NOVELTY - A coal gangue composite fuel comprises (pts. wt.) coal powder (90-110), coal gangue (65-85), straw (15-35), sodium nitrate (1-2), lime (3-5), sodium (0.2-0.5), lacquer putty powder (0.4-0.6), sodium hydroxide (0.4-0.6), smoke suppressor (1-1.5), starch (0.3-0.7), magnesium oxide (2-5), and carbon powder (8-10).    USE - A coal gangue composite fuel.    ADVANTAGE - The fuel is energy saving and capable of combustion duration of 1.5-2 hours without peculiar smell, produces white combustion smoke, is cheap and environment-friendly, has combustion heat value that can reach more than 4000 kcal thus making the fuel applicable to industrial and civil application, and has high efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the fuel comprising mixing the raw materials, setting aside for 5-8 days, and recycling.
NOVELTY - A coal slime composite fuel comprises (pts. wt.) coal powder (70-90), coal (70-90), straw (35-45), smoke suppressor (1-2), wollastonite (3-4), sodium hydroxide (0.5-0.7), sodium nitrate (1-1.4), starch (0.3-0.6), magnesium oxide (4-5 kg), and calcium carbonate (1-4).    USE - A coal slime composite fuel.    ADVANTAGE - The fuel is energy saving and capable of combustion duration of 1.5-2 hours without peculiar smell, produces white combustion smoke, is cheap and environment-friendly, has combustion heat value that can reach more than 4000 kcal thus making the fuel applicable to industrial and civil application, and has high efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the fuel comprising mixing the raw materials, setting aside for 5-8 days, and recycling.
NOVELTY - A biomass coal water slurry is manufactured by providing a biomass solution comprising a biomass material, an alkalinizing agent, and a solvent; adding hydrogen peroxide to the biomass solution; heating up the biomass solution for reacting; and adding coal to the biomass solution reacted and mixing to obtain biomass coal water slurry.    USE - Method for manufacturing a biomass coal water slurry (claimed).
NOVELTY - Integrated processing of kitchen green waste comprises: (i) collecting the kitchen waste, sorting and performing solid-liquid separation; (ii) performing anaerobic fermentation of solid waste to produce marsh gas; (iii) separating the waste liquid into oil-aqueous phase; (iv) producing microbial oil by microbial fermentation of the aqueous phase; (v) performing methyl esterification of oil phase and microbial oil to produce bio-diesel; and (vi) producing an organic fertilizer using the waste residue obtained in the step (iv).    USE - The method is useful for integrated processing of kitchen green waste.    ADVANTAGE - The method is ecofriendly, has high practical value, prevents the problem of resource utilization of the kitchen waste, and infectious diseases caused by the kitchen waste, and produces product, which does not cause secondary pollution.
NOVELTY - Alcohol ester fuel, comprises (pts.wt.): 70-95% of modified methanol, 3.5-25% of biological diesel oil, 1-10% of cosolvent and 0.5-5% of nanometer composite emulsion.    USE - The alcohol ester fuel is useful for industrial and commercial applications.    ADVANTAGE - The method of the invention has simple process, short flow, little investment, no special device at normal temperature and under normal pressure; it can continuously and intermittently production, prepared alcohol ester fuel mainly making commercial and civil clean and environment-friendly, high combustion efficiency, little environmental pollution and is convenient to use, good in stability, capable of partially replacing mineral diesel and other civil fuel, and can be used as commodity oil of popularization and application.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a preparation method of the alcohol ester fuel, comprising: weighing nano composite emulsion into a container, weighing metering and fully stirring in a container the biodiesel containing nanometer composite emulsion, adding modified methanol and latent solvent and stirring at 20-30 degrees C, and adding with the mixed material until the solution is clear and transparent, then standing for 24 hours to obtain the product.
NOVELTY - Modified methanol gasoline comprises (wt.%) gasoline (40-80), methanol (40-70), acetone (1-6), and isopropyl ether (0.1-3).    USE - The modified methanol gasoline is useful for engines.    ADVANTAGE - The invention reduces the explosion risk of fire source and heat source, without any harm to human. In addition, the methanol is provided with the following advantages: best cooling effect, can reduce the temperature of the engine does not overheat, explosion-proof capability is high, and allows lower combustion without knocking.
NOVELTY - Device for converting bio-energy into natural gas, comprises a feeding part, an air stripping tank, a filtering system, and an air outlet part, where the feeding part is connected with the air stripping tank which is connected with the filtering system, and the filtering system is connected with the air outlet part.    USE - The device is useful for converting bio-energy into natural gas (claimed).    ADVANTAGE - The invention has high gas purity without impurities or odorous smell, protects and purifies the environment via the bio-energy and saves energy consumption.
NOVELTY - A marine microalgae, i.e. Isochrysis sphaerica CCMM 5001 (CCTCC M2010138), is new.    USE - The I. sphaerica is used a raw material for biodiesel production (claimed).    ADVANTAGE - The culture of the marine microalgae uses carbon dioxide in the industrial waste gas, which relieve the discharge of greenhouse gases, and can absorb the oxynitride in the industrial waste gas so as to reduce the environmental pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for culturing the marine microalgae.
NOVELTY - The dry fermentation method, comprises mixing multiple raw materials (manure, straw, and organic garbage) uniformly, delivering to the fermentation tank, charging and discharging one time a day, discharging recycled blender (25-35%), and uniformly mixing the raw material. The percolate in the fermentation tank is sprayed to the retort after being heated by the heat exchanger through the spraying pump.    USE - The dry fermentation method is useful for preparing biogas.    ADVANTAGE - The dry fermentation method is capable of preparing biogas with energy consumption in a cost effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for continuous dry fermentation for preparing biogas.
NOVELTY - A nuciferine is extracted from lotus leaf by crushing lotus leaf and adding 8-15 times of acidic solution for being heated and extracted for 2-3 times to obtain extract; adding the extract to macroporous resin column and cation resin column, washing the cation resin to be neutral, and using 4-7 times of sodium chloride solution for eluting effective component to obtain eluent; adding the eluent with nanofiltration membrane for being condensed to obtain concentrated solution; and adjusting pH at 8-10, crystallizing the precipitate with ethanol for 2-3 times, and drying.    USE - Method for extracting nuciferine from lotus leaf (claimed).    ADVANTAGE - The method has simple operation, low energy consumption, less pollution and high product content. There is no inorganic solvent residue; and it is suitable for industrial popularization.
NOVELTY - A fruit and vegetable pesticide composition comprises plant pesticide and additive. The plant pesticide comprises (kg) Coptis chinensis (28-35), black pepper (20-25), trifoliate orange (15-20), radix stemonae (18-28), toosendan fruit (15-20), camphor (4-10), and pepper (5-10). The additive comprises (kg) emulsifier (7-11.5), turpentine (5-8), penetrant (2-5), preservative (1-1.5), and 85-95% ethanol (12-20). Weight ratio of the plant pesticide to the additive is 1.5-2:1.    USE - Fruit and vegetable pesticide.    ADVANTAGE - The pesticide is pollution-free and environmental-friendly, and has no residue and no secondary toxicity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the pesticide, comprising: (A) adding 5 times water into Coptis chinensis, black pepper, trifoliate orange, radix stemonae, toosendan fruit, camphor and pepper to soak the materials at normal temperature for 6-10 hours, heating with steam to 80-95 degrees C, boiling and extracting for two times; (B) combining and filtering the two medicine liquids, condensing the filtrate into 1/3 condensed medicine liquid at 90 degrees C; (C) taking condensed liquid (4 pts.wt.), 85% ethanol, mixing at weight ratio of 4:1 for 40 minutes, placing in a precipitate tank to precipitate for 30 hours, and filtering away the insoluble substance; and (D) sending the filtrate in a distillation tower, heating to 80-95 degrees C, recycling the ethanol to 1/3 the raw material volume, taking the mother liquor, putting in a reaction kettle, adding (kg) turpentine (6), 85% ethanol (20), Tween 60 (RTM: polyoxyethylene (20) sorbitan monostearate) (9) as emulsifier, sorbic acid (0.8) as preservative and dimethyl sulfoxide (3) as penetrant, mixing and emulsifying for 2 hours to obtain the pesticide.
NOVELTY - An ozagrel methyl ester is prepared by reacting methyl p-methoxy cinnamate with N-bromosuccinimide (NBS) to obtain methyl 3-(4-bromomethyl) cinnamate, and reacting methyl 3-(4-bromomethyl) cinnamate with imidazole to obtain the ozagrel methyl ester.    USE - Method for preparation of ozagrel methyl ester (claimed).    ADVANTAGE - The method is high in yield, less in environmental pollution, and more suitable for industrialized production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing ozagrel ethyl ester, comprising reacting ethyl 4-methylcinnamate with NBS to obtain ethyl 4-bromomethylcinnamate, and reacting ethyl 4-bromomethylcinnamate with imidazole.
NOVELTY - Preparing N-(2-indane-yl) glycine alkyl ester comprises reacting glycine alkyl ester with 2-indenone in the presence of sodium triacetoxyborohydride as reducing agent to obtain N-(2-indane-yl) glycine alkyl ester crude product, where the molar ratio of 2-indenone to sodium triacetoxyborohydride is 1: (0.79-1.59).    USE - The method is useful for preparing N-(2-indane-yl) glycine alkyl ester.    ADVANTAGE - The method does not require use of sodium cyanoborohydride, produces no toxic materials, and produces product with high yield (up to 77.2%).
NOVELTY - A method of recycling and reusing 3-(S)-amino-4-(2,4,5-trifluorophenyl)-butyrate (I) involves reacting (I) with substituted benzaldehyde to obtain 3-substituted imine-4-(2,4,5)-butyrate (II); reducing (II) using precious-metal catalyst and then debenzylating to obtain racemic 3-amino-4-(2,4,5-trifluorophenyl)-butyrate.    USE - For recycling and reusing 3-(S)-amino-4-(2,4,5-trifluorophenyl)-butyrate to form racemic amino-4-(2,4,5-trifluorophenyl)-butyrate, which is used as vildagliptin intermediate (claimed).    ADVANTAGE - The method has mild reaction condition, simple and convenient operation, and high yield and has good industrial prospect.
NOVELTY - Extracting corytuberine involves taking qinling plough bucket root, crushing, and adding to carbon dioxide supercritical extraction, and extraction solvent ethyl acetate (2-4%) as entrainer to obtain extract, adding the extract to D102 macro-porous absorbing resin column with 70% of ethanol, collecting volume of the column, decompressing and recycling ethanol and concentrating, drying, adding to the silica gel chromatography column, collecting the eluent, concentrating, adding acetone, separating and crystallizing, washing and drying to obtain corytuberine.    USE - For extracting corytuberine (claimed) useful for resisting bacteria, diminishing inflammation, and relieving pain.    ADVANTAGE - The method is consumes low energy and reduces environmental pollution.    DETAILED DESCRIPTION - Extracting corytuberine from Root of Chinling Mountain Columbine involves taking qinling plough bucket root, crushing, and adding to carbon dioxide supercritical extraction, and taking extraction solvent ethyl acetate (2-4%) as entrainer, where extracting pressure is 20-40 MPa, the temperature is 50-60 degrees C, and the flow ratio of carbon dioxide to crude drug-min is 3 ml/g and the extracting time is 130-150 minutes to obtain extract, adding the extract to D102 macro-porous absorbing resin column with 70% of ethanol, collecting 3-8 times of volume of the column, decompressing and recycling ethanol and concentrating, drying, adding to the silica gel chromatography column, where volume ratio of methanol-chloroform mixed solvent elution is 2:1, collecting the eluent, combining the 3-6 of column volume of eluent, concentrating, adding acetone, separating and crystallizing, washing and drying to obtain corytuberine.
NOVELTY - The device has a heat storage and exchange tank that is connected with the branch tank. A heat evaporator is installed on the heat storage and exchange tank. An interface over-heat evaporator is connected with solar light condensing device. A biomass gasification furnace is provided with heat storage and exchange tank. A temperature mixer is provided on the exchanging pot. A biomass gasification furnace is provided with combustion chamber, fuel gas nozzle and air outlet which is connected with biomass storage bag.    USE - Solar and biomass energy heat power generating device.    ADVANTAGE - The performance of heat power generating device can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of solar and biomass energy heat power generating device.
NOVELTY - The method involves collecting and drying a peach branch, and cutting the peach branch. Block charcoal is fed to a gasification furnace by adding biomass particle fuel. A material in a granule fuel layer is burnt, and a blower transmission shaft is checked. Industrial alcohol is injected, and a control loop regulating valve is connected with a spraying water pump. A roots blower is started, and blower outlet flow rate is adjusted. A feed port is provided in the gasification furnace, and a hearth particle fuel layer is formed in the feed port.    USE - Method for producing combustible gas.    ADVANTAGE - The method enables improving heat energy utilization rate of biomass, and saving walnut resources.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic illustration of a method for producing combustible gas.
NOVELTY - The device has a feeding port (2) provided at an upper end, and a gasification furnace crude outlet (8) provided at a lower end. An ash outlet (7) is connected with a gasification furnace (1), and an air inlet (6) is connected with the gasification furnace crude outlet. An end of a circulating pipe of the gasification furnace is formed with a catalyst layer. The catalyst layer is made of dolomite, nickel or alkali metal compound. An internal circulation pipeline is provided in the gasification furnace.    USE - Biomass gasification device.    ADVANTAGE - The device has high conversion rate, low tar content, and is easy to use.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass gasification device.    Gasification furnace (1)    Feeding port (2)    Air inlet (6)    Ash outlet (7)    Gasification furnace crude outlet (8)
NOVELTY - The system has a centralized double-pump gasification furnace connected with a fully automatic blanking fuel gas generator (1), a gas cooling device (2), a water circulation filter (3), a biomass gas concentrated storage device (4) and a user terminal gasification furnace (5). A cone container is provided with a feeding port and equipped with a discharging opening. The container is provided with a charging chamber and a filter chamber. The charging chamber is provided with a blanking device. A feeding device comprises a fixed loading chamber of an annular track.    USE - Electrically rotating fully automatic centralized gas supply gasification furnace system for wheat straw root resource.    ADVANTAGE - The system is stable, and exhibits large storage capacity, simple structure and convenient usage, improves the gas production efficiency and reduces the use cost and the labor intensity.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of an electrically rotating fully automatic centralized gas supply gasification furnace system.    Fully automatic blanking fuel gas generator (1)    Gas cooling device (2)    Water circulation filter (3)    Biomass gas concentrated storage device (4)    User terminal gasification furnace (5)
NOVELTY - The system has a centralized double-pump gasification furnace connected with a core tail seat. A fuel gas generator (1) is connected with a gas cooling device (2), and a water circulation filter (3) is orderly connected with a biomass gas concentrated storage device (4) and a gasification furnace (5). An upper part of a cylindrical lower part is provided with a cone container. A bottom part of the cone container is provided with a feeding port, and cone container is formed with a discharging opening.    USE - Automatic centralized gas supply gasification furnace system for resource of wheat straw root.    ADVANTAGE - The system is stable, and has high storage capacity. The system reduces the usage cost and labor intensity of a worker, improves the production efficiency, and is simple in structure and convenient to use.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of an automatic centralized gas supply gasification furnace system.    Fuel gas generator (1)    Gas cooling device (2)    Water circulation filter (3)    Biomass gas concentrated storage device (4)    Gasification furnace (5)
NOVELTY - The system has a container provided with a feeding port, a discharging opening, a charging chamber and a filtering chamber. A heat insulating plate is provided with a residue leakage hole. A thermal baffle is provided with a gas generator. The filtering chamber is provided with a liquid outlet. A gas cooling device (2) is provided with a gas cooling box. Top of the gas cooling box is provided with a liquid hole. Bottom of the gas cooling box is provided with a drain hole. A gas filter box is equipped with filtering liquid. A filter tank is provided with a drain device.    USE - Centralized gas supply gasification furnace system for developing resource of a wheat straw.    ADVANTAGE - The system has storage capacity, and reduces use cost. The system is simple in structure and convenient to use.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a centralized gas supply gasification furnace system.    Centralized double-pump gasification furnace manual discharging combustion gas generator (1)    Gas cooling device (2)    Water circulating filter (3)    Biomass gas concentrated storage device (4)    User gasification furnace (5)
NOVELTY - The device has an air chamber (1-4) equipped with an air distribution plate that is connected with a gasifying reaction section (1-5) of a fluidized bed gasification reactor (1), where the gasifying reaction section is provided with a vapor inlet (1-3) and a feeder (1-1). The fluidized bed gasification reactor is connected with a cyclone smelting furnace (2). A heat pipe heat exchanger (5) is connected with a dust remover (6), a desulfurizing tower (7), a compression device (8) and an air storage tank (9).    USE - Biomass gasification and smelting device for preparing high calorific value gas.    ADVANTAGE - The device can reduce fuel gas in tar, carbon particles and ash content, and is high in thermal efficiency and safe and reliable.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing a high calorific value gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass gasification and smelting device.    Fluidized bed gasification reactor (1)    Feeder (1-1)    Vapour inlet (1-3)    Air chamber (1-4)    Gasifying reaction section (1-5)    Cyclone smelting furnace (2)    Heat pipe heat exchanger (5)    Dust remover (6)    Desulfurizing tower (7)    Compression device (8)    Air storage tank (9)
NOVELTY - The device has a hydrogen generating element (100) that is provided with silicide layer (103) and a base (101). A needle-like silicon structure or dome-like silicon structure (105) is provided over the base. The height of the silicon structure is in the range of 0.1-30 nm. The hydrogen generating element is made to contact with water to generate hydrogen. An exterior portion is provided with gas extraction portion, water introduction portion and the hydrogen generating element. The silicide layer is made of either Titanium isopropoxide (Ti) or nickel (Ni).    USE - Hydrogen generation device used in driving device and power generation device.    ADVANTAGE - The hydrogen generating element can supply hydrogen efficiently and stably. The hydrogen can be safely generated. The environmental load can be extremely reduced. The separator is provided to prevent contact between facing surfaces of the folded hydrogen generating element. The water introduction portion can be provided with a check valve for preventing backflow of hydrogen gas. The filter is provided to prevent the foreign substance from moving between the inside and outside of the cartridge. The sealing is performed to prevent the generated hydrogen gas from leaking through the gap, when the cartridge is loaded into the main portion.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) power generation device; and    (2) driving device.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the hydrogen generating element.    Hydrogen generating element (100)    Base (101)    Silicide layer (103)    Silicon structure (105)
NOVELTY - The method involves injecting gaseous fuel and liquid fuel into engine cylinder. Air-fuel mixture of engine cylinder is diluted with exhaust gas recirculation (EGR). Amount of EGR is adjusted responsive to fuel level of liquid fuel storage tank. Fraction of gaseous fuel is increased relative to fraction of liquid fuel injected into cylinder based on EGR amount of engine cylinder, where gaseous fuel comprises vaporized alcohol, hydrogen, carbon monoxide and methane. Spark advance is adjusted in response to increase in fraction of gaseous fuel.    USE - Method for operating internal combustion engine of hybrid vehicle.    ADVANTAGE - As the fraction of gaseous fuel is increased relative to fraction of liquid fuel injected into cylinder based on EGR amount of engine cylinder, the engine can be operated at higher charge dilution levels, so that the efficiency of engine can be improved, the engine emissions during transient operating conditions can be reduced and the combustion stability is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the engine.    Internal combustion engine (10)    Microprocessor unit (102)    ROM (106)    RAM (108)    Keep alive memory (110)
NOVELTY - Treating lignocellulosic biomass to be supplied to fermentation system for producing a fermentation product, involves: pre-treating the biomass into pre-treated biomass; separating pre-treated biomass into liquid component comprising sugars and solids component comprising cellulose and lignin; and treating the solids component of pre-treated biomass into treated component, where the biomass comprises lignocellulosic material, and treating the solids component comprises application of an enzyme formulation and makeup water to form slurry. The enzyme formulation comprises cellulase enzyme.    USE - For treating lignocellulosic biomass in a fermentation system for producing a fermentation product, particularly ethanol (claimed).    ADVANTAGE - In the method, treatment of pre-treated biomass before it is supplied to a fermentation system facilitates efficient production of ethanol. Moreover, the method provides cost effective means for increasing the efficiency of the conversion of cellulosic materials into fermentable sugars. The method has a glucose yield of at least 60%, preferably at least 90% of the theoretically available glucose.
NOVELTY - A storage section stores the natural by-product that is ejected from one side. The natural by-product is compressed for manufacturing as cylindrical-shaped firewood (101). The natural by-product ejected from the storage section is transferred by one transport section. Another transport section is operated for transferring the natural by-product to a firewood manufacturing machine (110). A cutter (160) is mounted on the transport section, for cutting the ends of firewood moved according to the operation of transport section.    USE - System for manufacturing firewood (claimed).    ADVANTAGE - The operational malfunction of the firewood manufacturing system can be avoided. The undesired breakage of the firewood manufacturing machine can be prevented. The productivity of the firewood manufacturing system is increased. The cutting process of firewood is performed easily while ensuring improved usage.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for firewood manufacturing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the firewood manufacturing system.    Firewood manufacturing system (100)    Firewood (101)    Firewood manufacturing machine (110)    Conveyor (151)    Cutter (160)
NOVELTY - Recombinant microorganism comprising a recombinant pathway including enzymes consisting of keto-thiolase, acetyl-coenzyme A (CoA) acetyltransferase, hydroxybutyryl-CoA dehydrogenase, crotonase, crotonyl-CoA reductase, butyryl-CoA dehydrogenase, and an alcohol dehydrogenase, is new, where NADH is tightly coupled to the butanol production pathway.    USE - The recombinant microorganism is useful for producing biofuels, such as ethanol and butanol.    ADVANTAGE - The recombinant microorganism provides producing biofuels with high yield in a simple and economical manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the production of recombinant microorganism.
NOVELTY - Process for purification of biodiesel, involves performing primary filtration step using self-cleaning filter, where the purification process is carried out for time period of at least 24 hours.    USE - The process is useful for purification of biodiesel which is used as fuel for trucks, buses, cars and heavy equipment as well as in marine and stationary applications.    ADVANTAGE - The process reduces the concentration of steryl glucosides to at least one third, preferably one fifth of the initial steryl glucosides concentration as the filtration steps are carried out in combination with additives and thus allows biodiesel to be used in all climatic conditions, improves filterability of biodiesel even at temperatures as low as -20 degrees C with filter plugging tendency (FPT) values just above one, prevents cloud like haze in the diesel, prevents fouling of fuel filter in engines, injector and injector nozzle as well as widens the temperature range in which biodiesel can be used as fuel and increases the volume of fuel delivered to the engine, thus improving the engine power.
NOVELTY - The system has a hydrogen-producing unit that generates hydrogen by oxidation reaction with water. An electric power generation/electrolysis unit consists of electrolysis function and electric power generation function for electrolyzing the water and generating electric power by using the hydrogen supplied from the hydrogen-producing unit as a fuel. A water replenishment unit which replenishes water is located in a space in which the gas containing hydrogen and water are circulated between the hydrogen-producing unit and electric power generation/electrolysis unit.    USE - Secondary battery type fuel cell system.    ADVANTAGE - Since the fuel cell system can be charged even if hydrogen is not supplied from the outside, stable battery performance can be maintained.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fuel cell system. (Drawing includes non-English language text)    Hydrogen-producing apparatus (1)    Fuel cell apparatus (2)    Container (3)    Solid electrolyte (4)    Oxidizing agent electrode (5)
NOVELTY - A culture soil has organic soil conditioner which contains foodstuff sludge, and charcoal compost as essential component.    USE - Culture soil for cultivation of plants.    ADVANTAGE - Organic components, such as nitrogen is contained abundantly, exhibits sufficient fertilizer action, and germination and growth of plant are promoted.
NOVELTY - The device has supports (15) on front top and back top of frame (33) near the sewage pond (17). The bearing bases (13) are arranged on supports. The belt roller (12) is arranged in bearing bases. The belt (10) is sleeved on belt rollers. The convex-concave bar slot is arranged on circumference of belt roller. Multiple fishing grid plates (11) are arranged on external surface of belt transversely. The sliding plate (16) is arranged between belt roller and sewage pond for enabling immersed microbe soft sponge foam type carrier (9) to slide into sewage pond.    USE - Mechanization immersion device for putting microbe into soft spongy foam type carrier.    ADVANTAGE - The immersion device is reasonable in design, convenient to use, and compact in structure. The consumption of labor intensity and time can be reduced, thus the operation efficiency can be greatly improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the mechanization immersion device for putting microbe into soft spongy foam type carrier.    Immersed microbe soft sponge foam type carrier (9)    Belt (10)    Fishing grid plate (11)    Belt roller (12)    Bearing base (13)    Support (15)    Sliding plate (16)    Sewage pond (17)    Frame (33)
NOVELTY - Producing dry powder using concentrated solution of molasses alcohol fermentation liquid comprises: (a) mixing a concentrated solution of molasses alcohol fermentation liquid of 50-60 Baume degrees concentration with rice bran to obtain a mixture, where the concentrated solution accounts for 83-92% of weight percentage of the mixture and the rice bran accounts for the balance amount; and (b) adding yeast strain into the raw material in a weight ratio of 3-5 kg:1000 kg, fermenting at normal temperature for 24-36 hours, drying and crushing.    USE - The method is useful for producing dry powder using concentrated solution of molasses alcohol fermentation liquid.    ADVANTAGE - The method utilizes a concentrated solution of molasses alcohol fermentation liquid of cane sugar industry in preparing the dry powder, which is a waste, and ensures zero discharge of pollutants and hence is ecofriendly.
NOVELTY - Blue-green algae mud stack is converted into organic fertilizer by drying and concentrating blue-green algae mud until water content is 90-95% to obtain concentrated mud, adding environmental induction material (0.1-1.5 wt.%) into the concentrated mud, uniformly stirring mixture, and warmly stacking mixture at 20-50 degrees C and at humidity of 65-100 g/m3 and normal pressure for 3-5 days in a dark condition so as to convert into organic fertilizer.    USE - Method of converting blue-green algae mud stack into organic fertilizer (claimed).    ADVANTAGE - The method has short pure compost fermenting time and less nutrient loss, does not accumulate bacteria, virus, microbial toxin, and heavy metal, does not cause problem of secondary pollution, reduces transportation and storage cost, saves floor space and device investment, and can solve problem on organic pollutants.
NOVELTY - Static aerobic fermentation reactor, comprises fermentation chamber, drainage, ventilation pipe and air blower, where the fermentation chamber is a three box brick concrete structure surrounded by main wall and uniformly spaced side walls, three box brick chamber sidewalls are arranged in parallel, and reactor is connected and provided with drainage ventilation pipe.    USE - The static aerobic fermentation reactor is useful for household garbage (claimed).    ADVANTAGE - The static aerobic fermentation reactor is simple structured, convenient to use and cost-effective.
NOVELTY - Use of the grape seed in a high temperature composting process of pig manure-straw, is claimed. The grape seed is added as additive in the process, where the ratio of the pig manure to the straw is (10.5:1).    USE - The grape seed is useful for high temperature composting process of pig manure-straw.    ADVANTAGE - The grape seed provides rich nutrient elements to microbes and reduces the pH of the compost during the composting process; improves the ventilating condition of the compost to reduce loss of nitrogen element, and provides a theoretical basis and reference data for the control of nitrogen loss from animal manure in the composting process.
NOVELTY - The fertilizer comprises 30-40 parts by weight (pbw) of organic fertilizer, 30-40 pbw of urea, 10-20 pbw of leaf, 10-15 pbw of humic acid, 15-25 pbw of straw ash, 0.5-0.8 pbw of potassium chloride, 3-8 pbw of nanometer calcium carbonate powder, 0.3-0.5 pbw of trace element fertilizer, 0.3-1.5 pbw of datura flower plant powder, and 2-5 pbw of bio-potassium fertilizer. The organic fertilizer comprises dairy manure, pig manure, sheep manure, chicken manure, duck manure, human manure and/or monosodium glutamate drug.    USE - The fertilizer is useful for crops. No biological data given.    ADVANTAGE - The fertilizer can be simply prepared with high nutritional value.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of preparing fertilizer.
NOVELTY - Microbial organic fertilizer for organic kiwi, comprises (parts by weight) soya-bean oil dregs (50-250), ginger plant (300-450), pumpkin stalk (50-200), white gourd stalk (100-250), greenhouse cucumber stalk (120-220) and microorganism bacterium agent (5-10).    USE - As a microbial organic fertilizer for organic kiwi (claimed).    ADVANTAGE - The fertilizer has high nutrient content, and improves fruit yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of special microbial organic fertilizer involving weighing half of pumpkin stalk, white gourd stalk, greenhouse cucumber stalk and microorganism bacterium agent, uniformly mixing; regulating water content of the mixture to 55-60 wt.%, timing when the temperature is raised to 55 degrees C, stacking and fermenting for 4-9 days; turning, and raising temperature to 50 degrees C and timing, stacking and fermenting for 4-7 days; taking half of the soya-bean oil dregs, pumpkin stalk, white gourd stalk, greenhouse cucumber stalk and microorganism bacterium agent to the fermented mixture, regulating water content to 55-60 wt.%, timing when the temperature is raised to 55 degrees C, stacking and fermenting for 5 to 7 days; turning, timing as soon as the temperature is raised to 50 degrees C, stacking and fermenting for 3-5 days; adding the residual soya-bean oil dregs, ginger plant to the fermented mixture, regulating water content of the mixture to 50-55 wt.%, timing as soon as the temperature of material is raised to 50 degrees C, stacking and fermenting for 10-12 days to obtain fermented material; airing or drying the fermented material till water content is less than 20 wt.%, obtaining powdery product.
NOVELTY - The method comprises taking and crushing dry basis of pacan outer peel (70 wt.%), crop straws (12 wt.%), lake mud (18 wt.%) having a grain size of 0.1-1.5 cm and water (62 wt.%) and then mixing, adding 0.1-0.3% of fermentation inoculants to the mixed materials and then uniformly stirring, stacking the mixed materials inoculated with inoculants into fermentation slot with a height of 1.5-2 m and width of 2-3 m, and warming the stacked substance at 60-65 degrees C and then turning one time for each 2-3 days when the stacking temperature reduces to 40-45 degrees C after 10-12 days.    USE - The method is useful for treating pecan husk compost.    ADVANTAGE - The method is capable of simply treating the pecan husk compost in an environmentally friendly manner.    DETAILED DESCRIPTION - The method comprises taking and crushing dry basis of pacan outer peel (70 wt.%), crop straws (12 wt.%), lake mud (18 wt.%) having a grain size of 0.1-1.5 cm and water (62 wt.%) and then mixing, adding 0.1-0.3% of fermentation inoculants to the mixed materials and then uniformly stirring, stacking the mixed materials inoculated with inoculants into fermentation slot with a height of 1.5-2 m and width of 2-3 m, warming the stacked substance at 60-65 degrees C and then turning one time for each 2-3 days when the stacking temperature reduces to 40-45 degrees C after 10-12 days and then stopping turning, transferring the mixed materials out, stacking the transferred materials to a pyramid with a height of 1-2 m and a width of 2.5-3 m, inserting holes by wood rod on a top and side of the pyramid, where the density is 5-7 piece/m2, at a normal temperature for 20-30 days, and utilizing it after the mixed materials turns black and has no foreign taste. The lake mud is river mud. The fermentation inoculants contain green microbial inoculants, which are beneficial to the high temperature fermentation.
NOVELTY - Breeding seedling bedding for mechanized transplant, involves treating mushroom waste, and cake fertilizer or animal manure at high temperature for fermentation, and then dried, crushed, processed and then mixed with accessories to form finished product bedding, where weight ratio of mushroom waste and cake fertilizer or animal manure is 75-85:25-15.    USE - For breeding seedling bedding for mechanized transplant (claimed).    ADVANTAGE - The method provides good quality and survival seedling; shorten the fermentation time; utilizes waste material, thus reducing the environment pollution and production cost; and provides stable product quality, small grains, and high nutrient.
NOVELTY - The device has a container (1) provided with an air inlet port (101) and an air outlet port (102) and connected with a washing chamber (3) and a gas-liquid separation chamber (4). The air inlet and the outlet port are fixed on a top part of the washing chamber and the gas-liquid separation chamber by a vertical baffle plate (2). A bottom part of the container is filled with cleaning solvent (6) through an opening (5). An end of a baffle plate (401) is provided with an air circulating port. The air circulating port is fixed on two sides of the gas-liquid separating chamber.    USE - Purifying device for a biomass waste resource pyrolysis gasification system.    ADVANTAGE - The device can separate gas and liquid particle in an effective manner. The device is simple in structure. The device occupies less space. The device is provided with a shielding plate so as to prevent the device from being damaged.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a purifying device.    Container (1)    Vertical baffle plate (2)    Washing chamber (3)    Gas-liquid separation chamber (4)    Opening (5)    Cleaning solvent (6)    Air inlet port (101)    Air outlet port (102)    Baffle plate (401)
NOVELTY - The method comprises taking and crushing crop straw and then adding edible fungi culture and an auxiliary raw material, sterilizing the edible fungi cultivation base material for inoculating and culturing, generating marsh gas and biogas residue through fermenting the mushroom bran produced by the edible fungi fungal chaff and by-product can, establishing centralized gas supply marsh gas engineering, and putting the fungus chaff in marsh gas anaerobic tank at a medium temperature to generate marsh gas and then processing anaerobic fermentation to generate marsh gas.    USE - The method is useful for treating and recycling crop straw.    ADVANTAGE - The method is capable of economically treating and recycling the crop straw with high yield and efficiency and reduced energy consumption.    DETAILED DESCRIPTION - The method comprises taking and crushing crop straw and then adding edible fungi culture and an auxiliary raw material, sterilizing the edible fungi cultivation base material for inoculating and culturing, generating marsh gas and biogas residue through fermenting the mushroom bran produced by the edible fungi fungal chaff and by-product can, establishing centralized gas supply marsh gas engineering, putting the fungus chaff in marsh gas anaerobic tank at a medium temperature to generate marsh gas and then processing anaerobic fermentation to generate marsh gas for the engine, connecting the engine with a comprehensive power generation device to generate electrical energy and heat energy, and generating the biogas residue by fermenting into organic fertilizer.
NOVELTY - The biomass gasifier (10) has discharge pipe (50) in lower portion of chamber, for discharging the residue including ash, tar and moisture. A heat exchanger (30) separates the residue and lowers temperature of synthetic gas. A scrubber (40) removes the minute residue within the heat-exchanged synthetic gas. A water seal structure has water storing tub in lower portion of discharge pipe while preventing the submerge of lower portion of discharge pipe under water stored in the water storing tub and the flow of external air into the chamber through the discharge pipe.    USE - Biomass gasifier.    ADVANTAGE - The synthetic gas impurity can be ejected effectively at low cost. The fabrication cost of the biomass gasifier can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass gasifier.    Biomass gasifier (10)    Gasifier unit (20)    Heat exchanger (30)    Scrubber (40)    Discharge pipe (50)
NOVELTY - Absorbent solution (I), comprises: (a) at least one amine; (b) water; and (c) at least one combination of first degradation inhibitor compound with second degradation inhibitor compound, where the first degradation inhibitor compound is sulfites and bisulfites, and the second degradation inhibitor compound is triazole or tetrazole compound, in which at least one of substituent includes a sulfur atom.    USE - The absorbent solution is useful to absorb acidic compounds from a gaseous effluent comprising natural gas, flue gases, synthesis gas, refinery gases, gases obtained by Claus process tail, fermentation gases from biomass, gas cement and fume incinerator.    ADVANTAGE - The absorbent solution has improved thermal and chemical stability. The process for capturing carbon dioxide is eco-friendly. The degradation of absorbent solution is substantially reduced over the entire temperature range of the absorption process.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) process for absorbing acidic compounds contained in a gaseous effluent, comprising contacting the gaseous effluent with an absorbent solution; and    (2) process for capturing carbon dioxide contained in the flue gases, comprising contacting the flue gases with an absorbent solution.
NOVELTY - Absorbent solution (I), comprises: (a) at least one amine; (b) water; and (c) at least one combination of first degradation inhibitor compound with second degradation inhibitor compound, where the first degradation inhibitor compound is sulfites and bisulfites, and the second degradation inhibitor compound is azole compound (A).    USE - The absorbent solution is useful to absorb acidic compounds from a gaseous effluent comprising natural gas, flue gases, synthesis gas, refinery gases, gases obtained by Claus process tail, fermentation gases from biomass, gas cement and fume incinerator. The absorbent solution is useful for capturing carbon dioxide contained in the flue gases (all claimed).    ADVANTAGE - The absorbent solution has improved thermal and chemical stability. The absorbent solution increases the rate of absorption of acidic compounds in the aqueous solution. The absorption of acidic compounds is carried out at reduced cost.    DETAILED DESCRIPTION - Absorbent solution (I), comprises: (a) at least one amine; (b) water; and (c) at least one combination of first degradation inhibitor compound with second degradation inhibitor compound, where the first degradation inhibitor compound is sulfites and bisulfites, and the second degradation inhibitor compound is azole compound of formula (A).    X, Z = H, alkaline element or alkaline-earth element, a monovalent or multivalent metal, ammonium cation NH4+, phosphonium cation, or 1-12C hydrocarbon group;    R = -S-Z, H, -R1-R2 or -NR3R4;    R1 = 1-12C hydrocarbon group or O;    R2 = 1-12C hydrocarbon group; and    R3, R4 = H or 1-12C hydrocarbon group.    INDEPENDENT CLAIMS are included for:    (1) process for absorbing acidic compounds contained in a gaseous effluent, comprising contacting the gaseous effluent with an absorbent solution; and    (2) process for capturing carbon dioxide contained in the flue gases, comprising contacting the flue gases with an absorbent solution.
NOVELTY - A methane-tank consisting of hermetic housing with the branch pipes of supply of initial substrate and withdrawal of the processed substrates, branch pipe of withdrawals of biogas, comprises a drive connected through the shaft, where drive is made in the form of a blade pneumatic motor, housing of which is rigidly fixed in the upper part of the housing of the methane-tank, and input and output branch pipes of the blade pneumatic motor through reversibly gas distributor are connected to the branch pipe for supplying biogas and the pressuring chain of the compressor.    USE - As methane-tank (claimed).    DETAILED DESCRIPTION - A methane-tank consisting of hermetic housing with the branch pipes of supply of initial substrate and withdrawal of the processed substrates, branch pipe of withdrawals of biogas, comprises a central pipe, the upper and lower part of the pipe are open relative to the working space of the methane-tank, inside the bottom surface of central pipe is coaxially placed branch pipe for supplying biogas, connected through the compressor with branch pipe of withdrawals of the biogas, supplied with the vertically oriented devices for immobilizing-microflora, which are placed in an annular space, between the central pipe and the housing of the methane-tank, and are made in the form of vertical rods with a porous structure with the possibility of reversibly rotation of the totality and combined in the upper part via rigid frame suspension, connected with the drive through the shaft, where drive is made in the form of a blade pneumatic motor, housing of which is rigidly fixed in the upper part of the housing of the methane-tank, and input and output branch pipes of the blade pneumatic motor through reversibly gas distributor are connected to the branch pipe for supplying biogas and the pressuring chain of the compressor.
NOVELTY - A soil improvement biological preparation comprises (%) Trichoderma (20), Streptomyces microflavus (20), starch (30), turf (10), silicon fertilizer (8.15), humic acid (6), urea (5), biological bacteria (0.2) including 1/3 of Bacillus subtilis, 1/3 of Bacillus cereus and 1/3 of Bacillus licheniformis, vitamin C (0.1), sodium nitrophenolate (0.5), and diethyl aminoethyl hexanoate (DA-6) (0.05).    USE - Soil improvement biological preparation.    ADVANTAGE - The biological preparation can effectively prevent hardening of soil and continuous cropping which can affect healthy growth and harvest of crops.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of the soil improvement biological preparation, comprising uniformly mixing the materials, and packaging.
NOVELTY - A garbage biochemical decomposing bin comprises round bin, heater (6), biochemical liquid spraying pipe (2) and air exhaust pipe. A bottom of the round bin has the heater and a discharging control valve, its middle part has heater and lower temperature controller, its upper part has the biochemical liquid spraying pipe, and its neck part has the air exhaust pipe.    USE - A garbage biochemical decomposing bin.    ADVANTAGE - The bin has simple structure, provides short time for decomposing organic material, and provides for convenient feeding and discharging.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of the garbage biochemical decomposing bin.    Feeding pipe (1)    Liquid spraying pipe (2)    Air pipe (4)    Cabin body (5)    Heater (6)
NOVELTY - A strengthening reoxygenation circulating outlet water pipeline sewage treatment method comprises selecting pipe with length of 300-5000 m, adding filler so that the sewage flow rate is 30-100% of added water flow speed filler, where microorganism on the filler is 1000-5000 mg/L, and setting with a reflux pipeline, where the water volume flow rate in the pipeline is 10-100% of reflux sewage on the pipeline. The pipe device is set with air drawing device, and inspection well is sealed. The sewage flows out of the sewage pipeline. The hydraulic retention time is 3-5 hours.    USE - Method for treating and circulating outlet water sewage from confluence of city and town, a shunt, a drain pipe net of confluence.    ADVANTAGE - The method can make the chemical oxygen demand value of sewage in the sewage pipeline reduced by 30-70%.    DETAILED DESCRIPTION - A strengthening reoxygenation circulating outlet water pipeline sewage treatment method comprises selecting pipe with length of 300-5000 m, adding filler so that the sewage flow rate is 30-100% of added water flow speed filler, where microorganism on the filler is 1000-5000 mg/L, and setting with a reflux pipeline, where the water volume flow rate in the pipeline is 10-100% of reflux sewage on the pipeline. The pipe device is set with air drawing device, and inspection well is sealed. The height of the wind device is 5-10 m, low wind device is 1-2 m, the diameter of wind device is 20% of the pipe section which is 30% times of the pipe diameter, and the ventilating device in 100-500 m. The sewage flows out of the sewage pipeline. The hydraulic retention time is 3-5 hours.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of strengthening reoxygenation circulating outlet water pipeline sewage treatment device.
NOVELTY - The blade has a mixing driver (140) in which rotary shaft (142) is installed at the bottom side of grate (130). A restore unit (150) is provided to accommodate ash which is burnt with the grate through opening formed on lower portion. A transport unit (160) is installed at transfer pipe (162) connected in the lower portion of the restore unit with vent (159). A discharge blade (170) is adhered to the bottom surface while rotating the grate. The ash stored in the restore unit is smoothly ejected in a specific direction.    USE - Ash-discharge blade in wood chip gasifier.    ADVANTAGE - The ash can be effectively discharged by discharge blade, so that the gasifier damage due to overheat is prevented and the high temperature generated in the exhaust apparatus can be generated. The carbon is not reacted using the biomass, so that the synthetic gas can be manufactured and the ash component is ejected for regularly maintaining the floor height of the gasifier inside.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the wood chip gasifier including ash-discharge blade.    Grate (130)    Mixing driver (140)    Rotary shaft (142)    Restore unit (150)    Vent (159)    Transport unit (160)    Transfer pipe (162)    Discharge blade (170)
NOVELTY - A fermentation tank comprises tank body, top cover, separation plate, material discharge channel pipe, gas guide pipe and material feeding channel pipe. The tank body is a cylinder. A separation plate is arranged in the middle upper part in the tank body. The material discharge channel pipe is penetrated into the separation plate to directly reach the bottom of the tank body. The gas guide pipe is penetrated into the separation plate, and the material feeding channel tube is penetrated into the separation plate to directly reach the middle lower part of the tank.    USE - Fermentation tank for biogas waste fertilizer used in greenhouse shed.    ADVANTAGE - The fermentation tank has high pertinency, special structure, innovative design, short fermentation and fertilizer production cycle. Since, the wastes such as dry branches, fallen leaves or defective agricultural products produced in the production process of greenhouse shed are used as the organic materials, not only the requirement to high-quality organic fertilizer and carbon dioxide fertilizer in the growth of greenhouse shed can be met, but also the pollution problem of waste in the production can be solved.
NOVELTY - Recharging biogas slurry to farmland, involves contacting the biogas slurry with bladderwrack extract; and recharging to the farmland, where the contact between the biogas slurry and the bladderwrack extract makes the weight ratio of total carbon element to total nitrogen element in the contacted biogas slurry of 5-40:1.    USE - For recharging biogas slurry to farmland (claimed).    ADVANTAGE - The method effectively improves carbon nitrogen balance in the biogas slurry; improves fertilizing of the biogas on the soil; improves utilization rate of the fertilizer; has low cost and simple operation; avoids secondary pollution of methane tank side product; and ensures safe recharging of the biogas slurry.
NOVELTY - A pesticide composition comprises matrine and tea saponin of synergistic effective quantities.    USE - As pesticide composition which is useful for preventing and treating plant diseases and insect pests in agriculture and garden crops (claimed).    ADVANTAGE - The pesticide composition has obvious synergistic function to matrine; has low cost; is more environment-friendly; provides high efficiency, low toxicity, broad spectrum and is not easy to lead to resistance of the insecticidal bactericide pesticide.
NOVELTY - Forming (I) an addition product/oxidation product, comprises: (a) combining a first catalyst, a second catalyst, an oxidant, a reductant/a sterically bulky alcohol, and an olefin reactant in a reaction vessel to form a reaction mixture; and (b) allowing the reaction mixture to react for a period of time to form the addition product/oxidation product.    USE - The method is useful for forming an addition product/oxidation product, preferably organic alcohol (claimed) which are useful in bulk/fine chemical and pharmaceutical industries.    ADVANTAGE - The method utilizes: the peroxides in the second step (i.e. oxidation) which causes safety issues in large-scale production; and the catalysts for direct anti-Markovnikov hydration of alkenes in terms of synthetic efficiency, economy and waste reduction.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) forming (II) a product organic alcohol comprising: (a1) contacting an olefin reactant containing an asymmetrically substituted olefin with a first catalyst in the presence of a first alcohol to form a carbonyl-containing compound, and reduced first catalyst; (b1) contacting the reduced first catalyst with an oxidant to reform the first catalyst; (c1) contacting the carbonyl-containing compound with a second catalyst and a second alcohol to form the product organic alcohol and inactivated second catalyst; and (d1) contacting the inactivated second catalyst with a reducing agent to reform the second catalyst; and    (2) a composition comprising the first catalyst capable of catalyzing an oxidation reaction of an olefin-containing compound, the second catalyst capable of catalyzing a reduction reaction of a carbonyl-containing compound, the oxidant and the reductant.
NOVELTY - High frequency induction heating bio-oil production device comprises screw conveyor, reactor, high frequency induction heating system, cyclone separator, and condenser. The screw conveyor is connected with upper part of reactor and provided with a hopper far away from the rotary type reactor and an air inlet pipe. The outer wall of the reactor is fixedly connected with the high frequency induction heating system. The rotary type reactor is connected to the upper part of cyclone separator by a product conveying pipe.    USE - High frequency induction heating bio-oil production device.    ADVANTAGE - The device has improved heating efficiency; and prevents the secondary cracking of biomass to reduce the production cost of bio-oil.    DETAILED DESCRIPTION - High frequency induction heating bio-oil production device comprises screw conveyor, reactor, high frequency induction heating system, cyclone separator, and condenser. The screw conveyor is connected with upper part of reactor and provided with a hopper far away from the rotary type reactor and an air inlet pipe. The outer wall of the reactor is fixedly connected with the high frequency induction heating system. The rotary type reactor is connected to the upper part of cyclone separator by a product conveying pipe. It is provided with tar outlet at the bottom. The cyclone separator is connected to condenser through oil conveying tube at its upper part. The bottom of cyclone separator is provided with a carbon outlet. The condenser is provided with fuel gas outlet. It is provided with bio-oil outlet at its bottom.
NOVELTY - The immobilized phosphorus bacteria fertilizer comprises phosphorus bacteria fermentation liquor, crosslinking agent solution, and aqueous solution of poly(vinyl alcohol) and sodium alginate, where the phosphorus bacteria fermentation liquor and the aqueous solution of poly(vinyl alcohol) and sodium alginate are present in a volume ratio of 1:40-50, and the crosslinking agent solution contains calcium chloride and boric acid.    USE - Used as immobilized phosphorus bacteria fertilizer. Tests details are described but no results given.    ADVANTAGE - The immobilized phosphorus bacteria fertilizer can be prepared with less energy consumption, high fertilizer effect, and long shelf-life, in non-toxic, an economical and environmentally friendly manner.    DETAILED DESCRIPTION - The aqueous solution of poly(vinyl alcohol) and sodium alginate is obtained by mixing poly(vinyl alcohol) and sodium alginate in water till final concentration of poly(vinyl alcohol) in mixed solution is 60-90 g/l, and final concentration of sodium alginate is 10-30 g/l. The phosphorus bacteria fermentation liquor is a bacteria suspension of 2-5 x 108 obtained by fermenting the phosphorus bacteria to 2-5 x 1010, centrifugating or filtering, and preparing the precipitate bacteria with sterile water. The crosslinking agent solution is obtained by dissolving calcium chloride in boric acid solution until the final concentration of the calcium chloride in the solution is 1-3% and final concentration of boric acid is 2-4%. An INDEPENDENT CLAIM is included for a method of preparing immobilized phosphorus bacteria fertilizer.
NOVELTY - A highly efficient biomass formed fuel is prepared by taking agricultural waste raw material and naturally drying until water content is 5-20% wb; dried agricultural waste crushing until grain diameter is less than 50 mm; mixing crushed agricultural waste and papermaking waste liquor at wt. ratio of 1000:50-300, and fully and uniformly stirring; and putting mixed material into stamping forming machine at normal temperature into biomass forming fuel. The agricultural wastes is straw, saw dust, rice shell, bagasse and papermaking waste liquor.    USE - Method for preparing highly efficient biomass formed fuel (claimed).    ADVANTAGE - The method solves agricultural waste use. It does not only save raw material cost, but also reduces pollution discharge. The method also avoids cooking process of traditional technique, reduces heat energy loss of mechanical equipment and raw material caused by heating, which can greatly improve production efficiency. The prepared fuel has high heat value, no pollution, and low cost.
NOVELTY - Sieving of denitrified bacteria comprises enriching culture of denitrified flora on aerobic activated sludge using ammonia-containing sewage; cultivating heterotrophic flora at low dissolved oxygen condition; separating and purifying heterotrophic nitrobacteria from enriched heterotrophic flora; domesticating growth capability on purified heterotrophic nitrobacteria; and domesticating denitrifying capability on purified flora using ammonia-containing sewage.    USE - Sieving of denitrified bacteria used for sewage denitrifying treatment or used as biologic repairing agent under different environmental conditions.    ADVANTAGE - The method provides sieved denitrified bacteria that overcomes defect in existing biologic denitrifying technology and provides quick recovery of treatment capability of sewage treatment system. The sieved denitrified bacteria provide synchronous nitration and denitrification.
NOVELTY - An acid-alkali combination pretreatment method for efficiently saccharifying straw comprises reacting the raw material sizing agent composed of straw particles, inorganic metal salt, inorganic acid and peroxide at 100-200 degrees C for 1-50 minutes, then cooling and ending the reaction; and separating solid from liquid. The liquid product is hydrolysis saccharide liquid and the solid product is soaked with alkali solution in the concentration of 0.1-1.5 mass% for 1-30 hours. In the soaked solid product, solid is separated from liquid as the raw enzymolysis material.    USE - An acid-alkali combination pre-treatment method for efficiently saccharifying straw.    ADVANTAGE - The method has simple operating process, short treatment time, low energy consumption, high utilization rate of straw and good enzymolysis effect of cellulose.
NOVELTY - Solid, liquid organic waste treatment system comprises a dry-wet separation device and a waste liquid processing device (3). The dry-wet separation device is connected with the waste liquid processing device by a liquid transportation pipeline. The dry-wet separation device is provided for treatment of solid organic waste of a solid organic waste treatment device (1). The solid organic waste treatment device comprises a box body. The bottom of the box body is provided with a filter screen for filtering solids. The inner side of the box body is equipped with a stirrer.    USE - Used as a solid, liquid organic waste treatment system.    ADVANTAGE - The solid, liquid organic waste treatment system occupies a small space and is environment friendly.    DETAILED DESCRIPTION - Solid, liquid organic waste treatment system comprises a dry-wet separation device and a waste liquid processing device (3). The dry-wet separation device is connected with the waste liquid processing device by a liquid transportation pipeline. The dry-wet separation device is provided for treatment of solid organic waste of a solid organic waste treatment device (1). The solid organic waste treatment device comprises a box body. The bottom of the box body is provided with a filter screen for filtering solids. The inner side of the box body is equipped with a stirrer. A waste inlet is provided on the top of the box and the box with microorganism flora is placed in the box body. The solid organic waste treatment device is further provided with a drive of the stirrer of a power device.    DESCRIPTION OF DRAWING(S) - The figure 1 shows a schematic representation of the solid, liquid organic waste treatment system (Drawing includes non-English language text).    Solid organic waste treatment device (1)    Waste liquid processing device (3)
NOVELTY - An automobile bio-fuel diesel comprises (wt.%) modified vegetable oil acid (40-50), carbon (30-40), water (10-20), and additive (1.6-3.2) comprising (%) cetane number improver (0.5-1), flash point modifier (0.5-1), corrosion inhibitor (0.3-0.5), and pour point depressant (0.3-0.8).    USE - Automobile bio-fuel diesel.    ADVANTAGE - The biodiesel does not need expensive device investment, is simple, and can reach or better than GB252-2000 national standard.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a preparation of the automobile bio-fuel diesel comprising adding modified plant oil acid into tank, adding carbon, methanol and additive, stirring for 1 hour, standing for 24 hours, and obtaining bio-fuel applied to car.
