuticals, agrochemicals, optical materials, and electronic materials.    ADVANTAGE - The method enables easy, safe and efficient manufacture of 1,5-diketone, with easy separation/recovery of solid acid catalyst and without discharge of hazardous wastes.    DETAILED DESCRIPTION - 1,5-Diketone of formula: R1CO-(CH2)3-COR1 is obtained by reacting an aromatic compound of formula: R1H with glutaric acid (in which some hydrogen atoms of methylene group are optionally substituted by group not involved in reaction) or dihydro-2H-pyran-2,6(3H)-dione (in which some hydrogen atoms of methylene group are optionally substituted by group not involved in reaction) in the presence of a solid acid catalyst.R1=monovalent hydrocarbon ring group or organic heteroaryl, with a portion of hydrocarbon ring or heterocyclic hydrogen atoms being optionally substituted by group which is not involved in reaction.    An INDEPENDENT CLAIM is included for 1,5-diketone of formula: R3CO(CH2)3COR4.    R3,R4=2,3-dihydrobenzofuran-5-yl or 1,4-benzodioxan-6-yl, or one is phenyl and the other is 2,3-dihydrobenzofuran-5-yl.
NOVELTY - A biomass feedstock is pre-processed in alcohol and hydrocracked by a catalyst to obtain hydrocarbon.    USE - Manufacture of hydrocarbon used as fuel.    ADVANTAGE - The hydrocarbon is manufactured with high yield.
NOVELTY - The water washing tower has separating tower whose top portion and bottom portion are provided crude fatty acid methyl ester inlet and washing water outlet respectively. The top or bottom of crude fatty acid methyl ester outlet and washing water inlet are provided with separation tower oil-water separating section. The separating tower is provided with baffle plate and filler. The outside of separating tower is provided with heat exchanging jacket or external heater.    USE - Water washing tower for producing biological diesel.    ADVANTAGE - The water-washing tower produces biological diesel continuously, so that automation level of production is improved. The tower is simple in structure. The washing time can be shortened, so that disease caused by water washing acid regurgitation can be prevented. The consumption of water can be reduced, so that environment can be protected effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of water washing tower.
NOVELTY - The esterification reactor has gas phase methanol esterification reactor main portion which is provided methanol inlet and methanol outlet respectively. The outlet is connected with methanol moisture separator. The methanol moisture separator is provided with gas methanol outlet. The vaporized methanol outlet of branch is connected to main portion inlet.    USE - Esterification reactor for producing biological diesel.    ADVANTAGE - The methanol is recycled into the reactor so as to reduce temperature-sensing and color-changing process, so that time for producing biological diesel is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of esterification reactor.
NOVELTY - Bio-diesel oil preparing tank comprises a tank body, in which its upper part is provided with a feeding port, and a mixing kettle is provided with a multiple connection with a preparing tank in the additive tank. The middle part of tank is provided with stirrer. The bottom part of tank body is provided with a high pressure mixer, and a pollution discharge opening.    USE - Used as a bio-diesel oil preparing tank.    ADVANTAGE - The tank is simple in structure, and easy to operate; utilizes stirrer and high pressure mixer for uniform mixing of the raw materials; and assures the stability and uniformity of the product.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the bio-diesel oil preparing tank.
NOVELTY - Biomass energy burner comprises combustion chamber provided with feeding port, main air inlet, and open air outlet; and firebox with bottom provided with carbon outlet. The feed port is provided with feeding auger connected with shifting fork rotating coaxially with feed port. The shifting fork rotation is larger than feeding auger.    USE - Biomass energy burner.    ADVANTAGE - The biomass energy burner inhibits smoke and provides low fuel accumulation.    DETAILED DESCRIPTION - The shifting fork is connected with one end of feeding auger and with at least two deflector rods at other end. The burner is also provided with carbon discharging auger provided with spiral blade having thread pitch. The outer side of combustion chamber surrounds layer of distribution chamber. The combustion chamber is provided with air distribution plate. The bottom of firebox with distribution chamber is provided with air outlet holes through air distribution board. The air distribution plate is uniformly distributed with bumps, such that side hole of bump forms wind distributing holes. The air distribution hole opening direction is 45-135 degrees with respect to port opening direction. The air outlet of combustion chamber is connected with annular wall. The outer chamber of burner further comprises fan.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of biomass energy burner.
NOVELTY - An organic substrate comprises (pts. wt.) earthworm feces (25-45), biomass carbon (10-30), biomass extract (5-15), rice bran cake (10-20), vermiculite powder (9-11), and perlite (4-6).    USE - Organic substrate.    ADVANTAGE - The organic substrate has high seedling germination rate and realizes efficient waste utilization.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of organic substrate by curing all raw materials in greenhouse for 9-11 days, adding bio-organic fertilizer fermentation agent (1.5-2.5, preferably 2 kg/ton raw materials), uniformly mixing, standing, stacking, and fermenting at 55-60 degrees C and 55-65% relative humidity for 20-25 days, while regularly turning and supplying oxygen.
NOVELTY - An indoor organic waste anaerobic digestion renewable energy device comprises hydrolysis acid production tank (1); gas production tank (2); and gas storage device (3). The acid production tank has feeding port (6) and slag outlet (113). The gas production tank has sealing structures. The middle upper part of side wall of acid production tank adjacent to the gas production tank is provided with acid liquid pump (16), normally-closed outlet (164) with gas production tank, and fixed pressure one-way gas guide pipe (20) at the top of the gas production tank connected with storage device.    USE - Indoor organic waste anaerobic digestion renewable energy device for urban and rural room.    ADVANTAGE - The indoor organic waste anaerobic digestion renewable energy device has simple and compact structure, convenient operation and use, high gas production efficiency, and does not need other auxiliary energy. It can directly process the organic waste, not only ensures the organic anaerobic digestion efficiency, but also saves a large amount of water resource use of discharging, avoids the discharging process to the environment, and generates energy for life.    DESCRIPTION OF DRAWING(S) - The drawing is a perspective view of an indoor organic waste anaerobic digestion renewable energy device.    Acid production tank (1)    Gas production tank (2)    Storage device (3)    Feeding port (6)    Liquid pump (16)    Guide pipe (20)    Slag outlet (113, 164)
NOVELTY - A feed kitchen waste processing device comprises crushing system, heating system, storage system, and dehydration system. The crushing system is provided with storage space, at least a breaker, and sludge pump. Bones and hard object are crushed, and introduced into the heating system. The heating system is provided on crushing downstream, with storage space, and is provided with heater. The storage system is provided on heating system downstream. The timing controller is provided on proper position.    USE - Feed kitchen waste processing device.    ADVANTAGE - The device can conveniently and quickly processed kitchen waste to feed or fertilizer.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating a feed kitchen waste processing device.
NOVELTY - A composting device comprises main body, sensor and driver. The main body is cone structure, where cone part is hollow. Inside sensor is connected with corresponding line from top lifting. Outer controller is connected with driving device and external power supply connected with main body.    USE - Composting device.    ADVANTAGE - The device can be taken out from the stack, to clean and maintain.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for composting system which comprises two or more of the compost device. Two or more composting tail are connected in parallel, each sensor is connected with centralized by same corresponding controlled by the controller through circuit.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating a composting device.
NOVELTY - Biological fuel multifunctional reactor comprises a mixing container and a set of pumps. Each pump pumps a fuel oil, water and an emulsifier into the mixing container in a tangential direction, and forms eddy current to mix the materials in the mixing container.    USE - Used as a biological fuel multifunctional reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the biological fuel multifunctional reactor.
NOVELTY - Removing impurities from a biomass derived biocrude, comprises: (a) providing a biomass derived biocrude comprising at least one metal impurity and at least one high molecular weigh component; (b) mixing the biomass derived biocrude with a first solvent and a second solvent to form a mixture; (c) subjecting the mixture to a separation device to form a liquid phase and a solid phase; and (d) recovering the liquid phase.    USE - The process is useful: for removing impurities from a biomass derived biocrude; for upgrading the biomass derived biocrude to the fuel range hydrocarbon; and for converting the biomass to the fuel range hydrocarbon (all claimed).    ADVANTAGE - The process: prevents potential catalyst poisoning and catalyst bed plugging in biocrude-to-transportation fuel upgrading process; is cost-effective; utilizes the solvents which can be easily removed and recycled; and can be carried out in any suitable reaction zone which enables intimate contact of the treated biomass derived biocrude with the catalyst and control of the operating conditions e.g. pressure and temperature.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) upgrading the biomass derived biocrude to a fuel range hydrocarbon, comprising (a)-(d) as above per se and reacting the liquid phase with a catalyst under a condition to produce a reaction product containing fuel range hydrocarbon; and    (2) converting the biomass to the fuel range hydrocarbon comprising either (a)-(d) as above per se and pyrolyzing the biomass to produce a biomass derived biocrude or pyrolyzing the biomass to produce biomass derived biocrude, (b)-(d) as above per se and reacting the liquid phase with a catalyst under a condition to produce a reaction product containing fuel range hydrocarbon.
NOVELTY - The method involves spraying high-temperature smoke into a gasification chamber, and heating the smoke in the gasification chamber gradually. Oxygen is added into the smoke to make volume concentration of the oxygen to 7-10 percent when the gasification chamber is heated up to 1000-1300 degrees Celsius. Biomass powder is fed into the gasification chamber by a feeding opening and mixed with the smoke to gasify the smoke in the gasification chamber to produce synthetic gas. The synthetic gas is discharged from a synthetic gas outlet of a gasification furnace.    USE - Method for fusing and gasifying biomass at high temperature.    ADVANTAGE - The method enables producing fuel gas with high thermal value, and reducing tar content in the fuel gas. The method enables realizing high carbon conversion rate, and improving gasification efficiency to the biomass.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for implementing a biomass fusing and gasifying method at high temperature, comprising a high-temperature gasifying agent generator.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a device for implementing a biomass fusing and gasifying method.
NOVELTY - The furnace has a furnace body provided with a thin upper part and a thick lower part. An ash leaking disk is arranged at a bottom part of a sealing cover. The ash leaking disk is provided with a stirring rod. A gas outlet pipe is assembled at the upper part of the furnace body. A water jacket is provided at a bottom part of a water inlet pipe. A water outlet pipe is provided in an upper part of the water jacket. The gas outlet pipe is connected with a filter that is connected with a compressor. The stirring rod is driven by a motor. The ash leaking disk is formed with a concave disk.    USE - Straw gas furnace.    ADVANTAGE - The furnace ensures negative pressure formed by shape of the furnace body and the design of a bottom part of the compressor. The furnace has better performance for combustion of fuel, and can reduce generation of waste gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a straw gas furnace.
NOVELTY - The device has a reaction tank that is provided with a stirrer. The stirring blades are distributed in the stirrer. A chip is arranged on the mixing arm. The reaction tank is provided with the steam inlet and the steam outlet. The reaction tank is provided with a coil pipe. The coil pipe is connected with the steam inlet and the steam outlet. The reaction tank is provided with a catalyst inlet, a catalyst outlet, an oil inlet and an oil outlet. The steam outlet is provided with a drain valve. The catalyst inlet is provided with a flow meter.    USE - Bio-diesel esterification reaction device.    ADVANTAGE - The steam can be circulated through the coil pipe in the reaction tank, since the coil pipe is connected with the steam inlet and the steam outlet. The esterification reaction can be promoted, since the stirring of the reaction is performed. Hence the completion of the reaction can be ensured.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the bio-diesel esterification reaction device.
NOVELTY - The apparatus has a solid-thermal medium circulation unit (D) which circulates solid thermal medium between the thermal decomposition space (P) and thermal-medium heating space (H). A material supply unit (I) supplies a raw material (X) to the thermal decomposition space. A thermal decomposition unit heats a raw material in the thermal decomposition space and generates a combustible gas and a char. A mixing prevention unit prevents mixing of the oxygen-containing gas with combustible gas. A combustible-gas and char discharge unit discharges the combustible gas and char.    USE - Thermal decomposition apparatus for manufacturing useful substance from untapped natural resources containing organic substance such as biomass and plastics.    ADVANTAGE - As the mixing prevention unit is provided to prevent mixing of the oxygen-containing gas to the thermal decomposition space, the mixture of the combustible gas and oxygen-containing gas is prevented, and the operation is easy.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the thermal decomposition apparatus.    Solid thermal-medium circulation unit (D)    Thermal-medium heating space (H)    Thermal decomposition apparatus (HK)    Thermal decomposition space (P)    Raw material (X)
NOVELTY - The gasifier (1) has a burner in a furnace wall and the burner (15) ejects a carbon containing solid raw material and an oxidizing agent in the furnace. A detector (29) detects the pressure loss of the ejection fluid. A judging unit (8) determines the slag adhered to the fluid jet nozzle of the burner, based on the detected value. A removal unit removes the slag and carries out the partial combustion and gasifies the carbon by the oxidizing agent. The judging unit compares and determines the detected value and the judgment value.    USE - Gasifier for preventing obstruction of burner.    ADVANTAGE - The gasifier determines the precision of slag and the slag adherence is improved and obstruction of the burner is prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the gasifier. (Drawing includes non-English language text)    Gasifier (1)    Slag cooling unit (7)    Judging unit (8)    Burner (15)    Detector (29)
NOVELTY - A fuel is castor oil obtained by washing, drying and heating seeds of Ricinus communis (castor oil plant) by chemical reaction, and pressing oil.    USE - Fuel for combustion machine and transport device.    ADVANTAGE - The fuel having high efficiency is manufactured economically with improved yield.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) Method for using the oil; and    (2) computer system for using the oil.
