NOVELTY - The system has main heat exchanger internally provided with feed gas passage, mixed refrigerant passage, nitrogen heat-exchanging passage. The feed gas from upstream coal gasification device is entered into main heat exchanger for exchanging heat, and then feed gas is cooled. An inlet and outlet of mixed refrigerant passage are respectively connected with inlet and outlet of closed mixed refrigerant circulation unit. An inlet/outlet of nitrogen heat-exchanging passage is respectively connected with outlet/inlet of nitrogen circulating compressor.    USE - Heat exchanging system for cryogenic separating device of methane in feed gas from coal gasification device.    ADVANTAGE - The closed mixed refrigerant circulation is combined with nitrogen refrigerating circulation unit of nitrogen circulating compressor, so that the heat transferring temperature difference of main heat exchanger can be improved. The irreversible loss of main heat exchanger can be reduced and energy consumption of cryogenic separating device can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic circuit diagram of the heat exchanging system for methane cryogenic separating device. (Drawing includes non-English language text)
NOVELTY - Concentrated or fuming sulfuric acid or phosphoric acid is added to industrial sludge to form a mixture. The sludge mixture is mixed, aged and the water in the mixture is transformed to free water. The sludge mixture is dehydrated to separate the free water and industrial sludge, and the sludge is baked to obtain phosphate fertilizer.    USE - Manufacture of phosphate fertilizer.    ADVANTAGE - The phosphate fertilizer is manufactured economically by a simple and environmental-friendly process.
NOVELTY - A rotary excrement drainage device is located in the toilet cylinder. A pulp pump (50) is automatically controlled by a weight sensor to start up and run for a certain time to convey the excrement pulp in excrement storage tank to main transfer tank where excrement is conveyed to methane plant with tanker or pipelines. A crushing and milling device is mounted on the top of the excrement storage sub-tank, to crush and mill the excrement entering the sub-tank, so that it is easy for the pulp pump to convey the crushed excrement.    USE - Recovery and usage method of excrement from flushing-free toilet of automatic type, energy-saving type or semi-automatic type (all claimed), used in industrialized methane plant as raw material to produce fuel gas, and for use in agricultural production.    ADVANTAGE - The energy conservation, emission reduction and environmental protection effects can be improved. Since the flushing-free toilet, propeller-type closed rotary excrement drainage device, foggy gas spray device and spiral conveyor are housed in the toilet cylinder, the purposes of no flushing and no smell, sanitation and simple operation are realized.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of the system used for recovery and usage method of excrement.    Centralizing excrement drainage pipe (41)    Milling motor (43)    Closed slide device (44)    Reamer rod (45)    Pulp pump (50)
NOVELTY - The structure has dirt discharging well at which sludge is recycled. The organic material containing nitrogen, potassium and trace elements in sewage is purified. The sludge mud in river is purified by river sand discharging well. The water and organic material are purified by water-grass and by decomposing micro-organism in successive purification stages. The water purification process is performed by organic material and micro-organism in fish water, in the final purification stage.    USE - Structure for radically managing odor from river flowing across small bridge, for achieving natural landscape effect.    ADVANTAGE - The purified water is passed to small bridge flowing across the river, along with illumination effect attained by illumination mechanisms installed at the side of bridge, to achieve the desired natural landscape effect effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for radically managing odor from river flowing across small bridge.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the structure for radically managing odor from river flowing across small bridge.    Sludge filling box (1)
NOVELTY - Feed additive is prepared by using (a) (in parts weight): choline chloride (4-8), green tea powder (1-5), insect chitin and/or selenoprotein (4-8) and vitamin (0.01-0.03), or (b) choline chloride (3-7), glycine betaine, methionine or carnitine (0.5-1), green tea powder (1-5), insect chitin and/or selenoprotein (4-8) and vitamin (0.01-0.03). The vitamin is vitamin A, vitamin C and/or vitamin E.    USE - The additive is useful for controlling liver-gall syndrome of fish (claimed), preventing aquatic animals (e.g. shrimp) from hemorrhagic disease, and improving immunity and production performance of fish.    ADVANTAGE - The additive is prepared by simple process, convenient to use, environment-friendly, improves water quality and generates no toxic residue.
NOVELTY - Balanced composition comprises N-(phosphonomethyl) glycine, glyphosate, surfactant and carbonates and/or bicarbonate in solid form. The composition comprises (in %): glyphosate acid (40-74), ammonium bicarbonate (10-21) and surfactant aggregates (50-50). The composition comprises (in %): glyphosate acid (40-64), magnesium carbonate (20-32) and surfactant aggregates (4-40). The composition comprises (in %): glyphosate acid (40-68), potassium bicarbonate (16-28) and surfactant aggregates (4-44).    USE - Balanced composition used as herbicide in agriculture.    ADVANTAGE - The balanced composition is economic, eco-friendly and prepared on industrial scale in form of powder, granule, flake and pellets by simple method. The composition is not harmful to farmers.    DETAILED DESCRIPTION - Balanced composition comprises N-(phosphonomethyl) glycine, glyphosate, surfactant and carbonates and/or bicarbonate in solid form. The composition comprises (in %): glyphosate acid (40-74), ammonium bicarbonate (10-21) and surfactant aggregates (50-50). The composition comprises (in %): glyphosate acid (40-64), magnesium carbonate (20-32) and surfactant aggregates (4-40). The composition comprises (in %): glyphosate acid (40-68), potassium bicarbonate (16-28) and surfactant aggregates (4-44). The composition comprises (in %): glyphosate acid (40-72), sodium bicarbonate (12-22) and surfactants aggregates (6-48).
NOVELTY - The water electrolyzer has film electrode which is positioned between double-electrode plates. The ends of double-electrode plates on outermost layer are respectively provided with electric conducting plates, insulating plates and end plates which are fixed by screws and nuts. Each double-electrode plate is compounded by titanium-made anode-side field plate, and graphite or stainless steel-made cathode-side field plate. Several ridges with openings, and channels are formed in the anode-side field plate.    USE - Solid polymer electrolyte film water electrolyzer.    ADVANTAGE - Water can be distributed uniformly on the surface of film electrode, the size and weight reductions of the water electrolyzer can be achieved, and the life time of the water electrolyzer can be prolonged reliably.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of the solid polymer electrolyte film water electrolyzer.
NOVELTY - The automatic adjusting devices (A,A',B,B') are installed on pipelines to control normal and differential pressures of chlorine, respectively. The current gradient is set to 50 A/minute and current value is boosted to set gradient to converge chlorine and nitrogen when nitrogen control valve is shut off while stabilizing normal and differential pressures to 10 and 40 mbar. An operation console and distributed control system are provided to control opening and closing of adjusting devices with respect to increase in current value in the range of 2.7-3.5 kA.    USE - Method for synchronizing opening/closing time of valve of electrolyzer producing chlorine and hydrogen used for production of caustic soda.    ADVANTAGE - The opening and closing time can be synchronized easily and reliably, and the operation time can be reduced reliably.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the electrolyzer. (Drawing includes non-English language text)    Automatic adjusting devices (A,A',B,B')
NOVELTY - Biocide comprises Bacillus subtilis KB-401 (KFCC 11388P) as an active ingredient.    USE - The biocide is useful for controlling fruit tree disease caused by Diaporthe citri, Alternaria kikuchiana, Venturia nashicola, V.inaequalis, Botrytis cinerea, Cladosporium fulvum, Colletotrichum coccodes, Fusarium oxysporum, Phytophthora capsici, F.solani, P.melonis, F.moniliforme, C.caudatum, Pythium sp. and Rhizoctonia solani (all claimed).    ADVANTAGE - The biocide is environment-friendly.
NOVELTY - A metal precursor mixed solution containing main catalyst metal precursor and ionic liquid is prepared. The solution is reduced using a reducing agent to obtain a reduced product. The reduced product is refined and dried to obtain the catalyst, and the ionic liquid is collected.    USE - Manufacture of catalyst for electrode used for membrane electrode assembly of fuel cells (all claimed) e.g. polymer electrolyte fuel cell, phosphoric acid fuel cell, molten carbonate fuel cell and solid oxide fuel cell.    ADVANTAGE - The method enables to manufacture catalyst with high activity by a simple process. The fuel cells having excellent power density are provided.    DESCRIPTION OF DRAWING(S) - The drawing shows the structure of the fuel cell. (Drawing includes non-English language text)    Anode (20)    Cathode (30)    Electrolyte film (40)    Anode separator (50)    Cathode separator (60)
NOVELTY - The device has a barrel body (1) whose upper end and lower end are connected to an upper sealer (5) and a lower sealer (8), respectively, where the lower sealer is connected to an oil drain tank (10). A lower sealing barrel (12) is equipped with a valve (9), and the barrel body is equipped with a water inlet pipe (7). Central part of an upper sealer is equipped with an overflow pipe (4), where one side of the upper sealer is equipped with a fuel gas inlet pipe and a fuel gas outlet pipe that are connected with two adjacent circulation pipes (2).    USE - Biomass gas cooling and circulating device.    ADVANTAGE - The device provides excellent cooling effect, and prevents blockage in pipelines. The device is compact in structure, convenient to operate and inexpensive.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass gas cooling and circulating device in partial section.    Barrel body (1)    Circulation pipes (2)    Overflow pipe (4)    Upper sealer (5)    Water inlet pipe (7)    Lower sealer (8)    Valve (9)    Oil drain tank (10)    Lower sealing barrel (12)
NOVELTY - The invention claims a preparation method of 4-hydroxy-6-decyloxy-7-ethoxy-3-decoquinate lactone which comprises following steps that A. preparing the pyrocatechol diethyl ether, B. preparing 3,4-diethoxyethylcyanide nitrobenzene, C. 2-ethoxy-4-nitrophenol, D. preparing 3-ethoxy-4-decyloxynitrobenzene, E. preparing 3-ethoxy-4-decyloxy aniline, F. preparing N-methylene demethyl malonate diethyl 3-ethoxy-4-decyloxy aniline, G. preparing 4-hydroxy-6-decyloxy-7-ethoxy-3-decoquinate lactone. There are some advantages; firstly the raw material of every step can be bought on market easily; secondly the reaction condition is relatively temperate with simply technology; thirdly each reaction in every step is operated commonly and relevant reaction orders are like this substitution reaction, hydrolyzing reaction, condensation reaction which are easy to control, without complicated equipments; besides, during the whole process, nothing has been wasted so as to avoid some serious demands of reaction condition and equipment and pollution to the environment by the used nitrite and acid.    USE - Used as anticoccidial drugs.    ADVANTAGE - There are some advantages; firstly the raw material of every step can be bought on market easily; secondly the reaction condition is relatively temperate with simply technology; thirdly each reaction in every step is operated commonly and relevant reaction orders are like this substitution reaction, hydrolyzing reaction, condensation reaction which are easy to control, without complicated equipments; besides, during the whole process, nothing has been wasted so as to avoid some serious demands of reaction condition and equipment and pollution to the environment by the used nitrite and acid.
NOVELTY - A sludge-disposal agent contains microorganisms group containing Sphingobacterium genus microbe, Pedobacter genus microbe, Ureibachillus genus microbe, and Lysobacter genus microbe.    USE - A sludge-disposal agent.    ADVANTAGE - The agent can decompose sludge simply, inexpensively and efficiently.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a processing method of sludge; and    (2) a recycling water.
NOVELTY - An equipment and a method for dehulling jatropha seeds are disclosed which consists mainly of feed hopper, impeller assembly, drive mechanism, discharge chute, supporting frame, screen grader and air classifier. The equipment and method for dehulling jatropha seeds help in the maximum recovery of oil of superior quality which is used for production of biodiesel. The equipment works on the principle of impacting the seed at high centrifugal force on a hard stationary surface to break the hull and subsequently generating shear force to separate the hull from the seed. The method of dehulling of jatropha seeds is provided to obtain the maximum dehulling efficiency, the minimum broken percentage and the maximum dehulling index with respect to different impeller speeds of the equipment. Image 1/1
NOVELTY - Preparing a catalyst comprises: (i) preparing a calcined shaped calcium aluminate catalyst support, (ii) treating the calcined shaped calcium aluminate support with water, and then drying the support, (iii) impregnating the dried support with a solution containing one or more metal compounds and drying the impregnated support, (iv) calcining the dried impregnated support, to form metal oxide on the surface of the support and (v) optionally repeating steps (ii), (iii) and (iv) on the metal oxide coated support.    USE - The catalysts are useful for methanation reactions, and steam reforming processes (all claimed) such as primary steam reforming, secondary reforming of a primary reformed gas mixture and pre-reforming. The catalysts are useful for hydrogenation reactions and, in oxidic unreduced form, for the decomposition of hypochlorite in aqueous solutions.    ADVANTAGE - The catalytic metal oxide is concentrated at the surface of the support to achieve improved catalytic activity with reduced metal loadings.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) an eggshell catalyst material obtainable by the method;    (2) steam reforming of a hydrocarbon comprising contacting a mixture of hydrocarbon and steam at elevated temperature and pressure with the catalyst; and    (3) methanation of a hydrogen gas stream containing carbon monoxide and carbon dioxide in amounts of 0.1-0.5 vol.% comprising the step of contacting the hydrogen gas stream at a temperature of 230-450 degrees C with the catalyst.
NOVELTY - Producing carbohydrate degradation products, comprises (a) treating lignocellulosic material with an aqueous solution containing hydrogen peroxide, an alcohol, preferably a 1-4C alcohol or a phenol and a base to oxidatively cleave lignocellulose and to separate the degradation products from the material to obtain a material enriched with cellulose and hemicellulose; and (b) treating the cellulose and hemicellulose enriched material with a carbohydrate-cleaving enzyme to obtain the carbohydrate degradation products.    USE - The method is useful for producing carbohydrate degradation products.    ADVANTAGE - The method: provides higher yields of carbohydrate degradation products at a reaction temperature below 100 degrees C; and has high selectivity of lignin degradation at low energy consumption.
NOVELTY - An activated sludge tank comprises calcium carbonate which is thrown in tank. The tank nitrifies and denitrifies organic substance and nitrogen within one tank.    USE - An activated sludge tank used for activated sludge process equipment used for gasification gas-purification apparatus (claimed).    ADVANTAGE - The tank activates activated sludge easily and reliably.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) an activated sludge process equipment;    (2) a gasification gas-purification apparatus; and    (3) an activated-sludge processing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of activated sludge process equipment and activated sludge tank. (Drawing includes non-English language text).    Primary sedimentation basin (9)    Coagulation-sedimentation tank (10)    Ammonia stripping (11)    Activated sludge tank (12)    Final sedimentation tank (13)
NOVELTY - Carbonization furnace comprises furnace main body (1) with ignition opening (2) and air supply port (3), center heat radiation pipe (5) with exhaust gas introduction hole, lid (4) which opens and closes the material entrance and exit of furnace main body, exhaust gas recovery cylinder in the center heat radiation pipe, periphery hollow heat sink, and insulating plate which prevents introduction of combustion gas in the heat radiation pipe.    USE - Carbonization furnace for organic raw materials such as ground material of timber or bamboo material.    ADVANTAGE - Has high combustion efficiency for a short time, simple, has high thermal efficiency and produces carbonized material with no non-uniformity.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the carbonization furnace.    Furnace main body (1)    Ignition opening (2)    Air supply port (3)    Lid (4)    Center heat radiation pipe (5)
NOVELTY - The apparatus (100) has positioning apparatus (40) that arranges gas diffusion layers (G) on membrane electrode assembly (MEA) (10). A hot press apparatus (20) presses the gas diffusion layers arranged on MEA for preset time. The gas diffusion layer and MEA are joined by moving press apparatus synchronizing with conveyance speed of MEA.    USE - Manufacturing apparatus of fuel cell.    ADVANTAGE - Joining of MEA and gas diffusion layer can be performed rapidly during manufacture of fuel cell, so that productivity of fuel cell can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing method of fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fuel cell manufacturing apparatus. (Drawing includes non-English language text)    MEA (10)    Hot press apparatus (20)    Positioning apparatus (40)    Fuel cell manufacturing apparatus (100)    Gas diffusion layer (G)
NOVELTY - The system (1) has a crusher (2) for crushing a plant seed. A briquette shaping pipe (3) receives the plant seed crushed by the crusher. A squeezer (4) squeezes the crushed seed received in briquette shaping pipe and presses vegetable oil at the bottom of briquette shaping pipe by squeezing the crushed seed. Several briquette shaping pipes are arranged in circular shape and rotated to a direction to accept the insertion portion (9) of the squeezer.    USE - System for extraction of plant seed such as jatropha, soybean, rapessed, maize, sesame seed, cottonseed, rice, sunflower, grape, etc for manufacture of briquette.    ADVANTAGE - The extraction of plant seed and the manufacture of briquette can be performed simultaneously.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for extraction and briquette manufacturing method of vegetable oil, involves conveying plant seed crushed by a crusher to briquette shaping pipe. The briquette is shaped at the time of squeezing the crushed plant seed in briquette shaping pipe to press the vegetable oil.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the extraction and briquette manufacturing system.    Extraction and briquette manufacturing system (1)    Crusher (2)    Briquette shaping pipe (3)    Squeezer (4)    Insertion portion (9)
NOVELTY - Operating a biogas plant, comprises converting a substrate into a fermenter under the participation of bacteria to produce a biogas, which contains methane, where: the substrate is maintained at a pH value of greater than 6; additives such as carbon dioxide, bicarbonate ion or carbonate ion, serving as a carbon dioxide supplier, is added to the substrate in finely divided form; and the addition of the additives is carried out continuously.    USE - The method is useful for operating the biogas plant for producing methane.    ADVANTAGE - The method increases the efficiency of the biogas plant in an ecological manner thus increasing the production of methane with high yield.
NOVELTY - A device (100) comprises a feeding area (104) for receiving a moving bed from biomass (102), preferably wood, having an upper segment (140) for drying, a middle segment (142) and a flame zone for degassing. A lower segment (146), a smoldering zone for carbonizing the biomass into a solid converted product (158), particularly charcoal, are also provided. A grate (110) for supporting the moving bed and permeable downward for the solid converted product is included in the device. A collection tank (136) for collecting the solid converted product is disposed below the grate.    USE - Device used in a system for continually converting biomass, preferably wood chips into charcoal (all claimed).    ADVANTAGE - The device ensures simple construction and improved working efficiency.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a method for continually converting biomass, which involves supplying moving bed from biomass, preferably wood, in a feeding area, where the moving bed is dried in an upper portion of the feeding area; and    (2) a system, which comprises the device, a biogas plant and/or a combined heat and power plant, where a liquid converted product from converting of biomass, particularly pyroligneous acid or acetic acid, is fed to the biogas plant.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic longitudinal sectional view of a device.    Device (100)    Biomass (102)    Feeding area (104)    Grate (110)    Collection tank (136)    Upper segment (140)    Middle segment (142)    Lower segment (146)    Solid converted product (158)
NOVELTY - Preparing an ammonia borane compound selected from ammonia borane, ammonia alkyl borane and/or ammonia aryl borane involves: a) incorporating a reaction mixture into a pressure vessel, where the reaction mixture comprises anhydrous liquid ammonia and a boron containing compound that can react under pressure with the liquid ammonia to form the ammonia borane compound; and, b) causing the reaction mixture to warm from a first temperature of greater than or equal to -33 degrees C to a second temperature under pressure to form the ammonia borane compound.    USE - For preparing an ammonia borane compound (claimed), which is used as a key component in hydrogen storage fuels.    ADVANTAGE - The reaction of diborane or a Lewis base adduct of borane and liquid ammonia at elevated temperatures, either with or without added ether solvent, results in the high yield formation of ammonium borohydrate (NH3BH3) with minimal formation of the diammoniate of diborane contaminant.
NOVELTY - Preparing waste fry fuel, involves deep frying cut down branch, bamboo branch, pruned branch, house demolition wood chip, perennials such as bamboo grass, pampas grass, mugwort and Japanese knotweed, straw, bean husk, old newspapers and corrugated cardboard with used oil for deep frying.    USE - The method is useful for preparing waste fry fuel.    ADVANTAGE - The waste fry fuel is prepared by utilizing scrap that is usually thrown without utility value, and thus reduces environmental pollution.
NOVELTY - A photoelectric cell consists of a cell filled with an alkaline solution containing lignin and porphyrin as solute in a space formed by a transparent component in which at least one portion transmits light, and a pair of electrodes (2,4) mutually opposed and provided in a state contacting the alkaline solution of the cell.    USE - Photoelectric cell e.g. solar cell is used for producing hydrogen ions used as fuel in fuel cells.    ADVANTAGE - The photoelectric cell efficiently separates hydrogen ions which provide electromotive force to a fuel cell, from lignin. Electrical potential difference is generated just by irradiating light, such as sunlight and UV ray, to mixture of lignin and porphyrin. Natural energy, such as solar energy, is exploited from lignin which is a non-fossil fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows an exploded perspective view of the photoelectric cell.    Front component (1)    Electrodes (2,4)    Spacer (3)    Film (5)    Back component (11)
NOVELTY - A packaged hydrogen-producing agent is provided with a covering material (2) which constrains the surroundings of hydrogen-producing agent (1) and permits a deformation.    USE - Packaged agent is used for hydrogen production (claimed) in fuel cells.    ADVANTAGE - The packaged agent enables stable and repeated hydrogen production, is resistant to influence from changes in the environmental temperature, and simplifies the structure of hydrogen-production apparatus.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of packaged hydrogen-producing agent; and    (2) hydrogen-production method.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the packaged hydrogen-producing agent.    Hydrogen-producing agent (1)    Covering material (2)    Water-absorption component (3)    Contact portion (3a)    Extension portion (3b)
NOVELTY - A biogas is passed through a low pressure inlet of a positive displacement device having high pressure outlet. The biogas from inlet is passed into apparatus located between low pressure and high pressure sides of positive displacement device. A gas eductor is coupled to the apparatus, and air is added to biogas through gas eductor. The biogas is compressed and passed through high pressure outlet to digester vessel. Thus, hydrogen sulfide in biogas is reduced.    USE - Method for reducing hydrogen sulfide in biogas.    ADVANTAGE - The amount of hydrogen sulfide in biogas is efficiently reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus for reducing hydrogen sulfide in biogas.    DESCRIPTION OF DRAWING(S) - The drawing shows the flowchart of waste processing system and system for reducing hydrogen sulfide.    Waste processing system (10)    Biogas storage (59)    Turbine and electric generator (139)    Power company (332)    Hydrogen sulfide reduction system (400)
NOVELTY - A composition comprises an ionic liquid and a thermostable cellulase.    USE - For hydrolyzing cellulose; in the host cell (claimed); for converting of the carbohydrates of lignocellulose to sugars; and for converting lignocellulosic biomass to sugars for the production of bio fuels.    ADVANTAGE - The composition converts the carbohydrates of lignocellulose to sugars with improved yield and rate of sugar production; and improves the efficiency (in terms of yield and reaction rates) of saccharification of cellulose.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for following:    (1) hydrolyzing a cellulose, involving providing a solution comprising an ionic liquid and a cellulose, and introducing a thermostable cellulase to the solution, such that the cellulose is hydrolyzed by the cellulose;    (2) new Thermatoga maritima thermostable cellulase mutant with increased cellulase activity, where the thermostable cellulase mutant comprises an amino acid sequence having at least 70% identity as compared to the amino acid sequence of Tma Ce15A;    (3) a nucleic acid encoding a Thermatoga maritima thermostable cellulase mutant;    (4) a host cell comprising the nucleic acid; and    (5) producing a thermostable cellulase mutant involving providing a host cell capable of expressing the thermostable cellulase mutant, culturing the host cell in a culture medium under conditions to form thermostable cellulase mutant.
NOVELTY - Fine solid solution alloy particles are mixed with several metallic elements at atomic state.    USE - Fine solid solution alloy particles are used as catalyst for organic synthesis, electrode catalyst for fuel cell, and catalyst for reducing nitrogen dioxide.    ADVANTAGE - The fine solid solution alloy particles have excellent hydrogen storage characteristics.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of fine solid solution alloy particles.
NOVELTY - Generating algal biomass, involves forming algal culture by combining population of algal cells and culture medium comprising industry wastewater, optionally municipal sewage effluent, and nutritional supplement comprising organic carbon source for supporting proliferation of mixotrophic algal species, mineral, buffer or their combination, and maintaining the algal culture for the proliferation of population of algal cells.    USE - The method is useful for generating an algal biomass for producing a biofuel from industrial wastewater (both claimed).    ADVANTAGE - The 65% of algal oil obtained from the algal consortium cultured on industry wastewater could be converted into biodiesel. The method is environment-friendly with no secondary pollution.    DETAILED DESCRIPTION - Method for generating algal biomass, involves (a) forming an algal culture by combining (i) population of algal cells distinguished as proliferating in a culture medium comprising an industry wastewater, and (ii) culture medium comprising an industry wastewater, optionally municipal sewage effluent, and nutritional supplement, where the nutritional supplement increases the yield of algal culture compared to the culture medium which does not comprise the nutritional supplement, and (b) maintaining the algal culture for the proliferation of population of algal cells. The nutritional supplement comprises an organic carbon source for supporting the proliferation of mixotrophic algal species, mineral, buffer or their combination. An INDEPENDENT CLAIM is included for method for producing a biofuel from industrial wastewater.
NOVELTY - Catalytic system comprises at least one metal oxide or metalloid oxide and having a specific combined meso and macro surface area of 1-100 m2/g.    USE - The catalytic system is useful in catalytic pyrolysis of solid biomass material (claimed).    ADVANTAGE - The catalyst system provides: production of liquid pyrolysis products with increased oil yield and low oxygen content; and a low coke yield. The catalyst system is available in low cost.
NOVELTY - A selective methanation catalyst (GG) of carbon monoxide contains a composite oxide precursor having nickel and aluminum in non-stoichiometric ratio, as support. The metallic nickel particles are precipitated on support surface of precursor. The catalyst removes carbon monoxide from hydrogen rich gas containing carbon monoxide and carbon dioxide, as methane.    USE - Selective methanation catalyst of carbon monoxide for hydrogen purifier used in polymer electrolyte fuel cell (claimed).    ADVANTAGE - The selective methanation catalyst economically enables removal of carbon monoxide without externally adding a special reactant gas.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of selective methanation catalyst, which involves heating the complex oxide precursor at 200-700 degrees C in reducing gas atmosphere, and depositing metallic nickel particles on the surface of precursor; and    (2) hydrogen purifier, which is mounted with the selective methanation catalyst.    DESCRIPTION OF DRAWING(S) - The drawing shows the flowchart of hydrogen production system. (Drawing includes non-English language text)    Raw material fuel (AA)    Desulfurizer (BB)    Reforming catalyst (CC)    Cooling water (FF)    Co-selective methanation catalyst (GG)
NOVELTY - A self-maintaining methane fermentation pool temperature-control system comprises a single chip computer for collecting temperature and pressure signal of methane pool, a circulation water pipeline connected to the methane pool, a heating resistance wire, and an electromagnetic valve. Part of circulation water pipeline exposed on methane pool is heated by the heating resistance wire. The electromagnetic valve is located at the opening of methane pool and automatically ignites based on pressure in the methane pool to heat the circulation water pipeline.    USE - Self-maintaining temperature-control system used for methane fermentation pool.    ADVANTAGE - Methane generated by combustion is used for heating the fermentation pool to maintain temperature of pool main body at 30 degrees C, thus, methane pool can maintain high methane production rate in winter, solving the problem of energy use in the winter of rural area.
NOVELTY - The furnace has furnace top (2) whose top part is equipped with a feeding port (4) and bottom part is connected with a furnace body (3). A water jacket (10) is located between the furnace body and a hearth (17), where the furnace body is internally equipped with multiple water pipes (13) connected with the water jacket. A fire grate (11) is formed on each water pipe. An air vent (12) is connected with the hearth, and the furnace body is equipped with an ash discharge port (15).    USE - Straw gasification generation furnace.    ADVANTAGE - The furnace has low heat loss and better gasification effect. The water pipes are located below the fire grate for supporting the water pipes and preventing the water pipes from deformation. The fire grate can be protected from being deformed, thus prolonging service life of the fire grate.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial sectional view of a straw gasification generation furnace.    Furnace top (2)    Furnace body (3)    Feeding port (4)    Water jacket (10)    Fire grate (11)    Air vent (12)    Water pipes (13)    Ash discharge port (15)    Hearth (17)
NOVELTY - An impurity concentration apparatus (20) has an electrochemical hydrogen pump formed by laminating several cells (22A,22B), a distribution unit for distributing hydrogen gas supplied to hydrogen pump to anode flow path of each cell, a manifold (26) connecting exit of anode flow path of each cell, and an exhausting unit connected to manifold. The cells (22B) are low-pressure loss cells, in which pressure loss in anode flow path is less than other cell.    USE - Impurity concentration apparatus is used for concentrating impurities contained in hydrogen gas used as fuel in fuel cell.    ADVANTAGE - The difference of concentration rate of impurities between cells is relieved.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of impurity concentration apparatus.    Impurity concentration apparatus (20)    High pressure cell (22A)    Low pressure cell (22B)    Exhaust valve (24)    Outlet manifold (26)    Power supply (28)    Impurity concentration region (40)
NOVELTY - A distribution unit distributes hydrogen gas supplied to an electrochemical hydrogen pump, with respect to an anode channel of each fuel cell. A measuring unit measures the dispersion (Vd1) of voltage applied between the fuel cells. A control unit starts the discharge process of impurity contained in hydrogen gas, at predetermined timing and adjusts the execution time of discharge process according to immediate dispersion in the applied voltage.    USE - Impurity concentration apparatus of hydrogen gas used in fuel cell system.    ADVANTAGE - The accumulation of impurity in the fuel cells can be prevented reliably, and the collected impurity can be discharged out completely.    DESCRIPTION OF DRAWING(S) - The drawing shows a timing chart explaining the discharge control process carried out in impurity concentration apparatus. (Drawing includes non-English language text)    Voltage dispersion values (Vd1-Vd3)
NOVELTY - A generating station (24) receives energy source such as wind/solar source and converts it to electricity. An electrolysis station (28) powered by electricity (26) produces and dispenses hydrogen (30). A water supply and distribution station provides water (38) to electrolysis station. A hydrogen distribution system in communication with stations receives hydrogen and water. A separator and delivery system in communication with hydrogen distribution system depressurizes, extracts and delivers hydrogen dissolved in water for use as fuel in location apart from electrolysis station.    USE - Hydrogen-based energy system for generating electricity in electric-utility industries.    ADVANTAGE - The adverse environmental impacts from the use of fossil fuels to generate electricity is reduced, energy losses, thermal pollution, and risk of outages inherent in the existing generating and grid structures is minimized by using hydrogen as the fuel. The vertical-axis radial-flow turbine of the oscillating water column generator can simultaneously extract additional mechanical energy from the energy in wind.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method of using mass distribution hydrogen energy system;    (2) vertical-axis radial-flow turbine system;    (3) system for extracting mechanical energy from wave energy; and    (4) method of extracting mechanical energy from wave energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the hydrogen-based energy system.    Generating station (24)    Electricity (26)    Electrolysis station (28)    Hydrogen (30)    Water (38)
NOVELTY - A fuel tank (1) stores the fuel. A filling port (10) supplies fuel to fuel tank. A defective fuel detection unit (8) detects whether the fuel supplied between the filling port and fuel tank is defective. An electronic control unit (100) receives signal output from defective fuel detection unit and operates the alarm lamp (87) according to received signal.    USE - Fuel storage system mounted in fuel-cell vehicle.    ADVANTAGE - The failure of fuel cell due to the supply of defective fuel to fuel cell can be prevented reliably. The structure of fuel storage system is simplified so that manufacturing cost of fuel storage system can be reduced. The reliability of fuel cell vehicle can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fuel storage system. (Drawing includes non-English language text)    Fuel tank (1)    Defective fuel detection unit (8)    Filling port (10)    Alarm lamp (87)    Electronic control unit (100)
NOVELTY - Oxidizing carbon monoxide (CO) and volatile organic compounds (VOCs) comprises contacting a gas containing water vapor, CO and VOCs with a catalyst composition comprising at least one base metal promoter and at least one base metal catalyst supported on an oxide support material comprising one or more alumina, silica, zirconia, ceria and titania, where the VOCs comprises one or more of methyl acetate, methane, methyl bromide, benzene, methanol, methyl ethyl ketone, butane and butene.    USE - The method is useful for oxidizing carbon monoxide and volatile organic compounds.    ADVANTAGE - The catalyst composition: is free of platinum group metals; has good catalytic activity, superior durability and longevity. The nickel based catalyst maintains good activity in converting methyl bromide and benzene.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the catalyst composition for the oxidation of CO and VOC.
NOVELTY - Pesticide comprises (in parts by weight): calcium hydroxide (5-12), starch (8-10), carboxymethyl cellulose (1-2), polyvinyl alcohol (1-2), humic acid (2-4), organosilicon (0.1-0.5), 1,3-butanediol (0-1), ethanol (0-1), 4-(2-methyl-4-chlorophenoxy) butyric acid (0-1), buffer (0-1), preservative (0-1) and ethephon (0-1).    USE - The pesticide useful for preventing jujube black-top disease.    ADVANTAGE - The pesticide: can be used repetitively; is free of resistance, safe and non-poisonous; is stored for long duration without degenerating; has good solubility; is compatible and can be mixed with several medicaments, thus expressing adhered synergy and controlling the release and synergic gaining function; decomposes into an organic matter within 30-50 days and hence does not pollute the environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for the application of the pesticide comprising: adding starch, polyvinyl alcohol, humic acid, organosilicon, 1,3-butanediol, carboxymethyl cellulose, ethanol, 4-(2-methyl-4-chlorophenoxy) butyric acid, buffer, preservative and ethephon into water (4-5 times the total weight of the components) at 12-35 degrees C; stirring; heating at 85-95 degrees C for accelerating the dissolving rate; maintaining the temperature for 2-2.5 hours; filtering the impurities through 28 mesh sieve; and adding calcium hydroxide and stirring uniformly.
NOVELTY - A bi-phase anaerobic fermentation method for preparing biogas with oil-extracted algae residue comprises: (a) performing thermokalite pretreatment on oil extracted algae residue; (b) carrying out a first-phase anaerobic hydrogen-generating fermentation on the pre-treated oil extracted algae residue; and (c) carrying out a second-phase anaerobic methane-generating fermentation on fermentation solution after the first-phase anaerobic hydrogen generating fermentation.    USE - The bi-phase anaerobic fermentation method is useful for preparing biogas with oil-extracted algae residue (claimed).    ADVANTAGE - The bi-phase anaerobic fermentation method greatly improves energy utilization rate of oil extracted algae residue. Moreover, it has social and economic benefits.    DETAILED DESCRIPTION - A bi-phase anaerobic fermentation method for preparing biogas with oil-extracted algae residue comprises: (a) performing thermokalite pretreatment on oil extracted algae residue; (b) carrying out a first-phase anaerobic hydrogen-generating fermentation on the pre-treated oil extracted algae residue; where the inoculation material is thermally treated anaerobic digestion sludge; the starting pH value of the first-phase anaerobic hydrogen generating fermentation is 6.0-6.5; and the fermentation temperature is 30-37 degrees C; and (c) carrying out a second-phase anaerobic methane-generating fermentation on fermentation solution after the first-phase anaerobic hydrogen generating fermentation; where the inoculation material is thermally treated anaerobic digestion sludge; the starting pH value of the second-phase anaerobic hydrogen generating fermentation is 7.0-8.0; and the fermentation temperature is 30-37 degrees C.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of the bi-phase anaerobic fermentation method for preparing biogas with oil-extracted algae residue (Drawing includes non-English language text).
NOVELTY - Fuel cell (100) comprises hydrogen generating system (110) comprising an organic polymer material in combination with beta particle emitting material selected from 35S, 45Ca and 63Ni; and membrane electrode assembly (130) in communication with hydrogen generating system. The fuel cell further comprises dispersed oxygen scavenging material.    USE - For storing and generating hydrogen to convert chemical energy into electrical energy.    ADVANTAGE - The system is extremely reliable since there are no moving parts or device control schemes used. The system constructed as polymer film provides for inexpensive and flexible processing. The system is scalable to small sizes that can be employed for on-chip applications where the energy density of batteries is extremely poor. By separating irradiated material from active electrochemical generating material, degradation of the electrical generating capacity with time is prevented. By using beta particles to degrade organic polymer material pure hydrogen is released. No valving of reactants, tubing, reformars or high storage device is required, thus resulting in lower system volume than prior art fuel cell systems. The device is only moderately affected by temperature; the radiation source is unaffected by temperature. The materials are not particularly toxic or volatile compared to currently available hydrogen generation systems.    DESCRIPTION OF DRAWING(S) - The figure shows schematic drawing of fuel cell.    Fuel cell (100)    Hydrogen generator (110)    Membrane electrode assembly (130)    Electrodes (135, 140)
NOVELTY - A fat and oil containing waste water is processed by decomposing fats and oils using lipase secretion microorganisms which can decompose fats and oils and increases on weakly acidic conditions.    USE - Processing of fat and oil containing waste water used for cleaning of grease-trap (claimed).    ADVANTAGE - The method processes high concentration of fat and oil containing waste water efficiently and effectively.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a grease-trap cleaning method; and    (2) a fat splitting agent.
NOVELTY - A microorganism belonging to genus Raoultella and capable of producing ethanol from glycerol, is new.    USE - The microorganism and wastewater treatment apparatus are useful for treating wastewater containing glycerol for producing ethanol and hydrogen, which are used as biofuel (all claimed).    ADVANTAGE - The ethanol and hydrogen are produced simultaneously in high quantity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) treating wastewater containing glycerol, involves contacting wastewater containing glycerol with the above-mentioned microorganism and recovering ethanol; and    (2) wastewater treatment apparatus for treating wastewater, for producing and recovering hydrogen and ethanol.
NOVELTY - An organic waste is supplied to methane-fermentation tank (1) by arranging a support for microorganisms capture (12) formed by molding a fibrous material to sheet form in fixed position. The methane fermentation of organic waste is carried out by anaerobic microbe, and by arranging support for foreign material capture formed by molding fibrous material to sheet form, in feed route of organic waste of the methane-fermentation tank. The organic waste is contacted with support for foreign material capture, and then supplied to methane-fermentation tank.    USE - Methane fermentation of organic waste.    ADVANTAGE - The method enables stable methane fermentation of organic waste. The clogging of support for microorganism capture in the methane-fermentation tank is suppressed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus for methane fermentation of organic waste.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the methane-fermentation tank.    Methane-fermentation tank (1)    Draft tube (11)    Support for microorganism capture (12)    Support materials (13a,13b)    Pipings (L4-L7)
NOVELTY - Methane fermentation of organic waste is carried out using a methane fermentation treating apparatus having methane fermentation tank (1) for methane fermentation of waste and producing biogas, a boiler (3) for circulating hot water such that fermented liquor temperature in tank (1) is set to predetermined value, and a biogas utilization apparatus (5) for utilizing biogas discharged to upper portion of tank (1). Bubble generated on liquid level of tank (1) is heated and defoamed, with heated fluid by exhaust heat of hot water from boiler and/or apparatus (5).    USE - Methane fermentation of organic waste.    ADVANTAGE - The methane fermentation of organic waste is stably, economically and efficiently enabled for long period of time using simple apparatus.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for methane fermentation treatment apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic block diagram of methane fermentation apparatus. (Drawing includes non-English language text)    Methane fermentation tank (1)    Boiler (3)    Biogas utilization apparatus (5)    Support (10)    Hot water line (L3)
NOVELTY - Obtaining biocombustible products involves performing thermal cracking of residual organic matter in a reactor, which contains a section for receiving the raw materials (2). A positive displacement pump is provided for transporting the material. A heat exchanger is provided for heating the residual organic matter. A circulating bed reactor (3) is provided for performing thermal cracking of residual organic matter. A heating chamber (4) is present in the reactor for heating residual organic matter at 7000 degrees C.    USE - Method for obtaining biocombustible products i.e. fuel and biofuel.    ADVANTAGE - The method enables continuous production of biocombustible products.    DETAILED DESCRIPTION - Obtaining biocombustible products involves performing thermal cracking of residual organic matter in a reactor, which contains a section for receiving the raw materials (2). A positive displacement pump is provided for transporting the material. A heat exchanger is provided for heating the residual organic matter. A circulating bed reactor (3) is provided for performing thermal cracking of residual organic matter. A heating chamber (4) is present in the reactor for heating residual organic matter at 7000 degrees C. A transporter (8) is also provided for transporting the materials into the heating chamber. A combustion chamber (6) and a tank (7) are also present in the reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of biocombustible products production method.    Raw materials (2)    Circulating bed reactor (3)    Heating chamber (4)    Combustion chamber (6)    Tank (7)    Transporter (8)
NOVELTY - The method involves selecting materials such as livestock manure and straw, removing impurities, and regulating water content of the materials to be 65 to 70 percentages. The materials are uniformly stirred and conveyed to a solar greenhouse fermentation plant. Fermenting temperature is controlled at 55-65 degrees centigrade, and a decomposed fertilizer is checked. The fermented material is sent to the pelletizing plant, dried till water content is not more than 20 percentages, polished, selected, metered and packed. The finished product is sent to a storehouse.    USE - Efficient fast stepped fermentation method for an organic biological fertilizer.    ADVANTAGE - The method can be applied to continuous production of the organic biological fertilizer.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating an efficient fast stepped fermentation method for an organic biological fertilizer. '(Drawing includes non-English language text)'
NOVELTY - A mud removing device connected with a reactor comprises a control system, a flushing pump, a water body main input passage, a water body distributor, a water body output pipeline, and a gate valve; where the control system is connected with the flushing pump, the gate valve and the check valve via electrical signal; the water body distributor is located in the middle under the reactor; the flushing pump is connected with the upper part of the reactor; and the flushing pump is connected with the water body distributor via the water body main output pipeline.    USE - The mud removing device connected with a reactor is useful for mud removing in sewage gas engineering.    ADVANTAGE - The mud removing device solves the defect that the current device cannot completely and smoothly remove mud with poor effect. Moreover, it can increase production rate and gas rate of anaerobic reaction device.    DETAILED DESCRIPTION - A mud removing device connected with a reactor comprises a control system, a flushing pump, a water body main input passage, a water body distributor, a water body output pipeline, and a gate valve; where the control system is connected with the flushing pump, the gate valve and the check valve via electrical signal; the water body distributor is located in the middle under the reactor; the flushing pump is connected with the upper part of the reactor via the water body main input pipeline; the flushing pump is connected with the water body distributor via the water body main output pipeline; the gate valve is located on the pipeline of the flushing pump inlet or outlet; and the water body branch output pipeline is connected with the water body distributor.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the mud removing device connected with a reactor.
NOVELTY - Producing biomass fuel, comprises crushing the biomass and coal powder, adding diatomite and mixing, controlling temperature of drying hot air to control humidity of the mixed powder to obtain humidity of 10-20% which is easy for producing and conveying to a forming device to obtain granules.    USE - The method is useful for producing biomass fuel.    ADVANTAGE - The fuel prepared by the biomass fully uses wastes of straw, sawdust, bush and weeds, reduces needs of non-renewable energy resource e.g. coal and natural gas, improves environment pollution caused by firing, and the calorific value is stable, and there is no alkali corrosion, the ignition is fast, the combustion efficiency is high, the volume heat load of the boiler and the hearth temperature are improved, the boiler heat efficiency is improved. The method can be applied to biomass combustion power generation to solve the problem that the current of biomass power generation cannot be continuously and stably operated due to insufficient biomass.
NOVELTY - An automatic control system for biogas engineering comprises a fermentation material system, a temperature-increasing/limiting system, a methane processing system, a central processing system, an agitating and feeding control system, a temperature-increasing/limiting control system, a methane processing control system, and a display system; where the temperature-increasing/limiting system and the methane processing system are respectively connected with the fermentation material system; and the agitating and feeding control system is mounted in the fermentation material system.    USE - The automatic control system is useful for biogas engineering (claimed).    ADVANTAGE - The automatic control system is simple in structure, rational in design, and easy to popularize.    DETAILED DESCRIPTION - An automatic control system for biogas engineering comprises a fermentation material system, a temperature-increasing/limiting system, a methane processing system, a central processing system, an agitating and feeding control system, a temperature-increasing/limiting control system, a methane processing control system, and a display system; where the temperature-increasing/limiting system and the methane processing system are respectively connected with the fermentation material system; the agitating and feeding control system is mounted in the fermentation material system; the temperature-increasing/limiting control system is mounted on the temperature-increasing/limiting system; the methane processing control system is installed on the methane processing system; and the agitating and feeding control system, the temperature-increasing/limiting control system, and the methane processing control system are connected to the central processing system and the display system via electronic circuits.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the automatic control system for biogas engineering.
NOVELTY - Coal production uses organic waste, Cocos nucifera, mineral fertilizers, fertilizers, bio-fertilizers, remedial agent, soil enhancers and compost. The production process includes steps such as waste collection, deposition of wastes in rural areas, industry or in specific locations, and transportation of the waste collected by cores of carbonization, where carbonization is performed at controlled atmosphere, presence of free oxygen and suitable temperature. The waste is ground in order to obtain coal with physical characteristics resemble with organic fertilizers.    USE - Method for producing coal used for preparing and enrichment of organic fertilizers and for promoting carbon sequestration (claimed).    ADVANTAGE - The coal producing method is eco-friendly process, has commercialization and industrialization features and utilizes organic wastes.    DETAILED DESCRIPTION - Coal production uses organic waste, Cocos nucifera, mineral fertilizers, fertilizers, bio-fertilizers, remedial agent, soil enhancers and compost. The production process includes steps such as waste collection, deposition of wastes in rural areas, industry or in specific locations, and transportation of the waste collected by cores of carbonization, where carbonization is performed at controlled atmosphere, presence of free oxygen and suitable temperature. The waste is ground in order to obtain coal with physical characteristics resemble with organic fertilizers, mineral fertilizers, fertilizers, bio-fertilizers, remedial agent, soil improvers and compost. The crushed charcoal is stored and ground into organic fertilizers to produce coal or fertilizer at manufacturing site, where fertilizer has nutritional value. The product is transported and applied to agricultural areas.
NOVELTY - Defoaming organism aerobic large-scale culture, which is an active defoaming method distinguished from defoaming agent and defoaming device, comprises backflowing partial mixed solution to the reaction material to form false continuous run; and suppressing the production of the foams by a source.    USE - The method is for defoaming organism aerobic large-scale culture, which is an active defoaming method distinguished from defoaming agent and defoaming device (claimed). It is useful for removing the foam produced during sludge large-scale aerobic culturing process in wastewater biological treatment field and aerobic large-scale fermentation process in biological fermentation field.    ADVANTAGE - Defoaming agent or defoaming device is not needed for the method, so that pollution of defoaming agent to the culture liquid is avoided. There is no need to reform the original material structure so that the investment cost is saved to the largest extent. Low running cost in the actual operation is achieved.
NOVELTY - White solid incense comprises (in wt.%): sludge carbon powder (60-80), charcoal powder (0-7), potassium nitrate (10-16.3), starch (10-20) or carboxymethyl cellulose (2.3-3.7) and mugwort leaf (0-5.7).    USE - White solid incense used as mosquito repellent (claimed).    ADVANTAGE - The white solid incense is smokeless and eco-friendly, and uses resource materials with reducing disafforestation for incense manufacturing industries.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing white solid incense, which involves:    (A) grinding sludge carbon that is obtained after pyrolysis and screening process of sludge;    (B) dissolving combustion improver and binder in water with agitating the mixture uniformly;    (C) mixing carbon powder with combustion improver-binder mixture with agitating the mixture to obtain paste;    (D) placing the paste in mold to press compactly and then de-molding; and    (E) drying the mold to obtain white incense solid.
NOVELTY - Agrochemical smoke composition comprises (in wt.5): azoxystrobin (5-10), prochloraz (10-20) and triazole (15-30) in the ratio of 1:2:3.    USE - Agrochemical smoke composition used for preventing and treating disease on rubber tree, particularly anthracnose and powdery mildew (claimed).    ADVANTAGE - The agrochemical smoke composition is eco-friendly and not affected by terrain, trunk and water source, produces dense fog with uniform distribution and strong osmotic force, reduces drug resistance on the anthracnose and powdery mildew, and has efficient broad spectrum and low toxicity on the human and poultry.
NOVELTY - Sewage processing method through granular sludge aerobic denitrification, comprises pumping wastewater containing nitrate nitrogen into continuous-batch bioreactor; adding phosphorus and trace elements to the wastewater to maintain normal growth of microbe; providing an aerating apparatus at the bottom of the reactor, where air ascending speed is 43.2-90 m/hour, and then precipitating for 1-5 minutes; and retaining temperature in the reactor at 10-28 degrees C, and also controlling pH value at 7.0-8.5, dissolved oxygen at 3-8 mg/L and water residence time at 3-8 hours.    USE - Method for processing sewage.    ADVANTAGE - The aerobic denitrifying bacteria is granulated, so that the reactor has high efficiency while having denitrifying capacity. The sludge concentration is high, and the duration for separating sludge from water is short. The prepared aerobic granular sludge is excellent in settling.    DETAILED DESCRIPTION - Sewage processing method through granular sludge aerobic denitrification, comprises pumping wastewater containing nitrate nitrogen into continuous-batch bioreactor; adding phosphorus and trace elements to the wastewater to maintain normal growth of microbe; providing an aerating apparatus at the bottom of the reactor, where air ascending speed is 43.2-90 m/hour, and then precipitating for 1-5 minutes; and retaining temperature in the reactor at 10-28 degrees C, and also controlling pH value at 7.0-8.5, dissolved oxygen at 3-8 mg/L and water residence time at 3-8 hours. In wastewater, the concentration of nitrate nitrogen is 50-200 mg/L, and chemical oxygen demand (COD) concentration is 200-800 mg/L. A draining port is arranged in the middle of the reactor or at the position of 1/4 away from the reactor bottom, where the reactor operation cycle is 4, 6, 8 hours.    DESCRIPTION OF DRAWING(S) - The drawing is a perspective view of a sewage processing device.
NOVELTY - Bacillus-algae preparation comprises nitrobacteria, Bacillus licheniformis, Scenedesmus obliquus and Selenastrum bibraianum at a volume ratio of 1-2: 1-3: 1-3: 1-3. Each mL of microbe inoculum size is 7x 106-9x 106 colony forming unit.    USE - Immobilized Bacillus-algae preparation used for purifying aquiculture wastewater.    ADVANTAGE - The Bacillus, the algae and the immobilized material have no toxic side-effect to aquaculture animals. The Bacillus and the algae can inhibit the harmful pathogenic bacteria to grow at a certain degree. The immobilized preparation has simple operation and high-efficiency Bacillus-algae microbe fungicide is easily preserved and transported after immobilization. The immobilized material is economical and practical and easily recycled.
NOVELTY - Production of industrial ethanol with ethanol-diesel manufacturing method, comprises: (i) disposing ethanol amine and naphthenic acid in industrial alcohol to obtain denatured alcohol; (ii) adding oleinic acid, petroleum acid and/or naphthenic acid to obtain diesel fuel mixing liquid; (iii) preparing diesel fuel modifier by mixing e.g. alkyl phenol polyoxyethylene, methyl-carbonate and ethyl oleate; (iv) disposing into a container, stirring to prepare the ethanol diesel fuel; (v) adding the fuel mixing solution into denatured alcohol, adding the fuel modifier, mixing to obtain the product.    USE - The method is useful for the production of ethanol diesel fuel by industrial alcohol.    ADVANTAGE - The method has good stability no corrosions, no swelling, no emulsification, strong explosive power, convenient usage and low manufacture cost.    DETAILED DESCRIPTION - Production of industrial ethanol with ethanol-diesel manufacturing method comprises: (i) disposing ethanol amine (0.5-1.5%) and naphthenic acid (0.2-1%) in industrial alcohol to mix to obtain denatured alcohol; (ii) adding at least one mixture of oleinic acid (5-15%), petroleum acid and naphthenic acid, mixing to obtain diesel fuel mixing liquid; (iii) preparing diesel fuel modifier by mixing alkyl phenol polyoxyethylene (54-84%), methyl-carbonate (10-30%), ethyl oleate (5-10%) and para-tertiary butyl phenol (1-6%); (iv) disposing the raw materials in sequence into a container to uniformly stir for 20-30 minutes to prepare the ethanol diesel fuel; (v) adding the diesel fuel mixing solution (70%) into denatured alcohol (25%) to stir, adding diesel fuel modifier (5%), mixing to obtain the ethanol diesel fuel.
NOVELTY - Compound fuel comprises (in pts.wt.): sludge (20-40), straw powder (60-40), cow dung powder (5), wood powder (5) and combustion improver (10). The sludge is obtained from sewage treatment plant.    USE - Compound fuel used for industrial boiler, electricity-generating boiler, warming boiler, bathing pool and cooking.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for processing compound fuel, which involves:    (A) conveying 20-40 pts.wt. of sludge into a mixer by a belt conveyor;    (B) adding 60-40 pts.wt. of straw powder, 5 pts.wt. of cow dung powder and 5 pts.wt. of wood powder into the mixer;    (C) mixing and agitating the mixture to obtain a material;    (D) discharging the material from the mixer;    (E) sending the discharged material in an auger;    (F) sending the material in a drier from auger;    (G) sending the dried material in a another mixer by a hoisting machine;    (H) adding 10 pts.wt. of combustion improver into the latter mixer;    (I) sending the material into auger;    (J) sending the material in a granulator or a briquetting machine by scraper-trough conveyor;    (K) discharging the product; and    (L) sending the product in a cooler by belt for cooling to obtain compound fuel.
NOVELTY - A liquefied gas mixture is obtained by mixing 10-50 parts weight of liquid carbon dioxide with 100 parts weight of liquid containing propane and butane.    USE - Liquefied gas mixture is used for foaming of polymer.    ADVANTAGE - The liquefied gas mixture has excellent flame retardant property.
NOVELTY - A Dunaliella sallina is cultured to obtain Dunaliella sallina solution, and obtained solution is concentrated using hollow fibrous membrane. The concentrated product is subjected to centrifugal separation to obtain algae paste containing water. The algae paste is extracted using supercritical carbon dioxide at 30-60 degrees C under pressure of 7-30 MPa to obtain carotenoid product and algae slag liquor. The algae slag liquor is liquefied using supercritical water, to obtain biofuel oil.    USE - Method for extracting carotenoid used for producing biofuel.    ADVANTAGE - The carotenoid is extracted in high yield, by simple and environmental-friendly method, with reduced energy consumption.    DETAILED DESCRIPTION - A Dunaliella sallina is cultured to obtain Dunaliella sallina solution, and obtained solution is concentrated using hollow fibrous membrane. The concentrated product is subjected to centrifugal separation to obtain algae paste containing water. The algae paste is extracted using supercritical carbon dioxide at 30-60 degrees C under pressure of 7-30 MPa to obtain carotenoid product and algae slag liquor. The algae slag liquor is liquefied using supercritical water at 300-420 degrees C in presence of catalyst under pressure of 10-40 MPa, to obtain biofuel oil. The mass ratio of catalyst and algae slag liquor, is 2-7:100.
NOVELTY - A Candida viswanathii CY21-21 (CGMCC 3456), is new.    USE - The C.viswanathii is useful for treating crude oil and organics in the oil field (claimed) for producing mineralized water.    ADVANTAGE - The C.viswanathii can be prepared simply, rapidly and inexpensively, does not changes the chemical characteristic of the water, reduces corressiveness of the water.
NOVELTY - Charcoal production involves performing pre-drying, drying, pre-carbonization and charring of biomass to obtain a product.    USE - Method for producing charcoal (claimed).    ADVANTAGE - The method enables to produce charcoal continuously with high yield and quality, and without generating fuel gasses.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an equipment for producing charcoal, which comprises an oven container, a lid, a gas outlet pipe, a thermal device, a pipe and a combustion chamber.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional side view of the charcoal production equipment.    Oven container (1)    Lid (2)    Pipe (5)    Combustion chamber (16)    Gas outlet pipe (23)    Thermal device (31)
NOVELTY - Termite medicine wrapped in silk fibroin comprises silk fibroin, N-succinimide and bifenthrin according to mol ratio of 5:500:1.    USE - The medicine is useful for preventing termite.    ADVANTAGE - The termite medicine wrapped in silk fibroin has long-term slow-release effect, improves toxic effect toward termite and relieves pollution toward environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for producing the termite medicine wrapped in silk fibroin comprising: (a) mixing silk fibroin with N-succinimide according to ratio of 1:50 to 1:500, dissolving them in 1-fluo-2,4,dinitro benzene and phosphate buffered saline (PBS), and mixing the materials in condition of ice bath to form photoactive silk fibroin solution; and (b) dripping photoactive silk fibroin solution onto the surface of clean material, adding termite medicine, spreading another layer of photoactive silk fibroin solution, refrigerating, drying and wrapping, and irradiating by ultraviolet rays for 15-20 minutes so that the wrapped medicine is grafted onto material.
NOVELTY - Producing high temperature activated anaerobic sludge, involves fermenting anaerobic sludge in sewage disposal plant. The anaerobic sludge comprises livestock excretion, butchery byproducts, organic waste and byproducts of food processing.    USE - The method is useful for producing high temperature activated anaerobic sludge used for producing methane (claimed) used as biogas for generating energy and electricity.    ADVANTAGE - The obtained high temperature activated anaerobic sludge enables stable and increased production of methane in a rapid and cost-effective manner without causing harmful effects to environment.
NOVELTY - A carbon-based feedstock (320) rendering constituent system (100) comprises pressure chamber (200) defining an enclosed interior volume, feedstock input port (300) and gas output port; and liquid hot mix heat transfer medium (500) positioned in interior volume of pressure chamber forming a pool of hot mix transfer medium having an upper surface level. The carbon-based feedstock input into pressure chamber through feedstock input port is broken into constituent component by hot mix transfer medium. A gas constituent component can exit the pressure chamber through gas output port.    USE - A carbon-based feedstock rendering constituent system.    ADVANTAGE - The system is efficient in constituent rendering of carbon-based feedstock, e.g. biomass.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of constituent rendering of carbon-based feedstock (320).    DESCRIPTION OF DRAWING(S) - The drawing is a cross-sectional side view of carbon-based feedstock rendering constituent system.    Constituent system (100)    Pressure chamber (200)    Feedstock input port (300)    Carbon-based feedstock (320)    Liquid hot mix heat transfer medium (500)
NOVELTY - Electrochemically removing impurities that adhere to an electrode surface in a fuel cell system, comprises: providing a fuel cell stack comprising a pair of end plates and a unit cell containing a gas diffusion layer in contact with a membrane electrode assembly which is constructed of a polymer electrolyte membrane enclosed between two electrodes, where the unit cell is stacked between the end plates; and applying a cyclically varying voltage across the fuel cell stack using voltage supplied by a voltage supply means to remove impurities from the electrode surface.    USE - The methods are useful for electrochemically removing impurities that adhere to an electrode surface in a fuel cell system; for electrochemically removing impurities that adhere to a catalyst; and for electrochemically removing impurities that are adhered to catalyst reaction sites on electrodes of a fuel cell stack due to reaction in the fuel stack during generation of electricity (all claimed).    ADVANTAGE - The methods effectively and efficiently reduce and remove impurities to an electrode surface in a fuel cell, and impurities adhered to a catalyst.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method of electrochemically removing impurities that adhere to a catalyst, comprising: providing a catalyst with a surface and impurities adhered to the surface; and applying a cyclically varying voltage across the catalyst surface using voltage supplied by a voltage supply means to remove the impurities from the catalyst surface.
NOVELTY - Extraction of a biofuel (biogas) from marine macro algae (cryptogams) using a new biomass, is claimed, where a composition of microalgae includes lipids, sugar, and genera (Ulva, Caulerpa and Gracilaria).    USE - The process is useful for extraction of a biofuel (biogas), preferably methane from marine macro algae (cryptogams).    ADVANTAGE - The fermentation duration (20) of the macro algae biomass (cryptogams) is shorter than that of the vegetables due to the biochemical nature of the microalgae.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for structure of formulation of inoculum for fermentation comprising original ingredients, where the structure changes the formulation during the biological phases including: phase 1 (65% of cow slurry diluted 2 times in water, 25% of red wine (Magon), 5% of black liquor, yeast 5%) fermenting for 6 days at room temperature in anaerobic condition; phase 2 (components from the first phase of 40% and 60% of marine algae crushed with water constituting a homogeneous mixture, the secondary inoculum is fermented for long time (4 days) with anaerobic fermentation in an ambient temperature); and phase 3 (secondary inoculum with 10% and 90% of crushed algae with water, in a test temperature, and (32-34 degrees C)).
NOVELTY - Reduction (M1) of the amount of surplus sludge including organic matrix with solid fraction and cellular fraction produced in a wastewater treatment method, involves: reducing the dimensions of the solid and cellular fraction components; and hydrolyzing the components of the solid and cellular fractions having dimensions reduced in first step.    USE - For reducing the amount of surplus sludge including organic matrix with a solid fraction and cellular fraction produced in a wastewater treatment method (all claimed); for dupuration or treating residential and industrial wastewaters capable of allowing considerably reducing the surplus sludge production with respect to the traditional plants.    ADVANTAGE - The method is cost effective and has a positive impact on the production of biogas. The hydrolysis reaction performed subsequently to reduce the dimensions of the organic components of sludge which allows to make the part of the organic components of sludge soluble and more biodegradable reducing the solid mass that shall form the surplus sludge.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a plant for reducing the amount of surplus sludge produced in a wastewater treatment plant, where the sludge includes organic matrix comprising a solid fraction and a cellular fraction, where the plant includes: a stage for reducing the dimensions of the solid and cellular fraction components; and stage for hydrolysis at room temperature of the components of the solid and cellular fractions having dimensions reduced in the reduction stage.
NOVELTY - Improvement of flow properties of particulate solid biomass material comprises mixing the particulate solid biomass material with a particulate solid inorganic material.    USE - The method is for improving flow properties of particulate solid biomass material (claimed). It is used in preparing the biomass material for conversion reaction, particularly conversion reaction involving fluidization and/or pneumatic transport of the solid particulate biomass material. The method is for use with catalytic biomass conversion process. It is useful for conveying solid particulate biomass material by a screw feeder system, pneumatic conveyance, or fluidizing the material, in preparation to conducting a conversion reaction with the biomass material.    ADVANTAGE - Upon mixing of the solid biomass particles and inorganic particles, interaction between the 2 types of particles can reduce the particle size of the solid biomass particles, thus, flow properties of the mixture of solid particulate biomass material and particulate solid inorganic material are better than are the flow properties of the solid particulate biomass material alone.
NOVELTY - Liquid waste is distilled by feeding liquid waste stream into a heated film evaporator, where distillation takes place from a falling thin liquid film in which vapors are collected from heated inner evaporation surfaces (6) at 0.1 kPa and 80-330 degrees C.    USE - Method of distilling liquid waste comprising transmission oil, motor oil, transformer oil, waste solvents, cooling liquids, brake liquids, or G-phase or wastes containing glycerin from production of biofuels (claimed).    ADVANTAGE - The method provides shorter contact time with heated surface, thus minimizing heat stress on the distillation stream and causing higher product quality. The use of the film evaporator involving parallel flow of liquid film and vapors, allows the fitted separator of oil vapors and liquid residue to separate vapor phase from the distillation residue. The film evaporator is simple in design and suitable also for small-scale production, and has low incrustation at heat exchanging surfaces and the ease with which smooth surfaces can be cleaned.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a film evaporator for liquid waste with condenser of distillation vapors, comprising vertically disposed distillation body (5) with inner evaporation surface, and a heating block (4) for transferring heat to the outer surface of the hollow distillation body.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a design of vacuum film evaporator for liquid waste with parallel stream of liquid film and vapors.    Waste oil tank (1)    Cooler (2)    Heating block (4)    Distillation body (5)    Inner evaporation surface (6)    Distillation residue container (8)
NOVELTY - Domestic sewage disposing machine comprises machine case; machine cover on the machine case; hollow water air pump inside the machine case; air suction pipe arranged on one end of the hollow water air pump, and located outside the water surface; an air exhaust pipe installed on the other end of the hollow water air pump, and located inside the machine case; water pump located inside the machine case and provided with a water discharge pipe on one end; and net barrel installed inside the machine case.    USE - Domestic sewage disposing machine.    ADVANTAGE - Compared with the prior art, the machine has simple structure and light weight.    DETAILED DESCRIPTION - Domestic sewage disposing machine comprises machine case; machine cover on the machine case; hollow water air pump inside the machine case; air suction pipe arranged on one end of the hollow water air pump, and located outside the water surface; an air exhaust pipe installed on the other end of the hollow water air pump, and located inside the machine case; water pump located inside the machine case and provided with a water discharge pipe on one end; and net barrel installed inside the machine case. The water pump and hollow water air pump are installed inside the net barrel. Large amount of filtration material is filled between the machine case and the net barrel. A shell of the machine case is provided with more than one small holes.
NOVELTY - The element (1) has a target gas electrode formed on a surface of a solid electrolyte with an oxygen ion conductivity. A reference gas electrode is formed on another surface of the solid electrolyte. A catalyst layer (2) is formed on an outer surface of a porous diffusion resistance layer (14) by which target gas is introduced into the interior of the element. The catalyst layer contains noble-metal catalysts (21) that comprise an average particle size of not less than 0.3 micrometers, where porosity of the catalyst layer is not less than porosity of the porous diffusion resistance layer.    USE - Gas sensor element for use in direct injection engines for injection of fuel into a combustion chamber, turbocharged engine and an engine for compressed natural gas and for detecting concentration of a specific content in target gas (all claimed).    ADVANTAGE - The catalyst layer is provided with high resistance, thus preventing occurrence of issuing an incorrect detection signal while avoiding deterioration of the catalyst layer in the element.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method of manufacturing a gas sensor element.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of a catalyst layer of a gas sensor element.'(Drawing includes non-English language text)'    Gas sensor element (1)    Catalyst layer (2)    Porous diffusion resistance layer (14)    Aluminum oxide particles (20)    Noble-metal catalysts (21)
NOVELTY - The carbonization furnace has a hollow heat sink connected to a heat radiation pipe (5). The combustion gas (G) is introduced in heat radiation pipe from exhaust gas introduction hole (7), when combusting the carbonization material (T). The combustion gas is introduced in hollow portion of hollow heat sink (9) through a lower communicating hole (10), while carbonization material is heated. The combustion gas in hollow heat sink and carbonization material in furnace main portion (1) is heated by heat radiation of hollow heat sink.    USE - Carbonization furnace for spontaneous combustion of organic raw materials such as ground material of timber or bamboo material, pellet, chip, waste material, etc, used for household applications.    ADVANTAGE - The high quality carbonized material can be produced without non-uniformity burning in short time. Since heat radiation energy is consumed efficiently, the heat amount of combustion gas in the furnace can be decreased. Hence, the thermal efficiency can be improved, the carbonization furnace can be manufactured inexpensively and the structure of carbonization furnace can be simplified.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of the carbonization furnace.    Furnace main portion (1)    Heat radiation pipe (5)    Exhaust gas introduction hole (7)    Hollow heat sink (9)    Combustion gas (G)    Carbonization material (T)
NOVELTY - Bioremediation of highly aromatic hydrocarbon waste comprises: preparing a microbial blend capable of degrading aromatic hydrocarbons, where microorganisms in the microbial blend are adsorbed on a biodegradable carrier; preparing a biopile comprising a mixture of the hydrocarbon waste, soil and a bulking agent; adding the microbial blend into the biopile followed by the addition of nutrients to promote bioremediation reaction; and maintaining aeration and moisture of the biopile to complete the bioremediation of the highly aromatic hydrocarbon waste.    USE - The method is useful for bioremediation of highly aromatic hydrocarbon waste, contaminated soil and slurries.    ADVANTAGE - The method removes highly aromatic compounds in a safe, eco-friendly, economical and intensive manner. The method provides a synergistic combination of selective microorganisms to develop a blend enabling effective degradation of highly hazardous aromatic waste and converting them into harmless and environment friendly substances.
NOVELTY - A fuel electrode (9) made of porous ceramic and having gas flow path for flowing fuel gas is covered by solid electrolytic membrane (6), and is electrically connected to air electrode which contacts oxidizing gas. A bonding material (17) is provided between fuel electrode and electrically-conductive board (12). The bonding material is generated by baking mixture of 10-55 volume% of nickel metal oxide powder and 90-45 volume% of metal powders with average particle diameter of 10 micrometer or less in 800-1000? oC in oxidative atmosphere.    USE - Manufacturing method of electrochemical cell such as solid oxide fuel cell.    ADVANTAGE - The sufficient joint-strength and electroconductivity of fuel electrode and electrically-conductive board can be maintained by baking mixture of metal oxide powder and nickel metal powders in oxidative atmosphere.    DESCRIPTION OF DRAWING(S) - The drawings show the sectional views of the electrochemical cell.    Solid electrolytic membrane (6)    Fuel electrode (9)    Electrically-conductive board (12)    Sealing material (13)    Bonding material (17)
NOVELTY - The method involves preparing the metallic substrate (20) of porous shape by passing sintering of metal particle (10). An electrode (30) and electrolyte (40) containing ceramics are formed into a film on the metallic substrate. The cobaking process is performed with respect to the metallic substrate, electrode and electrolyte. The preparatory process includes porositization treatment process that performs porositization process to the metallic substrate obtained by sintering of metal particle.    USE - Manufacturing method of fuel cell such as solid oxide fuel cell.    ADVANTAGE - The difference of shrinkage volume of electrolyte and the shrinkage volume of metallic substrate in cobaking process is reduced such that the peeling of electrolyte and the generation of crack are suppressed.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the process of manufacturing fuel cell.    Metal particle (10)    Metallic substrate (20)    Electrode (30)    Electrolyte (40)    Fuel cell (100)
NOVELTY - The method involves attaching a battery cell laminated structure (12) with respect to the end plate (14) positioned in the lower end side of a shaft guiding jig (40). A tension shaft (16) is moved with respect to the end plate along perpendicular direction, when the shaft guiding jig contacts the end surface of the end plate. The tension shaft is moved with respect to the grooved line (13R) formed in the buffer (13) along cell lamination direction of the battery cell laminated structure.    USE - Manufacturing method of fuel cell.    ADVANTAGE - Tension shaft can be moved appropriately with respect to grooved line formed in buffer along cell lamination direction of battery cell laminated structure. Reaction force can be applied reliably and rapidly with respect to the battery cell laminated structure. Variation in the reaction force with respect to lamination direction can be suppressed and fuel cell can be manufactured reliably and effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view depicting manufacturing procedure of fuel cell using manufacture tool.    Battery cell laminated structure (12)    Buffer (13)    Grooved line (13R)    End plate (14)    Tension shaft (16)    Shaft guiding jig (40)
NOVELTY - The fuel cell system (10) has a fuel reservoir (14) having a raw fuel stored in fuel reservoir. A replaceable fuel filter element receives raw fuel from the fuel reservoir and refines the raw fuel to a refined fuel, where the replaceable filter includes a data storage device to store filter property information. A fuel cell stack (40) receives refined fuel from the fuel filter and utilizes the refined fuel to generate electricity. A control system (20) access the data storage device of the fuel filter element.    USE - Fuel cell system.    ADVANTAGE - The replaceable fuel filter element can be utilized in the fuel cell system, which receives raw fuel from the fuel reservoir and refines the raw fuel to a refined fuel and hence improved fuel filter is obtained.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for controlling fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram illustrating the fuel and signal flow of the fuel cell system.    Fuel cell system (10)    Fuel reservoir (14)    Control system (20)    Fuel cell stack (40)    Cathode air pump (46)
NOVELTY - Method of producing fatty acid ester or fatty acid ethyl ester, involves culturing genetically engineered microorganism to produce an alcohol, a fatty acid, and at least one ester synthase.    USE - The method is useful for producing fatty acid ester, preferably fatty acid ethyl ester, where the produced fatty acid ester is useful as biofuel.    ADVANTAGE - The fatty acid esters are produced without using exogenous alcohol.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) fatty acid ester obtained by the above-mentioned method; and    (2) genetically engineered microorganism, comprising fatty acid synthesis regulator gene, pyruvate oxidase gene and lactate dehydrogenase gene, where fatty acid synthesis regulator gene, pyruvate oxidase gene and lactate dehydrogenase gene has reduced expression relative to wild-type microorganism.
NOVELTY - The device has a combustion chamber (6) including a combustion chamber inlet (201), a combustion chamber outlet (203) and an electron beam heater (7). The combustion chamber inlet has a sample inlet (0) and a gas pass inlet (1). The combustion chamber outlet has a solid outlet (14) and a useful gas outlet. A production tank (10) is flange mounted at the useful gas outlet. An evacuating device is flange mounted at the production tank for evacuating the production tank. The chamber is formed from titanium, molybdenum or graphite.    USE - Converter device for converting biomass or carbon dioxide into hydrocarbon compounds.    ADVANTAGE - The device effectively converts the biomass or carbon dioxide into hydrocarbon compounds without requiring additional energy.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a method for partially converting biomass into hydrocarbon compounds, useful gas and solids    (2) a method for partially converting contaminated material into carbon dioxide.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a converter device.    Sample inlet (0)    Gas pass inlet (1)    Combustion chamber (6)    Electron beam heater (7)    Production tank (10)    Solid outlet (14)    Combustion chamber inlet (201)    Combustion chamber outlet (203)
NOVELTY - Mixing 2 phase fuel mixture comprising vapor component and liquid component in vessel (10) comprises providing 2 phase fuel mixture in vessel, where fuel mixture comprises gaseous methane (50-80 mole%) and at least one other hydrocarbon; withdrawing at least portion of vapor component of mixture from vessel; and re-introducing withdrawn vapor component into vessel by bubbling withdrawn vapor component into liquid component of fuel mixture at gravitational low point of vessel.    USE - Method is used for mixing two phase fuel mixture comprising vapor component and liquid component in vessel.    ADVANTAGE - The method reduces stratification of fuel mixture.    DETAILED DESCRIPTION - Mixing 2 phase fuel mixture comprising vapor component and liquid component in vessel comprises providing 2 phase fuel mixture in vessel, where fuel mixture comprises gaseous methane (50-80 mole%) and at least one other hydrocarbon; withdrawing at least portion of vapor component of mixture from vessel; and re-introducing withdrawn vapor component into vessel by bubbling withdrawn vapor component into liquid component of fuel mixture at gravitational low point of vessel such that bubbled vapor component is dissolved into liquid component and fuel mixture is sufficiently agitated to mix two phase fuel mixture. The mixture of methane and at least one other hydrocarbon is maintained at - 1 degrees C or greater and at pressure of greater than or equal to 8.0 MPa.    DESCRIPTION OF DRAWING(S) - The drawing is a cross-sectional view of mixing and storage tank.    Vessel (10)    Inlet tube (12)    Liquid outlet tube (14)    Vapor outlet tube (16)    Openings (20)
NOVELTY - Catalyst comprising platinum(II) precursor, and optionally metal ion precursor M supported on heteropolyanion (HPA) particles, is new, where the: platinum(II) precursor has degree of oxidation of 2+, optionally complexed with organic or inorganic ligand; the metal ion precursor M is a metal ion comprising silver ion (Ag+), ruthenium ion (Ru2+), nickel ion (Ni2+), cobalt ion (Co2+), ferrous ion (Fe2+) and their two or more mixtures; and the HPA is silicotungstic acid or phospho-potassium tungstic acid (K6P2W18O62).    USE - The catalyst is useful for: the conversion of methane into methanol; and the conversion of methane into carbon dioxide. The catalyst is useful for manufacturing electrode, preferably fuel cell (all claimed).    ADVANTAGE - The catalyst allows to use very little platinum and the conversion of methane to methanol or carbon dioxide at 80 degrees C, hence the catalyst is stable.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) an electrode, preferably fuel cell, comprising a support made of an electronically conductive material on at least one surface of a catalyst;    (2) manufacturing the electrode, comprising: (a) dissolving HPA in a solvent comprising 1-4C alcohol and its mixtures, and a mixture of water and at least one 1-4C alcohol; (b) depositing the obtained solution on at least one surface of a substrate made of an electronically conductive material; (c) evaporating the solvent; (d) spraying, on the coated surface of heteropolyanion obtained in step (c), of a solution comprising the catalyst in a solvent comprising water, a mixture of water and at least one 1-4C alcohol and a mixture of 1-4C alcohol; and (e) evaporating the solvent of the solution sprayed in step (d);    (3) process for direct oxidation of methane into carbon dioxide, comprising contacting methane with a catalyst; and    (4) a fuel cell comprising the catalyst or the electrode.
NOVELTY - Gasifying system of mixed fuel water coal slurry airflow bed comprises airflow bed water coal slurry gasifying furnace, preprocessing module, water coal slurry preparing module, purifying module, and separating oxygen supplying module. The output end of the water coal slurry preparing module is connected with an air flow bed water coal slurry gasifying furnace, which is connected with the purifying module to discharge the burnt waste gas. The purifying module is connected with an air separator and outputs combustion-supporting gas.    USE - Gasifying system of mixed fuel water coal slurry airflow bed.    ADVANTAGE - The system can make use of biomass in large scale, does not generate gasified tar, and improves carbon conversion rate of coal gasification.    DETAILED DESCRIPTION - Gasifying system of mixed fuel water coal slurry airflow bed comprises airflow bed water coal slurry gasifying furnace, preprocessing module, water coal slurry preparing module, purifying module, and separating oxygen supplying module. The preprocessing module receives the biomass to be processed and is connected with the input end of the water coal slurry preparing module, which receives the biological coke material output by the preprocessing module and grinds to prepare slurry. The output end of the water coal slurry preparing module is connected with an air flow bed water coal slurry gasifying furnace and outputs the water coal slurry. The airflow bed water coal slurry gasifying furnace is connected with the separating oxygen supplying module to receive combustion-supporting gas, and connected with the purifying module to discharge the burnt waste gas. The purifying module is connected with an air separator and outputs combustion-supporting gas.
NOVELTY - A Shewanella, specifically Shewanella xiamenensis sp.nov.S4 deposited under CCTCC M 209017, is new.    USE - The strain is useful in microorganism fuel cell for generating electricity (claimed) in seawater environment.    ADVANTAGE - The strain has comparatively high electricity generating activity.
NOVELTY - The combustion system (10) has a liquid fuel extracting device extracting a biomass liquid fuel from biomass i.e. plant seed. A gasifier (14) produces biogas from a biomass extraction residue after the biomass liquid fuel is extracted by the liquid fuel extracting device. A mixed combustion engine (17) combusts the biomass liquid fuel extracted by the liquid fuel extracting device and the biogas produced by the gasifier.    USE - Combustion system for combusting biogas and vegetable oil derived from a plant seed.    ADVANTAGE - The mixed combustion engine combusts the biomass liquid fuel extracted by the liquid fuel extracting device and the biogas produced by the gasifier, so that the combustion system can perform combustion with the biomass-derived fuel, thus improving thermal efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a combustion method.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of a combustion system.'(Drawing includes non-English language text)'    Combustion system (10)    Gasifier (14)    Gas holder (15)    Plant oil tank (16)    Mixed combustion engine (17)
NOVELTY - A desulfurizing apparatus (3) comprises desulfurizer (7) which accommodates desulfurization catalyst which removes sulfur content from liquid fuel for supplying modifier which produces reformed gas containing hydrogen, heater (8) which heats liquid fuel in desulfurizer, temperature measuring unit (13) which measures temperature of desulfurization catalyst in desulfurizer, power supply which applies voltage to heater, and control unit (15) which controls power supply.    USE - Desulfurizing apparatus for fuel cell system (claimed).    ADVANTAGE - The apparatus can shorten starting time and suppresses hunting phenomenon.    DETAILED DESCRIPTION - A desulfurizing apparatus (3) comprises desulfurizer (7) which accommodates desulfurization catalyst which removes sulfur content from liquid fuel for supplying modifier which produces reformed gas containing hydrogen, heater (8) which heats liquid fuel in desulfurizer, temperature measuring unit (13) which measures temperature of desulfurization catalyst in desulfurizer, power supply which applies voltage to heater and is controlled to apply first voltage with respect to heater after start up until temperature reaches target temperature at time of normal operating and apply second voltage lower than first voltage with respect to heater, and control unit (15) which controls power supply. An INDEPENDENT CLAIM is included for a fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fuel cell system. (Drawing includes non-English language text).    Desulfurizing apparatus (3)    Desulfurizer (7)    Heater (8)    Temperature measuring unit (13)    Control unit (15)
NOVELTY - Method (M1) of producing one or more fermentation end-products, involves fermenting a lignocellulosic biomass comprising hexose and pentose saccharides with first microorganism, where the first microorganism simultaneously hydrolyzes and ferments the lignocellulosic biomass to produce fermentation end-product.    USE - The method (M1) is useful for producing fermentation end-products, preferably biofuel product, more preferably ethanol (both claimed).    ADVANTAGE - The method obtains ethanol at a yield of 45 g/l or more. The method is inexpensive, and robust.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) biofuel product produced by (a) culturing a strain of Clostridium phytofermentans in a medium comprising the lignocellulosic biomass; and (2) system for producing the fermentation end product, comprising fermentation vessel, lignocellulosic biomass, and the first microorganism, where the fermentation vessel is adapted to provide suitable conditions for simultaneous hydrolysis and fermentation of the lignocellulosic biomass.
NOVELTY - Conversion (M1) of a triglyceride to an alkyl ester and glycerol using a transesterification process involves: mixing the triglyceride with an alcohol to produce a reactant mixture; flowing the reactant mixture over a heterogeneous catalyst with a relative velocity of at least 0.005 m/s to obtain high reactant shear at a reactant-heterogeneous-catalyst interface; and producing alkyl ester and glycerol.    USE - For conversion of a triglyceride to an alkyl ester and glycerol using a transesterification process (claimed); for producing bio-fuels.    ADVANTAGE - The method converts triglyceride to an alkyl ester and glycerol in higher process rate and higher conversion levels with increase yield and reduce reaction time over existing biodiesel transesterification and esterification techniques.
NOVELTY - A mixed gas of carbon dioxide and hydrogen is introduced into catalyst filled layer, heated the catalyst filled layer and reacting the mixed gas under the reduced pressure, to obtain methanol. The catalyst in a catalyst filled layer contains binder and catalyst component containing copper oxide, zinc oxide and aluminum oxide. The molar ratio of aluminum with respect to total content of copper and zinc in the catalyst component is 98:2-94:6.    USE - Synthesis of methanol used for fuel, petrochemical intermediate compound, and raw material for methyl tertiary butyl ether.    ADVANTAGE - The method efficiently provides methanol under reduced pressure and mild reaction conditions using catalyst having excellent moldability, mechanical strength and durability.
NOVELTY - A desulfurizing apparatus (3) comprises cylindrical desulfurizer (7) which accommodates desulfurization catalyst which removes sulfur content from liquid fuel for supplying modifier which generates reformed gas containing hydrogen and has inlet port of liquid fuel among outer periphery of desulfurizer, heater (8) for heating liquid fuel in desulfurizer, and power supply (9) which supplies with electricity to heater. The space of adjacent coil of heaters is set to become smallest in inlet port.    USE - Desulfurizing apparatus for fuel cell system (claimed).    ADVANTAGE - The apparatus can suppress life decline of desulfurization catalyst and accelerates desulfurization reaction.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the desulfurizing apparatus. (Drawing includes non-English language text).    Desulfurizing apparatus (3)    Desulfurizer (7)    Heater (8)    Power supply (9)    Storage container (19)
NOVELTY - A high ion conductivity solid electrolyte comprises complex compound containing polyvinyl alcohol, inorganic compound chosen from silicic acid compound, tungstic acid compound and/or zirconic acid compound and compound other than polyvinyl alcohol and having sulfonic acid group.    USE - High ion conductivity solid electrolyte for use in electrochemical system e.g. fuel cell, steam pump, dehumidifier, air-conditioning equipment, electrochromic device, electrolyzer, humidity sensor, hydrogen sensor, electrolytic hydrogen generating apparatus, electrolytic hydrogen peroxide manufacturing apparatus and electrolyzed water manufacturing apparatus (all claimed).    ADVANTAGE - The high ion conductivity solid electrolyte has reduced swelling characteristics, high conductivity and excellent moisture absorbability, and is manufactured economically.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for electrochemical system, which consists of electrodes separated by the high ion conductivity solid electrolyte.    DESCRIPTION OF DRAWING(S) - The drawing shows the flowchart of the manufacture of high ion conductivity solid electrolyte. (Drawing includes non-English language text)    Raw material solution preparation process (2)    Mixing process (4)    Neutralization process (5)    Neutralized solution manufacture process (6)    Organic compound addition process (7)
NOVELTY - The apparatus has an exhaust gas purifying catalyst (6) oxidizing hydrocarbon in waste gas, which improves low-temperature startability of an internal combustion engine (1) and discharges from the internal combustion engine. A sub-injector (8) supplies supplementary fuel to the internal combustion engine in a low-temperature period when the start-up initial stage period of an engine and the engine temperature are less than a predetermined value. The supplementary fuel contains a chain type saturated hydrocarbon.    USE - Apparatus for supplying fuel e.g. alcohol fuel and gasoline fuel, to an internal combustion engine of a vehicle i.e. flexible fuel vehicle.    ADVANTAGE - The sub-injector supplies the supplementary fuel to the internal combustion engine in a low-temperature period when the start-up initial stage period of the engine and the engine temperature are less than the predetermined value, so that the time of start-up of the engine and the low temperature startability of the internal combustion engine is improved, thus reducing the usage-amount of a noble metals for oxidation of catalysts in the exhaust gas purifying catalyst.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a fuel supply apparatus.'(Drawing includes non-English language text)'    Internal combustion engine (1)    Intake passage (2)    Exhaust gas purifying catalyst (6)    Main injector (7)    Sub-injector (8)    Control apparatus (13)
NOVELTY - The manufacturing apparatus (20) has a raw material insertion bag (11) filled with raw material containing chaff or bark as moisture control agent. A turntable (12) rotates the raw material insertion bag. A vibration unit (27) such a motor arranged at the lower portion of the positioning base (15), applies vibration to the turntable by vibrating the base. A support portion (28) supports the insertion bag and the turntable. A relaxing portion (28a) of support portion relieves the vibration.    USE - Compost manufacturing apparatus.    ADVANTAGE - The raw material can be compressed and air can be removed from the material The generation of offensive odor can be suppressed and requirement of large scale storage area can be suppressed. Hence the compost can be manufactured inexpensively and simply.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for compost manufacturing method that involves sealing the raw material insertion bag and performing anaerobic fermentation of the raw material. The raw material is heated and the moisture content of the raw material is 50-55 mass%.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the compost manufacturing apparatus.    Raw material insertion bag (11)    Turntable (12)    Positioning base (15)    Manure manufacturing apparatus (20)    Vibration unit (27)    Support portion (28)    Relaxing portion (28a)
NOVELTY - Coconut husk (palm kernel shell) is dry-distilled with a self-sustained combustion-type direct heating-type rotary kiln (3). The hot coconut husk charcoal after dry-distillation is supplied to heat insulation chamber in which the air inflow is controlled, and hot coconut husk charcoal is maintained in heat insulation chamber for 30 minutes or more to obtain coconut husk charcoal, after removing volatile material using self-potential heat.    USE - Manufacture of coconut husk charcoal used as biomass fuel.    ADVANTAGE - The method enables economical manufacture of coconut husk charcoal having high fixed carbon and low volatile material.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus (1) for manufacturing coconut husk charcoal, which has self-sustained combustion-type direct heating-type rotary kiln, and heat insulation chamber.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the apparatus for manufacturing the coconut husk charcoal.    Apparatus for manufacturing coconut husk charcoal (1)    Self-sustained combustion-type direct heating-type rotary kiln (3)    Kiln main component (7)    Secondary combustion chamber (11)    Heat insulating material (19)
NOVELTY - The system for power supply to residential buildings under using a water electrolysis unit (2) and/or a photovoltaic unit (1), with which the water electrolysis unit is connected with a pressure-gas tank (3) for hydrogen and/or a pressure-gas tank (4) for oxygen, is claimed. The pressure-gas tank for hydrogen and/or the pressure-gas tank for oxygen are connected with a carburetor, which provides heat energy for a heater and a hearth on one hand and provides current via a generator for consumers on other hand. The pressure-gas tank for hydrogen is arranged downstream to a fluid gas tank (6).    USE - System for power supply to residential buildings under using a water electrolysis unit and/or a photovoltaic unit.    ADVANTAGE - The system avoids the emission of carbon dioxide, does not require a fuel cell block, and can be economically operated with high efficiency.    DETAILED DESCRIPTION - The system for power supply to residential buildings under using a water electrolysis unit (2) and/or a photovoltaic unit (1), with which the water electrolysis unit is connected with a pressure-gas tank (3) for hydrogen and/or a pressure-gas tank (4) for oxygen, is claimed. The pressure-gas tank for hydrogen and/or the pressure-gas tank for oxygen are connected with a carburetor, which provides heat energy for a heater and a hearth on one hand and provides current via a generator for consumers on other hand. The pressure-gas tank for hydrogen is arranged downstream to a fluid gas tank (6) over a cooling unit (5). The generator is connected with the water electrolysis unit over a pipeline.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of a system for power supply to residential buildings.    Photovoltaic unit (1)    Water electrolysis unit (2)    Pressure-gas tank for hydrogen (3)    Pressure-gas tank for oxygen (4)    Cooling unit (5)    Fluid gas tank. (6)
NOVELTY - Fuel management system having at least one fluororubber article in contact with biodiesel fuel, the improvement where the fluororubber article comprises: a polyhydroxy cured fluoroelastomer comprising copolymerized units of vinylidene fluoride and at least one other fluoromonomer and a diester of a dicarboxylic acid (I) (1-10 parts by weight per hundred parts fluoroelastomer).    USE - The fuel management system is useful in motor vehicle, stationary diesel powered device, biodiesel supply system and biodiesel manufacturing plant (all claimed).    ADVANTAGE - The fluororubber article in the fuel management system has excellent (i.e. low (less than 10 vol.%, preferably less than 5 vol.%)) volume swell when exposed to biodiesel fuel for long periods of time and/or at elevated temperatures.    DETAILED DESCRIPTION - Fuel management system having at least one fluororubber article in contact with biodiesel fuel, the improvement where the fluororubber article comprises: a polyhydroxy cured fluoroelastomer comprising copolymerized units of vinylidene fluoride and at least one other fluoromonomer and a diester of a dicarboxylic acid of formula (R1(COOR2)2) (I) (1-10 parts by weight, per hundred parts fluoroelastomer).    R1 = 2-10C alkylene; and    R2 = 1-6C alkyl.    An INDEPENDENT CLAIM is also included for reducing the volume swell of a polyhydroxy cured fluororubber article in contact with biodiesel fuel, comprising incorporating the diester of a dicarboxylic acid (I) (1-10 parts by weight, per hundred parts by weight fluoroelastomer) into the polyhydroxy curable fluoroelastomer composition prior to curing the composition.
NOVELTY - Controlled-leaching coated fertilizer comprises coating layer containing (in parts weight): olefin-based resin including polyethylene (20-60) and ethylene vinyl acetate (10-20), biodegradable resin (5-30), water-insoluble talc or diatomaceous earth (10-70), anionic or cationic surfactant (0.2-2) and starch (3-15).    USE - The coated fertilizer is useful for promoting growth of rice plants.    ADVANTAGE - The fertilizer is environmental-friendly, degrades naturally, controls leaching and promotes stable growth of rice plants through just a single application to the seedbed performed in lieu of a pre-plant application (base manure), tillering fertilizer (topdressing at tillering stage) and fertilizer for grain ripening (topdressing at young ear formation stage), and thus the fertilizer exhibits improved activity at reduced dosage. The fertilizer does not cause river water contamination, prevents damage in the rice plant field caused by birds due to over-fertilization, and reduces labor by 80% or more as compared to standard coated fertilizer, as the fertilizer is applied once to the seedbed.
NOVELTY - Agrochemical composition comprises tebuconazole and mancozeb in a ratio of 4:1-1:4.    USE - Agrochemical composition used for controlling Physoderma maydis (Miyabe) disease (claimed) and rust.    ADVANTAGE - The agrochemical composition has improved inhibition effect on dormant spore of Physoderma maydis, decreases use of systemic fungicide and its using cost, improves resistance against systemic fungicide, and protects corn seedling, thus it ensures high economic, ecological and social benefits.
NOVELTY - Insecticidal composition comprises tetramethrin and bifenthrin as active ingredients, where auxiliary material and solvent are also included in the composition. The active ingredients are 1-70 wt.% of finished product in which tetramethrin is 1-99 wt.%.    USE - Insecticidal composition.    ADVANTAGE - The insecticidal composition is economic, eco-friendly, easily degradable in environment and prepared in simple dosage forms, reduces pesticide residue and lowers resistance power of insect pest.
NOVELTY - Feed additive comprises sophorolipid.    USE - The feed additive is useful in preparing feed for livestock, for breeding birds or mammals, and for preventing and treating infectious disease caused by Gram-positive bacteria in ruminants. The Gram-positive bacteria is chosen from Staphylococcus, preferably S.aureus and S.epidermidis and Streptococcus, preferably S.suis and S.bovis. The infectious disease is tympanites caused by S.bovis (all claimed).    ADVANTAGE - The feed additive is environment-friendly, has excellent biodegradability, causes no side effects and can be prepared by a simple process.
NOVELTY - The apparatus has stir and mixture unit that rotates an enzyme liquid (B) and mixed to-be-processed plant in horizontal axial center, to perform mixing stirring with enzyme liquid to ferment to-be-processed plant such as chaff. An injection unit (30) and a discharge unit (40) of to-be-processed plant are attached to cylinder outer wall surface (11A) of stir and mixture unit. The to-be-processed plant deposited on cylinder bottom portion is stirred, so that fermentation process is performed, when the stir and mixture unit is driven by autorotation drive unit (60).    USE - Fermentation apparatus for use in organic fermented fertilizer manufacturing system (claimed) for fermenting plants such as chaff. Can also be used in fermenting straw, disposed tree and bamboo.    ADVANTAGE - The fermentation efficiency at the time of stirring is improved. The load and power consumption of the apparatus are reduced and the need for providing large motor is prevented.    DETAILED DESCRIPTION - The angle between tangent of cylinder and reference plane is set to 70-75 degrees in rotation direction of cylinder. An INDEPENDENT CLAIM is included for organic fermented fertilizer manufacturing system.    DESCRIPTION OF DRAWING(S) - The drawing shows the front view of the organic fermented fertilizer manufacturing system.    Outer wall surface (11A)    Injection unit (30)    Discharge unit (40)    Autorotation drive unit (60)    Enzyme liquid (B)
NOVELTY - The apparatus (1) has a mixing vessel (4) for stirring and solubilizing the organic refuse in specified manner. The methane fermentation process is performed with respect to liquid metaplasia garbage emitted from vessel, by a methane fermentation tank (6). The digestive processing is performed with respect to organic substance in liquid metaplasia garbage by processing tanks (7a,7b) in continuous manner. The deposits of organic refuse are removed by performing cannibalism with respect to micro-organisms adhered to a synthetic fiber board (8a).    USE - Organic refuse processing apparatus for generating methane gas used as fuel of yard vehicle.    ADVANTAGE - An environment-friendly organic refuse processing apparatus can be provided efficiently. The methane gas can be generated from the organic refuse effectively, and the discharge amount of the sludge and residues can be reduced reliably.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the organic refuse processing apparatus.    Organic refuse processing apparatus (1)    Mixing vessel (4)    Heater (5)    Methane fermentation tank (6)    Digestive processing tanks (7a,7b)    Synthetic fiber board (8a)
NOVELTY - Organic fertilizer comprises (in wt.%): ammoniated sludge (40-70), active ingredient (0.1-20) and additives (10-55), where ammoniated sludge is treated by ammonification process. The active ingredient is selected from polymerized amino acid, rare earth or their mixture. The additive is inorganic nutrient material, filler or their mixture.    USE - Organic fertilizer used for planting food crop, commercial crop and grassland (claimed), and for treating waste material.    ADVANTAGE - The organic fertilizer has improved nutrient materials and changes organic waste material into its useful resource material. The organic fertilizer improves environment, recycles wastes and develops a new path for producing materials that are utilized in fertilizer production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing organic fertilizer, which involves:    (A) putting separated sludge, removed metal, plastic, glass, sand rock and organic material in a hydrolysis kettle;    (B) reacting the mixture with acid catalyst for 1-2 hours at 80-180 degrees C and 0.8-1.2 megapascal (MPa) to finish hydrolysis reaction, where organic material is animal residue, organic waste or river and lake damaging organism, and acid catalyst is inorganic acid or inorganic strong acid with concentration of 10-20%;    (C) putting the materials in reaction kettle and reacting for 1-2 hours at 80-150 degrees C and 0.8-1.2 MPa;    (D) aerating liquid ammonia (3-16 wt.%) and catalyst (copper salt, ferric salt or ferrous salt in dose of 0.5-1 wt.% of materials) in the reaction kettle to finish ammonation reaction;    (E) removing water from the materials after completion of reaction to obtain solution containing nutrient and solid material with a water content of 30-60%, where solid material is ammoniated sludge; and    (F) preparing organic fertilizer by using ammoniated sludge, active ingredient and additives through conventional production method.
NOVELTY - Lignin is catalyzed and thermally cracked by preheating the molecular sieve catalyst at 200-300 degrees C, heating further at 500-800 degrees C in the presence of protective atmosphere of inert gas, adding lignin gradually to the molecular sieve catalyst for catalytic cracking reaction at 590-610 (preferably 600) degrees C, and separating the catalyzed and thermally cracked product of the lignin to obtain the liquid, gas and solid product.    USE - Method of catalyzing and thermally cracking lignin (claimed) for preparing fuel or aromatic chemicals.    ADVANTAGE - The method produces gas product having methane and carbon monoxide (more than 90 vol.%), and carbon solid product (75-85 mass%).
NOVELTY - A high-energy biomass and biocarbon preparation and utilization technology comprises high-energy biomass plant of C4 plant, that is Chinese silvergrass and Switchgrass. The high energy biomass plant is planted, harvested and dried before being processed. Ethanol or butanol biofuel is produced from high carbohydrate of high-energy biomass plant through microorganism fermentation technology. Then, biofuel block is produced by drying and squeezing high combustion part of high energy biomass plant, and biocarbon is produced by crushing and drying the other part of high energy biomass plant.    USE - A high-energy biomass and biocarbon preparation and utilization technology used for generating biofuel of high fuel value and low fuel value coal used as robot fuel, and for generating organic waste, which can be prepared into organic fertilizer or soil improver for high-energy plantation.    ADVANTAGE - The fuel value of biofuel block and biocarbon is 3-3.7x 107 J/g, equal to that of excellent coal. The technology can rationally utilize raw material, reduce cost, and optimize rational circulation of energy and carbon, thus realizing zero emission generation.
NOVELTY - Common ignition mosquito repelling incense, comprises adhesive or sticky matter, where it can repel the mosquito with other matters of toxic farm chemical of pyrethrin, the adhesive of the incense is water based adhesive and comprises organic starch, less amount of sodium hydroxide and borax and the condensate of wild Chinese mugwort is added to the incense and taken as the additive.    USE - The common ignition mosquito repelling incense is useful for repelling the mosquito and smaller flying insects.    ADVANTAGE - The common ignition mosquito repelling incense: is smoke free; environmental friendly; can be ignited in indoors, outdoors and the wild; and is not harmful for human and poultry. The fragrance of Chinese mugwort is very strong and can remove the peculiar smell in the air and purify the air.
NOVELTY - Fumigating insecticide containing natural plant essence, comprises (in parts by weight) eucalyptus oil containing greater than or equal to 80% cineole (70-90), 2, 2-dichlorovinyl dimethyl phosphate miscible oil containing greater than or equal to 80% 2, 2-dichlorovinyl dimethyl phosphate (5-15) and ethyl formate (4-10).    USE - Used as the fumigation insecticide.    ADVANTAGE - The insecticide: has high insecticidal efficiency and quick acting effect due to the presence of natural plant essence; is non-toxic; does not have a bad odor; is environmental friendly; and does not cause insect-resistance. The method is simple, easy, has a short production period, good repeatability and thus applied for industrial production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for the preparation of the insecticide, comprising weighing eucalyptus oil, 2,2-dichlorovinyl dimethyl phosphate miscible oil and ethyl formate; adding to a mixer in an orderly manner and instantly sealing to obtain a mixture; and uniformly mixing the mixture and filtering to obtain the compound suffocating insecticide containing natural plant essence.
NOVELTY - Biomass is made into synthesis gas by pre-processing biomass raw material, carbonizing at low temperature to obtain pyrolysis gas and charcoal; cooling the charcoal; separating pyrolysis gas from carbon powder in gas discharged from upper side of a carbonizing furnace (5) by a cyclone separator (5); combusting a part of the separated pyrolysis gas in a combustion bed (7); and heating the other part of pyrolysis gas using hot smoke generated from combustion of the combustion bed.    USE - Method of making biomass into synthesis gas (claimed).    DETAILED DESCRIPTION - Biomass is made into synthesis gas by:    (A) pre-processing biomass raw material, carbonizing at low temperature to obtain pyrolysis gas and charcoal, and cooling the charcoal to 60-280 degrees C;    (B) separating pyrolysis gas from carbon powder in gas discharged from upper side of a carbonizing furnace (4) by a cyclone separator (5), combusting a part of the separated pyrolysis gas in a combustion bed (7), and heating the other part of pyrolysis gas using hot smoke generated from combustion of the combustion bed;    (C) transporting the heated pyrolysis gas to the carbonizing furnace to function as heat source of the carbonizing furnace;    (D) drying the raw material by the residual heat smoke obtained after exchanging heat in the biomass raw material pre-processing, and collecting the separated carbon powder; and    (E) grinding the carbon powder to obtain slurry, filling the carbon slurry to the gasifying furnace by a high pressure carbon slurry pump to gasify the slurry.    An INDEPENDENT CLAIM is included for a gasifying system.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of method of making biomass into synthesis gas.    Drying system (2)    Carbonizing furnace (4)    Cyclone separator (5)    Combustion bed (7)    Charcoal material cabin (12)
NOVELTY - A synthesis gas is produced by pre-treating raw material biomass; subjecting biomass to fast pyrolysis technology to obtain a pyrolysis gas and carbon powder; separating the pyrolysis gas, carbon powder and solid hot carrier by a cyclone separator; separating carbon powder and solid hot carrier by a solid-solid separator; collecting the carbon powder; and heating solid hot carrier on a carrier heating fluidized bed.    USE - Method of producing synthesis gas (claimed).    DETAILED DESCRIPTION - A synthesis gas is produced by:    (A) pre-treating raw material biomass, and subjecting biomass to fast pyrolysis technology to obtain a pyrolysis gas and carbon powder;    (B) separating the pyrolysis gas, carbon powder and solid hot carrier by a cyclone separator;    (C) separating carbon powder and solid hot carrier by a solid-solid separator, and collecting the carbon powder;    (D) heating solid hot carrier on a carrier heating fluidized bed, and transporting the carrier into a pyrolysis bed (5) for circulation;    (E) transferring generated pyrolysis gas into a condensing pot, condensing a part of the pyrolysis gas to generate biological fuel oil;    (F) transporting generated biological fuel oil by a high-pressure oil pump to a gasifying furnace to be gasified;    (G) transporting a part of uncondensed pyrolysis gas into a combustion bed to be combusted with the air; and    (H) transporting the other part of uncondensed pyrolysis gas into pyrolysis bed to obtain a fluidizing medium.    An INDEPENDENT CLAIM is included for a gasifying system.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a method of producing synthesis gas.    Pyrolysis bed (5)    Condensing tank (12)    Circulating oil pump (13)    Biological fuel oil exchanger (14)    Uncondensed pyrolysis gas compressor (15)
NOVELTY - The system has a disposable edible oil storage unit (112) storing the disposable edible oil. A disposable edible oil processing unit (113) converts the disposable edible oil into fuel oil. An organic waste storage unit (121) stores the organic waste. An anaerobic digestion part (123) generates the biogas from the organic waste. A gas making module utilizes the bio-diesel delivered from a bio-diesel manufacture module (110) and the biogas delivered from a biogas manufacture module (120). A controller (140) analyzes the quality of the organic waste.    USE - Environment-friendly energy system.    ADVANTAGE - The system can easily produce the bio-diesel and biogas by using the disposable edible oil and the organic waste, and can prevent the environmental contamination. The system produces the environment-friendly renewable energy by using the bio-diesel and the biogas.    DETAILED DESCRIPTION - The system has an ethanol manufacture module producing ethanol by using the biomass, and a bio-ethanol manufacture module manufacturing bio-ethanol by using the biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of an environment-friendly energy system. '(Drawing includes non-English language text)'    Bio-diesel manufacture module (110)    Disposable edible oil storage unit (112)    Disposable edible oil processing unit (113)    Biogas manufacture module (120)    Organic waste storage unit (121)    Anaerobic digestion part (123)    Controller (140)
NOVELTY - Low thioester based composite fuel oil, comprises (in wt.%) biodiesel (51-99), dimethyl ether (1-49) and an anti-oxidative stabilizer (0.0001-2), where the biodiesel comprises soybean oil, rap oil, Jatropha curcas oil, palm oil, biological microalgae aquatic plant oil and animal fat, waste restaurant oil and swill-cooked dirty oil as raw material and performing the ester exchange reaction with the methanol and ethanol to form the fatty acid methanol and fatty acid ethanol.    USE - Used as a low thioester based composite fuel oil.    ADVANTAGE - The fuel oil: uses low cost regenerative resources instead of high cost fossil fuel resource; is oxygen-enriched fuel; can be fully burned, thus reduces the smoke discharging quantity, decreases the smoke discharging heat loss and largely reduces the viscosity of sulfide, nitride and granular dust in the smoke; and is environmental friendly, saves energy and reduces emission.
NOVELTY - The gasifier has an outlet provided on a top part of a conduction dome. A ventilation hole is formed on a pitch plate, and a bead is arranged on a top part of the pitch plate. A beader layer formation dome is provided with a beader layer, and a pump is equipped between a gas purification unit (20) and a storage tank to pump the gas to the storage tank. A gas generation unit (10) produces the mixing gas, and the gas purification unit condenses the liquid ingredient from the mixing gas generated from the gas generation unit. A steel network layer is formed at a lower part of a housing.    USE - Wooden composite biomass gasifier for use in an industry field for generating combustible gas.    ADVANTAGE - The gasifier effectively removes the tar and generates the combustible gas by using the wood composite biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a wooden composite biomass gasifier.    Gas generation unit (10)    Gas purification unit (20)    Gas preservation unit (30)    Combustor (40)    Control unit (50)
NOVELTY - The gas-liquor self-flowing circulation hydrogen electrolytic device (10) has a hydrogen outlet which is provided in a liquor storage tank (9). The stainless steel plates are arranged between the upper and lower cover boards. The stainless steel plates are anode plate, cathode plate or neutral plate. An insulation rubber ring is arranged among the stainless steel plates. Each stainless steel plate is drilled with a gas-liquor opening. The cover boards are fixed by bolts. The upper cover board is provided with a gas-liquor outlet. The lower cover board is provided with an electrolyte inlet.    USE - Gas-liquor self-flowing circulation hydrogen electrolytic device.    ADVANTAGE - Realizes automatic circulation and separation of the gas liquor in the whole system by using the self-flowing hydrogen electrolytic device. Effectively improves the gas outlet efficiency. Reduces the electric consumption and corresponding electrolytic heat.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the gas-liquor self-flowing circulation hydrogen electrolytic device. (Drawing includes non-English Language text).    Liquor storage tank (9)    Gas-liquor self-flowing circulation hydrogen electrolytic device (10)
NOVELTY - Separating acetone, butanol and ethanol via biomass fermentation coupled with pervaporation in situ, comprises using the pre-treated biomass as a fermentation substrate; inoculating with strain acetone, butanol and ethanol (ABE) for fermentation; pumping out fermentation broth in the fermentation tank by a pump and inputting into a pervaporation membrane separator; and collecting by a condenser to obtain the concentrate of condensed acetone, butanol and ethanol.    USE - The process is useful for separating acetone, butanol and ethanol via biomass fermentation coupled with pervaporation in situ (claimed).    ADVANTAGE - In utilizing the process, the inhibition effect of ABE solvent generated during the fermentation process on the growth of micro cell is decreased greatly, and both the production strength and efficiency of ABE fermentation are improved. Moreover, in comparison with the common distillation process, the process also decreases the consumption of energy on separating ABE solvent generated during the fermentation of biomass. Additionally, the production time is shortened; and the production cost of fuel butyl alcohol is also greatly decreased.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the system used in separating acetone, butanol and ethanol via biomass fermentation coupled with pervaporation in situ.