NOVELTY - Preparation of fuel alcohol comprises mixing tapioca flour with water at mass ratio of tapioca flour to water of 1:(2.0-2.3); steaming and boiling for 55-65 minutes at 85-90 degrees C; adding amylase at 8-12 U/g of tapioca flour; performing enzymolysis for 55-65 minutes at 80-85 degrees C to obtain liquefied mash; adjusting pH of liquefied mash at 4.0-4.5; adding saccharifying enzyme at 140-160 U/g tapioca flour; performing enzymolysis for 5-15 minutes at 60-65 degrees C to obtain saccharified mash; and adding nitrogen source, sylvite, magnesium salt and saccharomycetes in saccharified mash.    USE - Preparation of fuel alcohol used as car fuel.    ADVANTAGE - The method has wide material sources, low manufacturing cost, and energy saving. The fuel alcohol relieves supply and demand contradiction of energy.    DETAILED DESCRIPTION - Preparation of fuel alcohol comprises mixing tapioca flour with water at mass ratio of tapioca flour to water of 1:(2.0-2.3); steaming and boiling for 55-65 minutes at 85-90 degrees C; adding amylase at 8-12 U/g of tapioca flour; performing enzymolysis for 55-65 minutes at 80-85 degrees C to obtain liquefied mash; adjusting pH of liquefied mash to 4.0-4.5; adding saccharifying enzyme at 140-160 U/g tapioca flour; performing enzymolysis for 5-15 minutes at 60-65 degrees C to obtain saccharified mash; and adding nitrogen source, sylvite, magnesium salt and saccharomycetes in saccharified mash, in which first time culturing is performed for 1.5-2.5 hours at 28-32and second time culturing is performed for 70-74 hours at 28-32 degrees C to obtain fuel alcohol. The amount of nitrogen (N) element in added nitrogen source is 0.6-1.0 g/l of saccharified mash, amount of potassium element in added sylvite is 0.4-0.6 g/l of saccharified mash, amount of magnesium element in added magnesium salt is 0.1-0.3 g/l of saccharified mash, and amount of added saccharomycetes is 1.2x 106-1.2x 108/ml saccharified mash.
NOVELTY - Preparing lutein comprises extracting the Calendula officinalis extract by using the backflow extract method, obtaining the extract fluid; recycling the extract fluid and obtaining the filter fluid via filtering; after absorbing the filter fluid via the macroporous absorption resin, eluting the filter fluid by using water and ethanol sequentially; collecting the eluent; depressurizing and concentrating the eluent; recycling ethanol, obtaining the lutein aqueous solution; and drying the lutein aqueous solution, and obtaining the product.    USE - Method for preparing lutein (claimed).    ADVANTAGE - The method uses raw material that can be easily obtained, has low cost, and is environment-friendly.
NOVELTY - An organic seaweed fertilizer comprises seaweed industrial waste residue which is fermented and decomposed by using microaerophilic fermentation process to obtain an organic seaweed fertilizer or compounding the organic seaweed fertilizer with the compound of seaweed residue in fresh kelp industry, with wheat bran, straw, traditional Chinese medicine residues, pomace, activated sludge and/or stillage.    USE - Organic seaweed fertilizer useful as base fertilizer or topdressing (claimed).    ADVANTAGE - The organic seaweed fertilizer improves the soil internal hole space, increases biological activity, increases buffer performance of soil to acid-base and soil fertility keeping and water storage ability, and has low production cost.
NOVELTY - Liquid phase preparation of chloromethane and ammonia comprises, in a high pressure reaction kettle, charging mixture of methanol, ammonium chloride and water; and adding catalyst, chloromethane and ammonia to the mixed solution. The catalyst is zinc chloride and nickel chloride at a mass ratio of 0.8:1.1:1. A mass ratio of methanol, ammonium chloride, water and catalyst is 1:1-1.3:1.2-1.8:3.5.    USE - Method for liquid phase preparation of chloromethane and ammonia (claimed).    ADVANTAGE - The method has short process flow, uses inexpensive raw material, has high selectivity and less by-product, has short reaction time and low reaction temperature, has low energy consumption, uses simple device, and provides no pollution to the environment.
NOVELTY - Taurine is prepared by mixing 2-aminoethanesulfinic acid and hydrogen peroxide, subjecting mixture to oxidation, cooling obtained solution, centrifuging, filtering, washing the filter cake, and cooling.    USE - Method of preparing a taurine.    ADVANTAGE - The method is short and environment-friendly, has good production environment and high yield, and produces product having good quality.
NOVELTY - A mangiferin is prepared by mixing mangiferin containing material and alcohol aqueous solution, extracting the mixture, filtering, concentrating the filtrate, adding organic solvent to concentrated filtrate, extracting, filtering, adding acetone aqueous solution to the filtrate for crystallization, and filtering.    USE - Method of preparing a mangiferin.    ADVANTAGE - The method has improved transfer rate, reduces usage of organic solvent and production cost, does not utilize benzene organic solvent thus making the method environment-friendly, prepares product having high purity, and does not use macroporous resin thus eliminating pre-treatment, adsorption and elution process.
NOVELTY - Recycling glyphosate comprises extracting glyphosate mother liquid 2-4 times by solvent A, dividing extraction solution into upper and lower layers, distilling solvent, recycling residual solvent, and distilling residual liquid as glyphosate aqueous solution.    USE - Method for recycling glyphosate (claimed).    ADVANTAGE - The method has low energy consumption, is simple, does not need complex production device, low waste discharge, no slag, no toxic waste gas discharge, no extra wastewater discharge, and is environment-friendly.
NOVELTY - A fospropofol disodium is synthesized by mixing bromochloromethane and propofol at a weight ratio of 5-7:1 (preferably 5:1) at 30-40 degrees C for 5 hours, filtering, reacting obtained filtrate with 60% phosphoric acid for 1 hour, adding triethylamine and tetrabutyl ammonium bromide having a mole ratio of 6-7:1, heating at 90-100 degrees C for 1 hour, regulating pH, adding sodium hydroxide, and mixing.    USE - Method of synthesizing fospropofol disodium.    ADVANTAGE - The method is short, low cost, environment-friendly, and prepares product having high purity.
NOVELTY - A phosphorylcholine derivative (I), is new.    USE - Compound (I) for use as surface treating agent for modifying material surface for improving anti-protein adsorption or anti-thrombocyte adhesion performance of the material surface or enhancing biocompatibility or blood compatibility of the material surface (claimed).    ADVANTAGE - The compound has good biocompatibility and bio-pollution resistance, and does not easily absorb or deposit organism component.    DETAILED DESCRIPTION - A phosphorylcholine derivative of formula (R1O)3SiR2+N(CH3)2CH2CH2OP(=O)(O-)OR3 (I), is new.    R1, R3=Me or Et;    R2=(CH2)n;and    n=1-20.    INDEPENDENT CLAIMS are included for:    (1) preparation of (I); and    (2) modification of material surface comprising soaking the material to be treated in sulfuric acid and hydrogen peroxide mixture, heating at 80-100 degrees C for 0.5-2 hours, soaking treated material in de-ionized water, subjecting to ultrasonic washing, washing with deionized water, drying using nitrogen gas, dissolving compound (I) in absolute ethyl alcohol, soaking treated material in the obtained solution for 1-10 hours, extracting, washing with absolute ethyl alcohol, subjecting to ultrasonic treatment, washing with absolute ethyl alcohol, drying at 50-80 degrees C, washing ethanol and deionized water, and drying at 50-80 degrees C.
NOVELTY - Composite biological soil conditioner comprises Trichoderma pseudokoningii fermentation liquor and Bacillus subtilis fermentation liquor.    USE - The composite biological soil conditioner is used for improving and protecting the farmland soil quality, i.e. improving the physicochemical property of the soil, adjusting the root zone soil beneficial microflora structure, promoting the growth of plant root system, enhancing the nutrient absorption of root system, improving soil stability and porosity, accelerating the decomposition of precipitate, and improving the soil structure. It is used for improving e.g. paddy soil, aquatic soil, pedocal soil, alfisol, and saline-alkali soil. The soil conditioner is used for increasing the production e.g. of muskmelon, wheat, and navel orange (all claimed); reducing the soil bulk density; improving soil air permeability; keeping the soil microbial activity; enhancing disease resistance of crops; improving the yield and quality of crops; and recovering the natural property of crops.    ADVANTAGE - The composite biological soil conditioner is environmentally friendly, highly efficient, and convenient to use.
NOVELTY - Around the world, treatment of municipal solid waste (MSW) by local bodies is a great challenge for them and the treatment includes collection, transportation and segregation of waste and lastly final disposal. Now existing unsatisfactory final disposal such as landfill, incineration, composting and anaerobic digestion through microbes without solid solution for segregation of waste which is most essential for treatment of waste and due to this, solid waste management is not functioning successfully. The solid waste management research gives a very simple solution for segregation of waste materials, on application of laws of flotation of elementary physics and the whole work of treatment involves 3 stages, all under wet process. The stage 1 works with the new technology to segregate MSW and the stage 2 and 3 are conventional method (being adopted in France) for grinding of MSW and final disposal of anaerobic digestion respectively to generate biogas, an energy source. Image 0/0
NOVELTY - Converting a biomass-derived mono-functional alcohol feedstock comprises (a) providing a biomass-derived feedstream comprising 5C or 6C hydrocarbon mono-functional alcohols, and (b) contacting the feedstream of step (a) with a catalyst in a reactor, where the contacting step results in an acidic condensation reaction that converts a least a portion of the feedstream to condensation products, where the condensation products comprise at least 10C and at least one ether functional group.    USE - The process is useful for converting a biomass-derived mono-functional alcohol feedstock (claimed).    ADVANTAGE - The process provides: the improved fuel with increased cetane number, and/or decreased emissions of environmental pollutants during combustion; and product utilized as fuel additives without the need for any further modification.
NOVELTY - The assembly (14) has a roller adapted for rotation on a shat. A fixture is coupled to an end of the shaft, where the fixture is used for height adjustment of the roller and the shaft in reference to a floor portion of a compost receptacle (12) for holding mushroom compost to create a nip between the roller and a floor portion of the compost receptacle. A mid-section is coupled to a sleeve removably mounted on a sidewall (20) of the compost receptacle. An end of another fixture is mounted on a support i.e. channel member, of the compost receptacle.    USE - Portable roller assembly for compacting mushroom compost e.g. Phase I, Phase II or Phase III mushroom compost. Can also be used for straw-bedded horse manure compost.    ADVANTAGE - The assembly allows properly compacted mushroom compost bed to use a mushroom compacting system to shorten mushroom grow time cycle by one or two days. The mushroom compacting system expedites mushroom bed preparation with Phase II or Phase III compost, and produces more consistent compost compaction that can lead to enhanced yield in a shorter grow time cycle.    DETAILED DESCRIPTION - The support is a joist or post. An INDEPENDENT CLAIM is also included for a method for compacting mushroom compost.    DESCRIPTION OF DRAWING(S) - The drawing shows a top perspective view of a mushroom compost bed with a mushroom composting system.    Mushroom compost bed (10)    Compost receptacle (12)    Portable roller assembly (14)    Sidewall (20)    Vertical post or member (24)
NOVELTY - Hydrogen and oxygen are electrolyzed from distilled water/sodium hydroxide solution, using oxyhydrogen gas producing cell. By isolating electrolyte in each cell from electrolyte in all the other cells, each cell is able to use all of electricity to produce oxyhydrogen gas without heating water. Preparation of oxyhydrogen gas is completely scalable based on the size and fuel demand of the engine and the travel range desired. Scalability is possible by increasing the size of the individual cells, increasing the number of cells, and/or increasing the electrical supply.    USE - Manufacture of oxyhydrogen gas used in motor vehicles (claimed).    ADVANTAGE - Motor vehicles using oxyhydrogen gas are maintained economically.    DETAILED DESCRIPTION - Hydrogen and oxygen are electrolyzed from distilled water/sodium hydroxide solution, using oxyhydrogen gas producing cell. By isolating the electrolyte in each cell from the electrolyte in all the other cells, each cell is able to use all of the electricity to produce oxyhydrogen gas without heating the water. Fossil fuels are limited in quantity and are generally assumed to be highly polluting as a fuel source for internal combustion engines. The need for fossil fuels to be used as fuel source for motor vehicles using gasoline powered internal combustion engine, is explained in the method. The preparation of oxyhydrogen gas is completely scalable based on the size and fuel demand of the engine and the travel range desired. Scalability is possible by increasing the size of the individual cells, increasing the number of cells, and/or increasing the electrical supply.
NOVELTY - Manufacture of stainless steel involves processing stainless steel containing chromium (10 %mass or more) electrolytically, and then treating in a solution containing fluorine.    USE - Manufacture of stainless steel used for separator used in fuel cell (all claimed). Uses include but are not limited to molten carbonate fuel cell, phosphoric acid fuel cell, solid oxide fuel cell, alkaline fuel cell and proton-exchange membrane fuel cell.    ADVANTAGE - The method efficiently and economically provides stainless steel having excellent electroconductivity and durability.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic structure of fuel cell. (Drawing includes non-English language text)    Membrane-electrode assembly (1)    Gas-diffusion layers (2,3)    Separators (4,5)    Air flow path (6)    Hydrogen flow path (7)
NOVELTY - Method of producing ethanol from lignocellulosic biomass, involves obtaining cellulose fraction from lignocellulosic biomass, mixing the cellulose fraction having solid content of 100 g dry mass/l or more with cellulose hydrolase formulation, treating the mixture enzymatically for 0.5-10 hours to obtain saccharification biomass, mixing yeast with the saccharification biomass, and cultivating the mixture.    USE - The method is useful for producing ethanol.    ADVANTAGE - The method produces ethanol cost-effectively and rapidly even by using small amount of enzyme formulation for saccharification, and improves yield of ethanol. The produced bioethanol prevents global warming and emits reduced amount of carbon dioxide.
NOVELTY - The coating apparatus has a die head (2) having an ejection opening (21) formed along the film width direction perpendicular to the conveyance direction of a film (F). An air supply unit is arranged at the downstream side of the die head in the conveyance direction of the film for spraying air on the liquid agent. The air supply unit is arranged in the vicinity of the ejection opening of die head for discharging air in the film width direction.    USE - Coating apparatus for applying liquid agent on film for forming catalyst layer in manufacture of polymer electrolyte fuel cell.    ADVANTAGE - A high quality catalyst layer is manufactured by crushing and removing the bubble on the film reliably by spraying air on the bubble generated on the film.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for coating method.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of the coating apparatus.(Drawing includes non-English language text)    Conveyance roller (1)    Die head (2)    Ejection opening (21)    Tubular block (31)    Film (F)    Air discharge direction (X)
NOVELTY - Fertilizer processing apparatus (10) comprises a processing tank (11), which is provided for biodegradation of organic substance. A water supply unit (12) is provided for adjusting moisture content of the organic substance. A bubble generation unit (13) is provided to obtain colloid dispersion. A heat retention unit (14) is provided for retaining heat, which is utilized for decomposing the organic substance inside of the processing tank by aerobic microbe. A stirring unit (15) is provided for stirring the organic substance. A ventilation unit (16) is provided inside of the processing tank.    USE - Fertilizer processing apparatus used for organic substance (claimed).    ADVANTAGE - The fertilizer processing apparatus suppress odor in the processing tank, where the processing tank has short processing time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for processing fertilizer, which involves:    (A) supplying water and organic substance in the processing tank with forming bubble to form colloidal organic substance, where moisture content is adjusted;    (B) stirring the organic substance in the processing tank;    (C) retaining heat of organic substance in the processing tank for decomposing aerobic microbe in the processing tank; and    (D) ventilating air inside the processing tank.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the fertilizer processing apparatus.    Fertilizer formation processing apparatus (10)    Processing tank (11)    Water supply unit (12)    Bubble generation unit (13)    Heat retention unit (14)    Stirring unit (15)    Ventilation unit (16)
NOVELTY - An organic substance fertilizer forming apparatus (10) has container main portion (11) having opening (11a) for supplying and removing to-be-biodegraded organic substance (W), lid (12) for opening and closing the opening of main portion, a sealing unit (14) for sealing clearance gap between lid and main portion, another opening (16) formed in container main portion and/or lid, and gas permeable film (17) for permitting passage of oxygen molecules, blocking passage of solid and liquid and suppressing passage of water vapor and provided such that secondary opening is closed.    USE - Apparatus is used for forming organic substance fertilizer and fermenting organic waste e.g. organic refuse.    ADVANTAGE - The apparatus promotes decomposition of organic substance and formation of fertilizer. The reduction of air permeability of container main portion is suppressed. The interior of container main portion is heat-retained, and microorganisms effectively enable decomposition of organic substance.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of organic substance fertilizer forming apparatus.    Fertilizer forming apparatus (10)    Container main portion (11)    Openings (11a)    Lid (12)    Sealing unit (14)    Secondary opening (16)    Permeable film (17)
NOVELTY - Carbon dioxide and hydrogen are reacted to obtain carbon monoxide, and the obtained carbon monoxide is reacted with hydrogen to obtain methane.    USE - Synthesis of methane from carbon dioxide and hydrogen, for town-gas supply use and supply of fuel for electric power generation, natural gas vehicles, etc.    ADVANTAGE - The method enables direct synthesis of highly purified methane with reduced residual carbon dioxide and carbon monoxide, and high yield. Even though catalysts suitable for each elementary process differ, and since selection of optimal catalyst is attained for every elementary process, the flexibility of catalyst selection increases yield and reduces cost. Since heat generated during reaction (exothermic) of carbon monoxide and hydrogen can be used for reaction (endothermic) of carbon dioxide and hydrogen, heat balance is attained. When using hydrogen obtained by photovoltaic power generation to the system in a desert, water separated during reaction of carbon dioxide and hydrogen can be used effectively for another use.    DESCRIPTION OF DRAWING(S) - The drawing shows a methane synthesis apparatus. (Drawing includes non-English language text)    Methane synthesis apparatus (1)    Compressor (2a)    Reactor (3)    Carbon dioxide regeneration unit (4)    Flash distilling column (6a)
NOVELTY - A catalyst containing noble metal is coated on an electrode. The electrode is contacted with aqueous solution containing a mineral acid. Thus, the reactivation method of electrode is carried out.    USE - Reactivation method of electrode (claimed) e.g. cathode for brine electrolysis and water electrolysis.    ADVANTAGE - The electrolysis is economically carried out with reduced power consumption, using the reactivated electrode.
NOVELTY - A heat accumulating type burner is arranged in a pre-heating chamber and the reaction chamber. A water pipeline is provided in the inlet of reactor. An oxidant pipeline is placed in the pre-heating chamber of the reactor. The high temperature combustion supporting air inlet and fuel gas inlet are arranged in the heat accumulating type burner. A mixed gas pipeline is provided in the fuel pipeline, and is connected with the mixing gas tube outlet.    USE - Heat accumulating type burning supercritical gasification oxidation device used for processing organic waste, organic sludge, industrial waste water, coal and organic waste water (all claimed).    ADVANTAGE - The energy consumption of the heat accumulating type burning supercritical gasification oxidation device can be reduced. The efficiency, operability and reliability of the heat accumulating type burning supercritical gasification oxidation device can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the heat accumulating type burning supercritical gasification oxidation device.
NOVELTY - Dairy processing waste-water treatment, comprises (i) discharging waste-water into a hydrolysis regulating tank through a mechanical grid for hydrolysis acidification, (ii) conveying waste-water into an up-flow anaerobic sludge blanket (UASB) reactor for anaerobic treatment through a waste-water sedimentation tank and a clear water tank, and (iii) then conveying into an sequencing batch reactor (SBR) for aerobic treatment, and discharging the treated waste-water after the treated waste-water passes the inspection standards through monitoring well.    USE - The method is useful for dairy processing waste-water treatment.    ADVANTAGE - The method can increase the yield of bio-gas production; can save energy consumed in the aerobic process; can reduce the chemical oxygen demand of the discharged water; can solve the problem of production of large amount of dross in the treatment; can decrease the yield of aerobic sludge by 30-50%; and saves the cost of sludge dehydrating and outward transportation.
NOVELTY - The submarine (1) has fuel cells that are provided for generating electrical energy for electrical loads (11,13) on the device. The fuel cells are activated using hydrogen as fuel. An electrolyzer (20) produces hydrogen for fuel cells through electrolysis of water using the generated electrical energy. A hydrogen reservoir (21) stores hydrogen produced by the electrolyzer before supplying to the fuel cells.    USE - Floating/submersible device e.g. submarine.    ADVANTAGE - The electrolyzer can be operated without noise and emission of pollutants and purity of hydrogen produced by the electrolyzer can be improved. Safe operation of the electrolyzer can be ensured and excess electrical energy generated by the fuel cells can be buffered and stored for future use.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the floating/submersible device.    Submarine (1)    Generator (6)    Electrical loads (11,13)    Electrolyzer (20)    Hydrogen storage unit (21)
NOVELTY - The device has an air channel and an air chamber fixed on a machine frame. An upper furnace cavity is formed on a port. A cracking-gasification chamber is fixed at a left side of a hearth. The cracking-gasification chamber and the hearth are provided with an opening. An upper part of the machine frame is provided with a chain grate. A grate mechanism is fixed on a lower part of the hearth. An upper part of the hearth is provided with a secondary air inlet. The secondary air inlet is connected with a hearth cavity.    USE - Chain grate biomass fuel combustion device.    ADVANTAGE - The device has short length, high combustion efficiency, prolonged service life, stable performance, rational structure and better popularization and application values, and is energy-saving and environment-friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a chain grate biomass fuel combustion device.
NOVELTY - A biomass carbonizing furnace comprises combustion chamber and carbonization chamber above the combustion chamber. Carbonization chamber is provided with feeding port, discharging port and pyrolysis gas outlet. Periphery of the carbonizing chamber is provided with a heat transmission jacket. One end of safe piece also comprises pyrolytic gas leading-out pipe, pyrolysis gas inlet pipe and fan. Gas outlet of pyrolysis gas outlet is connected with pyrolysis gas outlet. Other end of pyrolysis gas outlet is connected with fan inlet.    USE - Biomass carbonizing furnace.    ADVANTAGE - The furnace does not only save energy, reduce burning room by fuel, and reduce production cost, but also solves problem that the organic gas direct discharge caused by pollution.    DETAILED DESCRIPTION - Biomass carbonizing furnace comprises combustion chamber and carbonization chamber above the combustion chamber. Carbonization chamber is provided with feeding port, discharging port and pyrolysis gas outlet. Periphery of the carbonizing chamber is provided with a heat transmission jacket. One end of safe piece also comprises pyrolytic gas leading-out pipe, pyrolysis gas inlet pipe and fan. Gas outlet of pyrolysis gas outlet is connected with pyrolysis gas outlet. Other end of pyrolysis gas outlet is connected with fan inlet. Fan inlet is connected with air inlet pipe. One end of air inlet pipe is communicated with combustion chamber, where other end of the air inlet pipe is connected with fan outlet.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating a biomass carbonizing furnace.
NOVELTY - A heat storage type fuel gas radiating pipe furnace life garbage carbonization method comprises pre-treating domestic garbage by distillation, subjecting to rotary garbage incinerator and to recirculating fluidized bed dry distillation controlled at 400-700 degrees C to produce gaseous substance and residual solid, and collecting the gaseous substance, heating residual solid in a rotary hearth furnace bed having heat provided with heat accumulating type fuel gas radiating pipe arranged in the rotary hearth furnace.    USE - A heat storage type fuel gas radiating pipe furnace life garbage carbonization method.    ADVANTAGE - The method is safe and reduces garbage pollution.    DETAILED DESCRIPTION - A heat storage type fuel gas radiating pipe furnace life garbage carbonization method comprises:    (A) pre-treating domestic garbage by distillation, and subjecting to rotary garbage incinerator and to recirculating fluidized bed dry distillation controlled at 400-700 degrees C to produce gaseous substance and residual solid;    (B) collecting the gaseous substance, heating residual solid in a rotary hearth furnace bed having heat provided with heat accumulating type fuel gas radiating pipe arranged in the rotary hearth furnace;    (C) subjecting to post-treatment to obtain dry distillation product by condensation, and carbonizing the condensed liquid; and    (D) separating tar and sewage, and discharging residual solid comprising carbide substance and waste residue.    DESCRIPTION OF DRAWING(S) - The drawing is a flow chart of a heat storage type fuel gas radiating pipe furnace life garbage carbonization method (Drawing includes non-English language text).
NOVELTY - A pyrolysis device of comprehensive gasification transformation system comprises a furnace body (1) having a furnace hearth (2), a furnace cover (3) arranged on top of furnace hearth, an air outlet (101) communicated with furnace hearth, a heat collector (4) arranged around the furnace hearth and having a water inlet and a water outlet, a water storage buffer kettle of heat supply system, a carbon outlet, a carbon powder collecting device installed below the carbon outlet, and a material distributor.    USE - A pyrolysis device of comprehensive gasification transformation system for biomass waste resource pyrocarbon.    ADVANTAGE - The device has simple structure and low maintenance cost, achieves high utilization rate of heat, and uniformly and densely distributes raw materials inside the furnace by thus having improved production efficiency.    DETAILED DESCRIPTION - A pyrolysis device of comprehensive gasification transformation system comprises a furnace body (1) having a furnace hearth (2), a furnace cover (3) arranged on the top of the furnace hearth, an air outlet (101) communicated with the furnace hearth, a heat collector (4) arranged around the furnace hearth and having a water inlet and a water outlet, a water storage buffer kettle of a heat supply system, a carbon outlet communicated with the furnace hearth and arranged on the bottom of the furnace body, a carbon powder collecting device installed below the carbon outlet, and a material distributor installed on the upper part inside the furnace hearth and connected with an electric motor on the furnace cover.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a pyrolysis device of comprehensive gasification transformation system.    Furnace body (1)    Furnace hearth (2)    Furnace cover (3)    Heat collector (4)    Air outlet (101)
NOVELTY - An internal heat type biomass pyrolysis device comprises a pyrolyzing furnace main body comprising outer layer and inner layer concentric steel high temperature cylinders, an open tube opening, a biomass inlet pipe, and a gasification agent inlet pipe extending to outer cylinder wall, a motor (5) driving a spiral elevator (3) for lifting material, and an ignition device. The outer-layer concentric steel high temperature cylinder comprises cylinder cover, ash chamber, a funnel type, a fuel gas outlet, and an insulating layer.    USE - An internal heat type biomass pyrolysis device.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of an internal heat type biomass pyrolysis device.    Spiral elevator (3)    Motor (5)    Gas outlet (6)    Top cover (11)    Ash chamber (13)
NOVELTY - The method involves considering a wood flour as a raw material. Wood powder i.e. tree powder, is mixed with fatty alcohol solvent under an acid catalyst. Temperature of the catalyst is 130-220 degrees centigrade. Reaction water and recycling solvent are separated with each other. Diameter of the wood powder is 0.45 mm. Concentrated sulfuric acid or polyphosphoric acid is mixed with fatty alcohol. Dosage of the alcohol is 1-3 percent greater than weight of the wood powder. Temperature of the wood powder is 130-220 degrees centigrade.    USE - Method for preparing fuel oil in an industry.    ADVANTAGE - The method ensures better burning effect.
NOVELTY - The method involves maintaining reaction temperature of a super-gravity reactor from 180 to 500 degrees Celsius and pressure value of about 5100 atm. Synthesis gas is carried out under action of catalyst synthesizing petrol or diesel oil product. A catalyst bed layer is existed to calculate ambient acceleration, where ambient acceleration is greater than gravity acceleration. The catalyst bed layer is provided with a honeycomb or plate-type structure and fixed on a super-gravity reactor rotor.    USE - Fischer-Tropsch method for stereospecifically synthesizing petrol and diesel.    ADVANTAGE - The method enables synthesizing petrol or diesel oil from synthetic gas under combined action of super-gravity environment and catalyst during reaction process. The method enables rotating certain speed of a reactant bed layer.    DETAILED DESCRIPTION - The method enables providing a reaction material e.g. coal-based synthetic gas, natural gas-based synthetic gas, coal bed-based synthetic gas or biomass-based synthetic gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram illustrating a Fischer-Tropsch stereospecific synthesizing method.
NOVELTY - The furnace has a furnace body whose top part is provided with a rubbish inlet and a pyrolysis gas outlet. A bottom part of the furnace body is provided with a fire grate body and a bottom air inlet pipe. The furnace body is provided with two single-furnace parts. The single-furnace parts are provided with a common wall. The common wall is connected with the bottom air inlet pipe and a furnace wall. The bottom air inlet pipe is connected with one of the single-furnace parts. The rubbish inlet is connected with the fire grate body.    USE - Combined rubbish gasification furnace.    ADVANTAGE - The furnace independently ensures rubbish gasification process so as to save manufacturing cost. The furnace is simple in structure. The furnace avoids heat loss and increases production yield.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a combined rubbish gasification furnace.
NOVELTY - The device has a microwave gasification device part provided with a furnace body. The furnace body is fixed with a feeding port. A microwave generator is installed on the furnace body. An inner wall of the furnace body is provided with a heat insulating material. The feeding port is fixed with a gas sealing valve. A lower end of a gasification furnace is provided with an air inlet pipeline. The air inlet pipeline is fixed with an air inlet adjusting valve. An outlet port of a gas cooling device part is connected to the air inlet pipeline of a coke.    USE - Biomass-microwave pyrolysis and gasification device.    ADVANTAGE - The device is reasonable in structure, environment-friendly and safe and reliable to use, and saves energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a biomass-microwave pyrolysis and gasification device.
NOVELTY - The furnace has a furnace body (19) whose outer wall is surrounded with a water gas vent pipe (6). The gas vent pipe is inserted into dry gas vent pipes via a gas collecting pipe (9). The furnace body is divided into left and right half parts. A top part of the furnace body is provided with two material pressing hydraulic cylinders (12, 13), rubbish feeding openings (11, 14) and two material pushing hydraulic cylinders (10, 15). Lower and upper grate bars (4, 5) are coated with carbonization layers. Distance between each bar is 150-300 mm.    USE - Destructive rubbish distillation and gasification processing furnace.    ADVANTAGE - The furnace adopts furnace striped fire bars to bear pressure on rubbish weight. The furnace enables adopting the bars that are coated with the carbonization layer to ensure ventilation property. The furnace avoids decomposing of inorganic composition of rubbish and discharging of gray ash from a dust pan.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a destructive rubbish distillation and gasification processing furnace.    Lower and upper grate bars (4, 5)    Water gas vent pipe (6)    Gas collecting pipe (9)    Material pushing hydraulic cylinders (10, 15)    Rubbish feeding openings (11, 14)    Material pressing hydraulic cylinders (12, 13)    Furnace body (19)
NOVELTY - The furnace has a two-section producer gas generator (I) provided with two low temperature dry distillation rubbish carbonization furnaces (II, III). Vertical rubbish drying pre-heating sections (3, 17) are provided with a pre-heating furnace low-temperature carbonization furnace. Water gas vent pipes (2, 18) and a dry distillation gas aeration pipe are connected to a gas outlet pipe (9). Rubbish gasification waste of a combustion inlet is controlled by a gas generator. An outer wall of a water gas vent pipe is provided with the drying pre-heating sections.    USE - Dry distillation-gasifying refuse treatment furnace.    ADVANTAGE - The furnace avoids waste gas discharge and generation of pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a dry distillation-gasifying refuse treatment furnace.    Two-section producer gas generator (I)    Distillation rubbish carbonization furnaces (II,III)    Water gas vent pipes (2,18)    Rubbish drying pre-heating sections (3,17)    Gas outlet pipe (9)
NOVELTY - The boiler has a furnace cover provided with a hollow shaped furnace body, where the furnace body is connected with a feeding device. A lower part of the furnace body is provided with an ignition device and a discharging device. The furnace body is provided with a stewing box. A material stewing tank side wall is fixed with the furnace body. A water outlet pipe and a cold water preheating device are arranged with a heat collecting water tank. An air outlet is provided with a flue gas filter cover.    USE - Carbonizing straw gasification hot water boiler.    ADVANTAGE - The boiler has high combustion efficiency, high yield and better energy-saving and environment-friendly effects.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a carbonizing straw gasification hot water boiler.
NOVELTY - Improving cathode carbon catalytic agent oxygen reducing performance of a proton exchange membrane fuel cell comprises processing the catalyst by cyclic volt-ampere or linear scanning electrochemical acid under the condition of introducing organic functional group and micro noble metal on a carbon catalyst.    USE - Method for improving cathode carbon catalytic agent oxygen reducing performance of a proton exchange membrane fuel cell (claimed).    ADVANTAGE - The method improves glass carbon, carbon nanotube and heteroatom with carbon nanotube under the acidic condition.
NOVELTY - A composition contains ion conductive solid electrolyte consists of lithium and sulfur, nitrile compound which is liquid at 25 degrees C and 101325 Pa, and binder.    USE - A composition for lithium ion battery.    ADVANTAGE - Preservation in the state to which sulfide-type solid electrolyte is dispersed is possible for a long period of time.    DETAILED DESCRIPTION - A composition of formula (Y+Z)/(X+Y+Z)=0.05-0.75 (I) and formula Z/(Y+Z) less than or equal to 0.5 (II), where X is weight of nitrile compound, Y is weight of lithium ion conductive solid electrolyte, and Z is weight of binder, contains ion conductive solid electrolyte consists of lithium and sulfur, nitrile compound of formula RCN (1) which is liquid at 25 degrees C and 101325 Pa, and binder.    R=3-40C hydrocarbon group, 1-20C hydrocarbon group, and/or 3-10C (cyclic) hydrocarbon group.
NOVELTY - The apparatus has a lifting unit (10) that increases the excrements put into the lower portion of the bucket elevator. A circulation screw portion is connected with the vent formed in the lower portion of silo (20) to eject the excrements. A dust collector (40) is connected to the inside of the silo to filter the mixing gas in which the excrements gas and air are mixed.    USE - Sewage treatment apparatus.    ADVANTAGE - The excrements in the apparatus can be dried rapidly. The bad smell can be removed. The excrements gas e.g. methane etc, can be recycled.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the sewage treatment apparatus.    Lifting unit (10)    Silo (20)    Dust collector (40)    Pipes (42,43)    Distributor (50)
NOVELTY - The bio-reactor (1) has bubble movable units (51,52) that are respectively provided with nozzles (81,82). The bubble guide units (61,62) are respectively arranged in the top portion of the bubble movable units for guiding the ultra micro bubble to the floor structure through the nozzles (81,82) respectively. A vent structure (110) is positioned in the upper portion of bio-reactor section to discharge the processing water to outside.    USE - Ultra micro bubble bio-reactor.    ADVANTAGE - The high concentration effluent can be effectively converted into low concentration effluent. The oxygen dissolution effect of the ultra micro bubble bio-reactor is improved. The efficiency of the ultra micro bubble bio-reactor is increased. The size of the bio-reactor is reduced. The maintenance cost of the ultra micro bubble bio-reactor is reduced. The ultra micro bubble bio-reactor can be conveniently operated.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of ultra micro bubble bio-reactor.    Ultra micro bubble bio-reactor (1)    Bubble movable unit (51,52)    Bubble guide unit (61,62)    Nozzle (81,82)    Vent structure (110)
NOVELTY - The anaerobic digestion tank (10) has a reaction bath (20) that creates the organic acid from the organic waste flowed in from the outside. Another reaction bath (30) generates organic acid in the reaction bath. A fluid path (25) is installed between the reaction baths. A backflow preventing unit (40) is provided to open and close the fluid path and prevent the reaction water of the reaction bath.    USE - Anaerobic digestion tank for treating organic waste in sludge, excrement, food waste.    ADVANTAGE - The acceleration of pH value in water can be ensured. The generation of the scum can be reduced. The production of the methane gas can be optimized. The backflow of the organic acid flowed can be prevented. The heavy particulate in air long stays in reaction bath and analysis can be promoted.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the anaerobic digestion tank.    Anaerobic digestion tank (10)    Reaction baths (20,30)    Fluid path (25)    Backflow preventing unit (40)    Cover (44)
NOVELTY - Method for preparing mycobiota, involves (a) using mycobiota, livestock waste and human excreta as raw material, (b) injecting the above-mentioned components to fermentation synthesis tub, (c) adding culture medium, specialty bacteria, nutraceutical and enzyme to the tub, and (d) subsequently adding saccharides, protein, mineral and vitamin to the tub.    USE - The method is useful for preparing mycobiota.
NOVELTY - Method for processing manure, involves feeding an optionally concentrated manure feed (a) though a stream to system comprising centrifugal type separator (1) from which effluents (b) and (c) are obtained, where effluent contains majority of solids present in the feed stream and where at least a portion of effluent is fed to flotation device (2), where flocculation agent (d) is added for obtaining stream of flocculated solids (f) and permeate stream (e).    USE - The method and apparatus are useful for processing manure (claimed), preferably liquid or semi-liquid manure which is in the form of slurry, where the processed manure is used as fertilizer.    ADVANTAGE - The method is cost effective, efficient and consumes less energy, provides solid fractions that has relatively low content of flocculation salts e.g. ferric chloride which prevents plants from effectively absorbing phosphates when present in higher amounts, and hence environmental-friendly, produces dry manure product which facilitates carefree handling and excellent storage stability, and can be performed using less chemicals.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus for processing manure, which comprises dewatering device (4), manure feed, filtrate line (a') connected to centrifugal separator, retentate line (m), liquid line, floatation device, discharge for flocculated solids and discharge for permeate stream.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic representation of process for treating manure.    Centrifugal type (1)    Floatation device (2)    Dewatering device (4)    Manure feed (a)    Filtrate line (a')    Effluents (b,c)    Flocculation agent (d)    Permeate stream (e)    Stream of flocculated solids (f)    Retentate line (m)
NOVELTY - Device for processing of biowaste with the use of vermiculture, containing housing on supports, comprises housing has a hole in each face of housing for performing the measurements of the medium of biowaste, system of heating the bottom surface of housing, the system of unloading biohumus via at least one unloading worm conveyor, the system of collection and removing of surpluses of moisture.    USE - As device for processing of biowaste with the use of vermiculture (claimed).    DETAILED DESCRIPTION - Device for processing of biowaste with the use of vermiculture, containing housing on supports, which consists of two parts: upper in form of rectangular duct with vertical boards and lower in the form of truncated inverted pyramid, rigidly connected with upper portion with the slope angle of the faces of the truncated pyramid to the horizon at least 45 degrees , equipped with the system of the flow of biowaste, comprises housing has a hole in each face of housing for performing the measurements of the medium of biowaste, system of heating the bottom surface of housing, the system of unloading biohumus via at least one unloading worm conveyor, the system of collection and removing of surpluses of moisture.
NOVELTY - Producing aminopyridine compounds or their analogs, substituted forms, derivatives, salts, esters, amides or prodrugs, comprises: either reacting pyridine carboxamide with hypohalite followed by hydrolysis of the resultant and isolating the aminopyridine, where the reaction is carried out in absence of solvent; or isolating aminopyridine compound employing a solvent followed by filtering and optionally drying the resultant mass.    USE - The aminopyridine is useful as an intermediate for producing antineoplastic, fungicides, herbicides, anticoagulant, antiinflammatory, antispasmodic and antiasthmatic drugs, and as additives for foodstuffs.    ADVANTAGE - The method provides aminopyridine compounds with high purity and yield at industrial scales, in an economical manner. The method is single pot and eco-friendly.
NOVELTY - A microorganism fuel cell catalytic acceleration degradation method of submarine organic pollutant, comprise using marine sediment microbiological fuel battery for accelerating degradation of submarine organic pollutant. A total anode output end is formed by anodes (1) connected in series.    USE - Microorganism fuel cell catalytic acceleration degradation method of submarine organic pollutant.    ADVANTAGE - The method can effectively accelerate the degradation of the submarine pollutant, has no proton exchange membrane, and has low preparation cost, simple installation, simple structure and obvious removing effect, and it is green and environment-friendly.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a system for microorganism fuel cell catalytic acceleration degradation method of submarine organic pollutant.    Anode (1)    Cathode (2)    Voltage meter (3)    Small electronic device (4)    Current meter (5)    Lead (6)
NOVELTY - The device has an organic garbage discharge pipe (3) whose lower end is connected with biogas pool (9). The toilets (7) are connected with excrement discharge pipe (8) in bathrooms (4) of floor. The biogas residue outlet (12) is opened on surface at lower portion of biogas pool. The efficient biogas bacteria feed pipe (10) and biogas conveyor pie (13) are mounted at top of biogas pool connected with biogas storage tank (14). The biogas storage tank is connected with biogas power generator (15) which is connected with the LED lamps (6) by electric lead (16).    USE - Independent biogas power generation device for treating garbage and excrement of single residential building.    ADVANTAGE - The efficient biogas bacteria in the biogas pool decomposes the organic garbage and excrement to generate biogas under certain temperature and humidity conditions. The biogas is conveyed into biogas storage tank by biogas conveyor pipe and into biogas power generator for generating current. The current is conveyed into the LED lamp of floor by electric lead for electric illumination. The organic fertilizer is discharged from biogas residue outlet.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the independent biogas power generation device for treating garbage and excrement of single residential building.    Organic garbage discharge pipe (3)    Bathroom (4)    LED lamp (6)    Toilet (7)    Excrement discharge pipe (8)    Biogas pool (9)    Efficient biogas bacteria feed pipe (10)    Biogas residue outlet (12)    Biogas conveyor pie (13)    Biogas storage tank (14)    Biogas power generator (15)    Electric lead (16)
NOVELTY - System comprises fermenter process unit for performing fermentation and gasification unit, where organic waste is generated during ethanol production using marine biomass which is collected in the fermenter process unit and methanol is produced by gasification process in the gasification unit.    USE - The system is useful for producing bioenergy used as fuel.
NOVELTY - Rhizobium bio-organic fertilizer composition comprises a granulated fertilizer main body. A spherical Rhizobium group is set in the center of the granulated fertilizer main body. A layer of slow release protective film is covered on the outer surface of the spherical Rhizobium group. An organic fertilizer layer is covered on the outer part of the slow release protective film. A layer of drought resisting agent layer is covered on the outer surface of the organic fertilizer layer. A layer of water-absorbing membrane is covered on the drought resisting agent layer.    USE - The fertilizer composition is useful for accelerating the growth of the crops.    ADVANTAGE - The fertilizer composition is economical for the agricultural production.    DETAILED DESCRIPTION - Rhizobium bio-organic fertilizer composition comprises a granulated fertilizer main body, where a spherical Rhizobium group is set in the center of the granulated fertilizer main body. A layer of slow release protective film is covered on the outer surface of the spherical Rhizobium group. A layer of organic fertilizer layer is covered on the outer part of the slow release protective film. A layer of drought resisting agent layer is covered on the outer surface of the organic fertilizer layer. A layer of water-absorbing membrane is covered on the outer surface of the drought resisting agent layer, and a layer of coating is covered on the outer surface of the water-absorbing membrane.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the Rhizobium bio-organic fertilizer.
NOVELTY - The biogas device comprises a unit for preparing an initial feedstock, a dry substrate, biologically active additives, a feedstock fermenter, a unit for cleaning and storing biogas, a unit for producing electricity and heat, a control unit, and a temperature sensor installed in the fermenter. The fermenter is provided with a thermal housing, and is connected with a source of water network. The control unit is connected to the initial feedstock preparation unit. The sensor is configured for carrying out microbiological analysis.    USE - Used as a biogas device.
NOVELTY - Treating sludge comprises: (i) mixing dehydrated sludge, wheat bran, crop straw and humic acid and fermenting; (ii) mixing the sludge and agricultural waste straw to form mixed material; (iii) adding the mixed material to the humic acid and mixing with strains, where the carbon to nitrogen ratio, is 25:1-13:1, the moisture content of the mixed material is 58-70% and the amount of humic acid and strain according to the wt. of the mixed material is 0.01-0.02% and 5-40%; and (iv) uniformly mixing the raw materials obtained in the step (iii), stacking and allowing to stand for 8-16 days.    USE - The treated sludge is used as high quality raw material for producing organic fertilizer and agricultural fertilizer.    ADVANTAGE - The method treats the sludge in a cost efficient manner.    DETAILED DESCRIPTION - Treating sludge comprises (i) mixing dehydrated sludge, wheat bran, crop straw and humic acid with weight ratio of 13:1:1:0.1-10:1.5:0.3:0.1 and fermenting for 10-15 days at 55-60 degrees C; (ii) mixing the sludge and agricultural waste straw to form mixed material; (iii) adding the mixed material to the humic acid and mixing with strains, where the carbon to nitrogen ratio, is 25:1-13:1, the moisture content of the mixed material is 58-70% and the amount of humic acid and strain according to the wt. of the mixed material is 0.01-0.02% and 5-40%, respectively; and (iv) uniformly mixing the raw materials obtained in the step (iii), stacking and allowing to stand for 8-16 days at -15-30 degrees C.
NOVELTY - Ecofriendly organic fertilizer, prepared by using municipal rubbish, drain sludge and livestock manure as main materials, fermenting strain, i.e., yeast and carbamide or ammonium carbonate as auxiliary materials, mixing the main materials, spreading on the floor, adding water, adjusting humidity, adding the fermentation strain and carbamide or ammonium carbonate, preparing a layer of mixture material, dispersing a layer of the fermenting strain, continuously stacking 10-20 layers, covering with a black plastic film, fermenting, turning and fermenting, sieving and packaging, is claimed.    USE - The ecofriendly organic fertilizer is useful for producing pollution-free vegetables.    ADVANTAGE - The ecofriendly organic fertilizer solves the problem of difficult processing of the urban domestic rubbish, and utilizes waste.    DETAILED DESCRIPTION - Ecofriendly organic fertilizer, prepared by using municipal rubbish, drain sludge and livestock manure as main materials (1000-2000 kg), fermenting strain, i.e., yeast (2-4 kg) and carbamide or ammonium carbonate as auxiliary materials (20-4 kg), mixing the main materials, spreading on the floor, adding suitable amount of water, adjusting humidity to 60%, adding the fermentation strain and carbamide or ammonium carbonate, preparing a layer of mixture material, dispersing a layer of the fermenting strain, continuously stacking 10-20 layers, covering with a black plastic film, naturally fermenting the materials for 8-10 days, turning in first 15 days and fermenting, sieving and packaging, is claimed.
NOVELTY - Aerobic denitrification Methylobacterium comprises Methylobacterium phyllosphaerae (SDN-3) CGMCC 3660.    USE - Aerobic denitrification methylobacterium (claimed).    ADVANTAGE - The Methylobacterium ( SDN-3) has high nitrate reductase activity, capable of expressing under aerobic and limited oxygen condition, has aerobic denitrification and limited oxygen denitrification function, and has nitrification effect and denitrification effect; and utilizes cheap carbon source and nitrate nitrogen as single nitrogen source to perform aerobic denitrification, aerobic nitrification and aerobic denitrification synchronously. The bio-activity of Methylobacterium (SDN-3) is stable at 22-40?oC and pH 7-9.5, and the denitrification effect is excellent. The Methylobacterium (SDN-3) is capable for processing waste water with COD, nitrate nitrogen or ammonia nitrogen, with total nitrogen removal rate of more than 90%, and the average total nitrogen removal rate of more than 9 mg/(L.hour); and the COD removal rate is more than 85%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for application of Methylobacterium (SDN-3) used for sewage processing field.
NOVELTY - Rubbish harmless purifying value-added processing device comprises a pyrolysis chamber (1) of a pyrolysis purifying mechanism. The pyrolysis chamber is provided with a rubbish inlet and an ash fertilizer outlet. The chamber wall of the pyrolysis chamber is provided with a water channel (2) and a smoke channel (3).    USE - The device is useful for harmless value-added processing of urban household rubbish.    ADVANTAGE - The device: continuously purifies rubbish without smoke emission or dioxin production, and completely deodorizes, sterilizes and purifies; and obtains 410 yuan net profit by processing one ton urban household rubbish.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of rubbish harmless purifying value-added processing device.    Pyrolysis chamber (1)    Water channel (2)    Smoke channel (3)    Plenum chamber (4)    Cooling chamber (5)
NOVELTY - Manufacturing method for high concentration particle potassium fertilizer, involves reacting salt and alkaline matter to generate the colloidal compound; mixing the colloidal compound with potassium fertilizer raw material, bonding and granulating; drying, screening and cooling granulated product to obtain the particle potassium fertilizer.    USE - For manufacturing method for high concentration particle potassium fertilizer (claimed).    ADVANTAGE - The method provides simple operation technology, is low cost, big producing capability, smooth product particle and high strength, and there is no three wastes during the production process, it is energy saving and environment friendly, and the market prospect is very wide.
NOVELTY - Ionic liquid catalyst comprises an ionic liquid and one or two kinds of metal salt or alkali, where ratio between the ionic liquid and the metal salt is 1:0.05-3, and molar ratio between the ionic liquid and the alkali is 1:0.05-2.    USE - The ionic liquid catalyst is useful for catalyzing liquefaction and gasification of biomass waste.    ADVANTAGE - The ionic liquid catalyst: has high activity, good stability and low cost; and converts biomass waste into liquid-phase or gas-phase low molecular weight pyrolysis product, and thus it develops a new way for using biomass waste with low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for use of the ionic liquid catalyst to catalyze liquefaction and gasification of biomass waste, comprising (i) preparing the ionic liquid catalyst by mixing one kind of ionic liquid with one or two kinds of metal salt or alkali according to the biomass waste need to be translated into a different liquid or gaseous low molecular weight pyrolysis products, (ii) drying biomass waste, crushing and sieving to obtain powder with grain diameter of 10-60 meshes, then mixing the catalyst and biomass waste powder in a weight ratio of 1:0.03-15, placing the mixture in a reactor, discharging surplus air in the reactor, and carrying out pyrolysis under anaerobic condition for 10-50 minutes at 160-300 degrees C, (iii) cooling the pyrolysis gas generated in the reaction mixture by using condensation device, and collecting condensed product in a container to obtain pyrolysis product, then adding small quantity of water into the residue of the reactor and centrifuging at high speed to remove the residue, and recycling aqueous solution of ionic liquid catalyst.
NOVELTY - Preparation of a biological gasoline comprises adding (pts.wt.) methanol (53), turpentine (20), and industrial benzene (25) to a homogenizing groove, and starting a circulating pump to obtain a homogenized liquid; dissolving paraffin wax (60) in cyclohexane (10), adding potassium permanganate (2), and calcium peroxide (3) while of stirring to obtain a composite additive; and slowly adding 3 pts. vol. additive to the homogeneous liquid, and homogenizing for 60 minutes via injecting.    USE - Method for the preparation of a biological gasoline (claimed).    ADVANTAGE - The biological gasoline has good ignition performance and high heat efficiency, is inexpensive, and prepared using simple method.
NOVELTY - A methanol gasoline comprises (vol.%) degeneration methanol (10-35), and a component oil (65-90). The component oil comprises (vol.%) non-aromatic matter (10-30), naphtha (20-30), and No. 90 gasoline (40-70).    USE - A methanol gasoline used for automobile.    ADVANTAGE - The methanol gasoline is inexpensive and environment friendly. It reduces hydrocarbon, nitrogen oxide, and carbon monoxide discharge.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the methanol gasoline, comprising:    (A) adding an additive in methanol;    (B) blending until that the mixed solution has no silk phenomenon, to obtain a degeneration methanol;    (C) uniformly mixing non-aromatic matter, naphtha, and No. 90 gasoline to obtain a component oil; and    (D) mixing the component oil with the degeneration methanol for 1 hour.
NOVELTY - The biogas for fermentation of complex microbial agents, is claimed. The agents comprise Acetobacter, Pseudomonas (CGMCC No.4764) and Pantoea agglomerans (CGMCC No.4765) to ferment the bacteria in the form of liquid. A weight ratio of the Acetobacter, Pseudomonas (CGMCC No.4764) and Pantoea agglomerans are 1:1:1.    USE - The biogas is useful for fermentation of complex microbial agents.    ADVANTAGE - The biogas is capable of fermenting the complex microbial agents with low temperature.
NOVELTY - Production of biodiesel comprises separating microalgae by microbial separation and purification to obtain purified microalgae, filtering and centrifuging biogas slurry, and taking supernatant; transferring processed biogas slurry into internal circulating optical reactor, inoculating and culturing seed liquor, periodically measuring the growth amount and nutrient variation of microalgae, and evaluating experimental results; and collecting microalgae, extracting oil in microalgae, and obtaining biodiesel.    USE - Method for producing biodiesel (claimed).    ADVANTAGE - The method uses biogas slurry to culture microalgae, has low cost, implements resource utilization of biogas slurry and double benefits of renewable energy sources and environmental management, and is suitable for industrial production.
NOVELTY - Composite organic soil comprises vinegar residue (5 pts. wt.), cassava dregs (3 pts. wt.), carbonized bran or plant ash (1.2 pts. wt.), perlite (0.2 pts. wt.), vermiculite (0.6 pts. wt.), fertilizer (0.1-0.5 wt.%), synergistic agent, and chlormequat chloride. The organic soil has water content of 46-50%, organic material content of greater than or equal to 40%, total nutrient (nitrogen+phosphorus pentoxide+potassium oxide) content of 2.2-2.8%, pH of 5.5-7, electrical conductivity of less than or equal to 3, and particle size of less than or equal to 5 mm, in which 2-4 mm particles account for 55-60%.    USE - Composite organic soil used for growing rice seedlings (claimed).    ADVANTAGE - The organic soil promotes robust growth of rice seedlings.    DETAILED DESCRIPTION - Composite organic soil comprises vinegar residue (5 pts. wt.), cassava dregs (3 pts. wt.), carbonized bran or plant ash (1.2 pts. wt.), perlite (0.2 pts. wt.), vermiculite (0.6 pts. wt.), fertilizer (0.1-0.5 wt.%), synergistic agent (0.2-0.5 wt.%), and chlormequat chloride (0.2-0.3 wt.%). The organic soil is prepared by fermenting organic raw materials with high-temperature decomposing agent or effective microorganism (EM) formulation, drying, crushing, and uniformly mixing other components. The organic soil has water content of 46-50%, organic material content of greater than or equal to 40%, total nutrient (nitrogen+phosphorus pentoxide+potassium oxide) content of 2.2-2.8%, pH of 5.5-7, electrical conductivity of less than or equal to 3, and particle size of less than or equal to 5 mm, in which 2-4 mm particles account for 55-60%.