NOVELTY - The system has a gasification device converting combustible material into product gas and rest fraction. An eductor is connected with a discharge of the gasification device for pumping a part of the rest fraction of the combustible material out of the gasification device. The eductor is connected with another discharge for leading of product gas through the eductor as a propellant for the purpose of pumping the rest fraction out of the gasification device. The product gas is selected from flue gas, methane, water vapor, nitrogen, carbon monoxide, hydrogen, and/or carbon dioxide.    USE - System for treating and transporting biomass such as coal, coal products and charred material in thermal cracking installations and pyrolysis installations.    ADVANTAGE - The drive gas is blown into the eductor placed in the middle part of the pneumatic system to create flow of the drive gas in one direction so as to create lower pressure in the pipe section before the joint when the eductor is placed, so that the lower pressure creates flow of gas created by a pyrolysis or gasification process to carry particles from one reactor to another reactor, thus avoiding combustion of the gas or particles.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for treating combustible material.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a system for treating and transporting biomass.
NOVELTY - The device has a separation unit for separating hydrolyzed organic material product flow originating from a hydrolysis compartment (1) in solid fraction and liquid fraction. An anaerobic digestion compartment (2) digests the product of solid to gaseous fraction. Another anaerobic digestion compartment (3) digests the product of liquid fraction. Another separation unit separates the product flow originating from the latter anaerobic compartment in the liquid fraction and biogas. The separation units are adapted for retaining micro-organisms present in the anaerobic compartments.    USE - Device for anaerobic digestion of organic material e.g. animal fat and garden waste, to produce biogas by using micro-organisms e.g. microbes.    ADVANTAGE - The device performs anaerobic digestion for breaking organic material such as animal fat and garden waste, into smaller molecules such as instance methane and carbon dioxide, in number of different stages without any source of air and oxygen. The device reduces time of conversion, and reduces size and cost of separation and preprocessing tanks.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for anaerobic digestion of organic material to produce biogas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a device for anaerobic digestion of organic material to biogas.    Hydrolysis compartment (1)    Solid fraction anaerobic digestion compartment (2)    Liquid fraction anaerobic digestion compartment (3)    Membranes (5, 6)
NOVELTY - An anode (DD) and a cathode (CC) are arranged in an electrolyte phase. While water is supplied, light (BB) is irradiated to the anode zone, water is decomposed, and proton, electron and oxygen gas are formed. Nitrogen gas (AA) is supplied to the cathode zone, electron produced in the anode zone is transferred to the cathode zone through a lead wire, azide ion is formed in the cathode zone, and ammonia is synthesized by reaction with proton moved inside the electrolyte phase to the cathode zone side from the anode zone, and azide ion.    USE - Synthesis of ammonia.    ADVANTAGE - The method enables synthesis of ammonia without using hydrogen sources, such as fossil fuels e.g. natural gas, which avoids increase in ammonia synthesis cost due to rising fossil-fuel prices and also avoids burdening the environment with carbon-dioxide emission. The method is carried out at normal temperatures and pressures and thus can be carried out by a small-scale facility which uses little energy, making the method highly economical.    DETAILED DESCRIPTION - An anode and a cathode are arranged in an electrolyte phase at preset intervals. While water is supplied, light is irradiated to the anode zone, water is decomposed by light absorption reaction, and proton, electron and oxygen gas are formed. Nitrogen gas is supplied to the cathode zone, electron produced in the anode zone is transferred to the cathode zone through a lead wire, azide ion (N3-) is formed in the cathode zone, and ammonia is synthesized by reaction with proton moved inside the electrolyte phase to the cathode zone side from the anode zone, and N3-.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow sheet of the apparatus used for synthesis of ammonia. (Drawing includes non-English language text)    Nitrogen gas (AA)    Light (BB)    Cathode (CC)    Anode (DD)
NOVELTY - Method (M1) for producing Euglena containing wax ester, involves culturing microalga Euglena aerobically by photosynthesis using carbon dioxide as carbon source, culturing the microalga Euglena under nitrogen-starved conditions to increase the amount of accumulated paramylon per cell, and leaving the microalga Euglena under anaerobic conditions for producing euglena containing wax ester.    USE - The method is useful for producing wax ester with high content of Euglena which is used as raw material for biofuel, and biomass feedstock.    ADVANTAGE - The method produces wax ester with high content of Euglena cost-effectively with reduced energy in large amounts. The biomass feedstock has high content of fat and oil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method (M2) for manufacturing wax ester, which involves using the Euglena containing wax ester, extracting oil-component using organic solvent to obtain extract, concentrating the obtained extract to obtain wax component, separating wax ester from the wax component using column chromatography, and performing purification for the obtained product.
NOVELTY - Isolated microbial consortia comprises a first-bite microbial consortium that converts a starting hydrocarbon comprising a complex hydrocarbon into two or more first-bite metabolic products, and a downstream microbial consortium that converts a starting hydrocarbon metabolic product into a downstream metabolic product, where at least one of the first-bite microbial consortium and downstream microbial consortium comprises one or more species of Desulfuromonas, Fusibacter and Acetobacterium.    USE - The isolated microbial consortia is useful for biogenic methane production (claimed).    ADVANTAGE - The isolated microbial consortia provides products with greater percentage of hydrogen than the starting hydrocarbon, and enhances the methane production rate.    DETAILED DESCRIPTION - Isolated microbial consortia comprises: either a first-bite microbial consortium that converts a starting hydrocarbon comprising a complex hydrocarbon into two or more first-bite metabolic products, and a downstream microbial consortium that converts a starting hydrocarbon metabolic product into a downstream metabolic product, where the downstream metabolic product has a greater mol.% hydrogen than the starting hydrocarbon; or a first microbial consortium that converts a starting hydrocarbon into one or more intermediate compounds, a second microbial consortium that converts at least one type of the intermediate compounds into carbon dioxide and hydrogen or acetate, and a third microbial consortium that converts the carbon dioxide and hydrogen or acetate into methane and water, where at least one of the first-bite microbial consortium, downstream microbial consortium, and first, second and third microbial consortiums comprises one or more species of Desulfuromonas, Fusibacter and Acetobacterium.
NOVELTY - Reducing water in a biomass-derived pyrolysis oil, comprises: (204) condensing pyrolysis gases comprising condensable pyrolysis gases and non-condensable gases to separate the condensable pyrolysis gases from the non-condensable gases, where the non-condensable gases has a water content; (206) drying the non-condensable pyrolysis gases to reduce the water content of the non-condensable gases to form reduced-water non-condensable pyrolysis gases; and (208) providing the reduced-water non-condensable pyrolysis gases to a pyrolysis reactor for forming the biomass-derived pyrolysis oil.    USE - The process is useful for reducing water in a biomass-derived pyrolysis oil, or for preparing low water biomass-derived pyrolysis oil (claimed), which is useful as fuel for certain boiler and furnace applications.    ADVANTAGE - The process provides the low water biomass-derived pyrolysis oil having water content of 2-30%, and having substantially increased storage stability.    DESCRIPTION OF DRAWING(S) - The figure shows a flow diagram of the process for reducing water content of biomass-derived pyrolysis oil.    Pyrolyzing biomass to obtain pyrolysis gases (202)    Condensing pyrolysis gases to separate the condensable pyrolysis gases from the non-condensable gases (204)    Drying the non-condensable pyrolysis gases to form reduced-water non-condensable pyrolysis gases (206)    Providing the reduced-water non-condensable pyrolysis gases to a pyrolysis reactor (208)    Subjecting the non-condensable pyrolysis gases to pre-treatment (210)
NOVELTY - A reformer (A1) comprises a catalyst bed having an inlet with a cross section, configured of other than monolithic open cell foam, catalyzed to process fuel mixtures to produce a hydrogen-containing reformate gas; and a monolithic, open cell foam mixing and spreading section connected to receive a flow of components of a mixture (i) to be mixed, (ii) to be spread across the cross section, and (iii) to be reformed in the catalyst bed, the catalyst bed connected to receive outflow of the mixing and spreading section.    USE - For reforming hydrocarbon fuel or alcohol in reformer having a catalyst supported by unified foil or ceramic honeycomb (claimed).    ADVANTAGE - The reformer is an autothermal reformer having very short mixing and distributing section. The monolithic, open cell foam core mixes the incoming steam and/or air and fuel gases together very effectively, i.e. achieving complete mixture in a very short longitudinal distance along the path of mass flow of the gases, the monolithic; and distributes the mixture laterally, over a very large cross sectional area within a short longitudinal distance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for reforming hydrocarbon fuel or alcohol involving reforming a fuel to provide hydrogen-rich reformate gas in a reformer having a catalyst supported by other than open cell foam, and having an inlet with a cross section; and mixing and spreading, across the entire cross section of the inlet, components of fuel, steam and air or fuel and air in a section of monolithic, open cell foam.
NOVELTY - Bio-distillate composition having a total oxygen content of less than 15 wt.%, where at least 75 wt.% of the bio-distillate composition has a boiling point of 180-380 degrees C, comprises at least 50 wt.% of oxygen-free hydrocarbons.    USE - Used as bio-distillate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a renewable distillate composition comprising a petroleum-derived-distillate-range stream in an amount of 5-99 wt.%, a bio-distillate fraction in an amount of at least 0.5 wt.%, and a stabilizing additive having surfactant properties in an amount of 0.5-25 wt.%.
NOVELTY - Converting lignocellulosic biomass into monosaccharides comprises: (a) heating the biomass in a medium comprising at least one inorganic salt hydrate, with at least one metal hydrated salt or non hydrated salt, in the presence or absence of an organic solvent; (b) separating the solid fraction from the step (a); and (c) enzymatically hydrolyzing the solid fraction.    USE - The process is useful for converting lignocellulosic biomass into monosaccharides.    ADVANTAGE - The process uses inexpensive reagents that can be recycled, thus the process is cost effective. The process achieves high yields or significant gain in productivity.    DETAILED DESCRIPTION - Converting lignocellulosic biomass into monosaccharides comprises: (a) firing the biomass in a medium comprising at least one inorganic salt hydrate of formula (MXn-n1H2O) (I) with at least one metal hydrated salt or non hydrated salt, of formula (M1aY1m-m1H2O) (II), in the presence or absence of an organic solvent; (b) separating the solid fraction from the step (a); and (c) enzymatically hydrolyzing the solid fraction.    X, Y1 = an anion;    M = Groups 1 and 2 metal of Periodic Table;    n = 1 or 2;    n1 = 0.5-6;    M1a = metal of Groups 3-13 of the periodic table;    m = 1-6; and    m1 = 0-6.
NOVELTY - Converting lignocellulosic biomass into monosaccharides comprises: (a) heating biomass at 120-250 degrees C in the presence or absence of an organic solvent, in a medium comprising one or more hydrated inorganic salts; (b) separating the solid fraction from the step (a); and (c) enzymatically hydrolyzing the solid fraction.    USE - The process is useful for converting lignocellulosic biomass into monosaccharides.    ADVANTAGE - The process uses inexpensive reagents that can be recycled, thus the process is cost effective. The process achieves high yields or significant gain in productivity.    DETAILED DESCRIPTION - Converting lignocellulosic biomass into monosaccharides comprises: (a) heating biomass at 120-250 degrees C in the presence or absence of an organic solvent, in a medium comprising one or more hydrated inorganic salts of formula (MXn-n1H2O); (b) separating the solid fraction from the step (a); and (c) enzymatically hydrolyzing the solid fraction.    X = an anion;    M = Groups 1 and 2 metal of periodic table;    n = 1 or 2; and    n1 = 0.5-6.
NOVELTY - Synthesis of isothiocyanate (I) and their derivative, comprises reaction of amine compound (II) in the presence of carbon disulfide and di-tert-butyl dicarbonate for the formation of the corresponding isothiocyanate.    USE - (I) is useful: as depigmenting agent or for the treatment of hyperpigmentation; as an inducer of the phase II enzyme, as an inhibitor or moderator of phase I enzymes in anti-cancer treatment, in skin protection against the effects of pollution; and for the treatment of baldness, for skin protection against UV radiation and other effects e.g. in phototherapy, radiation therapy, and sun exposure, for the treatment of erythema, DNA damage, repair, signaling and cancerization of the skin for the treatment of lucite, inflammation, preferably atopic dermatitis (all claimed). No biological data given.    ADVANTAGE - The process provides (I) with high yield. (I) is stable, eco-friendly, non toxic and inexpensive.    DETAILED DESCRIPTION - Synthesis of isothiocyanate of formula (SCN-R1-R4-R2) (I) and their derivative, comprises reaction of amine compound of formula (NH2-R1-R4-R2) (II) in the presence of carbon disulfide and di-tert-butyl dicarbonate for the formation of the corresponding isothiocyanate.    R1, R2 = alkyl, aryl or alkylaryl; and    R4 = carbonyl, sulfinyl, sulfonyl, or sulfide.    An INDEPENDENT CLAIM is included for a synthetic and isolated amine compound of formula (R7-R1-R4-R2) (III) obtained by the process.    R7 = amino, isothiocyanato, amino group of formula (-NH-C(=S)R1a);    R1a = alcoholate (-DR2a), thiolate (SR2a), or amino (-NR1aR3a); and    R1a, R2a, R3a = not defined.