NOVELTY - The disposer has inner and outer sleeves that are arranged with respect to the base and mounted to form an opening in the upper portions such that the diameter of the inner and outer sleeves differs. Several holding barrels are provided in the fermentation chamber formed inside the inner sleeve for accommodating organic waste. A mesh-like cover is arranged with respect to the holding barrels positioned within the fermentation chamber and fixed with respect to the outer sleeves using fixing rings.    USE - Disposer installed in underground, warming room and greenhouse, for processing organic waste such as organic trash and crop waste for generating marsh gas.    ADVANTAGE - Organic waste can be accommodated effectively in the holding barrels so that the organic waste can be processed precisely to generate marsh gas. Structure of the disposer can be simplified at low cost and disposer can be used conveniently and reliably. Insulation of the disposer can be performed reliably and slag can be used effectively as fertilizer. Electricity can be generated appropriately by processing organic waste.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing method of disposer.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the disposer.
NOVELTY - Aerobic composting of organic solid waste in cabin manner at extremely low temperature, involves mixing organic solid waste and compost regulating agent uniformly to obtain compost material, heating compost material in fermenting cabin of closed aerobic compost device until temperature of the compost material is 20-30 degrees C, stopping the heating process and raising the temperature of the composting material naturally for composting, ventilating composting material at regular intervals and turning the piles until compost is completely decomposed.    USE - The method is useful for aerobic composting of organic solid waste in cabin manner.    ADVANTAGE - The temperature of piles of compost can be increased rapidly and cost-effectively at extremely low temperature. The method does not cause secondary pollution and is environmental-friendly.    DETAILED DESCRIPTION - Aerobic composting of organic solid waste in cabin manner at extreme low temperature, involves (a) mixing organic solid waste (55-80 %mass) and compost regulating agent uniformly to obtain the compost material, where amount of the compost material is 0.5-2.5 times the volume of organic solid waste, (b) adding the compost material in fermenting cabin of a closed aerobic compost device, (c) heating the bottom surface of the fermenting cabin until the temperature of the compost material is 20-30 degrees C, (d) stopping the heating process and raising the temperature of the composting material naturally for composting, (e) ventilating composting material every 30 minutes for 10 minutes each time, where air used for ventilation is 0.05-2 m3 pile.hour, (f) turning the piles when the temperature of the compost is higher than 50 degrees C every 48 hours and when temperature of compost is reduced to 40 degrees C until the compost is completely decomposed.
NOVELTY - Garbage is coarsely crushed, and inorganic substances are removed. The garbage is crushed, and grain diameter is controlled to less than 10 cm. Crushed garbage is dried, and iron is removed from dried garbage. Garbage is further crushed and transferred to cracking furnace, and gas-liquid mixed liquid and carbon mixture are produced. The mixed liquid is separated by a gas-liquid separator to obtain combustible gas and mixed liquid. Combustible gas is reclaimed to dry the garbage or using combustible gas as combustible gas source. Thus, processing of garbage is enabled.    USE - Processing of garbage.    ADVANTAGE - The garbage is quickly and efficiently processed.    DETAILED DESCRIPTION - Garbage is coarsely crushed, and inorganic substances including stone, brick, concrete and sand are removed. The garbage is conveyed to a garbage crushing machine by a conveyer, and grain diameter is controlled to less than 10 cm. The crushed garbage is dried, and water content is set to 30-25%. Iron is removed from dried garbage. The garbage is further crushed, and grain diameter is controlled to less than 2.5 cm. The crushed garbage is transferred to cracking furnace, and gas-liquid mixed liquid and carbon mixture are produced. The gas-liquid mixed liquid is separated by a gas-liquid separator to obtain combustible gas and mixed liquid. The temperature of cooling water is maintained at temperature of less than 15 degrees C, during separation. Oil and water are separated from the liquid mixed solution at normal temperature under normal pressure to obtain tar substances and water. The combustible gas is reclaimed to dry the garbage by the garbage drying machine or using combustible gas as combustible gas source. Thus, processing of garbage is enabled. An INDEPENDENT CLAIM is included for cracking furnace, which has a furnace main portion, a carbon mixture outlet and a gas-liquid mixture outlet.
NOVELTY - The method involves utilizing the sludge power generator flue for the biogas residue drying process. The dried flue is water-washed using a water-washing tower. The washing water is returned to a sludge digestion tank. The hot water is recycled through the heat exchanger by a biogas power generator. The flue of a sludge digestion roaster is used for the biogas residue drying process. The back-pressure steam of the turbine is used by air heat exchanger. The hot air is used for the biogas residue drying process.    USE - Cyclic power generation method using sludge energy.    ADVANTAGE - The environment protection and energy utilization effect can be improved. The recycling cost is reduced. The production efficiency can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram illustrating the cyclic power generation method. (Drawing includes non-English language text)
NOVELTY - The generator has a water inlet pipe (2) and a steam outlet pipe connected between an electrolytic cell and water case. A separator (8) is located near to the shell, and a water inlet groove (13) is arranged between the separator and the shell of electrolytic cell. The upper end of water inlet groove is connected with the water inlet pipe. A water passage (14) is provided between the lower end of the separator and bottom portion of the shell. The electrode plates (15) are clamped in an installation groove opened on the shell and separator at both ends.    USE - Hydrogen and oxygen generator installed in engine of vehicle.    ADVANTAGE - The combustion of fuel can be supported effectively and the thermal efficiency of the hydrogen and oxygen generator can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen and oxygen generator.    Water inlet pipe (2)    Separator (8)    Water inlet groove (13)    Water passage (14)    Electrode plate (15)
NOVELTY - The system has impervious wall, infiltration bed, ventilation pipe, water-collecting pipe, water-distributing tank and water-distributing pipe. The ventilation pipe is inserted in infiltration bed installed in impervious wall. The water-collecting pipe is installed at bottom of infiltration bed to collect sewage purified under action of matrix, microorganism and plant. A limestone layer is covered on four sides of water-collecting pipe. Water-distributing layers are installed on two sides above water-distributing tank, and are made of non-woven fabrics.    USE - Anti-blocking rapid-infiltration system for sewage treatment.    ADVANTAGE - The simple structure of low operation cost of rapid-infiltration system can be ensured.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the anti-blocking rapid-infiltration system.
NOVELTY - Quinolone carboxylic acid derivative (I) and piperazine derivative (II) are subjected to piperazine condensing reaction in presence of catalyst and water as solvent to obtain quinolone compound (III). The catalyst is cerium trichloride heptahydrate, N,N-carbonyldiimidazole, 4-dimethyl piperidine, tetrabutyl ammonium bromide, benzyltriethyl ammonium chloride, and/or tetrabutyl ammonium hydroxide.    USE - Preparation of quinolone compound.    ADVANTAGE - The method efficiently provides quinolone compound having high productivity without using acid binding agent.    DETAILED DESCRIPTION - Quinolone carboxylic acid derivative of formula (I) and piperazine derivative of formula (II) are subjected to piperazine condensing reaction in presence of catalyst and water as solvent to obtain quinolone compound of formula (I). The catalyst is cerium trichloride heptahydrate, N,N-carbonyldiimidazole, 4-dimethyl piperidine, tetrabutyl ammonium bromide, benzyltriethyl ammonium chloride and/or tetrabutyl ammonium hydroxide.    R1=H or 1-4C alkoxy;    R2,R3=halo;    R4=H;    R5=H, methyl or ethyl;    R6=H or methyl;    X=1-3C alkyl or cyclopropyl;and    R1+X=-(CH)(CH3)-CH2-O- bridge bond, in which carbon is coupled with nitrogen in quinolone ring.
NOVELTY - The device has a positive chamber (5) that is separated from negative chamber (6) through separating film (7). A positive pole (1), silver chloride electrode (3) and shell breaking agitator (4) are arranged in positive chamber. The upper end of agitator is fixed to top cover of positive chamber. An exhausting hole (12) with air inlet, is formed on top cover of positive chamber. The air inlet is connected to air outlet of positive chamber. The positive pole is connected to negative pole (2) in negative chamber, through conducting wire and external resistor (14).    USE - Device for generating electricity using cow dung.    ADVANTAGE - The stable electricity can be generated conveniently by simple structured electricity generating device. The 264mW/M3 of maximum output power can be achieved and output voltage is maintained between 416-456 mV.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for generating electricity using cow dung.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of electricity generating device.
NOVELTY - The destructive distilling and heating pyrolysis system has a heating and insulating layer that is mounted on an outer layer of tank housing. The inner spiral rollers of positive and negative directions and a delivering ring are arranged in the tank housing. The spiral rollers of positive direction are connected by delivering ring are uniformly distributed on a periphery. A heating and cracking pipeline is formed by the inner spiral rollers of the positive and negative directions. A pyrolysis reaction tank is driven and rotated by an external link device.    USE - Destructive distilling and heating pyrolysis system for organic matter and biomass.    ADVANTAGE - The heating pyrolysis pipeline improves the contact area and heating time of the heating matter with high heating efficiency. The heat carrier can cycle in a sealed environment to realize self-sufficiency of energy. The reaction system has high efficiency of using raw material with low energy consumption and environmental friendliness. The system is provided with good controllability, wide application range and long service life.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the destructive distilling and heating pyrolysis system.
NOVELTY - Composition for preventing and treating plant viral diseases, comprises giant knotweed extract liquid and plant-derived surfactant in the weight ratio of (1-6):(2-9), where the plant-derived surfactant comprises (in wt.%): plant protein amino acid solution (10-40), saponin extract liquid (20-50) and tea saponin (100).    USE - The composition is useful for preventing and treating several plant viral diseases.    ADVANTAGE - The composition degrades naturally, does not pollute agricultural product or accumulate toxin in environment and human body, and has less toxicity and residue, hence and the composition is safe to human and livestock. The composition has high activity, is convenient to use and improves the quality of agricultural product.
NOVELTY - A diesel-oil composition comprises base diesel oil containing biodiesel and additive. The additive contains component (A), and arylamine antioxidant and/or hindered phenol antioxidant as component (B). The component (A) is prepared by mixing alkenyl succinimide and low carbonic ester containing hindered phenol and then reacting at 60-200 degrees C for 0.5-20 hours in presence of solvent. The molar ratio of polyene-polyamine in alkenyl succinimide to low carbonic ester containing hindered phenol is 1:0.5-5.    USE - Diesel-oil composition.    ADVANTAGE - The diesel-oil composition has excellent oxidation stability and detergent dispersibility.
NOVELTY - A diesel-oil composition comprises base diesel-oil containing biodiesel and additive. The additive contains component (A), and arylamine antioxidant and/or hindered phenol antioxidant as component (B). The component (A) is prepared by mixing Mannich base with low carbonic ester containing hindered phenol at 50-200 degrees C for 0.5-20 hours in presence of solvent. The Mannich base is obtained by reacting polyolefin phenol, 1-6C aldehyde, and polyene-polyamine. The molar ratio of Mannich base to low carbonic ester containing hindered phenol is 1:0.5-5.    USE - Diesel-oil composition.    ADVANTAGE - The diesel-oil composition has excellent oxidation stability and detergent dispersibility.
NOVELTY - An electric converter (21) has secondary coil that is connected with voltage doubling circuit (1) formed by connecting several voltage doubling units (100). A rotary super-high pressure impulse switch (4) and coaxial fluid treatment cavity (3) are connected in series. The fluid containing micro algae is fed from intake pipe and is discharged from outlet pipe. The cell wall of micro algae is broken by applying the super-high pressure impulse electric field to fluid containing micro algae, when fluid is passed through the discharging gap, so as to extract biodiesel.    USE - Biodiesel preparing device.    ADVANTAGE - The need for using a special device for breaking the cell wall of micro algae can be eliminated, so that manufacturing cost of biodiesel preparing device can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a circuit diagram of the biodiesel preparing device.    Voltage doubling circuit (1)    Coaxial fluid treatment cavity (3)    Rotary super-high pressure impulse switch (4)    Electric converter (21)    Voltage doubling unit (100)
NOVELTY - An organic fertilizer comprises wastewater condensate, and straw, organic waste and/or accessory substance of plant slurry stock.    USE - Organic fertilizer.    ADVANTAGE - The organic fertilizer accelerates the growth of crops, and improves the quality and resilience of crop.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for recycle of wastewater condensate. Black liquor obtained during slurrying using ammonium sulfite is concentrated, to obtain wastewater condensate. The wastewater condensate is mixed with straw, organic waste and/or accessory substance of grass slurry stock and fertilized using carbon and nitrogen in presence of heat, to obtain organic fertilizer.
NOVELTY - A straw biological fire coal contains (in wt.%) carbon powder (40-60), sodium nitrate (4-6), sodium silicate (0.5-1), additive (0.5-21), binding agent (0.2-5) and water (25-45). The straw biological fire coal is obtained by dissolving sodium nitrate in water at 10-35 degrees C to obtain solution. The obtained solution, carbon powder, sodium nitrate, sodium silicate, additive and binding agent are evenly mixed, molded with a molding equipment comprising 7-16 cylindrical holes and dried at natural environment to obtain fire coal.    USE - Straw biological fire coal is used as honeycomb coal and fuel for boiler.    ADVANTAGE - The straw biological fire coal is safe and environmental friendly.    DETAILED DESCRIPTION - A straw biological fire coal contains (in wt.%) carbon powder (40-60), sodium nitrate (4-6), sodium silicate (0.5-1), additive (0.5-21), binding agent (0.2-5) and water (25-45). The straw biological fire coal is obtained by dissolving sodium nitrate in water at 10-35 degrees C to obtain solution. The obtained solution, carbon powder, sodium nitrate, sodium silicate, additive and binding agent are evenly mixed, molded with a molding equipment comprising 7-16 cylindrical holes and dried at natural environment to obtain fire coal. The carbon powder is carbon powder of maize straw, wheat straw, sorghum straw, sesame straw, rice straw, branch straw and weed straw. The additive is sodium hydroxide or sawdust. The binding agent is starch or clay.
NOVELTY - A co-production system consists of an underground coal gasification system coupled to a coal-based energy chemical-product co-production system for converting coal into coal-based energy and chemical products.    USE - Co-production system is used for underground gasification of coal-based energy and chemical products (claimed).    ADVANTAGE - The system enables conversion of coal into clean energy and chemical products, and electric power, implementing use of wastewater, waste gas, and solid waste material, and near-zero release of carbon dioxide.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for co-production method, which involves carrying out underground gasification of coal-based energy to obtain crude synthesis gas, purifying and separating methane from the crude synthesis gas, and synthesizing methanol, methane, glycol, low-carbon alcohol, electric power, and/or dimethyl ether using the co-production system.
NOVELTY - Admixture comprises dehydration absorber, dehydration condensation agent, desiccant, fungicide and soil conditioner.    USE - The admixture is useful for producing fertilizer.    ADVANTAGE - The fertilizer can be produced eco-friendly and economically as it uses food waste, sludge, and livestock excretions as raw materials.
NOVELTY - Moulded fuel contains a dry mixture of wood wastes and wastes from starch production in ratio of 3:1 and lipid-containing animal wastes in the following ratio of components, wt %: said lipid-containing wastes 30-60; mixture of ground solid fuel and starch production wastes - the rest. The lipid-containing wastes are wastes from fish processing, meat processing and bird processing. The method of producing moulded fuel involves selection of components, grinding and mixing the ground solid fuel, moulding the mixture, wherein before grinding, the solid components are separated on vibrating screens into two fractions with particle size less than 8 mm and greater than 8 mm and the latter is taken for grinding. Each fraction is then taken for drying and the components are dried to moisture of 12-16%. The components are then mixed and the mixture is then moulded in an extruder at pressure of 5-10 MPa and temperature of 140-200 degrees C. The ready fuel is packed into sacks.    USE - Chemistry.    ADVANTAGE - Invention enables recycling and utilisation of wastes from food production and improves physical and mechanical properties of the fuel blocks. 5 cl, 3 ex, 1 tbl
NOVELTY - Method involves dropwise addition of diesel fuel to a pelleting press while pressing crushed wood wastes. The method of producing biofuel from wood wastes involves crushing, drying, mixing components and subsequent pressing, wherein the binder and component which reduces the load on the press matrix owing to increase in the slip coefficient between the material and cavities of the matrix is diesel fuel which is added in the following ratio, wt %: wood wastes 99.0-99.9; diesel fuel 0.1-1.    USE - Chemistry.    ADVANTAGE - Higher cost-effectiveness of the technological process without loss of quality characteristics of the obtained biofuel, improved water-repellent properties and higher combustion heat of the biofuel, lower ash content and high wear resistance of the press matrix. 1 ex
NOVELTY - A device comprises inlet pipes (1,2) arranged perpendicular to each other. The inlet pipe opening into a premixing chamber (5) is axially encompassed along with a segment by a jacket (3) including holes (9), which is applied to side of the jacket facing segment (4). Sheathing and section of the inlet pipe form a double pipe, in which pre-mixing of the gaseous media takes place before the entry into the pre-mixing chamber of reformer. Flow direction is adjusted in the sheathing against inflow direction of the inlet pipe.    USE - Device for mixing two gaseous media, preferably air and natural gas in a fuel cell system (claimed).    ADVANTAGE - The device has small and compact construction, and ensures optimum mixing of gas flows and low pressure loss.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic cross-sectional view of the device.    Inlet pipes (1,2)    Jacket (3)    Segment (4)    Pre-mixing chamber (5)    Holes (9)
NOVELTY - The recirculation toilet has a fermentation tank (2), fermentation composite tank (3) and a fermentation sedimentation tank (4). The composite tank has the shape which is narrow in horizontal direction and deep in vertical direction and in which fermentation takes place with higher aerobicity towards the downstream side. The sedimentation and composite tanks are arranged directly above the fermentation tank having the shape which is wide in horizontal direction and shallow in vertical direction.    USE - Complex fermentation method-based recirculation toilet such as temporary lavatory, movable toilet, etc., installed in residence of area where sewerage equipment has not prevailed, park, river bed, hut, etc.    ADVANTAGE - Since excretion such as excrement and paper is processed using a complex fermentation method, its possible to process the excretion effectively, without producing offensive odor and its possible to re-circulate water by allowing to pass through the water processed by the composite tank. The excretion efficiency can be improved in the limited space, so that space-saving can be achieved. The treated water can be re-circulated more safely.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic explanatory view of the recirculation toilet. (Drawing includes non-English language text)    Toilet bowl (1)    Fermentation tank (2)    Fermentation composite tank (3)    Fermentation sedimentation tank (4)    Combination tank (5)
NOVELTY - Manufacture of biomass charcoal involves performing primary dry distillation of biomass forming primary biomass charcoal and dry distillation product, isolating tar from the dry distillation product, mixing tar with primary biomass charcoal, granulating and performing secondary dry distillation.    USE - A manufacture of biomass charcoal.    ADVANTAGE - Has high yield of biomass charcoal.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the manufacture of biomass charcoal.    Primary pyrolysis furnace (1)    Separation apparatus (2)    Mixing apparatus (3)    Granulator (4)    Secondary pyrolysis furnace (5)
NOVELTY - The cell (300) has flow-field plates (310a,310b) which exhibits a cambering in relaxing condition for producing a contact pressure when the plate is assembled in the cell. The plate exhibits inlet and outlet openings for supplying and draining off fuel or oxidant.    USE - Fuel cell or reformer cell.    ADVANTAGE - The amount of applied contact pressure on the gas diffusion layer can be adjusted by the amount of cambering thus the need for applying the contact pressure from the outside of the cell is avoided. The damage of the fuel cell can be prevented since the maximum temperature of the cell is not exceeded. The thermal heat produced while operating the fuel cell can be dissipated and the flow of electrical current can be enabled by improving the electrical and thermal connection of the flow plates.    DESCRIPTION OF DRAWING(S) - The drawings show cross-sectional views of the fuel cell before and after assembly.    Fuel cell (300)    Flow-field plate (310a)    Channel sidewalls (311,311a)    Sealing elements (340a,340b)    Cambered area (350)
NOVELTY - The device has a cold water box (4) connected with a water cooling machine (7) through a cold water pipe (5). A hot water box (3) is connected with the water cooling machine through a hot water pipe (6). A tar collecting box (8) is arranged on a lower side of a fuel gas collecting box (1). The tar collecting box is connected with the fuel gas collecting box through a connection pipe (9). A gas discharging pipe (10) is arranged in a lower side of the tar collecting box. A valve (11) is arranged on a connection pipe and another valve (12) is arranged on the gas discharging pipe.    USE - Tar processing device.    ADVANTAGE - The device is suitable for biomass gasifying process.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a tar processing device.    Fuel gas collecting box (1)    Hot water box (3)    Cold water box (4)    Cold water pipe (5)    Hot water pipe (6)    Water cooling machine (7)    Tar collecting box (8)    Connection pipe (9)    Gas discharging pipe (10)    Valves (11,12)
NOVELTY - The system has a generator room (FC1) in which several fuel cells (CE) are arranged, and a combustion chamber (FC2) arranged above the generator room. A fuel cell module (FCM) has a partial oxidation modifier (RFP) that performs partial oxidation reforming of fuel gas during electric power generation shutdown mode and starting mode. A steam reforming device (RFS) is arranged in an upper portion of combustion chamber, to perform steam reforming of fuel gas in power generating mode.    USE - Fuel cell system e.g. solid oxide fuel cell (SOFC) system.    ADVANTAGE - The non-uniform heat generation in fuel cell or whole fuel cell stack at the time of initialization of operation of fuel cell system, can be prevented. The oxidation of fuel cell is suppressed, and the fuel cell system is transferred to partial oxidation reforming reaction smoothly and efficiently from steam reforming reaction at the time of shutdown mode.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the fuel cell module vicinity of fuel cell system.(Drawing includes non-English language text)    Fuel cell (CE)    Generator room (FC1)    Combustion chamber (FC2)    Fuel cell module (FCM)    Partial oxidation modifier (RFP)    Steam reforming device (RFS)
NOVELTY - A meltable fat-and-oil aerosol composition contains fat-and-oil component having melting point of 10-40 degrees C, and propellant having liquefied petroleum gas or dimethyl ether in which fat-and-oil component is dissolved. The amount of fat-and-oil component is 10-70 %mass with respect to total amount of fat-and-oil component and propellant. A solid discharging material is formed on the skin by heat of vaporization of propellant, and dissolved.    USE - Meltable fat-and-oil aerosol composition is used as body batter e.g. cream for skin care and hair care.    ADVANTAGE - The meltable fat-and-oil aerosol composition has excellent adherence with respect to skin, and effectively changes from solid state to liquid state.
NOVELTY - The method involves generating oxygen in an air separation unit that is supplied with air produced from air compressors driven by a gas turbine. Part of nitrogen is utilized from the air separation unit for mixing with carbon-di-oxide depleted syn-gas plus evaporated water for providing fuel gas for a power producing gas turbine. Part of heat is utilized in the gas turbine exhaust for providing part of heat required for preheating fuel plus oxygen plus steam feeds to a syn-gas generation system.    USE - Method for producing fuel gas mixture from natural gas or hydrocarbons with carbon capture.    ADVANTAGE - The method enables eliminating, minimizing or reducing carbon-di-oxide missions to atmosphere in connection with generating synthesis products. The method enables producing synthesis gas from combination of partial oxidation/gas-heated catalytic reformer plus a steam boiler in a single compact vessel for allowing the system to be modularized at large sizes for minimizing or otherwise reducing erected capital cost.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a power producing method    (2) a hydrogen producing system comprising a partial oxidation reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a synthesis gas generation system.    Synthesis gas generation system (800)    Partial oxidation reactor stage (810)    Burner (812)    Perforated plate (830)    Particulate layer (860)
NOVELTY - A fuel reformer comprises flat type module reactors which produce reformed gas which has hydrogen gas as main component which reforms hydrocarbon type raw fuel and becomes fuel of fuel cell and are equipped with process space inside used by production treatment process of reformed gas, and exterior container which accommodates reactors inside and is filled with granular heat insulating material which insulates reactors from exterior container.    USE - A fuel reformer.    ADVANTAGE - The fuel reformer is simple and can make cost of heat insulation constriction low.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a manufacture of fuel reformer.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the apparatus main body accommodated in exterior container.    Desulfurization process part (1)    Steam production part (2)    Steam reforming part (3)    Combustion part (4)    Denaturation process part (5)
NOVELTY - Density of organic waste and density of supernatant liquid obtained by removing fats and oils from organic waste are measured. The concentration of fats and oils in organic waste supplied to methane fermentation tank (3) is adjusted by calculating the fats and oils concentration of waste based on density. Water for dilution is added to organic waste such that concentration of fats and oils is set to predetermined value. Thus, methane fermentation is enabled.    USE - Methane fermentation method of organic waste containing fats and oils e.g. milk, yoghurt and ice cream.    ADVANTAGE - The methane fermentation of organic waste is stably carried out using simple installation. The generation of odor is prevented.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for methane fermentation apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic block diagram of methane fermentation apparatus. (Drawing includes non-English language text)    Storage tank (1)    Methane fermentation tank (3)    Transfer pumps (4,6)    Organic substance concentration measurement unit (10)    Controller (20)
NOVELTY - A heat transfer or refrigerant composition comprises a first component which is E-1,3,3,3-tetrafluoroprop-1-ene (R1234ze(E)); a second component comprising 3,3,3 trifluoropropene (R-1243zf) or a difluoropropene (R-1252) including R-1252zf, R-1252yf, R-1252ye, R-1252ze, and/or R-1252zc; and a third component including difluoromethane (R32), carbon dioxide (R744), fluoromethane (R41), propene (R1270), propane (R290), and/or fluoroethane (R161).    USE - A heat transfer or refrigerant composition used for a heat transfer device (including automotive air conditioning systems, residential air conditioning systems, commercial air conditioning systems, residential refrigerator systems, residential freezer systems, commercial refrigerator systems, commercial freezer systems, chiller air conditioning systems, chiller refrigeration systems, and commercial, or residential heat pump systems); for a blowing agent; for a foamable composition; and for a sprayable composition (claimed).    ADVANTAGE - The composition has a reduced GWP, has improved coefficient of performance, and has reduced toxicity and acceptable flammability.
NOVELTY - Method of producing methane by two-stage anaerobic digestion of organic feed, involves (a) subjecting organic feed suspension to acidogenesis and methanogenesis in first reactor, (b) collecting effluent from the first reactor, subjecting the effluent to solid/liquid separation, obtaining effluents having high and low concentration of solids, where volatile fatty acid (VFA) concentration in the first reactor is controlled by collection rate, and (c) subjecting effluent having low concentration of solids to acidogenesis and methanogenesis in second reactor.    USE - The method is useful for producing methane.    ADVANTAGE - The method enables to perform semi-continuous or continuous biogas production from organic feed.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) methane production unit, comprising first reactor and second reactor, where the first reactor comprises outlet that is connected to solid/liquid separation unit to the inlet of second reactor, the separation unit has a part that forwards a stream relatively having low concentration of solids to the second reactor, and optionally part that returns stream having high concentration of solids to the first reactor, the reactors comprise acidogens and methanogens, to anaerobically ferment organic feed subjected to the first reactor into methane; and    (2) plant comprising the methane production unit.
NOVELTY - The processor has a combustion chamber providing process heat to a closed gasification chamber (12) having a controlled process air inlet and a crude synthesis gas outlet. The combustion chamber includes a diesel burner (18), a crude synthesis gas feed and combustion air inlet to combust crude synthesis gas. A wet scrubber (44) decontaminates flue gas from the combustion chamber. A process controller (15) controls operation of the diesel burner to reduce contribution of heat by the burner as the heat is provided by combustion of crude synthesis gas in the combustion chamber.    USE - Gasification waste processor i.e. gasifier, for gasification of organic waste in small installation. Uses include but are not limited to ship, apartment building, hospital and residence.    ADVANTAGE - The gasifier can operate in a batch mode to process small batches of waste efficiently for small installations. The gasifier can ensure that the amount of crude synthesis gas produced can be within the capability of the scrubbing equipment by controlling heating of the gasifier and the amount of process air allowed into the gasifier.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a gasification process.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a gasifier.    Closed gasification chamber (12)    Process controller (15)    Diesel burner (18)    Flow transmitter (30)    Wet scrubber (44)
NOVELTY - The hydrogen generation device (100) has a housing (1) which is provided with an electrolytic solution containing water. A photoelectrode (2) in the housing has a surface which is in contact with the electrolytic solution and generates gas by decomposing the water during the irradiation with the light transmitted through the housing. A conductor (3) at the back surface of the photoelectrode has a surface and a groove portion (3a) that extends along the direction of flow of generated gas is in contact with the electrolytic solution.    USE - Hydrogen generation device used in fuel cell and electric power generation system.    ADVANTAGE - As the groove portion in the conductor extends along the direction of flow of generated gas and is in contact with electrolytic solution, the fall of contact area of the surface and the water with the generated gas is suppressed and the hydrogen generation efficiency is improved and as the co-catalyst is arranged in the front portion of a projective convex portion, the coating of the co-catalyst with the generated gas can be reduced and the function of the co-catalyst is exhibited efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the hydrogen generation device.    Housing (1)    Photoelectrode (2)    Conductor (3)    Groove portion (3a)    Hydrogen generation device (100)
NOVELTY - The cooker has a lug boss (5) equipped at a middle lower part of an inner wall (4) of a furnace body (2), and an annular air pipe (6) mounted in the lug boss. A grate (7) is placed on the lug boss, and an inlet pipe (10) is mounted on the annular air pipe and passes through the furnace body. A gas outlet (12) is mounted on an upper part of the furnace body, and a dust removal port (8) is opened on a lower part of the furnace body. A furnace cover (1) is covered on a top part of the furnace body.    USE - Straw gasification cooker.    ADVANTAGE - The cooker has high efficiency, energy conservation function, high practicability, simple structure, low manufacturing cost, better safety and reliability, and is simple and convenient to operate and environment friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a straw gasification cooker.    Furnace cover (1)    Furnace body (2)    Inner wall (4)    Lug boss (5)    Annular air pipe (6)    Grate (7)    Dust removal port (8)    Inlet pipe (10)    Gas outlet (12)
NOVELTY - The reactor has a separation plate (3) provided with three separation plate bodies (3-1) and a guide plate, where the separation plate is made up of cement. The separation plate bodies are vertically arranged on a bottom end face of a reactor body (1). A throttle valve is utilized for adjusting flow quantity of a water cold wall (2). A reaction region (6) is utilized for mixed combustion of coal and residual carbon. Another reaction region (7) is utilized for gasification of coal. A third reaction region (8) is utilized for biomass gasification process.    USE - Biomass and coal gasification combustion circulating fluid bed reactor.    ADVANTAGE - The reactor realizes combustion of coal and residual carbon, coal gasification and biomass gasification at same time, and can effectively reduce environmental pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass and coal gasification combustion circulating fluid bed reactor.    Reactor body (1)    Water cold wall (2)    Separation plate (3)    Separation plate bodies (3-1)    Reaction regions (6, 7, 8)
NOVELTY - An oil-and-fat and alcohol are reacted in presence of solid catalyst, to obtain a reaction liquid (I). The obtained reaction liquid (I) is phase-separated (i) into fatty-acid alkylester phase (Ia) and glycerin phase (Ib), using an oil-water separation film. The oil-and-fat and alcohol contained in the fatty-acid alkylester phase are further reacted in presence of solid catalyst, to obtain fatty-acid alkylester and/or glycerin. The size of hole formed in the oil-water separation film is 20 mu m or less.    USE - Manufacture of fatty-acid alkylester and/or glycerin used for biodiesel fuel, cosmetics and pharmaceuticals.    ADVANTAGE - The fatty-acid alkylester and/or glycerin is economically and efficiently manufactured with high quality and yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing apparatus (1) of fatty-acid alkylester and/or glycerin, which comprises reactor (10) to obtain a reaction liquid (I), phase-separation device (i) to phase-separate fatty-acid alkylester phase (Ia) and glycerin phase (Ib), and reactor (20) to react oil-and-fat and alcohol contained in the fatty-acid alkylester phase in presence of solid catalyst.    DESCRIPTION OF DRAWING(S) - The drawing shows a manufacturing apparatus of fatty-acid alkylester and/or glycerin.    Manufacturing apparatus of fatty-acid alkylester and/or glycerin (1)    Oil-and-fat storage tank (2)    Alcohol storage tank (3)    Reactors (10,20)    Alcohol refining tower (13)
NOVELTY - A zinc anode plate (12) is placed spaced apart from an aluminum cathode plate (14) having multiplicity of apertures (15). The cathode plate is electrically connected to a negative terminal of a direct current electrical power supply by a cathode end connector (18). The anode plate is electrically connected to a positive terminal of the direct current electrical power supply by an anode end connector (24).    USE - Apparatus for producing hydrogen from salt water.    ADVANTAGE - The surface area of the cathode and the amount of hydrogen produced are significantly increased, by connecting the aluminum cathode plate having multiplicity of apertures electrically with the negative terminal of the direct current electrical power supply. Thus, the efficiency of the salt water electrolysis is increased.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing hydrogen from salt water.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the apparatus for producing hydrogen form salt water.    Anode plate (12)    Cathode plate (14)    Apertures (15)    Cathode end connector (18)    Anode end connector (24)
NOVELTY - A microalgae, Navicula oiliticus JPCC DA0580 (FERM BP-11201) capable of producing aliphatic hydrocarbon having 16-26 carbon atoms, is new.    USE - The microalgae capable of producing aliphatic hydrocarbon is useful for producing oil component, dry alga and fuel (all claimed).    ADVANTAGE - The fuel prevents global warming as carbon dioxide is fixed by microalgae.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method (M1) for producing oil component, involves culturing the microalgae;    (2) oil component produced by the above-mentioned method;    (3) dry alga produced by drying the microalgae;    (4) fuel obtained from the microalgae; and    (5) method (M2) for fixing carbon dioxide, involves culturing the microalgae.
NOVELTY - A system consists of vessel containing aqueous solution, anode positioned in the bottom of the vessel, cathode positioned near the top of the vessel and connected to the anode, and electromagnetic energy source which emits day-light energy. The vessel contains photosynthetic aerobic microbial culture comprising microbes having photosynthetic ability and the ability to provide electrons from the electron transfer chain.    USE - System e.g. aerobic solar power microbial fuel cell for generating electricity (claimed).    ADVANTAGE - The system does not use organic substrate as energy source, does not require buffer or exogenous electron transfer mediators and carbon dioxide. The system can be easily setup and maintained under normal atmospheric conditions.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for generating electricity, which involves providing an aqueous solution containing photosynthetic aerobic microbial culture in contact with anode coated with carbon and cathode, and providing electromagnetic energy source to induce electron transfer chain in the culture; and    (2) aerobic solar power microbial fuel cell in which electrical energy is derived from sunlight.
NOVELTY - The device has a heat supply room (27) divided into a lower air heating room (14) and an upper clean heat air room (13) which are provided with a circulating fan (19). A charging cabin and a feeding mechanism (2) are arranged outside the air heating room, and a combustion furnace (3) is arranged in the air heating room. A cyclone separator (15) is arranged between the furnace and a heat exchanger (16). The exchanger is connected with an air leading and discharging pipe (18) that is provided with a speed regulating draught fan (20) and a waster gas port (21) located outside the heat air room.    USE - Straw gasified tobacco leaf curing and heat supplying device.    ADVANTAGE - The device has long combustion duration, adjustable heat supply function and high heat utilizing rate, and is convenient to clean.    DETAILED DESCRIPTION - The combustion furnace is a straw gasified hot air furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a straw gasified tobacco leaf curing and heat supplying device.    Feeding mechanism (2)    Combustion furnace (3)    Upper clean heat air room (13)    Lower air heating room (14)    Cyclone separator (15)    Heat exchanger (16)    Air leading and discharging pipe (18)    Circulating fan (19)    Speed regulating draught fan (20)    Waster gas port (21)    Heat supply room (27)
NOVELTY - An ethanol/water mixed solvent pre-treated biomass is prepared by using ethanol/water mixed solvent to process biomass rich in fibrin in a high-temperature high-pressure reaction kettle for 10-30 minutes; filtering the mixture using a vacuum pump; subjecting obtain filter cake to enzymolysis, saccharification and fermentation; distilling the filtrate and recycling the ethanol; extracting oily matter; drying and dehydrating the extracted oily matter; and adding the recycled ethanol to the residue to obtain fluid fuel.    USE - Method of preparing an ethanol/water mixed solvent pre-treated biomass (claimed).
NOVELTY - Safe application of livestock excrement in intensive farming comprises: adding water to the livestock excrement; composting; using the composted livestock excrement as base fertilizer and spraying compound Bacillus suspension liquid. The preparation of the compound bacillus suspension liquid comprises: mixing brown sugar and yeast cream; heating to boil; adding compound Bacillus powder reagent, sodium chloride, brown sugar and yeast cream which are pre-heated to boil with water; mixing and uniformly stirring; stirring and fermenting until an acid taste is obtained.    USE - The method is useful for the safe application of livestock excrement in intensive farming.    ADVANTAGE - The method: improves the yield and quality of the farm produce; ensures edible safety; improves the number and the diversity of the solid microbes; improves the soil enzymatic activity and the physicochemical property of the soil; and reduces the livestock excrement agricultural zoological risk.    DETAILED DESCRIPTION - Safe application of livestock excrement in intensive farming comprises: adding water (60-70%) to the livestock excrement; composting for 7-10 days in summer and for 15-20 days in winter; and using the composted livestock excrement as base fertilizer, where the used amount of the base fertilizer is 200-300 kg/mu and spraying compound Bacillus suspension liquid 2-3 times during the growing period, where each interval time is 5-10 days. The preparation of the compound bacillus suspension liquid comprises: mixing brown sugar (200-300 g) and yeast cream (400-600 g); heating to boil; adding compound Bacillus powder reagent (400-600 g), sodium chloride (0.2-0.4 kg), brown sugar and yeast cream which are pre-heated to boil with water (40-60 l); mixing and uniformly stirring; stirring and fermenting until an acid taste is obtained.
NOVELTY - The device has high-pressure hydrolyzers connected with an intermediate buffer tank, where the high-pressure hydrolyzers are connected in parallel manner. A heating furnace is connected with a liquefy tower having a rear part that is connected with a high-pressure three-phase separator. A liquid phase outlet of the high-pressure three-phase separator is connected with a heat exchanger and an oil-water separator. A lower part of the oil-water separator is connected with the high-pressure hydrolyzers and an exhausting mouth.    USE - High-pressure continuous tower type biomass liquefaction device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a high-pressure continuous tower type biomass liquefaction device.
NOVELTY - The furnace has an internal layer furnace body (3) arranged in an external layer furnace body (2), and an exhaust port (4) arranged on a furnace wall of the internal layer furnace body. A gas channel (5) is fixed between the internal layer furnace body and the external layer furnace body. A wind inlet (1) is arranged at an upper part of the external layer furnace body, and a gas outlet (6) is arranged at a bottom of the external layer furnace body. A tar absorption layer (7) is arranged at the bottom of the external layer furnace body.    USE - Double-layered straw gasification furnace.    ADVANTAGE - The furnace reduces the tar exhaust by more than 90 percent and secondary pollution. The furnace allows the user to supplement and process the material randomly in the furnace body operation process for the lower circulation mode.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a double-layered straw gasification furnace.    Wind inlet (1)    External layer furnace body (2)    Internal layer furnace body (3)    Exhaust port (4)    Gas channel (5)    Gas outlet (6)    Tar absorption layer (7)
NOVELTY - Fungicide comprises ethylicin and pyraclostrobin as active contents in a weight ratio of 1-50:1-20.    USE - Fungicide used for preventing fruit tree diseases (claimed), particularly strawberry anthracnose, powdery mildew and root rot, white rot of grape fruit and pear scab.    ADVANTAGE - The fungicide is cost-effective, eco-friendly and good in preventing multiple diseases, reduces drug resistance due to use of single preparation for long time, has synergistic effect and low toxicity, and ensures improved treatment effect and increased fungicide effect for long time, where used amount of the fungicide is reduced.
NOVELTY - The spiral pyrolysis device includes a pyrolysis product collecting system, a feeding system, and a spiral pyrolysis reactor which comprises the circular cylinder sealed by cover at both ends. The biomass feeding pipe and pyrolysis product outlet pipe are arranged on the sidewall of the circular cylinder. The feeding pipe is connected with the feeding cabin, and the outlet pipe is extended to the coke collecting tank. The coke collecting tank is orderly connected to the condenser, the biological oil collecting tank, and the tail gas exhausting pipe by the ventilation pipeline.    USE - Spiral pyrolysis device for biomass.    ADVANTAGE - Performs easy refinement and extraction of chemicals since the device controls the retention time of the biomass accurately, and separately controls the pyrolysis temperature.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic illustration of the spiral pyrolysis device.
NOVELTY - The transmission gear ring kickoff device has lower carbonization chamber which is designed into two segments connected together through a ring-shaped transmission device sealing box. A ring-shaped gap is formed between the two segments of lower carbonization chambers, and the ring-shaped transmission device sealing box is equipped with a transmission ring gear. A kickoff plate penetrates through the ring-shaped gap of lower carbonization chamber to be symmetrically connected to the transmission ring gear.    USE - Transmission gear ring kickoff device for continuous carbonization furnace.    ADVANTAGE - Allows the carbon to be kicked off smoothly with reduced resistance. Uniformly lowers the material layer and carbon layer. Improves the operating performance of the continuous carbonization device and the production efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a transmission gear ring kickoff device for continuous carbonization furnace.
NOVELTY - The blanking device has a horizontal swinging ring (7) arranged in a material barrel. A swinging rod (8) is arranged on the swinging ring, crossing out of the material barrel. The outer end of the swinging rod is connected to a swinging mechanism. Shifting forks (1) and downward-extending vertical rods (6) are connected to the swinging ring. A blanking board (2) is arranged among the vertical rods.    USE - Blanking device used in gasification furnace.    ADVANTAGE - Provides a blanking device which can hermetically finish blanking automatically or manually without opening the cover of the material barrel, and which realizes mechanical operation and compaction of the blanking of the gasification furnace so as to solve the problem of great effort and fire deflection caused by incompact material operated by manpower. Ensures even and stable gas-producing and burning of the gasification furnace, and pushes the upper material in the gasification furnace to burning position, thus avoiding cavitation of fuel and fire deflection and improving the dry distillation effect, biological material and gas-producing effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the blanking device used in gasification furnace.    Shifting forks (1)    Blanking board (2)    Downward-extending vertical rods (6)    Horizontal swinging ring (7)    Swinging rod (8)
NOVELTY - Environment-friendly biomass gasification furnace comprises furnace body, furnace liner, and gasification chamber below the furnace liner. The furnace liner is arranged in the inner cavity of the furnace body. The bottom of the furnace liner is installed with a furnace gate. A waste outlet is provided below the furnace liner. A fuel outlet is arranged above the furnace body. The side wall of the furnace body is provided with a feed inlet. A purifier is provided between furnace gate and waste outlet. Mixed heating chamber is provided between the furnace liner and hollow cavity of furnace body.    USE - Environment-friendly biomass gasification furnace used for preparing clean fuel using biomass, such as waste after agricultural and forest processing.    ADVANTAGE - The fuel in the gasification furnace can be combusted adequately to increase gas production efficiency of fuel and discharge the waste, such as dust after purification. It has simple structure, low cost, safe and reliable operation, and no pollution to environment; and is convenient to assemble.
NOVELTY - An astragaloside IV is prepared by adding acid into total astragaloside saponin solution, acidifying, crystallizing and separating.    USE - Method is used for preparation of astragaloside IV (claimed).    ADVANTAGE - The method is environment friendly, and has good economic performance and high extraction rate.
NOVELTY - Methane production comprises: (a) feeding a material and pre-treating; (b) injecting water or biogas slurry; (c) fermenting; and (d) discharging material after running of anaerobic tank is finished.    USE - The method is useful for producing methane (claimed).    ADVANTAGE - In the method, an organic material with high total solid and content of suspended matter is used as the raw material; the material is prevented from encrustation in the methane producing process with high material degradation ratio and methane yield.    DETAILED DESCRIPTION - Methane production comprises: (a) feeding a material and pre-treating it, directly adding inoculum or conditioner without the need of cutting or crushing the material, mixing and stacking in an anaerobic tank until the fiber of the mixed material is softened, partially decomposing materials of waxiness and pectin, and reaching a certain temperature; (b) injecting water or biogas slurry to the anaerobic tank where the material is stacked, submerging the material in the tank is a standard for the water level, controlling the content of the total solid in the anaerobic tank within a range of 10%-20%, and sealing to ferment; (c) in the fermenting process, the biogas slurry reflowing or adding water every 1-10 days so as to control the variation range of the water level in the anaerobic tank and the water level before sealing fermenting within a range of plus minus 5%, guaranteeing the content of the total solid in the anaerobic tank within a range of 10%-20%, stirring at regular intervals so as to prevent the material from encrustation on a large scale, and collecting the methane at the same time; and (d) discharging the material after running of the anaerobic tank is finished.
NOVELTY - A fluidized bed reactor comprises an amplifying pipe (1), a straight pipe (2), a cone bottom (3), a cyclone separator (4), an internal component (5), a heat exchanging device (6), a production gas outlet (7), a catalyst filling port (8), a heat-transfer medium outlet (9), a gas distributor (10), a heat-transfer medium inlet (11), a raw material inlet pipe (12), and a catalyst discharging port (13).    USE - A fluidized bed reactor used in synthesizing methane (claimed).    ADVANTAGE - The reactor has a rational in design, a balanced bed layer temperature, a low bed layer pressure drop, a high mass transfer heat transfer efficiency, and a large reaction capacity.    DESCRIPTION OF DRAWING(S) - The drawing is a sectional view of the fluidized bed reactor.    Amplifying pipe (1)    Straight pipe (2)    Cone bottom (3)    Cyclone separator (4)    Internal component (5)    Heat exchanging device (6)    Production gas outlet (7)    Catalyst filling port (8)    Transfer medium outlet (9)    Gas distributor (10)    Heat-transfer medium inlet (11)    Raw material inlet pipe (12)    Catalyst discharging port (13)
NOVELTY - A coal tailings biomass solid formed fuel comprises 40-85 wt.% of coal tailings with heat of combustion of more than 2000 kilocalorie, 10-50 wt.% of agricultural organic waste, 1-5 wt.% of combustion improver, and 1-5 wt.% of bond.    USE - The coal tailings biomass solid formed fuel is useful for boiler, kitchen stove, and other fuelling device.    ADVANTAGE - The coal tailings biomass solid formed fuel is steady in heat of combustion and environment-friendly. Moreover, it has social and economical benefits.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a preparation method of the coal tailings biomass solid formed fuel comprising: (a) crushing raw material: crushing the coal tailings with heat of combustion of more than 2000 kilocalorie; (b) weighing materials based on proportion: adding agricultural organic waste, combustion improver, and bond to the coal tailings powder obtained in (a) based on certain proportion; and uniformly mixing; (c) forming mechanically: preparing the mixture in (b) into granular, columnar, spherical, blocked or biomass solid fuel by forming machine; (d) naturally drying or drying by using drying devices; (e) sieving; and (f) measuring and packing.
NOVELTY - A Corynebacterium sp. SG-20 deposited under CGMCC No.3557, is new.    USE - The Corynebacterium sp. SG-20 is useful as active ingredient for preparing a bacterial agent that is used in degrading toxic material, removing chromium (VI), and processing wastewater (all claimed).    ADVANTAGE - The Corynebacterium sp. SG-20 has low producing and using cost, convenient using, comparatively wide degrading spectrum, and good removing effect. Moreover, the strain and the bacterial agent can ensure that the contents of phenol, p-chlorophenol and other organic pollutants and chromium (VI) in the wastewater are accordant with wastewater discharge standard. Additionally, it solves the problem comprising poor effect of removing phenol, p-chlorophenol and other organic pollutant in the chromium-containing organic wastewater, reduces producing and using labor, and lowers producing and using cost; and it is beneficial for protecting ecological environment and protecting health of people.
NOVELTY - The device includes heat insulating layers, each with a thickness of 3 centimeters, provided in four sides of the inner wall of a straw gasifying furnace (6). The same furnace is also equipped with air rotational flow wind supplying systems (5), each arranged at 75 degree angle, and a water seal big feeding opening (4). The furnace further includes four rolling wheels (7). The device further includes a span (17) formed by connecting more than two long strip-shaped steel plate pans.    USE - Straw gasifying and heating adjusting device for tea plant processing.    ADVANTAGE - The device rationally uses the available energy from e.g. corn stem, straw, rice stem, tree branch, sawdust, serving as fuel, solving the issue of low efficiency associated with use of traditional wood or wooden carbon as fuel. The fuel added once can be used for 4 to 5 hours, saving the fuel adding time. The force of flames is conveniently adjusted by rotating the switch, ensuring the quality of processed tea.    DESCRIPTION OF DRAWING(S) - The drawing shows the side view of a straw gasifying and heating adjusting device.    Water seal big feeding opening (4)    Air rotational flow wind supplying systems (5)    Straw gasifying furnace (6)    Rolling wheels (7)    Span (17)
NOVELTY - The device has a supporting layer (2) arranged on bottom of an artificial pond (1). A water filtration layer (3) is arranged above the supporting layer. A fungus layer (4) for eliminating and decomposing containments in sewage is positioned above the water filtration layer. A layer of wetland filler (8) is arranged between the water filtration layer and the fungus layer. Discharge pipes (10) are set is artificial pond and at the bottom of the supporting layer.    USE - Sewage treatment device for vertical flow constructed artificial wetland containing multilayer embedded microorganism.    ADVANTAGE - The sewage can be treated efficiently and quickly so that the removal efficiency is enhanced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the sewage treatment device.    Artificial pond (1)    Supporting layer (2)    Water filtration layer (3)    Fungus layer (4)    Wetland filler (8)    Discharge pipe (10)
NOVELTY - The generator has bed material that enters into secondary bed structure and transferred to primary bed structure to heat the biomass. The heated biomass is transferred into biofuel and synthetic gas is discharged. The synthetic gas enters the secondary bed structure and is mixed with air entering the secondary bed structure, so that the bed material in the secondary bed structure is heated. A separating device is connected with the bed material outlet to separate the biofuel and bed material.    USE - Biofuel generator.    ADVANTAGE - The biomass can be transferred into biofuel by the generator.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biofuel generator.
NOVELTY - The processor has a solid combustible garbage processing unit and solid food garbage processing unit whose rotating components are linked with a motor installed in series inside a case. A gas treatment system is installed at the side bottom of the garbage processor and connected with the pipe of combustible garbage processing unit. An electrical apparatus control box is connected to apparatuses using wires, for inspecting and controlling the working process of each apparatus according to the feedback signals from the sensors.    USE - Energy-recycling domestic garbage processor.    ADVANTAGE - The solid combustible garbage can be automatically converted into combustible gas for storage.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the energy-recycling domestic garbage processor.
NOVELTY - The method involves pumping waste emulsified liquid into a preprocessing tank by adding the calcium chloride and aluminum sulfate. The waste emulsified liquid is transferred into a mechanical air flotation system. The oil-containing matter is recycled to input the waste emulsified liquid into a regulating pool. The sewage from sewage well is pumped into a delivery pool to add sodium silicate to sewage. The precipitate-free sewage is given as input to slant plate oil-separating pool to separate floating oil and to input the sewage into a microorganism purifying system.    USE - Method for processing waste emulsified liquid.    ADVANTAGE - The working cost of the device is reduced by reducing the energy consumption of the device. The area required by the device is reduced. The waste emulsified liquid generated by machine manufacturing and other industries is processed. The waste oil is recycled in large amount. The waste oil recycled can be used for producing protective fat so as to utilize the resources fully.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the device for processing waste emulsified liquid.
NOVELTY - A purifying box has top and bottom portions provided with through holes (17,18). A purifying device (8) having purifying agent (16) is inserted into the gas inlet pipe connector (7) from the connection end of the gas inlet pipe connector using a screw thread. The purifying device is provided with a purifying box and box lid (13) whose outer surfaces are provided with sealing rings (14,15).    USE - Biogas purifying device for fuel gas appliance.    ADVANTAGE - The changing of purifying agent is performed efficiently by conveniently detaching the device, while attaining simplification in structure of device.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the biogas purifying device.    Gas inlet pipe connector (7)    Purifying device (8)    Box lid (13)    Sealing rings (14,15)    Purifying agent (16)    Through holes (17,18)
NOVELTY - The device has a straw crushing device (1) connected with a straw cracking furnace (2) whose upper portion is connected with a dry dust remover (3) in communication with a wet dust remover (4). A gas-holder tank (6) is connected with the furnace through a fractionating tower (7). A liquid storage tank (8) is connected with a comprehensive processing device (12) and a straw stack retting tank (9) connected with a mixing tank (10). The mixing tank is connected with an aerobic digestion tank (11) which is connected with the processing device.    USE - Biomass processing device.    ADVANTAGE - The structure of the biomass processing device is simplified, while increasing the comprehensive processing capacity and the material adaptability of the device. The device is featured with economic and social benefits.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of biomass processing device.    Straw crushing device (1)    Straw cracking furnace (2)    Dry dust remover (3)    Wet dust remover (4)    Gas-holder tank (6)    Fractionating tower (7)    Liquid storage tank (8)    Straw stack retting tank (9)    Mixing tank (10)    Aerobic digestion tank (11)    Comprehensive processing device (12)
NOVELTY - The device comprises gasoline engine (1) and vacuum pump (2) that are arranged on machine frame (5). The vacuum pump is connected with the biogas residue tank housing (3). The machine frame is provided with a protective shade (4) having hat radiating hole (41) in end.    USE - Portable residue pumping device for car.    ADVANTAGE - The structure of the pumping device is simplified. Since the device is compact, the device can be carried easily in mountain areas.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the portable residue pumping device.    Gasoline engine (1)    Vacuum pump (2)    Tank housing (3)    Protective shade (4)    Machine frame (5)    Radiating hole (41)
NOVELTY - The system has a vertical flow constructed wetland pool (29) that is connected with a horizontal underflow constructed wetland pool (30) whose sides of are respectively equipped with a gravel area. The middle portion of pool (30) is base material area. The shallow root plants and deep root plants are planted in the pools (29), and pool (30) respectively. The upper portion and lower portion of pool (29) are provided with water distributing pipe (6) and draining groove (10) respectively.    USE - Composite constructed wetland sewage treatment system.    ADVANTAGE - The system occupies less space, has high sewage processing efficiency, good outlet water quality.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of composite constructed wetland sewage treatment system.    Pre-processing pond (1)    Water distributing pipe (6)    Draining groove (10)    Vertical flow constructed wetland pond (29)    Horizontal underflow constructed wetland pond (30)
NOVELTY - The energy-saving, eco-friendly waste collection device collects food waste and lavatory excrements from urban areas, and wastages from farm markets, to avoid pollution for conserving methane used as energy resource.    USE - Energy-saving, eco-friendly waste collection device.    ADVANTAGE - Avoids pollution by collecting wastages, thus conserving methane used as energy resource.
NOVELTY - The pedestal shell cover (2) is fixedly connected at the rear portion of the upper port of the pedestal shell (1) by a rotating shaft. The bottom port of the shell connected with an excrement and urine separator (3) whose bottom is connected with a urine collecting pipeline (4). The rear and upper portions of the separator is connected with an excrement fermenting and processing case (6) and a gas purifying case (7) respectively. The upper portion and bottom port of the case are connected with an exhaust pipe (8) and the upper port of the case respectively.    USE - Water-free closestool for separating and processing excrement and urine used in residential building of sub-district.    ADVANTAGE - The water-free mode is used by close stool, and the fermentation pollution-free treatment is performed in excrement and urine to utilize them without adding processing device respectively, thus the water and energy can be saved, with small investment and also socio-beneficial. The processed excrement and urine are directly made into fertilizer, which can reclaim some expenditure and add benefit of sub-district. The process is controlled by a micro computer procedure so that it is convenient to use.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the closestool.    Pedestal shell (1)    Pedestal shell cover (2)    Excrement and urine separator (3)    Urine collecting pipeline (4)    Excrement fermenting and processing case (6)    Gas purifying case (7)    Exhaust pipe (8)
NOVELTY - The heat exchanger has a radiating pipe whose two ends are extended to the outer portion of a cooling room by the through holes. An inlet of the pipe is connected with the outlet of an electrolytic groove in a peripheral device and an outlet is connected with the inlet of a gas-liquid separating device. A wave line is installed on the outer surface of the pipe. A portion of the pipe is located in the inlet and outlet of the cooling room to act as the spiral structure.    USE - Spiral type cold liquid heat exchanger.    ADVANTAGE - The heat exchanger has good radiating effect that is not easily interfered by the outer environment. The temperature of the electrolyzed gas-liquid mixture is not reduced when preparing hydrogen and oxygen by electrolytic water. The device suited for radiating the liquid, gas and gas-liquid mixture is not corroded.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the spiral type cold liquid heat exchanger.
NOVELTY - A completely mixed reaction pool (7) is connected to water inlet tank (1) through water inlet pump (6), and is connected with sediment pool (14) through a pipeline. The reaction pool is internally provided with a dissolved oxygen (DO) probe (12) and a pH probe (13) which sends data to programmable logic controller (PLC) system (5). A switch of air compressor (9) is closed based on DO and pH value variation characteristic during discontinuous starting process, and opening degree/rotating speed of air compressor is adjusted during stable maintaining process.    USE - Device for realizing and maintaining short-distance nitration in domestic sewage and wastewater.    ADVANTAGE - DO concentration of reaction pool is controlled within optimized range. Quick starting and stable maintenance of the short-distance nitration can be realized. Aeration energy consumption can be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of realizing and maintaining short-distance nitration in urban domestic sewage and wastewater.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for realizing and maintaining short-distance nitration in domestic sewage and wastewater.    Water inlet tank (1)    PLC system (5)    Water inlet pump (6)    Reaction pool (7)    Air compressor (9)    DO probe (12)    PH probe (13)    Sediment pool (14)
NOVELTY - Pressure of catalytic dry gas is increased and cooled. 4C Fraction containing n-butane, 1-butene and 2-butene is used as absorbent and 2C fraction and heavy component are absorbed from cooled gas in a main absorption tower. Bottom fluid from tower is supplied to a desorber, and fluid from top of the tower is supplied to reabsorption tower for recycling absorbent. The bottom fluid from tower is supplied to desorber, recycled 2C concentrated gas is obtained from top of desorber, and desorbed 4C fraction absorbent is obtained. The absorbent is cooled and returned to main tower.    USE - Separation of catalytic dry gas.    ADVANTAGE - The separation of catalytic dry gas is easily and economically enabled.    DETAILED DESCRIPTION - Pressure of catalytic dry gas from a refinery cracking device is increased to 4-6 MPa. The compressed dry gas is cooled to 5-15 degrees C. 4C Fraction containing n-butane, 1-butene and 2-butene is used as absorbent and 2C fraction and heavy component are absorbed from the cooled gas in a main absorption tower. Bottom fluid from main absorption tower is supplied to a desorber, and fluid from top of the tower is supplied to reabsorption tower for recycling absorbent. The bottom fluid from tower is supplied to desorber, recycled 2C concentrated gas is obtained from top of desorber, and desorbed 4C fraction absorbent is obtained. The absorbent is cooled and returned to main tower.
NOVELTY - A spacer (3) and water jacket (4) are installed in upper region of device main portion (10). An air channel (5) is formed between the water jacket and outer surface of spacer. An air hole (8) is formed in the air channel. Smoke discharging holes communicate with the smoke discharging channel. An upper heater (13) is placed on upper combustion cavity. The upper heater has lower side that communicates with water jacket and upper side that communicates with main hot water outlet tube (18). A water inlet (14) is formed in lower side of water jacket.    USE - Device for combusting and heating of solid mineral fuel and biomass fuel.    ADVANTAGE - The solid mineral fuel and biomass fuel can be combusted and heated effectively. Thermal efficiency of device is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of the device for combusting and heating of solid mineral fuel and biomass fuel.    Spacer (3)    Water jacket (4)    Air channel (5)    Air hole (8)    Device main portion (10)    Upper heater (13)    Water inlet (14)    Main hot water outlet tube (18)
NOVELTY - Cybernetic plant comprises multiple evaporating units coupled to combustion engines, which promote burning of coal or bagasse.    USE - Cybernetic plant used for producing electrical energy (claimed).    ADVANTAGE - The cybernetic plant enables to produce electrical energy without smoke and noise.    DESCRIPTION OF DRAWING(S) - The drawing shows an exploded perspective view of the cybernetic plant.
NOVELTY - Method for preparing pellet type solid fuel, involves washing aquatic plants, drying washed aquatic plants, pulverizing dried aquatic plant into fine powder, preparing igniter by mixing dried powder of aquatic plant, substrate for fermentation and water, mixing igniter, aquatic plant powder, charcoal dust and starch powder, molding the mixture, carbonizing the molded product and drying the carbonized pellets.    USE - The method is useful for preparing pellet type solid fuel using aquatic plants.    ADVANTAGE - The method is cost-effective and environment-friendly and prevents secondary water pollution in aquatic plants.
NOVELTY - The device has a material hopper (13) whose upper end hole is covered hermetically by a sealing cover (15). The sealing cover is locked by a locking device. An end of a feeding pipe (4) is interconnected with a furnace chamber of a gasification furnace (19) by a feeding hole (1). A feeding shaft (11) is arranged at an inner side of the feeding pipe, where a front end of the feeding shaft is connected with a feeding sheet (12). A post end of the feeding shaft is fixed in the feeding pipe by a bearing and connected with a rocker (10) after extended out from an outer side of the feeding pipe.    USE - Gasification furnace feeding device.    ADVANTAGE - The device is environment-friendly. The device prolongs gas producing and utilizing time optionally according to requirements. The device reduces discharging of smoke and harmful gases. The biomass gasification raw material is added to the device dynamically and continuously according to gas amount and utilization time, thus realizing a filler of the gasification furnace without spark.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a gasification furnace feeding device.    Feeding hole (1)    Feeding pipe (4)    Rocker (10)    Feeding shaft (11)    Feeding sheet (12)    Material hopper (13)    Sealing cover (15)    Gasification furnace (19)
NOVELTY - A water conveyance source e.g. pump (42) supplies water of a water source e.g. tank (44) to an evaporation unit. A control unit (100) controls the water conveyance source. The output of the water conveyance source is increased based on flow volume of water per unit time when the temperature of water vapor generated in the evaporation unit is more than the threshold-value temperature.    USE - Fuel cell system such as solid oxide fuel cell system for electric machine, fixation object, electronic device and vehicle.    ADVANTAGE - The water exhaustion in the evaporation unit by the water rise process can be suppressed. The caulking in the modification unit can be suppressed.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the evaporation unit.    Fuel cell module (3)    Pump (42)    Tank (44)    Control unit (100)    Operation unit (160)
NOVELTY - A suction conveyance portion (4) sucks and conveys the supplied stacking portion. A positioning unit positions supplied stacking portion for suction by the suction conveyance portion. A peeling unit peels the protection sheets on electrolytic membrane surfaces of stacked portion. A negative pressure is applied on support plate (67) of conveyance portion, by controlling rotation speed of blower and the gas diffusion layer is sucked from the support plate. The electrolytic membrane is adhered to gas diffusion layer, and sucked through gas diffusion layer.    USE - Fuel cell manufacturing apparatus.    ADVANTAGE - The suction conveyance of the air permeable gas diffusion layer and electrolytic membrane can be performed efficiently. The generation of protection sheet peeling defects is suppressed, and the reliability of the fuel cell is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the fuel cell manufacturing apparatus.    Suction conveyance portion (4)    Suction hose (20)    Hole (58)    Support plate (67)    Suction hole (68)
NOVELTY - The method involves projecting an electrolytic membrane (1) to the side rather than a gas transmission layer. A separator (7) is projected to the side rather than the electrolytic membrane. The location (1a) which projected the electrolytic membrane is fixed to the gas transmission layer. An integral unit is accommodated in the molding die for molding a gasket to the periphery of membrane electrode assembly (MEA) (3) and gas transmission layer to form a fuel cell.    USE - Manufacturing method of fuel cell (claimed) mounted in electric vehicle.    ADVANTAGE - Since the integral unit is accommodated in the molding die for molding a gasket to the periphery of membrane electrode assembly (MEA) and gas transmission layer to form a fuel cell, the cross leak path of gas can be eliminated effectively, the cross leak durability of the fuel cell can be reduced, and the manufacturing efficiency of the fuel cell can be raised efficiently.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a longitudinal cross sectional view of the fuel cell.    Electrolytic membrane (1)    Projection location (1a)    MEA (3)    Electrode portion (5)    Separator (7)
NOVELTY - The liquid measurement system (100) includes two electrodes (122) arranged oppositely on outer surface of a storage device and formed a capacitor. Charging and discharging circuit (130), electrically connected with the two electrodes, is adapted to charge and discharge the capacitor, cyclically between two voltages to generate an output signal. A processing unit (140), connected with the charging and discharging circuit, obtains a wave number of output signal within a specific time interval and determines surplus status of liquid fuel (150) in containing space (112) according to wave number.    USE - Liquid measurement system for detecting surplus liquid fuel in fuel cell.    ADVANTAGE - Detects a surplus status of liquid fuel in a fuel cell, precisely by counting the number of times of charging and discharging cycles of the capacitor. Prevent electrodes from being corroded by the liquid fuel and prevents malfunction of the fuel cell resulting from the electrodes polluting the liquid fuel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the liquid measurement method.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of a liquid measurement system.    Liquid measurement system (100)    Containing space (112)    Electrodes (122)    Charging and discharging circuit (130)    Processing unit (140)    Liquid fuel (150)
NOVELTY - The method involves pleating a single layer or multilayer planar material. A pleat laminated object (2) which has several pleat portions (2a) is formed, and pleat laminated object end surface (4) in the edge of pleat portions is sealed by a sealing portion (4a). An adhesive agent is supplied inside the pleat laminated object end surface while applying centrifugal force to the outer side with respect to the pleat laminated object end surface. The sealing portion formed in the pleat laminated object end surface is removed.    USE - Manufacturing method of pleat molded object (claimed) used for gas-liquid separation apparatus. Can also be used in gas treatment and liquid processing, hydrogen separation, water vapor separation, ammonia separation, volatile organic compound separation, deoxygenation, nitrogen separation, and used in chemical processing plant, fuel cell, medical treatment, household appliance and engine combustion.    ADVANTAGE - The pleat molded object of high processing capacity is manufactured reliably. The usage amount of the adhesive agent can be ensured reliably and effective area of the pleat surface and pleat portions are achieved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for pleat molded object.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the method of supplying adhesive agent using centrifugal force. (Drawing includes non-English language text)    Pleat laminated object (2)    Pleat portion (2a)    Pleat laminated object end surface (4)    Sealing portion (4a)    Container (16)
NOVELTY - A gas treatment equipment comprises porous body which has through-holes (4a), first and second electrodes (8) which are arranged at one or other of outer side of porous body, high voltage application unit (20) which applies high voltage between first and second electrodes and makes through-hole of porous body generate plasma, abnormal discharge detection unit (21) which detects abnormal discharge generated between first and second electrodes, and control unit (CNT) which controls application of high voltage to decrease generation amount of plasma generated in through-hole of porous body.    USE - Gas treatment equipment for producing hydrogen used for fuel cell.    ADVANTAGE - The equipment suppresses generation of abnormal discharge, continues processing process target and keeps untreated gas from remaining.    DETAILED DESCRIPTION - A gas treatment equipment comprises porous body which has through-holes (4a) which process target gas which is arranged in ventilation path and flows through inside of ventilation path passes, first and second electrodes (8) which are arranged at one or other of outer side of porous body, high voltage application unit (20) which applies high voltage between first and second electrodes and makes through-hole of porous body generate plasma, abnormal discharge detection unit (21) which detects abnormal discharge generated between first and second electrodes, and control unit (CNT) which controls application of high voltage to decrease generation amount of plasma generated in through-hole of porous body when generation of abnormal discharge is detected by abnormal discharge detection unit.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the principal part of gas treatment equipment. (Drawing includes non-English language text).    Through-holes (4a)    Electrodes (8)    High voltage application unit (20)    Abnormal discharge detection unit (21)    Control unit (CNT)
NOVELTY - A foreign material removal apparatus (1) has raw material tank (4) storing biomass (35) to be crushed by crushing part. A trapping part (12) is provided integrally in the stirring part (8) rotatably provided in the raw material tank. The stirring and trapping parts both capture the foreign material contained in the biomass in the raw material tank.    USE - Foreign material removal apparatus used biomass gasification system for removing foreign material in biomass.    ADVANTAGE - Removes foreign material in biomass in raw material tank efficiently, and biomass is supplied to crusher afterwards so that fuel gas can be produced efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic of the stirring part and trapping part of the foreign material removal apparatus.    Foreign material removal apparatus (1)    Raw material tank (4)    Stirring part (8)    Trapping part (12)    Biomass (35)
NOVELTY - The filter (8) has filter portions that are attached to middle of material supply pipe (5) provided between the crushers (4) with a raw material tank (3), and are mutually polymerized so that openings of each filter portion are set orthogonal to each other. A filtration unit filters the foreign material (36) provided in filtration target object (35) stored in the raw material tank.    USE - Filter for removing foreign material such as excretion and wings of bird such as hen, contained in filtration target object such as biomass used as raw material for biomass gasification system used for generating fuel gas.    ADVANTAGE - The foreign material contained in filtration target object can be removed effectively by using the filter.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the raw material supply apparatus. (Drawing includes non-English language text)    Raw material supply apparatus (2)    Raw material tank (3)    Crusher (4)    Material supply pipe (5)    Filter (8)    Filtration target object (35)    Foreign material (36)
NOVELTY - The fuel cell system has a control unit that determines the change rate or variation of the state quantity of the fuel cell so as to determine abnormality generation. The control unit stops the electric power extraction process performed in the electric power extraction unit when the change rate or variation of state quantity of fuel cell is deviated from the permissible range. The monitoring of the state quantity measured value is continued and the next abnormality determination process is performed.    USE - Solid oxide fuel cell system.    ADVANTAGE - The condition of the fuel cell system can be determined easily and accurately.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating the abnormality determination control process. (Drawing includes non-English language text)
NOVELTY - The gas sensor has electrode pins that are penetrated into a through hole formed in a spacer (4), so that the electrode pin is covered by the spacer and made to protrude into a mount base. The leads (5a-5c) are inserted into the spacer and connected to the tip of the electrode pins, so that clamping fixing of the leads is performed using a pressing element (6) and connection region of the leads and electrode pins is not exposed.    USE - Gas sensor for detecting leakage of carbon monoxide gas from combustion apparatus, hydrogen gas in fuel cell electric vehicle, etc.    ADVANTAGE - The heat dissipation efficiency and heat resistance of the gas sensor can be improved, by using a simple structure. The damage of the connection region of the electrode pins due to external stress can be suppressed, since the connection region of the leads and electrode pins is not exposed.    DESCRIPTION OF DRAWING(S) - The drawings show the perspective views of the gas sensor.    Holder (1)    Cap (3)    Spacer (4)    Leads (5a-5c)    Pressing element (6)
NOVELTY - A desulfurizer (3) removes a sulfur component from source gas serving as a raw material for fuel gas containing hydrogen required for power generation of a fuel cell. A flow sensor (17) measures flow rate of source gas passing in upstream of the desulfurizer. One end of a raw material pipe (11) is connected to lower end of desulfurizer while other end is connected to flow sensor. A trap portion (16) prevents catalyst powder or dust in desulfurizer, which has entered through one end of raw material pipe from reaching the flow sensor provided in the middle of the raw material pipe.    USE - Fuel cell power generation system.    ADVANTAGE - The malfunction of the flow sensor can be prevented by preventing the catalyst powder or dust in the desulfurizer from reaching the flow sensor provided in middle of raw material pipe.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the fuel cell power generation system.    Desulfurizer (3)    Booster pump (5)    Raw material pipe (11)    Trap portion (16)    Flow sensor (17)
NOVELTY - The apparatus (100) comprises a hydrogen generator (1) that generates hydrogen containing gas by reforming reaction using raw fuel. A combustor (2) heats the generator. A shut-off valve (8A) interconnects gas flow path (8) which supplies the gas send from the generator to the combustor. An ignition device (5) provided in the combustor, and a controller (30). The controller carries out ignition operation of the ignition device while maintaining the open state of the shut-off valve, when the combustor misfires during generation of hydrogen-containing gas in the startup process.    USE - Hydrogen generation apparatus for fuel cell system (claimed).    ADVANTAGE - The firing operation is performed while connection of gas flow path into which the gas supplied to the combustor from a hydrogen generator flow is maintained, when the combustor is misfired, thus the pressure damage to the hydrogen generation apparatus is reduced conventionally.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the hydrogen generation apparatus.(Drawing includes non-English language text).    Hydrogen generator (1)    Combustor (2)    Ignition device (5)    Flow path (8)    Shut-off valve (8a)    Controller (30)    Hydrogen generation apparatus (100)
NOVELTY - A hydrogen supply device comprises a super water absorbent material for containing water and/or alcohol; and a solid hydrogen fuel directly contacting the super water absorbent material to generate hydrogen.    USE - In a fuel cell (claimed).    ADVANTAGE - The water absorbent materials are combined with solid hydrogen fuel to complete a stable hydrogen supply device. Performance of the hydrogen supply device is not affected by inverting or tilting. Even if inverting or tilting the device, the water contained in the water absorbent materials does not flow out from the device. The membrane electrode assembly film in the fuel cell connected to the hydrogen supply device does not blocked by the water, thereby avoids the fuel cell performance degradation even breakdown.
NOVELTY - A paper waste material is solubilized using methane-fermentation waste liquid. The ratio of content (kg) of paper waste material injected into solubilization tank with respect to volume (L) of paper waste material immersed in methane-fermentation waste liquid is 0.1-0.8. The ratio of volume (L) of paper waste material immersed in methane-fermentation waste liquid with respect to inflow (L/day) of methane-fermentation waste liquid to solubilization tank is 0.2-10.    USE - Solubilization of paper waste material used for producing biogas (claimed).    ADVANTAGE - The method enables efficient solubilization of paper waste material. The biogas is produced efficiently and easily using solubilized paper waste material.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) production of biogas, which involves carrying out methane fermentation of solubilizate of paper base material; and    (2) processing method of paper waste material.
NOVELTY - Method for preparing beta -glucanase and xylanase, involves culturing microorganism belonging to Trichoderma using liquid medium containing beer lees as a carbon source and ammonia nitrogen or amino nitrogen as a nitrogen source.    USE - The method is useful for preparing beta -glucanase and xylanase for degrading or saccharifying cellulose resources (both claimed) such as bagasse, rice straw and straw, which is useful for producing ethanol, and for producing cellulase capable of degrading cellulose resource containing xylan.    ADVANTAGE - The beta -glucanase and xylanase are prepared simultaneously with high productivity and without causing environmental pollution by reducing industrial waste of beer lees. The cellulase is prepared by a cost-effective process.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) liquid medium comprising beer lees as a carbon source and ammonia nitrogen or amino nitrogen as a nitrogen source; and (2) beta -glucanase and xylanase prepared by performing above-cited method.
NOVELTY - A feedstock containing organic material is heated and pressurized to obtain slurry. The obtained slurry and feedstock containing organic material are mixed to obtain mixture. The obtained mixture is heated to obtain renewable fuel. The pressurization is performed such that evaporation of water contained in the slurry is prevented.    USE - Method for converting organic material into renewable fuel e.g. methane.    ADVANTAGE - The method effectively converts organic material into renewable fuel with short period of time.
NOVELTY - A minimum flow rate of hydrocarbon fuel supplied to modifier is set if reforming catalyst layer temperature is greater than temperature conditions of catalyst layer. The fuel flow rate is gradually increased if measured temperature is lesser than or equal to temperature conditions corresponding to fuel flow rate in reformation stop possible state, and if temperature of catalyst layer is greater than temperature conditions of catalyst layer. The anode temperature is made to be lesser than oxidative degradation point if current fuel flow rate is largest fuel flow rate.    USE - Stop method of indirect internal reforming type solid oxide fuel cell.    ADVANTAGE - The modifier can be reformed reliably and the oxidative degradation of the anode can be prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart explaining the stop process of indirect internal reforming type solid oxide fuel cell. (Drawing includes non-English language text)
NOVELTY - Isolated polypeptide (A) having pesticidal activity against Ostrinia nubilalis, Helicoverpa zea, Agrotis ipsilon and Scirpophaga incertulas, is new. (A) is: a polypeptide comprising a fully defined sequence of 670 amino acids of SEQ ID NO: 2 (derived from Bacillus thuringiensis) as given in the specification; or a polypeptide that is encoded by a fully defined sequence of 2013 nucleotide bases of SEQ ID NO: 1 (derived from B. thuringiensis) as given in the specification.    USE - (A) is useful for: controlling or killing lepidopteran pests including at least one of Ostrinia nubilalis, Helicoverpa zea, Agrotis ipsilon and Scirpophaga incertulas (all claimed); and producing its corresponding nucleic acid sequence (via back-translating) which is useful for transforming a crop plant e.g. Zea mays. The efficacy of (A) to kill Scirpophaga incertulas larvae was tested using bioassays. The result showed that (A) exhibited a mortality rate of 100% among the larvae.    ADVANTAGE - (A): has enhanced insecticidal activity against lepidopterans when compared to the corresponding wild-type polypeptide; is biodegradable; and displays activity against wide range of insect pests, including economically important agronomic, forest, greenhouse, nursery, ornamentals, food and fiber, public and animal health, domestic and commercial structure, household, and stored product pests.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a composition comprising (A).
NOVELTY - Use of Chrysophyllum gonocarpum is claimed as alternative fuel and for preparing biofuels, oils, oil products and medicines.    USE - Used as alternative fuel and used for preparing biofuels, oils, oil products and medicines (claimed).    ADVANTAGE - The Chrysophyllum gonocarpum provides biofuel, which has high energy, power and optimum miscibility characteristics for automotive fuels than other vegetable oils and which is superior to the biofuel derived from castor oil and olive oil.
NOVELTY - Preparing environment-friendly catalyst for producing cephalosporin comprises generating the boron trifluoride gas from sulfuric acid, boric acid and hydrofluoric acid, mixing with dimethyl carbonate for the complex reaction to obtain the complex parent liquid, and cooling for separating to collect the solid crystal from the complex parent liquid, which is the environment-friendly catalyst for producing cephalosporin.    USE - The process is useful for preparing environment-friendly catalyst for producing cephalosporin (claimed).    ADVANTAGE - The process has stable performance of complex product by multiplying the effective ingredient content on the product, which solves the defects of product with low concentration.
NOVELTY - Method of disposal of bird droppings includes division of the bird droppings removed from the poultry house into two parts. One part of the droppings without preliminary preparation is used as a biofuel with obtaining thermal energy and concentrated ash constituents for plant nutrition - ash. Burning is carried out in heat generators of known design with a direct or torch burning. Another part of dropping is treated with a stabiliser, held for the time of stabilisation, finally dried to the desired moisture and mixed with dropping ash obtained from the burning of the first part. The resulting mixture of humidity 20-25% is granulated and finally dried to a moisture content of granules 12-14%. Final drying is carried out with air heated by burning the first part of the dropping.    USE - Agriculture.    ADVANTAGE - Full utilisation of poultry manure while obtaining cheap thermal energy and high-quality organic manure.
NOVELTY - The stove has a heat transfer oil type heating tank (1) equipped with a heat conducting oil layer (2), a recycling oil tank, a water lever thermometer and oil temperature meter (4) and a water inlet tube interface (5). A lower biological gas furnace (8) is equipped with an insulating layer (9). A power-failure dual-purpose fan (28) is equipped with a gas tube flange interface (19), a gasifying gas tube (20), an oil-collecting depositing device (21), and a fan flange interface (27).    USE - Heating type biomass gasification stove.    ADVANTAGE - The stove is simple, scientific and rational in structure, convenient to operate, strong in practicality, safe and reliable, clean and sanitary, energy-saving, free from discharge of three wastes, innocuous and pollution-free.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial sectional view of a heating type biomass gasification stove.    Heat transfer oil type heating tank (1)    Heat conducting oil layer (2)    Water lever thermometer and oil temperature meter (4)    Water inlet tube interface (5)    Lower biological gas furnace (8)    Insulating layer (9)    Gas tube flange interface (19)    Gasifying gas tube (20)    Oil-collecting depositing device (21)    Fan flange interface (27)    Power-failure dual-purpose fan (28)
NOVELTY - Charcoal preparation involves utilizing an industrial system (1) with a horizontal transport unit (2). The horizontal transport unit directs load to a vertical lift structure (3). The vertical lift structure is connected to a diagonal ramp (4). The diagonal ramp releases load at top of carbonization unit (5). Turning blades (7), drive motor (8), gas mixer (9), gas cooler (10) and water combustion chamber (11) are also provided. The water combustion chamber is used for producing hot gas, where hot gas is used for pyrolysis.    USE - Method for preparing charcoal (claimed) used for blast furnaces.    ADVANTAGE - The method enables to prepare charcoal with high quality in cost-effective and eco-friendly manner.    DETAILED DESCRIPTION - Charcoal preparation involves utilizing an industrial system with a horizontal transport unit. The horizontal transport unit directs load to a vertical lift structure. The vertical lift structure is connected to a diagonal ramp. The diagonal ramp releases load at top of carbonization unit. Turning blades, drive motor, gas mixer, gas cooler and water combustion chamber are also provided. The water combustion chamber is used for producing hot gas, where hot gas is used for pyrolysis. Wood chips, wood shavings and sawdust are also used in preparation of charcoal.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the charcoal preparation method.    Industrial system (1)    Horizontal transport unit (2)    Vertical lift structure (3)    Diagonal ramp (4)    Carbonization unit (5)    Turning blades (7)    Drive motor (8)    Gas mixer (9)    Gas cooler (10)    Water combustion chamber (11)
NOVELTY - Producing fuel oil by liquefying biomass through water heat comprises: (a) crushing and sieving the biomass raw material to be particle with grain diameter of less than 80 meshes; (b) biomass raw material in step (a) and solvent water are fully mixed to obtain pulp liquid in the mass ratio of 1:2 to 1:8; and (c) the mixing liquid obtained in step (b) is reacted in pulp bed reactor under reducing atmosphere at temperature of 300-450 degrees C and pressure of 5-30MPA for 5-40 minutes.    USE - The method is useful for producing fuel oil by liquefying biomass through water heat (claimed).    ADVANTAGE - The heat value of the obtained oil is as high as that of standard oil, so it can relieve dependence on fossil energy; it can protect environment and reduce production cost along with good social and economic benefit.    DETAILED DESCRIPTION - Producing fuel oil by liquefying biomass through water heat comprises: (a) crushing and sieving the biomass raw material to be particle with grain diameter of less than 80 meshes; (b) biomass raw material in step (a) and solvent water are fully mixed to obtain pulp liquid in the mass ratio of 1:2 to 1:8; and (c) the mixing liquid obtained in step (b) is reacted in pulp bed reactor under reducing atmosphere at temperature of 300-450 degrees C and pressure of 5-30MPA for 5-40 minutes (it is the stop time for the continuous reactor and it is the time for maintaining the pre-set reacting condition in the interval reactor); the product is separated after reaction to obtain fuel oil, solid residue, water and gas; the biomass raw material is wood or straw biomass; and the reducing atmosphere is hydrogen or carbon monoxide.
NOVELTY - A biological liquid fuel comprises (wt.%) methanol (59.8-85), porcellanite (0.01-1), carbon tetrachloride (0.5-1), straw or sawdust pyrolysis oil (10-30), ethyl acetate (0.1-1), tertiary butanol (0.01-0.5), Peregal(RTM: fattyalcohol polyoxyethylene ether) (0.1-1), hydrogen peroxide (0.5-1.5), water (3-6), and alkyl sodium soap (0.1-0.03); where the straw or sawdust pyrolysis oil is prepared by drying straw or sawdust and filling to a fully closed reaction kettle at pressure of 1.0 MPa and at less than 550 degrees C; where the liquid product obtained by cranking straw or sawdust is oil phase.    USE - The biological liquid fuel is useful for industrial and commercial applications.    ADVANTAGE - The biological liquid fuel can protect natural resource and environment. Moreover, it can greatly reduce production cost and use cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a preparation method of the biological liquid fuel comprising: (a) weighing the raw materials based on prescription; (b) putting carbon tetrachloride and straw or sawdust pyrolysis oil to the container and uniformly stirring at 60-70 degrees C for 10-20 minutes; reducing temperature; adding tertiary butanol and stirring at 10-15 degrees C for 10-20 minutes to obtain mixture A; (c) uniformly mixing water with peracetic acid and adding porcellanite and ethyl acetate to prepare mixture B; (d) uniformly mixing the mixture A, mixture B, Peregal(RTM: fattyalcohol polyoxyethylene ether), and alkali sodium soap for 30-60 minutes to obtain mixture C; and (e) adding methanol to the mixture C and stirring for 30 minutes.
NOVELTY - The sludge microwave fast high-temperature compost processor has a sludge inlet (1), a microwave process tunnel, a drum-type compost reactor (10) and a sludge outlet (9). A transmission belt (4) is arranged in the microwave process tunnel. The sludge inlet is arranged on the front segment. The microwave reflectors (2) are arranged on the middle segment. The drum-type compost reactor is arranged on the rear segment.    USE - Sludge microwave fast high-temperature compost processor for use in the process of reduction, detoxification and recycling of sludge or river bottom sediment in sewage treatment plant.    ADVANTAGE - Implements the front microwave process that can crush the sludge, which is beneficial for the post-process of dehydration. Provides the sludge microwave fast high-temperature compost processor which realizes non-pollution of sludge by sterilizing the sludge, and improves the temperature of sludge for the post-process of compost to enter high-temperature period and allows the sludge to be recycled after being composted.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the sludge microwave fast high-temperature compost processor. (Drawing includes non-English language text).    Sludge inlet (1)    Microwave reflectors (2)    Transmission belt (4)    Sludge outlet (9)    Drum-type compost reactor (10)
NOVELTY - Domestic garbage is naturally fermented after filling. Garbage is dug after several years. Non-rotting substance such as plastic material is screened. Heavy metal ion is removed by a series of physical and chemical method, to obtain fertilizer.    USE - Manufacture of fertilizer.    ADVANTAGE - The fertilizer is manufactured with high perishable organic substance content.
NOVELTY - Composition comprises chill-proof nutrient, anti-freeze agent, surfactant and distilled water.    USE - The composition is useful for providing cold resistance to corn seedlings (claimed).    ADVANTAGE - The composition can be sprayed easily, and can be prepared cost-effectively without causing environmental pollution. The composition prevents growth retardation and death of corn plant due to low temperature in Northern region, and the corn plant is not damaged even at 5-10 degrees C.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the composition, which involves dissolving (in g): chill-proof nutrient (0.5-10) in water (10-20 ml) to obtain solution A, dissolving antifreeze agent (5-50) in water (15-60 ml) to obtain solution B, mixing solution A and solution B, adding surfactant (0.02-2), adjusting the volume of solution to 100 ml with water, and uniformly mixing the solution.
NOVELTY - The device has a hard straw cutting machine with a feeder whose back portion is provided with a rotating drum of knife blade. The lower portion of rotating drum is provided with a sieve in an inclined manner and is connected with a discharging machine. A feeding baffle is arranged along the upper portion of feeder and is connected with a comparator. The feeder of the wood chip briquetting machine is connected with a feeding hopper. The feeding hopper is connected with a pressing machine and is provided with a chute connected to discharging machine.    USE - Preparation device of biomass fuel for power plant.    ADVANTAGE - The biomass fuel is prepared in a simple manner with reduced cost and the energy source is saved.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the preparation device.
NOVELTY - Producing dry-scattered type bio-fermenting product comprising strain portion of the fermenting product containing padding portion and zymocyte agent, and two layer of diluted zymocyte agent scattered as substrate on the padding portion with thickness of 20 cm each, where the bio-fermenting product contains two layers of substrates with thickness 40 cm.    USE - The method is useful for producing dry-scattered type bio-fermenting product which is used as feed for animals and poultry, and used along with antibiotic for decomposing urine and excrement of animals.    ADVANTAGE - The bio-fermenting product can be produced simply and inexpensively, and has reduced thickness, and reduces cultivation cost. The bio-fermenting product reduces rearing period of animals and poultry, and is suitable in summer and winter seasons.
NOVELTY - Preparation of fertilizer, involves mixing potassium feldspar powder and potassium carbonate, sintering the raw materials, mixing the obtained materials with water and performing hydrothermal extraction, introducing carbon dioxide to extract, separating carbon from the slurry by liquid-liquid extraction, filtering the material to obtain silicon aluminum filter cake, mixing potassium hydroxide and water uniformly with cake and performing hydrothermal crystallization, filtering and washing the mixture, and parching the filtrate to obtain powder.    USE - The method is useful for preparing fertilizer.    ADVANTAGE - The fertilizer is inexpensive and prepared conveniently without discharging waste gas, water and residue, and hence is environment-friendly.    DETAILED DESCRIPTION - Method for preparing fertilizer, involves (a) mixing potassium feldspar powder and potassium carbonate in the mass ratio of 1:0.5, preferably 1:1 and sintering the raw materials at 750-900 degrees C for 1.5-3 hours, (b) mixing the obtained materials with water in the mass ratio of 1:1-1:2.5, performing hydrothermal extraction at 100-200 degrees C for 1-3 hours, introducing carbon dioxide to extract, subjecting the slurry to liquid-liquid extraction for separating carbon until pH value of the slurry is regulated to 8-9 and filtering the slurry material, and (c) mixing the obtained filter cake with potassium hydroxide and water, stirring the mixture uniformly and performing hydrothermal crystallization at 90-120 degrees C for 12-48 hours, filtering and washing the cake (pH 8.5-9.5) and parching the filtrate to obtain powder containing material of L type molecular sieve and kaliophilite.
NOVELTY - Coal is reacted with high temperature high pressure water and hydrogen, carbon monoxide or oxygen, in a fluidized bed reactor or continuous stirring type reactor to obtain reaction product containing methane.    USE - Manufacture of methane from coal.
NOVELTY - Producing biogas using straw as biomass, involves (a) pretreating the raw material (straw), (b) fermenting the pretreated material, (c) dewatering the obtained primary gas and (d) transferring obtained gas to gas storage cabinet.    USE - The method is useful for producing biogas using straw as biomass.    ADVANTAGE - The biogas is conveniently produced using abundantly available raw materials and has high calorific value.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for device for producing biogas, which comprises stirring pool, feeding unit, anaerobic tank, gas storage cabinet and gas-liquid separator, where inlet of feeding unit is connected with chamber of stirring pool, gas-liquid separator is arranged between the anaerobic tank and gas storage cabinet, gas outlet of anaerobic tank is connected with inlet of gas-liquid separator, and outlet of gas-liquid separator is connected with gas inlet of gas storage cabinet.
NOVELTY - High-quality pearls are crushed to size of 20-200 meshes, and ultra-finely crushed using air-flow crusher. The obtained micron-sized pearl powder is mixed with ionized water, scattering agent, sterilizing agent and suspension-stabilizing agent to form mixed liquid. Then, the mixed liquid is scattered using high-speed cutter, and crushed and ground for 0.5 hour using nanometer crushing grinder, to obtain pearl powder-scattered liquid having grain diameter of 20-200 nm.    USE - Preparation of nanometer pearl-scattered liquid.    ADVANTAGE - The method economically provides nanometer pearl-scattering liquid, and is environmental-friendly.
NOVELTY - A seed kernel of shiny-leaved yellowhorn is ground and a sieve is passed. A sodium hydroxide or potassium hydroxide is dissolved in methanol. A sodium hydroxide-methanol solution or mixture of sodium hydroxide-methanol solution and petroleum ether is added and heated. An extraction of seed kernel of shiny-leaved yellowhorn and synthesis of biodiesel are carried out, and the product is poured, and separated into upper layer containing biodiesel and lower layer containing glycerol. The solvent from biodiesel is distilled, recycled, washed and dried, to obtain biodiesel.    USE - Preparation of biodiesel.    ADVANTAGE - The biodiesel is economically manufactured using simple method.    DETAILED DESCRIPTION - A seed kernel of shiny-leaved yellowhorn is ground and a sieve is passed. A ground seed kernel of shiny-leaved yellowhorn is weighed and subjected to an extraction-synthesis device. 0.4-0.7 %Mass of sodium hydroxide or potassium hydroxide is dissolved in methanol (10-17 volume%). A sodium hydroxide-methanol solution or mixture of sodium hydroxide-methanol solution and petroleum ether is added to the extraction-synthesis device and heated using water bath for 1.5-2 hours. An extraction of the seed kernel of shiny-leaved yellowhorn and synthesis of the biodiesel are carried out, and the product is poured to a separation bucket, allowed to stand and separated into upper layer containing biodiesel and lower layer containing glycerol. The solvent from biodiesel is distilled, recycled, washed and dried, to obtain biodiesel.
NOVELTY - O-phenylenediamine compound is added to a reactor. A mixed solvent of water and alcohol is added under stirring. Aromatic aldehyde is added such that molar ratio of o-phenylenediamine compound to aromatic aldehyde is 1:2-2.5. The mixture is heated, reflown, and weak acid catalyst is added. The mixture is continuously reflown and reacted for 30-90 minutes. The reaction is stopped, and mixture is poured into ice water, stirred, filtered, washed and re-crystallized to obtain 2-substituted aryl-1-substituted phenmethyl benzimidazole compound.    USE - Synthesis of 2-substituted aryl-1-substituted phenmethyl benzimidazole compound used as inhibitor of methionine aminopeptidase.    ADVANTAGE - The phenmethyl benzimidazole compound is quickly produced at high yield by simple method. The catalyst is economically and easily produced.    DETAILED DESCRIPTION - O-phenylenediamine compound is added to a reactor. A mixed solvent of water and alcohol is added in amount of 30-100 times of o-phenylenediamine compound under stirring. Aromatic aldehyde is added such that molar ratio of o-phenylenediamine compound to aromatic aldehyde is 1:2-2.5. The mixture is heated, reflown, and weak acid catalyst is added. The mixture is continuously reflown and reacted for 30-90 minutes. The reaction is stopped, and mixture is poured into ice water, stirred, filtered, washed with water and re-crystallized using ethanol to obtain 2-substituted aryl-1-substituted phenmethyl benzimidazole compound.
NOVELTY - Method (M1) of producing hydrogen and/or methane through fermenting fiber waste, involves (a) crushing fiber waste raw material, (b) mixing the crushed raw material with nutritive salt solution to obtain mixture, and (c) inoculating thermophilic bacteria seed liquid into the obtained mixture, and performing fermentation at 55-65 degrees C and pH of 6.5-7.5.    USE - The method is useful for producing hydrogen and/or methane.    ADVANTAGE - The method is inexpensive and saves energy.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method (M2) for co-producing hydrogen and methane through two-stage of fermenting fiber waste;    (2) device for performing the above-cited method (M1); and    (3) device for performing the above-cited method (M2).
NOVELTY - Pellet fuel is prepared by mixing (in wt.%): corn starch (4-7) or corn (10-15) with the pulverized rice straw or pulverized barley straw (93-96), steaming and maintaining the mixture at a moisture content of 12-15%, and compression molding the mixture.    USE - The pellet fuel is useful for meat roasted seasonings.    ADVANTAGE - The meat roasted seasonings can be produced cost-effectively without causing environmental pollution, as the pellet fuel reduces ignition time during meat roasting. The fuel does not generate harmful gas, and improves taste of the flesh.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing the pellet fuel, which involves steaming the above-mentioned ingredients, maintaining the mixture at 60-65 degrees C and compression molding the mixture.
NOVELTY - Composition comprises 0.01-200 mu g per ml of phytotoxins obtained from pathogenic Streptomyces and an aqueous solution.    USE - Composition for use as elicitor for inducing resistance in plants against fungi, bacteria and viruses (all claimed).    ADVANTAGE - The composition is eco-friendly, does not contain additive, and ensures that its lower dose stimulates the defense mechanisms of plants.
NOVELTY - Invention relates to method for hydrogenation of benzene in adiabatic reactor of shelf type by means of benzene contact with catalyst placed on shelves, at higher temperature and pressure in presence of hydrogen-containing gas supplied to reactor together with benzene in upper part, and also in space between layers of catalyst, characterised by the fact that 50-70 wt % are supplied to upper part of reactor, from initial benzene together with 40-70% of overall volume of hydrogen-containing gas, and remaining part of benzene and hydrogen-containing gas is evenly distributed and supplied together in space between layers of catalyst.    USE - Explosives.    ADVANTAGE - Improved efficiency of process, increased volume speed of raw materials feed, production of cyclohexane of high extent of purity or high-octane component of commercial petrol with minimum content of benzene. 3 cl, 3 ex
NOVELTY - A hydrogen is manufactured by controlling supply amount of water into hydrogen producing material, stopping supply of water, detecting amount of produced hydrogen, computing water consumption equivalent to amount of produced hydrogen, and supplying same amount of water as water consumption to hydrogen producing material after stopping supply of water.    USE - Manufacture of hydrogen for fuel cell system used as power supply for small portable devices.    ADVANTAGE - The method generates hydrogen efficiently and steadily.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a manufacturing apparatus of hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of the manufacture of hydrogen. (Drawing includes non-English language text).
NOVELTY - A hydrogen-producing system comprises hydrogen-producing material container (1) which accommodates hydrogen-producing material, hydrogen-producing material (10) which generates hydrogen by reaction with water, hydrogen-producing amount detection unit which detects hydrogen-producing amount Qty in hydrogen-producing material container, and hydrogen-producing inhibitor which inhibits hydrogen-producing reaction of hydrogen-producing material.    USE - A hydrogen-producing system used for fuel cell system (claimed).    ADVANTAGE - The hydrogen-producing system has high reliability, prevents excessive generation of hydrogen, and is excellent in safety.    DETAILED DESCRIPTION - A hydrogen-producing system comprises hydrogen-producing material container (1) which accommodates hydrogen-producing material, hydrogen-producing material (10) which generates hydrogen by reaction with water, hydrogen-producing amount detection unit which detects hydrogen-producing amount Qty in hydrogen-producing material container, and hydrogen-producing inhibitor which inhibits hydrogen-producing reaction of hydrogen-producing material when hydrogen-producing amount Qty in hydrogen-producing material container satisfies relationship of Qty1 less than or equal to Qty with respect to amount Qty1 of threshold-values set beforehand. Water is supplied in hydrogen producing material container, and hydrogen is generated.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of hydrogen-producing system. (Drawing includes non-English language text).    Hydrogen-producing material container (1)    Liquid selection valve (2)    Hydrogen-producing inhibitor container (3)    Water container (4)    Hydrogen-producing material (10)
NOVELTY - A fuel cell system comprises fuel cell, anode fluid and cathode fluid, purification part (51) which is maintained regularly or irregularly while purifying fluid used for fuel cell, conveyance source (53) which conveys fluid, and control part (7) which controls conveyance source. The flow volume per unit time of fluid which passes purification part is reduced by control part when deterioration of purification part advances. The duration extension process which extends duration of purification part is performed, and maintenance stage of purification part is delayed.    USE - A fuel cell system.    ADVANTAGE - The maintenance stage of purification part of fuel cell system is delayed.    DESCRIPTION OF DRAWING(S) - The drawing shows a conceptual diagram of fuel cell system. (Drawing includes non-English language text).    Control part (7)    Anode (10)    Cathode (11)    Purification part (51)    Conveyance source (53)
NOVELTY - A fuel cell system comprises fuel cell of solid electrolyte form, modifier (RF) which performs steam reforming of fuel gas supplied to fuel cell, exhaust gas which is discharged by burning in fuel gas which passed fuel cell, heat exchanger (HW1) to heat-exchange, water supply unit for supplying water to modifier, control unit which controls water supply unit, water storage tank (WP2a) which stores dew condensation water in heat exchanger as water supplied to modifier, and water level detection unit to detect water level of water storage tank.    USE - A fuel cell system.    ADVANTAGE - The system can carry out running continuation as much as possible even if water level detection unit malfunctioned.    DETAILED DESCRIPTION - A fuel cell system comprises fuel cell of solid electrolyte form, modifier (RF) which performs steam reforming of fuel gas supplied to fuel cell, exhaust gas which is discharged by burning in fuel gas which passed fuel cell, heat exchanger (HW1) to heat-exchange, water supply unit for supplying water to modifier, control unit which controls water supply unit, water storage tank (WP2a) which stores dew condensation water in heat exchanger as water supplied to modifier, water level detection unit to detect water level of water storage tank, and pump which pumps water stored by water storage tank to modifier. The abnormality determination process which judges abnormality presence/absence of water level detection unit is performed according to supply of exhaust gas to heat exchanger aside from initial check of start-up period.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of fuel cell system which consists of part which supplies water to fuel cell module.    Feed pipe (10)    Solenoid valve (101)    Heat exchanger (HW1)    Modifier (RF)    Water storage tank (WP2a)
NOVELTY - The method comprises determining a specification for a fuel volatility characteristic such that a fuel complying with the specification provides an applicable regulatory requirement for the volatility characteristic and a mixture of the fuel with a specified percentage of ethanol provides an applicable regulatory requirement for the volatility characteristic, and blending fuel components by a fuel blending mechanism (21) so that the blend of components meets the specification for the volatility characteristic.    USE - The method is useful for blending the fuel components to provide regulatory requirements for gasoline with or without ethanol, where the gasoline is useful as a fuel for internal combustion engines.    ADVANTAGE - The method is capable of efficiently and economically blending the fuel components with improved yield thus accurately providing the regulatory requirements for gasoline with or without ethanol and producing enough vapor to allow a cold engine to start.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an apparatus for blending the fuel components.    DESCRIPTION OF DRAWING(S) - The diagram shows a block diagram of a fuel blending apparatus.    Fuel blending apparatus (10)    Storage tanks (11, 12, 13, 14)    Fuel blending mechanism (21)    Valve (26)    Electronic control unit. (31)
NOVELTY - A high water content organic waste is desalinized by dehydrating high water content organic waste using screw press with circumferential speed of less than or equal to 4.5 m/min or less, and setting as dechlorination organic waste with chlorine concentration of less than or equal to 2500 ppm and moisture content of less than or equal to 75 mass%.    USE - Desalination of high water content organic waste used as biomass fuel (claimed).    ADVANTAGE - The method obtains dechlorination organic waste with low moisture content easily, and has improved work time in dehydration process, working efficiency and manufacturing cost.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a fuel formation method of high water content organic waste; and    (2) a biomass fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of screw press of desalination/fuel-formation installation.    Shaft (11)    Screw (12)    Screw shaft (13)    Screen (14)    Motor (15)
NOVELTY - An iron oxide is reduced by filling container which stores iron oxide with high pressure hydrogen obtaining by-product in liquid state at same time of chemical reaction of iron oxide with high pressure hydrogen and reducing iron oxide in container.    USE - Reduction of iron oxide for hydrogen producing system (claimed) used for fuel cell system of fuel cell electric vehicle.    ADVANTAGE - The method generates water as liquid and reduces size of the system.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a hydrogen-producing system (1).    DESCRIPTION OF DRAWING(S) - The drawing shows a systematic diagram of the hydrogen-producing system. (Drawing includes non-English language text).    Hydrogen-producing system (1)    High pressure hydrogen tank (2)    Hydrogen station (3)    Piping (4)    Generated water storage container (5)
NOVELTY - A hydrogen supply method involves vaporizing hydrogen storage bodies, making vaporized hydrogen storage bodies contact with catalyst heated by less than or equal to 200 degrees C, performing dehydrogenation, producing hydrogen and dehydrogenation body, removing dehydrogenation body from catalyst, and sending out hydrogen storage bodies which were unreacted at dehydrogenation to system outside at timing which changes with effects of catalyst.    USE - A hydrogen supply method.    ADVANTAGE - The method can produce hydrogen efficiently even if temperature is less than or equal to 200 degrees C, and store and convey hydrogen easily to another apparatus.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a hydrogen supply system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of hydrogen supply system. (Drawing includes non-English language text).    Hydrogen supply system (1)    Vaporization part (11)    Supply part (12)    Catalyst part (13)    Supply timing controller (123)
NOVELTY - A fuel cell system comprises fuel cell of solid electrolyte form, modifier which performs steam reforming of fuel gas supplied to fuel cell, water supply unit for supplying water to modifier, control unit which controls water supply unit, water storage tank which water stores water supplied to modifier, pump which pumps water stored by water storage tank to modifier, flow volume detection unit to detect supply amount of water to modifier with pump, and pressure detection unit to detect pressure of fuel gas in modifier.    USE - A fuel cell system.    ADVANTAGE - The fuel cell system can make smooth and safe transfer to reforming reaction using water from partial oxidation reforming reaction.    DETAILED DESCRIPTION - A fuel cell system comprises fuel cell of solid electrolyte form, modifier which performs steam reforming of fuel gas supplied to fuel cell, water supply unit for supplying water to modifier, control unit which controls water supply unit, water storage tank which water stores water supplied to modifier, pump which pumps water stored by water storage tank to modifier, flow volume detection unit to detect supply amount of water to modifier with pump, and pressure detection unit to detect pressure of fuel gas in modifier. The water supply determination process in which presence or absence of water supply to modifier is determined based on detection result of pressure detection unit is performed after switching pump from halt condition to pumping state and starting pumping of water at the time of starting.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of transfer control to auto thermal reforming reaction of fuel cell system. (Drawing includes non-English language text).    Monitoring of pressure in modifier (S04)    Monitoring of water flow of pipe line (S05)    Controlling of supply capacity (S07)    Water supply determination process (S08)    Judging of whether predetermined time passed (S12)
NOVELTY - A composite processing method of waste water and organic residue involves adding coagulant and separating into solid content part and liquid waste water part, carrying out methane fermentation of solid content part which contains organic residue, extracting and separating methane fermentation residue into solid and liquid, and introducing solid content part into methane fermentation treatment process.    USE - A composite processing method of waste water and organic residue.    ADVANTAGE - The method processes waste water and organic residue easily and efficiently.