NOVELTY - The method comprises applying ethylene as a plant growth regulator to grain, cotton, vegetable and fruit tree, spraying leaf surface with 40% of ethephon, applying fertilizer on the ground stem to extend 3 meters long, spraying 40% per mu ethephon for 60-30 kg of water, and uniformly spraying fertilizer to dropping bud falling flower.    USE - The method is useful for increasing yield of herbal Codonopsis medicine.    ADVANTAGE - The method is capable of economically increasing the yield of herbal Codonopsis medicine with less energy consumption.
NOVELTY - The method involves crushing potash feldspar, limestone, and assistant to 50-100 mm. The crushed material is added to ring kiln for roasting. The roasted material is cooled to about 100 degrees C. The cooled material is grinded to average grain diameter of 0.5-1.5 mm. The grinded powder is mixed with organic waste according to mass ratio of (1:10)-(10:1). The mixed material is moved to anaerobic fermentation pool. The product material is transferred to aerobic fermentation pool. The product is partially dehydrated so as to obtain long-efficiency soil conditioner.    USE - Method for manufacturing soil conditioner by using potash feldspar and organic waste.    ADVANTAGE - The efficiency and durability of the soil conditioner are improved. Since the soil conditioner contains certain nitrogen, phosphorus, potassium, calcium, magnesium, sulfur, soluble silicon and humic acid, the soil condition is improved. Hence nutrition components are supplied to crops within relatively long time effectively. The soil conditioner can be directly applied or applied together with chemical fertilizer. The production raw material uses natural mineral and waste in livestock farm, thus the manufacturing cost of the soil conditioner is reduced. The energy required for manufacturing the soil conditioner is reduced. The environmental-friendly effect of the soil conditioner is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating process for manufacturing soil conditioner. (Drawing includes non-English language text)
NOVELTY - Recycling effective ingredients in enzyme amoxicillin mother liquor by nanofiltration includes adjusting pH of mother solution by alkali; hydrolyzing amoxicillin in the mother liquor using penicillin G acylase to obtain mother liquor containing D-hydroxyphenylglycine and 6-aminopenicillanic acid; nanofiltering and concentrating the mother liquor; crystallization separating and recovering D-hydroxyphenylglycine and 6-aminopenicillanic acid by adding acid to the mother liquor; and regulating pH.    USE - Recycling effective ingredients in enzyme amoxicillin mother liquor, useful for preparing D-hydroxyphenylglycine methyl ester hydrochloride used for preparing neohesperidin (claimed).    ADVANTAGE - The method has high throughput and better economical efficiency.    DETAILED DESCRIPTION - Recycling effective ingredients in enzyme amoxicillin mother liquor by nanofiltration comprises:    (A) adjusting pH of the mother solution at 9.0-9.5 using alkali, where crystalline particles in the mother solution are totally dissolved, and the effective component dissolved in the mother liquor is in the form of salt;    (B) hydrolyzing amoxicillin in the mother liquor using penicillin G acylase to obtain mother liquor containing D-hydroxyphenylglycine and 6-aminopenicillanic acid;    (C) nanofiltering and concentrating the mother liquor; and    (D) crystallization separating and recovering D-hydroxyphenylglycine and 6-aminopenicillanic acid by adding acid to the mother liquor; and regulating pH at 3.5-5.0.
NOVELTY - Preparation of proanthocyanidin mixture from broomcorn, involves grinding and sieving broomcorn to obtain powder, adding ethanol to the powder, regulating pH of the mixture by adding e.g. metaphosphoric acid, stirring the mixture, placing the mixture in ultrasonic water bath, decompressing the mixture, filtering the mixture, condensing the obtained supernatant, subjecting the obtained extract to chromatography, eluting the extract using water and ethanol sequentially, condensing the eluate and freeze-drying the condensate to obtain proanthocyanidin powder.    USE - The method is useful for preparing proanthocyanidin mixture from broomcorn which is used for preventing and/or treating tooth decay (claimed) caused by bacteria, and clearing acid and superoxide anion generated by bacteria.    ADVANTAGE - The method is simple, convenient and environmentally-friendly.    DETAILED DESCRIPTION - Preparation of proanthocyanidin mixture from broomcorn, involves (a) grinding and sieving broomcorn to obtain powder, (b) adding 70% ethanol (10-25 times) mass/volume (m/v) to the powder, (c) regulating pH of the mixture to 4-7 by adding metaphosphoric acid and sodium bisulfite and stirring the mixture uniformly, (d) placing the mixture in ultrasonic water bath of 20-60 degrees C for 10-70 minutes, where the frequency of the ultrasonic waves is 20-40 kHz, (e) decompressing the mixture under pressure of 0.1 MPa, (f) filtering the mixture to obtain supernatant, (g) condensing the supernatant under vacuum to obtain extract and recovering ethanol from the mixture, (h) passing the extract through ADS-17 macroporous resin chromatography column, and eluting the extract using water and 10-50% ethanol sequentially, (i) condensing the eluate under vacuum and freeze-drying the condensate to obtain proanthocyanidin powder.
NOVELTY - A preparation of N,N-diene-propyl-5-methoxy tryptamine hydrochloride involves dissolving 5-methoxy tryptamine in N,N-dimethylformamide, reacting the organic amine solid load catalyst and chloropropene for 6-8 hours at room temperature, filtering the reaction liquid and evaporating the filtrate, using the isopropanol for dissolving, and adding hydrochloric acid (36 wt.%) for having hydrochlorinated operation to obtain the N,N-diene-propyl-5-methoxy tryptamine hydrochloride.    USE - For preparation of N,N-diene-propyl-5-methoxy tryptamine hydrochloride, which is used in clinic.    ADVANTAGE - The process provides N,N-diene-propyl-5-methoxy tryptamine hydrochloride having yield of greater than or equal to 88%; reduces the production cost, and pollution to the environment; provides the product that is stable; is simple and efficient process; and is large scale production process.    DETAILED DESCRIPTION - A preparation of N,N-diene-propyl-5-methoxy tryptamine hydrochloride involves dissolving 5-methoxy tryptamine in N,N-dimethylformamide, reacting the organic amine solid load catalyst and chloropropene for 6-8 hours at room temperature, filtering the reaction liquid and evaporating the filtrate, using the isopropanol for dissolving, and adding hydrochloric acid (36 wt.%) for having hydrochlorinated operation to obtain the N,N-diene-propyl-5-methoxy tryptamine hydrochloride. The preparation of the organic amine solid load catalyst involves adding the organic amine and solid load phase into the toluene without water, reflowing for 5-6 hours at 105-110 degrees C, reducing to room temperature, drying the solid, which is the organic amine solid load catalyst.
NOVELTY - Residue comprises (in wt.%): monoammonium phosphate (0.05-0.5%), auxiliary material (0-30%), microbial leavening agent (0.025-0.5%) and carrageenan algae residue (remainder).    USE - The residue is useful as organic fertilizer (claimed).    ADVANTAGE - The residue changes waste into valuable, and has high efficiency, and is cost-effective and does not pollute the environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the residue, which involves adding phosphate in carrageenan algae residue and adjusting the pH to 7-8, and adding wheatbran and microbial leavening agent in the carrageenan algae residue and adequately mixing and stirring, and fermenting the obtained compost at 65-68 degrees C, turning the compost and supplementing water simultaneously for the first and second day, and carrying out inoculating process on fifth day and seventh day, and maintaining temperature of 45-65 degrees C, and performing aerobic fermentation of the product for 12-20 days, and after composting the water content of the fermented material is 20-50% at 50-70 degrees C to obtain the residue.
NOVELTY - Invention can be used in chemical industry. Natural gas is compressed, heated and purified from sulphur compounds in a radial-spiral reactor. Two-step catalytic conversion of methane under pressure is carried out in a radial-spiral reactor which is divided into two sections. Steam conversion is carried out in the first section at temperature 800 - 1000 degrees C using heat from the gas which is converted at the second step, as well as portions of natural gas, blow-off and flash gases additionally burnt at a burner. The temperature of flue gases after the burner is kept in the range of 900-1100 degrees C by recycling a portion of cooled flue gases with mixture thereof with air fed into the burner. The mixture of gases fed into the burner is first heated using heat from flue gases from the first section. Air-steam conversion is carried out in the second section at 900-1400 degrees C. Heat of the converted gas is used to heat the initial natural gas and generate steam. Catalytic conversion of carbon oxide is carried out in a single step in the radial-spiral reactor at temperature 200-220 degrees C, which is maintained via water evaporation cooling. The nitrogen-hydrogen mixture is cleaned from carbon dioxide and oxygen-containing compounds in the radial-spiral reactor, compressed and fed for ammonia synthesis into the radial-spiral reactor.    USE - Chemistry.    ADVANTAGE - Cost effectiveness and ecological cleanness. 6 cl, 1 dwg, 1 ex
NOVELTY - The method involves processing a low potential anode by oxide surface modification treatment process. A conductive substrate is passed by electrolytic deposition process and filled with iron oxide material. High power is output by a microorganism fuel battery.    USE - Method for depositing iron salt ferric oxide on a surface of a low potential graphite calomel anode electrode in a high voltage and power outputting seabed settled layer microbial fuel cell.    ADVANTAGE - The method enables depositing the iron salt ferric oxide on the graphite surface with anode potential of about -775mV, current density of about 1.240 /asterisk 10-3A/cm2 and output voltage of about 1.0 to 1.1V, thus improving battery maximum output power density for about 743.7mW/m2.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph illustrating a method for depositing iron salt ferric oxide on a surface of a low potential graphite calomel anode electrode in a high voltage and power outputting seabed settled layer microbial fuel cell.'(Drawing includes non-English language text)'
NOVELTY - Producing a refine edible grease, by cycling and using a material slag, comprises: collecting a oil residue and waste water; sending the collected waste water and oil residue into the methane tank; producing dregs in the methane tank; producing waste water in the methane tank can be induced into the first cleaning pool; planting aquatic plant into the first cleaning pool to clean the water quality; pouring the cleaned water from the first cleaning pool into the second cleaning pool; feeding fish, shrimp and other aquatic plants; and purifying the water quality treatment.    USE - The method is useful for producing refine edible grease, by cycling and using material slag.    ADVANTAGE - The method is simple and cost effective.    DETAILED DESCRIPTION - Producing a refine edible grease, by cycling and using a material slag, comprises: collecting a oil residue and waste water produced in the oil smelting furnace and oil filter device by the pipeline; sending the collected waste water and oil residue into the methane tank by the pipeline for producing methane; producing dregs in the methane tank can be used as the manufacturing material of fertilizer or as industrial chemicals; producing waste water in the methane tank can be induced into the first cleaning pool by the pipeline; planting aquatic plant into the first cleaning pool by the physical method to clean the water quality, after cleaning the first cleaning pool for a long time; pouring the cleaned water from the first cleaning pool into the second cleaning pool; feeding fish, shrimp and other aquatic plants in the second cleaning pool; and purifying the water quality treatment.
NOVELTY - Method for treating wastewater, involves carrying out anaerobic fermentation of high nitrogen-containing wastewater containing 5000 mg/l or more of nitrogen at 30-50 degrees C, performing pressure reduction process for removal of ammonia in wastewater produced during anaerobic fermentation process, and performing methane fermentation of the wastewater in which ammonia content is reduced.    USE - The method and apparatus are useful for treating wastewater (claimed).    ADVANTAGE - The methane gas produced during wastewater treatment is used as bioenergy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus for treating wastewater, which comprises unit for performing anaerobic fermentation (1) of the nitrogen-containing wastewater, unit for performing pressure reduction process (2), methane fermentation unit (3), and an unit for collecting methane gas (4) produced in the methane fermentation unit.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of wastewater treatment apparatus.    Unit for performing anaerobic fermentation (1)    Unit for performing pressure reduction process (2)    Methane fermentation unit (3)    Unit for collecting methane gas (4)    Solid-liquid separation unit (5)    Decompression device (25)
NOVELTY - The method involves stacking an anode electrode (6) of a membrane electrode assembly (2) on an electrolyte layer. A unit cell is provided with a gas diffusion layer and an air supply member (4). The gas diffusion layer is immersed in water and stacked on a side of the assembly. The gas diffusion layer immersed in the water is frozen. A cathode side diffused layer (9) of a fuel-supply member (3) and anode side diffused layer (8) are stacked on another side of the assembly. The anode electrode is arranged in a surface along thickness direction of a side of an electrolytic membrane (5).    USE - Method for manufacturing a liquid fuel cell such as direct methanol type fuel cell, direct dimethyl-ether type fuel cell and hydrazine form fuel cell.    ADVANTAGE - The method enables immersing the gas diffusion layer in the water so as to ensure affinity respect to liquid fuel of the gas diffusion layer, outstanding fuel diffusibility and stabilization of a fuel cell and manufacture the fuel cell with reduced period of break-in operation, so that rigidity of the gas diffusion layer can be ensured and attachability/assemblability during lamination process can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of arrangement of a fuel-supply member and an air supply member on a gas diffusion layer.'(Drawing includes non-English language text)'    Membrane electrode assembly (2)    Fuel-supply member (3)    Air supply member (4)    Electrolytic membrane (5)    Anode electrode (6)    Anode side diffused layer (8)    Cathode side diffused layer (9)
NOVELTY - The food waste disposal unit has a milling unit that is positioned at inside of drying furnace. A food disposal unit (100) having gas discharge openings (240) is positioned at the inside of the drying furnace.    USE - Food waste disposal unit used in home and restaurant.    ADVANTAGE - The food waste can be disposed easily with improved energy saving effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of food waste disposal unit.    Food disposal unit (100)    Exhaustion opening and closing unit (140)    Gas pipe line (210)    Filter section (230)    Gas discharge opening (240)
NOVELTY - Biomass briquette comprises at least one raw material chosen from cornstalk, corn, wheat stalk, straw, weeds, bean stalks, peanut shells, Sorghum stalks, cotton stalks, palm, coconut, rice, Sorghum, sweet potatoes, and rice hulls, where all the raw materials were mixed and molded to obtain briquette and punched with air holes to obtain final product.    USE - The biomass briquette is used as solid fuel source (claimed).    ADVANTAGE - The biomass briquettes are utilized as inexpensive fuel substitute to coal. The biomass briquette provides sufficient calories equivalent to that of coal. The biomass briquette is environmentally-friendly and is prepared using various waste biomass, hence recycling of residues left out after combustion is also enabled.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the above-mentioned biomass briquette, which involves mixing all the above-mentioned raw materials, crushing all the biomass raw materials, mixing bonding agent to crushed mixture, molding mixture to obtain briquette, and punching air holes to obtain final product.
NOVELTY - System has a receiver, separator and crusher with clatter, and further has vertical mine-receiver connected to the separator, and fermenter made in the form of the inclined slowly rotating cylinder, and through which by fan is sucked air, where the waste from the fermenter come to the second separator, to the clatter for separation of non-composting material, and to the crusher, the waste glass in non-composting material is broken into small pieces, and non-composting material is processed into fuel through pyrolysis.    USE - The system is useful for continuous composting of wastes, preferably non-composting waste for producing fuel.    DETAILED DESCRIPTION - System has a receiver, separator and crusher with clatter, and further has vertical mine-receiver connected to the separator, which is a horizontal transporter, fermenter made in the form of the inclined slowly rotating cylinder with a diameter of 4 microns and with the length of 60 microns, and through which by fan is sucked air, where the waste from the fermenter come to the second separator, to the clatter for separation of non-composting material, and to the crusher, the waste glass in non-composting material is broken into small pieces, and non-composting material is processed into fuel through pyrolysis.
NOVELTY - The machine has housing (100) having supporting unit (110). A presser portion (200) is protruded outside housing. A drive motor (300) is provided for rotating main pivot (2). Inner and outer covers (400,500) are provided with respect to presser portion. A lubricant supplying unit (600) is provided with lubricant receiving portion (610) and delivery hose (620) for supplying lubricant to contact surface of supporting unit.    USE - Machine for manufacturing refused derived fuel.    ADVANTAGE - Manufacturing of refused derived fuel is performed effectively. Service life of machine is enhanced.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the machine for manufacturing refused derived fuel.    Main pivot (2)    Housing (100)    Supporting unit (110)    Presser portion (200)    Drive motor (300)    Inner cover (400)    Outer cover (500)    Lubricant supplying unit (600)    Lubricant receiving portion (610)    Delivery hose (620)
NOVELTY - The device (200) has a storage unit (210) which stores the biogas supplied from the anaerobic digestion tub (100). A capture unit (230) is provided for refining the biogas ejected from storage unit for collecting the carbon dioxide. A feed port (250) is provided for supplying the carbon dioxide sampled in the capture unit.    USE - Carbon-dioxide collecting apparatus for anaerobic digestion tank used in gardening facility (claimed).    ADVANTAGE - The carbon dioxide generated in the anaerobic digestion tub can be supplied to the gardening facility so that the growth of the plant can be accelerated. The environmental contamination of carbon dioxide can be reduced with reduced cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for gardening facility.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of gardening facility. (Drawing includes non-English language text)    Anaerobic digestion tub (100)    Carbon-dioxide collecting device (200)    Storage unit (210)    Capture unit (230)    Feed port (250)
NOVELTY - The method involves coating metal oxide powder on an electrode layer by using an aerosol deposition method. Another electrode layer is formed on an electrolyte layer. The electrolyte layer is made of metal oxide, yttria-stabilized zirconia, samaria doping ceria, gadolinia doped ceria, scandia stabilized zirconia and strontium manganese doping lanthanum gallate and silver yttria doping bismuth oxide. Average granularity of the electrolyte layer is 0.3-3.0 units.    USE - Method for manufacturing a solid oxide fuel cell.    ADVANTAGE - The method enables improving reliability and productivity of the solid oxide fuel cell and improving quality of the solid oxide fuel cell by limiting thermal annealing temperature during an electrode formation process.    DESCRIPTION OF DRAWING(S) - The drawing shows a photographic view illustrating a solid oxide fuel cell manufacturing method.'(Drawing includes non-English language text)'
NOVELTY - The device has a main body equipped with a catalytic unit. A mixing gas splitter (30) is equipped with the main body. Anode exhaust gas and air of a fuel cell stack are uniformly mixed in the catalytic unit. A gas distribution part (50) is utilized for supplying mixing gas to the catalytic unit. A blow pipe (40) is equipped with the main body. An exhaust flow path ejects the mixing gas from an influx tract part. The gas distribution part is provided with a dispersion passage part, which is utilized for distributing the mixing gas ejected from the blow pipe.    USE - Exhaust gas processing device for a fuel cell.    ADVANTAGE - The device ensures stable operation for the fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of an exhaust gas processing device.    Mixing gas splitter (30)    Blow pipe (40)    Gas distribution part (50)    Plate-like outer supporting part (60)
NOVELTY - Utilizing thermal energy of gases generated in biomass to liquids (BtL) plant comprises utilizing thermal energy of gases generated in the production process of the BtL plant in superheating steam for driving the turbine machineries of the BtL plant.    USE - The method is useful for utilizing thermal energy of gases generated in BtL plant. The thermal energy of gases generated in BtL plant is useful for superheating steam streams driving the turbine machineries of the BtL plant and post-processing gas streams for hydrogen recovery; and for utilizing saturated steam streams generated in BtL plant, where superheating increases the self-supported electrical balance of the BtL and facilitates self-contained operation of the BtL plant as a stand-alone facility independent from another industrial plant or power utility, while simultaneously the yield of end product is maximized. The steam reformer such as SMR reactor integrated with the BtL plant equipment is useful for superheating the discharge gas streams generated in the BtL plant to drive the plant's compressors and/or electricity generation units and, additionally, to maximize the yield of end products of the BtL plant, where hydrogen is recovered with the help of PSA unit; for utilizing the thermal energy of the flue gases and/or reformed gas for superheating the steam that is used in the BtL plant for driving the syngas turbo-compressor and/or producing electricity; and for improving the yield of the BtL plant, where a WGS process is used having a steam reformer and PSA unit integrated with the BtL plant equipment (all claimed).    ADVANTAGE - The invention utilizes the excess steam on-site and thus reduces the quantity of purchased electricity.
NOVELTY - Treating fibers and fiber bundles containing cellulose fraction, lignin fraction and hemicellulose fraction, involves softening the fibers; swelling the fibers; macerating the fibers; and removing at least a portion of the lignin fraction and hemicellulose fraction from the fibers.    USE - For treating fibers and fiber bundles (claimed).    ADVANTAGE - The method provides treated fiber having improved water holding capacity and improved crystallinity; and has improved conversion efficiency in the production of biofuels.
NOVELTY - A catalyst contains metal(s) including nickel which is loaded into a composite oxide containing cerium and/or praseodymium, zirconium, oxygen and has specific surface area of 11-90 m2/g. The content of each of cerium and/or praseodymium, and zirconium is 10-90 mol%, respectively. The amount of element other than oxygen, cerium and/or praseodymium, and zirconium is 0-20 mol%. The composite oxide has maximum peak at wavelength of 200-800 cm-1 and maximum-peak-half-value width of 20-72 cm-1, when measured by Raman spectroscopy.    USE - Catalyst is used for reforming hydrocarbon for producing hydrogen used for polymer electrolyte fuel cell for domestic appliances and motor vehicle.    ADVANTAGE - The catalyst is manufactured efficiently and economically with excellent quality and catalytic activity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of catalyst.
NOVELTY - Method for preparing starting material for enzymatic saccharification by treating lignocellulose-containing plant biomass with ammonia, involves analyzing moisture content in system in which the above-mentioned treatment is conducted satisfies as: the ratio of mass of water, and biomass and mass of water less than or equal to 0.30 and analyzing ammonia phase diagram, where the pressure is plotted in isobars with temperature on the abscissa axis against density on the ordinate axis.    USE - The method is useful for preparing starting material for enzymatic saccharification which is useful for preparing sugar and ethanol (all claimed).    ADVANTAGE - The method enables preparing starting material with high energy saccharification efficiency, and reducing energy for recovering/separating ammonia.    DETAILED DESCRIPTION - Method for preparing starting material for enzymatic saccharification by treating lignocellulose-containing plant biomass with ammonia, involves analyzing moisture content in system in which the above-mentioned treatment is conducted satisfies: the ratio of mass of water, and biomass and mass of water less than or equal to 0.30, and analyzing ammonia phase diagram, where the pressure is plotted in isobars with temperature on abscissa axis against density on ordinate axis, temperature and pressure of the ammonia in treatment located in closed area that is surrounded by saturated vapor pressure line, curve obtained by parallel displacement of the saturated vapor pressure line by -1.5 kmole/m3 in ordinate axis direction, and line orthogonally crossing abscissa axis at point of 60 degrees C, density of 0 kmole/m3 and isobaric pressure of 1.7 MPa. INDEPENDENT CLAIMS are included for the following:    (1) method for preparing sugar, involves saccharifying the obtained raw material from the above-mentioned process using enzyme; and    (2) method for preparing ethanol, involves fermenting the above-mentioned sugar.
NOVELTY - Process for the destruction of organics in Bayer process stream (12) comprises: (a) Passing a volume of a Bayer process stream to a reactor vessel (24), which is provided with a population of a mixed bacterial culture; and (b) Retaining that volume of the Bayer process stream in the reactor vessel for a period of time during at least 10 mass.% as carbon of the organic compounds destroyed originate from non-oxalate organic compounds.    USE - The process is useful for the destruction of organics in a Bayer process stream (claimed).    ADVANTAGE - The process has improved performance.    DETAILED DESCRIPTION - DETAILED DESCRIPTION -Process for the destruction of organics in Bayer process stream (12) comprises: (a) Passing a volume of a Bayer process stream to a reactor vessel (24), which is provided with a population of a mixed bacterial culture; and (b) Retaining that volume of the Bayer process stream in the reactor vessel for a period of time during at least 10 mass.% as carbon of the organic compounds destroyed originate from non-oxalate organic compounds, where the mixed bacterial culture comprises a mixture of bacterial species capable of destroying organics, which has previously been adapted to the Bayer process stream, or a stream of substantially similar composition prior to introduction to the reactor vessel.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a process for the destruction of organics in Bayer process streams.    Bayer process stream (12)    Lake water (14)    Carbonator (16)    Carbon dioxide (18)    Reactor vessel. (24)
NOVELTY - The gas detector (300) has a dual etalon receiver (DUET) (305) to accept light (110) from a light source through gas. The light source and etalon have a bandwidth on the order of the absorption linewidth of gas. The transmission bandwidth of etalon is smaller than the bandwidth of light source. A first detector (130) senses light transmitted through the etalon. A second detector (140) senses light reflected from the etalon. A processor (250) determines quantity of gas based on detected transmitted and reflected light.    USE - Gas detector for atmospheric species detection.    ADVANTAGE - Gas detector has potential for high sensitivity over long range for remote detection of gases. Pointing and overlap issues are eliminated since the gas detector comprises a self-referencing receiver. Effect of frequency-induced noise sources are removed at the receiver by using a spectrally sensitive detector. Minimizes walk-off between incident beams and enables beams reflected from the etalon to be separated from the incident beams at an intermediate focus, while maintaining near-normal incidence on the etalon.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method of detecting gas. Uses include but are not limited to ammonia, carbon monoxide, hydrogen fluoride, hydrogen sulfide, hydrogen cyanide, acetylene, methane, benzene, hydrogen chloride, formaldehyde and hydrogen bromide.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of the optical setup for a dual-etalon geometry for the gas detector.    Light (110)    First detector (130)    Second detector (140)    Processor (250)    Gas detector (300)    DUET (305)
NOVELTY - Generating electricity, where a reformer produces hydrogen (H2) and carbon dioxide (CO2) from a hydrocarbon and water (H2O), where a photo-bioreactor (PBR) produces oxygen (O2) from at least one of the CO2 and carbonate, where at least a portion of the H2 and at least a portion of the O2 is burned in a combustion chamber in a hydrogen engine, where the hydrogen engine creates rotating mechanical energy, where at least a portion of the mechanical energy turns a generator, and where the generator creates electricity.    USE - The method is useful for generating electricity (claimed).    ADVANTAGE - The method is highly improved, efficiently generates electricity, and economical.
NOVELTY - The device is set with a marsh gas air extracting pump, a water-sealing device, a gas-water separator, a filter, a gas compressor, a cooler, an air reservoir, a methane concentration monitoring and warning device, a pressure regulating valve and a marsh gas power generation set. The marsh gas power generation set is connected with energy storage device.    USE - Household garbage landfill marsh gas power generation device used in small workshop.    ADVANTAGE - The organic solid waste can be recycled. The obtained methane can be purified or separated.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the household garbage landfill marsh gas power generation device.
NOVELTY - The system comprises a door such as a window, a chute (14) such as a conveyor belt, and a portable compost bin. One end of the chute is proximal to a portion of the door. The compost bin is configured to receive a compost material from the chute, and comprises a wire. The door has a pane. The chute is affixed to a door frame (11) and an exterior portion of a building.    USE - The system is useful for composting indoor organic waste such as a kitchen waste including vegetable waste, coffee grounds, paper waste or compostable materials, where the organic waste is useful as fertilizer.    ADVANTAGE - The convenient system allows users to bypass the inconvenience of collecting compost materials in a bucket or strainer for later transportation outdoors, and reduces trash.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of composting indoor organic waste.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic front elevational view of a door.    Fixed frame (11)    Gasket (12)    Latch (13)    Chute (14)    Handle. (15)
NOVELTY - The device has an air inlet device and an air outlet device that are respectively arranged at an upper part and a lower part of a gas inlet and a gas outlet of a low temperature plasma reaction chamber. The air outlet device is connected with a photochemical catalysis device and provided with a door. A gas inlet end and a gas outlet end of the air inlet device are provided with an aslant guide plate. The low temperature plasma reaction chamber is provided with a honeycomb vertical reaction chamber. Central position of a longitudinal corona is provided with independent reaction cavities.    USE - Waste gas treatment device.    ADVANTAGE - The device is simple in structure and convenient to install, protect and maintain, realizes large floor area, high balance air quantity flow rate and better treatment effect, and ensures better system security performance.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a waste gas treatment device.
NOVELTY - A mixing device comprises supplying device by screw and belt conveyers of components in batch mixer. Mixing process is accomplished in worm conveyor with working length not less than 8.0 m. Feeding of manure and dung is conducted by strip transporter, equipped with system of automatic control of supply.    USE - Device for mixing organic components for fermentation.
NOVELTY - Preparing compost involves piling composted mixture in fermenter with finished compost, aerobic enzyme and subsequent unloading, packaging the fermenter without the coverage on top with ready compost top layer and the lateral layers are placed inside the discharged weight, and continuing the fermentation in the upper and side layers.    USE - For preparing compost (claimed).
NOVELTY - The furnace has a flange (7) fixed with a compressing screw rod (8), and a sleeve (1) arranged between a bevel gear (2) and the flange. The bevel gear is fixedly connected with an upper end of a compressing screw rod (8). Another bevel gear (4) is fixedly connected with an end of a rocker shaft (6). The bevel gears are matched with each other. The latter bevel gear on the rocker shaft is installed at a rear part of a bearing (26). The bearing is fixed with a bearing seat on a furnace cover. An end of the rocker shaft is connected with a rocker (10).    USE - House-hold straw gasification furnace.    ADVANTAGE - The furnace improves transformation of each structure so as to ensure convenient house-hold straw gas stove operation and ideal stable effect. The furnace improves thermal efficiency, and lays foundation for automation.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a house-hold straw gasification furnace.    Sleeve (1)    Bevel gears (2, 4)    Rocker shaft (6)    Flange (7)    Compressing screw rod (8)    Rocker (10)    Bearing (26)
NOVELTY - The method involves carrying a cracking deoxidizing catalyst i.e. alumina-molecular sieve, under heating condition of a biological oil catalytic cracking process deoxidization reaction. The cracking deoxidizing catalyst is made of alumina, molecular sieve or mixture. A hydrodeoxygenation catalyst i.e. load type metal catalyst, is carried under the heating condition of a catalytic hydrodeoxygenation reaction. Dry gas is utilized in the cracking deoxidizing catalyst, where reactant mass ratio of the hydrodeoxygenation catalyst is 1:5-1:20.    USE - Method for preparing fuel from biological grease e.g. animal source, plant source and microorganism source.    ADVANTAGE - The method enables refining crude oil obtained by a fuel component so as to clean a biological oil raw material in an effective manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a fuel preparing method.'(Drawing includes non-English language text)'
NOVELTY - The method comprises cutting a garden fruit tree branch in a diameter of 15-20 cm using 20-30 cm long cutting saw, digging 100-150 cm long along a line of the tree with a width of 60 cm and a depth of 50 cm deep groove, applying straw and animal excrement ring mixing stack to the branch and then mixing by mechanical crusher, catalytically decomposing the straw and animal excrement ring mixing stack, and applying orchard with other farmyard manure. A content of the straw and animal excrement ring mixing stack is 100-310 wt.%.    USE - The method is useful for processing a surface for a fruit tree branch in the garden to provide the rich nutrition and energy for the growth and propagation of soil microorganism.    ADVANTAGE - The method is capable of efficiently cutting the garden fruit tree branch thus providing good ventilation, fertility ability and good living condition for the beneficial biological bacterium and propagation of environmental conditions, providing partial nitrogen-phosphorus-potassium and nutritious egg with enhanced microelement and promoting the fruit tree root growth.    DETAILED DESCRIPTION - The method comprises cutting a garden fruit tree branch in a diameter of 15-20 cm using 20-30 cm long cutting saw, digging 100-150 cm long along a line of the tree with a width of 60 cm and a depth of 50 cm deep groove, applying straw and animal excrement ring mixing stack to the branch and then mixing by mechanical crusher, catalytically decomposing the straw and animal excrement ring mixing stack, and applying orchard with other farmyard manure. A content of the straw and animal excrement ring mixing stack is 100-310 wt.%. The catalyst is calcined lime, or urea. A weight proportion of the branch with calcined lime is 100:3, a weight proportion of the branch and biogas slurry is 100:10, and a weight proportion of the branch and urrea is 100:3.
NOVELTY - By-products of ethanol, biodiesel and biogas processing method involves stillage processing of glycerol, soap water and condensate from evaporative drying. The obtained product is pretreated to decrease the degree of concentration of organic, inorganic and suspended solids. The pre-treated streams are mixed, treated and further processed by anaerobic and aerobic processes. Part of the aerobically treated effluent is recirculated from an anaerobic stage.    USE - Method for processing by-products of ethanol, biodiesel and biogas.
NOVELTY - The system has a forced dryer connected to an organic Rankin cycle apparatus (30) that is utilized for supplying a raw material (21). The Rankin cycle apparatus is connected with a cyclone part (23). The cyclone part passes through the forced dryer.    USE - Biomass synthetic gas middle low temperature waste-heat recovery electric power system.    ADVANTAGE - The system utilizes a gas reservoir that is equipped in a gas reformer, so that combustibility synthetic gas can be refined in an effective manner, and has high thermal efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass synthetic gas middle low temperature waste-heat recovery electric power system.    Raw material (21)    Cyclone part (23)    Organic Rankin cycle apparatus (30)
NOVELTY - The organic fertilizer comprises 65 wt.% of medicine dreg, 15 wt.% of livestock dung, 15 wt.% of corn, and 5 wt.% of wooden meal.    USE - Used as an organic fertilizer. No biological data given.    ADVANTAGE - The organic fertilizer can be easily, economically and safely prepared with high quality and improved efficiency in an environmentally friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for producing organic fertilizer.
NOVELTY - Vinasse volume reduction involves using potential energy of combustion gases that is generated from biomass combustion in boilers. The vinasse is processed with sugar and alcohol by total or partial thermal vaporization of water of composition.    USE - Method for reducing volume of vinasse (claimed).    ADVANTAGE - The vinasse volume reduction method enables to produce powder fertilizers.
NOVELTY - Refined clay is manufactured by freezing clay mineral dispersion liquid (1), dissolving frozen object (2), and separating clay mineral aggregate (5) from dissolved clay mineral dispersion liquid (3).    USE - A manufacturing method of refined clay for agrochemical base material, cosmetics, catalyst, and raw material for functional nanocomposite material.    ADVANTAGE - Mass consumption and expensive investment cost are unnecessary, practicability is high, clay is efficiently concentrated from aqueous dispersion of clay mineral, and energy saving is achieved.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) clay mineral dispersion-liquid frozen object containing frozen clay mineral dispersion liquid with aggregate of clay mineral particle formed inside; and    (2) refined clay manufacturing system comprising levigation part which disperses clay mineral to dispersion medium and levigates clay mineral, condensed part which concentrates clay mineral dispersion liquid obtained by process in levigation part, and freezing unit which makes possible the freezing treatment of clay mineral dispersion liquid.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of the manufacturing method of refined clay.    Clay mineral dispersion liquid (1)    Frozen object (2)    Dissolved clay mineral dispersion liquid (3)    Clay mineral aggregate (5)    Freezing process (P1)
NOVELTY - Filtering structure (200) comprises a filtering medium for removing impurities from gas produced by gasifying coal or biomass; and a catalyst (100) for converting methane and carbon dioxide into synthesis gas by a dry reforming reaction and a steam reforming reaction, where the filtering medium is coated with the catalyst.    USE - The filtering structure is useful: in a filtering unit; and in filtering method to remove dust from the gas mixture and convert methane and carbon dioxide into synthesis gas (all claimed).    ADVANTAGE - The filtering structure: performs both filtering function for removing impurities and function for converting hydrocarbons into synthesis gas, thus an additional process of separating and treating greenhouse gas, comprising carbon dioxide or methane, facilities for carrying out additional treatment are not required, thus reduces additional costs and increases the production yield of synthesis gas; reduces the discharge of carbon dioxide or methane, thus it is environment-friendly; and prevents energy loss attributable to the additional heat supply in subsequent processes to be conducted at high temperatures.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a filtering method, comprising: gasifying coal or biomass to obtain a gas mixture; removing nitrogen or sulfur from the gas mixture; and passing the gas mixture through the filtering structure to remove dust from the gas mixture and convert methane and carbon dioxide into synthesis gas by a dry reforming reaction and a steam reforming reaction.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic view showing a filtering structure coated with a catalyst for reforming synthesis gas.    Catalyst (100)    Filtering structure (200)
NOVELTY - Liquid energy source comprises 50-99% of fuel formed by one or multiple alcohols with four carbons, n-butanol, isobutanol, sec.-butanol or tert.-butanol. 0.5-5.0% of one or multiple additives are provided for increasing detonation of butanol by diethylene glycol dinitrate or tetraethylene glycol dinitrate or their mixture. 0.005-1.0% of one or multiple additives are provided for increasing lubricity of carboxylic acids mixture, amine and oleic acid-based mixed ethoxylated amine mixture, carboxylic acid ester mixture, amides mixture, polyethylene glycol or polypropylene glycol mixture.    USE - Liquid energy source for providing fuel for diesel cycle.    ADVANTAGE - The liquid energy source provides a substitute for diesel fuel in urban transport vehicles or plants in conventional manner, reduces carbon content in fossil cycle and replaces fossil fuels, and ensures reduced emissions of carbon compounds and cost.    DETAILED DESCRIPTION - Liquid energy source comprises 50-99% of fuel formed by one or multiple alcohols having four carbons, n-butanol, isobutanol, sec.-butanol or tert.-butanol. 0.5-5.0% of one or multiple additives are provided for increasing detonation of butanol by diethylene glycol dinitrate or tetraethylene glycol dinitrate or their mixture. 0.005-1.0% of one or multiple additives are provided for increasing lubricity of carboxylic acids mixture, amine and oleic acid-based mixed ethoxylated amine mixture, carboxylic acid ester mixture, amides mixture, polyethylene glycol or polypropylene glycol mixture. 0.0005-1.0% of a stabilizer additive selected from ethanolamine, diphenylamine, diphenylurea or morpholine, and 0.0005-1.0% of an additive selected from polyether or carboxylic acid amide, are also included.
NOVELTY - The method involves processing and recycling of urban sewage, rural sewage and industrial sewage with or without urban organic waste, rural organic waste, industrial organic waste, gases, pressurized biogas, organic sanitized matter, biomass, cleaned water and drinking water at high flow rates with quality control.    USE - Method for utilizing anaerobic digestion for degradation of organic materials.    ADVANTAGE - The method involves processing and recycling of urban sewage, rural sewage and industrial sewage, and hence enables to provide economic and eco-friendly process.
NOVELTY - A biological tar modified asphalt is prepared by removing fraction of biological tar at below 220 degrees C by heating method for collecting residue biological asphalt; dumping residue to container with stirrer so that temperature of the liquid biological asphalt is 90-110 degrees C; and adding latex asphalt modifier of chloroprene rubber, heating and stirring to obtain biological modified asphalt.    USE - Method for preparation of biological tar modified asphalt (claimed).    ADVANTAGE - The method makes full use of biological tar, thus solving problem of secondary pollution of biological tar in carbon gasification technology utilization of agricultural wastes. It turns waste into wealth for increasing economical benefit of carbon gasification technology utilization of agricultural wastes.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating a method for preparation of biological tar modified asphalt. (Drawing includes non-English language texts).
NOVELTY - Pretreatment system for food waste and wastewater, comprises anaerobic digester for processing food effluent, acid fermenter comprising scum separator for removing the scum, first stirring unit including a fiber and fat ingredient, hydrolysis tub including the second stirring unit for raising scum and flowing the sludge precipitated in the bottom surface of food and the food effluent processed at the acid fermenter, first heating unit for heating the hydrolysis tub, and remainder components for transferring liquid ingredient to the anaerobic digester for processing.    USE - The system is useful for pretreatment of food waste and wastewater.    ADVANTAGE - The system pretreats waste rapidly, and smoothly.    DETAILED DESCRIPTION - Pretreatment system for food waste and wastewater, comprises anaerobic digester for processing food effluent, acid fermenter comprising scum separator for removing the scum, first stirring unit including a fiber and fat ingredient which utilize a carbon dioxide generated by hydrolysis and acid fermentation of organic compound from food and food effluent, where the fermentation is carried out with acid and hydrogen gas for separating the fiber and fat ingredient and reducing or raising specific gravity of the separated products, hydrolysis tub including the second stirring unit for raising scum and flowing the sludge precipitated in the bottom surface of food and the food effluent processed at the acid fermenter, first heating unit for heating the hydrolysis tub at 75 degrees C such that the retention produces saponification in the hydrolysis tub, and remainder components for transferring liquid ingredient except scum and sludge to the anaerobic digester for processing.
NOVELTY - The method involves stabilizing dewatered sewage sludge from biogas plants. Biomass is mixed with absorbent selected from a group consisting of wood chips, straw, hay, sawdust and green waste. Initial moisture of a mixture is about 55 to 65 weight percentages. Aerobic fermentation is initiated by aerobic microorganisms in the sewage sludge for 3-4 weeks depending on climatic conditions. The Aerobic fermentation is controlled by forced aeration. Temperature of the mixture decreases from 70 to 40 degree Celsius. Humidity of the mixture is about 35 to 40 weight percentage.    USE - Method for preparing biofuel based on sewerage sludge and biomass by aerobic fermentation.
NOVELTY - Processing organic waste through vermiculture with earthworms Eisenia fetida, comprises mixing the organic waste simultaneously with the worms and Trichoderma asperellum MG-97 strain, in the form of spores and mycelium, or adding Trichoderma at an amount of 105-106 CFU/kg of the organic waste.    USE - The method is useful for processing organic waste through vermiculture with earthworm Eisenia fetida.
NOVELTY - Cosmetic composition comprises at least one zinc salt, at least one cationic polymer ( greater than or equal to 0.4 wt.%) and at least one propellant.    USE - As cosmetic composition which is used in the form of foam and for conditioning keratin fibers and protecting their artificial color; and in cosmetic process for treating keratin fibers (claimed).    ADVANTAGE - The cosmetic composition affords efficient and long-lasting protection of the color of keratin fibers against the degradation caused by light, ultraviolet radiation and/or repeated washing (fading of the color, modification of the initial shade), while at the same time giving the hair a good level of care and smoothness.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for cosmetic treatment process for treating keratin fibers involving applying the cosmetic composition to the keratin fibers, with or without (preferably without) subsequent rinsing.
NOVELTY - The device has an outer cylinder (4) that is fixedly provided with a heat insulation layer (9). The heat insulating layer is fixedly connected with the outer wall provided with a supporting roller (10). The heat insulating layer is fixed to the external driving device which is connected with a transmission gear (11) of the main heat conducting tube. A feeding port (8) of the housing (6) and the outer cylinder is provided with an axial which is composed of reinforced circular structure of a heat conducting pipe (7).    USE - Papermaking waste residue cracking device.    ADVANTAGE - The device has high mechanical strength, and has high heating efficiency. The safe and stable operation is obtained.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of papermaking waste residue cracking device.    Outer cylinder (4)    Housing (6)    Heat conducting pipe (7)    Feeding port (8)    Heat insulation layer (9)    Supporting roller (10)    Transmission gear (11)
NOVELTY - An artificial wetland comprises a wetland bed arranged in a cut-off wall, planted with wetland plant (4) and uniformly distributed with water distribution pipes and water collecting pipes. The wetland bed is equipped with a gas-guide tube and a horizontal pipe (8) connected with each other. The horizontal pipe extends in a microporous aeration pipe extending out of the wetland bed and being connected with an air compressor (3). The bottom of the wetland bed is provided with an impermeable layer.    USE - Artificial wetland for purifying sewage.    ADVANTAGE - The artificial wetland has strong oxygen supply compared with the existing technology, has reasonable design, and simple structure.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of artificial wetland.    Pipe film (1)    Air guide pipe (2)    Air compressor (3)    Wetland plant (4)    Water pipe (5)    Antiseepage wall (7)    Horizontal pipe (8)
NOVELTY - A biological oil hydrogenation method involves taking hydrogenation catalyst as raw material oil. The raw material oil and hydrogen pass through hydrogenation reactor, at low temperature operation followed by increasing at high temperature operation. Hydrogenation effluent from the reaction is separated into gas phase and liquid phase followed by passing into a fractionating tower. Naphtha, diesel oil and unconverted oil in the fractionating tower are fractionated. The diesel oil and/or un converted oil are recycled by the reaction system.    USE - Method for hydrogenating biological oil that is utilized for producing high-quality motor fuels.    ADVANTAGE - The method enables hydrogenating biological oil with improved storage stability and high industrial application value.    DETAILED DESCRIPTION - A biological oil hydrogenation method involves taking hydrogenation catalyst as raw material oil. The raw material oil and hydrogen pass through hydrogenation reactor, at low temperature operation followed by increasing at high temperature operation, where the active component of hydrogenation catalyst is reduced platinum and/or palladium. Hydrogenation effluent from the reaction is separated into gas phase and liquid phase followed by passing into a fractionating tower. Naphtha, diesel oil and unconverted oil in the fractionating tower are fractionated. The diesel oil and/or unconverted oil are recycled by the reaction system.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow chart illustrating a method for hydrogenating biological oil.'(Drawing includes non-English language text)'
NOVELTY - A biological grease hydrogenation method involves passing biological grease with hydrogen as reactant through noble metal catalyst bed layer comprising low content of hydrogenation active component followed by processing through catalyst bed layer comprising high content of hydrogenation active component. The obtained product is transferred to hydrogenation active component separator to obtain gas and liquid phases. The gas phase is recycled. The liquid phase is transferred to a fractionating tower to obtain naphtha, diesel oil and unconverted oil.    USE - Method for hydrogenating biological grease for producing motor fuel.    ADVANTAGE - The method enables hydrogenating biological oil motor fuel with high quality and better storage stability.    DETAILED DESCRIPTION - A biological grease hydrogenation method involves passing biological grease with hydrogen as reactant through noble metal catalyst bed layer comprising low content of hydrogenation active component followed by processing through catalyst bed layer comprising high content of hydrogenation active component. An obtained product is transferred to a hydrogenation active component separator to obtain gas and liquid phases. The gas phase is recycled. The liquid phase is transferred to a fractionating tower to obtain naphtha, diesel oil and unconverted oil, where the hydrogenation active components are reduced platinum and/or palladium and the diesel oil and/or unconverted oil is recycled to the reaction system, which prohibits entry of sulfur and nitrogen-containing material.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram illustrating a method for hydrogenating biological grease.'(Drawing includes non-English language text)'
NOVELTY - A biological grease hydrogenation method involves passing biological grease with hydrogen and active component of hydrogenation catalyst through two hydrogenation reactors performing at low temperature and high temperature, where active component is selected from tungsten, molybdenum, cobalt and nickel. The hydrogenated effluent is transferred into fractionating tower to obtain gas phase and liquid phase, where the gas phase is recycled, and the liquid phase is transferred to fractionating tower prohibiting sulfur-containing substances to maintain the recycle gas with hydrogen sulfide content.    USE - Method for hydrogenating biological grease for producing motor fuel.    ADVANTAGE - The method enables effectively improving storage stability of the biological grease.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram illustrating a method for hydrogenating biological grease.'(Drawing includes non-English language text)'
NOVELTY - Preparing the rhizoma curculiginis Chinese medicinal herb nutrient fertilizer, is claimed. The fertilizer comprises (in g): towel gourd powder (2000), balsam pear powder (3000), bamboo leaf powder (5000), hawthorn fruit powder (10000), bean cake powder (20000), peanut cake powder (20000), dried rabbit dung powder (20000), dung powder (20000), cow dung powder (15000), organic fertilizer powder (5000), potash powder (3000) and tangerine powder (2000).    USE - The method is useful for preparing the rhizoma curculiginis Chinese medicinal herb nutrient fertilizer.    ADVANTAGE - The method: produces nutrient fertilizer, utilizes simple material source; has a simple preparation process; can meet fast growth requirement of rhizoma curculiginis, and hence ensures sufficient fruit weight and drug content of leaf; increases the yield; prevents fertilizing for many times; and improves the disease resistance.
NOVELTY - The method comprises putting raw materials into a stirrer for 600 minutes, taking and then putting into a crusher into a powder, taking out the crushed powder into a fermenting tank and then tightly pressing and covering with a plastic cloth, and hermetically fermenting the powder for 90 hours. The raw materials comprise 10-16 wt.% of dried sheep-dung, 8-12 wt.% of dried rabbit dung, 12-16 wt.% of rapeseed cake powder, 6-8 wt.% of beanstalk powder, 10-12 wt.% of sesame powder, 4-8 wt.% of cotton seed shell powder, 2-6 wt.% of cabbage powder, and 2-6 wt.% of garlic powder.    USE - The method is useful for preparing fertilizer for planting and culturing Helwingia himalaica. No biological data given.    ADVANTAGE - The method is capable of economically and simply preparing the fertilizer for planting and culturing Helwingia himalaica with high quality.    DETAILED DESCRIPTION - The method comprises putting raw materials into a stirrer for 600 minutes, taking and then putting into a crusher into a powder, taking out the crushed powder into a fermenting tank and then tightly pressing and covering with a plastic cloth, and hermetically fermenting the powder for 90 hours. The raw materials comprise 10-16 wt.% of dried sheep-dung, 8-12 wt.% of dried rabbit dung, 12-16 wt.% of rapeseed cake powder, 6-8 wt.% of beanstalk powder, 10-12 wt.% of sesame powder, 4-8 wt.% of cotton seed shell powder, 2-6 wt.% of cabbage powder, 2-6 wt.% of garlic powder, 1-3 wt.% of pin needle powder, 1-3 wt.% of semen Cassia powder, 8-10 wt.% of tea seed cake powder, 2-4 wt.% of dried blood, 2-4 wt.% of radix Paeonia alba powder, 2-4 wt.% ginger powder, 2-4 wt.% safflower powder, and 2-4 wt.% Angelica powder.
NOVELTY - Manufacturing method for high concentration particle potassium fertilizer, involves reacting salt and alkaline matter to generate the colloidal compound; mixing the colloidal compound with potassium fertilizer raw material, bonding and granulating; drying, screening and cooling granulated product to obtain the particle potassium fertilizer.    USE - For manufacturing method for high concentration particle potassium fertilizer (claimed).    ADVANTAGE - The method provides simple operation technology, is low cost, big producing capability, smooth product particle and high strength, and there is no three wastes during the production process, it is energy saving and environment friendly, and the market prospect is very wide.
NOVELTY - Preparing compost for Herba Artemisiae Scopariae, involves mixing raw materials containing (wt.%): bean cake powder (22-28), dry rabbit's excreta (18-26), bamboo leaf powder (8-12), rhizome anemarrhenae powder (6-10), semen cassia powder (4-8), folium llicis latifoliae powder (4-8), radix gentianae powder (2-6), sophora alopecuroide powder (8-10), root of subprostrate sophora powder (4-8), and green fruit powder (2-6); pouring them into grinder to grind them into particle with 150 mesh; pouring them into grinder to stir for 90 minutes; adding water; piling up them in fermenting tank.    USE - For preparing compost for Herba Artemisiae Scopariae (claimed).    ADVANTAGE - The compost is cheap and easy to take; preparing method is simple; large amount of beneficial microorganism and the granule organic fertilizer can meet the need of capillary Artemisia growing; the artemisia compost is big and it grows quickly, which not only increases output but also overcomes the defects that capillary artemisia grows slowly and it is easy to get sick.    DETAILED DESCRIPTION - Preparing compost for Herba Artemisiae Scopariae, involves mixing raw materials containing (wt.%): bean cake powder (22-28), dry rabbit's excreta (18-26), bamboo leaf powder (8-12), rhizome anemarrhenae powder (6-10), semen cassia powder (4-8), folium llicis latifoliae powder (4-8), radix gentianae powder (2-6), sophora alopecuroide powder (8-10), root of subprostrate sophora powder (4-8), and green fruit powder (2-6); pouring them into grinder to grind them into particle with 150 mesh; pouring all of them into grinder to stir them for 90 minutes; adding water of 1:1.2 ratio to mix them uniformly; piling up them in fermenting tank; closing it tightly with plastic cloth; and obtaining the compost by fermenting for 60 hour.
NOVELTY - Bio-organic fertilizer comprises effective viable microbial cells (cfu) ( greater than or equal to 33 million/g (ml)), organic matter (based on dry weight) ( greater than or equal to 28%), nitrogen ( greater than or equal to 5%), water ( less than or equal to 20%), pH (5.5-7), faecal coliforms ( less than or equal to 100 /g(ml)), Ascaris eggs mortality rate ( greater than or equal to 90%) and validity period ( greater than or equal to 6 months).    USE - The bio-organic fertilizer is useful in agriculture and forestry production (claimed).    ADVANTAGE - The bio-organic fertilizer ensures the effects of a microbial fertilizer and an organic fertilizer, utilizes waste products, and protects the environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing the bio-organic fertilizer, comprising (i) preparing the materials to be biologically fermented, (ii) dividing the fertilizer in a flow divider, (iii) breaking, (iv) mixing in a mixer, (v) inoculating microbes, (vi) blending in a blender, and (vii) performing bio-fermentation.