NOVELTY - Device comprises (i) fermenter (106), (ii) solid state fermenter (103), (iii) solar based distillation unit (122), (iv) biogas digester (113), and (v) floating platform (130).    USE - The device is useful for producing alcohol, biofuel, preferably methane and other compounds.    ADVANTAGE - The device produces useful compounds cost-effectively on sea in large scale from bulky organic matter made with low carbon footprint, and is environmentally-friendly.    DETAILED DESCRIPTION - Device comprises (i) fermenter (106) made of flexible plastic film as separator barrier between sea water and media, and held by floats near sea surface, coupled to a open and closed type inlet channel (100) made of flexible plastic film to convey media and fresh water with closed type channel converted into continuous fermentation process channel, (ii) solid state fermenter (103) made of flexible plastic film for pretreatment of media, (iii) solar based distillation unit (122) with vacuum support for purifying product by vacuum pump operated by wave and tidal energy, (iv) biogas digester (113) made of flexible plastic film as separator between sea water and to-be-digested organic waste matter to generate methane, and (v) floating platform (130) with engine (135), pumps (131), sterilization unit (133), centrifuge (134) and microprocessor for control.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of device.    Open and closed type inlet channel (100)    Solid state fermenter (103)    Fermenter (106)    Biogas digester (113)    Distillation unit (122)    Floating platform (130)    Pumps (131)    Sterilization unit (133)    Centrifuge (134)    Engine (135)
NOVELTY - The apparatus (10) has a shelf suspension prevention unit (20) that stirs biomass within the filling moving bed (P), and includes a shaft element (21) which reciprocatingly moves a horizontal component from the inner wall of the carbonization furnace (11). The stirring element (22) is provided in the front-end of the shaft element, and is extended along the height direction of carbonization furnace. The biomass is stirred without preventing the movement in the filling moving bed along downward direction of the biomass.    USE - Biomass carbonization apparatus.    ADVANTAGE - The adhering of biomass and carbonized materials can be crushed by shelf suspension prevention unit. The yield of carbonized material can be improved. The stirring effect of the stirring element can be improved. The shelf suspension can be prevented. The heat transfer rate from hot gas to biomass can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the biomass carbonization apparatus. (Drawing includes non-English language text)    Biomass carbonization apparatus (10)    Carbonization furnace (11)    Shelf suspension prevention unit (20)    Shaft element (21)    Stirring element (22)    Filling moving bed (P)
NOVELTY - Preparing 5-amino-3-cyano-1-(2,6-dichloro-4-trifluoromethylphenyl)-4-trifluoromethylsulfinyl-pyrazole (I), fipronil, involves mixing 5-amino-3-cyano-1-(2,6-dichloro-4-trifluoromethylphenyl)-4-trifluoromethylthiopyrazole with dichloroacetic acid and hydrogen peroxide in the presence of a strong acid; quenching the reaction mixture; isolating the compound (I); and optionally purifying the obtained compound.    USE - For preparing 5-amino-3-cyano-1-(2,6-dichloro-4-trifluoromethylphenyl)-4-trifluoromethylsulfinyl-pyrazole, fipronil (claimed) useful as insecticide used to control ants, beetles, cockroaches, fleas, ticks, termites, mole crickets, thrips, rootworms, weevils, and other insects; and use in pesticide products such as granular products for grass, gel baits, spot-on pet care products, liquid termite control products, and products for agriculture.    ADVANTAGE - The process prepares compound with purity of at least 95%. The process is suitable for industrial use, simple, low-cost, highly efficient and environmentally friendly.
NOVELTY - A composition comprises 2-chloro-3,3,3-trifluoropropene; and a component selected from E-1-chloro-3,3,3-trifluoropropene and 1,1,1,2,3-pentafluoropropane, where component is present in an amount to form an azeotrope-like or azeotropic combination with the 2-chloro-3,3,3-trifluoropropene.    USE - As a solvents, heat transfer media, dielectrics, blowing agents for preparing thermoplastic or thermoset foam, refrigerants for producing refrigeration in the vicinity of the body to be cooled; as propellants for preparing aerosol product, fire extinguishing or suppression agents for extinguishing or suppressing a fire (claimed), cleaning agents, power cycle working fluids, polymerization media, particulate removal fluids, carrier fluids, buffing abrasive agents, and displacement drying agents.    ADVANTAGE - The composition has low ozone depleting potentials (ODPs) and low global warming potentials (GWPs).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparing a thermoplastic or thermoset foam involving using the azeotrope-like or azeotropic composition as a blowing agent;    (2) producing refrigeration involving condensing the azeotrope-like or azeotropic composition and thereafter evaporating the composition in the vicinity of the body to be cooled;    (3) process involving using the azeotrope-like or azeotropic composition as solvent, heat transfer media, and dielectrics;    (4) producing an aerosol product involving using the azeotrope-like or azeotropic composition as a propellant; and    (5) process for extinguishing or suppressing a fire involving using the azeotrope-like or azeotropic composition as a fire extinguishing or suppression agent.
NOVELTY - Increasing conversion of glucans, comprises incubating lignocellulosic biomass with an extract, where the extract is obtained from plant biomass.    USE - The method is useful for: increasing conversion of glucans; increasing yield of fermentation product from a fermentative organism; starch hydrolysis; bleaching cellulosic material and reducing biomass recalcitrance of lignocellulosic biomass (all claimed).    ADVANTAGE - The method improves silage quality or pretreatment efficiency and increases starch hydrolysis.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) increasing yield of fermentation product from a fermentative organism, comprising growing a fermentative organism in a medium comprising the extract obtained from plant biomass;    (2) a method of starch hydrolysis comprising incubating starch with the extract obtained from plant biomass;    (3) bleaching cellulosic material comprising incubating the cellulosic material with the extract obtained from plant biomass; and    (4) reducing biomass recalcitrance of lignocellulosic biomass, comprising hydrating and pressing the lignocellulosic biomass.    DESCRIPTION OF DRAWING(S) - The figure depicts a process flow diagram illustrating extraction of soluble components from biomass, pretreatment and enzyme hydrolysis.
NOVELTY - Shaped foam agent comprises (a) at least an indole and/or indoline derivative (I) as a color-forming component in the form of a dye precursor of a natural analogue dye and/or their salts with an organic or inorganic acid, (b) at least one alkalinizing agent, and (c) at least one blowing agent, in a carrier at an alkaline pH of 8-10.5. The agent comprises no additional oxidizing agent for the color-forming components.    USE - The agent is useful for color intensification of atmospheric oxygen induced dyeing of keratin fibers, preferably human hair (claimed).    ADVANTAGE - The agent: can be evenly distributed on the application area; and exhibits an increased contact area of the agent with its environment and good dyeing effect.    DETAILED DESCRIPTION - Shaped foam agent comprises (a) a natural analogue dye of at least an indole and/or indoline derivative of formula (I) as a color-forming component in the form of a dye precursor and/or their salts with an organic or inorganic acid, (b) at least one alkalinizing agent, and (c) at least one blowing agent, in a in a carrier at an alkaline pH of 8-10.5. The agent comprises no additional oxidizing agent for the color-forming components.    R1 = H, 1-4C alkyl or 1-4C hydroxyalkyl; either    V1 = CHR3; and    W1 = CHR 2, so that bond between V1 and W1 is single bond; or    V1 = CR3; and    W1 = CR2, so that bond between V1 and W1 is double bond;    R2 = H or -COOH-, where -COOH- group is present as salt with cation;    R3 = H or 1-4C alkyl;    R4, R5 = H, 1-4C alkyl group or -CO-R6; and    R6 = 1-4C alkyl.
NOVELTY - Preparing saturated polyfarnesene involves polymerizing farnesene in the presence of catalyst to form polyfarnesene; and hydrogenating at least a portion of the double bonds in the polyfarnesene in the presence of hydrogenation reagent.    USE - For preparing saturated polyfarnesene (claimed).    ADVANTAGE - The process provides environmentally friendly and/or renewable saturated polyfarnesene polymer e.g. polymer is derived from isoprenoid compound that is obtained from natural sources. The saturated polyfarnesene has unique physical, chemical and biological properties.
NOVELTY - The compost comprises a mixture of biomass and glycerol in the form of pellets and briquettes. The biomass is selected form one or multiple sources such as oilseeds oil, agro-industrial waste, sawdust, municipal waste, coconut shell, general plants parts, organic material like bran, gum and sludge.    USE - Compost.    ADVANTAGE - The compost has high calorific value and can be manufactured in an eco-friendly manner by using waste from biodiesel production such as pie and gum.
NOVELTY - Composition comprises horse manure (30-45), dried sawdust (30-45), hue paper (0-5), charcoal dust (0-5) and viscosity regulator (0-10).    USE - The composition is useful as solid fuel, preferably coal and petroleum.    ADVANTAGE - The composition utilizes waste resource and hence is cost-effective, and is highly efficient.
NOVELTY - The method involves coating metal paste layer (20) in a metal plate (10). The end cell (30) is positioned in the upper side of metal paste layer. The space (21) in metal paste layer among pipe furnace (11) and end cell (30) is sintered with high temperature sintering process.    USE - Method for manufacturing fuel cell.    ADVANTAGE - The fuel supply efficiency is improved efficiently by removing the element obstructing the fuel supply between end cell and metal plate. The manufacturing cost of fuel cell is reduced effectively while simplifying the manufacturing process of fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the metal paste supported fuel cell.    Metal plate (10)    Pipe furnace (11)    Metal paste layer (20)    Space (21)    End cell (30)
NOVELTY - Product comprising a fuel cell component, comprises a substrate (12) including a hydrocarbon material, a porous surface layer (18) over the substrate, where the porous surface layer includes silicon and oxygen, and a hydrocarbon moiety attached to at least one of the silicon or oxygen, where at least a portion of the porous surface layer is hydrophobic.    USE - The product/ composite bipolar plate is useful for conducting electricity generated by the fuel cells from one cell to the next cell and out of the stack.    ADVANTAGE - The product/ composite bipolar plate utilizes a super-hydrophobic porous layer which improves channel water transport in the flow channel of the fuel cell, thus reducing the inlet humidification and increasing the efficiency of the fuel cell.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a composite bipolar plate for a fuel cell, comprising the substrate including the hydrocarbon material and the porous surface layer over the substrate, where the porous surface layer includes silicon oxide of formula (SiOx) (I), where x is greater than 0.1 and less than 2, and the substrate includes a base and a first layer over the base, where the first layer includes the hydrocarbon material, and the base is a metal.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of the product including making a super-hydrophobic fuel cell.    Substrate (12)    Lands (14)    Channel (16)    Porous surface layer (18)    Diffusion barrier material (100)
NOVELTY - Woody biomass is heated, dried (2), pulverized, and molded (10) with coal to obtain molded product. The molded product is inserted into coke oven (13) and dry-distilled to obtain coke. The coke is inserted into a blast furnace (14) and blast furnace is operated.    USE - Operation of blast furnace during manufacture of steel.    ADVANTAGE - The operation of blast furnace is enabled without fall of reduction material ratio and emission of carbon dioxide, using reduced amount of woody biomass.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of coke.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view illustrating operation of blast furnace.    Biomass chip tank (1)    Drying (2)    Cooler (3)    Coal (7)    Molding (10)    Coke oven (13)    Blast furnace (14)
NOVELTY - Carbonizing biomass in a reaction chamber using vapor to provide the required temperature and pressure values, is claimed. The reaction chamber is operated with at least two fluidically-connected vapor storage units. The vapor is conducted into the reaction chamber from at least one storage unit or at least one storage unit of the reaction chamber, depending on the process phase.    USE - The method is useful for carbonizing biomass.    ADVANTAGE - The method is economical and environmental friendly, avoids the use of chemical additives (catalysts), saves energy, and reduces the wastewater production amount.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for carrying out the above mentioned method, where Ruth's storage units are used as vapor storage units.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the device for carrying out the carbonization of biomass.
NOVELTY - The machine has an air chamber side wall provided with a purifying gas outlet that is connected to a smoke discharge port by a four way pipe. An upper vertical part is connected with an odorizing secondary purification chamber. A lower connecting box is connected with an air inlet of a fuel gas generator. An air outlet is provided with a tertiary air outlet and connected with the odorizing secondary purification chamber. A fuel gas dividing room bottom of the odorizing secondary purification chamber is provided with multiple dividing valves for dividing gas into a gas stove through a gas pipe.    USE - Straw gas heat source machine.    ADVANTAGE - The machine continuously burns gas heat production, rapidly releases heat of circulating water, and saves energy resources. The machine is suitable for production and life, and has high circulating water heating efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial sectional view of a straw gas heat source machine.