NOVELTY - A liquid feeding system (100) has cooling/pressure reducing unit (102) to cool and/or reduce pressure of liquid fuel, pump (105), and gas-liquid separation unit (103). The pump supplies the cooled and/or pressure-reduced liquid fuel, to gas-liquid separation unit. The liquid fuel is desulfurized at high temperature and/or high pressure. The cooling/pressure reducing unit and gas-liquid separation unit are provided in upstream of pump. The gas-liquid separation unit has tank (104) in which gas-liquid separation of liquid fuel is carried out.    USE - Liquid feeding system is used for fuel cell system (claimed).    ADVANTAGE - The liquid feeding system efficiently supplies liquid fuel to fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of fuel cell system. (Drawing includes non-English language text)    Fuel cell system (1)    Liquid feeding system (100)    Cooling/pressure reducing unit (102)    Gas-liquid separation unit (103)    Tank (104)    Pump (105)
NOVELTY - The gas recovery apparatus (10) has a heat exchanger (11) which pre-cools the waste gas containing carbon dioxide using liquefied natural gas, and supplies to a heat exchanger (12). A fuel tank supplies liquid-hydrocarbon mixture to heat-exchanger (12) which vaporizes the mixture. The heat-exchanger (12) liquefies the carbon dioxide gas in waste gas, and discharges waste gas of gas-liquid mixed state to gas-liquid separator (13). The liquefaction carbon dioxide and gas components are separated by the separator.    USE - Carbon dioxide gas recovery apparatus for fuel cell installation of thermal power station (claimed).    ADVANTAGE - The waste gas can be cooled efficiently and the high density carbon dioxide gas can be recovered without the requirement of vacuum pumps. Hence the manufacturing cost and energy cost of carbon dioxide gas recovery apparatus are reduced effectively.    DETAILED DESCRIPTION - A modification unit boils the hydrocarbon gas mixture and generates hydrogen. A heating chamber supplies heat required for steam reforming to the modification unit. The hydrogen separated from liquid hydrocarbon gas mixture is supplied to the anode of the fuel cell, and the carbon dioxide and oxygen are supplied to cathode of fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of carbon dioxide gas recovery apparatus. (Drawing includes non-English language text)    Carbon dioxide gas recovery apparatus (10)    Heat exchangers (11,12)    Gas-liquid separator (13)    Expansion valve (14)
NOVELTY - A heat exchanger (3) generates condensed water and cools gas received from gasifier (1) by heat exchange process relative to thermal medium. A water spraying apparatus (4) sprays water in gas accommodation space of heat exchanger. The heat exchanger discharges tar containing water, after measuring quantity of discharge tar containing water by water quantity measuring device (5). A water quantity control apparatus (6) adjusts quantity of water sprayed into gas accommodation space, such that quantity of water containing discharged tar is set equal to predefined range.    USE - Apparatus for removing tar in gas produced from wood type biomass such as bark, wood chip, etc., by gasifier.    ADVANTAGE - The deterioration of heat exchange performance in heat exchanger by adhesion of tar to the heating surface of heat exchanger is prevented efficiently.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for tar removal processing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the tar removal processing apparatus. (Drawing includes non-English language text)    Gasifier (1)    Tar removal apparatus (2)    Heat exchanger (3)    Water spraying apparatus (4)    Water quantity measuring device (5)    Water quantity control apparatus (6)
NOVELTY - The gasifier (1) has a water supply apparatus (2B) supplying water to biomass from another water supply apparatus (2A). The latter water supply apparatus supplies the water to the biomass before supplying to gasifier. Total water supply amount is set so that moisture content of a moisture layer in a top part of a biomass filled layer is 30 percentage. A heat exchanger (3) condenses the water vapor, and a water quantity measuring device (4) receives gas from the gasifier. The generated gas is cooled with a thermal medium.    USE - Biomass gasifier for use in an industrial application.    ADVANTAGE - The gasifier can prevent tar from adhering to heating surface of the heat exchanger of the gas cooling apparatus, thus discharging the biomass in a smooth manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biomass gasification method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a biomass gasifier.'(Drawing includes non-English language text)'    Biomass gasifier (1)    Water supply apparatus (2A, 2B)    Heat exchanger (3)    Water quantity measuring device (4)
NOVELTY - Seed husk (S) having hardgrove grindability index (HGI) of 30 or less is carbonized at 400-600 degrees C to obtain biomass fuel.    USE - Manufacture of biomass fuel used for powdered coal boiler.    ADVANTAGE - The biomass fuel is manufactured by simple method.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the carbonization apparatus.    Insertion opening (1)    Carbonization portion (2)    Heating portion (3)    Seed husk (S)    Carbonized seed husk (S')
NOVELTY - The electric power generating apparatus (1) has a particulate matter removal unit (3) that removes particulate matter from hydrocarbon type waste gas from gas discharging unit (2). A solid oxide fuel cell (SOFC) (4) produces electric power with mixed gas of waste gas from which particulate matter is removed and oxidizing agent gas.    USE - Electric power generating apparatus for hybrid system.    ADVANTAGE - Since electric power is generated by the SOFC using waste gas from which particulate matter is removed, the utilization of waste gas can be performed effectively and electric power can be generated efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of electric power generating apparatus. (Drawing includes non-English language text)    Electric power generating apparatus (1)    Gas discharging apparatus (2)    Particulate matter removal unit (3)    SOFC (4)    Power supply (5)
NOVELTY - Electrochemically removing hydrogen from a hydrogen-containing reaction mixture using a gas-tight membrane electrode assembly containing at least one selectively proton-conducting membrane and at least one electrode catalyst on each side of the membrane, comprises oxidizing at least part of hydrogen contained on the anode catalyst to form protons on the retentate side of the membrane, where: the protons, after passing the membrane and on the permeate side on the cathode catalyst is (i) reduced to hydrogen and/or (ii) reacted with oxygen to form water.    USE - The removed hydrogen is useful for producing energy, preferably in a combustion chamber or fuel cell.    ADVANTAGE - The method effectively removes hydrogen from the reaction mixture without consuming high equipment costs and energy, hence economical.    DETAILED DESCRIPTION - Electrochemically removing hydrogen from a hydrogen-containing reaction mixture using a gas-tight membrane electrode assembly containing at least one selectively proton-conducting membrane and at least one electrode catalyst on each side of the membrane, comprises oxidizing at least part of hydrogen contained on the anode catalyst to form protons on the retentate side of the membrane, where: the protons, after passing the membrane and on the permeate side on the cathode catalyst is (i) reduced to hydrogen and/or (ii) reacted with oxygen to form water; and the oxygen coming from an oxygen-containing flow is contacted with the permeate side of the membrane. An INDEPENDENT CLAIM is included for a reactor comprising at least a reaction zone and at least a gas-tight membrane electrode assembly, where the reaction zone has an electrode catalyst on a retentate side of the selectively proton-conducting membrane and on each side of the membrane.
NOVELTY - Producing a triglyceride product comprises subjecting a triglyceride feedstock to an alcoholysis reaction with an alcohol having 1 to 6 carbon atoms (C1-C6) to obtain a reaction mixture; separating from the reaction mixture fractions comprising (i) unsaturated C18 fatty acid alkyl esters and (ii) glycerides; and using the fractions (i) and (ii) or their subfractions in a condensation reaction catalyzed by a lipase.    USE - The process is useful for producing a triglyceride product. The fraction of saturated fatty acid alkyl ester is used as fuel or fuel additive (all claimed).    ADVANTAGE - The present invention provides an efficient and less expensive processes to modify triglycerides by reducing the content of saturated lipids and thus obtain consumer products with increased amounts of unsaturated lipids. One advantage of such process is a very efficient use of the triglyceride feedstock. The triglyceride product obtained can be used in products for human consumption and has a higher value in such products than the triglyceride feedstock. And saturated fatty acid alkyl esters obtained as a by-product can be used, e.g., as fuel. The process can proceed without further supply of unsaturated fatty acids from another source.    DETAILED DESCRIPTION - Producing a triglyceride product comprises (a) subjecting a triglyceride feedstock comprising at least 25 mole%, based on the total amount of acyl groups in the triglycerides, unsaturated C18 fatty acid residues to an alcoholysis reaction with an alcohol having 1 to 6 carbon atoms (C1-C6) to obtain a reaction mixture, where the conversion is at least 65%; (b) separating from the reaction mixture produced in step (a) fractions comprising (i) unsaturated C18 fatty acid alkyl esters and (ii) glycerides; and (c) using the fractions (i) and (ii) or their subfractions in a condensation reaction catalyzed by a lipase to produce a triglyceride product comprising at least 80 mole% unsaturated fatty acids.
NOVELTY - The method involves arranging a pair of separator (30,40) on both surfaces of membrane-electrode assembly (10) and sealing element (20) is arranged in the outer periphery to membrane-electrode assembly. Several fuel cells (100) are stacked together and are fastened by fastening element (340). A positioning element for positioning pair of separators is inserted before the completion of fuel cell stacking process. The positioning element is removed after the completion of stacking process.    USE - Manufacturing method of fuel cell stack.    ADVANTAGE - The sealing of the fuel cell stack is performed efficiently. The size and the number of components used for the fuel cell stack are reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the fuel cell stack.    Membrane electrode assembly (10)    Sealing element (20)    Separators (30,40)    Fuel cells (100)    Fuel cell stack (300)    Fastening element (340)
NOVELTY - Extraction of lipids and dehydration of wet algal biomass comprises centrifuging wet algal biomass (210) to increase solid content to 10-40%; mixing centrifuged algal biomass with amphiphilic solvent (220) to obtain mixture; heating mixture until producing dehydrated, defatted algal biomass (230); separating amphiphilic solvent (240) to obtain amphiphilic solvent, water and lipids; evaporating amphiphilic solvent from water and lipids (250); and separating water from lipids (260).    USE - Method of extraction of lipids and dehydrating wet algal biomass (claimed) used for generating biofuels and renewable energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the method for extracting lipids from and dehydrating wet algal biomass.    Centrifuging wet algal biomass (210)    Mixing centrifuged algal biomass with amphiphilic solvent (220)    Heating mixture until producing dehydrated, defatted algal biomass (230)    Separating amphiphilic solvent (240)    Evaporating amphiphilic solvent from water and lipids (250)    Separating water from lipids (260)
NOVELTY - A molded article (30) comprising a concave-convex pattern portion (32) to which a specific concave-convex pattern (3) is transferred, is formed by pressurizing a sheet-shaped material (20) that includes 60-95 vol% of filler and a resinous composition, using a pair of molds (40) having concave-convex pattern comprising concave portions (3a-3c) and convex portions (23a-23d). A dummy pattern comprising dummy convex portions (24a) which compensate for the difference between the total volume of the convex portions and the concave portions is provided in the interior portion of the pair of molds.    USE - Sheet press molding method for manufacturing separator for fuel cell (claimed).    ADVANTAGE - Molded articles with a small sheet thickness deviation is obtained. The separator for fuel cell with small thickness is obtained efficiently, since the patterns for flow paths are formed by pressurizing sheet-shaped material.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing separator for fuel cell.    DESCRIPTION OF DRAWING(S) - The drawings show cross-sectional views of the sheet press molding method for manufacturing separator for fuel cell.    Concave-convex pattern (3)    Concave portions (3a-3c)    Sheet-shaped material (20)    Convex portions (23a-23d)    Dummy convex portions (24a)    Molded article (30)    Concave-convex pattern portion (32)    Mold (40)
NOVELTY - The device (100) has raw material suppliers (102, 103) and water suppliers (104, 105) which cuts off the supply of raw material and water vapor respectively. A controller (140) cuts off the supply of raw material and vapor from the raw material and vapor supplier, and closes the closing device (116). The pressure supplementing operation supplies the vapor from the vapor supplier in the state containing hydrogen with respect to pressure drops inside the device accompanying reduction in the temperature of reforming device after closing of the closing device.    USE - Hydrogen generation device used in fuel cell system (claimed).    ADVANTAGE - The modification catalyst exposed only to the hot water vapor is reduced, and deterioration of modification catalyst by the water vapor oxidation is also suppressed.    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 block diagram of the hydrogen generating apparatus. (Drawing includes non-English language text)    Hydrogen generation device (100)    Raw material suppliers (102,103)    Water suppliers (104,105)    Closing device (116)    Controller (140)
NOVELTY - Products recovering system from a gas stream comprises a cooled chamber having an inlet for receiving the gas stream and for feeding sequential conduit loops within the chamber; a critical orifice following each loop; and an output port in communication with each loop to output a product condensed from the gas stream based upon the physical characteristics of the loop, the sizing of the critical orifice following the loop, and the temperature within the chamber.    USE - Products recovering system from a gas stream for extracting ethane, propane, butane, carbon dioxide, methane, nitrogen or hydrogen (claimed).    ADVANTAGE - The system is operated at a very reducing environment thus having reduced contaminants.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of extracting products from a gas stream.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of injection and collection sides of a well.    Processing gas inlet conduit (20)    Hole (22)    Effluent gas conduit (26)    Overburden (32)    Oil shale body or formation (34)
NOVELTY - A frame-shaped support substrate has an inner side sensor region in which holding sections is provided such that the holding section is extended from the support substrate. Thin film heat sensors (46) are provided on the holding sections and provided with a meandering structure with curve shaped bend portions (D) such that the cross sectional shape of the sensors is trapezoidal. The membrane structure is arranged in the holding section and provided with circular/polygonal through holes distributed and arranged at specific intervals in the sensor region.    USE - Thin film type gas sensor e.g. contact burning gas sensor and micro electro mechanical system type gas sensor used as gas leakage detector used for detecting hydrogen and methane in home and industry.    ADVANTAGE - Since the heat sensor is provided with meandering shape, thermal stress on the sensors is reduced. Thus, distortion of the holding portion holding the sensors is also prevented. Cracking of the sensors and the holding portion is avoided and long life of the sensor is ensured. Bending of holding section by pressure of gas flow can be restrained small. Usability of the sensor can be improved.    DESCRIPTION OF DRAWING(S) - The drawings show enlarged plan view and sectional view of a thin film gas sensor.    Thin film heat sensor (46)    Inner portion of heat sensor (46b)    Linear portion of heat sensor (46c)    Inclined surface of heat sensor (46d)    Bend portion of heat sensor (D)
NOVELTY - A frame shaped support substrate (41) has an inner side sensor region (R) and holding sections consisting of beams (43a-43d) extending from the substrate towards the sensor region. Thin film heat sensors (46a-46d) are provided on the beams. The sensors are provided spaced apart and arranged symmetrically with respect to the centre (B) of the sensor region. The sensors have the same thermal capacity and are mutually connected via metal thin film resistors (45a-45f).    USE - Thin film type gas sensor e.g. contact burning gas sensor/microelectro mechanical system type gas sensor used as gas leakage detector for detecting hydrogen, methane in home, industries etc.    ADVANTAGE - Since the thin film heat sensors are arranged spaced apart and symmetrically relative to centre of the sensor region, concentration of heat at a specific region is avoided. Thus damage to the beams is avoided and the life of the sensor is extended. The resistance of the heat sensors can be increased and hence the sensitivity and the reaction characteristics with respect to the detected gas are improved.    DESCRIPTION OF DRAWING(S) - The drawings show the top and side sectional views of a thin film type gas sensor.    Substrate (41)    Beams (43a-43d)    Thin film resistors (45a-45f)    Thin film heat sensors (46a-46d)    Centre of sensor region (B)    Inner side sensor region (R)
NOVELTY - Provision of combustion fuel comprises collecting by-product (100) of process for producing alcoholic product; and forming briquette from by-product.    USE - Method for provision of combustion fuel for use with barbecues and domestic fires (claimed).    ADVANTAGE - Since the material used to form briquettes is impregnated with alcohol, the briquettes are more flammable and quicker to catch fire. During burning in fire, the pleasant aroma of spirit is released. The alcohol acts as preservative to increase shelf-life and resist mold.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a combustion fuel, comprising briquette formed from by-product of process for producing alcoholic product.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a briquette forming process.    Storage unit (10)    Crusher (20)    Mixer (40)    Container (50)    By-product (100)
NOVELTY - The method involves manufacturing a half fuel cell with a substrate, anode arranged on the substrate and an electrolyte arranged on the anode, where the anode is made of nickel-containing cermet. The half cell is reduced, and a value for leak-tightness of the electrolyte or a value for cell resistance is determined for the half cell. The half cell is coated with a cathode, and the manufactured fuel cell and another fuel cell are built into a fuel cell stack. The cathode of the former fuel cell is sintered during starting the stack.    USE - Method for producing a fuel cell i.e. solid oxide fuel cell, stack.    ADVANTAGE - The method enables assembling the fuel cells to the fuel cell stack in a simple and cost-effective manner, thus avoiding installation of incorrect cells to the fuel cell stack while testing efficiency and/or leak-tightness at the cells.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic flow diagram of a method for producing a fuel cell stack during test of power and leakage.'(Drawing includes non-English language text)'
NOVELTY - Method for preparing fermented neem, involves mixing complex microorganisms, natural enzyme and to be fermented base material, depositing mixture on neem or its processed material, and fermenting the mixture at 60 degrees C or less under agitation.    USE - The method is useful for preparing fermented neem, which is useful as soil improving agent, feed and fertilizer for stimulating growth of agricultural product, livestock, and for protecting agricultural products from insects and microorganism.    ADVANTAGE - The method prepares fermented neem without causing environmental pollution. The prepared fermented neem is convenient to use.
NOVELTY - The device has an induced air pipe (2) connected with a gasification furnace inner cavity (1) and comprising an induced draft fan (3). The induced air pipe is connected with a rinsing pipe (4) whose outlet end is arranged on a lower part of a gasification furnace sandwich layer (5). A combustion outlet (6) is connected with a fuel gas device. A waste gas outlet is provided with a control valve (7). The rinsing pipe is provided with a water vapor check valve (9). A bottom part of a gasification furnace is provided with an adjusting valve (10) that is connected with the inner cavity.    USE - Induced air rinsing anti-backfire device for a biomass gasification furnace.    ADVANTAGE - The device is simple in structure and convenient to use. The device can purify the fuel gas in the furnace and make the fuel in the furnace fully combust and obtain high output, and can prevent the generation of backfire.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial sectional view of an induced air rinsing anti-backfire device.    Gasification furnace inner cavity (1)    Induced air pipe (2)    Induced draft fan (3)    Rinsing pipe (4)    Gasification furnace sandwich layer (5)    Combustion outlet (6)    Control valve (7)    Water vapor check valve (9)    Adjusting valve (10)
NOVELTY - The system has electrolytic cell having inner electrode (2) within outer electrode (4) so as to leave gap between electrodes for containing aqueous electrolytic solution comprising water and silver colloid. The electrode receives voltage less than 3 volts and combustion engine generates electrical signal between 200-300 milliamps. A water distribution system (30) contains and delivers aqueous electrolytic solution between electrodes, and also maintains desired level of solution. The gas exits electrolytic cell by passing through gas collection port (40).    USE - System for generating brown gas for supplying into air entering combustion chamber of internal combustion engine.    ADVANTAGE - The water distribution system connected to base of electrolytic cell is arranged to contain and deliver aqueous electrolytic solution between electrodes and also maintains desired level of solution within electrolytic cell, so that frequent replacement of electrolytes is not required and can be fitted in the cramped engine spaces.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the hydrogen gas generating system.    Inner electrode (2)    Outer electrode (4)    Water distribution system (30)    Water reservoir (37)    Gas collection port (40)
NOVELTY - A 4S-phenyl-3-((5S)-5-(4-fluorophenyl)-5-hydroxypentanoyl)-1,3 oxazolidin 2-one is synthesized by esterifying 4S-phenyl-3-((5R)-5-(4-fluorophenyl)-5-hydroxypentanoyl)-1,3 oxazolidin 2-one with esterification reagent in organic solvent in the presence of Lipase enzyme at 0-100 degrees C to obtain resolution of 4S-phenyl -3((5RS)-5-(4-fluorophenyl)-5-hydroxypentanoyl)-1,3 oxazolidin 2-one; and isolating.    USE - Method of synthesizing 4S-phenyl-3-((5S)-5-(4-fluorophenyl)-5-hydroxypentanoyl)-1,3 oxazolidin 2-one (claimed).    ADVANTAGE - The process is eco-friendly, hazard free and cost effective; has better efficiency and selectivity; and synthesized compound with enantiomeric purity of greater than or equal to 98%.
NOVELTY - Intraorally disintegrating coated tablet contains a medicament which is coated with a coating layer that contains water soluble substance with 5 wt.% or less of polyvinyl alcohol resin which relates to weight of coating layer. The water soluble substance is dissolved in water (10 ml or less) in 1 g or more at 20 degrees C has hydroxyl group in each molecule, and molecular weight of 200 or less per unit of hydroxyl group.    USE - Coated tablet.    ADVANTAGE - The coated tablet is stable, easy to ingest and environmental-friendly. The coated tablet exhibits therapeutic effect and improves external appearance, water-resistant provision, abrasiveness and optical stabilization and prevents crack in tablet. The coating layer disintegrates in intraoral area at a rate of 18 seconds or less, preferably 60 seconds or less.
NOVELTY - Producing triglyceride or fatty acid in a photosynthetic microorganism, involves culturing a modified photosynthetic microorganism comprising exogenous polynucleotides encoding enzymes associated with triglyceride or lipid biosynthesis.    USE - The method is useful for producing triglyceride or fatty acid in photosynthetic microorganism, preferably Cyanobacteria chosen from Synechococcus elongatus PCC 7942, salt tolerant variant of S.elongatus PCC 7942, Synechococcus PCC 7002 and Synechocystis PCC 6803 (all claimed). The triglyceride or fatty acid is used as feedstock for producing biofuels and other chemicals e.g. glycerin which is used in cosmetics and pharmaceuticals.    ADVANTAGE - The polynucleotides in the expression constructs are stably integrated into the photosynthetic microorganism. The microorganism produces an increased amount of triglyceride or fatty acid when compared to wild-type photosynthetic microorganism.
NOVELTY - The catalytic system comprises a product for mixing a proton exchange resin solution with an organic or inorganic salt absorbed at an active carbon surface, and a reducing agent. The metal of the salt is present in the form of cation with a degree of oxidation. The reducing agent is used to minimize the solubility of the water in a metal cation. The active carbon particles are covered with a layer of hydrophobic material. The resin is carbo-fluorinated or non-fluorinated polymer carrying sulfonates or sulfonic acids.    USE - The system is useful for catalyzing a reaction for electrolysis of water in an acid medium for the oxidation of a molecule having weak molecular mass and for producing hydrogen by electrolysis, and in a proton exchange membrane for making a membrane electrode assembly (all claimed), where the hydrogen is useful for generating electricity and in a fuel cell used in automobile industry and electric motor.    ADVANTAGE - The system allows economic and energy efficient catalysis of water electrolytic reaction, ensures safe and high production of hydrogen and electricity in an environmental friendly manner, and avoids the accumulation of sludges and corrosion of electrodes.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a process for preparing a catalytic system;    (2) a membrane electrode assembly;    (3) a modified electrode for electrolysis of water;    (4) an electrolysis cell; and    (5) a process for preparing hydrogen by electrolysis.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a functioning of catalytic system.
NOVELTY - A balanced fertilizer is produced from an anaerobic digestion process by anaerobically digesting a diluted influent slurry and producing a digester effluent; separating water to produce a dewatered solids effluent and liquid effluent; removing toxic compounds from the liquid effluent to produce separated toxic compounds and detoxified liquid effluent; mixing the detoxified liquid effluent with an influent slurry; and combining the separated toxic compounds or converted compounds with the dewatered solids effluent to produce a balanced fertilizer.    USE - Method for producing a balanced fertilizer from an anaerobic digestion process (claimed).    ADVANTAGE - The method can improve the efficiency of the digester during the conversion of a slurry having a high solids concentration of 8-80% solids to gas by the controlled separation and dilution of water recycle.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an anaerobic digestion process comprising:    (A) anaerobically digesting a diluted influent slurry and producing a digester effluent and gas;    (B) separating water from the digester effluent to produce a dewatered solids effluent and a liquid effluent;    (C) removing toxic compounds from the liquid effluent and/or the gas to produce separated compounds and detoxified liquid effluent from the liquid effluent and/or to produce separated compounds from the gas;    (D) mixing the detoxified liquid effluent with influent slurry to produce the diluted influent slurry; and    (E) combining the separated compounds from the liquid effluent and/or the gas with the dewatered solids effluent.
NOVELTY - A culture medium comprises (wt.%) glycerol or mannitol (0.5-20), peptone (1.5-2.5), monopotassium phosphate (0.05-0.1), magnesium sulfate (0.03-0.05), agar-agar (1.5-2), and water (balance); or rice (30-40), glycerol or mannitol (0.5-10), monopotassium phosphate (0.3-0.4), magnesium sulfate (0.15-0.25), and water (balance).    USE - Culture medium used for culturing Cordyceps kyushuensis sporocarp (claimed).    ADVANTAGE - The culture medium has low cost. Culturing method is simple; has short culture cycle, high percentage conversion, low cost, and no pollution and wastes; and can be used for continuous production in batches.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of artificially culturing Cordyceps kyushuensis sporocarp by storing Cordyceps kyushuensis strains on inclined plane of potato dextrose agar (PDA) culture medium in test tube; sterilizing and cooling bottled and activated culture medium, inoculating Cordyceps kyushuensis strains on inclined plane of PDA culture medium, and culturing at 20-30 degrees C for 7-20 days; sterilizing and cooling inducing culture medium to room temperature, and inoculating cultured Cordyceps kyushuensis strains under sterile condition; and putting inoculated Cordyceps kyushuensis in constant-temperature tank, collecting sporocarp, venting, and drying at 40-60 degrees C.
NOVELTY - Organic fertilizer comprises dry components (in wt.%): ammoniated sludge (40-70), active ingredient (0.1-20) and additives (10-55), where ammoniated sludge is treated by ammonification process. The active ingredient is polymerized amino acid, rare earth or their mixture. Additive is inorganic nutrient material, filler or their mixture.    USE - Organic fertilizer used for planting food crop and commercial crop (claimed), and for treating waste matter.    ADVANTAGE - The organic fertilizer has improved nutrient materials and changes organic waste material into its useful resource material. The organic fertilizer improves environment, recycles wastes and develops a new path for producing materials that are utilized in fertilizer production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing the organic fertilizer, which involves:    (A) putting sludge, metal, plastic, glass, sand rock and organic material in a hydrolysis kettle;    (B) reacting the mixture with acid catalyst for 1-2 hours at 80-180 degrees C and 0.8-1.2 megapascal (MPa) to complete hydrolysis reaction, where organic material is animal residue, organic waste or river and lake damaging organism, and acid catalyst is inorganic acid or inorganic strong acid with concentration of 10-20%;    (C) putting the materials in reaction kettle and aerating liquid ammonia (3-16 wt.%) and catalyst (copper salt, ferric salt or ferrous salt in dose of 0.5-1 wt.% of the materials) in the kettle for 1-2 hours at 80-150 degrees C and 0.8-1.2 MPa to finish reaction;    (D) removing water from the materials to obtain solution containing nutrient and solid material with a water content of 30-60%, where solid material is ammoniated sludge; and    (E) obtaining organic fertilizer by using active ingredient and additives through conventional production method.
NOVELTY - A burner unit burns off gas containing hydrogen, source gas or reformed gas using the combustion air supplied by air blower. A source gas supply apparatus supplies source gas to burner unit through modification unit. The amount of combustion air delivered to the burner unit by blower is adjusted during start-up operation of fuel cell system, according to the aggregate amount of source gas supplied to burner unit and estimated amount of source gas out of the source gas components absorbed in the modification catalyst or carbon monoxide reduction catalyst.    USE - Fuel cell system for performing steam reforming of hydrocarbon type raw material such as town gas and liquefied petroleum gas.    ADVANTAGE - Stable start-up operation of the fuel cell system and stable combustion in the burner unit during the start-up operation can be enabled.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart explaining the control process of the fuel cell system.(Drawing includes non-English language text)
NOVELTY - Preparation of compost, involves adding (in parts mass) carbon source (0.01-3) chosen from carbohydrate and lipid to organic waste (100) and composting the mixture under aerobic condition. The ratio of carbon to nitrogen is 15 or less.    USE - The method is useful for preparing compost.    ADVANTAGE - The compost has high nitrogen content and hence improves vegetation. The compost is obtained by utilizing domestic fowl and hence is environment-friendly.
NOVELTY - An electron and ion mixed conductive film contains an electronic conductor and a solid ion conductor.    USE - Electron and ion mixed conductive film is used for unit film used in chemical reactor for manufacturing compound e.g. hydrogen peroxide (all claimed). Can also be used for secondary battery, fuel cell, oxygen permselective membrane and molecule sensor.    ADVANTAGE - The electron and ion mixed conductive film is easily and efficiently manufactured. The external wiring circuit having the mixed conductive film has favorable contact resistance and conducting resistance. Hydrogen peroxide having high purity is produced by simple method.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) unit film (6) having an oxidation catalyst film laminated on one surface of mixed conductive film and reduction catalyst film laminated on other surface of mixed conductive film;    (2) chemical reactor (15). The reactor has an oxidizing chamber (8) and a reduction chamber (7), which are divided by the unit film. The oxidizing chamber is arranged at oxidation catalyst film side of unit film, and reduction chamber is arranged at reduction catalyst film side of unit film;    (3) manufacture of compound, which involves introducing reducing substance and oxidizing substance to oxidizing chamber and reduction chamber, respectively, and producing compound by oxidation-reduction reaction; and    (4) manufacture of hydrogen peroxide, which involves introducing hydrogen donor and oxygen gas to oxidizing chamber and reduction chamber, respectively, and producing hydrogen peroxide.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of chemical reactive.    Unit film (6)    Reduction chamber (7)    Oxidizing chamber (8)    Ion exchange water of reduction chamber (9)    Ion exchange water of oxidizing chamber (10)    Supply ports (11,13)    Exits (12,14)    Chemical reactor (15)
NOVELTY - Converting a sugar-containing biomass material comprises dissolving the sugar-containing biomass material in an inorganic molten salt hydrate; and hydrolyzing components of the sugar-containing biomass material in the inorganic molten salt hydrate medium to form monosaccharides.    USE - Method for converting a sugar-containing biomass material including saccharose, cellulose, lignocellulose, sugar cane or sugar beet into products (i.e. derivatized dianhydro sugars) that are useful as fuel additives and/or fuel substitutes (claimed).    ADVANTAGE - The method has enhanced yield, and reduced formation of byproducts.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram of the method for converting a sugar-containing biomass material.    Lignocellulosic material (1)    Inorganic molten salt hydrate mixture (2)    Hydrochloric acid (3)    Lignin (4)    Reactors (10, 30)
NOVELTY - A polymeric-type solidification agent and dehydrated sludge (12) are mixed and granulated. An addition material (14) which enables germination and growth of plant is mixed with pulverized sludge. The water content of mixture is evaporated, and the mixture of sludge and addition material is fermented. The fermented mixture is pulverized to obtain greening base material (24). The greening base material, seed, fertilizer and binder are mixed to obtain a mixed material. The mixed material and water are mixed, and sprayed on formation level from a blower outlet.    USE - Method used for recycling construction sludge.    ADVANTAGE - The method enables efficient recycling of construction sludge.    DETAILED DESCRIPTION - Sludge discharged from contaminated water-treatment facility (100) e.g. worksite is filtered with a filter and subjected to high-pressure dehydration. A polymeric-type solidification agent and dehydrated sludge are mixed and granulated. The granulated sludge is pulverized. An addition material which enables germination and growth of plant is mixed with pulverized sludge. The water content of mixture is evaporated by heat generated from the mixture with stirring, and the mixture of sludge and addition material is fermented. The fermented mixture is pulverized to obtain greening base material. The greening base material, seed, fertilizer and binder are mixed to obtain a mixed material. The mixed material and water are mixed, and sprayed on formation level from a blower outlet.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the system for recycling construction sludge. (Drawing includes non-English language text)    Dehydrated cake (10)    Dehydrated sludge (12)    Addition material (14)    Greening base material (24)    Contaminated water-treatment facility (100)
NOVELTY - Sludge is spin-dried, to obtain dehydrated sludge which is subjected to composting process by carrying out fermentation using fermenter, to obtain manure. The fermenter has upper portion with insertion opening (11), exhaust portion of dehydrated sludge and lower air-supply portions (21,24,25). The composting process is carried out by providing ventilation from top air-supply portion provided in upper portion of fermenter. Thus, suppression of nitrous oxide during composting process is carried out.    USE - Suppression of nitrous oxide during composting process.    ADVANTAGE - The generation of nitrous oxide during composting process is suppressed with reduced energy consumption, and generation of dew condensation in the apparatus is suppressed.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic sectional view of composting apparatus.    Fermentation tanks (1,4,5)    Insertion opening (11)    Top air-supply portion (12)    Lower air-supply portion (21,24,25)    Composting apparatus (100)
NOVELTY - The furnace has a furnace liner and a supporting block arranged in a furnace shell. A wind inlet pipe, a T-branch pipe and a fan are connected with an outer side of a wind room. A handle is arranged in a middle part of a furnace cover. A pressing rod is connected to a lower part of the handle. Two connecting pipes are arranged at a left side of a purifier and connected with the purifier. An air supply pipe (6) is connected with the side of the purifier. A waste pipe (8) is arranged on the supply pipe. An oxygenation pipe (10) is arranged below the supply pipe and connected with T-branch pipe.    USE - Straw gasification furnace.    ADVANTAGE - The furnace is simple to operate and convenient to use, and has high heating efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a straw gasification furnace.    Air supply pipe (6)    Waste pipe (8)    Oxygenation pipe (10)    Ash outlet cover (11)
NOVELTY - Ethanolic micelles preparation involves utilizing oil-rich micelles.    USE - Method for preparing ethanolic micelles used for producing fatty acid ethyl esters i.e. biodiesel by performing transesterification (all claimed).    ADVANTAGE - The method enables to prepare ethanolic micelles in eco-friendly manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of ethanolic micelles preparation method. (Drawing includes non-English language text).
NOVELTY - Mini biodiesel plant comprises a frame (1), an automatic pump (9), purification filters (36,13,15), a discharge valve, a magnetic field (12), a reactor (5), electronic proportional valve and a booster pump (10). The booster pump is equipped between the reactor and purification filters. Automatic directional control valves, a tank baffle (19), a condenser (31) and a tank (14) are also provided. The condenser is connected to the tank.    USE - Mini biodiesel plant for producing biodiesel (claimed).    ADVANTAGE - The mini biodiesel plant enables to produce biodiesel continuously.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the mini biodiesel plant.    Frame (1)    Reactor (5)    Automatic pump (9)    Booster pump (10)    Magnetic field (12)    Tank (14)    Tank baffle (19)    Condenser (31)    Purification filters (36,13,15)
NOVELTY - Water treatment plant sludge processing involves using (in pts.wt.): sludge (80-100), meadow peat (50-70), saw dust (20), wheat bran (1.5), microbial bacterium (6-10), urine (0.3-0.5), calcium superphosphate (3-5), potassium chloride (1.5-2), magnesium sulfate (1.5-2) and compound microbial bacterium (1.5-2). The sludge, meadow peat and saw dust are mixed and added to putty powder and calcium superphosphate by gradually regulating the water content at 50-60%.    USE - Method for processing sludge of water treatment plant (claimed).    ADVANTAGE - The water treatment plant sludge processing method produces organic fertilizer, which has strong efficacy for fertilizing soil, thus activating biological strain in the soil, improving the soil, which in turn resists draught, retains water and soil, fixing nitrogen, and releasing pralidoxime and potassium functions.    DETAILED DESCRIPTION - Water treatment plant sludge processing involves using (in pts.wt.): sludge (80-100), meadow peat (50-70), saw dust (20), wheat bran (1.5), microbial bacterium (6-10), urine (0.3-0.5), calcium superphosphate (3-5), potassium chloride (1.5-2), magnesium sulfate (1.5-2) and compound microbial bacterium (1.5-2). The sludge, meadow peat and saw dust are mixed and added to putty powder and calcium superphosphate by gradually regulating the water content at 50-60%. The compound microbial bacterium, urine, potassium chloride and magnesium sulfate solution are spread in a fermenting pool. The obtained mixture is fermented for 8-10 days at 55-70 degrees C. The mixture is discharged and dried at 40 degrees C. The mixture is ground into powder through 20-40 meshes sieve to obtain organic fertilizer.
NOVELTY - The furnace has an air inlet pipeline (4) arranged between a furnace body (2) and a cooking range part (3). A purification device (5) is mounted on the air inlet pipeline. A blowing device (6) is provided at a lower part of the furnace body. An ash discharging fire banking plate (7) is fixed with an inner wall of the furnace body. The ash discharging fire banking plate is opened with an ash discharging through hole part (8). A mobile through hole corresponding with a position of the ash discharging through hole is provided on a mobile plate.    USE - Fire dragon energy conservation gasification furnace for cooking and heating water in household.    ADVANTAGE - The furnace has simple structure and better design. The furnace provides better combustion efficiency of the cooking range part by avoiding uneven combustion of the straw gasification furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a fire dragon energy conservation gasification furnace.    Furnace body (2)    Cooking range part (3)    Air inlet pipeline (4)    Purification device (5)    Blowing device (6)    Ash discharging fire banking plate (7)    Ash discharging through hole (8)
NOVELTY - The furnace has a gasification chamber (1) whose upper side is connected to a purifying device (3). An air blower air inlet pipe is divided into a gasification chamber air inlet pipe (9) and a combustion air inlet pipe (10). The chamber and combustion air inlet pipes are respectively connected to the bottom of the gasification chamber and the purifying device. An air outlet at an upper side of the purifying device is connected to an infrared furnace head (15) via a fuel gas pipe (13). A discharge hole of the purifying device is connected to the gasification chamber via a flexible pipe (16).    USE - Clean and effective straw gasification furnace.    ADVANTAGE - The furnace is simple in structure, convenient to use and inexpensive, and ensures high straw use rate, so that the furnace is adapted to be used in rural area. The configuration of the furnace is such that the fuel gas obtained by the straw gasification is used to discharge tar oil obtained after purification of the purifying device to the gasification chamber for recycle, thus simplifying the tar oil recycling process, and avoiding environmental pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic side view of a clean and effective straw gasification furnace.    Gasification chamber (1)    Purifying device (3)    Gasification chamber air inlet pipe (9)    Combustion air inlet pipe (10)    Fuel gas pipe (13)    Furnace head (15)    Flexible pipe (16)
NOVELTY - The structure has an air supplying device (6) i.e. fan, connected with an air inlet through an air inlet pipe. An upper section and a lower section of a furnace body (1) are provided with gas outlets, where each gas outlet is connected with a gas extraction pipe (7). The gas extraction pipe and a reflux inclined pipe (9) are connected with a gas supply main pipe (10) of a stove. The air supplying device is connected with the gas supply main pipe of the stove via an oxygen supply pipe (11). Gas outlets of the reflux inclined pipe are arranged along the gas supply main pipe.    USE - Tar and distilled water reflux re-burning structure for a biomass gasification furnace.    ADVANTAGE - The structure has low tar pollution, easy material preparation function, long burning time, high working efficiency and high gas yield function.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a tar and distilled water reflux re-burning structure.    Furnace body (1)    Air supplying device (6)    Gas extraction pipe (7)    Reflux inclined pipe (9)    Gas supply main pipe (10)    Oxygen supply pipe (11)
NOVELTY - The oven has a porous vaporizable oven hearth (3) inserted to a water heating oven container (2) and a fire gate (6), and separated at intervals to form a secondary air inlet passage (4).    USE - Dual-purpose firewood and coal vaporizable water heating oven.    ADVANTAGE - The heat power generated by fire and extraction of a smoke discharging pipe makes a plenty of air to enter porous vaporizable oven hearth from a firewood adding opening to burn with the firewood when the firewood is added to the porous vaporizable oven hearth from the firewood adding opening. The burning in the porous vaporizable oven hearth is more sufficient under the action of secondary air inlet passage, which has micro-smoke and micro-dust. The oven prevents high energy consumption, flow of water, and has simple structure and high heat efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a dual-purpose firewood and coal vaporizable water heating oven.    Water heating oven container (2)    Porous vaporizable oven hearth (3)    Secondary air inlet passage (4)    Smoke discharging opening (5)    Fire grate (6)
NOVELTY - The gasifier has a combustion chamber surrounded by a circulating water sleeve. A moveable cover plate is arranged at an upper end of the combustion chamber. A fuel automatic feeding device is made of a lifting spiral fuel propeller connected with a fuel box. A fuel elephant trunk is connected with an upper end of the fuel propeller. A disposable air inlet pipe is connected to an outlet of the fuel elephant trunk and a spiral fuel propeller drive motor. An ordinary control circuit controls rotating speed of a motor.    USE - Dust-suppression intelligent and environment-friendly straw compression particle gasifier.    ADVANTAGE - The fuel is added automatically, so as to stabilize combustion state of a furnace and prevent smoke.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a dust-suppression intelligent efficient and environment-friendly straw compression particle gasifier.
NOVELTY - The structure has an air supply device (6) i.e. air blower, connected with a gas inlet by a gas feeding pipe (5). An upper section, a middle section and a lower section of a furnace body (1) are respectively provided with a gas outlet. The gas outlets of the upper, middle and lower sections are respectively connected with gas production pipes (7-9). The gas production pipes are connected with a gas supply bus (10) on a cooking range, where the bus is connected with the air supply device by an oxygen supply pipe (11).    USE - Sectional gas production accelerated circulating oxygen supply structure for a biomass gasifying boiler.    ADVANTAGE - The structure can combust large and hard firewood, and ensures easy preparation of material, long combustion time of furnace body, high working efficiency and high gas output. The structure can avoid gas breaking off phenomenon when the middle section of the furnace body combusts in air.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a sectional gas production accelerated circulating oxygen supply structure.    Furnace body (1)    Gas feeding pipe (5)    Air supply device (6)    Gas production pipes (7-9)    Gas supply bus (10)    Oxygen supply pipe (11)
NOVELTY - The furnace has a feed bucket (1) whose bottom is provided with an air inlet pipe (2) and an inner part is provided with an inner barrel (3) forming a clamping sleeve. An upper opening of the inner barrel is connected with the feed bucket, and the clamping sleeve at a lower end is arranged with a lower plate (12). The inner barrel corresponding to the lower plate is provided with a return pipe (4) to transport ungasified water and tar in the clamping sleeve to the lower cavity of the feed bucket. An air outlet (5) is placed on a side wall of the feed bucket on the return pipe.    USE - Circulating straw gasification furnace.    ADVANTAGE - The furnace allows designing the feed bucket in the form of the clamping sleeve, and dries and gasifies water and tar in the mixed gas to form fuel gas by high temperature in the clamping sleeve and discharges fuel gas. The residual water and tar are returned to the bottom of the feed bucket and re-gasified by a high temperature gasification layer, so as to increase content of carbon monoxide, methane and hydrogen, and gasification efficiency. The cross-shaped air distribution rack is provided for supplying oxygen rationally to the fully closed combustion, so as to realize full combustion of straw, reduce tar content and pollution, save energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a circulating straw gasification furnace.    Feed bucket (1)    Air inlet pipe (2)    Inner barrel (3)    Return pipe (4)    Air outlet (5)    Lower plate (12)
NOVELTY - The device has a box cover (22) installed on a box body (21). An operating hole (23) is formed at an end of the box body. A dust-proof sealing cover (24) is fixed at an edge of the operating hole. An ash receiving port (26) is abutted with the ash outlet that is provided at another end of the box body. A sealing rubber ring (27) is arranged at a surface of the box body. The dust-proof sealing cover is a rubber thin film or a plastic thin film. A handle (28) is arranged on the box cover.    USE - Dust-free ash outlet device for a biomass gasification furnace.    ADVANTAGE - The device effectively prevents the ash from flying.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a dust-free ash outlet device.    Box body (21)    Box cover (22)    Operating hole (23)    Dust-proof sealing cover (24)    Ash receiving port (26)    Sealing rubber ring (27)    Handle (28)
NOVELTY - The feeder has a material discharge element (31) connected with a feed opening of a gasification furnace and a baffle plate (32) for retaining fuel. Shape of the discharge element is matched with shape of the feed opening of the gasification furnace. The baffle is covered on a water sealing groove of the gasification furnace. Shape of the baffle is matched with shape of the gasification furnace. The baffle plate is formed in round or square shape. Diameter of the round baffle plate is larger than or equal to diameter of the furnace body of the gasification furnace.    USE - Leak-proof feeder for a biogenic gasification boiler for combustion of biological materials.    ADVANTAGE - The feeder effectively prevents leakage of fuel from the water sealing groove, so that fuel can be completely fed into the furnace via the feeding opening to obtain smooth feeding process, without affecting the normal operation of the furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a leak-proof feeder.    Material discharge element (31)    Baffle plate (32)
NOVELTY - The furnace has gas braking disks (17, 18) and ash outlet doors (11, 12) arranged at lower ends of two vaporization burning chambers (7, 8). Two material adding holes (13, 14) are formed at the top of a gasification furnace body (1). A filtering layer is arranged at the bottom of a gas storing chamber (2). Middle part and upper part of the storing chamber are connected with two sides of the burning chambers and isolated with a middle filtering plate (15) and an upper filtering plate (16). The gas storing chamber is connected with a main air supplying pipeline (6) via a heat pump (5).    USE - Double-system type tobacco flue-curing biomass gasification furnace.    ADVANTAGE - The furnace vaporizes biomass to replace coal and electric power to carry out tobacco flue-curing, easily controls firepower and saves energy.    DESCRIPTION OF DRAWING(S) - The drawing shows an exploded perspective view of a double-system type tobacco flue-curing biomass gasification furnace.    Gasification furnace body (1)    Gas storing chamber (2)    Heat pump (5)    Main air supplying pipeline (6)    Vaporization burning chambers (7, 8)    Ash outlet doors (11, 12)    Material adding holes (13, 14)    Middle filtering plate (15)    Upper filtering plate (16)    Gas braking disks (17, 18)
NOVELTY - Curvularia lunata B6 has a preservation number of CGMCC No. 2928, and is new.    USE - Curvularia lunata B6 CGMCC No. 2928, spores of Curvularia lunata B6 CGMCC No. 2928 and biological agent used for exhibiting growth of barnyardgrass (all claimed).    ADVANTAGE - The Curvularia lunata B6 strain is eco-friendly and absolutely safe for preventing and treating amboceptor.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a method for preparing Curvularia lunata B6 CGMCC No. 2928 strain, which involves culturing Curvularia lunata B6 CGMCC No. 2928 in potato dextrose agar (PDA) culture medium at a temperature of 15-30 degrees C, in dark conditions for 10-14 days and obtaining spores of Curvularia lunata B6 CGMCC No. 2928; and    (2) a biological agent, which comprises Curvularia lunata B6 CGMCC No. 2928 or 4x 104-5x 106 spores per ml of spores of Curvularia lunata B6 CGMCC No. 2928, surface active agent and sterilized water as active ingredients.
NOVELTY - The excrement transportation and treatment system has a channel for collecting excrement disposed at the animal house, and a transferring pool disposed at the rear end of the channel. The transferring pool is internally provided with a transporting pump for transporting the excrement to a screening device which separates the solid and the liquid particles. The screened solid can be divided into a fiber solid or a granular solid and is transported to a liquid processing region while screened liquid is transported to the liquid storage pool.    USE - Excrement transportation and treatment system used in scaled animal cultivation.    ADVANTAGE - Performs highly efficient and economic transportation and treatment of excrement according to the actual condition of the pasture. Achieves hazard-free treatment and can produce excellent organic fertilizer and clean energy source.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the excrement transportation and treatment system.
NOVELTY - Solid fertilizer comprises (in pts.wt.): potassium carbonate (0-2), potassium bicarbonate (1-4), citric acid (5-8.6), monopotassium phosphate (2-5) and poly(ethylene glycol) 6000 (0.2-4).    USE - Solid fertilizer used for flower plants.    ADVANTAGE - The solid fertilizer has small volume, saves packaging material, is eco-friendly, dissolved quickly and easy to carry, can be pressed in tablet form in different quantity, thus it can meet the requirements of different sites such as home, office and restaurant.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing solid fertilizer, which involves:    (A) mixing potassium carbonate, potassium bicarbonate, citric acid, monopotassium phosphate and poly(ethylene glycol) 6000 uniformly; and    (B) pressing the mixture by using tablet press to obtain tablet form of solid fertilizer.
NOVELTY - Fertilizer comprises (in parts): active compound (10-15), nitrogenous fertilizer (30-40), phosphate fertilizer (20-30) and potassium fertilizer (20-30), where active compound prevents disease in synergistic manner.    USE - Fertilizer used for preventing special disease of lawn grass (claimed) and pest of plants.    ADVANTAGE - The fertilizer maintains greenery of lawn and is effective for long time in reduced dosage and prepared by simple and pollution free method, which improves the utilization rate of the fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing fertilizer, which involves:    (A) mixing medicated stone powder, diatomite powder, zeolite powder, lime nitrogen, dicyandiamide and brown coal with stirring uniformly to prepare disease-preventing active compound; and    (B) mixing the active compound with nitrogenous fertilizer particles, phosphate fertilizer and potassium fertilizer with stirring uniformly to prepare finished product.
NOVELTY - The flange mechanism has a flange fixed on an end head of a wring cage; and a bearing located in a bearing sleeve cylinder. The bearing sleeve cylinder is connected with the flange. A bearing cover plate is arranged outside the bearing cylinder. The bearing at one end of the spiral shaft is sealed in the bearing sleeve cylinder. A gap same as the sliding distance of a bearing baffle is formed between the bearing cover plate and the end face of the spiral shaft. The gap is filled with high temperature lubricating oil.    USE - Flange mechanism for preventing expansion and contraction of spiral shaft of biomass carbon device.    ADVANTAGE - Flange mechanism enables enough extension room of spiral shaft to prevent damage to device caused by unreleased force produced by temperature change during extension or contraction of spiral shaft. Sealing flange and bearing sleeve cylinder are continuously casted to control proper alignment of spiral shaft and central circle of auger flange and increase stability of device. Safety of biomass carbon device is increased since poisonous and combustible gas does not easily leak.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic cross-sectional view of the flange mechanism for preventing expansion and contraction of spiral shaft of biomass carbon device.
NOVELTY - The wool spinning printing and dyeing treatment system has reaction precipitation tank (4) and secondary precipitation tank has inclined tubes. The bottom of the secondary precipitation tank has second precipitation zone. The first precipitation zone (5) and second precipitation zone are connected to the sludge concentration tank (11) through the sludge pipe (10). The secondary precipitation tank (8) is in communication with the sewage storage pond (12) through a sewage pipe (3).    USE - Wool spinning printing and dyeing treatment system for sewage.    ADVANTAGE - The sewage treatment operation is simplified while fully dispersing the sewage during precipitation and improving the precipitating effect.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the wool spinning printing and dyeing sewage treatment system.    Sewage pipe (3)    Reaction precipitation tank (4)    First precipitation zone (5)    Secondary precipitation tank (8)    Sludge pipe (10)    Sludge concentration tank (11)    Sewage storage pond (12)
NOVELTY - Sun-exposed fermentation tanks (1) are covered with a dismountable glass fiber-reinforced plastic made cover (2) using a sealing ring. The cone top of fermentation tanks is provided with a safety valve (14) and gas transport valve (10) respectively. The base of the gas storage tank (3) is provided with a gas transport valve connected to a methane pipeline (9). The fermentation tanks and hydraulic gas storage tank (11) are connected into a sealed unit.    USE - Methane tank for producing gas using feces or straw, installed in farmland.    ADVANTAGE - The highly efficient, low cost and small sized methane tank is simple to transport and easy to install. Methane tank can be assembled in small methane stages to treat the feces. Large scale production of gas can be realized.    DESCRIPTION OF DRAWING(S) - The drawing shows a structural view of the methane tank. (Drawing includes non-English language text)    Fermentation tank (1)    Cover (2)    Gas storage tank (3)    Methane pipeline (9)    Gas transport valve (10)    Hydraulic gas storage tank (11)    Safety valve (14)
NOVELTY - The device has a photocatalytic ozone oxidation module in to which waste water enters for treatment. A membrane bioreactor module is provided for treating waste water from the photocatalytic ozone oxidation module. The photocatalytic ozone module is composed of reaction cylinder case whose inner side is connected with an ozone generator, a titanium oxide (TiO2) adding device and multiple ultraviolet light lamp tubes. A pool house is welded by carbon steel and structural steel and is mounted with a water inlet and outlet pipelines and an empty pipeline.    USE - Device for recycling wastewater from dyeing industry.    ADVANTAGE - The quality of yielded water is improved, the coking can be processed effectively and water that is hard to be degraded can be processed easily.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the recycling device.(Drawing includes non-English language text)
NOVELTY - The device has a sleeve mounted at top of a fermenting tank whose top and side are provided with doors and bottom is provided with a groove. A pipeline has a flow-rising tube whose lower port is communicated with inner top of the fermenting tank and upper port is connected with lower port of a tee joint whose upper port is connected with an air duct. Upper port of a reflux circulating tube of the pipeline is communicated with top of the fermenting tank to reach bottom of the sleeve.    USE - Dual-power self-circulating anaerobic treating system for city garbage.    ADVANTAGE - The system is simple in structure and has low construction and running costs.    DETAILED DESCRIPTION - The treating system has the reflux circulating tube having an end connected with upper port of another tee joint whose lower port is communicated with inner bottom of the fermenting tank and side port is connected with a discharging tube. Upper port of an end of the discharging tube is penetrated out of the tank. The pipe line has a charging tube that is bigger than the discharging orifice. The lower port of the charging tube is higher than that of the reflux circulating tube.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the anaerobic treating system.
NOVELTY - A fertilizer contains rapeseed dreg (2-8%), pig manure (50-60%), active carbon (10-30%), bentonite (10-30%) and nutrient compound (3-9). The nutrient compound contains nitrogen, phosphorus pentoxide and potassium oxide in the ratio of 1:2:3. The total amount of nutrient compound is 45% or more.    USE - Fertilizer is used for improving stress resistance of notoginseng plant, and promoting growth of continuous cropping of notoginseng.    ADVANTAGE - The fertilizer enables to provide notoginseng with high yield, and is economical and environmental-friendly.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparation of fertilizer, which involves mixing urea, monopotassium phosphate, potassium sulfate, zinc sulfate heptahydrate, boric acid and zeolite, obtaining nutrient compound, rotting rapeseed dregs and pig manure, fermenting, drying, mixing uniformly crushed active carbon having particles size of 0.4 nm or less and bentonite, and packaging; and    (2) using method of fertilizer, which involves supplying calcined lime to disinfect notoginseng continuous cropping land, controlling supplying amount of calcined lime to 750-2250 kg/hour.m2, applying fertilizer and controlling the supplying amount of fertilizer.
NOVELTY - Biofertilizer is obtained by fermenting (in wt.%) steel slag (15-20), vinegar residue (65-73) and weathered coal (10-15) using microorganism (0.05-0.1).    USE - Biofertilizer.    ADVANTAGE - The biofertilizer is odorless and bright, and safely converts various industrial and agricultural waste into valuable products and thus protects the environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the bio fertilizer, which involves (a) activating frozen microbial strains chosen from Hansenula anomala, H.pelliculosa spp., powdered Pichia pastoris, Saccharomyces cerevisiae, Geotrichum candidum Link, Bacillus subtilis, B.licheniformis, B.megaterium, Lactobacillus acidophilus and Streptomyces microflavus under sterile condition, (b) culturing the microorganism for 48-72 hours at 28-30 degrees C using potato dextrose (PD) or potato sucrose (PS) as culture medium, (c) mixing steel slag with vinegar residue, weathered coal and the microbial strains, and agitating the mixture uniformly, (d) allowing the mixture to ferment naturally, (d) supplementing oxygen to the mixture, (e) finishing product to obtain reddish brown biological fertilizer, applying granulating device to produce globular substance with diameter of 3-6 mm, (f) drying the substance at low temperature (50 degrees C) for 15 minutes, (g) detecting number of bacteria, nitrogen, phosphorus, potassium, organic substances, moisture, pH value, chromium, cadmium, mercury, arsenic, lead, and their oxide substances, (h) weighing the fertilizer using electronic weighing machine or scales, where weight error is allowed to 40 plus minus 0.04 kg and 50 plus minus 0.05 kg, and (i) packaging the fertilizer using a plastic bag or compacted plastic paper bag.
NOVELTY - Organic fertilizer comprises (in parts weight) tobacco straw (1000), dry livestock excrements (25-30), carbamide (5-10) and fermentation bacteria (3).    USE - The organic fertilizer is useful for exterminating subterranean insect pest (claimed).    ADVANTAGE - The organic fertilizer increases content of organic colloid in soil, improve water and nutrient preserving property of soil, and provide beneficial bacteria to the soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing organic fertilizer, which involves (a) drying and dewatering the livestock excrements under sun, (b) crushing the tobacco straw into small pieces having particle size of 3-5 cm, (c) adding carbamide to the mixture obtained in step (a) and (b) and stirring the mixture, (d) inoculating the solid efficient microbial fermentation bacteria into the obtained mixture, adding water into mixture and uniformly stirring the mixture with moisture content of 65-70%, at pH of 6.8-7.2, (e) stacking the obtained product into fermentation stack in height of 1.5 m or less, leveling the top portion and externally covering the stack with a black plastic film, (f) storing the stack for 3 or 4 days, unfolding the film from the stack at 50-60 degrees C and turning over the material in fermentation stack through turner, (g) turning over the material again for several times till the volume of the fermented material is 2/3 of the original volume of the stack, (h) drying the stack in natural ventilation and packaging the dried material for storage with moisture of 20% or less.
NOVELTY - A secondary processed diesel oil, and vegetable oil and/or animal fat are mixed. The mixed material is contacted to a hydrogenation refined catalyst, and hydrogenation reaction is carried out at 300-450 degrees C in presence of hydrogen having partial pressure of 3.2-8 MPa, and with space velocity of 2.1-6/hour and volume ratio of hydrogen and oil of 300-800 Nm3/m3. The reaction mixture is cooled, separated and fractionated to obtain diesel oil containing vegetable oil and/or animal fat (5-35%).    USE - Improvement of cetane number of secondary processed diesel oil e.g. catalytic cracking diesel oil, coking diesel oil, visbreaking diesel oil, thermal cracking diesel oil and coal directly-liquefied diesel oil (all claimed).    ADVANTAGE - The method provides diesel oil having low sulfur content, and high cetane number, with high yield.
NOVELTY - A low-temperature fluidity improving agent is ethylene-vinyl acetate-maleic anhydride-vinyl benzene quaternary copolymer (I).    USE - Low-temperature fluidity improving agent is used for biodiesel.    ADVANTAGE - The low-temperature fluidity improving agent has excellent dispersibility and sensitivity with respect to biodiesel, and reduces condensing point and cold filtering point of biodiesel.    DETAILED DESCRIPTION - A low-temperature fluidity improving agent is ethylene-vinyl acetate-maleic anhydride-vinyl benzene quaternary copolymer of formula (I).    k,l,m,n=5-50.    An INDEPENDENT CLAIM is included for preparation of low-temperature fluidity improving agent, which involves dissolving ethylene, vinyl acetate, maleic anhydride and vinyl benzene in methylbenzene in mole ratio of 1:1:1:1 under nitrogen atmosphere, mixing, maintaining the mixed solution for 0.5-1 hour, adding azodiisobutyronitrile to the mixed solution, reacting at 60-100 degrees C under pressure of 6-8 MPa for 1-2 hours, adding mixed solution of alcohol and water containing sodium hydroxide, removing solvent, polymerizing monomer and washing the product using water, to obtain ethylene-vinyl acetate-maleic anhydride-vinyl benzene quaternary copolymer. The content of methylbenzene is 2-4 times of total content of the monomers. The content of mixed solution of alcohol and water is 5-10% with respect to the polymerizing monomer. The volume ratio of alcohol and water is 1:1. The content of azodiisobutyronitrile is 1-3% of total weight of the polymerizing monomers.
NOVELTY - A bean curd lees extract contains bean curd lees and ethanol. The extract is obtained by adding ethanol to bean curd lees, extracting soluble part, filtering, and removing ethanol.    USE - A bean curd lees extract used for bio diesel fuel, drink, and cosmetics (claimed).    ADVANTAGE - The discard cost of bean curd lees as industrial waste is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a manufacturing method of bean curd lees extract.    DESCRIPTION OF DRAWING(S) - The drawing shows an expalanatory view of acquisition of bean curd lees extract.    Beaker (101)    Bean curd lees (102)    Ethanol (103)    Glass rod (104)
NOVELTY - Fats and oils containing waste water is processed by decomposing fats and oils by lipase secretion microorganisms which hydrolyze fats and oils into fatty acid and glycerol and microorganisms which consume and assimilate hydrolysis product.    USE - Processing of fats and oils containing waste water used for cleaning of grease-trap (claimed).    ADVANTAGE - The method processes high concentration of fats and oils containing waste water effectively.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a grease-trap cleaning method; and    (2) a fat splitting agent.
NOVELTY - The gasifier (1) has moisture layer position control apparatus (7) which controls at least one of the supply conditions of a biomass granulated material or biomass molding supplied with a biomass supply apparatus (2), and the gasifying agent supply conditions containing the composition ratio of gasifying agent supply amount and gasifying agent. The moisture layer position detection apparatus (6) detects the upper surface height position of the moisture layer which moisture-content condensation of the upper section of the gasifying agent supply apparatus (5) which supplies gasifying agent.    USE - Gasifier for biomass.    ADVANTAGE - The gasification apparatus prevents the nodulizing of the biomass within the gasifier to form uniform gas flow and enable the stable gasification.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a gasification method of biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows the outline block diagram of the gasifier. (Drawing includes non-English language text).    Gasifier (1)    Biomass supply apparatus (2)    Gasifying agent supply apparatus (5)    Moisture layer position detection apparatus (6)    Moisture layer position control apparatus (7)
NOVELTY - The fuel cell apparatus has a modifier (4) that receives water at the time of operating water pump (11) and mixes water and raw fuel received from fuel supply unit (2). A controller (14) determines whether usage amount of water pump reaches a predetermined value after starting water pump. The controller controls operation of the water pump to increase quantity of the water supplied to the modifier, when the usage amount of water pump reaches predetermined value.    USE - Fuel cell apparatus for electric power generation.    ADVANTAGE - Operation of water pump can be controlled reliably even when usage amount of water pump reaches predetermined value so that the quantity of water supplied to modifier can be increased. The necessity of flow sensor for measuring quantity of water supplied from water pump is eliminated so that the structure of the fuel cell apparatus can be simplified at low cost and reliability of the fuel cell apparatus can be improved. Electric power generation amount can be increased and replacement time of the water pump can be judged appropriately. Performance of the fuel cell apparatus can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fuel cell apparatus. (Drawing includes non-English language text)    Fuel cell stack (1)    Fuel supply unit (2)    Modifier (4)    Water pump (11)    Controller (14)
NOVELTY - Rendering (M1) petroleum oil as an essentially environmentally carbon dioxide-neutral fuel and regenerative carbon source for producing methanol or dimethyl ether involves subjecting petroleum oil to refining or combustion conditions sufficient to produce carbon dioxide; capturing and purifying produced carbon dioxide; and combining purified carbon dioxide with water and light hydrocarbon fraction or with hydrogen produced from water under reaction conditions to produce methanol or dimethyl ether, so that carbon dioxide generated from petroleum oil is not introduced into the atmosphere.    USE - For rendering petroleum oil as an essentially environmentally carbon dioxide-neutral fuel and regenerative carbon source for producing methanol or dimethyl ether (claimed); used as fuel or feedstock for derived synthesis hydrocarbons and products.    ADVANTAGE - The method provides the recycling of carbon dioxide from refining or combustion of petroleum oil for the production of methanol, dimethyl ether, and their derived products in an integrated, efficient and economical industrial operation that is environmentally beneficial by not releasing the carbon dioxide into the atmosphere.
NOVELTY - The Magneli-phase-oxide useful as catalyst for electrochemical hydrogen generation by electrolysis using acid electrolytes, is claimed.    USE - Magneli-phase-oxide useful as catalyst for electrochemical hydrogen generation by electrolysis using acid electrolytes.    ADVANTAGE - The Magneli-phase-oxide ensures generation of hydrogen with high quality and quantity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a cathode for electrochemical hydrogen generation;    (2) a layer composite;    (3) a method for the production of a catalyst layer for a cathode for electrochemical hydrogen generation; and    (4) a method for electrochemical hydrogen generation.    DESCRIPTION OF DRAWING(S) - The figure shows a graph of time dependence of the flow strength in water electrolysis in a proton exchange membrane-electrolysis cell (Drawing includes non-English language text).
NOVELTY - The method involves providing synthesis gas (27) obtained by gasification of carbon-containing solids. The synthesis gas is introduced into a gas scrubbing unit (26) for obtaining scrubbed synthesis gas (40). A common multi-strand compressor (56) is provided with a main compressor (42) and an auxiliary compressor (54). The scrubbed synthesis gas is compressed to an operating pressure using the main compressor for methanol production. The auxiliary compressor is used for performing intermediate compression of the synthesis gas before scrubbing the synthesis gas in the gas scrubbing unit.    USE - Method for treating synthesis gas from gasification of carbon-containing solid for producing methanol that is utilized as fuel in motor vehicle.    ADVANTAGE - The method ensures that the intermediate compression of the synthesis gas takes place with same mass flow, such that a flow rate and apparatuses required for the treating system are reduced. The method enables a high cold expansion effect to be achieved in the gas scrubbing unit during expansion of separated carbon dioxide in the gas scrubbing unit, so that energy required for cooling the gas scrubbing unit can be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a system for treating synthesis gas from gasification of carbon-containing solid, comprising a cooling device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic flow diagram of a system for treating synthesis gas from gasification of carbon-containing solid.    Gas scrubbing unit (26)    Synthesis gas (27)    Scrubbed synthesis gas (40)    Main compressor (42)    Auxiliary compressor (54)    Common multi-strand compressor (56)
NOVELTY - Biocoke production involves crushing, drying and mixing biomass (1), where the crushed biomass is subjected to torrefaction for forming solid residue. The torrefaction process is carried out in a fluidized-bed system (2), which comprises a fluidized bed (3) region having a high solid concentration and a free space (4) having a low solid concentration.    USE - Method for producing biocoke from plant biomass (claimed) for gasification in an entrained-flow reactor.    ADVANTAGE - The biocoke production method enables to produce the biocoke in a cost-effective manner by reduced consumption of energy. The method is simple and eco-friendly also by releasing a small amount of carbon monoxide and carbon dioxide.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for carrying out process, which comprises a facility for crushing, drying and mixing of biological, plant-based fuels, a stationary fluidized bed, a gas chamber, a grinding apparatus and devices for covering finely ground coke.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of conical or cylindrical shaped sections of reactor wall in the fluidized bed area.    Biomass (1)    Fluidized-bed system (2)    Fluidized bed (3)    Free space (4)    Fluidizing gas (5)
NOVELTY - The preparation method involves forming a three-electrode system by working electrode, pair electrode and reference electrode, taking platinum electrode as pair electrode and taking saturated calomel electrode as reference electrode, and electro-chemically depositing in aqueous solution; and infusing nitrogen into the solution in the electro-chemically depositing process, and preparing the catalytic electrode for electro-catalytically oxidizing ammonia and taking nickel or titanium electrode as base plate. The additive is one of polyethylene glycol, lead acetate and citric acid.    USE - Method for preparing nickel-base or titanium-base catalytic electrode for electro-catalytically oxidizing ammonia.    ADVANTAGE - The preparation method can large-scale reduce the cost of catalytic electrode for electro-catalytically oxidizing ammonia and make the catalytic electrode for electro-catalytically oxidizing ammonia have excellent performance of electro-catalytically oxidizing ammonia.    DESCRIPTION OF DRAWING(S) - The drawing shows the characteristic graph of the nickel-base or titanium-base catalytic electrode.
NOVELTY - Hydrogen and carbon monoxide are produced by irradiating microwave (17) to carbon material (2) and steam (1) supplied to a reactor (10), heating the carbon material and reacting it with steam. A rotational flow (18) of steam is formed within the reactor, and air residence time of the carbon material within steam is ensured according to the rotational flow. Irradiation of microwave is carried out in the air retention region.    USE - Production of hydrogen.    ADVANTAGE - The method enables efficient production of hydrogen by improving the reaction efficiency of carbon material and steam. Since the carbon material of powder-form or granule-form exists in the air retention region during microwave exposure, contact of carbon material with the wall surface of reactor is prevented. The method consumes less energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for hydrogen production apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic cross-sectional block diagram of the hydrogen production apparatus.    Steam (1)    Carbon material (2)    Reactor (10)    Microwave (17)    Rotational flow (18)
NOVELTY - Purifying waste liquid, involves introducing microorganisms immobilized carrier in a waste liquid, and purifying the waste liquid. The carrier is formed by immobilizing hypha membrane of filamentous fungi and/or Actinomyces, and performing solid fermentation. The carrier is porous carrier having water content or fiber.    USE - The method is useful for purifying waste liquid and removing suspended solid (claimed), where the waste liquid is food processing waste liquid such as rinse water of rice, hot water used for boiling of Udon noodle, and extract of vegetables.
NOVELTY - The machine includes an electrolysis bath, two flame arresters, a heat exchanger, a welding and cutting head and a welding and cutting head. The electrolysis bath is U-type electrolysis bath with symmetrical sides, and provided with electrolytes. A pipeline at the middle lower part accessing the heat exchanger is provided with a water pump to communicate with the radiating pipe in the heat exchanger. The hydrogen outlets of the flame arresters are provided with pipelines to respectively connect with the hydrogen connecting pipe and oxygen connecting pipe on the welding and cutting head.    USE - Water electrolysis oxyhydrogen flame welding and cutting machine.    ADVANTAGE - Provides a water electrolysis oxyhydrogen flame welding and cutting machine that is convenient to use, ensures quick operation, is environment-friendly, and is energy-saving.    DETAILED DESCRIPTION - The sides of the electrolysis baths are respectively connected to the anode and cathode of direct current (DC) power. The upper end of the electrolysis bath is provided with an air outlet pipeline to respectively connect to the two flame arresters. Each flame arrester has a hydrogen outlet provided with a pipeline to connect with the pipeline at the bottom of the electrolysis bath and connect with the pipeline accessing the middle lower part of heat exchanger. The pipelines on the electrode copper pipe connecting the cathode and anode in the electrolysis bath are respectively connected to the upper end and lower end of a radiating pipe of the heat exchanger.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of the water electrolysis oxyhydrogen flame welding and cutting machine.
NOVELTY - An ezetimibe derivative (III) or its intermediates (I) or (II), are new.    USE - Compounds (I)-(III) for preparing an ezetimibe (claimed) for use as hypocholesterolemic agent.    ADVANTAGE - The compound inhibits the intestinal absorption of cholesterol and related phytosterols; has convenient, low cost, eco-friendly and commercial viable preparation; allows recovery of chiral auxiliary during preparation, thus reducing production cost; and utilizes cheap enzymes.    DETAILED DESCRIPTION - An ezetimibe derivative of formula (III) or its intermediates of formula (I) or (II), are new.    P1-P2=OH protecting group;    R=1-6C alkyl, 1-6C alkoxycarbonyl, benzyl, or Ph or naphthyl (both optionally substituted); and    R1=aryl or 1-6C alkyl (both optionally substituted).    Provided that one the protecting group is benzyl. INDEPENDENT CLAIMS are included for:    (1) preparation of (I);    (2) process of preparing (S)-5-(4-fluoro-phenyl)-5-hydroxy-1-morpholin-4-yl-pentan-1-one comprising subjecting 1-(4-fluoro-phenyl)-5-morpholin-4-yl-pentane-1,5-dione to asymmetric reduction using a ketoreductase enzyme in the presence of a solvent and a buffer; or by subjecting 5-(4-fluoro-phenyl)-5-morpholin-4-yl-pentane-1,5-dione to lipase enzyme in the presence of a solvent and an acylating agent; and    (3) process of preparing an ezetimibe comprising preparing (S)-5-(4-fluoro-phenyl)-5-hydroxy-1-morpholin-4-yl-pentan-1-one, and converting (S)-5-(4-fluoro-phenyl)-5-hydroxy-1-morpholin-4-yl-pentan-1-one to ezetimibe; or reacting an oxazolidine derivative with a protected amine of formula (VI) in a solvent in the presence of an organic amine base and Lewis acid to obtain (I), reacting (I) with an alkali metal oxide or aryloxide in a solvent to obtain (II), cyclizing (II) in the presence of non-nucleophilic base to obtain (III), removing the hydroxy protecting groups, and isolating the ezetimibe.
NOVELTY - The membrane separator (11) have several membrane elements (14) that connects to a water collection unit (16) to collect the permeated liquid from each membrane elements. The internal flow path of the water collection unit makes upgradient in the top region or becomes high in the top region. The chemical solution supply piping (20) supplies a washing lotion liquid to the lowest potion of the internal flow path of the water collection unit and degassing piping (23) emits gas to the highest portion of the flow path.    USE - Membrane separator used for activation sludge treatment and methane fermentation treatment.    ADVANTAGE - As the chemical solution supply piping supplies washing lotion liquid to the internal flow path of the water collection unit, the washing lotion liquid is smoothly supplied to the each membrane element, without gas emitted in the system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the membrane separator.    Membrane separator (11)    Membrane elements (14)    Water collection unit (16)    Chemical solution supply piping (20)    Degassing piping (23)
NOVELTY - The fuel cell performs steam reforming of fuel gas (BB) by making the fuel gas to react with steam, to heat up the modifier, when the fuel gas reformation state temperature is more than the predetermined temperature. The partial oxidation reformation of fuel gas is skipped and restarting control of fuel cell is performed, when the fuel gas reformation state temperature exists within the partial oxidation temperature range.    USE - Solid oxide fuel cell (SOFC) used in fuel cell system.    ADVANTAGE - The durability of the fuel cell can be improved, since load acting on the fuel cell can be reduced, by preventing the influence of oxidation on the fuel cell. The starting time of the fuel cell can be reduced significantly, so that restarting control of the fuel cell can be performed actively. The damage to the fuel cell can be suppressed by prohibiting different restarting control of the fuel cell, even if the reformation state temperature exists within the partial oxidation temperature range. Temperature recovery of fuel cell modules can be performed efficiently, rapidly and appropriately, by preventing oxidation using the exothermic reaction. The fall in the temperature fall of modifier at the time of restarting can be suppressed exactly, without using a special heating unit.    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)    Auxiliary machine unit (4)    Water supply source (24)    Fuel gas (BB)
NOVELTY - The fuel cell (1) has a control unit which performs combustion driving for heating modifier (20) when reformation state temperature is lower than partial oxidation start temperature, and performs partial oxidation at the time of starting normally when reformation state temperature is higher than partial oxidation start temperature. The control unit skips ATR during normal startup and restarts the fuel cell module (2), when the fuel cell module shut down after operating at high temperature, is restarted while reformation state temperature is within ATR temperature.    USE - Solid oxide fuel cell.    ADVANTAGE - The temperature fall of modifier or cell at the time of restarting is suppressed and the time for restarting fuel cell module is shortened.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the solid oxide fuel cell. (Drawing includes non-English language text)    Solid oxide fuel cell (1)    Fuel cell module (2)    Auxiliary machine unit (4)    Combustion chamber (18)    Modifier (20)
NOVELTY - A fuel supply source (30) supplies fuel to fuel cell unit (16) arranged in power generation chamber (10), and temperature sensor detects temperature of power generation chamber. An adaptive controller adjusts amount of fuel supply based on temperature signal from temperature sensor such that temperature of power generation chamber is maintained within monitoring temperature range.    USE - Solid oxide fuel cell (SOFC).    ADVANTAGE - The temperature change of fuel cell can be suppressed, so that the damage to fuel cell can be reduced. Thus, the durability of SOFC can be improved. The power generation efficiency of fuel cell can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the SOFC. (Drawing includes non-English language text)    Power generation chamber (10)    Fuel cell unit (16)    Fuel supply source (30)    Air supply source (40)    Inverter (54)
NOVELTY - The assembly has pair of fuel cells that are provided with power generating unit. The power generating unit generates electricity with ground electrode layer within which gas flows and inner side electrode terminal within which another gas flows. A collector allows electricity generated in one fuel cell to be distributed and flow out to inner side electrode terminal of other fuel cell from two different positions of ground electrode layer of the fuel cell.    USE - Fuel cell assembly.    ADVANTAGE - The electric power generating efficiency of the fuel cell assembly is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows the perspective view of the fuel cell stack.    Fuel cell stack (14)    Fuel gas flow channel (88)    Metal collector (102)    External terminal (104)    Connection portion (110)
NOVELTY - The tub (10) consists of organic waste (1) mixed with a moisture control material at its upper portion, and particulate material forming an air diffusion layer (2) at its lower portion. Several air supply pipes (11) with air jet holes (11a) are arranged spaced apart on lower surface of tub. An air guide unit is extended from inner wall or lower surface of tub, along longitudinal direction of the tub. The front end of air guide unit is located lower than or in level with upper surface of air diffusion layer.    USE - Compost fermentation tub of compost manufacturing equipment used for manufacture of compost from organic waste.    ADVANTAGE - Since the front end of air guide unit is lower than or in level with upper surface of air diffusion layer, the concentration of air jetted from the air supply pipes on the inner wall of the compost fermentation tank tube can be prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows the cross-sectional view of the compost fermentation tub.    Organic waste (1)    Air diffusion layer (2)    Fermentation tub (10)    Air supply pipe (11)    Air jet hole (11a)
NOVELTY - A flow medium of fluidized bed-type gasifier (1) comprises mixture having particles containing silicon dioxide and particles containing alumina. The content of alumina in the mixture is 20-80 wt.%. The temperature of fluid bed (3) of fluidized bed-gasification furnace is maintained at 740 degrees C or less, and to-be-gasified raw material (M) is gasified.    USE - Operation of fluidized bed-type gasifier used for gasifying high-potassium-content raw material (both claimed), sugarcane waste material, bagasse, bamboo waste material, construction waste material, driftwood, rice straw and chaff. The synthesis gas produced by fluidized bed-type gasifier is used for synthesizing ethanol and methanol.    ADVANTAGE - The method enables efficient gasification of to-be-gasified raw material using fluidized bed-type gasifier, by suppressing large usage of fluid medium.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fluidized bed-type gasifier.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the fluidized bed-type gasifier. (Drawing includes non-English language text)    Fluidized bed-type gasifier (1)    Fluid bed (3)    Gasifying material-supply apparatus (7)    Temperature control portion (21)    To-be-gasified raw material (M)
NOVELTY - Producing biofuels from lignocellulosic feedstocks, comprises depolymerizing pentose from a lignocellulosic feedstock to form a remainder, where the depolymerizing step results in a stream comprises primarily pentose, and converting the pentose to a biofuel material.    USE - The process is useful for producing biofuels from lignocellulosic feedstocks, which is bagasse, rice straw, corn stover, miscanthus, switch grass, wheat straw, wood, wood waste, paper, paper waste, agricultural waste, municipal waste, sugarcane, energy cane, corn, maize, sorghum, sweet sorghum, and/or sugar beet (claimed). The process is useful for producing biogasoline and/or biodiesel, which is useful in compression engines such as automotive diesel internal combustion engines, turbines, and heaters. The biodiesel is useful as aviation fuels (jet), lubricant base stocks, and kerosene fuels.    ADVANTAGE - The process is cost effective.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a biofuel made by the process; and    (2) a biofuel plant (110) for producing biofuels from a lignocellulosic feedstock, comprising: a lignocellulosic feed system; a pentose depolymerization unit (118) for removing pentose from the lignocellulosic feedstock to form a remainder; and a pentose conversion unit for converting pentose to a biofuel material.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a biofuel plant.    Biofuel plant (110)    Feed system (114)    Pentose depolymerization unit (118)    Biofuel line (126)    Powerhouse. (128)
NOVELTY - A soil conditioner comprises (wt.%) ammoniated slurry (70-90), polyamino acid (0.1-1) and auxiliary material (5-25). The auxiliary material is animal residue, humic acid, bentonite, medical stone, fly ash, grass peat, ardealite or calcium superphosphate. The ammoniated slurry is slurry from sewage disposal factory, bottom sediment from river or lake, domestic garbage and/or industrial garbage.    USE - A soil conditioner for growing crops (claimed).    ADVANTAGE - The product has improved nutrient content, thus treating waste and improving environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of preparing soil conditioner by hydrolyzing sorted slurry from metal, plastic, glass, sand and stone for 1-2 hours under 0.8-1.2 MPa in the presence of acid catalyst (0.5-1, preferably 0.5-2 wt.%); performing ammonification for 1-2 hours under 0.8-1.2 MPa at 80-150 degrees C with liquid ammonia (3-16 wt.%), and dewatering to obtain solid material with nutrient solution containing 30-60% water; and mixing with polyamino acid and auxiliary material. The organic material is animal residue, organic waste or organism which is harmful to river and lake. The acid catalyst is 10-20% inorganic acid or organic strong acid, copper salt, or iron salt. The solid material is ammoniated slurry.
NOVELTY - A biogenic production of a metabolic product with enhanced hydrogen content is stimulated by accessing a geologic formation that includes a carbonaceous material, introducing an amendment to the geologic formation, and removing the metabolic products with enhanced hydrogen content from the formation.    USE - Method of stimulating biogenic production of a metabolic product with enhanced hydrogen content, preferably methane or hydrogen (claimed).    ADVANTAGE - The method can extract resources from formations with lower expenditures of energy and costs.    DESCRIPTION OF DRAWING(S) - The drawing is a flowchart of a method of introducing hydrogen and phosphorus amendment to microorganisms in geologic formations.    Access microorganisms in geologic formation (102)    Provide hydrogen to microorganisms (104)    Provide phosphorus compound to the microorganisms (106)    Measure concentration of metabolic product (108)
NOVELTY - Microorganism fish guano is produced by fermenting chicken manure, edible mushroom residue, bran, straw powder, stillage, edible salt and fermenting agent, drying to adjust water content; crushing and screening; adding monoammonium phosphate or diammonium phosphate, Ferrochel (RTM: iron glycine), zinc sulfate, manganese sulfate, copper sulfate, and photosynthetic bacteria; mixing the materials; and packing.    USE - Method of producing microorganism fish guano (claimed).    ADVANTAGE - The method has improved yield of 40%, is low cost and safety, and produces less pollutants.    DETAILED DESCRIPTION - Microorganism fish guano is produced by mixing (pts.wt.) chicken manure (45-55), edible mushroom residue (8-12), bran (12-18), straw powder (8-12), stillage (8-12), edible salt (0.5-1.5) and fermenting agent (3-5) while controlling water content at 30-40% to obtain mixture A; fermenting mixture A at 20-25 degrees C for 3-6 days, fermenting at 5-10 degrees C for 6-9 days, and fermenting at 5-10 degrees C for 12-15 days; drying at 80 degrees C to adjust water content to below 10%; crushing and screening using a 80-mesh screen; adding (pts.wt.) monoammonium phosphate or diammonium phosphate (10-20), Ferrochel (RTM: iron glycine) (1-3), zinc sulfate (0.1-1), manganese sulfate (0.1-1), copper sulfate (0.1-1), and photosynthetic bacteria (15-30); mixing the materials; and packing.
NOVELTY - Multifunctional fertilizer comprises (in Kg): fermented organic fertilizer (900), calcium superphosphate (50), potassium sulfate (30), zinc sulfate (5), Borax (RTM: Boric acid) (3), nanometer silicate (10) and composite Bacillus (2).    USE - Multifunctional fertilizer used for agricultural product.    ADVANTAGE - The multifunctional fertilizer is a highly-concentrated, diversified, long-acting, harmless and economic.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing multifunctional fertilizer, which involves:    (A) agitating and mixing animal manure with crop straw powder in a ratio of 4:1;    (B) adding 0.7 kg of the composite Bacillus in per cubic meter of material and agitating uniformly;    (C) keeping the mixture in stacks to perform aerobic and anaerobic fermentation;    (D) overturning the material one time in every 7 days, where temperature is 60-70 degrees C;    (E) overturning the material for multiple times, where material is cooled at normal temperature; and    (F) obtaining the fermented organic fertilizer with moisture content of 20% and more than 35% of organic substance.
NOVELTY - The gasifier has a firepower adjusting switch (13) and a wind adjusting switch (14) arranged on a pipeline. A blast blower (5) is arranged between two switches. Bottom of purifier (4) is provided with a tar exhaust port (15). Lower part of the tar exhaust port is provided with a water discharging switch (16). A gas inlet is connected with a secondary filter (3) through the pipeline. A suction fan (6) is arranged between the purifier and a cooking range unit (7). The secondary filters (2, 3) are arranged between a gas-making furnace (1) and the purifier.    USE - Straw energy-saving gasifier.    ADVANTAGE - The gasifier has prolonged combustion time, is convenient to ignite. The gasifier prevents reverse flow of water vapor, can effectively filter the water and tar, and can be assembled conveniently with rational structure.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a straw energy-saving gasifier.    Gas-making furnace (1)    Secondary filters (2, 3)    Purifier (4)    Blast blower (5)    Suction fan (6)    Cooking range unit (7)    Firepower adjusting switch (13)    Wind adjusting switch (14)    Tar exhaust port (15)    Water discharging switch (16)
NOVELTY - Use of (1S)-(-)- alpha -terpene, myrcene, 3-carene and their mixture are claimed.    USE - Used for attracting Pissodes yunnanensis (claimed) and monitoring and forecasting number of insects in forest.    ADVANTAGE - The (1S)-(-)- alpha -terpene, myrcene, 3-carene and their mixture are eco-friendly without producing resistance in insect against drug, kills insect, and has low cost, high efficiency and safe to human and poultry.
NOVELTY - Pesticide formulation comprises (in wt.%): rotenone (0.5-50), an antibiotic (0.5-55) and an auxiliary agent (remaining portion), where the antibiotic is streptomycin sulfate or validamycin.    USE - The formulation is useful as a pesticide.    ADVANTAGE - The formulation is: a single agent pesticide formulation; and convenient to use, safe to man, animal and ecological environment. The components of the formulation exhibit synergisitic activity.
NOVELTY - The method involves placing Eisenia foetida in polluted soil, and uniformly mixing fermented chicken manure and cow dung with the soil. The fermented chicken manure and cow dung are added for every three months. Water content in the soil is maintained upto 55-65 percentage during restoration process. A fermentation process is performed with a straw screen or thin plastic film.    USE - Earthworm bio-enhanced pollution restoration method for degrading dichlorodiphenyltrichloroethane (DDT) pesticide residue in soil.    ADVANTAGE - The method reduces the requirement in an external environment, is simple and effective, and can be operated at low-cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical representation illustrating an earthworm bio-enhanced pollution restoration method for degrading dichlorodiphenyltrichloroethane pesticide residue in soil. '(Drawing included non-English language text)'
NOVELTY - A ground-source heat pump system has an underground heat exchange system having a buried pipe heat exchanger, a circulation water pump and a pipeline. The buried pipe heat exchanger is a vertical buried pipe heat exchanger, and absorbs the heat energy in the ground surface shallow soil and transmits the heat energy to water. The water heats an anaerobic digestion tank by circulation pipe to accelerate the anaerobic digestion. A hot water circulation pipe is placed in the anaerobic digestion tank or outside the anaerobic digestion tank.    USE - Ground-source heat pump biogas tank.    ADVANTAGE - The high production cost of the biogas project is eliminated and the increase in the energy consumption is reduced.    DETAILED DESCRIPTION - The ground-source heat pump biogas tank is formed by connecting the anaerobic digestion system, a heat-insulating and warm-keeping system, the ground-source heat pump system and a controlling system. The heat pump system has a heat pump main-auxiliary machine system having a cold-heat source side heat exchanger, a compressor, a reversing valve and a throttle valve. A terminal heat exchange apparatus has a condenser and is connected with the heat-insulating and warm-keeping system and the anaerobic digestion system by the hot water circulation pipe.
NOVELTY - Mixing compost of dredging sludge and living sludge, by mixing preliminarily fermented living sludge with preliminarily dried sludge, adding agricultural wastes to the mixture, adding special microbial inoculum of VT fermentation bed to the mixture to form compost, subjecting the compost to aerobic fermentation to obtain organic fertilizer, reflowing the organic fertilizer and then adding to the mixed material as source of the special microbial inoculum of VT fermentation bed.    USE - The method is useful for mixing compost of dredging sludge and living sludge for producing fertilizer.    ADVANTAGE - The method is simple, cost-effective, environmental-friendly and practical. The number of beneficial microorganism is improved.    DETAILED DESCRIPTION - Method for mixing compost of dredging sludge and living sludge using microbial composition, involves (i) subjecting living sludge to preliminary fermentation to remove odor and reduce mosquitoes and flies, and reducing the water content of the preliminarily fermented sludge from 80-85% to 70-75%, (ii) mixing the preliminarily fermented living sludge with preliminarily dried sludge in the volume ratio of 1:1-2, adding agricultural wastes as adjusting agent to the mixture to form mixed material, controlling the water content of the mixed material to 50-60%, adding 0.08-0.15% of special microbial inoculum of VT fermentation bed to the mixed material, mixing uniformly and stacking the mixture to form compost, (iii) subjecting the compost to aerobic fermentation and maintaining the ventilating amount to 0.2-0.3 m3.minute/time, ventilating for 30-40 minutes for every 3-5 hours and closing the ventilating duct after 22-28 days, and obtaining organic fertilizer, and (4) reflowing the organic fertilizer and then adding into the mixed material as source of the special microbial inoculum of VT fermentation bed, where the added amount is 15-20 vol.% of the mixed material.
NOVELTY - Product preparation involves utilizing seed, stem and leaf of cassava. The seed, stem and leaf of cassava are dried and crushed in rotary dryer to obtain a mixture. The obtained mixture is introduced into briquette machine to obtain a product.    USE - Method for preparing a product used as firewood or charcoal for furnaces or boilers for industrial, domestic and general use (claimed).    ADVANTAGE - The method enables to prepare product in cost-effective and eco-friendly manner.
NOVELTY - The method involves selecting fresh mint plants as experimental materials and using a dynamic adsorption method to separate and identify volatile compounds of menthol, menthone, linalool, eugenol, alpha-pinene, myrcene, trans-ocimene, pepper ketone, 3-octanol and beta-bourbon alcohol from smell of fresh mint plants. The strongest-inducement menthol, menthone and linalool are selected to Ectropis obliqua adult. An inducement core and a khaki adhesive plate are placed into a trapper. The trapper is placed in a tea garden to trap Ectropis obliqua adult.    USE - Method for trapping and preventing Ectropis obliqua adult in a tea garden.    ADVANTAGE - The adult is trapped during beginning of eclosion aceme of Ectropis obliqua adult, so as to decrease the number of eggs laid by next generation to decrease chemical control. The method prevents environment pollution, satisfies environmentally-friendly control principle of pest and construction requirement of standard ecological tea garden.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical representation of a method for trapping and preventing Ectropis obliqua adult. '(Drawing includes non-English language text)'
NOVELTY - The alarm has a main control circuit (1) connected with a data storing circuit (3), a gas detecting loop (5), a clock circuit (7), an alarm circuit (9), a display circuit (10) and a control panel (12) of a panel part. The data storing circuit is connected with a serial port circuit (4). The alarm circuit is connected with an alarm device (11) of the panel part. The gas detecting loop is connected with a sensor (6) of the panel part. A voltage stabilizing power source (2) is provided with a universal serial bus (USB) automatic charging port.    USE - Portable gas such as carbon monoxide, hydrogen sulfide, oxygen and methane (all claimed), detection alarm.    ADVANTAGE - The alarm can communicate data with a computer, and can display alarm and charge while accessing, and is high in automation.    DETAILED DESCRIPTION - The sensor is selected from one of carbon monoxide sensor, hydrogen sulfide sensor, oxygen sensor and methane sensor.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a portable gas detection alarm.'(Drawing includes non-English language text)'    Main control circuit (1)    Voltage stabilizing power source (2)    Data storing circuit (3)    Serial port circuit (4)    Gas detecting loop (5)    Sensor (6)    Clock circuit (7)    Alarm circuit (9)    Display circuit (10)    Alarm device (11)    Control panel (12)
NOVELTY - 24-Epibrassinolide is prepared by oxidizing hydroxy in ergosterol compound to carbonyl using osmium tetroxide as oxidizing agent and meta-chloroperoxybenzoic acid, morpholine, sodium bromate, t-butyl hydrogen peroxide, or hydroperoxide as co-oxidizing agent; and performing deoxidization, rearrangement, dihydroxylation and lactonization steps to the obtained intermediate product.    USE - Method of preparing 24-Epibrassinolide (claimed) used as plant growth regulator.    ADVANTAGE - The method involves convenient operation, and is environment-friendly and suitable for the industrialized production.
NOVELTY - The oil-saving device has a solar panel which is installed to the roof of a vehicle, and a torque sensor installed on the output shaft of engine. The solar panel and torque sensor are connected to a control circuit board. The output of the control circuit board is connected to an electrolysis water device. The sidewall of electrolysis water device is provided with the water storage tank for replenishing the water. The oxygen supply pipe and the hydrogen supply pipe of electrolysis water device are connected into the air inlet pipe of engine.    USE - Solar electrolysis water oxyhydrogen oil-saving device for vehicles.    ADVANTAGE - Improves the burning effect to fully burn the fuel and reduces the exhaust since the electrolyzed oxygen and hydrogen with low concentration are supplied to the combustion chamber. Simplifies the structure of the device without changing the inner structure of the vehicle so that the fittings are easy to buy, and utilizes the solar energy to save the oil.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram of the solar electrolysis water oxyhydrogen oil-saving device.
NOVELTY - Fertilizer (master-batch) comprises (in wt.%): yeast (10-30), Lactobacillus (10-30), photosynthetic bacteria (10-30) and cellulose-decomposing bacteria (10-30). The fertilizer (master-batch) is also comprised of Chinese medicinal herbs (in wt.%): Chinese mugwort (0.8-1.2), medlar (0.8-1.2), fructus amomi (0.8-1.2), hawthorn (0.8-1.2), Chinese yam (0.8-1.2), Polygonum multiflorum (0.8-1.2), malt (0.8-1.2), pericarpium citri reticulatae (0.8-1.2), Areca nut (0.8-1.2), rhizoma ligustici wallichii (0.8-1.2), lysine (2.8-3.2), methionine (2.8-3.2) and salt (3.8-4.2).    USE - Fertilizer used as secondary fertilizer for regulating bacteria balance in plant and soil.    ADVANTAGE - The fertilizer is safe and eco-friendly, contains nutritional biological material, promotes growth of plant, improves soil, strengthens fertility of soil and enhances plant resistance against disease.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing fertilizer, which involves:    (A) crushing and mixing Chinese mugwort, medlar, fructus amomi, Polygonum multiflorum, malt, pericarpium citri reticulatae, Areca nut and rhizoma ligustici wallichii uniformly;    (B) adding lysine, methionine, salt, yeast, Lactobacillus, photosynthetic bacteria and cellulose-decomposing bacteria to the mixture;    (C) adding 10-30% of water to the mixture and stirring uniformly; and    (D) fermenting the mixture in anaerobic condition for 15-20 days at room temperature to obtain fertilizer.
NOVELTY - An organic fertilizer comprises (wt.%) castor dreg (5-50), humic acid (5-20), abamectin (5-50), and fermented chicken manure and/or cow dung (5-50).    USE - An organic fertilizer for grass (claimed) for golf course, football field or public green landscape.    ADVANTAGE - The fertilizer has subterranean pest resistance and total nutrient of above 5%; is rich in nitrogen, phosphorus, potassium, iron, manganese, zinc, selenium and trace amount of castor toxin and abamectin; and utilizes natural resources thus not harming the environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the fertilizer mixing raw materials, granulating the mixture, and drying.
NOVELTY - Organic fertilizer is produced by using vinegar residue, where vinegar residue is produced as associated secondary product in the production process of edible vinegar. Plant ash is utilized as auxiliary material. The raw materials are mixed with bacteria for processing aerobic fermentation and rotten fermentation to obtain fertilizer with organic matter content which is not lower than 50% and pH value of 6.5-8.0, where moisture content is less than 20% and total nutrient content is not less than 4.0%.    USE - Organic fertilizer used as agrochemical fertilizer.    ADVANTAGE - The organic fertilizer is eco-friendly and free from harmful matter with high fiber content and high acidity, and utilizes plant ash that contains potash fertilizer as acidity regulator. The preparation of fertilizer uses waste material.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing organic fertilizer, which involves:    (A) preparing raw material and mixing it with bacteria;    (B) composting the mixture to carry out fermentation process, where vinegar residue with moisture of 72-75% is produced in the production process of edible vinegar by using filter press;    (C) using raw material vinegar residue (90-92 wt.%) and plant ash (8-10 wt.%) with pH higher than 9 and potassium content higher than 7%;    (D) mixing raw materials uniformly to obtain fermentation material with pH value of 6.0-7.0;    (E) adding bacteria strain with 0.1-0.2 wt.% of the fermentation material; and    (F) composting the mixture to carry out aerobic and rotten fermentation processes.
NOVELTY - Household garbage processing involves selecting ventilated place free from noise, building a bioreactor according to life habit of earthworm and culturing earthworm in 20000-40000 m2 area. Household garbage is selected, earthworm is processed, and earthworm is mixed with soil in 10:1 ratio and kept for 3 days. Earthworm feed is prepared and 10Kg of the feed is put in bioreactor for each square meter of earthworm culture. Temperature of culturing bed is 15-25 degrees C, moisture content is 50-70% and pH value is 6-8. Growing earthworms are placed into another feeding bed for processing next garbage.    USE - Method for processing household garbage in an earthworm bioreactor (claimed).    ADVANTAGE - The method enables to process household garbage on large scale by using the modern earthworm bioreactor, where traditional Chinese medicine, health products, fish food and green organic fertilizer are also produced by using the metabolized garbage feed and garbage products produced during the process.
NOVELTY - The furnace has a gasification pipe consisting of a fuel gas production barrel (1), a fan (2), a gas guide pipe (3), a separation barrel (5), a gas return conduit (6), a gas furnace (9), a chimney (11), an air duct (4), a gas division duct (7), a gas stove (8) and a hot water tank (12). The gas division duct is connected with the gas stove. The hot water tank is fixedly set at periphery of the fuel gas production barrel to form a multi-functional furnace structure generating burning gas by carbonizing at high temperature and high oxygen.    USE - Multifunctional bio-waste gasification furnace.    ADVANTAGE - The furnace produces strong fire, reduces the amount of smoke discharge, and avoids environmental pollution. The furnace can be used for warming, and the hot water tank provides water, so that the stove has wide range of application, and is convenient to use.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a multifunctional bio-waste gasification furnace.    Fuel gas production barrel (1)    Fan (2)    Gas guide pipe (3)    Air duct (4)    Separation barrel (5)    Gas return conduit (6)    Gas division duct (7)    Gas stove (8)    Gas furnace (9)    Chimney (11)    Hot water tank (12)
NOVELTY - The methane generator has a hot air opening (1) arranged in communication with top gas cavity (3) formed in the upper portion of generator main portion (5). A side gas cavity (4) is formed on the side surface of generator main portion. A side gas cavity hot air outlet (6) and side gas cavity hot air inlet (7) are connected to side gas cavity. The generator main portion is arranged in methane tank (8).    USE - Methane generator.    ADVANTAGE - The operation efficiency of methane generator is improved. The methane gas production amount is increased, and the energy consumption amount and cost of the methane generator are reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the methane generator.    Hot air opening (1)    Top gas cavity (3)    Side gas cavity (4)    Generator main portion (5)    Side gas cavity hot air outlet (6)    Side gas cavity hot air inlet (7)    Methane tank (8)
NOVELTY - The processor has filter units having side plates connected to side face of screen holder along length direction of case. The side plates between upper and lower rolling drums are evenly provided with multiple rotatable idler rollers. The filter screen on outer side of idler roller is sleeved between upper and lower rolling drums. A deslagging mechanism is arranged between top sides of side plates at one side of dump tank fixed on side face of side plate in opposite to screen holder.    USE - Biogas residue and liquid biogas processor.    ADVANTAGE - The biogas residue and liquid biogas processor is durable, reliable and has high suspension organic mass filtering rate.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of biogas residue and liquid biogas processor.
NOVELTY - Edible mushroom cultivating material comprises (in parts weight): traditional Chinese medicinal residue (50-70), cotton seed shell (10-20), corn powder (5-10), quick lime (2-5), nitrogen fertilizer (5-10), monopotassium phosphate (2-4), montricin (0.1-0.2), microelements (0.4-0.8) and iron salt (0.2-0.4).    USE - As edible mushroom cultivating material.    ADVANTAGE - The edible mushroom cultivating material can be prepared by cost-effective process without causing environmental pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing edible mushroom cultivating material, which involves mixing the above-cited raw materials, adding water to the mixture, agitating the mixture and subjecting to heap-building fermentation treatment to prepare cultivating material, adding the cultivating material into a bag and sterilizing the bag, and naturally cooling to obtain the edible mushroom cultivating material.
NOVELTY - Amantadine hydrochloride is added to nitrifying agent, reacted in ice-water bath for 1-2 hours, and then reacted at room temperature. The obtained light yellow liquid is poured into ice, and stirred, to obtain bluish green liquid. Solid alkali is added to bluish green liquid, stirred, the temperature is maintained at less than 80 degrees C, pH is regulated to 10-12, and stirred. The solution is pumped, filtered and extracted using methylene dichloride. The reaction product is dried, methylene dichloride is vaporized-out, and recrystallized, to obtain 3-amino-1-adamantane alcohol.    USE - Preparation of 3-amino-1-adamantane alcohol used in preparation of vildagliptin used for treating diabetes.    ADVANTAGE - The 3-amino-1-adamantane alcohol is prepared easily, rapidly and economically in high yield, without causing environmental pollution.    DETAILED DESCRIPTION - Amantadine hydrochloride is added to nitrifying agent in different stages, reacted in ice-water bath for 1-2 hours, and then reacted at room temperature for 1-30 hours, to obtain light yellow liquid. The light yellow liquid (1 ml) is poured into the ice (0.1-10 g), and stirred continuously for 0.5-2 hours, to obtain bluish green liquid. Solid alkali is added to bluish green liquid, stirred, the temperature is maintained at less than 80 degrees C, pH is regulated to 10-12, and the solution is stirred for 30 minutes. The solution is pumped, filtered and extracted using methylene dichloride. The obtained reaction product is dried using anhydrous sodium sulfate, methylene dichloride is vaporized-out, and recrystallized using ethyl acetate, to obtain 3-amino-1-adamantane alcohol in form of white solid.
NOVELTY - A burning supporting chamber (14) is connected with an upper end of the burning chamber (8) having a feed hole (7). A blanking chamber (10) is provided at the lower end of burning chamber. A water jacket (13) is covered outside the burning chamber. A water inlet and outlet joints are connected with a heating device. A chimney (15) is installed at the top of the furnace. An automatic discharge door is installed at the bottom of the blanking chamber. Gas storage tank is provided with a gas pump for providing carbonizing gas.    USE - Burning furnace for producing charcoal using cotton and linen straws.    ADVANTAGE - Recycling efficiency of cotton and linen straws can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of burning furnace.    Feed hole (7)    Burning chamber (8)    Blanking chamber (10)    Water jacket (13)    Burning supporting chamber (14)    Chimney (15)
NOVELTY - Magnetic powder is added to biochemical pond, to obtain sewage containing reduced concentration of sludge.    USE - Sewage treating technique.    ADVANTAGE - The method effectively and stably removes nitrogen and other pollutants from sewage containing high concentration of active sludge and low-dissolved oxygen within short period of time.
NOVELTY - Sludge composting method, involves adding auxiliary material to sludge to obtain sludge windrow, spraying and inoculating cytokeratin (CK)21 bacteria on sludge windrow, processing aerobic fermentation to sludge windrow, to obtain powdered windrow, adding curing agent to the fermented powdered windrow, drying and crushing the powdered windrow, adding nutritious element and again inoculating the CK21 bacteria to the powdered windrow, crushing the obtained product, granulating and forming the crushed product to obtain organic-inorganic-microbial organic fertilizer.    USE - The method is useful for composting sludge, which is useful for preparing fertilizer.    ADVANTAGE - The method reduces moisture of the sludge, reduces energy consumption for overturning the windrow, rapidly degrades organic substance without producing odor, reduces damage of the heavy metal to environment, and is performed in a short period of time. The prepared product is rich in nutrients and is easily absorbed by plants.
NOVELTY - Creation of multilayer supporting electrode with derivative-porous structure and subsequent application of gas-proof thin-film electrolyte layer is carried out in the following manner. Creation of electrode layer with minor volume porosity and pore size is carried out by melting surface electrode layer with electron beam to depth of 1-1.5 micron, and gas-proof thin-film electrolyte application is carried out using magnetron sputtering method. Before melting surface electrode layer with electron beam, this layer is covered with electrolyte film using magnetron sputtering method. Melting of surface layer is carried out with electron beam having following parametres: beam energy density is 0.8/3 J/cm2, pulse number is 1/6.    USE - Electricity.    ADVANTAGE - Decrease in porosity and pore size of support electrode surface layer. 3 cl, 6 dwg, 1 tbl, 2 ex
NOVELTY - Electrolysis cell for producing hydrogen and oxygen has a housing with an electrolyte, for example aqueous sodium hydroxide solution, as well as working electrodes which directly take part in the electrolysis process. The electrolysis cell also contains solution-polarising electrodes which are electrically insulated from the electrolyte by an insulator and are placed on the sides of the inter-electrode space.    USE - Chemistry.    ADVANTAGE - More efficient water decomposition. 1 dwg
NOVELTY - Providing a combustion fuel comprises: collecting a by-product of a process for producing an alcoholic product; and providing the by-product as a combustion fuel.    USE - The method is useful for providing a combustion fuel.    ADVANTAGE - The by-product, rather than being discarded, is an excellent combustion fuel for industrial or domestic applications. In the combustion fuel: the material used to form the briquettes is impregnated with alcohol, thus the briquettes are more flammable and quicker to catch fire; during burning in a fire, the pleasant aroma of the spirit is released; and the alcohol acts as a preservative to increase shelf-life and resist mold.    DETAILED DESCRIPTION - An INDEPENDENT CLAIMS is also included for the combustion fuel comprising the briquette formed from the by-product of a process for producing the alcoholic product.
NOVELTY - Producing fuels from biomass comprises preparing a mixture of biomass with a carbonate-containing solids, reacting the mixture by heating at 280-450 degrees C. The carbonate-containing solid is a wood ash, an alkali- or alkaline earth metal carbonate.    USE - The method is used for producing fuels or lubricant (claimed).    ADVANTAGE - The method comprises wood ash which has special surface structure and surface chemistry, thus obtained product has a lower viscosity and a lower acid value.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for device for producing fuels from biomass comprising a reactor container containing the mixture of biomass and the carbonate-containing solid, where the reactor container has a pressure of 0.1-2, preferably 0.8-1.2 bar and equipment for heating the reactor container at 280-450 degrees C.    DESCRIPTION OF DRAWING(S) - The figure shows a flow diagram of the process of producing fuels from biomass(Drawing includes non English language text).
NOVELTY - Concentrated producer gas generator includes concentrated oxygen for heating wood, where the concentrated oxygen is blown into a closed combustion chamber. The combustion chamber is filled with wood or waste wood.    USE - Concentrated producer gas generator.    ADVANTAGE - The concentrated producer gas generator enables to produce the concentrated producer gas having very high quality in an eco-friendly and cost-effective manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a concentrated producer gas generator. (Drawing includes non-English language text).