NOVELTY - Application of biodiesel comprises adding transition metal salt on carrier, dipping isopyknic or excessively dipping, soaking for 1-5 hour, drying, roasting for 2 hours in muffle furnace at 300-700 degrees C to obtain slurry; with 5-25% molybdenum oxide or tungsten oxide and 1-10% nickel oxide as catalyst, infusing catalyst in diammonium phosphate or solution of rare earth salt, and drying to obtain slurry; and adding phosphorus oxide (1-10%) or lanthanum oxide (0.5-5%) and cerium oxide as multi-metal catalyst into reactor, and adding vegetable oil in reactor under hydrogen partial pressure.    USE - Method of application of biodiesel used for preparing vehicle fuel (claimed).    ADVANTAGE - The method avoids corrosion of hydrogen sulfide, environmental pollution and harm to human body, is simple and low cost, utilizing high raw material conversion rate, and has high product yield and good stability.    DETAILED DESCRIPTION - Application of biodiesel comprises adding transition metal salt on carrier, dipping isopyknic or excessively dipping, soaking for 1-5 hour, drying, roasting for 2 hours in muffle furnace at 300-700 degrees C to obtain slurry; with 5-25% molybdenum oxide or tungsten oxide and 1-10% nickel oxide as catalyst, infusing catalyst in diammonium phosphate or solution of rare earth salt, and drying 2-8 hours in muffle furnace at 300-700 degrees C to obtain slurry; and adding phosphorus oxide (1-10%) or lanthanum oxide (0.5-5%) and cerium oxide as multi-metal catalyst into reactor under 1-7 MPa, flow speed of 20-200 ml/minute, at 200-700 degrees C for 2-8 hours, and adding vegetable oil in reactor under hydrogen partial pressure of 1-7 MPa, ratio of 500-1500, airspeed of 0.5-5/hour, at 200-400 degrees C.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the application of biodiesel. (Drawing includes non-English language text)
NOVELTY - Preparing natural calcium-based porous solid alkali catalyst, comprises mixing the calcium and magnesium rich natural calcium base material powder comprising limestone and dolomite with 12-22C fatty acid to a mass ratio of 1:1.2-12, heating and stirring for 0.2-3 hours at 100-300 degrees C, then transferring into the crucible at 700-1000 degrees C for burning, and cooling and grinding to 100-120 meshes to obtain natural calcium-based porous solid alkali catalyst.    USE - The method is useful for preparing natural calcium-based porous solid alkali catalyst, which is useful for ester exchange reaction for producing biological diesel oil (claimed).    ADVANTAGE - The method is capable of economically preparing natural calcium-based porous solid alkali catalyst with high operability and catalytic conversion rate (93%) in a simple manner.
NOVELTY - A sewage treatment material comprises sulfur and limestone as main component, and microelement needed for growth of iron chloride hexahydrate (FeCl3.6H2O), copper sulfate heptahydrate (CuSO4.5H2O), potassium iodide (KI), manganese chloride tetrahydrate (MnCl2.4H2O), zinc sulfate heptahydrate (ZnSO4.7H2O), cobalt chloride hexahydrate (CoCl2.6H2O), boric acid (H3BO3), sodium manganate dihydrate (Na2MnO4.2H2O), or EDTA. Mass ratio of sulfur, limestone, microelement is 2x 106:1x 106: 3.693. Heat preservation time is 2-6 hours and reaction temperature is 220-260 degrees C.    USE - A sewage treatment material used in processing industrial wastewater with ammonia nitrogen in wastewater and domestic sewage (claimed).    ADVANTAGE - The material can effectively remove nitrate nitrogen in the water. It has no need of processing organic residue, low operation cost, simple operation, is convenient to manage, and economical.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for use of the sewage treatment material in processing the industrial wastewater with ammonia nitrogen in wastewater and domestic sewage.
NOVELTY - Producing lactic acid from restaurant-kitchen waste, comprises (i) adding bio-bacterial liquid including Bacillus licheniformis, Bacillus megaterium, Bacillus natto, Bacillus subtilis and Lactobacillus plantarum, and mixed enzyme preparation including amylase, cellulase, lipase protease, protease and pectinase to restaurant-kitchen waste; (ii) adding the kitchen waste with bio-bacteria liquid and enzyme preparation into a fermenter, and fermenting at 30-37 degrees C for 48-84 hours; and (iii) measuring the fermented liquid through a bio-sensor.    USE - The method is useful for producing lactic acid from restaurant-kitchen waste.    ADVANTAGE - This method is eco-friendly, and recycles the restaurant-kitchen waste.
NOVELTY - A dermal collagen fiber is prepared by utilizing secondary waste containing chromium of tanning. It is blue fibrous material, and has 18-25% water content, linear density of 1.2-2 dtex, length of 20-30 mm, rupture strength of 3.5 cN/tex, elongation at break of 10-30%, and moisture 6-10%. The naked eyes can see the impurity.    USE - A dermal collagen fiber used as high simulation leather (automobile seat leather, furniture leather, shoe leather, garment, shoes lining leather, belt leather, luggage leather), vacuum, carpet, wall paper, and leather fiber quilt (claimed).
NOVELTY - Micro-emulsified biodiesel comprises (%) biodiesel (86-93), EL-12 (RTM: emulsifying agent) (1-2), Span 80 (RTM: sorbitan monooleate) (1-2) and water (5-10).    USE - Micro-emulsified biodiesel.    ADVANTAGE - The biodiesel has low cost; and the micro-emulsified biodiesel is low in viscosity, good in stability and high in combustion rate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a preparation of micro-emulsified biodiesel comprising mixing (%) biodiesel (86-93), EL-12 (RTM: emulsifying agent) (1-2), Span 80 (RTM: sorbitan monooleate) (1-2) and water (5-10) uniformly, adding mixture to water and stirring materials to prepare micro-emulsified biodiesel.
NOVELTY - M15-M85 methanol diesel oil composition comprises (pts.wt.) GB diesel oil (20-40), methanol (30-85), and additive (0.1-5). The additive comprises cosolvent, cetane value improver, thermal value agent, anticorrosive agent, anti-swelling agent, seasonal adjustment agent, and other components (0.1-5).    USE - M15-M85 methanol diesel oil composition.    ADVANTAGE - The M15-M85 methanol diesel oil is environment friendly and energy saving.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for gas detonation by using explosive and space fuel to provide ideal measure for making up methanol deficit calorific value, such that raw material is nitric acid ester, nitrate, nitro-compound, non-aromatic compound, and peroxide.
NOVELTY - Producing biological water scavenging agent via microbial alternation chicken manure fermentation, comprises mixing fresh chicken manure (50-65%), Pleurotus eryngii bacterial bran (20-30%), and inorganic compound fertilizer (15-20%), and inoculating Aspergillus oryzae, Saccharomyces cerevisiae, photosynthetic bacteria and Bacillus subtilis in the mixture and stacking and fermenting for 15-20 days to obtain the final product.    USE - The method is useful for producing biological water scavenging agent via microbial alternation chicken manure fermentation.    ADVANTAGE - The method is capable of producing biological water scavenging agent with high nutrient material and high conversion rate, improved quality, reducing nitrite, ammonia nitrogen, hydrogen sulfide, fertilizer, and easy to digest.    DETAILED DESCRIPTION - Producing biological water scavenging agent via microbial alternation chicken manure fermentation, comprises mixing fresh chicken manure (50-65%), Pleurotus eryngii bacterial bran (20-30%), and inorganic compound fertilizer (15-20%), and inoculating Aspergillus oryzae, Saccharomyces cerevisiae, photosynthetic bacteria and Bacillus subtilis in the mixture for fermenting, where the effective microbial quantity after the fermentation is 3-4asterisk10 (8) colony forming units (CFU)/g, the inoculated strain can be Aspergillus oryzae ACCC30155 solid bacterial strain, Saccharomyces cerevisiae ACC20065 liquid bacterial strain, Bacillus subtilis ACCC10148 liquid bacterial strain, and photosynthetic bacteria ACCC10650 liquid bacterial strain, and the inoculating quantities of the Aspergillus oryzae (2-6 wt.%), the Saccharomyces cerevisiae, (1-2 wt.%), the Bacillus subtilis (1-2 wt.%) and the photosynthetic bacteria (1-2 wt.%), stacking and fermenting for 15-20 days to obtain the final product.
NOVELTY - Preparing 2-chloro-6-trichloromethyl pyridine (I) comprises: (a) introducing 2-methyl pyridine into a chlorination kettle (1) to chlorinate reaction; (b) introducing obtained product into a secondary chlorination kettle (2) and introducing chlorine, where the mass flow ratio of chlorine is 0.1-1 and the chlorination kettle temperature is 80-230 degrees C; introducing obtained product into a third chlorination kettle (3), and introducing chlorine; (d) introducing obtained product into a fourth chlorination kettle (4) and introducing chlorine; and (d) preparing crude (I).    USE - The process is useful for preparing 2-chloro-6-trichloromethyl pyridine, which is useful as pesticide intermediates and fertilizer. No biological data given.    ADVANTAGE - The process: is simple, inexpensive and eco-friendly; and provides (I) with high efficiency.    DETAILED DESCRIPTION - Preparing 2-chloro-6-trichloromethyl pyridine (I) comprises: (a) introducing 2-methyl pyridine into a chlorination kettle (1) to chlorinate reaction, where the mass flow ratio of pyridine and chlorine is 1:4-10 and the chlorination kettle temperature is 80-210 degrees C; (b) introducing obtained product into a secondary chlorination kettle (2) and introducing chlorine, where the mass flow ratio of chlorine is 0.1-1 and the chlorination kettle temperature is 80-230 degrees C; introducing obtained product into a third chlorination kettle (3), and introducing chlorine; (d) introducing obtained product into a fourth chlorination kettle (4) and introducing chlorine; and (d) preparing crude (I).    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of a process for preparing 2-chloro-6-trichloromethyl pyridine.    Chlorination kettle (1)    Second chlorination kettle (2)    Third chlorination kettle (3)    Fourth chlorination kettle (4)    Cooling well. (5)
NOVELTY - Extracting radix Tinospora lactone, comprises crushing radix Tinospora herb into 40-80 meshes, placing in an extraction kettle, infusing liquid carbon dioxide and a cosolvent at 20-30 l/hour flowing speed, extracting at 45-55 degrees C in 20-25 MPa extraction pressure for 2-3 hours, dialyzing to obtain an extracted liquor, recycling reagent from the extracted liquor using dry aluminum oxide, loading into a short column, eluting with ethanol solution (90-95%), concentrating eluate into a small volume, crystallizing, re-crystallizing crystal using ethanol solution, and drying.    USE - The method is useful for extracting radix Tinospora lactone.    ADVANTAGE - The method has high efficiency, short extraction period, and is environmental friendly and suitable for industrial production.
NOVELTY - Production of biogas, involves pre-processing raw materials, piling up the raw materials, adding Chinese medicinal residues (25-35 parts) into anaerobic reactor, adding biogas slurry (10-15 vol.%) (as inoculum) to the materials and adding water to the total solid (TS) material (7-9%) and performing anaerobic fermentation.    USE - The method is useful for producing biogas, organic fertilizer and liquid fertilizer (claimed).    ADVANTAGE - The method is simple as it doesn't use cow dung or other fermented raw materials for producing the biogas, enables utilization of the raw material effectively during the process, reduces environmental pollution by using medicinal residues and wastewater as raw materials.
NOVELTY - An aminosalicylic acid isoniazid preparing method involves dissolving p-aminosalicylic acid in water, and adding acid until pH value of the reaction mixture is 3-4.5. Non-water-soluble organic solvent is added. A water layer is removed. An organic layer is washed by using water. The organic layer is separated. Extracting solution is obtained. Different callose smoke is added in the extraction solution. The mixture is heated and stirred. The obtained mixture is cooled, crystallized and dried. The crystal is separated to obtain target product pamino salicylic different callose smoke.    USE - Method for preparing aminosalicylic acid isoniazid.    ADVANTAGE - The method enables preparing the aminosalicylic acid isoniazid in simple and environment-friendly condition of the recycled extraction solvent, thus saving the preparation cost of the acid isoniazid.
NOVELTY - A fuel forming method from crops straw by using production line involves processing raw material by crushing crops straw into filamentous, granulating resultant product, adding water and mixing completely. The obtained mixture is made to swell at 40 -60 degrees C, followed by compression molding the material completely under pressure to produce an adhesive material.    USE - Method for forming fuel i.e. utilized as coal substitute product, from crops straw by using production line    ADVANTAGE - The method enables forming fuel with high quality.
NOVELTY - The method involves connecting a gasification furnace (1) with a high temperature filter dust remover (3). Multiple tar collectors are connected with an air outlet of the high temperature filter dust remover. A gas air inlet pipe (21) is connected to a top part or bottom part of the gasification furnace. An air guide pipe (5) is connected with each tar collector for treating domestic rubbish. A bottom part of a coke collecting pool is provided with a coke discharging pipe. Temperature of the gasification furnace is 350-800 degrees C.    USE - Tar grading and collecting fixed bed biomass gasification method.    ADVANTAGE - The method enables realizing classification, collecting and eliminating of tar in an environment in a better manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a tar grading and collecting fixed bed biomass gasification device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a tar grading and collecting fixed bed biomass gasification method.    Gasification furnace (1)    High temperature filter dust remover (3)    Air guide pipe (5)    Gas air inlet pipe (21)
NOVELTY - Producing biofuel, comprises either: (a) producing a slurry comprising organic matter feedstock, water and oil, (b) treating the slurry in a reactor apparatus at 200-450 degrees C and a pressure of 180-350 bar, and (c) cooling the slurry and releasing the pressure thus providing a product comprising the biofuel; or treating organic matter with an oil-based solvent comprising less than 50 wt.% water at a temperature of 200-400 degrees C, and a pressure of 100-300 bar.    USE - The method is useful for producing biofuel (claimed) which is bio-oil, where the biofuel can be used as e.g. petroleum products.    ADVANTAGE - The method: provides biofuels with reduced oxygen content, increased hydrogen content, increased energy content and increased stability; and is cost effective.
NOVELTY - Vegetative soil composition comprises (in parts weight): sawdust (100), paper sludge (200), fermented livestock manure (500), food scrapped fermented compost (50), shell crushed material (10), granite soil (200), bamboo leaf tea fermented manure (20) and Paulownia leaf extract (5).    USE - The vegetative soil composition is useful for rearing and sprouting plants.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for planting method, which involves sprinkling the above-mentioned vegetative composition on soil.
NOVELTY - Biogas production process with two enzymatic pre-treatments, comprises: (a) providing a slurry of a lignocellulose- and pectin-containing material, water and at least one enzyme including pectate lyase, pectin lyase or pectin methylesterase; (b) allowing enzyme to catalyze the degradation of the material at a suitable temperature and a starting pH, where the pH drops to below 7 over time; (c) adding additional enzyme to catalyze the degradation of the material further at a suitable temperature and pH; and (d) adding enzyme-degraded material to a biogas digester tank to convert it to biogas.    USE - Used as biogas production process with two enzymatic pre-treatments.    ADVANTAGE - The process has higher conversion rate in the biogas digester tank, higher productivity/unit volume in the digester tank, lower investment in tank capacity, higher gas production/tank volume, more efficient conversion of the lignocellulosic-pectinaceous material at higher dry matter concentration, reduced amount of unconverted material in the purge, higher dry matter content in the unconverted solids, no requirement of post-converter or storage tank, and easy dewatering of unconverted material and cleaning of the gas phase.    DETAILED DESCRIPTION - Biogas production process with two enzymatic pre-treatments, comprises: (a) providing a slurry of a lignocellulose- and pectin-containing material, water and at least one enzyme including at least one pectate lyase, pectin lyase or pectin methylesterase; (b) allowing at least one enzyme to catalyze the degradation of the material at a suitable temperature and a starting pH, where the pH drops to below 7 over time; (c) adding at least one additional enzyme and allowing it to catalyze the degradation of the material further at a suitable temperature and pH; and (d) adding the enzyme-degraded material to a biogas digester tank at a suitable rate and ratio to convert it to biogas in the digester.
NOVELTY - Zeolite adsorbent material (I) comprises a mixture of zeolite X or LSX and zeolite exchanged by cations.    USE - (I) is useful: in adsorber, which is a radial adsorber; and for the purification or separation of a gas or a gas mixture, preferably air from impurities comprising carbon dioxide, ethylene, propane and nitrous oxide (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) adsorber comprising the adsorbent material;    (2) process-I for the purification or separation of a gas or a gas mixture comprising using a zeolite adsorbent material; and    (3) manufacturing (I) consisting of a mixture formed of particles consisting of crystals of X or LSX zeolite and zeolite X or LSX exchanged by calcium and barium cations agglomerated together, comprises (a) subjecting the X or LSX zeolite containing sodium and/or potassium cations to at least ion exchange by contacting with a solution containing calcium and/or barium ions, (b) optionally repeating step (a) up to the desired exchange rates for each of the barium and calcium cations, (c) recovering crystals of X or LSX zeolite exchanged with barium and calcium cations; (d) agglomerating the crystals of X or LSX zeolite exchanged with barium and calcium cations from step (c) and crystals of X or LSX zeolite to form agglomerated particles and (e) carrying out heat treatment and drying the particles.
NOVELTY - A fuel composition comprises fuel (91-98 vol.%) and biodiesel (2-9 vol.%). The fuel is liquefied petroleum gas or dimethyl ether. The biodiesel is fatty acid alkylester.    USE - Fuel composition for direct injection type internal combustion engine.    ADVANTAGE - The fuel consumption has favorable viscosity, reduces the generation of toxic gas and improves the lifetime of the internal combustion engine.
NOVELTY - The apparatus has a stirring reaction unit (10) for stirring and reacting the raw material and reaction solution. A turbulence reaction tube (31) is provided for delivering the sonochemical reaction raw material from the sonochemical reaction unit (20) by driving circulating pump (40) such that the turbulence reaction is made with the turbulence of the turbulence reaction tube.    USE - Biodiesel reaction apparatus in diesel engine.    ADVANTAGE - The productivity of biodiesel reaction apparatus can be improved with high reaction efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for esterification reaction method of biodiesel.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of biodiesel reaction apparatus.    Stirring reaction unit (10)    Reaction bath (11)    Sonochemical reaction unit (20)    Turbulence reaction tube (31)    Circulating pump (40)
NOVELTY - The device (100) has transfer conveyor (200) for transferring sample reduction ejected from sample reduction exhaust apparatus (150). A fuel forming unit (300) compresses sample reduction, molds and cuts into fixed size. A dryer (400) dries sample reduction.    USE - Solid fuel manufacturing device installed in gardening farmhouse and stockbreeding farmhouse.    ADVANTAGE - Greenhouse gas generation rate is reduced at low cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the solid fuel manufacturing device.    Solid fuel manufacturing device (100)    Sample reduction exhaust apparatus (150)    Transfer conveyor (200)    Fuel forming unit (300)    Dryer (400)
NOVELTY - A biomass fuel is manufactured using fallen leaves.    USE - Manufacture of biomass fuel.    ADVANTAGE - The method easily provides environmentally-friendly biomass fuel.
NOVELTY - Device for bio-fuel production, comprises heat-generator connected with a unit of drying-rushing through an air feeder which is clamped with gravitational conveyor of charging device of moist sawdust, where the unit of drying-rushing is connected with cyclone and a device of pressure of extending from cyclone dry product, through air feeder and dust fan, for separating dry product from humid air, and the complete devices are placed on one common mobile base.    USE - The device is useful in bio-fuel production.
NOVELTY - The device has an electrolyzer that is in the form of vertically placed cylinder that is filled with non-conducting material e.g. plastics through the bottom openings. The electrolyte based on potassium hydroxide is sucked in special pump from metallic pan by the hose connected with the electrolysis cells through bottom openings.    USE - Hydrogen processing device.
NOVELTY - The device is connected to electrolyzer which is provided with electrolysis of hydrogen and oxygen. A source of direct current is obtained through electrolysis of hydrogen and oxygen. The electrolyzer is placed on metal sheet with pallets. The end regions of electrolyzer are connected with anode and cathode terminals of power supply system. The electrolyzer is made of plastic material. The hydroxideions are removed from electrolyzer through opening formed in bottom pours of pallet. A hose is extended from a pump to electrolyzer. The quartz and ceramic tube are provided to heat electrolyte.    USE - Device for obtaining hydrogen by electrolysis of water.    ADVANTAGE - The power consumption of the device for obtaining hydrogen by electrolysis of water is improved effectively.
NOVELTY - Producing biodiesel involves adding glycerol in effluent, which is treated in a device. Mesophilic anaerobes and thermophilic anaerobes are also added with the effluent.    USE - Method for producing biodiesel and biogas from domestic and industrial wastewater (all claimed).
NOVELTY - Filter bed comprises a cement base which is provided with circle of partition wall forming a square. The upper part of the partition wall is set with a slant awning. The upper part of the filtering bed is provided with a slant feed pipe opening to the fermentation filter bed. The feed pipe is connected with a soft pipe. The outlet of the soft pipe is located on the fermentation filter bed. The partition wall is set with several material outlets, where the material outlet is set corresponding to the fermentation filter bed and opposite to the feed pipe.    USE - The filter bed is useful for performing biological fermentation of pig waste. The fermented waste is useful for producing organic fertilizer or fish fertilizer.    ADVANTAGE - The filter bed is convenient to use and is eco-friendly.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of the filter bed for biological fermentation of pig waste.
NOVELTY - Modular system has a containment unit (10) in which organic matter undergoes for anaerobic biological transformation. The containment unit has an opening (11), a collection pipe (20) and an extractor (21). The extractor is connected to the opening.    USE - Modular system for collecting gas and biogas from organic matter.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a modular system.    Containment unit (10)    Opening (11)    Collection pipe (20)    Extractor (21)
NOVELTY - The method involves filling biomass (3) in a bag (2). Temperature of the biomass is maintained at 37 degrees Celsius. The interspace between bags is filled with heated air. Gases are collected in an upper hose (5) and blown into a bottom hose (4). The biogas is removed from the bottom hose. The bottom hose is connected with a drive unit (12) via a connecting channel (11). The upper hose is connected with a biogas outlet (9). An outer bag (1) is processed with a heated air inlet (7).    USE - Method for preparing biogas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating preparation of biogas.    Outer bag (1)    Bag (2)    Biomass (3)    Bottom hose (4)    Upper hose (5)    Heated air inlet (7)    Biogas outlet (9)    Connecting channel (11)    Drive unit (12)
NOVELTY - Dry fermentation system comprises heating device for heating rice hulls.    USE - The dry fermentation system is useful for producing rice hull charcoal using rice hull.    ADVANTAGE - The rice hull charcoal produced by the dry fermentation system is environmentally-friendly.
NOVELTY - Method for decomposing lignin residue involves using microorganism.    USE - The method is useful for decomposing lignin residue for ethanol production (all claimed).    ADVANTAGE - The method improves production of bioethanol, cost-effectively and environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for degradation product of lignin residue, which is obtained by the above method.
NOVELTY - Alcohol is fermented by adding ground material of seed of Perilla frutescens to alcohol fermentation ingredient and fermenting to 28-32 degrees C.    USE - An alcohol fermenting method for alcohol fuel or alcoholic beverage.    ADVANTAGE - Fermentation ability of alcohol fermentation microorganisms, such as yeast, is increased, activity is increased, fermentation rate is improved, fermentation period is shortened, installation utilization efficiency and labor productivity are improved, cost reduction is achieved, and carbon dioxide gas generation is reduced.
NOVELTY - Degrading lignocellulosic biomass, involves (a) pretreating lignocellulosic biomass to obtain pretreated slurry, (b) separating slurry into part A and part B, (c) incorporating part A into raw growth medium to obtain final growth medium, and culturing at least one microorganism capable of producing at least one enzyme having cellulolytic or hemicellulolytic activity in final growth medium to obtain microorganism suspension, (d) processing the suspension, and (e) subjecting part B and product of step (d) to reactor for hydrolyzing biomass to obtain soluble sugars.    USE - The method is useful for degrading lignocellulosic biomass for producing ethanol (all claimed).    ADVANTAGE - The method has high selectivity and high productivity with respect to ethanol production, is cost-effective, and consumes less energy.    DETAILED DESCRIPTION - Method (M1) for degrading lignocellulosic biomass, involves (a) pretreating lignocellulosic biomass physico-chemically to obtain pretreated slurry, (b) separating the above pretreated slurry into part A and part B, (c) incorporating part A into raw growth medium to obtain final growth medium, and culturing at least one microorganism capable of producing at least one enzyme having cellulolytic or hemicellulolytic activity in final growth medium to obtain microorganism suspension comprising at least one enzyme, (d) processing the microorganism, and/or suspension, and (e) subjecting part B and product of step (d) to reactor for hydrolyzing biomass to obtain soluble sugars. An INDEPENDENT CLAIM is included for method (M2) of degrading pretreated lignocellulosic biomass, which involves performing above-mentioned steps (c)-(e) of method (M1).
NOVELTY - Livestock excrement treating device comprises dispersion tub (1) containing photosynthetic bacteria and Bacillus, storage tank (2) which stores the livestock excrement, fermentor (3) for fermenting the excrement aerobically, submerged membrane system (10) for treating the fermented product, where the system comprises carrier, and nanomembrane separation unit (11) for filtering the obtained product.    USE - The device is useful for treating livestock excrement (claimed).    ADVANTAGE - The device is cost-effective and environmentally-friendly and does not generate bad odor or gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for treating livestock excrement.    DESCRIPTION OF DRAWING(S) - The drawing shows perspective view of device.    Dispersion tub (1)    Storage tank (2)    Fermentor (3)    Submerged membrane system (10)    Nanomembrane separation unit (11)
NOVELTY - The invention relates to a process for recovering waste starch solutions resulting from food industry. According to the invention, the process consists in filtering the effluents, correcting the pH to 6 with sodium hydroxide solution, the resulting solution is dispersed and homogenized with cold water, then hot water is added while stirring, the solution is cooled down to the room temperature and the volume is brought to 1000 ml with distilled water, 0.2...0.3 g/l of calcium chloride are added to the formed starch gel, said gel is liquefied by the addition of Termamyl enzyme and heated further to a temperature of 105...108 degrees C, pH 4.5...5, with a primary liquefaction for 5...10 min at 98...105 degrees C, the saccharification takes place after adjusting the pH to 5.5...6 with phosphate buffer by adding, to 1 ml of suspension, 0.5...1 ml of enzymatic Dextrozyme GA preparation dilluted 1/250, while stirring at 60...80 degrees C for 48...72 h, afterwards the reaction is stopped by cooling, it is filtered, the content of the glucose syrup is analyzed, the content of glucose syrup is analyzed and retained on active carbon, thereby resulting the natural glucose sweetener.
NOVELTY - The apparatus has an electrolysis tank (10) that accommodates the water and is electrolyzed. A positive electrode portion (21) and negative electrode portion (22) produce a hydroxygen gas (HHO). The positive electrode portion and negative electrode portion are formed in surface of base material (30). The base material has titanium (Ti) and catalyst layer (31) has iridium (Ir).    USE - Combustion assistance apparatus for internal combustion engine of vehicle such as motor vehicle, boat and ship.    ADVANTAGE - Since the combustion of state is similar to complete combustion is realized, the fuel consumption of internal combustion engine can be improved efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the internal structure of electrolysis tank.    Electrolysis tank (10)    Positive electrode portion (21)    Negative electrode portion (22)    Base material (30)    Catalyst layer (31)
NOVELTY - The system has palette transport unit to move palette (53) into incubation room (70). The air conditioner (90) controls temperature and humidity according to angular domain of incubation room. The lighting device (100) controls lamp according to angular domain of incubation room. The larva recovery system (110) receives maggot breaking away from tray (40). The storage hopper (130) stores loading and dumping device (120) to allow transformed compost from tray. The empty tray and palette recovery system (140) move empty palette to feeder (50).    USE - Sample reduction compost system.    ADVANTAGE - The condition of temperature, humidity, lamp, and ventilation can be controlled effectively, thus realizing the environment control. The artificial culture system ensures the fast growth and activity of the larva.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the sample reduction compost system.    Tray (40)    Feeder (50)    Palette (53)    Incubation room (70)    Air conditioner (90)    Lighting device (100)    Larva recovery system (110)    Loading and dumping device (120)    Storage hopper (130)    Palette recovery system (140)
NOVELTY - The apparatus has feed port which supplies marine algae. A primary pressure maintenance unit is provided to maintain pressure within reactor in which marine algae is provided from the feed port. Catalyst storage for storing the catalyst is connected to the reactor. A secondary pressure maintenance unit is connected with the reactor to maintain pressure within the reactor during glycosylation reaction at pressure of 1-10 bar.    USE - Continuous conversion apparatus for marine algae biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the continuous conversion apparatus for marine algae biomass.
NOVELTY - The equipment has liquid heating device and liquid cooling device, which are arranged on emulsifying kettle. Liquid water soluble fertilizer dispersing and diluting kettle is connected to dispersing kettle provided with feed port and discharge port. A material conveying device is provided with vacuumizing device and material conveying pipe and connected with inner cavity of kettles. The vacuumizing device is connected with emulsifying kettle and dispersing kettle. The valves are arranged between material conveying pipe and emulsifying kettle or dispersing kettle.    USE - Water-soluble fertilizer production equipment.    ADVANTAGE - The liquid water-soluble fertilizer emulsifying, dispersing and stirring process can be performed at high speed. The quality of the produced product can be improved. The energy consumption can be reduced. The material is prevented from pollution. The production efficiency is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the water-soluble fertilizer production equipment.
NOVELTY - A solid waste processing device comprises a material dissolution tank; an absorption tank; a decolorizing kettle provided with filtration tank; a pyridine and bromine distillation kettle; a pyridine and bromine distillation extraction kettle outlet channel; pyridine and bromine distilling kettle residual channel connected with the distillation kettle; a liquid outlet channel; a water separator of distilling device; and a nitrogen unit separated from a negative pressure distilling device.    USE - Device used for processing solid waste containing pyridinium chloride, ammonium bromide and urea.    ADVANTAGE - The device has rational structure and simple operation, and can effectively reduce environmental problems.
NOVELTY - The extravasor has a lower conductor placed on a circular cross sectional part. The sectional part is arranged vertically and symmetrically inside a tank (A) along lengthwise direction. A central pipe is formed in a rectilinear shape and arranged symmetrically in the lower conductor. A lateral pipe (2B) is formed in rectilinear cross-section circular shape and horizontally arranged on a side of the central pipe. A funnel is arranged vertically and symmetrically on top part of the central pipe and slightly spaced vertically from an upper-side of the tank.    USE - Extravasor for use in a barrel-type digester that is utilized for obtaining biofertilizer.    ADVANTAGE - The extravasor ensures collection of lighter parts of waste and debris out of the tank. The extravasor is inexpensive, high in strength and resistance, safe and versatile to use, simple in structure, high in performance, reduced in size and weight, low in manufacturing cost, fast to operate, easy to handle, reduced in maintenance cost, and convenient to handle.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of an extravasor.    Tank (A)    Lateral pipe (2B)
NOVELTY - Production of granular organic fertilizer involves putting sludge in horizontal rotating drum fermentation device, in which barrel length is 12 m, inner diameter is 1 m, tube angle is 2 degrees degree and rotation speed is 0.03 revolution/minute, with natural ventilation according to different seasons (air humidity), forced ventilation and intermittent forced ventilation; fermenting for 5 days, in which barrel temperature reaches 55-75 degrees C and sludge water content is reduced from 66% to 45%; and extruding and granulating.    USE - Method for producing organic fertilizer (claimed).    ADVANTAGE - The method not only kills all kinds of worm eggs and pathogens, but also reduces sludge water content suitable for subsequent granulation process.
NOVELTY - Production of bioorganic fertilizer involves fermenting and producing microbial agent, adsorbing, and crushing; spray granulating lignin waste liquid; and adding lignin organic granules to granulator and rotating, adding microbial agent and uniformly spreading on surface of organic granules, spraying water or lignin waste liquid so that microbial agent is adsorbed on surface of organic granules to form microbial coating, and cold air-drying.    USE - Method for producing bioorganic fertilizer (claimed).    ADVANTAGE - The method ensures viable compound microbial fertilizer and improves fertilizer bioavailability.    DETAILED DESCRIPTION - Production of bioorganic fertilizer involves (A) fermenting and producing microbial agent (preferably Bacillus subtilis, B. megaterium and/or B. mucilaginosus), adsorbing on adsorption medium, and crushing to obtain microbial agent with total viable bacterial count of greater than or equal to 3x 108 cells/g; (B) spray granulating lignin waste liquid (preferably by-product of straw or wood papermaking process), and combining organic granules and solid powder; and (C) adding lignin organic granules to granulator and rotating, adding microbial agent (5-15% of microbial fertilizer weight) and uniformly spreading on surface of organic granules, spraying water or lignin waste liquid so that microbial agent is adsorbed on surface of organic granules to form microbial coating, cold air-drying, in which inlet drying temperature is 120-150 degrees C and material temperature in the drying barrel is less than or equal to 80 degrees C, and cooling, in which outlet temperature of cooling barrel is less than 35 degrees C. The grain size of bioorganic fertilizer is 1-4 mm. Organic raw material and nitrogenous, phosphate, potash and/or microelement fertilizer may be added to the spray granulation process.
NOVELTY - Microbial organic fertilizer from straw prepared by adding 95-99 parts by weight of decomposed organic matter with 1-5 parts by weight of Trichoderma fermentation liquor to prepare a Trichoderma fermentation product, adding 95-99 parts by weight of decomposed organic matter with 1-5 parts by weight of actinomycetes fermentation liquor to prepare an actinomycetes fermentation product and mixing the Trichoderma fermentation product and the actinomycetes fermentation product in a mass ratio of 0.5-1:0.5-1, where the water content is 20-22 wt.%, is claimed.    USE - The microbial organic fertilizer is useful to prevent plant diseases, pepper root rot disease, cotton blight and soil-borne diseases. No biological data given.    ADVANTAGE - The process is cost effective and increases the utilization rate of renewable energy sources.
NOVELTY - The separator has a raw material input pipe arranged on a bottom side of a separating cavity. The separating cavity is arranged in an outer cavity. An end of a waste solution output pipe is arranged on the bottom side of the separating cavity. An end of an exhaust pipe is arranged on a top side of the separating cavity. A condenser is arranged in the separating cavity. The condenser is provided with a liquid nitrogen input pipe and a nitrogen output pipe. A supporting plate is utilized for supporting a filler.    USE - Gas separator.    ADVANTAGE - The separator has wide application range. The separator is convenient to operate and use and simple in structure.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a gas separator.
NOVELTY - Recovering lipase for preparing biodiesel by enzymatic method, comprises taking a short chain alcohol (I) as a reaction acyl receptor, and free lipase as a catalyst to catalyze oil, reacting with short chain alcohol to obtain biodiesel, recovering free lipase by membrane complex separation, concentrating to aqueous phase after reaction with large aperture of coarse filtration membrane and collecting the filtrate, concentrating the filtrate with smaller aperture filter, and combining free lipase recovered after two processes.    USE - The method is useful for recovering lipase for preparing biodiesel by enzymatic method.    ADVANTAGE - The method: solves the problem of recovering free lipase; improves the production efficiency and prolongs the service life of the membrane; and shortens the enzyme recovery time, and reduces the recovery cost.    DETAILED DESCRIPTION - Recovering lipase for preparing biodiesel by enzymatic method, comprises taking a short chain alcohol (ROH) (I) as a reaction acyl receptor, and free lipase as a catalyst to catalyze oil, reacting with short chain alcohol to obtain biodiesel, recovering free lipase by membrane complex separation, concentrating to aqueous phase after reaction with large aperture of coarse filtration membrane and collecting the filtrate, concentrating the filtrate with smaller aperture filter, and combining free lipase recovered after two processes.    R = 1-5C alkyl.
NOVELTY - Producing pellet for roasting, involves selecting a raw material, crushing the raw material using crusher, drying the crushed raw material by natural or artificial drying method, pulverizing the dried raw material, cutting the pulverized raw material by maintaining temperature of molding device by mold-high-compressing through a dice, and transporting the raw material to the molding device.    USE - The method is useful for producing pellet for roasting (claimed).    ADVANTAGE - The method is environmentally-friendly.    DETAILED DESCRIPTION - Method for producing pellet for roasting, involves selecting a raw material, crushing the raw material into size of 10 mm or less using crusher, drying the crushed raw material for 7 days by natural or artificial drying method to maintain moisture content to 10-34%, pulverizing the dried raw material into size of 5 mm or less, cutting the pulverized raw material to have a thickness of 6 mm, and length of 2 cm in condition that water content is maintained to 0.8-0.9% by maintaining temperature of molding device at 30-80 degrees C by mold-high-compressing through a dice, and transporting the raw material to the molding device. An INDEPENDENT CLAIM is included for pellet prepared by above-mentioned method.
NOVELTY - A Ziziphus jujube mill rhizosphere accretion Bacillus subtilis (CGMCC 5318), is new.    USE - A Z. jujube mill rhizosphere accretion B. subtilis for preparing microbial liquid fertilizer (claimed).    ADVANTAGE - The Z. jujube mill rhizosphere accretion B. subtilis improves root system activity, increases content of the root system secretion, and has reinforced absorption and utilization capability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for use of Z. jujube mill rhizosphere accretion B. subtilis comprising cultivating Z. jujube mill rhizosphere accretion B. subtilis to obtain bacterial suspension (0.5x 108 to 1x 108 colony forming unit/ml), and inoculating the suspension to an organic fertilizer.
NOVELTY - Coal gas heating device containing methane, comprises a humidifier (2) connected with a steam pipeline (1) and a gas pipe (3), where an outlet of the humidifier is connected to a coal gas heater (4), and an outlet of the coal gas heater is connected to a coal gas connection pipeline (5). The coal gas connection pipeline is connected with an oxygen regulating device and an oxygen pipe.    USE - Useful as a coal gas heating device containing methane.    ADVANTAGE - The device: has simple structure; utilizes oxygen for partial oxidation to maintain temperature, and thus it reduces material requirements of coal gas heater and investment; and reduces fuel required for heating gas, and flue gas emission.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of the coal gas heating device containing methane (Drawing includes non-English language text).    Steam pipeline (1)    Humidifier (2)    Gas pipe (3)    Coal gas heater (4)    Coal gas connection pipeline (5)
NOVELTY - Preparing organic fertilizer, involves uniformly mixing traditional Chinese medicinal residue with animal manure or sludge in the weight ratio of 1:9-3:7, adding organic matter degrading inoculant of 0.1-0.5% of the weight of the mixture, uniformly mixing the contents and fermenting the mixture.    USE - The method is used for preparing organic fertilizer (claimed).    ADVANTAGE - The total content of nitrogen, and potassium oxide in the fertilizer is 5-9%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for organic fertilizer prepared by the above-mentioned method.
NOVELTY - A magnesium-based hydrogen storage material comprises (in %mass) rare-earth element (0.1-20) and magnesium metal (80-99.9). The rare-earth element is lanthanum, cerium, praseodymium, neodymium, samarium or erbium.    USE - Magnesium-based hydrogen storage material.    ADVANTAGE - The magnesium-based hydrogen storage material is efficiently prepared with excellent dynamic property.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of magnesium-based hydrogen storage material.
NOVELTY - Method for preparing heliotropin, involves (a) crushing Cynoglossum, and extracting the crushed material in extract kettle by supercritical carbon dioxide (CO2) extraction, and (b) subjecting the extract to chromatography using solvent system containing n-hexane, ethyl acetate, acetonitrile and water in a volume ratio of 3-6:4-9:4-8:1-3, obtaining the eluents, detecting the eluents in spectroscopy, concentrating the product, and drying the product at low temperature.    USE - The method is useful for preparing heliotropin.    ADVANTAGE - The method is highly specific, causes no pollution, has high separation efficiency, and produces high content of heliotropin.
NOVELTY - Gas water linkage system for treating municipal solid waste, is claimed.    USE - The system is useful for treating municipal solid waste (claimed).    ADVANTAGE - The system carries out hydrolysis of urban household waste, is ecofriendly, and recycles plastic materials.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for the use of spiral rotary machine, a vibration sieve, a crusher and an arc vibration sieve in treating municipal solid waste.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the gas water linkage system for treating municipal solid waste.
NOVELTY - Improving running effect of artificial wetland in winter comprises planting aquatic plant to be harvested easily in the artificial wetland; harvesting one part of the plant in winter for generating biogas through anaerobic fermentation; using the generated biogas as fuel to heat sewage near the root of the plant of the artificial wetland; after mixing the biogas liquid with the raw water of the artificial wetland, purifying through the artificial wetland; and preparing fermentation residue into organic fertilizer.    USE - Method for improving running effect of artificial wetland in winter.    ADVANTAGE - The method avoids the waste discharge and secondary pollution and has low construction investment, excellent processing effect, low running cost and easy management.    DETAILED DESCRIPTION - Improving running effect of artificial wetland in winter comprises:    (A) planting aquatic plant to be harvested easily in the artificial wetland, where the aquatic plant comprises water hyacinth, reed, and ryegrass;    (B) harvesting one part of the plant in the artificial wetland in winter for generating biogas through anaerobic fermentation;    (C) using the generated biogas as fuel to heat the sewage near the root of the plant of the artificial wetland so as to improve the purifying ability of the artificial wetland for the sewage;    (D) after mixing the biogas liquid with the raw water of the artificial wetland to be processed, purifying through the artificial wetland; and    (E) preparing the residue generated by fermentation into organic fertilizer through composting, and changing the waste into valuable.
NOVELTY - Purifying methane and co-producing calcium carbonate comprises adding calcium hydroxide solution into a reactor, passing methane through the bottom of the reactor, reacting to generate calcium carbonate and calcium sulfide mixture, passing the purified methane through the output at the top of the reactor, filtering the obtained calcium carbonate and calcium sulfide mixture through a filter to obtain white calcium carbonate and calcium sulfide filter cake and filtrate, reusing the filtrate for hydrogenation of calcium oxide, washing filter cake, drying and crushing to obtain calcium carbonate.    USE - The method is useful for purifying methane and co-producing calcium carbonate.    ADVANTAGE - The method: is simple in operation and convenient; absorbs carbon dioxide and hydrogen sulfide impurity in methane, hence improves the purity and quality of methane; recycles waste; produces a high yield of calcium carbonate; and improves the economic value of methane.    DETAILED DESCRIPTION - Purifying methane and co-producing calcium carbonate comprises: (a) adding calcium hydroxide solution into a reactor, passing methane through the bottom of the reactor at a flow rate of 200-240 m3/hour, regulating the reactor pressure at 1.2-1.8 MPa, where the mass ratio of carbon dioxide and the pure calcium hydroxide is 1:(1.48-1.88), reacting to generate calcium carbonate and calcium sulfide mixture, and passing the purified methane through the output at the top of the reactor, (b) filtering the obtained calcium carbonate and calcium sulfide mixture through a filter to obtain white calcium carbonate and calcium sulfide filter cake and filtrate, ignoring calcium sulfide in minimal quantities, and reusing the filtrate for hydrogenation of calcium oxide by adding into the reactor, and (c) washing the obtained filter cake through a washing machine, drying and crushing in a pulverizer to obtain the calcium carbonate product.
NOVELTY - A methane is generated by using blue-green algae as raw material; mixing the blue-green algae with water by breaking with pig manure, and using an Anaerobic Baffled Reactor (ABR) reactor; performing anaerobic digestion at middle temperature; collecting the methane via desulfite treatment; and taking the generated residue as fertilizer.    USE - Method for the generation of methane (claimed).    ADVANTAGE - The method obtains high methane yield and improves the value in use of the blue-green algae.
NOVELTY - Preparing glycosides, involves (a) crushing linden tree and extracting the material using saturated lime water for 2-3 times to obtain extraction liquid, (b) adsorbing the extraction liquid (pH 5-6) using macroporous resin and decompressing and recycling the extraction liquid using 6-8BV of ethanol to obtain concentrated liquid, (c) adding the concentrated liquid to polyamide resin column and eluting ethanol and filtering the liquid to obtain crude crystal, and (d) dissolving the obtained crystals in 2-3 times of ethanol, and drying the mixture to obtain product.    USE - The method is useful for preparing glycosides from linden tree.    ADVANTAGE - The method is simple and suitable for industrialization, and enables production of glycosides at high yield. The glycoside prepared by the method is cost-effective and environmentally-friendly.    DETAILED DESCRIPTION - Method of preparing glycosides, involves (a) crushing linden tree and extracting the material using 7-12 times of saturated lime water for 2-3 times to obtain extraction liquid, (b) adsorbing the extraction liquid (adjusting pH 5-6) using macroporous resin and decompressing and recycling the extraction liquid using 6-8BV of ethanol to obtain concentrated liquid, (c) adding the concentrated liquid to polyamide resin column and eluting ethanol and filtering the liquid to obtain crude crystal, and (d) dissolving the obtained crystals in 2-3 times of ethanol, and drying the mixture to obtain product.
NOVELTY - The solid mechanism firewood carbon rod comprises a main body (1), which is a cylindrical solid structure, where an outer surface of the main body is provided with grooves (2) that are present along an axial direction. The diameter of the main body is 50 mm.    USE - The solid mechanism firewood carbon rod is useful for producing solid charcoal.    ADVANTAGE - The solid mechanism firewood carbon rod can be simply manufactured with high efficiency and strength and good appearance.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a solid mechanism firewood carbon rod.    Main body (1)    Grooves. (2)
NOVELTY - The dryer has stirrer is formed within the drying room. The hot air distributor plate is provided with distribution holes. The inlet port supplies the waste into the drum. The hot air supplying duct supplies the hot air. The hot air guide element guides the hot air towards the inlet port.    USE - Dryer for solid waste fuelization.    ADVANTAGE - The drying efficiency is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the dryer for solid waste fuelization.
NOVELTY - The furnace has feeding opening and cracking gas outlet pipe (16) that are provided in upper cover. A cavity inside the top cover is communicated with a discharge opening of feeding device (1). A stirring power input shaft (15) is arranged in axis direction of cover, and is provided with a material distributor at the lower end of the discharge opening. The tail end of the input shaft is connected with a rotating shaft of spiral agitating retainer in micro-wave cracking furnace main portion. The discharge opening is provided with a discharge device (14).    USE - Micro-wave cracking furnace for garbage.    ADVANTAGE - The garbage treatment can be performed by the micro-wave cracking furnace efficiently. The speed of the micro-wave cracking furnace in performing garbage treatment process is increased. The structure of the micro-wave cracking furnace is simplified, thus the cost of the micro-wave cracking furnace is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the micro-wave cracking furnace.    Feeding device (1)    Micro-wave inlet (5)    Discharge device (14)    Stirring power input shaft (15)    Cracking gas outlet pipe (16)
NOVELTY - The furnace has a feeding system located in an inner wall of a furnace body. A dust removing system is arranged in an adjustable height tower-type eccentric rotating grate. An inner lifting screw thread shaft is connected with a rotating shaft of a control motor. An oxygen supply system is utilized for injecting oxygen to the furnace body. The oxygen supply system is provided with an air nozzle and an air compressor. The air nozzle is located in a top part of the furnace body. An air pre-heater is utilized to heat air while entering into the air nozzle.    USE - Biomass adjustable height grate gasification furnace.    ADVANTAGE - The furnace can improve gasification of raw material adaptability and stable output of gasification gas composition.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a biomass adjustable height grate gasification furnace.
NOVELTY - The furnace has a gasification furnace body provided with a feeding system and an oxygen supply system. The oxygen supply system injects oxygen into a throat at a top part of the furnace body. The oxygen supply system is provided with an air nozzle. An air compressor provides gas to the air nozzle. The air nozzle is located in the furnace body. The oxygen supply system is provided with an air pre-heater. A dust removing system is located at an inner wall of the furnace body. A grate is provided with a shaft and a control motor.    USE - Biomass grading oxygen supply gasification furnace.    ADVANTAGE - The furnace removes heat under environment with oxygen, reduces energy consumption and tar component utilization and increases generated gas phase products.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a gasification method for biomass grading oxygen supply.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a biomass grading oxygen supply gasification furnace.
NOVELTY - The method involves preparing the intermediate portion which joined each end of the several catalyst support carbon nanotube (12) with the ionomer (16) to the polymer electrolyte membrane (10). The other end coated ionomer which covers the surface of other end of the catalyst support carbon nanotube is removed among the ionomers after preparation of the intermediate portion. The other end of carbon nanotube is joined to gas diffusion layer after the removal of the other end coated ionomer.    USE - Manufacturing method of fuel cell.    ADVANTAGE - Since the other end of carbon nanotube is joined to gas diffusion layer after the removal of the other end coated ionomer, the electro-conductive fall between catalyst layer and gas diffusion layer can be suppressed. The fuel cell can be manufactured efefctively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fuel cell. (Drawing includes non-English language text)    Electrolyte membrane (10)    Carbon nanotube (12)    Platinum catalyst (14)    Ionomer (16)    Jig (18)
NOVELTY - Production of carbon dioxide and/or hydrogen gas streams comprises thermally treating feedstock material to produce syngas comprising carbon monoxide and hydrogen and plasma-treating syngas (5) in plasma treatment unit; reacting plasma-treated syngas with water in further treatment unit, with at least some of the carbon monoxide converted into carbon dioxide; and recovering hydrogen and/or, separately, carbon dioxide from the syngas.    USE - Method for production of carbon dioxide and/or hydrogen gas streams (claimed) used to treat waste feedstock.    ADVANTAGE - The method derives energy from waste product, and utilizes energy sufficiently.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) recovering oil and/or gas from oil and/or gas well comprising introducing recovered carbon dioxide into oil and/or gas well, displacing oil and/or gas from well, and recovering oil and/or from well;    (2) producing electricity comprising passing recovered hydrogen into hydrogen fuel cell and contacting hydrogen with a source of oxygen to generate electricity; and    (3) an apparatus comprising optional gasification unit for the gasification of a feedstock, plasma treatment unit in communication with gasification unit, and amine separation unit in fluid communication with plasma treatment unit.    DESCRIPTION OF DRAWING(S) - The drawing is a flow chart of the production of carbon dioxide and/or hydrogen gas streams.    Syngas (5)    Steam (10)    Process gas (15)    Carbon dioxide gas (25)    Hydrogen rich gas (40)
NOVELTY - The mold has a separator arranged between an upper mold and a lower mold. A molding material is injected through an inlet port and a runner. A fuel cell gasket is molded in top and bottom parts of the separator. A respective arranged phase is arranged in the top and bottom parts of the separator. A provisional chamber is arranged in the separator. A mobility rubber is injected through the inlet port to the provisional chamber. A side gate part is connected with the respective arranged phase. A lower side passage part is arranged in the separator.    USE - Injection mold for manufacturing a fuel cell gasket.    ADVANTAGE - The mold reduces unnecessary addition processing, separator turnaround time, requirement of composite material-type graphite material in the separator and manufacturing cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for molding a fuel cell gasket.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of an injection mold.
NOVELTY - Producing fuel comprises crushing, dosing and mixing the organic wastes including plant residues and liquid, warm heating the mixture, and fractionating the aged mixture in to two or more fractions, where crushing the plant residues in to 50-100 microns, mixing components with addition 5-65 wt.% of water, and repeated grinding of the obtained mixture to 20-50 microns for 30-300 hours.    USE - The method is useful for producing fuel.
NOVELTY - A hydrogen based fuel is made in the form of mixture of air and hydrocarbon inhibitor explosion, where the inhibitor is iso-butene.    USE - As a hydrogen based fuel (claimed).
NOVELTY - A biogas installation comprises reactor; fermentation unit(s) having input and output openings; and loading and unloading units. The units are connected via adapter and arranged under each other with the offset one relative to another so that the output opening of the preceding unit is connected with input opening of the following unit.    USE - Biogas installation for anaerobic fermentation of organic waste.
NOVELTY - A container fermentor comprises a multilayer insulation cover (1), waterproof and airproof door (9), and heating elements (6) on the internal sides, where on the top of an internal side is equipped with spray nozzles (11) connected to a container (4) and a control unit (3) connected to sensors (2) of parameters of fermentation placed inside the fermentor, where the fermentor includes at least one chamber (8) consisting of a frame, floor, side walls and a front wall which are filled in by a network.    USE - As a container fermentor used in biomass processing (claimed) such as a non-waste biomass processing.    ADVANTAGE - The container fermentor lies in its mobility and allows for biogas and fermented substrate production with assistance of biomass processing in an anaerobic environment; allows for a simple and a quick manipulation of a biomass during loading and unloading; and allows controlling the whole fermentation process.    DESCRIPTION OF DRAWING(S) - The figure shows a diagram of a fermentation container.    Multilayer insulation cover (1)    Sensors (2)    Control unit (3)    Container (4)    Heating elements (6)    Chamber (8)    Waterproof and airproof door (9)    Spray nozzles (11)
NOVELTY - A seawater desalination system (2S, 4S) comprises membrane bioreactor (MBR) (1) which transmits sewage and removes and cleans activated sludge, ultra filtration (UF) membrane (3) which transmits seawater and removes particles from seawater, 1st reverse osmosis (RO) membrane (2, 4) which produces drinking water (s2) while treated water (s22) is transmitted and salt content of treated water is contained in 1st concentrated water (s7) and removed, and stirring apparatus (5) where 1st concentrated water removed with 1st RO membrane and treated water transmitted by MBR are sent and stirred.    USE - A seawater desalination system (claimed).    ADVANTAGE - Drinking water can be produced from seawater, industrial water can be water-risen, and water-forming cost reduction is achieved.    DETAILED DESCRIPTION - A seawater desalination system (2S, 4S) comprises membrane bioreactor (MBR) (1) which transmits sewage and removes and cleans activated sludge, ultra filtration (UF) membrane (3) which transmits seawater and removes particles from seawater, 1st reverse osmosis (RO) membrane (2, 4) which produces drinking water (s2) while treated water (s22) is transmitted and salt content of treated water is contained in 1st concentrated water (s7) and removed, stirring apparatus (5) where 1st concentrated water removed with 1st RO membrane and treated water transmitted by MBR are sent and stirred, and 2nd RO membrane (6) which produces industrial water (s21) while liquid mixture stirred by stirring apparatus is transmitted and salt content is contained in 2nd concentrated water and removed.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a desalination system. (Drawing includes non-English language text).    MBR (1)    1st RO membrane (2, 4)    Seawater desalination system (2S, 4S)    UF membrane (3)    Stirring apparatus (5)
NOVELTY - Preparation of a material from biomass comprises (i) heating a reaction mixture comprising biomass, water and a base, and (ii) adding biomass to the reaction mixture and heating the reaction mixture to give a reaction mixture comprising the material.    USE - The process is useful for preparing material from biomass, where the material is coal or humic substance and the material useful as soil additive, ion binder or cement additive. The aqueous dispersion is useful as cement additive (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) the material obtainable by a process;    (2) a hydrothermal process-I for the disintegration of biomass, comprising heating the reaction mixture to result in an aqueous dispersion; and    (3) the aqueous dispersion obtainable by the process.