NOVELTY - The furnace has a hearth whose bottom part is provided with a raw material pre-heating zone, a raw material pyrolysis area, a reduction area and a high temperature cracking area. A region is equipped with a temperature control device. A gasification furnace unit is connected with a steam inlet main pipe that is divided into parallel vertical branch pipes. A bottom end of each branch pipe is inserted into the hearth of the reduction area and provided with a spraying device.    USE - Steam spray straw gasification furnace.    ADVANTAGE - The furnace utilizes high pressure steam as a gasification agent for oxidization so as to improve a heat value and to have high efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a steam spray straw gasification furnace.
NOVELTY - The purifying device has a case that is fixed with desulfurization bottle. The one end of liquid outlet is provided with desulfurization bottle. The bottle mouth is provided with exhaust valve. The two ends of the upper portion mouths are respectively provided with air inlet and air outlet. The air inlet is connected with one end of joint connected with control valve. The two ends of control valve are connected with air inlet pipe.    USE - Biogas purifying device.    ADVANTAGE - The mounting and dismounting of the biogas purifying device can be made simply and conveniently. The air tightness of the biogas purifying device can be ensured. The safety and reliability of the biogas purifying device can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biogas purifying device.
NOVELTY - The machine has a material inlet that is provided in a liquid separating device. A turning air drying device of liquid separating device is connected with a feeding port. A discharge port is connected with the spiral lifting device and feeding inlet of the particle forming device.    USE - Machine for processing manure particle.    ADVANTAGE - The design, efficiency, combustion performance and operability of the machine for processing manure particle can be improved. The combustion amount of sulfur in the machine for processing manure particle can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the machine for processing manure particle.
NOVELTY - The electrolytic cell (10) has an anode (30) that is located within reaction space between an inlet reservoir (24) and an outlet chamber (26). The cathodes (32) are spaced around the anode. A fluid inlet is communicated with the inlet reservoir. A portal section is between the inlet reservoir and a reaction chamber that is communicated with a gas outlet. The electrolytic fluid (F) is provided within housing space (18) to cover the anode and the cathode. The current is supplied to the anode such that the free oxygen and hydrogen ions are generated.    USE - Electrolytic cell used in internal combustion engine.    ADVANTAGE - The current is supplied to the anode, so that the free oxygen and hydrogen ions are generated from the fuel. Hence the performance of internal combustion engine can be enhanced.    DESCRIPTION OF DRAWING(S) - The drawing shows a longitudinal cross-sectional view of electrolytic cell.    Electrolytic cell (10)    Housing space (18)    Inlet reservoir (24)    Outlet chamber (26)    Anode (30)    Cathodes (32)    Electrolytic fluid (F)
NOVELTY - The generator (14) has a merging chamber discharging a feed stream to include oxidant, recycle gas and hydrocarbon fuel. A recycle pump is connected with the merging chamber, and pressurizes a flow of the recycle gas. The recycle pump discharges pressurized flow into the merging chamber. A reformer is connected with the merging chamber, and reforms the feed stream into reducing gas. A junction part receives a portion of the reducing gas and diverts the portion of the reducing gas to the recycle pump.    USE - Reducing gas generator for use in a fuel cell system.    ADVANTAGE - The junction part diverts the portion of the reducing gas to the recycle pump, thus protecting a fuel cell from being damaged.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for generating reducing gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a fuel cell system.    Fuel cell system (10)    Fuel cell (12)    Reducing gas generator (14)    Electrical load (16)    Electrical power line (18)
NOVELTY - Composition comprises: (a) an extract of blood orange, oranges, bitter orange and/or grapefruit; and (b) an extract of green coffee.    USE - The composition is useful as a foodstuff, dietary supplements, a diet food, over-the-counter medicines or medicines, and for reducing body weight and/or improving endurance and regeneration after doing physical activities (all claimed).    ADVANTAGE - The composition uses renewable raw materials, and avoids complex chemical synthesis steps for producing individual natural products, and thus it reduces associated waste products.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a kit of parts comprising a composition containing the component (a), and a composition containing the component (b), where the compositions are separated from each other.
NOVELTY - The arrangement (1) has a thermoelectric generator (9) arranged at a fuel cell (2) i.e. high temperature fuel cell, for generating electrical energy using heat prevailing in the fuel cell. Housing (4) partly surrounds the fuel cell. The housing comprises an insulating layer (8) that is arranged adjacent to a wall element (7a) at an opposite side of the fuel cell. The thermoelectric generator is partly arranged within the insulating layer. A thermal isolating movement compensating element is arranged between the insulating layer and the thermoelectric generator.    USE - Fuel cell arrangement e.g. high temperature fuel cell arrangement (claimed) such as molten carbonate fuel cell arrangement and solid oxide fuel cell arrangement. Can also be used for low-temperature fuel cell arrangement, proton exchange membrane fuel cell arrangement and polymer electrolyte fuel cell arrangement.    ADVANTAGE - The thermoelectric generator is arranged at the high temperature fuel cell for generating electrical energy using heat prevailing in the fuel cell, thus increasing efficiency of the fuel cell arrangement at low cost. The thermal isolating movement compensating element is arranged between the insulating layer and the thermoelectric generator, thus avoiding a thermal damage of the thermoelectric generator with high temperature at a wall element.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of a fuel cell arrangement.    Fuel cell arrangement (1)    Fuel cell (2)    Housing (4)    Wall element (7a)    Insulating layer (8)    Thermoelectric generator (9)
NOVELTY - Utilization of series of unit for processing hazardous waste e.g. household garbage, electronic waste and steel scrap leftover is claimed.    USE - Utilization of series of unit for processing hazardous waste e.g. household garbage, electronic waste and steel scrap leftover.    ADVANTAGE - The method efficiently utilizes series of unit for processing hazardous waste e.g. household garbage, electronic waste and steel scrap leftover.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic structure of garbage-processing plant.    Garbage trucks discharging into a garbage pit (1)    Elevating conveyor charging into magnetic separator (2)    Wet magnetic separator (3)    Metal carrying conveyors (4,5)    Hand picked glass and ceramic to carrier to disposal place (6)
NOVELTY - The method involves generating biomass thermal cracking biological diesel oil through a quartz reactor (1). The biomass thermal cracking of biomass gas generated by a quartz reactor is collected by biomass. Biodiesel is discharged into a laser generator (6). Inert gas is introduced into the quartz reactor in cooling for 3-5 degrees centigrade. The quartz reactor is provided at a lower end of a side wall of a slag outlet (4) for the biomass decomposing after discharging waste slag.    USE - Method for performing craft flow of biological diesel oil preparation with strong pulse laser.    ADVANTAGE - The method enables simplifying biological diesel oil at the same time, thus effectively improving preparation efficiency and reducing production cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a method for performing craft flow of biological diesel oil preparation with strong pulse laser.    Quartz reactor (1)    Feeding hole (2)    Wall (3)    Slag outlet (4)    Laser generator (6)
NOVELTY - The device has a draught fan (13) connected with an upper part of an air cooling pipe (9). An outlet of a second-stage cooling gas conveying pipe (10) is connected with an upper part of a connecting pipe of a tar filter (11) and a tar reflowing tank (18). An upper part of the tar filter is connected with the draught fan. An outlet of the draught fan is located in a tar sinking tank (14). An upper part of the tar sinking tank is connected with a burning device by a gas conveying pipe (15). A lower part of the tar sinking tank is connected with the tar reflowing tank.    USE - Tar processing, recycling and burning device for a domestic straw gasification furnace.    ADVANTAGE - The device forms a self-closed circulating clean production system, promotes rural environment and develops wider path for creating resource-saving and environment-friendly rural area.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a tar processing, recycling and burning device.    Air cooling pipe (9)    Second-stage cooling gas conveying pipe (10)    Tar filter (11)    Draught fan (13)    Tar sinking tank (14)    Gas conveying pipe (15)    Tar reflowing tank (18)
NOVELTY - Preparing fertilizer for plants comprises providing whey, adding yeast into the whey for aerobic fermentation, and aerobic fermentation of whey for the production of biomass as a fertilizer.    USE - The fertilizers are useful for the fertilization of plants (claimed), also includes improving the nutrient poor soils in biological farming and improving the water and nutrient storage capacity of permeable soils.    ADVANTAGE - The fertilizer ensures a longer availability to soil due to slow dissolution in aqueous solutions, thus prevents the leaching to deeper soil layers and improves the upper soil layers qualitatively sustainable. The fertilizer has a good fertilizing and storage properties.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for the fertilizer for plants prepared by the above method.
NOVELTY - Production of hydroxytyrosol using eugenol as a starting material, involves converting eugenol to 4-(2-hydroxyethyl)-2-methoxyphenol, which is subsequently converted to hydroxytyrosol.    USE - For producing hydroxytyrosol (claimed) used as anti-inflammatory agent, vasodilator, antihypertensive agent, and fungicidal agent and used for preventing thrombocyte aggregation and cognitive functions.    ADVANTAGE - The overall yield of the conversion of eugenol to hydroxytyrosol is at least 60% (preferably at least 80%). The hydroxytyrosol is obtained in an efficient and mild reaction and at a relatively high yield. The starting compound is the natural product eugenol, which is readily available and relatively inexpensive. The reaction only requires a limited number of process steps. In this respect, the oxidation and reduction can be carried out subsequently in the same batch and thus could be considered as one reaction step. The method can be performed with reagents and catalysts which are readily available, inexpensive and relatively innoxious in food applications. The process does not require harsh reaction conditions. The process steps can be carried out at room temperature or lower temperatures. It is not necessary to carry out reaction steps at high temperatures, high pressures or other extreme conditions. The process can be carried out under mild conditions and without or with only low amounts of undesired side products, especially when using ozone as the oxidizing agent. Since the process uses mild chemicals and does not require high energy consumption, the overall process is environmentally friendly. Since the starting compound eugenol is a natural product, the overall process avoids petroleum-derived starting materials and is sustainable.
NOVELTY - The mode involves using cow breeding, and performing fermentation in a marsh gas pool, where a cattle manure is produced into a rotten organic fertilizer. A red lifting spring bud large expansion period, a young fruit expansion period and a big harvesting period is applied to the soil. Nutrient content e.g. milk cow dung, is added to a dirt grape area.    USE - Agriculture milk cow ecological cultivation mode.    ADVANTAGE - The cultivation mode enables reducing the investment and production cost, improving soil physicochemical property or fertility of the soil, improving the economic benefit, and achieving better mouth feel, better quality and excellent nonpollution for the market extracting red grape.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating an agriculture milk cow ecological cultivation mode.
NOVELTY - A garbage carbonization device comprises carbonizing reactor (1), feeding device (2), heating device (3), gas output device (15), and output port of inner reactor discharge device (4) connected to feeding device. Discharging device is connected with output port at the external part of the carbon substance collecting device. Gas output device is connected with inner cavity of the carbide sensor. Output end of gas processing gas output device is provided on external part of the device.    USE - Garbage carbonization device for urban waste (containing biomass waste, without sorting), kitchen garbage medical garbage, sludge, processed livestock excrement, grass, leaf, and root.    ADVANTAGE - The device greatly improves reaction speed of silicon carbide, and can generate combustible gas, oil and carbon.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating a garbage carbonization device.    Carbonizing reactor (1)    Feeding device (2)    Heating device (3)    Inner reactor discharge device (4)    Gas output device (15)
NOVELTY - A biomass carbonization device comprises retorting reactor (1), feeding device (2), heating device (3), gas output device (7), discharging device (4) and gas processing device. The feeding device is connected with feeding port of dry distillation reactor. The discharging device is connected with dry distillation reactor inner cavity, where output port is connected with outside carbon substance collecting device. Gas output device is connected with inner cavity of dry sensor. Gas output device of discharging device is connected with gas processing device.    USE - Biomass carbonization device for household garbage (kitchen garbage), medical waste, and sludge.    ADVANTAGE - The device can transfer biomass into electric energy and carbon, and realizes energy substance circulation and recycling. It greatly improves reaction speed of dry distillation, and generates combustible gas, oil and carbon    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating a biomass carbonization device.    Retorting reactor (1)    Feeding device (2)    Heating device (3)    Discharging device (4)    Gas output device (7)
NOVELTY - Decomposition of polylactic acid involves impregnating an organic material containing polylactic acid with treatment solution containing organic acid salt and/or inorganic acid salt of amine compound.    USE - Decomposition of polylactic acid.    ADVANTAGE - The method efficiently decomposes polylactic acid by biological treatment such as methane fermentation.    DETAILED DESCRIPTION - Decomposition of polylactic acid involves impregnating an organic material containing polylactic acid with treatment solution containing organic acid salt and/or inorganic acid salt of amine compound of formula: R1-N(-R2)-R3.    R1-R3=H or 1-5C alkyl.    INDEPENDENT CLAIMS are included for the following:    (1) processing method of organic substance containing polylactic acid; and    (2) processing system.