NOVELTY - Use of oxygen storage materials deposited on positively charged anodes of electrolyzers in contact with anodic active catalyst materials for preventing oxidation of the anodic active catalyst materials using preferential oxidation of oxygen storage materials to allow unlimited on-off switching without corrosion of electrodes during stand-by mode, shut down mode, intermittent operation, and normal operation of electrolyzer powered by renewable energy and other power sources.    USE - The oxygen storage materials deposited on positively charged anodes of electrolyzers is useful for preventing limited on-off switching cycle in conventional electrolyzers.    ADVANTAGE - The use of oxygen storage material and the use of the reduction load to convert the oxides into pure metal by reduction eliminate the use of protective current in stand-by mode as in conventional electrolyzers, and as a result, nitrogen purging during stand-by mode and start-up phase of electrolyzer becomes unnecessary (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for oxygen storage materials and the anodic active catalyst materials of positively charged anodes become partially oxidized over a period of time, which is reduced to pure metal by connecting a unidirectional, resistive reduction load across the anode and cathode of electrolyzers to break the oxides from anodes to supply oxygen to react with hydrogen stored in cathodes.
NOVELTY - Treatment of ligno-cellulosic biomass involves soaking a ligno-cellulosic biomass feedstock in vapor and/or liquid water at 100-210 degrees C for 1 minute to 24 hours to create a soaked biomass containing a dry content and a first liquid; separating at least a portion of the first liquid from the soaked biomass to create a first liquid stream and a first solid stream, where the first solid stream contains the soaked biomass; steam exploding the first solid stream to create a steam exploded stream comprising solids and a second liquid.    USE - For treatment of ligno-cellulosic biomass (claimed), used to produce ethanol.    ADVANTAGE - The process has improved severity of the steam explosion which at the same time produces a product with low furfural; and is improved method for pretreatment of biomass.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for composition of ligno-cellulosic biomass comprising a solid, a liquid, furfural, an amount of C5's based upon the amount of arabinan and xylan and the monomers, dimers, oligomers and polymers of arabinose and xylose in the liquid and solid of the composition, an amount of C6's based upon the glucan content which includes the monomers, dimers, oligomers and polymers of glucan in the liquid and solid of the composition, where the ratio of the amount of C5's to the amount of C6's is less than 0.50 and the ratio of the amount of the furfural to the amount of C5's and C6's added to together is less than 0.0060.
NOVELTY - Method for treating aqueous effluents comprising a complex mixture of substances containing native hydrocarbons of petrol and additives present in petrol or diesel, comprises: growing a bacteria comprising Rhodococcus wratislaviensi CNCM I-4088 and Rhodococcus aetherivorans CNCM I-4089 under aerobic conditions in the presence of a growth substrate containing the mixture as carbon source; and degrading the part of the mixture by the bacteria to give final degradation products comprising carbon dioxide, water and the biomass.    USE - The method is useful for treating aqueous effluents for preparing carbon dioxide, water and biomass.    ADVANTAGE - The process is capable of lowering the residual concentrations in pollutants, urban or industrial wastewater or contaminated aquifers.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for Rhodococcus wratislaviensi CNCM 1-4088 and Rhodococcus aetherivorans CNCM I-4089.
NOVELTY - The method involves providing natural gas, and pre-cooling and liquefying the natural gas by heat exchange of the natural gas with a refrigerant fluid contained in a pre-cooling and liquefaction cycle, where the fluid is made of propane and mixture of hydrocarbons and nitrogen. A compressor (7) is included in the cycle and driven by driving units including a gas turbine i.e. aero-derivative turbine, that produces fumes at a temperature less than 510 degree Celsius. A part of heat of fumes is transferred from the gas turbine towards a refrigerating machine.    USE - Method for producing liquefied natural gas for an engine of a jet aircraft.    ADVANTAGE - The method optimizes the energetic efficiency of the natural gas liquefaction installation without using a complex equipment such as high pressure vapor system, thus providing profitable output in an effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an installation for production of liquefied natural gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a natural gas liquefaction installation.    High pressure evaporator (2)    Average pressure evaporator (3)    Low pressure evaporator (4)    Compressor (7)    Heat exchangers (9-11)
NOVELTY - Producing biofuel by heterogeneous catalysis of triglycerides with alcohols comprises: (a) thermal activation of basic solid catalyst precursor; (b) transesterification; (c) removing product of transesterification; (d) filtration of the product of transesterification to remove catalyst particles; (e) neutralization of remaining catalyst in the transesterification product after extraction and filtration; (f) decanting and obtaining organic phase (ester phase) and aqueous phase (alcohol phase); and (g) removing traces of alcohol and its ester derivatives by heat treatment.    USE - The method is useful for producing biofuel by heterogeneous catalysis of triglycerides with alcohols (claimed), preferably for producing biodiesel.    ADVANTAGE - The invention offers the following advantages: simplicity, reproducibility and easy scaling of synthesis. The precursor of the active catalyst is stable in air; the temperature of decomposition or activation of the catalyst is lower than that of other basic solid catalysts. The kinetics of the reaction are similar to those described in homogenous catalytic reactions and significantly faster than in the case of other solid catalysts.
NOVELTY - A catalyst biodiesel composition comprises calcined natural waste materials.    USE - For transesterification of vegetable oil or animal fats to produce biodiesel (claimed).    ADVANTAGE - The catalyst has a surface area of 50-200 m2/g, has pore volume of 0.0001-0.6 cc/g, and an average pore size of 50-200 Angstrom ; and is derived from inexpensive easily available natural waste materials preferably fresh or waste natural seashell and eggshells alone or in complex with alcohol or phenol. Thus the catalyst composition is inexpensive, recyclable and works under normal temperature and pressure conditions. By using the catalyst an easy and fast transesterification process is carried out to produce biodiesel with excellent yields and conversion. The catalyst is recyclable and reusable.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparation (p1) of the catalyst composition for producing biodiesel involving washing and drying of seashells followed by grounding and sieving; calcining the sieved and dried seashell; washing and drying of eggshell followed by grounding and sieving; calcining the dried and sieved eggshells; grinding to fine particles a composition of calcined seashells and eggshells homogenously; calcining the dried extrudated material in a furnace at 750-1000 degrees C for a time period of 3-12 hours, resulting in an in situ generation of the active components; and obtaining final catalyst composition; and    (2) production (p2) of a biodiesel by reacting triglycerides with an alcohol in presence of the catalyst composition derived from natural waste materials.
NOVELTY - A transformant, preferably Corynebacterium glutamicum capable of producing butanol, comprising one or more of endogenous genes (foreign genes) (a)-(e), is new. The gene (a) encodes acetohydroxy acid synthase enzyme, gene (b) encodes acetohydroxy acid isomeroreductase enzyme, gene (c) encodes dihydroxy-acid dehydratase enzyme, gene (d) encodes 2-ketoacid decarboxylase enzyme and gene (e) encodes alcohol dehydrogenase enzyme.    USE - The transformant is useful for producing isobutanol (claimed). The isobutanol is used as bio-fuel, and as additive in diesel or gasoline.    ADVANTAGE - The isobutanol can be efficiently produced and can be collected and purified easily as the transformant can produce isobutanol from e.g. carbohydrate without propagating substantially, and the carbonaceous source is chiefly utilized for producing isobutanol and not consumed for microbial proliferation. The isobutanol production can also be enabled using renewable raw materials. The rational method can be used for industrial production of isobutanol. The isobutanol mixed with diesel or gasoline can prevent moisture and corrosion.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of isobutanol, which involves adding transformant or its processed material to culture medium containing saccharides in reduction condition, and collecting the produced isobutanol.
NOVELTY - Housing (500) accommodates the cell stacks (100,110) and modifier (200). The cell stacks are arranged under the vaporization section and modification section of modifier respectively. The modification section modifies the raw fuel gas supplied from vaporization section. Oxidant gas chamber (310) is formed in the center portion of oxidant gas introducing element (300). The oxidant gas flow channels (320,330) are asymmetrically formed in cell stacks respectively, so that heat transfer amount of cell stack (110) is more than that of the cell stack (100).    USE - Solid oxide fuel cell for fuel cell system of vehicle.    ADVANTAGE - The uniformity of temperature distribution in cell stacks of fuel cell can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a top view of the solid oxide fuel cell. (Drawing includes non-English language text)    Cell stacks (100,110)    Modifier (200)    Oxidant gas introducing element (300)    Oxidant gas chamber (310)    Oxidant gas flow channels (320,330)    Housing (500)
NOVELTY - The catalyst layer (12A) is formed continuously at surface of belt-shaped electrolytic membrane (12S) or diffused layer (14A) for mutual connection. The predetermined shaped catalyst layers (12C) and diffused layer (14C) are formed at fixed space of opposite side of connected region of belt-shaped electrolytic membrane or diffused layer. The strip-shaped electrolytic membrane and diffused layer are pierced on the outer side of visible outline of the predetermined shaped catalyst layer and diffused layer.    USE - Manufacturing method of fuel cell electrode (claimed).    ADVANTAGE - The strip-shaped electrolytic membrane and diffused layer are pierced on outer side of visible outline of predetermined shaped catalyst layer and diffused layer. Hence the generation of short circuit between structural components of fuel cell electrode corresponding to anode and cathode sides, can be prevented. The fuel cell electrode is operated effectively without influence of difference in outside dimensions of cathode and diffused layers at anode and cathode sides. The manufacturing process of fuel cell electrode is simplified by avoiding unnecessary positioning operation of structural components. The utilization of reinforcement film is avoided to improve handling property of electrolytic membrane for ensuring smooth manufacturing process of fuel cell electrode without increasing the manufacturing cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell electrode.    DESCRIPTION OF DRAWING(S) - The drawing shows the perspective view explaining the manufacturing process of fuel cell electrode.    Membrane electrode assembly (12)    Catalyst layers (12A,12C)    Electrolytic membrane (12S)    Diffused layers (14A,14C)    Water repellent paste (24)
NOVELTY - Indirect internal reformed solid oxide fuel cell system comprises modifier (2) with a modification-catalyst (3) layer which manufactures reformed gas from hydrocarbon fuel, solid oxide fuel cell (1), electric heater (4) which heats the modification-catalyst layer with resistors, temperature detectors (5) which detects the temperature of the modification-catalyst layer, and heater controller which selectively supplies electricity to the resistor.    USE - Indirect internal reformed solid oxide fuel cell system for electric power generating apparatus and cogeneration system for moving bodies.    ADVANTAGE - Easily prevents lack of heating during operation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for operating indirect internal reformed solid oxide fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block-diagram of the indirect internal reformed solid oxide fuel cell system. (Drawing includes non-English language text).    Solid oxide fuel cell (1)    Modifier (2)    Modification-catalyst (3)    Electric heater (4)    Temperature detectors (5)
NOVELTY - Hydrogen generating apparatus (1) for fuel cells comprises modification part (7), combustion part (14) which heats the modification part, raw fuel supply part (6) which supplies fuel to the modification part, temperature detection part, raw fuel supply patterns, storage part (19) which stores raw fuel supply pattern, and control part which selects raw fuel supply pattern based on detected temperature.    USE - Hydrogen generating apparatus for fuel cells.    ADVANTAGE - Maintains modification temperature simply.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the hydrogen generating apparatus. (Drawing includes non-English language text).    Hydrogen generating apparatus (1)    Raw fuel supply part (6)    Modification part (7)    Combustion part (14)    Storage part (19)
NOVELTY - The removal method involves conducting the flue gasses at a temperature of at most 500 degrees Celsius over a noble metal catalyst comprising a noble metal on a solid oxidic support under the conditions of no poisoning or inhibition of noble metal catalyst by sulfur dioxide and/or nitric oxide. The noble metal catalyst is selected from palladium and/or platinum, and optionally promoted with copper and provided on oxidic support. The conditions of no poising or inhibition of catalyst occurs are obtained by upstream removal of nitric oxide and/or sulfur dioxide from the flue gasses.    USE - Removal method for methane from flue gasses to be used as carbon dioxide for horticultural applications.    ADVANTAGE - Provides method which can also remove ethylene simultaneously with the removal of methane. Prolongs the service life of catalyst, and prevents the need for a separate heating step since the activation or calcination is simply done in air at 350 to 500 degrees Celsius, or with flue gas in the same temperature range.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph of the conversion of methane.
NOVELTY - A diesel-manufacturing catalyst contains a metal phosphorus compound.    USE - Catalyst is used for manufacturing biodiesel (claimed).    ADVANTAGE - The catalyst enables production of high quality biodiesel having low pour point.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of biodiesel.    DESCRIPTION OF DRAWING(S) - The drawing shows the flowchart of manufacture of biodiesel.
NOVELTY - A biomass containing hard substrate is contacted with exogenous microbe (110), and obtained reaction mixture is fermented to improve the conversion of biomass into methane.    USE - Anaerobic method used for improving conversion of biomass into methane (claimed).    ADVANTAGE - The method enables efficient conversion of biomass, and provides methane in high yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for anaerobic fermentation system, which has anaerobic fermenter having biomass with hard substrate, and an exogenous microbe.    DESCRIPTION OF DRAWING(S) - The drawing shows flowchart of anaerobic method.    Exogenous microbes (110)    Hydrolysis (115)    Acidogenesis (122)    Acetogenesis (125)    Methanogenesis (140)
NOVELTY - A hydrogen generator (1) consists of modification portion (5), transformation portion (6), heater (3), ambient-temperature measurement unit (15), and transformation-portion temperature controller. The modification portion produces reformed gas. The transformation portion reduces carbon monoxide in reformed gas. The heater maintains temperature of modification and transformation portions. The measurement unit measures ambient temperature of transformation portion. The temperature controller adjusts heat amount to transformation portion.    USE - Hydrogen generator is used in fuel-cell power generators (claimed).    ADVANTAGE - The hydrogen generator completely reduces carbon monoxide concentration and suppresses flooding phenomenon. Optimal operating temperature is maintained.    DETAILED DESCRIPTION - A hydrogen generator consists of a modification portion, a transformation portion, a heater, an ambient-temperature measurement unit, and a transformation-portion temperature controller. The modification portion produces reformed gas containing hydrogen as main component from water vapor and raw material containing hydrocarbon as main component, by reforming reaction. The transformation portion reduces carbon monoxide contained in the reformed gas. The heater maintains the temperature of modification portion and transformation portion. The ambient-temperature measurement unit measures the ambient temperature of transformation portion. The temperature controller adjusts the heat amount to the transformation portion by the heater based on the measured ambient temperature. An INDEPENDENT CLAIM is included for fuel-cell power generator.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the hydrogen generator. (Drawing includes non-English language text)    Hydrogen generator (1)    Heater (3)    Modification portion (5)    Transformation portion (6)    Ambient-temperature measurement unit (15)
NOVELTY - A CBM hydrate manufacturing apparatus (1) consists of a unit (2) for synthesizing CBM hydrate from a mixture containing CBM and accompanied water taken out from a seam (G1), a separator (3) for separating CBM hydrate and residual water, and a circulation unit (4) for circulating residual water by mixing with the mixture.    USE - Apparatus is used for manufacturing CBM hydrate (claimed).    ADVANTAGE - The apparatus has a simple structure and enables efficient conveyance of CBM taken out from the seam. Water taken out simultaneously with CBM can be used effectively. CBM is more economical than liquefied natural gas and can be stored with high density than compressed gas. High concentration of ingredients in residual water and high purification of CBM are achieved. Efficient transport of CBM is achieved by hydrating the mixture containing CBM and accompanied water in a raw material. The apparatus also contributes to environmental protection and resource development.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of CBM hydrate, which involves pumping up stratum water existing in a seam and taking out CBM from seam, synthesizing CBM hydrate from the mixture, separating residual water, and circulating residual water.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the CBM hydrate manufacturing apparatus. (Drawing includes non-English language text)    CBM hydrate manufacturing apparatus (1)    CBM hydrate synthesis unit (2)    Separator (3)    Circulation unit (4)    Seam (G1)
NOVELTY - Biomass charcoal (3) is obtained by carbonizing biomass (1) using a rotary kiln (10). Biomass is contacted with exhaust gas (4) containing tar generated by carbonization and discharged from the rotary kiln, before being supplied to the rotary kiln. Biomass to which at least one portion of tar is adhered is supplied to the rotary kiln.    USE - Manufacture of biomass charcoal for use as fuel.    ADVANTAGE - The method enables efficient manufacture of biomass charcoal having high calorific value, with high yield and reduced quality deterioration. Since tar is used effectively, burden of tar process is eased. Dry distillation product is lightened and waste-gas treatment is reduced. Recycling of biomass is accelerated and emission of carbon dioxide is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing apparatus of biomass charcoal, consisting of a rotary kiln, a filling tank (11) which supplies biomass to the kiln, and a gas flow path which supplies the gas discharged from the kiln to the lower portion of filling tank.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the manufacturing apparatus of biomass charcoal.    Biomass (1)    Biomass charcoal (3)    Exhaust gas (4)    Rotary kiln (10)    Filling tank (11)
NOVELTY - A waste treatment apparatus has high temperature reactor (5) having gas reforming furnace (5a) and gasified melting furnace (5b). The gasified melting furnace has oxygen-containing gas top supply port (13a) and oxygen-containing gas lower supply port (15a). The oxygen-containing gas top supply port supplies oxygen-containing gas to upper part of waste material deposit (12) while the oxygen-containing gas lower supply port supplies oxygen-containing gas to the lower part of waste material deposit.    USE - Waste treatment apparatus for melting treatment of waste material in refuse processing facility.    ADVANTAGE - Prevents lack of heating of the waste material in waste material deposit. Enables waste treatment apparatus to perform stable partial oxidation and gasification and as well as melting of the waste material.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a waste material processing method in refuse processing facility.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional side view of the refuse treatment facility. (Drawing includes non-English language text).    High temperature reactor (5)    Gas reforming furnace (5a)    Gasified melting furnace (5b)    Waste material deposit (12)    Oxygen-containing gas top supply port (13a)    Oxygen-containing gas lower supply port (15a)
NOVELTY - Preparing a product involves contacting at least a portion of a material with an alcohol and an acid catalyst so as to form a reacted mixture comprising alkyl esters of free fatty acids, and/or glycerides comprising portion of a material (at least 25 wt.%), and contacting occurring at 80-200 degrees C and at greater than atmospheric pressure.    USE - For preparing a product, particularly biodiesel product.    ADVANTAGE - The method is capable of converting feedstocks, such as restaurant trap grease, which contain higher levels of free fatty acids (FFAs) and provides a cost-effective way to convert feedstock containing used oils, such as restaurant trap grease, into esters of FFAs, including biodiesel.
NOVELTY - The feed separating process involves partially condensing feed (1) to provide a hydrogen-enriched vapor fraction (4) and a carbon monoxide-enriched liquid fraction (5). Portion of carbon monoxide-enriched liquid fraction is combined with regulated portion of hydrogen-enriched vapor fraction to form two-phase admixture (6) which will be separated cryogenically in a fractionator (103) to form a first product gas having hydrogen carbon monoxide molar ratio of 0.5:1 and 2.5:1. Liquid fraction of two-phase admixture and a portion of carbon monoxide-enriched liquid fraction are vaporized partially.    USE - Feed separating process for use in e.g. syngas production.    ADVANTAGE - Provides product gas with desired hydrogen and carbon monoxide at molar ratio at desired pressure without further compression. Reduces power requirements for compressing syngas product streams. Reduces amount and size of capital equipment and the associated costs for syngas production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the apparatus for separating a feed comprising hydrogen, carbon monoxide, methane, and optionally nitrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of the process flow diagram for producing a product gas as hydrogen product gas and a carbon monoxide product gas.    Condensing feed (1)    Hydrogen-enriched vapor fraction (4)    Carbon monoxide-enriched liquid fraction (5)    Two-phase admixture (6)    Fractionator (103)
NOVELTY - The process involves contacting a natural gas feed with a nonflammable biphasic refrigerant i.e. liquid-gaseous refrigerant, and a gaseous refrigerant comprising nitrogen. The refrigerated natural gas feed is expanded using an expansion device e.g. flashing expander, for forming a fuel gas stream (30) and a liquefied natural gas stream, where the flash gas stream is recycled. A portion of the gaseous refrigerant following contact with the natural gas feed is expanded in an isentropic process for cooling the natural gas feed.    USE - Process for performing liquefaction of a natural gas feed during crude oil production in an offshore crude production facility.    ADVANTAGE - The process enables performing liquefaction of natural gas feed while performing crude oil production in the offshore crude production facility in simple manner with high thermodynamic performance and inherent safety levels. The method enables performing natural gas liquids (NGL) extraction before feed gas enters the main liquefaction heat exchanger for avoiding freezing of heavy components at cryogenic temperatures in cost effective manner.    DETAILED DESCRIPTION - The process pre-treats the natural gas feed to recover volatile hydrocarbon stream i.e. liquid petroleum gas (LPG) stream, present in the natural gas feed prior to a liquefaction process, and retains ethane, propane and butane in the liquefied natural gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram illustrating a process for performing liquefaction of a natural gas feed.    Amine contactor (25)    Fuel gas stream (30)    Nitrogen refrigerant compressor (41)    Expander-compressor (43)    Turboexpander (44)
NOVELTY - A hydrogen generation system (100) comprises a reactor (102) including a solution inlet port (106) and a hydrogen outlet port (108); a reactant fuel material (101) added to the reactor; and an aqueous solution added via the solution inlet fill port to the reactant fuel material in the reactor to generate hydrogen gas to be routed via the hydrogen outlet port to an industrial application.    USE - A hydrogen generation system (claimed).    ADVANTAGE - The system does not require an additional catalyst chamber, and is easily start-stop controlled by the simple addition of an appropriate aqueous medium to satisfy the hydrogen demand of a fuel cell or hydrogen-drawing system.    DESCRIPTION OF DRAWING(S) - The drawing is a sectional view of the hydrogen generation system.    Hydrogen generation system (100)    Reactant fuel material (101)    Reactor (102)    Solution inlet port (106)    Hydrogen outlet port (108)
NOVELTY - Removal of hydrocarbon impurity from acetic acid production intermediate comprises extracting intermediate with hydrocarbon extracting agent to form light phase comprising hydrocarbon impurity and extracting agent and heavy phase comprising acetic acid.    USE - Method for removing hydrocarbon impurity from acetic acid production intermediate (claimed).    ADVANTAGE - The method removes both high boiling and low boiling hydrocarbon impurities from acetic acid production process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for producing acetic acid comprising reacting methanol and carbon monoxide in presence of carbonylation catalyst, catalyst stabilizer, methyl iodide, water and methyl acetate to produce acetic acid stream comprising hydrocarbon impurity; flashing acetic acid stream into vapor stream comprising acetic acid, water, methanol, methyl acetate, methyl iodide and hydrocarbon impurity, and a liquid stream comprising catalyst and catalyst stabilizer; separating vapor stream by distillation into product stream comprising acetic acid and water, and overhead stream comprising methyl iodide, water, methyl acetate, acetic acid, and hydrocarbon impurity; condensing overhead stream into light, aqueous phase comprising water, and acetic acid, methyl acetate, and heavy, organic phase comprising methyl iodide, acetic acid, water, and the hydrocarbon impurity; distilling heavy, organic phase into a vapor stream comprising methyl iodide and a bottoms stream comprising acetic acid, methyl iodide, water, and hydrocarbon impurity; and extracting bottoms stream with hydrocarbon extracting agent, and forming light phase comprising hydrocarbon impurity and extracting agent and heavy phase comprising methyl iodide, water, and acetic acid.
NOVELTY - The method involves washing hydrogen sulfide containing raw gas in a bioscrubber (2) with a washing liquid including hydrogen sulfide oxidizing microorganism. The liquid is conveyed to a bioreactor (3) after washing the gas. The hydrogen sulfide is absorbed in the liquid during washing the gas. The liquid is loaded with the oxygen and the detention period of the liquid in the bioscrubber is specified such that biological oxidation takes place in the bioscrubber by the microorganism immobilized in absorption surface of the bioscrubber and the microorganism contained in the liquid.    USE - Method for biological desulfurization of gas i.e. biogas (claimed), from a biogas plant.    ADVANTAGE - The method enables biological desulfurization of the biogas into the hydrogen sulfide-residual concentration in the clean gas below 100 parts per million with less investment and operational costs.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a desulfurization system for biological desulfurization of biogas from a biogas plant including a bioscrubber.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a desulfurization system.    Desulfurization system (1)    Bioscrubber (2)    Bioreactor (3)    Feed line (4)    Return line (5)
NOVELTY - A calculating unit calculates actual weight of fuel supplied to gasifier based on variation of fuel weight per unit time in hopper detected by load cell. A potentiometer detects rotation speed of screw conveyer that supplies fuel in hopper to gasifier. A memory stores map prescribing relationship between rotation speed of screw conveyer, and fuel weight. A touch panel sets fuel weight supplied to gasifier based on map. A correction unit reduces/increases rotation speed of screw conveyer when calculated fuel weight is larger/smaller than set fuel weight.    USE - Control apparatus of gasifier for woody biomass power generating plant.    ADVANTAGE - The fuel of a fixed weight can be supplied steadily, by correcting the rotation speed of screw conveyer according to the fuel weight actually supplied to the gasifier while preventing the malfunction of the gasifier resulting from rapid change of rotation speed. Hence, the amount of generated gas of a gasifier is stabilized.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart explaining the control process of gasifier. (Drawing includes non-English language text)
NOVELTY - An elastomer composition is obtained by mixing a raw material containing dreg generated during fermentation process of organic substance with respect to elastomer component, and biomass extracted residue obtained by immersing biomass in a solvent and performing solid-liquid extraction. The ratio of elasticity modulus of high strain region with respect to elasticity modulus of low distortion region of tire formed using the elastomer composition is 2.7 or less.    USE - Elastomer composition is used for forming tire (claimed).    ADVANTAGE - The elastomer composition has improved physical properties, and is economically and easily manufactured without causing environmental pollution. The tire formed using the elastomer composition has low environmental impact.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for tire, which contains at least 1 portion containing the elastomer composition.    DESCRIPTION OF DRAWING(S) - The drawing shows sectional view of tire.    Bead portion (1)    Side wall portion (2)    Tread portion (3)    Carcass (4)    Belt (5)
NOVELTY - An air injection fan (21) injects air to an inlet port of desulfurization reaction tank (3). A hydrogen-sulfide sensor (31) provided in gas channel (11) detects content of hydrogen sulfide. An oxygen sensor (32) provided in an exhaust gas channel (12) detects the oxygen. A control apparatus (41) connected with hydrogen-sulfide sensor and oxygen sensor, controls air injection apparatus to determine air injection rate of air injection fan from the content of oxygen and hydrogen-sulfide.    USE - Desulfurizing apparatus for removing impurities such as hydrogen sulfide contained in biogas.    ADVANTAGE - Since the air injection rate of air injection fan is controlled from the content of oxygen and hydrogen-sulfide, the hydrogen sulfide can be removed stably and the hydrogen sulfide can be oxidized efficiently within the piping.    DETAILED DESCRIPTION - The gas channel sends biogas emitted from methane fermentation tank to desulfurization reaction tank. The exhaust gas channel discharges the desulfurized biogas. The desulfurization reaction tank comprises a piping in which the biogas is flowed. A filler is provided in the piping. The waste-water discharged from the methane fermentation tank is flowed to the inner pipe.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the desulfurizing apparatus. (Drawing includes non-English language text)    Desulfurization reaction tank (3)    Gas channel (11)    Exhaust gas channel (12)    Air injection fan (21)    Hydrogen-sulfide sensor (31)    Oxygen sensor (32)    Control apparatus (41)
NOVELTY - The water electrolyzing hydrogen-oxygen generator has a self-convection cooling system which is connected with upper end of electrolyte storing tank, and consists of self-convection radiating pipes, air duct, axial flow fan, and self-convection water tank. The self-convection radiating pipes are distributed in the air duct opened with an air inlet. The air inlet is connected to air sending opening of axial flow fan. An air outlet is provided at an upper end of self-convection water tank.    USE - Water electrolyzing hydrogen-oxygen generator.    ADVANTAGE - Energy consumption and size of water electrolyzing hydrogen-oxygen generator are effectively reduced, by removing electrolyte through hydrogen and oxygen.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the water electrolyzing hydrogen-oxygen generator.
NOVELTY - Enzymolysis of mixture of corncob acidolysis residues and stalk alkali-boiling residues comprises: (a) washing corncobs with water and acid to hydrolyze the corncobs, with the product of corncob acidolysis residues; (b) cutting and washing stalks, and hydrolyzing stalk chips under basic condition, with the product of stalk alkali-boiling residues; and (c) mixing corncob acidolysis residues with stalk alkali-boiling residues into enzymolysis substrate according to the weight ratio of 1-2:1; mixing their wash waters into enzymolysis bottom water, and carrying out enzymolysis by using cellulose.    USE - The process is useful for enzymolysis of mixture of corncob acidolysis residues and stalk alkali-boiling residues (claimed).    ADVANTAGE - In utilizing the process, the wash water mixture effectively reduces the consumption of acid and alkali in the enzymolysis, and almost all the wash water can be recycled to reduce effects to the environment; where the substrate can be quickly liquefied in the case of high concentration. Moreover, the process greatly reduces manufacturing cost without any influences to the hydrolysis rate of raw material.
NOVELTY - Circularly utilizing nitrogen source by fermenting waste cell through microorganism comprises: (a) pre-processing waste cell; (b) preparing hydrolyzed cell solution; and (c) preparing microorganism fermentation medium by using hydrolyzed cell solution as nitrogen source for fermentation production.    USE - The process is useful for circularly utilizing nitrogen source by fermenting waste cell through microorganism (claimed).    ADVANTAGE - In utilizing the process, the hydrolyzed cell solution prepared from fermented waste cell is used as nitrogen source for fermentation production of microorganism, which not only can reduce use amount of yeast powder, tryptone and other expensive nitrogen source but can also circularly use nitrogen source during fermentation process. Moreover, the process not only reduces production cost of product but also reduces burden for processing waste. Additionally, it is environment-friendly and has energy-saving social benefit; thus, it is effective and feasible.
NOVELTY - The device has a body (1), a chamber (2), a sealing cover (3), an air inlet pipe (4), and an escape pipe (5), where a periphery of a lower part of the chamber is provided with an oxygen supplying loop (6) communicating with the air inlet pipe. An upper part of the chamber is provided with a storage vat (7). An outlet barn (8) is arranged between the storage vat and an inner wall of the chamber. The outlet barn communicates with the escape pipe. Top portion of the body is provided with a hearth (10) communicating with the escape pipe.    USE - Integral composite gasification device for a biomass gasification stove.    ADVANTAGE - The device has quick gas forming function, less fuel consumption, low cost , simple structure, convenient use and avoids fume emission.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of an integral composite gasification device.    Body (1)    Chamber (2)    Sealing cover (3)    Air inlet pipe (4)    Escape pipe (5)    Oxygen supplying loop (6)    Storage vat (7)    Outlet barn (8)    Hearth (10)
NOVELTY - Oil in water dermo-cosmetic emulsion comprises: micelles containing at least one oil containing an active ingredient to diffuse through the skin, where the micelles have a minimum size (D10) of greater than or equal to 0.1 mu m and a maximum size (D90) of less than or equal to 0.4 mu m; water in which polysaccharide is dissolved, where the polysaccharide is able to form a film, after polymerization, and is present at 0.7-5 mass% of emulsion.    USE - The emulsion is useful: to treat or prevent itching on the skin of an animal other than that man; for treating itching and/or atopic dermatitis (all claimed); in the field of animal cosmetic; for protecting the skin surface against external aggression; and for diminishing and/or inhibiting the discomfort of skin sensations such as e.g. irritation, tingling, or tightness, where the animal is cat, dog, horse, rat, rabbit, or pig. No biological data given.    ADVANTAGE - The emulsion: is rapidly penetrated into the skin and permanently effective for prolonged time; prevents the action of free radicals on the hair and prevents the passage of ultraviolet radiation and dust; and quickly relieves irritated skin and/or itching, and limits the risk of skin damage and associated infections. The polysaccharide is more biocompatible and biodegradable.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a preparation of the emulsion comprising mixing at least one oil comprising an active ingredient to diffuse through the skin, an emulsifier, water and polysaccharide capable of forming a film after polymerization, where the mixing is carried out and emulsifier and polysaccharide are chosen to obtain the emulsion, after mixing step; and    (2) an animal other than man in which at least part of the skin carries the emulsion or the film resulting from polymerization of the polysaccharide of the emulsion.
NOVELTY - The device has a selector switch (1) connected with an intelligent control module (2) by signals (3, 4). Output signals (5, 6) of the selector switch are respectively matched with oil injection signal and ignition signal of an engine. Intelligent oil injection signal (7) of the intelligent control module is sent to an oil nozzle of the engine. An intelligent ignition transmission signal (8) is sent to an ignition device of the engine.    USE - Intelligent gasoline-butanol mixing fuel control device for engine.    ADVANTAGE - The device has reasonable design, energy-saving function, emission-reducing function and environment-friendly effect, low investment cost, quick effect and wide application range.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing an intelligent control device of gasoline-butanol mixing fuel for engine.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of an intelligent gasoline-butanol mixing fuel control device.    Selector switch (1)    Intelligent control module (2)    Signals (3, 4)    Output signals (5, 6)    Intelligent oil injection signal (7)    Intelligent ignition transmission signal (8)
NOVELTY - Aqueous type pesticide micro-emulsion of cypermethrin, comprises (in wt.%) cypermethrin (1.5-5), Triton X-100 (RTM: A nonionic surfactant comprising a hydrophilic polyethylene oxide group and a hydrocarbon lipophilic or hydrophobic group) (5-10), sodium dodecylbenzene sulfonate (5-15), cosurfactant (3-16) and deionized water (remaining).    USE - Used as an aqueous type pesticide micro-emulsion of cypermethrin.    ADVANTAGE - The aqueous type pesticide micro-emulsion of cypermethrin is a transparent single phase liquid and belongs to a green pesticide preparation.
NOVELTY - A methane gas refinery processing installation (3) comprises anaerobic digester tank which emits biogas, biogas holder which stores biogas from anaerobic digester tank through gas-sending line (8), methane gas holder (4) which stores purified gas from methane gas purifier through purification gas lines (10), methane gas purifier which raises purity of gas sent through supply gas line (8), gas densitometer which measures concentration of gas containing oxygen, and cutoff valve which blocks gas line when measured value of oxygen concentration increases in one of gas sampling points.    USE - A methane gas refinery processing installation.    ADVANTAGE - The installation can perform exploitation of energy of methane gas safely.    DETAILED DESCRIPTION - A methane gas refinery processing installation (3) comprises anaerobic digester tank which emits biogas, biogas holder which stores biogas from anaerobic digester tank through gas-sending line (8), methane gas holder (4) which stores purified gas from methane gas purifier through purification gas lines (10), methane gas purifier which raises purity of gas sent through supply gas line (8), gas densitometer which measures concentration of gas containing oxygen, and cutoff valve which blocks gas line when measured value of oxygen concentration increases in one of gas sampling points. The gas is regularly collected from four points which are gas-sending line, biogas holder, supply gas line and purification gas line.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of methane gas refinery processing installation.    Methane gas refinery processing installation (3)    Methane gas holder (4)    Supply gas and Gas-sending line (8)    Purification gas lines (10)
NOVELTY - Granule comprises (in %mass): agrochemical active components (3-30) including 1,3-dicarbamoyl thio-2-(N,N-dimethylamino)-propane hydrochloride and/or 5-dimethylamino 1,2,3-trithiane oxalate, biodegradable thermoplastic resin (50-90), and elution-in water stimulating material (7-42).    USE - The granule is useful for preventing or controlling fresh water spiral shell, preferably Pomacea canaliculata in paddy field (claimed).    ADVANTAGE - The granule can be prepared simply and cost-effectively, is environment-friendly, and does not cause any damage to the paddy crop. The granule controls freshwater spiral shell in paddy field for 2-3 weeks or more irrespective of influence caused by external environments such as rainfall. No dosage details given.
NOVELTY - The device has an unloading hopper (1) arranged upon a plate feeder (2). The plate feeder, a refuse crusher (3), a roller sieve (4), a magnetic separator (5), a dewatering machine (6), a drum dryer (7) and a refuse block press (8) are orderly connected with each other. An air blasting device (13) is connected with a slag discharging outlet (11) via a pipeline. A gas port (12) is placed on top of a normal pressure fixed bed gasification furnace body (9) and connected with a cyclone dust collector (14) in a gas purifying system via a gas output pipe (19).    USE - House refuse gasification processing device.    ADVANTAGE - The device processes the combustible material in the refuse into refuse derived fuel (RDF), and uses a fixed bed gasification furnace to pyrolyze, gasify and purify the refuse, so as to produce pure gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic side view of a house refuse gasification processing device.    Unloading hopper (1)    Plate feeder (2)    Refuse crusher (3)    Roller sieve (4)    Magnetic separator (5)    Dewatering machine (6)    Drum dryer (7)    Refuse block press (8)    Normal pressure fixed bed gasification furnace body (9)    Slag discharging outlet (11)    Gas port (12)    Blasting device (13)    Cyclone dust collector (14)    Gas output pipe (19)
NOVELTY - The device has a shell (1) whose upper part is provided with an air outlet pipe (7) and middle part is provided with an impurity removing zone (13) and a cylindrical gas and liquid separating zone (12). A lower part of the shell is provided with a water discharge descending pipe (3) and a lifting pipe that conveys mixing liquid of gas and water. An outlet of the descending pipe is connected with an inert gas pipe (5), and a discharge pipe (10) is provided at bottom of the device. A liquid caustic soda adding pipe (9) is provided on a middle part of the device.    USE - Device for separating and defoaming liquid and gas in anaerobic methane generated during biological anaerobism.    ADVANTAGE - The device is simple in structure and inexpensive. The device effectively separates the gas and liquid in methane generated during biologic anaerobism, so as to remove impure gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a device for separating and defoaming liquid and gas in anaerobic methane generated during biological anaerobism.    Shell (1)    Water discharge descending pipe (3)    Inert gas pipe (5)    Air outlet pipe (7)    Liquid caustic soda adding pipe (9)    Discharge pipe (10)    Cylindrical gas and liquid separating zone (12)    Impurity removing zone (13)
NOVELTY - A biodegradable agricultural mulching film is a thin film comprising traditional Chinese medicine (TCM) active component that can control root-knot nematode, and polybutylene succinate (PBS) or PBS copolymer. Mass ratio of active component and PBS or PBS copolymer is 1-500:1000.    USE - Biodegradable agricultural mulching film used for controlling root-knot nematode (claimed).    ADVANTAGE - The film is transparent or semitransparent which can be degraded easily easier, and has improved elongation at break and tensile strength, and good performance of resisting root-knot nematode with controlling rate above 90% and degradation rate in manure for six months of up to 80%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biodegradable agricultural mulching film, comprising washing the TCM containing active component, then drying, and crushing it, and soaking the crushed TCM in solvent at room temperature for 1-50 hours, and then performing water bath at 30-90 degrees C for 1-50 hours and keeping the temperature constant for 1-10 hours, filtering, and concentrating the filtrate, cooling and drying it to obtain TCM active component powder. Then, the biodegradable PBS or PBS copolymer particles are placed in an internal mixer to melt the PBS or PBS copolymer. The TCM active component powder is doped and mixed with the PBS or PBS copolymer. The mixture is then extruded by a single screw extruder for blowing film to produce the agricultural mulching film. The solvent is ethanol aqueous solution, acetone aqueous solution, ether, petroleum ether, or ethyl acetate.
NOVELTY - Fertilizer comprises (in wt.%): silicon-potassium fertilizer (9-10), urea (11-25), potassium chloride (10-20), monoammonium phosphate (25-35), ammonium chloride (12-26), synthetic ammonia (1.3-1.7), sulfuric acid (2.5-3) and attapulgite (not greater than 0.05), where fertilizer contains nitrogen, phosphorus, potassium and silicon.    USE - Fertilizer.    ADVANTAGE - The fertilizer is prepared by eco-friendly process with less consumption of energy and without using mineral slag and furnace slag, and has less transportation cost. The fertilizer is directly absorbed by root that avoids loss of fertilizer, and improves soil quality without polluting soil and rice quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing fertilizer, which involves:    (A) weighing, mixing and crushing raw materials other than synthetic ammonia to obtain granules;    (B) granulating the raw materials by using a granulator;    (C) adding synthetic ammonia and sulfuric acid to the raw materials during granulating process to obtain wet granules;    (D) drying the wet granules by using drier to obtain semi-finished product, where temperature of gas inlet and outlet is controlled; and    (E) sieving the semi-finished product by using sieving device to obtain fertilizer.
NOVELTY - The method involves taking 50-70 parts of ether as solvent, and adding ether into 30-50 parts of biologic oils in a uniform speed. Rotary evaporation is performed to the ether soluble substance to obtain a solvent ether. 60-70 parts of methylene dichloride are taken as solvent and adding into 30-40 parts of ether insoluble substance in a uniform speed. Rotary evaporation is performed to the methylene dichloride soluble substance to obtain the methylene dichloride. Decompressing and filtering are performed to the obtained methylene dichloride insoluble substance.    USE - Poly-generation method for using double solvent to extract and separate biologic oil.    ADVANTAGE - The ether soluble substance is taken as the derivative of the biologic oil, so that the physicochemical properties are improved greatly. The method avoids the aging problem of the integral biologic oil. The method easily achieves the poly-generation application of the biologic oil.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of a poly-generation method.'(Drawing includes non-English language text)
NOVELTY - Producing biogas, involves cutting straw to 3-15 cm, steaming the cut straw, producing biogas by solid-state fermentation, and pressing the straw residue obtained by solid-state fermentation using mechanical extrusion method to obtain solid fuel for power generation.    USE - The method is useful for producing biogas.    ADVANTAGE - The method cost-effectively produces biogas at high stability. The alkali metal and chlorine ion in the fermentation slag is produced efficiently in comparison with straw material. The method improves combustion performance and calorific value.
NOVELTY - Concentrated sulfuric acid, fuming sulfuric acid or phosphoric acid is added to industrial sludge. The sludge mixture is mixed and aged, and water in sludge mixture is converted to free water. The treated sludge mixture is dewatered, and free water and industrial sludge are separated. The sludge mixture is then dried, and compound fertilizer is produced.    USE - Production of compound fertilizer.    ADVANTAGE - The compound fertilizer is economically produced without affecting the environment.
NOVELTY - The device has a material mixing bunker which is arranged within fermentation tank assembled with a biological filtering and deodorization device. A feeding hole is provided in upper portion of the tank. An agitator connected with a motor through transmission mechanism is provided at interior portion of bunker whose wall is provided with a discharge opening. A sand filtration tank is provided at bottom of tank, and is connected with the bunker by a filtering mesh.    USE - Device for composting home or hotel kitchen waste.    ADVANTAGE - The volume of the device is small and garbage treatment speed, cleanness and sanitary property of the device is improved. The device can be placed inside or outside of the room, thus the economical value of the device can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of the composting device.
NOVELTY - Method for producing marsh gas using steam exploded straw in microreactor, involves obtaining crop straw, forest waste and wood waste as raw materials, steam exploding the obtained raw materials in microreactor, fermenting raw material in anaerobic condition, again fermenting preprocessed straw and methanogen and/or Pseudomonas aeruginosa in an anaerobic fermentation tank at 40-50 degrees C for 7-14 days. The inoculation amount of methanogen to the fermentation tank is 10-20%.    USE - The method is useful for producing marsh gas using steam exploded straw in micro reactor.    ADVANTAGE - The method utilizes high amount of straw cellulose and hence produces large amount of gas without producing marsh waste.
NOVELTY - Method of preparing salidroside from Rhodiola crenulata, involves extracting R.crenulata, removing tannin by filtering the extract condensing the filtrate, adding the ZTC clarifying agent to the condensed liquid and centrifuging the mixture, adding the supernatant to macroporous adsorbent resin, detecting by thin layer chromatography (TLC), analyzing the fraction by silica gel column chromatography and again detecting the fraction by TLC and HPLC, crystallizing the fraction, and recrystallizing the coarse particle to obtain the product.    USE - The method is useful for preparing salidroside from R.crenulata.    ADVANTAGE - The salidroside can be produced simply with high purity. The macroporous adsorbent resin, silica gel column and organic phase used in the extraction process can be recycled and thus repeatedly used in industrial production.    DETAILED DESCRIPTION - Method of preparing salidroside from Rhodiola crenulata, involves (a) drying R.crenulata, extracting the dried material using hot water, where the ratio of material and water is 1:15-30, (b) removing the tannin by filtering the extract and then condensing the filtrate, (c) adding the proper ZTC clarifying agent to the condensed liquid and centrifuging the mixture, (d) adding the macroporous adsorbent resin to the liquid supernatant, eluting the supernatant using water and ethanol with different densities and detecting by thin layer chromatography (TLC), (e) adding R.crenulata fraction to silica gel column chromatography, eluting the fraction using diethyl ether and chloroform-methanol mixture and detecting the fractions using TLC and HPLC, (f) crystallizing the fraction, and (g) recrystallizing the condensed fractions by heating the coarse particle to dissolve and then cooling the particle to obtain product.
NOVELTY - The device has a feeder with a stirrer whose inlet and outlet are connected with an outlet of feeder and an inlet of a material guide pipe, respectively. A feed hole provided on an upper portion of an end face on one side of a barrel, and a purified water outlet is installed on upper portion of other end face of barrel in a gas-collecting chamber. A ball valve and a biogas outlet pipe of a fire arrestor are installed on the barrel. A biogas outlet pipe is connected with inlet of a gas distributing bag, and a delivery pipe.    USE - Device for producing biogas by degradation of excrement and organic garbage.    ADVANTAGE - A large amount of biogas can be produced efficiently by the respective device which can be used repeatedly, so as to enhance environmental protection.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for producing biogas by degradation of excrement and organic garbage.
NOVELTY - Immobilizing petroleum degrading bacteria with reed straw as carrier, involves separating and purifying petroleum degrading bacteria, preparing the bacterial suspension, and immobilizing the bacteria on reed straws.    USE - The method is useful for immobilizing petroleum degrading bacteria on reed straw for biotic purification in wetland areas polluted by petroleum.    ADVANTAGE - The method can be performed cost-effectively by a simple process, and the bacteria can be produced in large quantities.
NOVELTY - One-shot heat source is made in the form of solid body from wood, at least two edges of which are parallel to each other and form its end parts; at that, solid body on one of the edges has longitudinal saw cuts the depth of which represents larger part of its height; it is proposed to make saw cuts in two groups ; at that, in each group the saw cuts are located in parallel planes, and saw cuts of one group are located at an angle of 70-90 degrees to saw cuts of the other group. One-shot heat source can be equipped with ignition device from the row: wind matches, ignition fluid on the basis of paraffin, and dry fuel. Number of saw cuts can be 6 to 12. Distance between saw cuts can be 0.5-1.5 cm. Surface area of each of end faces can not be less than 250 cm2. For arrangement in the place of burnt out fragments of solid body the one-shot source can be equipped with additional fuel cells of the row: dry branches, chips, thinnings, coal. Solid body of one-shot heat source can be made in the form of log piece or beam piece mainly of rectangular section.    USE - Heating.    ADVANTAGE - Invention allows increasing ignition and combustion efficiency and usability, as well as enlarging application area of heat source owing to enlarging raw material base. 7 cl, 6 dwg
NOVELTY - A methane preparation system comprises high-pressure plunger pump (1), conveyer pipes (8), supercritical reactor (3), condenser (4), gas-liquid separator (5), and heater (9) installed in supercritical reactor.    USE - A methane preparation system.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of preparing methane from coal in the presence of supercritical water.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of methane preparation system.    High-pressure plunger pump (1)    Supercritical reactor (3)    Condenser (4)    Gas-liquid separator (5)    Conveyer pipes (8)    Heater (9)
NOVELTY - The metal mold for molding mixture of thermosetting resin and graphite, has lower mold (20) having edge upper surface (22) that is formed in circumference of lower mold upper surface (21) and set in a position lower than lower mold upper surface. A spring (60) joins outer frame (30) to lower mold edge upper surface. The outer frame upper surface (35) is set to a position higher than lower mold upper surface in a state in which the spring is extended, and is set to a position lower than or equal to lower mold upper surface in a state in which the spring is cringed.    USE - Three-unit type metal mold for manufacturing fuel cell separator (claimed).    ADVANTAGE - The hardening process can be simultaneously performed with respect to several separator raw materials, and several molded separator raw materials can be handled within single simple structured electric furnace. Hence the manufacturing cost of the fuel cell separator can be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing method of fuel cell separator.    DESCRIPTION OF DRAWING(S) - The drawings show the sectional views explaining the manufacturing process of fuel cell separator.(Drawing includes non-English language text)    Lower mold (20)    Lower mold upper surface (21)    Lower mold edge upper surface (22)    Outer frame (30)    Outer frame upper surface (35)    Spring (60)
NOVELTY - Biomass is injected from top portion or side upper portion of a vertical furnace. Hot air is blown from top portion or side upper portion of furnace, and biomass is carbonized. The exhaust gas (3) containing tar (5) is discharged from side middle portion of furnace. Portion(s) of tar is blown into furnace, and biomass charcoal is manufactured.    USE - Manufacture of biomass charcoal.    ADVANTAGE - The biomass charcoal having high quality is efficiently manufactured at high yield. The emission of carbon dioxide is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing apparatus of biomass charcoal, which has vertical furnace (10) for carbonizing biomass, insertion opening of biomass provided in top portion or side upper portion of furnace, a blowing inlet of hot air (4) provided in top or side upper portion of furnace, a discharge port of exhaust gas provided in side middle portion in downward position than blowing inlet, and partial combustion unit for burning portion(s) of exhaust gas with excess air ratio of less than 1.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of manufacturing apparatus of biomass charcoal.    Raw material (1)    Carbide material (2)    Exhaust gas (3)    Hot air (4)    Tar (5)    Carbonization furnace (10)    Filled layers (12)
NOVELTY - A portion of exhaust containing tar generated during carbonization discharged from the rotary kiln (10) is cooled. The biomass charcoal (3) discharged from the rotary kiln is contacted and a portion of the tar is adhered on the biomass charcoal.    USE - Manufacture of biomass charcoal.    ADVANTAGE - The biomass charcoal is manufactured efficiently and with improved yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing apparatus of the biomass charcoal, which consists of rotary kiln which carbonizes biomass, chiller which cools the gas discharged from the rotary kiln, gas flow path which supplies exhaust gas from the rotary kiln to the chiller (15), filling tank (12) of the biomass charcoal discharged from the rotary kiln, and gas flow path which supplies the exhaust gas from the chiller to the filling tank.    DESCRIPTION OF DRAWING(S) - The drawing shows the structure of the biomass charcoal manufacturing apparatus.    Raw material (1)    Biomass charcoal (3)    Rotary kiln (10)    Filling tank (12)    Chiller (15)
NOVELTY - A biomass (1) is utilized by pulverizing biomass and obtaining biomass ground material, pulverizing iron content containing material (2) and obtaining iron content containing-material ground material, mixing biomass ground material and iron content containing-material ground material and obtaining mixture, and dry-distilling mixture obtaining mixing dry distilled material which is mixture of biomass charcoal (9) and carbon deposition iron content containing material (10).    USE - Utilization of biomass for iron making.    ADVANTAGE - The method improves yield of biomass charcoal and modifies poor grade iron ore.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the utilization of biomass. (Drawing includes non-English language text).    Biomass (1)    Iron content containing material (2)    Mixing process (5)    Biomass charcoal (9)    Carbon deposition iron content containing material (10)
NOVELTY - A fluidized bed-type gasifier (1) is operated by maintaining temperature at less than or equal to 740 degrees C, gasifying raw material, and satisfying relationship between fluidization gas velocity and fluidization start rate at greater than or equal to 4. The fluidized bed-type gasifier consists of flow medium (3') which has particle having silicon dioxide as main component.    USE - Operating fluidized bed-type gasifier for gasifying industrial waste and organic waste e.g. biomass containing alkali metal.    ADVANTAGE - The method suppresses large drop of flow medium, prevents flow damage and efficiently enables gasification.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a fluidized bed-type gasifier.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the fluidized bed-type gasifier. (Drawing includes non-English language text).    Fluidized bed-type gasifier (1)    Free board (2)    Fluid bed (3)    Flow medium (3')    Wind box (4)    Partition plates (5)
NOVELTY - A natural carbohydrate-based composition comprises a combination of greater than or equal to 2 natural carbohydrate derivatives selected from cell wall polysaccharides such as pectin; polysaccharides such as dextrin; or exuded gums from plants such as gum tragacanth, xanthan gum, gum arabic, gum karaya or mastic gum.    USE - The natural carbohydrate-based composition is used for protection of crops against pathogenic organisms (claimed). The crops are families of solanaceae (e.g. pepper, potato, or tomato), musaceae (e.g. plantain/banana), rosaceae (e.g. rose), vitaceae (grape), cucurbitaceae (e.g. melon, watermelon, zucchini, or cucumber) plants, families of ornamental plants (e.g. carnation), fruits, leaves, grains, legumes, seeds, flowers, pastures, or roots. The pathogenic microorganism is Mycosphaerella fijiensis fungus. Test details are described but no results given.    ADVANTAGE - The composition is capable of activating the natural defense mechanisms of plants against pathogenic microorganisms, such that when a pathogenic microorganism appears, its action is neutralized by those preformed defenses. The composition is designed biorationally with the structure of natural phytoalexin-eliciting substances and is not biocidal, and offers a mechanism of action which is effective, environmentally friendly and safe for humans.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph of percentage area with plantain disease, Black Sigatoka, over time.
NOVELTY - Composition comprises corticosteroid and biopolymer provided in cream base. The cream base is preservative, primary and secondary emulsifier, waxy material, cosolvent, acid or water, preferably purified water. The biopolymer is chitosan.    USE - The composition is useful for treating skin inflammations and their related wound healing (claimed).    ADVANTAGE - The composition causes no side effects and is environmental-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the composition, which involves providing the above-cited ingredients and mixing the above-cited ingredients to form a homogeneous cream.
NOVELTY - A solid biomass material comprising minerals is converted to high quality bio-oil by pretreatment step and pyrolysis step. The pretreatment step comprises at least partially demineralizing solid biomass and/or improving accessibility of solid biomass by opening texture of particles of solid biomass.    USE - Method is used for converting solid biomass material comprising minerals to high quality bio-oil (claimed).    ADVANTAGE - The method obtains bio-oil in high yield, and enhances accessibility of biomass material.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic representation showing method for producing high quality bio-oil.    Soaking vessel (110)    Aqueous solvent (111)    Biomass particle (112)    Filter box (120)    Liquid phase. (121)
NOVELTY - Heating material or motor fuel comprises citric acid ester (I) or its derivative.    USE - The heating or motor fuel is useful for mobile and stationary combustion engines or heating systems with burners.    ADVANTAGE - The heating materials and motor fuels are: obtained from plants, bacteria, fungi or algae or predominantly based on vegetable raw materials; and cleaner than conventional heating materials and motor fuels so that no soot filtering is required.
NOVELTY - Fluorine contained in coal gasification wastewater (AA) is removed by coagulation-sedimentation (HH). Cyanogen in wastewater is decomposed by wet oxidation (FF) or pyrohydrolysis. Selenate is reduced using a metal reductant (GG), and chemical oxygen demand and/or ammonia in wastewater is removed. Processing of coal gasification wastewater is enabled (LL).    USE - Processing of coal gasification wastewater.    ADVANTAGE - The coal gasification wastewater is efficiently treated, and treated water with high quality is obtained and reused.    DESCRIPTION OF DRAWING(S) - The drawing shows the flowchart of processing of coal gasification wastewater. (Drawing includes non-English language text)    Coal gasification wastewater (AA)    Wet oxidation (FF)    Metal reductant (GG)    Coagulation sedimentation (HH)    Catalytic wet oxidation (II)    Processing of coal gasification wastewater (LL)    Oxidizing agent (QQ)    Selenic acid (RR)
NOVELTY - Biomass is carbonized to obtain biomass charcoal. Exhaust gas (3) containing tar (4) generated during carbonization is discharged. At least one portion of tar contained in exhaust gas is contacted with biomass and/or biomass charcoal, and converted into carbide (2).    USE - Manufacture of biomass charcoal.    ADVANTAGE - The biomass charcoal having high quality is efficiently manufactured at high yield. The emission of carbon dioxide is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing apparatus of biomass charcoal, which has vertical furnace (10) for carbonizing biomass, insertion opening of biomass provided in top portion or side upper portion of furnace, a discharge port of exhaust gas provided in top portion or side upper portion of furnace, a blowing inlet of hot air (5) provided in bottom portion of furnace, and partial combustion unit for burning portion(s) of exhaust gas with excess air ratio of less than 1.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of manufacturing apparatus of biomass charcoal.    Raw material (1)    Carbide material (2)    Exhaust gas (3)    Tar (4)    Hot air (5)    Carbonization furnace (10)    Hot blast inlet (11)    Filled layers (12)
NOVELTY - A gas diffusion electrode (26) has a catalyst layer formed on surface of a base material. The catalyst layer consists of metal chosen from zirconium, titanium, niobium, tantalum and their complex oxide.    USE - Gas diffusion electrode is used for fuel cell and brine electrolysis cell (both claimed).    ADVANTAGE - The gas diffusion electrode is economically manufactured. The catalyst layer is formed with excellent catalytic activity and durability, and large specific surface area.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of gas diffusion electrode, which involves forming metal oxide or metal complex oxide on surface of base material as catalyst layer by sol-gel process using a solution containing ion of zirconium, titanium, niobium and/or tantalum.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of fuel cell and brine electrolysis cell.    Ion exchange membrane (1)    Oxygen electrode (2)    Hydrogen electrode (3)    Frame-like gasket for oxygen electrode (4)    Gasket for hydrogen electrode (5)    Gas diffusion electrode (26)
NOVELTY - A waste sludge (A) is pulverized by a disintegrator (3), and the pulverized material and a waste oil absorber (W) are mixed, to obtain a waste oil-type solid fuel (O).    USE - Manufacture of waste oil-type solid fuel used for manufacturing cement (claimed).    ADVANTAGE - The method provides waste oil-type solid fuel having excellent fluidity and handling property.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for utilization of waste oil-type solid fuel, which involves providing waste oil-type solid fuel from kiln front portion of kiln, kiln bottom portion, and/or calcination furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of apparatus for manufacturing waste oil-type solid fuel.    Electrically-driven hoist (1)    Disintegrators (3,11)    Waste sludge (A)    Waste oil-type solid fuel (O)    Waste oil absorber (W)
NOVELTY - Crushing mixing of waste sludge (A) and adjustment waste oil (X) is carried out. The obtained mixture (Y) is mixed with waste oil absorber (W), and waste oil group solid fuel (O) is manufactured.    USE - Manufacture of waste oil group solid fuel used for manufacturing cement (claimed).    ADVANTAGE - The waste oil group solid fuel is manufactured by effectively using waste sludge.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for utilization of waste oil group solid fuel, which involves adding solid fuel to front portion of cement kiln, bottom portion of cement kiln and calcination furnace, and using solid fuel as fuel for manufacturing cement.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of manufacturing equipment of waste oil group solid fuel.    Disintegrator (2)    Waste sludge (A)    Waste oil group solid fuel (O)    Waste oil absorber (W)    Adjustment waste oil (X)    Mixture (Y)
NOVELTY - The gasifier has a heat exchanger main body (43) cooling gas from cyclone, and a gas pipe (42) whose upper end part is protruded from an upper end surface of the heat exchanger main body in upper direction. A puddle part (46) is formed between an upper end part outer peripheral surface of the gas pipe and an upper end surface of the heat exchanger main body. A piping (442) supplies water to the puddle part. A sprinkler nozzle (41) is provided in a heat exchanger (40). The heat exchanger is provided in a water-storage tank.    USE - Fuel gasifier for use in a woody biomass power generating plant.    ADVANTAGE - The puddle part is formed between the upper end part outer peripheral surface of the gas pipe and the upper end surface of the heat exchanger main body, thus easily supplying the water to the puddle part by piping even if another piping is blocked.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial sectional view of a puddle part of a heat exchanger.'(Drawing includes non-English language text)'    Heat exchanger (40)    Sprinkler nozzle (41)    Gas pipe (42)    Heat exchanger main body (43)    Puddle part (46)    Piping (442)
NOVELTY - Planting selenium-rich strawberry involves breeding strawberry before fruiting period by existing method, spraying selenium-rich liquid fertilizer onto leaf surface during fruiting period, and harvesting mature fruit. The liquid fertilizer comprises sodium selenite solution (200-500 mg/L) and monopotassium phosphate solution (100-250 mg/L) at weight ratio of 1:1.    USE - Method for planting selenium-rich strawberry (claimed).    ADVANTAGE - The method is simple and has low cost and low pollution on the environment. The produced strawberry is rich inorganic selenium and can supply 50-200 mg organic selenium for each person everyday by eating 0.5-1 kg strawberry.
NOVELTY - Waste drilling fluid soil remediation involves adding 1-2% of calcium aluminate salt into waste drilling fluid and rapidly putting drilling fluid into gel to form slurry granule of proper size. Water is removed from the slurry and 0.015-0.02% of calcium salt is added in the slurry. Organic pollutant is decomposed, heavy metal is removed, and biological oxygen demand (BOD) and chemical oxygen demand (COD) are reduced. Drilling fluid is stirred, and 0.5% of humic acid loess and 2-6% of wood meal, sawdust or hay are added in the fluid, where volume ratio of loess to drilling fluid is 1:1.    USE - Method for remediation of waste drilling fluid soil in loessial plateau region (claimed).    ADVANTAGE - The waste drilling fluid soil remediation method is simple and cost-effective, utilizes local natural loess resources without adding any medical agent and without damaging the original soil system.
NOVELTY - Composition comprises cyazofamid, propineb and auxiliary component. The mass ratio of cyazofamid to propineb is 1:80-1:50.    USE - The composition in the form of wet powder or granule is used for controlling diseases of fruit trees, fruits and vegetables caused by epiphytes (all claimed).    ADVANTAGE - The composition is inexpensive and environment-friendly and has synergistic effect.
NOVELTY - Substrate for organic cultivation, obtained by fermenting and composting waste sawdust and sludge from paper industry, and mixing the materials at volume ratio of 3:1-7:1.    USE - The substrate is useful for organic cultivation, and is useful in soilless cultivation of plants, preferably vegetables and flowers.    ADVANTAGE - The substrate has excellent physical and chemical properties, is rich in nutrients, does not cause environmental pollution, and is inexpensive.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing substrate, which involves (a) adding 1-2 kg of urea to every cubic meter of sieved waste sawdust from paper industry to increase nitrogen resource and regulate carbon-nitrogen ratio, adding superphosphate to the mixture to regulate pH to 6.5-7.5, and again adding 0.2-0.3 wt.% of strain to the mixture and regulating water content to 55-65 wt.%, mixing the mixture and composting the mixture, fermenting the mixture periodically, maintaining the mixture for 6-7 days, and airing the mixture and reducing the temperature of the mixture when the temperature is raised to 60 degrees C, (b) processing the sludge from paper industry until the water ratio of the sludge is 45-55 wt.%, carrying out aerobic composting by forced ventilation, and airing the processed sludge and grinding the processed sludge, and (c) mixing the obtained raw materials of waste sawdust in the step (a) and the obtained raw material of sludge in step (b).
NOVELTY - The method involves making uncured component to remain in a portion of gasket portion which contacts adjacent fuel cell in case of gasket molding of each fuel cell, so as to manufacture the fuel cell. The fuel cell which passed the electric power generation test performed at a temperature less than the temperature at which curing process of uncured component is started, is extracted. The extracted fuel cell is adhered with adjacent fuel cell and stacked where the vulcanized gasket portion adjoins by curing uncured component, and fuel cell module is manufactured.    USE - Manufacturing method of polymer electrolyte fuel cell for electric vehicle.    ADVANTAGE - The adherence of dissimilar material to the electrolytic membrane in each fuel cell can be prevented effectively. The quality of electric power generation performance can be confirmed before forming fuel cell module and the fuel cell which passed the performance test can be extracted, so that the fuel cell of electric power generation defect can be discovered earlier and the maintenance effort of extracting and exchanging the defective fuel cell out of the fuel cell stack can be eliminated. The fuel cell manufacturing efficiency can be improved by curing uncured component while performing electric power generation test.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart explaining the manufacturing process of fuel cell. (Drawing includes non-English language text)
NOVELTY - The furnace has a hearth (21) connected with multiple gas outlet holes (5) by a center hole of an annular water tank (15). A cavity is arranged between a fireproof layer (8) and an inner furnace barrel (20). A spiral partition board (11) is arranged on a spiral air pre-heating chamber (10). An upper edge of an ash bucket (13) is tightly contacted with an inner wall of a lower end of the inner furnace barrel. A lower end of the ash bucket is arranged in an ash chamber (14). The hearth is connected with the ash chamber by the ash bucket.    USE - Household up-draft tar-free biomass gasification direct-fired furnace.    ADVANTAGE - The generated gas can be burned directly via a gas stove for cooking, so as to eliminate gas output process. The tar in the gas is directly burned to solve difficulty to process the tar.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a household up-draft tar-free biomass gasification direct-fired furnace.    Gas outlet holes (5)    Fireproof layer (8)    Spiral air pre-heating chamber (10)    Spiral partition board (11)    Ash bucket (13)    Ash chamber (14)    Annular water tank (15)    Inner furnace barrel (20)    Hearth (21)
NOVELTY - The boiler has a grate arranged at a bottom part of a gasification chamber. A fuel igniting port is arranged on an upper side of the grate. Multiple heating pipes are arranged at an upper side of a combusting chamber and are communicated with a water sleeve. A top part of a boiler body is provided with a counter type fume discharging channel. A heat conducting plate is arranged between the combusting chamber and the counter type fume discharging channel. A top end part of the water sleeve is provided with a water outlet, and a bottom part is provided with a water inlet.    USE - Biomass counter gasification boiler for use in a restaurant and a hotel.    ADVANTAGE - The boiler is environment-friendly and saves energy. The boiler has simple structure, convenient usage, and high heating efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass counter gasification boiler.
NOVELTY - The boiler has a body provided with two fans, and a heated device and a heating device installed in an inner side of the body. The heated device is provided with a water sleeve whose inner wall is provided with a transverse tube and a vertical tube. Upper parts of the transverse tube and the vertical tube are welded with a heated plate i.e. water sleeve inner wall top plate. An internal side of the top plate is welded with a smoke discharging tube. An upper part of a combustive air filter storage cylinder is installed with an iron tube connected with a combustive air generator.    USE - Binocular integrated type hot-water central heating boiler.    ADVANTAGE - The boiler has simple design, rational structure, full combustion effect, better thermal energy utilization effect, high gas purity and better energy saving functions, shortened operation time, wide application range and better safety factor. The boiler is environment friendly and convenient to use.    DETAILED DESCRIPTION - The boiler is provided with combustive materials such as straws, leaves, coals, waste plastic, waste rubbers and waste cloth.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a binocular integrated type hot-water central heating boiler.
NOVELTY - A microorganism belonging to Marasmiellus candidus or Gymnopus dryophilus and having laccase activity and manganese peroxidase activity, is new.    USE - The microorganism is useful in processing agent for lignin decomposition of lignin-containing materials, e.g. mowed grass, rice straw, lawn grass (claimed), Camellia japonica, and bamboo grass.    ADVANTAGE - The lignin is biologically decomposed without using chemical preparation.
NOVELTY - Nucleophilic group-containing alkene compound (I) is contacted with an aluminosilicate to obtain a cyclic compound. The cyclic compound is oxetane group-containing compound (II), when the nucleophilic group is carboxyl group. The cyclic compound is heteroatom-containing compound (III), when the nucleophilic group is hydroxyl group, thiol group or amino group.    USE - Manufacture of cyclic compound e.g. lactone used as intermediate for bioactive substances e.g. pharmaceuticals, agrochemicals and fragrance.    ADVANTAGE - The method provides cyclic compound having high conversion ratio without affecting the environment.    DETAILED DESCRIPTION - Nucleophilic group-containing alkene compound of formula: H2C=C-(CH2)n-X (I) is contacted with an aluminosilicate to obtain a cyclic compound. The cyclic compound is oxetane group-containing compound of formula (II), when the nucleophilic group is carboxyl group. The cyclic compound is heteroatom-containing compound of formula (III), when the nucleophilic group is hydroxyl group, thiol group or amino group.    X=at least one of nucleophilic group chosen from carboxy, hydroxy, thiol and amino;    n=2-3;and    Y'=O, S or NH.
NOVELTY - A Sphingobium japonicum HZ-A1 with preservation number of CGMCC No.3539, is new.    USE - The Sphingobium japonicum HZ-A1 is useful in the decomposition of hexachlorocyclohexane soprocide (claimed).    ADVANTAGE - In utilizing the Sphingobium japonicum HZ-A1, the gamma-hexachlorocyclohexane of 20 mg/kg within the soil can be decomposed in 30 days; thus, the strain has excellent decomposing effect to the polluted soil; and it can repair the soil and water polluted by hexachlorocyclohexane soprocide.
NOVELTY - The feeding device has a feeding hopper (1), a processing cabin (2), and a shaftless screw conveyer (3). The processing cabin is provided with crushing cutters (4) inside. A central portion at a bottom of the processing cabin is provided with a rotary shaft (5) on which the crushing cutters are uniformly installed.    USE - Feeding device of e.g. vegetable leaves and straw in process of anaerobic fermentation.    ADVANTAGE - The shaftless screw conveyer transfer the processed material so as to realize the continuity of feeding material. The materials are mixed conveniently and uniformly in the crushing treatment on the material through the front end so as to crush the waste material into certain size. The device is convenient for conveying the input and output materials in the anaerobic fermentation process and outputs the biogas residue easily. The anaerobic fermentation process and gas generating rate is improved also the transfer efficiency is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the feeding device.    Feeding hopper (1)    Processing cabin (2)    Shaftless screw conveyer (3)    Crushing cutter (4)    Rotary shaft (5)
NOVELTY - The bio gas has a fermenting tank (1) whose one side is connected with a waste material tank (3) having connected with a water storing tank (10) on specific side. A gas storing tank (2) is located on a fermenting tank, whose middle portion on one side is provided with a feeding hole (5). The joint between the fermenting tank and the waste material tank is provided with a square door hole (11). The waste material tank is provided with a sealing plate (7) that is capable of lifting and lowering and whose central position is provided with multiple ventilation holes (4).    USE - Small-sized biogas tank.    ADVANTAGE - The 10-100 cubic meter of biogas tank can be built with simple structure at low cost, so the energy source can be saved.    DESCRIPTION OF DRAWING(S) - The drawing shows a structural view of the small-sized biogas tank.    Fermenting tank (1)    Gas storing tank (2)    Waste material tank (3)    Ventilation holes (4)    Feeding hole (5)    Sealing plate (7)    Storing tank (10)    Square door hole (11)
NOVELTY - The generator has feed pipe (2) that is connected to circular fermentation gas-forming chamber (1) whose lower portion at end opposite to feed pipe is connected with PVC made tubular discharge soft element (3). The height of cylinder is not less than height of fermentation gas-forming chamber. The tubular discharge soft element whose one side is tightly close to fermentation gas-forming chamber and other side is provided with movable baffle plate (6). The movable baffle plate, flash gate (4), and tubular discharge soft element forms movable trunk-shaped discharge chamber.    USE - Trunk-shaped discharge methane generator.    ADVANTAGE - The discharge chamber of the methane tank can be moved up and down like a trunk, so that difficulty in discharging and removing slag of the methane tank can be eliminated.    DESCRIPTION OF DRAWING(S) - The drawing shows a structural view of the trunk-shaped discharge methane generator.    Fermentation gas-forming chamber (1)    Feed pipe (2)    Tubular discharge soft element (3)    Flash gate (4)    Movable baffle plate (6)
NOVELTY - The drying machine has a drying box (1) which is connected with an outlet of an air heating tube (5) of a burning type heat exchanger (2) through a hot air conveying tube (12). A gas inlet of a gas burner (7) is connected with a straw gasifier (3) and a methane chamber (4) through three-way valve (8) and a gas conveying tube (13). The inlet of the air heating tube is connected with a solar preheater (6) through a preheated air conveying tube (14).    USE - Pasture drying machine.    ADVANTAGE - The pasture drying machine has a simple structure, utilizes agricultural waste material effectively, thus eliminates environment pollution and enhances drying effect. The cost of manufacturing the machine is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the pasture drying machine.    Drying box (1)    Burning type heat exchanger (2)    Straw gasifier (3)    Methane chamber (4)    Air heating tube (5)    Solar preheater (6)    Gas burner (7)    Three-way valve (8)    Hot air conveying tube (12)    Gas conveying tube (13)    Preheated air conveying tube (14)
NOVELTY - Insecticidal composition comprises clothianidin and phoxim as effective components, adjuvant and filler. The weight of ratio of clothianidin and phoxim is 1-50:1-80.    USE - The composition in the form of wettable powder, water dispersible granule, suspension, aqueous emulsion and microemulsion is useful for preventing and treating insect on rice, vegetable and cotton (all claimed).    ADVANTAGE - The composition has excellent synergistic effect and broad spectrum insecticidal effect, reduces the usage and residue of agrochemical on crop and environmental pollution, and is safe with respect to human and poultry. The drug-resistant insect cannot be produced easily.
NOVELTY - Method of composting by biologically dewatering livestock excrement, involves adding livestock excrement to fly larvae and fungicide obtained by biological fermentation for fermentation, and adding livestock excrement and fungicide obtained by biological fermentation in batches during fermentation, where the fermentation is carried out for 3-7 days at 22-42 degrees C, the weight of added fly larvae and livestock excrement are 0.5-5% and 14-33%, respectively of the total weight of the excrement after adding livestock excrement and fungicide obtained by biological fermentation in batches.    USE - The method is useful for composting livestock excrement (claimed) and producing high-quality feed protein.    ADVANTAGE - The initial moisture content of livestock excrement is reduced by the microbes, without using any auxiliary material. The processing cost of livestock excrement is reduced and the compost quality is improved. High-quality feed protein can be produced in large quantities. The organic waste can be recycled, hence environment can be protected.
NOVELTY - Nutrient composition comprises nano-selenium, organic fertilizer and microbial fertilizer in weight ratio of 2-8:1-3:0.1-0.4, where the concentration of selenium is 2000-13000 mg/kg.    USE - The nutrient composition is useful for enriching soil for growing pear trees.
NOVELTY - A new biomass gasification furnace has a material drum, a purifier, a pipeline and a burner, and carries out generation of gas from biomass, gas purification and automatic separation.    USE - New biomass gasification furnace is used for producing liquefied gas and natural gas used in hotels, restaurants, food stalls, breakfast stalls, night markets, factories and household works.    ADVANTAGE - The biomass gasification furnace has longer combustion time, and is simple, economical and environmental-friendly. The blackening of bottom surface of furnace by soot is prevented.
NOVELTY - Water is used as initial hydrogen source and hydrogen is continuously produced using green and continuable energy. The green and continuable energy is transformed into secondary energy for water decomposition. Water is decomposed into hydrogen and oxygen, and oxygen is collected as by-product. Hydrogen is transformed into ammonia and stored as liquid ammonia. Ammonia is liquefied and stored. Hydrogen is supplied by on-site ammonia decomposition to the client terminal.    USE - Clean and continuous production of hydrogen for automobile fuel cells.    ADVANTAGE - The method solves adverse effects of intensity variation of solar energy, wind energy, wave energy, and tide energy, which can be partially or completely stored as water level energy for continuously generating power.    DETAILED DESCRIPTION - Water is used as initial hydrogen source and hydrogen is continuously produced using green and continuable energy in an area enriched with water source and having easily available green and continuable energy. The green and continuable energy is transformed into secondary energy such as electricity and heat which can be used conveniently for water decomposition. Water is decomposed into hydrogen and oxygen, and oxygen is collected as by-product. A water pump is driven to raise the water level in a storage reservoir for use at night or other poor green and continuable energy via surplus power when the green and continuable energy is enriched. Hydrogen is transformed into ammonia and stored as liquid ammonia. All the energy consumed in ammonia synthesis is obtained from the green and continuable energy. Ammonia is liquefied and stored. Hydrogen is supplied by on-site ammonia decomposition to the client terminal, where ammonia can be decomposed by common thermal catalysis and plasma catalysis method.
NOVELTY - The hydrolyzing device has a circulated spraying filter reactor (a) comprising a top inlet (b) that is connected with an acid storage tank (11) and a water storage tank (10) through a pump (9). The top inlet is interconnected with a bottom outlet (c) of circulated spraying filter reactor through a heat exchanger (7) and a pressure valve (8). Another heat exchanger (5) is connected with bottom outlet of circulated spraying filter reactor.    USE - Hydrolyzing device for treating citric acid waste water discharged from citric acid factory.    ADVANTAGE - The citric acid waste water can be treatment easily and efficiently by simple technique.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing method of hydrolyzing device, which involves mixing the citric acid waste water and plant cellulose that comprises corn stalk, corn cob, sorghum stalk, wheat straw hood, saw dust, wood and rice husk.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the hydrolyzing device.    Heat exchangers (5,7)    Pressure valve (8)    Pump (9)    Water storage tank (10)    Acid storage tank (11)    Circulated spraying filter reactor (a)    Top inlet (b)    Bottom outlet (c)
NOVELTY - A tetrahydropyrrole, chloroacetic acid, and ethyl acetate/petroleum ether are mixed, stirred and warmed at room temperature, to obtain tetrahydropyrrole hydrochloride. The resultant solution is filtered, to obtain chloroacetyl pyrrolidine. The obtained chloroacetyl pyrrolidine is mixed with (E)-3,4,5-trimethoxy cinnamon acyl piperazidine, to obtain cinepazide. The obtained cinepazide is mixed with maleic acid and absolute ethyl alcohol and heated, to obtain white solid. The obtained white solid is dried and recrystallized, to obtain crystalline cinepazide maleate.    USE - Preparation of cinepazide maleate.    ADVANTAGE - The method simply provides cinepazide maleate with stable crystalline form and high melting point, and is environmental-friendly.    DETAILED DESCRIPTION - A tetrahydropyrrole is dripped in chloroacetic acid solution at -10 degrees C to 10 degrees C, stirred and warmed at room temperature. The warmed solution is mixed with mixed solution of ethyl acetate/petroleum ether in a weight ratio of 1:3, to obtain tetrahydropyrrole hydrochloride. The obtained tetrahydropyrrole hydrochloride is filtered and recycled, to obtain tetrahydropyrrole. The filtrate is distilled, dried and cured at room temperature, to obtain chloroacetyl pyrrolidine. The carboxyl group of (E)-3,4,5-trimethoxy cinnamic acid (raw material) is activated using activated agent in the presence of polar aprotic solvent and reacted with anhydrous piperazine, to obtain (E)-3,4,5-trimethoxy cinnamon acyl piperazidine. The obtained piperazidine is dissolved in solvent and alkali is added and reacted with chloroacetyl pyrrolidine, to obtain alkali free cinepazide. The resultant cinepazide is mixed with maleic acid and absolute ethyl alcohol solution, heated, uniformly-stirred at room temperature and white solid is separated out. The separated white solid is filtered, dried and recrystallized with ethyl alcohol-butanone, to obtain stable crystalline cinepazide maleate.
NOVELTY - The device has an improved anaerobic adjusting tank for pre-treating percolate, a recharge zone for treating the percolate, a mineralizing garbage reaction bed for adsorbing and degrading the percolate, and a high-grade oxidizing tank for making the percolate to generate chemical reaction. An artificial wetland is connected with the high-grade adsorbing settling tank for treating the percolate biologically, and an ecological landscape treatment tank is connected with the artificial wetland for treating the percolate.    USE - Biological percolate materialization device of household garbage landfill site.    DESCRIPTION OF DRAWING(S) - The drawing shows the block flow diagram of the biological percolate materialization device. (Drawing includes non-English language text)
NOVELTY - The garbage treatment device has a main belt conveyer that is connected between a hopper (4) and m-shaped rotary sorting machine (6). The lower portion of main belt conveyor is provided with a chained sieving conveyor belt (10). A winnowing machine (11) is arranged at one side of chained sieving conveyor belt. Sub belt conveyers (C-5,C-6) are arranged at another side of chained sieving conveyor belt. A sub conveying belt (5-3) protruded outside the housing is connected with a vibrating screen (14) that is installed on a frame.    USE - Garbage treatment device.    ADVANTAGE - The garbage can be treated easily and efficiently by simple technique while preventing the environment pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the garbage treatment device.    Hopper (4)    Sub conveying belt (5-3,C-5,C-6)    Rotary sorting machine (6)    Chained sieving conveyor belt (10)    Winnowing machine (11)
NOVELTY - The fermentation device has a feeding pool and a discharging pool which are located on a side of anaerobic fermentation pool. The upper end of feeding pool and discharging pool is higher than anaerobic fermentation pool. The top of anaerobic fermentation pool is sealed. A multilayer partition board or partition wall is installed in anaerobic fermentation pool to form a group or several groups of S type channels.    USE - Anaerobic fermentation device for use in sewage gas treatment plant.    ADVANTAGE - The anaerobic fermentation device can be designed with simple structure and convenient construction with reduced material consumption. The anaerobic fermentation is prolonged by using S type channels. The flowability of gas is promoted by S type channels such that gas yield is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of anaerobic fermentation device.
NOVELTY - A dredge pipe (1) is mounted at bottom of biogas production region. A three-phase separating region is provided with cylinder wall including overflow water outlet pipe (8) and spraying liquid reflow pipe (24). A sulfur separating region is provided with spraying liquid storage tank (22). A gas monitoring sampling pipe (13) and sulfur discharge pipe (23) are mounted outside cylinder wall. A desulfurization cylinder (20) of biogas desulfurization region is internally provided with biologic padding (15), spraying head (16) and gas chamber (17).    USE - Biogas production and desulfurization device.    ADVANTAGE - The hydrogen sulfide in gas phase can be removed and the hydrogen sulfide can be released.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biogas production and desulfurization device.    Dredge pipe (1)    Overflow water outlet pipe (8)    Gas monitoring sampling pipe (13)    Biologic padding (15)    Spraying head (16)    Gas chamber (17)    Desulfurization cylinder (20)    Spraying liquid storage tank (22)    Sulfur discharge pipe (23)    Spraying liquid reflow pipe (24)
NOVELTY - Composite microbial inoculum comprising natural microorganisms is used for treating cyclohexanone wastewater. Wastewater having chemical oxygen demand of 2000-3000 ml/L and containing alicyclic hydrocarbon is treated by degrading harmful substance contained in wastewater with microorganisms in multi-section oscillatory baffled reactor. Treatment is carried out at 15-40 degrees C, pH of 7 plus minus 1, dissolved oxygen content of 2-4 ml/L and hydraulic retention time of 30-40 hours. Treated water having chemical oxygen demand (CODcr) of less than 60 mg/L is obtained.    USE - Method for biochemically treating cyclohexanone wastewater.    ADVANTAGE - The cyclohexanone wastewater is efficiently treated. Thus, environmental pollution is prevented.    DETAILED DESCRIPTION - Composite microbial inoculum comprising natural microorganisms is used for treating cyclohexanone wastewater. Wastewater having chemical oxygen demand of 2000-3000 ml/L and containing alicyclic hydrocarbon is treated by degrading harmful substance contained in wastewater with microorganisms in multi-section oscillatory baffled reactor. Treatment is carried out at 15-40 degrees C, pH of 7 plus minus 1, dissolved oxygen content of 2-4 ml/L and hydraulic retention time of 30-40 hours. Treated water having chemical oxygen demand (CODcr) of less than 60 mg/L is obtained. Wastewater is treated using a wastewater collecting tank, a regulating tank, a homogenizing tank, a three-section oscillatory baffled reactor, a settling tank and a discharging tank. Each section of baffled reactor has a reaction region and a settling region.
NOVELTY - The invention relates to a process and an installation for obtaining biogas from municipal wastes. According to the invention, the process consists of methanogenic fermentation, while maintaining pH at values of 7.2-8.2, at a temperature of maximum 55-65 degrees C, for approximately 10 days, after the retention of the hydrogen sulphide and dioxide there resulting a biogas with methane concentration over 80%. The installation, as claimed, consists of a fermentation basin (4) wherefrom the biogas is discharged through a filter (6) filled with steel cuttings for retaining hydrogen sulphide and a filter (7) filled with Raschig rings and system for washing the biogas for carbon dioxide retention, a tank (8) for storing the resulting purified biogas and enriched with methane.
NOVELTY - Process of using pyrolysis water, comprises injecting pyrolysis water into a combustion chamber.    USE - The process is useful for using pyrolysis water in: an integrated-gasification-combined-cycle plant that works with or without co-production of liquid fuels; a biomass-to-liquids plant; or a coal-to-liquids plant (claimed).    ADVANTAGE - The process utilizes pyrolysis water, which reduces the: nitrogen oxide emissions of the combustion chamber by more than 20%, preferably more than 70%; and risk of an explosion in a gasifier.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a system for using pyrolysis water, comprising a combustion chamber with separate means configured for injection of pyrolysis water and/or for injection of mixtures of pyrolysis water with additional water.
NOVELTY - A method for biomethanation of lipid rich feed, is disclosed. The method involves the steps of treatment of lipid rich feed by physical, chemical and/or enzymatic methods, and further, hydrolyzing the lipid rich feed by adding lipolytic enzymes or microbial population capable of producing required lipolytic enzymes, in a first reactor. Thereafter, acidogenesis of hydrolyzed lipid rich feed is carried out by adding enriched microbial consortia in an acidogenic reactor, and simultaneously, heating the acidogenic reactor and stirring the lipid rich feed. Thereafter, the lipid rich feed is treated with methanogenic microorganisms in the methanogenic reactor, and simultaneously, heating the methanogenic reactor and stirring occasionally the lipid rich feed. The biomethanation of lipid rich feed is conducted under anaerobic conditions and is monitored for acid accumulation and production of methane rich gas.
NOVELTY - Generating a combustible bio-fuel comprises mixing up together two solutions. The first solution is a distilled carbonic liquid made from warming charcoal and purified water. The second solution is a distilled carbonic oil liquid made from warming charcoal, purified water, and palm-oil.    USE - Method for generating a combustible bio-fuel (claimed).    ADVANTAGE - The method provides non-polluting conversion of wood to renewable oil.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a method for reducing the carbon dioxide in the environment by using bio-fuel made from a distillation process comprising all-natural ingredients; and    (2) a method for reducing fuel pollutants by adding a combustible fuel made from charcoal, water, and palm-oil to regular gasoline or diesel fuel.
NOVELTY - Increasing (M1) transesterification conversion of oils which uses oils and additives as raw materials, involves heating the oils and additives, injecting the oils and the additives into a high gravity field, performing a transesterification reaction, inducing a phase separation, and post-treating effluent to obtain biodiesel, preferably highly converted oils, in which the transesterification reaction is carried out under the high gravity field.    USE - For increasing transesterification conversion of oils; for biodiesel converted from edible oil (claimed).    ADVANTAGE - The method improves the transesterification conversion of oils and obtains higher transesterification conversion; provides less reaction time.
NOVELTY - A silicon carbide hydrogen separation film is manufactured by forming layer which consists of precursor of ceramic on porous support body, dissolving formed precursor layer, making dissolved precursor layer permeate in pore, making diameter of pore small, and converting precursor in pore into silicon carbide.    USE - Manufacture of silicon carbide hydrogen separation film used for selectively permeating hydrogen used in fuel cell.    ADVANTAGE - The hydrogen can selectively control more pore diameters in small diameter which can be permeated.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of preparation method of silicon carbide film. (Drawing includes non-English language text).    Formation of precursor layer (101)    Dissolution of precursor layer (102)    Crosslinking and insolubilizing of precursor layer (103)    Baking of precursor layer (104)
NOVELTY - A system for generating hydrogen and oxygen gases from water used as an electrolyte by means of passing electricity from a source through the electrolyte, the system including an electrolyzer (10), a means for controlling the electricity supplied to the system from the source, a reservoir for storing one or more of the gases produced from the electrolyzer and a means for pressurizing the reservoir.    USE - The system and electrolyzer are useful for generating hydrogen and oxygen gases from water (claimed).    ADVANTAGE - The system is highly efficient in generating hydrogen and oxygen gases.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is an electrolyzer, for producing hydrogen and oxygen from water, the electrolyzer including a chamber for holding water, a water supply valve for maintaining water in the chamber at a pre-determined level and a cathode and anode, each in the form of a generally helical coil arranged such that there is a generally constant gap between the anode and the cathode, the two coils being held in place by plastics material formed around the outside of the coils.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an electrolyzer.    Electrolyzer (10)    Anode (12)    Cathode (14)    Plastic tube (16)    Chamber (18)    Fill level (20)    Water inlet (22)    Float valve (24)    Gas outlet (26)
NOVELTY - Fuel contains water-insoluble fatty acid material obtained by water-insolubilizing fatty acid contained in crude glycerin or fatty-acid mixtures which are produced as by-products in the process for producing biofuel from animals and plant-derived fats and oils.    USE - Fuel.    ADVANTAGE - The fuel has excellent performance and high combustion heat.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of fuel.
NOVELTY - A source gas supply device (5) is provided in the source gas supply path (21) to supply gas to modifier (1). The supply path is opened/closed by valve (41). The water is supplied to evaporator (2) by water supplier (6). The modifier is communicated with the atmosphere by communication path which is opened/closed by valve (42). The operation of gas supply device and water supplier is stopped by controller (10) to close the valves. The valve (42) is opened before opening the valve (41) when the supply of the gas from the gas supply device to the modifier is resumed.    USE - Hydrogen generating apparatus of fuel cell system (claimed).    ADVANTAGE - The obstruction of the source gas supply path is reduced, by controlling the operation of gas supply device and water supplier to close the valves such that one valve is opened before opening the other valve when the supply of the gas from the gas supply device to the modifier is resumed.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) fuel cell system;    (2) operating method of hydrogen generating apparatus; and    (3) operating method of fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the hydrogen generating apparatus. (Drawing includes non-English language text)    Modifier (1)    Evaporator (2)    Source gas supply device (5)    Water supplier (6)    Controller (10)    Source gas supply path (21)    Valves (41,42)
NOVELTY - A hydrogen generating apparatus (1) has a modifier for reforming and reacting raw material and water vapor, to generate hydrogen-containing gas. The hydrogen-containing gas emitted from a fuel cell (5) and the combustion air supplied by a combustion air supply portion (10) are burnt by combustor. The hydrogen-containing gas path of hydrogen generating apparatus is sealed by sealing valve (13). The sealing valve is opened and closed to perform pressure relief of hydrogen generating apparatus, when electric power generation of fuel cell is stopped.    USE - Fuel cell electric power generation system.    ADVANTAGE - The increase in the supply rate of the combustion air at the time of pressure relief of the hydrogen generating apparatus can be reduced effectively. The start-stop driving of the fuel cell electric power generation system can be performed efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the fuel cell electric power generation system. (Drawing includes non-English language text)    Hydrogen generation apparatus (1)    Fuel cell (5)    Combustion air supply portion (10)    Sealing valve (13)    Fuel cell electric power generation system (100)
NOVELTY - A microorganism comprises bacteria which has lipolysis ability and grows by 10 degrees C and at pH 10.    USE - Microorganism for lipolysis process composition and for processing fat and oil containing wastewater (claimed).    ADVANTAGE - The microorganism decomposes stably and efficiently fat and oil containing wastewater in low temperature and high pH.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) lipolysis process composition; and    (2) processing of fat and oil containing waste water.
NOVELTY - Deodorizing apparatus comprises unit for supplying carbon dioxide, unit for supplying ammonia, unit for supplying water, packed column for contacting carbon dioxide, ammonia and water, and filler of packed column containing stainless steel.    USE - The apparatus is useful for deodorizing (claimed) livestock excrements.
NOVELTY - A composite of metal hydride has metal hydrides (A,B). The metal hydride (B) is formed by pulverizing metal hydride (A). The metal hydride (A) generates hydrogen gas by chemical reaction with water. In cross-sectional view of metal hydride composite, the metal hydrides (A,B) are in mixed state.    USE - Composite of metal hydride is used as hydrogen source of fuel cell.    ADVANTAGE - The composite of metal hydride is manufactured in high yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of composite of metal hydride.    DESCRIPTION OF DRAWING(S) - The drawing shows the cross-sectional view of composite of metal hydride.    Metal hydrides (A,B)
NOVELTY - The gasifier has a scrubber edge part of water channel (532A) and a water channel edge part in scrubber (50) with a width (B) of the horizontal direction orthogonal to the center (532Aa) direction of water channel which are made the same. The water channel through which circulating water of scrubber flows into a drain pipe (53) is formed in a connection part (532). The drain pipe discharges the water in the scrubber to the water-storage tank and is connected to the scrubber side through the connection part.    USE - Gasifier e.g. woody biomass power generating plant for gasifying fuel.    ADVANTAGE - Flow of water becomes favorable since the water channel width in a connection part is the same as the scrubber side and since soot retained in connection part vicinity is eliminated. Discharges soot smoothly to a water-storage tank since the soot in a scrubber can be guided to the drain pipe side. Structure of scrubber is made compact since the structure of the drain pipe side part of a connection part is made small.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional end elevation view of the scrubber.    Scrubber (50)    Drain pipe (53)    Connection part (532)    Water channel (532A)    Center (532Aa)    Width (B)
NOVELTY - A feed pipe (52) arranged in one side of a water-storage tank (60) supplies water from the water-storage tank to a scrubber. A drain pipe (53) arranged in another side of the water-storage tank discharges the water from the scrubber to the water-storage tank. The partition plates (63,64) are standingly arranged between the feed pipe and the drain pipe.    USE - Gasifier for woody biomass power generating plant.    ADVANTAGE - The soot and tar flowing into the feed pipe can be prevented by using the partition plates, and hence the soot returning to the scrubber is prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of the water-storage tank.    Feed pipe (52)    Drain pipe (53)    Water-storage tank (60)    Partition plates (63,64)
NOVELTY - The apparatus (10) has seal groove (64a) that is lapped to the outer side of anode side-electric power feeding portion (40) at anode side separator (34) to position sealing element (62a). The seal groove (68a) is lapped to the outer side of cathode side-electric power feeding portion (42) at cathode side separator (36) to position sealing element (66a). The seal grooves are set at mutually different positions on both sides of the solid polymer electrolytic membrane (38) with respect to lamination direction of separator.    USE - Water electrolysis apparatus for polymer electrolyte fuel cell.    ADVANTAGE - The seal grooves are set at mutually different positions on both sides of solid polymer electrolytic membrane with respect to lamination direction of separator such that the electrolytic membrane is maintained reliably by the sealing elements and the retention capacity of the electrolytic membrane is improved. Hence the damage of the electrolytic membrane is prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross sectional view of unit cell.    Water electrolysis apparatus (10)    Anode side separator (34)    Cathode side separator (36)    Solid polymer electrolytic membrane (38)    Anode side-electric power feeding portion (40)    Cathode side-electric power feeding portion (42)    Sealing elements (62a,66a)    Seal grooves (64a,68a)
NOVELTY - A unit cell (12) clamps electrolytic membrane and electrode structure (32) with anode side and cathode side separators (34,36). The anode side separator includes flow path (54) into which water is supplied and the cathode side separator includes flow path (58) in which water is electrolyzed to obtain high-pressure hydrogen. A pressure release chamber (72) connected to seal groove (68a), releases hydrogen outside through pressure relief channel (70) while sealing element (66a) is inserted into seal groove rotating at outer side of flow path (58).    USE - Water electrolysis apparatus for manufacturing hydrogen gas for polymer electrolyte fuel cell for generating direct current electrical energy.    ADVANTAGE - The hydrogen gas leaking from sealing element can be discharged outside favorably by pressure release chamber through pressure relief channel and desired thrust can be provided stably to electrolytic membrane. The electrolytic voltage raise can be suppressed and desired electrolysis capability can be ensured over a long period of time.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the unit cell.    Unit cell (12)    Electrolytic membrane and electrode structure (32)    Anode side separator (34)    Cathode side separator (36)    Flow paths (54,58)    Sealing element (66a)    Seal groove (68a)    Pressure relief channel (70)    Pressure release chamber (72)
NOVELTY - The gas chromatograph detector (30) has a decomposing pipe (31a) that is heated by a cracking unit (31b) so that oxygen compound inside the decomposing pipe is converted into carbon monoxide that is introduced into a catalyst pipe. The catalyst pipe is heated by a catalyst furnace so that carbon monoxide is converted into methane. A decomposing pipe is filled with particle (34) made of platinum compound.    USE - Gas chromatograph detector for detecting oxygen compound e.g. alcohol and ester.    ADVANTAGE - Since the particle filled inside the decomposing pipe made of platinum compound, the cost is reduced by eliminating the use of decomposing pipe made of platinum palladium alloy.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the gas chromatograph detector. (Drawing includes non-English language text)    Capillary column (5)    Gas chromatograph detector (30)    Decomposing pipe unit (31a)    Cracking unit (31b)    Particle (34)
NOVELTY - A biomass granulating system comprises a crusher (3) for crushing biomass, blower (6) for extracting the crushed biomass, cyclone (8) for separating gas and solids, granulator (11) for granulating separated materials, temperature sensor in a shaping cavity, and variable frequency motor (15) for driving biomass granulator and can be automatically adjusted via monitored temperature signal.    USE - A biomass granulating system.    ADVANTAGE - The system extends biomass granule shaping time thus increasing shaping density, and overcomes the slag falling problem of the current granulator.    DETAILED DESCRIPTION - A biomass granulating system comprises a crusher (3) for crushing biomass, blower (6) for extracting the crushed biomass, cyclone (8) for separating gas and solids, granulator (11) for granulating separated materials, temperature sensor in a shaping cavity, variable frequency motor (15) for driving biomass granulator and can be automatically adjusted via monitored temperature signal, a straight hole or tapered straight compound through hole (11) placed on flat-die of granulator, and additive hopper set in the crusher and used for adding coal powder or diatomite into the biomass of the crusher.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a biomass granulating system.    Crusher (3)    Blower (6)    Cyclone (8)    Granulator (11)    Variable frequency motor (15)
NOVELTY - A medicament feed device (D1) comprises air cushion whose top is connected with fixing plate, supporting rods and medicament kettle in turns, where the sidewall or bottom wall of medicament kettle is provided with valves and top wall is equipped with liquid inlet, and rope is connected with air cushion or supporting rods.    USE - Medicament feed device (D1) for restoring urban river.    ADVANTAGE - The device (D1) has simple structure, low cost and convenient use; and is portable and convenient to install.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating a medicament feed device.
NOVELTY - Method of producing dry organic material, involves drying organic raw material containing water by fermentation using microorganism to obtain dry granular powder, where the microorganism is chosen from edible mushrooms, yeast, Aspergillus and Bacillus subtilis natto.    USE - The method is useful for producing dry organic material including organic waste of food industries and domestic waste.    ADVANTAGE - The method is simple, rapid and cost-effective as large quantities of organic materials can be dried without using petroleum energy within 20 days.
NOVELTY - Raw material oil is subjected to transesterification reaction with lower-alkyl alcohol in presence of catalyst, to obtain fatty acid alkyl ester. The transesterification reaction is performed in homogeneous phase system by adding solvent chosen from acetone and/or isopropanol to the reaction system.    USE - Manufacture of fatty acid alkyl ester used for biodiesel fuel.    ADVANTAGE - The fatty acid alkyl ester is manufactured rapidly and efficiently in high yield by economical method.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for system for manufacturing fatty-acid alkyl ester. The system has fatty-acid alkyl ester production unit for carrying out transesterification reaction between raw material oil and lower-alkyl alcohol in presence of catalyst in homogeneous phase system to which organic solvent is added and producing fatty-acid alkyl ester, and stationary separation unit in which stationary separation of glycerin phase and fatty-acid alkyl ester phase containing lower-alkyl alcohol, fatty-acid alkyl ester and organic solvent is carried out.
NOVELTY - A biogas generating device (D1) comprises soft biogas generating device, where outer side of lower part of the device (D1) is combined with woven outer protecting layer produced by silk substance, wire substance and/or fiber substance mixed with powder solid substance (such as concrete). The powder solid substance can be reacted with corresponding liquid substance (such as water) in order to harden outer protecting layer. The inner side of lower part of device (D1) is combined with woven inner protecting layer produced by silk substance, wire substance and/or fiber substance.    USE - Biogas generating device (D1) including biogas pond, toilet, hogpen, or sunshine brooder.    ADVANTAGE - The device (D1) can be produced in batches in matching, standard, scale, factory or automation manner; and has low cost, small volume, convenient storage and conveying, short construction period, simple construction, standard matching, economy and durability.
NOVELTY - Separating lactic acid from fermentation liquor comprises adding fermentation liquor into ammonia aqueous solution or sodium hydroxide to alkalinize and heat; adding flocculating agent and blending to produce flocculate; standing and settling to layer; and separating solid and liquid; transferring liquid phase into the next membrane separation purification technique for lactic acid; and returning solid phase to the fermenting tank to join the fermentation of organic wastes to produce lactic acid and enhance the output of lactic acid.    USE - Method for separating lactic acid from fermentation liquor (claimed).    ADVANTAGE - The method is simple; has high flocculating rate, easy separation of solid and liquid, low cost, and nearly no loss of the target product lactic acid; achieves comprehensive utilization; and reduces the pretreatment cost of the fermentation liquid.
NOVELTY - Manufacture of methanol and dimethyl ether from gas containing hydrogen and carbon monoxide involves using catalyst formed by coating surface of solid particulates containing chromium and zinc with zeolite ZSM-5 film formed by hydrothermal synthesis.    USE - Manufacture of dimethyl ether used as light oil, and methanol used as raw material of formaldehyde and acetic acid.    ADVANTAGE - The methanol and dimethyl ether are selectively and economically manufactured in high yield.
NOVELTY - Treating pig farm excrement sewage comprises: subjecting the pig farm excrement sewage in an excrement sewage rich-thin separating device and separating the sewage into rich sewage and the thin sewage and subjecting it into a rich sewage anaerobic digestion system, a thin sewage treatment system and a biogas liquid use system.    USE - The method is useful for treating pig farm excrement sewage.
NOVELTY - A trifluoroiodomethane-containing mixed refrigerating agent comprises (wt.%) trifluoroiodomethane which can inhibit combustion and explosion (1-10); 1,1,1,2-tetrafluoroethane and/or 1,1,2,2-tetrafluoroethane (20-40); and propane and/or propylene (50-75).    USE - A trifluoroiodomethane-containing mixed refrigerating agent.    ADVANTAGE - The product has zero ozone-depleting potential value, and global warming potential value that is less than the conventional hydrofluorocarbons working medium. The intersolubility of product with lubricating oil is good. The R22 work medium can be directly substituted, and the refrigerating system does not need to be changed. Because the refrigerating agent comprises combustion-inhibiting component, the combustibility of refrigerating agent is greatly reduced or the refrigerating agent will not be completely combusted, and the safety of refrigerating system is greatly improved.
NOVELTY - Method of using oil shale ash comprises grinding oil shale ash and adding in alkali processor together with alkali liquor at mass ratio of 1:1-1:5, mixing and melting at 70-95 degrees C for 1-3 hours, filtering, adding distilled water into residue, filtering to pH less than 9, drying and uniformly mixing with solid alkali substance at mass ratio of 1:1-1:3; and firing and activating at 650-750 degrees C for 1 hour, sequentially washing with dilute acid, washing with deionized water, drying, grinding, cooling and screening to obtain decolorizer.    USE - Method of using oil shale ash for producing decolorizer of oil including gasoline, kerosene, diesel, biodiesel, vegetable oil and waste oil (claimed).    ADVANTAGE - The decolorizer is easy to control, and has simple pre-processing and preparation, high decoloring efficiency which is up to 90%, and extensive raw material resources, which can provide deep processing and utilization of waste, thus reducing preparation cost and fully utilizing oil shale ash.
NOVELTY - Oil microorganism purificant for restaurant and home comprises the following components according to weight percentages: 5-10% of Alcaligenes eutrophus, 5-10% of Bacillus cereus, 2-5% of Butyrivibrio fibrisolvens, 2-5% of filamentous fungi, 5-10% of Bacillus coagulans, 5-10% of Bacillus subtilis, 5-10% of methanogen and remaining humic acid.    USE - The oil microorganism purificant is useful for restaurant and home (claimed) for reducing biochemical oxygen demand of watering and output of solid sludge, and reducing organic waste of oil.
NOVELTY - The production method involves locating water filling passage (13) at upper part of gas chamber. The micro-drive motor is connected with external power supply, and drives circulating pump to rotate through connecting device, when armature passage (5) is filled with liquid conductor and is sealed. The liquid conductor moves circumferentially so as to cut the magnetic line, then closed loop is formed, and two electrodes (8) and strong electrolyte water solution (10) are used for electrolyzing.    USE - Production method of hydrogen.    ADVANTAGE - Saves energy when producing hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of the production method of hydrogen.    Permanent magnet (4)    Armature passage (5)    Electrodes (8)    Strong electrolyte water solution (10)    Water filling passage (13)
NOVELTY - The apparatus has a fermentor (1) provided with a pull-fermentation container (7) and connected with a co-generation unit (4). Casters (11) and gripping hook (8) are arranged on bottom of the pull-fermentation container. A cooling circuit is connected with an engine, where the engine is powered by biogas. A circulating system is installed in an upper part of the fermentor.    USE - Anaerobic biomass processing apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of an anaerobic biomass processing apparatus.    Fermentor (1)    Co-generation unit (4)    Pull-fermentation container (7)    Gripping hook (8)    Caster (11)
NOVELTY - Electric power is produced using methane gas as fuel, and carbon dioxide produced by electric power generation is adsorbed to heated seawater. The resulting water is injected into submarine hydrate stratum (H), and isolation fixing of carbon dioxide is carried out. The heat is transmitted to methane hydrate, and methane gas produced by dissociation of methane hydrate is recovered. The recovered gas is supplied to electric power generation facility, and low carbon dioxide discharge electric power generation is enabled.    USE - Low carbon dioxide discharge electric power generation method.    ADVANTAGE - The discharge of carbon dioxide in atmosphere is effectively suppressed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for low carbon dioxide discharge electric power generation system.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of electric power generation system.    Offshore plant (1)    Hot-water transport pipe (2)    Methane gas recovery pipe (3)    Submarine cable (5)    Submarine hydrate stratum (H)    Mining point (P)    Sea bottom (S)
NOVELTY - A steam reforming catalyst contains metallic element supported by a carrier containing complex oxide containing ceria and alumina dispersed in nanometer scale. The metallic element is chosen from element of groups 8-10.    USE - Steam reforming catalyst is used for modifying oxygen-containing hydrocarbon e.g. ethanol (both claimed) used for generating hydrogen used as fuel for internal combustion engine of motor vehicle.    ADVANTAGE - The catalyst efficiently modifies oxygen-containing hydrocarbon to produce hydrogen without generation of caulking.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) steam reforming method, which involves contacting oxygen-containing hydrocarbon with the catalyst in presence of water vapor; and    (2) steam reforming reaction apparatus.