NOVELTY - A negative pressure separator comprises a sealed tank body (9), where an exhaust pipe (1) and a safety pipe (2) are arranged at the top of the body; one upper side of the body is provided with a feed pipe (3) fixedly connected with a mesh screen (7) in the tank, and the other side opposite to the feed pipe is equipped with a material filter (8) sleeved outside the mesh screen; one lower side of body is provided with a discharge pipe (4), the sealed tank below the discharge pipe is equipped with a filter screen (10) and a pipe of the discharge pipe is connected with a sewage pump (11).    USE - As negative pressure separator (claimed) for production of large methane projects.    ADVANTAGE - Using the separator, the negative pressure formed for the raw materials are subjected to the suction force of the sewage pump and the resistance of the filter so that the coarse material separation and saturated water adsorption can be quickly implemented, therefore, it solves the difficult problem that the straws are floated to form a crusting layer after entering an aerobic fermentation tank, and improves the methane yield and production efficiency of the large methane projects. The separator can be applied for large biogas engineering or sewage treatment engineering.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic diagram of the negative pressure separator.    Exhaust pipe (1)    Safety pipe; (2)    Feed pipe (3)    Discharge pipe (4)    Mesh screen (7)    Material filter (8)    Sealed tank body (9)
NOVELTY - Organic wastewater is treated by purifying organic wastewater in a wastewater aeration tank containing beneficial microorganism and liquid microbial active agent. The liquid microbial active agent can dissolve inorganic component and activate the beneficial microorganism in acid solvent to make the microorganism easy to absorb. Then, sludge is separated in a sludge separating device from drainage processed by the aeration tank and the sludge is circulated in the aeration tank.    USE - Method for treating organic wastewater (claimed).    ADVANTAGE - The method is suitable for purifying treatment of sewage or excrement, drainage from food factory and other organic wastewater by utilizing liquid microbial active agent which can form powerful microbiota.
NOVELTY - The system has dryer (300) that dries the crushed material by injecting hot air to hot wind generation furnace (200). A filter dust collector (820) is provided to remove the dust existing in dry distillation gas ejected through the deodorization unit from the heat exchanger (800). A lubricant supplying unit is provided with a delivery hose for supplying lubricant to boundary surface of main pivot and a lubricant receiving unit for accommodating the lubricant.    USE - System for disposing combustibility or organic waste.    ADVANTAGE - The efficiency of refuse treatment system is improved by recycling the generated heat in solid fuel manufacture. The fossil fuel is saved and the system can be used in environment-friendly manner.    DETAILED DESCRIPTION - A reservoir (400) is provided for storing dried crushed material. A molding unit (500) is successively provided with predetermined amount of calcium hydroxide from calcium hydroxide apparatus for supplied material stored in the reservoir and the solid fuel is produced. The dry distillation gas is supplied to the furnace by dust collector (600) and the foreign substance is removed. The dry distillation gas remained in furnace is supplied to deodorization unit (700) to heat the dust collector by combustion air. An INDEPENDENT CLAIM is included for method for disposing combustibility or organic waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the system for disposing combustibility or organic waste.    Hot wind generation furnace (200)    Dryer (300)    Reservoir (400)    Molding unit (500)    Dust collector (600)    Deodorization unit (700)    Heat exchanger (800)    Filter dust collector (820)
NOVELTY - Lutein extraction (100) comprises: (a) contacting silk fibers with many solvents to obtain a first solution, where the solvents comprise hexane, ethyl alcohol and ethyl acetate; (b) partitioning the first solution into a non-aqueous phase and an aqueous phase; (c) drying the non-aqueous phase to obtain dried residue; (d) dissolving the dried residue with at least one of the solvent to obtain a second solution; and (e) filtering (160) the second solution to obtain lutein extract.    USE - The method is useful for extracting lutein (claimed), which is useful in food supplements and pharmaceutical products.    ADVANTAGE - The method: can be conveniently carried out at ambient condition or at high temperature and pressure; utilizes the solvents that can be evaporated and recycled for multiple uses, thus it is environmental friendly and economical; and provides lutein with a purity level of greater than 95% and having high bioactivity and bioavailability in both retina cells and mice as compared to that of commercially available lutein ester.    DESCRIPTION OF DRAWING(S) - The figure shows a process flow diagram of the lutein extraction method.    Lutein extraction method (100)    Degumming silk cocoon (110)    Extracting first solution (120)    Obtaining aqueous phase (130)    Filtering second solution (160)
NOVELTY - The apparatus (10) has outer jacket (20) and inner jacket (30) in which rice hulls inlet port, hot air flow path, and hot air inlet port (32) and hot wind outlet are formed. A heating unit with multiple heating wires for igniting the rice hulls is installed at lower portion of outer jacket. The blower (70) is provided for supplying oxygen to lower portion of heating unit. An exhausting unit is installed in order to eject rice hull charcoal which is heated from heating unit.    USE - Apparatus for manufacturing chaff charcoal without energy.    ADVANTAGE - High-quality rice hull charcoal can be manufactured continuously since the heat loss in jacket is reduced.    DETAILED DESCRIPTION - A heat transfer pipe (40) is installed in outer jacket and is connected to inner jacket hot air inlet port. A hot-air blower (50) is connected with hot air inlet port of outer jacket.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the apparatus for manufacturing chaff charcoal.    Chaff charcoal manufacturing apparatus (10)    Outer jacket (20)    Inner jacket (30)    Hot air inlet port (32)    Heat transfer pipe (40)    Hot-air blower (50)    Blower for supplying oxygen to lower portion (70)
NOVELTY - A feedstock for biofuels production comprises: glycerides derived from an oleaginous microorganism; and less than or equal to 16C fatty acid chains (at least 10 wt.%).    USE - In biorefinery for biofuels production, where the biofuel comprises diesel, jet fuel (claimed) and blends with other biofuels and petroleum.    ADVANTAGE - The feedstock has a density below 940 kg/m3 at 15 degrees C. The biofuel obtained from hydroprocessing the feedstock has a cold-flow pour point of less than or equal to 20 degrees C, a cetane value of 50, and iodine value of less than or equal to 100. Due to the relatively short chain lengths in the glycerides, there is no need for the biorefinery to include any units for carrying out isomerization, or hydroisomerization, or catalytic isomerization, or a significant amount of isomerization.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) producing (M1) a biofuel involving hydroprocessing glycerides derived from an oleaginous microorganism and composed of less than or equal to 16C fatty acid chains (at least 10 wt.%) resulting in a biofuel having a cold-flow pour point of less than or equal to 20 degrees C;    (2) a biofuel produced according to the method (M1); and    (3) a biorefinery for producing a feedstock for biofuels production comprising a hydroprocessing unit for hydroprocessing glycerides derived from an oleaginous microorganism and composed of less than or equal to 16C fatty acid chains (at least 10 wt.%).
NOVELTY - Removing inorganic components from raw material for the production of clean materials, where raw material is biomass, coal, residues, wastes and/or sludge~s, comprises providing a salt, mixing water with the salt to produce an aqueous solution that contains salt and leaching the raw material with the aqueous solution that contains salt.    USE - The method is useful for removing inorganic components from raw material e.g. biomass, coal and/or residues, for the production of clean materials (claimed), where the inorganic components are potassium, sodium, chlorine, sulfur, phosphorus and heavy metals (copper, lead, zinc, chromium and mercury) from biomass of different origins, such as from agricultural, forest and/or urban origin, from low quality coals such as peat, lignite or sub-bituminous and/or bituminous coals, and from urban and/or industrial origin residues and wastes.    ADVANTAGE - The method: improves the properties of the treated material; minimizes gas emissions and corrosion and agglomeration problems that are caused during the thermo-chemical conversion of these specific materials; and minimizes or eliminates ash deposition; reduces/eliminates the greenhouse effect, hence eco-friendly and cost-effective.
NOVELTY - An optical semiconductor contains niobium oxynitride having baddeleyite-type crystal structure.    USE - Optical semiconductor is used for optical semiconductor device and photocatalyst for hydrogen generation device used in energy system (all claimed) e.g. light-emitting device, laser and solar cell.    ADVANTAGE - The optical semiconductor is manufactured efficiently and economically, by simple method.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of optical semiconductor;    (2) optical semiconductor device;    (3) photocatalyst;    (4) hydrogen generation device; and    (5) energy system.
NOVELTY - The system has solid oxide fuel cell (SOFC) (5) which electrolyzes water for generating the hydrogen supplied to the electric power generation function so as to produce electric power by using the hydrogen as fuel. The gas containing hydrogen and water vapor is circulated between hydrogen generator (1) and SOFC. The temperature sensor (7) controls the temperature of the portion which electrolyzes SOFC at the time of charge of the secondary battery type fuel cell system.    USE - Secondary battery type fuel cell system such as lithium battery type fuel cell system and nickel cadmium battery type fuel cell system used for portable electronic devices such as mobile telephone, portable information terminal, notebook-type personal computer, portable audio apparatus and portable visual apparatus.    ADVANTAGE - The decline in charge efficiency of the secondary battery type fuel cell system can be prevented at the time of charge.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of secondary battery type fuel cell system. (Drawing includes non-English language text)    Hydrogen generator (1)    Heater (2)    SOFC (5)    Temperature sensor (7)    Controller (9)
NOVELTY - The apparatus has desulfurization unit (2) with desulfurization catalyst (21) to desulfurize hydrogen containing fuel flowing into desulfurization duct (23,24). A heat exchanger is arranged so as to cover side of desulfurization unit, and is provided with heating medium duct to exchange heat between heating medium and desulfurization unit by making heating medium to flow after heating medium has recovered cell stack waste heat. The heat exchanger is formed so that direction of fluid flow of heating medium duct and direction of fluid flow of desulfurization duct form countercurrent.    USE - Desulfurizing apparatus for fuel cell system (claimed).    ADVANTAGE - Since the direction of fluid flow of heating medium duct and direction of fluid flow of desulfurization duct form countercurrent, thermal efficiency of the desulfurizing apparatus is improved and the desulfurization duct can retain heat in efficient manner.    DETAILED DESCRIPTION - The apparatus comprises a folding unit (25) that circulates hydrogen containing fuel from one side of fluid entrance (21a) to another side of the desulfurization duct. A baffle plate changing flow of fluid is arranged in the fluid entrance and the fluid exit (21b) inside the desulfurization duct. A baffle plate changes flow of fluid into the folding unit. The inner wall is arranged in the outer peripheral wall of the desulfurization duct. The radius and surface area of the desulfurization duct, and the predetermined catalyst amount accommodated in the desulfurization duct are set to minimum value. An INDEPENDENT CLAIM is included for fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the desulfurizing apparatus. (Drawing includes non-English language text)    Desulfurization unit (2)    Desulfurization catalyst (21)    Fluid entrance (21a)    Fluid exit (21b)    Desulfurization duct (23,24)    Folding unit (25)
NOVELTY - Fermentation method for producing alcohol, involves adding ground material of Japanese pepper (Zanthoxylum piperitum) to alcohol fermentation ingredient and carrying out fermentation reaction at 28-32 degrees C, where the ground material is ground material of Japanese pepper fruit skin and the addition amount of ground material (dry weight) is 0.0004-0.4 weight/volume% with respect to alcohol fermentation ingredient.    USE - The fermentation method is useful for producing alcohol (claimed), which is used as fuel and alcoholic beverage.    ADVANTAGE - The method efficiently produces alcohol even in high temperature conditions by reinforcing fermentation ability and maintaining activity of microorganism, improving fermentation speed and reducing fermentation duration, and thus saves energy resources and reduces cost by reducing electric power for cooling, and cooling resources, and does not require apparatus for temperature control. The amount of carbon dioxide emitted during the process is reduced significantly and hence global warming is prevented.
NOVELTY - Fermentation method for producing alcohol involves adding ground material of Japanese pepper (Zanthoxylum piperitum) to alcohol fermentation ingredient and fermenting at 33-40 degrees C, where the ground material is ground material of Japanese pepper fruit skin and the addition amount of ground material (dry weight) is 0.0004-0.4 weight/volume% with respect to alcohol fermentation ingredient.    USE - The fermentation method is useful for producing alcohol (claimed), which is used as fuel and alcoholic beverage.    ADVANTAGE - The method efficiently produces alcohol even in high temperature conditions by reinforcing fermentation ability and maintaining activity of microorganism, improving fermentation speed and reducing fermentation duration, and thus saves energy resources and reduces cost by reducing electric power for cooling, and cooling resources, and does not require apparatus for temperature control. The amount of carbon dioxide emitted during the process is reduced significantly and hence global warming is prevented.
NOVELTY - A imine group-containing compound (II) is reduced to obtain dihydroacridine compound (III). The dihydroacridine compound (III), and halogen or sulfonyl group-containing compound (IV) are reacted to obtain imine group-containing compound (V). The imine group-containing compound (V) is oxidized, to obtain azine type-compound (I).    USE - Manufacture of azine type-compound used in pharmaceuticals as a dye, fluorescent material, and labeling material for biomaterial.    ADVANTAGE - The azine type-compound having high purity is economically and efficiently manufactured with high yield, by simple method.    DETAILED DESCRIPTION - A imine group-containing compound of formula (II) is reduced to obtain dihydroacridine compound of formula (III). The dihydroacridine compound (III) and halogen or sulfonyl group-containing compound of formula: Z-L (IV) are reacted to obtain imine group-containing compound of formula (V). The imine group-containing compound (V) is oxidized, to obtain azine type-compound of formula (I).    R1-R7=H or substituent;    or R1+R2,R1+R4,R2+R3,R5+R6=5-membered, 6-membered or 7-membered ring;    X=-N(R8)-, -O-, -S- or -SO2-;    R8=H, alkyl, alkenyl, aryl or heterocyclic group;    Z=alkyl, alkenyl, aryl or heterocyclic group;    L=halo, -OSO2R9, or -SO2-R9;and    R9=alkyl, alkenyl or aryl.
NOVELTY - A desulfurization system (20) has fuel-supply unit (2) which supplies hydrocarbon fuel containing water and sulfur compound to a subsequent unit, and desulfurization unit (3) which desulfurizes the hydrocarbon fuel supplied from the fuel-supply unit using catalyst formed by supporting silver to zeolite-X. The content of water in the hydrocarbon fuel supplied by the fuel-supply unit is 0.2-0.4 volume%.    USE - Desulfurization system is used in hydrogen production system of fuel cell system for manufacturing hydrogen (all claimed).    ADVANTAGE - The desulfurization system efficiently desulfurizes fuel, by simple method.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) hydrogen production system (30);    (2) fuel cell system (1);    (3) desulfurization method of fuel; and    (4) manufacture of hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of fuel cell system.(Drawing includes non-English language text)    Fuel cell system (1)    Fuel supply unit (2)    Desulfurization unit (3)    Hydrogen-producing unit (4)    Desulfurization system (20)    Hydrogen production system (30)
NOVELTY - A desulfurization system (20) has fuel-supply unit (2) which supplies hydrocarbon fuel containing water and sulfur compound to a subsequent unit, and desulfurization unit (3) which desulfurizes the hydrocarbon fuel supplied from the fuel-supply unit using catalyst formed by supporting silver to zeolite-X, at 65-105 degrees C.    USE - Desulfurization system is used in hydrogen production system of fuel cell system for manufacturing hydrogen (all claimed).    ADVANTAGE - The desulfurization system efficiently desulfurizes fuel, by simple method.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) hydrogen production system (30);    (2) fuel cell system (1);    (3) desulfurization method of fuel; and    (4) manufacture of hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of fuel cell system. (Drawing includes non-English language text)    Fuel cell system (1)    Fuel supply unit (2)    Desulfurization unit (3)    Hydrogen-producing unit (4)    Desulfurization system (20)    Hydrogen production system (30)
NOVELTY - The electrolytic vessel has a coil cushion material (4) that is formed between a negative electrode and the conductive plate of a negative electrode chamber, and the cathode (3) is contacted with the ion-exchange membrane (5). The conductive plate is provided with a nonporous plate (2), and the expansion/contraction direction of the coil in the coil cushion material is positioned corresponding to the vertical direction of the electrolytic vessel.    USE - Ion-exchange-membrane-process electrolytic vessel used for brine electrolysis. Can also be used in potassium chloride aqueous electrolysis and alkaline water electrolysis.    ADVANTAGE - The coil cushion material is formed between the negative electrode and the conductive plate of the negative electrode chamber, so that the mesh of cathode and the adhesiveness of the ion-exchange membrane can be improved. Hence the voltage reduction effect can be exhibited. The energy of the electrolytic vessel can be saved effectively. The energy required for electrolysis of electrolysis industry low in long term-stable can be suppressed. The deformation of the cushioning material by the load of the pressure can be prevented using electrolytic vessel while preventing the damage of ion-exchange membrane.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial expanded sectional view of the ion-exchange-membrane-process electrolytic vessel. (Drawing includes non-English language text)    Partition (1)    Non-porous plate (2)    Cathode (3)    Coil cushioning material (4)    Ion-exchange membrane (5)
NOVELTY - The electrolytic vessel has an electrode supporting portion that is accommodated between a flexible cathode (5) and a current collecting plate (7). The electrode supporting portion is made from corrosion-resistant frames (9,13) which are covered and/or not covered by elastic mat. The flexible cathode and the electrode support portion are fixed to the current collector by a pin (8) that passes through the flexible negative electrode but does not pass through the space having the elastic mat of the electrode support portion.    USE - Ion-exchange-membrane-process electrolytic vessel used in electrolysis industry for performing chloro alkali electrolysis and brine electrolysis. Can also be used in performing potassium-chloride aqueous electrolysis and alkaline water electrolysis.    ADVANTAGE - Since electrode supporting portion is accommodated between flexible cathode and current collecting plate, the energy required for electrolysis can be reduced. Since the electrode supporting portion is made from corrosion-resistant frames, the damage of the electrolytic vessel can be prevented. The distance between the anode and cathode can be reduced and the required electrolytic voltage can be reduced. Long term-stable operation of the electrolytic vessel can be ensured and the performance of the electrode can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the electrolytic vessel.    Ion-exchange membrane (3)    Flexible cathode (5)    Current collecting plate (7)    Pin (8)    Corrosion-resistant frames (9,13)
NOVELTY - A primary methane synthesis reaction is carried out by mixing vapor with synthetic gas (EE) generated after fuel-gasification and dust-collection processes are performed. A water-gas shift reaction process is then carried out on a portion of the synthetic gas from the methane synthesis reaction, and the remaining gas is bypassed. The synthetic gas from the water-gas shift reaction process and the bypassed synthetic gas are remixed to perform a secondary methane synthesis reaction process, to obtain synthetic natural gas.    USE - Production of synthetic natural gas.    ADVANTAGE - The generation of heat during methane synthesis reaction is controlled.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus for producing synthetic natural gas, which comprises a saturation unit (1) which mixes the vapor with the synthetic gas, a primary methane synthesis reaction unit (2) which methanates the saturation gas generated from the saturation unit, a water-gas shift reaction unit (4) in which the water-gas shift reaction process is performed on the portion of the synthetic gas from the primary methane synthesis reaction unit, a bypass unit (5) which bypasses the remaining gas from the primary methane synthesis reaction unit which is not passed through the water-gas shift reaction unit, and a secondary methane synthesis reaction unit (7) in which the synthetic gas from the water-gas shift reaction unit and the synthetic gas of bypass unit are remixed to perform a secondary methane synthesis reaction process.    DESCRIPTION OF DRAWING(S) - The drawing shows a view explaining the manufacturing process of synthetic natural gas. (Drawing includes non-English language text)    Synthetic gas (EE)    Saturation unit (1)    Methane synthetic reaction units (2,7)    Water-gas shift reaction unit (4)    Bypass unit (5)
NOVELTY - Process for dehydrating a water-containing medium, where the medium is a pressurized gas having a pressure of at least 0.5 MPa, comprises contacting the water-containing medium with a dry ionic liquid choline salt to dehydrate the water-containing medium, and separating a dehydrated medium from the hydrated ionic liquid choline salt.    USE - The process is useful for dehydrating a water-containing medium comprising carbon dioxide (preferred), nitrous oxide, methane, ethane, ethylene propane, cyclopropane, propylene and/or butane (claimed). The dehydrated water-containing media is useful for the production of foodstuffs, beverages, nutritional formulations and pharmaceutical preparations.    ADVANTAGE - The ionic liquid cholines salts utilized in the process are very easily regenerated, surprisingly heat-stable, non-toxic and largely inert, hence the ionic liquid choline salts is suitable to dehydrated water-containing media that are subsequently employed in the production of foodstuffs, beverages, nutritional formulations and pharmaceutical preparations.
NOVELTY - The apparatus has fixed quantity discharger that is equipped in inner space of main structure. The screw is arranged in portion adjacent to the vent. Multiple discharging axes in which the pedal is formed, are included. The top air feeder and center air feeder are formed with horizontal direction. The reciprocating cylinder is provided for reciprocating shifter pipe in horizontal direction. The permeability of content around the discharging axis is secured by lower air feeder, so as to reduce the power resistance of discharging axis.    USE - Organic composting apparatus for producing high-quality compost.    ADVANTAGE - The dehydration solid material can be uniformly dispersed. Air can be smoothly supplied to the space of the content, thus effectively realizing the aerobic composting effect. The improvement of deagglomeration and permeability can be attained.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for organic composting method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the organic composting apparatus.
NOVELTY - The system has fermenter (10) whose ceiling (13) controls internal space which is formed in path (8) and generates bad smell gas. The depositing ceiling (20) is protruded in the ceiling and depositing ceiling light is irradiated in inside of transparent cover (22) and a side of depositing ceiling is connected. An air supplying unit (11) is formed in bottom surface of fermenter and sampled air is supplied from depositing hood (7) of path through air supply line (60) to air supplying unit.    USE - Livestock excretion composting system.    ADVANTAGE - The work environment of the compost depot can be improved. The bad smell of the path space is decreased and the vehicle working channel is maintained efficiently. The power required for collecting the bad smell is minimized. The mechanical life of the vehicle can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the livestock excretion compost system. (Drawing includes non-English language text)    Depositing hood (7)    Path (8)    Fermenter (10)    Air supplying unit (11)    Ceiling (13)    Depositing ceiling (20)    Transparent cover (22)    Air supply line (60)
NOVELTY - The invention relates to a strain of Bacillus subtilisUsa2, DSMZ deposit number 23654, for fighting the soil phytopathogenic agents, stimulating plant growth and for the controlled biodegradation of vegetable material within conservation agriculture exerting beneficial activities upon crops plants due to the protection activity against soil phytopathogenic fungi Fusarium graminearum, Alternaria spp, Botrytis cinerea, Sclerotinia sclerotiorum, Sclerotium cepivorum, Gaeumannomyces graminis, Phytium debaryanum, Verticillium dahliae, Rhizoctonia solani, Fusarium oxysporum f. sp. radicis-lycopersici, Sclerotium bataticola, for in-situ production of plant growth factors and the capacity of the controlled degradation of vegetable material while forming polyamines, compounds increasing the resistance to biotic and abiotic stresses. This beneficial actions are materialized by production increase in sunflower crops obtained in conservation agricultural system wherein the costs for using herbicides and performing the tillage are reduced.
NOVELTY - A methane fermentation tank comprises feeding and discharging pipes set on a lower part of a tank body at two corresponding sides of the tank body. The tank body is linked with a biogas residue processing device via the discharging pipe. It is mounted with a heating pipe connected between the tank body and a heating boiler. It is arranged with a thermometer. A mesh cage is equipped in the tank body.    USE - A methane fermentation tank.    ADVANTAGE - The fermenting temperature in the fermentation tank is ensured. The methane output is guaranteed. As the mesh cage is set on the tank body, the methane produced from the bottom of the tank body can raise along the mesh cage to ensure even gas production rate.    DETAILED DESCRIPTION - A methane fermentation tank comprises a tank body (1) with a feeding pipe (7), a discharge pipe (3), and an air outlet pipe (9). The feeding pipe and discharging pipe are set on the lower part of the tank body at two corresponding sides of the tank body. The tank is connected with a storage tank via the feeding pipe. The tank body is linked with a biogas residue processing device via the discharging pipe. A top of the tank body is installed with the air outlet connected between the tank body and the methane purifying device. The tank body is mounted with a heating pipe connected between the tank body and a heating boiler. It is arranged with a thermometer. A mesh cage is equipped in the tank body.    DESCRIPTION OF DRAWING(S) - The drawing is a sectional view of a methane fermentation tank.    Tank body (1)    Discharge pipe (3)    Feeding pipe (7)    Air outlet pipe (9)
NOVELTY - The plastic-steel biogas digester comprises a digester body (5). An outer wall of the digester body is constituted by an arc shaped plastic plate (1) and a galvanized sheet (2) from inside to outside. An outer part of the galvanized sheet is provided with an insulation board (3). An outer part of the insulation board is provided with a color plate (4).    USE - Used as a plastic-steel biogas digester.    ADVANTAGE - The plastic-steel biogas digester can be simply, rapidly and economically manufactured with improved corrosion resistance and long service life in an environmentally friendly manner, is capable of adopting reclaimed materials to produce arc plastic plate, and is convenient and rapid to install and transport.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a plastic-steel biogas digester.    Arc shaped plastic plate (1)    Galvanized sheet (2)    Insulation board (3)    Color plate (4)    Digester body. (5)
NOVELTY - The apparatus (A) has stirrers (61) arranged at an inner side of a main body (2). A water jacket is fixed with a heating unit. A cleansing water supply pipe (15) is arranged at an upper part of a process bath part (1). A blocking plate (14) is connected with a cylinder (14a). A dehumidification unit (4) is connected with the process bath part by a connection line. A side of the main body is connected with an air suction line part. An end of an air supply line part is connected with an intake unit (3). Another end of the air supply line part is connected with the air suction line part.    USE - Food waste fermentation treatment apparatus.    ADVANTAGE - The apparatus removes moisture at the inner side of the process bath part by the dehumidification unit, maintains constant thickness and temperature of internal space of the process bath part, raises fermentation process efficiency and enhances marketability of a food waste fermentation processor.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a food waste fermentation treatment apparatus.    Food waste fermentation treatment apparatus (A)    Process bath part (1)    Main body (2)    Intake unit (3)    Dehumidification unit (4)    Blocking plate (14)    Cylinder (14a)    Cleansing water supply pipe (15)    Stirrers (61)
NOVELTY - The fermentation and drying device has a fermentation unit (110) that is heated by a heating line (116), an internal space that is divided by a partition wall (114) and an inlet port (101). Multiple exhaust holes (132) are provided in fermentation unit main body (100). The fermentation unit main body is equipped with an exhaust pipe (130).    USE - Fermentation and drying device for edible waste material.    ADVANTAGE - The fermentation and drying device has a fermentation unit that is heated by a heating line, an internal space that is divided by a partition wall and an inlet port, and hence ensures efficient fermentation and drying device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a fermentation and drying device.    Fermentation unit main body (100)    Inlet port (101)    Fermentation unit (110)    Partition wall (114)    Heating line (116)    Exhaust pipe (130)    Exhaust holes (132)
NOVELTY - The system has multiple multi-stage cyclone devices fixed with a cyclone exhaust part. A cyclone inlet is provided with an inlet connection line that is connected with a vent. A connection hole is formed in a lateral part of a cyclone body. A connection air-outlet is fixed in a top of the connection hole and connected with the cyclone body. The inlet connection line and a transferring apparatus are connected with a cyclone connection line to pump bio-gas. An absorption liquid mixture apparatus is fixed in an inner side of the cyclone body.    USE - Bio-gas preprocessing system.    ADVANTAGE - The system is simple in structure, easy to maintain and inexpensive. The system enables easily removing impurities in the bio gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a bio-gas preprocessing system.'(Drawing includes non-English language text)'
NOVELTY - A mutant Chlorella vulgaris strain CV-18 (KCTC 11776BP), is new.    USE - The mutant C.vulgaris strain CV-18 is useful for producing biodiesel, lipid and fatty acid (claimed).    ADVANTAGE - The mutant Scenedesmus sp. strain M003 enables mass production of biodiesel, and has rapid proliferation rate. The method is environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of biodiesel, which involves culturing the mutant C.vulgaris strain CV-18, and then separating out lipid, fatty acid and biodiesel from the culture.
NOVELTY - Method of cultivating Chlorella vulgaris 16 (KCTC 11775BP) involves cultivating Chlorella vulgaris and inducing mutation using ethyl methanesulfonate (EMS).    USE - The method is useful for cultivating Chlorella vulgaris 16 (KCTC 11775BP) which is useful for producing biodiesel (claimed).    ADVANTAGE - The method increases the cell growth rate, enhances carbon dioxide fixation due to fast outgrowth, enables high biomass productivity and produces environmentally-friendly fuel.
NOVELTY - A mutant Scenedesmus sp. strain M003 (KCTC 11778BP), is new.    USE - The mutant Scenedesmus sp. strain M003 is useful for producing biodiesel, lipid and fatty acid (claimed).    ADVANTAGE - The mutant Scenedesmus sp. strain M003 enables mass production of biodiesel, and has rapid proliferation rate. The method is environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of biodiesel, which involves culturing the mutant Scenedesmus sp. strain M003, and then separating out lipid, fatty acid and biodiesel from the culture.
NOVELTY - A mutant Scenedesmus sp. strain M001 (KCTC 11777BP), is new.    USE - The mutant Scenedesmus sp. strain M001 is useful for producing biodiesel, lipid and fatty acid (claimed).    ADVANTAGE - The mutant Scenedesmus sp. strain M001 enables mass production of biodiesel, and has rapid proliferation rate. The method is environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of biodiesel, which involves culturing the mutant Scenedesmus sp. strain M001, and then separating out lipid, fatty acid and biodiesel from the culture.
NOVELTY - A cattle excretion compost has controlled moisture content by subjecting sample including fowl droppings, pig ordure and cow dung to reduction process.    USE - Cattle excretion compost.    ADVANTAGE - The cattle excretion compost is eco-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for manufacturing cattle excretion compost.
NOVELTY - A Ralstonia strain (CS274 strains, accession number KCTC 18201p, 2010.11.15) having 16S ribosomal RNA gene base sequence of SEQ ID NO. 1 (having a defined sequence of 1505 base pair, given in the specification) is new, where the strain is generated from a lipase enzyme using gel electrophoresis, the enzyme has molecular weight of 31 kDa, optimum pH of the enzyme is 8-9 or 8-11, and optimum activity temperature of the enzyme is 45-55 degrees C and the presence of calcium ion (Ca2+) and magnesium ion (Mg2+) increases the lipase activity of the enzyme.    USE - Ralstonia strain (CS274 strains, accession number KCTC 18201p, 2010.11.15) for producing biodiesel.
NOVELTY - The plant has a culture portion provided with a water tub. A blade is installed at a rotary shaft. Another blade is installed at an end of the former blade. A rotary motor rotates the rotary shaft. An aberration control unit controls an operation of the rotary motor. An aberration part is connected to a supporting member. A light emitting part is installed at the blades and the rotary shaft and surrounded by a water-proof material. Light is sent to fluid stored in a water tub body (210). A partition wall is protruded in an inner side of the water tub along upper direction.    USE - Microalgae biofuel manufacturing plant.    ADVANTAGE - The plant can easily control a growth condition, maintain culturing temperature and improve growth of microalgae.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a microalgae biofuel manufacturing plant.'(Drawing includes non-English language text)'    Water tub body (210)
NOVELTY - The tank has a culture portion preparing fluid in different locations. A fluid flow part supplies oxygen to the fluid. A supporting member is provided with a rotary shaft that is fixed at the culture portion. Multiple blades are arranged on a board, which is arranged in circumference of the rotary shaft. A rotary motor is connected to the rotary shaft. A fluid flow part control unit controls operation of the rotary motor. A storage part is arranged in a sidewall of the culture portion for storing the fluid. A supporting frame is arranged among the rotary shaft and the blades.    USE - Bio-fuel manufacturing massive culturing tank for a micro-algae massive multiplying apparatus (claimed).    ADVANTAGE - The tank is inexpensive and easy to maintain. The tank massively increases bio-fuel production efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a micro-algae massive multiplying apparatus comprising a boiler.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a bio-fuel manufacturing massive culturing tank.
NOVELTY - Selenium-enriched watermelon, produced under routine management of cultivation conditions, comprising performing foliar-spraying (3-5 times at once) of a selenium-enriched biological agent (each time 100 ml) on watermelon in every 6-8 days after 5 days of watermelon pollination to obtain selenium-enriched watermelon fruit, is claimed.    USE - The selenium-enriched watermelon is useful for improving selenium level in people, and preventing and treating diseases.    ADVANTAGE - The selenium-enriched watermelon: transforms inorganic selenium into organic selenium; overcomes the problem of environmental pollution caused by traditional method of directly adding sodium selenite and inorganic selenium; ensures pollution-free selenium-enriched agricultural products with sustainable development; and has effectively improved selenium content, where the fresh juice contains selenium content of up to 0.39-0.41 mg/kg.
NOVELTY - A plant promoting agent carrier matrix is prepared by treating leaf straw (7.29% in shade) at 60-80 degrees C, or drying in shade with the water mass content in leaf of crop straw, and crushing leaf with straw, where aperture is 0.02-0.2 mm; putting sieved straw powder with 60-100 degrees C water, or sieved straw powder with 35-100 degrees C water at 250-2000 W of microwave radiation auxiliary and extracting for 5-50 minutes; neutralizing, leaching and filtering, and adjusting pH to 6.7-7.3; and drying filtrate to water content of less than 7.2% and sterilizing to obtain plant promoting agent carrier matrix.    USE - Method for preparing plant promoting agent carrier matrix (claimed).    ADVANTAGE - The method is simple, has environment-friendly pollution-free raw material, and is convenient to use.
NOVELTY - A Nitzschia cf. pusilla strain having 28s recombinant DNA gene sequence of SEQ ID NO. 1 (having a defined sequence of 776 base pair, given in the specification) is new.    USE - Nitzschia cf. pusilla strain for biodiesel production (claimed).    ADVANTAGE - The strain improves production rate and quality of biodiesel.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a composition for biodiesel production, comprising strain and/or culture material of the strain    (2) a method for manufacturing biodiesel, which involves utilizing the strain as a supply source of lipid    (3) a method for treating sewage, which involves cultivating the strain and/or culture material of the strain    (4) a strain culture method, which involves cultivating sewage in a culture medium comprising potassium dihydrogen phosphate, calcium chloride dihydrate, magnesium sulfate heptahydrate, sodium nitrate, dipotassium phosphate, sodium chloride and boric acid with a strain and trace element.
NOVELTY - Oil-rich Nitzschia closterium BC6 (I) under a preservation number of CGMCC No.3747 in a China general microbiological culture collection centre, is new.    USE - (I) is useful for preparing oil, which is useful for preparing biodiesel (claimed).    ADVANTAGE - (I) provides rich oil. The algal cells used in (I) are rapid in growth, high in specific growth rate, high in cell density, and high in oil content of 65%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of (I).
NOVELTY - Organic seaweed fertilizer is obtained by composting and performing micro-aerobic fermentation of industrial seaweed residue or mixture of seaweed residue and at least one chosen from wheat bran, straw, residue of traditional Chinese medicine, fruit residue, activated sludge and lees particles.    USE - The organic seaweed fertilizer is useful as plant growth regulator and basal or top dressing for cultivation of crops in soil, cultivating plants and other seedling of fruit plants in laboratory application (claimed).    ADVANTAGE - The organic seaweed fertilizer is cost-effective and environmentally-friendly as it contains natural active ingredients and other raw materials from recycling waste and has rapid effect on crops.
NOVELTY - Synthesis of gamma aminobutyric acid (I) comprises ring opening reaction of polyvinylpyrrolidone aqueous solution in a presence of solid alkali as catalyst to obtain reaction liquid, filtering the reaction liquid, concentrating the gamma-aminobutyric acid solution, cooling, crystallizing and drying.    USE - (I) is useful: in medicine, health food, baked food and food ingredients; as capsule, oral liquid, powder, syrup, drink, bread, biscuit, chocolate and sugar product; and as antihypertensive agent and anticonvulsant agent; and for promoting urination. No biological data given.    ADVANTAGE - The process is simple, cost effective for preparing (I) with good yield (94%) and purity (greater than 99%) shortens reaction time and synthesizes the one step method; and does not produce pollution to damage environment so as to reflect clean production.
NOVELTY - Decoloration pretreatment system of acetaminophen comprises a material transportation device and a pulping tank (40). The material transportation device is used for transporting the crude acetaminophen which is obtained by centrifugating the material obtained by acylation crystallization to the pulping tank in sealed environment, pulping the crude acetaminophen and water in the pulping tank, transporting the mixture containing crude acetaminophen and water after pulping in the pulping tank to a decolorization tank (50) and decolorizing.    USE - Used as a decoloration pretreatment system of acetaminophen.    ADVANTAGE - The system acquires clean production requirement; prevents cross pollution, and meets requirement of current good manufacturing practices (cgmp) authentication; improves decoloration effect of decoloration treatment; and accelerates production speed and improves product quality.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the decoloration pretreatment system of acetaminophen.    Sealed material chamber (20)    Material transportation device (30)    Pulping tank (40)    Decolorization tank (50)
NOVELTY - The method involves removing water from a fermentation residue. A chemical treatment is performed to the dewatered fermentation residue by adding an additive. The treated fermentation residue is dried by action of air with temperature range of 60 to 190 degree Celsius and performing stripping process. The stripping process is performed for production of substrates for culturing a wide spectrum of plants. The substrates are replaced by products of peat moss, bark, compost or other organic materials.    USE - Process for producing cultural substrates from a fermentation residue.
NOVELTY - A racemic clopidogrel preparing method involves esterifying alpha-bromo-o-chloro-phenylacetic acid (III) with methanol in the presence of sulfuric acid to obtain alpha-o-methyl acetate (I). The non-separated esterification products and 4, 5, 6, 7-thiophane (3, 2-c) pyridine hydrochloride (IV) are directly reacted to obtain racemic clopidogrel (II).    USE - Method for preparing racemic clopidogrel in industry.    ADVANTAGE - The method enables preparing the racemic clopidogrel in a simple, economical and eco-friendly manner, and providing product with high productivity and purity.    DETAILED DESCRIPTION - A racemic clopidogrel preparing method involves esterifying alpha-bromo-o-chloro-phenylacetic acid of formula (III) with methanol in the presence of sulfuric acid to obtain alpha-o-methyl acetate of formula (I). The non-separated esterification products and 4, 5, 6, 7-thiophane (3, 2-c) pyridine hydrochloride of formula (IV) are directly reacted to obtain racemic clopidogrel of formula (II).
NOVELTY - The solid oxide fuel cell includes a cell body (11) which is arranged between a first thin plate or mesh (32) and a second thin plate or mesh (33). The second thin plate or mesh is fixed to an air electrode layer (23) via a current collection material (41).    USE - Solid oxide fuel cell for generating electric power.    ADVANTAGE - Enables reliable holding of the cell body, and ensures a small current collection resistance.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic cross-sectional view of a solid oxide fuel cell.    Cell body (11)    Air electrode layer (23)    First thin plate or mesh (32)    Second thin plate or mesh (33)    Current collection material (41)
NOVELTY - The method involves generating a fuel cell by system operating voltage with constant potential. An electric potential of the fuel cell is fluctuated. Electric power generation is turned on/off to carry out an electric potential cycle. The fuel cell is provided with a polymer electrolyte membrane. An anode pole and a cathode pole are joined to the polymer electrolyte membrane. A separator is provided with a fuel chamber to supply hydrogen gas to the anode pole. Another separator is provided with an air chamber to supply air to the cathode pole.    USE - Method for activating a fuel cell of power supplies of an electric vehicle, an outdoor installing power supply and a portable power supply.    ADVANTAGE - The method enables activating the fuel cell without a special apparatus, shortening activation time and reducing activation cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical illustration of a relationship between time and current density. '(Drawing includes non-English language text)'
NOVELTY - The assembly has cell stacks (60a-60d) formed by arranging multiple arrays of solid electrolyte form fuel cells in a housing (2). An end part of the cell stacks is fixed to fuel gas cases (58a-58d). Modifiers (78a-78d) are fixed by holding members (90a-90c, 98) for producing the fuel gas supplied to the fuel cells through one of the gas cases. A fuel gas supply pipe supplying the fuel gas modified by the modifiers is connected to the gas case. A heat insulating material made of ceramics is positioned between the cell stacks and the housing.    USE - Solid electrolyte form fuel cell assembly.    ADVANTAGE - The modifiers are fixed by the holding member such that the assembly can prevent the vibration of the modifiers, thus preventing the damage of a gas supply system by movement of the modifiers at the time of conveyance.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of an electric power generation unit assembly connected to modifiers by a holding member.    Housing (2)    Fuel gas cases (58a-58d)    Cell stacks (60a-60d)    Modifiers (78a-78d)    Holding members (90a-90c, 98)
NOVELTY - A biomass carbonizing device comprises carbonization furnace. Furnace body of carbonizing furnace comprises feeding chamber on upper section, oxygen-enriched ignition combustion chamber in middle section, and carbonized section off cooling cabin in lower section. Bottom layer of furnace body is provided with discharging port. Igniting and combusting furnace body wall is provided with at least five ignition port and at least one heating ring on oxygen inlet. Oxygen inlet port is provided with waste gas exhaust pipeline.    USE - Biomass carbonizing device.    ADVANTAGE - The device has simple structure and easy use and is reliable. Biomass raw material carbonized product basically keeps original volume.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating a biomass carbonizing device.
NOVELTY - Household landscape type kitchen waste earthworm composting reactor for preserving fresh air in indoors, comprises a miniature garden, a perforated clapboard, a side wall, a foot frame, an earthworm composting reaction groove, a side wall plug-board and an air distribution hole, where the miniature garden is located at the upper end of the a perforated clapboard. The earthworm composting reaction groove is located in the perforated clapboard, and the earthworm composting reaction groove is separated by the side wall plug-board. The side wall is mounted at two sides of the perforated clapboard.    USE - The composting reactor is useful for preserving fresh air in indoors.    ADVANTAGE - The composting reactor has simple structure; ensures simple operation; and does not impart any effect on human beings.    DETAILED DESCRIPTION - Household landscape type kitchen waste earthworm composting reactor for preserving fresh air in indoors, comprises a miniature garden, a perforated clapboard, a side wall, a foot frame, an earthworm composting reaction groove, a side wall plug-board and an air distribution hole, where the miniature garden is located at the upper end of the a perforated clapboard. The earthworm composting reaction groove is located in the perforated clapboard, and the earthworm composting reaction groove is separated by the side wall plug-board. The side wall is mounted at two sides of the perforated clapboard, and the air distribution hole is mounted on the side wall surface, the bottom of the miniature garden and the lateral face of the earthworm composting reaction groove.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the composting reactor for preserving fresh air in indoors.
NOVELTY - Slide way type household kitchen waste earthworm composting reactor, comprises an outer wall, a perforated side wall, an earthworm composting reactor, a slide way, a percolate recycling inclined surface, a percolate recycling slot, an inserting plate and a perforated clapboard. The outer wall fixed on the perforated clapboard is internally provided with the multiple earthworm composting reactors. The sides of the earthworm composting reactors are provided with the perforated side walls. The inserting plate is arranged between two earthworm compost reactors.    USE - Used as a slide way type household kitchen waste earthworm composting reactor.    ADVANTAGE - The reactor has low cost and does not cause secondary pollution to the environment.    DETAILED DESCRIPTION - Slide way type household kitchen waste earthworm composting reactor, comprises an outer wall, a perforated side wall, an earthworm composting reactor, a slide way, a percolate recycling inclined surface, a percolate recycling slot, an inserting plate and a perforated clapboard. The outer wall fixed on the perforated clapboard is internally provided with the multiple earthworm composting reactors. The sides of the earthworm composting reactors are provided with the perforated side walls. The inserting plate is arranged between two earthworm compost reactors. The slide way is arranged between the perforated clapboard and the earthworm compost reactor. The lower end of the perforated clapboard is fixed with the percolate recycling inclined surface, and the lower end of the percolate recycling inclined surface is fixedly provided with the percolate recycling slot.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the slide way type household kitchen waste earthworm composting reactor.
NOVELTY - High-temperature and high-speed aerobic fermentation machine for processing organic waste, comprises a cabinet equipped with a stirring shaft. The stirring shaft is provided with a helical shaped stirring harrow. The stirring shaft protrudes out of the cabinet which is connected to a motor. A steam nozzle and an electrical bar are arranged in the cabinet. The outer side of the cabinet is equipped with a fan. The cabinet is further provided with a temperature measuring appliance.    USE - The machine is useful for processing organic waste.    ADVANTAGE - The machine does not produce foul smell; and is not influenced by weather and environmental-friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the high-temperature and high-speed aerobic fermentation machine for processing organic waste.
NOVELTY - The device has a hopper connected with a reaction kettle through a pipe, where the reaction kettle is connected with a separating kettle. The reaction kettle is provided with an acid pipe, a discharge pipe and a stirrer, where the discharging pipe is provided with a condensing unit. The separating kettle is provided with a waste gas outlet, where bottom of the separation kettle is provided with an oil discharging opening. The reaction kettle is provided with an electric heating unit. A reservoir is provided with an oil filter.    USE - Plants or animal waste catalytic oil production device for a diesel engine.    ADVANTAGE - The device has simple process, environmental friendly effect, wide range of applications, high production efficiency and popularization effect. The device reduces waste discharge and saves energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a plants or animal waste catalytic oil production device.
NOVELTY - Production device comprises a reaction kettle (1), a cooling device and a distillation device, which are sequentially connected. The cooling device comprises a cooling filter (2) and a segmented cooling device. The segmented cooling device comprises a first section of a cooler I (3), a second section of a cooler II (4) and a third section of a cooler III (5), which are sequentially connected. The distillation device comprises a distillation tower, a condenser and a collecting tank, which are sequentially connected.    USE - The production device is useful for bio-based gasoline additive monoglyceride.    ADVANTAGE - The production device ensures continuous production with high efficiency and high raw material utilization rate.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the production device.    Reaction kettle (1)    Cooling filter (2)    Cooler I (3)    Cooler II (4)    Cooler III (5)
NOVELTY - Water distributor comprises a first annular manifold (1), a second annular manifold (2), a branch pipe (3) and a water outlet head (4). The first annular manifold is connected to a water inlet (5). The first annular manifold is connected to the second annular manifold by several branch pipes. Several water outlet heads are uniformly distributed on a pipe wall of the second annular manifold, and are connected on the inner side of the second annular manifold.    USE - Used as a water distributor.    ADVANTAGE - The water distributor increases the uniform water distribution range by expanding the water covering range of the water outlet heads; guarantees complete contact of the materials with water; and improves the utilization rate of the materials.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biogas generation tower, comprising the water inlet. The tower further comprises the water distributor. The water distributor is set in the biogas generation tower. The first annular manifold and second annular manifold of the water distributor are connected to each other.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the water distributor.    First annular manifold (1)    Second annular manifold (2)    Branch pipe (3)    Water outlet head (4)    Water inlet (5)
NOVELTY - A precursor solution comprising nickel, yttrium, and zirconium is prepared and subjected to hydrothermal treatment and to obtain a nickel-yttria-stabilized zirconia composite.    USE - Manufacture of nickel-yttria-stabilized zirconia composite for manufacturing fuel cell (claimed).    ADVANTAGE - The nickel-yttria-stabilized zirconia composite is easily and economically manufactured.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of fuel cell.
NOVELTY - A carbonated water comprising water and carbon dioxide is reacted in the presence of a catalyst in at least one reactor, to form a reaction product comprising hydrocarbons, hydrogen and oxygen. An exit stream comprising unreacted carbonated water and the reaction product is directed from the reactor to a separator unit and the reaction product is separated from the unreacted carbonated water in the separator.    USE - Production of hydrocarbons, hydrogen and oxygen used as fuel in power industry.    ADVANTAGE - The method economically provides hydrocarbons, hydrogen and oxygen, with reduced power consumption and reduced generation of environmentally harmful products.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a pilot unit layout.    Reaction column with heating unit (1)    Mixing unit (2)    Separator-collector (3)    Gas chromatograph (4)    Carbon dioxide cylinder (5)
NOVELTY - A desulfurization system (20) consists of a fuel supply unit (2) for supplying a hydrocarbon fuel having a Wobbe index of 12-16 kWhour/m3, and containing sulfur compound and oxygen (1 ppm to 4 vol.%), to a later stage, and a desulfurization unit (3) containing a desulfurization catalyst which desulfurizes the hydrocarbon fuel. The desulfurization catalyst comprises silver-supporting zeolite and/or copper-supporting zeolite.    USE - Desulfurization system is used for desulfurizing hydrocarbon fuels used in hydrogen production systems for manufacturing hydrogen in fuel cell systems (all claimed).    ADVANTAGE - The desulfurization system supplies sufficient amount of hydrocarbon fuel with reduced sulfur content.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) hydrogen production system (30) provided with the desulfurization, and a hydrogen-producing unit (4) which generates hydrogen from the hydrocarbon fuel passing through the desulfurization unit;    (2) desulfurization of hydrocarbon fuel; and    (3) manufacture of hydrogen, which involves reforming desulfurized hydrocarbon fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a conceptual view of the fuel cell system. (Drawing includes non-English language text)    Fuel supply unit (2)    Desulfurization unit (3)    Hydrogen-producing unit (4)    Desulfurization system (20)    Hydrogen production system (30)
NOVELTY - A desulfurization system consists of unit (3a) for removing sulfur compound from circulating hydrocarbon fuel. The unit is provided with porous desulfurizing agent having different pore diameter. The desulfurizing agent is arranged from upstream side of the fuel distribution direction to downstream side such that the pore diameter increases towards the downstream side.    USE - Desulfurization system for use in hydrogen production system for fuel cells (claimed). Uses include but are not limited to solid oxide fuel cell, polymer electrolyte fuel cell, phosphoric acid fuel cell and molten carbonate fuel cell.    ADVANTAGE - The desulfurization system has excellent durability and desulfurization performance over a long period of time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for desulfurization of hydrocarbon fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the desulfurization system.    Fuel supply portion (2)    Desulfurization portion (3a)    Hydrogen producing portion (4)    Catalyst layers (101-105)
NOVELTY - A desulfurization system has a desulfurization unit (3a) for removing sulfur compound from circulating sulfur compound-containing hydrocarbon fuel, and comprising desulfurizing agent and several zeolites supporting active metal in different concentrations. The zeolites are arranged from upstream side of flow direction of hydrocarbon fuel to downstream side, in order from highest active metal concentration to lowest.    USE - System for desulfurization of fuel used in hydrogen production system of fuel cell system (all claimed).    ADVANTAGE - The system has excellent durability and desulfurization performance maintained for a very long period of time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for hydrogen production system, which has the desulfurization system and a hydrogen-producing unit (4) for generating hydrogen from the hydrocarbon fuel passed through desulfurization unit.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of desulfurization system.    Fuel supply unit (2)    Desulfurization unit (3a)    Hydrogen producing unit (4)    Catalyst layers (101,102,103)
NOVELTY - The apparatus has desulfurizing unit (2) that is provided with desulfurization flow paths (22,23). A desulfurization type heat-exchange unit (82) is accommodated in the desulfurization flow paths for distributing thermal medium after collecting the exhaust heat of the cell stack, and heat-exchanging the thermal medium so that fluid distribution direction of the desulfurization type heat-exchange unit and fluid distribution direction of desulfurization flow paths correspond to countercurrent flow state.    USE - Desulfurizing apparatus used for fuel cell system (claimed) such as polymer electrolyte fuel cell (PEFC), solid oxide fuel cell (SOFC), phosphoric acid form fuel cell (PAFC) and molten carbonate fuel cell (MCFC).    ADVANTAGE - The desulfurization unit can be heat-retained efficiently with improved energy saving effect.    DETAILED DESCRIPTION - The desulfurization catalyst (21) is accommodated in desulfurization flow paths so as to distribute desulfurization flow paths and desulfurize hydrogen-containing fuel. The folding unit distributes the hydrogen-containing fuel for distributing from fluid entrance to one side to the other side of the contrary formed in the desulfurization flow paths. A baffle plate is provided for changing the flow of the fluid with respect to fluid entrance, provided in the inside of the desulfurization flow paths. A surface area is set based on the radius of the desulfurization unit and predetermined catalyst amount accommodated in the desulfurization unit. An INDEPENDENT CLAIM is included for fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of desulfurizing apparatus. (Drawing includes non-English language text)    Desulfurizing unit (2)    Fluid entrance (20a)    Fluid exit (20b)    Desulfurization flow paths (22,23)    Desulfurization type heat-exchange unit (82)
NOVELTY - A fuel cell system (1) has hydrogen generation unit (4) to generate hydrogen-containing gas using hydrogen-containing fuel. A cell stack (5) generates power using hydrogen-containing gas. A combustion unit (20) combusts prescribed amount of hydrogen-containing fuel and oxidizer. A determination unit determines temperature change in combustion unit based on result of temperature detection unit (21). An adjustment unit adjusts amount of hydrogen fuel supplied to hydrogen generation unit when temperature change is determined by determination unit.    USE - Fuel cell system.    ADVANTAGE - The adjustment unit adjusts amount of hydrogen fuel supplied to hydrogen generation unit when temperature change is determined by determination unit, so that the operation can be performed according to the characteristic changes due to the varying amount of fuel supplied, without any special apparatus for the measurement.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of fuel cell system. (Drawing includes non-English language text)    Fuel cell system (1)    Hydrogen generation unit (4)    Cell stack (5)    Combustion unit (20)    Temperature detection unit (21)
NOVELTY - Fermentation method for producing alcohol involves adding ground seed of Perilla frutescens to alcohol fermentation ingredients and fermenting the mixture at 33-40 degrees C.    USE - The fermentation method is useful for producing alcohol (claimed) used as alcoholic beverages and fuel.    ADVANTAGE - The method efficiently produces alcohol even in high temperature conditions by reinforcing fermentation ability and maintaining activity of microorganism, improving fermentation speed by adding ground seed of P.frutescens and reducing fermentation duration, and thus saves energy resources and reduces cost by reducing electric power for cooling, and cooling resources, and does not require apparatus for temperature control. The amount of carbon dioxide emitted during the process is reduced significantly and hence global warming is prevented.