NOVELTY - Anti-crust methane tank comprises methane tank body provided with feeding port, discharge port, and methane outlet. The upper part of the methane tank body is an air storage chamber. The lower part of the methane tank body is a fermentation chamber. The discharge port is a water pressure chamber. The methane tank body is provided with a projection protruded out of the inner wall surface for lacerating the scum.    USE - Anti-crust methane tank.    ADVANTAGE - The anti-crust methane tank achieves production efficiency and safety.
NOVELTY - Methane tank comprises methane tank body, which is provided with feeding port, discharge port, and methane outlet. The upper part of the interior of the methane tank body is used as gas storage chamber. The lower part of the interior of the methane tank body is used as fermentation chamber. The bottom of the methane tank body is a bevel. The feeding port corresponds to the higher part of the bevel. The discharge port corresponds to the lower part of the bevel.    USE - Methane tank.    ADVANTAGE - The methane tank provides convenient removal of the residue. The user does not need to enter into the fermentation chamber, avoiding the risk and saving time and effort. The impact of stirring effect of the tank provides full contact of methane bacteria and fermentation material, thus, improving gas yield.
NOVELTY - Method of preparing saccharified liquid of marine algae, involves pulverizing marine algae using wet mill, adding sulfuric acid to marine algae powder to obtain slurry, and adding the slurry and monosaccharide into reaction tube of continuous saccharification apparatus through mono pump.    USE - The method is useful for preparing saccharified liquid of marine algae for producing biofuel chosen from methanol, ethanol, propanol, butanol and acetone (claimed).    ADVANTAGE - The method is economic.
NOVELTY - Electrode material comprises a complex oxide having a perovskite structure.    USE - The electrode material is useful in solid oxide fuel cell (claimed), which is vertically-striped fuel cell.    ADVANTAGE - The electrode material has improved durability. The electrode material deterioration can be inhibited by enhancing uniformity of the concentrations of the components of the electrode material.    DETAILED DESCRIPTION - Electrode material comprises a complex oxide having a perovskite structure of formula AB1O3.    A = at least one of La or Sr, where A-site element has a standard deviation of an atomic concentration of 10.3 or less, and the atomic concentration is measured by energy dispersive X-ray spectroscopy at 10 spots within one field of view; and    B1 = not defined.    INDEPENDENT CLAIMS are included for a solid oxide fuel cell comprising a cathode (14) composed of an electrode material, an anode (11), and a solid electrolyte layer disposed between the cathode and the anode; or an porous substrate of insulation having a gas passage inside, a power generating element composed of an anode, a solid electrolyte layer and a cathode stacked in this order on the porous substrate, and an interconnector composed of an electrode material, where the interconnector is connected to the power generating element.    DESCRIPTION OF DRAWING(S) - The figure shows a cross sectional view of the principal part of a vertically-striped fuel cell.    Fuel cell stack (10)    Current collector (4)    Anode (11)    Barrier layer (13)    Cathode. (14)
NOVELTY - Composition for obtaining solid composite high-carbon fuel includes organic binding agent, coal and coke fillers. As organic binding agent there used is fermented residue formed as a result of anaerobic fermentation of organic animal residues, vegetation residues, domestic waste and sewage sludges. The following component ratio, wt %, is used: coal filler 10-80, coke filler 10-80, fermented residue is the rest.    USE - Oil and gas industry.    ADVANTAGE - Use of the composition allows simplifying the technology and increasing the efficiency of preparation process of the composition for obtaining solid composite high-carbon fuel, reducing ash content of the obtained composite fuel, increasing ecological properties of the process and reducing financial costs. 12 tbl, 5 ex
NOVELTY - Method involves preparation of plant oil with heating to 80 degrees C, alkaline ethanolysis using potassium hydroxide in ethanol with molar concentration of 2 mol/dm3 to obtain an ether-glycerine mixture which is separated to form two fractions - glycerine and a mixture of ethers. The mixture of ethers (biodiesel fuel) undergoes filtration, sorption purification and dehydration. The obtained biodiesel fuel is stored. Preparation of the plant oil is carried out such that before heating, the plant oil is mixed with 1% aqueous solution of an Ecofriend enzyme-probiotic preparation and the obtained mixture is held for 24 hours at temperature 23-27 degrees C. After holding for 24 hours, the mixture of plant oil and this preparation is heated to said heating temperature. The products are taken in the following ratio, pts.wt: plant oil 5; 1% aqueous solution of Ecofriend enzyme-probiotic preparation 5; potassium hydroxide in ethanol 5.    USE - Chemistry.    ADVANTAGE - Method increases the amount of the obtained biodiesel fuel. 2 tbl, 3 ex
NOVELTY - Carbonaceous biomass feedstock is pyrolyzed (10) using heat transfer medium to obtain pyrolyzed products and spent heat transfer medium (12). The spent heat transfer medium is separated into segregated (70) char and char-depleted spent heat transfer medium. The char-depleted spent heat transfer medium is introduced (80) into a dense bed of heat transfer medium fluidized by stream of oxygen-containing regeneration gas.    USE - Pyrolysis of carbonaceous biomass feedstock e.g. wood, agricultural waste, algae, forestry byproduct, cellulose, lignin, municipal waste and construction/demolition debris.    ADVANTAGE - The pyrolysis of carbonaceous biomass feedstock is efficiently enabled.    DESCRIPTION OF DRAWING(S) - The drawing shows flowchart of pyrolysis of carbonaceous biomass feedstock.    Pyrolysis of carbonaceous biomass feedstock (10)    Forming pyrolyzed product and spent heat transfer medium (12)    Separating spent heat transfer medium (70)    Introducing char-depleted spent heat transfer medium into fluidized bed (80)    Combustion (90)    Exporting portion of segregated char (300)
NOVELTY - A portion of a porous filter element is coated with biomass filter aid particles for producing a coated filter element. The initial bio-oil consisting of liquid phase and residual solids is made to pass through the coated filter element so that the residual solids are retained by the filter element and liquid phase is made to pass through the filter element for providing filtered bio-oil.    USE - Treatment method for bio-oil produced in biomass conversion process.    ADVANTAGE - The biomass filter aid promotes the efficiency or effectiveness of filtration process for removing solids from a fluid. The biomass filter aid spent for bio-oil production is recycled as conversion feedstock or used as a combustion heat resource in the biomass conversion system instead of performing waste disposal of the filter aid.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biomass conversion system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the biomass conversion system.    Biomass conversion system (10)    Biomass source (14)    Biomass feed system (18)    Conversion reactor (22)    Regenerator (26)
NOVELTY - An aerosol hairspray product for styling and/or shaping hair, comprises: (i) a container for storing a hairstyling formulation and a propellant; (ii) a hairstyling formulation; (iii) a propellant; and (iv) a spraying device.    USE - The aerosol hairspray product is useful for styling, fixing and/or shaping hair (claimed).    ADVANTAGE - The aerosol hairspray product is sustainable, environmentally friendly, safe and affordable. Also, the hairspray product is provided in a container with more flexibility as to shape and form. Furthermore, the container is made from more sustainable materials and can be easily recycled. The products exhibit excellent performance; performance benefits may include, for example: excellent hold; long-lasting hold; good humidity resistance; shapeable hold; acceptable drying time; excellent soft, natural hair feel; acceptable or non-stickiness of the hands and hair.    DETAILED DESCRIPTION - An aerosol hairspray product for styling and/or shaping hair, comprises: (i) a container for storing a hairstyling formulation and a propellant, where the container wall comprises at least about 80% plastic material by total weight of the container; (ii) a hairstyling formulation comprising: (a) 35-99% water by total weight of the hairstyling formulation and propellant, and (b) 0.01-10% hairstyling polymer by total weight of the hairstyling formulation and propellant; (iii) a propellant, which is selected from compressed gas propellants, liquefied gas propellants, and mixtures; and (iv) a spraying device; where the product comprises 15-54% volatile organic compound (VOC) by total weight of the hairstyling formulation and propellant; where the pressure inside the container is from about 1 bar to about 16 bar at 50 degrees C. An INDEPENDENT CLAIM is a method for styling hair comprising: (a) applying to hair an ejected composition, which is ejected by the hairspray product; and (b) drying the ejected composition on the hair.
NOVELTY - Curable perfluoropolyether gel composition comprises a straight chain fluorine-containing polymer (I), a polyfluoromonoalkenyl compound containing one alkenyl group per molecule and having a perfluoropolyether structure in its backbone, an organosilicon compound containing at least two hydrogen atoms bonded to the silicon atom per molecule, and a hydrosilylation catalyst.    USE - The curable perfluoropolyether gel composition is useful: in a gel product, which is used in automobiles, chemical plants, ink jet printers, semiconductor production lines, physical and chemical analysis equipment, medical equipment, aircrafts or fuel cell production (all claimed); as a moisture-proof coating agent for electro-electronic equipment, a potting agent for sensors, and a sealant for fuel cells; and in a gas pressure sensor, liquid pressure sensor, temperature sensor, humidity sensor, rotation sensor, G sensor, timing sensor, airflow meter, electronic circuit, semiconductor module, and control units.    ADVANTAGE - The curable perfluoropolyether gel composition exhibits excellent heat resistance, solvent resistance, chemical resistance, weatherability, releasability, water repellency, oil repellency, and acid resistance.    DETAILED DESCRIPTION - Curable perfluoropolyether gel composition comprises a straight chain fluorine-containing polymer having at least two alkenyl groups per molecule, of formula (I) and a polyfluoromonoalkenyl compound containing one alkenyl group per molecule and having a perfluoropolyether structure in its backbone, an organosilicon compound containing at least two hydrogen atoms bonded to the silicon atom per molecule, and a hydrosilylation catalyst.    R1 = vinyl or 1-4C alkyl;    R2 = 1-6C alkylene;    R3 = 1-4C alkyl (optionally substituted with F) or H; and    R4 = perfluoroalkylene or divalent perfluoropolyether structure-containing group.
NOVELTY - Hydrogenated vegetable oil mixed with dry hay in a ratio of 1:1 is claimed. A first variant of the above mixture is prepared by taking natural dry hay in a dry state and hydrogenated vegetable oil in powder or solid form, pressing both under heat in a closed container and cutting the obtained material into small pieces after cooling. A second variant of the above mixture is prepared by taking hay, chopping and mixing with hydrogenated vegetable oil in a ratio of 1:1.    USE - The hydrogenated vegetable oil mixed with dry hay is useful as a fire material in small heating systems or larger heating systems to generate heat and energy, and for heating home.    ADVANTAGE - The hydrogenated vegetable oil mixed with dry hay is easy to produce, cost-efficient and environmentally-friendly.
NOVELTY - Molded fuel based on ground products, comprises ground bran, ground fodder and/or ground waste materials.    USE - Used as molded fuel.    ADVANTAGE - The molded fuel: requires less processing costs; and makes use of waste products for its production and thus ecologically friendly.
NOVELTY - Producing biogas comprises: (a) providing a reactor fitted with fillers; (b) immobilizing methanogenic microorganisms (methane bacteria) on the surface of the fillers; (c) sprinkling the fillers with a nutrient solution for the micro-organisms along with the immobilized methanogenic microorganisms; (d) introducing gaseous substrates in the reactor for biogas production; and (e) discharging the biogas produced from the reactor.    USE - The method is useful for producing biogas.    ADVANTAGE - The method: ensures good mass transfer between gas and liquid and rapid adjusting of the equilibrium; has short transport paths, thus it exhibits high process intensity; is carried out in a small reaction chamber, thus has increased controllability of the gas production; and avoids the negative impact of the substrates on the formation of biofilm, thus allows rapid regeneration of the biofilm.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for producing the biogas, comprising at least one biogas reactor, which is filled with fillers, where immobilized microorganisms are provided on the surface, a sprinkler for sprinkling the filler with a nutrient solution, an inlet for introducing the gaseous substrates into the bioreactor and a diverter to derive the resulting biogas.
NOVELTY - Wastewater containing excrement and/or purification-tank sludge are nitrified-denitrified biologically. A portion of wastewater is branched before being sent to the nitrification-denitrification process and an alkali chemical is added. Wastewater added with alkali chemical is retained and supplied for denitrification. The pH of wastewater after addition of alkali chemical is set to 11.6-12.5. The residence time of wastewater in the alkali treatment process is 0.5-2 hours, and the residence time of wastewater in the retention process is 12-48 hours.    USE - Sewage disposal is used for purifying wastewater containing excrement and purification-tank sludge.    ADVANTAGE - The method economically stabilizes nitrification-denitrification process, without deteriorating treated-water quality. The usage amount of hydrogen donors, such as methanol, is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for sewage treatment unit (1).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the sewage disposal unit.    Sewage treatment unit (1)    Alkali treatment liquid (4)    Excrement injection path (10)    Purification-tank sludge injection path (11)    Nitrification tank (13)
NOVELTY - Biogas generation system comprises fermenter for fermenting organic waste and produces biogas, biodesulfurization column for desulfurizing hydrogen sulfide present in the biogas sent from the fermenter by bioreaction, and organic waste storage tank for storing organic waste before injecting to the front stage of the fermenter, where ammonia gas emitted in the organic waste storage tank is supplied to the circulation liquid system of the biodesulfurization column so that oxidation of circulation liquid is neutralized.    USE - The system is useful for generating biogas, preferably methane gas.    ADVANTAGE - The system uses ammonia produced from organic waste without requiring special apparatus, and produces biogas cost-effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biological desulfurization method of the biogas, which involves de-sulfurizing hydrogen sulfide present in the biogas sent from the fermenter which ferments organic waste and produces biogas by bioreaction in biodesulfurization column, injecting organic waste stored in organic waste storage tank to the front stage of the fermenter, supplying ammonia gas emitted in the organic waste storage tank to the circulation liquid system of the biodesulfurization column, and neutralizing oxidation of circulation liquid.