NOVELTY - A hybrid hydrogen refuelling station comprises on-site type hydrogen refuelling station which manufactures and supplies hydrogen, and off-site type hydrogen refuelling station which stores and supplies conveyed hydrogen by carrying out steam reforming of liquefied neutral gas (LNG) or liquefied petroleum gas (LPG).    USE - A hybrid hydrogen refuelling station.    ADVANTAGE - The hybrid hydrogen refuelling station can effectively process carbon dioxide gases emitted in natural gas modification plant processed using cooling-heat of liquid hydrogen generated in liquid hydrogen plant.    DETAILED DESCRIPTION - A hybrid hydrogen refuelling station comprises on-site type hydrogen refuelling station which manufactures and supplies hydrogen, off-site type hydrogen refuelling station which stores and supplies conveyed hydrogen by carrying out steam reforming of LNG or LPG, carbon dioxide gas compression line which guides carbon dioxide gas produced in gas reforming device to heat exchanger, and gas reforming device which carries out steam reforming. The cooling-heat is produced within heat exchanger (33) with latent heat and/or sensible heat of hydrogen. The carbon dioxide gas guided to heat exchanger is liquefied by cooling in high pressure state more than triple point.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of hybrid hydrogen refuelling station. (Drawing includes non-English language text).    Modifier (11)    Gas-compression machine (13)    Accumulator (15)    Second gas-compression machine (17)    Second accumulator (19)
NOVELTY - Method for composting sludge involves dehydrating sludge using an electro-endosmosis dehydrator which carries out direct dissociation of intracellular organic substance, and fermenting the dehydrated sludge forming compost by using a fermenter with an insertion opening on the upper part, exhaust port of dehydrated sludge, lower air supply part and top air supply part.    USE - Method for composting sludge from a sewage works and farm village colony waste-watertreatment station.    ADVANTAGE - Manufactures good quality compost, has reduced energy consumption and forms aerobic atmosphere while reducing moisture of sludge and maintaining fermentation heat cycle.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the apparatus used in composting sludge.    Tank (1)    Insertion opening (11)    Top air supply part (12)    Exhaust port (13)    Composting apparatus main body (100)
NOVELTY - Biogas is subjected to gas separation process by performing pressure-fluctuation separation method. Then, methane contained in biogas is concentrated and concentrated methane is extracted from adsorption tower, stored in product tank (13) and supplied to use destination from tank. The pressure-fluctuation separation method involves performing adsorption process during which the pressure of adsorption towers (A,B) filled with adsorption agent is increased, and regeneration process during which pressure of tower is reduced.    USE - Method of concentrating methane in biogas obtained by carrying out anaerobic fermentation of livestock excrement, sewage material and foodstuff waste material.    ADVANTAGE - The methane in biogas is concentrated and recovered efficiently with reduced electric power consumption.    DETAILED DESCRIPTION - Biogas is subjected to gas separation process by performing pressure-fluctuation separation method. Then, methane contained in biogas is concentrated and concentrated methane is extracted from adsorption tower, stored in product tank and supplied to use destination from tank. The pressure-fluctuation separation method involves performing adsorption process during which the pressure of adsorption towers filled with adsorption agent is increased, and regeneration process during which pressure of tower is reduced. The maximum pressure is calculated by measuring pressure of adsorption tower or product tank. The content of biogas which is introduced into adsorption tower is adjusted based on calculated maximum pressure.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of pressure-fluctuation adsorption separation apparatus.    Compressor (11)    Cooler (12)    Product tank (13)    Inverter (26)    Adsorption towers (A,B)
NOVELTY - A fuel mixture contains glycerin and activated clay, and has pH of 6-8. Glycerin is obtained as byproduct during manufacture of biodiesel fuel, which is produced by transesterification of fats and oils in homogeneous system in presence of alkali catalyst.    USE - Mixture is used as raw material for fuel (claimed).    ADVANTAGE - The mixture is efficiently and economically produced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for usage of mixture as raw material of fuel.
NOVELTY - The stove has a dust outlet and a fan, where a cooking range is provided on an upper part of a hearth and is integrated with a stove body. A self-heating cracking combustion cooking range, a sealed boiler cradle and a top part of the hearth are provided with a gas-releasing pipe and releasing valves. The gas pipe and the releasing valves are connected to a chimney. An upper side of the stove body is provided with a feeding opening. A bottom part of the hearth is provided with a manual rotary dust-expelling blanking and an air intake device.    USE - Direct-fired self-heating biomass gasification stove for a socialist countryside construction.    ADVANTAGE - The stove avoids blocking of pipes and burners by condensation deposition, thus raising heating efficiency, removing pungent smell, avoiding pollution to indoor air, avoiding flameout, ensuring normal combustion fire generation, avoiding gas leakage, expelling dust, providing easy blanking, and hence saving energy and reducing emission.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross sectional view of a direct-fired self-heating biomass gasification stove.
NOVELTY - The gasifier has an air inlet pipe (6) whose end penetrates through a side wall of an external drum (10) above a hearth neck (22), a thermal insulation layer (15), a fire-resisting layer (14), a gas cracking chamber (17) and a side wall of an internal drum to communicate with a hearth. Another end of the air inlet pipe is arranged inside and threaded to a plug-up (7) outside the external drum. An end of an air outlet pipe (8) penetrates through the side wall of the external drum, the thermal insulation layer and the fire-resistant layer to communicate with the gas cracking chamber.    USE - Downdraft gasifier for biomass.    ADVANTAGE - The gasifier can realize cracking of tar in gas in a high temperature zone to greatly reduce the content of tar in the gas and satisfy the gas need for rural residents.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a downdraft gasifier.    Air inlet pipe (6)    Plug-up (7)    Air outlet pipe (8)    External drum (10)    Fire-resisting layer (14)    Thermal insulation layer (15)    Gas cracking chamber (17)    Hearth neck (22)
NOVELTY - The device has a burning chamber fixed on a base of an inner chamber of a shell. Two sliding tracks are fixed in the shell. An upper part of the sliding tracks is connected with a storing and holding box. An upper part of the storing and holding box is fixedly connected with a support net. An end part of the storing and holding box is provided with hooks. Top end of the shell is provided with an oil outlet and an air outlet. The sliding tracks are connected with the storing and holding box by a pulley.    USE - Waste rubber oil making device.    ADVANTAGE - The device is simple and convenient to operate, and can efficiently improve production efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial sectional view of a waste rubber oil making device.
NOVELTY - The furnace has water tanks, where rings of tanks surround the furnace. A water inlet is arranged on a lower part of the water tanks. A water outlet is arranged at a higher part of the water tanks, where the furnace is provided with a 220V alternating current (AC) or 12V direct current (DC) dual purpose speed regulation fan and an air inlet i.e. slope type air inlet.    USE - Straw gasification furnace.    ADVANTAGE - The oil tar generated by the furnace flows to the oil tar waste water backflow port due to gravity and mixes with the ashes to form oil tar waste ash mixture. The oil tar can be split and converted to combustive gas, so as to improve the yield and quality of the combustive gas. The furnace can be used as heater, so as to lower temperature on the external surface of the furnace body and prevent people from being hurt. The furnace improves combustion efficiency and heat utilization rate, completely processes oil tar, prolongs combustion time and widens the flue selecting range. The furnace has automatic blanking function and simple structure, so that the furnace can be used continuously.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a straw gasification furnace.
NOVELTY - Method for processing waste gas, involves decomposing organic halogen compound contained in waste gas by contacting microorganisms layer supported by carrier in the waste gas, dispersing the liquid which moistens the microorganisms layer by dispersion unit, collecting the liquid dispersed by the microorganisms layer in a tank, collecting the liquid containing decomposed microorganisms in the tank by collection material, and circulating the liquid containing decomposed microorganisms through dispersion unit.    USE - The method is useful for processing waste gas.    ADVANTAGE - The method is cost-effective. Increase of pressure loss is prevented. The decrease of contact area of waste gas and carrier can be prevented. The exhaust-gas treatment can be performed efficiently and stably for a long period of time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus for processing the waste gas.
NOVELTY - Coated granular fertilizer is obtained by forming at least one layer of film consisting of semi-drying oil derived from vegetable oil containing highly water absorbent substance of particle size 1-200 mu m and urethane resin, on exterior of granular fertilizer.    USE - Coated granular fertilizer.    ADVANTAGE - The coated granular fertilizer has increased initial elution rate, high biological oxygen demand and is environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of the above-cited coated granular fertilizer, which involves preparing coating material using prepolymer containing terminal isocyanate groups and semi-drying oil, and coating the granular fertilizer using prepared coating material.
NOVELTY - The device has fermentation pot, primary and secondary gas storing pots, and air compressor that form closed loop. The fermentation pot is provided with pot main portion, side wall gas bag with inlet valve, gas discharging valve, water inlet valve and water discharging valve. The fermentation pot has bottom portion gas bag with gas inlet valve, water inlet valve, water discharging valve. The fermentation pot has pot main portion gas inlet valve, feeding opening, discharging opening and temperature-control system.    USE - Device for enhancing solid fermentation such as anaerobic solid fermentation and aerobic solid fermentation for generating marsh gas (all claimed), ethanol and butanol.    ADVANTAGE - The mass transfer and heat transfer of solid fermentation can be performed easily so that the reaction is uniform and fermentation efficiency is increased. The fermentation cycle is reduced and fermenting strength and raw material conversion rate are increased.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for enhancing solid fermentation.
NOVELTY - The stove has an outer stove (5) that is covered on an inner stove (1). The location adjacent to the bottom of the inner stove is provided with the multiple rows of ventilating openings (4) that penetrate the stove wall. The location adjacent to the bottom of the outer stove is provided with the single row of lighting openings (6) that penetrate the stove wall. The upper end of the stove is connected with the outer side through the smoke channel (2) whose lower end is provided with an air door (3).    USE - Fast carbonizing stove for burning agricultural and forest waste.    ADVANTAGE - The biomass molded carbon is manufactured using the agricultural and forest waste. The forest, soil and fossil fuel are protected, while preventing the loss of soil and water. The dependence on the natural gas and petroleum is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of the fast carbonizing stove.    Inner stove (1)    Smoke channel (2)    Air door (3)    Ventilating openings (4)    Outer stove (5)    Lighting openings (6)
NOVELTY - Agent comprises waste ardealite, zinc sulfate, copper sulfate, humic acid and potassium sulfate in the weight ratio of 1000:2.5-10:1-4:1-12:5-20.    USE - The agent is useful as fertilizer for increasing yield of tomato (claimed).    ADVANTAGE - The method enables recycling of ardealite pollutant obtained as waste product of phosphorus chemical. The agent improves soil fertility. The agent promotes the growth of tomato, and improves the quality of tomato.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the agent, which involves crushing dried waste ardealite, zinc sulfate, copper sulfate, humic acid and potassium sulfate into power having particle size of 200-400 meshes, and mixing the components to obtain the product.
NOVELTY - The effluent water obtained by separating and shunting the electroplating wastewater is made to contact the ozone, to degrade macromolecular organic matter. The effluent water is made to flow through a composite material so that organic matter and heavy metal ion are adsorbed by material physically. The adsorbed organic matter is degraded by microorganism and adsorbed metal ion is diffused into material to perform ionic exchange with material, to break the adsorption equilibrium and to proceed physical adsorption. The effluent water is treated by a reverse osmosis unit for reusing.    USE - Electroplating wastewater treatment method.    ADVANTAGE - The service life of the sorbing material is prolonged and the trouble of changing the sorbing material frequently is avoided.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for electroplating wastewater treatment apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the electroplating wastewater treatment apparatus. (Drawing includes non-English language text)
NOVELTY - Method for composting municipal sludge, involves mixing (in wt.%) sludge with 75-85% of moisture content (70-90), straw (5-15) and pulverized coal ash (5-15), uniformly mixing the artificial manure (10-30) and the obtained mixture, transferring the resultant mixture into composite pile, decanting at 60 degrees C for 2-4 days or more, preferably 3-5 days at 50-60 degrees C, more preferably less than 50 degrees C, controlling total composting time for 20-25 days, and discharging the material when the composite pile is cooled at room temperature.    USE - The method is useful for composting municipal sludge, where the composed sludge is used as fertilizer.    ADVANTAGE - The large sludge dosage can be effectively produced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for compositing bin, which comprises temperature sensor, temperature controller, time controller and forced ventilation fan. The temperature sensor is connected with the temperature controller which is connected with the forced ventilation fan connected with the time controller.
NOVELTY - A transition metal modified MCM-41 molecular sieve is obtained by hydrothermal synthesis. Titanium dioxide is added on surface of molecular sieve and catalyst is produced. The catalyst is provided on catalyzing bed, and bed is fixed in a photocatalytic reactor. Mixed air and marsh gas are filled to the reactor under irradiation of visible light, and photocatalytic oxidation of hydrogen sulfide in mixed gas is performed. Hydrogen sulfide is deposited on bed through the catalyst, and purified gas is discharged.    USE - Removal of hydrogen sulfide contained in marsh gas.    ADVANTAGE - Hydrogen sulfide contained in marsh gas is economically and easily removed without pollution.
NOVELTY - Method of producing biological organic fertilizer, involves installing production device near livestock farm, concentrating the excrements of livestock on spot, adding the concentrated excrements of livestock into the device, stirring the excrements of livestock with biological bacteria in the device for fermenting, and discharging the fermented excrements to obtain the product.    USE - The method is useful for producing biological organic fertilizer from excrements of livestock (claimed).    ADVANTAGE - The method prevents pollution as the fertilizer is produced near livestock farms. The method reduces the labor power and material resources.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for device for producing biological organic fertilizer from excrements of livestock, which comprises horizontal machine enclosing cavity for holding excrements of livestock and biological bacteria. The device has feed port installed at front end and discharging port installed at the back end, a spiral conveying device for conveying the excrement of livestock and biological bacteria from the feed port to the discharging port, where the outer wall of groove has vent for discharging smell and heat and the lower part of the groove has air intake system. The spiral conveying device has driving device installed on the external part of the cavity, shaft and spiral blade fastened on the shaft.
NOVELTY - Method for processing waste and effluent, involves supplying effluent and waste to single phase anaerobic digestion tank, then fermenting the obtained mixture, dividing solid material which is not soluble in the single phase anaerobic digestion tank, transferring solid material to hydrolysis/acid formation reactor for performing hydrolysis and acid formation, reprocessing a transferred solid material, transferring a solution generated through a reprocessing, fermenting the solution, and collecting methane produced through anaerobic fermentation.    USE - The method is useful for processing waste and effluent for generating methane.    ADVANTAGE - The method has reduced processing costs, and provides high yield of methane.
NOVELTY - The invention relates to a process for producing an alternative fuel for installations meant to make cement clinker in rotary kilns. According to the invention, the process consists in mixing some flammable wastes with sawdust, in a ratio of 0.2 : 1...0.5 : 1, for 0.5-2 h.
NOVELTY - The invention relates to a process and a plant for obtaining a fuel. According to the invention, the process consists in separating a fluid mixture containing paraffin hydrocarbons from the existing fuel gases, liquefying and storing the same while discharging the water. The claimed plant comprises a branched suction device (1) for the suction of the fluid mixture, a suction pipe (2) placed on the sea bottom or at the ground level, a centrifugal pump (3) having several stages, depending on the type of mixture, a delivery pipe (4) meant to increase the water flow to a hydraulic turbine (5) which drives an electric generator (6) for the supply of the plant services and the change of physical parameters of the fluid mixture, a conditioning basin (7) for the separation of fuel gases through a crank discharge pipe (8) which also provides the hydraulic turbine water flow, a spill pipe (9) for the separation of purified water discharged through a pipe (10) from the separated gases led through a pipe (11) into a buffer storage tank (12) wherefrom gases are led through a pipe (13) to a liquefaction zone (14) and, further on, through the pipe (15), to some storage tanks (16).
NOVELTY - The invention relates to a process and to an installation for the dissociation of water into hydrogen and oxygen. The claimed process consists in the dissociation of water into hydrogen and oxygen by electrolysis in electric pulsatory field, by applying between the anode and the cathode a potential difference of 10...100 kV in pulses with a frequency of 109 Hz of electron orbital resonance. The claimed installation comprises an externally insulated cylindrical vessel (1) which plays the role of an anode, being made of stainless steel, a cathode (2) provided with a central orifice, located in the centre of the vessel (1), a cover (15), a system for supplying water into the vessel (1) provided with a tap (8), some connectors (9 and 10) for supplying with high voltage, a high voltage transformer (14) in pulsed mode with a frequency of 109 Hz, two vessels (12) for collecting the hydrogen and the oxygen, a compression pump (13) for the liquefaction of hydrogen and oxygen and a pump (11) for vacuuming the collecting vessels (12).
NOVELTY - Biomethanation is a microbial conversion of a substrate, including a complex substrate like coal, to biomethane. Biomethanation is accelerated in coal which has a favorable environment for microbial growth. Design and construction of coal bioreactor accelerate coal biomethanation process in all types of coal including coal which lacks a favorable environment for microbial growth. Thus, energy is extracted from targeted coal in form of biomethane. Image 1/1
NOVELTY - A fuel cell system (1) has a liquid feeding unit (4) for feeding liquid hydrocarbon fuel, a liquid feeding unit (9) for feeding water, a vaporizer (7) for vaporizing fuel and water, a modifier (12) for producing reformed gas using vaporized material, fuel cell stack (13) operated using reformed gas, a spraying unit (6) for spraying fuel in vaporizer, and a spraying unit (11) for spraying water in vaporizer.    USE - Fuel cell system.    ADVANTAGE - The fuel cell system has improved electric power generation efficiency, and is compact.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of fuel cell system.    Fuel cell system (1)    Liquid feeding units (4,9)    Spraying units (6,11)    Vaporizer (7)    Modifier (12)    Fuel cell stack (13)
NOVELTY - The domestic biomass gasification furnace comprises a lower gas discharging pipe (11) provided above a furnace bridge (5), and an upper gas discharging pipe (8) provided above a furnace body (3). An upper absorption gas discharging pipe (18) is connected between two valves, in such manner that one end of upper absorption gas discharging pipe is connected in a purifier (14), and the other end thereof is directed towards a gas discharging chimney. The purifier is connected with a gas-cooker (16) by a fuel gas conveying pipe (15).    USE - Domestic biomass gasification furnace for burning large material.    ADVANTAGE - Can effectively filter moisture content of tar and easily burn any large material.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of the Domestic biomass gasification furnace.    Furnace body (3)    Furnace bridge (5)    Upper gas discharging pipe (8)    Lower gas discharging pipe (11)    Purifier (14)    Fuel gas conveying pipe (15)    Gas-cooker (16)    Upper absorption gas discharging pipe (18)
NOVELTY - Device for gasifying organic materials, such as plastics, substitute fuels and biomass, comprises a heating zone (5), a reformer zone (6) and a thermolysis zone (7) arranged in a common gasifier housing (3). Transition zones (10) and chicanes (11) are arranged between the individual zones so that a free space (12) impinged with a barrier gas is formed in the heat carrier medium. The individual zones are separated from each other by the total play of the heat carrier medium with the barrier gas.    USE - Device for gasifying organic materials, such as plastics, substitute fuels and biomass.    ADVANTAGE - The yield of synthesis gas and usable gas is increased.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for gasifying organic materials, such as plastics, substitute fuels and biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device.    Gasifier housing (3)    Heating zone (5)    Reformer zone (6)    Thermolysis zone (7)    Transition zones (10)    Chicanes (11)    Free space (12)
NOVELTY - A micro hollow structure body comprises radiation property gas as raw material, spherical form micro cavities which are mutually connected in succession between inlet for transmitting gas and discharge port, and structure inner wall part which forms micro cavity and carries catalyst substance on surface. The nonequilibrium state of gas molecule by which excitation of generated gas from source gas is suppressed while excitation heating of source gas is carried out by electromagnetic waves of specified wavelength near absorption band is formed in micro cavity.    USE - Micro hollow structure body for hydrogen generating apparatus, thermal decomposition of water vapor and high temperature steam electrolysis (claimed).    ADVANTAGE - The micro hollow structure body efficiently generates hydrogen.    DETAILED DESCRIPTION - A micro hollow structure body comprises radiation property gas as raw material, spherical form micro cavities which are mutually connected in succession between inlet for transmitting gas and discharge port, and structure inner wall part which forms micro cavity and carries catalyst substance on surface. The nonequilibrium state of gas molecule by which excitation of generated gas from source gas is suppressed while excitation heating of source gas is carried out by electromagnetic waves of specified wavelength near absorption band is formed in micro cavity when internal diameter from which electromagnetic wave absorption band and coinciding cavity resonance wavelength are obtained. INDEPENDENT CLAIMS are included for:    (1) hydrogen generating apparatus;    (2) steam reforming process;    (3) thermal decomposition of water vapor;    (4) high-temperature-steam electrolysis process; and    (5) preparation of structure containing micro cavity.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph of the relationship between resonance spectrum in micro cavity and absorption band of source gas.
NOVELTY - Aqueous composition comprises: (a) a suspended pesticide, which is soluble in water at 20 degrees C for a maximum of 10 g/l; (b) a salt; and (c) a protective colloid, which is a polysaccharide substituted with 3-32C-alkylcarbonyl- and/or 3-32C-alkylcarbamoyl groups.    USE - The composition is useful for combating phytopathogenic fungi and/or undesired plant growth and/or undesired insect- or mite infestation on plants and/or for regulating the growth of plants (all claimed).    ADVANTAGE - The aqueous composition does not crystallize and sediment during the prolonged storage. The particle size of the aqueous composition is not increased during the storage period. The composition is stabilized with an environmentally friendly surface-active compound, so that the composition avoids the damaging of the plants during application.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) preparing the aqueous composition, comprising contacting the suspended pesticide, the salt and the protective colloid to obtain the composition;    (2) use of the salt for slowing down the particle growth in the aqueous composition;    (3) use of the composition for combating phytopathogenic fungi and/or undesired plant growth and/or undesired insect- or mite infestation on plants and/or for regulating the growth of plants, where the composition is allowed to act on the respective pests, their habitat or the plants to be protected before the respective pest, the soil and/or on the undesired plant and/or the cultivated plants and/or their habitat, or treating the seeds of the cultivated plants with the composition; and    (4) seeds comprising the composition.
NOVELTY - Separating at least one acid gas from gas mixture comprises contacting the gas mixture with a porous metal-organic framework, where the framework adsorbs the acid gas and contains at least one bidentate organic compound coordinatively bonded to at least one metal ion, and the framework is impregnated with an amine suitable for gas scrubbing.    USE - The process is useful for separating at least one acid gas from gas mixture, where the acid gas is gases comprising carbon dioxide, sulfur oxide, nitrogen oxide or hydrogen sulfide (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the porous metal-organic framework.
NOVELTY - Reversibly absorbing and releasing hydrogen comprises releasing hydrogen at 120-350 degrees C, converting piperidine to pyridine under the action of a hydrogen-storing alloy, and releasing hydrogen; and absorbing hydrogen at 95-115 degrees C, inputting hydrogen to pyridine, and reacting pyridine and hydrogen under the action of hydrogen-storing alloy.    USE - Method for reversibly absorbing and releasing hydrogen (claimed) used for a fuel battery.    ADVANTAGE - The method uses piperidine as the hydrogen-storing medium, and the piperidine provides the higher hydrogen-storing amount than the hydrogen-storing alloy. The hydrogen generated by decomposing piperidine does not contain carbon monoxide and can be directly applied to the fuel battery. The hydrogen is not required to be purified like the hydrogen obtained by modifying methanol. The method is simple and convenient.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for reversibly absorbing and releasing hydrogen.
NOVELTY - A system employs carbon dioxide and methane contained in air by adding snow to indoor unit, air conditioning with refrigeration, and applying pressure to snow.    USE - System is used for employing carbon dioxide in chamber interior of tent, dome outdoor system and structure of indoor system (claimed).    ADVANTAGE - The system prevents global warming.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of air conditioned system. (Drawing includes non-English language text)
NOVELTY - A volatile organic compound adsorbent comprises carbonized material obtained by carrying out carbonization and activation of wooden residue containing lignin originating in manufacturing process of bioethanol which used wood type biomass as raw material or its molded material.    USE - A volatile organic compound adsorbent.    ADVANTAGE - The adsorbent adsorbs volatile organic compound effectively, and can be manufactured inexpensively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a manufacturing method of volatile organic compound adsorbent.
NOVELTY - A portable electric power feeding system comprises hydrogen-producing unit (1), fuel cell (3), fuel flow control apparatus (2) and storage battery (4). The hydrogen-producing unit consists of a case (20) in which reaction liquid and metal are reacted, to generate hydrogen. The generated hydrogen and oxygen are reacted in the fuel cell, to generate electricity. The fuel flow control apparatus is provided between hydrogen-producing unit and fuel cell, and controls the electric charge generated in fuel cell. The storage battery stores the electricity generated in fuel cell.    USE - Portable electric power feeding system is used for charging electrical equipment.    ADVANTAGE - The electrical equipment is charged using the system without outlet socket.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of portable electric power feeding system.    Hydrogen-producing unit (1)    Fuel flow control apparatus (2)    Fuel cell (3)    Storage battery (4)    Case (20)
NOVELTY - Agricultural product (1) comprises: an agricultural liquid composition (11); and a casing (10) containing the liquid composition, where the casing is constituted of a water-insoluble oxo-biodegradable polymeric material.    USE - Used as agricultural product.    ADVANTAGE - The product: is eco friendly; does not generate toxic residues. The liquid composition in (I) is viscous whose viscosity is high enough to avoid the risk of being washed away by rain (once released).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the agricultural product comprising a substantially agricultural liquid composition (11) and the casing, where the casing is constituted of a non polymeric material and substantially spherical form, comprising: supplying two films of similar material polymer; preparing the substantially liquid composition; laying films in an encapsulating unit comprising two molding drums, each comprises a cylinder in which many hemispherical cavities are formed, where the drums are arranged so that their axes are parallel and cylinders are adjacent, and the films are continuously rolling in encapsulation unit tangentially on the cylinders; transforming films into parts of capsule to form substantially hemispherical capsule by counterrotary movement of the cylinders of molding drums and simultaneously introducing the composition for agricultural use in the parts of capsule; and closing the capsule to form the casing filled with the agriculture composition, where films of water-insoluble and oxo-biodegradable polymer material is provided and the films are heated at 90-140 degrees C, prior to providing films on cylinders of drums.    DESCRIPTION OF DRAWING(S) - The figure shows a sectional view of an agricultural product.    Agricultural product (1)    Casing (10)    Agricultural liquid composition. (11)
NOVELTY - Reducing pollution of potato starch processing wastewater and recycling organic matter comprises: (a) infusing ozone into the potato starch processing wastewater and adjusting pH value to 6-9; and (b) biochemically processing: (i) activating strain; (ii) culturing seed solution; and (iii) adding into the wastewater processed by ozone according to 5-10% of inoculum size, and shaking and culturing for 28-56 hours at 28 degrees C.    USE - The process is useful for reducing pollution of potato starch processing wastewater and recycling organic matter (claimed).    ADVANTAGE - The process has simple technique and low cost.    DETAILED DESCRIPTION - Reducing pollution of potato starch processing wastewater and recycling organic matter comprises: (a) infusing ozone into the potato starch processing wastewater; where the ozone infusion amount is 0.20-5.00 g/hour; the wastewater temperature is 0-30 degrees C; and the infusion time is 60-180 minutes; adjusting pH value to 6-9; and (b) biochemically processing: (i) activating strain: selecting the strain that is Geotrichum candidum, taking potato culture medium as solid culture medium; (ii) culturing seed solution: culturing the shake-bottle seed culture medium comprising 10 g of glucose, 5 g of ammonium sulfate, 1 g of magnesium sulfate, 5 g of potassium dihydrogen phosphate, 2 g of yeast paste, and 1000 ml of deionized water, where the pH value is 6; inoculating the Geotrichum candidum with activated slant into the shake-bottle seed culture solution, and shaking and culturing for 24 hours at 28 degrees C in speed of 150 rotations/minute; and (iii) adding into the wastewater processed by ozone according to 5-10% of inoculum size, and shaking and culturing for 28-56 hours at 28 degrees C.
NOVELTY - A three-stage biomethanation process for conversion of protein rich feed into a combustible mixture of methane and carbon dioxide (biogas), is disclosed. The overall retention time for biomethanation is reduced by pre-treatment of protein rich feed, which is by physical, chemical and/or enzymatic methods. The process brings about faster conversion of protein rich biomass into biogas in three stages namely hydrolysis, acidogenesis and methanogenesis. The pre-treatment step fastens the hydrolysis process which substantially reduces the hydraulic retention time and increases the cost effectiveness of the plant. The biogas generated has applications as kitchen fuel and electrical power generation or transportation fuel from renewable biomass, in a cost effective manner. Image 0/0
NOVELTY - The apparatus (1) has a stirring apparatus (20) arranged to stir the liquid in a reaction tank (10), and a viewing window (40) arranged to view the reaction taking place in the reaction tank. A tempered glass is oriented towards the exterior from the outer side of the reaction tank, to block through-hole formed in reaction tank. A reaction liquid holding portion is contacted with the inner side of tempered glass. A reaction liquid flow through-hole which is formed in the reaction tank in vertical direction, and connected with the reaction liquid holding portion.    USE - Apparatus for manufacturing bio-diesel fuel.    ADVANTAGE - The isolation condition of the bio-diesel fuel and glycerin can be confirmed easily, and the methanol solvent which is not used for the reaction can be collected effectively by simple process.    DETAILED DESCRIPTION - The diameter of the lower portion of the reaction liquid through-hole is larger than the upper portion of the reaction liquid through-hole. A methanol recirculation apparatus (30) has a switching valve that is arranged to determine whether liquefied methanol is thrown into the reaction tank or methanol collection tank (110).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the bio-diesel fuel manufacturing apparatus.    Bio-diesel fuel manufacturing apparatus (1)    Reaction tank (10)    Stirring apparatus (20)    Methanol recirculation apparatus (30)    Viewing window (40)    Methanol collection tank (110)
NOVELTY - The method for generation of methane by anaerobic digestion of organic substrate, production of hydrogen gas steam and methane reforming process are disclosed. Image 0/0
NOVELTY - Treating a biodiesel (1) stream containing impurities comprises: cooling the biodiesel stream to a temperature of 40-80 degrees F, to produce a cooled biodiesel (2) stream; storing the cooled biodiesel stream for 2.5-5 hours, to produce a retained biodiesel stream; and passing the retained biodiesel stream through an ion exchange resin to produce a treated biodiesel (5) stream, where the treated biodiesel stream meets the specification of the cold soak filtration test method (American society for testing and materials (ASTM) D6751-08).    USE - The method is useful for treating a biodiesel stream.    ADVANTAGE - The method is cost effective.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic presentation of a system for treating biodiesel.    Biodiesel (1)    Cooled biodiesel (2)    Chilled biodiesel (3)    Filtered biodiesel (4)    Treated biodiesel (5)
NOVELTY - Integrated production and utilization of synthesis gas for production of mixed alcohols, hydrocarbon recovery and gasoline/diesel refinery comprises: forming hydrocarbon fuel; gasifying hydrocarbon fuel to form synthesis gas; synthesizing mixed alcohols from carbon monoxide and hydrogen; directing remaining hydrogen and sufficient oxygen to a downhole gas combustion unit; combusting the remaining hydrogen with the oxygen via downhole gas combustion unit; and adding water to combustion, to produce high-pressure steam for the recovery of crude oil from the hydrocarbon bearing formation.    USE - The method is useful for integrated production and utilization of synthesis gas which is useful for production of mixed alcohols, hydrocarbon recovery and gasoline/diesel refinery, where the mixed alcohols produced includes 1-8C alcohols and there is a greater amount of methanol than ethanol (all claimed).    ADVANTAGE - The method produces optimal high octane gasoline that is ready for sale and utilization, with optimal efficiency and limited waste and/or environmental impact.    DETAILED DESCRIPTION - Integrated production and utilization of synthesis gas for production of mixed alcohols, hydrocarbon recovery and gasoline/diesel refinery comprises: forming a hydrocarbon fuel comprising coal and/or gas oil; gasifying the hydrocarbon fuel to form synthesis gas comprising hydrogen and carbon monoxide; synthesizing mixed alcohols from carbon monoxide and stoichiometric amount of hydrogen; directing remaining hydrogen to a downhole gas combustion unit positioned underground within a hydrocarbon bearing formation; directing sufficient oxygen to the downhole gas combustion unit for combustion with the hydrogen; combusting the remaining hydrogen with the oxygen via the downhole gas combustion unit; and adding water to the combustion, to produce high-pressure steam for the recovery of crude oil from the hydrocarbon bearing formation.
NOVELTY - A liquid compost making automated system comprises carousel mounted for rotation above fluid collection mechanism and including screen, a mechanism for conveying organic material to region above carousel, a mechanism for depositing organic material on carousel, a mechanism for directing liquid on screen to form suspension having some of organic material and liquid where suspension can flow through screen and into collection mechanism, and a mechanism for forcing spent organic material off screen and into discharge mechanism for removing spent organic material from carousel.    USE - A liquid compost making automated system.    ADVANTAGE - The system can be automatically cleaned, and is cheap.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of automated manufacture of liquid compost.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic elevational view of a vessel.    Extraction/brewing unit (2)    Hopper (5)    Elevating conveyor (7)    Conduit (15)    Sensor (41)
NOVELTY - The method involves press forming the material plate made of stainless steel, so that the material plate has a cross section having a concavo-convex shape. The convex of the concavo-convex shape of the material plate is plated with a conductive metal and the current is supplied between a plating solution holding element which contact only the convex, and the material plate. The plating is performed in condition that hydrogen is generated on surface of material plate, and reduction of passivation film is simultaneously performed together with plating.    USE - Fuel cell separator production method.    ADVANTAGE - Since the solution holding element contacts only the convex, the plating can be selectively performed on the convex. So that deposition of noble metal to an unnecessary portion other than the convex can be inhibited even when a defect exists on the passivation film due to the press forming, and so etching can be omitted. Since the plating is performed in the condition that hydrogen is generated on the surface of the material plate, the reduction and removal of the passivation film can be simultaneously performed together with the plating. so that mechanical polishing can be omitted. Therefore processes can be shorter and production cost can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating process of producing fuel cell separator.
NOVELTY - Organosulfur compound contained in natural gas is hydrogenated and converted into hydrogen sulfide by primary conversion process (1a). Hydrogenation is further carried out at temperature different from primary conversion process, and unconverted organosulfur compound is converted to hydrogen sulfide by secondary conversion process (1b). Acidic gas is removed (2), and water contained in natural gas is removed by adsorption process (3). Sulfur is recovered (4) from removed acidic gas, and natural gas is processed.    USE - Processing of natural gas.    ADVANTAGE - The natural gas is efficiently and economically processed with high sulfur recovery rate. The adsorption processing of organosulfur compound in molecular sieve is not required.    DESCRIPTION OF DRAWING(S) - The drawing shows the flowchart of processing of natural gas. (Drawing includes non-English language text)    Conversion processes (1,1a,1b)    Acidic gas removal process (2)    Adsorption process (3)    Sulfur recovery process (4)
NOVELTY - An aggregate is formed by aggregating crystalline substance particles and has whole surface as C surface of crystalline substance.    USE - Aggregate used as catalyst for synthesizing methanol from carbon dioxide and environmental purification.    ADVANTAGE - The aggregate has high bond strength and shape maintenance capability.
NOVELTY - Method for promoting composting of organic waste material, involves increasing decomposition reaction by bacteria in organic waste, and increasing destruction of internal structure of waste material by stimulating volume expansion of the internal structure of waste material.    USE - The method is useful for promoting composting of organic waste material.    ADVANTAGE - The speed of composting of organic waste is increased by increasing the reaction surface area of bacterial activity. The activity of aerobic bacteria in waste material is increased and anaerobic bacteria are suppressed, hence generation of offensive odor can be minimized. Large amount of waste material can be decomposed in short time by an environmental-friendly method.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus for promoting composting of organic waste material, which comprises crushing unit for increasing decomposition reaction by bacteria in organic waste and destruction of internal structure of waste material by volume expansion of internal structure of organic waste and cooling unit to refrigerate the organic waste.
NOVELTY - The method involves making hydrocarbon oil i.e. kerosene, to contact desulfurizing agent containing gallium and indium, and aluminum oxide at temperature of 100 degrees Celsius or less to de-sulfurize the hydrocarbon oil, where the hydrocarbon oil contains sulfur compound such as thiophenes, benzothiophenes and dibenzothiophene. The desulfurizing agent is made of Lewis' acid group, activated carbon group or Broensted-acid group.    USE - Method for desulfurizing hydrocarbon oil i.e. kerosene, utilized in a fuel cell system (all claimed) of a fuel cell electric vehicle. Can also be used for desulfurizing paraffin type hydrocarbon oil such as octane, nonane, decane, undecane, dodecane, tridecane, tetradecane and pentadecane, aromatic hydrocarbon oil such as benzene, toluene, xylene, ethylbenzene and trimethylbenzene, and light oil.    ADVANTAGE - The method enables efficient desulfurization of the hydrocarbon oil in a liquid phase state at temperature of about 100 degree Celsius or less and removal of sulfur from the hydrocarbon oil at low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a fuel cell system comprising a desulfurizing part.
NOVELTY - A transesterification product comprises fats and oils, and lower alcohol which are transesterified in presence of basic catalyst. The transesterification product has fatty acid ester phase and glycerin phase. The transmittance of light of wavelength 600 nm of fatty acid ester phase is greater than or equal to 70%, and transmittance of light of wavelength 550 nm of glycerin phase is greater than or equal to 30%.    USE - A transesterification product used for manufacture of fatty acid ester for bio diesel fuels.    ADVANTAGE - The transesterification product can be obtained inexpensively, easily, and simply.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a manufacturing method of transesterification product involving transesterifying fats and oils and lower alcohol in presence of basic catalyst. The basic catalyst is strongly basic anion exchange resin. The molar ratio of fatty acid triglyceride and lower alcohol which comprise fats and oils is 1:2-1:4.5.
NOVELTY - Tablet (I) comprises a component (II) comprising an active ingredient, a drug and a drug substance; and an excipient; where (I) has a concavity or concavities; and (II) is disposed entirely within the concavity or at least one of the concavities of (I).    USE - (I) is useful as sugar-coated tablets, film-coated tablets, enteric coated tablets, multiple compressed tablets (such as layered tablets and press-coated or dry-coated tablets), controlled release tablets, solution-purpose tablets, effervescent tablets, compressed suppositories/inserts, buccal tablets, sublingual tablets, dispensing tablets and hypodermic tablets.    ADVANTAGE - The method of manufacturing (I) suppresses the generation of drug powders or drugs, thus protecting the health of the human involved in the method. The method of preparing (I) is environmentally safe and cost-effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of (I) comprising preparing a tablet having a concavity or concavities; and disposing, into the concavity or at least one of the concavities of the tablet, a dispersion comprising (II).    DESCRIPTION OF DRAWING(S) - The figure shows a cross section view of a tablet having two concavities on the opposite faces of the tablet, where the concavities are in the form of indentations.
NOVELTY - A biodiesel is prepared by squeezing Chenopodium glaucum to obtain oil extract; subjecting to natural sedimentation method to remove impurity; mixing obtained oil and methanol solution; adding potassium hydroxide catalyst; subjecting to esterification; setting aside to obtain fatty acid methyl ester layer on the upper layer and glycerin on the lower layer; separating the upper layer; decompressing and distilling separated fatty acid methyl ester layer to remove residual methanol to obtain fatty acid methyl ester; and adding petroleum diesel into the refined fatty acid methyl ester.    USE - Method of preparing biodiesel (claimed).    ADVANTAGE - The method is simple and low cost is low, and can produce biodiesel in batches which can meet the demands of the market.    DETAILED DESCRIPTION - A biodiesel is prepared by squeezing C. glaucum to obtain oil extract; subjecting to natural sedimentation method to remove impurity; mixing obtained oil and methanol solution at a mass ratio of 1:1-6; adding potassium hydroxide catalyst (0.5-1.5 wt.%); subjecting to esterification at 60-80 degrees C for 0.5-1.5 hours; setting aside to obtain fatty acid methyl ester layer on the upper layer and glycerin on the lower layer; separating the upper layer; decompressing and distilling separated fatty acid methyl ester layer to remove residual methanol to obtain fatty acid methyl ester having a purity of more than 90%; and adding petroleum diesel (23 wt.%) into the refined fatty acid methyl ester.
NOVELTY - Manufacture of honeycomb briquette comprises using materials comprising (kg) straw carbon (800-1000), clay (loess) (1600-2300), and self-adhering additive (600-1000).    USE - Method for manufacture of honeycomb briquette (claimed).    ADVANTAGE - The honeycomb briquette is buried for 3-4 hours with the same heat efficiency as current standard coal technique; and the time for sealing water in furnace is more than 11 hours. The output is 2.5 times more than honeycomb briquette in current standard coal technique. The self-adhering additive is used for controlling burning time, and saves more than 60% energy.
NOVELTY - Manufacture of straw composite fuel comprises pretreating straw, pulverized coal and papermaking sludge to form straw material, pulverized coal material and papermaking sludge material; and mixing and stirring materials at weight ratio of 7:1.5:1.5, and rolling mixture to form straw composite fuel.    USE - Method for manufacture of straw composite fuel (claimed).    ADVANTAGE - The method for manufacturing straw composite fuel can use crop straw and papermaking sludge for producing straw composite fuel with good combustion performance, in order to realize recycle of resource. In combustion of straw composite fuel, calcium carbonate in papermaking sludge acts desulfurization function and can remove sulfur dioxide generated by pulverized coal in straw composite fuel, thus reducing pollution to environment by sulfur dioxide.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a straw composite fuel, comprising straw material, pulverized coal material and papermaking sludge material.
NOVELTY - The water electrolysis system has water supplying device and electrolysis device. The water supplying device is used for supplying water to electrolysis water inlet of electrolysis device through electrolysis water outlet. The water supplying device receives and stores water discharged by electrolysis device from electrolysis water outlet of device through a condensing water returning opening. The electrolysis device is used for electrolyzing water at the state of supplying power into hydrogen and oxygen and discharging the water in the hydrogen and oxygen.    USE - Water electrolysis system for SPE.    ADVANTAGE - Ensures easy production and convenient repair and maintenance of the system when each mold has errors or abnormal conditions.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a control method.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of the water electrolysis system of SPE.
NOVELTY - Wall cracking for extracting DNA from algae and fungal cells comprises separating fermented algae or fungal fermentation liquor, maintaining bacterial sludge content at 70-80%, adjusting pH to 2-4 with acid, and stirring at 200-250 revolutions/minute for 20-40 minutes; controlling temperature at 10-20 degrees C; adding 1-3 wt.% antioxidant; performing high-pressure homogenization wall cracking; and increasing the temperature of the sludge to 80-90 degrees C, adding water at 80-90 degrees C, stirring at 250-350 revolutions/minute for 50-80 minutes, and separating the liquid material.    USE - Method for wall cracking for extracting DNA from algae and fungal cells (claimed).    ADVANTAGE - The method is simple, protects biological activity in the algae and fungal cells, and is environmental-friendly without toxicity and residues.    DETAILED DESCRIPTION - Wall cracking for extracting DNA from algae and fungal cells comprises:    (A) separating fermented algae or fungal fermentation liquor using a separation system to collect cell, maintaining bacterial sludge content at 70-80%, adjusting pH of bacterial sludge to 2-4 with acid, and stirring the bacterial sludge at 200-250 revolutions/minute for 20-40 minutes;    (B) controlling temperature of the bacterial sludge at 10-20 degrees C;    (C) adding 1-3 wt.% antioxidant in the bacterial sludge;    (D) performing high-pressure homogenization wall cracking with a high pressure homogenizer; and    (E) inreasing the temperature of the bacterial sludge to 80-90 degrees C, adding water at 80-90 degrees C to the bacterial sludge at a weight ratio of (1-3):1, stirring at 250-350 revolutions/minute for 50-80 minutes, and separating the liquid material with a tri-phase separator.
NOVELTY - The method involves avoiding the generation of short circuit between anode and cathode coils by exertion of preset elastic restoring force. The anode and cathode coils are attached to the groove formed at the support stand of electrolysis tank to avoid generation of short circuit. The major amount of hydrogen generated due to electrolysis reaction between anode and cathode coils are collected at the lower side of the electrolysis tank.    USE - Installation method of anode and cathode coils at hydrogen supply apparatus (claimed) for internal combustion engine of hydrogen fuel vehicle.    ADVANTAGE - The anode and cathode coils are installed at electrolysis tank effectively to avoid the generation of short circuit. Hence the oxidization reaction can be performed effectively in the electrolysis tank. The predetermined gap can be maintained between anode and cathode coils to ensure stabilized electrolysis process. The electrolysis tank endurance period can be shortened when the concentrations of anode and cathode coils used as electrolytes are increased.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacturing method of anode and cathode coils; and    (2) hydrogen supply apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the wiring configuration of electrolysis tank and vehicle-component.
NOVELTY - Greenhouse plant cultivation system has a structure in which waste material having organic refuse as main component is decomposed by bacteria to produce organic fertilizer and undecomposed residue (that does not succumb to decomposition by the bacteria) is incinerated to generate carbon dioxide, where the carbon dioxide obtained by incineration of the undecomposed residue is fed into the greenhouse to promote photosynthesis of plants inside the greenhouse, and the organic fertilizer produced by bacterial decomposition is spread on soil inside the greenhouse.    USE - The system is useful for cultivation of greenhouse plant.    ADVANTAGE - The organic fertilizer and carbon dioxide required for plant growth are produced using waste material. The system enables both growth and yield improvement of plant in greenhouse and reduction of cost burden by reclamation or combustion of organic refuse simultaneously. The waste material can be recycled and global warming can be prevented.    DETAILED DESCRIPTION - Greenhouse plant cultivation system has (a) structure in which waste material having organic refuse as main component is decomposed by bacteria to produce organic fertilizer and undecomposed residue (that does not succumb to decomposition by the bacteria) is incinerated to generate carbon dioxide, or (b) organic refuse decomposition unit in which waste material having organic refuse as main component is decomposed by bacteria to produce organic fertilizer, and combustion unit in which the undecomposed residue (that does not succumb to decomposition by the bacteria) is collected and incinerated to generate carbon dioxide, where the carbon dioxide obtained by incineration of the undecomposed residue is fed into the greenhouse to promote photosynthesis of plants inside the greenhouse, and the organic fertilizer produced by bacterial decomposition is spread on soil inside the greenhouse.
NOVELTY - A desulfurizer (5) removes the sulfur content from liquid fuel. A reforming reaction unit (6) reforms the liquid fuel removed in the sulfur content by desulfurizer and generates reformed gas. A shift reaction unit (7) removes the carbon monoxide contained in reformed gas from the reforming reaction unit by aqueous based shift reaction. A shift water line (L4) is connected between the reforming reaction unit and shift reaction unit for introducing the shift water into the shift reaction unit.    USE - Hydrogen production apparatus for fuel cell system (claimed) comprising polymer electrolyte fuel cell and solid oxide fuel cell, used in domestic application.    ADVANTAGE - The need for the selective-oxidation reaction unit is eliminated hence the size and cost of the hydrogen production apparatus can be reduced. The efficiency of the aqueous-based shift reaction process can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the fuel cell system. (Drawing includes non-English language text)    Fuel cell system (1)    Desulfurizer (5)    Reforming reaction unit (6)    Shift reaction unit (7)    Shift water line (L4)
NOVELTY - Removing greenhouse gas and manufacturing bio energy comprises ejecting exhaust gas in hybrid discharge facilities such as generating station, iron mill, engine, boiler and incineration plant, and aquatic plant, cultivation, and removing cultivated aquatic plant.    USE - The method is useful for removing greenhouse gas and manufacturing bio energy (claimed).    ADVANTAGE - The method produces environment-friendly bio energy.    DETAILED DESCRIPTION - Removing greenhouse gas removal and manufacturing bio energy comprises ejecting exhaust gas in hybrid discharge facilities such as generating station, iron mill, engine, boiler and incineration plant, and aquatic plant, cultivation, and removing cultivated aquatic plant, where the aquatic plant is a large seaweeds comprising Bacillariophyceae, brown seaweed, kelp, laver, green laver, Gelidium amansii including the flagellates, Skeletonema costatum, Chaetoceros curvisetus, Chaetoceros debilis, Chaetoceros didymus, Chaetoceros socialis, Ditylum brightwellii, Hemiaulus sinensis, Leptocylindrus danicus, Odontella aurita, Thalassiosira nordenskioeldii, Chaetoceros spp. including the flagellates, Heterosigma akashiwo, Chattonella spp., Rhodomonas salina, Isochrysis spp., cryptophytes, eumetazoa comprising protozoan, Oxyrrhis marina, Gyrodinium spp., Gymnodinium spp., Polykrikos spp., Protoperidinium spp., the Pfiesteria spp., Stoeckeria spp, Luciella spp., naked ciliate, rotifer cypridina, rotifera and zoobenthos and predator of the aquatic plant which absorbs the greenhouse gas while being alive in the exhaust gas hybrid which has the toxic component selected from egg, and larva for predator including the aquatic plant Amphidinium carterae and Prorocentrum minimum.
NOVELTY - Methanol and triglyceride are subjected to transesterification reaction using oxidized slag of electric furnace as solid phase catalyst, to obtain biodiesel fuel.    USE - Manufacture of biodiesel fuel.    ADVANTAGE - The method economically provides biodiesel fuel in high yield.
NOVELTY - Insect repellent composition comprises a compound having a desired Euclidean distance from a cluster defined by the structural-data information as given in the specification, where the compound reversibly or irreversibly binds a carbon dioxide receptor neuron of a dipteran insect.    USE - The composition is useful for repelling an insect pest comprising flies and mosquitoes including an Anopheles, Aedes, and Culex mosquito, in which the mosquito comprises at least one mosquito species comprising Tiger mosquitoes, Aedes aboriginis, Aedes Aegypti, Aedes albopictus, Aedes cantator, Aedes sierrensis, Aedes sollicitans, Aedes squamiger, Aedes sticticus, Aedes vexans, Anopheles quadrimaculatus, Culex pipiens, and Culex quinquefasciatus (all claimed). Tests details are described but no results given.    ADVANTAGE - The compounds are utilizing in small quantities, can be delivered in multiple forms like vapors and lotions, are economical, environmentally friendly, and are present in natural sources.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) an insect trap comprising the compound; and    (2) repelling an insect pest, comprising applying the repellent to a subject.
NOVELTY - A fuel cell membrane electrode assembly (1) is provided with an electrolytic membrane (11), electrode catalyst layer (12) and gas diffusion layers (15,17) which are laminated sequentially. The electrode catalyst layer and gas diffusion layer are adhered through radical-trapping compound.    USE - Membrane electrode assembly is used for manufacturing fuel cell (both claimed).    ADVANTAGE - The fuel cell comprising membrane electrode assembly has favorable voltage withstand property.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of fuel cell membrane electrode assembly; and    (2) manufacture of fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows the cross-sectional view of fuel cell membrane electrode assembly.    Fuel cell membrane electrode assembly (1)    Electrolytic membrane (11)    Electrode catalyst layer (12)    Catalyst coating membrane (14)    Gas diffusion layers (15,17)    Layer of radical-trapping compound (18)
NOVELTY - Membrane for growing plant capable of accumulating heavy metal in medium, comprises cultivating container having cultivating soil with water-permeable portion.    USE - The membrane is useful for growing plant, preferably Cyperaceae family Eleocharis, preferably E.acicularis, and collecting heavy metal (claimed) which is useful as resources.    ADVANTAGE - The heavy metals can be accumulated at high concentration using cultivation soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of collecting heavy metal, which involves adding cultivating soil and placing plant capable of accumulating heavy metal into the cultivation container having water-permeable portion, and growing the plant on the membrane, such that to absorb heavy metal.
NOVELTY - Abamectin sewage is concentrated in sewage evaporation tower by supplying hot-air from hot-air furnace and then the concentrated sewage is re-fermented. Thus, preparation of methane is carried out.    USE - Preparation of methane used as fuel.    ADVANTAGE - The method effectively and economically prepares methane.
NOVELTY - Organic fertilizer comprises (in parts): biogas residue (85-95) with moisture content of 30 wt.% or less, humic acid (3-10) with organic substance content of 50 wt.% or more, ammonium sulfate (1-2.5), potassium sulfate (0.5-1), ammonium phosphate (0.25-1), manganese sulfate (0.2-0.3), zinc sulfate (0.2-0.3) and boric acid (0.1-0.2).    USE - Organic fertilizer for wheat and vegetables.    ADVANTAGE - The organic fertilizer provides nutrients for crops, enriches soil, and improves product yield. The biogas residue solidifies easily as the moisture content is reduced effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the organic fertilizer, which involves (a) reducing the moisture content of biogas residue to 85-90 wt.% in an anaerobic fermentation tank, transferring the biogas residue into solid-liquid separator using a slurry pump, where the moisture content of the separated biogas residue is 55-65 wt.%, and transferring the separated biogas residue into solidifying tank for air-drying, where solidifying time is 5-6 months to reduce the moisture content of biogas residue to 30 wt.% or less, (b) crushing the biogas residue into powder using a chain-type crusher and mixing the powder with humic acid, ammonium sulfate, potassium sulfate, ammonium phosphate, manganese sulfate, zinc sulfate and boric acid, (c) transferring the mixed material into squeezing granulator for granulating into columnar granule and placing the granule in disc shaping machine to obtain granule, and (d) drying the granule using dryer to reduce the moisture content to 20 wt.% or less and cooling to 40 degrees C or less.
NOVELTY - Powdered biomass is sieved and dried, to obtain dried raw material having size of 20 meshes. The dried raw material is pressed and molded at 200-350 degrees C for 5-30 minutes under pressure of 5-20 MPa. The molded product is carbonized at 600-900 degrees C for 10-120 minutes. The carbonized product is activated at 700-900 degrees C for 10-120 minutes in presence of activating agent having water vapor density of 0.1-0.5 ml/minute, to obtain coal having high strength and density.    USE - Method for enhancing strength and density of coal used in engineering field and intersectional technique field of nano materials, carbon material, fibrin science and renewable energy sources.    ADVANTAGE - The method economically provides coal having high strength, density and excellent mechanical property by simple process.
NOVELTY - Biogas is infused from inlet of a packed spray absorber, and reacted with spraying solution containing sodium hydroxide and sodium carbonate to remove hydrogen sulfide. Gas is discharged from outlet of absorber, and spraying solution is discharged. The resulting spraying solution is partially returned to absorber, and a nutrient solution is added to remainder portion. Mixed solution is passed to biological filter tower and sprayed on biological filter material, and air is blown. Treated solution is recycled to absorber. Thus, hydrogen sulfide is removed from biogas.    USE - Removal of hydrogen sulfide from biogas.    DETAILED DESCRIPTION - Biogas is infused from gas inlet of a packed spray absorber, and reacted with spraying solution containing sodium hydroxide and sodium carbonate to remove hydrogen sulfide. The purified gas is discharged from gas outlet of the absorber, and spraying solution is discharged through solution discharging port arranged at bottom of the absorber. The resulting spraying solution is partially returned into the packed spray absorber to circularly spray, and a nutrient solution is added to remainder portion. The mixed solution of spraying solution and nutrient solution is passed to a biological filter tower. The nutrient solution contains nitrogen source and a phosphorus source. The mixed solution is sprayed on a biological filter material, and air is blown from the air inlet of filter tower. The solution is treated with microorganism within the biological filter material through the oxygen to transfer the sulfur ion to sulfate. The treated solution is recycled to the packed spray absorber. Thus, hydrogen sulfide is removed from biogas.
NOVELTY - The method involves changing air flow in a high temperature gasification chamber (1) from linear movement to downward spiral movement. A vortex flow field is formed in the high temperature gasification chamber. Heat required in gasification reaction is released, and upper temperature of the high temperature gasification chamber is controlled at 850-1100 degrees centigrade. Gas in a gas-solid separated substance is discharged by an exhaust pipe (2), and fly ash in the gas-solid separated substance is entered into an ash bucket (5) via a sedimentation pipe (4).    USE - Granular biomass such as rice hull and wood flour, cyclone staged gasification method.    ADVANTAGE - The method can be implemented utilizing a compact structure.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a granular biomass cyclone staged gasification device.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial sectional view of a granular biomass cyclone staged gasification device.    High temperature gasification chamber (1)    Exhaust pipe (2)    Gas-solid separating chamber (3)    Sedimentation pipe (4)    Ash bucket (5)
NOVELTY - Pest-trapping bottle contains (in wt.%) apple residue (15-40), edible vinegar (15-25), edible sugar (5-10), white spirit (5-10), stramonium dried powder of natural pesticidal plant (1-5) and remainder of water.    USE - Bottle is used for trapping pest.    ADVANTAGE - The pest-trapping bottle is manufactured by simple process. The bottle has excellent trapping effect. The bottle effectively traps pest without environmental pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for pest-trapping bottle, which involves mixing apple residue, vinegar, alcohol and stramonium dried powder of natural pesticidal plant, disinfecting and bottling.
NOVELTY - Method of fermenting cattle dung under anaerobic condition, involves (a) separating fiber and raw material using screw press solid-liquid separating device, and obtaining solid and liquid components, and (b) subjecting the liquid to two-phase anaerobic fermentation at 35 degrees C, placing the liquid in methanogenesis device after acidizing for 3 days, fermenting the liquid discharged from the device for one day, and obtaining methane. The mass ratio of the cattle dung to water is 2:1. The screw rotating speed is 68 revolutions per minute. The separating gap is 1.5 mm.    USE - The method is useful for fermenting cattle dung to obtain methane.    ADVANTAGE - The method reduces hydraulic retention time, consumes less amount of water, and yields methane in large amount.    DETAILED DESCRIPTION - Method of fermenting cattle dung under anaerobic condition, involves (a) separating fiber and raw material using water which can be fermented rapidly in cattle dung using a screw press solid-liquid separating device, and obtaining solid and liquid components after the separation, and (b) subjecting the liquid to two-phase anaerobic fermentation at 35 degrees C (in which inoculating amount of microorganism 30%), placing the liquid in a methanogenesis device after acidizing for 3 days (where the feeding amount of liquid for each day accounts for one seventh of the volume of the methanogenesis device), fermenting the liquid discharged from the device for one day (where the total hydraulic retention time is 11 days), and obtaining methane. The mass ratio of the cattle dung to water is 2:1. The screw rotating speed is 68 revolutions per minute. The separating gap is 1.5 mm.
NOVELTY - Method for biologically producing hydrogen using photosynthetic bacteria, involves fermenting and culturing the photosynthetic bacteria under one or more light sources at wave length of 400-500 nm, 510-550 nm, 575-600 nm, 600-640 nm, 780-880 mm or color temperature (2650-10000 K) corresponding to white light at 3000-7000 Lux of light intensity under anaerobic condition using organic acid as fermentation substrate to produce mixed gas and separating hydrogen from the mixed gas.    USE - The method is useful for biologically producing hydrogen using photosynthetic bacteria, preferably purple non-sulfur bacteria (claimed).    ADVANTAGE - The energy transforming efficiency is improved and cooling of the fermenting system is prevented.
NOVELTY - Invention refers to biotechnology, particularly microbiological natural environment purification, mainly for decomposition of non-utilisable (forbidden) pesticides and plant protection agents both solid and liquid with using a decomposition preparation. The preparation contains a glauconite-containing substance, biologically-active anaerobic sludge including adapted anaerobic microflora of biodecomposers, a growth factor in the form of succinic acid for vital activity of said adapted microflora of biodecomposers and water in the following ratio, wt %: glauconite-containing substance - 73.45 - 78.98, biologically-active anaerobic sludge - 10.00-25.00, succinic acid as a growth factor - 0.02 - 0.55, water - 1.00 - 10.00.    USE - Medicine.    ADVANTAGE - Invention allows improving effectiveness of pesticide processing. 3 cl, 2 tbl
NOVELTY - A diesel oil composition contains base diesel oil including biodiesel and additive. The additive contains components (a) and (b). The component (b) is arylamine type antioxidant and/or hindered phenol type antioxidant. The component (a) is prepared by mixing alkenyl succinimide with phenolic group-containing organic acid at 60-200 degrees C for 0.5-20 hours in the presence of solvent. The mole ratio of alkenyl succinimide and phenolic group-containing organic acid is 1:0.5-5.    USE - Diesel oil composition.    ADVANTAGE - The diesel oil composition has improved oxidation stability, and dispersibility.
NOVELTY - A diesel oil composition contains biodiesel and additive. The additive contains components (a) and (b). The component (b) is arylamine type antioxidant and/or hindered phenol type antioxidant. The component (a) is prepared by mixing Mannich base generated from reaction of polyolefin phenol, 1-6C aldehyde and polyethylene polyamine with phenolic group-bearing organic acid at 50-200 degrees C for 0.5-20 hours. The mole ratio of polyethylene polyamine in the Mannich base and phenolic group-bearing organic acid is 1:0.5-5.    USE - Diesel oil composition.    ADVANTAGE - The diesel oil composition has improved oxidation stability, and dispersibility.
NOVELTY - The hydrogen generator has a hydrogen production unit (100) provided with a storage space (300) in which hydrogen is accommodated. Hydrogen is generated using electrolyte placed within the hydrogen production unit, while the anode (210) provided in the storage space is connected with cathode. A cover (110) is provided for covering the storage space and hydrogen production unit.    USE - Hydrogen generator for use in electric-power generation applications and for use in detection of submarine device and emergency instrument in sea.    ADVANTAGE - Automatic control of hydrogen generation rate using the electrolyte can be easily achieved. Excess accumulation of hydrogen in storage space of hydrogen production unit can be easily prevented, and interruption of wire connection can be prevented, while ensuring stability. Effective removal of metal oxide generated in hydrogen production unit can be easily performed. A hydrogen generator of simpler structure and having improved service lifetime can be easily provided.    DESCRIPTION OF DRAWING(S) - The drawing shows the exploded perspective view of the hydrogen generator.    Hydrogen production unit (100)    Cover (110)    Hydrogen transmission pipe (120)    Anode (210)    Storage space (300)
NOVELTY - A sand biofilter and a wastewater collecting tank is connected with a precipitation tank. The sand biofilter is formed of lower cobblestone layer, yellow sand layer, upper cobblestone layer and thick soil layer. An aerating tube is connected with a blast blower and a water outlet is paved on lower cobblestone layer. A wastewater tube connected with the regulation tank is paved on the upper cobblestone layer.    USE - Oligodynamic wastewater treatment system for treating organic waste.    ADVANTAGE - The operating cost and the construction costs are reduced and the operating efficiency is improved. The wastewater treatment efficiency is improved in small floor space by saving land resource.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the oligodynamic wastewater treatment system.
NOVELTY - A pre-treated organosilicon wastewater is neutralized, to obtain wastewater with pH of 1-1.5. The neutralized wastewater is treated using iron-carbon micro-electrolysis treatment process, to obtain discharged water. The obtained discharged water is neutralized, to obtain wastewater with pH of 7-8. The discharged water is introduced to biochemical treatment system. Microorganism and active carbon as immobilized microorganism carrier are added to the resultant solution, then deposited and filtered. Thus, organosilicon wastewater is treated.    USE - Treatment of organosilicon wastewater.    ADVANTAGE - The method economically treats organosilicon wastewater, and is environmental-friendly.    DETAILED DESCRIPTION - A pre-treated organosilicon wastewater is neutralized using alkali substance, to obtain wastewater with pH of 1-1.5. The neutralized wastewater is supplied to micro-electrolysis reactor which is filled with filler, and iron-carbon micro-electrolysis treatment process is performed for 1-2 hours, to obtain discharged water. The obtained discharged water is neutralized, to obtain wastewater with pH of 7-8. The discharged water is introduced to biochemical treatment system which is composed of facultative tank and secondary level aerobic tank. An active sludge is not added in the facultative tank and the aerobic tank. Microorganism and active carbon as immobilized microorganism carrier are added to the resultant solution, then deposited and filtered. Thus, organosilicon wastewater is treated. The content of dissolved oxygen during the facultative process is less than 0.5 mg/L. The pH of the treated water is 4-5. The organosilicon wastewater has chemical oxygen demand of 1000-1500 mg/L, pH of 0.4-0.6 and chloride ion concentration of 7000-11000 mg/L. The volume ratio of filler with respect to water is 1:2.5. The iron-carbon micro-electrolysis treatment process is packing iron-carbon micro-electrolysis treatment process.
NOVELTY - Impurities are removed from traditional Chinese medicine Rheum officinale, crushed and sieved, to obtain Rheum officinale powder. Pre-treated Rheum officinale powder is added into an extracting kettle with supercritical carbon dioxide, solvent is added into kettle and extracted at 30-50 degrees C for 300 minutes under pressure of 15-30 MPa, and separated in steel bottle and storage tank having pressure of less than 4 MPa using pump. The separated product is collected, decompressed, sprayed and dried, to obtain rheum emodin powder.    USE - Method for extracting rheum emodin from Rheum officinale.    ADVANTAGE - The method enables extraction of rheum emodin from Rheum officinale, without environmental pollution.    DETAILED DESCRIPTION - Impurities are removed from traditional Chinese medicine Rheum officinale, crushed and sieved using sieve having size of 40 meshes, to obtain Rheum officinale powder. The pre-treated Rheum officinale powder is added into an extracting kettle with supercritical carbon dioxide, solvent is added into kettle and extracted at 30-50 degrees C for 300 minutes under pressure of 15-30 MPa and separated at 30 degrees C under pressure of 9 MPa and again separated at 30 degrees C under pressure of 6 MPa in steel bottle and storage tank having pressure of less than 4 MPa using pump at frequency of 20 F. The separated product is collected, decompressed, sprayed and dried, to obtain rheum emodin powder in yield of more than 15%. The content of rheum emodin in powder is 0.35 g/particles and increases to 6.6-10 mg/particles.
NOVELTY - The microorganism reservoirs (20) supply microorganism to fermentation tank (18) with organic waste. The gas holders (26) collect methane gas generated in fermentation tank. A quicklime reservoir supplies quicklime to mixer (38) to which fermented organic waste is supplied from fermentation tank connected to mixer by metal-nitride-oxide semiconductor structure. A water tank supplies water to mixer. Several reservoirs store the mixture of mixer. Several stabilization reservoirs (64) stabilize the mixture to produce liquid lime fertilizer and organic lime fertilizer.    USE - Organic waste disposal apparatus for producing organic fertilizer such as fast-acting fertilizer and slow-acting fertilizer for crops.    ADVANTAGE - The methane gas and heat generated during the process of mixing organic waste and quicklime can be extracted and the methane gas can be reused. The environmental contamination due to methane gas can be prevented. The salinity of the organic waste can be removed and the quality of the organic fertilizer can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of organic waste treatment.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the organic waste disposal apparatus.    Fermentation tank (18)    Microorganism reservoir (20)    Gas holder (26)    Mixer (38)    Stabilization reservoir (64)
NOVELTY - Chinese herbal product comprises (in parts by wt.): bleeding sap (5-10) of Luffa acutangula, aqueous extract of Sophora flavescens Ait. radix (8-17), aqueous extract of Cnidium monnier fruit (10-16), aqueous extract of a spray of Hemerocallis fulva (15-22), beeswax (2.5-5.5), emulsifier (1-4) and deionized water (25-45).    USE - The product is useful as care product for fur, preferably for cleaning, polishing, moisturizing the fur and for preventing water and mold from the fur.    ADVANTAGE - The product does not pollute the environment as it contains all the natural raw material, allows cleaning, polishing, moisturizing, preventing water and mold at a time and provides single step for caring the fur.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the Chinese herbal product comprising (i) preparing an aqueous phase, (ii) preparing an oil phase and (iii) emulsifying. The step (i) comprises adding bleeding sap of the aqueous extract of the Luffa acutangula, aqueous extract of the Sophora flavescens Ait. radix, aqueous extract of the Cnidium monnier fruit and a spray of the Hemerocallis fulva and deionized water to a water phase pot. The step (ii) comprises adding beeswax and an emulsifier into an oil phase pot. The step (iii) comprises heating the oil phase pot to 80-95 degrees C, melting the beeswax completely, uniformly stirring, transferring the melted beeswax into a vacuum emulsifying pot, heating the aqueous phase pot to 90-100 degrees C, injecting the aqueous phase into the vacuum emulsifying pot under stirring, homogenizing and emulsifying at 85-95 degrees C for 10-30 minutes, introducing the cooled water to cool and stirring to cool to room temperature.
NOVELTY - Endoglucanase, exoglucanase and beta -glucosidase derived from Fomitopsis pinicola and capable of decomposing red algae (Gelidium amansii) cellulose, are new.    USE - The endoglucanase, exoglucanase and beta -glucosidase are useful in composition for producing bioethanol (claimed) useful as fuel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing bioethanol, which involves decomposing red algae cellulose using the above-cited enzymes.
NOVELTY - Production of bioethanol, involves hydrolyzing Typha and culturing ethanol-producing strain using the hydrolyzed Typha solution as carbon source.    USE - Production of bioethanol useful as fuel.    ADVANTAGE - The bioethanol can be produced cost-effectively with high yield using weed (Typha) as raw material, hence global warming and deforestation can be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for culture medium for producing bioethanol, which comprises hydrolyzed Typha solution as carbon source.
NOVELTY - Method for preparing delayed release fertilizer, involves mixing and pulverizing compound fertilizer powder and oxide powder to obtain reaction product of poor solubility in water by mechanochemical reaction.    USE - The method is useful for preparing delayed release fertilizer, which is useful for cultivating plants (claimed).    ADVANTAGE - The delayed release fertilizer is environmental-friendly, and can be prepared by a simple and cost-effective process without using organic macromolecular material.
NOVELTY - Preparation of culture medium for plants, involves adding chicken manure, cow dung and pig manure into crop straw powder to obtain organic substance, adding substance into compressor, filling the obtained granule into air-permeable woven bag, soaking the bag in water, stacking the bag in warm environment, fermenting granule using microorganisms, mixing the fermented dry organic substance with expanded perlite and aged clean fine earth, and placing the obtained mixed material into a crusher to obtain culture medium with particle diameter of 0.5-2 microns.    USE - The method is useful for preparing culture medium which is used as organic fertilizer for promoting growth of plants.    ADVANTAGE - The culture medium is water-permeable and air-permeable, and has excellent water retention property.    DETAILED DESCRIPTION - Method of preparing culture medium for plant, involves (a) adding (in kg): chicken manure (10), cow dung (10) and pig manure(10) into crop straw powder (100) and mixing the contents uniformly to obtain organic substance, (b) adding the mixed organic substance into a compressor to obtain rod-like substance with particle diameter of 10-20 microns to obtain organic granule, (c) filling the organic granule into an air-permeable woven bag, soaking the bag into water to sufficiently absorb the water, stacking the bag in warm environment, covering a plastic film and fermenting using microorganisms, opening the woven bag when the temperature is cooled to environmental temperature, and naturally air-drying the bag, (d) mixing the fermented dry organic substance (100) with expanded perlite (10) and aged clean fine earth (500) to obtain mixed material, and (e) placing the mixed material into a crusher for crushing into culture medium particle with diameter of 0.5-2 microns.
NOVELTY - Method of preparing biofertilizer, involves regulating pH of biomass power plant ash, culturing microorganisms, and mixing cultured microbial suspension with pH regulated biomass power plant ash.    USE - The method is useful for preparing biofertilizer.    ADVANTAGE - The biofertilizer is inexpensive and environmental friendly as the biomass power plant ash is used as raw material. The sterilization of biomass power plant is prevented as it contains low bacterial content.
NOVELTY - Combined aerobic composting of rural solid waste, involves spraying microbial inoculum on straw stack and fermenting the pH regulated straw through natural ventilation for 10-15 days, mixing decomposable organic substance obtained from domestic garbage with fermented straw, and carrying out first composting for 3-5 days, introducing the gas produced in first composting process to the mixture containing first compost and livestock manure, and carrying out second composting for 3-5 days, followed by third composting of the second compost for 5-7 days.    USE - The method is useful for aerobic composting of rural solid waste.    DETAILED DESCRIPTION - Combined aerobic composting method of rural solid waste, involves cutting straw in length of 5-10 cm, spraying microbial composite inoculum on the straw stack, (where the concentration of microbial inoculum is (4-5 ml)/kg of straw), regulating water content of the straw to 50-55% and fermenting the pH regulated straw through natural ventilation for 10-15 days, mixing decomposable organic substance obtained from domestic garbage with the fermented straw, regulating initial water content and carbon/nitrogen content of mixture to 50-65% and 22-35 respectively, and carrying out first composting for 3-5 days, introducing the gas produced in first composting process to the mixture containing the first compost and livestock manure, regulating initial water content of resultant mixture to 50-60% and carrying out second composting for 3-5 days, followed by third composting of the second compost for 5-7 days, where the initial water content of second compost mixture is regulated to 40-50%.
NOVELTY - Hydrochloric acid and mixed acid are added to mother liquor salt accumulation of hydrolyzed D-(-)-p-hydroxyphenylglycine p-methyl benzene sulfonate in predetermined amount, maintaining temperature for predetermined time, cooled at predetermined temperature and centrifuged. Thus, mother liquor salt accumulation of hydrolyzed D-(-)-p-hydroxyphenylglycine p-methyl benzene sulfonate is carried out.    USE - Mother liquor salt accumulation of hydrolyzed D-(-)-p-hydroxyphenylglycine p-methyl benzene sulfonate used as intermediate for pharmaceutical.    ADVANTAGE - The method economically enables mother liquor salt accumulation of hydrolyzed D-(-)-p-hydroxyphenylglycine p-methyl benzene sulfonate with reduced energy consumption.
NOVELTY - Fully mixing anaerobic reaction circulation device comprises a full mixing anaerobic reaction kettle (100) and a circulation kettle (200), where the top of the fully mixing anaerobic reaction kettle is connected with the circulation kettle by an overflow tube (301). The lower portion of the circulation kettle is connected with the lower portion of the anaerobic reaction kettle by a transmission pipeline (303) and a material transmission pump (305). The circulation kettle is connected with a transmission tube providing raw materials for methane reaction.    USE - The device is useful for methane production.    ADVANTAGE - The device promotes large-scale industrial methane engineering, and can be used in cold region.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for circulation of raw materials, comprising constructing a fully mixing anaerobic reaction kettle with a first volume and a circulation kettle with a second volume, at first pumping the raw materials to the circulation kettle, pumping the raw materials to the bottom of the fully mixing anaerobic reaction kettle from the bottom of the circulation kettle, driving the supernatant liquid to overflow into the circulation kettle when the fully mixing anaerobic reaction kettle is full, mixing the supernatant liquid and the raw materials in the circulation kettle, and pumping the mixture into the fully mixing anaerobic reaction kettle to use the supernatant liquid in the full mixing anaerobic reaction kettle to carry out self circulation.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of a fully mixing anaerobic reaction circulation device.    Full mixing anaerobic reaction kettle (100)    Circulation kettle (200)    Overflow tube (301)    Transmission pipeline (303)    Material transmission pump (305)
NOVELTY - An anode plate and a negative plate are installed in the oxygen and hydrogen generation containers. A control unit controls the emission quantity of the hydrogen gas generated in the hydrogen generation container so that the inner pressure of the hydrogen and oxygen generation containers is maintained in the balance state during electrolysis process. A separation film is formed between the anode plate and negative plate. The separation film contacts with the negative plate.    USE - Electrolytic cell for use in water cleaner.    ADVANTAGE - The control unit controls the emission quantity of the hydrogen gas generated in the hydrogen generation container to maintain the inner pressure of the hydrogen and oxygen generation containers in the balance state during electrolysis process, hence the deformation of the separation film can be prevented. The structure of the electrolytic cell is simplified. The maintenance of the electrolytic cell is performed easily. The durability of the electrolytic cell is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for determining emission quantity of hydrogen gas ejected in electrolytic cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of the method for determining emission quantity of the hydrogen gas ejected in the electrolytic cell. (Drawing includes non-English language text)
NOVELTY - Converting a polysaccharide-containing material comprises: (a) dissolving the material in an inorganic molten salt hydrate; (b) hydrolyzing components of the material in the inorganic molten salt hydrate medium to form monosaccharide; (c) hydrogenating the obtained monosaccharide in the medium to the corresponding sugar alcohols; and (d) dehydrating the obtained sugar alcohols in the medium to form the corresponding anhydro sugars and/or dianhydro sugars, characterized in that the inorganic molten salt medium of step (d) is substantially free of transition metal salt.    USE - The process is useful for converting the polysaccharide-containing material (lignocellulose or hemicellulose) to form the corresponding anhydro sugars and/or dianhydro sugars (which comprise or consist substantially of isosorbide, which is dimethyl isosorbide (preferred) and/or diethyl isosorbide), where the dianhydro sugars are useful as a fuel additive or a fuel substitute (all claimed).    ADVANTAGE - The process converts polysaccharides to anhydropolyols with minimized formation of byproducts. The dianhydro sugars are converted in the inorganic molten salt medium to compounds that are less soluble in the inorganic molten salt medium thus can be readily separated from the medium.    DESCRIPTION OF DRAWING(S) - The figure illustrates a process comprising the combined steps of dissolution and hydrolysis of cellulose, hydrogenation of glucose to sorbitol and dehydration to isosorbide in molten salt hydrate medium.    Lignocellulosic material (1)    Lignin (4)    Isosorbide mixture (9)    Hydrolysis (10)    Hydrogenation reactor (30)
NOVELTY - Catalytically forming reaction products, comprises: providing an ionic liquid phase comprising catalyst and ionic liquid; and reacting at least one reactant in the ionic liquid phase to produce the reaction products, where the ionic liquid is hydrophobic, which prevents substantial water in the ionic liquid phase, and the reaction products comprising at least one of methanol and dimethyl ether.    USE - The method is useful in catalytic reactions to form reaction products e.g. methanol and dimethyl ether (all claimed).    ADVANTAGE - The method: utilizes highly hydrophobic ionic liquids, which prevents water from entering the ionic liquid phase, and thus prevents catalysts deactivation, and reduces or eliminates residual catalyst carrier, i.e. ionic liquid, in downstream steps; and facilitates complete separation of products and undesirable by-products.    DESCRIPTION OF DRAWING(S) - The figure shows a flow diagram of a process for producing hydrocarbon fuels.    Methane production (10)    Synthesis gas formation (12)    Methanol synthesis (14)    Dimethyl ether synthesis (16)    Hydrocarbon fuel synthesis (18)
NOVELTY - Producing product stream comprising mixture of aliphatic and aromatic 2-6C hydrocarbons by Fischer-Tropsch synthesis, comprises contacting a Fischer-Tropsch catalyst with a reformed gas that is produced by autothermal dry reforming of a hydrocarbon feed in the presence of a reforming catalyst and where the reformed gas essentially consists of syngas (hydrogen and carbon monoxide), oxygen and optionally a further component, which is methane, carbon dioxide and inert gas.    USE - The process is useful to produce aliphatic and aromatic 2-6C hydrocarbon by Fischer-Tropsch synthesis.    ADVANTAGE - The process exhibits: improved selectivity for aliphatic and aromatic 2-6C hydrocarbons; and reduced feedstock. The 2-6 C hydrocarbon selectivity of a Fischer-Tropsch synthesis reaction can be significantly increased in case the feed stream of Fischer-Tropsch synthesis reaction comprises molecular oxygen and loss of carbon atoms in the form of carbon dioxide can be reduced, which greatly increases the carbon efficiency of the Fischer-Tropsch synthesis process.
NOVELTY - Improving at least one property of a fuel composition, involves: deriving a fuel composition from oil selected from vegetable oil and/or animal oil; and blending the fuel composition with alkyl levulinate(s) to provide a fuel composition blend; where the alkyl levulinate(s) are selected and blended in an amount to have the fuel composition blend exhibit improvement relative to the fuel composition in at least one property.    USE - For improving at least one property of a fuel composition (comprising diesel fuel composition) to provide a fuel composition blend (claimed).    ADVANTAGE - The fuel composition blend exhibits relative to the fuel composition an increased initial boiling point, decreased 90% boiling point, increased flash point, increased density, or decreased viscosity; further exhibits relative to the fuel composition a decreased cold filter plugging point (CFPP); and has a density of 0.80-0.88 (preferably 0.820-0.845, especially 0.83-0.85) g/cm3. The high quality (diesel) fuels can be obtained by blending renewable diesel fuel derived from vegetable oil(s) with alkyl levulinates.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the fuel composition blend comprising: the fuel composition derived from oil selected from vegetable oil and/or animal oil; and the alkyl levulinate(s).
NOVELTY - Production of marsh gas, involves pre-treating lignocellulose raw material through squeezing and swelling in machine for 1-3 times, adding water to the processed lignocellulose raw material, adjusting the pH of the material to 6-7.5, mixing the obtained material with nutrient substance containing strain capable of producing marsh gas in anaerobic condition, and performing anaerobic fermentation with marsh gas strain (20-50 wt.%) and the lignocellulose raw material (5-30 wt.%) in the sealed reactor.    USE - The method is useful for producing marsh gas and fermented residues, which is used as fertilizer.    ADVANTAGE - The method is simple, increases the biodegradability of lignocellulose materials, capable of continuously producing the gas and increases the converting rate of biomass as the fermentation process is rapid.
NOVELTY - Methane fermentation treatment apparatus comprises membrane separation unit (13) which concentrates digested sludge in a methane fermentation tank (12), biological treatment unit (16) which processes in aerobic state the membrane transport liquid which permeated through the separation membrane (15) of the membrane separation unit, membrane transport liquid leading-out piping (27) which transfers membrane transport liquid to the biological treatment unit, and injection unit which injects biologically treated process liquid to the membrane transport liquid leading-out piping.    USE - Apparatus for performing methane fermentation treatment (claimed).    ADVANTAGE - Inexpensive and prevents precipitation of magnesium ammonium phosphate in the membrane transport liquid leading-out piping.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for methane fermentation method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the methane fermentation tanks. (Drawing includes non-English language text).    Methane fermentation tank (12)    Membrane separation unit (13)    Separation membrane (15)    Biological treatment unit (16)    Membrane transport liquid leading-out piping (27)
NOVELTY - A load provision portion (15) which provides predetermined load with respect to fuel cell component (2) and a cavity surface for forming a predetermined shape cavity according to a gasket (6) are formed by stacking a fuel cell component and a separator (3) and molding it in a metal mold (1). The injection filling of the material of gasket is carried out into the cavity. The molded gasket and separator are pierced and the internal surface of the gasket and the manifold hole (3h) of the separator which comprise a manifold are formed.    USE - Manufacturing method of fuel cell (claimed).    ADVANTAGE - The flow of the material of gasket into the manifold hole can be prevented, and a load can be reliably provided with respect to the fuel cell component at the time of fastening, without being influenced by the variation in the thickness of fuel cell component. Generation of short circuits can be prevented, and a gasket of uniform interference can be molded by a simple structure.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacturing apparatus of fuel cell; and    (2) fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the principal portion of the gasket molding die.    Metal mold (1)    Fuel cell component (2)    Separator (3)    Manifold hole (3h)    Gasket (6)    Load provision portion (15)
NOVELTY - The protrusions formed in the feed rollers (50,60) engage with the conveyance hole formed in the both sides edge of the continuous sheet (1) such as protective film. A restriction mechanism (70) presses the circumference of the of the conveyance hole of the sheet on the circumference of the feed roller protrusion.    USE - Apparatus for conveying fuel cell cells contained continuous sheet during manufacture of fuel cell.    ADVANTAGE - The cells of the fuel cell can be efficiently conveyed reliably by a simple structure without generating slack in the fuel cell cells contained continuous sheet.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) continuous sheet conveyance method; and    (2) fuel cell cells contained continuous sheet.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the continuous sheet conveying apparatus.    Continuous sheet (1)    Folding unit (20)    Rotary cutter (40)    Feed rollers (50,60)    Restriction mechanism (70)
NOVELTY - The position of single-sided catalyst layer (12A) is determined before the process of fixing protective film (20c) to the surface opposite to the surface comprising the catalyst layer coated to the strip-shaped electrolytic membrane (12s). An opening (20a) is formed in the strip-shaped protective film based on the position of the catalyst layer.    USE - Manufacturing method of fuel cell electrode.    ADVANTAGE - The position shift of catalyst layer formed on both surface of electrolytic membrane by correcting the formation position of opening based on the position shift of opening and strip-shaped protective film is prevented, and the quality of electrode for fuel cell is stabilized.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing apparatus of fuel cell electrode.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the manufacturing apparatus of fuel cell electrode and an explanatory view of the position of opening in strip-shaped protective film.    Catalyst layer (12A)    Electrolytic membrane (12s)    Opening (20a)    Protective film (20c)    Camera unit (32)
NOVELTY - The fuel cell system has an oxidant gas supply system for supplying oxidant gas to the fuel cell (102) fixed to the moving object e.g. vehicle (200). An exhaust flow path (50) discharges moisture content produced by the fuel cell according to the inclination angle of the moving object by the principle of siphon.    USE - Fuel cell system mounted in moving object e.g. electric vehicle, hybrid vehicle, etc.    ADVANTAGE - Appropriate discharge of moisture content produced by the fuel cell can be easily achieved, without the influence of the sloped state of vehicle mounted with fuel cell. A fuel cell system having improved structure can be easily provided.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of the vehicle mounted with fuel cell system.    Exhaust flow paths (50,52)    Valves (56,58)    Inclination sensor (60)    Fuel cell (102)    Moving object (200)
NOVELTY - Method for treatment of material, involves providing a material comprising lignocellulosic fibres, inoculating the material with one or more microorganisms and incubating the material under aerobic conditions.    USE - The method is useful for treatment of materials having lignocellulosic fibres for producing methane from manure where manure is chosen from cows, poultry, pigs or other livestock. The lignocellulosic fibres is chosen from corn silage, grass silage, and bagasse (all claimed).    ADVANTAGE - The treatment yields high yield of methane.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) method of producing methane from material comprising lignocellulosic fibres, involves (a) providing a material comprising lignocellulosic fibres, (i) performing a first anaerobic fermentation of the material from step (a) for generation of a first amount of methane, (ii) optionally separating a fraction comprising fibres, (b) inoculating the material of step (i) or (ii) with one or more microorganisms, (c) incubating the inoculated material from step (b) under aerobic conditions, and (d) performing a second anaerobic fermentation of the material obtained in step (c), for generation of a second amount of methane; and (2) microorganism or a mixture of two or more microorganisms capable of enhancing the methane potential of a lignocellulosic fibre fraction chosen from Bacillus subtilis (NRRL B-50136), Pseudomonas monteilii (NRRL B-50256 or 50258 or 50250 or 50251 or 50252 or 50253), Enterobacter dissolvens (NRRL B-50257), P.plecoglossicida (ATCC 31483), P.putida (NRRL B-50247 or ATCC 49451), P.plecoglossicida (NRRL B-50248), Rhodococcus pyridinivorans (NRRL 50249), P.mendocina (ATCC 53757), Acinetobacter baumanii (NRRL B-50254), B.pumilus (NRRL B-50255), B.licheniformis (NRRL B-50141), B.amyloliquefaciens (NRRL B-50151 or 50019 or ATCC 55405), Aspergillus niger (NRRL 50245) and A.oryzae (NRRL 50246), or their combinations.
NOVELTY - An alcohol liquid fuel comprises (pts.wt.) methanol (70-85), aromatic hydrocarbon (15-25), high-calorific-value poly-carbon hydrocarbon (2-5) and acetone (3-5).    USE - An alcohol liquid fuel.    ADVANTAGE - The fuel has easy to obtain raw materials, improved sanitation and safety, combustion value equivalent to liquefied petroleum gas and emission of the combusted waste gas of more than 100% which is lower than liquefied petroleum gas; does not have residue and raffinate; does not block the boiler bottom; is low cost; and can be used conveniently.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the fuel comprising mixing high-calorific-value poly-carbon hydrocarbon, aromatic hydrocarbon and acetone, adding methanol solution, and mixing.
NOVELTY - System comprises a heat storing device and a solar energy heat collector. A heat storing device connected to an automatic constant temperature control device via a pipeline is also provided. The automatic constant temperature control device is connected to a methane chamber for holding temperature, and a heater connected to the heat storing device, automatic constant temperature control device and solar energy heat collector via a pipeline is also provided. The solar energy heat collector is connected with the heat storing device.    USE - System for continuously producing methane.    ADVANTAGE - The system enables to produce methane continuously and stably all around the year and effectively controls temperature fluctuation.    DETAILED DESCRIPTION - System comprises a heat storing device and a solar energy heat collector. A heat storing device connected to an automatic constant temperature control device via a pipeline is also provided. The automatic constant temperature control device is connected to a methane chamber for holding temperature, and a heater connected to the heat storing device, automatic constant temperature control device and solar energy heat collector via a pipeline is also provided. The solar energy heat collector is connected with the heat storing device, a valve is arranged at the pipeline in the heater, heat storing device and automatic constant temperature control device, the automatic constant temperature control device is connected to a heating medium temperature sensor in the methane chamber, and a temperature sensor is located in the heater and valve. A material inlet, a gas outlet arranged at the upper part of the methane chamber, and a material outlet arranged at the lower part of the methane chamber are also provided.
NOVELTY - Methane generation involves cutting the crop straws and dipping them in water. An aqueous solution of straw complex bacterial agent and ammonium bicarbonate is added to the dipped straw and stirred. The water content of the crop straw is maintained at 60-80%. The straws are stacked for 60-80 hours at 30-60 degrees C to obtain a fermented material solution. 15-25 wt.% of inoculum and 55-75 g of accelerator are added to the fermented material solution and methane is generated by anaerobic fermentation at normal temperature.    USE - Method for generating methane (claimed).    ADVANTAGE - The methane generation method optimizes the conditions of crop straw pre-treatment and dry fermentation process and thus increases methane production effectively.    DETAILED DESCRIPTION - Methane generation involves cutting the crop straws and dipping them in water. An aqueous solution of straw complex bacterial agent and ammonium bicarbonate is added to the dipped straw and stirred. The water content of the crop straw is maintained at 60-80%. The straws are stacked for 60-80 hours at 30-60 degrees C to obtain a fermented material solution. 15-25 wt.% of inoculum and 55-75 g of accelerator are added to the fermented material solution and methane is generated by anaerobic fermentation at normal temperature. The anaerobic fermentation solution has concentration of 20-30 wt.% and pH of 6.0-8.0.
NOVELTY - Plant comprises at least one compost line (2, 3, 4) for the intake of organic material (1), which laterally bounds the walls (5, 6), where the interior of the walls is arranged with line channels (7, 8, 9) for media.    USE - The plant is useful for biological treatment of organic material.    ADVANTAGE - The plant effectively prevents the disturbance such as rain or sunlight, that delays the decaying process of the organic material and thus the process of biological treatment is carried out fast.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a precast concrete component (10, 11) for using in the plant.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the partial view of a plant for biological treatment of organic material with a converting machine.    Organic material (1)    Compost lines (2, 3, 4)    Walls (5, 6)    Line channels (7, 8, 9)    Precast concrete components (10, 11)
NOVELTY - A solid-liquid borohydride composite hydrogen storage material comprises alkali metal borohydride solid hydrogen storage material and aluminum base borohydride liquid hydrogen storage material at mole ratio of 2:8 to 8:2.    USE - Solid-liquid borohydride composite hydrogen storage material used for movable or portable hydrogen gas storage or transportation apparatus, particularly hydrogen fuel cell and hydrogen-combustion internal combustion engine vehicle-mounted hydrogen supply system.    ADVANTAGE - The composite hydrogen storage material overcomes difficulties including ultrahigh reaction temperature and severe hydrogenation condition of single borohydride.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of composite hydrogen storage material by adding aluminum chloride and alkali metal borohydride to vacuum reactor at mole ratio of 1:3, heating to 60-80 degrees C and thermally insulating for 5 hours, distilling, and purifying at less than or equal to - 129 degrees C to prepare liquid aluminum base borohydride; and uniformly mixing solid hydrogen storage material with liquid hydrogen storage material at mole ratio of 2:8 to 8:2, and mechanically ball milling at room temperature.
NOVELTY - Extract of Evodia suaveolens Scheff, which is obtained from aerial parts of plant through at least one step of extraction by an organic or aqueous solvent and has insect repellent activity, is claimed.    USE - The extract has insect repellent activity, including mosquitoes, preferably European/Mediterranean mosquitoes of Aedes aegypti (claimed). Tests details are described but no results given.    ADVANTAGE - The extract is: obtained from natural plant; biodegradable; and non toxic.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a composition comprising the extract and excipient, as insect repellent active agent, preferably against mosquitoes.
NOVELTY - Sewage treatment comprises pumping sewage to a pre-precipitating tank such that upper part sewage flows to an adjusting tank automatically; pumping to a physical reaction tank; sending to a primary sedimentation tank, then sending supernatant to an active sludge tank to perform biochemical treatment; firstly passing the effluent to a biochemical sedimentation tank, and sending supernatant to a contact aeration tank; sending effluent of the contact oxidation tank to a reaction tank; sending reacted sewage to a final sedimentation tank, then sending to an aeration bacteria filter.    USE - A sewage treating method in leather manufacturing course.    DETAILED DESCRIPTION - Sewage treatment comprises sending sewage in a collecting tank, pumping the sewage in the collecting tank with a sludge pump to a pre-precipitating tank to perform primary solid-liquid separation in the pre-precipitating tank, such that upper part sewage flows to an adjusting tank automatically; pumping sewage in the adjusting tank to a physical reaction tank; after reacting sewage in the physical reaction tank, sending to a primary sedimentation tank to separate solid and liquid, then sending supernatant of the primary sedimentation tank to an active sludge tank to perform biochemical treatment; firstly passing the effluent performed active sludge tank to a biochemical sedimentation tank, and sending supernatant of the biochemical sedimentation tank to a contact aeration tank; sending effluent of the contact oxidation tank to a reaction tank to react; sending reacted sewage to a final sedimentation tank to precipitate, then sending to an aeration bacteria filter, and finally, discharging effluent of the aeration bacteria filter.    DESCRIPTION OF DRAWING(S) - The drawing is a flow diagram illustrating the sewage treatment (Drawing includes non-English language text).
NOVELTY - One or more alcohols are prepared by incubating biomass cellulose or waste cellulose with ionic liquid to form a solution; precipitating amorphous cellulose and/or cellulose of reduced crystallinity by mixing with anti-solvent; adding cellulases to cellulose precipitate under conditions which promote hydrolysis of cellulose to sugars; and converting sugars to one or more alcohols.    USE - Method is used for preparation of one or more alcohols particularly ethanol or methanol (claimed).    ADVANTAGE - The liquid (I)-treated cellulose exhibits improved hydrolysis kinetics with optically transparent solutions formed after about two hours of reaction, thus providing opportunity for separation of products from catalyst (enzyme) easing enzyme recovery. The initial hydrolysis rates for liquid (I)-treated cellulose were up to two orders of magnitude greater than those of untreated cellulose with an appropriate selection of enzymes. The anti-solvent can be easily stripped from liquid (I)/anti-solvent mixture for recovery and recycle of both ionic liquid and anti-solvent.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating a regeneration unit.
NOVELTY - The system has a conduit (6) for withdrawing a portion of compressed natural gas. A dehydration membrane is connected to the conduit, where the dehydration membrane comprises an output comprising dried natural gas. The output of the dehydration membrane is connected to a fuel line, which connects a gas engine (7) to operate a compressor (3). A gas-separation membrane (17) is connected between the dehydration membrane and the gas engine, where the gas engine receives the dried natural gas as fuel from which carbon dioxide is removed.    USE - System for producing and conditioning natural gas for a gas engine for driving a compressor at or near a natural gas well.    ADVANTAGE - The system enables conditioning a stream of natural gas, and improves the process of natural gas production, by providing a conditioned fuel for the gas engine used to drive a compressor at a wellhead. The system reduces the cost of operation and maintenance, and improves the efficiency of a gas engine used to drive a compressor at the well-head. The system produces the stream of natural gas, which is free of carbon dioxide.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for making compressed natural gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a system for producing and conditioning natural gas.    Buffers (2, 5)    Compressor (3)    Conduit (6)    Gas engine (7)    Gas-separation membrane (17)
NOVELTY - A method comprises: generating heat and electricity using a photovoltaic system; producing hydrogen using an electrolyzer at least partially powered by the generated electricity; and boosting the pressure of the produced hydrogen via a metal-hydride compressor at least partially powered by the generated heat.    USE - The method is useful for producing integrated solar-powered high-pressure hydrogen.    ADVANTAGE - The stored high pressure hydrogen may be used to fill fuel-cell electric vehicle (FCEV) tanks. The electricity can also be used to efficiently charge the batteries in an extended range electric vehicle (EREV).
NOVELTY - Shutting down a water electrolysis apparatus which applies an electrolysis voltage between current collectors disposed on the respective sides of an electrolyte membrane comprises: applying a voltage between the current collectors after the cathode electrolysis chamber stops supplying the hydrogen; and reducing a pressure in at least the cathode electrolysis chamber while the voltage is being applied between the current collectors.    USE - The method is useful for shutting down a water electrolysis apparatus (claimed).    ADVANTAGE - The method prevents catalytic electrode layers from deteriorating for an effective water electrolyzing process.    DETAILED DESCRIPTION - Shutting down a water electrolysis apparatus which applies an electrolysis voltage between current collectors disposed on the respective sides of an electrolyte membrane thus to electrolyze water to generate oxygen in an anode electrolysis chamber and hydrogen in a cathode electrolysis chamber under a pressure higher than a normal pressure, comprises: applying a voltage between the current collectors after the cathode electrolysis chamber stops supplying the hydrogen; and reducing a pressure in at least the cathode electrolysis chamber while the voltage is being applied between the current collectors.
NOVELTY - An electrode comprises a volumetrically compressed and structurally stable mixture (m1) of reactive metal particles having a high reactive surface area, and metal substrate particles having a lesser surface area than the reactive metal particles, where the quantity of metal substrate particles provides structural stability to the electrode upon compression. The electrode is volumetrically compressed to a percentage of the mixture's original volume so as to minimize volume while still permitting an amount of permeability to maintain a high catalytic efficiency.    USE - As an electrode which is useful in at least one electrochemical or catalytic application, particularly in electrochemical sensor, and in a fuel cell or in an electrolyzer (claimed) to generate hydrogen and oxygen.    ADVANTAGE - The electrode comprises anode and cathode terminal compressed to either side of an ion exchange membrane, where when the assembly is exposed to water, hydrogen is generated at the cathode terminal and oxygen is generated at the anode terminal. This configuration minimizes the volume of the device and there is no need for an aqueous electrolyte. The electrode utilizes more cost-efficient metals as catalyst.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) an electrolyzer (e1) comprising the mixture (m1), configured to generate hydrogen and oxygen when energy is applied in the presence of water and an electrolyte;    (2) a fuel cell (c1) comprising the mixture (m1), configured to generate electrical energy from reactions of anode and cathode fuels comprising an ion-exchange membrane and first and second electrodes disposed on opposite sides of the ion-exchange membrane; and    (3) an electrochemical sensor comprising the mixture (m1), where the sensor is configured to detect an analyte capable of undergoing electrochemical reaction at the sensor.
NOVELTY - Tetrahydroxo aluminate is added during reaction of water and aluminum, to produce hydrogen.    USE - Production of hydrogen used for fuel cell for portable device.    ADVANTAGE - The hydrogen is produced economically at high rate in short period of time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for hydrogen-producing apparatus, which has a hydrogen-producing portion in which water and aluminum are reacted under state of addition of tetrahydroxo aluminate.
NOVELTY - The device has a cracking part connected with a distilling part. The distilling part is composed of a distillation column that is connected with an oil-water separator. The oil-water separator is connected with a fractionation catalyst part that is connected with a condensing water tank. The condensing water tank is connected with a semi-finished product oil tank. The fractionation catalyst part is connected with a clean oil tank. The cracking part is composed of a cracking tank that is connected with a reactive filter tank by a pressure-type filter through an oil pump.    USE - Waste oil type energy regenerating device by utilizing waste oil such as waste engine oil, residual oil, coal tar, waste plastic, waste wheel, plant and animal oil, leftovers, saponin and swill-cooked dirty oil (all claimed).    ADVANTAGE - The device increases production of oil by 1.67 percentages.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a processing method for regenerating energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an energy regenerating device.
NOVELTY - The method involves establishing large-scale gasification furnace inside or near a water head site. Light is provided to the furnace. A cracking reaction is performed among carbon, hydrogen, oxygen, nitrogen compound and water to generate combustible gases such as hydrogen, carbon oxide, methane and ammonia gas in the furnace. Fuel gas is sent to houses through pipelines. Uncooled gases are directly used for combustion, and for generating electricity. Juice formed from compression is concentrated and layered to extract various nutrition constituents for processing food.    USE - Method for producing energy source from hyacinth.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a method for producing energy source from hyacinth.
NOVELTY - Device for producing biogas through high-solid two-phase three-section anaerobic digestion of corrosive organic garbage comprises a hydrolysis acid-produced reactor and a methane-produced reactor.    USE - The device is useful for producing biogas (claimed).    ADVANTAGE - The device has simple processing procedure, low cost, easy maintenance and stable and reliable performance, and is suitable for anaerobic digestion treatment of the corrosive organic garbage and has effective and stable capability of producing the biogas through the anaerobic digestion of corrosive organic garbage.    DETAILED DESCRIPTION - Device for producing biogas through high-solid two-phase three-section anaerobic digestion of corrosive organic garbage comprises a hydrolysis acid-produced reactor and a methane-produced reactor, where the two reactors are connected and communicated with each other on the bottom through a circulating pump and a pipeline; the hydrolysis acid-produced reactor is a solid infiltration bed reactor, and the top is provided with a water distributor and a spraying head; a feeding port is arranged on the middle upper part, the middle upper part is provided with a porous plate and a discharging port, the bottom is provided with a slag discharge port, an infiltration filler is placed on the porous plate; the methane-produced reactor consists of a filtering filler bed and a fiber filler bed, where the filtering filler bed is positioned at the lower part and the fiber filler bed is positioned at the upper part; a filling filler is placed in the filtering bed, a fiber filler frame is placed inside the fiber filler bed, and the fiber filler is wound on the fiber filler frame.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for producing biogas.
NOVELTY - Pyrazole derivatives (I) and (II), or their N-oxides and salts are new.    USE - In fungicidal composition for controlling plant diseases caused by fungal plant pathogens (claimed).    ADVANTAGE - The compound is less costly and environmentally safer.    DETAILED DESCRIPTION - Pyrazole derivatives of formulae (I) and (II), or their N-oxides and salts are new.    Q1=e.g. phenyl ring or naphthalenyl ring system, or 5- to 6-membered fully unsaturated heterocyclic ring or 8- to 10-membered heteroaromatic bicyclic ring system;    Q2=e.g. phenyl ring or naphthalenyl ring system; or 5- to 6-membered saturated, partially unsaturated or fully unsaturated heterocyclic ring or 8- to 10-membered heteroaromatic bicyclic ring system, 1-12C alkyl, 2-12C alkenyl, 2-12C alkynyl, 3-12C cycloalkyl or 3-12C cycloalkenyl;    X=O, C(O) or C(=S);    R1=e.g. H, halo, 1-6C alkyl, 1-6C haloalkyl, 2-4C alkenyl, 2-4C alkynyl, 3-7C cycloalkyl, cyano, 1-6C alkoxy, 1-6C haloalkoxy, 2-5C alkoxyalkyl or phenyl;    R1a=H;    X'=NH;and    R2=cyclopropyl (optionally up to di-substituted with halo or methyl), CH3, CH2CH3, halo, cyano, cyanomethyl, halomethyl, hydroxymethyl, methoxy or methylthio.    Full Definitions are given in the DEFINITIONS (Full Definitions) section. INDEPENDENT CLAIMS are included for the following:    (1) a fungicidal composition (C1) comprising the compound (I), and at least one other fungicide;    (2) a fungicidal composition (C2) comprising the compound (I), and at least one additional component selected from surfactants, solid diluents and liquid diluents;    (3) controlling plant diseases caused by fungal plant pathogens involving applying the compound (I) to the plant or portion of it, or to the plant seed; and    (4) a composition (C3) comprising the compound (I), and at least one invertebrate pest control compound or agent.
NOVELTY - An oxidation reaction is generated using reaction tank containing compound activated with light on optical anode of electrode unit installed on bio-photogalvanic cell. The aqueous solution of waste materials and waste liquid, waste suspension liquid, air and oxygen are blown into the tank. The photolysis purification of biomass, organic and inorganic compound, waste material and waste liquid is performed by irradiating light to biomass from transparent electroconductive glass side of optical anode.    USE - Method for performing photolysis purification and electric power generation of biomass.    ADVANTAGE - The efficiency of photolysis and electric power generation can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for bio-photogalvanic cell.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view illustrating the reaction mechanism. (Drawing includes non-English language text)
NOVELTY - A transplastomic plant comprising one or more plastids engineered to express genes encoding enzymes for production of polyhydroxyalkanoate (PHA), is new.    USE - The transplastomic plant is useful for producing PHA, biorefinery fuel or energy feedstock, where the plant is dicot or monocot. The plant is chosen from Brassica, preferably B.napus, B.rapa, B.carinata and B.juncea, oilseeds such as Camelina sativa, Crambe, Jatropha, castor,Arabidopsis thaliana, maize, soybean, cottonseed, sunflower, palm, algae, coconut, safflower, peanut, mustards including Sinapis alba, sugarcane, silage corn, alfalfa, switchgrass, Miscanthus, hemp, sorghum, and tobacco (claimed). The PHA is useful to produce plastics for use in injection molded goods, films, fibers and non-woven articles, foams, bottles and other containers and coating materials including paper coatings and paints. The PHA can also be converted to chemical intermediates and is useful in medical field.    ADVANTAGE - The transgenic plant is stable, fertile, and produces greater than 10%, preferably at least 20% PHA per unit dry cell weight in leaves.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) seed of the transplastomic plant; and    (2) method for producing a transplastomic plant.
NOVELTY - The mold has a flanging mold having a same shape with that of a blanking forming mold, where periphery of the flanging mold and fluid exit are provided at two ends of a flow field plate. Punch flanging orifices are provided at the periphery of the flanging mold. A die (2) of the flanging mold is a flow field face of the flow field plate.    USE - Thin metal flow field plate stamping mold for processing a fuel cell.    ADVANTAGE - The mold is simple in structure and easy to manufacture, and the metal flow field plate has high precision and convenient manufacturing. The produced flow field plate has little buckling deformation.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a thin metal flow field plate stamping mold.    Terrace die (1)    Die of a flanging mold (2)
NOVELTY - The boiler has a right interface located under a vaporizer and connected with a combustion chamber of a boiler. A discharge hole of a loading machine is located opposite to a feed inlet of the vaporizer. An air distribution outlet arranged on a wall of the vaporizer is connected with an air outlet duct of a draught fan. A chain furnace grate is located opposite to the vaporizer and the combustion chamber. A speed reducer is connected with motor and a main shaft of a chain furnace grate. A side wall of a left end of the vaporizer is provided with a fire door.    USE - Biomaterial fuel fired boiler.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial sectional view of a biomaterial fuel fired boiler.