NOVELTY - The system has an electric power generation unit (21) that generates electric power using a hydrogen containing gas. An exhaust port (26) discharges an exhaust gas which is emitted from electric power generation unit. A damper (22) closes and opens the exhaust port. If a flow direction sensor (23) detects that the flow direction of the circulating gas in the exhaust port is flowing backward, a control unit (24) closes the damper and stops the system.    USE - Fuel cell system e.g. solid oxide fuel cell system for use in indoor application. Can also be used in phosphoric acid form fuel cell system and molten carbonate fuel cell system.    ADVANTAGE - The inflow of the external waste gas in the system can be suppressed. Also the life shortening caused by the backward flow of the exhaust gas to the power generation unit for the fuel cell stack, various catalysts, absorbing agents, and ion exchange resins are minimized and the stable power generation can be achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the fuel cell system. (Drawing includes non English text)    Electric power generation unit (21)    Damper (22)    Flow direction sensor (23)    Control unit (24)    Exhaust port (26)
NOVELTY - The fuel cell system has a damper (22) that adjusts the flow volume of an exhaust gas which flows toward an exhaust port (24). An electric power generation unit (21) contains a cell stack which produces an electric power using hydrogen containing gas. The exhaust port makes the exterior of the system to discharge the exhaust gas discharged from the electric power generation unit.    USE - Fuel cell system such as PEFC cell system for use in indoor applications. Can also be used in solid oxide fuel cell (SOFC) system, phosphoric acid form fuel cell (PAFC) system and molten carbonate fuel cell (MCFC) system.    ADVANTAGE - The decline in the operational efficiency of the fuel system or life shortening of the cell stack is suppressed by suppressing fluctuations in the flow of exhaust gas in the fuel cell system so that the stable electric power generation unit is attained effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the fuel cell system. (Drawing includes non-English language text).    Heat exchange unit (15)    Electric power generation unit (21)    Damper (22)    Exhaust port (24)    Exhaust route (30A)
NOVELTY - Organic-refuse processing container using soil is laterally long container (1) (without a bottom face) segmented into several layers comprising upper cover (2) in the upper opening of the container each layer, and the first front cover (4), second front cover (5) and third front cover (6) provided in the front lower part.    USE - Organic-refuse processing container, preferably fresh soybean extract refuse-disposal container (claimed). The organic-refuse includes bamboo shoot, watermelon refuse, and maize weeds.    ADVANTAGE - The container completely and rapidly processes organic-refuse without using fermentation promoter and electric power.    DESCRIPTION OF DRAWING(S) - The drawing shows perspective view of organic-refuse processing container.    Organic-refuse processing container (1)    Upper cover (2)    First front cover (4)    Second front cover (5)    Third front cover (6)
NOVELTY - The fire-lighter comprises 40-60 splinters of wood having a length of 4-13 cm impregnated with paraffin, and a cone made of a combustible material having a circumference of 14-18 cm impregnated in its upper part by 50% of its length to form a bundle (5) traversed by a match of which ignition causes a first level of igniting. The cone causes a second level of igniting. The combustible material consists of paper and cardboard. The splinters follow the wood fibers, which are very fibrous and split easily, such as fir or pine.    USE - Used as a charcoal grill fire-lighter.    ADVANTAGE - The rapid and efficient fire-lighter does not release unpleasant odors.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of producing a fire-lighter.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic view of a fire-lighter.    Splinters of wood (1)    Cone (2)    Match (3)    Bundle. (5)
NOVELTY - Moldings from organic and/or inorganic waste for energetic and/or material utilization in a melting gasifier or in a comparable aggregate comprises adjusting the optimum humidity of organic and/or inorganic wastes to be compacted to (5-20%) and the organic content (0.5-50%) without the addition of hydraulically-acting binders.    USE - The moldings from organic and/or inorganic waste are useful for energetic and/or material utilization in a melting gasifier or in a comparable aggregate.    ADVANTAGE - The method allows recycling of phosphorus from dehydrated and dried sewage sludge and/or ash from the mono-combustion, and allows recycling of materials from ash of waste incinerators.
NOVELTY - Plant for treating vegetable oils for fuel suitable for engines and diesel motors, is claimed. Pure vegetable oil (2) is treated with flue gas until the quality and the flash point are changed correspondingly. The flue gas is conveyed into a lower chamber (9) via a flue gas supply (1) and discharged to an upper chamber (10) via flue gas outlet. The vegetable oil is pumped from the bottom chamber through a pump into a distribution pipe of the upper chamber and passes over the guide plates back into the lower chamber of the plant.    USE - The plant is useful for treating vegetable oils for fuel suitable for engines and diesel motors.    ADVANTAGE - The plant treated vegetable oil does not produce hazardous sediments, thus preventing damage of the motors. The produced oil has modified quality and flash point, thus enables easy operation of the motors and diesel motors.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the plant for treating vegetable oils for fuel suitable for engines and diesel motors.    Flue gas supply (1)    Pure vegetable oil (2)    Plant (3)    Lower chamber (9)    Upper chamber (10)
NOVELTY - Performing denitrogenation of sewage through Penicillium strain, involves adding organic matter in sewage under of temperature 5-40 degrees C, the pH value of 5-9, and dissolved oxygen concentration of 0.5-6.5 mg per liter; stirring the sewage; adding Penicillium (0.05-30%) and mixing with the sewage to culture for 4-8 hours according to the different concentrates range of the ammonia nitrogen in sewage and sewage amount; and performing the synchronous nitrification and denitrification with help of the Penicillium.    USE - For denitrogenation of sewage through Penicillium strain (claimed).    ADVANTAGE - The Penicillium strain provides more than 3 times processing efficiency as compared to the other strains; accelerates the whole denitrogenation reaction process; decreases the hydraulic power staying time; and reduces reactor volume. The method has excellent developing application prospect at the wastewater biological denitrification field.
NOVELTY - Solid fuel is manufactured by using activated sludge generated in organic waste processing method, adding organic-type coagulated sludge, and mixing with coffee grounds which are foodstuff-type waste materials with deodorizing function.    USE - A manufacturing method of solid fuel for recycling system (claimed).    ADVANTAGE - Pelletization is carried out easily, reduction of energy consumption is possible, and odor of activated sludge is suppressed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a recycling system which is utilized at a foodstuff factory and uses solid fuel.
NOVELTY - The biogas system (100) has a thermal decomposition apparatus (2) which sends the normal-pressure superheated steam in with respect to the thermal decomposition tank which accommodates the organic waste, then maintains interior of thermal decomposition tank to a hypoxic condition or an anoxic state. The thermal decomposition apparatus generates the pyrolysis gas as biogas. An exothermic reaction apparatus (3) generates high temperature/high pressure steam using the pyrolysis gas.    USE - Biogas system for producing electric power using biogas from organic waste.    ADVANTAGE - Reduces residue produced during electric power generation since most organic waste are gasifiable to the pyrolysis gas by generating high temperature/high pressure steam using the pyrolysis gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biogas method.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of the processes in the biogas system. (Drawing includes non-English language text).    Hydrolysis process apparatus (1)    Thermal decomposition apparatus (2)    Exothermic reaction apparatus (3)    Electric power generating apparatus (7)    Heat exchanger (8)    Hydrogen recovery apparatus (10)    Biogas system (100)
NOVELTY - Crystalline forms A and B of 1-((3R)-6,8-difluoro-3,4-dihydro-2H-1-benzopyran-3-yl)-1,3-dihydro-5-(2-((phenylmethy-amino)ethyl)-2H-imidazole)-2-thione (I) and amorphous form of (I), where the crystalline form A is unsolvate form and the crystalline form B is ethyl acetate solvate, is new.    USE - The crystalline forms and amorphous form of (I) are useful for the treatment of anxiety disorders (including social anxiety disorders, post-traumatic stress disorder, acute distress disorder, obsessive compulsive disorders, panic disorders such as panic attacks, and phobias such as agoraphobia, social phobias, and specific phobias), migraines, cardiovascular disorders, hypertension, chronic or congestive heart failure, angina, arrhythmias, and circulatory disorders such as Raynaud's phenomenon. No biological data given.    ADVANTAGE - The crystalline forms and amorphous form of (I): has improved storage stability, filterability, processability, easy drying and wettability properties; and provides drug in a simple, economically or environmentally friendly manner with higher purity and yield. The crystalline form A has low hygroscopicity and remains stable as a crystal form upon mechanical and aqueous vapor stress.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a process to purify crystalline form A of (R)-5-(2-(benzylamino)ethyl)-1-(6,8-difluorochroman-3-yl)-1H-imidazole-2(3H)-thione (II) comprising recrystallization of (R)-5-(2-(benzylamino)ethyl)-1-(6,8-difluorochroman-3-yl)-1H-imidazole-2(3H)-thione hydrochloride (III) in at least one organic solvent.
NOVELTY - Controlling growth of contaminant microorganisms in a fermentation process, comprises adding a nitrogen-free peroxygen-releasing compound to one or more steps of a fermentation process, where the fermentation process comprises (i) providing a fermentation vessel, (ii) providing an inoculant, a fermentable sugar and process water, (iii) introducing separately, or in any combination, the inoculant, fermentable sugar and process water into a fermentation vessel to provide a fermentation broth and (iv) contacting the inoculant with the fermentable sugar in the fermentation vessel.    USE - The method is useful for controlling growth of contaminant microorganisms in a fermentation process.    ADVANTAGE - The method controls growth of contaminant microorganisms in a fermentation process using a nitrogen-free peroxygen-releasing compound in a simple and economical manner.    DETAILED DESCRIPTION - Controlling growth of contaminant microorganisms in a fermentation process, comprises adding a nitrogen-free peroxygen-releasing compound to one or more steps of a fermentation process, where the fermentation process comprises (i) providing a fermentation vessel, (ii) providing an inoculant, a fermentable sugar and process water, (iii) introducing separately, or in any combination, the inoculant, fermentable sugar and process water into a fermentation vessel to provide a fermentation broth and (iv) contacting the inoculant with the fermentable sugar in the fermentation vessel at a temperature at which the inoculants converts the fermentable sugar to ethanol.
NOVELTY - Culturing a microorganism comprises culturing the microorganism in the culture medium comprising a carboxylate counterion source (0.5 mM).    USE - The method is useful for culturing the microorganism that produces a free fatty acid in a culture medium (claimed), synthesizing products including biofuels or chemicals, and converting fatty acids to various derivatives including hydrocarbons, esters or alcohols.    ADVANTAGE - The method is capable of easily culturing microorganism with improved yield.
NOVELTY - Purification of organic liquids comprises (a) contacting an organic liquid with methanesulfonic acid; (b) separating methanesulfonic acid from the organic liquid.    USE - The methanesulfonic acid is useful for the purification of organic liquids (claimed) by removing phospholipids and metal ions from organic liquids, preferably triglycerides and other fatty acid esters or biodiesel.
NOVELTY - Producing benzene, toluene, ethyl benzene, and xylene (BTEX) or gasoline, comprises contacting a feedstock comprising at least one renewable oil with a catalyst comprising a catalytically-active form of gallium, at an elevated temperature.    USE - The process is useful for producing BTEX or gasoline for use in the petrochemical industry and/or for blending components or additives for fuels.    ADVANTAGE - The process: provides product stream containing BTEX (yield of greater than 35 wt.%, preferably greater than 42 wt.%); utilizes renewable oil, hence economical and the deoxygenation of renewable oils before feeding to the reaction zone prevents excessive water production and hydrogen consumption in the reaction zone.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for    (1) producing BTEX aromatics and/or hydrogen from renewable oil, comprising providing a reactor vessel or riser containing catalyst, where the catalyst comprising a gallium cation catalyst and contacting a feedstock with the catalyst at elevated temperature, where the feedstock comprises renewable oil comprising oil derived from biomass living in the past 50 years, canola oil, oils extracted from vegetables including corn, soybean, sunflower, and sorghum, algae oil from naturally-occurring algae, algae oil from genetically modified algae, oil from seeds, oil from fungi, or oil from a photosynthetic or non-photosynthetic bacteria; and    (2) a renewable oil product produced by the above process.
NOVELTY - A methane collection device comprises a cylindrical tank body, and a three-phase separator having upper layer and lower layer that are disposed in the cylindrical tank body. The three-phase separator comprises upper alternately-disposed triangular gas collection covers and lower alternately-disposed triangular gas collection covers. The upper alternately-disposed triangular gas collection covers having bevel edges partially superposed with the adjacent lower triangular gas collection covers, and top part connected with a methane main tube via methane branch tubes.    USE - A methane collection device for an expanded granular sludge bed.    ADVANTAGE - The device has simple structure, is capable of collecting methane generated in reaction chambers below three-phase separators.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a methane collection device.
NOVELTY - Method for preparing organic fertilizer from organic waste, involves using solid organic waste as raw material, grinder, material stirrer, plastic weaving bag, dryer, granulator and weighing and packaging machine, where the method does not use pile-turning machine, and comparing with the process which use a pile-turning machine in fermentation.    USE - The method is useful for preparing organic fertilizer.    ADVANTAGE - The method is cost-effective, occupies less land during fermentation, has less fermentation cost, and requires no electricity and oil during the whole fermentation process.
NOVELTY - A biological film carrier comprises a hollow outer cylinder (1). The outer cylinder of the inner cavity is provided with a hollow middle column body (2) in the axial direction and a hollow inner cylinder. The inner cylinder is sleeved in the pipe cavity in the middle cylinder, inner cylinder and middle cylinder sleeve. It is also provided with a rib (4) plate between the middle cylinder and the outer cylinder. The inner and outer surfaces and the inner column body (3) are of a concave-convex structure.    USE - Biological film carrier for treating sewage.    ADVANTAGE - The biological film carrier has simple structure, and can be easily manufactured and maintained.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the biological film carrier.    Hollow outer cylinder (1)    Hollow middle column body (2)    Inner column body (3)    Rib (4)    Wing plate (6)
NOVELTY - A flow comprising steam (16) is added to feed comprising carbon oxide (preferably, carbon monoxide and/or carbon dioxide), hydrogen and at least 1% 2C or more hydrocarbons. Obtained reacting feed mixture (12) is reacted in presence of catalyst, and withdrawn, to obtain methane-rich product gas (20). The ratio (S/HHC) of water molecules and carbon atoms in higher hydrocarbons, is less than 25. The maximum catalyst temperature is 460 degrees C or more, preferably 500 degrees C. The maximum catalyst temperature is less than critical carbon formation temperature for S/HHC value for catalyst.    USE - Production of methane-rich product gas used for producing substitute natural gas.    ADVANTAGE - The method economically provides methane-rich product gas, with reduced steam consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for reactor system for production of methane-rich product gas from feedstock derived from coke oven (2), which is configured for combining feedstock line (A) with feed line (B) into a reactor inlet line which is configured for feeding a reactor comprising a methanation catalyst. The feed line (B) comprises an ejector configured for having a steam feed as motive gas and a recycled methane-rich product gas as driven gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view explaining the production of methane-rich product gas.    Coke oven (2)    Coke oven gas (4)    Feed mixture (12)    Steam (16)    Methane-rich product gas (20)
NOVELTY - Processing system has a mechanism for processing municipal solid waste by using an operating methodology, where discharge material is placed on a ramp and transported for pre-grinding step. The waste product is processed by thermophilic and aerobic composting process, where organic fraction is completely transformed into compost, solid and dry material with total recovery or recycling of inorganic fractions.    USE - Processing system for municipal solid waste unit for mechanical and automatic blending, composting and screening of waste material (claimed).    ADVANTAGE - The processing system has a mechanism for processing municipal solid waste by using an operating methodology, and hence ensures reduced labor requirement with environmental benefits.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the processing system.    Transfer belt (3)    Bucket (8)    Composting windrow (9)    Helices (10)    Rotating sieve (14)
NOVELTY - The apparatus (100) has an anaerobic digester (110) provided with a livestock waste part (10). A processing water tank (30) is installed at an upper end of the anaerobic digester. An external gas reservoir sheltered housing (120) is installed in top of the anaerobic digester. Bio-gas is supplied from a bio-gas exhausting tube (133). A gas reservoir capacity meter (135) is connected to a gas reservoir (130). The bio-gas exhausting tube is connected to a heat exchanger (150).    USE - Integrated anaerobic digestion bio-gas apparatus.    ADVANTAGE - The apparatus is convenient to use and inexpensive. The apparatus has high energy efficiency, and improves renewable energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of an integrated anaerobic digestion bio-gas apparatus.'(Drawing includes non-English language text)'    Livestock waste part (10)    Processing water tank (30)    Integrated anaerobic digestion bio-gas apparatus (100)    Anaerobic digester (110)    External gas reservoir sheltered housing (120)    Gas reservoir (130)    Bio-gas exhausting tube (133)    Gas reservoir capacity meter (135)    Heat exchanger (150)
NOVELTY - The apparatus (100) has an anaerobic digester (110) provided with a livestock waste part (10) and maintaining water level in the livestock waste part. An external gas reservoir sheltered housing (120) is installed at a top part of the anaerobic digester. A bio-gas exhausting tube (133) is connected to a heat exchanger (150). A heating system (151) provides warm water that is supplied from a boiler (152). A gas reservoir capacity meter (135) is connected to a gas reservoir (130). An atmospheric pressure connection pipe is connected to the anaerobic digester.    USE - Livestock waste bio-gas producing apparatus.    ADVANTAGE - The apparatus is convenient to use and inexpensive. The apparatus has high energy efficiency. The apparatus improves renewable energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a livestock waste bio-gas producing apparatus.'(Drawing includes non-English language text)'    Livestock waste part (10)    Livestock waste bio-gas producing apparatus (100)    Anaerobic digester (110)    External gas reservoir sheltered housing (120)    Gas reservoir (130)    Bio-gas exhausting tube (133)    Gas reservoir capacity meter (135)    Heat exchanger (150)    Heating system (151)    Boiler (152)
NOVELTY - Invention relates to agriculture and can be used in processing organic wastes, particularly manure and turf to obtain organic fertiliser. The method involves layering manure and water-absorbing material - turf, adding compost followed by aerobic composting at 50-60% moisture content of the mixture. The compost used is inoculating compost based on poultry droppings and a consortium of microbial strains Bacillus subtilis B-168, Bacillus mycoides B-691, Streptomyces sp. Ac-154, Mukor psychrophilus F-1441, Candida utilis Y-2441 in amount of 1.106-1.107 cells per millilitre per ton of poultry droppings. The inoculating compost is taken in weight ratio to the compost mixture of 1:20. Composting is carried out in piles.    USE - Chemistry.    ADVANTAGE - Simple process of making compost and obtaining compost with stable properties. 2 tbl, 2 ex
NOVELTY - Invention relates to bioconversion of poultry wastes and can be used in production of ecologically clean effective fertiliser for agricultural crops. The method involves successive layering of droppings and a water-absorbing organic material, forming at least one pile and adding microorganisms in liquid form in form of a suspension, stirring the mixture, biological heating and aerobic fermentation of the mixture. Aerobic fermentation of the mixture is carried out until temperature of the mixture naturally drops to 25-30 degrees C. The microorganisms used are consortium of Bacillus subtilis B-168, Bacillus mycoides B-691, Streptomyces sp. Ac-154, Mukor psychrophilus F-1441, Candida utilis Y-2441 in amount of 1.106-1.107 cells per millilitre per ton of poultry droppings.    USE - Chemistry.    ADVANTAGE - Cutting time for processing poultry droppings and improved quality of the biocompost. 2 tbl, 4 ex
NOVELTY - Invention relates to biotechnology and specifically to methods of recycling household wastes. The method involves removing inorganic impurities, grinding, mixing wastes with an organic additive containing a culture of microorganisms and composting to obtain organic fertiliser. The organic additive used is compost based on poultry droppings, which is taken in amount of 300-500 kg per ton of wastes, and microbial strains Bacillus subtilis B-168, Bacillus mycoides B-691, Streptomyces sp. Ac-154, Mukor psychrophilus F-1441, Candida utilis Y-2441 in amount of 1.106-1.107 cells per millilitre per ton of poultry droppings.    USE - Chemistry.    ADVANTAGE - Simple process and low cost of processing household wastes. 1 tbl, 3 ex
NOVELTY - A multifunctional organic plant base plate comprises agricultural waste flakes, binder and water. The agricultural waste flakes form culture medium with bearing strength and permeability, and having size-to-weight ratio of 500x 330x 50:2.18-2.79. Plant seeds are uniformly distributed to form a seed layer 1-2 cm from the base plate.    USE - Multifunctional organic plant base plate used for greening grass, particularly tall fescue or bermuda grass; and crops including tomato, pepper, eggplant, or scallion (claimed).    ADVANTAGE - The plant base plate uses and recycles agricultural waste, achieves greening when laid on arid zone or desert, promotes weathering of soil layer or lead mold soil, and improves soil condition.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of plant base plate by drying crop waste and crushing into 5-10 mm, sterilizing, mixing with binder and water, and stirring for 5-10 minutes; mixing with fine wood chips, adding soil modifier and nutrient granules, extruding, pressing under 0.785 MPa using 1.5-2 t hydraulic platform, uniformly sprinkling seeds to form seed layer, and extruding at less than or equal to 0.8 MPa; and drying at 80-100 degrees C for 20 minutes or naturally drying until water content is 3-5%, vacuum drying at less than or equal to 0.785 MPa and 15-35 degrees C until water content of less than 15% and naturally drying until water content of 1.5-5.5.
NOVELTY - The method comprises mixing silkworm excrement with microbial strain, stirring uniformly and fermenting at high temperature by adjusting moisture content of 55-60% and carbon/nitrogen ratio of 25-30/1, raising the temperature to 60 degrees C, turning once for every 24 hours, reducing stack temperature to the environment temperature, carrying the fermenting process for 12-16 days, then drying, granulating, and sieving. The silkworm excrement comprises mixed silkworm dropping directly collected from farmers or waste silkworm dropping after extracting chlorophyll.    USE - The method is useful for producing special organic fertilizer for cultivation by fermenting silkworm excrement. No biological data given.    ADVANTAGE - The method is capable of economically producing special organic fertilizer for cultivation by fermenting silkworm excrement with improved crop yield, quality and soil fertility, and reduced energy consumption in a simple and an environmental friendly manner.    DETAILED DESCRIPTION - The method comprises mixing silkworm excrement with microbial strain, stirring uniformly and fermenting at high temperature by adjusting moisture content of 55-60% and carbon/nitrogen ratio of 25-30/1, raising the temperature to 60 degrees C, turning once for every 24 hours, reducing stack temperature to the environment temperature, carrying the fermenting process for 12-16 days, then drying, granulating, and sieving. The silkworm excrement comprises mixed silkworm dropping directly collected from farmers or waste silkworm dropping after extracting chlorophyll. The microorganism bacteria comprises Bacillus, actinomycetes, nitrogen-fixing bacteria, lactic acid bacteria, and/or non-pathogenic.
NOVELTY - The method comprises e.g. (a) adding Chinese herbal medicine to animal feed by weighing 1-5 parts by weight (pbw) of radix codonopsitis, 1-2 pbw of radix Astragalus, 5-8 pbw of Atractylis ovata, 2-4 pbw of red peony, and grinding into the powder for feeding livestock, (b) adding water solution containing 20-50 pbw of solid nitrogen bacteria, 1-30 pbw of potassium mineral powder, 2-80 pbw of powdered rock phosphate, and 1-6 pbw of ferrous sulfate powder in the livestock manure, and mixing the potassium ore, powdered rock phosphate and ferrous sulfate.    USE - The method is useful for producing active ecological livestock organic raw material (claimed), which is useful for: removing bad smell and harmful gas in waste; killing ascarid eggs and bacteria; and converting crude protein in animal into amino acids, and starch into sugar. No biological data given.    ADVANTAGE - The method is capable of producing active ecological organic raw material with high-quality in a simple manner.    DETAILED DESCRIPTION - The method comprises (a) adding Chinese herbal medicine to animal feed by weighing 1-5 parts by weight (pbw) of radix codonopsitis, 1-2 pbw of radix Astragalus, 5-8 pbw of Atractylis ovata, 2-4 pbw of red peony, and grinding into the powder for feeding livestock, (b) adding water solution containing 20-50 pbw of solid nitrogen bacteria, 1-30 pbw of potassium mineral powder, 2-80 pbw of powdered rock phosphate, and 1-6 pbw of ferrous sulfate powder in the livestock manure, mixing the potassium ore, powdered rock phosphate and ferrous sulfate, adding 3-8 kg of power mixture, then adding 3-8 times of water into 6-15 kg of solid nitrogen bacteria solution for diluting, and then spraying to the livestock manure, uniformly stirring, packing the materials in the plastic frame, and sealing to ferment for 25-45 days to obtain the active ecological livestock organic raw material.
NOVELTY - Preparation of organic liquid fertilizer by using coenzyme Q10 fermentation liquor comprises adjusting the pH of coenzyme Q10 fermentation waste liquor at 6-8.0; eliminating the flocculent sediments; passing the fermentation liquor through polyethylene (PE) microfiltration device; nanofiltering; concentrating; adding with potassium fulvate (BSFA), sodium alginate, and urea; and fully mixing to obtain the organic liquid fertilizer.    USE - Preparation of organic liquid fertilizer (claimed) used for promoting the germination of seeds, increasing output of crops, enhancing stress resistance of crops, and improving the quality of the crops.    ADVANTAGE - The method is easy to carry out; can concentrate the effective ingredients of the fermentation liquor; and recycles fermentation waste liquor, thus, reducing the pollution of waste liquor to the environment. The organic liquid fertilizer can provide the plants with organic material nutrients, nitrogen-phosphorus-potassium, and amino acid.
NOVELTY - Submicron powder vegetable seed coating (I) prepared by performing a superfine grinding on a bactericide, plant growth regulators, trace element fertilizers, a film forming agent, a warning color pigment and an additive, where the bactericide is carbendazim, the plant growth regulators are naphthylacetic acid and paclobutrazol, the trace element fertilizers are zinc fertilizer and boron fertilizer, the film forming agent is chitosan, the warning color pigment is basic fuchsin or basic rhodamine toner and the additive is clay or bentonite, is claimed.    USE - (I) is useful for: controlling vegetable seedling diseases, promoting seed germination and enhancing stress resistance; and coating melon, fruit and leaf vegetable seeds in different ecological conditions. No biological data given.    ADVANTAGE - The process: is cost effective, simple, eco-friendly and convenient to use; uses low toxic agent and growth regulator.    DETAILED DESCRIPTION - Submicron powder vegetable seed coating prepared by performing a superfine grinding on a bactericide, plant growth regulators, trace element fertilizers, a film forming agent, a warning color pigment and an aid, where the bactericide is carbendazim, the amount of bactericide is 2-8 mass%, the plant growth regulators are naphthylacetic acid and paclobutrazol, the amount of plant growth regulators is 0.05-0.5 mass%, the trace element fertilizers are zinc fertilizer and boron fertilizer, the amount of trace element fertilizers is 0.1-1 mass%, the film forming agent is chitosan, the amount of the film forming agent is 0.5-5 mass%, the warning color pigment is basic fuchsin or basic rhodamine toner, the amount of warning color pigment is 1-5 mass% and the additive is clay or bentonite, and the amount of additive is balance, is claimed.
NOVELTY - Biologic organic fertilizer (I) comprises organic mixture absorbed with composite microbial liquid preparation, organic matter, Bacillus subtilis agent, Bacillus licheniformis fungicide, Saccharomyces cerevisiae fungicide, Rhodopseudomonas palustris fungicide, Lactobacillus plantarum and Lactobacillus acidophilus.    USE - The biologic organic fertilizer (I) is useful for: improving rice stress resistance; and promoting crop growth and improving crop output, where the crop is rice, which is planted, and (I) is applied to base fertilizer or after manuring of the rice (all claimed). Tests details are described but no results given.    ADVANTAGE - (I) is rich in beneficial microbe flora and plenty and track elements needed by the growth of multiple crops, capable of filling and regulating soil ecological flora and trace element, reinforcing the capability of dissolving phosphorus and separating potassium, forcibly decomposing, converting and synthesizing effective nutrients, improving utilization ratio of the fertilizer, improving the physicochemical character of the soil, promoting the formation of the particle structure, repairing the hardened and pathological soil, increasing the soil fertility, inhibiting multiple soil-borne diseases, multiple soil-borne diseases, accelerating the growth and the burliness of the crop.
NOVELTY - The composite reversible hydrogen storage material, comprises rare-earth element, and a composition consisting of yttrium fluoride (10-56.26 mass%) and sodium borohydride (43.74-90 mass%).    USE - The composite reversible hydrogen storage material is useful for a hydrogen fuel cell.    ADVANTAGE - The composite reversible hydrogen storage material can be energy-efficiently manufactured with improved performance and high energy density and storage capacity thus enhancing efficiency of the hydrogen fuel cell.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of manufacturing a composite reversible hydrogen storage material.
NOVELTY - Methane, hydrogen, fertilizer and organic compounds obtaining involves using municipal and industrial wastes, organic fraction of garbage and other fermentable organic waste.    USE - Method for obtaining methane, hydrogen, fertilizer and organic compounds for industrial purpose.
NOVELTY - Invention relates to agriculture and can be used to process poultry droppings and pig manure. The method involves delivering components of the mixture to a platform with a solid coating, moulding two spaced-apart rollers from a water-absorbing agent at the platform, applying a layer of the water-absorbing agent and a layer of manure mass in the space between the rollers, selecting components of the mixture, mixing said components, stacking and subsequent natural composting of the obtained mixture. The water-absorbing agent used is chicken droppings with underlying material with moisture content 15-45%. The manure mass used is chicken droppings without underlying material with moisture content 50-75%. The components of the mixture also include pig manure with moisture content 70-96%. The layer of pig manure is placed on the layer of manure mass and said components are taken in weight ratio (0.9:1.2):(3.3:3.6):(1.1:1.4), respectively. Natural composting is carried out for not less than 30 days in the warm season and for not less than 90 days in the cold season. Initial heating of the mixture takes 7-10 days. During natural composting, the mixture is mixed at least twice. Composting is carried out in a pile.    USE - Chemistry.    ADVANTAGE - Invention enables to process chicken droppings with underlying material, chicken droppings without underlying material and pig manure into organic fertiliser, thus improving the environment when producing poultry and pig farming products. 2 cl, 2 tbl, 1 ex
NOVELTY - A biomass fast thermal cracking device comprises an automatic feeding device; a quality mass flow meter having nitrogen inlet; a gas pre-heater; a thermal cracking reactor having a discharging opening; a chilling mechanism; a separator having a steam outlet connected to inlet of the chilling mechanism; a carbon collector; a cooler; a circulating pump; a temporary storage tank; a second oil collecting tank (1); a water-cooling condenser (2); an oil collecting tank; a water condenser (3); and an oil gathering tank.    USE - A biomass fast thermal cracking device.    ADVANTAGE - The device has high yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of biomass fast thermal cracking.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a biomass fast thermal cracking device.    Second oil collecting tank (1)    Water-cooling condenser (2)    Water condenser (3)
NOVELTY - Producing food waste compost, involves subjecting the waste to primary anaerobic fermentation tub for performing fermentation in the tub using anaerobe e.g. Lactobacillus, drying the fermented material to obtain primary decomposed compost, subjecting the first decomposed compost to secondary fermentation in the aerobic condition using e.g. Saccharomyces to obtain secondary product as completely decomposed manure.    USE - The method is useful for producing food waste compost (claimed) for producing manure.    DETAILED DESCRIPTION - Method of producing food waste compost, involves obtaining food waste, removing foreign substance from food waste through refining process using vibrator, packaging refined food waste, reducing the moisture content of the food waste to 45-50%, subjecting the moisture reduced waste to primary anaerobic fermentation tub in which moisture content is adjusted to 73-76%, maintaining the temperature of the sealed anaerobic fermentation tub at 40 degrees C, with 40?, performing fermentation in the tub using anaerobe of Lactobacillus, Staphylococcus, Streptococcus, Pseudomonas, and Enterobacter, drying the fermented material at 60 degrees C for 12-24 hours to obtain primary decomposed compost having moisture content of 45-55%, and subjecting the first decomposed compost to second aerobic fermentation tank for performing the secondary fermentation in the aerobic condition using Saccharomyces, heat-resistance sporophytic Bacillus, and Aspergillus at 60 degrees C for 12-24 hours to obtain secondary product as completely decomposed manure. An INDEPENDENT CLAIM is included for compost of food waste produced by above-mentioned method.
NOVELTY - Bacillus laterosporus (I) under a preservation number of CGMCC No. 5090 in China microbial culture preservation management committee common microorganism center, is new.    USE - (I) is useful for preparing B. laterosporus microorganism inoculant and microorganism fertilizer (all claimed). Tests details are described but no results given.    ADVANTAGE - (I) can be isolate in high yield and has stable property by domesticating. (I) has high count and long service life.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) B. laterosporus microorganism inoculant obtained by culturing the B. laterosporus, fermenting, mixing with grass, and pelletizing to obtain the product; and (2) a microorganism fertilizer formed by mixing B. laterosporus microbe strain agent, normal fertilizer and/or organic carrier.
NOVELTY - Para-transformation of solid waste into organic fertilizer and biogas involves optimizing recovery of useful inorganic waste, where process variables such as level of acidity, temperature and pH of fermentation product are examined. Concentration of methane in biogas and amount of nutrients are determined from the waste product. A vision system detects materials of waste, where a magnetic detector separates ferrous materials. The organic waste is crushed and ground before bio-digestion of fermentation material.    USE - Method for para-transformation of solid waste into organic fertilizer and biogas as alternative energy source.    DETAILED DESCRIPTION - Para-transformation of solid waste into organic fertilizer and biogas involves optimizing recovery of useful inorganic waste, where process variables such as level of acidity, temperature and pH of fermentation product are examined. Concentration of methane in biogas and amount of nutrients are determined from the waste product. A vision system detects materials of waste, where a magnetic detector separates ferrous materials. The organic waste is crushed and ground before bio-digestion of fermentation material. The crushed waste is placed in a mixer and then homogenized with adding water to obtain slurry with 80% of humidity. The homogeneous mixture is inspected through a tunnel spectrometry to analyze chemical composition of the mixture. A monitoring system and supervisory control system receive signals from sensors, where a screen displays properties of product.
NOVELTY - Method for producing biodiesel, involves adding 1-20 wt.% of substrate, and 10-50 wt.% of concurrent lipase in which non-regioselective lipase and 1,3-regioselective lipase are concurrently fixed, and processing the mixture at 36-54 degrees C and at agitation speed of 160-340 revolutions per minute.    USE - The method is useful for producing biodiesel (claimed).    ADVANTAGE - The immobilized lipase can be recycled and used.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biodiesel, which is produced by the above-cited method.
NOVELTY - A composition comprises (in parts weight) pyroligneous liquor (100) containing rare earth (0.5-3) having an average particle size of 300-500 mesh, and fermented liquid manure (100-150). The fermented liquid manure is obtained by mixing (in wt.%) natural organic mixture (85-92), effective microorganisms (EM) stock solution (3-5), and molasses (5-10), and fermenting for 6-9 months. The natural organic mixture is obtained by mixing rice bran, cornstalk cut to 5-10 cm, and oil cake in a weight ratio of 1:1.5-2.5:1-3 with water (6-8 times).    USE - The composition is useful for managing functional lawn, and preventing functional lawn from harmful insects.
NOVELTY - High efficient agriculture and forestry biomass based heat, energy and power generating fertilizer comprises hydrogen producing nanometer material produced using a special hydrogen producing equipment, capable of generating electricity.    USE - The high efficient agriculture and forestry biomass based heat, energy and power generating fertilizer is useful for protecting the ecological environment of urban and rural, developing the national economy, and increasing agricultural production.    ADVANTAGE - The high efficient agriculture and forestry biomass based heat, energy and power generating fertilizer does not discharge carbon dioxide, and the generating waste is used for producing agricultural high efficiency fertilizer, thus the fertilizer is environmentally-friendly, economical, and has high environmental, economical and social benefits.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing high efficient agriculture and forestry biomass based heat, energy and power generating fertilizer, which involves mixing new nanometer hydrogen producing material, agriculture and forestry biomass, microorganism fermentation and crushed substance in a mass ratio of 0.01-10000:10000-0.01:0.01-10000:10000-0.01.
NOVELTY - Invention relates to complex treatment and recovery of fish wastes for production of organic fertilisers. Proposed method comprises loading the mix of organic wastes in reactor, heating it and anaerobic fermentation. Fish press water is used as said mix of organic wastes. Said press water is heated to 80-90 degrees is separated to suppress and extract residual fish oil. Liquid fraction is loaded into reactor for anaerobic fermentation at 50-55 degrees C at constant mixing for 2-3 weeks. Obtained liquid fertiliser is fed into cooling reactor wherein oxygen ingress is either partially limited or completely inhibited. Temperature id reduced for 2 days to 0 degrees C to minus 10 degrees C. Thereafter, fertiliser is packed.    USE - Process engineering.    ADVANTAGE - Higher quality of finished products, better ecology.
NOVELTY - A microbial organic fertilizer comprises (in weight parts) Effective Microorganism (EM) soil modifier (5-8), wormcast (60-63), EM initial liquid (0.5-1) and chlorine-free wafer (34.5-28), where the microbial organic fertilizer is prepared by fermenting for 6-7 days in the condition of sealing and depositing.    USE - Microbial organic fertilizer for restraining continuous cropping obstacle of flue-cured tobacco.    ADVANTAGE - The fertilizer has high efficiency and does not affect soil, so that soil structure and moisture containing function of the soil can be improved. The fertilizer improves disease-proof function of flue-cured tobacco and photosynthesis of the tobacco, thus improving quality of the tobacco leaf without public hazard. The fertilizer has wide market foreground and better social and economic benefit in production of the flue-cured tobacco.
NOVELTY - A soil stabilizing agent comprises combination of mineral component (1-99 vol.%) containing alginite, and biological compost (1-99 vol.%) as an active substance, where the compost is obtained by aerobic fermentation of waste sludge from the production of penicillin, thymidine and/or threonine, optionally along with pre-composted mycelium without residual penicillin and mixed in sawdust.    USE - Soil stabilizing agent.    ADVANTAGE - The soil stabilizing agent has improved fertilizing activity.
NOVELTY - Biomass is heated (A) at heating temperature (I), and the obtained gasified product (a1) or biomass residue (a2) is heated (B) at heating temperature (II) higher than heating temperature (I).    USE - Method for obtaining useful organic compound by pyrolyzing plant biomass, e.g. lignin-derived decomposition product containing phenol or cresol, and hemicellulose-derived decomposition product containing furan (all claimed).    ADVANTAGE - The method enables convenient extraction of useful organic compounds from plant biomass, by heat treatment alone.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of the method for obtaining useful organic compound by pyrolyzing plant biomass.    Heating processes (A-D)    Gasified product (a1,c1,d1)    Biomass residue (a2,c2,d2)    Product (b1)
NOVELTY - A sulfur concentration maintaining method involves combining sulfur and carbonaceous material to produce a sulfur containing carbonaceous feed. A portion(s) of sulfur containing carbonaceous feed is gasified to produce a syngas. A sulfur concentration in the syngas is detected. An amount of the sulfur combined with the carbonaceous material is adjusted based on the detected sulfur concentration.    USE - Method for maintaining a sulfur concentration in a syngas to reduce metal dusting in downstream components of gasifier(s).    ADVANTAGE - The method enables reducing the metal dusting in downstream components of gasifier(s) in a simple and effective manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram illustrating a gasification system for producing a syngas.    Gasification system (100)    Lock hopper or storage bin (110, 130)    Feeder (120)    Gasifier feed system (140)    Gasifier (150)
NOVELTY - A wooden tar-manufacturing apparatus (1) has gasifier (5) in which biomass thermally decomposes to generate carbonized material and pyrolysis gas and generated hot pyrolysis gas is heat-exchanged with clean gas at normal temperature, heat exchanger (6) which cools pyrolysis gas to temperature which condenses wooden tar in pyrolysis gas, and tar tank (8) which recovers the wooden tar condensed with cooling of pyrolysis gas.    USE - Apparatus is used for manufacturing wooden tar used as fuel.    ADVANTAGE - The apparatus enables efficient manufacture of wooden tar, without generation of byproduct.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of wooden tar.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the wooden tar-manufacturing apparatus. (Drawing includes non-English language text)    Wooden tar-manufacturing apparatus (1)    Gasifier (5)    Heat exchanger (6)    Tar tank (8)    Secondary combustion chamber (9)
NOVELTY - A tool (9) having upper tool section (9O), central tool section (9M) and lower tool section (9U) is provided on bipolar plate having anode plate and cathode plate. The metal substrate strips (5,6) are provided between upper tool section and central tool section and between lower tool section and central tool section for producing anode and cathode plates in time intervals (S1-S4).    USE - Device for manufacturing bipolar plate for fuel cell, used in fuel cell stack production apparatus (claimed).    ADVANTAGE - The manufacturing cost, production time and production cost of bipolar plate can be reduced. The bipolar plates can be produced with high degree of automation and with little manpower.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus for producing fuel cell stack.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the multi-stage tool.    Metal substrate strips (5,6)    Tool (9)    Individual tools (9.1-9.4)    Central tool section (9M)    Upper tool section (9O)    Lower tool section (9U)    Time intervals (S1-S4)
NOVELTY - The wood billet useful as burning firewood, is claimed, where the wood billet is derived from a tree timber (10), a wood block, and a wood panel. The firewood is implemented by a continuous aperture, which passes from one side of the wood billet to another side of the wood billet. The continuous aperture is a transverse aperture running continuously through the wood billet, where the aperture runs in a right angle (90 degrees ) or at an under angle deviating from 20-40 degrees , and is formed as millimeters of broad slot.    USE - The wood billet is useful as burning firewood.    DETAILED DESCRIPTION - The wood billet useful as burning firewood, is claimed, where the wood billet is derived from a tree timber (10), a wood block, and a wood panel. The firewood is implemented by a continuous aperture, which passes from one side of the wood billet to another side of the wood billet. The continuous aperture is a transverse aperture running continuously through the wood billet, where the aperture runs in a right angle (90 degrees ) or at an under angle deviating from 20-40 degrees , and is formed as millimeters of broad slot. A bored, milled or pressed recess is formed by the continuous aperture. The wood billet is opened or closed at an edge side of the continuous aperture, which forms a motif in the form of a symbol, an alphanumeric character and a pictogram or a graphic course. An INDEPENDENT CLAIM is included for a method for producing a wood billet derived from a tree timber.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic view of a tree timber (Drawing includes non-English language text).    Tree timber. (10)
NOVELTY - A recombinant beta -glucosidase (Bg11) variant comprising amino acid sequence having at least 80% homology to polypeptide comprising a 870 amino acid sequence (SEQ ID NO: 2) fully defined in the specification and comprising amino acid substitution Q291, D369 and E402, is new, where the positions are numbered with reference to SEQ ID NO: 2.    USE - The recombinant beta -glucosidase variant or method is useful for producing glucose, ethanol (claimed), and other soluble sugars from cellulosic biomass and biofuels.    ADVANTAGE - The recombinant beta -glucosidase polypeptide variant has increased thermo stability and/or increased thermo activity, compared to wild type C1Bg11 protein.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) enzyme composition comprising the recombinant Bg11 variant;    (2) method for producing glucose, involves incubating cellobiose with the recombinant Bg11 variant; and    (3) method for producing ethanol, involves incubating cellobiose with recombinant Bg11 variant in which glucose is produced, and incubating the glucose with at least one fermenting microorganism in a fermentation reaction under conditions.
NOVELTY - Integrated process is claimed, where the process uses lignocellulosic material and their fractions as raw material for single cell oil and alcohol production, and the alcohol production process uses enzymes from the single cell oil production process.    USE - The integrated process is useful for producing single cell oil and alcohol as a component of biofuel or as a starting material for biofuel production, where the biofuel is biodiesel or renewable diesel, gasoline and/or jet fuel (all claimed).    ADVANTAGE - The process improves biofuel production with: reduced down-stream processing costs including water and enzyme stabilization; decreased transportation and packaging costs; decreased losses by direct transfer of enzymes to second biofuel production process; decreased capital costs and the utilization of raw material for enzyme production and biofuel production in direct induction and adaptation of enzymes to the raw material; and straightforward process control and output tuning and improvement opportunities directly within the biorefinery in enzyme production and biofuel production.
NOVELTY - The apparatus has separation membranes (33,34) which are made from different materials. When the first mixed gas is supplied to the separation membrane (33), carbon dioxide and steam are passed through the first separation membrane (33) selectively, to separate a second mixed gas comprising carbon dioxide and steam. When the second mixed gas is supplied to the separation membrane (34), steam is passed through the separation membrane (34) selectively.    USE - Gas separation apparatus for membrane reactor used in hydrogen production apparatus (all claimed).    ADVANTAGE - Since the steam is separated from the mixed gas by passing through the separation membrane, the separated steam can be recycled. The energy utilization efficiency of gas separation apparatus is improved.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) membrane reactor;    (2) hydrogen production apparatus;    (3) gas separation method; and    (4) hydrogen production method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of hydrogen production apparatus. (Drawing includes non-English language text)    Hydrogen production apparatus (1)    Membrane reactor (20)    Processing units (32,36)    Separation membranes (33,34)    Circulation unit (38)
NOVELTY - Improved process of treatment applied to biomass from microalgae and macroalgae, comprises a physical-chemical treatment of the algal biomass using mixtures of organic solvents with inorganic acids at 100-200 degrees C, pressure of 101.14-303.42 kPa for 10-300 minutes, where the organic solvent is methanol and the inorganic acid is sulfuric acid.    USE - The method is used for improved process of treatment applied to biomass from microalgae and macroalgae (claimed).    ADVANTAGE - The method above provides increased fermentable-sugar hydrolysis yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a fermentation process comprising the product of the process above, and bacteria, yeasts and fungi, or their mixtures.
NOVELTY - The fuel production system has two apparatuses (12,14). The apparatus (12) generates carbon monoxide (CO) and hydrogen (H2) by electrolysis of CO2 and water. A apparatus (14) generates H2 by electrolysis of water. The apparatus (14) is strongly affected by fluctuation of the electric power, when electric power derived from natural energy is used, such that steady component of generated electric power is supplied to the apparatus (12).    USE - Fuel production system.    ADVANTAGE - The fuel production system can produce hydrocarbon fuel (HC) by using fluctuating energy effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the fuel production system. (Drawing includes non-English language text)    Electricity generation apparatus (10)    Apparatuses of fuel production system (12,14)    Electric power control and distribution apparatus (16)    Carbon monoxide and hydrogen storage apparatus (18)    Hydrogen storage apparatus (20)
NOVELTY - The instrument has a main body (6) whose inner part is provided with a direct current (DC) motor (4), where an output end of the DC motor is connected with a rod of a grinding head (1) by a clamping head. A lower part of an inner cavity of the clamping head is provided with a bottom cover of the main body. A cavity (8) is provided with a power source for supplying power for the DC motor. An inner wall of the main body is provided with ribs (5) for fixing the DC motor. A charging interface (10) is formed as a universal serial bus (USB) charging interface.    USE - Crushing instrument for use in a biomass film of a portable microcomputer.    ADVANTAGE - The instrument avoids damaging nucleic acid under quick crushing biomass membrane. The instrument ensures stable and reliable quality with quick and large mutation resistance to maintain constant rotating speed with improved grinding quality.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a crushing instrument in partial section.    Grinding head (1)    DC motor (4)    Ribs (5)    Main body (6)    Cavity (8)    Charging interface (10)
NOVELTY - Biomass drying carbonization furnace comprises high temperature gas and heat guide oil inlet, pipe beam assembly, high temperature gas inlet, left shaft assembly, feed port, seal head, cylinder body, scraper blade, high temperature gas ejection pipe beam, high temperature gas and heat guide oil heating pipe beam, right shaft assembly, high temperature gas and heat guide oil outlet, high temperature gas outlet, and material outlet.    USE - Biomass drying carbonization furnace.    ADVANTAGE - The furnace has improved biomass carbonization efficiency.    DETAILED DESCRIPTION - Biomass drying carbonization furnace comprises high temperature gas and heat guide oil inlet, pipe beam assembly, high temperature gas inlet, left shaft assembly, feed port, seal head, cylinder body, scraper blade, high temperature gas ejection pipe beam, high temperature gas and heat guide oil heating pipe beam, right shaft assembly, high temperature gas and heat guide oil outlet, high temperature gas outlet, and material outlet. The high temperature gas and heat guide oil inlet, pipe beam assembly, high temperature gas and heat guide oil heating pipe beam, and high temperature gas and heat guide oil outlet form an indirect heating pipeline. The high temperature gas inlet, pipe beam assembly, high temperature gas ejection pipe beam, and high temperature gas outlet form a high temperature gas ejection pipeline. The feed port, cylinder body, scraper blade, and material outlet form a biomass shaped particle carbonization space. The biomass drying carbonization furnace is in the form of a heat exchanger. The carbonization space composed of the cylinder body, seal head, and scraper blade can rotate around the pipe beam assembly.
NOVELTY - The value-added device comprises a cavity (1) for containing the sewage. The cavity has a slag discharge mechanism (2), a sewage input mechanism (4), an air intake slag washing mechanism (5) and a sewage level control discharge mechanism (6). An opening of the sewage level control discharge mechanism in the cavity is lower than an opening outside the cavity, and is located in the sewage in the cavity. An opening of the sewage level control discharge mechanism outside the cavity is coincident with the liquid level height required by the sewage in the cavity.    USE - The value-added device is useful for removing slag in sewage to generate methane.    ADVANTAGE - The value-added device ensures automatic and economical removal of slag without water source pollution thus efficiently generating methane with high quality.    DETAILED DESCRIPTION - The value-added device comprises a cavity (1) for containing the sewage. The cavity has a slag discharge mechanism (2), a sewage input mechanism (4), an air intake slag washing mechanism (5) and a sewage level control discharge mechanism (6). An opening of the sewage level control discharge mechanism in the cavity is lower than an opening outside the cavity, and is located in the sewage in the cavity. An opening of the sewage level control discharge mechanism outside the cavity is coincident with the liquid level height required by the sewage in the cavity. The openings of the slag discharge mechanism and the sewage input mechanism in the cavity are close to a bottom of the cavity. A methane storage cavity (3) connected with the cavity for containing the sewage is located on the cavity.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic view of a device for removing slag in sewage.    Cavity (1)    Slag discharge mechanism (2)    Methane storage cavity (3)    Sewage input mechanism (4)    Air intake slag washing mechanism (5)    Sewage level control discharge mechanism. (6)
NOVELTY - Composition (A) comprises a dispersion comprising and detergent comprising polyester quaternary ammonium salt, where the dispersion comprises: an organic phase; at least one amphiphile; and particles dispersed in the organic phase, of colloidal dimensions, consisting of an iron compound.    USE - The composition is useful as a fuel additive for internal combustion engines, preferably for the regeneration of diesel particulate filter, where the fuel is diesel fuels and biofuels (claimed).    ADVANTAGE - The composition is eco-friendly. The composition has high stability over time and an improved catalytic activity a relatively low concentration.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) fuel additive comprising a fuel and a composition; and    (2) method of implementation of an internal combustion engine comprising step of routing of a fuel and a composition to engine.
NOVELTY - The cell has a compartment (10) comprising an ion exchange membrane that separates oxidizing fluid and reducing fluid. Oxidizing and reducing fluid circulation systems (50, 52) circulate the oxidizing fluid and the reducing fluid along sides of the membrane based on different flow directions, respectively. The oxidizing and reducing fluid circulation systems have reversal systems (68, 78) that reverse the fluid flow directions in a cathodic fluid exchange pipe and an anodic fluid exchange pipe (16), respectively.    USE - Fuel cell for generating electric current from an oxidation-reduction reaction between oxidizing fluid i.e. pure dioxygen, and reducing fluid i.e. pure dihydrogen (all claimed), to supply the electric current to a motor vehicle, a boat or a transportable energy source requiring device.    ADVANTAGE - The oxidizing and reducing fluid circulation systems circulate the oxidizing fluid and the reducing fluid along the sides of the membrane based on the different flow directions, respectively, thus assuring satisfactory hydration of the membrane, and limiting the heterogeneity of hydration of the membrane. The reversal systems have simple design and are inexpensive so as to reduce the complexity and fabrication cost of the fuel cell.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for supplying oxidizing fluid and reducing fluid to a fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a fuel cell.    Compartment (10)    Anodic fluid exchange pipe (16)    Oxidizing fluid circulation system (50)    Reducing fluid circulation system (52)    Reversal systems (68, 78)
NOVELTY - Catalytic cracking of a lipid containing feedstock, comprises contacting the lipid-containing feedstock with at least one cracking catalyst at at least 450 degrees C to obtain a product stream; and separating at least one hydrocarbon fraction from the product stream, where the lipid containing feedstock comprises lipids derived from microalgae and further comprises a hydrocarbon feedstock.    USE - The process is useful in the catalytic cracking of a lipid containing feedstock to obtain a hydrocarbon fraction which is used in a gasoline product for a gasoline composition (claimed).    ADVANTAGE - The process: has improved efficacy; has a reduced carbon footprint; and provides a hydrocarbon stream that can be used to produce gasoline having improved research octane number.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a gasoline composition comprising a gasoline product prepared from a hydrocarbon fraction, sulfur (less than 1000 parts per million weight), and at least one additive.