NOVELTY - Producing energy-rich gases involves adding liquid stream formed during production of ethanol from agro-forestry and agro-industrial residues. The liquid stream contains pentoses or cellulose and microbial flora, which are processed under anaerobic conditions.    USE - Method for producing energy-rich gases such as hydrogen and methane from lignocellulosic materials (claimed).
NOVELTY - An organic substance-containing wastewater is purified by diluting useful microorganism in silicon sol gel and discharging treated water from wastewater treatment tank (3) in a zigzag direction, up and down, flowing upward to pass a narrow path part (41).    USE - An organic wastewater processing method for sewage and night soil.    ADVANTAGE - Sludge is effectively separated when treated water passes a narrow path part, whole apparatus size is reduced, whole treatment process time is shortened, backward flow of sludge is prevented, treated water is discharged from wastewater treatment tank easily, recyclable treated water and useful microorganisms are obtained, blockage of membrane filter is prevented, and storage and conveyance of microorganism activator are easy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a microorganism activator for organic wastewater processing method containing silicon sol gel which dissolves silicon-containing material, which is mixed with alkaline substance in acid solvent and heat-processed.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the organic wastewater processing method.    Wastewater treatment tank (3)    Drainage channel (4)    Flat film tank (5)    Sludge discharge mechanism (6)    Narrow path part (41)
NOVELTY - A rotational drive unit (16) rotates hollow-shaped drum (14) whose lower portion is immersed in solution. A heating unit (18) heats outer peripheral surface (14A) of drum from inside of drum. An extraction unit (20) extracts the emission which evaporates from outer peripheral surface. The solution adhered on drum during rotation is scraped off by spatula to which outer peripheral surface of drum is contacted. The residue in solution is removed with filter and the solution scraped off by spatula is stored.    USE - Purifier for purifying ethanol solution. Can also be used for purifying seawater.    ADVANTAGE - The yield of biofuel can be increased by using grease trap and waste edible oil as raw material, so that ethanol solution can be purified at low cost. The biofuel can be produced from vegetable oil and fat containing grease trap, waste edible oil and ethanol solution efficiently. The structure of purifier is simplified and the cost is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for purification method of ethanol solution, which involves fermenting organic substance. The vegetable oil is supplied to accommodation pan. The lower portion of drum is oriented in horizontal direction and is immersed in ethanol solution. The temperature of outer peripheral surface of the drum is set to 70-90 degrees C and the drum is rotated. The azeotropy of ethanol is performed with water, on outer peripheral surface of drum.    DESCRIPTION OF DRAWING(S) - The drawing shows the front view of the purifier. (Drawing includes non-English language text)    Drum (14)    Outer peripheral surface of drum (14A)    Rotational drive unit (16)    Heating unit (18)    Extraction unit (20)
NOVELTY - Catalytic electrode comprises a substrate; and a complex oxide deposited on the substrate, the complex oxide includes ruthenium, oxygen, and at least one other metal, where the percentage of metal content that is ruthenium is less than about 20 percent; and where the percentage and the other metal are selected so as to allow the electrode to maintain sufficient electro catalytic activity during a redox reaction at the electrode; and where the other metal does not exceed the ruthenium in cost.    USE - The catalytic electrode is useful for producing fuel cell, flow battery, and electrolysis cell (all claimed).    ADVANTAGE - Electrodes can be synthesized using ruthenium cobalt (RuCo) oxides with ruthenium content reduced to about 5%, or using ruthenium manganate (RuMn) oxides having ruthenium content reduced to about 10%, while maintaining good catalytic activity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a fuel cell comprising the electrode;    (2) a flow battery comprising the electrode; and    (3) an electrolysis cell comprising the electrode.
NOVELTY - Cell retaining biomatrix (CRB) for producing organic solvents and alcohols by microbe(s) from different substrates, comprises cellulosic fibers, selected from wood cellulosic fibers, pulp cellulosic fibers, vegetable cellulosic fibers, such as mechanical pulp, dissolving pulp, lignocellulosic fibers, and cellulosic fibers originated from vegetable peels; and microbes, which have been immobilized into the cellulosic fibers, and which can save their biological activity in CRB.    USE - The CRB is useful for producing organic solvents and alcohols, by microbe(s) from different substrates, as feedstock for liquid fuels, chemicals, polymers and biomaterials (all claimed).    ADVANTAGE - The invention provides biomatrix, which provides a technically simple process for producing solvents and alcohols from different substrates.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a bio-column (BC) comprising CRB;    (2) an apparatus for producing organic solvents and alcohols from different substrates by microbe(s), comprising at least BC;    (3) a method for producing organic solvents and alcohols from different substrates comprising feeding substrate (SU1, SU2) to the CRB; producing organic solvents and alcohols by microbes by feeding substrate to the CRB; and recovering solution comprising organic solvents and alcohols; and    (4) organic solvents and alcohols, such as acetone, butanol, ethanol and isopropanol, produced by CRB, and where substrate(s) is/are selected from monomeric and oligomeric sugars, substrate originated from wood biomass and lignocellulosic biomass and substrate originated from vegetable peels, such as palm oil mill effluent (POME), and empty-fruit bunches (EFB).
NOVELTY - Fermentation system comprises alcohol fermentation tank (12) for fermenting sugar solution (11) by adding yeast (13) and producing organic raw material and unit for adding hydrothermally treated biomass (20) feedstock to the alcohol fermentation tank.    USE - The fermentation system is useful for fermenting sugar solution and producing organic materials chosen from alcohol, petroleum substitutes and amino acids (claimed). The alcohol includes chosen from ethanol and methanol. The petroleum substitutes includes liquefied petroleum gas (LPG), naptha, nylon, kerosene and diesel. The amino acid is used as raw material for foodstuff and feed.    ADVANTAGE - The system improves the efficiency of alcohol fermentation and is cost-effective as inorganic salts are not removed from the solid residue fraction and hence external addition of inorganic salt is not required.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic representation of alcohol production system. (Drawing includes non-English language text)    Sugar solution (11)    Alcohol fermentation tank (12)    Yeast (13)    Distillation residue (15a)    Alcohol (18)    Hydrothermally treated biomass (20)
NOVELTY - Molding (1) comprises a combustible material comprising a first portion having several organic particles, preferably wood chip particles (4), and a second portion having several wax granule particles (5). The wood chip particles and wax granule particles are mixed with each other, deformed by pressing and are glued with each other.    USE - The molding is useful as ignition aid for solid fuels e.g. wood, charcoal and coal.    ADVANTAGE - The molding: requires less time for producing; exhibits high burning point and high calorific value; maintains prolonged combustion; and can be produced in cost-effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for producing several moldings, comprising a pressing device, on whose cylindrical output at least one knife-like element is arranged for dividing cylindrical molding in two semi-cylindrical moldings.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the molding.    Molding (1)    Wood chip particles (4)    Wax granule particles (5)    Average length (6)    Storage container (10)
NOVELTY - Process for selectively extracting monoglycerides present in a fatty acid alkyl ester cut, comprises liquid-liquid extraction of a polar solvent including a lower alcohol, and optionally a non-polar solvent comprising a solvent immiscible with lower alcohol.    USE - The process is useful for extracting monoglycerides present in a fatty acid alkyl ester cut, preferably fatty acid methyl esters cut, which is useful in biodiesel (all claimed).    ADVANTAGE - The process does not require the use of a special adsorbent, and further step of filtration.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) fatty acid methyl esters cut of vegetable or animal origin, obtained by the method, where the monoglyceride content is less than 0.6 wt.%, preferably 0.25 wt.%; and    (2) biodiesel comprising purified fatty acid alkyl ester whose monoglyceride content is less than 0.6%.
NOVELTY - Stiorin (hydrogenated vegetable oil) that is mixed with dry corn stalks in a ratio of 1:1, is claimed, where the dry corn stalks are naturally present in a dry condition and the stiorin powder or stiorin mass is compressed in closed containers under heat effect, and the stiorin-corn stalk-brand fuel is cut into small pieces after cooling.    USE - The stiorin is useful in small heating systems for domestic heating or in larger heating systems used for generating heat and energy.
NOVELTY - Stiorin (hydrogenated vegetable oil) that is mixed with dry straw in a ratio of 1:1, is claimed, where the dry straw is naturally present in a dry condition and the stiorin powder or stiorin mass is compressed in closed containers under heat effect, and the stiorin-straw-brand fuel is cut into small pieces after cooling.    USE - The stiorin is useful in small heating systems for domestic heating or in larger heating systems used for generating heat and energy.
NOVELTY - Processing of coppiced timber involves water-vapor blasting of coppiced timber, and then drying and transferring product.    USE - Processing of coppiced timber used for fuel used in power stations.    ADVANTAGE - The method efficiently and economically processes coppiced timber using simple process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus for processing coppiced timber, which has blasting apparatus (6), movement units for mounting blasting apparatus and drying machine.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic side view of blasting apparatus.    Blasting apparatus (6)    Feed hopper (61)    Supply-adjustment valve (62)    Pressure tank (63)    Ball valve (64)
NOVELTY - The apparatus has waste-water-treatment tank (3) that purifies the organic waste water containing organic substance by using a useful microorganism. The waste-water-treatment tank is arranged in zigzag direction. A drainage channel (4) that discharges the treated water is provided. A narrow path portion (41) is formed in upward flow path portion (4a) of drainage channel.    USE - Apparatus for processing organic-waste-water containing ammonia ejected from restaurant, foodstuff industry, drink industry and livestock.    ADVANTAGE - The sludge contained in treated water can be purified easily and rapidly. The need for solid-liquid-separation tank is unnecessary. The organic-waste-water can be treated within short time. The backward flow of the isolated sludge can be prevented. The life time of the membrane filter can b prolonged. The sludge discharged from the discharge channel can be decomposed reliably. The processing cost can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the organic-waste-water processing apparatus.    Waste-water-treatment tank (3)    Drainage channel (4)    Upward flow path portion (4a)    Narrow path portion (41)    Discharge tank (52)
NOVELTY - The furnace has a fan (2) connected with a material barrel (1) and a bottom part of a cooker (4). The material barrel is provided with a purifying device (3). A charging basket is connected with the cooker. An upper part of the purifying device is connected with the cooker.    USE - Energy-saving straw gasification furnace.    ADVANTAGE - The furnace is environment friendly. The furnace saves energy and material and reduces labor intensity and production cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of an energy-saving straw gasification furnace.    Material barrel (1)    Fan (2)    Purifying device (3)    Cooker (4)
NOVELTY - The furnace has a furnace panel arranged on a shell and provided with a burner. A combustion chamber is arranged in the shell and installed with a fire grate. The burner is located at an upper part of the combustion chamber. A chimney interface is fixed on a furnace body. A feed opening is formed on the combustion chamber. Length of an opening end of a feed port is greater than 50 cm. A pot is provided with multiple holes. A continuous material is fixed below an oven. Each hole is formed on a furnace channel.    USE - Firewood and coal two-purpose biomass furnace.    ADVANTAGE - The furnace can be added with overlong pay diesel. The furnace has fuel that can fully dry overflow of combustible gas in a long continuous material. The furnace ensures constant temperature. The furnace avoids heating requirements of high cold area. The furnace has better burning effect, high working efficiency and low discharge rate. The furnace saves renewable energy, and protects ecological environment.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a firewood and coal two-purpose biomass furnace.
NOVELTY - The stove has a combustion chamber orderly connected with an air distribution ring and a burner, where a bottom part of the combustion chamber is connected with a grate. An end part of a pipe is connected with an opening and closing part of a door. The combustion chamber is connected with an insulating layer.    USE - Biomass ground stove.    ADVANTAGE - The stove improves low-emission biomass fuel generated in the semi-gasification combustion of the combustion-supporting gas in the combustion chamber by the air distribution ring and the air combined combustion. The stove is aesthetic in appearance and environment friendly, and saves energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass ground stove.