NOVELTY - Atmosphere control system, comprises: first air delivery means and first air extraction means for delivering and extracting air respectively from a first treatment zone (40) in a waste treatment chamber (10); and second air delivery means and second air extraction means for delivering and extracting air respectively from a second treatment zone (42) in the chamber, where the second air delivery means is connected to the first extraction means so that air is extracted from the first treatment zone and delivered to the second treatment zone by the second air delivery means.    USE - The atmosphere control system is useful for controlling the atmosphere in a waste treatment chamber (claimed).    ADVANTAGE - The atmosphere control system: accelerates biological breakdown of waste by supplying air or oxygen and water in varying amount to different treatment zones in the waste treatment chamber; and is easily and accurately controlled.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for controlling the atmosphere in a waste treatment chamber, comprising delivering and extracting air from the first and second treatment zones in the waste treatment chamber, where the air extracted from the first treatment zone is communicated to and delivered into the second treatment zone.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic cutaway view of a waste treatment chamber including a waste turning machine.    Waste treatment chamber (10)    First treatment zone (40)    Second treatment zone (42)    Third treatment zone (44)    Elongated lower conduit (46)
NOVELTY - An improved gobar gas plant comprises a filter (1), in which the water and human manure is separated. The separated water is filtered and recycled to use in garden. The separated human manure, sewage sludge, municipal solid waste, biodegradable waste or any other biodegradable feedstock, under anaerobic conditions and fall down leaves of trees/plant are crushed with roller crusher (5). The crushed waste paste is supplied into the plant, where the gas formed under the metallic covered drum (16) and the waste managements gas can be utilized for heat energy generation. Image 0/1
NOVELTY - A nickel-based biomass tar reforming catalyst comprises 10-35 wt.% of nickel oxide (NiO), 8-30 wt.% of cerium oxide (CeO2), and gamma -aluminum oxide as carrier.    USE - The nickel-based biomass tar reforming catalyst is useful for steam reforming process of biomass gasified tar.    ADVANTAGE - The nickel-based biomass tar reforming catalyst has simple preparation method and high activity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a preparation method of the nickel-based biomass tar reforming catalyst comprising: (a) carrying out preparation of metal salt solution and precipitator: dissolving analytically pure nickel salt, cerium salt, and aluminum salt with pure water to make an aqueous solution; and confecting the analytically pure water soluble weak alkali to the aqueous solution as precipitator; (b) carrying out coprecipitation: letting the metal salt solution and the precipitator confected in (a) flow in parallel to drip in the container; continuously stirring the material in the container; where the pH value is controlled to 9-10; and the flocculent suspension is formed after the dripping is finished; (c) aging and filtering: continuously stirring for 1 hour and letting it stand for 4-12 hours to filter; and (d) drying the filter cake obtained in (c) at 90-110 degrees C to remove water, and calcining for 3-8 hours at 500-700 degrees C to form the nickel-based biomass tar reforming catalyst.
NOVELTY - An exotic soil used as revetment of plants in loess slope comprises (pts.wt.) sandy loess (800-900), soil conditioners (100-200), water retention agents (1-2), bonder (0-1), and compound fertilizers (2-5).    USE - The exotic soil is useful as revetment of plants in loess slope (claimed).    ADVANTAGE - The exotic soil can improve the structure of the sandy loess and provide the required soil environment to the plants in loess slope; where it effectively solves the problems that it is difficult to protect the vegetation of the slope because of lack of water and difficult water retention in the semiarid area in the north. Moreover, it mainly uses the waste and unusable waste soil; the raw material can be easily obtained; it has low price and simple construction; and it reduces construction investment of slope protection project.
NOVELTY - The oxyhydrogen producer has electrolysis water generator with a group of positive and negative electrodes which are arranged alternatively. The polar plates of the electrodes having same polarities are connected electrically, while insulating polar plates of the electrodes having opposite polarities. Two clamping plates are arranged at outer side of the polar plates. The inner side of the clamping plate is isolated from the polar plate by a sealing ring. A water inlet is arranged on one clamping plate and an air outlet is arranged on the other clamping plate.    USE - Oxyhydrogen producer for producing oxyhydrogen used as auxiliary fuel for motor vehicle and steamship.    ADVANTAGE - Since the need for electrolysis tank structure and air outlet passage is eliminated, oxyhydrogen producer is simple and compact in structure. Engine oil can be saved and high electrolysis efficiency is achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the oxyhydrogen producer. (Drawing includes non-English language text)
NOVELTY - Biological foliar fertilizer is obtained by soaking medicinal stone particle (250 kg) in edible rice vinegar (500 kg) contained in aluminum container for 20-25 days, filtering the obtained solution, and filling the product in barrel.    USE - The fertilizer is useful for producing drought resistant, cold resistant and disease resistant plants. Can also be used for inhibiting bacteria and eliminating toxins in foliage crops.    ADVANTAGE - The fertilizer is non-toxic, environment-friendly, increases the yield of plants, absorbs harmful substances, and promotes early maturing of plants.
NOVELTY - Propane production involves using raw gas storage kettle, a sampler feeder, a separating column, an analyzing controller, an automatic valve, a left cold trap and a right cold trap assembled by connecting pipes.    USE - Method for producing propane (claimed).    ADVANTAGE - The propane production method enables to produce the propane with mass production having high-purity. The method has advanced rational design.
NOVELTY - Shell catalyst comprises a zirconium oxide containing open-pore catalyst support with a shell, in which ruthenium is enclosed.    USE - The shell catalyst is useful for the gasification of biomass (claimed).    ADVANTAGE - The shell catalyst has high activity and selectivity for the generation of methane.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the shell catalyst, comprising: (a) providing the zirconium oxide containing open-pore catalyst support; (b) impregnating the catalyst support with a solution of a ruthenium precursor compound; and (c) impregnating the catalyst support with a precipitating agent to precipitate the ruthenium component of the ruthenium precursor compound.
NOVELTY - A waste gas containing organic halogen compound is processed by decomposing organic halogen compound contained in waste gas by making waste gas contact microorganisms layer which consists of decomposition microorganisms which decompose organic halogen compound supported by support, dispersing liquid which moistens microorganisms layer in microorganisms layer by dispersion unit, collecting liquids on tank, performing deionization process with respect to liquid collected by tank, and making dispersion unit circulate through liquid in which deionization process was performed.    USE - Processing of waste gas containing organic halogen compound.    ADVANTAGE - The method can process organic halogen compound efficiently over a long period of time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a waste gas processing apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of waste gas processing apparatus.    Waste gas processing apparatus (10)    Waste gas piping (12)    Gas treatment column (24)    Tank (28)    Process piping (34)
NOVELTY - An oxyhydrogen-gas generator carries out electrolysis of water solution in an electrolytic cell (1), and produces oxygen gas and hydrogen gas in mixed state, and has a condenser (3), gas discharge portion (2) and heat radiator (4). The condenser condenses water vapor contained in gas generated in gas discharge portion, by heat radiator, and water produced by condensation is circulated to electrolytic cell.    USE - Oxyhydrogen-gas generator is used for generating hydrogen gas and oxygen gas used during welding, cutting and thermal spraying processing.    ADVANTAGE - The oxyhydrogen-gas generator has high safety and reliability, and dew condensation of pipe-interior is prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows the perspective view of oxyhydrogen-gas generator. (Drawing includes non-English language text)    Electrolytic cell (1)    Gas discharge portion (2)    Condenser (3)    Heat radiator (4)    Gas and water separator (5)    Recovered water (7)
NOVELTY - A hydrogen-producing apparatus comprises reaction chamber (11) in which hydrogen-producing substance (9) which reacts with solution for reaction and produces hydrogen is accommodated, reaction container provided with reaction chambers, exhaust passage which discharges produced hydrogen, and solution flow path (4) which liquid-feeds solution for reaction to reaction chambers.    USE - A hydrogen-producing apparatus used for fuel cell system (claimed).    ADVANTAGE - The apparatus can generate hydrogen with necessary minimum water without requiring large-scale mechanism.    DETAILED DESCRIPTION - A hydrogen-producing apparatus comprises reaction chamber (11) in which hydrogen-producing substance (9) which reacts with solution for reaction and produces hydrogen is accommodated, reaction container provided with reaction chambers, exhaust passage which discharges produced hydrogen, solution flow path (4) which liquid-feeds solution for reaction to reaction chambers, and change unit which switches to next reaction chamber with downstream liquid feeding of solution for reaction one by one when specified amount liquid feeding of solution for reaction is carried out in upstream reaction chamber and generation reaction of hydrogen arises. The specified amount is regulated by volume of reaction chamber. An INDEPENDENT CLAIM is included for a fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of circulation situation of solution for reaction.    Solution flow path (4)    Hydrogen-producing substance (9)    Reaction chamber (11)    Inlet (13)
NOVELTY - The method involves providing natural gas, and pre-cooling the natural gas by carrying out heat exchange with refrigerant fluid i.e. propane, contained in a pre-cooling cycle at which a compressor is driven by a vapor turbine (109). The natural gas is liquefied by carrying out heat exchange with another refrigerant fluid e.g. hydrocarbon and nitrogen mixture, contained in a liquefaction cycle at which another compressor is driven by a gas turbine (101) producing fumes. Part of heat is recovered from the fumes, and vapor is produced for the vapor turbine by using the recovered part.    USE - Method for producing liquefied natural gas.    ADVANTAGE - The method economizes the combustible gas to 34 percent, and optimizes energy efficiency of natural gas liquefaction plants while minimizing maintenance constrains for a heavy equipment i.e. gas turbine.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an installation for producing liquefied natural gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an energy supply system of compressors presented in a liquefied natural gas production installation.    Gas turbine (101)    Combustion chamber (104)    Recovery boiler (107)    Vapor turbine (109)    Condenser (111)
NOVELTY - Transition metal-promoted iron (Fe (II))-zinc (Zn) solid acid catalyst comprises potassium ferrocyanide, zinc chloride, organic ligand tert-butanol, and polyethylene glycol, where transition metal taking up 1-10% of zinc chloride is added in the course of synthesis.    USE - The transition metal-promoted Fe (II)-Zn solid acid catalyst is used for synthesizing biodiesel (claimed). It is used for esterification reaction and transesterification reaction in the synthesis of biodiesel.    ADVANTAGE - The catalyst is hardly affected by water and acid; and has good repeatability. The activity of the catalyst after being added with transition metal is greatly improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of Fe (II)-Zn solid acid catalyst by coprecipitation comprising dissolving potassium ferrocyanide into deionized water to prepare into 0.25 mol/L solution I; adding transition metal(s) (1-10% of zinc chloride), same volume of tert-butanol and aqueous solution of hydrogen dioxide into zinc chloride to prepare 5 mol/L solution II; dissolving polyethylene glycol into water and tert-butanol at 30:4:80 g/ml/ml ratio to prepare solution III; slowly dropping solution I into solution II at 323 K with stirring; precipitating; adding solution III within 5-10 minutes; continuously reacting for 2 hours; washing with water; filtering; drying in vacuum; and sintering to obtain Fe (II)-Zn catalyst.
NOVELTY - An electrolytic membrane (11) is clamped by a catalyst layer (12) containing an electrolyte having glass transition temperature (i), and a catalyst layer (13) comprising an electrolyte having glass transition temperature (ii). The catalyst layers (12,13) are heat-processed such that the strength of catalyst layer (12) is more than the strength of catalyst layer (13) with the relationship of glass transition temperature (i) of catalyst layer (12) and glass transition temperature (ii) of catalyst layer (13), to obtain a fuel cell (CL).    USE - Manufacture of fuel cell (claimed).    ADVANTAGE - The method enables manufacture of fuel cell having excellent workability.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the fuel cell.    Separator (6)    Electrolytic membrane (11)    Catalyst layers (12,13)    Gas diffusion layers (14,15)    Fuel cell (CL)
NOVELTY - Preparation of salt-resistant sewage-purifying microbial inoculum involves inoculating salt-resistant sewage-purifying bacteria (CGMCC 3314) to nutritious agar-agar culture medium, shaking bottle, and oscillating and culturing at 25-40 degrees C and 120-180 revolutions/minute (rpm) to logarithmic phase; inoculating bacteria (1-2%) to culture medium in fermentation cylinder and culturing to exponential phase; and filling sterile air into fermentation cylinder at 4-6 L/minute, stirring at 60-120 rpm, fermenting at 25-40 degrees C for 24-48 hours, separating or adsorbing, and drying in sterile environment.    USE - Method for preparing salt-resistant sewage-purifying microbial inoculum used for processing salt-containing wastewater or processing wastewater after using seawater (claimed).    ADVANTAGE - The microbial inoculum improves processing ability of salt-containing wastewater and has low cost.
NOVELTY - Production of an organic pollutant decaying agent comprises placing a solid culture medium in a culture container; sterilizing and inoculating white rot fungi to the culture medium; controlling temperature, humidity, pressure, and pH condition of the culture medium; adding (%) attapulgite (10-20), turves (20-50), and kaolin (10-20); and absorbing, air drying, and crushing.    USE - Method for the production of an organic pollutant decaying agent used as wastewater, sewage, and manure processing agent in papermaking factory, fabric factory, printing factory, food factory, and animal farm (claimed).
NOVELTY - The container has lining paper or cloth layer (14) that lines inner surface of box (12) with ventilation openings (10) for accommodating mixture of inoculum (18), aerobic bacterium and/or anaerobic bacterium, and organic refuse in microbial bed. A cover cloth (16) covers upper opening (12a) of box. The lining layer and cover cloth are made of material that do not allow of passage of insects e.g. fly. The box is in form of cage with mesh-shaped side and bottom walls, and handle (20) at its top periphery. Microbial bed consists of humus mixed with chaff or rice bran.    USE - Organic refuse compost container for use in home, store such as supermarket, and foodstuff factory.    ADVANTAGE - Since ventilation holes are provided in the box, fermentation of organic refuse can be performed with sufficient ventilation. Since the lining layer and cover do not let insects to pas through, the possibility of insects laying an egg in an inoculum can be prevented. The structure is simple, inexpensive and easily portable.    DESCRIPTION OF DRAWING(S) - The drawing shows the perspective view and top view of the organic refuse compost container.    Box (12)    Upper opening (12a)    Lining layer (14)    Cover cloth (16)    Inoculum (18)    Handle (20)
NOVELTY - A reforming unit generates a hydrogen-containing gas. A vaporization unit (8) has a deformed hollow spiral material (18) that is arranged in a spiral state in a space formed between an inner cylinder (9) and an outer cylinder (10). The vaporization unit supplies water to a spiral flow path (8A) surrounded by the inner cylinder, the outer cylinder and the hollow spiral material and evaporates water in a burner (2).    USE - Hydrogen generation apparatus for fuel cell system (claimed).    ADVANTAGE - Since the occurrence of clearance gap between the between the inner and the outer cylinder is prevented, the generation of carbon monoxide by the fall of hydrogen generative capacity and crack of catalyst are prevented. Thus the reliability of the apparatus is increased.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing method for hydrogen generation apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the hydrogen generating apparatus.    Burner (2)    Vaporization unit (8)    Spiral flow path (8A)    Inner cylinder (9)    Outer cylinder (10)    Hollow spiral material (18)
NOVELTY - A hydrogen generating apparatus has a fuel reformer (2) for reforming hydrocarbon fuel (8) to hydrogen rich gas (10) comprising hydrogen, carbon monoxide and unconverted fuel compounds, and a molten salt reactor (12) arranged in connection with the fuel reformer for supplying hydrogen rich gas from the reformer. The reactor carries out reaction of unconverted fuel compounds and/or carbon monoxide, and produces hydrogen rich gas (22) having less amount of carbon monoxide and/or unconverted fuel compounds with respect to hydrogen rich gas (10).    USE - Apparatus is used for generating hydrogen from hydrocarbon fuel, used for fuel cell e.g. molten carbonate fuel cell and solid oxide fuel cell in auxiliary power unit for providing electrical energy (all claimed) to vehicles e.g. car, truck, construction equipment, airplane, ship and boat.    ADVANTAGE - The apparatus easily enables to produce hydrogen from hydrocarbon fuel. The auxiliary power unit having the hydrogen generating apparatus efficiently enables to provide electrical energy.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) auxiliary power unit (1) for providing electric energy; and    (2) manufacture of hydrogen from hydrocarbon fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of apparatus for generating hydrogen from hydrocarbon fuel.    Auxiliary power unit (1)    Fuel reformer (2)    Hydrocarbon fuel (8)    Hydrogen rich gases (10,22)    Molten salt reactor (12)    Molten salt (20)
NOVELTY - Fuel injection system (1), for injecting hydrocarbon fuel into a fuel reformer generating hydrogen rich gas from the hydrocarbon fuel, where the fuel injection system (1) is adapted to inject a pulsating spray of hydrocarbon fuel into the fuel reformer.    USE - The fuel injection system (1) is used for injecting hydrocarbon fuel into a fuel reformer generating hydrogen rich gas from the hydrocarbon fuel (claimed).    ADVANTAGE - The present invention provides a cost efficient fuel injection system and method which provides an increased quality of the spray, but also provides an increased turn down ratio. It provides liquid hydrocarbon fuel, into a fuel reformer for generating a hydrogen rich gas from the hydrocarbon fuel, where the hydrocarbon fuel is sprayed into the fuel reformer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a fuel injection method for injecting hydrocarbon fuel into a fuel reformer for generating hydrogen rich gas from hydrocarbon fuel by injecting the liquid hydrocarbon fuel as at least one pulsating spray of hydrocarbon fuel into the fuel reformer.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a fuel injection system.    Fuel injection system (1)    Fuel injection element (2)    Fuel supply system (4, 6, 8)    Valve (10)    Fuel stream stopping element (12)    Gas accumulator (14)
NOVELTY - An apparatus for manufacturing methane and chemicals from sequestered carbon has an apparatus for providing a source of carbon, a primary processing chamber configured and arranged to receive water, carbon and a biomass, and a secondary processing chamber in fluid flow communication with the primary processing chamber. The biomass metabolizes at least a portion of the carbon to produce additional biomass. The secondary processing chamber carries out substantial anaerobic digestion of at least a portion of the biomass and produces methane as a digested product.    USE - Apparatus used for manufacturing methane and chemicals e.g. fermentation substrate, biopolymer, bioplastics, oil, pigment, fiber, protein, vitamin, fertilizer and animal feed (all claimed).    ADVANTAGE - The apparatus enables to produce methane and other chemicals with high productivity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) deep well bioreactor (100); and    (2) method for producing methane from carbon dioxide.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of deep well bioreactor.    Deep well bioreactor (100)    Carbon-sequestering biomass incubator (102)    Anaerobic digester (104)    Intermediate chamber (106)    Outer chamber (108)    Light source (124)
NOVELTY - A catalyst comprises nickel-aluminum intermetallic compound nanoparticle on the surface consists of nickel-aluminum system phase.    USE - Catalyst for producing hydrogen by steam reforming reaction of methane (claimed).    ADVANTAGE - The catalyst does not contain a noble metal or rare element, exhibits high efficiency in steam reforming reaction of methane at less than or equal to 600 degrees C and the conversion ratio of methane is near the value of methane equilibrium conversion in theory.
NOVELTY - A reformation processing unit generates reformed gas by reforming raw fuel and hydrogen gases. A combustion unit heats reformation processing unit. The reformation process is started after stopping combustion process if detected temperature of processing unit does not satisfy combustion confirmation conditions during initial stage. The combustion and reformation processes are stopped if temperature does not satisfy combustion conditions during reformation, and ventilation fans (57,58) for exhausting combustion gas from combustion unit are not in operation state.    USE - Hydrogen-containing-gas generation apparatus for fuel cell system comprising polymer type fuel cell, solid oxide type fuel cell and phosphoric acid type fuel cell.    ADVANTAGE - The discharging of the fuel gas and carbon monoxide gas having high concentration to outside can be prevented even if the combustion detection sensor is not provided in the combustion unit.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the hydrogen-containing-gas generation apparatus. (Drawing includes non-English language text)    Casing (54)    Inlet port (55)    Ventilation fans (57,58)    Fuel cell (G)    Fuel gas generation unit (P)
NOVELTY - A hydrogen production apparatus comprises reforming reaction part (6) which reforms liquid fuel and produces reformed gas, shift reaction part (7) which removes carbon monoxide contained in reformed gas from reforming reaction part by water-based shift reaction, and heat-exchange part (14) which adjusts temperature of reformed gas from reforming reaction part. The heat-exchange part is positioned between reforming reaction part and shift reaction part.    USE - A hydrogen production apparatus used for fuel cell system (claimed).    ADVANTAGE - The apparatus has improved temperature control capability and stable operability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of fuel cell system. (Drawing includes non-English language text).    Fuel cell system (1)    Reforming reaction part (6)    Shift reaction part (7)    Heat-exchange part (14)    Waste heat recovery water branch line (L6)
NOVELTY - A solid hydrogen fuel is manufactured by providing solid hydride powder(s) and solid catalyst(s) where the solid hydride powder reacts with water to bring a hydrogen releasing reaction to produce hydrogen and the solid catalyst catalyzes the hydrogen-releasing reaction; mixing the solid hydride powder and the solid catalyst; and forming the well-mixed solid hydride powder and the solid catalyst into a solid press-formed block.    USE - Method of manufacturing a solid hydrogen fuel (claimed).    ADVANTAGE - The method manufactures fuel that can release hydrogen completely at a short time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for solid hydrogen fuel.
NOVELTY - A solid fuel (1) is obtained by mixing paper sludge (in weight%) (30-50) and wooden waste material (70-50), adjusting water content in obtained mixture, mixing binder (0.7-0.9), and press-molding of resultant mixture.    USE - Solid fuel is used for domestic purpose, fireplace and heating stove.    ADVANTAGE - The solid fuel is economically manufactured using waste materials, without generation of environmental pollution. The solid fuel has excellent handleability and external appearance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of solid fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows perspective view of solid fuel.    Solid fuel (1)    Vertical V-shaped groove (2)    Horizontal V-shaped groove (3)    Through-hole (4)    Film (5)
NOVELTY - A fuel cell electric power generation system has desulfurizer (12) for desulfurizing biogas, modifier (2) for producing fuel gas containing hydrogen from desulfurized biogas, a fuel cell main portion (1), a cooling water circulation path, absorption-type water cooler-heater (6), and cooler (11). Path circulates cooling plate (1c) through battery cooling water which removes heat produced by power generation. The water cooler-heater uses exhaust heat of system as heat source. The cooler cools biogas with cold water produced by water cooler-heater and performs dehumidification.    USE - Fuel cell electric power generation system.    ADVANTAGE - The moisture content contained in biogas is efficiently cooled and condensed, and condensation of moisture content in biogas within fuel cell electric power generation system is reliably prevented.    DETAILED DESCRIPTION - A fuel cell electric power generation system has a desulfurizer for desulfurizing biogas, a modifier for producing fuel gas containing hydrogen from desulfurized biogas, a fuel cell main portion for performing power generation using fuel gas and air, a cooling water circulation path, absorption-type water cooler-heater, and cooler. The circulation path circulates cooling plate (1c) through battery cooling water which removes heat produced by power generation. The water cooler-heater uses exhaust heat of electric power generation system as heat source. The cooler carries out cooling of biogas with cold water produced by water cooler-heater and performs dehumidification.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of fuel cell electric power generation system. (Drawing includes non-English language text)    Fuel cell main portion (1)    Cooling plate (1c)    Modifier (2)    Absorption-type water cooler-heater (6)    Cooler (11)    Desulfurizer (12)
NOVELTY - The apparatus has casing (54) accommodating a hydrogen-containing-gas generation unit (P). A detector detects the operation state of ventilating fan (58). Hydrogen-containing-gas generation process and raw fuel gas charging process are not performed when the ventilating fan is not operated.    USE - Hydrogen-containing-gas generation apparatus for generating and supplying fuel gas to fuel cell of polymer type. Can also be used for solid oxide fuel cell, phosphoric acid fuel cell, etc.    ADVANTAGE - Avoids the retaining of raw fuel gas in inside of the casing, and the gas leakage.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the casing of hydrogen-containing-gas generation apparatus. (Drawing includes non-English language text)    Casing (54)    Exhaust port (56)    Ventilating fan (58)    Fuel cell (G)    Hydrogen-containing-gas generation unit (P)
NOVELTY - A hydrogen generating apparatus (1) has an ammonia storage container for storing ammonia, and a modifier (8) for producing fuel gas having hydrogen and nitrogen as main components by decomposing ammonia supplied from storage container. The storage container has honeycomb structure having several flow paths partitioned by a flow path wall supported with catalyst.    USE - Hydrogen generating apparatus is used for producing hydrogen used as fuel for fuel cell e.g. polymer electrolyte fuel cell.    ADVANTAGE - The hydrogen generating apparatus stably enables generation of hydrogen. The residual ammonia concentration is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of structure of hydrogen generating apparatus.    Hydrogen generating apparatus (1)    Ammonia cylinder (2)    Heat exchanger (6)    Flow meter (7)    Modifier (8)
NOVELTY - Hydrogen storage material powder is maintained as a storage material mixture with a surfactant. The storage material mixture is supplied to different reaction areas from the area where the storage material mixture is maintained during generation of hydrogen. The hydrogen storage material is hydrolyzed with coexistence of reaction water in the reaction area, and hydrogen is generated from the hydrogen storage material.    USE - Production of hydrogen used for fuel cell system.    ADVANTAGE - The method enables efficient production of hydrogen.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for hydrogen producing system (10).    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the hydrogen producing system. (Drawing includes non-English language text)    Hydrogen producing system (10)    Storage material supply tank (11)    Water recovery tank (13)    Reaction container (16)    Fuel cell system (20)
NOVELTY - A hydrogen gas generator (100) consists of a reaction tank (111), a reaction-water supplier (124) which supplies reaction water (2) to the reaction tank, a slurry tank (120A) which stores raw material slurry (1) obtained by mixing a water-miscible solvent which is non-reactive with respect to metal hydride, and metal hydride, and a raw-material-slurry supplier (118) which supplies the raw material slurry from the slurry tank to the reaction tank.    USE - Hydrogen gas generator is used in fuel-cell electric-power generation system (claimed).    ADVANTAGE - The hydrogen gas generator easily controls the generation amount of hydrogen. Emission of hydrogen gas from the raw material slurry is prevented even when the raw material slurry is stored for a long period of time. The metal hydride is reliably contacted with reaction water in the reaction tank. The hydrogen gas generator enables stable and reliable running of fuel-cell electric-power generation system.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel-cell electric-power generation system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the hydrogen gas generator. (Drawing includes non-English language text)    Raw material slurry (1)    Reaction water (2)    Hydrogen gas generator (100)    Reaction tank (111)    Raw-material-slurry supplier (118)    Slurry tank (120A)    Reaction-water supplier (124)
NOVELTY - A reducing agent is added to hot waste gas discharged from a metallurgical furnace. A reforming reaction is induced between carbon dioxide and the reducing agent which is added to the waste gas to reform the waste gas by adding water or 10 mole percent or less steam when the oxygen concentration in the waste gas is 1 volume percent or less. The reforming reaction is completed by the waste gas temperature exceeding 800 degrees Celsius.    USE - Reformation method for waste gas generated by metallurgical furnace, e.g., converter.    ADVANTAGE - Effective uses heat of hot waste gas discharged from metallurgical furnaces, e.g., converter. Achieves reduction of carburation of waste gas and amount of carbon dioxide emissions without causing generation or deposition of carbon or non-burning component. Uses mass-produced substance as reducing agent, fuel or chemical material, thus achieving economy. Non-fossil resource organic compounds such as bioethanol and biodiesel are used, thus further contributing to reduction in carbon dioxide emissions.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph illustrating the influence of steam mixed with reducing agent on the carbon dioxide conversion ratio and methane conversion ratio. (Drawing includes non-English language text).
NOVELTY - The apparatus (1) has a preliminary carbonization heat processing unit in which the precursor (4) is impregnated with resin and subjected to continuous preliminary carbonization processing. A high temperature carbonization heat processing unit is provided in which the precursor is subjected to high temperature carbonization in an inert atmosphere. Each of the heat processing units is provided with a precursor conveyance bar or roll (9) and a waste gas exhaust port (10). The exhaust port is arranged in downward direction at the lower surface of the precursor.    USE - Apparatus for continuous heat processing of porous carbon fiber sheet precursor used for manufacture of electrode for polymer electrolyte fuel cell.    ADVANTAGE - By arranging the exhaust port in downward direction at the lower surface of the precursor, the generation of precipitate in exhaust port periphery is suppressed and the fall of the precipitate on upper surface of the precursor can be prevented. Thus, appearance defects caused by fall of the precipitate can be avoided. By supporting the precursor with a conveyance roll or bar, the contact of the precursor with refuse collected at bottom portion of the heat processing apparatus can be avoided. Also, the damage of the precursor can be prevented and long term continuous operation of the apparatus is possible. High quality fiber sheet can be obtained and high productivity and yield can be ensured.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for continuous heat processing method of porous carbon fiber sheet precursor.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic longitudinal cross-sectional view of the apparatus for continuous heat processing of porous carbon fiber sheet precursor. (Drawing includes non-English language text)    Heat processing apparatus (1)    Precursor (4)    Conveyance bar or roll (9)    Exhaust port (10)    Shutter (11)
NOVELTY - Fuel comprises solid metal hydride; and aqueous solution comprising water, catalyst, and alcohol.    USE - The fuel is used for hydrogen-generating system (1) (claimed) for a small device, such as mobile phone. The hydrogen-generating system is used for supplying desired gas to micro fuel cell.    ADVANTAGE - When the first portion of the hydrogen-generating system is separated from the second portion, the reactants (14, 20) cannot be mixed to react with each other. The hydrogen-generating system can function regardless of how it is positioned, e.g. sideway, diagonal, or upside-down. The fuel exhibits improved hydrogen storage.    DESCRIPTION OF DRAWING(S) - The drawing is a cross-sectional view of gas-generating apparatus that is capable of supplying desired gas to micro fuel cell.    Hydrogen-generating system (1)    Cartridge (10)    Reactants (14, 20)    Reaction chamber (18)    Receiver (30)
NOVELTY - Absorbent comprises N-ethylethanolamine (10-50 wt.%), sulfolane (10-40 wt.%) and water.    USE - Absorbent used for absorbing and separating multiple gas mixtures including carbon dioxide from flue gas, refinery gas, natural gas, synthetic gas and hydrogen, and used in an absorption tower provided with a conventional decarbonization technology for desorption, flash evaporation, heat exchange and desorption, or a technology for extracting half barren liquid from desorption tower and extruding it into absorption tower after heat exchange, or multiple-absorption multiple-desorption technology, or a technology for absorbing sulfur dioxide, hydrogen sulfide and some organic sulfides such as carbonyl sulfide and methyl mercaptan in order to trap or separate carbon dioxide from gas mixture (all claimed).    ADVANTAGE - The absorbent has good desorption effect because it contains N-ethylethanolamine, which is suitable for solubilizing low pressure carbon dioxide, produces less heat during absorption reaction, and consumes less energy during carbon dioxide separation and desorption because sulfolane improves desorption and decreases water volatilization.
NOVELTY - The switch has shell equipped with a total air inlet, an oxygenation mixed outlet, and a lower air outlet. A cavity is internally equipped with an internal core composed of a straight rod and a hollow cylinder. One end of the straight pipe is connected to the hollow cylinder, and other end is connected to a handle. A wall of the hollow cylinder is equipped a through hole. An outer surface for a section of the hollow cylinder is equipped with a cambered groove. A shell of a position of the cambered groove is equipped with a position bolt.    USE - Multifunctional air inlet switch for a bio gasifier.    ADVANTAGE - The air inlet switch can be used for managing the airflow inlet/outlet of three air passages, so that air passages can be timely switched and the flux can be timely regulated, the blocking phenomenon of tar can be prevented, the material within the material chamber can be prevented from burning loss, the leakage of oil and gas can be prevented. The switch has simple structure, and effectively controls condition of the furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a multifunctional air inlet switch.
NOVELTY - The method involves pre-processing the organic solid waste, and accumulating the pre-processed material into strip piles. The sensors are arranged on strip piles, and the strip piles are covered by a waterproof ventilating film. The oxygen is supplied to pre-processed material by a fan and a ventilating pipe. The fermenting process is optimized by an intelligent ventilating control system. The material is decomposed, and the waterproof ventilating film is removed from strip pile. The processed material is conveyed to a material storing zone or a manufacturing zone.    USE - Aerobic fermenting method of organic solid waste.    ADVANTAGE - The aerobic fermenting process of organic solid waste is performed at high temperature in a short time, and at low cost, while reducing the emission of odor. The processed material is protected from damage caused due to external factors such as rain and wind.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram illustrating the aerobic fermenting process of organic solid waste.(Drawing includes non-English language text)
NOVELTY - A waste microwave cracking comprehensive treatment system comprises a municipal solid waste (MSW) pretreatment system A, a vertical waste continuous microwave heating and low temperature cracking furnace B, a system C for producing solid product, a system D for preparing fuel gas from cracking gas, and a system for distilling and extracting light oil and fuel oil from liquid product and a matched wastewater treatment system G.    USE - A waste microwave cracking comprehensive treatment system.    ADVANTAGE - The treatment system has low carbon discharge, no toxic substance such as solid carbon or dioxin discharge, and no heave metal solid powder. In the system, the treated wastewater can be recycled, and the waste can be utilized.    DETAILED DESCRIPTION - A waste microwave cracking comprehensive treatment system comprises an MSW pretreatment system A, a vertical waste continuous microwave heating and low temperature cracking furnace B, a system C for producing solid product, a system D for preparing fuel gas from cracking gas, and a system for distilling and extracting light oil and fuel oil from liquid product and a matched wastewater treatment system G. The MSW pretreatment system, the system for producing solid product, a system for preparing fuel gas from cracking gas are respectively connected with a first level feeder, a discharger, a cracking steam outlet of the vertical waste continuous microwave heating and low temperature cracking furnace. The system for distilling and extracting light oil and fuel oil from liquid product is connected with the oil pipeline of the system for preparing fuel gas from cracking gas.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram of a waste microwave cracking comprehensive treatment system.    MSW pretreatment system (A)    Cracking furnace (B)    System for producing solid product (C)    System for preparing fuel gas (D)    Waste treatment system (G)
NOVELTY - An alloy containing nickel, manganese, aluminum and cobalt is pulverized, the alloy powder is stirred in aqueous alkali solution, heated, and treated with alkali. The alkali-treated alloy powder is washed using water, the alkaline component is removed and dried, to obtain hydrogen occlusion alloy powder.    USE - Manufacture of hydrogen occlusion alloy powder for alkaline storage battery.    ADVANTAGE - The method efficiently provides hydrogen occlusion alloy powder with excellent electrode activity. The alkaline storage battery containing hydrogen occlusion alloy powder has excellent battery characteristics, output characteristics, durability and charging/discharging characteristics.    DETAILED DESCRIPTION - An alloy containing nickel, manganese, aluminum and cobalt is pulverized, the alloy powder is stirred in aqueous alkali solution, heated, and treated with alkali. The alkali-treated alloy powder is washed using water, the alkaline component is removed and dried, to obtain hydrogen occlusion alloy powder. The alloy is of compositional formula: MmNiaMnxAlyCoz, where a is 3.308-3.381, x is 0.387-0.389, y is 0.282-0.288 and z is 0.736-0.751, and Mm is mixture of cerium (40-50%), lanthanum (20-40%), praseodymium and neodymium.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic sectional view of alkaline storage battery.    Positive electrode plate (1)    Negative electrode plate (2)    Separator (6)    Upper collector (7)    Lower Collector (8)
NOVELTY - The wastewater is supplied to liquid-accumulating groove via discharge pipe. The organic liquid containing carbon, nitrogen and phosphorus is obtained by natural decomposition and precipitation, and supplied to reflowing sludge pump chamber. The active sludge and to-be-processed sludge are transferred to oxidizing ditch and organic substances are decomposed with microorganism by anaerobic-anoxic-oxic process. The mixture of sludge and water is supplied to secondary precipitating pool for separating sludge and water, and the clean water is discharged.    USE - Method for processing poultry effluent wastewater.    ADVANTAGE - The poultry effluent wastewater can be processed using simple technique at low cost. The generation of pollutants can be suppressed and the useful products can be obtained by processing the wastewater.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for device for processing poultry effluent wastewater.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the device for processing poultry effluent wastewater. (Drawing includes non-English language text)
NOVELTY - A biomass coke contains (in wt.%) biomass charcoal (20-50) and coal (35-80).    USE - Biomass coke.    ADVANTAGE - The biomass coke has high calorific value, and excellent strength and durability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biomass coke, which involves pulverizing biomass charcoal and coal, adding into carbonized furnace, compacting, heating at 900-1050 degrees C for 14-18 hours and quenching the refined coke.
NOVELTY - The methane generator has fermentation material acidification tank (2) which communicates with a fermenting tank (1) for the delivery of fermenting material into the fermenting tank. A floating cover (4) with a methane cavity (41) is set on the fermenting tank. The inner walls (12) of the fermenting tank are provided with floating cover guide mechanism (6). The outer walls of floating cover are provided with a limit mechanism (7). Multiple guide rails (111) are located at edges (11) of fermenting tank corresponding to position of limit mechanism.    USE - Floating cover type methane generator.    ADVANTAGE - The floating cover guide mechanism and the limit mechanism allow the floating cover to float on the opening of the fermenting tank and then it floats upwards as the methane pressure increases and vice-versa, without any danger such as explosion.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of the floating cover type methane generator.    Fermenting tank (1)    Fermentation material acidification tank (2)    Floating cover (4)    Methane outlet pipe (5)    Floating cover guide mechanism (6)    Limit mechanism (7)    Edges of fermenting tank (11)    Inner walls (12)    Methane cavity (41)    Guide rails (111)
NOVELTY - Agrochemical water dispersing granule comprises (in wt.%): cymoxanil and dimethomorph (30-75), dispersant (1-10), wetting agent (0.5-5), disintegrating agent (1-4), binding agent (1-4) and carrier, where the weight ratio of cymoxanil and dimethomorph is 2:0.5-9.    USE - Agrochemical water dispersing granule.    ADVANTAGE - The granule is less toxic, exhibits synergistic effect, does not cause environmental pollution and leaves fewer residues.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the agrochemical granule, which involves mixing dimethomorph, cymoxanil, dispersant, wetting agent, disintegrating agent and carrier in a mixer, kneading the ground materials with aqueous solution of binding agent (1.5-2.5%), granulating the kneaded materials, and drying the granules (0.5-5 mm).
NOVELTY - Pesticidal composition comprises (in wt.%): indoxacarb (0.2-10) and pyridaphethione (10-30).    USE - The pesticidal composition is useful for preventing and controlling Cnaphalocrocis medinalis.    ADVANTAGE - The compound exhibits broad insecticidal spectrum and controls C.medinalis rapidly. The composition is less toxic, and thus causes less harm to human and less environmental pollution. The composition is cost-effective, and co-toxicity coefficient with respect to C.medialis is 245-410.
NOVELTY - A mechanically dewatered residual active sludge is collected, and mixed with 20-50 weight% of waste organic acid mother liquid to obtain slurry. The obtained slurry is supplied to reaction tank, heated at 60-100 degrees C for 0.5-5 hours, enzymes are added to slurry and denatured. Then, reactant and vegetable filler are added to reaction tank and dried to obtain dry sludge having moisture content of 10-20 weight%.    USE - Method for dewatering residual active sludge used for agricultural fertilizer and fuel (claimed).    ADVANTAGE - The dewatering of residual active sludge is efficiently carried out.
NOVELTY - A sulfur-nitrogen fertilizer contains (in weight%) ammonium carbonate (60-90), ammonium sulfate (20-40) and calcium sulfate (20-30).    USE - Sulfur-nitrogen fertilizer.    ADVANTAGE - The sulfur-nitrogen fertilizer is manufactured economically. The fertilizer can neutralize excessive alkaline in soil and regulates acid-base balance in soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of sulfur-nitrogen fertilizer, which involves agitating ammonium carbonate, ammonium sulfate and calcium sulfate, adding aqueous ammonia, extruding and packaging.
NOVELTY - A dispersible metamifop liquor comprises (in weight%) metamifop (5-40), cosolvent (10-30), emulsifier (5-15) and remainder of methyl ester of vegetable oil.    USE - Dispersible metamifop liquor is used as herbicide in paddy field.    ADVANTAGE - The dispersible metamifop liquor is environmental friendly, and can be manufactured safely.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of dispersible metamifop liquor, which involves dissolving metamifop and emulsifier in solvent, and adding methyl ester of vegetable oil.
NOVELTY - The truck has waste sucking tank (2) arranged on a base plate (1) of compartment. An engine chamber (3) is arranged between base plate and waste sucking tank. A rail in engine chamber, is fitted with the base of chaff cutter (4) that moves in and out of the engine chamber along the rail.    USE - Methane tank waste sucking truck.    ADVANTAGE - The straw crushing efficiency can be improved and residue cleaning can be performed conveniently.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the methane tank waste sucking truck.    Base plate (1)    Waste sucking tank (2)    Engine chamber (3)    Chaff cutter (4)    Belt (13)
NOVELTY - Agent for providing cold resistance and protecting root of wheat, comprises (in wt.%): turpentine oil (15-55), wintergreen oil (0-55), and auxiliary agents. The auxiliary agents comprise Tween 60 (RTM: Polyoxyethylene sorbitan monostearate) (6-25), Eucalyptus globulus oil (0-5), gallic acid (0-5), glycerol (0-5), ethyl acetate (5-15), and UV absorber (2-(2'-hydroxy-5'-methylphenyl)benzotriazole (UV-P)) (0-5).    USE - The agent is useful for wheat for providing cold resistance, protecting root (claimed), and exhibiting bactericidal and insecticidal effect.    ADVANTAGE - The agent contains several bioactive components, exhibits excellent synergistic effect, does not cause environmental pollution, has low application frequency, and is cost-effective, prepared by a simple method and convenient to popularize. The agent is safe, as it does not cause toxic side effect.
NOVELTY - The device has a preparation tank connected with a heating device and a fermentation tank which is connected with heat exchange tank. A fermentation liquid pipe is installed above the preparation tank and connected with preparation tank. A biogas outlet is installed on the heat exchange tank.    USE - Anaerobic fermentation device for treating livestock manure and sewage in farms for producing biogas.    ADVANTAGE - The high rate of production of biogas is obtained in short duration and at low cost. The size of the anaerobic fermentation device is reduced, so that the installation area of device is reduced efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the anaerobic fermentation device.
NOVELTY - A biodiesel material is produced using oil obtained by extracting fruits of Dimocarpus.    USE - Biodiesel material.    ADVANTAGE - The biodiesel material is efficiently prepared without polluting the environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biodiesel material. A hopper-shaped black gauze is sleeved on the stem of Dimocarpus tree. The edges of the gauze are faced down in spring, summer and early autumn to cover the ground around the root. The edges are lifted up in late autumn to hold the naturally dropped fruits. The fruits are squeezed to produce oil.
NOVELTY - Biodiesel is provided by frequency conversion constant-current transportation, mixed with predetermined amount of alkali, and stirred. Then, crystal growth is carried out after predetermined time, and obtained crystals are subjected to aging and washing. The crystals are centrifugally separated from obtained solution, and resultant solution is dehydrated in vacuum.    USE - Deacidification of biodiesel.    ADVANTAGE - The method provides biodiesel having acid value of less than 0.8 mg potassium hydroxide/g.
NOVELTY - Method for treating wastewater obtained from ethanol distillation, involves inoculating microorganism, fermenting the inoculated strain and producing the fermented strain to obtain probiotics.    USE - The method is useful for treating wastewater using ethanol distillation and probiotics is used for breeding of animals (all claimed).    ADVANTAGE - The method is environment-friendly.
NOVELTY - Assessment of service value of artificial wetland ecosystem, involves combining economic method with energy systematic ecological method.    USE - The method is useful for assessing service value of artificial wetland ecosystem used for sewage treatment (claimed).    ADVANTAGE - The local resource and foreign resource investment can be distinguished based on features of the artificial wetland used for treating wastewater. The service value of the artificial wetland ecosystem can be assessed continuously and service value of the artificial wetland can be checked and calculated simultaneously.
NOVELTY - The device has air exposure device (5) that is connected with pneumatic column type photo-biotic reactor (3). The sewage water feeding device (1) is connected with the reactor through a mixing tank (2). A film separating device (6) is connected to the reactor. The algal concentration in the reactor is adjusted for obtaining concentrated algal liquid.    USE - Device for performing micro-algae sewage water treatment and production of biological oil.    ADVANTAGE - The nitrogen and phosphor removing effect from the water can be improved without complicated procedure so that biological oil production efficiency can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for performing micro-algae sewage water treatment and production of biological oil.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view explaining the process of performing micro-algae sewage water treatment and production of biological oil. (Drawing includes non-English language text)    Sewage water feeding device (1)    Mixing tank (2)    Pneumatic column type photo-biotic reactor (3)    Air exposure device (5)    Film separating device (6)
NOVELTY - An organic silicon fertilizer contains (in wt.%) oil shale powder raw material (60-70), superphosphate (10-15), potassium sulfate (10-15) and magnesium sulfate (5-10). The oil shale powder raw material contains oil shale (70), straw powder (14), medical stone powder (10), bran (5), saccharomycetes (0.6) and urea (0.4).    USE - Organic silicon fertilizer.    ADVANTAGE - The organic silicon fertilizer increases production and quality of agricultural products, and is environmental-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of organic silicon fertilizer. Oil shale is parched at 100-150 degrees C for 24 hours, and crushed to 100-200 mesh. The resulting product is filtered, and Saccharomycetes, straw powder, medical stone powder, bran and urea are added and fermented at 50-70 degrees C. The mixed powder is added to a cylinder parching machine after 7-8 days of fermentation. The temperature is maintained at 70-100 degrees C, and obtained oil shale powder raw material is mixed with superphosphate, potassium sulfate and magnesium sulfate. The mixture is granulated at rotating speed of 16-20 rpm. The molded granular fertilizer is dried, filtered and sealed to obtain finished-product.
NOVELTY - Preparation of straw briquettes fuel, involves cutting straw into sections of 1-10 cm length, subjecting cut straw to enzymolysis using cellulase after subjecting the straw to gas eruption or dilute acid pre-treatment, and compressing the straw after enzymolysis by mechanical extruding process to obtain solid fuel.    USE - The method is useful for preparing straw briquettes fuel used for biomass power generation and boiler combustion (claimed) e.g. domestic boiler.    ADVANTAGE - The fuel can be obtained easily by removing cellulose and hemicellulose in the straw. The method removes potassium ion, sodium ion and chloride ion in the straw, and thus ash fusion point of straw is improved, combustion and corrosion of boiler during cooking can be reduced, and combustion property of the straw is improved. The fuel has high lignin content.
NOVELTY - Method for improving acid production from sludge through anaerobic fermentation, involves obtaining sludge left from city waste water processing factory as raw material, breaking cellular wall of micro dust by ultrasonic wave such that large amount of organic substance inside the cell is dissolved, adjusting pH value of the sludge to alkalinity and enhancing dissolubility of sludge and preventing activity in producing methane bacteria during anaerobic fermentation such that the organic substance in the sludge is converted into volatile organic acid.    USE - The method is useful for improving acid production from sludge through anaerobic fermentation (claimed).    ADVANTAGE - The method enables environmental-friendly recycling of sludge and acid production with high yield.
NOVELTY - Bioorganic fertilizer comprises (in wt.%): urea (10-33), fermenting microorganism (5-20), organic material (20-45) and water (33-45).    USE - Bioorganic fertilizer.    ADVANTAGE - The bioorganic fertilizer has standard of NY884-2004 and high nitrogen content, prolongs fertilizer efficiency period of urea and improves use efficiency of urea. The bioorganic fertilizer reduces pollution to natural environment, and can be applied to AA grade agricultural products and organic agricultural products.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the bioorganic fertilizer, which involves obtaining the above-cited raw materials, adding the materials into container and then agitating uniformly, carrying out anaerobic fermentation for 15-180 days, drying or parching the fermented material (after a large amount of gas is generated and the weight of the ammonium nitrogen is detected to be less than 3%), adding Bacillus megaterium and Escherichia coli to the dried product and packaging the mixture. The quickly effective inorganic nitrogen contained in the chemical nitrogen fertilizer is converted to slow-releasing organic nitrogen by microbial anaerobic fermentation, where the conversion rate is 90%.
NOVELTY - A methanol gasoline comprises (in parts weight) methanol (15-25), isopropanol (5-10), isobutanol (5-10), acetone (2-6), mixed benzene (8-12), 5C component (8-12), light oil (15-25) and naphtha (20-25).    USE - Methanol gasoline is used for automobile.    ADVANTAGE - The methanol gasoline is economical, and has high power and caloric value. The automobile using methanol gasoline does not delaminate and has excellent stability in high temperature and low temperature. The oil consumption in the automobile is reduced using the gasoline.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of methanol gasoline. Isopropanol and isobutanol are mixed with methanol, to obtain mixed solution (A). The mixed benzene is mixed with acetone, to obtain mixed solution (B). The obtained mixed solution (A) is mixed with mixed solution (B), to obtain mixed solution (C). The light oil is uniformly-mixed with naphtha, to obtain mixed solution (D). The obtained mixed solution (C) is uniformly-mixed with mixed solution (D), to obtain methanol gasoline.
NOVELTY - An agrochemical antibiotic agent (A1) comprises (wt.%): carbonic ester (65), pulse flour (25), additive (8), and solvent (2).    USE - Agrochemical antibiotic agent (A1) in the form of liquid or powdery solid (claimed).    ADVANTAGE - The agent (A1) improves effect of agrochemical, reduces effective using amount by 3%, overcomes and delays drug fastness of harmful organism, and reduces environmental pollution by sticking, wetting, penetrating and film-forming effects of the agent (A1); has strong comprehensive function and low toxicity; and is free from public hazard, and has broad-spectrum.
NOVELTY - The system has a fuel cell line connected to a simulator (110). A power control system (130) operates a protection circuit, and an amplifier arrangement (120) amplifies model data output from the simulator and delivers the data to the power control system. The amplifier arrangement controls signal size corresponding to command toward driving of the protection circuit output from the power control system, where the model data includes information about ground fault accident, low voltage, overvoltage, harmonic generation, frequency and power factor of a fuel cell.    USE - Fuel battery evaluation system i.e. electro magnetic transient program restructured version (EMTP- RV) fuel battery evaluation system (claimed). Uses include but are not limited to a solar power generation facility, wind-driven electric plant, fuel cell generation facility and a distribution type power plant.    ADVANTAGE - The system improves quality of the fuel cell, and reduces the processing cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a fuel battery evaluation system.'(Drawing includes non-English language text)'    Simulator (110)    Fuel cell model (111)    Conspiracy part (112)    Amplifier arrangement (120)    Power control system (130)
NOVELTY - The biomass production system has a floating offshore plant that collects the marine biomass from marine farming area and generates biofuel from marine biomass. A biofuel carrier receives the biofuel from offshore plant and transports the biofuel to land. A biomass feeder supplies the collected biomass to the offshore plant.    USE - Biofuel production system.    ADVANTAGE - The biofuel can be produced efficiently and reliably using the marine biomass. The production efficiency of biofuel production system is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biofuel production method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biofuel production system. (Drawing includes non-English language text)
NOVELTY - Herbicidal composition comprises solution of acetic acid and surfactant.    USE - The composition is useful for killing weeds.    ADVANTAGE - The composition is non-toxic and does not cause environmental pollution.
NOVELTY - The reactor has a water inlet and a water outlet and reaction micro-organism. The 10-100% of the area of the wall of the reactor is made of flexible material. The remaining area of the wall of the reactor is made of rigid material. The 5-100% of the area of flexible material is made of filter cloth.    USE - Efficient flexible sewage treatment biochemical reactor.    ADVANTAGE - The reactor is easy to be made into a detachable, movable and retractable structure, and is convenient and the cost is low. The structure of reactor is simple. The need of a sedimentation tank is eliminated. The occupation area of the reactor is reduced and the processing speed is made fast. The electricity consumption and the operation cost are reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the sewage treatment biochemical reactor.
NOVELTY - The furnace has a body (1) divided into an oxygen supply burning area (2), a conversion gas generation area (3) and a material storage area (4). A wind supply device (6) is connected an air inlet through an air inlet pipe (5), where the wind supply device is connected with a main air supply pipe (10) through an oxygen supply tube (11). Air vents are arranged on a return sloped steel tube (9) that is provided in a direction of the main air supply pipe. The main air supply pipe is connected with a branch air supply pipe (18) via an air supply sloped tube (17).    USE - Biomass gasification furnace.    ADVANTAGE - The furnace can burn large and hard firewood, and can generate large amount of gas. The furnace has high working efficiency and little tar pollution, and is environment-friendly and pollution-free.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass gasification furnace.    Body (1)    Oxygen supply burning area (2)    Conversion gas generation area (3)    Material storage area (4)    Inlet pipe (5)    Wind supply device (6)    Return sloped steel tube (9)    Return sloped steel tube (10)    Oxygen supply tube (11)    Air supply sloped tube (17)    Branch air supply pipe (18)
NOVELTY - A residue obtained in the process of manufacturing sulfuric acid is sintered using pyrite. The pyritic sintered residue is milled into fine powder, and added into a dilute phosphoric acid storing tank. The viscosity of the material slurry is improved. The material is agitated using an agitator in the storing tank, and transferred into a neutralization reactor by a pump to react phosphoric acid with ammonia in the reactor. Then, the material slurry is neutralized, concentrated and dried, to obtain a monoammonium phosphate product which is prevented from caking.    USE - Method for preventing caking of ammonium phosphate.    ADVANTAGE - The ammonium phosphate is efficiently prevented from caking, without causing environmental pollution.    DETAILED DESCRIPTION - A residue obtained in the process of manufacturing sulfuric acid is sintered using pyrite. The pyritic sintered residue is milled into fine powder, and added into a dilute phosphoric acid storing tank. The dilute phosphoric acid is a raw material for manufacturing ammonium phosphate. The viscosity of the material slurry is improved. The material is agitated using an agitator in the storing tank, and transferred into a neutralization reactor by a pump to react phosphoric acid with ammonia in the reactor. Then, the material slurry is neutralized, concentrated and dried, to obtain a monoammonium phosphate product which is prevented from caking.
NOVELTY - A diol amine and benzaldehyde are cyclized into oxazole in a cyclic compound solvent, and the solvent is distilled to obtain timolol maleate intermediate. The molar ratio of the solvent to the diol amine is 1:2-6.5 and the molar ratio of diol amine to benzaldehyde is 0.2-0.4:0.91-1.82.    USE - Synthesis of timolol maleate intermediate.    ADVANTAGE - The timolol maleate intermediate of high quality is manufactured with high yield by a simple and environment-friendly process. The solvent can be recycled efficiently.
NOVELTY - Biomass pre-processing method, involves pulverizing biomass to powder, sterilizing the powder, cooling the sterilized material and then adding protease to the cooled material.    USE - The method is useful for pre-processing biomass (claimed) e.g. crop straw, grass, wood or fiber plant.    ADVANTAGE - The method is cost-effective and does not cause environmental pollution.
NOVELTY - An oxidizing pool is connected with mineralized garbage reacting bed for processing the percolate. An absorption and sedimentation tank is connected with the oxidizing pool. Activated carbon for absorbing precipitate from percolate is filled in absorption and sedimentation tank. Artificial wetland is connected with absorption and sedimentation tank for treating the percolate through biological method. A biological treating pool is connected with artificial wetland.    USE - Device for biological treatment of percolate of household garbage landfill.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the biological treatment device. (Drawing includes non-English language text)
NOVELTY - Method for producing coated product, involves heating coating material, dissolving the heated material in organic solvent to obtain coating solution, evenly mixing the coating solution with talc powder, spray coating the mixture on the surface of urea and then drying to obtain coated controlled release urea, where the organic solvent is dipentene.    USE - The method is useful for producing coated product (claimed).    ADVANTAGE - The coated product has stable quality and can be produced by a cost-effective process without causing environmental pollution. The coated product enables controlled release of urea.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for coated product, which is produced by above-mentioned method.
NOVELTY - Bismuth vanadate nano photoelectrode comprises a bismuth vanadate nano-pore film on a conducting substrate, where the bismuth vanadate is doped with a metal cation. The metal cation is strontium, barium, chromium, molybdenum and/or tungsten ion.    USE - The bismuth vanadate nano photoelectrode is useful for the decomposition of water (claimed).    ADVANTAGE - The bismuth vanadate nano photoelectrode increases photocurrent and greatly increases conversion quantum efficiency. The conversion quantum efficiency reaches 70% within 360-450 nm wavelength range, and photo response range is also widened to 510 nm.
NOVELTY - Method for removing food garbage, involves crushing the classified food garbage, adding auxiliary material for obtaining food garbage culture material, inoculating ovum of housefly into the culture, allowing the produced larva to eat the culture material for removing the food garbage.    USE - The method is useful for removing food garbage.    ADVANTAGE - The method is safe as the food garbage is treated using housefly maggots and reduces the capacity of municipal solid waste efficiently. The method is environmental-friendly. The biological protein and bio-organic fertilizer of housefly maggot can be recycled.
NOVELTY - Ecologically recycling kitchen waste, involves grinding organic materials from kitchen waste to obtain slurry, precipitating the organic materials and removing the moisture content to obtain nutrition mud, mixing soil with the nutrition mud to obtain culture medium, adding the culture medium into an earthworm breeding box, adding worm cast and earthworm to the culture medium, culturing the earthworm and recycling the earthworm and the worm cast.    USE - The method is useful for ecologically recycling kitchen waste to obtain earthworm as feed for tortoise and fish or as raw material for next recycling process, and to obtain worm cast as organic fertilizer for planting vegetables, fruits and flowers.    ADVANTAGE - The method does not produce secondary pollutants, saves energy, and is inexpensive.    DETAILED DESCRIPTION - Ecologically recycling kitchen waste, involves (a) sorting out the organic materials from the kitchen waste and grinding the organic materials in a grinder to obtain slurry, (b) precipitating the organic materials for a predetermined duration and then removing the moisture content for obtaining nutrition mud, (c) mixing soil to the nutrition mud to obtain culture medium, (d) adding the culture medium into an earthworm breeding box, (e) placing worm cast on the surface of the culture medium, adding earthworm in the culture medium and culturing the earthworm, (f) recycling the earthworm and the worm cast, (g) then using the earthworm as feed for tortoise and fish or as raw material for next recycling process, and (h) using the worm cast as organic fertilizer for planting vegetables and flowers.
NOVELTY - Preparing household fertilizer, involves decomposing food waste by earthworm, and converting the decomposed waste into fertilizer.    USE - The method is useful for preparing household fertilizer (claimed) and feed for livestock and poultry.    ADVANTAGE - The waste products can be recycled.
NOVELTY - Calcium and selenium-enriched fertilizer comprises medical stone, potash feldspar, diatomite, chicken manure, bone powder, oil cake of soybean, powder of fermentation bacteria, bone soup, urea, calcium superphosphate, potassium sulfate, inorganic salts including zinc sulfate, boron sulfate, copper sulfate and sodium selenite, and insecticidal agents including radix euphorbiae lantu, Sophora flavescens and tobacco stem.    USE - The calcium and selenium-enriched fertilizer is useful for preventing rice blast and improving soil. The products e.g. fruit obtained using the fertilizer are useful for improving immunity and promoting health.    ADVANTAGE - The residual pesticide of chemical fertilizer can be absorbed effectively. The produced farm and sideline products have no toxicity. The products are rich in beneficial trace elements, preferably calcium, iron, zinc and selenium.
NOVELTY - A catalyst contains metal oxide as carrier and noble metal as active component. The metal oxide and noble metal are used as catalyst for separation of oxygen. The noble metal is supported on carrier. The carrier contains nanoparticles of noble metal on its surface. The nanoparticles do not overlap with each other mutually. The catalyst has average aperture of 3-8 nm. The content of active component is 2-70 % mass.    USE - Catalyst is used as double effect oxygen electrode catalyst for integrated renewable fuel cell (both claimed).    ADVANTAGE - The catalyst has excellent catalytic activity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for application of catalyst.
NOVELTY - A carbon dioxide methanation catalyst comprises an aerogel oxide carrier on which nickel and an auxiliary agent as active component are loaded. The amount of active component is 5-40 wt.% based on metal element. The amount of auxiliary agent is 0.01-30 wt.% based on metal element. The auxiliary agent is chosen from lithium, sodium, potassium, beryllium, magnesium, calcium, strontium and barium. The aerogel oxide carrier is chosen from silicon dioxide aerogel, titanium dioxide aerogel, zirconium dioxide aerogel and alumina aerogel.    USE - Carbon dioxide methanation catalyst is used for preparation of methane by hydrogenation of carbon dioxide (claimed).    ADVANTAGE - The carbon dioxide methanation catalyst is easily and economically manufactured with improved catalytic activity and stability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of carbon dioxide methanation catalyst. A mixed salt solution of nickel and auxiliary agent in mass ratio of 1.5-30:1 is prepared. Then, the solution is soaked based on water absorbing capacity of the aerogel oxide carrier, stirred for 1-5 hours and stood for 0.5-12 hours. The solution is penetrated into the carrier, dried for 3-10 hours in an oven at 80-100 degrees C and further dried for 3-10 hours at 120-160 degrees C. The product is sintered for 3-5 hours in a muffle furnace at 400-550 degrees C under flowing air atmosphere with temperature raising velocity of 5-10 degrees C/minute. A reducing gas is supplied and reduced, to obtain the catalyst.
NOVELTY - Organic liquid fertilizer comprises (in parts weight) earthworm manure (6-10), myiasis manure (0-4), urea (1-3), monoammonium phosphate (2-4), potassium sulfate (2-4) and water (85-95).    USE - Organic liquid fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the above-cited organic liquid fertilizer, which involves (a) mixing (in parts weight) earthworm manure (containing 37.94% of water) (6-10) and myiasis manure (containing 37.84% of water) (0-4) with well water (50), stirring the mixture for 20 minutes at 1000 rotations per minute and at room temperature, then maintaining in still condition for predetermined duration and filtering the mixture using 100-mesh filter net, (b) washing the deposit using well water (50), combining the obtained solution and filtering the combined solution, (c) mixing urea (1-3), monoammonium phosphate (2-4) and potassium sulfate (2-4) with the filtrates obtained in step (a) and step (b), stirring the mixture for 10 minutes at 1000 rotations per minute and at room temperature, inoculating Lactobacillus acidophilus into the mixture (where the mass ratio of mixture and L.acidophilus is 9:1), and obtaining yellow colored organic liquid fertilizer, and (d) using the pH test paper to check pH of the liquid fertilizer, and sampling the liquid fertilizer to check effective viable count, where the pH of organic liquid fertilizer is 4-5, and the effective viable count is 1x 105-2x 106 cells.
NOVELTY - Microbial ecological conditioner is prepared by inoculating Bacillus megaterium into sterilized culture medium, culturing at 26-35 degrees C for 36-48 hours, inoculating B.subtilis into the culture, continuously culturing for 48 hours, inoculating Trichoderma viride into the culture, culturing for 48-144 hours, adding calcium carbonate or clay to the culture, adding absorbing agent to the culture, stacking and fermenting the mixture for 3-6 hours, and drying and condensing the culture to obtain product in the form of solid or powder.    USE - The microbial ecological conditioner is useful as biofertilizer and soil conditioner, and for amending constrained soil (all claimed).    DETAILED DESCRIPTION - Microbial ecological conditioner is prepared by maintaining the culture medium in culture container, sterilizing the culture medium, inoculating Bacillus megaterium (4-10% with respect to the weight of the culture medium) into the sterilized culture medium, culturing at 26-35 degrees C for 36-48 hours, inoculating B.subtilis (3-8% with respect to the weight of the culture medium) into the culture, continuously culturing for 48 hours, inoculating Trichoderma viride (0.5-6% with respect to the weight of the culture medium) into the culture, culturing for 48-144 hours, adding (in wt.%) carrier chosen from calcium carbonate (5-10) and clay (5-15) to the culture, adding absorbing agent (100-1000 times the weight of the culture medium) to the culture, mixing uniformly, stacking and fermenting the mixture for 3-6 hours, and drying and condensing the culture to obtain product in the form of solid or powder.
NOVELTY - An anti-slag additive is obtained by adding magnesium carbonate (15-25%, preferably 20% or 25%), alumina (20-30%, preferably 25% or 30%), and calcium carbonate (45-65%, preferably 55% or 45%) into a special dry container, uniformly mixing and adding anti-slag additive (1-5%, preferably 3.5% or 5%) to different biomass raw material. Also claimed is preparation of anti-slag additive.    USE - Anti-slag additive is used for biomass solid molded fuel.    ADVANTAGE - The anti-slag additive improves the burning efficiency of molded fuel, and reduces slag formation during burning of molded fuel.
NOVELTY - Coal-fried thermal power plant having coal storage bunkers containing coal is cooled by plenty of water. The coal, domestic waste and garbage leachate are mixed and processed in a ball mill at high temperature to produce fuel of boiler. Thus, treatment of waste material is enabled.    USE - Treatment of waste material.    ADVANTAGE - The waste material is efficiently treated and recycled.
NOVELTY - Method for producing bio-organic fertilizer, involves using (in parts weight) livestock excrement, straw or peat (40), drying and crushing the above material, inoculating strain (2) into the crushed material, fermenting the mixture under wet condition, mixing the fermented product with oil cake (20), phosphate fertilizer (20), growth promoter (8), fish meal (5) and potassium fertilizer (5), and pelleting the mixture.    USE - The method is useful for producing bio-organic fertilizer.    ADVANTAGE - The fertilizer is inexpensive and increases the yield and quality of plant products.
NOVELTY - Crushed straw is bagged in a plastic woven net bag and put into a marsh-gas pool, to produce marsh gas.    USE - Production of marsh gas.    ADVANTAGE - The method enables easy removal of residue, does not use any special de-slagging device, reduces production cost of marsh gas, and develops a new path for reuse of straw.
NOVELTY - Synthesis of metaflumizone, comprises: (i) synthesizing N-(4-(trifluoromethoxy)phenyl)acetamide (I) by reacting 4-trifluoromethoxy-phenylamine and ethyl chloroformate; (ii) synthesizing N-(4-(trifluoromethoxy)phenyl)hydrazinecarboxamide (II) by taking (I) and using hydrazine hydrate as a solvent, reacting for 8-10 hours at 60-100 degrees C, extracting with dichloromethane, adding active carbon, agitating at 70-80 degrees C, filtering and spin-drying; and (iii) synthesizing metaflumizone by reacting (II) with 4-(2-oxo-2-(3-trifluoromethyl-phenyl)-ethyl)-benzonitrile for 6-10 hours at 20-80?OC.    USE - Metaflumizone is used as an insecticide.    ADVANTAGE - The method is simple, economical, gives high yield and less side reactions. The reagents used are less toxic, thus does not corrode the equipment and pollute the environment. The solvents are recycled.
NOVELTY - Composition comprises (in kg): swollen straw (1 m3), bean or rapeseed cake powder (4-6), phosphorus fertilizer (5), nitrogen fertilizer (1) and water (150-200). The composition is obtained by preparing swollen straw which is prepared by mixing the straw in water by stirring until the straw gets swollen with water and moistening the swollen straw for 10-20 minutes, adding bean or rapeseed cake powder, phosphorus fertilizer and nitrogen fertilizer to the moistened straw and mixing the components to obtain the product.    USE - The composition is used for providing nutrients to soil and thus useful as fertilizer for promoting growth of flowers and plants, and for afforestation.    ADVANTAGE - The composition has excellent water retention effect as 1 m3 of swollen straw powder can absorb 250 kg of water without water loss, and enables fast growth of roots, strong seedling, flowering to take place for a long period of time and nutritional contents to be available for long period of time.
NOVELTY - Agent comprises phosphoric gypsum, zinc sulfate, copper sulfate, manganese sulfate, humic acid and borax in the weight ratio of 1000:2-8:0.3-3:0.5-5:1-10:0.5-8.    USE - The agent is useful as fertilizer for promoting growth of rapeseed.    ADVANTAGE - The agent improves quality of rapeseed, improves soil capacity, and recycles industrial waste residue of phosphoric gypsum, and thus prevents environmental pollution caused by phosphorus chemical waste phosphoric gypsum.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the agent, which involves separately grinding above-mentioned dried waste raw materials to 200-400 meshes, and mixing the powders.
NOVELTY - Composition comprises materials for composting chosen from water hyacinth, urban domestic sludge and kitchen garbage.    USE - The composition is used as raw material in composting method (claimed) for degrading the inorganic substance.    ADVANTAGE - The composting method has inorganic substance degradation rate of 40% or more. The pH value of the composition need not be adjusted as the components are stable and does not require controllable factor to further enhance the practicability, controllability and stability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for composting method, which involves using the above composition as raw material.
NOVELTY - A nitrous-acid-type-nitrification reaction sludge is manufactured by dominantly integrating ammonium oxidizing bacteria and acid treating activated sludge (12) containing ammonium oxidizing bacteria and nitrous-acid-oxidation bacterial so that pH may become less than or equal to 6.    USE - Manufacture of nitrous-acid-type-nitrification reaction sludge for wastewater treatment (claimed).    ADVANTAGE - The method has low energy cost and manufactures nitrous-acid-type-nitrification reaction sludge which can simply perform wastewater treatment over a long time.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) nitrous-acid-type-nitrification reaction sludge;    (2) manufacturing apparatus of nitrous-acid-type-nitrification reaction sludge;    (3) wastewater treatment; and    (4) wastewater-treatment apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the manufacturing apparatus of nitrous-acid-type-nitrification reaction sludge.    Reaction sludge manufacturing apparatus (10)    Activated sludge (12)    Acid treatment tank (14)    PH measurement machine (16)    Acid liquid tank (18)
NOVELTY - Liquefying a natural gas comprises processing 5-7 degrees C cold water by steam absorption using lithium bromide as absorbing agent; inputting the cold water to a pre-cooling heat exchanger to pre-cool natural gas, and mixing a pre-cooling agent out from a cooling agent compressor to 9-11 degrees C; recycling the cold water; inputting to a liquefying cold case; cooling the mixed cooling agent, and inputting to a cooling agent compressor.    USE - Method for liquefying a natural gas (claimed).
NOVELTY - Formulation of an anti-fouling coating system designed to be applied to submerged support, comprises at least 50 wt.% of an aqueous solvent-co-solvent system, at least 10 wt.% of a silicone resin based water repellent, and at least 15 wt.% of an non sticking active agent.    USE - The formulation is useful as an antifouling agent against adhering of marine organisms such as seaweed, shellfish and other crustaceans on any submerged support, including the ship hulls (claimed). No biological data given.    ADVANTAGE - The formulation is non-toxic, non-flammable, eco-friendly and inexpensive.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a process for treatment of support to be submerged with the formulation, where the formulation is applied in at least one layer by spray, roller or brush on the support to protect against marine fouling, after cleaning and prior drying the support, applied at an external temperature of 5-50 degrees C, preferably 15-30 degrees C, and then dried at room temperature for 25-40 minutes between two successive layers, and between 30-50 minutes before placing in water.
NOVELTY - Formulation of an anti-fouling coating system designed to be applied to submerged support, comprises at least 30 wt.% of water, at least 10 wt.% of a silicone resin based water repellent, and at least 15 wt.% of an non sticking active agent.    USE - The formulation is useful as an antifouling agent against adhering of marine organisms such as seaweed, shellfish and other crustaceans on any submerged support, including the ship hulls (claimed). No biological data given.    ADVANTAGE - The formulation is non-toxic, non-flammable, eco-friendly and inexpensive.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a process for treatment of support to be submerged with the formulation, where the formulation is applied in at least one layer by spray, roller or brush on the support to protect against marine fouling, after cleaning and prior drying the support, applied at an external temperature of 5-50 degrees C, preferably 15-30 degrees C, and then dried at room temperature for 25-40 minutes between two successive layers, and between 30-50 minutes before placing in water.
NOVELTY - Liquefying biomass comprises adding at least one microorganism of the type Clostridium sartagoformum, Paenibacillus macerans or Clostridium sporosphaeroides to the biomass substrate.    USE - The method is useful for liquefying biomass using individual microorganism of the type C. sartagoformum, P. macerans or C. sporosphaeroides, or a mixture of two or three of the above microorganisms. The liquefied biomass is useful for preparing biofuel (preferably bioethanol or biogas) (all claimed). The bioethanol is useful as fuel in combustion plants, or as fuel or fuel additive in engines to generate electricity and heat.    ADVANTAGE - The efficient method: significantly increases the liquefaction and significantly improves the effectiveness and efficiency of systems producing biofuel by using the above microorganisms; utilizes less energy; avoids the thickening of the substrate and the further addition of biomass-liquid substrate in the form of water during liquefaction to maintain stable process; conserves freshwater resources; has significantly increased loading rate and improved process stability; does not cause acidification; and does not deteriorate the methane content of the biogas.
NOVELTY - Producing biodiesel by catalyzing with free enzyme comprises: (a) mixing the free lipase and additive at 1:1-2; (b) synthesizing short chain fatty acid; and (c) stopping to stir after the reaction, standing the reaction solution for 15minutes, removing the oil phase (biodiesel) on the upper layer after the oil and water in the reaction solution are separated and adding the stock oil again.    USE - The method is useful for producing biodiesel by catalyzing with free enzyme (claimed).    ADVANTAGE - The method is of low cost, has high conversion rate, has simple operation, and a stable production.    DETAILED DESCRIPTION - Producing biodiesel by catalyzing with free enzyme comprises: (a) mixing the free lipase and additive at 1:1-2; (b) synthesizing short chain fatty acid: adding stock oil to a reactor, preheating to 35-45 degrees C, putting into a catalyst based on 0.25-0.4wt.% (enzyme/oil), feeding 2-8wt.% water by weight of the stock oil, mixing, adding short chain alcohol for multiple times or once and reacting for 20-32hours at 35-50 degrees C; and (c) stopping to stir after the reaction, standing the reaction solution for 15minutes, removing the oil phase (biodiesel) on the upper layer after the oil and water in the reaction solution are separated and adding the stock oil again.
NOVELTY - Producing methanol by oxygenated hydrocarbon reforming, comprises contacting the oxygenated hydrocarbon and water with a group VIIIB catalyst at a reaction temperature of at least 380 degrees C, to yield methanol.    USE - The method is useful for producing methanol (claimed), which is useful in the production of biodiesel.    ADVANTAGE - The oxygenated hydrocarbon is derived from biomass (renewable source), which is a by-product of biodiesel production, thus the method provides methanol in economic, environmental and energy efficiency manner. The method: provides a direct and efficient route to methanol production by avoiding the step of methanol synthesis from hydrogen and carbon monoxide; provides high levels of conversion and selectivity for methanol; provides clean alternatives to the use of fossil fuels as a source for vehicle fuel; and functions comparatively at low temperatures and pressure.    DESCRIPTION OF DRAWING(S) - The figure shows the schematic representation of the apparatus used to demonstrate the direct synthesis of methanol from glycerol.    Tubular reactor system (2)    Pre-heating zone (4)    Reaction zone (6)    Heater (7)    Liquid supply line (8)
NOVELTY - The apparatus has evaporator that evaporates water fed from water fed device and generates steam. A modifier has a modification catalyst that generates hydrogen containing gas in a reforming reaction using raw material and steam. A valve connects or interrupts modifier and air in downstream gas path of modifier. The raw material is supplied from a material supply device when the valve is opened and when the supply of water is stopped. The supply of raw material is stopped when the valve is closed before the inside of the modifier is purged by the starting material.    USE - Hydrogen generating apparatus used in fuel cell system.    ADVANTAGE - The apparatus avoids deterioration of modification catalyst by steam oxidation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for operating hydrogen generating apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart explaining the process for operating hydrogen generating apparatus (Drawing includes non-English language text).
NOVELTY - A process (P1) for preparing a salt (S1) of the (R)- or (S)-isomer of 1-naphthylethylamine with mandelic acid, involves reacting racemic 1-naphthylethylamine with mandelic acid to obtain the (R)- or (S)-isomer of 1-naphthylethylamine salt with the acid.    USE - For preparing a salt of (R)- or (S)-isomer of 1-naphthylethylamine with mandelic acid; for preparing cinacalcet or its salt (claimed); and in the manufacture of a medicament for treating hyperparathyroidism.    ADVANTAGE - The process is a simple and industrially-scaleable process which prepares cinacalcet that does not generate impurities. The cinacalcet is simple, avoids generation of impurities, is easy to scale up, and is safe to handle. The process avoids the use of any organic solvents for the reaction which makes the process environmentally friendly. The resolution process is highly advantageous as it is simple and affords the product in high purity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a salt (S1) of the (R)- or (S)-isomer of 1-naphthylethylamine with mandelic acid;    (2) a process (P2) for preparing cinacalcet (I) and/or its salt, involving reacting an ester (II) with a salt of mandelic acid with (R)-1-naphthylethylamine, to obtain cinacalcet, and optionally converting the cinacalcet to a salt; and    (3) a process (P3) involving: (i) preparing a salt of (R)-naphthylethylamine with mandelic acid and obtaining a mother liquor enriched in (S)-naphthylethylamine; (ii) converting (S)-naphthylethylamine to racemic naphthylethylamine; and (iii) if desired, using racemic (S)-naphthylethylamine obtained from step (ii) in a process (P1).
NOVELTY - Recycling and exploitation of biodegradable domestic waste produced in the dwellings of a community, by means of prefabricated biogas-production plants, in order to produce electricity and fertilizer and to heat water, comprises grinding waste in a grinder provided in the kitchen sinks; and conveying by means of a network separate from the sewage network, to a biogas-production plant formed by digesters, where biogas is produced by means of anaerobic digestion.    USE - The method is useful for recycling and exploitation of biodegradable domestic waste produced in the dwellings of a community, by means of prefabricated biogas-production plants, for producing electricity and fertilizer and to heat water, where the generated electricity is introduced back into the system; and where the hot water is useful in building (all claimed).    DETAILED DESCRIPTION - Recycling and exploitation of biodegradable domestic waste produced in the dwellings of a community, by means of prefabricated biogas-production plants, in order to produce electricity and fertilizer and to heat water, comprises grinding waste in a grinder provided in the kitchen sinks; and conveying by means of a network separate from the sewage network, to a biogas-production plant formed by digesters, where biogas is produced by means of anaerobic digestion, where the method uses safety and control mechanisms, a biogas consumer, a biogas reservoir and a place where the inert material resulting from biodigestion can be deposited.
NOVELTY - Method for processing glycerin (reaction product obtained during production of biodiesel fuel using vegetable oil and primary alcohol as raw material) by produced with alkyl ester of fatty acid by alkali catalyst method, involves fermenting mixture containing glycerin with surplus sludge using anaerobic fermentation microbe plexus to obtain decomposition product.    USE - The method is useful for processing glycerin for producing decomposition product chosen from hydrogen, 1,3-propanediol (claimed) and organic acid.    ADVANTAGE - The glycerin can be processed easily into industrially useful decomposition products, using less amount of surplus sludge without addition of waste material containing solid substance.
NOVELTY - Material for processing organic substance, comprises microorganisms capable of fermenting at 70-120 degrees C, and facultative anaerobic microorganisms.    USE - The material is useful for processing organic substance (claimed) from dairy industries, livestock excrement, food processing residues, foodstuff sludge, agricultural residues, gardening or forestry, lumber industry and sewage sludge, and is useful in sewage disposal.    ADVANTAGE - The method processes organic substance in a short period of time, and suppresses the production of odor.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for processing organic substance; and    (2) apparatus for processing organic substance.
NOVELTY - Carrier comprises microorganisms capable of performing methane fermentation immobilized on the surface of the carrier, where the surface of the carrier is positively charged.    USE - The carrier is useful for immobilizing microorganism capable of performing fermenting methane and in apparatus for performing methane fermentation (claimed).    ADVANTAGE - The carrier improves the methane fermentation rate.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) methane fermentation apparatus; and    (2) method for producing the carrier.
NOVELTY - Cultivation of tea plant, involves applying granular fertilizer once in two or more years from upper portion of plant such that 80% or more fertilizer is distributed under tree crown. The granular fertilizer is chosen from coated granular fertilizer composition and/or chemosynthetic slow release nitrogen fertilizer. The elution rate or mineralization rate of nitrogen component after 3 days is less than or equal to 10%. The 80% of elution and mineralization is observed in 40-250 days.    USE - Cultivation of tea plants and other perennial crops.    ADVANTAGE - The method reduces labor used for applying fertilizer to plants, and increases yield of perennial crops by raising the fertilizing effect. The method has reduced environmental effects as it uses reduced amount of fertilizer. The method provides the fertilizer to the plants required for a year in single process, thus overcomes the inconvenience of customers in applying fertilizers.
NOVELTY - A wastewater treatment system has an aerator for accommodating water, gas-flowing water permeable container having filter medium adhered with aerobic microbe, and an aeration device for supplying air to wastewater in aerator. The filter medium is obtained using several granular active carbons and capable of adsorbing organic substance. Inoculum solution containing microorganisms and nutrient capable of promoting proliferation of microorganism are injected (102) to aerator. Organic substance in wastewater is decomposed and biofilm is formed on surface of activated carbon.    USE - Wastewater treatment system installed in nuclear power station, conversion plant, enrichment plant, reprocessing plant, and nuclear laboratory. Uses include but are not limited to wastewater discharged during washing equipment, clothes, kitchen and bathroom.    ADVANTAGE - The wastewater treatment system quickly enables treatment of wastewater.    DETAILED DESCRIPTION - A wastewater treatment system has an aerator for accommodating water, gas-flowing water permeable container having filter medium adhered with aerobic microbe, and an aeration device for supplying air to wastewater in aerator. The filter medium is obtained using several granular active carbons having average particle diameter of 1.3-2 mm and capable of adsorbing organic substance. Inoculum solution containing microorganisms (107-1010/ml) and nutrient capable of promoting proliferation of microorganisms are injected (102) to aerator. Organic substance in wastewater is decomposed and biofilm is formed on surface of activated carbon.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of wastewater treatment system. (Drawing includes non-English language text)    Wastewater receiving tank (1)    Filter (2)    Wastewater pipe (3)    Film apparatus (49)    Microbial culture process (102)
NOVELTY - The method involves supplying sludge (6) obtained after treatment of to-be-processed water using biological treatment system into a fish breeding tank (8). The surplus sludge generated in organic material treatment tank (4) is supplied to another organic material treatment tank (2). The sludge produced in the organic material treatment tank (2) is guided to fish breeding tank. Effluent solution (5) is supplied to the organic material treatment tank (4).    USE - Biological treatment method of to-be-processed water such as sewage water, industrial wastewater and polluted river water.    ADVANTAGE - The amount of disposal sludge obtained after the treatment of to-be-processed water can be reduced reliably, by using the sludge as feed for fishes in fish breeding tank. The need for providing special energy source in biological treatment apparatus is eliminated, so that size and installation space of biological treatment apparatus are reduced. The breeding of fishes can be increased.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biological treatment apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the biological treatment apparatus.    To-be-processed water (1)    Organic material treatment tanks (2,4)    Effluent solution (5)    Sludge (6)    Fish breeding tank (8)
NOVELTY - A measuring apparatus (20) measures the parameter of aerobic treatment in the membrane separation tank (4) which separates to-be-processed water into solid and liquid. A controller (21) adjusts the circulation load of the to-be-processed water through the circulating circuit (8) based on the measured value.    USE - Sewage treatment unit.    ADVANTAGE - Dissolved oxygen rate of membrane separation tank is maintained at appropriate value so that generation of causative agent of film fouling can be suppressed. Denitrification reaction and phosphorus discharge reaction can be maintained in favorable state within the anaerobic tank.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for operating method of sewage treatment unit.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the sewage treatment unit. (Drawing includes non-English language text)    Aerobic tank (3)    Membrane separation tank (4)    Circulating circuit (8)    Measuring apparatus (20)    Controller (21)
NOVELTY - The method involves collecting pyrolysis gas from a piping (12) with cool water in a collection tube (2). Tar in the collected pyrolysis gas is collected by a cooling collection part and melts collection according to an organic solvent, where the cooling collection is performed at 30 degrees celcius. The tar remaining in the pyrolysis gas is collected by a backup filter (6).    USE - Method for collecting tar in pyrolysis gas that is generated by a sewage-sludge carbonization installation and a biomass fuel carbonization installation.    ADVANTAGE - The method enables eliminating need to perform dust removal and heating of dust operations, so that obstruction by adhesion and generation of carbide material are suppressed even in a high concentration tar atmosphere, thus ensuring appropriate tar collection process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a tar collection apparatus comprising a collector.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a collection apparatus of tar. '(Drawing includes non-English language text)'    Tar collection apparatus (1)    Collection tube (2)    Backup filter (6)    Pump (8)    Piping (12)
NOVELTY - A disinfestation composition comprises (wt.%) fipronil (0.5-20), spinosad (4-20), and additive (balance) to prepare particulate agent.    USE - A disinfestation composition for preventing lepidoptera, homoptera, thysanoptera or Chilo suppressalis (claimed)    ADVANTAGE - The composition can delay generation of resistance to drugs, and reduces pollution on environment.
NOVELTY - A mixed chemical comprises (pts.wt.) diniconazole (1-10), carbendazim (1-10), high-fat containing membrane (1-20), and water (500-24000).    USE - A mixed chemical for preventing or treating groundnut early leaf spot (claimed).    ADVANTAGE - The mixed chemical can prevent groundnut early leaf spot and inhibit groundnut from overgrowth thus improving production yield, requires less usage and fewer application, produces less pollutant thus protecting the environment, and can protect the plant physically.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of mixed chemical comprising mixing diniconazole and carbendazim, and adding water to the mixture at a mass ratio of 500-600:1.
NOVELTY - The system has a pressurizing pump (1) comprising gas feeding hole that is connected with main gas feeding pipe (5). The gas discharge hole of the pressurizing pump is connected with gas feeding hole of absorbing tower (3) through a valve (41). The gas discharge hole of the absorbing tower is connected with main gas discharge pipe (6) through a valve (42). The gas discharge end of the absorbing tower is provided with a bypass valve (8) connected with the gas feeding hole of vacuum pump (2) through a valve (43).    USE - Methane recycling system for use in coal mine.    ADVANTAGE - The concentration of methane in the recycled gas can be improved, while ensuring the recycling efficiency of methane and improving the eco-friendly effect of the recycling system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the methane recycling system for use in coal mine.    Pressurizing pump (1)    Vacuum pump (2)    Absorbing tower (3)    Main gas feeding pipe (5)    Main gas discharge pipe (6)    Bypass valve (8)    Valves (41-43)
NOVELTY - A naturally degraded disposable excrement collecting device comprises hinge, barrel body having a powdered drier for mixing with excrement and absorbing excrement water, a barrel cover having a side that is movably connected with one side of the opening of the barrel body via a hinge, and buckle installed on the other side of the barrel cover and the other side of the opening of the barrel body.    USE - A naturally degraded disposable excrement collecting device for killing eelworm (claimed).    ADVANTAGE - The device reduces water pollution, saves energy, can act as biological organic strainer, and reduces polluted liquid discharge.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of naturally degraded disposable excrement collecting device.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a naturally degraded disposable excrement collecting device.
NOVELTY - Production of biodiesel comprises adding dewatered raw material oil and composite catalyst in catalytic cracking reactor; heating raw material oil under the action of composite catalyst with heat conducting oil as heating medium to produce biodiesel; filling deodorizing agent in distillation column to process deodorization; and recycling generated rich gas (noncondensable gas) as fuel.    USE - Method for production of biodiesel (claimed) used as fuel.    ADVANTAGE - The biodiesel is sulfur-free; has good ignitability, high cetane number, and little colloid; and can be directly used on tractors. The burning tail gas is pollution-free and completely meets with environmental protection requirements. The rich gas completely recycled as fuel to save energy and eliminate pollution.
NOVELTY - A catalyst consists of porous carrier supported with active metal. The carrier has bimodal structure and contains pores with diameter of 2-10 nm and 20-200 nm, and contains zirconium.    USE - Catalyst used for manufacturing hydrogen from hydrocarbon or hydrocarbon containing oxygen e.g. vegetable oils and fats such as rapeseed oil, sesame oil and sunflower oil (all claimed). The hydrogen produced is used in fuel cell for motor vehicles, non-commercial use and commercial use.    ADVANTAGE - The catalyst has excellent durability, modification activity and enables to manufacture hydrogen efficiently even from vegetable oils and fats.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of hydrogen, which involves contacting hydrocarbon or hydrocarbon containing oxygen with the catalyst.
NOVELTY - Natural fermentation of organic substance-containing wood chip.    USE - Natural fermentation of organic substance-containing wood chip useful for producing fertilizer.    ADVANTAGE - The fertilizer does not produce offensive odor, exert bad influence to environment and cause water pollution. The fertilizer can be produced cost-effectively in large quantities.
NOVELTY - The furnace has a pipe (5) whose lower side is provided with an ash collecting chamber (6), where the pipe is made of refractory material bricks. The pipe and a body heat insulating layer (1) are arranged for forming a secondary air supplying chamber (8). A lower side of a body (2) is provided with an air box (9). An air outlet of the air box is connected with the secondary air supplying chamber. An inner part of the ash collecting chamber is provided with a pulling type ash collecting hopper that is matched with the ash collecting chamber.    USE - Coal-firewood dual-purpose biomass gasification furnace.    ADVANTAGE - The furnace has wide range of applications, simple structure and convenient usage, and can conveniently adjust primary air supplying amount and secondary air supplying amount. Combustion can achieve better effect through rational upper and lower air inlet ratio. The furnace can effectively utilize residual heat of waste gas in smoke channel.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a coal-firewood dual-purpose biomass gasification furnace in partial section.    Body heat insulating layer (1)    Body (2)    Pipe (5)    Ash collecting chamber (6)    Secondary air supplying chamber (8)    Air box (9)
NOVELTY - The boiler has a wind pipe provided with a primary wind pipe and a secondary wind pipe. A wind layout pipe is equipped with primary wind ports and secondary wind ports. The primary wind ports are provided with straight wind port units and inclined wind port units located at lower part and middle part of the wind layout plate, respectively. Projections formed on the straight wind port units are positioned parallel to a central axis of the boiler. Shape and distribution of the inclining wind port units match with that of the secondary wind port units.    USE - Biomass gasification and combustion boiler.    ADVANTAGE - The boiler is environment friendly, and reduces labor intensity of a worker and improves working environment. The boiler enables biomass fuel to generate fuel gas such as carbon monoxide, propane and methane by utilizing fluidized combustion principle and heat energy reaction.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a biomass gasification and combustion boiler.
NOVELTY - The furnace has an ingle tray (4) whose one side is connected with an assisting shell (7). An upper water jacket (8) coated outside a flue is arranged at an inner-upper part of the shell and at a side of the ingle tray. Periphery of an internal furnace (2) is equipped with a lower water jacket (9). Periphery of the upper water jacket is mounted with a heat insulating layer (10). The upper water jacket and the lower water jacket are interconnected by a pipeline (11). The upper water jacket is opened with a water inlet (12). The lower water jacket is opened with a water outlet (13).    USE - Biomass gasification furnace for cooking.    ADVANTAGE - The furnace has strong fire power for cooking rapidly and heating an area of 60 to 100 square meters, so as to satisfy the needs of people for heat supply in winter. The furnace has improved integral appearance, and stable and better heating effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a biomass gasification furnace.    Internal furnace (2)    Ingle tray (4)    Assisting shell (7)    Upper water jacket (8)    Lower water jacket (9)    Heat insulating layer (10)    Pipeline (11)    Water inlet (12)    Water outlet (13)
NOVELTY - The furnace has a gas supply machine core arranged in a fuel cabin. A top end of the machine core is formed as a mushroom cap head that is equipped with a set of uniform small holes. A bottom part of the machine core is provided with a set of right-angled air suction pipes. An upper part of the machine core is provided with an isolating layer. An upper part of the fuel cabin is provided with an annular water tank.    USE - Straw gasification furnace for use in a village.    ADVANTAGE - The furnace has large and uniform air spray area and high thermal efficiency. The right-angled air suction pipe sucks the waste air and ensures a quick burning of the fuel. The furnace is simple in structure, inexpensive, and can generate gas quickly. The furnace avoids smoke, and can easily burn the thick straw. The furnace has better market value.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a straw gasification furnace.
NOVELTY - A fuel is obtained by providing 35% of shattered coal and 35% of shattered municipal solid waste in a container to mix and mold.    USE - Fuel is used for power plant.    ADVANTAGE - The fuel reduces pollution to environment of sludge produced by municipal solid waste and sewage disposal plant.
NOVELTY - A nitro-bacterium microbial inoculum comprises nitro-bacterium and nitroso-bacterium with weight ratio at 1:1-10:1.    USE - A nitro-bacterium microbial inoculum used for converting ammonia-nitrogen into nitro-nitrogen (claimed), and processing wastewater.    ADVANTAGE - The inoculum provides excellent wastewater treatment effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of preparing nitro-bacterium microbial inoculum by culturing, screening, and acclimatizing processed nitro-bacterium and nitroso-bacterium under aerobic condition; inoculating active sludge into nitro-bacterium enriching culture medium and nitroso-bacterium enriching culture medium, and culturing for 3-7 days at 28-38 degrees C under 120-180 rpm; taking 1-5 ml nitro-bacterium and nitroso-bacterium enriching culture solutions respectively, inoculating, and culturing for 7-15 days at 28-38 degrees C; and inoculating obtained strains, and culturing.
NOVELTY - The furnace has a gas conveying chamber (16) connected with a gasification chamber (18) by a leakage hole of a grate (14). A top of the conveying chamber is connected with a purifying chamber (4) by a gas guide pipe (1) provided with a fresh air port (2) with a control valve. The purifying chamber is connected with another purifying chamber (11) by a top gas guide pipe (6) and a bottom U-shaped pipe (20). The latter purifying chamber is connected with a stove head (10) with a gas valve via a conveying pipeline and connected with the gasification chamber via a bottom U-shaped return pipe (9).    USE - Pollution-free biomass gasification furnace.    ADVANTAGE - The furnace has high gas converting efficiency and no tar smell. The pressures at the inside and outside of the furnace body are balanced relatively, so as to avoid safety hidden hazard. The furnace is rational in design, has simple operation, and realizes programmable running. The furnace prevents requirement of heat source fuel for the village, mountain and pasturing area cooking, heating, steam, plantation plant, farm and processing factory.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a pollution-free biomass gasification furnace.    Gas guide pipe (1)    Fresh air port (2)    Purifying chambers (4, 11)    Top gas guide pipe (6)    Bottom U-shaped return pipe (9)    Stove head (10)    Grate (14)    Gas conveying chamber (16)    Gasification chamber (18)    Bottom U-shaped pipe (20)
NOVELTY - A hydrocarbon refrigerant comprises (in weight%) dimethylmethane (90-96), isobutane (2-7), alcohol ester (1.5-2.8) and ethanol (0.2-0.5).    USE - Hydrocarbon refrigerant.    ADVANTAGE - The hydrocarbon refrigerant has excellent stability and efficiency, and is economical, safe and environmental friendly.
NOVELTY - A bioactivator comprises (in parts weight) cyclopentadienyl (52-62), pentaerythritol (40-50), agar-agar (10-20), sodium dodecyl benzene sulfonate (7-15), biological saponin paste (60-70), oil component (45-55), organic solvent (70), water (250-350) and cellulose-decomposed bacteria (reduced amount).    USE - Bioactivator.    ADVANTAGE - The method efficiently produces bioactivator without causing environmental pollution, and reduces discharge of hydrosulfide. The bioactivator has excellent corrosion resistance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of bioactivator, which involves adding agar-agar into clear water in reactor, stir-dissolving, heating to 110 degrees C, controlling the temperature to 65-75 degrees C, stirring at low speed, adding saponin paste solution, stirring, adding pentaerythritol, controlling the temperature to 75-85 degrees C, adding cyclopentadienyl, organic solvent and sodium dodecyl benzene sulfonate, stirring, cooling to 25-35 degrees C, adding cellulose-decomposed bacteria, and stirring at low speed for 3-6 hours.
NOVELTY - An energy-conservative additive comprises (in parts weight) cellulose-decomposed bacterial solution (75-85), ammonium perchlorate emulsion (10-15) and reinforcing agent (5-15).    USE - Energy-conservative additive is used for aqueous coal slurry used for coal-tar packaging material.    ADVANTAGE - The aqueous coal slurry containing energy-conservative additive has excellent stability, flowability and combustion efficiency.
NOVELTY - Preparation of high-F pig blood oligopeptide comprises: (i) anticoagulation of pig blood; (ii) hydrolyzing blood protein by alkaline protease (0.35-0.45 g/100ml) at 45-55 degrees C for 6-8 hours at pH 10-12; (iii) hydrolyzing by protease (0.35-0.50 g/100 ml) at 45-47 degrees C for 5-7 hours at pH 10-12; (iv) processing with active carbon for 2-4 hours to increase F value, where the ratio of carbon to solution is 1:8-15 at 40-50 degrees C and pH 4-6; (v) drying by spraying using soluble starch as carrier to obtain milky product, where temperature of incoming air is 190-210 degrees C and that of outgoing air is 80-100 degrees C.    USE - The method is useful for the preparation of high-F pig blood oligopeptide.    ADVANTAGE - The method is environmental friendly. The molecular weight of high-F pig blood oligopeptide is 800-1200 Da. The aromatic amino acid content is less than 0.1%, F value is higher than 25 and yield rate is higher than 10.74%.
NOVELTY - A methylamino abamectin benzoate suspending agent comprises (%) methylamino abamectin benzoate (0.2-5), lubrication dispersing agent (1-10), antifreeze agent (2-10), stabilizer (1-6), defoamer (1-5), thickening agent (0.1-1), preservative (0.1-1), and water (balance).    USE - Methylamino abamectin benzoate suspending agent.    ADVANTAGE - The suspending agent has reduced environment pollution caused by organic solvent and has low dosage cost, and reduced solvent, packaging and transportation costs.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of methylamino abamectin benzoate suspending agent, comprising preparing methylamino abamectin benzoate, lubrication dispersing agent, antifreeze agent, stabilizer, and defoamer into stock solution, and grinding to grain diameter of 3-5 mu m using wet grinding method; and mixing thickening agent and preservative into the stock solution to obtain the suspending agent.
NOVELTY - The furnace has an air passage (5) respectively opened on ends of a hot air pipe (3) and an outer housing (1) and connected with an air outlet (6). Four baffle plates (4) are arranged in the air passage. A heat insulation layer is arranged below the hot air pipe, and an air inlet and a secondary air inlet are arranged on a fuel cabinet. A gasification grate is arranged on a bottom side of the fuel cabinet and below the heat insulation layer, and a lateral air inlet is arranged at a position of a bottom side of the furnace and parallel to the gasification grate.    USE - Biomass dehumidification hot air furnace for drying and heating application. Uses include but are not limited to industry, factory, workshop and big-arch shelter.    ADVANTAGE - The furnace is arranged in heat pipe box arrangement with three return strokes, so as to design natural air supply and a cubic gasification combustion system according to the combustion characteristic of the biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a front sectional view of a biomass dehumidification hot air furnace.    Outer housing (1)    Inner housing (2)    Hot air pipe (3)    Baffle plates (4)    Air passage (5)    Air outlet (6)
NOVELTY - The device has a branch air supply pipe (15) that is installed on a side of air lifter unit (1), and is connected with an aeration pipe (13). Several ventilation holes (12) for discharging air to aeration pipe from branch air supply pipe, are installed between branch air supply pipe and aeration pipe. Several self-closing gas outlets (14) are installed on side of aeration pipe. The sewage area is formed on four sides of aeration pipe so that aeration pipe is distributed in sewage area by self-closing gas holes.    USE - Sewage backflow device for integral bioreactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of sewage backflow device.    Air lifter unit (1)    Ventilation holes (12)    Aeration pipe (13)    Self-closing gas outlets (14)    Branch air supply pipe (15)
NOVELTY - The rectifying device has a re-boiler provided with a vapor heating coil pipe. The outlet on the upper portion of the rectifying tower is connected to the inlet of the condenser (3) whose outlet is connected to inlet of esterification device (1). The outlet of esterification device is connected with the inlet of the rectifying tower by pipes. The lower portion of rectifying tower has a water discharge hole (7).    USE - Rectifying device for preparing bio-diesel.    ADVANTAGE - Since high concentration methanol is provided continuously for the reaction and the water is discharged smoothly, esterification reaction can be performed smoothly without increasing the acid value so that consumption of methanol is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the rectifying device.    Esterification device (1)    Condenser (3)    Water discharge hole (7)
NOVELTY - A nano metal catalyst comprises nano palladium catalyst granules, silica granules as catalyst carrier, and crosslinked poly(styrene-divinylbenzene) covering the surface of catalyst granules.    USE - Nano metal catalyst used in hydrogenation of 2,4-dimethyl-1,3-pentadiene and propene (both claimed).    ADVANTAGE - The nano metal catalyst enables hydrogenation with high selectivity and reactivity, and can be manufactured steadily by a simple method. After reaction completion, the catalyst can be separated and reused easily. The steric effect of polymer coating is expressed completely during catalytic reaction.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparation of nano metal catalyst, which involves copolymerizing styrene, divinylbenzene, allylamine, and nano palladium catalyst loaded on the carrier; and    (2) hydrogenation of 2,4-dimethyl-1,3-pentadiene and hydrogenation of propene in the presence of the catalyst.
NOVELTY - Bioactive compound fertilizer comprises (in wt.%): tea cake (20-40), tea shell (30-50), bioactive base agent (10-15) and quick-acting agent (10-15). The bioactive agent comprises waste of marsh mud, beer residue, biological food and biological drug. The quick acting agent comprises urea or ammonium sulfate that provides nitrogen element, and trace element including zinc sulfate, borax and ammonium molybdate.    USE - Bioactive compound fertilizer for Camellia (claimed).    ADVANTAGE - The fertilizer contains abundant quantity of nutrients and organic matter, and complete fertilizer components. The fertilizer saves energy and protects environment.    DETAILED DESCRIPTION - Bioactive compound fertilizer comprises (in wt.%): tea cake (20-40), tea shell (30-50), bioactive base agent (10-15) and quick-acting agent (10-15). The bioactive agent comprises waste of marsh mud, beer residue, biological food and biological drug. The quick acting agent comprises urea or ammonium sulfate that provides nitrogen element, and trace element including zinc sulfate, borax and ammonium molybdate. The composition contains standard fertilizer components chosen from 65% or more of bioactive organic mater content, 15% or more of nitrogen content, 8% or more of phophorus pentoxide content, 10% or more of potassium oxide content, 0.001% of zinc, 0.001% of boron and 0.001% of molybdenum. An INDEPENDENT CLAIM is included for method of producing the fertilizer, which involves crushing tea cake and tea shell to more than 60 mesh size, adding calcium-magnesium-phosphorus fertilizer (5% of the weight of crushed substance), blending uniformly, fermenting the mixture at high temperature of 50 degrees C or more, blending the fermented mixture with bioactive base agent and quick-acting agent, drying the mixture at low temperature of less than 30 degrees C, and packaging the product.
NOVELTY - Ethanol (1 mole parts) and an ionic liquid (0.2-0.6 mole parts) are added to three-mouth flask, stirred, heated and reacted at 70-80 degrees C for 4-6 hours. The reaction liquid is maintained still over night, and separated using a separating funnel to obtain animal fatty acid ethyl ester. The ionic liquid is 1-ethyl-3-methylimidazolium tetrafluoroborate ionic liquid or N-methyl-2-pyrrolidone mesylate ionic liquid.    USE - Manufacture of animal fatty acid ethyl ester.
NOVELTY - Fertilizer comprises (in weight%) urea (6-11), mono-ammonium phosphate (23-30), Streptomyces microflavus culture (6-15), composite bacteria culture (50-60) and amide high molecular compound adhesive (0.3-0.35). Composite bacteria are capable of fermenting kitchen organic wastes. S.microflavus culture and composite bacteria culture are obtained by enlarging and cultivating strain. Concentration of S.microflavus in S.microflavus culture is 70 million/g or more. The content of organic substrate in composite bacteria culture is 46% or more.    USE - Fertilizer is used for sweet sorghum in saline and alkaline land.    ADVANTAGE - The fertilizer has high nutritive value, and is capable of improving microbiota of soil, accelerating nitrogen fixation, phosphate-solubilizing and potassium-solubilizing of soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fertilizer, which involves crushing urea and mono-ammonium phosphate, culturing composite bacteria and S.microflavus, mixing crushing urea, mono-ammonium phosphate and composite, bacteria culture, S.microflavus culture, and amide high molecular compound adhesive, pelletizing, sieving, cooling, and packing.
NOVELTY - Shampoo comprises (pts.wt.) surfactant (10-60), chelating agent (0.01-0.5), humectant (1-20), regulating agent (1-15), thickening agent (1-20), chlorine dioxide or chlorine dioxide precursor (0.001-5), pH adjuster, which adjusts the pH to 5.5-7.5, and deionized water (balance to 100).    USE - The shampoo is useful for washing hair, protecting hair, removing dandruff, and stopping itching. It is used for treating dandruff caused by seborrheic dermatitis and tinea capitis.    ADVANTAGE - Safe and environment-friendly A1 grade green disinfector, i.e. chlorine dioxide is introduced into shampoo. The shampoo is mild, safe, and environment friendly; can keep hair moistened, smooth, and lustrous; and overcomes the shortcoming of prior art dandruff-removing shampoo. The scalp is relaxed after washing; and dandruff does not reoccur.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of shampoo comprising providing deionized water, chelating agent, and humectant; stirring to dissolve; adding surfactant; heating at 60-75 degrees C; stirring to dissolve; adding regulating agent; stirring to dissolve; adding thickening agent; stirring and reducing the temperature below 30 degrees C; adding chlorine dioxide or chlorine dioxide precursor; stirring; and adjusting pH at 5.5-7.5 by pH adjuster.
NOVELTY - Bio-oil catalysis and quality improvement comprises using double-functional catalyst of metal coordination and acid coordination to further hydrogenation, esterification, and quality improvement of aldehyde and acid in bio-oil system. A model reaction of the furfural-acetic acid one-step hydrogenation and esterification comprises putting furfural, methylbenzene solution of acetic acid and double-functional catalyst into high-pressure agitated reactor, introducing hydrogen to make pressure reach 10-40 atm, stirring at 800 plus minus 2 rpm, and reacting at 80-200 degrees C for 2-10 hours.    USE - Method for bio-oil catalysis and quality improvement (claimed).    ADVANTAGE - The method makes possible for percent conversion of aldehyde to reach 56.9%, selectivity of ester to reach 13.6%, and selectivity of alcohol to reach 52.8%.    DETAILED DESCRIPTION - Bio-oil catalysis and quality improvement comprises using double-functional catalyst of metal coordination and acid coordination to further hydrogenation, esterification, and quality improvement of aldehyde and acid in bio-oil system. A model reaction of the furfural-acetic acid one-step hydrogenation and esterification comprises putting furfural, methylbenzene solution of acetic acid and double-functional catalyst into high-pressure agitated reactor, introducing hydrogen to make pressure reach 10-40 atm, stirring at 800 plus minus 2 rpm, and reacting at 80-200 degrees C for 2-10 hours. A mass ratio of acetic acid/furfural is 6 plus minus 0.05:9.6. A mass ratio of catalyst/furfural is 1:48-1:6.4. The double-functional catalyst is silicic acid carrier Al2(SiO3) loaded with palladium (mass%).
NOVELTY - An Acidovorax avenae SS-1 strain (CGMCC 3633), is new.    USE - The A.avenae is useful for degrading natural estrogen (e.g. estrone, 17 beta -estradiol and estriol), which is used in wastewater treatment technology and soil treatment technology (all claimed).    ADVANTAGE - The A.avenae degrades 99% of estrone and 17 beta -estradiol within 24 hours.