NOVELTY - Process for catalytic cracking of a lipid containing feedstock, comprises contacting the lipid-containing feedstock with at least one cracking catalyst at at least 450 degrees C, to obtain a product stream; and separating at least one hydrocarbon fraction from the product stream, where the lipid containing feedstock comprises lipids derived from a diatomic microalgae species.    USE - The process is useful for: catalytic cracking of a lipid containing feedstock; and gasoline product, which is useful in gasoline composition (all claimed)    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a gasoline product prepared from a hydrocarbon fraction of the at least one hydrocarbon fraction; and    (2) a gasoline composition comprising the gasoline product, less than 1000 ppmw sulfur, and one or more additives.
NOVELTY - Catalytic cracking aquatic microbial biomass comprises contacting the aquatic microbial biomass with at least one cracking catalyst at a temperature of at least 450 degrees C to obtain a product stream; and separating one or more hydrocarbon fractions from the product stream.    USE - The process is useful for catalytic cracking aquatic microbial biomass (claimed).    ADVANTAGE - The invention provides an economical and efficient process for obtaining usable chemicals and fuel products from aquatic microbial biomass.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a hydrocarbon fraction obtainable by the process comprising amines, pyrroles, pyridines, quinolines, indoles, acridines and carbazole; and    (2) a gasoline composition comprising the hydrocarbon fraction, and further comprising at least one or more additives.
NOVELTY - Breaking water to hydrogen and oxygen using sunlight, is claimed.    USE - The process is useful for splitting water to hydrogen and oxygen, where the hydrogen is useful in hydrogen cells to produce electrical energy.    ADVANTAGE - The process: provides hydrogen, which is good to produce electricity and good to power a car; provides oxygen, which supports our life, saves nature and civilization; does not produce carbon dioxide, which is harmful for health and cause global warming; and is cheaper, take less time for installation of a new plant and production cost/unit of electricity is 1/10 of the present other processes.    DETAILED DESCRIPTION - INDEPENDENT CLAIM are also included for:    (1) scientific details and engineering design for procedure for breaking water to hydrogen and oxygen using sun light; and    (2) M-catalyst and its metallurgical details, physical and chemical properties.
NOVELTY - The method involves measuring climate parameter indicating climate in the interior (2) of motor vehicle (1) using a climate measuring device (5). A heat transfer device (6) is provided for transferring heat generated by a fuel cell (3) to the interior of vehicle. The rate of heat generated by the fuel cell is controlled by adjusting operating parameters of the fuel cell based on the climate parameter.    USE - Method for heating interior of motor vehicle.    ADVANTAGE - Temperature in the interior of vehicle can be controlled favorably according to the requirement of driver or passenger and the interior heating system can be simplified.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the motor vehicle.    Motor vehicle (1)    Interior (2)    Fuel cell (3)    Climate measuring device (5)    Heat transfer device (6)
NOVELTY - A garbage fermentation bin comprises a unit fermentation bin body and an air vent which is arranged at bottom part of the fermentation bin body and communicated with an external air supply machine (10). A ventilating channel (9) is arranged at bottom part of the unit fermentation bin body and communicated with the external air supply machine via the air vent. Panels at two sides of bottom part of the unit fermentation bin body for inclining towards the ventilating channel form a fermentation bin base plate. A percolate outlet is provided with a percolate pool (12).    USE - Garbage fermentation bin.    DETAILED DESCRIPTION - A garbage fermentation bin comprises a unit fermentation bin body and an air vent which is arranged at bottom part of the fermentation bin body and communicated with an external air supply machine (10). A ventilating channel (9) is arranged at bottom part of the unit fermentation bin body and communicated with the external air supply machine via the air vent. Panels at two sides of bottom part of the unit fermentation bin body for inclining towards the ventilating channel form a fermentation bin base plate. Lower base plate of the ventilating channel is inclined. The ventilating channel and a percolate channel (11) are the same channel. Lower base plate of the percolate channel is communicated with a percolate outlet on side wall of the fermentation bin. A percolate outlet is provided with a percolate pool (12).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a garbage fermentation bin.    Ventilating channel (9)    External air supply machine (10)    Percolate channel (11)    Percolate pool (12)    Fermentation bin feeding hole (13)
NOVELTY - Organic waste biochemical processor comprises a feeding port (1), a stirring device (2), a thermal insulation layer (4), a ventilating device, a power device (5), a chamber exchange port, a baffle plate, a discharge port and a frame. The processor further comprises multiple fermentation chambers (3), where each fermentation chamber is vertically stacked and combined and fixed by the frame. The feeding port is arranged at upper part of the fermentation chamber at the upper surface. The discharge port is arranged at the lower part of fermentation chamber at the lower surface.    USE - Used as an organic waste biochemical processor.    ADVANTAGE - The processor requires less surface area; utilize gravitational force, and reduce the energy input; can achieve multi-phase fermentation by using multiple fermentation chambers, and can feed new material continuously; and can assure that the produced fertilizer does not contain new material, which is not totally fermented.    DETAILED DESCRIPTION - Organic waste biochemical processor comprises a feeding port (1), a stirring device (2), a thermal insulation layer (4), a ventilating device, a power device (5), a chamber exchange port, a baffle plate, a discharge port and a frame. The processor further comprises multiple fermentation chambers (3), where each fermentation chamber is vertically stacked and combined and fixed by the frame. The feeding port is arranged at upper part of the fermentation chamber at the upper surface. The discharge port is arranged at the lower part of fermentation chamber at the lower surface. The adjacent fermentation chambers are connected through the chamber exchange port.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the organic waste biochemical processor.    Feeding port (1)    Stirring device (2)    Fermentation chambers (3)    Thermal insulation layer (4)    Power device (5)
NOVELTY - Producing ethanol from the fermentation of xylose, involves culturing a yeast strain in contact with a xylose-containing material under suitable conditions for a period of time sufficient to allow fermentation of at least a portion of the xylose to ethanol.    USE - The method (M1) is useful for producing ethanol from the fermentation of xylose. The method (M2) is useful for producing xylitol from xylose (claimed). The ethanol is useful as fuel.    ADVANTAGE - The method is cost-effective and easy.    DETAILED DESCRIPTION - Method (M1) of producing ethanol from the fermentation of xylose, involves culturing a yeast strain in contact with a xylose-containing material under suitable conditions for a period of time sufficient to allow fermentation of at least a portion of the xylose to ethanol, where the yeast strain comprises a nucleic acid comprising a coding sequence operably linked to a promoter not natively associated with the coding sequence, and the coding sequence encodes a glucose/xylose transporter polypeptide which is capable of exhibiting at least 80% homology polypeptide comprising a 566 or 550 amino acid sequence (SEQ ID NO: 2 or 4) fully defined in the specification. An INDEPENDENT CLAIM is included for method (M2) of producing xylitol from xylose, involves culturing the yeast strain in contact with a xylose-containing material under suitable conditions for a period of time sufficient to allow conversion of at least a portion of the xylose to xylitol.
NOVELTY - Producing a polyol, involves: providing an alcohol reactant comprising unrefined crude glycerine, where the unrefined crude glycerine is a by-product of a transesterification process of non-petroleum oil sources for producing biodiesel fuel, where the unrefined crude glycerine includes fatty acid (at least 30 wt.%) of the unrefined crude glycerine; and heating the alcohol reactant to a sufficient temperature for a sufficient time to produce a liquid polyol where the liquid polyol is capable of being reacted with an isocyanate to produce a useful polyurethane.    USE - For producing a polyols from crude glycerine/ligand cellulosic biomass. The polyol is further used to form polyurethanes (claimed) useful in foams and elastic products such as in the construction industry and in applications such as furniture, mattresses, shoe soles, automobile seats, sun visors, steering wheels, arm rests, door panels, noise insulation parts and dash boards.    ADVANTAGE - The polyol has a viscosity falling of 100-50000 cP at 25 degrees C; a hydroxyl number of 200-800 (preferably 150-750) mg KOH/g; and an acid number of 0.5-5 mg KOH/g, or 5 mg KOH/g.
NOVELTY - A biologically active solution preparing process involves adding nutrients in the form of sugars and proteins to biomass to achieve a carbon-nitrogen (C:N) ratio of 1:18 and diluting the mixture, where the solid content in the solution is 2-6 wt.%. The resulting solution is anaerobically fermented at 35-60 degrees C using anaerobic fermentation biogas in a biogas reactor.    USE - Process for preparing a biologically active solution that is utilized for dry fermentation of biomass.
NOVELTY - Electrochemical synthesis of hydrogen peroxide, comprises reacting oxygen and hydrogen in the presence of a catalyst comprising at least gold and palladium deposited on a carrier, where the molar ratio of gold to palladium is higher than 1:1, preferably greater than or equal to 5:1.    USE - The process is useful for electrochemical synthesis of hydrogen peroxide in a fuel cell (all claimed).    ADVANTAGE - The process: is environmentally friendly; is operated under mild operating conditions, with a reduced energy usage; is suitable for on-site/on-demand production of hydrogen peroxide, among others due the small size of the production devices; is safer than catalytic hydrogen peroxide direct synthesis, as hydrogen and oxygen are introduced separately which avoids hydrogen and oxygen mixing thus minimizing the risk of hydrogen/oxygen explosions; provides hydrogen peroxide having a high purity and high strength; and utilizes bimetallic catalyst system that improves stability of the produced hydrogen peroxide, thus resulting in an improved productivity.
NOVELTY - Method for preparing powder fuel, involves selecting rice raw materials, removing foreign materials including soil and stone from the raw material, subjecting the product for thermal decomposition for obtaining rice straw, crushing the obtained product and preparing fuel from the product.    USE - The method is useful for preparing powder fuel.    ADVANTAGE - The powder fuel has improved energy yield, reduced hygroscopic property and storage stability.
NOVELTY - The bio-organic fertilizer comprises sludge (55-65%), conditioner (0.5-0.75%), straw (25-35%), humic acid (5-15%), rotten agent (0.01-0.02%), and adjusting agent comprising sodium polyacrylate, where the bio-organic fertilizer is prepared by mixing the sludge, conditioner, straw, humic acid and rotten agent and then fermenting at 10 degrees C, stacking the Angel yeast (2-3%) at 55-65 degrees C, controlling the fermentation at 55-60 degrees C for 5-7minutes, and continuously decomposing for 3-5 days to obtain the urban sludge bio-organic fertilizer.    USE - Used as a bio-organic fertilizer. No biological data given.    ADVANTAGE - The bio-organic fertilizer can be simply and economically prepared with high efficiency and quality in an environmentally friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing bio-organic fertilizer using city sludge.
NOVELTY - A carbon-containing material is reacted with steam (EE) in the presence of a catalyst, to generate synthetic gas containing hydrogen, carbon monoxide and/or carbon dioxide. A portion of the synthesis gas is subjected to a combustion process and/or hydrogen and carbon monoxide are separated from the synthetic gas, to generate carbon dioxide rich gas. The obtained carbon dioxide rich gas is provided to synthetic gas containing hydrogen, carbon monoxide and/or carbon dioxide.    USE - Gasification of carbonaceous material e.g. coal, biomass and coke used for manufacture of device for separation, collection and storage of greenhouse gas.    ADVANTAGE - The method enables gasification of carbonaceous material by economical process.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of gasification of carbonaceous material. (Drawing includes non-English language text)    Supplied material (AA)    Ash (CC)    Synthesis gas (DD)    Steam (EE)    Oxygen (FF)
NOVELTY - The apparatus has dry anaerobic biodegrading room that is filled with biodegradation waste. The gas stream bypass passage (23) is positioned within the dry anaerobic biodegrading room for accelerating the gas fuel generated in the dry anaerobic biodegrading room. The leachate water collecting basin (24) collects the leachate generated in the dry anaerobic biodegrading room. The warm water circulation pipe (18) maintains the temperature within the dry anaerobic biodegrading room.    USE - Dry anaerobic biodegrading apparatus.    ADVANTAGE - The biodegradable waste can be processed environment-friendlily at low cost. The residual solid whole quantity generated in the dry anaerobic biodegrading of the biodegradation property waste is produced and used as the solid fuel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for dry anaerobic and solid fuel manufacturing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the dry anaerobic biodegrading apparatus.    Injection door (11)    Outflow door (13)    Warm water circulation pipe (18)    Gas stream bypass passage (23)    Leachate water collecting basin (24)
NOVELTY - Methanol gasoline comprises (pts.wt.) methanol (33-53), gasoline (40-65), additive (5.8-8), detergent (0.1-0.5), and corrosion inhibitor (0.1-0.5).    USE - Methanol gasoline.    ADVANTAGE - The methanol gasoline is stable, and reduces exhaust gas carbon monoxide, hydrocarbon and nitrogen oxide emissions. It is environment friendly. It uses additive with sufficient combustion power, and has water absorption, anti-swelling and corrosion property. The methanol gasoline replaces Nos. 90, 93, and 97 gasoline. It is energy saving, low cost, and economical.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of methanol gasoline by adding raw materials in reaction kettle at normal pressure and temperature; and stirring and dispersing for 20-30 minutes to uniformly mixed raw materials and to obtain finished product.
NOVELTY - Method for processing surplus sludge of papermaking wastewater into afforestation fertilizer, involves dehydrating residual sludge of papermaking wastewater through biological treatment, mixing the dehydrated sludge with crushed inorganic impurities and wheat straw material uniformly, granulating the mixture, drying the granules using coal burning boiler flue gas until the water content of the granule is 15% or less, uniformly spraying Bacillus subtilis bacterial liquid (3-5 %mass) on the granules, and drying the granules.    USE - The method is useful for processing surplus sludge of papermaking wastewater into afforestation fertilizer.    DETAILED DESCRIPTION - Method for processing surplus sludge of papermaking wastewater into afforestation fertilizer, involves dehydrating residual sludge of papermaking wastewater through biological treatment, where the water content in the sludge is not greater than 75%, mixing the dehydrated sludge with crushed inorganic impurities and wheat straw material uniformly, granulating the mixture, drying the granules using coal burning boiler flue gas until the water content of the granule is 15% or less, uniformly spraying Bacillus subtilis bacterial liquid (3-5 %mass) on the granules, and drying the granules.
NOVELTY - Selenium-enriched rapeseed meal fertilizer is prepared by (a) adding animal excrement, leftover food, residues and rapeseed meal to fermentation tank, adding suitable amount of water, covering the fermentation tank and fermenting the mixture, (b) adding water continuously to the mixture and fermenting the mixture, (c) filtering fermented liquid to obtain fertilizer mother liquor, and (d) adding sodium selenate to mother liquor, dissolving and stirring the mixture uniformly, and packaging the product.    USE - As selenium-enriched rapeseed meal fertilizer used for rice plants.    ADVANTAGE - The fertilizer improves organic selenium content in total selenium content of agricultural products and thus can be applied in low selenium areas and selenium levels of population in the area can be improved and associated diseases can be prevented or treated.    DETAILED DESCRIPTION - Selenium-enriched rapeseed meal fertilizer is prepared by (a) adding animal excrement, leftover food, residues and rapeseed meal to fermentation tank, adding suitable amount of water, covering the fermentation tank and fermenting the mixture for 40-50 days, (b) adding water continuously to the mixture until the solid content is dissolved completely and further fermenting the mixture for 20-40 days, (c) filtering fermented liquid through 100-200 meshes sieve to obtain fertilizer mother liquor, and (d) adding 3 kg of sodium selenate to each 100 kg of mother liquor, dissolving and stirring the mixture uniformly until precipitate is not formed, and packaging the product.
NOVELTY - Composite multicarbon alcohol cosolvent is prepared by taking (mass%) ethanol (40-70); propyl alcohol and isopropanol (5-15); n-butyl alcohol, isobutanol and tert-butanol (5-15); amyl alcohol, isopentanol, hexyl alcohol, heptanol, octanol, nonyl alcohol and decyl alcohol (1-5), and water (14-40); pretreating materials; subjecting material through pervaporation membrane to dehydrate; and regulating to obtain composite multicarbon alcohol cosolvent with water content of less than 0.5%.    USE - Composite multicarbon alcohol cosolvent.    ADVANTAGE - The composite multicarbon alcohol cosolvent has high hydrotropy than that of each monomer multicarbon alcohol, has lower toxicity than aromatic hydrocarbon alcohol oil cosolvent, and lower corrosivity than acetone alcohol oil cosolvent. It has preparation that overcomes difficulty to dewater by fractionation because boiling point of propyl alcohol, isobutanol and n-butyl alcohol is close to that of water, together with azeotropic effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of composite multicarbon alcohol cosolvent by pretreating raw materials by filtering or centrifuging solid particles to obtain water-containing multicarbon alcohol leftovers; subjecting alcohol leftovers through pervaporation membrane to dehydrate; heating in specific device at 70-95 degrees c by heat exchanger; delivering it to membrane machine contacted with macromolecule imporous compact composite pervaporation membrane via charging pump at 0.4 MPa; absorbing moisture; dispersing; and permeating via vaporizing film, such that permeated side of membrane is vaporized by 10 mmHg to condensed into liquid by - 10 degrees C saline condenser; collecting and removing; and regulating composite multicarbon alcohol to reach mass requirement of multicarbon alcohol cosolvent and to guarantee product quality of composite multicarbon alcohol cosolvent.
NOVELTY - Generating methane by fermenting ammonia pre-processed wheat stalk, is claimed, where methane is prepared from pre-treating wheat stalk through performing completely mixed anaerobic fermentation.    USE - The method is useful for generating methane by fermenting ammonia pre-processed wheat stalk (claimed).    ADVANTAGE - The method improves the energy efficiency and is harmless. The method provides considerable high clean energy from wheat straw. The operation with wheat straw is simple and cheap, and the condition is mild. The use of marsh gas compared with direct use of wheat straw, improves the total yield, production and utilization rate. The raw material gas is more stable, and avoids the floating slag crust. The fermentation period is greatly shortened.
NOVELTY - Method for producing agent containing dextran 1000, involves culturing Leuconostoc intestinal membrane in shaking culture, sterilizing the product, fermenting the product, inoculating the product to seed culture, sterilizing the product, subjecting the product to alcohol precipitation, fermenting the product, subjecting the product to alcohol hydrolysis, drying the product, adding sodium hydroxide to the medium, and spray drying the product to obtain dextran.    USE - The method is useful for producing agent containing dextran 1000 for treating biological sewage (claimed) and industrial wastewater.    ADVANTAGE - The method is inexpensive and less labor intensive, consumes less energy and has excellent adaptability and production efficiency.    DETAILED DESCRIPTION - Method for producing agent containing dextran 1000, involves culturing Leuconostoc intestinal membrane in shaking culture at 25-28 degrees C for 25 hours, where the culture medium comprises (in g/l): sucrose (10), peptone (0.3), magnesium sulfate heptahydrate (0.5), dipotassium (0.1), and acetate (0.1), sterilizing the product at 121 degrees C for 15-20 minutes, fermenting the product at 25-28 degrees C for 25 hours, inoculating at least 1% of product to seed culture, where the seed culture medium comprises (g/l): sucrose (120), corn pulp (10), disodium potassium (1), magnesium sulfate heptahydrate (0.1), ferrous sulfate heptahydrate (0.1), and sodium chloride (0.1), sterilizing the product at 121 degrees C for 15-20 minutes, subjecting the product to alcohol precipitation, fermenting the product at 80 degrees C for 2 hours, subjecting the product to alcohol hydrolysis using 3-8 %mass of diluted sulfuric acid for 1 hours at 100 degrees C, drying the product, adding sodium hydroxide to the medium, and spray drying the product to obtain 50 %mass of dextran.
NOVELTY - Garbage cleaning, hydrogen energy generating and organic compound fertilizer generating material, comprises anti-pollution nanomaterial sterilization new garbage processed material, and a special garbage hydrogen generating material.    USE - The garbage cleaning, hydrogen energy generating and organic compound fertilizer generating material is used to generate electricity (claimed).    ADVANTAGE - The material is suitable for development of national economy, good harvest and urban environment of agriculture and for all places, economical, and has zero discharge and zero pollution. Urban garbage pollution becomes serious, until 2009, the garbage total amount is 3.25 billion tons, two-thirds of the city of the whole nation is surrounded by a seat of garbage, therefore, the garbage pollution is a trouble that every local government faces. The green nanometer new material garbage treatment has garbage clean new energy hydrogen energy power generation and uses remainder for producing efficient fertilizer.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) organic compound fertilizer comprising trash hydrogen generating residue and microbial leavening for microbial fermentation, after fermentation, which are mixed in predetermined amount, processed in advanced biological fertilizer production line, and respectively measuring and packaging to obtain the finished product; and    (2) production of the garbage cleaning, hydrogen energy generating and organic compound fertilizer generating material, which involves mixing the sterilized anti-pollution nanomaterial, garbage, and microbial fermentation material in a ratio of 0.01-10000:10000-0.01 or 0.01-10000:10000-0.01.
NOVELTY - A Streptomyces H323 capable of producing adriamycin or its analog, is new.    USE - The Streptomyces H323 is used for producing adriamycin or its analog (claimed).    ADVANTAGE - The method produces adriamycin by direct fermentation, and thus the method is cost-effective and reduces environmental pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing adriamycin or its analog, which involves aerobically fermenting the Streptomyces H323 in a nutrition culture medium containing assimilable carbon source and nitrogen source.
NOVELTY - Chitosan biomass complex is obtained by adding bacterial biomass to chitosan.    USE - As chitosan biomass complex.    ADVANTAGE - The chitosan biomass complex improves adsorption performance, and is easily applied to process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the above-mentioned complex, which involves stirring mixture containing the bacterial biomass, chitosan, and acid solution to obtain mixture, and curing the mixture by adding alkaline solution to the mixture.
NOVELTY - The device has screen filter unit that filters powdered sludge complex. The kneader transfers and mixes sludge complex ejected in the water tank. The aging tank mixes the sludge complex supplied from the kneader. The bunker coal molding unit carbonizes the sludge complex in the aging tank. The exhausting unit dries the bunker coal in bunker coal molding unit by hot air.    USE - Fuel manufacturing device.    ADVANTAGE - The flying of the fine dust generated among the process of manufacturing the bunker coal is prevented.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel manufacturing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the fuel manufacturing device.
NOVELTY - Method of producing low-sulphur diesel fuel and high-octane naphtha is characterised by that the output stream of distillate from the hydrodesulphurisation reaction zone and the output stream from the hydrocracking reaction zone, supplied with dealkylated, high-aromatic material, are mixed and separated to obtain a gas stream of hydrogen, low-sulphur diesel fuel and high-octane naphtha.    USE - Chemistry.    ADVANTAGE - Feeding hydrogen as a source of hydrogen for the hydrodesulphurisation reaction zone minimises the load on the recirculation compressor, and use of a common separation and fractionation zone gives the advantage of lower capital and operational costs. 10 cl, 1 dwg, 2 tbl, 1 ex
NOVELTY - A surface-modified copper component is obtained by forming an oxide layer containing cuprous oxide by heat-processing the surface of a substrate containing copper (alloy) in an atmosphere of chemical species containing carbon and oxygen, supplied to the surface.    USE - Manufacture of surface-modified copper component useful as catalyst component in organic synthesis of ethylene and ethane (all claimed).    ADVANTAGE - The method enables easy and economical manufacture of surface-modified copper component having excellent catalytic activity and durability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) catalyst component consisting of the oxide layer formed on the surface of substrate; and    (2) organic synthesis method, which involves immersing an anode (14) and a cathode (15) in an electrolyte solution (11), and carrying out electrochemical reduction of carbon dioxide to synthesize an organic compound, selectively synthesizing 2C or more organic compound. The catalyst component is used as the cathode.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the apparatus used for organic synthesis.    Electrolyte solution (11)    Electrolysis chamber (12)    Anode (14)    Cathode (15)    Gas-diffusion component (16)
NOVELTY - The invention relates to a process for obtaining black coal and to the use thereof in agriculture. According to the invention, the process consists in carbonizing maize vegetable wastes and comprises the following stages: mechanically breaking the waste down to a size of 10...15 cm, drying it naturally or in furnaces at 175 degrees C, charging 0.6...0.7 m3 of biomass into the furnace and carbonizing it under a controlled CO2 atmosphere at 1.1...1.25 bar and 330...365 degrees C, for 3...3.5 h, thereby resulting black vegetable coal with an efficiency of 23...32% after drying. The black carbon is administered into the soil, upon setting up fruit farming plantations, by 30...40 cm-deep furrow, or, in case of in bearing tree plantations, by discing at a depth of 15...20 cm, in order to ameliorate the soil physical, chemical and biological properties.
NOVELTY - Integrated device for converting municipal sludge to a biological coal, comprises a pneumatic vacuum pressure conveyor; where a material outlet of the pneumatic vacuum pressure conveyor is connected with a motor. The pneumatic vacuum pressure conveyor is connected with a material unloading hopper. The material unloading hopper is connected with a material storage tank, where a stirring machine is installed in the material unloading hopper. The one end of a material conveying pipeline of the positive pressure conveying device is connected with a material storage hopper.    USE - The integrated device is useful for converting municipal sludge to a biological coal.    ADVANTAGE - The device conveys the powder material in a closed way, recycles the waste, has multiple conveying points and is eco-friendly.    DETAILED DESCRIPTION - Integrated device for converting municipal sludge to a biological coal, comprises a pneumatic vacuum pressure conveyor; where a material outlet of the pneumatic vacuum pressure conveyor is connected with a motor. The pneumatic vacuum pressure conveyor is connected with a material unloading hopper. The material unloading hopper is connected with a material storage tank, where a stirring machine is installed in the material unloading hopper, and a positive pressure conveying device is provided below the material unloading hopper. The one end of a material conveying pipeline of the positive pressure conveying device is connected with a material storage hopper, and the other end is connected with a conveying motor.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of the integrated device for converting municipal sludge to a biological coal.
NOVELTY - Enzymes are produced by cultivating microorganism capable of producing both single cell oil and enzymes under conditions for single cell oil production and enzyme production in a single cell oil production process, and producing single cell oil and enzymes by the microorganisms; and obtaining microorganism culture comprising single cell oil and enzymes, and recovering part of microorganism culture, supernatant and/or microorganism cells, protein fraction enriched from the supernatant, and/or protein fraction from the cells.    USE - Method for producing enzymes/lipids used as biofuel, component of biofuel or as a starting material for biofuel production, the biofuel being biodiesel or renewable diesel, gasoline and/or jet fuel (claimed).    ADVANTAGE - The method enables upgrading the economy of large-scale single-cell oil production, while reducing environmental burden caused by large-scale single-cell oil production.    DETAILED DESCRIPTION - Producing enzymes comprises cultivating microorganism capable of producing both single cell oil and enzymes under conditions for single cell oil production and enzyme production in a single cell oil production process, and producing single cell oil and enzymes by the microorganisms; obtaining microorganism culture comprising single cell oil and enzymes, and recovering part of (i) the microorganism culture, of (ii) the supernatant and/or microorganism cells separated from the microorganism culture, of (iii) protein fraction enriched from the supernatant, and/or of (iv) protein fraction from the cells, for use as enzyme preparation or as source of enzymes; and recovering single cell oil from the microorganism cells.
NOVELTY - Integrated process for single cell oil production and pulp and/or paper industry process, comprises the use of organic material from the pulp and/or paper industry process as raw material for lipid production in the single cell oil production process, and the use of enzymes from the single cell oil production process in the pulp and/or paper industry process.    USE - The process is useful in the integration of single cell oil production process and pulp and/or paper industry process, where the single cell oils produced are used as biofuel, a component of biofuel or a starting material for biofuel production, where the biofuel is biodiesel, renewable diesel, gasoline and/or jet fuel (all claimed).    ADVANTAGE - The process: enables upgrading the economy of large-scale single cell oil production; reduces the environmental burden; provides a way to more complete utilization and valorization of the lignocellulosic biomass in pulp and/or paper industry processes; and improves cost-efficiency of pulp and/or paper industry processes.
NOVELTY - The method involves absorbing lignin-derived material and various materials inhibiting enzymatic activity using specific additive. Enzymatic saccharification or simultaneous saccharification of cellulose by cellulase is promoted. Fermentation process is performed.    USE - Treatment method for biomass.    ADVANTAGE - Lignin-derived material and various materials inhibiting enzymatic activity can be absorbed effectively using specific additive so that yield of sugar obtained from biomass is maximized.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for additive.
NOVELTY - Controlling growth of contaminant microorganisms in a fermentation process, comprises adding stabilized chlorine dioxide and a peroxide compound to at least one step of fermentation process, where the fermentation process comprises: providing a fermentation vessel; providing and introducing inoculant, fermentable sugar and process water separately or in any combination into the vessel to obtain a fermentation broth; and contacting the inoculant with the sugar in the vessel at a temperature at which the inoculant converts the sugar to ethanol.    USE - The method is useful for controlling growth of contaminant microorganisms a fermentation process.    ADVANTAGE - The method utilizes the combination of stabilized chlorine dioxide and peroxide compound that exhibit synergistic effect in controlling the growth of contaminant microorganisms without detrimental effect on the inoculant used in the fermentation process, and provides the treated carbohydrate feedstock that can remain stable for at least one month.
NOVELTY - Growth of contaminant microorganisms in a fermentation process is controlled by adding peroxide compound and a quat. ammonium compound to step(s) of fermentation process.    USE - Method of controlling growth of contaminant microorganisms in a fermentation process, preferably carbohydrate feedstock (claimed).    ADVANTAGE - The method is antibiotic-free, does not produce residues that accumulate in fermentation coproducts or give rise to antibiotic-resistant bacteria, can be done at a wide variety of pH ranges and conditions encountered in the fermentation industry, utilizes treatment that has a desired shelf life prior to use, and improves large volume fermentation processes.    DETAILED DESCRIPTION - Growth of contaminant microorganisms in a fermentation process is controlled by adding peroxide compound and a quat. ammonium compound to step(s) of fermentation process. The fermentation process comprises providing a fermentation vessel; providing an inoculant, a fermentable sugar and process water; introducing separately, or in any combination, the inoculant, fermentable sugar and process water into a fermentation vessel to provide a fermentation broth; and contacting the inoculant with the fermentable sugar in the fermentation vessel at a temperature at which the inoculant converts the fermentable sugar to ethanol.
NOVELTY - Obtaining a fuel from plant seeds or nuts, preferably from Jatropha seeds with a fat content of 30 wt.%, preferably at least 40 wt.%, and simultaneously obtaining a protein-rich bruised grain, comprises (a) separating shell fractions, (b) crushing the shelled seeds, (c) adding water and/or acid to the crushed plant seeds to form an oil-containing suspension, (d) depositing crude oil from the suspension, where the pH of the suspension prior to deposition of crude oil is less than or equal to 3.5, (e) oil polishing the oil or crude oil, (f) neutralizing, and (g) drying the oil.    USE - The method is useful for obtaining fuel from plant seeds or nuts, preferably from Jatropha seeds with a fat content of 30 wt.%, preferably at least 40 wt.%, and simultaneously obtaining a protein-rich bruised grain.    ADVANTAGE - The method produces fuel with high yield.    DESCRIPTION OF DRAWING(S) - The figure 1 shows a schematic representation of the system for obtaining a fuel from Jatropha seeds.    Grinder (1)    Buffer tank (2)    Stirrer (6)    Decanter (8)    Centrifuge (12)
NOVELTY - The process involves partially oxidizing carbonaceous feedstock/biomass with molecular oxygen-comprising gas to obtain synthesis gas comprising carbon monoxide and hydrogen. Carbon dioxide content of the synthesis gas is measured and compared with a pre-determined value range. Carbonaceous feedstock/biomass ratio is adjusted by changing a biomass feed rate. The carbonaceous feedstock/biomass is provided in a range from 10 weight percent to 50 weight percent of biomass. A level of biomass is adjusted within a range to control the carbon conversion.    USE - Process for controlling carbon conversion of a gasifier fueled with a carbonaceous feedstock by mixing in biomass. Uses include but are not limited to applications of power generation, production of hydrogen, fertilizer, Fischer tropsch liquids and other chemicals.    ADVANTAGE - The process enables controlling the carbonaceous feedstock conversion by mixing in biomass fuel in simple and energy efficient manner, providing the biomass with high oxygen content, and providing part of the oxygen required for full conversion of the carbonaceous feedstock, thus reducing the requirement of moderator gas such as steam. The minimum biomass fraction in the biomass/carbonaceous feedstock mixture eliminates the steam.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a system for producing and cleaning synthesis gas.    Gasification reactor (9)    Cooling section (10)    Fed via line (12)    Dry or wet solids removal unit (13)    Wet scrubber (15)
NOVELTY - A system for production of at least one biofuel, biofuel additive or biochemical comprises Fischer-Tropsch (FT) production apparatus comprising at least one FT reactor for production of FT hydrocarbons from synthesis gas; and upgrading apparatus (40) fluidly connected with FT production apparatus and configured to receive, via one or more inlets, first component comprising FT hydrocarbons and second component comprising biomass oil and decrease degree of unsaturation via hydrogenation.    USE - System for production of at least one biofuel, biofuel additive or biochemical (claimed).    ADVANTAGE - The products produced by the system exhibit improved physical properties that enhance cetane rating of diesel fuel when combined. The system is operable to convert triglycerides to diesel range materials having enhanced cetane number over that of the feedstock.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing biofuel or biochemical which comprises introducing first component comprising FT hydrocarbons and second component comprising at least one triglyceride into an upgrading apparatus to receive, via one or more inlets, first component and second component and decrease degree of unsaturation via hydrogenation, and extracting upgraded product comprising at least one component selected from group consisting of fuels and chemicals from the upgrading apparatus.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating a system for production of biofuels and/or biochemicals from Fischer-Tropsch hydrocarbons and biomass oil.    Synthesis gas production apparatus (10)    Synthesis gas clean-up apparatus (20)    Fischer-Tropsch conversion apparatus (30)    Upgrading apparatus (40)    Biomass supply apparatus (50)
NOVELTY - Degrading Organic Fraction of Municipal Solid Waste in stirred tank reactors, where semicontinuous regime runs in two phases of different temperatures: a first phase of thermophilic pretreatment regimen, and a second phase of treatment in mesophilic regime, the residue prehydrolyzed and solubilized from the previous pretreatment.    USE - The method is used for degrading Organic Fraction of Municipal Solid Waste in stirred tank reactors (claimed).    ADVANTAGE - The present invention provides a method for anaerobic digestion of municipal solid waste in temperature phases.
NOVELTY - Steam delivery system for biomass processing comprises compressor(s) (1, 5) for pressurizing low temperature water to greater than or equal to 5 bars; series of heat exchangers (2, 6) supplied with turbine steam (3, 7) from an electrical power generation plant for preheating pressurized low temperature water to temperatures of greater than or equal to 150 degrees C; and delivery mechanism (4, 8) for delivering the preheated, pressurized water as steam having pressure of greater than or equal to 5 bars to hydrothermal pretreatment reactor, distillation unit, evaporator, and/or dryer.    USE - The steam delivery system is used for biomass processing. It is used for providing steam to biomass processing facility (claimed). The system is used for delivering steam produced by electrical power generation plant to lignocellulosic biomass refinery.    ADVANTAGE - Because turbine steam is used only indirectly, to feed a pressurized water preheating train, steam delivery is not associated with any significant loss of high quality boiler water. The indirect steam delivery system is highly flexible in its steam pressure requirements. Relative to direct use of turbine steam, the overall energy cost associated with indirect use of steam to preheat pressurized water is offset by the savings of process energy provided by avoiding the requirement for replenishment of high quality boiler water.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for provision of steam to biomass processing facility.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of steam delivery system.    Compressor (1, 5)    Heat exchangers (2, 6)    Turbine steam (3, 7)    Delivery mechanism (4, 8)
NOVELTY - Modified alkylphenol-aldehyde resin obtained by a Mannich condensation of alkylphenol-aldehyde resin with at least one 1-8C aldehyde and/or 1-8C ketone and at least one hydrocarbon compound having at least one 4-30C alkyl monoamine or 4-30C alkyl polyamine (alkylamine), where the alkylphenol is substituted by at least one 1-30C alkyl, preferably monoalkylphenol, is claimed.    USE - The resin is useful: as additives for improving the cold properties of fuels and hydrocarbon liquid fuels; and in fuel and/or fuel having a boiling point of 120-500 degrees C, preferably 140-400 degrees C, preferably jet fuels, gas oils and diesel fuels, domestic oil and heavy fuel oil (all claimed).    ADVANTAGE - (I) improves the dispersion of paraffins and/or limits the sedimentation of paraffins in the fuel and liquid fuel based on hydrocarbon oils and whose middle distillates boiling temperature is 100-500 degrees C.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a fuel and liquid hydrocarbon fuel composition whose boiling temperature is 100-500 degrees C comprising a majority proportion of hydrocarbon compounds, vegetable or animal oils, ester oils and/or biodiesel from animal and/or plant and a minor proportion, preferably 5-5000 ppm by weight of at least one of the resins.
NOVELTY - The process involves selecting a key parameter e.g. compositional property and fluidization property, for an optimal biomass feedstock (24c) and determining an optimal value for the key parameter. Biomass feedstocks (20c, 22c) e.g. wood, are provided with values for key parameter. A cumulative biomass feedstock (19) comprising biomass feedstocks is introduced into a biomass conversion reactor (18) e.g. riser reactor, where the cumulative feedstock has a combined average value for the parameters. The cumulative feedstock is thermochemically converted in the reactor to produce bio-oil.    USE - Process for producing bio-oil from biomass.    ADVANTAGE - The process efficiently and effectively optimizes various properties of the cumulative biomass feedstock, thus providing the biomass feedstock with optimal properties that maximizes the quality and yield of the produced bio-oil.    DETAILED DESCRIPTION - The compositional property of the optimal biomass feedstock is selected from lignin content, mineral content, carbon content, hydrogen content, oxygen content, natural oil content, hemicellulose content, cellulose content, extractives content and water content. The fluidization property is density, particle cohesion force or particle size. The biomass feedstocks are selected from cotton linter, herbaceous plants, aquatic biomass, waste paper and mixtures. INDEPENDENT CLAIMS are also included for the following:    (1) a biomass conversion process for determining an optimal lignin content    (2) a biomass conversion system comprising a biomass source.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a biomass conversion system with multiple biomass feedstocks mixed before introduction into a biomass conversion reactor.    Biomass conversion system (10)    Biomass conversion reactor (18)    Cumulative biomass feedstock (19)    Biomass feedstocks (20c, 22c)    Optimal biomass feedstock (24c)    Analyzer (32)
NOVELTY - Biomass fuel structure for coal-based production of reduced iron, is claimed. The straw and leaves of crops are crushed to obtain cylindrical granular material with a diameter of 3-5 mm and length of 2-5 mm.    USE - Used as a biomass fuel structure for coal-based production of reduced iron.    ADVANTAGE - The structure has cylinder granular material bulk density of less than or equal to 0.60, large space, high amount of volatile matter, high carbon utilization rate and high product metallization rate; generates sufficient carbon monoxide and methane; enhances penetration of iron ore concentrate into oxygen element during reaction; reduces usage of coke to 10-15%; and is economical.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of the biomass fuel structure.
NOVELTY - The stove has a square shape stove body provided with a gas generator. A storage reaction chamber is provided with a distribution system. A main combustion chamber is equipped with a heating water jacket. A lower air distribution pipe is connected with an upper distribution tee joint. A gas inlet is connected with a gas converting pipe. An upper surface of an upper cover is provided with a gas mixture room. The heating water jacket is provided with an upper water inlet and an oil return water inlet. An upper part of a lower water seal groove is provided with a smoke switch.    USE - Biomass energy-saving stove for use in a multifunctional kitchen.    ADVANTAGE - The stove is inexpensive and environment-friendly. The stove realizes rated power for heating, ensures stable gas generation and saves energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a biomass energy-saving stove.
NOVELTY - The separator has an outer cylinder (4) arranged with a side wall of a biomass gasification furnace that generates a gas mixture. The gas mixture is passed to the outer cylinder and an inner cylinder (3). The outer cylinder is fixed at a side wall of an air inlet pipe (5) via the inner cylinder. The inner and outer cylinders are connected with an air outlet pipe (1). The inner cylinder is connected with a liquid outlet (7) via a connecting tube (6). The liquid outlet leads to the outer cylinder. The inner cylinder is arranged on a clapboard (2) that is provided with a vent hole (9).    USE - Biomass producer tar separator.    ADVANTAGE - The separator adopts a simple cyclone separating and dust removing baffle plate and an air filter composite structure in a better way so as to improve processing reliability and reduce maintenance workload. The separator has low resistance, and saves energy consumption.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a biomass producer tar separator.    Air outlet pipe (1)    Clapboard (2)    Inner cylinder (3)    Outer cylinder (4)    Air inlet pipe (5)    Connecting tube (6)    Liquid outlet (7)    Vent hole (9)
NOVELTY - The device has an inlet pipe (1) located at a middle lower part of a tank body (8). A ceramic filling layer (2) is covered on a middle upper part of the tank body. A liquid baffle (7) is located above the tank body. A tail gas outlet (3) is located at a top part of the tank body. The ceramic filling layer is provided with a discharge opening (6) and a manhole (5). The inlet pipe is connected with a buffer. The tail gas outlet is connected with a vacuumizing system.    USE - Oil, coke and tail gas separating device for use during bio-diesel rectifying process.    ADVANTAGE - The device can be prevented from being corrosion, and has high vacuum degree. The device improves working process in a stable manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of an oil, coke and tail gas separating device.    Inlet pipe (1)    Ceramic filling layer (2)    Tail gas outlet (3)    Manhole (5)    Discharge opening (6)    Liquid baffle (7)    Tank body (8)
NOVELTY - A wood powder (1) having moisture content of 4-13% and particle diameter of 60-70 meshes and Cryptomeria japonica (Japanese cedar) leaf powder (2) having particle diameter of 100-150 meshes are mixed. The mixture is heated at 40-60 degrees C for 2-5 hours, and fatty acid contained in leaf powder is permeated into wood powder to produce modified mixed powder. The modified powder is filled in a molding die, and heat-pressed at 190-210 kg/cm2. Joint solidification of wood powder and leaf powder is carried out, and wooden fuel pellet is manufactured.    USE - Manufacture of wooden fuel pellet (claimed).    ADVANTAGE - The wooden fuel pellet is reliably manufactured without using binder.    DETAILED DESCRIPTION - A wood powder (80-95%) having moisture content of 4-13% and particle diameter of 60-70 meshes and Cryptomeria japonica (Japanese cedar) leaf powder (5-20%) having moisture content of 4-13% and particle diameter of 100-150 meshes are mixed without adding binder. The mixture is heated at 40-60 degrees C for 2-5 hours, and fatty acid contained in leaf powder is permeated into wood powder to produce modified mixed powder. The modified powder is filled in a molding die, and heat-pressed at 140-190 degrees C and pressure of 190-210 kg/cm2. Joint solidification of wood powder and leaf powder is carried out such that lignin and cellulose are in molten state, and wooden fuel pellet of predetermined shape is manufactured.    DESCRIPTION OF DRAWING(S) - The drawing shows the explanatory view of coupling structure of wooden fuel pellet. (Drawing includes non-English language text)    Wood powder (1)    Japanese cedar leaf powder (2)
NOVELTY - Reducing the energy consumed by drying biomass and carbonaceous materials comprises preparing feedstock (1) to expose its moisture-containing structure; compacting the prepared material to form a compacted material (7); and separating liquid water (9) expressed during compaction from the compacted material to form a dried compacted material (11).    USE - Method for reducing the energy consumed by drying biomass and carbonaceous materials (claimed).    ADVANTAGE - The method can reduce thermal energy and cost required to dry the material to a specified level, and treats mixtures of particulate biomass and carbonaceous materials to form low-moisture, compacted products that possess uniform chemical and physical properties.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a biomass compacted material having a moisture content of 7-17 wt.%; and    (2) a method for forming a briquette comprising biomass and a carbonaceous material comprising sizing a first feed stream comprising biomass into a size that maximizes exposure of the porous structure of the biomass; compacting the sized first feed stream in a roll press (4) to rupture and collapse the first feed's porous structure and to express moisture held within the pores of the first feed stream material; communiting a second feed stream comprising mined or reclaimed carbonaceous materials; compacting the second feed stream in a roll press; combining the compacted first feed stream and the compacted second feed stream to form a combined material stream; and briquetting the combined material stream to form a briquette comprising processed and dried biomass and carbonaceous materials.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the method for reducing energy consumed by drying biomass and carbonaceous materials.    Feedstock (1)    Roll press (4)    Compacted material (7)    Water (9)    Dried compacted material (11)
NOVELTY - The charcoal briquette (1) includes shell of coconut.    USE - Charcoal briquette used for heating furnaces, boilers and fireplaces.    ADVANTAGE - The charcoal briquette ensures high combustion rate and provides a perfect substitute of coal and wood in an eco-friendly manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic front view of the charcoal briquette.    Charcoal briquette (1)
NOVELTY - The sensor (10) has a membrane stack arranged in an interior portion of a body for producing an electrical signal that represents a concentration of a target gas in air at the stack. The stack includes a proton exchange membrane (20) arranged between top and bottom semi-permeable electrically conductive membranes (18, 22). A filter film is arranged between openings (36, 38) in the body and the stack. A pair of conductive pads (25, 27) provides electrical connection to the stack to access the electrical signal. A hygroscopic material (34) is located between the filter film and the stack.    USE - Thin film/micro-electro-mechanical systems (MEMS) electrochemical gas sensor for detecting carbon monoxide (claimed) generated by a fuel cell. Can also be used for propane, methane and ammonia.    ADVANTAGE - The thickness of contact pads is between 100 nanometer and 5 micrometer, so that the total thickness of a sensor is less than about 0.1-3 mm, thus reducing size of the sensor. The sensor includes shorter gas diffusion path for a gas to travel through the sensor and the membrane stack, thus resulting in a corresponding improvement in the response time of the sensor. The sensor allows contact and alignment between proton exchange membrane and top and bottom electrode membranes in the membrane stack is consistently achieved by thin film deposition of membranes.    DETAILED DESCRIPTION - The hygroscopic material is selected from the group consisting of zeolites, alumina, polysulfonates and desiccants.    DESCRIPTION OF DRAWING(S) - The drawing shows an exploded, side view of a thin film/MEMS electrochemical gas sensor.    Thin film/MEMS electrochemical gas sensor (10)    Thin film subassemblies (12, 14)    Top semi-permeable electrically conductive membrane (18)    Proton exchange membrane (20)    Bottom semi-permeable electrically conductive membrane (22)    Conductive vias (24, 26)    Contact pads (25, 27)    Hygroscopic material (34)    Openings (36, 38)
NOVELTY - The traditional Chinese medicine transdermal agent, which is in the form of an oil-in-water cream, comprises dandelion, honeysuckle, Trichosanthes kirilowii maxim, fructus Forsythia, Hibiscus, Astragalus mongholicus, Rheum officinale, and Angelica sinensis, where the weight ratio is 1:1:1: 0.6:0.5:0.3:0.3:0.2.    USE - The traditional Chinese medicine transdermal agent is useful for treating dairy cow recessive mastitis (claimed). No biological data given.    ADVANTAGE - The traditional Chinese medicine transdermal agent is prepared in simple, cost-effective and environmentally friendly manner. The traditional Chinese medicine transdermal agent is safe, and has reduced adverse events.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of preparing traditional Chinese medicine transdermal agent.
NOVELTY - The method comprises connecting a valve of marsh gas tank with an air compressor, supplying the power supply using an electric machine, filling marsh gas in a marsh gas tank, supplying the electric power into the pipe of the marsh gas tank at 20 degrees C, heating the tank, fermenting the gas generated in a input gas storage bag using anaerobic gas-producing ferment process, controlling the temperature in the anaerobic gas-producing fermentation, connecting the other valve set with the air compressor, and aerobically composting the tank to form biogas.    USE - The method is useful for aerobic and anaerobic fermentation of biogas.    ADVANTAGE - The method is capable of aerobically, economically and anaerobically fermenting the biogas with high stability and reduced energy consumption in an environmentally friendly manner.    DETAILED DESCRIPTION - The method comprises connecting a valve of marsh gas tank with an air compressor, supplying the power supply using an electric machine, filling marsh gas in a marsh gas tank, supplying the electric power into the pipe of the marsh gas tank at 20 degrees C, heating the tank, fermenting the gas generated in a input gas storage bag using anaerobic gas-producing ferment process, controlling the temperature in the anaerobic gas-producing fermentation, connecting the other valve set with the air compressor, and aerobically composting the tank to form biogas. The biogas tank body is filled with solid material. The fermentation step is carried out at a heating temperature of an electric heating mechanism and a heat preservation function of an insulating layer. An INDEPENDENT CLAIM is included for a column integrated aerobic and anaerobic fermentation device.
NOVELTY - The fertilizer comprises fermented organic fertilizer and inorganic fertilizer for mixing and pelletizing, where the organic fertilizer is manure, rice hull, or straw and the inorganic fertilizer is urea, ammonium phosphate, potassium chloride, or potassium sulfate.    USE - Used as fertilizer. No biological data given.    ADVANTAGE - The fertilizer can be prepared with improved yield in a simple manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of preparing fertilizer.
NOVELTY - A civil-adapted non-pollution clean fuel comprises (wt.%) methanol (60-15, preferably 69.9); and solvent oil including 9C (15-25, preferably 20), acetone (95-15, preferably 10), and hydrogen peroxide (0.5-2, preferably 1).    USE - A civil-adapted non-pollution clean fuel used in kitchen, restaurant, bath, and boiler.    ADVANTAGE - The fuel is inexpensive; and has no pollution, residue, and peculiar smell.
NOVELTY - Method for preparing fuel, involves (a) heating foodstuffs, sample and sludge at 80-200 degrees C, (b) pulverizing the obtained product to 0.5-10 mm, (c) agitating the pulverized powder with clay and charcoal, and (d) compressing the mixture using compression press, and drying the mixture and subjecting the mixture to solidification process.    USE - The method is useful for preparing fuel.
NOVELTY - Method of making a fuel composition comprises contacting a fatty acid- or triglyceride-containing component and a paraffin-rich component with hydrogen under catalytic hydroprocessing conditions to provide a hydroprocessed biofuel.    USE - The method is useful for making a fuel composition.    ADVANTAGE - The method is capable of efficiently making fuel composition in an economical manner. The fuel composition exhibits reduced greenhouse gas (GHG) emissions, based on a lifecycle assessment (LCA) from the time of cultivation of feedstocks (in the case of plant materials used as biomass) required for the compositions, up to and including the ultimate combustion of the fuel composition by the end user.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a process of making a hydroprocessed biofuel from a renewable carbon source comprising (a) contacting a hydroprocessing feedstock with hydrogen in a first reaction zone in the presence of a first catalyst to provide a reactor effluent comprising a deoxygenated component, (b) contacting the reactor effluent with hydrogen in a second reaction zone in the presence of a second catalyst to provide a hydrocracked effluent, (c) feeding a hydrogen-containing stripping gas and the hydrocracked effluent into a hot high pressure product stripper to selectively separate at least a portion of the hydroprocessed product as an overhead portion exiting the separator, and (d) fractionating the hydroprocessed product to recover the hydroprocessed biofuel; and    (2) a fuel composition comprising a hydroprocessed diesel biofuel or a hydroprocessed aviation biofuel obtained from hydroprocessing a fatty acid or triglyceride-containing component.
NOVELTY - Preparing pure crystalline imipenem monohydrate, comprises: dissolving crude imipenem in carbonated water and morpholinopropane sulfonic acid; treating with activated carbon; filtering by micron filter; and adding an organic solvent to precipitate imipenem monohydrate as a crystalline product.    USE - The process is useful for preparing pure crystalline imipenem monohydrate.    ADVANTAGE - The process: is ecofriendly, cost effective, commercially viable and ease to operate on a large scale; provides dissolution of imipenem at low temperature, thus minimizes the impurity formation; significantly reduces crystallization time compared to prior processes; avoids the use of capital intensive techniques of lyophilization or freeze crystallization and time consuming chromatography; provides a very stable imipenem whose color does not change even after storing at room temperature; and provides imipenem monohydrate at high yield (90% or more) and high purity (i.e. crystalline imipenem having thienamycin content less than 0.05% and mixture of diastereoisomers of impurity less than 0.05%).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for crystalline imipenem having thienamycin content less than 0.05% and mixture of diastereoisomers of impurity less than 0.05%.
NOVELTY - Fuel composition comprises: (a) 50-98 wt.% of petroleum derived gasoline; (b) 1-20 vol.% of ethanol; and (c) 1-30 wt.% of pyrolysis derived gasoline.    USE - Used as fuel composition.    ADVANTAGE - The fuel composition exhibits reduced greenhouse gas (GHG) emissions, based on a lifecycle assessment from the time of cultivation of feedstocks (in the case of plant materials) or extraction of feedstocks (in the case of fossil fuels) required for the compositions (up to and including the ultimate combustion of the fuel composition by the end user).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for making a fuel composition comprising (a1) pyrolyzing a feedstock comprising biomass to provide a pyrolysis oil, (b1) contacting the pyrolysis oil with hydrogen under catalytic hydroprocessing conditions to provide a hydroprocessed pyrolysis oil, (c1) separating a pyrolysis derived gasoline from the hydroprocessed pyrolysis oil, and (d1) blending the pyrolysis derived gasoline with 30-98 wt.% of a petroleum derived gasoline.