NOVELTY - Liquefaction of biomass, comprises: combining biomass with a solvent combination containing at least one liquefaction solvent and at least one make-up solvent in a pressurized reaction container to form a liquefaction mixture; and heating the liquefaction mixture to at least 250 degrees C under pressure of at least 200 psi to produce a crude reaction product containing a liquid bio-oil product, where the liquefaction solvent has a Hansen radius of interaction with coniferyl alcohol of less than 15 MPa1/2.    USE - The method is useful for liquefaction of biomass for producing bio-oil that can be further processed to provide a transportation fuel (all claimed) or petroleum refinery.    ADVANTAGE - The method: quickly promotes liquefaction and reduces the need to transport large amounts of hydrogen or hydrogen-carrying solvents, due to the presence of the solvent combination; is more economical and environmental friendly; operates at lower pressure, does not require a catalyst, hydrogen gas or carbon monoxide input, and provides very high conversion of biomass into the bio-oil; produces less solid byproduct (less than 10% of char); and provides a way to recycle a portion of the crude liquefaction product for use as part of the solvent combination.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a system for liquefaction of biomass, comprising a reaction container (1) suitable for conducting the biomass liquefaction process at above 300 degrees C and a pressure above 300 psi, where the reaction container comprises the solvent combination and biomass;    (2) a composition comprising: biomass; recycle stream from a biomass liquefaction reaction; and the make-up solvent; and    (3) a bio-oil produced by the process.    DESCRIPTION OF DRAWING(S) - The figure illustrates a schematic representation of the system.    Reaction container (1)    Separation subsystem (2)    Thermal or chemical separation subsystem (3)    Heating element (4)
NOVELTY - Increasing oil accumulation in microalgae Chlorococcum pamirum comprises incubating the microalgae in a culture medium and inducing oil accumulation in the microalgae.    USE - The methods are useful for increasing oil accumulation in microalgae Chlorococcum pamirum; for making feedstock for production of biodiesel; and for producing oil-rich microalgae useful as feedstock for biodiesel production. The microalgae and oil-enriched microalgae cell collection are useful as feedstock for biodiesel production; and for producing oil or lipids, where microalgae are enriched with oil by cultivation in a culture medium (all claimed).    ADVANTAGE - The methods induce and enhance accumulation of oil within the cells of Chlorococcum pamirum, thus the methods are suitable for large-scale production of oil-rich microalgae.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are: (1) an oil-enriched microalgae cell collection comprising Chlorococcum pamirum strain, where the cell collection is enriched with oil at a level higher than the oil level in the corresponding natural microalgae cells prior to incubation; and (2) a method of making feedstock for production of biodiesel, comprising: (a) incubating microalgae Chlorococcum pamirum in a culture medium; (b) inducing oil enrichment in the microalgae; (b) isolating the oil-enriched microalgae from the culture medium; and (c) extracting lipids and/or oil from the oil-enriched microalgae.
NOVELTY - A strain of Chlamydomonas pitschmannii YSL03 (KCTC 11715BP) having high lipid content and strong resistance to wastewater, is new.    USE - The strain of C.pitschmannii YSL03 is useful for producing biodiesel and treating wastewater (claimed).    ADVANTAGE - The strain effectively provides production of biodiesel, is strongly resistant to waste water and can eliminate nitrogen and phosphorus in waste water.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) starter culture liquid of C.pitschmannii YSL03; (2) method (M1) for separating lipid, involves culturing C.pitschmannii YSL03 in culture medium; (3) method (M2) for producing biodiesel, involves processing the lipid isolated from C.pitschmannii YSL03; (4) microbial agents for wastewater treatment comprising C.pitschmannii YSL03 strain and starter culture liquid of C.pitschmannii YSL03; (5) method (M3) for culturing C.pitschmannii YSL03, involves culturing the strain in the culture medium; and (6) method (M4) for removing nitrogen and phosphorus from wastewater, involves culturing C.pitschmannii YSL03 in wastewater.
NOVELTY - The organic waste water processing system (A) has an anaerobic treatment unit (2) that includes an anaerobic circulating water channel (21) in which a fixed bed (22) with methane fermentation microorganisms is installed. The organic waste water is circulated through the anaerobic circulating water channel so that the organic substance in the waste water is decomposed into aerobic microbe.    USE - System for processing organic waste water from household and industry.    ADVANTAGE - Running cost and installation cost of the organic waste water processing system can be reduced and purification performance of the waste water processing system can be improved significantly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for organic waste water processing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the organic waste water processing system.    Anaerobic treatment unit (2)    Aerobic treatment unit (3)    Anaerobic circulating water channel (21)    Fixed bed (22)    Organic waste water processing system (A)
NOVELTY - A base material layer which supports a catalyst is formed on a substrate. Carbon nanotubes are grown perpendicularly in the surface direction using the catalyst as starting point, by supplying a carbon source gas to the base material layer heated to preset temperature. The base material layer is heated at a temperature higher than the preset temperature after growth of carbon nanotubes. An electrode catalyst is then supported on the carbon nanotubes, and the base material layer is removed.    USE - Manufacture of fuel cell.    ADVANTAGE - The method enables manufacture of fuel cells with reduced raw-material loss of added electrode catalyst, as the surface roughness or porosity of base material layer is made small, and the adsorption surface area of the catalyst in the base material layer is reduced. Since the base material layer can be annealed without deforming the substrate by melting, carbon nanotubes can be transferred to an electrolytic membrane favorably.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic cross-sectional view of the fuel cell.    Polymer electrolyte membrane (12)    Anode (14)    Cathode (16)    Membrane electrode assembly (18)    Separator (20)
NOVELTY - Hydrogenated vegetable oil mixed with dry wood shavings in a ratio of 1:1 is claimed. A first variant of the above mixture is prepared by taking natural dry wood shavings in a dry state and hydrogenated vegetable oil in powder or solid form and pressing both under heat in a closed container. A second variant of the above mixture is prepared by taking wood shavings, chopping and mixing with hydrogenated vegetable oil in a ratio of 1:1.    USE - The mixture of hydrogenated vegetable oil mixed with dry wood shavings is useful to generate heat energy, preferably for domestic heating or larger scale heating systems.    ADVANTAGE - The heat energy producing mixture is easy to produce and is environmental friendly and economical.
NOVELTY - Hydrogenated vegetable oil mixed with dry tree leaves in a ratio of 1:1 is claimed. A first variant of the above mixture is prepared by taking natural dry tree leaves in a dry state and hydrogenated vegetable oil in powder or solid form and pressing both under heat in a closed container. A second variant of the above mixture is prepared by taking dry tree leaves, chopping and mixing with hydrogenated vegetable oil in a ratio of 1:1.    USE - The mixture of hydrogenated vegetable oil mixed with dry tree leaves is useful to generate heat energy, preferably for domestic heating or larger scale heating systems.    ADVANTAGE - The heat energy producing mixture is easy to produce and is environmental friendly and economical.
NOVELTY - Device for producing biogas from manure, comprises a Kuchel reactor.    USE - Used as a device for producing biogas from manure.    ADVANTAGE - The device is affordable, profitable, and easy to maintain.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the device for producing biogas from manure.    Kuchel reactor (A)    Cascade channel (B)    Reservoir for liquid manure (C)    Reservoir (D)    Fan engine (E)
NOVELTY - Dust containing miscellaneous materials with more than 4 mesh/25.4 mm net and sand powder with less than 60 mesh/25.4 mm net is completely removed from a raw material. The screened raw material is pulverized and fine powder is formed. The fine powder and a liquid adjuvant are mixed and stirred, and moisture content of substance is made into 32-38%. The substance containing moisture is rolled into a sheet having thickness of 0.1-0.2 mm. The sheet is dried until moisture content is 12-14%, cooled and rolled to form a multifunctional-type organic mulch sheet.    USE - Manufacture of multifunctional-type organic mulch sheet used as agricultural sheet in production of root vegetables, seedbed, ornamental plant, fruit, etc.    ADVANTAGE - The environmentally-friendly multifunctional-type organic mulch sheet is easily manufactured with favorable mechanical strength, light transmittance, air permeability, heat retaining property and moisture retention property.    DETAILED DESCRIPTION - Dust containing miscellaneous materials with more than 4 mesh/25.4 mm net and sand powder with less than 60 mesh/25.4 mm net is completely removed from a raw material using a sieving machine until raw material purity is 99.5% or more. The screened raw material is pulverized and fine powder is formed. The fine powder has 80% of particles with size of 60-120 mesh/25.4 mm and remaining particles with size of 120 mesh/25.4 mm or less. The fine powder and a liquid adjuvant are mixed and stirred, and moisture content of substance is made into 32-38%. The deviation of a moisture content is made into 1% or less. The substance containing moisture is rolled into a sheet having thickness of 0.1-0.2 mm. The sheet is dried until moisture content is 12-14%, cooled and rolled to form a multifunctional-type organic mulch sheet.
NOVELTY - Preparing a bone protein preparation (I), comprises: (a) demineralizing the bone and extracting the bone matrix with guanidine hydrochloride solvent to obtain a bone protein extract; (b) filtering the extract with a microfilter with cut-off size sufficient for removing big particles and non-proteinous material but enabling proteins to pass; and (c) filtering the flow-through with a cassette ultrafilter having the cut-off size of 5-10 kDa to recover the bone protein preparation.    USE - (I) is useful for inducing formation of bone, cartilage, tendon or tooth, in vitro or in vivo. (I) is useful: in an osteogenic device, which is a bone implant; and as coating on the pellet, disc, block or granule. (I) is useful for treating disorders related to bone or cartilage defects, where regeneration, repair or growth is desired, or other diseases, such as cancer (all claimed), wound healing, ectopic bone induction, skeletal disorders, deformations, acute fractures, chondral defects, osteochondral defects or subchondral defects. Tests details are described but no results given.    ADVANTAGE - The method provides (I) with improved scalability and high yield in an economical and environmentally friendly manner. (I) has improved synergistic effect, physiological effect or high bone formation activity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) (I) obtained by the method;    (2) a paste, putty, pellet, disc, block or granule comprising (I); and    (3) a pharmaceutical composition containing (I).
NOVELTY - Method for producing synthesis gas, involves (a) feeding a carbonaceous material to a gasification reactor, (b) feeding oxidizing gas to the bottom of the reactor, (c) filtering the solid particles dragged by the gas in a cyclone filter placed internally at the top of the reactor, (d) discharging gaseous stream from the cyclone filter, and (e) recycling the filtered solid particles discharged at the base of the cyclone directly in the biphasic fluid bed.    USE - The method is useful for producing synthesis gas. The device is useful for performing gasification of the carbonaceous material (claimed). The method and device are useful for producing energy.    DETAILED DESCRIPTION - Method for producing synthesis gas, involves (a) feeding a carbonaceous material having particle size of less than or equal to 50 mm to a gasification reactor, (b) feeding oxidizing gas to the bottom of the reactor at a flow rate to provide the solid mass present in the reactor with an aspect of stable biphasic fluid bed comprising a dense phase consisting of solid and interstitial gas, and a dilute phase consisting of gas bubbles ascending along the bed, (c) filtering the solid particles dragged by the gas in a cyclone filter placed internally at the top of the reactor, (d) discharging gaseous stream from the cyclone filter consisting of synthesis gas and unreacted oxidizing gas, and (e) recycling the filtered solid particles discharged at the base of the cyclone directly in the biphasic fluid bed by an inner duct. An INDEPENDENT CLAIM is included for a device for performing gasification of the carbonaceous material, which comprises a cylindrical vertical reactor to hold the carbonaceous material to-be-subjected to gasification, feeding unit of the carbonaceous material and oxidizing gas which is placed at the bottom of the vertical reactor, and a filtration unit of the dragged powders placed internally at the head of the reactor.
NOVELTY - An organic wastewater containing organic chemicals is decomposed using microorganisms. The treated water is subjected to biological-activated carbon treatment process in which the treated water is supported by activated carbon, and then the processed water is subjected to oxidative-degradation process.    USE - Treatment of wastewater discharged from flat panel display manufacturing plant, semiconductor device manufacturing plant and liquid crystal display manufacturing plant.    ADVANTAGE - The wastewater treatment is efficiently and economically enabled with reduced consumption of energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for wastewater treatment apparatus (1).    DESCRIPTION OF DRAWING(S) - The drawing shows flowchart of wastewater treatment apparatus. (Drawing includes non-English language text)    Wastewater treatment apparatus (1)    Biological treatment apparatus (2)    Filtration processing apparatus (3)    Reverse osmosis processing apparatus (4)    Biological-activated carbon processing apparatus (5)    Ultraviolet-ray processing apparatus (6)
NOVELTY - Preparing 4-hydroxy-2-oxo-1,2-dihydro-quinoline-3-carboxylic acid phenylamide compound (I), comprises: reacting 4-hydroxy-2-oxo-1,2-dihydro-quinoline-3-carboxylic acid compound (II) with toluene compound (III) in a refluxing mixture containing an aliphatic solvent or its mixture, where the aliphatic solvent has a boiling point of 68-191 degrees C; condensing vapors of the refluxing mixture; treating the condensed vapors with an alcohol scavenging agent or a mixture of alcohol scavenging agents; and returning the condensed vapors back to the reaction mixture.    USE - (I) is useful for treating autoimmune diseases and cancer. No biological data given.    ADVANTAGE - The method shows large scale in high yield and in high purity, without the need for prolonged reaction times and excessive solvent and energy consumption. The method is economical and environmental friendly.    DETAILED DESCRIPTION - Preparing 4-hydroxy-2-oxo-1,2-dihydro-quinoline-3-carboxylic acid phenylamide compound of formula (I), comprises: reacting a 4-hydroxy-2-oxo-1,2-dihydro-quinoline-3-carboxylic acid compound of formula (II) with toluene compound of formula (III) in a refluxing mixture containing an aliphatic solvent or its mixture, where the aliphatic solvent has a boiling point of 68-191 degrees C; condensing vapors of the refluxing mixture; treating the condensed vapors with an alcohol scavenging agent or a mixture of alcohol scavenging agents; and returning the condensed vapors back to the reaction mixture.    R1 = ethyl, chloro or methoxy;    R2 = ethyl or methyl;    R3 = H or trifluoromethyl; and    R4 = 1-4C alkyl, preferably methyl, ethyl, n-propyl, iso-propyl or n-butyl.