NOVELTY - Hemp plant oil, short-chain alcohol, co-solvent and solid catalyst are mixed and reacted at predetermined temperature and pressure. The reaction product is filtered to recover solid catalyst. The filtered product is supplied to flash tank to recover alcohol and co-solvent. The product is clarified and separated. Crude biodiesel as upper layer, and crude glycerine as lower layer are separated. The crude biodiesel is rectified to obtain biodiesel product.    USE - Preparation of biodiesel.    ADVANTAGE - Biodiesel having excellent quality is economically produced at high yield by simple method. The catalyst, alcohol and co-solvent are recycled.
NOVELTY - A feed inlet (2) is provided at top of main structure (1). A circulating air guide ring (3) is connected to air blower (5) through a pipeline (4). A gas output hole (10) is connected to purifier pipeline (9) in furnace cavity (6). The air inlets (11,12) are provided at middle of cavity and connected to wind handle (13) which is mounted on outer side of main structure. A dust-removing door (15) is provided on lower portion of purifier pipeline in a state connected to main structure. A skimming door (14) is provided on lower portion of outer side of main structure.    USE - Straw gasification furnace for burning and gasifying leaves and grass.    ADVANTAGE - The burning residue of large density is removed, so that block in bridge of furnace is removed efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the straw gasification furnace.    Furnace main structure (1)    Feed inlet (2)    Circulating air guide ring (3)    Pipeline (4)    Air blower (5)    Furnace cavity (6)    Purifier pipeline (9)    Gas output hole (10)    Air inlets (11,12)    Wind handle (13)    Skimming door (14)    Dust-removing door (15)
NOVELTY - Agent comprises (in parts weight): growth inducer (1-40), solvent (10-75), surfactant (10-75) and protein (10-60).    USE - The agent is useful for accelerating decomposition and fermentation of organic substances (both claimed) in solid waste management industries for increasing production of useful enzymes.    ADVANTAGE - The agent is inexpensive, and induces microorganism to propagate rapidly, and ferments organic substances rapidly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the agent, which involves (a) pulping crushed rapeseed oil cake, soybean oil cake or waste tobacco in solid-liquid ratio of 1:9 at pH 8.5, extracting mixture at 65 degrees C for 90 minutes for 3 times, centrifuging the mixture, filtering the mixture at pH 3.5, precipitating the filtrate for 5-7 degrees C for 6 hours, centrifuging the precipitate, filtering obtained product, neutralizing the precipitate using alkaline liquid until the pH reaches 7-7.5 and drying product under vacuum to obtain protein, (b) adding growth inducer, solvent and surfactant in a reaction kettle, heating and mixing uniformly the obtained mixture at 50-65 degrees C for 30-90 minutes, (c) adding the obtained protein into the reaction kettle, dispersing the mixture at 50-65 degrees C for 20-90 minutes, and (d) molding the obtained mixture.
NOVELTY - Carbon dioxide contained in natural gas having carbon dioxide content of more than 40 mol% is separated by film separator. Natural gas with carbon dioxide content of 3 mol% or less is discharged from penetrating side of the film separator. Penetrated gas is passed through a transformation absorbing device. Carbon dioxide is further separated by adsorbent selective absorption and vacuum analysis, and product having carbon dioxide content of 98 mol% or more is produced. Natural gas is purified to gas having carbon dioxide content of 3 mol% or less, and discharged.    USE - Removal and recycling of carbon dioxide in natural gas.
NOVELTY - Osmuncla japonica extract is prepared by using a multifunctional extracting tank. Osmuncla japonica powder is soaked with organic solvent (alcohol) in the ratio of 1:2-1:8 for 4-24 hours in hot and cold environment. The mixture is filtered and dried to obtain extract. The extraction process is carried for 2-10 times or reflowing the mixture continuously for 4-10 hours.    USE - Osmuncla japonica extract used for preparing acaricide (claimed) for preventing and treating Acarus on fruit tree and vegetable.    ADVANTAGE - The Osmuncla japonica extract is eco-friendly and has high efficiency and low toxicity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing acaricide, which involves:    (A) using effective components of Osmuncla japonica;    (B) dissolving the Osmuncla japonica total biflavone with co-solvent and chloroform, hexamethylene, benzene, dimethylbenzene or alcohol, and potentiating agent, emulsifier, penetrating agent and/or suspending agent; and    (C) preparing acaricide by using (in pts.wt.): extract (5-32), solvent (35-95), co-solvent (1-30), emulsifier and/or suspending agent (2-35), potentiating agent (0.5-25) and penetrating agent (0.5-20).
NOVELTY - Carbon dioxide is injected into a high-pressure crystallizing kettle at constant speed. The temperature and pressure of the kettle are stabilized under supercritical state. Absolute ethyl alcohol solution of glycyrrhetic acid solution is sprayed into the kettle through a nozzle at constant speed by a high-pressure plunger. Glycyrrhetic acid powder of not greater than 300 nm is separated, and carbon dioxide is continuously processed in the kettle for at least half an hour and the obtained nano-glycyrrhetic acid powder is dried.    USE - Preparation of water-soluble nano-glycyrrhetic acid powder by supercritical antisolvent method.    ADVANTAGE - The method enables environmental-friendly, economical and easy industrial production of nano-glycyrrhetic acid powder having excellent surface smoothness and water solubility, uniform granularity distribution, and no solvent residue, with high yield.    DETAILED DESCRIPTION - A carbon dioxide high-pressure pump is started and carbon dioxide is injected into a high-pressure crystallizing kettle at constant speed. The temperature and pressure of the kettle are stabilized under supercritical state. Absolute ethyl alcohol solution of glycyrrhetic acid solution is sprayed into the kettle through a nozzle at constant speed by a high-pressure plunger. Glycyrrhetic acid powder of not greater than 300 nm is separated, and carbon dioxide is continuously processed in the kettle for at least half an hour and the obtained nano-glycyrrhetic acid powder is dried. The solvent and carbon dioxide are separated in a separating kettle, the solvent is recovered and reused, and carbon dioxide is directly recycled.
NOVELTY - A floating plant has storage tank which stores methane hydrate, methane substituent injecting line which injects methane substituent to methane hydrate layer, methane gas suction line which sucks methane gas generated by substituting methane hydrate with methane substituent in methane hydrate layer, and reformer. The reformer produces carbon monoxide and hydrogen by performing modification reaction with methane gas sucked through suction line.    USE - Floating plant is used for extraction of methane gas (claimed) for producing synthetic oil.    ADVANTAGE - The floating plant efficiently provides methane gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for extraction of methane gas from methane hydrate layer.
NOVELTY - Composition comprises Cucumis melo seed extract and D-sorbitol.    USE - The composition is useful for treating constipation (claimed), headache, fatigue, colon carcinoma, liver diseases and menorrhagia.    ADVANTAGE - The composition is eco-friendly, free from fat, increases beneficial bacteria in stomach and provides feeling of excellent bowel movement.
NOVELTY - Hydrodeoxygenation of charges obtained from renewable sources with 10% conversion by decarboxylation/decarbonylation, by implementing a mass catalyst or support comprising an active phase constituted of at least one element of group VIB and at least one group VIII element, where the elements are as sulfide and the atomic ratio of metal of group VIII to metal of the group VIB is strictly greater than 0 to less than 0.095, the process is carried out e.g. at a temperature of 120-450 degrees C, and at a pressure of 1-10 MPa, is claimed.    USE - The process is useful for hydrodeoxygenation of charges obtained from renewable sources with 10% conversion by decarboxylation/decarbonylation for producing biofuels such as diesel.    ADVANTAGE - The process allows efficient and economical hydrodeoxygenation of charges obtained from renewable sources with less consumption of energy without creating global warming, carbon dioxide emissions and other greenhouse gas emissions.    DETAILED DESCRIPTION - Process for hydrodeoxygenation of charges obtained from renewable sources with 10% conversion by decarboxylation/decarbonylation, implementing a mass catalyst or support comprising an active phase constituted of at least one element of group VIB and at least one group VIII element, where the elements are as sulfide and the atomic ratio of metal (or metals) of group VIII to metal (or metals) of the group VIB is strictly greater than 0 to less than 0.095, the process is carried out at a temperature of 120-450 degrees C, at a pressure of 1-10 MPa, at a space velocity of 0.1-10 h-1 and in the presence of a total amount of hydrogen mixed with charge such as the ratio of hydrogen/charge is 50-3000 Nm3 of hydrogen/m3 of charge, is claimed.
NOVELTY - Water electrolysis system comprises: (a) a water electrolysis apparatus including current collectors and an electrolyte membrane disposed in between for electrolyzing water; and (b) a water storage apparatus for separating between the oxygen and residual water discharged from the water electrolysis apparatus.    USE - The water electrolysis system is useful for water treatment applications.    ADVANTAGE - The water electrolysis system has a simple structure and is capable of reliably preventing formation of a continuous hydrogen passage from a water electrolysis apparatus through a water storage apparatus in an oxygen discharge path to the outside.    DETAILED DESCRIPTION - Water electrolysis system comprises: (a) a water electrolysis apparatus including current collectors and an electrolyte membrane disposed in between for electrolyzing water, thus generating oxygen at an anode side and generating hydrogen at a cathode side; and (b) a water storage apparatus for separating between the oxygen and residual water discharged from the water electrolysis apparatus, thus storing the water, where the water storage apparatus includes a tank for storing the water and an inlet for introducing the oxygen and the residual water discharged from the water electrolysis apparatus into the tank, and the position of the inlet is determined so that the inlet is constantly opened in the water stored in the tank.
NOVELTY - Producing hydrocarbons comprises: (a) culturing an engineered cyanobacterium in a culture medium, where the engineered cyanobacterium comprises a recombinant acyl carrier protein (ACP) reductase (AAR) enzyme and a recombinant alkanal decarboxylative monooxygenase (ADM) enzyme; and (b) exposing the engineered cyanobacterium to light and carbon dioxide.    USE - The method is useful for producing hydrocarbons (claimed).    ADVANTAGE - The method provides efficient biosynthetic production of fuels.    DETAILED DESCRIPTION - Producing hydrocarbons comprises: (a) culturing an engineered cyanobacterium in a culture medium, where the engineered cyanobacterium comprises a recombinant acyl carrier protein (ACP) reductase (AAR) enzyme and a recombinant alkanal decarboxylative monooxygenase (ADM) enzyme; and (b) exposing the engineered cyanobacterium to light and carbon dioxide, where the exposure results in the conversion of the carbon dioxide by the engineered cynanobacterium into n-alkanes, where at least one of the n-alkanes is selected from n-tridecane, n-tetradecane, n-pentadecane, n-hexadecane, and n-heptadecane, and where the amount of the n-alkanes produced is between 0.1% and 5% dry cell weight and at least two times the amount produced by an otherwise identical cyanobacterium, cultured under identical conditions, but lacking the recombinant AAR and ADM enzymes.
NOVELTY - The method involves gasifying thermally a carbon-containing raw material. The synthesis gas produced during the gasification is purified. The temperature of the synthesis gas is changed. A straw-like biomass is selected as the carbon-containing raw material. The gasification is performed in a fixed bed reactor (1) and the ash-softening temperature of the straw-like raw material is increased by adding an alkaline-earth salt.    USE - Method for recycling carbon-containing raw material.    ADVANTAGE - The synthesis gas produced during the gasification is purified and the temperature of the synthesis gas is changed, and hence ensures efficient recycling of raw material.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for transforming carbon-containing raw material and biomass into liquid fuels.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the recycling method.    Fixed bed reactor (1)
NOVELTY - Method to pre-treat biomass, comprises: preparing the biomass into prepared biomass; and pre-treating the prepared biomass into pre-treated biomass by application of a dilute acid having a concentration of 0.8-1.1 wt.% at a temperature of 130-170 degrees C for 8-12 minutes, where the fermentation product can be obtained by separating the pre-treated biomass into a liquid component comprising xylose and a solid component from which glucose can be made available and accessing xylose for fermentation into the fermentation product.    USE - The method is useful to pre-treat biomass used in a biorefinery to produce a fermentation product.    ADVANTAGE - The method facilitates improvement in the efficiency and yield of cellulosic ethanol from the biomass.    DETAILED DESCRIPTION - Method to pre-treat biomass to be used in a biorefinery to produce a fermentation product, comprises: preparing the biomass into prepared biomass; and pre-treating the prepared biomass into pre-treated biomass by application of a dilute acid having a concentration of 0.8-1.1 wt.% at a temperature of 130-170 degrees C for 8-12 minutes, where the fermentation product can be obtained by separating the pre-treated biomass into a liquid component comprising xylose and a solid component from which glucose can be made available and accessing xylose for fermentation into the fermentation product/where the biomass comprises lignocellulosic material comprising at least one of corn cobs, corn plant husks, corn plant leaves and corn plant stalks.    DESCRIPTION OF DRAWING(S) - The figure shows a perspective view of a biorefinery comprising a cellulosic ethanol production facility.
NOVELTY - An electrolytic cell (12) has a cathode and an anode provided with water as electrolyte. An electrical power supply applies a voltage across the cathode and anode. A main reserve tank (14) supplies water to the cell in a cycle and receives hydrogen and oxygen gas produced on the cell. The main reserve tank is operably connected to an air scrubber (24) for filtering the gas regulated by gas output regulating valve.    USE - Electrolytic fuel reformer system for internal combustion engine used in vehicle.    ADVANTAGE - The system allows complete combustion of fuel so that the mileage of vehicle is increased with same amount of fuel. The fuel reformer system can be manufactured easily and inexpensively.    DESCRIPTION OF DRAWING(S) - The drawing shows a plan view of the electrolytic fuel reformer apparatus.    Electrolytic cell (12)    Main reserve tank (14)    Gas outlet port (20)    Conduit (22)    Air scrubber (24)
NOVELTY - The method involves removing obtained synthesis gas from a reaction chamber (1) in a direction leading upward or downward via an outlet connector so that the gas is conducted into a collecting chamber (6) to be cooled down by adding cool gaseous, vaporous or liquid cooling medium. Fuel consisting of renewable or biological fuels is introduced into the gas in a cooling chamber via a burner level (4) so that the thermal enthalpy of the gas is utilized for endothermic gasification reaction of biological raw material.    USE - Method for utilizing enthalpy of synthesis gas during endothermic gasification reaction of biological raw material.    ADVANTAGE - The method introduces the fuel consisting of renewable or biological fuels into the gas in the cooling chamber via the burner level so that the thermal enthalpy of the gas is utilized for endothermic gasification reaction of biological raw material, thus enabling utilization of enthalpy of synthesis gas for endothermic gasification reaction process in an energy-saving manner with less machine expenditure.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an apparatus for utilizing enthalpy of synthesis gas, comprising a fire-proof reaction area.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a gasification reactor for gasification of renewable fuel.    Reaction chamber (1)    Pressure-type coated container (2)    Burner level (4)    Collecting chamber (6)    Addition nozzle (7)
NOVELTY - The crystallizing glass solder for high temperature application, comprises barium oxide (45-60 wt.%), silicon dioxide (25-40 wt.%), diboron trioxide (5-15 wt.%), aluminum oxide (0-2 wt.%), zirconium oxide (5 wt.%) and/or alkaline-earth oxides such as magnesium oxide, calcium oxide (0-3 wt.%) and strontium oxide and/or vanadium pentoxide, antimony trioxide and/or cobalt oxide (0.5 wt.%). The sum of the alkaline-earth oxides is 2-15 wt.% and the sum of the silicon dioxide and diboron trioxide is 36-51 wt.%.    USE - Crystallizing glass solder useful for the production of fuel cell, in sintering body with high temperature stability, for the production of films with high temperature stability (all claimed).    ADVANTAGE - The crystallizing glass solder can be simply manufactured with good temperature stability and improved crystallization properties.    DETAILED DESCRIPTION - The crystallizing glass solder for high temperature applications, comprises barium oxide (45-60 wt.%), silicon dioxide (25-40 wt.%), diboron trioxide (5-15 wt.%), aluminum oxide (0-2 wt.%), zirconium oxide (5 wt.%) and/or alkaline-earth oxides such as magnesium oxide, calcium oxide (0-3 wt.%) and strontium oxide and/or vanadium pentoxide, antimony trioxide and/or cobalt oxide (0.5 wt.%). The sum of the alkaline-earth oxides is 2-15 wt.% and the sum of the silicon dioxide and diboron trioxide is 36-51 wt.%. The thermal expansion coefficient in glassy condition is 6x 10-6 K-1 to 11x 10-6 K-1 and/or in crystalline condition is 8x 10-6 K-1 to 13x 10-6 K-1. The molar ratio of the silicon dioxide and barium oxide is less than 2.3 and a hemisphere temperature is 850-1080 degrees C. The difference in the thermal expansion before and after the crystallization process is 1x 10-6 K-1. The portion of amorphous phase in crystallized condition is 10 wt.%. An INDEPENDENT CLAIM is included for a composite having crystallizing glass solder.
NOVELTY - Wastewater purification processing agent, comprises a mixture of lactic acid bacteria chosen from Lactobacillus fermentum and Enterococcus faecium, and pineapple enzyme.    USE - The agent is useful for purification of wastewater (claimed).    ADVANTAGE - The agent removes scum within grease trap or putrefactive smell. The wastewater purified using the agent has biological oxygen demand of less than 150 ppm, preferably less than 6 ppm.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for purification of wastewater.
NOVELTY - An electric power generating apparatus comprises electric power generating apparatus main body, storage chamber (20) which accommodates solid material (28) and fluid material (27), hydrogen source container (2) which sends out hydrogen, fuel cell (11) which produces electric power, and mounting part which mounts with hydrogen source container detachably. The hydrogen is generated by contact of solid material and fluid material.    USE - An electric power generating apparatus.    ADVANTAGE - The apparatus can generate electric power, and can replace solid material and fluid material which are hydrogen sources simply.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a hydrogen source container; and    (2) an electric power generating apparatus main body.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional side view of electric power generating apparatus in electric power generation halt condition. (Drawing includes non-English language text).    Hydrogen source container (2)    Fuel cell (11)    Storage chamber (20)    Fluid material (27)    Solid material (28)
NOVELTY - Fuel cell system comprises fuel cell, fuel vaporization unit (2) which vaporizes the liquid fuel sprayed from a fuel sprayer (1), fuel modification unit (3) which modifies the vaporized fuel into fuel gas, primary air introduction unit (A1) which introduces primary air in the path from fuel gas discharge part of fuel cell to the fuel vaporization unit, secondary air introduction unit which introduces secondary air in the path from fuel vaporization unit to fuel modification unit and modification heating unit (4).    USE - Fuel cell system for motor vehicles.    ADVANTAGE - Vaporizes liquid fuel without depositing carbon and has highly efficient electric power generation performance which can be maintained over a long period of time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for controlling the 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 sprayer (1)    Fuel vaporization unit (2)    Fuel modification unit (3)    Modification heating unit (4)    Primary air introduction unit (A1)
NOVELTY - Organic wastewater purifying apparatus (1) comprises microbial treatment unit (3, 4) which processes wastewater using microorganisms, porous body (62) which removes microorganisms by adsorption, and ozone treatment unit (7) for removing the microorganisms using ozone.    USE - Apparatus for purifying organic wastewater (claimed) such as domestic waste water.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for purifying organic wastewater.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the.    Organic wastewater purifying apparatus (1)    Tank (2)    Microbial treatment unit (3, 4)    Ozone treatment unit (7)    Porous body (62)
NOVELTY - Controller controls the removal of active ingredient from a supply container of a syringe electrochemically operated with hydrogen as compressed gas. The hydrogen is produced in zinc/hydrogen cells as short circuit current between a zinc anode and hydrogen cathode. The cell housing contains an aqueous electrolyte, preferably alkaline lye, as well as the anode and cathode. Paraffin oil is present in the cell to prevent entry of atmospheric oxygen. The zinc/hydrogen cells are arrange in pairs to generate hydrogen.    USE - Controller for controlling the removal of active ingredient from a supply container of a syringe electrochemically operated with hydrogen as compressed gas.    ADVANTAGE - The removal process is easily controlled.    DETAILED DESCRIPTION - Preferred Features: The controller comprises a regulating resistor to control the hydrogen rate. The hydrogen cathode has a hydrogen storage alloy.
NOVELTY - Hydrogen generating apparatus (1) comprises water supply part (3), material supply part (4), desulfurization part (5) which contains a desulfurizing agent which adsorbs sulfur compound in the raw material, desulfurization temperature detecting part, modification part which produces hydrogen containing gas by reforming the raw material, combustion part (2) which heats the modification part, combustion-air supply part which supplies air for combustion to the combustion part, and control part which controls the operation of the combustion-air supply part and material supply part.    USE - Hydrogen generating apparatus for a fuel cell system.    ADVANTAGE - The combustion part is stabilized by controlling the flow rate of raw material.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for operating the hydrogen generating apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the fuel cell system. (Drawing includes non-English language text).    Hydrogen generating apparatus (1)    Combustion part (2)    Water supply part (3)    Material supply part (4)    Desulfurization part (5)
NOVELTY - Method for producing hydrogen involves preparing predetermined amount of mixture of a hydrogen storage material powder and nonaqueous and water-soluble storage medium to a region, preparing reaction water which hydrolyzes the hydrogen storage material powder to a region, hydrolyzing the hydrogen storage material by supplying the mixture and reaction water to a reaction area, and recovering residues produced.    USE - Method for producing hydrogen.    ADVANTAGE - The amount of hydrogen produced is regulated.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a hydrogen production system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the hydrogen producing system. (Drawing includes non-English language text).    Hydrogen-producing system (10)    Storage material supply tank (11)    Storage material recovery tank (12)    Reaction water supply tank (13)    Water recovery tank (14)
NOVELTY - Method for manufacturing hydrogen involves reacting a gaseous water-soluble greater than or equal to 2C hydrocarbon and liquid water in the presence of metal containing catalyst.    USE - Method for manufacturing hydrogen used as raw materials (e.g. for ammonia, methanol, hydrogen peroxide, semiconductor manufacture and metallurgy) and clean energy source (e.g. for fuel cell and hydrogen fueled motor vehicle engine).    ADVANTAGE - Has low energy consumption and low carbon dioxide emission.
NOVELTY - Enhancing the growth of market garden plants belonging to the non-leguminous plant species, the growth of which is independent of Rhizobia and not highly dependent or independent of arbuscular mycorrhizal fungi, comprises cultivating the plants in a mixture of compost and a soil where Amaranthus spp was grown previously.    USE - The Amaranthus spp is useful as biofertilizing agent or enhancer of market garden plants belonging to the non-leguminous plant species, the growth of which is independent of Rhizobia and not highly dependent or independent of arbuscular mycorrhizal fungi, where the market garden plant is non-leguminous plant species not highly dependent of arbuscular mycorrhizal fungi and all the non-mycotrophic plant species (all claimed) e.g. cabbage, cauliflower, beets, onions, leeks, radishes, tomatoes, salads and strawberries. The biofertilizing property of A. veridis was tested on tomatoes. The result showed that the aerial biomass was 2.04 g for cultivation using a mixture of soil where A. veridiswas grown previously (5 volumes) and compost (95 volumes) and 0.58 g for compost alone.    ADVANTAGE - The biofertilizing composition is easy to use and inexpensive. The use of Amaranthus spp allows for sowing brick which may be used to grow garden market plants presenting low dependence for their growth from the mycorrhizal symbiosis.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) a biofertilizing composition comprising a mixture of compost and a soil where Amaranthus spp was grown previously; and (2) preparing the biofertilizing composition comprising: recovering the soil where Amaranthus spp is growing, mixing the soil with compost and storing it until use.
NOVELTY - The furnace has a pyrolysis drum made of high-temperature-resistant material arranged on a furnace body. A secondary gasifying agent inlet is located on a bottom part of the furnace body, and is in contact with a hollow cavity on a lower part of a fire grate. A tertiary gasifying agent inlet is connected with a gas distributing ring with a spraying nozzle in a combustion cavity. A gas reformer is provided with multiple reforming channels connected with a fuel gas cavity and the combustion cavity, where the gas reformer is made of high-temperature-resistant material.    USE - Biomass fixed bed gasification furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial sectional view of a biomass fixed bed gasification furnace.
NOVELTY - The gasifier has an air inlet ring passage (22) provided with an air inlet hole (21) that is connected with a hearth bottom part (23). The air inlet ring passage is connected with an air inlet pipe (15), and an upper part of the hearth is connected with a bottom part of a combustion chamber (24) in a stove body (25) through a gas through bridge (26). The stove body is provided with an air inlet cavity (13) that is connected with an oxygen supply pipe (28). The air inlet cavity is connected with the combustion chamber through an oxygen distribution hole (12).    USE - Biomass compound gasifier.    ADVANTAGE - The gasifier ensures that gas lead pipe can be prevented from being blocked. The gasifier saves energy, and has simple structure and convenient operation.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial sectional view of a biomass compound gasifier.    Oxygen distribution hole (12)    Air inlet cavity (13)    Air inlet pipe (15)    Air inlet hole (21)    Air inlet ring passage (22)    Hearth bottom part (23)    Combustion chamber (24)    Stove body (25)    Gas through bridge (26)    Oxygen supply pipe (28)
NOVELTY - The machine set has a horizontal connecting pipe connected between a draught fan (14) and an electric tar precipitator gas inlet valve (21). A side of the precipitator gas inlet valve is connected with an electric tar precipitator (16). A gas outlet of the electric tar precipitator is connected with a water seal (19). A lower part of the water seal is connected with a water seal draining valve (18). A control switch of an electric control cabinet (31) is connected with a feeding machine (2), a draught fan (14), an underwater pump (29) and a high-pressure water pump (28) via electric wires.    USE - Fixed bed biomass gasification machine set.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a fixed bed biomass gasification machine set.    Feeding machine (2)    Draught fan (14)    Electric tar precipitator (16)    Water seal draining valve (18)    Water seal (19)    Electric tar precipitator gas inlet valve (21)    High-pressure water pump (28)    Underwater pump (29)    Electric control cabinet (31)
NOVELTY - Device for processing swill into organic fertilizer comprises a waste processing room (4) including a processing gas inlet (4a) and a waste exhaust (4b) and equipped with a stirrer (5), and a processing gas supply device (1) for providing the processing gas to the processing room (4), where the processing gas supply room (1) is connected with a processing gas inlet (4a) of the waste processing room by an air inlet pump (3).    USE - The device is useful for processing swill into organic fertilizer (claimed).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for processing swill into organic fertilizer.    Processing gas supply device (1)    Gas heating device (2)    Air inlet pump (3)    Waste processing room (4)    Processing gas inlet (4a)    Waste exhaust (4b)    Stirrer (5)    Processing room gas outlet pipe (8)    Waste gas processing device (9)    Ozone inlet pipe (10)    Ozone reducing device (13)    Gas outlet pipe (14)    Filter (15)    Heater (17)    Waste gas processing room (91)    Overflow plate (94)    Overflow room (95)
NOVELTY - Detergent combination (I) comprises an aqueous solution comprising (a) 5-50 wt.% of an absorber component based on a tertiary amine or a mixture of several tertiary amines and (b) 1-25 wt.% of an activator comprising di- or polyvalent aliphatic amines, and (c) not more than 80 wt.% of water, where the molar ratio of (b) to total number of moles of (b) and (a) is 0.25-0.6.    USE - (I) is useful for chemisorptively purifying biogas or sewage gas (claimed).    ADVANTAGE - (I) exhibits high loading capacity, good aging stability, high separation (selectivity) efficiency, high washing performance, and enhanced synergistic effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a chemisorptive process for purifying biogas or sewage gas using the detergent combination in a washing column (K1) with filler, comprising supplying a raw gas at the bottom of the column and adding (I), as washing solution to the head of the column, regenerating the accumulated, contaminated detergent and circularly driving, where the purification is carried out in two-stages as coarse and fine purification steps, after the fine purification step, the accumulated washing solution is concentrated with supplied contaminated carbon dioxide loaded washing solution from the coarse purification step, and the use of concentrated washing solution in the coarse purification step results in the increased uptake of carbon dioxide.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of a biogas purification system.    Pipeline (01, 02, 03, 05, 06, 10, 11, 12)    Circuit line (04)    Supply lines (08, 09)    Washing column (K1, K2)    Regeneration unit (R)    Pump. (P1, P2)
NOVELTY - The device has split washers (10, 20) or perforated disks arranged in a region of a gas inlet opening and arranged on top of each other with preset distance, where the split washers exhibit reflective surfaces. Slit segments, slit-circular segments (27, 28), silt-ring segments, a light- and gas permeable cavity, upper- and lower circular rings, and upper- and lower rows of holes are covered by upper- and lower completely circular segments (25, 26), a circular ring segment, and a light- and gas permeable material in a vertical axis direction.    USE - Infrared-optical gas measurement device for use in a warning- and alarm system for monitoring concentration of gas e.g. explosive gas and harmful gas such as methane and carbon dioxide, for a human organism, in an industry.    ADVANTAGE - The device monitors the concentration of the gas in the industry in accurate manner, and reduces light loss in the measurement environment. The device exhibits simple and robust construction.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic exploded perspective view of an infrared-optical gas measurement device.    Cylindrical outer housing (2)    Split washers (10, 20)    Upper completely circular segment (25)    Lower completely circular segment (26)    Slit-circular segments (27, 28)
NOVELTY - A rhodium metal-modified nickel-based steam reforming catalyst is obtained by dipping rhodium and nickel-based catalyst powder in hydrotalcite-type precursor containing nickel, magnesium and aluminum.    USE - Rhodium metal-modified nickel-based steam reforming is used for manufacturing hydrogen gas (claimed) used as fuel for fuel cell vehicle and fuel cell reformer.    ADVANTAGE - The rhodium metal-modified nickel-based steam reforming catalyst has high surface area and excellent catalytic activity for a long period of time and stability.    DETAILED DESCRIPTION - A rhodium metal-modified nickel-based steam reforming catalyst is obtained by dipping rhodium and nickel-based catalyst powder in hydrotalcite-type precursor containing nickel, magnesium and aluminum. The rhodium metal-modified nickel-based catalyst is of formula: Rh-Nix/MgyAl.    x=0.25-1;    y=0.6-5.5;and    x/y=0.15-0.45.    INDEPENDENT CLAIMS are included for the following:    (1) manufacture of rhodium metal-modified nickel-based steam reforming catalyst; and    (2) manufacture of hydrogen gas, which involves carrying out steam reforming reaction of liquid petroleum gas in presence of rhodium metal-modified nickel-based steam reforming catalyst.
NOVELTY - The machine has an electric motor and a shaft bracket installed on a frame. The shaft bracket is equipped with a forming compacting mechanism, and an electric output wheel is connected with a reducer input belt. The forming compacting mechanism comprises a set of left and right closed chain conveying mechanisms for adjusting an angle of the machine. A bar mold of the left and right closed chain conveying mechanism is formed as infundibule structure with front and back baffles and installed on two sides of the included angle surface.    USE - Crocodile biomass fuel forming machine.    ADVANTAGE - The machine can control the density and the degree of the compression of the fuel, and remove leakage of material, thus saving material on the base in an environmental friendly manner, and shortening the working time with good compacting effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a crocodile biomass fuel forming machine.
NOVELTY - The furnace has a main body (1) provided with an ash hole (5), an air intake disk (6) and a furnace cover (8). A filter (7) is connected with the main body through a pipeline, and a vent pipeline is divided into an upper vent pipeline (2) and a lower vent pipeline (3). An outer side of the main body is provided with a heating plate, and an inner side of the main body is made up of a refractory material.    USE - Biomass straw gasification furnace.    ADVANTAGE - The furnace reduces coverage area, and improves combustion degree of large, long and crude firewood material, and combustion quality of raw material.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass straw gasification furnace.    Main body (1)    Upper vent pipeline (2)    Lower vent pipeline (3)    Ash hole (5)    Air intake disk (6)    Filter (7)    Furnace cover (8)
NOVELTY - The furnace (1) has two iron barrels (2, 3) arranged on two sides. A gasification furnace cover (4) is arranged above the furnace, and a gasification furnace feeding port (7) is arranged on the gasification furnace cover. A gas output switch (8) and an exhaust switch (9) are arranged above the furnace, and an oxygen inlet (5) is arranged behind the furnace. A waste material outlet (6) is arranged below the furnace. The gasification furnace cover is sealed by dry powder.    USE - Fuel gas generating furnace for automatically drying straw.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a fuel gas generating furnace.    Furnace (1)    Iron barrels (2, 3)    Gasification furnace cover (4)    Oxygen inlet (5)    Waste material outlet (6)    Gasification furnace feeding port (7)    Gas output switch (8)    Exhaust switch (9)
NOVELTY - The cover has multiple grooves (3) distributed on an outer surface of a cover body (1) along a circumference. An exhausting holes (5) are connected with a cavity inside the cover body and opened on a sidewall (4) of the grooves. The outer surface of the cover body is formed into an impeller structure. The sidewall of the grooves is perpendicular to the bottom. The cover body is made of metal or concrete or other temperature resistant material. An internal air guiding ring and an external air guiding ring concentric to each other are installed on the outer surface of the cover body.    USE - Exhaust cover for a biomass energy conversion furnace.    ADVANTAGE - The exhausting holes are opened on the side of the grooves on the outer surface of the cover body, so that the air enters the combustion chamber to form the rotary air, thus completely combusting the material in the combustion chamber. The exhausting holes are changed from the vertical direction to the horizontal direction to prevent the dust blocking phenomenon and improve the gas production property.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of an exhaust cover.    Cover body (1)    Grooves (3)    Side wall (4)    Exhausting holes (5)
NOVELTY - The storage unit has two hydrogen storage cavities arranged parallel to each other in a hydrogen storage container i.e. flat cube. A gas guide channel is formed in the hydrogen storage container, and is penetrated into the two hydrogen storage cavities. Hydrogen storage material is filled in the hydrogen storage cavities, and a fuel cell monomer is provided with a membrane electrode unit. A fuel cell monopole plate is formed at two sides of the membrane electrode unit, and a hydrogen runner receives hydrogen provided by the storage unit.    USE - Hydrogen storage unit for a coupling fuel cell (claimed).    ADVANTAGE - The hydrogen storage cavities are arranged parallel to each other, so as to evenly distribute the temperature of inner side hydrogen storage material. The storage unit prevents the hydrogen storage material from being contaminated by dust in a better manner, so as to extend the service life of the hydrogen storage material. The storage unit can realize better structure of the coupling fuel cell, so as to realize efficient thermal management of the hydrogen storage and the fuel cell.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a coupling fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows an exploded perspective view of a hydrogen storage unit.
NOVELTY - Biological treating method for oil field polymer-containing sewage, comprises: (a) treating the oil field polymer-containing sewage by a floatation process, and performing bio-augmentation on the sewage from the floatation process by anaerobic process; (b) strengthening the yielding water from the anaerobic process by aerobic process and bringing the yielding water generated to a filter system; (c) bringing the yielding water from the filter system to a twice settling tank and finishing the efficient biological treatment of oil field polymer-containing sewage.    USE - The biological treating method is useful for oil field polymer-containing sewage.    ADVANTAGE - The biological treating process achieves stable running of the treatment of oil field polymer-containing sewage. The biological treating process is easy and can be carried out with small investment and there is no secondary pollution and it is an environmental-friendly process.    DETAILED DESCRIPTION - Biological treating method for oil field polymer-containing sewage, comprises: (a) treating the oil field polymer-containing sewage through floatation process and performing bio-augmentation on the sewage from the floatation process by anaerobic process, where the hydraulic residence time is 24-36 hour; (b) strengthening the yielding water from the anaerobic process by aerobic process, where the hydraulic residence time is 10-14 hour and bringing the yielding water generated to a filter system, where the hydraulic residence time is 5-8 hour; (c) bringing the yielding water from the filter system to a twice settling tank, where the hydraulic residence time is 5-6 hour and finishing the efficient biological treatment of oil field polymer-containing sewage.
NOVELTY - A biomass environment pollution coal comprises fuel and an adhesive composition which includes soluble glass. The fuel is a mixture composed of biomass powdered carbon and anthracite duff. The concentration of adhesive composition is controlled at modulus of 3.2. The content of soluble glass adhesive composition of the raw material of coal is 12-30 weight% and the content of fuel of the raw material of coal is 88-70 weight%.    USE - Biomass environment pollution coal.
NOVELTY - A molded coal contains charcoal dust and adhesive composition which consists of soluble glass.    USE - Molded coal.    ADVANTAGE - The molded coal has high purity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of molded coal, which involves mixing raw material containing charcoal dust and adhesive composition, stirring, pressing and drying.
NOVELTY - Crop waste is dried such that moisture content in crop waste is 18-30%, crushed and stirred to obtain powder having small particles. Then, the obtained powder is mixed with clay additive, and extruded at 150-210 degrees C under pressure of 300-600 Psi/cm2, to obtain solid fuel block.    USE - Method for producing solid fuel block.    ADVANTAGE - The method efficiently provides solid fuel block, and is environmental-friendly and safe.
NOVELTY - Composted cow dung cultivation substrate for cultivating earthworm and its preparation is claimed. The preparation cultivation substrate comprises: (i) adding fermentation strain (13-17 kg) to fresh cow dung (1 ton), adding water (40-50 kg), adding brown sugar (0.8-1.2 kg) to water, spraying the fermentation strain to the dung stack and fermenting under anaerobic condition; (ii) regulating the pH of the fermented fresh cow dung to 6.5-7.5; and (iii) adding water (100 kg) to urea (0.65 kg), saccharine (8 g) and pineapple essence (6 g) and spraying to the cultivation substrate.    USE - The composted cow dung cultivation substrate is useful for cultivating earthworm.    ADVANTAGE - The fermenting time of the compost is short, and the culture medium can be fully fermented. The compost does not cause any harmful effects to the earthworm.    DETAILED DESCRIPTION - Composted cow dung cultivation substrate for cultivating earthworm and its preparation is claimed. The preparation cultivation substrate comprises: (i) adding fermentation strain (13-17 kg) to fresh cow dung (1 ton), adding water (40-50 kg), adding brown sugar (0.8-1.2 kg) to water, directly spraying the fermentation strain to the dung stack till the water flows out from the base layer of the dung stack, and fermenting under anaerobic condition; (ii) regulating the pH of the fermented fresh cow dung to 6.5-7.5 to obtain the cultivation substrate; and (iii) for 1 mm3 of cultivation substrate, adding water (100 kg) to urea (0.65 kg), saccharine (8 g) and pineapple essence (6 g) to dissolve, spraying half to the cultivation substrate, overturning, and spraying the remaining half to the cultivation substrate, where the cultivation substrate can be used after 2-3 days.
NOVELTY - The method involves mixing 20-100 parts weight of obnoxious in-situ control covering material with 0.1-80 parts weight of garbage landfill site covering to prepare a garbage landfill site obnoxious in-situ control covering. 0.1-10 parts of deodorizing microorganism is added in the covering and mixed, to form middle, final and initial coverings. The initial covering is used to cover surface of an embedded garbage, and is flattened and pressed. The thickness of initial covering of garbage landfill site, middle and final coverings are in range of 10-20 cm, 25-35 cm and 45-55 cm, respectively.    USE - In-situ control method for obnoxious gas in garbage landfill site.    ADVANTAGE - The method effectively improves and monitors the odor pollution control effect in the garbage embedding process, reduces the use of the covering, optimizes the storage capacity and prolongs the useful time of the garbage landfill site. The method controls the waste to reduce the exhaust of obnoxious gas and facilitates resource recycling of agricultural and municipal solid wastes so as to obtain social, environment and economic benefits.
NOVELTY - The apparatus has a manifold for introducing contaminated gas i.e. natural gas, into a vessel. The manifold introduces the gas into the vessel below a top level of a pool of contaminant-absorbing liquid. A flow disperser i.e. perforated plate, is provided within the vessel and positioned above the manifold and beneath the level of the pool. A set of spray nozzles is arranged within the vessel and positioned above the level of the pool to introduce contaminant-absorbing liquid counter-current to flow of contaminated gas in the vessel.    USE - Apparatus for treating contaminated gas e.g. natural gas (claimed) such as carbon dioxide and hydrogen sulfide, using an amine plant during oil and gas production.    ADVANTAGE - The apparatus allows removing contaminants from the natural gas in an efficient manner. The apparatus has compact structure, and can be easily placed on two skid mounted units while reducing cost of relocating the amine plant of comparable capacity. The apparatus reduces construction cost by eliminating the need for crane and tall towers. The apparatus reduces amount of amine circulated, so that that an initial charge of amine is inexpensive while minimizing fuel cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for treating contaminated gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a gas treating apparatus.    Amine plant (10)    Gas treating system (12)    Inlet conduit (16)    Humidifier (18)    Mixer (26)
NOVELTY - Producing a biofuel comprises: hydrolyzing an extract from a seaweed in the presence of a heterogeneous catalyst; and converting the hydrolysate through enzymatic fermentation or chemical reaction into the biofuel. The seaweed is red algae, brown algae and/or green algae.    USE - The method is useful for producing a biofuel comprising an oxygen-containing compound (ethanol, propanol, butanol, pentanol and/or hexanol) or a biohydrocarbon (biogasoline, biodiesel, a jet fuel and/or an additive) (all claimed).    ADVANTAGE - The method makes use of heterogeneous catalysts that can be recycled without a load of wastewater treatment, hence making the method simpler and cost-effective (as by-product treatment expenses are eliminated). The heterogeneous catalyst can be applied to a fixed bed reactor, which makes it possible to carry out the method in a continuous manner, where a smaller reactor can be employed at higher efficiency and productivity.
NOVELTY - The method involves generating (225) primary absorption spectrum based on ratio of primary spectral measurement from non-absorptive gas having no infrared absorptions in specified wavelength range of interest, and secondary spectral measurement from sample gas comprising biogas. The concentration of siloxane compound is calculated (235) using secondary absorption spectrum based on individual absorption spectrum for known concentration of siloxane compound.    USE - Method for monitoring siloxane compound in biogas used for turbine generator.    ADVANTAGE - The siloxane compound can be monitored in real time at measuring site without need for analyzing sample at laboratory. The rise in siloxane levels can be sensed by in-line continuous monitor such that operator can be notified automatically and hence unnecessary exposure of turbines to silicon dioxide is prevented.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) system for monitoring siloxane compound in biogas; and    (2) computer readable product for monitoring siloxane compound in biogas.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating the process of monitoring siloxane compounds in biogas.    Step for providing non-absorptive gas (205)    Step for providing biogas (215)    Step for generating primary absorption spectrum (225)    Step for generating secondary absorption spectrum (230)    Step for calculating concentration of siloxane compound (235)
NOVELTY - Water electrolysis system comprises a water electrolysis apparatus for electrolyzing water with an electric current supplied from a direct current (DC) power supply to generate hydrogen and oxygen; a water adsorption apparatus disposed downstream of and connected to a hydrogen outlet of water electrolysis apparatus, for adsorbing water contained in the hydrogen discharged from hydrogen outlet; a first pressure regulating valve connected between the hydrogen outlet and the water adsorption apparatus; and a second pressure regulating valve connected downstream of water adsorption apparatus.    USE - The water electrolysis system is useful for manufacturing high-pressure hydrogen.    ADVANTAGE - The invention provides water electrolysis system of simple structure which is capable of reliably preventing water contained in hydrogen from passing through a water adsorption apparatus and hence efficiently supplying desired dry hydrogen.
NOVELTY - The furnace has a body (2) whose upper side is provided with an air outlet (11) and lower side is connected with an ash cabin (8). A water cooling bracket (5) is installed between the body and the ash cabin. An ash scraping plate (3) is arranged on the water cooling bracket for reciprocating linear motion on a fire grate (4). A water tank (6) opposite to the ash scraping plate is arranged at an outer side of the body. Two ends of the plate are placed into the water tank, and the water cooling bracket is connected with the water tank. An air distributor (7) is connected with a blower (12).    USE - Industrial gasification furnace for gasifying xylose and furfural residue.    ADVANTAGE - The furnace is simple in structure and convenient to use. The furnace can gasify the xylose and furfural residue to generate combustible gas, thus increasing gasification area and gasification rate. The furnace is environment-friendly and prevented from being clogged with slag, thus protecting a fire grate. The furnace has high production efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of an industrial gasification furnace.    Body (2)    Ash scraping plate (3)    Fire grate (4)    Water cooling bracket (5)    Water tank (6)    Air distributor (7)    Ash cabin (8)    Air outlet (11)    Blower (12)
NOVELTY - The system (10) has gas-liquid separation mechanism (78) to separate water and oxygen from the water discharged from water electrolysis apparatus (12), and oxygen-containing fluid. A pressure detector (86) detects the pressure of water discharged to separation mechanism, and oxygen-containing fluid. A controller (22) judges the presence or absence of hydrogen leakage based on detected pressure value.    USE - Water electrolysis system for generating hydrogen gas used as fuel gas for polymer electrolyte fuel cell.    ADVANTAGE - The presence or absence of hydrogen leakage can be detected easily and reliably. Favorable water electrolysis can be performed.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the water electrolysis system. (Drawing includes non-English language text)    Water electrolysis system (10)    Water electrolysis apparatus (12)    Controller (22)    Gas-liquid separation mechanism (78)    Pressure detector (86)
NOVELTY - Hydrolase and sulfuric acid are added to pulp slurry containing regenerated pulp and pH of pulp slurry is adjusted to 5.8-8.2 using sulfuric acid. Then, cationic polymer having molecular weight of 100000-7000000 is added to the obtained product. Thus, manufacture of regenerated pulp containing paper is carried out.    USE - Manufacture of regenerated pulp containing paper.    ADVANTAGE - The method easily provides high quality regenerated pulp containing paper, without machine defects and deterioration of paper.    DESCRIPTION OF DRAWING(S) - The drawing shows block diagram of manufacture of regenerated pulp containing paper. (Drawing includes non-English language text)
NOVELTY - A fertilizer comprises (wt.%) slaked organic matter (30-60), inorganic fertilizer (30-54), chelating micronutrient fertilizer (3-7), microbiological agent (5-7), complex ore (2.5-4), and water quality improver (1).    USE - A fertilizer used in freshwater aquiculture (claimed) for growth of palatable biological baits for fishes, e.g. diatom, Euglena, Cryptomonas, and Chrysophyceae.    ADVANTAGE - The fertilizer improves utilization rate of mineral nutrients, and prevents pollution of water body due to over addition of trace elements.
NOVELTY - The gasifier has a gas-delivering pipe (17) whose tail part is connected with a high end of a sewage pipe (1). Another sewage pipe (11) is connected with a control valve (12). A lower end of the latter sewage pipe is connected with a tail of the former sewage pipe. A waste gas pipe (15) is connected with the gas-delivering pipe. A waste gas pipe valve (16) is installed on the gas-delivering pipe. A blast blower (5) is connected with an air pipe (10). A tail part of the air pipe is fixedly connected with a tail part of the gas-delivering pipe or a gas inlet of a furnace plate (4).    USE - Straw gasifier for cooking rice and boiling water.    ADVANTAGE - The gasifier has high straw utilization rate and provides strong firepower on the furnace plate. The gasifier saves straw, and avoids leakage of smoke, thus reducing environment pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a straw gasifier.    Sewage pipes (1, 11)    Furnace plate (4)    Blast blower (5)    Air pipe (10)    Control valve (12)    Waste gas pipe (15)    Waste gas pipe valve (16)    Gas-delivering pipe (17)
NOVELTY - Hydrogen manufacturing system comprises hydrogen-producing material container (1) which accommodates hydrogen producing material (10), liquid supply part (11) which supplies water or aqueous alkali solution to the hydrogen-producing material, and liquid selection determination part (8) which monitors production of hydrogen and determines whether liquid should be supplied to the hydrogen producing material after production of hydrogen.    USE - Hydrogen manufacturing system for a fuel cell system (claimed).    ADVANTAGE - Restarting time until next hydrogen production is shortened.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the hydrogen manufacturing system. (Drawing includes non-English language text).    Hydrogen-producing material container (1)    Liquid selection valve (2)    Liquid selection determination part (8)    Hydrogen producing material (10)    Liquid supply part (11)
NOVELTY - Sludge containing 10 weight% of microorganism is embedded with wool scouring sludge, fermented, and compost is formed. The wool scouring sludge contains water, organic substance, nitrogen, phosphorus and potassium. The microorganism is bacteria, fungus and/or actinomycetes. Bacteria is chosen from Bacillus substilis, Pseudomonas aeruginosa, and Bacillagjnosus. The fungus is chosen from Aspergillus niger and Penicillium simplicissim. Actinomycete is Streptomyces badius.    USE - Fermentation of wool scouring litter microorganism.    DETAILED DESCRIPTION - Sludge containing 10 weight% of microorganism is embedded with wool scouring sludge, fermented at 45-65 degrees C for 15-30 days, and compost is formed. The wool scouring sludge contains 5-50% of water, 40-80% of organic substance, 8-20% of nitrogen, 5-15% of phosphorus and 3-10% of potassium. The microorganism is bacteria, fungus and/or actinomycetes. The number ratio of bacteria, fungus and actinomycetes is 10-30:0.5-2.5:0-1.5. Bacteria is chosen from Bacillus substilis, Pseudomonas aeruginosa, and Bacillagjnosus. The number ratio of B.substilis, P.aeruginosa and B.gjnosus is 1-5:0.5-3:0.3-1.5. The fungus is chosen from Aspergillus niger and Penicillium simplicissim. The number ratio of A. niger and P.simplicissim is 1-3:0.5-1.5. Actinomycete is Streptomyces badius. The total content of organic substance, nitrogen, phosphorus and potassium in the compost is 30-80%, 3-15%, 2-10% and 1-7%, respectively.
NOVELTY - A refrigerant comprises propane (55-10 weight%) and difluoromethane (45-90 weight%).    USE - Refrigerant.    ADVANTAGE - The refrigerant is environmental-friendly.
NOVELTY - Antioxidant (1-2 parts weight) is added to alcohol (100 parts weight) and mixed. The obtained mixture is heated at 50-60 degrees C and electromagnetically stirred. The animal fatty acid ethyl ester is added to the obtained antioxidant solution (100 parts weight), to obtain biodiesel.    USE - Preparation of biodiesel.    ADVANTAGE - The method efficiently and economically provides biodiesel by simple process without environmental pollution.
NOVELTY - A natural antioxidant is obtained by extracting one or mixture of Smallanthus sonchifolius leaves, Acer truncatum and auranti cortex siccatus using ethanol. The natural antioxidant contains phenolic acid substance and flavone substance.    USE - Natural antioxidant is used for improving storage stability of biodiesel (claimed).    ADVANTAGE - The natural antioxidant is economical, and improves physical and chemical properties of biodiesel.
NOVELTY - City sludge (71.5-98%) having water content of more than 80% and biomass powder (2-28.8%) as raw material are mixed. The mixture is dehydrated, and water content is reduced to less than 50% to obtain pre-treated mixed material. Biomass powder (30-40 %mass) is doped into the mixture. The water content is reduced to less than 20% to obtain dehydrated solid sludge. Additive is added, agitated and transferred to molding machine to obtain molded solid fuel. The fuel is then packaged to obtain finished product.    USE - Manufacture of solid fuel.    ADVANTAGE - The solid fuel is reliably and stably produced without affecting the environment.    DETAILED DESCRIPTION - City sludge (71.5-98%) having water content of more than 80% and biomass powder (2-28.8%) as raw material are mixed and added to an agitator and mixed uniformly. The mixture is transferred to a spiral pressure filter and dehydrated. The water content is reduced to less than 50% to obtain dehydrated and pre-treated mixed material. Biomass powder (30-40 %mass) is doped into the mixture. The water content is reduced to less than 20% to obtain dehydrated solid sludge. Additive is added, agitated and transferred to a low-pressure double-stick molding machine to obtain molded solid fuel. The fuel is then packaged to obtain finished product.
NOVELTY - A biodiesel is generated by using pulp and kernel of woody oil-bearing plant as raw material, where plant is avocado; peeling off; extracting triglyceride and fatty acid for 5-10 minutes; transesterifying; and performing ester exchanging reaction.    USE - Method of generating biodiesel (claimed).    ADVANTAGE - The method develops biomass fuel energy industrial system.
NOVELTY - Electric-heating fly incense mat comprises a paper piece coated with pyrethroid.    USE - The electric-heating fly incense mat is useful as a fly repellent.    ADVANTAGE - The electric-heating fly incense mat is environmental friendly and is harmless to people and livestock.
NOVELTY - Use of alpha -amyrin for preparing acaricidal agent, is claimed.    USE - The acaricidal agent is useful for preventing mites on fruits, vegetables and cash crops.    ADVANTAGE - The acaricidal agent is highly effective, non-toxic and environmental friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an acaricide emulsifiable concentrate, comprising alpha -amyrin (20-50%), solubilizer (20-50%), a synergistic agent (10%), an emulsifier (10%) and a penetrating agent (10%).
NOVELTY - Biotechnological process for producing power resources preferably with a process mentioned in the German patent application 10 2008 004 732.5, comprises: collecting carbon source from the atmosphere or producing carbon source from waste water; performing methanogenesis by a hydrothermal carbonization of biomass; and converting biomass with water and at least one catalyst in a pressure vessel to substances e.g. coal and/or oil by temperature- and/or pressure increase.    USE - The biotechnological process is useful for producing power resources e.g. coal and/or oil.    ADVANTAGE - The process significantly improves the efficiency of current biogas plant as well as reduces the carbon dioxide content of such plants.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a reactor for carrying out the above method, comprising at least one storage vessel and at least one microreactor to the entry of gases and/or solutions or suspensions and/or dispersions of the reactor contents.
NOVELTY - The method involves detecting an engine parameter when an internal combustion engine (110) is in an idling state. Injection of a quantity of gaseous fuel e.g. methane, is timed when a piston is near a top dead center. Temperature of exhaust gas exiting from a combustion chamber is controlled such that the temperature is above predetermined temperature that is defined by an operating temperature range. The temperature of the exhaust gas is increased by increasing a delay in timing for injecting the gaseous fuel.    USE - Method for controlling a direct-injection gaseous-fueled internal combustion engine that is utilized in an over-the-road heavy vehicle.    ADVANTAGE - The temperature of the exhaust gas is increased by increasing the delay in timing for injecting the gaseous fuel, thus improving the conversion efficiency of a selective catalytic reduction converter that is operative to reduce levels of nitrogen oxide.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a direct-injection gaseous-fueled internal combustion engine system comprising an exhaust after-treatment subsystem and an exhaust gas recirculation loop.    Internal combustion engine system (100)    Internal combustion engine (110)    Diesel fuel delivery subsystem (112)    Gaseous fuel delivery subsystem (114)    Exhaust gas line (120)
NOVELTY - Catalytic composition preparation involves forming sulfonated metal oxides by impregnating gel with a carrier solution of a sulfonic compound. The formed compound is calcined to obtain the desired catalyst. The metal oxide is made of metal selected from IVB, VIIB or VIII group of the periodic table.    USE - Method for preparing catalytic composition used for isomerization of n-butane.
NOVELTY - A catalyst (I) is obtained by impregnating copper and molybdenum in ceria-zirconia carrier. The weight ratio of copper and molybdenum is 3-10:1.    USE - Catalyst used for manufacturing synthesis gas by water gas shift process, for fuel cell vehicle, domestic fuel reformer, fuel reformer for polymer electrolyte fuel cell, hydrogen station and petrochemical process (all claimed).    ADVANTAGE - The catalyst has high catalytic activity, thermal cycle durability and improves the efficiency of water gas shift reaction.    DETAILED DESCRIPTION - A catalyst is obtained by impregnating copper and molybdenum in ceria-zirconia carrier. The weight ratio of copper and molybdenum is 3-10:1. The catalyst has composition of formula: Cu-Mo/CexZr1-xO2.    x=0.0001-1 (excluding 1).    INDEPENDENT CLAIMS are included for the following:    (1) manufacture of the catalyst; and    (2) manufacture of synthesis gas using the catalyst.
NOVELTY - The method involves manufacturing carbon slurry by mixing a hydrophobic binder and a dispersive medium, where the dispersive medium is formed of 50-95 weight percentages of ethylene glycol, 2-40 weight percentages of water, 0.05-10 weight percentages of dispersing agent e.g. surfynol (RTM: nonionic surfactant) or Triton (RTM: nonionic surfactant), and carbon powder. The carbon slurry is coated by a material. A gas diffusion layer is formed by drying the coated carbon slurry.    USE - Method for manufacturing a gas diffusion layer for an electrode of a fuel cell (all claimed). Uses include but are not limited to a polymer electrolyte fuel cell e.g. polymer electrolyte membrane fuel cell (PEMFC), phosphoric-acid fuel cell (PAFC), molten carbonate fuel cell (MCFC) and solid oxide fuel cell (SOFC).    ADVANTAGE - The method enables improving the battery capacity of the fuel cell, and facilitates the mass production of the fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical representation illustrating a gas diffusion layer manufacturing method.'(Drawing includes non-English language text)'
NOVELTY - Disclosed is a process for production of biofuel like biodiesel, biopellets, biofertilizer, pellets for feed and pellets for food from algae at industrial scale. The process describes cultivation of suitable marine algae using a closed system e.g., photobioreactor or open system e.g., tank, circular pond and/or raceway pond. The process further involves growing algae sequentially in heterotrophic and autotrophic manner, where (a) the heterotrophic growth is achieved by cultivating algae to a high cell density in a closed system in presence of a carbon source; (b) the portion of the growth inoculum is transferred for photoautotrophic cultivation into open system or a photobioreactor; (c) the algae is allowed to grow in autotrophic manner using carbon dioxide generated during heterotrophic growth and using nutrients provided from reject water or other waste generated during process, in presence of minimum amount of nutrients provided additionally. After achieving target algae cell mass, algae cell is subjected to stress to achieve accumulation of lipid at high concentration and further processed to use for production of biofuel and extracted algae cell mass is used as raw material for fermentation using suitable microorganism to produce bioethanol and/or biomethane. Image 0/0
NOVELTY - Removing and recycling heavy metal from sludge for producing fertilizer, involves adding special treating solution to the sludge and agitating to obtain gelatinous slurry, centrifuging the slurry repeatedly by discharging upper wastewater, inoculating the obtained bottom sludge with microorganism and adding additives and agitating, fermenting the agitated sludge, granulating and pelleting the granulated sludge, cooling and packing the pellets to obtain organic fertilizer.    USE - The method is useful for removing and recycling heavy metal from sludge for producing fertilizer.    ADVANTAGE - The method is environment-friendly, inexpensive and economical.    DETAILED DESCRIPTION - Removing and recycling heavy metal from sludge for producing fertilizer, involves adding the sludge to a mixer for mixing, heating and pressurizing during the mixing process, adding special treating solution to the mixed sludge for treatment, agitating the sludge and solution to obtain gelatinous slurry, centrifuging the slurry for first time, discharging upper wastewater, adding the special treating solution to the bottom sludge and centrifuging for second time, repeating the two centrifugation steps, squeezing the sludge after subjecting into three centrifugation steps and then transferring the obtained sludge into mixing agitator, inoculating the obtained sludge with microorganism and adding additives, mixing in agitator, fermenting the agitated sludge, granulating the fermented product, pelleting the granulated sludge, cooling and packing the pellets to obtain organic fertilizer.
NOVELTY - Pesticide prepared from plant and microorganism source, comprises thunder god vine, tobacco leaf, kuhseng and liquorice in a weight ratio of 100:40-95:50-75:2-8:5-17:5-20.    USE - The pesticide is useful for killing 20 types of pests e.g. aphids, cotton bollworms and cabbage caterpillars and preventing and treating 5 types of diseases e.g. fusarium wilt and yellows.    ADVANTAGE - The pesticide has a broad spectrum activity, high efficiency, low toxicity, does not cause resistance and has long active duration. The composition is biodegradable, leaves no residue, causes no pollution, thus it is safe and environmental friendly.
NOVELTY - N-methylpiperazine is added into levofloxacin fluoride carboxylic acid, reacted and concentrated, to obtain residue in which water is added, neutralized using strong alkali and filtered, to obtain levofloxacin crude product.    USE - Synthesis of levofloxacin.    ADVANTAGE - The levofloxacin is manufactured with reduced generation of offensive odor and without affecting environment.
NOVELTY - The waste water pre-treated by physical precipitation is passed into a tower biological filter tank, and laser scanning is performed for the sewage for one time. The ultrasonic processing is carried out for the sewage for one time, and UV irradiation is executed for the sewage for treating organic pollutant, chroma, sulfide and basicity in the jean sewage.    USE - Pre-treatment production method of jean sewage treatment.    ADVANTAGE - The height of the tower biological filter tank is reduced, and the blast equipment such as fan is not needed. The energy consumption is reduced and the initial cost is decreased. The sludge quantity is largely decreased, and secondary pollution is prevented. The operation management is made convenient.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic perspective view of the jean sewage treatment apparatus.    Ultrasonic transducer (1)    Ultrasonic generator (2)    Frequency converter (3)    Sewage pump (4)    Spray pipe (5)
NOVELTY - A quadrate ignition molded coal has upper ignition layer (30 %mass) and lower combustion layer (70 %mass). The ignition layer contains (in weight%) raw coal (38-60) biomass (8-10), charcoal (15-35), combustion improver (5-8), catalyst (1-2), bentonite (5-9), and modified starch (0.4-1). The combustion layer contains raw coal (88-92), bentonite (7-11) and modified starch (0.4-1).    USE - Quadrate ignition molded coal.    ADVANTAGE - The quadrate ignition molded coal is economical, safe and easily ignited, and manufactured by simple process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of quadrate ignition molded coal.
NOVELTY - Hydrogen production using biomass fermentation-photosynthesis coupling method, involves crushing and hydrolyzing biomass to starch and organic matter, adding the hydrolyzed organic mixture in fermentation culture medium at 25-40 degrees C for 2-3 days, fermentation liquid after producing hydrogen is inoculated with photosynthetic bacteria and fermentation liquid continually produce hydrogen at 20-40 degrees C for 5-8 days, biomass is repeatedly added after producing hydrogen in photosynthesis to produce hydrogen.    USE - The method is useful for producing hydrogen by biomass fermentation-photosynthesis coupling method (claimed).    ADVANTAGE - The method converts high amount of biomass into hydrogen and thus suitable for large scale production.    DETAILED DESCRIPTION - Hydrogen production using biomass fermentation-photosynthesis coupling method, involves (a) crushing biomass at 60-120 degrees C and hydrolyzing the crushed biomass to starch and other macromolecular organic material containing sugar, (b) adding the hydrolysed organic mixture in the fermentation culture medium where the temperature in hydrogen producing reaction is controlled at 25-40 degrees C at pH 5.5-7.5 and the hydrogen producing time is 2-3 days, (c) inoculating the fermentation liquid with photosynthetic bacteria and then the fermentation liquid continually produce hydrogen where the temperature is controlled at 20-40 degrees C at pH 6.0-7.5 and illumination intensity is 2000-8000 lux, and (d) then the biomass is repeatedly added after production of hydrogen in photosynthesis, where the fermentation process of producing hydrogen and the photosynthetic process of producing hydrogen are done in a same reactor.
NOVELTY - Preparation of landiolol hydrochloride comprises reacting N-(2-aminoethyl)-4-morpholinecarboxamide ethanedioate for 7-24 hours under alkaline condition; reacting with ((S)-2,2-dimethyl-1,3-dioxolan-4-yl)methyl-3-(4-hydroxyphenyl)propanoate and (S)-(+)-glycidyl nosylate in a polar solvent; reacting with anhydrous oxalic acid in anhydrous methanol at lesser than 40 degrees C, placing in an ice water bath, and stirring for 0.5 hour; and dissolving in a sodium bicarbonate solution, adding to ammonium chloride, regulating pH value to 3 with hydrochloric acid, and adding to sodium chloride.    USE - Method for the preparation of landiolol hydrochloride (claimed) used for inhibiting the increase of cardiac activity caused by catecholamine, and for improving tachycardia arrhythmia.    ADVANTAGE - The method is simple, and environment-friendly.    DETAILED DESCRIPTION - Preparation of landiolol hydrochloride comprises reacting N-(2-aminoethyl)-4-morpholinecarboxamide ethanedioate for 7-24 hours under alkaline condition to obtain N-(2-aminoethyl)-4-morpholinecarboxamide (I); reacting ((S)-2,2-dimethyl-1,3-dioxolan-4-yl)methyl-3-(4-hydroxyphenyl)propanoate, (S)-(+)-glycidyl nosylate, and (I) for 18 hours in a polar solvent to obtain ((4S)-2,2-dimethyl-1,3-dioxolan-4-yl)methyl 3-(4-((2S)-2-hydroxy-3-(2-(morpholine-4-carbonylamino)ethylamino)propoxy)phenyl)propanoate (II); reacting (III) with anhydrous oxalic acid in anhydrous methanol at lesser than 40 degrees C, placing in an ice water bath, stirring for 0.5 hour to obtain 4-morpholinecarboxamide-N-(2-aminoethyl)-ethanedioate (III); and dissolving (III) in a sodium bicarbonate solution, adding to ammonium chloride, regulating pH value to 3 with hydrochloric acid, adding to sodium chloride until the solution is saturated.
NOVELTY - Preparation of 1-(4-(3-(4-(6-fluoro-1,2-benzoisoxazol-3-yl)-1-piperidinyl)propoxy)-3-methoxyphenoxy)ethanone comprises reacting 6-fluoro-3-(4-piperidinyl)-1,2-benzoisoxazole hydrochloride and 1-(4-(3-chloropropoxy)-3-methoxyphenyl)ethanone in an inorganic alkaline aqueous solution.    USE - Method for the preparation of 1-(4-(3-(4-(6-fluoro-1,2-benzoisoxazol-3-yl)-1-piperidinyl)propoxy)-3-methoxyphenoxy)ethanone (claimed).    ADVANTAGE - The method achieves high yield, is inexpensive, and is environment friendly.
NOVELTY - Aerosol formulation is prepared by using coal-based acid, potassium ferrate and water, where aerosol has 350g total weight and is a cylindrical body with length of 200cm, diameter of 80cm and central hole diameter of 15cm.    USE - Aerosol formulation used in greenhouses (claimed) and used for killing insect pests and treating multiple plant diseases.    ADVANTAGE - The aerosol formulation shows insecticidal effect for long time without causing public hazard, pollution, pesticide residue and drug resistance in compare to common agrochemicals.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for production of the aerosol formulation, which involves using metalaxyl, carbendazol, dicofol, cypermethrin and malathion in the ratio of 1:1:2:1:2.
NOVELTY - A dispersible liquid (L1) comprises spinosad and lambda-cyhalothrin, chlorfenapyr, lufenuron or chlorpyrifos at mass ratio of 1:1-300, and methyl ester of vegetable oil as substrate.    USE - Dispersible liquid (L1).    ADVANTAGE - The liquid (L1) has strong adhesion force; improves bioavailability of effective component and reduces using amount of agrochemical; prolongs drug resistance of the pest; uses biodegradable methyl ester of vegetable oil instead of organic solvent of aromatic hydrocarbons, thus effectively reducing photochemical pollution of agrochemical and protecting ecological environment; and forms film on target surface, thus increasing precipitating capability of effective component on surface of target and capability of penetrating wax layer on surface of target.
NOVELTY - Fast composting of a mushroom fertilizer comprising (in kg) dry straw hood (1000-10000), dry straw (500-5000), dry scandent hop (200-2000), dry soybean stem (200-2000), calcium super phosphate (10-150), fresh pig manure (1000-10000), fresh cow manure (1000-10000), soybean cake powder (20-300), gypsum powder (20-200), urea (5-50) and lime powder (20-200), is claimed.    USE - The method is useful for fast composting of a mushroom fertilizer.
NOVELTY - Traditional Chinese medicinal composition comprises (in parts weight): pseudoginseng (3.25-3.75), Angelica (1-1.5), Achyranthes (0.5-1), medlar (1.25-1.75), herba epimedii (0.5-1), oyster (0.5-1), glossy privet fruit (0.5-1), fiveleaf Gynostemma herb (1-1.5), colla corii asini (0.5-1), black bean (0.5-1), and licorice (0.5-1).    USE - The traditional Chinese medicinal composition in the form of capsule is useful for treating osteoporosis and degenerative osteoarthropathy (claimed).    ADVANTAGE - The traditional Chinese medicinal composition has excellent compatibility, causes no side effects, is environmental-friendly and inexpensive, and can be easily produced.    DETAILED DESCRIPTION - Traditional Chinese medicinal composition comprises (in parts weight): pseudoginseng (3.25-3.75), Angelica (1-1.5), Achyranthes (0.5-1), medlar (1.25-1.75), herba epimedii (0.5-1), oyster (0.5-1), glossy privet fruit (0.5-1), fiveleaf Gynostemma herb (1-1.5), colla corii asini (0.5-1), black bean (0.5-1), and licorice (0.5-1), and is prepared by heating pseudoginseng for 1 hour at 110 degrees C to obtain processed pseudoginseng, drying and crushing the extract to obtain mixture, and then sieving the obtained mixture through 120-mesh to obtain powder, removing impurities from other raw materials, drying and crushing the materials, sieving the crushed mixture through 120 mesh to obtain mixture, adding processed pseudoginseng powder to the obtained mixture, uniformly mixing the obtained mixture to obtain tablet, coating the obtained tablet with ethyl cellulose, shell-lac and seaweed gel, and finally filling the coated product into capsules.
NOVELTY - Intensifier comprises beta -glucosan, mannooligosaccharide, immunoregulatory factor and polyisomaltose, where the amount of each raw material is 1-40 wt.%.    USE - The agent is useful for producing feed for aquaculture animals chosen from fish, shrimp, crab, eel, sea cucumber and turtle for increasing immunity, for preventing disease (all claimed) and for improving the growth of aquaculture animals.    ADVANTAGE - The agent is cost-effective and improves resistance of aquaculture animals against disease causing organisms. The agent is non-toxic, and causes less environmental pollution without any residual leftovers.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing the intensifier, which involves mixing levamisole hydrochloride, FK-565 and muramyldipeptide (MDP) to obtain immunoregulatory factor, adding beta -glucosan, mannooligosaccharide and polyisomaltose, and mixing uniformly to obtain the intensifier.
NOVELTY - Fertilizer production uses aquatic plant, which includes sink boat system (1) and barge carriers (4). The aquatic plant is present on watershed, vehicles and pipelines. The aquatic plant worked as conveyor, sludge treatment plants and composting plant for sanitizing waste water.    USE - Method for producing fertilizer used as earthworm humus (claimed) in agricultural production.    ADVANTAGE - The fertilizer producing method enables to improve water quality.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of fertilizer producing plant.    Sink boat system (1)    Barge carriers (4)
NOVELTY - Supersaturated fertilizer solution comprises a solution of potassium nitrate (20-60 wt.%) with exopolysaccharide (0.2-0.7 wt.%) in water (balanced water).    USE - Supersaturated fertilizer solution used for plantation (claimed).    ADVANTAGE - The supersaturated fertilizer solution is stable, has less transportation cost and emits less amount of carbon dioxide to the atmosphere.
NOVELTY - The dryer has a conveying unit (120) having screw conveyors (121) for conveying the waste from outside to drying furnaces (110). A heat exchange unit (140) dries the supplied waste by exchanging heat with high-temperature steam. A microwave emission unit (130) emits microwave towards the waste to increase the heat for drying the waste in the drying furnaces. A vent unit (150) delivers the air to increase the air flow inside the drying furnaces. The furnaces have a reflector to reflect microwave in the lower side of the screw conveyor towards waste.    USE - Dryer for manufacturing fuel derived from refuse such as food refuse, waste papers, wastewood, waste synthetic resin, waste synthetic fiber, the polygon natural/synthetic leather etc.    ADVANTAGE - The time required to exhaustion can be shortened and resource consumption can be decreased. The waste heat is recycled, and the power consumption can be reduced. Hence the drying efficiency can be enhanced and the manufacturing cost of the refuse-derived fuel can be reduced.    DETAILED DESCRIPTION - The dryer has vent unit that delivers the air to increase the air flow inside the drying furnaces. A guidance duct guides the air from vent unit to drying furnace. Several exhaust ducts (117) eject the exhaust gas from drying furnace to outside.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the dryer.    Drying furnaces (110)    Exhaust duct (117)    Conveying unit (120)    Screw conveyors (121)    Microwave emission unit (130)    Heat exchange unit (140)    Vent unit (150)
NOVELTY - An amino acid nano fertilizer contains nano-sheet of layered clay minerals. The nano-sheet has swelling layer and amino acid material. The amino acid material is provided on surface or between the layered clay minerals. The amino acid material is reacted with surface electric charge of clay mineral, to form nano sheet. The nano sheet has uneven distance between layered clay minerals, and 3 dimensional structure.    USE - Amino acid nano fertilizer.    ADVANTAGE - The amino acid nano fertilizer has excellent storage stability and sustained-release property, has reduced environmental contamination, and can be manufactured rapidly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of amino acid nano fertilizer.
NOVELTY - The apparatus has a heating system including a heating coil and a plane heater, which is placed within the floor of a load chamber (10), and is heated at a temperature of 200 degrees C to 300 degrees C. The livestock waste is loaded in the load chamber which is agitated by a stirrer. The stirrer main structure (40) is provided with a right-and-left screw (50) for agitating the waste, and a breaking portion (70) with a wing segment for fracturing the waste.    USE - Composting apparatus for livestock waste e.g. cow dung, pig ordure and fowl droppings.    ADVANTAGE - The fermentation efficiency of the livestock waste can be enhanced and the compost of ampholyte can be produced. The livestock waste can be processed hygienically.    DETAILED DESCRIPTION - A motor (M) drives a roller (R) fitted in a rail section (20) provided in the sidewall of the stirrer main structure. The roller moves along the right and left sidewall of the load chamber.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the composting apparatus.    Load chamber (10)    Rail section (20)    Stirrer main structure (40)    Right-and-left screw (50)    Breaking portion (70)    Motor (M)    Roller (R)
NOVELTY - Method for producing liquid fertilizer from fish waste, involves removing fat of fish waste, preculturing first mixed microorganisms e.g. Brevibacillus, Bacillus subtilis, B.licheniformis and second mixed microorganisms e.g. B.cereus and Brevibacillus parabrevis, inoculating the microorganisms to the fish waste, and culturing to decompose the fish waste.    USE - The method is useful for producing liquid fertilizer from fish waste.    ADVANTAGE - The method is eco-friendly, as the disposed fish waste is used as raw material for producing fertilizer. The liquid fertilizer can be recycled.    DETAILED DESCRIPTION - Method for producing liquid fertilizer from fish waste, involves removing fat of fish waste, preculturing the first and second mixed microorganisms, inoculating the microorganism to the fish waste and culturing to decompose the fish waste, where the first mixed microorganism is chosen from Brevibacillus, Bacillus subtilis, B.licheniformis, B.coagulans, B.circulans, B.anthracis, B.fusiformis, and Brevibacillus agri, and the second mixed microorganism is chosen from B.cereus and Brevibacillus parabrevis.
NOVELTY - Liquid fertilizer comprises oregano extract.    USE - Liquid fertilizer is useful for crops and fruit trees.    ADVANTAGE - The liquid fertilizer has improved storage stability, is environment-friendly and does not clog in the nozzle of pipe and spray portion of the container.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the above-cited liquid fertilizer, which involves collecting pig feces and urine, separating solid and liquid of pig feces and urine, inoculating decomposing microorganisms and molasses to supernatant and fermenting the mixture under anerobic and aerobic condition, precipitating fermented product, filtering fermented product with membrane filter and mixing the filtrate with oregano extract.
NOVELTY - A water treatment tank (15) containing microorganisms receives effluent subjected to denitrification, aerobic, anaerobic and anoxic treatments, separates solid/liquid in effluent, and transfers effluent to dissolved air flotation tank (17) using pump. A scum tub (19) receives sludge from flotation tank, and sludge in tub is returned to denitrification chamber (2). Effluent is treated using volatile fatty acids and introduced into aeration tank (8,9) after circulation-controlled oxidation/reduction process. Circulation rate is controlled according to effluent amount.    USE - Waste water processing unit for processing livestock waste water or organic industrial waste water.    ADVANTAGE - The biological treatment safety is secured and stability of the wastewater treatment is maximized. High efficiency circulation control oxidation-reduction can be performed while process efficiency and environment contamination problem relating to the livestock wastewater can be effectively solved. Oxidation-reduction controllability can be improved while securing bio-stability in the high concentration organic waste water treatment. Treatment cost, foul smell and odor of treatment water, energy consumption, installation expense of system can be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for waste water processing method.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of the waste water processing unit.    Denitrification chamber (2)    Aeration tanks (8,9)    Water treatment tank (15)    Dissolved air flotation tank (17)    Scum tub (19)
NOVELTY - Method for preparing inulin prebiotic, involves mixing (in parts weight): water (100-120), vitamin E (0.08-0.15) and inulin (100), homogenizing the mixture at 50-60 degrees C, adding Sureteric (RTM: Combination of polyvinyl acetate phthalate, plasticizers and other ingredients) (1-3) to the homogenized mixture to prepare ultra fine powder and spray drying encapsulated inulin prebiotic.    USE - The method is useful for preparing inulin prebiotic, which is useful as bioactive diet material, as livestock feed antibiotic, for reducing blood pressure (all claimed) and for treating diabetes, colon cancer and obesity.    ADVANTAGE - The inulin prebiotic is environment-friendly.
NOVELTY - Method for recycling resources and advanced treatment of wastewater containing a high concentration of organic compounds, involves preprocessing livestock excrements in wastewater, removing organic compounds, nitrogen and phosphorus in the preprocessed water and suspended materials by a separation membrane module, and finally removing the residual organic compounds by photocatalytic oxidation reaction.    USE - The method is useful for recycling resources and advanced treatment of organic high concentration wastewater (claimed), and for producing liquid fertilizer.    ADVANTAGE - The produced fertilizer has no odor and is environment-friendly.
NOVELTY - The method comprises initially drying the bakery products by residual heat of a baking oven existing after baking, subsequently breaking the bakery products by grinding, and then agglomerating the bakery products to form fuel briquettes. A binder is added to the ground bakery products before the agglomeration, and is used in the form of sugar solution, glucose and/or sugar-containing bakery products. The ground bakery products are pelleted to fuel pellets. The fuel briquettes are burnt and a part of the released heat energy is used for heating the baking oven.    USE - Method for recycling bakery products such as old-bread as fuel and animal feed.    ADVANTAGE - The method is capable of simply, easily, flexibly and economically recycling the bakery products with less space requirements, high throughput and less energy consumption without requiring additional equipments, and prevents danger of explosion by the ignition of dust.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a system for recycling bakery products as fuel.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of a device of a system for recycling bakery products.    Housing (10)    Base (15)    Stainless steel frame (30)    Dosing tank (60)    Nozzle. (70)
NOVELTY - Processing a biomass, comprises: treating a biomass by heating the biomass at a first temperature; thermally converting the treated biomass into a product having an oil portion and an aqueous portion via pyrolysis at a second temperature, where the first temperature is lower than the second temperature; and selecting the first temperature based on a correlation between the first temperature and a desired anhydrosugar content in the oil portion of the product.    USE - The process is useful for: processing biomass (claimed); and producing liquid fuels from lignocellulosic materials e.g. agricultural and forestry residues, and energy crops.    ADVANTAGE - The bio-oil provided by the process is more enriched in sugars, less corrosive, and more stable.    DETAILED DESCRIPTION - Processing a biomass, comprises: treating a biomass by heating the biomass at a first temperature, thermally converting the treated biomass into a product having an oil portion and an aqueous portion via pyrolysis at a second temperature, where the first temperature is lower than the second temperature, and selecting the first temperature based on a correlation between the first temperature and a desired anhydrosugar content in the oil portion of the product; or providing a biomass having a first crystallinity, modifying a structure of cellulose in the biomass to have a second crystallinity higher than the first crystallinity, and thermally converting the biomass with the increased crystallinity into a pyrolysis product containing anhydrosugar via pyrolysis.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic flow diagram of a system for converting biomass into bio-oils.    System (100)    Dryer (102)    Pyrolysis reactor (106)    Steam reformer (116)    Gasification reactor. (118)
NOVELTY - A garbage decrement clear system engineering involves performing household garbage biologic treatment which disposes 60-70% of garbage, performing sorting recirculation which disposes 30-40% of garbage, performing burning utilization which disposes about 10% of garbage, producing braking-free brick which disposes not greater than 10% of garbage, and clearing garbage.    USE - A garbage decrement clear system engineering e.g. town garbage synthetic processing systematic engineering for garbage treatment.    ADVANTAGE - The garbage decrement clear system engineering has small investment, strong adaptability and convenient management, is pollution-free and zero-emission, and changes waste into valuables.
NOVELTY - The heating furnace has a heat exchange water tank that is arranged on the chimney and the furnace main portion (3). A vortex burner (13) is fixed to the upper end of an inner chamber of the furnace main portion. An auxiliary hollow heating pipe (4) is fixed on the vortex burner and is extended downward to a pyrolyzing gasification chamber (19) on the lower end of the inner chamber of the furnace main portion. A secondary air distribution adjuster (16) is provided in the vortex burner. A chimney baffle (10) is provided at outlet of chimney (11).    USE - Multifunctional heating furnace for biomass gasification system.    ADVANTAGE - The auxiliary hollow heating pipe is fixed on vortex burner and is extended downward to pyrolyzing gasification chamber at furnace main portion such that the utilization of fuel is reduced and incomplete burning of fuel is avoided. The structure of the heating furnace is simplified and the heating efficiency of the heating furnace is improved. The consumption of power is reduced. The fuel is gasified and burned again such that the emission of dust is avoided and the environmental pollution is prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the multifunctional heating furnace.    Furnace main portion (3)    Auxiliary hollow heating pipe (4)    Chimney baffle (10)    Chimney (11)    Vortex burner (13)    Secondary air distribution adjuster (16)    Pyrolyzing gasification chamber (19)
NOVELTY - An ecological water-free manure processing device comprises a main machine (1) comprising a motor room (12) having an electric motor connected with two stirrers by a mechanical transmission device, and fermenting tank (11) having a microorganism bactericide, an opening at the upper part corresponding movable baffle plate (113) at the bottom of the toilet bowl and a heating device is mounted at the outer bottom of the fermenting tank; and a toilet bowl (2).    USE - An ecological water-free manure processing device for locomotive or steamship driver.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of an ecological water-free manure processing device.    Main machine (1)    Toilet bowl (2)    Fermenting tank (11)    Motor room (12)    Movable baffle plate (113)
NOVELTY - Preparing low molecular low polymerized polylactic acid comprising low molecular low polymerized polylactic acid and lactic acid oligomer, involves condensation-polymerization reaction of cyclic type and ring opening type under reduced pressure, and heating fermented L-lactic acid step wise in an inert gas atmosphere, collecting low molecular low polymerized polylactic acid from dehydrated-separated distillate during condensation-polymerization, and pulverizing by freeze-drying to obtain soluble form.    USE - The low molecular low polymerized polylactic acid liquid is useful in fresh food additive, functional food, construction materials, pharmaceutical, cosmetics, culture pond, culture water tank and ornamental fish water tank for exhibiting antioxidant activity, disinfecting, and for preventing microbial infections caused by fungi and virus (all claimed).    ADVANTAGE - The low molecular low polymerized polylactic acid liquid does not cause harm to human, and can be produced without causing environmental pollution.
NOVELTY - Method for producing sugar, involves (a) processing biomass starting material containing type I cellulose with processing agent containing ammonia and/or an organic amine to obtain modified biomass starting material, (b) pulverizing the modified biomass starting material to obtain starting material for enzymatic saccharification, and (c) enzymatically saccharifying the starting material for enzymatic saccharification to obtain sugar.    USE - The method is useful for producing sugar, which is useful for producing lactic acid, and ethanol (all claimed). The ethanol is used for producing fuel and biodegradable plastics.    ADVANTAGE - The sugar, ethanol and lactic acid are produced at high yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of producing ethanol and lactic acid, which involves fermenting sugar produced by the above-cited method.
NOVELTY - The device has a comb shaped tube provided with taps, which are directly connected with a gas measuring tube, an absorbing bottle and a burning bottle, respectively. The taps randomly control a gas flowing direction in a rotating manner according to a direction of 0 to 360 degrees. Internal diameters of the taps and connecting tubes are 2.0 mm. The comb shaped tube is made up of connecting tubes. The taps are T shaped. A platinum wire of the burning bottle and a temperature measuring heat resistor are inserted into a burning room.    USE - Test device for detecting coal gas components. Uses include but are not limited to carbon dioxide, unsaturated hydrocarbon, oxygen, carbon monoxide, hydrogen, methane and nitrogen.    ADVANTAGE - The device improves the structure design of the comb shaped tube and the burning bottle so that an upper tap of the comb-shaped tube controls the whole test process with good tightness and constant volume. The device removes system errors. The burning room temperature can be monitored and measured so as to improve accuracy and precision of the burning test. The device has reasonable design. The device is simple in structure and convenient to operate.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a test device.
NOVELTY - A biological carbon pulp prepared from garbage leachate comprises (wt.%) biological carbon (40-55), garbage leachate (25-40), methanol (16-20), high temperature sand (1-2), and additive (0.3-1.2).    USE - A biological carbon pulp prepared from garbage leachate (claimed) for use in oil burning field of industrial boiler, utility boiler and industrial stove and in environmental treatment field.    ADVANTAGE - The use of the biological carbon pulp saves energy and reduces fuel cost, and obtains excellent treatment effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biological carbon pulp comprising conveying biological carbon and high temperature sand in a feeding mechanism, adding garbage leachate and additive, mixing and crushing, further adding additive, then adding methanol, and further crushing; homogenizing the mixture, filtering, and filling in a tank.
NOVELTY - A M85 methanolic gasoline comprises (vol.%) methanol (84-86), constituent oil (12-15), and additive (1-2), where the constituent oil is obtained by mixing (vol.%) 5-7C saturated paraffin (25-27), solvent oil (34-50), gasoline #90 (14-30) and toluene (10-12). The additive is obtained by mixing (vol.%) 4-6C prim. alcohol (20-45), petroleum ether (30-60), hydrogen peroxide solution (1-3), ethylene glycol methyl ether (2-5) and N,N'-disalicylidene-1,2-propylene diamine (1-3).    USE - A M85 methanolic gasoline for vehicle (claimed).    ADVANTAGE - The gasoline can be used directly in vehicles which does not require change to electric spraying system of the engine. It meets national standard GB/T 23799-2009.
NOVELTY - Enhancing hydrogen production, comprises: suppressing Tla1 gene expression in an alga (a1) to be used for hydrogen production; and cultivating (a1) under conditions in which hydrogen is produced.    USE - The methods are useful for: enhancing production of hydrogen, bio-oil or bio-diesel, beta -carotene, lutein or zeaxanthin, and astaxanthin; and screening for green algae that show enhanced yield of photosynthetic productivity under high density growth conditions, where the green algae are any one of (a1)-(a4) (all claimed).    ADVANTAGE - The suppression of Tla1 gene expression results in reduced chlorophyll antenna size, which improves solar conversion efficiency and photosynthetic productivity in green microalgae under bright sunlight conditions.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) enhancing bio-oil or bio-diesel production, comprising: suppressing Tla1 gene expression in an alga (a2) to be used for bio-oil or bio-diesel production; and cultivating (a2) under conditions in which bio-oil or bio-diesel is produced;    (2) enhancing beta -carotene, lutein or zeaxanthin production, comprising: suppressing Tla1 gene expression in an alga (a3) to be used for beta -carotene, lutein or zeaxanthin production; and cultivating (a3) under conditions in which beta -carotene, lutein or zeaxanthin is produced;    (3) enhancing astaxanthin production, comprising: suppressing Tla1 gene expression in an alga (a4) to be used for astaxanthin production; and cultivating (a4) under conditions in which astaxanthin is produced; and    (4) screening for green algae that show enhanced yield of photosynthetic productivity under high density growth conditions, comprising: introducing mutations into a population of green algae; and screening the green algae for inhibition of Tla1 gene expression, where inhibition of Tla1 gene expression is determined by measuring the level of Tla1 mRNA or Tla1 protein.
NOVELTY - Production of organic based fertilizer comprises collecting animal waste, separating animal waste into liquid waste and solid waste, clarifying liquid waste and thus producing supernatant and sludge; extracting ammonia from supernatant to produce ammonium salt and aqueous solution, and filtering aqueous solution to produce concentrate and usable water; and using ammonium salt, concentrate and sludge to supplement the solid waste, and forming solid waste into the organic based fertilizer.    USE - Method of producing organic based fertilizer (claimed).    ADVANTAGE - The method reduces water consumption on the agricultural operation through recycling of water filtrate to barn or another installation on agricultural operation, and reduces energy costs as the methane may be used to heat or power other aspects of the agricultural operation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the production organic based fertilizer further including a cell conditioner and anaerobic digester to allow for the production of methane.    Solid waste (102)    Solid waste storage tank (106)    Cell conditioner (186)    Anaerobic digestion (188)    Methane (192)
NOVELTY - Synthesizing 3,5-dibromo-4-hydroxybenzonitrile, comprises: reacting 4-hydroxybenzonitrile (8.4-1260 mmole) with a brominating reagent comprising alkali/alkaline earth metal bromide and alkali/alkaline earth metal bromate salts, where the active bromide content in the reagent is 16.8-2524 mmole, under continuous stirring; adding inorganic acid (0.015-3 mole) to the reaction mixture under stirring for 1-4 hours at room temperature; continuing the stirring further for 1-3 hours; and filtering the solid from liquid, washing with deionized water and drying the precipitate under vacuum at 155-165 mm Hg pressure.    USE - The process is useful for preparing 3,5-dibromo-4-hydroxybenzonitrile, which is useful as herbicide in the control of broad-leafed weeds, preferably in crops growing areas.    ADVANTAGE - The process is easy, eco-friendly and less energetic. The process requires a simple and solid brominating reagent for in situ generation of reactive species, which is subsequently utilized in the bromination of 4-hydroxybenzonitrile. The brominating reagent utilized in the process is solid and non-hazardous and does not require any special equipment or handling skills. The reaction occurs in solution at the room temperature and atmospheric pressure. The reaction does not require any catalysts. The brominating reagent can easily be obtained at reduced cost from one of the intermediate products in the bromine recovery process. The bromination reaction has high yield and atom efficiency. The process provides high yield (91-99%) and high purity (99%) of 3,5-dibromo-4-hydroxybenzonitrile. No biological data given.
NOVELTY - The carbonization furnace has several screw conveyers provided with a trough (10) in which a screw (8) is arranged. The trough of screw conveyer has a U-shaped trough main portion (11) that is spanned between the walls (3m) through the attachment holes (3a). The side wall extension elements (21-23) of screw conveyor are attached to the upper portion of the trough main portion so that the side wall portion of trough main portion in the width direction is extended upwards within the furnace. A carbonized-material moves in the inside of the screw conveyer.    USE - Multistage screw carbonization furnace.    ADVANTAGE - The side wall extension element can be replaced easily even if side wall extension element is deformed by heating. Hence the maintenance of a trough is improved by partial replacement.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the trough of screw conveyer in the multistage screw carbonization furnace.    Attachment hole (3a)    Walls (3m)    Screw (8)    Trough (10)    U-shaped trough main portion (11)    Side wall extension elements (21-23)
NOVELTY - The apparatus (10) has a flow path (54) formed between an anode side electric power feeding section (40) and an anode side separator (34). A flow path (58) is formed between a cathode side electric power feeding section (42) and a cathode side separator (36). The protrusion portions (44a-44c) are protruded in a horizontal direction outward at an outer peripheral portion of a unit cell (12). A hydrogen communicating hole (50) is set in protrusion portion (44c) and is connected to flow path (58), to condense the water content in hydrogen.    USE - Water-electrolysis apparatus for use in production of high-pressure hydrogen gas (claimed) used as fuel gas for fuel cell.    ADVANTAGE - The size of the water-electrolysis apparatus is reduced while reliably condensing and removing the water content contained in the hydrogen produced by the water-electrolysis apparatus of simple structure.    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)    Anode side electric power feeding section (40)    Cathode side electric power feeding section (42)    Protrusion portions (44a-44c)    Hydrogen communicating hole (50)    Flow paths (54,58)
NOVELTY - The apparatus (SEA) has counter electrode (S0) and measurement probe (S1-S5) made of nickel and arranged so as to be apart from electrolytic cell. An alternating current (AC) power supply circuit (510) supplies the alternating voltage between the measurement probe and counter electrode. An electric current detection circuit (51-55) connected to measurement probe and counter electrode includes a capacitor (501), to detect the electric current flowing into a resistor (503).    USE - Liquid level detection apparatus of gas generator (claimed) for generating fluorine gas used for cleaning semiconductor material. Can also be used in gas generator used for generating oxygen gas.    ADVANTAGE - The liquid level in the electrolytic cell can be detected stably, without the replacing the measurement probe and counter electrode.    DESCRIPTION OF DRAWING(S) - The drawing shows a circuit diagram of the liquid level detection apparatus. (Drawing includes non-English language text)    Electric current detection circuit (51-55)    Capacitor (501)    Resistor (503)    AC power supply circuit (510)    Counter electrode (S0)    Measurement probes (S1-S5)    Liquid level detection apparatus (SEA)
NOVELTY - The apparatus has a protection sheet (44) with several taper-shaped through holes (44a), provided between anode-side electric power feeding element (40), and solid polymer electrolytic membrane (38). The diameter of the through hole is reduced towards the solid polymer electrolyte membrane.    USE - Water electrolysis apparatus for generating hydrogen gas used as fuel gas for solid polymer electrolyte fuel cell.    ADVANTAGE - Damage of electrolytic membrane is prevented. Water supply property and gas discharging property can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of the water electrolysis apparatus.    Cathode-side separator (36)    Solid polymer electrolytic membrane (38)    Anode-side electric power feeding element (40)    Protection sheet (44)    Through hole (44a)
NOVELTY - The apparatus has a protection sheet (44) with through holes (44a), provided between anode-side electric power feeding element (40), and solid polymer electrolytic membrane (38). The taper-shaped portions (45a,45b) are provided in the ends of the through hole. The diameter of taper-shaped portion (45a) is increased towards the solid polymer electrolytic membrane while the diameter of the taper-shaped portion (45b) is increased towards the anode-side electric power feeding element.    USE - Water electrolysis apparatus for generating hydrogen gas used as fuel gas for solid polymer electrolyte fuel cell.    ADVANTAGE - Control of aperture diameter of through hole is performed easily. Since diameter of taper-shaped portion is increased towards the solid polymer electrolytic membrane, shear and elongation of membrane is suppressed. Damage of the membrane is prevented. Since diameter of the other taper-shaped portion is increased towards the anode-side electric power feeding element, water supply property and gas discharging property can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows the cross-sectional view of the unit cell.    Solid polymer electrolytic membrane (38)    Anode-side electric power feeding element (40)    Protection sheet (44)    Through hole (44a)    Taper-shaped portions (45a,45b)
NOVELTY - Solid fuel comprises pulverized mixture of livestock excrement and vegetable material.    USE - The solid fuel is useful for combustion apparatus chosen from boiler and stove, preferably hot-blast stove, and vinyl greenhouse.    ADVANTAGE - The solid fuel is cost-effective, and has high calorific value and excellent combustibility, handleability and usability. The offensive odor produced during combustion can be reduced. The solid fuel has high temperature combustibility, hence production of corrosive gas can be prevented.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the solid fuel, which involves obtaining livestock excrement and vegetable materials, adjusting size of each raw material, drying the raw materials, and mixing the dried raw materials.
NOVELTY - Manufacture of ethanol-gasoline comprises mixing (%) pentanol (0.1-0.5) and amyl ether (0.2-0.4) in 95% industrial alcohol; mixing fatty alcohol polyoxyethylene ether (54-85), dimethyl carbonate (10-30), ethyl oleate (5-10), and p-tertiary butyl phenol (1-6) in an ethanol gasoline modifier; and adding 70% gasoline to 26% modified ethanol, uniformly stirring, and adding 4% ethanol gasoline modifier.    USE - Method for the manufacture of ethanol-gasoline (claimed).    ADVANTAGE - The method prevents layering, corrosion, swelling, and emulsifying. It produces ethanol-gasoline with improved stability, convenient, and inexpensive.
NOVELTY - The microwave extracting device (10) has an essential oil extraction tank (2) provided with a rod shaped structure (3) formed with microwave permeability heat resisting material for transmitting the microwave irradiated from a microwave applicator (1). An extract storage tank (4) stores an extraction solvent (S) including the essential oil emitted from the essential oil extraction tank. An extraction solvent supply unit (12) supplies the extraction solvent to the essential oil extraction tank from the condensing apparatus for condensing the extraction solvent.    USE - Microwave extracting device for extracting essential oil from plant type biomass. Can also be used in extraction of fuel in industrial type biomass such as municipal solid waste, foodstuff residue, sewage sludge, livestock excrement, cultivated plants and agricultural products used in field of pharmaceutical, cosmetics, foodstuff, aromatic agent and dyestuff.    ADVANTAGE - The plant-derived essential oil can be extracted from the plant type biomass at once at low temperature and the thermal deterioration of microwave extracting device can be suppressed.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the microwave extracting device.    Microwave applicator (1)    Essential oil extraction tank (2)    Rod shaped structure (3)    Extract storage tank (4)    Microwave extracting device (10)    Extraction solvent supply unit (12)    Extraction solvent (S)
NOVELTY - A primer useful in PCR for detecting or quantifying bacteria capable of decomposing thiocyanogen, comprising a sequence of SEQ ID NO: 1 or 2, is new.    USE - The primer, primer set and probes are useful in PCR for detecting or quantifying bacteria capable of decomposing thiocyanogen (all claimed).    ADVANTAGE - The treated water has excellent quality and is obtained by a simple process. The bacteria have excellent versatility, and can be quantified rapidly and accurately.    DETAILED DESCRIPTION - A primer useful in PCR for detecting or quantifying bacteria capable of decomposing thiocyanogen, comprising base sequence of SEQ ID NO: 1 or 2, is new. The sequences include ggaagtcagcgatttcgaga (SEQ ID NO: 1) and tccacacgcggtggtctt (SEQ ID NO: 2). INDEPENDENT CLAIMS are included for the following:    (1) primer set comprising forward primer having base sequence of SEQ ID NO: 1 and reverse primer having base sequence of SEQ ID NO: 2;    (2) PCR probe useful in real-time PCR for detecting or quantifying the bacteria capable of decomposing thiocyanogen, comprising a base sequence of SEQ ID NO: 3, where the probe is used in presence of the primer set;    (3) fluorescence in situ hybridization probe comprising base sequence of SEQ ID NO: 1, 2 or 3; and    (4) biological treatment method, involves performing biological treatment in tank containing to-be-processed water including thiocyanogen with the bacteria capable of decomposing thiocyanogen in tank, decomposing the thiocyanogen, and quantifying the bacteria.    The sequence includes cgaactggccatcgaaaaaggcc (SEQ ID NO: 3).
NOVELTY - A hydrogen-producing apparatus comprises cartridge (3), liquid feeding operation part (7) which liquid-feeds reaction part, reaction part (5) where hydrogen-producing substance which reacts with solution for reaction and produces hydrogen is accommodated, solution container (6) where solution for reaction is stored, and drive unit (11) which gives operation motive power to liquid feeding operation part at the time of operation of liquid feeding operation part.    USE - A hydrogen-producing apparatus used for fuel cell system (claimed).    ADVANTAGE - The apparatus has simple structure, and reduced size.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of hydrogen-producing apparatus. (Drawing includes non-English language text).    Cartridge (3)    Reaction part (5)    Solution container (6)    Liquid feeding operation part (7)    Drive unit (11)
NOVELTY - A micro algae which belongs to the 0024 strains (FERM P-21749) of Scenedesmus genus and Rubescens species JPCC GA, for producing 14-22C aliphatic hydrocarbon, is new.    USE - The micro algae is useful for producing 14-22C aliphatic hydrocarbon, oil component, and fuel (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a method of manufacturing oil component comprising cultivating the micro algae;    (2) an oil component manufactured by the method;    (3) a dry alga body obtained by drying the micro algae;    (4) a fuel obtained from the micro algae; and    (5) a carbon-dioxide fixing method comprising cultivating the micro algae.
NOVELTY - A deodorizing method of organic waste involves removing or reducing odor component which contains acetoin, and diacetyl from organic waste by inoculating and cultivating a mushroom microbe in the organic waste.    USE - Deodorizing method for organic waste (claimed).    ADVANTAGE - Efficient deodorizing effect is acquired, mushroom fruiting body can be produced, does not impair the fragrance and waste material is utilized.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for deodorant for organic waste comprising mushroom microbe; and#production method of mushroom fruiting body which involves cultivating mushroom microbe on organic waste.
NOVELTY - The element has cylindrical portion (19) whose coefficient of thermal expansion is smaller than the metal that is joined to the shaft-end surfaces of the cylindrical portion (11). A taper surface is provided to join the cylindrical portions arranged at an angle of 53-70 degrees such that the cylindrical portion is arranged in the outer surface of the cylindrical portion.    USE - Joining element for solid oxide fuel cell (claimed).    ADVANTAGE - The joining reliability of the cylindrical portions is improved and the efficiency of the solid oxide cell is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing method of joining element.    DESCRIPTION OF DRAWING(S) - The drawing shows the partial enlarged vertical longitudinal sectional view of the joining element.    Cylindrical portions (11,19)    Fuel gas supply pipe (16)
NOVELTY - The frame has a furnace structure (1) provided with a tapered ash-discharging hopper (2). Several ash-discharging holes (3) are formed on the ash-discharging hopper which is supported by a rotating shaft (4). The bottom angle of the ash-discharging hopper is set to 15-17 degrees.    USE - Umbrella-shaped frame of biomass gasification furnace.    ADVANTAGE - The frame of simple structure can be used conveniently, and the service life of the frame can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the umbrella-shaped frame.    Furnace structure (1)    Ash-discharging hopper (2)    Ash-discharging holes (3)    Rotating shaft (4)
NOVELTY - The to-be-emulsified diesel is supplied to a Venturi pipe from an inlet section of the Venturi pipe. The to-be-emulsified diesel is provided to a throat portion from a shrinkage section of the Venturi pipe, and supplied to a dispersion section. The methanol and water are mixed in proportion of 1:1-1:2 with an emulsifier (1-3%) to obtain methanol-water solution. The solution is supplied to the Venturi pipe from the throat portion of the Venturi pipe, and mixed with diesel at a flowing portion to obtain a three-component emulsion.    USE - Formation of three-component emulsion.    ADVANTAGE - The method provides three-component emulsion having excellent stability. The methanol-water solution is quickly and uniformly dispersed in the diesel within short period of time.    DETAILED DESCRIPTION - The to-be-emulsified diesel is supplied to a Venturi pipe from an inlet section of the Venturi pipe. The pressure of diesel before entering the Venturi pipe is 0.48 MPa or more. The to-be-emulsified diesel is provided to throat portion from a shrinkage section of the Venturi pipe, and supplied to a dispersion section. The methanol and water are mixed in proportion of 1:1-1:2 with an emulsifier (1-3%) to obtain methanol-water solution. The pressure of the methanol-water solution before entering the Venturi pipe is 0.18 MPa or more. The solution is supplied to the Venturi pipe from the throat portion of the Venturi pipe, and mixed with diesel at a flowing portion to obtain a three-component emulsion, and the emulsion is discharged from the dispersion section. The flow ratio of diesel and methanol-water solution is 9:1-1:1.
NOVELTY - The tank has a U-shaped water tank whose ring section is fixed on an upper edge of a lower tank. A lower edge of an upper tank is arranged in the water tanks. An air outlet pipe is provided in the upper tank. An air inlet is arranged at a lower part of the lower tank.    USE - Fuel tank for a straw gasifier.    ADVANTAGE - The tank is conveniently ignited, and enables ash to be poured in a convenient manner. The tank is simple in structure.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a fuel tank.
NOVELTY - The electrolytic cell has several electrolytic small chambers each of which has two electrode plates arranged in electrolytic liquid, and a micropore diaphragm arranged between two electrode plates. Each electrode plate is composed of cathode electrode plate, anode electrode plate and an insulating spacer. The insulating spacer is connected with cathode and anode electrode plates in series by sealing. The electrodes of all electrolytic small chambers are connected in parallel to form electrolytic cell.    USE - Electrolytic cell for preparing hydrogen by electrolysis water.    ADVANTAGE - The energy consumption of the electrolytic cell can be reduced. The corrosion of electrolytic cell can be reduced and loss of electrolytic liquid can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the electrolytic cell.
NOVELTY - A substance with unsaturated bond is decomposed, to form reducing free radical. Then, trifluoromethyl sulfur pentafluoride and sulfur hexafluoride are decomposed using the obtained reducing free radical.    USE - Light reduction method for processing strong greenhouse gas e.g. trifluoromethyl sulfur pentafluoride and sulfur hexafluoride.    ADVANTAGE - The method enables efficient processing of strong greenhouse gas e.g. trifluoromethyl sulfur pentafluoride and sulfur hexafluoride at greenhouse temperature.
NOVELTY - A cinder-loaded solid base catalyst is obtained by dipping dry-cinder carrier having grain diameter of 1-10 mm into potassium carbonate aqueous solution having density of 0.3-1 g/ml, filtering after attaining absorption state, drying at 300-800 degrees C and roasting for 0.5-6 hours.    USE - Cinder-loaded solid base catalyst is used for preparing biodiesel.    ADVANTAGE - The cinder-loaded solid base catalyst is highly efficiently, and manufactured easily and economically in high yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of cinder-loaded solid base catalyst.
NOVELTY - A membrane electrode has a cathode porous supporting layer, a cathode catalyst layer containing non-noble metal cathode hydrogen evolution catalyst and alkali polymer electrolyte, an alkali polymer electrolyte membrane, an anode catalyst layer containing non-noble metal anode hydrogen evolution catalyst and alkali polymer electrolyte, and an anode porous supporting layer.    USE - Membrane electrode is used in water electrolysis.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of membrane electrode, which involves forming cathode catalyst layer on the cathode porous supporting layer using cathode hydrogen evolution catalyst slurry containing non-noble metal cathode hydrogen evolution catalyst and alkali polymer electrolyte, forming anode catalyst layer on the anode porous supporting layer using anode hydrogen evolution catalyst slurry containing non-noble metal anode hydrogen evolution catalyst and alkali polymer electrolyte and laminating cathode catalyst layer and anode catalyst layer.
NOVELTY - An unleaded petrol is produced by mixing (pts.wt.) isobutyl alcohol (2-4), acetone (1-3), methyl tert-butyl ether (2-4), toluene or dimethyl benzene (2-5.5), methyl cyclopentadienyl manganese tricarbonyl (0.01-0.03), butyl-octyl zinc dithiophosphate (0.03-0.1) and dicyclopentadienyl iron (0.1-3), and stirring to obtain yellow transparent liquid; adding into methanol (35-65), and stirring to obtain denatured methyl alcohol; and adding into petrol (60-30), and uniformly stirring.    USE - Method of producing unleaded petrol used for car (claimed).    ADVANTAGE - The method produces petrol with 99.99% methanol, low cost, less pollution, small oil consumption, low corrosion and high power.
NOVELTY - A high-performance methanol gasoline comprises (pts.wt.) petrochemical gasoline (65-90), methanol (9-30) and biodiesel (1-5).    USE - A high-performance methanol gasoline.    ADVANTAGE - The gasoline has low cost, good low-temperature cold start property, no air blockage, and no corrosion to rubber.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of preparing high-performance methanol gasoline by mixing methanol and biodiesel, uniformly stirring to obtain denatured alcohol liquid, adding petrochemical gasoline, and uniformly mixing.