NOVELTY - A modifier unit (10) comprises modifier (12), steam generation part which generates steam in modifier, source gas supply pipe which supplies source gas to modifier, and drain pot currently interposed by source gas supply pipe. The modifier unit produces hydrogen gas by reacting steam and source gas.    USE - Modifier unit for fuel cell unit.    ADVANTAGE - The inflow of steam to upstream of source gas supply pipe is suppressed. The water seal of source gas supply pipe is prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the fuel cell unit which has modifier unit.    Modifier unit (10)    Modifier (12)    Evaporator (14)    Reaction chamber (16)    Burner (18)
NOVELTY - A biomass charcoal apparatus (10) has a vertical carbonization furnace (11) in which biomass is filled, a biomass supply apparatus (12) and a hot gas supply apparatus (11E) which are connected to the carbonization furnace, and a filling moving bed of biomass which supplies biomass from biomass supply apparatus, formed within carbonization furnace. The charcoal apparatus has a large rump material supply apparatus (13) for supplying large rump material larger than biomass in carbonization furnace, and dispersing large rump material in moving bed of biomass in carbonization furnace.    USE - Biomass charcoal apparatus.    ADVANTAGE - The biomass charcoal apparatus produces carbonized material at high yield.    DETAILED DESCRIPTION - A biomass charcoal apparatus has a vertical carbonization furnace in which biomass is filled, a biomass supply apparatus and a hot gas supply apparatus which are connected to the carbonization furnace, and a filling moving bed of biomass which supplies biomass from biomass supply apparatus, formed within carbonization furnace. Hot gas is supplied into carbonization furnace from hot gas supply apparatus, biomass is contacted with hot gas, thermally decomposed, and a carbonized material is produced. The biomass charcoal apparatus has a large rump material supply apparatus for supplying large rump material larger than biomass in carbonization furnace, and dispersing large rump material in the filling moving bed of biomass in carbonization furnace. An INDEPENDENT CLAIM is included for method for producing charcoal from biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of biomass charcoal apparatus. (Drawing includes non-English language text)    Biomass charcoal apparatus (10)    Carbonization furnace (11)    Hot gas supply apparatus (11E)    Biomass supply apparatus (12)    Large rump material supply apparatus (13)
NOVELTY - A biomass charcoalized apparatus (10) comprises carbonization furnace (11) which produces carbonized material, stirrer (13) which stirs biomass within filling moving bed (P), stirring blade (13B) which rotates to circumference of axis line extended in up-down direction, and vane part which has slope which rotation direction tip direction side faces upwards.    USE - A biomass charcoalized apparatus.    ADVANTAGE - The apparatus can obtain carbonized material from biomass with high yield.    DETAILED DESCRIPTION - A biomass charcoalized apparatus (10) comprises carbonization furnace (11) which produces carbonized material, stirrer (13) which stirs biomass within filling moving bed (P), stirring blade (13B) which rotates to circumference of axis line extended in up-down direction, and vane part which has slope which rotation direction tip direction side faces upwards. The division formation of round area of circumference of axis line of stirring blade is carried out in circumferential direction at vane parts. The carbonized material is produced by supplying biomass from upper part of vertical carbonization furnace, forming filling moving bed of biomass, making biomass contact with hot gas, and thermally decomposing.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of biomass charcoalized apparatus. (Drawing includes non-English language text).    Biomass charcoalized apparatus (10)    Carbonization furnace (11)    Stirrer (13)    Stirring blade (13B)    Filling moving bed (P)
NOVELTY - The method involves providing a support base material supporting a solid-oxide fuel cell (10). An inter connector is provided in an adjoining solid-oxide fuel cell. A reaction barrier layer (14) is laminated after baking of a solid electrolyte layer (13). A fuel electrode layer (11) contacts fuel gas used as a hydrogen source. An active layer (12) and the solid electrolyte layer are produced by press-molding a two-layer lamination sheet. An intermediate laminated body and an unbaking air electrode layer are integrated into a solid-oxide fuel cell laminated body.    USE - Method for manufacturing a flat type solid-oxide fuel cell.    ADVANTAGE - The method enables improving production efficiency during manufacturing process.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a solid-oxide fuel cell.    Solid-oxide fuel cell (10)    Fuel electrode layer (11)    Active layer (12)    Solid electrolyte layer (13)    Reaction barrier layer (14)
NOVELTY - Selective hydrogenation of linear, polyunsaturated 4C-hydrocarbon and branched, polyunsaturated 5C-hydrocarbon in a hydrocarbon mixture under the addition of hydrogen and carbon monoxide and under the use of a heterogeneous hydrogenation catalyst in a hydrogenation reactor, is claimed, where the volume ratio of the feed stream in the reactor to the volume of the catalyst is maximum 30 l/l.hour.    USE - The process is useful for the hydrogenation of linear, polyunsaturated 4C-hydrocarbon and branched, polyunsaturated 5C-hydrocarbon.
NOVELTY - The kiln has a furnace body arranged with a furnace core, where the furnace core and a furnace body are provided with an annular clapboard arranged on an air channel. The air channel is connected with the furnace core provided with a furnace bridge. An upper part of the furnace core is connected with an air inlet plate and a fire wall. A side of the furnace core is formed as an opening part. A feeding groove passes via a furnace wall of the furnace core. A groove is formed on a material feeding groove cover. The feeding groove and the groove cover are arranged with an elastic switch.    USE - Effective biomass gasification kiln.    ADVANTAGE - The kiln ensures that fire is strong and fully burnt, and avoids full-gasification furnace tar and semi-gasification furnace. The kiln ensures that the furnace bridge avoids linkage via a connecting rod plate, and avoids difficulties in ash discharging and ash discharging hole during sealing.    DETAILED DESCRIPTION - The furnace bridge is formed as a circular plate structure. The air inlet plate is formed as an annular flat or horn shaped structure. The fire wall is formed as a straight cylindrical or taper shaped structure. The elastic switch is made of thin steel sheet.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of an effective biomass gasification kiln.
NOVELTY - The device has a biomass gasification furnace (1), two cooling spray towers, an oil tar purifier (4), a gas-water separator (5) and a buffer tank (6), where the biomass gasification furnace is provided with a feeding device (8) and a fire grate and equipped with an ash discharge device (12). The purifier is connected with a gas pressure drum fan. The gas-water separator is connected with the buffer tank. The fire grate consists of double layers, where each layer comprises a fixed fire grate and a movable fire grate.    USE - Production device for continuously preparing combustible gas by using biomass fuel.    ADVANTAGE - The device ensures requirement of continuous production and obtains biomass gasification fuel gas without dust, tar and moisture. The gas has high purity.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a production device for continuously preparing combustible gas by using biomass fuel.    Biomass gasification furnace (1)    Oil tar purifier (4)    Gas-water separator (5)    Buffer tank (6)    Feeding device (8)    Ash discharge device (12)
NOVELTY - The furnace has a furnace body (1), a furnace cover (2), a hearth (3), a purifier (4) and a blower (6), where the purifier is fixed on an inlet and an outlet of a secondary purifying device. The secondary purifying device is composed of a straight pipe (8). A three-way inlet branch is connected with a supply pipe to form a secondary wind device (14). The straight pipe is inclined upwards and is connected with the purifier. An upper part and a lower part of a vertical tube (16) are provided with a ball valve. An end of the ball valve is connected with a stove head.    USE - Straw gasification furnace.    ADVANTAGE - The secondary purifying device purifies and increases the oxygen supply.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a straw gasification furnace.    Furnace body (1)    Furnace cover (2)    Hearth (3)    Purifier (4)    Blower (6)    Straight pipe (8)    Secondary wind device (14)    Vertical tube (16)
NOVELTY - The charger has an acidic water matter fuel cell (2) that is connected with an electrolytic vessel (1). The hydrogen and oxygen are sent to the acidic water matter fuel cell via a gas-sending pipe (14). The electric power is produced by a chemical reaction, and charge is performed with respect to a battery module (3). The pure water generated by the acidic water matter fuel cell is injected in the electrolytic vessel via a pure-water pipe (22). The electric power is supplied by the battery module to a vehicular power system (4).    USE - Automatic battery charger for battery module of electric vehicle.    ADVANTAGE - The charger can be automatically charged with respect to the battery module of the electric vehicle. Hence the effort of the person is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the automatic battery charger for battery module of electric vehicle.    Electrolytic vessel (1)    Acidic water matter fuel cell (2)    Battery module (3)    Vehicular power system (4)    Gas-sending pipe (14)    Pure-water pipe (22)
NOVELTY - The method involves using a template membrane, where a thin layer of nickel oxide is deposited on the template membrane with vapor phase to obtain supported template membrane. Gas phase material is deposited on supported template membrane. Deposition of material is carried out by applying radiofrequency magnetron.    USE - Method for obtaining inorganic porous membrane for manufacturing fuel cells, sensors, functional electrode and materials with antiferromagnetic properties.    ADVANTAGE - The method involves using a template membrane, and hence ensures simple process to provide improved inorganic porous membrane.    DESCRIPTION OF DRAWING(S) - The drawing shows a photograph of the inorganic porous membrane.
NOVELTY - The method involves introducing vaporized natural gas in a storage tank (300) into a heat exchange unit (700, 800). A refrigerant i.e. liquid nitrogen, is introduced into the exchange unit. The natural gas is liquefied by exchanging heat with the refrigerant. The liquefied natural gas is returned to the tank. A fluid path is provided for flowing the vaporized natural gas from the tank, and the vaporized natural gas is introduced into the exchange unit. The liquefied natural gas is returned to the tank through another fluid path in fluid communication with the former fluid path.    USE - Method for storing liquefied natural gas that is utilized as combustion fuel such as petrol and diesel, in a storage tank such as stationary tank or mobile tank, of a vehicle.    ADVANTAGE - The vaporized nitrogen is directed through an outlet and vented to an atmosphere so as to minimize boil off losses, to conserve liquefied natural gas vapor generation, and to maintain the storage tank at a sufficiently cold temperature, thus minimizing vapor losses.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a system for storing liquefied natural gas, comprising a storage tank and a heat exchange unit.    DESCRIPTION OF DRAWING(S) - The drawing shows a circuit diagram of a gas liquefaction system for producing liquid natural gas.    Optional heater (160)    Storage tank (300)    Pair of gas pretreatment units (500, 600)    Heat exchange unit (700, 800)    Container (770)
NOVELTY - The device has a bed body whose upper part and lower part are equipped with a biomass jet feeding pipe (2). The biomass jet feeding pipe is extended to a heat conducting pipe (10) by connecting through a tapered transition section. The upper part of the bed body is connected to a cyclone separator (8) of large diameter. The lower part of the bed body is internally equipped with the heat conducting pipe. A feeder is connected to lower part of a biologic fluidized bed (7). A returning part is equipped with two-stage transmission wind inlet port and a loosening air mouth.    USE - Biomass and coal composite burning device.    ADVANTAGE - The device reduces production of biomass tar.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass and coal composite burning device.    Biomass jet feeding pipe (2)    Gas distributor (4)    Biologic fluidized bed (7)    Cyclone separator (8)    Heat conducting pipe (10)
NOVELTY - Manufacture of an electrode catalyst involves baking an electrode-catalyst precursor formed by hydrothermal reaction of a mixture containing materials (A, B, C) in the presence of water that is in a supercritical or subcritical state, under the conditions such that the material (B) changes to a carbon material. The material (A) is a metal compound comprising group 4A and/or group 5A elements, and hydrogen, nitrogen, chlorine, carbon, boron, sulfur and/or oxygen. The material (B) is a carbon-material precursor. The material (C) is an electroconductive material.    USE - Manufacture of electrode catalyst used for electrolysis of water, electrolysis of organic substance and electrochemical system of fuel cell e.g. polymer electrolyte fuel cell and phosphoric acid fuel cell.    ADVANTAGE - The method economically provides electrode catalyst, which can be used under high electric potential in acidic electrolyte. The electrode catalyst has high activity.    DETAILED DESCRIPTION - Manufacture of an electrode catalyst involves baking an electrode-catalyst precursor formed by hydrothermal reaction of a mixture containing materials (A, B, C) in the presence of water that is in a supercritical or subcritical state, under the conditions such that the material (B) changes to a carbon material. The material (A) is a metal compound comprising at least one metallic element selected from group 4A and group 5A elements, and at least one non-metallic element selected from hydrogen, nitrogen, chlorine, carbon, boron, sulfur and oxygen. The material (B) is a carbon-material precursor. The material (C) is an electroconductive material.    DESCRIPTION OF DRAWING(S) - The drawing shows the graph illustrating powder X-ray diffraction pattern of electrode catalyst. (Drawing includes non-English language text)