NOVELTY - The system (1) has a kiln (7) arranged along axial direction of several flow paths, to heat the water-containing sludge (W) pumped from pump (2) so as to form fuel (F). A pre-heating unit is arranged between the pump and kiln, to pre-heat the fuel. A chiller (8) cools the fuel formed by the kiln. An upper valve (10) is arranged in flow path for conveying of fuel from kiln to decompression tank (12) and opened or closed when a downstream valve (11) arranged at the side of tank is closed or opened respectively.    USE - System for formation of fuel using water-containing organic waste such as sludge (claimed) in underground water, river, etc. Can also be used in formation of fuel using dredge mud and industrial waste water.    ADVANTAGE - The safety for the fuel formation system can be ensured effectively, even when the pressurization temperature of the water-containing organic waste is increased.    DETAILED DESCRIPTION - The main portions of the valves are protruded along direction of valve-seat portion from edge portion of straight-cylinder. A convex-shaped seating portion is formed in virtual cylinder portion along axial-direction of straight-cylinder so as to contact and to be apart with respect to valve-seat portion.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the fuel-formation system.    Fuel formation system (1)    Pump (2)    Kiln (7)    Chiller (8)    Upper valve (10)    Downstream valve (11)    Decompression tank (12)    Fuel (F)    Water-containing sludge (W)
NOVELTY - Fungicidal composition comprises cyazofamid and Polyram (RTM: Fungicide) in a mass ratio of 1-50:1-80.    USE - The fungicidal composition is useful for controlling diseases caused by various lower fungi of fruit trees, melons and vegetables (claimed).    ADVANTAGE - The composition is safe and environmental friendly, low cost and good effect and has synergetic effect.
NOVELTY - Pesticidal composition comprises: an active ingredient component containing at least one formic acid or acetic acid, and/or their salts; a second acidic component which potentiates the activity of the active ingredient; and a carrier.    USE - The pesticidal composition is useful to control a pest (or its sites) including nematode, bacteria, fungus, weeds, (all claimed) oomycetes, of numerous crops, plants and forests, where the: weeds include nutsedges and other monocot and dicot weeds; bacteria includes Phytophthora capsici and Ralstonia (Ralstonia solanacearum; fungus is plant pathogenic fungi including Fusarium (Fusarium oxysporum) and Rhizoctonia solani; and oomycetes include Pythium aphanidermatum and Pythium myriotilum.    ADVANTAGE - The pesticidal composition: is inexpensive; and readily degrades to nontoxic inorganic residues e.g. water and carbon dioxide and thus it is eco-friendly; and controls the pests in the soil without causing phototoxicity to plants, thus avoiding reduction in the yield of the desired plants.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for making the pesticidal or herbicidal composition, comprising: providing an aqueous solution containing at least one acidic component of citric acid, malic acid, oxalic acid, sulfuric acid and/or hydrochloric acid; and adding water and mixing formic acid and/or acetic acid to the aqueous solution to form citric acid (10-40% wt/vol), and 15-50% vol/vol formic acid and/or acetic acid in the composition.
NOVELTY - A catalytic-hydrolysis system (100) has a solution containing a hydrogen-generating catalyst comprising aluminum ion, copper ion, and silver ion, a light providing device and an electric activation device.    USE - Catalytic-hydrolysis system is used for producing hydrogen (both claimed), and oxygen.    ADVANTAGE - The catalytic-hydrolysis system safely produces hydrogen, without environmental pollution.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) hydrogen production system, which has an aqueous solution containing electrolyte, and at least two electrodes (102A) which are electrically coupled with the aqueous solution. The voltage of 1.1 V or less is applied to a cathode, and water-electrolysis is carried out;    (2) hydrolysis method, which involves applying voltage to solution containing hydrogen generating catalyst comprising aluminum ion, generating hydrogen gas, regenerating hydrogen generating catalyst by reacting hydrogen generating catalyst with a catalyst reviving substance containing copper ions and/or silver ions, and regenerating catalyst reviving substance by exposing the catalyst reviving substance to light;    (3) production of hydrogen, which involves preparing solution containing ionic compound and applying voltage of 1 V or less to solution by electric hydrolysis reaction; and    (4) electric hydrolysis catalyst, which comprises a non-transition metal electric hydrolysis catalyst and a transition metal (c1) which regenerates the non-transition metal electric hydrolysis catalyst to active state by electric hydrolysis reaction.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the catalytic-hydrolysis system.    Catalytic-hydrolysis system (100)    Reactor (102)    Electrode (102A)    Controlling system (106)    Heat source (108)
NOVELTY - Lignin is liberated form biomass-based feedstock through pulp digester, and the biomass-based feedstock and liberated lignin are pelletized, to obtain biomass-based pellets.    USE - Preparation of biomass-based pellets used for production of biomass-based fuel for power-generation units e.g. boilers of cogeneration power plants.    ADVANTAGE - The method economically provides biomass-based pellets having high density.
NOVELTY - Carbonaceous material is contacted with supercritical fluid, catalyst and hydrogen source, to form reaction mixture. The obtained reaction mixture is maintained at 200 degrees C or less for 30 minutes or more and hydrocarbon is extracted and recovered from reaction mixture.    USE - Method for extracting and upgrading carbonaceous material e.g. oil sand, bitumen, oil shale, lignite, coal, tar sand, biofuel and polycyclic aromatic hydrocarbon (all claimed).    ADVANTAGE - The method for extracting and upgrading carbonaceous material is carried out economically and efficiently in short period of time without environmental pollution.
NOVELTY - Knock-down herbicidal composition comprises: water, limonene component (12-30 wt.%), and an emulsifying agent (0.05-10 wt.%), where the composition has a pH of greater than 5.    USE - The composition is useful against mature weeds to kill, control or suppress the plants (claimed). Test details are described but no results given.    ADVANTAGE - The herbicidal formulation: is environmentally-friendly, acceptable, non-toxic and has little deleterious effect on humans, wildlife and non-target vegetation; can be packaged as ready-to-use dispensing system for relatively small quantity (for home uses) or large quantity (for farmer or professional applicator); is nonselective and non-systemic and effective against almost any vegetation, specifically against common crop and garden weeds, both annual and perennial; is fast acting, typically within seven hours.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for killing, controlling or suppressing plant, comprising: (a) providing the liquid herbicidal composition; and (b) spraying the herbicidal composition onto at least one leaf of the plant.
NOVELTY - A fuel stream and an oxygen-containing gas stream are introduced into fuel processor (61) at an equivalence ratio. The equivalence ratio is sustained at a constant value, and fuel processor is operated to produce syngas stream comprising hydrogen and carbon monoxide at constant equivalence ratio.    USE - Operation of fuel processor for producing syngas stream comprising hydrogen and carbon monoxide, used in engine system.    ADVANTAGE - The fuel processor is continuously operated and syngas stream is produced with high fuel conversion efficiency for long period of time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for operating engine system (50).    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of engine system.    Engine system (50)    Fuel tank (51)    Fuel supply line (52)    Engine (53)    Fuel processor (61)    Particulate filter (62)
NOVELTY - The bio-solid fuel in the high efficiency boiler is subjected to pressure molding and dehydration process, drying process, heating process and pressurization process. The biogas fuel is produced for producing heat and electricity, when the recycling system and cogeneration system are operated at the same time.    USE - Energy recycling and utilization method for producing biomass derived fuel using livestock excretion and wood composite biomass.    ADVANTAGE - Synthesized energy efficiency of the cogeneration system can be improved thus producing biomass derived fuel effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram illustrating the energy recycling and utilization process. (Drawing includes non-English language text)
NOVELTY - The device has a titanium electrode that is arranged at the centre of water treating vessel. The titanium electrode is covered by titanium alloy net. The titanium electrode and titanium alloy net are connected with electrode to form a water electrolysis system. The bottom portion of water treating device is mounted with a water inlet pipe and the top portion is provided with a gas exhaust pipe and a water outlet pipe. The catalytic material like palladium on alumina catalyst is filled in the water treating vessel.    USE - Integrated device for production of hydrogen.    ADVANTAGE - The bromate can be removed from the water continuously and rapidly. The flow of feed water, current of electrolysis, and voltage can be adjusted efficiently. The efficiency of the device is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the integrated device for production of hydrogen.
NOVELTY - A methanol gasoline comprises (in vol.%) gasoline (55-80), methanol (15-30) and additive (5-15).    USE - Methanol gasoline for automobile engines.    ADVANTAGE - The methanol gasoline can be directly applied to automobile engines.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of methanol gasoline, which involves mixing additives at normal temperature and pressure, adding the mixture to methanol solution, mixing the methanol solution containing additive with gasoline, adding the mixed solution obtained to a reaction container, reacting the contents for 40 minutes with constant agitation, and further reacting the contents for 24 hours.
NOVELTY - Reducing the freezing point of the biomass diesel fuel comprises: introducing the biomass diesel fuel with isomethyl stearate in a reaction kettle according to a specified proportion, where the isomethyl stearate is added at normal pressure and at a temperature which is about 5 degrees C higher than the freezing point of the un-mixed biomass diesel fuel; and agitating the mixture for more than 0.5 hour, preferably 0.5 hour.    USE - The method is useful in reducing the freezing point of the biomass diesel fuel.    ADVANTAGE - The addition of isomethyl stearate into the biomass diesel fuel increases the stability and oxidization resistance of the biomass diesel fuel and increases the lubrication of the engine. The method is simple and safe.
NOVELTY - A highly-pure domestic fuel contains (in weight%) methanol (40-70), dimethyl ether (20-40), esterified vegetable oil (9-17), agent (0.8-2) for improving calorific value, energy-saving antismoking agent (0.1-0.5) and odor regulating agent (0.1-0.5). The esterified vegetable oil is obtained by providing residue of vegetable oil as raw material, extracting acid oil from raw material, hydrolyzing obtained product at normal pressure, esterifying obtained fatty acid mixture, distilling and esterifying.    USE - Highly-pure domestic fuel.    ADVANTAGE - The highly-pure domestic fuel has high flammability, and is safely and economically manufactured with reduced generation of waste and environmental pollution.
NOVELTY - A highly-pure domestic fuel contains (in weight%) methanol (30-80), esterified vegetable oil (18-65), oxidizing agent (0.5-3), agent (0.5-2) for improving calorific value, energy-saving antismoking agent (0.1-0.5) and metal corrosion inhibitor (0.01-0.05). The esterified vegetable oil is obtained by providing residue of vegetable oil as raw material, extracting acid oil from raw material, hydrolyzing obtained product at normal pressure, esterifying obtained fatty acid mixture, distilling and esterifying.    USE - Alcohol-based fuel is used in industrial furnace.    ADVANTAGE - The alcohol-based fuel has high flammability, and is safely and economically manufactured with reduced generation of waste and smoke which causes environmental pollution.
NOVELTY - A powder of silybum marianum fruit is prepared, added to supercritical extractor, and methanol is added to the extractor. Then, extraction is carried out, obtained extract is mixed with acetone, filtered, obtained filter liquid is condensed and filled in reverse-flow extractor. Then, a portion of silymarin is collected using water-acetone-chloroform system as solvent system. The obtained silymarin portion is condensed, separated as crystals, mixed with acetone and petroleum ether, re-crystallized, washed and dried, to obtain silymarin.    USE - Preparation of silymarin.    ADVANTAGE - The method provides silymarin having high purity, by simple process with reduced generation of pollution.    DETAILED DESCRIPTION - A powder of silybum marianum fruit is prepared, added to supercritical extractor, and methanol is added to the extractor. Then, extraction is carried out at 30-60 degrees C under pressure of 10-40 MPa for 150-250 minutes to obtain extract. The obtained extract is mixed with acetone, filtered, obtained filter liquid is condensed and filled into high-efficient reverse-flow extractor. Then, a portion of silymarin is collected using water-acetone-chloroform system as solvent system, lower phase as fixed phase and upper phase as flowing phase. The obtained silymarin portion is condensed, separated as crystals, mixed with acetone and petroleum ether, recrystallized, washed and dried, to obtain silymarin.
NOVELTY - A latent solvent comprises coal-based oil, assisting material and catalyst. The assisting material comprises tertiary butyl alcohol, 10-14C mixed alcohol, methanol, quinhydrone and pentene. The catalyst comprises active carclazyte or coal serial kaolin, zinc oxide powder, fine coke powder of 100-200 meshes and anhydrous aluminum trichloride. The latent solvent is obtained by pumping coal-based oil and assisting material into a distilling reactor, adding catalyst, and heating to 60-80 degrees C, insulating for 0.5-1.5 hours and continuing to heat for distilling.    USE - Latent solvent is used for methanol fuel used for vehicles.    ADVANTAGE - The latent solvent has excellent storage stability, and is economically prepared using simple method.    DETAILED DESCRIPTION - A latent solvent comprises 70-98% of coal-based oil, 2-30% of assisting material and 5-10% of catalyst. The assisting material comprises (in parts weight) tertiary butyl alcohol (0.4-6), 10-14C mixed alcohol (0-8), methanol (0.8-20), quinhydrone (0.1-0.2) and pentene (0-1). The catalyst comprises (in weight%) active carclazyte or coal serial kaolin (85-90), zinc oxide powder (7-12), fine coke powder (2-5) of 100-200 meshes and anhydrous aluminum trichloride (1-3). The latent solvent is obtained by pumping coal-based oil and assisting material into a distilling reactor with a blender, a heater and a condenser, adding catalyst, blending and heating to 60-80 degrees C, insulating for 0.5-1.5 hours and continuing to heat for distilling. The distilled substance obtained at condenser outlet at less than 160 degrees C is methane gasoline latent solvent, and the distilled substance obtained at 160-340 degrees C is methanol diesel fuel latent solvent.
NOVELTY - Two-step method for producing bioenergy using microalgae, involves culturing microalgae, collecting and disposing microalgae, then subjecting to biohydrogen production and biomethanation, and collecting the product and residue.    USE - The method is useful for production of bioenergy, preferably hydrogen and methane, and obtaining catabolite of microalgae chosen from fatty acid, alcohol, lactic acid and butyric acid. The hydrogen is useful as energy for hydrogen battery or for generating electricity. The methane is useful as gas or for generating electricity. The residue is useful as fertilizer (all claimed).    ADVANTAGE - The method is environment-friendly.
NOVELTY - The apparatus has a through-hole (21) segmented by a partition wall (23). A compressor (30) compresses mixed food waste, and an accumulator tank (40) collects workpieces ejected from the compressor. A blower (50) exhausts gas from a process chamber (3), and a smell removal device (60) removes bad smell from the transported gas of the blower. A slot lid (71) is formed in a cover (70) to inject the food waste at an upper part of a mixing room (1). The process chamber is arranged at an upper end of another mixing room (2), and a heater (80) is connected to the two mixing rooms.    USE - Food waste disposal apparatus for use in an apartment complex and a shopping mall.    ADVANTAGE - The apparatus collects the food waste, prevents the generation of gas, effectively removes the generation of steam and bad smell, and reduces the processing time of the food waste at low manufacturing cost. The apparatus is set up with an LED lamp or an LED video device to improve the visibility, and provides environment friendly effect. The apparatus is simple in structure and easy to maintain.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a food waste disposal apparatus.    Mixing rooms (1, 2)    Process chamber (3)    Through-hole (21)    Partition wall (23)    Compressor (30)    Accumulator tank (40)    Blower (50)    Smell removal device (60)    Cover (70)    Slot lid (71)    Heater (80)
NOVELTY - The unit (1000) has a residue electricity clean up part (100) provided with a fuel cell stack (400), a battery (300) and a case (200). A cooling water inflow opening (210) is formed in a side of the case, and a cooling water outlet (220) is formed in another side of the case. An electric heater (110) i.e. cartridge-heater, is connected to the battery, and another electric heater (120) i.e. positive temperature co-efficient heater, is connected to the fuel cell stack.    USE - Residue electricity processing unit for a fuel cell vehicle.    ADVANTAGE - The unit has improved energy efficiency by effectively using the residue electricity.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a residue electricity processing unit.'(Drawing includes non-English language text)'    Residue electricity clean up part (100)    Electric heaters (110, 120)    Case (200)    Cooling water inflow opening (210)    Cooling water outlet (220)    Battery (300)    Fuel cell stack (400)    Residue electricity processing unit (1000)
NOVELTY - The method involves obtaining a soybean straw as material to produce fuel ethanol, lignin and biogas. The soybean straw is crushed by using a hammer-type crusher with 3-10-mesh of bottom sieves. An aerating process is carried out on the crushed straw by using a continuous aerator, where steam pressure is 2-3 mega Pascal. The crushed straw is added to a reaction kettle till when volume of the reaction kettle is reached to 60-70 percentage. Water or separated clear biogas liquid is added till that the volume of the reaction kettle is reached to 85-90 percentage.    USE - Comprehensive soybean straw utilization method for commercially producing fuel ethanol, lignin and biogas that is utilized to generate electricity and provide fuel for a car.    ADVANTAGE - The method utilizes the soybean straw fully, so as to improve economic benefit and notable commercial production efficiency. The produced biogas can be directly used for generating electricity. The produced biogas can be compressed to liquefy and separate carbon dioxide to make methane content in the biogas arrive at greater than 90 percentage, store at high pressure and be used as green environment-friendly fuel for car. The fuel ethanol is used for ethanol gasoline and the lignin is used for chemical material.
NOVELTY - The fermenting device (100) supplies the organic waste sludge to the reaction space. A rotary shaft perpendicularly installed at the center of the reaction baths (110) is rotated. An opening/closing unit opens and closes the penetration portion of the reaction bath. The sludge stored inside the reaction space is agitated by rotating the rotating shaft and supplying the air to the reaction spaces separated by the partition walls (112).    USE - Fermenting device of organic waste sludge for use in treatment system (claimed) for organic waste matter of livestock, human being, sewage and food.    ADVANTAGE - The fermentation and drying efficiency of the organic waste sludge can be enhanced. The odor is reduced. The number of the rotary shaft can be reduced hence the cost of the fermenting device of the organic waste sludge is reduced. The number of the labor can be reduced.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) processing method of organic waste sludge; and    (2) treatment system for organic waste matter.    DESCRIPTION OF DRAWING(S) - The drawing shows a side cross-sectional view of the sludge fermenting device.    Sludge fermenting device (100)    Control panel (102)    Reaction paths (110)    Partition walls (112)    Temperature sensors (115)
NOVELTY - Sludge generated by biological treatment process is subjected to alkali solubilization by injection of an alkali. High-quality water obtained by alkali solubilization is returned to the biological treatment process and supplied for nutrients of microorganisms. The remaining sludge is dehydrated, and the separated filtrate is returned to the biological treatment process and supplied for nutrients of microorganisms.    USE - Processing of sludge from sewage disposal plants and industrial sites, to recycle as inorganic compounds e.g. iron compound, aluminum compound, calcium compound, and titanium compound (all claimed).    ADVANTAGE - The method enables efficient processing and recycling of sludge.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for reusing sludge.
NOVELTY - A two-phase apparatus has a supply unit for supplying preprocessed wastewater and waste materials to primary hydrolysis/acid formation reaction equipment, primary hydrolysis/acid formation reactor (R) in which wastewater and waste materials is hydrolyzed and acid is generated, unit for transferring molten solution generated by retreatment to methane formation reactor or reactor (R), and a formation reactor for generating methane by fermenting transferred solution. The solid material which is not solubilized in the primary hydrolysis/acid formation reactor is re-treated.    USE - Two-phase apparatus is used for treating wastewater and waste materials.    ADVANTAGE - The two-phase apparatus economically enables treatment of high concentration wastewater and waste materials with reduced generation of sludge, and methane is produced with high yield.    DETAILED DESCRIPTION - A two-phase apparatus has a supply unit for supplying preprocessed wastewater and waste materials to a primary hydrolysis/acid formation reaction equipment, a primary hydrolysis/acid formation reactor in which wastewater and waste materials supplied from supply unit is hydrolyzed and acid is generated, unit for transferring molten solution generated by retreatment to methane formation reactor or primary hydrolysis/acid formation reactor, and a formation reactor for generating methane by fermenting transferred solution in anaerobic condition. The solid material which is not solubilized in the primary hydrolysis/acid formation reactor is re-treated by thermal treatment, physical treatment, chemical treatment, and/or biological treatment using one device chosen from heating device, grinding device, ultrasonic devices, chemical device and biological device.
NOVELTY - A greenhouse gas generating unit (100) generates greenhouse gas comprising methane and carbon dioxide. The sampling filters (150,160) filter dust generated in greenhouse gas. A pressure gauge (210) senses pressure gradient of greenhouse gas supplied from three-way valve (170) and vacuum pump (220) and compresses greenhouse gas in oilless compressor. A pair of membranes (230,260) separates moisture content from the compressed gas according to the moisture permeation rate. A filter (250) filters dust from the processed gas.    USE - Greenhouse gas separating and storage control system installed in livestock excretion disposal facility, anaerobic fermentation facility, bio-industry and wastewater treatment digestion tank.    ADVANTAGE - The greenhouse gas having an effect on global warming can be collected and the carbon dioxide in the greenhouse gas can be recycled.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for greenhouse gas separating and storage control method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the greenhouse gas separating and storage control system. (Drawing includes non-English language text)    Greenhouse gas generating unit (100)    Sampling filters (150,160)    Three-way valve (170)    Pressure gauge (210)    Vacuum pump (220)    Membranes (230,260)    Filter (250)
NOVELTY - Microbial agent comprises culture material of Allochromatium palmeri, Ectothiorhodosinus mongolicus, Halochromatium roseum, Halorhodospira neutrophila, Isochromatium buderi, Marichromatium gracile, Thiobaca trueperi, Thiococcus pfennigii, Thiodictyon elegans, Thioflavicoccus mobilis, Thiohalospira alkaliphila, Thiorhodococcus pfennigii or Thiorhodospira sibirica.    USE - The microbial agent is useful for purifying wastewater (claimed).    ADVANTAGE - The wastewater can be purified by simple and cost-effective process.    DETAILED DESCRIPTION - Microbial agent comprises culture material of Allochromatium palmeri, Ectothiorhodosinus mongolicus, Halochromatium roseum, Halorhodospira neutrophila, Isochromatium buderi, Marichromatium gracile, Natronocella acetinitrilica, Rhabdochromatium marinum, Thermochromatium tepidum, Thioalkalicoccus limnaeus, Thioalkalispira microaerophila, Thiobaca trueperi, Thiococcus pfennigii, Thiodictyon elegans, Thioflavicoccus mobilis, Thiohalospira alkaliphila, Thiorhodococcus pfennigii or Thiorhodospira sibirica. The microorganism is cultured in culture fluid having pH of 6-7. An INDEPENDENT CLAIM is included for device for sewage disposal.
NOVELTY - Invention can be used for additional production-engineering processes on wood processing plants. Wood material is fed into the storage bin of the loading mechanism 1. Using a slanting auger conveyor 16, wood material is fed through an additional storage bin with a tamping auger into the top converter-chamber 9 of the reactor 4, where the material undergoes thermal treatment with formation of pyrolysis gases and carbonated charcoal. Using a horizontal bar-scrapper conveyor 11 of the converter-chamber 9, the material is moved with simultaneous mixing and is fed into converter-chamber 10 through unloading mechanism 13. The carbonated wood semi-finished product is activated in the converter-chamber 10.    USE - Chemistry.    ADVANTAGE - Invention increases output of the apparatus due to continuous pyrolysis and activation processes with simplification of the design of the apparatus. 5 cl, 2 dwg
NOVELTY - A biomass gasification process comprises drying and carrying out pyrolysis, carrying out combustion and deoxidation, and gas reforming; where the gasification agents are respectively introduced; and the processes are respectively and continuously performed in three independent spaces of same gasification device to obtain high-quality product gas.    USE - The process is useful for gasifying biomass (claimed).    ADVANTAGE - The process can obtain the clean product gas from the biomass; thus, it has no secondary pollution, and has high carbon conversion efficiency and simple implementation method.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of the biomass gasification process (Drawing includes non-English language text).
NOVELTY - Use of gas to liquid products as blending components for producing innovative biofuels, is disclosed.    USE - The gas to liquid products are useful as blending components for producing innovative biofuels, which are useful in electric car and hydrogen fuel cell.    ADVANTAGE - The gas to liquid products exhibit; positive effect on cold flow properties; decreased environmental emissions such as nitrogen oxide (NOx), sulfur dioxide, carbon monoxide and particulates; and improved density, and decreased flash point and cetane number. The gas to liquid products can increase the quantities of innovative biofuels used in diesel, and provide environmental-friendly biofuels.
NOVELTY - A dairy manure fuel block comprises 1000 kg of semi-dried dairy manure, 0.8-1.2 kg of nitrate, 0.8-1.2 kg of potassium permanganate, and 1.3-1.7 kg of sodium chloride; where the semi-dried dairy manure contains 36-44 wt.% of water.    USE - The dairy manure fuel block is useful for industrial and commercial applications.    ADVANTAGE - The dairy manure fuel block occupies small space, prevents mosquito and fly, needs no heating or drying, and saves energy. Moreover, the dairy manure fuel block that is shaped without chopped grass and straw has high strength and high burning value and free from the influence of season and temperature.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for producing the dairy manure fuel block comprising: (a) weighing 1000 kg of semi-dried dairy manure, 0.8-1.2 kg of nitrate, 0.8-1.2 kg of potassium permanganate, and 1.3-1.7 kg of sodium chloride; (b) agitating the materials uniformly by a rail agitator; and (c) processing the materials into honeycomb coal to obtain dairy manure fuel blocks; where the semi-dried dairy manure in (a) contains 36-44 wt.% of water.
NOVELTY - A carbonization incineration processing apparatus has a carbonization incineration furnace main portion (2), into which waste material (1) is supplied, primary and secondary heaters (4,7), gas combustion chamber (5) and air supply structures (3,6) for separately supplying air to furnace main portion and combustion chamber. The primary heater is provided at bottom portion of furnace main portion, and carries out heating, carbonization and incineration of waste material. The secondary heater is provided in combustion chamber.    USE - Carbonization incineration processing apparatus is used for processing waste material e.g. medical waste, used diaper and agricultural waste.    ADVANTAGE - The carbonization incineration processing apparatus is economical, and has simple structure.    DETAILED DESCRIPTION - A carbonization incineration processing apparatus has a carbonization incineration furnace main portion, into which waste material is supplied, primary and secondary heaters, gas combustion chamber and air supply structures for separately supplying air to furnace main portion and combustion chamber. The primary heater is provided at bottom portion of furnace main portion, and carries out heating, carbonization and incineration of waste material. The combustion chamber is provided in ceiling portion of furnace main portion, and combustion gas produced from heated waste material is supplied to chamber. The secondary heater is provided in combustion chamber, and carries out heating of combustible gas.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of carbonization incineration processing apparatus.    Waste material (1)    Furnace main portion (2)    Air supply structures (3,6)    Heaters (4,7)    Gas combustion chamber (5)
NOVELTY - Fertilizer formulation comprises domestic sludge or animal waste, nanometer colloid beam solution, silver colloid, nanometer titanium dioxide, hydrogen peroxide, phosphoric acid, aqueous ammonia, magnesium carbonate, calcium oxide and zeolite.    USE - Fertilizer formulation used for processing domestic sludge or animal waste, and soil conditioner and grain fertilizer (claimed).    ADVANTAGE - The formulation can homogeneously mix domestic sludge and animal waste with any regular movable mixer; the dried material can be converted into small grains, small spheres or the shape needed by the final dry fertilizer or soil conditioner by granulating device; and saves time, labor, space, transportation and energy source needed by processing the domestic sludge and animal waste.
NOVELTY - Producing biodiesel fuel comprises processing mesopelagic fish and/or marine algae to obtain lipids and transesterifying the lipids with an anhydrous potassium or sodium methoxide solution.    USE - The fuel can be used in road vehicles in winter conditions.
NOVELTY - Producing hydrogen from methanol involves providing flow of methanol and (1) catalytically converting part of methanol or fuel gas with air oxygen to carbon dioxide and water, while generating heat and (2) catalytically converting the methanol or remaining part of methanol at elevated temperature to hydrogen and carbon monoxide, followed by conversion of carbon monoxide with water to hydrogen and carbon dioxide, where both steps (1) and (2) are carried out in bed of sintered metal particles, where the beds of sintered metal particles are in heat exchanging relationship.    USE - For producing hydrogen from methanol (claimed), used in fuel cell; for mobile applications, such as, combined with fuel cells, and for automotive applications.    ADVANTAGE - The present method overcomes the disadvantages of prior art systems. As it producing hydrogen from methanol on a small scale which suitable for mobile applications, such as, combined with fuel cells, for instance, for automotive applications.    DETAILED DESCRIPTION - Producing hydrogen from methanol involves providing at least one flow of methanol and (1) catalytically converting part of the methanol or a fuel gas with air oxygen to carbon dioxide and water, while generating heat and (2) catalytically converting the methanol or the remaining part of the methanol at elevated temperature to hydrogen and carbon monoxide, followed by conversion of the carbon monoxide with water to hydrogen and carbon dioxide, where the heat generated in step (1) is sufficient to produce the elevated temperature required in step (2), where both steps (1) and (2) are carried out in a bed of sintered metal particles, the bed of sintered metal in step (2) having a surface that is catalytically active for the conversion of methanol to hydrogen, where the beds of sintered metal particles are in heat exchanging relationship.
NOVELTY - An organic fertilizer is obtained by preparing materials comprising (pts.wt.) sulfur (1-2), pine wood chips (50-70) and peanut skin (90-110); adding water (30-40 wt.% of total weight of materials); mixing fully and stirring uniformly; sending mixture to a fermentation tank to carry out sealing and fermentation at 30-40 degrees C; and after 45 days, measuring the temperature at 50 mm of the tank, and when the temperature is 40 degrees C, finishing the fermentation.    USE - Organic fertilizer used for blueberry planted in field (claimed).    ADVANTAGE - The fertilizer can regulate pH of the soil to 4.5-5.5, which can meet growth requirements of the blueberry.
NOVELTY - The device has a shell (1) i.e. vertical deodorizing tower body, whose top part and bottom part are respectively provided with an air outlet port (10) and an air inlet port (2). An upper side of the air inlet port is welded with a packing layer bracket (8) in a transverse section of the shell. A lower part of the packing layer bracket is provided with a water reservoir (9). A water circulating pump (6) is equipped at an outer side of the shell. The water reservoir is equipped with an automatic make-up valve (7) that is connected with a supplementary supply pipe.    USE - Biochemical and physicochemical combination deodorizing device for rubbish processing and waste water processing/fecal treatment.    ADVANTAGE - The device has high deodorizing efficiency, low energy consumption and low deodorant consumption, and reduces labor intensity.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a biochemical and physicochemical combination deodorizing device.    Shell (1)    Air inlet port (2)    Water circulating pump (6)    Automatic make-up valve (7)    Packing layer bracket (8)    Water reservoir (9)    Air outlet port (10)
NOVELTY - An off-grid wind-powered energy generating system comprises wind-powered generator (1), wire (2), electrolysis electrodes (3), water pool (4), gas compressor (5), gas guide pipe, gas tank and hydrogen electricity generating apparatus.    USE - An off-grid wind-powered energy generating system used for generating hydrogen used as fuel, and generating hydrogen used for generating electricity (claimed).    ADVANTAGE - The system solves problem about storage of energy in wind-powered electricity generation, and reduces requirement on wind-powered generator and requirement on stability of wind power.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of off-grid wind-powered energy generating system.    Wind-powered generator (1)    Wire (2)    Electrolysis electrodes (3)    Water pool (4)    Gas compressor (5)
NOVELTY - A Bionectria ochroleuca deposited under CGMCC NO.3470, for decomposing bioplastic, is new.    USE - The strain, mutant, variant or derivative of the strain, bacterial strain culture, or fermentation culture solution is useful for decomposing bioplastic comprising polybutylene succinate or polysuccinic acid/adipic acid butanediol ester (all claimed).    ADVANTAGE - The Bionectria ochroleuca has wide adapting range for natural environment conditions such as temperature and pH; is easy to culture and preserve; can rapidly decompose polybutylene succinate or polysuccinic acid/adipic acid butanediol ester bioplastic or waste; can reduce white plastic; and is good for environment protection.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are: (1) a mutant, variant or derivative of Bionectria ochroleuca; (2) a bacterial strain culture or fermentation culture solution prepared by the Bionectria ochroleuca; (3) a bacterial strain culture or fermentation culture solution prepared by the mutant, variant or derivative of the Bionectria ochroleuca; and (4) use of Bionectria ochroleuca for decomposing bioplastic.
NOVELTY - A fuel from algae and/or aquatic plant is prepared by putting algae and/or aquatic plant in a sealed reaction vessel, heating the reaction vessel to 200-500 degrees C at 5-100 degrees C/minute under 0-30 MPa, collecting generated gas, condensing, and distilling.    USE - Method of preparing fuel from algae and/or aquatic plant (claimed).    ADVANTAGE - The method does not require drying the raw materials, thus it reduces energy and simplifies the process, and produces biomass material with high water content.
NOVELTY - The apparatus (X) has a stirring reaction tank (10) for mixing of fat, oil and reaction liquid to obtain bio diesel fuel. A frame (30) to support the reaction tank, is comprised of poles so as to expose outer surface of tank. A control box (40) for controlling the operation of tank is attached to frame. A shut-off valve (22) is arranged in lower portion of reaction liquid injection container (20) used for injecting the reaction liquid from tank. A holding element (13) is arranged in upper portion of the tank, to store the reaction liquid.    USE - Bio diesel fuel production apparatus.    ADVANTAGE - The possibility for leakage of reaction liquid can be avoided and cost of the bio diesel fuel production apparatus can be reduced. The structure of the apparatus can be simplified and the need for arrangement of pump in apparatus can be simplified. The maintenance operation of the apparatus can be simplified. The freedom degree of layout of the apparatus can be increased. The rubber heater and heat insulating material can be easily attached to the outer surface of main portion of reaction tank.    DETAILED DESCRIPTION - The apparatus has a connection opening formed on the surface of tank, for connection of discharge port and discharge pipe arranged in tank.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of the reaction liquid injection container of bio diesel fuel production apparatus.    Stirring reaction tank (10)    Holding element (13)    Reaction liquid injection container (20)    Shut-off valve (22)    Frame (30)    Control box (40)    Bio diesel fuel production apparatus (X)
NOVELTY - An integrated process of producing ethanol and biogas from raw plant materials involves: fermenting sugars derived from raw plant materials to produce a beer comprising ethanol; distilling the beer into the ethanol and a whole stillage; separating the whole stillage into a thin stillage and wet distillers grains, the thin stillage comprising non-fermentable solids and organic acids; anaerobically digesting a first portion of the thin stillage to produce biogas and a biogas effluent; and recycling the biogas effluent as backset.    USE - For producing ethanol and biogas (claimed).    ADVANTAGE - The process relates to anaerobic digestion of byproducts of the ethanol production process to generate biogas and to render the byproducts more readily recyclable into the ethanol process, thus improves the energy efficiency and throughput of the ethanol production process and reduces or eliminates the need to dispose of wastewater and other byproducts.    DETAILED DESCRIPTION - An integrated process of producing ethanol and biogas from raw plant materials, involves: fermenting sugars derived from a mixture including the raw plant materials to produce a beer comprising ethanol, the mixture comprising fresh water and backset; distilling the beer into the ethanol and a whole stillage; separating the whole stillage into a thin stillage and wet distillers grains, the thin stillage comprising non-fermentable solids and organic acids; optionally concentrating a first portion of the thin stillage into a syrup by boiling off vapor from the thin stillage; anaerobically digesting a first portion of the thin stillage to produce biogas and a biogas effluent by converting the non-fermentable solids and organic acids into biogas, thereby reducing the concentration of non-fermentable solids and organic acids in the biogas effluent; and recycling the biogas effluent as backset.
NOVELTY - The fuel cell has a gasket (42) provided between anode board (44) and cathode board (46) so that porous membrane (30) and membrane electrode assembly (8) are covered. A space (2) for collecting gas generated by fuel cell reaction in anode electrode (28) is formed between porous membrane or anode electrode, and gasket.    USE - Fuel cell for personal computer and mobile telephone.    ADVANTAGE - Since porous membrane can perform gas-liquid separation, need for providing separate element for performing gas-liquid separation of methanol aqueous solution discharged through the anode flow path is eliminated so that size reduction is enabled. Pressure loss of anode flow path is reduced by suppressing generation of bubble by mixing of carbon dioxide in anode flow path.    DESCRIPTION OF DRAWING(S) - The drawing shows the cross sectional view of the fuel cell.    Space (2)    Membrane electrode assembly (8)    Anode electrode (28)    Porous membrane (30)    Gasket (42)    Anode board (44)    Cathode board (46)
NOVELTY - A plant oil-and-water property emulsion comprises vegetable oil which is dispersed with surfactant.    USE - A plant oil-and-water property emulsion for diesel fuel (claimed) used for internal combustion engine.    ADVANTAGE - The plant oil-and-water property emulsion has high oil component content, and is excellent in stability.    DETAILED DESCRIPTION - A plant oil-and-water property emulsion comprises vegetable oil which is dispersed with surfactant of formula R1-(O-R2-)n-OH.    R1=6-30C aliphatic hydrocarbon;    R2=1-3C alkylene; and    n=3-18.    An INDEPENDENT CLAIM is included for a method of manufacturing plant oil-and-water property emulsion involving mixing vegetable oil and surfactant and adjusting pre-mix liquid, mixing pre-mix liquid and water and adjusting aqueous dispersion, and adding dispersion stabilizer to aqueous dispersion while stirring.
NOVELTY - The bioreactor fluidized bed type biological treatment apparatus has a bioreactor tank (4) containing a carrier carrying microorganisms. A sludge peeling mechanism (6) is connected to the bioreactor tank. A sludge discharge mechanism (8) is connected with the sludge peeling mechanism and the bioreactor tank. The sludge discharge mechanism has a sludge separation tank for separating sludge and carrier, carrier returning unit returning the carrier to the bioreactor tank and a sludge sending unit sensing out the sludge from the sludge separation tank.    USE - Bioreactor fluidized bed type biological treatment apparatus for treatment of waste water such as industrial waste water, public waste water such as sewage and urine and water in lakes, marshes and rivers. Can also be used in treatment of foodstuff and chemicals.    ADVANTAGE - The separation of the sludge and the carrier and the collection of carrier are performed automatically without stopping circulation of waste water in the bioreactor tank for improving waste water treatment operation efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic block diagram of the principal portion of the bioreactor fluidized bed type biological treatment apparatus.(Drawing includes non-English language text)    Bioreactor tank (4)    Circulation tank (5)    Sludge peeling mechanism (6)    Blower (7)    Sludge discharge mechanism (8)
NOVELTY - The system has a filter for sucking air, a raw material compressor (1), an air purifying system (3), an air separating device, and a nitrogen refrigeration circulation device. The nitrogen refrigeration circulation device comprises a low-temperature nitrogen pressure machine (15), a liquified nitrogen gas (LNG) heat exchanger (16), and a gas-liquid separator (18). A heat exchanger (19) exchanges cool energy of low-temperature natural gas with ethylene glycol solution. The raw material compressor is provided with an intermediate cooler and an end-grade cooler (2).    USE - Air separating system.    ADVANTAGE - The air separating system saves cooling water, and reduces energy consumption.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of an air separating system.    Raw material compressor (1)    End-grade cooler (2)    Air purifying system (3)    Low-temperature nitrogen pressure machine (15)    Liquified nitrogen gas heat exchanger (16)    Gas-liquid separator (18)    Heat exchanger (19)
NOVELTY - The device has an open type discharge groove (8) connected to a material connector on a furnace chamber of a plasma gasification furnace. A joint of a charging chute (4) and a feed pipe (1) is provided with a closed air chamber (2), where an outlet end of the closed air chamber is provided with multiple closed wind nozzles (3) facing the chute. The joint of the charging chute and the discharge groove is provided with a sowing air chamber (5), where the outlet end of the sowing chamber is provided with multiple sweeping and sowing wind nozzles (6, 7) facing the charging chute and the groove.    USE - Feeding device for a plasma gasification furnace.    ADVANTAGE - The device allows biomass fuel to-be-distributed evenly in the furnace for gasifying the biomass fuel, thus improving stability and continuity of the plasma gasification furnace, and preventing burning down of the device by backward escaping of the high-temperature flue gas in the furnace. The device is simple, easy to be maintained and suitable for remodeling various plasma gasification furnaces at low cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a feeding device of a plasma gasification furnace.    Feed pipe (1)    Closed air chamber (2)    Multiple closed wind nozzles (3)    Charging chute (4)    Sowing air chamber (5)    Sweeping wind nozzles (6)    Sowing wind nozzles (7)    Open type discharge groove (8)
NOVELTY - The furnace has a gasification furnace shell body (1) provided with a raw material bed (3). A gasified gas inlet (6) is arranged below the bed. A bottom part of the body is provided with a slag discharging hole (8). A top part of the body is provided with a gasification separated wall (2). An upper part of the body is divided into left and right cavity chambers (a, b) by the wall. The left chamber is provided with a raw material input port (4). A circulating air inlet (7) is arranged on the input port. An upper part of the right chamber is provided with a crude synthetic gas outlet (5).    USE - Double-cavity biomass gasification furnace.    ADVANTAGE - The furnace has reduced production cost and operation cost. The tar in the synthetic gas is effectively removed in the furnace, the thermal value of the synthetic gas is improved, the processing of the purifying device is improved and the secondary pollution is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a double-cavity biomass gasification furnace.    Left cavity chamber (a)    Right cavity chamber (b)    Gasification furnace shell body (1)    Gasification separated wall (2)    Raw material bed (3)    Raw material input port (4)    Crude synthetic gas outlet (5)    Gasified gas inlet (6)    Circulating air inlet (7)    Slag discharging hole (8)
NOVELTY - The facility has a cracker shell (1) provided with a synthesis gas inlet (4) and a catalyst feeding device (3). A bottom part of the cracker shell is provided with a slagging opening (5) and a calcium oxide ejection gun (2). A top channel of the cracker shell is connected to a gas-solid separator (7). The separator includes a top section provided with a synthesis gas outlet (8) and a bottom section provided with a dust discharging opening (6).    USE - Tar cracking facility for a plasma gasification furnace.    ADVANTAGE - The facility improves tar cracking effect without polluting environment, while improving heat value of synthesis gas and reducing cost of biomass gasification device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of tar cracking facility of plasma gasification furnace.    Cracker shell (1)    Calcium oxide ejection gun (2)    Catalyst feeding device (3)    Catalyst feeding device (4)    Slagging opening (5)    Dust discharging opening (6)    Gas-solid separator (7)    Synthesis gas outlet (8)
NOVELTY - The device has a volute separator (4) whose tangential gas inlet end is connected with an end of an inlet smoke channel (3). Middle part of the volute separator is provided with a vertical central cylinder (2). An upper end of the vertical central cylinder is connected with an end of an outlet smoke channel (1). A tapered hopper-shaped lower end of the volute separator is connected with an upper end of a vertical pipe (5). A lower end of the vertical pipe is connected with an upper end of a feed-back inclined tube (7) through a feed-back valve (6).    USE - High-temperature fly ash and biomass gasified synthesis gas separating device.    ADVANTAGE - The device reduces carbon content of the fly ash, thus reducing solid grain concentration, and increasing dust removing rate to about 99 percentage. The device effectively improves the gasifying efficiency and purifies and removes dust of the synthesis gas, thus improving utilization rate of the biomass gasified synthesis gas. The device has low manufacturing cost and low operating cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a high-temperature fly ash and biomass gasified synthesis gas separating device.    Outlet smoke channel (1)    Vertical central cylinder (2)    Inlet smoke channel (3)    Volute separator (4)    Vertical pipe (5)    Feed-back valve (6)    Feed-back inclined tube (7)
NOVELTY - The gasifier has a cylindrical shell that is installed at a bottom part of the gasifier. An annular cover plate is installed at a top part of the cylindrical shell. Four sides of the gasifier are connected with an upper end of the cylindrical shell. A furnace cover with a hanging ring is installed on a central through hole of the cover plate. A through hole is formed on an upper part of the cylindrical shell in the hearth and connected with one end of the smoke pipe. An ash hole is formed on a lower part of the cylindrical shell.    USE - High-temperature short-flame straw gasifier for a furnace head.    ADVANTAGE - The gasifier reduces flame, enables high flame temperature, safe usage, long service life, less fuel dosage and long continuous firing time.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a high-temperature short-flame straw gasifier installed in the furnace head.
NOVELTY - The furnace has a hearth (2) arranged in a furnace body (1). A combustion chamber (3) connected with the hearth is arranged on the hearth. An air interlayer (4) is arranged among the sidewalls of the furnace body. A gas inlet hole (5) connected with the air interlayer is formed on the inner wall of the combustion chamber. A feed inlet (6) is connected with the upper part of the combustion chamber, and is provided on the sidewall of the furnace body.    USE - Direct burning straw gas furnace.    ADVANTAGE - The furnace has improved structure, so that the inflammable gas burns completely under the sufficient air mixture. The furnace can burn for a long time without an end boiler, and is simple in structure and low in cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a direct burning straw gas furnace.    Furnace body (1)    Hearth (2)    Combustion chamber (3)    Air interlayer (4)    Gas inlet hole (5)    Feed inlet (6)
NOVELTY - Lignite is processed by extracting lignite crystal with methanol to obtain extracting solution and residue, and thermally melting, catalyzing and liquefying extract residues.    USE - Method of processing lignite (claimed).    ADVANTAGE - The method has mild reaction condition, has simple operation process, is safe and stable, has high lignite converting rate, has low investment of equipment, and has low cost. The method also obtains humic acid, organic methyl ester and phenolic substances including phenol, methylphenol and dimethyl phenol to increase the added value of the product. The method removes alcohol and carboxylic micromolecule substances in the lignite and reduces hydrogen consumption upon thermal heating, catalyzing and liquefying processes, thus saving hydrogen waste. The method also reduces carbon dioxide discharge in the process, thus reducing contribution to greenhouse gas. The processed lignite has enhanced specific surface.
NOVELTY - The technique involves feeding water-containing biological oil into a normal-pressure distillation device, and recovering fraction liquid containing benzene, water and moderate carbon alcohol at 80-120 degrees centigrade. The liquid is cooled to normal temperature, and the cooled liquid is fed into a laying device to separate out the benzene. The liquid is delivered into a moderate carbon alcohol tower system and heated to 100-120 degrees centigrade to generate steam. The steam is fed into a condenser and a laying device in turn, and the water and the moderate carbon alcohol are separated out.    USE - Dehydrating technique for biological petrol and diesel fuel.    ADVANTAGE - The technique provides a better way for using the fraction liquid at 80-117 degrees centigrade during process of preparing biological oil to ensure dehydrating quality, recover precious chemical resource, improve caloric value of fuel and save great amount of energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of a biological petrol and diesel fuel dehydrating technique.'(Drawing includes non-English language text)'
NOVELTY - A decoking ash cleaner comprises 25-30% soda ash, 25-30% zinc oxide, 20-25% sodium nitrate or potassium nitrate, 5-10% borax, 5-10% sodium chloride, 1-4% vermiculite and 1-4% copper oxychloride.    USE - A decoking ash cleaner used for municipal solid waste incinerator.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of preparing decoking ash cleaner by mixing soda ash, zinc oxide, sodium nitrate or potassium nitrate, borax, sodium chloride, vermiculite and copper oxychloride; and crushing, sieving, agitating, and drying for 10-20 minutes at 100-150 degrees C.
NOVELTY - A process (P1) for converting biomass into soluble and insoluble fractions, involves: (i) incubating the biomass with an aqueous acidic liquor; (ii) separating the acidic liquor from the resulting solid residue of the biomass, where the acidic liquor contains the soluble fraction and the solid residue contains the insoluble fraction; and (iii) collecting the products of the biomass conversion.    USE - For converting biomass into soluble and insoluble fractions, where the biomass is selected from woody plants, gramineous plants, and/or herbage plants, and the biomass is converted to products selected from cellulose, hemicellulose, xylose polymer, xylose oligomer, xylose monomer, glucose, lignin, and/or other lignocellulosic products (all claimed), which useful in the preparation of clean, green or highly valuable biochemical, chemical, health-care products, bio-energy products, bio-originated chemicals and biodegradable plastics.    ADVANTAGE - The method reduces lignocellulosic waste; is clean process of preparing high grade biomass products; holds remarkable potential to turn the most abundant renewable resources into high value bio-fuel, biochemicals, fine chemicals and other bulk chemicals; and provides the dual advantage of a sustainable resource supply, not affecting food supplies, and all chemicals derived would have less environmental impact than petrochemicals.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for following:    (1) a lignocellulosic composition comprising at least 90% of glucose or at least 90% produced by the process (P1); and    (2) a lignocellulosic feedstock processing system comprising a set of devices capable of carrying out the process (P1).
NOVELTY - The method involves subjecting feed fraction, which contains nitrogen and hydrocarbon, to separation process into a nitrogen-rich fraction (4'') and a methane-rich fraction (5'') by rectification. The nitrogen-rich fraction and the methane-rich fraction are compressed temporarily during interruption of feed of the feed fraction and are jointly fed as the feed fraction for removing process. The compression of the nitrogen-rich and the methane-rich fraction is carried out in a separate and/or joint manner.    USE - Method for removing a nitrogen-rich fraction from a feed fraction which contains nitrogen and hydrocarbons, by a nitrogen rejection unit in a liquefied natural gas system.    ADVANTAGE - The compression of the nitrogen-rich and the methane-rich fraction is carried out in a separate and/or joint manner, thus realizing fast resumption of the nitrogen rejection unit after failure, and hence avoiding financial losses related to failure while reducing complexity of the removal process.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a nitrogen rejection unit.    Methane-outlet valve (e)    Methane compressor (V)    Lines (1,6,7)    Nitrogen-rich fraction (4'')    Methane-rich fraction (5'')
NOVELTY - A system comprises an organic polymer material in combination with nickel-63, sulfur-35 or calcium-45.    USE - System for air-breathing generating hydrogen (claimed) used in hydrogen/oxygen fuel cell (100).    ADVANTAGE - The system can generate hydrogen without the need for associated valving, tubing, reformers, shielding or high pressure storage mechanisms.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a fuel cell.    Fuel cell (100)    Hydrogen generator (110)    Membrane electrode assembly (130)    Electrodes (135, 140)    Hydrogen transporting medium (145)
NOVELTY - Fuel production involves mixing biodiesel (2) produced from vegetable oils, animal fats, from recovered or recycled oils and fats, with anhydrous ethyl alcohol (3) and additives (5).    USE - Method for producing fuel (claimed) used for spontaneous explosion engines.    ADVANTAGE - The fuel production method enables to produce the fuel in a simple and cost-effective manner. The produced fuel is eco-friendly without generating toxic emissions.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of the fuel production process.    Mixture (1)    Biodiesel (2)    Anhydrous ethyl alcohol (3)    Fuel (4)    Additives (5)
NOVELTY - Method for hydrolyzing fig residue to produce dietary fiber, involves soaking and washing fig residue, crushing washed fig residue, hydrolyzing fig residue using enzyme, precipitating using alcohol and drying the obtained product using vacuum.    USE - The method is useful for hydrolyzing fig residue to produce dietary fiber.    ADVANTAGE - The dietary fiber is of high quality and can be prepared by a simple and cost-effective process.
NOVELTY - Methyl isostearate is mixed with biomass diesel fuel at normal pressure and temperature of 5 degrees C more than the freezing point of the un-mixed biomass diesel fuel. The mixture is agitated for more than 0.5 hour and biomass diesel fuel with high oxidation stability is obtained.    USE - Method for increasing oxidation stability of biomass diesel fuel.    ADVANTAGE - The method increases the oxidation stability and low temperature flow performance of the biomass diesel fuel. The biomass diesel fuel increases the lubrication of the engine and is manufactured safely and by a simple process.
NOVELTY - Magnesium carbonate (in wt.%) (15-35), calcium carbonate (15-25), silica (3-10), iron oxide (5-20), aluminum oxide (3-10), sodium salt ore powder (15-35) and activator (3 or less) are milled into particles having grain size of 180-200 mesh and uniformly mixed. The mixed material is added into a container provided with thick wall, magnesium bar is added to the lower portion of the container to combust and natural stone powder fuel is prepared.    USE - Preparation of natural stone powder used for fuel.    ADVANTAGE - The method economically provides natural stone powder.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel, which comprises the natural stone powder (10-70 wt.%).
NOVELTY - Surplus industrial flue gas are recycled, and subjected to dust removal and desulfurization-purification processes to obtain a mixed gas containing polycarbon source and nitrogen. The mixed gas is subjected to pre-treatment and separation for discharging carbon-free flue gas. The polycarbon source is hydrogenated at 200-600 degrees C and pressure of 2-50 MPa in presence of a catalyst to obtain a liquid fuel.    USE - Preparation of liquid fuel e.g. methanol, dimethyl ether and ethanol.
NOVELTY - A low carbon biodiesel fuel comprises (in parts weight) methanol (5-30), butanol (0.3-4), octanol (0.5-5), oleic acid (10-30), 0# diesel fuel (40-70), 200# solvent oil (5-20), N,N'-diisobutyl phenylenediamine (0.01-0.05), sodium alkylsulfonate (0.1-0.4), copper naphthenate (0.1-0.2), alkyl acid amide (0.01-0.06), ethylene glycol monomethyl ether (0.02-0.08), mixture (0.05-0.1) of fatty acid and chromium-calcium salt, polyethylene-vinyl acetate (0.01-0.05), N,N'-bis-salicylidene-1,2-propanediamine (0.02-0.08) and alkyl nitrate (0.05-0.1).    USE - Low carbon biodiesel fuel is used for vehicle.    ADVANTAGE - The low carbon biodiesel fuel has excellent low-temperature starting performance and stability, and effectively reduces the content of carbon monoxide, hydrocarbon and nitrogen oxide in exhaust gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of low carbon biodiesel fuel, which involves mixing methanol, oleic acid, octanol and butanol at normal temperature and pressure, adding N,N'-diisobutyl phenylenediamine, sodium alkylsulfonate and copper naphthenate, stirring uniformly and pumping into an adjustment cylinder, fusing and adding 200# solvent oil and 0# diesel fuel in mixture of alkyl acid amide, ethylene glycol monomethyl ether, fatty acid, chromium-calcium salt, polyethylene-vinyl acetate and N,N'-bis-salicylidene-1,2-propanediamine, heating the mixture to 55 degrees C using fuel oil heat exchanger, pumping the mixture into the adjustment cylinder, adding alkyl nitrate into the adjustment cylinder and uniformly stirring.
NOVELTY - Volatile organic acid catalyst (3-12 wt.% of grease) is dissolved in alcohol and mixed with grease. The mixture is stirred and heated to 60-120 degrees C for complete reaction. Alcohol and catalyst left in the reaction liquid are removed, and the mixture is allowed to stand for layer separation. The upper reaction liquid is collected as biodiesel. The catalyst is methanesulfonic acid, ethanesulfonic acid, propanesulfonic acid, butanesulfonic acid, trifluoroacetic acid, trichloroacetic acid, chlorosulfonic acid, or trifluoromethanesulfonic acid.    USE - Preparation of biodiesel.    ADVANTAGE - The method is simple and environmental-friendly. The catalyst has excellent activity, recycle property, and reuse property.
NOVELTY - Ammonia and 2-10C polyalcohol are added to product of ester exchange reaction of oil with free fatty acid, stirred and stratified. The mixed ester phase containing aliphatic acid monoalkyl ester is collected on the upper layer, to obtain biodiesel with low acid value.    USE - Method used for reducing acid value of biodiesel.    ADVANTAGE - The method is environmental-friendly, and efficiently and economically reduces acid value of biodiesel. The generation of bad smell during reduction of acid value of biodiesel is suppressed.
NOVELTY - A harmonic diesel oil comprises (in parts weight) low temperature coal tar (70-85), cetane number improver (3-6), low temperature fluidity improver (2-5), ignition assistant (2-5) and lacquer solvent (10-120). The cetane number improver is dibutyl oxalate, the low-temperature fluidity improver is ethylene-vinyl acetate modified by maleic anhydride, the ignition assistant is t-amyl methyl ether, and the lacquer solvent is absolute ethyl alcohol.    USE - Harmonic diesel oil.    ADVANTAGE - The harmonic diesel oil has high stability, favorable combustion, improved safety, excellent fluidity and can be prepared at normal temperature and normal pressure by a simple process.
NOVELTY - A component oil comprises 120# solvent oil (20-25%), 200# solvent oil (20-25), methylbenzene (5-10), dimethylbenzene (3-5), heavy naphtha (20-30) and catalytically reformed gasoline (20-25).    USE - Component oil used for manufacturing low proportion methanol gasoline (claimed).    ADVANTAGE - The component oil effectively reduces the saturated vapor pressure of methanol gasoline, prevents vapor blocking at high temperature condition and ensures normal working of engine.
NOVELTY - A biomass coal paste is made by uniformly mixing anthracite, biomass, water and dispersing agent.    USE - Biomass coal paste.    ADVANTAGE - The biomass coal paste has low burning point and is manufactured economically. The high activity of the water hyacinth improves the combustion characteristics of the low activity anthracite. The manufacturing process of the biomass paste is environmental-friendly.
NOVELTY - A multilayer methane desulfurizer comprises a single-chamber desulfurizing main component. The lower portion of the desulfurizing main component is provided with a bracket for supporting the desulfurizing main component. The desulfurizing main component is internally provided with a two-layer or multilayer desulfurizing layer.    USE - Multilayer methane desulfurizer.    ADVANTAGE - The multilayer methane desulfurizer is compact, and has simple structure.
NOVELTY - A biological activating agent comprises (in weight parts) cellulose decomposed bacterial liquid (20), dicyclopentadienyl iron (0.8-1.2), sodium peroxide (0.81.2), methanol (9-13), and aviation kerosene (28-32).    USE - Biological activating agent is used for fuel oil for engines of vehicles.    ADVANTAGE - The biological activating agent has high efficiency, excellent corrosion resistance, and is safe to use. The vehicle engine using fuel oil containing biological activating agent has improved performance, consumes reduced amount of fuel oil, emits reduced amount of harmful gases, and prevents and eliminates accumulated carbon, and is durable.
NOVELTY - Biodiesel is mixed with methane acid, stirred, and heated. A catalyst and hydrogen peroxide mixed solution, and the reaction mixed solution is transferred to a separating tunnel after reaction completion. The upper layer liquid is separated and washed with water till neutral, to obtain epoxy biodiesel. The epoxy biodiesel is mixed with fatty alcohol, and a catalyst is added, stirred and reacted. 5% Sodium carbonate is added, and ester layer is separated. The low-boiling-point components are evaporated to obtain branched biodiesel.    USE - Production of branched biodiesel.    ADVANTAGE - The method provides branched biodiesel having excellent oxidation stability and low-temperature liquidity, by a simple operation under moderate reaction conditions suitable for large-scale industrial production.    DETAILED DESCRIPTION - Biodiesel is mixed with methane acid, stirred, and heated. A catalyst and hydrogen peroxide mixed solution, and the reaction mixed solution is transferred to a separating tunnel after reaction completion. The upper layer liquid is separated and washed with water till neutral, to obtain epoxy biodiesel. The epoxy biodiesel is mixed with fatty alcohol, and a catalyst is added, stirred and reacted. 5% sodium carbonate is added for washing and the reaction mixture is poured into a separating tunnel, to separate an ester layer. The low-boiling-point components are evaporated to obtain branched biodiesel.
NOVELTY - Producing fuel ethanol by cofermentation, involves (a) screening Rhizopus oryzae strain with amylase and cellulase enzymatic activity, and (b) inoculating yeast seed and R.oryzae into substrate containing kitchen waste (as raw material), stewing and fermenting the mixture for 96 hours at 25 degrees C, centrifuging fermented mixture, obtaining the supernatant and subjecting the supernatant to distillation.    USE - Production of fuel ethanol.    ADVANTAGE - The method overcomes the complexity in hydrolyzing kitchen waste due to the presence of inactivated enzyme, thus ethanol fermentation is performed completely. The method does not require any catalyst and nutrient to be added during fermentation, saves energy source and is simple, thus reduces the production cost of ethanol.
NOVELTY - A crosslinked-type perfluorinated sulfonic acid ion exchange membrane has crosslinked structure (I). The crosslinked structure is formed by crosslinking sulfonic acid group and sulfo group of perfluorosulfonate ion-exchange resin molecule by diamine or a compound containing 2 or more amino groups. The perfluorosulfonate ion-exchange resin (II) is hydrogen ion or sodium ion exchange resin.    USE - Crosslinked-type perfluorinated sulfonic acid ion exchange membrane is used for proton exchange membrane fuel cell.    ADVANTAGE - The proton exchange membrane fuel cell using crosslinked-type perfluorinated sulfonic acid ion exchange membrane has excellent oxidation resistance and reliability, and is economical.    DETAILED DESCRIPTION - A crosslinked-type perfluorinated sulfonic acid ion exchange membrane has crosslinked structure of formula: R1-S(=O)2-NH-R-NH-S(=O)2-R2 (I). The crosslinked structure is formed by crosslinking sulfonic acid group and sulfo group of perfluorosulfonate ion-exchange resin molecule by diamine or a compound containing 2 or more amino groups. The perfluorosulfonate ion-exchange resin of formula (II), is hydrogen ion or sodium ion exchange resin.    R1,R2=perfluorosulfonate ion-exchange resin molecular chain;    R=carbon chain;    x,y=1-1000;    x/(x+y)=55-95%;    y/(x+y)=10-45%;    m=0, 1 or 2;and    n=1-6.    An INDEPENDENT CLAIM is included for preparation of crosslinked-type perfluorinated sulfonic acid ion exchange membrane. N,N'-carbonyl diimidazole and perfluorosulfonate ion-exchange resin are dissolved in an organic solvent to form perfluorinated casting solution. The total content of N,N'-carbonyl diimidazole and perfluorosulfonate ion-exchange resin is 8-60%. A crosslinked agent is added to the obtained perfluorinated casting solution, stirred uniformly, and organic solvent is evaporated to obtain crosslinked-type perfluorinated sulfonic acid ion exchange membrane.
NOVELTY - A dispersible concentrate comprises plant oil methyl ester as substrate, abamectin (A), and spirodiclofen, lufenuron, capillary, nitenpyram or spinosad (B). The weight ratio of components A and B is 1:1-300.    USE - A dispersible concentrate.    ADVANTAGE - The concentrate has strong product adhesion thus improving deposit of active ingredient on target surface and ability for passing through wax layer on the target surface, has improved biological utilization, reduces dosage of agrochemical, delays pest resistance, lightens photo-chemical pollution of agrochemical, and is environment-friendly.
NOVELTY - A traditional Chinese medicinal composition comprises (mass%): radix sophorae flavescentis, Phytolacca acinosa (10-50), Stemona tuberosa (10-40), antipyretic Dichroa (5-20), and effective insecticide (1-30).    USE - Traditional Chinese medicinal composition (C1) used in preparing medicine for preventing and controlling parasite in water (claimed).    ADVANTAGE - The composition (C1) does not have toxic or side effect, and does not generate medicine residue; is convenient to use and low in cost; and does generate drug resistance, and is easily decomposed and pollution-free.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the composition (C1) which comprises respectively crushing and screening radix sophorae flavescentis, Phytolacca acinosa, Stemona tuberosa, and antipyretic Dichroa; drying, crushing and screening effective insecticide; and uniformly mixing, and obtaining desired composition (C1).
NOVELTY - Seedling substrate comprises byproduct of crops, an organic waste substance, a byproduct produced in preparing material during pulping of grass or mixture and ammonia water.    USE - Used as a seedling substrate.    ADVANTAGE - The seedling substrate reuses the waste material and the waste liquid produced during the ammonium sulfite pulping process, thus changes the waste to valuable and enhances permeability, nutrient content, growth and root number by more than 30%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the seedling substrate comprising mixing the byproduct of crops, the organic waste substance, the byproduct produced in preparing the material during the pulping of grass or mixture and ammonia water, obtaining a fermenting mixture, fermenting the mixture and finishing the fermenting at a mass ratio of carbon to nitrogen in the mixture of 30:1 and pH of 6.5-8.5.
NOVELTY - Producing bioorganic fertilizer comprises: powdering an organic substance, uniformly mixing, using a fermentation microorganism strain, fermenting and rotting, adding an inorganic element e.g. nitrogen, phosphorus or potassium when the colony content is 30 hundred million, obtaining the particle, drying the particle, uniformly mixing the dried particle, chitin, avermectin and water and dewatering.    USE - The method is useful for producing bioorganic fertilizer.    ADVANTAGE - The method improves soil and culturing land capability, quality of crops and utilization rate of the fertilizer, reduces content of harmful substance, heavy metal and environmental pollution.
NOVELTY - Crude DL-para-hydroxyphenylglycine is washed using water and alcohol to purify DL-para-hydroxyphenylglycine. The purified DL-para-hydroxyphenylglycine (98.5%) is in the form of white powder.    USE - Purification of DL-para-hydroxyphenylglycine used as intermediate of pharmaceutical.    ADVANTAGE - The method economically and easily provides highly-purified DL-para-hydroxyphenylglycine having excellent resolution, without causing environmental pollution. The discharged sewage is easily treated.
NOVELTY - D-(-)-p-hydroxybenzene glycine-p-methyl sulfonate is dissolved in water, and heat of the solution is maintained. Then, the reaction liquid is decolorized using activated carbon, heat retained and centrifuged after reducing temperature of the reaction liquid in order to obtain purified D-(-)-p-hydroxybenzene glycine-p-methyl sulfonate.    USE - Method for purifying D-(-)-p-hydroxybenzene glycine-p-methyl sulfonate used as intermediate for pharmaceuticals.    ADVANTAGE - The method is environmental-friendly and enables efficient and economical purification of D-(-)-p-hydroxybenzene glycine-p-methyl sulfonate with high purity, and reduced discharge of sewage. The discharged sewage is treated easily.
NOVELTY - A garbage carbon comprises (in parts weight) combustible garbage (100-300), coal powder (50-500), clay (20-100, 50-100 or 0-80) and quicklime (0.5-30 or 0-10).    USE - Garbage carbon.    ADVANTAGE - The garbage carbon is economically transported and manufactured without causing environmental pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of garbage carbon, which involves crushing combustible garbage, coal powder, clay and quicklime, adding water, uniformly stirring, extruding, press-forming and drying.
NOVELTY - An o-heterocycle formanilide compound (I) or (II), is new.    USE - An o-heterocycle formanilide compound used for preparing pesticide (claimed) for agricultural and gardening field.    ADVANTAGE - The compound has low toxicity and is environment-friendly.    DETAILED DESCRIPTION - An o-heterocycle formanilide compound of formulae (I) or (II), is new.    X1, X2=H, halo or CN;    Z=O or S;    R1, R2=1-5C alkyl, 1-5C halogenated alkyl, OH, 1-5C alkoxy, 1-5C halogenated alkoxy, sulfhydryl, 1-5C alkylthio, NH3, 1-5C alkylamino, 1-5C alkyl sulfonamido or 1-5C acyl.    INDEPENDENT CLAIMS are included for:    (1) a preparation of o-heterocycle formanilide compound;and    (2) a pesticide composition, i.e. emulsion in water, suspending agent, water dispersible granules or miscible oil agent, comprising compound (I) or (II) as active ingredient and pesticide additive.
NOVELTY - Lignocellulosic biomass pretreatment involves treating lignocellulose with a solution of alkaline hydrogen peroxide. The pretreated biomass undergoes enzymatic hydrolysis by using mixture, which comprises cellulase, beta -glycosidase or hemicellulase. The carbohydrate produced after pretreatment undergoes fermentation to obtain product for industrial production of ethanol or other alcohol.    USE - Method for pretreating lignocellulosic biomass for industrial production of alcohol.    ADVANTAGE - The lignocellulosic biomass pretreating method is substantially useful for obtaining product for producing alcohol.
NOVELTY - The method involves stacking lower gas diffusion layer (4'), membrane electrode assembly (MEA) (3) and upper gas diffusion layer (4) in order so as to electrode (5). The electrode is accommodated in molding die. The high temperature processing is performed by applying load to upper gas diffusion layer and side projected portions (1a) of MEA. The gasket molding processing is performed by injecting resin into molding die, from the side of electrode to periphery. The temperature at the time of high temperature and gasket molding processing are maintained at same value.    USE - Manufacturing method of fuel cell mounted in electric vehicle, hybrid vehicle and used for domestic application.    ADVANTAGE - The electric power generation efficiency can be improved. The durability of fuel cell can be improved. Since the electrolytic membrane can be shrunk without enlargement of center portion of electrode, the sealing performance of gas can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the fuel cell.    Side projected portions of MEA (1a)    MEA (3)    Upper gas diffusion layer (4)    Lower gas diffusion layer (4')    Electrode (5)
NOVELTY - The method involves forming MEA (3), gas permeation layers (4,4',6') and separator (7). The projecting edge (1a) of electrolytic membrane (1) is folded and changed, and the bending position is maintained. The separator, lower gas permeation layers, MEA and upper gas permeation layer are accommodated in order in the molding die. The resin in injected into the MEA accommodated in molding die. The gasket is molded to periphery of MEA and gas permeation layer such that fuel cell is formed.    USE - Manufacturing method of fuel cell used for electric vehicle, hybrid vehicle and domestic applications.    ADVANTAGE - The projecting edge is lifted by resin pressure in case of injection molding and outer surface of gasket is faced such that cross leak path is formed and the durability of fuel cell is increased effectively with simple manufacturing process.    DESCRIPTION OF DRAWING(S) - The drawing shows a longitudinal cross-sectional view of the gasket molded within molding die.    Electrolytic membrane (1)    Protruding edge of electrolytic membrane (1a)    Catalyst layer of cathode side (2)    Gas permeation layers (4.4',6')    Separator (7)
NOVELTY - The fuel cell (1) has a separator (8) which is positioned at the outer side of a fuel electrode collector (7) and air electrode collector (14) which are positioned at the outer side of an electric power generation cell (5). A recess (11) which does not contact an air electrode layer (3) is formed in a position opposite to an oxidizing agent gas discharge hole (10) formed on surface at the side of air electrode layer.    USE - Flat type solid oxide fuel cell for generating electric power. Can also be used as solid oxide fuel cell of circular form/polygonal shape/square shape.    ADVANTAGE - Reduction of the electric power generation performance can be prevented since the recess which does not contact the position opposite to the oxidizing agent gas discharge hole is formed on surface at the side of air electrode layer. The evaporation of the chromium contained in the stainless steel can be eliminated thus preventing the chromium poisoning and the fall of cell voltage.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the flat type solid oxide fuel cell. (Drawing includes non-English language text)    Flat type solid oxide fuel cell (1)    Air electrode layer (3)    Electric power generation cell (5)    Fuel electrode collector (7)    Separator (8)    Oxidizing agent gas discharge hole (10)    Recess (11)    Air electrode collector (14)
NOVELTY - The method involves a measuring an alternating current (AC) impedance of several frequencies in the several regions of membrane electrode assembly (MEA). The distribution of an electrolyte in thickness direction of primary electrode of MEA is estimated based on AC impedance. A secondary electrode is manufactured based on distribution estimation result by adjusting manufacturing conditions with respect to a region which does not corresponds to distribution of electrolyte in thickness direction of primary electrode of MEA.    USE - Manufacturing method of solid polymer type fuel cell.    ADVANTAGE - Since the secondary electrode is manufactured by adjusting manufacturing conditions with respect to region which does not correspond to distribution of electrolyte in thickness direction of primary electrode, the fuel cell can be manufactured efficiently with simple structure.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating the manufacturing process of fuel cell. (Drawing includes non-English language text)
NOVELTY - Catalyst metal and polymer electrolyte are mixed, to obtain microparticles which are mixed with a solvent which dissolves the polymer electrolyte, to obtain catalyst paste (S120). The obtained paste is molded into sheet form, and an original catalyst layer is formed (S130). The catalyst layer is then extended (S140), to form porous electrode.    USE - Manufacture of electrode used for fuel cell.    ADVANTAGE - The method provides electrode having favorable catalyst metal per unit area, thickness and porosity.    DESCRIPTION OF DRAWING(S) - The drawing shows the flowchart illustrating manufacture of electrode. (Drawing includes non-English language text)    Preparation of catalyst ink (S100)    Production of polymer electrolyte (S110)    Production of catalyst paste (S120)    Formation of catalyst layer (130)    Process of extending catalyst layer (S140)
NOVELTY - The fuel reformer (50) has a reforming reaction section (5) filled with modification catalyst (6) of fuel gas which is mixed with hydrocarbon type raw fuel (F) and water vapor. A burner (7) heats the burner combustion space (8) formed adjacent to reforming reaction section. A heat insulating element (9) is arranged so as to surround the burner combustion space, having chlorine content equal to or less than 20ppm-w.    USE - Fuel reformer of fuel cell electric power generation system (claimed).    ADVANTAGE - The material corrosion amount of heat exchanger or piping arranged below the burner of fuel reformer can be suppressed effectively. The fuel cell electric power generation system can be driven stably.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) fuel cell electric power generation system;    (2) pre-processing method of fuel reformer; and    (3) pre-processing method of fuel cell electric power generation system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the fuel cell electric power generation system. (Drawing includes non-English language text)    Reforming reaction section (5)    Modification catalyst (6)    Burner (7)    Burner combustion space (8)    Heat insulating element (9)    Fuel reformer (50)    Hydrocarbon type raw fuel (F)
NOVELTY - Extracting bezafibrate high efficient degrading strain comprises inoculating activated sludge and standing sample acclimatized and performing enrichment culture to guarantee pure single strain.    USE - The method is useful for extracting bezafibrate high efficient degrading strain (claimed).    ADVANTAGE - The resource is easy to obtain the separating and purifying method is simple; it has low cost and is environmental friendly; the degrading ratio of the strain to bezafibrate is more than 85%; and it has good application prospect.    DETAILED DESCRIPTION - Extracting bezafibrate high efficient degrading strain comprises: (a) inoculating activated sludge from the second precipitation pool of the urban sewage treatment plant into the inorganic salt culture with an inoculating amount if 5 wt%, acclimatizing it for 2 mouths by gradient pressure acclimatization method; and (b) standing the sample acclimatized for 2 mouths for 30 minutes, providing 1 mL of upper water sample for gradient dilution, inoculating 1 mL of strain solutions with different diluted concentration to the solid culture to perform enrichment culture so as to guarantee the pure single strain, then inoculating it to the inclined culture medium, preserving it at 4 degrees C.
NOVELTY - Gasoline comprises biomass-to-liquid (BTL) naphtha and oxygenated bio-components comprising ethanol and/or ethyl tert-butyl ether (ETBE).    USE - Used as a gasoline.    ADVANTAGE - The carbon number distribution of BTL naphtha can be used to balance out some of the negative impact of the non-linear blending properties of ethanol, hence reduces (reformulated blendstock for oxygenate blending) cost. The bio-component mixtures incorporate significant levels of BTL naphtha and ethanol/ETBE in volume ratios of 1:2-5 can be used to meet bio-energy targets, this involves the high octane quality of ethanol and/or ETBE being used to compensate for the low octane quality of the BTL naphtha. The gasoline utilizes high octane quality of ethanol and/or ETBE to compensate the low octane quality of the BTL naphtha. The higher the octane quality the greater the potential blend ratio in the gasoline before the gasoline constraints becomes restrictive. The naphtha in the gasoline reduces the amount of elastomer swell caused by ethanol.
NOVELTY - Jet fuel blend comprises a standard jet A-1 fuel derived from crude oil, a Fischer-Tropsch derived kerosene and a highly paraffinic, non-oxygenated, material derived from biomass (e.g. hydrotreated vegetable oil).    USE - The composition deals about blend for jet fuel.
NOVELTY - Invention relates to processing materials which contain organic substances and can be used in thermal decomposition of wood processing wastes, plant growing products, food industry wastes, animal and poultry farming wastes. The method for thermal processing materials which contain organic substances into gaseous and liquid fuel involves first heating in a drying chamber, which is a storage bin, with a drying agent at 160-200 degrees C which is obtained by mixing furnace gases passing through the jacket of a pyrolysis chamber, with air and then without air in a pyrolysis chamber with conversion of the pyrolysis products to carbon and gaseous fuel-vapour-gas mixture with subsequent condensation of a portion of the vapour-gas mixture to liquid fuel, where a portion of uncondensed vapour-gas mixture after pre-heating to 450-520 degrees C is fed into the pyrolysis chamber in an amount which provides for dwell time of the pyrolysis products in the pyrolysis chamber of not more than 2 seconds and excess pressure in the pyrolysis chamber between 500 and 1000 Pa.    USE - Chemistry.    ADVANTAGE - More efficient processing of material which contains organic substances. 4 cl, 1 dwg
NOVELTY - Producing coal from biomass by thermal carbonization, comprises crushing and charging the biomass into a reaction vessel (1) and heating together with a medium, which is situated in the reaction vessel, where during the reaction phase, the pressure in the reaction vessel is increased, the temperature is kept at least approximately constant and during the subsequent reaction phase, the pressure and temperature in the reaction vessel are lowered and the biomass converted into coal is withdrawn from the reaction vessel.    USE - The process is useful for producing coal from biomass.    ADVANTAGE - The process: simplifies the prevention or control of unstable operating conditions; reduces the time required for filling and emptying of the reactor; and provides coal with high yield and at low cost.    DETAILED DESCRIPTION - Producing coal from biomass by thermal carbonization, comprises crushing and charging the biomass into a reaction vessel (1) and heating together with a medium, which is situated in the reaction vessel, where during the reaction phase, the pressure in the reaction vessel is increased, the temperature is kept at least approximately constant and during the subsequent reaction phase, the pressure and temperature in the reaction vessel are lowered and the biomass converted into coal is withdrawn from the reaction vessel; and the reaction vessel is only partially filled with biomass, pressure-tightly closed and the reaction vessel is at least partially filled with steam and/or hot gas used as medium, before and/or during the reaction phase.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of a device for extraction and separation of hydrogen emerging from the reaction vessel.    Reaction vessel (1)    Settling tank. (19)
NOVELTY - The device has a rotatable turning plate (2) i.e. fence-shaped plate, mounted in a lower part of a furnace gasifying layer (5). A sealed rotatable turning plate (4) is installed at an ash outlet (6) of a furnace. A space is formed between the rotatable turning plate and the sealed rotatable turning plate for holding ash. The rotatable turning plate and the sealed rotatable turning plate are provided with a manual rotary shaft (3) or a dynamoelectric rotary shaft for driving the plates to turn.    USE - Ash clearing device for a biomass gasifying furnace.    ADVANTAGE - The device continuously ensures ash clearing to be carried out without influencing the work of the gasifying furnace. The device is simple to operate and environment friendly, and clears the ash at high working efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of an ash clearing device.    Rotatable turning plate (2)    Manual rotary shaft (3)    Sealed rotatable turning plate (4)    Furnace gasifying layer (5)    Ash outlet (6)
NOVELTY - The device has a gasification agent gas outlet pipe (2) provided with multiple gas inlet holes on a part in a tee joint (16). A lower end of the gasification agent gas outlet pipe is connected with a gasification agent injection pipe (4) with multiple gas injection holes. A transverse port of the gas inlet tee joint is connected with a gasification agent gas inlet pipe (15), and a joint place of the gasification agent gas inlet pipe, the gasification agent gas outlet pipe and the gas inlet tee joint are sealed by high-temperature oil.    USE - Gasification injection device for a biomass gasification furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a gasification injection device.    Furnace body (1)    Gasification agent gas outlet pipe (2)    Gasification agent injection pipe (4)    Gasification agent gas inlet pipe (15)    Tee joint (16)
NOVELTY - The system has multiple gas detectors (3) detecting different greenhouse gases in atmosphere and converting a collected greenhouse gases content signal into a data signal via an analog-to-digital (A/D) conversion chip (5). The detectors add data signal code of the detected greenhouse gases to a gas detecting device (1). A computer device (9) comprises a computer (7) and a general packet radio service (GPRS) module (6), which are connected via RS232 serial port. Greenhouse gases monitoring software is installed in the computer.    USE - Online monitoring system for greenhouse gases.    ADVANTAGE - The system enables monitoring multiple greenhouse gases including carbon dioxide, methane and nitrous oxide, so as to accurately analyze and evaluate greenhouse gases in relative large monitoring area in a real time manner with wide market prospect.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of an online monitoring system for greenhouse gases.    Gas detecting device (1)    Gas detectors (3)    Analog-to-digital conversion chip (5)    General packet radio service module (6)    Computer (7)    Computer device (9)
NOVELTY - The method involves mixing sea salt and lime stone with biomass to prepare a mixed material burnt in an oxygen deficit state and mixed gas is prepared. The stone and the salt are used as a catalyst to heat the gas to 850-950 degrees centigrade to prepare combustible gas. The salt has 70-80 weight percentages of sodium chloride, 5-10 weight percentages of magnesium chloride and magnesium carbonate, and 2-5 weight percentages of magnesium sulfate. The stone has 40-60 weight percentages of calcium oxide, 1-5 weight percentages of magnesium oxide, and 0.05-0.5 weight percentages of sodium oxide.    USE - Biomass gasifying method.    ADVANTAGE - The prepared combustible gas has low content of tar and quality of the combustible gas is improved by the method.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biomass gasifying furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial sectional view of a biomass gasifying furnace.
NOVELTY - The furnace has an air primary tangential inlet (3) and a fuel gas secondary tangential outlet (9) welded at an outermost layer of an inverted heat exchanger (2). A heat conducting bar (11) is installed in an internal furnace unit (1) that is arranged at center of the inverted heat exchanger. An upper end and a lower end of the internal furnace unit are provided with reducing holes. A groove is formed on an outer side of the internal furnace unit and embedded on a central baffle of the inverted heat exchanger.    USE - Corn/wheat straw high temperature gasification stove for use in a home.    ADVANTAGE - The inverted heat exchanger is utilized for cooling fuel gas and pre-heating air so as to realize high temperature gasification condition in the furnace. The furnace has self-pre-heating, self-heat-preserving and self-cooling functions, low energy consumption, high transferring rate, high thermal value of the produced fuel gas and low tar content.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a straw high temperature gasification furnace.    Internal furnace unit (1)    Inverted heat exchanger (2)    Air primary tangential inlet (3)    Fuel gas secondary tangential outlet (9)    Heat conducting bar (11)
NOVELTY - The reactor has a lockable fire-stirring door installed at a top part of a material storage device (1). The material storage device is connected with a settling chamber (6) by a fasting part and a sealing part in a sealing manner. An ash cleaning door is installed on a lower part of the settling chamber. A dumbbell reaction chamber (2) is arranged in the settling chamber. A grate (5) is fixed at a bottom part of the dumbbell reaction chamber. A gravity explosion door (3) is vertically installed on a gas outlet pipe (4). A refractory cement (8) is adhered to the dumbbell reaction chamber.    USE - Downdraft biomass gasification reactor.    ADVANTAGE - The reactor ensures that material can be fed by an automatic feeding device, so that continuous feeding of the material is achieved, and ensures that combustion condition and combustion layer are maintained in a stable manner. The reactor ensures that refractory cement is adhered to the dumbbell reaction chamber, so that reaction temperature is constant, and air energy on throat part of the dumbbell reaction chamber can effectively improve reaction temperature, ensure continuity of production and reduce tar content in gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a downdraft biomass gasification reactor.    Material storage device (1)    Dumbbell reaction chamber (2)    Gravity explosion door (3)    Gas outlet pipe (4)    Grate (5)    Settling chamber (6)    Refractory cement (8)
NOVELTY - The device has a gasification device (1) whose gas outlet is connected with an inlet of a one-stage filtering device (2). An inlet of a sprayer (4) is connected with an outlet of the one-stage filtering device. An outlet of the sprayer is connected with an inlet of a gas-water separating device (6). An outlet of a two-stage filtering device (7) is connected with a pressurization conveying device (9). A water jacket (15) covers a lower outer layer of the sprayer. A spraying water pump (5) and a circulation water pump are connected with the sprayer.    USE - Biomass gasification purifying device.    ADVANTAGE - The device reduces tar content in fuel gas and avoids corrosion and block of the pipeline due to low-temperature separation.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass gasification purifying device.    Gasification device (1)    One-stage filtering device (2)    Sprayer (4)    Spraying water pump (5)    Gas-water separating device (6)    Two-stage filtering device (7)    Pressurization conveying device (9)    Water jacket (15)
NOVELTY - An integrative catalyst is used in synthesizing biodiesel. The catalyst comprises cordierite as carrier and zirconia as active ingredient.    USE - An integrative catalyst for use in synthesizing biodiesel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for synthesis of biodiesel from fatty acid comprising filling prepared integrative catalyst into a reacting device, controlling ratio of fatty acid and methanol at 1:1-3 (g/ml), regulating the flux of peristaltic pump at 5 ml/minute and temperature of reactor at 60-90 degrees C, and reacting for 5 hours.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a synthesis of biodiesel from fatty acid.
NOVELTY - Zirconium-manganese alloy powder is melted into block alloy in a vacuum electric arc melting furnace using zirconium and manganese elements. The alloy is mechanically ground into powder. The atomic ratio of zirconium to manganese is 1:2 in zirconium-manganese alloy. The ground zirconium-manganese alloy powder (15-5 volume%) is mixed with pure magnesium powder (85-95 volume%), and magnesium-alloy of zirconium and manganese composite hydrogen storage alloy is manufactured by discharging plasma sintering method.    USE - Manufacture of magnesium-alloy of zirconium and manganese composite hydrogen storage alloy used for hydrogen fuel cell, hydrogen combustion engine, hydrogen fuel case and hydrogen memory.    ADVANTAGE - The magnesium-alloy of zirconium and manganese composite hydrogen storage alloy is easily manufactured with high productivity.
NOVELTY - The system (100) has downstream ends of oxidizing agent gas and hydrogen supply paths (124,121) connected to upper ends of oxidizing agent gas and hydrogen flow paths (52,51). The oxidizing agent gas and hydrogen supply devices (105,102) are connected to upper ends corresponding supply paths. The combustion gas generated by combustor (103) by burning of hydrogen, is passed into combustion gas discharge path (123). The total-heat exchange process between combustion gas and oxidizing agent gas is performed by total enthalpy heat exchanger (104).    USE - Polymer electrolyte fuel cell system for domestic application.    ADVANTAGE - The total-heat exchange process is performed between combustion gas generated by burning of hydrogen, and oxidizing agent gas by using total enthalpy heat exchanger. Hence the unnecessary mixing of carbon dioxide gas with oxidizing agent gas can be suppressed effectively. The oxidizing agent gas can be humidified reliably. The overall circuit structure of polymer electrolyte fuel cell system is simplified, so that the output efficiency of fuel cell system is increased effectively. The energy consumption efficiency of the fuel cell system is increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the polymer electrolyte fuel cell system. (Drawing includes non-English language text)    Hydrogen flow path (51)    Oxidizing agent gas flow path (52)    Polymer electrolyte fuel cell system (100)    Hydrogen supply device (102)    Combustor (103)    Total enthalpy heat exchanger (104)    Oxidizing agent gas supply device (105)    Hydrogen supply path (121)    Combustion gas discharge path (123)    Oxidizing agent gas supply path (124)
NOVELTY - The apparatus has several cassettes (2) provided with shelves (2a) for supporting cell configuration components such as membrane electrode assembly, which is provided in drying furnace (3) for heating components supported by each shelf. A conveying section (4) conveys the cassettes to furnace. A carrying-in section (5) sends the component from each shelf to carry-out position (Po) of furnace while a carrying-out section (6) sends each empty cassette to carry-in position (Pi) of furnace.    USE - Fuel cell manufacturing apparatus.    ADVANTAGE - The carrying-in section for sending the component from each shelf to carry-out position of furnace and carrying-out section for sending each empty cassette to carry-in position of furnace, are operated simultaneously and repeatedly so as to improve the productivity of the fuel cell by simple structure of the manufacturing apparatus.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell manufacturing method.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the fuel cell manufacturing apparatus.    Cassette (2)    Shelf (2a)    Drying furnace (3)    Conveying section (4)    Carrying-in section (5)    Carrying-out section (6)    Carrying-in position (Pi)    Carrying-out position (Po)
NOVELTY - A catalyst contains component (a) containing rhodium, and component (b) having steam reforming function of acetaldehyde.    USE - Catalyst is used for forming gas containing hydrogen used in hydrogen-oxygen fuel cell for motor vehicles, from ethanol.    ADVANTAGE - The catalyst has excellent catalytic activity, high hydrogen selectivity, high ethanol conversion rate, and is manufactured economically with reduced usage amount of rhodium.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of catalyst, which involves forming component (a) by impregnating alumina with rhodium-containing solution and sodium-containing solution simultaneously.
NOVELTY - A carbon-monoxide removal catalyst is obtained by contacting a nitrogen-containing ruthenium compound with fire-resistant oxide support and then ruthenium compound is supported on fire-resistant oxide support. The nitrogen content of the catalyst before baking is 0.5 wt.% or less.    USE - Carbon monoxide-removal catalyst is used for manufacture of hydrogen-containing gas for fuel cells (both claimed).    ADVANTAGE - The carbon monoxide-removal catalyst suppresses the generation of nitrogen compound and ammonia during manufacture of fuel cell, and is economical.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of hydrogen-containing gas which involves removing carbon monoxide in hydrogen-containing gas using the catalyst.
NOVELTY - A hydrogen generating apparatus (1) has a modification portion (2) having a modification catalyst, a heating portion (3) for heating modification portion, and a separation portion (4) having a hydrogen separation film capable of selectively permeating hydrogen from gas produced by modification portion. The portion (2) is separated into upstream portion capable of performing dehydrogenation and/or steam reforming reaction of fuel, and downstream portion capable of performing steam reforming reaction of methane and/or carbon monoxide produced by upstream portion.    USE - Apparatus is used for generating hydrogen used for fuel cell vehicle, from hydrocarbon fuel e.g. gasoline and ethanol.    ADVANTAGE - The hydrogen generating apparatus has reduced size, and economically enables to generate hydrogen with high concentration at high yield within short period of time.    DESCRIPTION OF DRAWING(S) - The drawings show the sectional view and perspective view of hydrogen generating apparatus. (Drawing includes non-English language text)    Hydrogen generating apparatus (1)    Modification portion (2)    Heating portion (3)    Separation portion (4)
NOVELTY - Special organic fertilizer for culturing organic herbaceous fruit, comprises (in parts): ginger plant (700-900), weathered coal (30-150), grain dreg (50-140) and microbial fermenting agent (5-20).    USE - The special organic fertilizer is useful for culturing the organic herbaceous fruit.    ADVANTAGE - The fertilizer has high nutrient content, increases fruit yield and provides new resource for the organic fertilizer production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the organic fertilizer, comprising: Preparing the materials by (i) drying the ginger until the moisture is below 60 wt% while using it and below 20 wt% while storing it for usage, cutting the ginger to 2-3 cm long, crushing the grain dreg and filtering by a sieve of 20 meshes; (ii) uniformly mixing the ginger with the weathered coal and the microbial fermenting agent; adjusting the moisture of the mixture to 55-60 wt% and fermenting for 21-27 days and again repeating the process and fermenting for 7-14 days for obtaining the fermented material, which is the special organic fertilizer for culturing organic herbaceous fruit.
NOVELTY - Ecological treatment of trash/landfill leachate in non-rainy comprises: (1) leading the landfill leachate from adjusting tank to aerating tank; (2) adding commercial microbial agents and extracellular enzyme in the aerating tank; (3) aerating in the aerating tank; (4) returning the aerated leachate to the trash and using the trash as carrier to consume the harmful components.    USE - The method is useful for the ecological treatment of trash/landfill leachate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an ecological treatment method of trash/landfill leachate when it is rainy comprising: (1) leading the landfill leachate from adjusting tank to aerating tank; (2) adding commercial microbial agent and extracellular enzyme in the aerating tank; (3) aerating in the aerating tank; (4) directly leading the aerated landfill leachate into sediment tank, adding in aluminum sulfate and polyacrylamide (PAM) and leading the liquid into the floatation planting tank after storage and sedimentation; (5) taking out the sewage after sedimentation and adding organic fertilizer to produce bio-fertilizer; 6) putting floating bodies in the floatation planting tank, boring holes on the floating bodies and inserting vegetations in the holes; (7) aerating in the floatation planting tank and letting the water in the floatation planting tank go into fish tank; and (8) feeding fishes in the fish tank till the water in the fish tank meets the emission standard.
NOVELTY - Special organic fertilizer for cultivating tuber organic agricultural products, comprises (in parts): vine crop seedling (500-700), ash (250-400), grain dreg (50-100) and a micro-organism fermenting microbial inoculum (10-20).    USE - The special organic fertilizer is useful for cultivating tuber organic agricultural product.    ADVANTAGE - The nutrients are added in a right proportion and the waste vine plant is used for manufacturing the organic fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the organic fertilizer, comprising: (i) preparing the raw materials by drying the vine crop seedling until the water content is less than 60% while using the vine crop seedling and less than 20% while storing the vine crop seedling; (ii) cutting the vine crop seedling to 1-2 cm before using, crushing the grain residues and sieving by a sieve of 20 meshes; (iii) weighing the vine crop seedling, ash, grain dreg and micro-organism fermenting microbial inoculum and uniformly mixing them, adjusting the water content of the mixed material to 55-60 wt.% and fermenting for 35-45 days for obtaining the fermentation material; (iv) soaking the grain residues in water for 8-12 hours and boiling for 15-30 minutes and adding the raw materials and grain residues along with the water into the fermentation material for obtaining the product.
NOVELTY - Aqueous composition comprises active ingredient (A) chosen from alpha -(4-chlorophenyl)- alpha -(1-cyclopropylethyl)-1H-1,2,4-triazole-1-ethanol (cyproconazole), 3-iodo-2-propynyl-n-butyl carbamate (IPBC), and 1-((6-chloro-3-pyridinyl)methyl)-4,5-dihydro-N-nitro-1H-imidazole 2-amine (imidacloprid), and active ingredient (B) chosen from inorganic salt or organic acid salt of dodecylamine, inorganic acid salt or organic acid salt of tetradecylamine, and organic acid salt of N,N-didecyl-N-methyl-poly(oxyethyl) ammonium propionate.    USE - The aqueous composition is useful for processing timber for preventing decay of timber and for repelling termites from timber (claimed).    ADVANTAGE - The composition has high permeability, reduced toxicity, and can be maintained stably for long period of time. The composition is transparent, economical and eco-friendly, and can be prepared easily. The composition can be easily diluted at the time of use. The composition does not leach out from the timber even when exposed to rain water. The method is reliable and prevents metal corrosion.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of processing the timber, which involves spraying the above aqueous composition or its water dilution to the timber with high pressure.
NOVELTY - The furnace has a material pressing device (6) arranged in a tar filter chamber (3) and connected with a drive device (11) out of a furnace body (1) by a transmission shaft (10). A dust removing device (7) is arranged in a gasification chamber (4) and connected with another drive device (13) out of the furnace body by another transmission shaft (12). The gasification chamber is connected with a wet type dust removing device (8) by the dust removing device. A lower part of the furnace body is provided with a blower (14).    USE - Middle suction type biomass gasification furnace.    ADVANTAGE - The furnace realizes that the biomass gasification furnace can produce the gas continuously and steadily without a time limit, thus achieving zero-tar emission and emission without dust and pollution of the biomass gasification furnace, and hence ensuring zero pollution to the environment with wide application range.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial sectional view of a middle suction type biomass gasification furnace.    Furnace body (1)    Tar filter chamber (3)    Gasification chamber (4)    Material pressing device (6)    Dust removing device (7)    Wet type dust removing device (8)    Transmission shaft (10, 12)    Drive devices (11, 13)    Blower (14)
NOVELTY - Ursolic acid is separated and purified from Ligustrum lucidum by mixing L. lucidum and water (15-20 wt.%); extracting for 8-10 hours; filtering; adding 40-80% ethanol to separated dregs; subjecting mixture to ultrasonic wave for 30 minutes; filtering; mixing filtrate; adding activated carbon to adsorb impurities; adding concentrated ammonia aqueous solution to regulate pH to 10-11; filtering; decompressing obtained filtrate; condensing; aging over night; filtering; adding hot absolute ethyl alcohol to the filtrate; filtering; recrystallizing; and drying obtained crystals.    USE - Method of separating and purifying ursolic acid from L. lucidum (claimed).    ADVANTAGE - The method is simple, produces less pollution, requires less equipment investment, and can be applied commercial production.
NOVELTY - Fabrication of an insecticide and rodenticide comprises mixing a gypsum compound containing a group formed by baked gypsum in an effective amount to destroy the insects (roaches and ants) and rodents (mice and rats), with attracting feed comprising processing corn.    USE - The process is useful for fabrication of the insecticide for destroying the roaches and rodenticide for destroying mouse and rodents (claimed). No biological data given.    ADVANTAGE - The process provides a mixture (baked gypsum compound and attracting feed) in the form of gel (insecticide) and paste (rodenticide), which do not dry up quickly, it remains fixed and soft in the warmth and in humid places, which provides efficiency for long term after its application, where the mixture is ecological, and the mode of preparation leaves neither residues (liquid, solid or gaseous) nor smell because the substances are made of natural, non-volatile components neither irritates the skin or nor eyes and has no bad effect on environment, and harmless to human being. In the process for the preparation of the mixture, water is not used.
NOVELTY - An ammonia electrolyzer comprises electrolysis cell(s) including anode (34) compartment(s) housing an anolyte; cathode (40) compartment(s) housing a catholyte; anodes connected in parallel and submerged within the anolyte, and comprising an anode catalyst; and cathodes connected in parallel and submerged within the catholyte, and comprising a cathode catalyst. The application of an electric potential between the anodes and the cathodes activates electrolysis.    USE - Electrolyzer for continuous and large scale generation of hydrogen via electrolysis of ammonia.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of replenishing the catalyst of a poisoned electrode anode of a multielectrode ammonia electrolyzer anode comprising individually monitoring the catalyst poisoning of each electrode anode; and reversing the polarity of an electric potential applied to the poisoned electrode anode and selectively isolating an electrode cathode corresponding to the poisoned electrode anode, where reversing the polarity reduces catalyst poisoning.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of an apparatus for the continuous generation of hydrogen via electrolysis of ammonia.    Catalyst replenisher (18)    Programmable control system (26)    Anode (34)    Cathode (40)    Power generating device (100)
NOVELTY - Treatment of a liquid comprising organic material comprises: anaerobic digestion of the liquid to produce a digestate (24); membrane separation of solids from the digestate; and recycling separated solids (28) to the digestion step.    USE - The process is useful for treating a liquid comprising organic material (claimed) to produce biogas.    ADVANTAGE - In the process: low solids feeds may be digested more efficiently at a higher, but not overly high, controlled solids concentration in the digester; bacteria and undigested biomass may be retained in the digester for a longer effective residence time, without increasing the hydraulic residence time of the digester tank; and the effluent is separated into at least two streams, which may reduce post-processing requirements before the effluent can be reused or safely disposed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an apparatus adapted to perform the process.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of flow sheet of a digestion process.    Thickened feed liquid (18)    Digester (20)    Digestate (24)    Separator (26)    Separated solids (28)    Separator effluent (30)
NOVELTY - A process (P1) to dehydrate a feed stream containing alcohol and small quantity of water involves: (a) using pressure swing adsorption to produce a first alcohol stream of substantially dehydrated alcohol and a second mixed stream of water and alcohol; (b) distilling the second mixed stream in a distillation column to produce a relatively purified water stream and a third alcohol stream; and (c) adding the third alcohol stream to the feed stream.    USE - For dehydrating feed steam containing alcohol and producing dry alcohol steam; and for producing biodiesel (claimed).    ADVANTAGE - The process produces highly purified, dehydrated alcohol streams; permits efficient recovery of excess alcohol from esterification reaction and the transesterification reaction in a dehydrated state for recycle and reuse in the biodiesel production process, particularly in the transesterification reaction.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a process (P2) to operate a biodiesel production facility, involving: (a1) reacting biodiesel feedstock in a reactor selected from a transesterification reactor and a esterification reactor to produce a product stream comprising fatty acid esters, water and alcohol; (b1) separating alcohol and water from the product stream to produce a first mixed stream containing water and alcohol; (c1) condensing the first mixed stream; (d1) feeding the first mixed stream into a pressure swing adsorption system to produce a first alcohol stream and a second mixed stream containing water and alcohol; (e1) distilling the second mixed stream in a distillation column to produce a relatively purified water stream and a third mixed stream containing alcohol and water; (f1) combining the third mixed stream with the first mixed stream; and (g1) feeding the first mixed stream and the third mixed stream into the pressure swing adsorption system.
NOVELTY - Continuous isolation of oils from microorganism slurry or algae slurry comprises liberation of oils by rupturing or permeabilization of cell walls of microorganisms or cell walls of algae; separating the slurry of liberated oils and ruptured or permeabilized cells in a three phase centrifugal separator having a stack of separating discs (28) and operating under force of greater than or equal to 4000, preferably greater than or equal to 5000 G; and obtaining three phases: one oil phase, one liquid phase, and one bioorganic phase. The outgoing bioorganic phase has dryness of greater than or equal to 30, preferably greater than or equal to 50%. The bioorganic phase contains cell parts.    USE - Continuous isolation of oils from microorganism slurry or algae slurry, useful for production of biodiesel or bio-fuels (claimed).    DESCRIPTION OF DRAWING(S) - The drawing is a cross-sectional view of centrifugal separator.    Rotor body (1)    Screw conveyor (2)    Outlet chamber (20)    Paring discs (21)    Separating discs (28)
NOVELTY - A solution containing 2-6C carboxylic acid or 2-6C carboxylate derived from biomass is contacted with solution containing solid catalyst, and decarboxylated to obtain 1-5C hydrocarbon.    USE - Decarboxylation of carboxylic acid or carboxylate used for forming hydrocarbon used as liquid petroleum gas.    ADVANTAGE - The decarboxylation of carboxylic acid or carboxylate is effectively enabled.
NOVELTY - A pair of current collectors are arranged on opposite sides of the electrolyte membrane (38). Flow field (54) supplies water defined between the current collectors and separators, and flow field (58) produces hydrogen under a pressure higher than normal pressure through electrolysis of the water is defined between the other current collector and other separator. The other separator includes a seal groove, which extends around the flow field (58), seal member arranged in the seal groove, and an opening provides fluid communication between the flow field (58) and groove.    USE - Electrochemical apparatus e.g. water electrolysis apparatus serves as high-pressure hydrogen manufacturing apparatus used to generate hydrogen gas for use as fuel gas for solid polymer electrolyte fuel cells.    ADVANTAGE - The electrochemical apparatus is capable of appropriately depressurizing a seal groove held in fluid communication with a flow field when the flow field is depressurized from a high-pressure level. Thus the electrolyte membrane is prevented from damage. No pressure difference is developed between the flow field and the seal groove when the flow field is released from the pressure. Thus the high-pressure fluid is prevented from moving abruptly from the seal groove into the flow field under unwanted increased pressure differences.    DESCRIPTION OF DRAWING(S) - The drawing shows a side elevation and cross section view of electrochemical apparatus.    Electrochemical apparatus (10)    Unit cell (12)    Stack assembly (14)    Electrolyte membrane (38)    Flow fields (54,58)
NOVELTY - The aluminum-silicon pillars (150-152) crossing the silicon wafer, are formed according to temperature gradient zone melting process. The cavities are formed on the wafer surface, outside the areas corresponding to the pillars. The doped silicon portions are formed on wafer surface by diffusing the dopant material such as boron into surface. The wafer is subjected to electrolysis for converting the pillars and the doped silicon portions into porous silicon.    USE - Formation method of support wafer from silicon wafer during fuel cell manufacture process (claimed).    ADVANTAGE - The formation of aluminum-silicon pillars crossing the silicon wafer and conversion of the pillars into porous silicon pillars enables to increase the surface area of exchange between the active component from the apertures through the silicon wafer and active layer of the cell and the etching is performed smoothly with low electrolysis current and hydrofluoric acid concentration.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for fuel cell fabrication method.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the fuel cell formation process on support wafer.    Aluminum-silicon pillars (150-152)    Conductor layer (160,180)    Catalyst layer (170,172)    Electrolyte layer (171)    Conductive layer (180)
NOVELTY - Making a fuel from biomass material, comprises: providing a biomass material containing a high molecular weight carbohydrate; hydrolyzing the biomass material to provide a hydrolyzed biomass material; combining the hydrolyzed biomass material with Clostridium phytofermentans cells in a medium, where the concentration of carbohydrates in the medium is greater than 20 mM; and fermenting the hydrolyzed biomass material under conditions and for a time sufficient to produce the fuel.    USE - The method is useful: for making a fuel from biomass material, where the fuel is an alcohol including ethanol (preferred), n-propanol, isopropanol, n-butanol (all claimed) and/or hydrogen; and to produce organic acids (e.g. formic acid, lactic acid or acetic acid), their conjugate bases (e.g. formate, lactate or acetate) or their salts.    ADVANTAGE - The method utilizes Clostridium phytofermentans, which: ferments a broad spectrum of materials (including waste products e.g. lactose, waste paper, leaves, grass clippings and/or dust) without pretreatment and thus provides the fuel with high yield; remains active even at high concentrations of carbohydrates and under wide range of temperatures and pH ranges, and thus avoids pH and temperature adjustments during fermentation; and ferments high concentrations of 5C sugars, polymers having 5C sugar repeat units or even higher cellulose concentrations to combustible fuels.
NOVELTY - Purifying a biodiesel fuel comprises: providing a mixture of triglyceride, methanol and homogeneous catalyst; reacting the mixture to form a product comprising a glycerol fraction and a crude biodiesel fuel fraction; separating the glycerol and crude biodiesel fuel fractions; subjecting the biodiesel fuel fraction to an electric field to form a precipitate in the crude biodiesel fuel fraction; and removing the precipitate from the remaining biodiesel fuel fraction. The remaining biodiesel fuel fraction after removal of the precipitate is more purified than the crude fraction.    USE - The method is useful for purifying a biodiesel fuel claimed.    ADVANTAGE - The method utilizes: the electric field assisted washing of the biodiesel fuel, which removes the soap and cleans the biodiesel faster, thus providing the biodiesel fuel with high purity; and homogeneous catalysts, which are economical, easy to access and have high conversion rates.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method of purifying a crude biodiesel fuel, comprising providing a crude biodiesel fuel formed by a process comprising homogeneous catalysis, placing the crude biodiesel fuel in an electric field to form a precipitate, and removing the precipitate from the crude biodiesel fuel.
NOVELTY - The biomass-fed fixed bed gasifier has an upper portion (1) and a lower portion. The interior of the upper portion has a top-down combustion chamber having tapered sections. The combustion chamber has radial feeding conduits used for feeding gasifying agents in the chamber, and a mixer formed by a worm with hollow vertical shaft. The mixer is electrically rotated to mix slowly the biomass in ascending vertical direction to avoid accumulation of gas.    USE - Biomass-fed fixed bed gasifier used for production of gas fed into internal combustion engine.    ADVANTAGE - Guarantees highest possible yield of gasification process by using an improved combustion chamber for mixing biomass.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an electrical energy production system.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view illustrating the upper portion of the gasifier with combustion chamber.    Upper portion (1)