NOVELTY - Catalytic cracking of a lipid-containing feedstock, comprises: contacting the lipid-containing feedstock with at least one cracking catalyst at at least 450 degrees C to obtain a product stream; and separating at least one hydrocarbon fraction from the product stream, where the lipid-containing feedstock comprises lipids derived from microalgae and further comprises a hydrocarbon feedstock.    USE - The process is useful for catalytic cracking of a lipid-containing feedstock to produce hydrocarbon fraction, which is useful for preparing gasoline product useful in gasoline composition (all claimed).    ADVANTAGE - The process utilizes the microalgae that has high growth rate, utilize large fraction of solar energy, can grow in conditions that are not favorable for terrestrial biomass, consume carbon dioxide at a high rate, and may reduce the carbon footprint of the overall process, and thus provides the hydrocarbon stream with higher conversion rate and more valuable lighter products, and gasoline having improved research octane number.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a gasoline product prepared from a hydrocarbon fraction of the above hydrocarbon fraction; and    (2) a gasoline composition having less than 1000 ppmw sulfur comprising the gasoline product and at least one additive.
NOVELTY - A process for catalytic cracking of a lipid-containing feedstock involves contacting the lipid-containing feedstock with at least one cracking catalyst at a temperature of at least 450 degrees C, to obtain a product stream; and separating at least one hydrocarbon fraction from the product stream, where the lipid-containing feedstock comprises lipids derived from diatomic microalgae species.    USE - For catalytic cracking of a lipid-containing feedstock to form gasoline product; in gasoline composition having less than 1000 ppmw sulfur (claimed) and in LPG.    ADVANTAGE - The method provides an improved process for catalytic cracking of biomass with improved efficacy. By using lipids derived from a diatomic microalgae species as a feedstock, contrary to the teachings in the prior art, a higher cracking temperature gives a higher conversion and hence more valuable lighter products (i.e. more products having a boiling point below 221 degrees C such as e.g. LPG and gasoline). The diatomic microalgae used have high growth rates, utilize a large fraction of solar energy and can grow in conditions that are not favorable for terrestrial biomass. The diatomic microalgae consume CO2 at a high rate, and may reduce the carbon footprint of the overall process. The diatomic microalgae contain high concentrations of lipids. The cracking of a lipid-containing feedstock that comprises lipids derived from a diatomic microalgae species, over a cracking catalyst at a temperature of at least 450 degrees C results in a desirable product stream.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a gasoline product prepared from a hydrocarbon fraction of the at least one hydrocarbon fraction; and    (2) a gasoline composition having less than 1000 ppmw sulfur comprising a gasoline product prepared from a hydrocarbon fraction of the at least one hydrocarbon fraction and at least one additive.
NOVELTY - A system for producing fuel comprises a deoxygenation stage, where the deoxygenation stage comprises deoxygenation reactor chamber and a catalyst containing a porous substrate and an electrolessly deposited metal coating having a nanoscale thickness; and optionally a product separation stage configured to receive products from the hydrocracking and isomerization stage and separate the products into diesel fuel, gasoline, and/or jet fuel.    USE - For producing fuel (preferably diesel fuel, gasoline, or jet fuel) from bio-oils (claimed).    ADVANTAGE - The system does not use a solvent during deoxygenation processes. The system consumes considerably less hydrogen and provides possible benefits such as favorable process economics, use of existing refinery infrastructure to produce synthetic biofuels, and easier reactor design. The system provides a high yield of distillate fuels with low or minimal production of undesired by-products. Deoxygenation reactor in the system comprises multiphase downflow packed bed configuration, continuous flow operation capability, and the absence of extraneous or process derived solvents or diluents.
NOVELTY - A catalyst comprises a porous substrate; and an electrolessly deposited catalytically effective metal coating having a nanoscale thickness.    USE - For deoxygenation of alcohols, ethers, aldehydes, ketones, carboxylic acids, phenolics, esters by decarbonylation and decarboxylation over hydrodeoxygenation; for hydrogenation and preferential deoxygenation of triglycerides by decarbonylation and decarboxylation over hydrodeoxygenation; and for deoxygenating bio-oils for fuel production (claimed).    ADVANTAGE - The catalyst is catalytically active to accomplish hydrogenation and preferential deoxygenation of triglycerides at efficiency greater than or equal to 90% at less than 2% loading of the metal for continuous operation; and has activation energy for deoxygenation is 54 kcal/g mole for Camelina oil.
NOVELTY - Deoxygenating oxygenated hydrocarbons, comprises: providing a catalyst comprising a porous substrate and an electrolessly deposited nanoscale metal coating on the substrate; and contacting the catalyst with the oxygenated hydrocarbons and hydrogen to accomplish hydrogenation and deoxygenation, where the deoxygenation is accomplished preferentially by decarbonylation and decarboxylation over hydrodeoxygenation.    USE - The method is useful for deoxygenating oxygenated hydrocarbons (claimed), and for converting plant oils to biofuels including jet fuel, gasoline, and diesel fuel.    ADVANTAGE - The method is simple and cost effective.
NOVELTY - Producing a hydrocarbon product comprises hydrotreating a feedstock (containing at least one of renewable feedstock triacylglyceride (TAG), fatty acids and/or fatty acid methyl ester (FAME)) in the presence of a nonsulfided hydrotreating catalyst at 470-530 degrees C and a pressure of 750-1000 psig to produce a first product containing hydrocarbons.    USE - The method is useful for producing hydrocarbon product that is useful as transportation fuel comprising gasoline, kerosene, jet fuel and diesel fuels (all claimed).    ADVANTAGE - The method: provides transportation fuel with minimal or no secondary petroleum-refining and processing operations; separates glycerine produced from fatty acid which is valuable coproduct; allows conversion of feedstock to paraffinic product at low temperatures and pressures with high yields; requires less hydrogen for hydrodeoxygenation reactor; and is robust to accommodate fatty acids with impurities.
NOVELTY - Catalyst (A) comprising (a) catalytic ceramic support comprising an arrangement of crystallites of the same size, same isodiametric morphology and same chemical composition or substantially the same size, same isodiametric morphology and same chemical composition in which each crystallite is contacting with crystallites that surround it; and (b) at least one active phase comprising metal particles that chemically interact with the catalytic ceramic support.    USE - The catalyst is useful for the steam reforming of methane (claimed).    ADVANTAGE - The catalyst has improved catalytic activity and improved stability.    DETAILED DESCRIPTION - Catalyst (A) comprising (a) catalytic ceramic support comprising an arrangement of crystallites of the same size, same isodiametric morphology and same chemical composition or substantially the same size, same isodiametric morphology and same chemical composition in which each crystallite is contacting with crystallites that surround it; and (b) at least one active phase comprising metal particles that chemically interact with the catalytic ceramic support and mechanical anchoring in the catalyst support such that coalescence and the mobility of each particle are limited to a maximum volume corresponding to that of a crystallite of the catalyst support. An INDEPENDENT CLAIM is included for the preparations of (I).
NOVELTY - The vehicle has an air pump (10) which supplies air to fuel cell (2). A hydrogen tank (3) supplies hydrogen gas to fuel cell. A temperature control unit adjusts the temperature in fuel cell system (1). An electronic controller (30) operates speaker (20) to produce additional noise, when vehicle speed exists in predetermined range. The amount of comprehensive proximity noises defined for every vehicle speed is produced, by calculating the sum of sound volume of noise produced from component of fuel cell system and additional generated sounds produced from speaker.    USE - Fuel cell vehicle.    ADVANTAGE - The alerting of own vehicle can be reliably performed to pedestrian. Since sound volume of noise produced from component of fuel cell system can be calculated accurately, the amount of additional generated sounds generated with the speaker can also be determined accurately. The amount of comprehensive proximity noises defined for every vehicle speed can be generated at the time of driving of fuel cell vehicle.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the fuel cell system mounted in the fuel cell vehicle. (Drawing includes non-English language text)    Fuel cell system (1)    Fuel cell (2)    Hydrogen tank (3)    Air pump (10)    Speaker (20)    Electronic controller (30)
NOVELTY - A biogenic turbine fuel (F1) comprises (wt.%) mesitylene (50-99) and at least one alkane (1-50).    USE - As biogenic turbine fuel, preferably hydroprocessed renewable jet (HRJ) fuel i.e. tallow HRJ fuel (claimed).    ADVANTAGE - The biogenic turbine fuel is fully renewable fuels, preferably derived from a biomass having high energy content, such as vegetable oils. Turbine fuel has a high net heat of combustion by mass and a low density. This means that the fuel is significantly lighter than current turbine fuel; weight savings are always important in aviation. The lower net heat of combustion by volume, however, results in less range per gallon.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a biogenic turbine fuel (F2) comprising: at least one synthetic paraffinic kerosene (SPK) and/or hydroprocessed renewable jet (HRJ) fuel; and mesitylene (8-25 vol.%).
NOVELTY - Processing organic matter, comprises: providing organic matter; optionally preparing organic matter; optionally sanitizing the organic matter or prepared organic matter; removing one or more target component from the sanitized organic matter; and optionally removing liquid from the target components depleted or reduced organic matter.    USE - The method is useful for processing organic matter, which is useful for: preventing, treating or stabilizing a health condition, where the health condition is hypertension, stroke, nervous system disorders, kidney disorders, osteoporosis, anemia, nausea, stress, anxiety, depression, mood disorders, menopause, morning sickness, pregnancy-related temperature disorders, hot flashes, heart burn, ulcers, cancer, constipation, diarrhea, macular degeneration, Crohn's disease, ulcerative colitis, cardiovascular disease, diabetes, obesity, nicotine withdrawal symptoms, alcohol withdrawal symptoms, mosquito bites, autoimmune diseases, inflammation, HIV infection, flu, colds, pain, viral infections, bacterial infections, muscle health, metabolic syndromes, Alzheimer's disease, infections, sinusitis, thrombosis, arthritis, multiple sclerosis, irritable bowel syndrome, exercise, vitamin deficiencies, protein deficiencies, enzyme deficiencies, mineral deficiencies and maintaining healthy levels of vitamins, proteins, minerals or enzymes; and treating or enhancing the appearance of keratin-containing tissues, where the appearance of keratin-containing tissues is impacted by a condition or event comprising excema, rashes, psoriasis, cancer, cellulitis, wrinkles, spider veins, dry skin, age spots or sun damage (all claimed). Tests details are described but no results given.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a processed organic matter derivative made by the method; and    (2) a product comprising the processed organic matter derivative.
NOVELTY - Method for producing bio green energy from garbage, is claimed.    USE - The method is useful for producing bio green energy from garbage.    ADVANTAGE - The method is economical, and environmentally-friendly.
NOVELTY - An organic fertilizer manufacturing method involves mixing acid with sewage sludge comprising heavy metals to extract liquid phase. The solid sludge and sludge comprising heavy metals are dissolved in the obtained liquid phase. The obtained solid sewage sludge is neutralized by mixing lime. The neutralized product is mixed with red clay to produce organic fertilizer.    USE - Method for manufacturing organic fertilizer.    ADVANTAGE - The method enables manufacturing organic fertilizer with high-quality in a cost-effective and eco-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an organic fertilizer manufacturing device.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating a method for manufacturing organic fertilizer.'(Drawing includes non-English language text)'
NOVELTY - Melting and evaporation of lignin-, cellulose and/or carbonaceous material streams comprises the dryer, the filling device, the pyrolysis reactor and the heat generation together with material flow moderate and energetic a closed and connected unit and over a wet product entry, the entry of the combustion gases and the discharge of the solids the hot gases and the wet steam.    USE - The method is useful for melting and evaporation of lignin-, cellulose and/or carbonaceous material streams.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for carrying out the method comprising carrying out the contact pressure and the material feed linearly and without interruption.
NOVELTY - A Botryococcus braunii capable of producing 60 %mass or more of hydrocarbons having molecular formula of C34H58 with respect to total hydrocarbon produced.    USE - The B.braunii is useful for producing hydrocarbon, preferably (E)-2,3,7,10,13,21-hexamethyl-6,17-dimethylene-10-vinyl-docosa-1,11,21-triene (claimed) which is used as direct fuel or fuel for internal combustion engine.    ADVANTAGE - The strain can be cultured easily and cost-effectively, and enables to produce hydrocarbon with high purity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing hydrocarbon, which involves using the B.braunii strain.
NOVELTY - The apparatus (200) has gasifier (210) which gasifies the gasification raw material and produces gasifying gas. A reforming furnace (220) reforms the gas generated by the predetermined time. A merging unit (230) makes the gas which is the gasifying gas generated after the predetermined time and the gas is merged.    USE - Gasifying gas generation apparatus for solid raw materials such as coal, biomass and tire chip.    ADVANTAGE - The apparatus prevents reduction of the ratio of the combustion gas per unit volume. A tar can be reduced efficiently with respect to the oxygen consumption in a reforming furnace.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for gasifying gas generation method.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the gasification gas purification systems. (Drawing includes non-English language text)    Booster (140)    Gasifying gas generation apparatus (200)    Gasifier (210)    Reforming furnace (220)    Merging unit (230)
NOVELTY - The biomass gasification system has a biomass gasifier (13) to gasify biomass (11). A dust removal unit (15) removes the biomass char (30) contained in the gasifying gas produced by the biomass gasifier.A generated gas cooler (16) cools thegenerated gas (14). An adsorption tower (18) filled with the char adhesion biomass grains adheres the biomass char and another dust removal unit (17) removesthe coal tar fractions and the multiple components of a sulfur compound.    USE - Biomass gasification system.    ADVANTAGE - The filled layer of the biomass char reduced pressure loss. The coal tar fractions and the multiple components of a sulfur compound are removed by the filled layer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for purification method of the biomass gasifying gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of biomass gasification system. (Drawing includes non-English language text)    Biomass (11)    Biomass gasifier (13)    Generated gas (14)    Dust removal unit (15,17)    Generated gas cooler (16)    Adsorption tower (18)
NOVELTY - The system (10A) has a biomass gasifier (13) which gasifies biomass (11). A generated gas cooler (16) cools the generated gas. A primary tar removal tower (19) adsorbs and removes the coal tar fractions in the generated gas dust and cooled. A secondary tar removal tower (41) adsorbs and removes the light hydrocarbon survives in generated gas.    USE - Biomass gasification system.    ADVANTAGE - As a heavy hydrocarbon is adsorbed and a light hydrocarbon is made to adsorb in a latter secondary tar removal tower, the efficient removal of the coal tar fractions is obtained efficiently at low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the purification method of the biomass gasifying gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of biomass gasification system. (Drawing includes non-English language text)    Biomass gasification system (10A)    Biomass (11)    Biomass gasifier (13)    Generated gas cooler (16)    Primary tar removal tower (19)    Secondary tar removal tower (41)
NOVELTY - The gasification system (10A) has dust removal unit (17) to remove the biomass char contained in the gasifying gas generated by the biomass gasifier (13). The generated gas cooler (16) cools the generated gas. The dust removal and acidic-gas removal apparatus (42) removes the dust and acidic gas in the hot air generated in the biomass firing air-heating furnace.    USE - Biomass gasification system for gasifying biomass for fuels used for gas turbine, and fuel cell.    ADVANTAGE - The coal tar fractions in the generated gas and the multiple components of a sulfur compound is removed and the dust collecting performance is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for purification method of biomass gasifying gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the biomass gasification system. (Drawing includes non-English language text)    Gasification system (10A)    Biomass gasifier (13)    Generated gas cooler (16)    Dust removal unit (17)    Dust removal and acidic-gas removal apparatus (42)
NOVELTY - The method involves generating raw material oil and hydrogen by utilizing a hydrogenation treatment reactor. An active component is provided with a catalyst and the hydrogenation treatment reactor. A gas phase reactor and a liquid phase reactor are fixed to a fractionating tower. Diesel oil and converted oil are recycled in a reaction system by utilizing the fractionating tower. Average reaction temperature of the hydrogenation temperature reactor is 50-300 degrees centigrade. A heating device is fixed with the hydrogenation treatment reactor.    USE - Biological grease motor fuel hydrogenation method.    ADVANTAGE - The method enables prolonging service life of the hydrogenation treatment reactor and reducing failure rate of the biological oil and ensures better storage stability.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram illustrating a biological grease motor fuel hydrogenation method.'(Drawing includes non-English language text)'
NOVELTY - The method involves performing a hydrogenation operation under condition of raw material oil. The raw material oil and hydrogen are passed through hydrogenation active component content of a catalyst bed layer. An active component is selected from tungsten, Muriaticum, Nickel and cobalt under multiple vulcanized states. Hydrogenation effluent is entered into a fractionating tower under gas phase and liquid phase. Diesel oil and converted oil are stored in a fractionating tower. Circulating gas hydrogen sulfide content is maintained by using a sulfur-containing material.    USE - Biologic oil production motor fuel hydrogenation method.    ADVANTAGE - The method enables improving storage stability of animal fats and vegetable oils in an effective manner and prolonging service life time of a hydrogenation device.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram illustrating a biologic oil production motor fuel hydrogenation method. '(Drawing includes non-English language text)'
NOVELTY - The sludge biomass molded fuel comprises a biomass powder material that is compressed to mold.    USE - The sludge biomass molded fuel is useful as an adhesive to compress mold by a machine such as double-roller molding machine including pressing molding machine, where the adhesive includes biomass hydrolysate, industrial organic waste liquid and waste slag or other adhesive for producing the briquette such as clay, lime and carbide slag (all claimed).    ADVANTAGE - The sludge biomass molded fuel can be economically and simply prepared with has low cost, high yield and good quality, and reduce carbondioxide emission.    DESCRIPTION OF DRAWING(S) - The figure shows a flowchart of a method for production of sludge biomass forming fuel (Drawing includes non-English language text).
NOVELTY - The gasification apparatus (10) has chambers (12,20) to temporarily store particulate material. An outlet channel (22) is arranged to provide particulate material from the chamber under the action of gravity. A guiding unit is positioned in the outlet channel for assisting passage of particulate material from chamber through the outlet channel. Elongate fingers (26a-26e, 28a-28d) are arranged to rotate about axes extending transversely across the outlet channel.    USE - Gasification apparatus of pyrolysis plant (claimed) for permitting controlled release of flowable particulate material.    ADVANTAGE - Since guiding unit is positioned in the outlet channel for assisting passage of particulate material from chamber through the outlet channel, the particulate material from the chamber can be guided without disrupting the flow of the material and waste materials can be processing easily and effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for permitting controlled release of flowable particulate material.    DESCRIPTION OF DRAWING(S) - The drawings show the sectional view of the gasification plant and top view of the outlet channel.    Gasification apparatus (10)    Chambers (12,20)    Oxidation zone (18)    Channel (22)    Fingers (26a-26e, 28a-28d)
NOVELTY - The present day energy cost is unaffordable despite of the providence of heavy subsidies by government of India. Even below poverty line (BPL) families who have been distributed liquefied petroleum gas (LPG) connections, cylinders and regulators free of cost by various state governments and government of India have been unable to bear the cost of regular refills. So, with the idea of bundling of biogas and LPG, this problem can be eradicated and the effective refill cost of this mixed gas will be affordable and available in such remote areas. Image 0/0
NOVELTY - An environment-friendly straw charcoal carbonization machinery comprises a furnace body; a furnace door; a pneumatic adjusting valve; an atomizing dust-removing room; a steam input pipe; a flue valve; a cooling water interlayer; a wet dust-removing room; a water pipe; a water gauge; a steam chamber; an air guide pipe; and a steam pipe.    USE - An environment-friendly straw charcoal carbonization machinery.    ADVANTAGE - The machinery has power without high voltage, and has an automatic protection and grounding device to ensure safety.    DETAILED DESCRIPTION - An environment-friendly straw charcoal carbonization machinery comprises:    (A) a furnace body;    (B) a furnace door;    (C) a pneumatic adjusting valve;    (D) an atomizing dust-removing room;    (E) a steam input pipe;    (F) a flue valve;    (G) a cooling water interlayer;    (H) a wet dust-removing room;    (I) a water pipe;    (J) a water gauge;    (K) a steam chamber;    (L) an air guide pipe;    (M) a steam pipe;    (N) a guide plate;    (O) an evacuating pipeline;    (P) an atomizing coke collecting chamber;    (Q) an air outlet pipe;    (R) a high pressure water nozzle;    (S) a steam pipe;    (T) a high pressure water pipe;    (U) a furnace body water interlayer;    (V) a tar collecting tank;    (W) a tar output pipe;    (X) a dust removing water overflow pipe;    (Y) a tar discharge valve;    (Z) a temperature controller;    (() a high pressure water pump;    (\) a water pump;    ()) a refractory material layer;    (^) a steam generating piece; and    (_) a hearth comprising a steam generation block and a humidity adjusting spray head.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of an environment-friendly straw charcoal carbonization machinery.
NOVELTY - The method involves performing gasification reaction of biomass pretreated raw material in a gasification furnace (1). Raw fuel gas is formed by a multi-grade composite purifying device (2). The raw fuel gas is generated by the gasification furnace from a tar cracker (4) at 800-900 degrees Celsius. Clean gasifying gas is returned to a roots blower (3) from the tar cracker. The gasification furnace is fixed into an air pre-heater (5). The air pre-heater is connected with the tar cracker.    USE - Gasification and high temperature cracking coupling biomass conversion method.    ADVANTAGE - The method enables organically forming gasification and pyrolysis coupling biomass conversion so as to reduce heat gas value and tar content, thus ensuring reliable operation and enlarging usage range of the gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a gasification and high temperature cracking coupling biomass conversion device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram illustrating a gasification and high temperature cracking coupling biomass conversion method.    Gasification furnace (1)    Multi-grade composite purifying device (2)    Roots blower (3)    Tar cracker (4)    Air pre-heater (5)
NOVELTY - The structure has a dust chamber opening cover that is provided with small holes at the side of ash chamber. The lower corner of specific purifier is opened in small hole of opening cover. The bottom portion of other purifier is provided with return pipe and oil return valve. An upper portion of purifier is provided with an air supply pipe which is connected with a stove. A lower condensed water tank is provided with a discharging valve, top stove air supply pipe and a stove head.    USE - Biomass gasification and direct combustion structure of dual-use furnace.    ADVANTAGE - The production speed and thermal efficiency of fuel can be improved. The heating efficiency of furnace can be improved. The pollution and blockage in furnace can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass gasification and direct combustion structure of dual-use furnace.
NOVELTY - A biomass pyrolyzing furnace comprises furnace shell, furnace liner, steam discharge pipe, air inlet pipe, and condensing tower. Furnace liner is provided in furnace shell. The furnace liner is mesh multifurnace. Layers separated exhaust chamber is provided between inner wall of furnace shell and internal furnace. Inner wall of furnace shell is provided with ringsheet baffle plate. Furnace inner wall of ring sheet forms exhaust chambers, each exhaust chamber is connected with the condensing tower by exhaust layer.    USE - Biomass pyrolyzing furnace.    ADVANTAGE - The furnace saves energy, has more labor saving operation, saves times, and has high production efficiency. Wood tar can be produced continuously. The wood tar quality is good. Yield is high. The pyrolysis furnace pyrolysis speed is fast and time is short.    DETAILED DESCRIPTION - Biomass pyrolyzing furnace comprises furnace shell, furnace liner, steam discharge pipe, air inlet pipe, and condensing tower. Furnace liner is provided in furnace shell. The furnace liner is mesh multifurnace. Layers separated exhaust chamber is provided between inner wall of furnace shell and internal furnace. Inner wall of furnace shell is provided with ringsheet baffle plate. Furnace inner wall of ring sheet forms exhaust chambers, each exhaust chamber is connected with the condensing tower by exhaust layer. One side of air inlet pipe is provided on oven shell and exhaust pipe. The condensation tower is provided with draught fan.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating a biomass pyrolyzing furnace.
NOVELTY - A strong pulse laser producing biological fuel device comprises transparent quartz reactor (1) and pulse laser generator (6). Quartz reactor is provided with feeding port (2), where bottom end is provided with oil outlet (5). Inner wall of quartz reactor is provided with air outlet (3), where lower end of side wall is provided with slag outlet. Quartz reactor wall of other side corresponds to laser generator. Quartz reactor is connected with oil outlet provided with filter core. Quartz reactor is provided as cone bottom.    USE - Strong pulse laser producing biological fuel device.    ADVANTAGE - The device can effectively process simplified biomass cracking, thus achieving purpose of improving efficiency of biological diesel oil and reducing producing cost.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating a strong pulse laser producing biological fuel device.    Quartz reactor (1)    Feeding port (2)    Air outlet (3)    Oil outlet (5)    Laser generator (6)
NOVELTY - Rice husk gasifier comprises a gasification furnace. The gasification furnace is provided with rice feeding inlet. The gasification furnace via pipe is connected with cooling tower. The cooling tower is connected with a coke gas capturing static device. The static device is connected with a spray tower. The spray tower with air pipe is connected with air storage tank.    USE - Used as a rice husk gasifier.    ADVANTAGE - The rice husk gasifier has simple structure and simple operation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the rice husk gasifier.
NOVELTY - Fuel source (S1) (100) comprises: multiple chemical hydride particles (104); multiple metal hydride particles; and a flexible, porous, liquid water impermeable, hydrogen and water vapor permeable membrane, at least partially surrounding the chemical hydride particles.    USE - The fuel source is useful: for an electrochemical cell (claimed); as supplying fuel to a combustion engine; and in a heating device, cooling device, a flame employed for lighting, a flame employed as part of an analytical instrument, a flame employed in a cutting or welding torch.    ADVANTAGE - The fuel source maintains low gas diffusion resistance throughout the discharging process, thus allowing higher average rates of hydrogen generation and increasing extracted energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a fuel source (S2) comprising: chemical hydride particles, positioned in at least two stacks; the flexible, porous, liquid water impermeable, hydrogen and water vapor permeable membrane, in contact with and at least partially surrounding each chemical hydride stack; and a porous metal hydride layer, separating each chemical hydride stack, where the fuel source is contained in a removable cartridge.    DESCRIPTION OF DRAWING(S) - The figure illustrates a cross-sectional view of a fuel source.    Fuel source (100)    Air gaps (102)    Chemical hydride pellets (104)    Gas diffusion channels (106)    Perforated enclosure (112)
NOVELTY - The gasifier (1) has a set of wedge plates projecting from an upper surface of one of grate rings, where the wedge plates include faces adjacent to openings of the grate rings. One of the grate rings is moved between a configuration, in which the openings of the grate rings are aligned, and another configuration in which the openings of the grate rings are misaligned. The wedge plates are oriented to push the material toward the openings of the other grate ring when the former grate ring is moved from the latter configuration toward the former configuration.    USE - Circular gasifier for gasifying a solid organic material e.g. biomass material, to generate syngas i.e. compressible synthetic combustible gas, to create energy in small and medium-sized energy recovery systems. Uses include but are not limited to gasify forestry and agricultural residues, industrial waste materials such as saw mill pulp, paper products, fowl litter e.g. chicken litter and turkey litter, and hydrocarbon based plastics in the energy recovery systems used in community centers, schools, nursing homes and small industrial and commercial establishments.    ADVANTAGE - The gasifier allows recovering biomass energy on a cost-effective manner in small and medium-sized energy recovery systems. The gasifier carries away the effluent through an insulated exit duct, and the velocity of the effluent above fuel pile through exit port is kept low, thus reducing particulate carryover.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for generating syngas from an organic material.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a circular gasifier.    Circular gasifier (1)    Solid mass feeder (2)    Auger feed (3)    Ash removal system (4)    Collection bin (5)
NOVELTY - A steam reformer (500) comprises an outer wall (204), an inner wall which includes a step extending outward toward the outer wall and downward toward a bottom of the steam reformer at a position between a top of the steam reformer and the bottom, and a reaction chamber (202) disposed between the outer wall and the inner wall.    USE - A steam reformer.    ADVANTAGE - The stem reformer has better heat transfer to a feed gas in reaction chamber thus improving efficiency of the reaction and thus reducing feed gas usage; and allows feed gas to enter the reaction chamber over a shorter reaction chamber length thus reducing an amount of materials needed for the steam reformer and a cost of the steam reformer.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic cross-sectional view of a steam reformer.    Reaction chamber (202)    Outer wall (204)    Heat exchanger (218)    Steam reformer (500)    Diffusion burner (504)
NOVELTY - The system has a biomass reformer (400A) comprising a cylindrical vessel (407) with multiple coiled tubes (410A, 410B), where vertical height of each of the tubes is in a range of 40 feet to 100 feet, and coil length of the tube is four times the vertical height. A burner (404) is provided to combust fuel and to provide heat to maintain the reformer at reformer temperature. An outlet (480) is provided for a reformer product comprising synthesis gas. Another outlet (470) is provided for flue gas produced via combustion of fuel in the burners.    USE - System for producing synthesis gas such as hydrogen, methane, fischer tropsch tail gas and carbon monoxide, from carbonaceous materials such as biomass.    ADVANTAGE - The system produces gas in an environment-friendly manner by allowing the utilization of sustainable and renewable feedstocks, facilitates sequestration of carbon dioxide and reduces amount of waste material.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a synthesis gas production system.    Biomass reformer (400A)    Burner (404)    Cylindrical vessel (407)    Coiled tubes (410A, 410B)    Outlets (470, 480)
NOVELTY - A recycled renewable clean energy source converted from garbage via pollution-free treatment and a production method, comprises the following steps: uniformly stirring 60-100 wt.% of garbage regenerative and recombined component of 35-50 meshes and 37-80 wt.% of regenerative optimized material to obtain 97-180 wt.% of combustible coal base materials; then crushing 3-15 wt.% of synthetic energy evolution agent to be secondarily synthesized with 97-180 wt.% of combustible coal base materials to obtain 100-200 wt.% of recycled renewable clean energy source.    USE - The method is useful for producing recycled renewable clean energy source converted from garbage via pollution-free treatment (claimed).    ADVANTAGE - The recycled renewable clean energy source converted from garbage via pollution-free treatment can increase the saving rate of the original coal by 65-85%, further effectively reduces emission of harmful substances and harmful gases by 65-85%, increases the utilization rate of the household and industrial garbage to 95-99%, improve 1500-3500 kilocalories of the garbage heat to the industrial coal standard, and improve the heat to 4200-6200 kilocalories which is completely suitable for requirements of various boilers, industrial power generation, chemical industries, industrial smelting, and civil use; and the pollution-free treatment and effectively comprehensive utilization to the household garbage are a great contribution to the human beings, and are significant to protection of the original coal resources, improvement of the original coal utilizing rate, storage of the original coals, and environmental protection.
NOVELTY - The anaerobic reactor has a pump, which is provided for pumping water to the inner part of the reactor.    USE - Anaerobic reactor for processing biogas.    ADVANTAGE - The anaerobic reactor is cost-effective.
NOVELTY - Environmentally friendly biomass composite fuel comprises biomass fuel, fuel coals with medium and low heat values and sulfur-fixing agent mixed together, where the weight ratio of the biomass fuel to the total quantity is 30-70%.    USE - The biomass composite fuel is useful in industrial and civil boilers.    ADVANTAGE - The biomass composite fuel: is environmentally friendly; exhibits strong firepower; can be fully combusted with less dust, high heat utilization rate and high strength; and can be easily transported and stored.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing the environmentally friendly biomass composite fuel, comprising the grinding the biomass fuel to powders through a grinding step (1); grinding the sulfur-fixing agent to powders through a grinding step (2); grinding coal to powders through a coal grinding step (3); mixing the biomass fuel with sulfur-fixing agent and coal through a mixing and stirring step (4) to form uniform mixture; adjusting the humidity of the mixture through a water adding step (5); forming the mixture to the required structure and shape through a forming step; and drying the mixture to obtain the finished product of fuel.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic flow chart of the process steps for producing the environmentally friendly biomass composite fuel.    Biomass fuel grinding step (1)    Sulfur-fixing agent grinding step (2)    Coal grinding step (3)    Mixing and stirring step (4)    Water adding step for adjusting the humidity of the mixture (5)
NOVELTY - Die (10) for producing pellets (61) from solid wood, preferably from solid wood portions, comprises at least one cutting assembly (20) and a compression region (30) downstream to the cutting assembly, where a splitting and compressing of the solid wood is carried out in one operation. The cutting assembly is detachably arranged in the die and the compression region is molded into the die.    USE - The die is useful for producing pellets.    ADVANTAGE - The die is included in the maintenance-friendly tool to form pellets of solid wood in a simple, energy- and cost-efficient manner, where the starting material is completely recovered.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a device (100) for producing pellets from solid wood or solid wood portions comprising the die;    (2) producing rod-shaped pellets by die or by using the device, comprising splitting the solid wood or solid wood portions and subsequently compressing the split solid wood or solid wood portion; and    (3) rod-shaped pellets made of solid wood of solid wood portions, which are split in the longitudinal direction of the wood fibers, and compressed parallel to the longitudinal direction of the wood fibers.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic sectional view of the die.    Die (10)    Cutting assembly (20)    Compression region (30)    Pellets (61)    Device (100)
NOVELTY - Utilizing biomass, in which the biomass is pyrolyzed within a temperature range from 550-750 degrees C to obtain driven-out gas and remaining carbon-rich solids, where the biomass used has a lignin content of 10-30% by weight and a water content of 5-25% by weight, and the residence time of the biomass within the temperature range is 10-60 minutes.    USE - The methods are useful for utilizing biomass to obtain driven-out gas and remaining carbon-rich solids; and for reducing the amount of CO2 within the Earth's atmosphere, where the obtained carbon-rich solids are used as a soil amendment, or as an adsorbent (all claimed).    ADVANTAGE - The method produces products of value with unusually good properties, the proceeds of which make the process economically viable.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a carbon-rich solid, obtainable by the method, characterized in a carbon content of 75-99% by weight; and    (2) a method for reducing the amount of carbon dioxide (CO2) within the Earth's atmosphere, comprising: (a) cultivating plants providing a biomass with a lignin content of 10-30% by weight; (b) harvesting the plants and separating the biomass from it; (c) drying the biomass when indicated to obtain a biomass with a water content of 5-25% by weight; (d) performing the method above to obtain a carbon-rich solid from the biomass; (e) storing of the carbon-rich solid in the soil.
NOVELTY - An additive comprises sodium hypochlorite, sodium hydroxide, hydrochloric acid, magnesium chloride, and a calcium hydroxide, and solubilizes water in fuel oil.    USE - Additive is used for manufacturing hydrolysis biofuel (all claimed).    ADVANTAGE - The additive is efficiently manufactured with excellent durability without polluting the environment.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of additive, which involves stirring and mixing sodium hydroxide into the sodium hypochlorite solution, stirring and mixed the magnesium chloride and calcium hydroxide to the hydrochloric acid solution, and stirring and mixing the two types of solutions;    (2) hydrolysis biofuel, which is obtained by mixing water and the additive with fuel oil; and    (3) manufacture of hydrolysis biofuel, which involves stirring and mixing additives and water, obtaining mixed solution, and mixing and stirring obtained solution to fuel oils.
NOVELTY - The machine (1) has a nature adjustment chamber (2) that is provided with electric power generation substance which is the mixture of water and light hydrogen tritium. The instant vaporization is performed on the light hydrogen tritiated water by a vacuum device (3). A double pendulum-type mechanical generator (12) performs semipermanent continuous operation of fuel cell electric power generation. A deuterium type light hydrogen nickel battery apparatus (13) adjusts the amount of deuterium in hydrogen.    USE - Fuel cell power generation machine for motor vehicle, electric airplane, electric construction machine, electric vehicle, electric space robot, and solar battery vehicle such as battery car.    ADVANTAGE - The harmless unlubricated semipermanent continuous operation of electric power generation can be performed by the fuel cell power generation machine efficiently, without destructing the nature and depleting the natural resource. Hence safety to the environment is ensured. High output dynamo of ultra-small water turbine is realized through fuel cell power generation machine.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of the fuel cell power generation machine. (Drawing includes non-English language text)    Fuel cell power generation machine (1)    Nature adjustment chamber (2)    Vacuum device (3)    Double pendulum-type mechanical generator (12)    Deuterium type light hydrogen nickel battery apparatus (13)
NOVELTY - Invention relates to plasmas thermal processing and recovery of solid and liquid industrial and agricultural wastes. Proposed method comprises plasma gasification of carbon-containing compounds, forming electric arc in fluid to produce high-power plasma gas. Used plasma-forming medium represents carbon-containing ultradispersed heterophase system with developed phase interface surface consisting of water-organic suspensions and/or emulsions containing solid and/or liquid organic components in amount of 0.07...0.7 of water volume formed in circulating flow at combined effects of hydrodynamic forces in creating centers of cavitation with subsequent formation of cavitation bubbles, and ultrasound fields with 19.5...100 kHz frequency and ultrasound intensity of 1.5...2.5 W/cm3. Note here that plasma thermal conversion of water-organic suspensions and/or emulsions is performed by pumping ultradispersed heterophase system through zone of electric arc discharge while portion of plasma gas formed is introduced in circulating flow for intensification of ultradispersed heterophase system formation. Proposed plant comprises plasma chemical reactor 1 with electrode system 2, power supply 3, loading vessel 8, cyclone 9, gas holder 10 and hydraulic pump 7. Additionally, said plant comprises rotary pulsating cavitator 6 communicated via pipeline with ultrasound activator 11 communicated with coaxial vortex chamber 4 and plasma chemical reactor 1, plasma gas feed circuit to feed plasma gas into activator 11 and dispenser 12 arranged in circuit feeding plasma gas into activator 11 Note here that plasma chemical reactor 1 is connected with loading vessel 8.    USE - Process engineering.    ADVANTAGE - Method of processing carbon-containing compounds and water into plasmagas. 3 cl, 1 dwg, 1 ex
NOVELTY - The system has input hopper through which the reclaimed waste is injected. The screen device (30) is provided with screen drum (32) to which the metallic species is supplied. The selection apparatus (50) selects the combustibles from the reclaimed waste in which soil less than 35 mm is ejected after dividing to the solid fuel object.    USE - System for processing transportable landfill mining and reclaimed combustibles.    ADVANTAGE - The moisture of the reclaimed waste is reduced and the generation of bad smell is avoided.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the system for processing transportable landfill mining and reclaimed combustibles. (Drawing includes non-English language text)    Input hopper (10)    Screen device (30)    Screen drum (32)    Selection apparatus (50)    Crusher (80)
NOVELTY - Hydrothermally processing (M1) biomass involves: contacting algae based feed with water in presence of catalyst particles under effective hydrothermal processing conditions to produce multi-phase product, where catalyst particles includes catalyst metal and has average particle size of at least 1000 mu m; separating multi-phase product to produce at least a gas phase portion, liquid hydrocarbon portion, aqueous portion, and solids portion, where the solids portion contains catalyst particles and algae based solids; and separating catalyst particles from algae based solids.    USE - For hydrothermally processing biomass (claimed) e.g. algae to produce hydrocarbon products such as distillate fuel.    ADVANTAGE - The method in the presence of a catalyst allow for conversion of biomass into molecules having a desired boiling range while also removing at least a portion of impurities that is less desirable in a distillate product, such as nitrogen impurities, oxygen impurities, olefin impurities or aromatic impurities.
NOVELTY - The device has an arm part connected with a fuel cell part that is provided with a membrane electrode assembly and a gas diffusion layer. A perforated device board is coated by the gas diffusion layer. The fuel cell part controls rotation of a gripper. An insertion hole is formed in the fuel cell part. A laser align key detects a location of the gas diffusion layer within the fuel cell part. A gas diffusion layer location comparison unit determines position error of the gas diffusion layer. A rotation angle operation unit measures a rotation angle of the gripper.    USE - Fuel cell manufacturing device.    ADVANTAGE - The device improves quality through gas diffusion layer location alignment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a fuel cell manufacturing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a fuel cell manufacturing device.
NOVELTY - Method for preparing fuel pellet, involves drying pine (70-80 wt.%), oak (9-14 wt.%) and herb (8-11 wt.%) at a room temperature, pulverizing the dried components into 200-500 meshes size, mixing the obtained powders, pressing the obtained mixture at 120-200 degrees C, adding Perilla frutescens (3-5 wt.%) to the obtained product, pressing the obtained product subsequently, and cooling and cutting the obtained product.    USE - The method is useful for preparing fuel pellet.
NOVELTY - Reducing the tar content of combustible raw gases from biomass gasification, comprises supplying the combustible raw gases over a molded body of catalyst-oxygen carrier, condensing the tar components of the combustible raw gases on the surface of the molded body and partially oxidizing the condensed tar components by oxygen supply to the molded body.    USE - The method is useful for reducing tar content of combustible raw gases from biomass gasification.    ADVANTAGE - The method is carried out in a cost efficient manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a system for reducing the tar content of raw gases of biomass gasification, comprising at least two reactors (R1, R2) filled with molded body of catalyst-oxygen carrier, where (a) the reactors respectively comprises a raw gas supply pipeline, a clean gas outlet, an air inlet- and an air outlet pipeline, (b) the gas pipelines are closable in a controlled manner y means of valves, (c) the reactors and the gas pipeline comprise a sensor for determining the gas composition, and (d) the reactors for reducing the tar content by means of the molded body and for the regeneration of used molded body are alternately loaded with raw gas or air.    DESCRIPTION OF DRAWING(S) - The figure 1 shows a schematic representation of the system for cleaning of combustible gases from biomass gasification (Drawing includes non-English language text).    Reactors (R1, R2)
NOVELTY - A carbonization furnace comprises an insulating furnace body; and a chimney. The insulating body is provided with a hearth. The chimney is connected with smoke outlet of hearth. The hearth in the middle part is provided with rice sieve. On the holding furnace and upper part of rice sieve are connected with discharging port of insulating furnace body. The top part of insulating furnace body is provided with rice feeding port.    USE - Carbonization furnace useful for rice hull.    ADVANTAGE - The carbonization furnace has simple structure, convenient use, easy operation, high yield and can move.
NOVELTY - The furnace has an air supply device provided with an air pre-heating cavity and an air outlet cavity, where the pre-heating cavity is located in a wall of a furnace body around a hearth. The air outlet cavity and an air inlet pipe are connected with a furnace wall of a lower part of the air pre-heating cavity. A top cover is connected with the furnace body. Upper and lower openings are formed on a storage chamber. A cover fixing device is provided with a screw rod, a handle and a screw hole that is connected with an inner cover. An inner cover fastening device comprises a connecting rod.    USE - Biological material gasification furnace.    ADVANTAGE - The furnace has simple structure and improved combustion quality.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial sectional view of a biological material gasification furnace.
NOVELTY - The device has a gasified gas outlet arranged on an upper part of a vertical cylindrical furnace body (5). An air outlet is provided with a horizontal gasification gas outlet pipe that is connected with a tapered pipe (9). An exhaust pipe (10) is connected with a clapboard, a lower pipe and a circulating pipe (8). The circulating pipe is arranged at a lower part of the vertical cylindrical furnace body. An end of an U-shaped liquid seal pipe is connected with a liquid sealing pipe. A tar cracking pipe (3) is provided with an air return pipe (4) of the vertical cylindrical furnace body.    USE - Biomass gasification tar separating cycling cracking transforming device.    ADVANTAGE - The device easily removes gasification gas cycling tar so as to improve purification capability of gasification gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial sectional view of a biomass gasification tar separating cycling cracking transforming device.    Tar cracking pipe (3)    Air return pipe (4)    Vertical cylindrical furnace body (5)    Circulating pipe (8)    Tapered pipe (9)    Exhaust pipe (10)
NOVELTY - The device has a combustion chamber (2) connected with a gasification furnace (1). The gasification furnace is located in a boiler unit (3). The boiler unit is provided with an upper boiler barrel (31). A water cooling wall pipe (33) is arranged between the upper boiler barrel and a lower boiler barrel (32). The boiler unit is provided with a boiler gas saving unit (4). The gasification furnace is provided with a gasification furnace water inlet pipe. A gas outlet is connected with the combustion chamber.    USE - Biomass gasification furnace combustion energy-saving device.    ADVANTAGE - The device is inexpensive, and reduces occupying space, and has improved production efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass gasification furnace combustion energy-saving device.    Gasification furnace (1)    Combustion chamber (2)    Boiler unit (3)    Boiler gas saving unit (4)    Upper boiler barrel (31)    Lower boiler barrel (32)    Water cooling wall pipe (33)
NOVELTY - The method involves driving a turbine rotating with steam to drive a generator to generate current for a steam turbine, where cow dung is supplied into a front boiler combustion chamber to perform a pre-processing dairy manure. A solid-liquid separation process of the cow dung and a water content is performed, where wet dairy manure and furfural residue are mixed and stirred uniformly to obtain a feces mixture. The feces mixture is dried to obtain a dry excrement slag mixture that is subjected to a hot pressing shaping process to generate electricity.    USE - Method for generating power by using fuel e.g. cow dung.    ADVANTAGE - The method ensures to generate electricity by using non-renewable resources in a reliable manner.
NOVELTY - The station has armature winding of synchronous generator, which is directly connected with the multi-pulse rectifier. An electrolytic hydrogen producing device is connected with direct current bus bar.    USE - Hydrogen station.    ADVANTAGE - Investment cost of hydrogen station can be reduced. Pollution to power system can be reduced effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen station. (Drawing includes non-English language text)
NOVELTY - An organic fertilizer is prepared by adding microbial inoculum to compost material to obtain compost organic fertilizer or adding compost raw material to organic fertilizer, where compost raw material comprises banana stalk, livestock manure, rice hull, and peanut straw.    USE - Method of preparing organic fertilizer (claimed).    ADVANTAGE - The method utilizes agricultural waste resource, and can provide fast fermentation process of the composting system while allowing low-carbon agricultural development and obtaining good quality fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an organic fertilizer.
NOVELTY - Preparation of Hypsizygus marmoreus compost, is claimed, where the compost comprises sawdust (10-30 wt.%), cotton straw (20-40 wt.%), wheat bran (10-20 wt.%), rice bran (15-25 wt.%), corn powder (2-10 wt.%), corn cob (1-5%), cotton-seed shell (5-10%), and gypsum powder (0.5-1 wt.%).    USE - The method is useful for preparation of Hypsizygus marmoreus compost.    ADVANTAGE - The method is capable of simply, rapidly and economically preparing the Hypsizygus marmoreus compost with high efficiency in an environmentally friendly manner.
NOVELTY - Method (M1) for separation of high caloric material from wood tar involves: obtaining an extract from wood tar in solvent; and removing solvent from the extract.    USE - For separation of high caloric material from wood tar (claimed) useful as high value added biofuel energy material for various industrial uses, and for recycle of wood tar in pyroligneous liquor manufacturer.    ADVANTAGE - The method solves problem associated with using charcoal kiln in which wood tar is produced as waste, solves problem of specific volume for wood tar condemnation by achieving validity use of waste resource by obtaining by-product having high caloric material from wood tar, allows recycle of wood tar in pyroligneous liquor manufacturer, and contributes to economic improvement. The solvent used for separation of high caloric material from wood tar has economical efficiency of solvent cost as is inexpensive as general solvent, has low boiling point, and results in excellent method of manufacturing high caloric material from wood tar that is cheap. The high caloric material obtained from wood tar has average caloric content of 7800-8600 kcal/kg, as compared to timber having average caloric content of 4500 kcal/kg, or wood tar having average caloric content of 5700-6300 kcal/kg. Thus high caloric material obtained from wood tar can be used as high value added energy material.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the high caloric material separated from the wood tar by the method (M1).
NOVELTY - Pelletizing culture medium for strawberry overhead cultivation, involves (a) stocking river sludge at outdoor, drying and placing in a crusher to crush into powder, (b) adding pig manure and mud in the river sludge, and then regulating pH value to 6.5-7 using lime, and mixing into the organic materials, (c) stirring the organic materials, pouring into a granulator, stirring and pelletizing, (d) putting the organic particle in oven for baking 8 minutes, and solidifying, and (e) cooling the organic particle using cold water at the moment of discharging.    USE - The method is useful for pelletizing culture medium used for strawberry overhead cultivation (claimed).    ADVANTAGE - The medium uses heavy metal polluted river sludge, provides strawberry needed organic fertilizer element and solves the problems of elevated strawberry cultivation, ventilation and water retention property.    DETAILED DESCRIPTION - Method for pelletizing culture medium for strawberry overhead cultivation, involves (a) stocking river sludge at outdoor, drying and placing in a crusher to crush into powder, (b) adding pig manure (10-20%) and mud (10-16%) in the river sludge (65-80%), and then regulating pH value to 6.5-7 using lime, and mixing into the organic materials, (c) stirring uniformly all the organic materials, pouring into a granulator, stirring uniformly and pelletizing, (d) putting the organic particle in oven at 800-1000 degrees C for baking 8 minutes, and solidifying, and (e) cooling the organic particle using cold water at the moment of discharging.
NOVELTY - A linezolid crystal form I is prepared by suspension crystallization process, which comprises mixing 1-10 pts.wt. of water with 1 pt.wt. of linezolid; increasing temperature to 95-105 degrees C to obtain suspension liquid; crystallizing at 70-100 degrees C; filtering at 0-90 degrees C; and vacuum-drying the filter cake at 30-90 degrees C to obtain linezolid crystal form I.    USE - Method for preparing linezolid crystal form I (claimed).    ADVANTAGE - The method uses water, rather than organic solvent, as suspension solvent, thus it is environment-friendly, safe and free from pollution. It provides high product yield. The filter cake is not washed, and the filtered mother liquid can be recycled, thus reducing energy consumption.
NOVELTY - An activated rice hull ash is prepared by mixing rice hull ash with 3 mol/liter hydrochloric acid to soak for 2-6 hours, water washing to neutral, drying, and baking for 2-8 hours at 500-600 degrees C.    USE - Method for preparation of an activated rice hull ash used in purification of biological diesel oil (claimed).    ADVANTAGE - The method is simple and convenient to prepare the activated rice husk ash with large specific surface area, strong absorbing ability, and low cost. It is provided with simple equipment, easy operation, no washing wastewater discharge, and environment pollution.
NOVELTY - The method involves crushing Turpinia Montana and adding into a super-critical extracting kettle. The liquid carbon dioxide is introduced. The extract is extracted and dissolved in the hot water. The active carbon is added for decoloring and polyamide resin is added into the decolored liquid for absorbing. The extract is eluted by ethanol aqueous solution in a gradient manner and the target component is collected. The concentrated solution is crystallized and the crystal is filtered.    USE - Method for extracting rhoifolin from turpinia montana leaves.    ADVANTAGE - The energy consumption is reduced, the pollution during the extraction of rhoifolin is reduced, the rhoifolin can be obtained by simple process, and purity of the obtained product is improved.
NOVELTY - As water base drilling fluid lubricant, biological diesel oil is used.    USE - As water base drilling fluid lubricant (claimed); and in research for biological diesel drilling fluid lubricant in water base drilling fluid.    ADVANTAGE - The biological diesel oil has excellent lubricant performance; has good dispersibility; and has good stability and anti-temperature performance.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a drilling fluid lubricant (L1) comprising biological diesel oil (100 ml), water (80-120 ml), emulsifying agent (4-10 g), and defoaming agent (2-6 g);    (2) preparing the drilling fluid lubricant (L1) involving adding water to the biodiesel, emulsifying agent and anti-foaming agent, and after emulsification to obtain the drilling fluid lubricant (L1).
NOVELTY - Method for producing organic fertilizer using tobacco waste, involves uniformly mixing pig manure as regulating agent with tobacco waste, then inoculating 0.1-0.5 wt.% of organic matter-decomposing inoculant to the mixed material, mixing the product uniformly, and fermenting the product, where the weight ratio of the pig manure and waste tobacco is 1:9-3:7.    USE - The method is useful for producing organic fertilizer (claimed).    ADVANTAGE - The fertilizer has organic matter content up to 40%, nitrogen, phosphorus pentoxide and potassium oxide content up to 6-9% and excellent quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for organic fertilizer prepared by the method.
NOVELTY - Preparing biomass gas from plant branches comprises performing hydrothermal treatment and cracking-gasification process for plant branches.    USE - The biomass gas is useful as fuel gas, coal gas and natural gas.    ADVANTAGE - The method produces product which has high yield, high calorific value and is ecofriendly.
NOVELTY - High clean bio-diesel comprises (in % by wt.): diesel oil (20-50), alcohol from biomass (5-25), vegetable oil (5-25), paraffin oil (5-15), a fatty acid (5-15) and an additive (3-10).    USE - The composition is useful for power generation, and as a substitute for diesel fuel in motor vehicles and in boilers of restaurants, hotels and canteens.    ADVANTAGE - The composition: is non-toxic and ensures complete combustion with high combustion efficiency, utilizes widely available and low-cost raw materials, saves fuel cost up to 10-25%, does not explode during combustion and is safe to transport and store, hence it is eco-friendly and economical.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing high clean bio-diesel, comprising weighing raw materials based on percentage by weight, transferring into a reaction kettle at normal pressure and at normal temperature, stirring with high speed shearing stirrer for 20-30 minutes, and filtering to obtain a finished product.
NOVELTY - Preparing biodiesel using high-acid-value waste oil comprises processing high-acid value waste animal/plant oil by performing hydrolysis to obtain fatty acid, separating to separate a residue containing non-lipid impurities and glycerol and hydrated fatty acid, dehydrating the hydrated fatty acid, performing esterification reaction with methanol, performing flash evaporation of methanol.    USE - The method is useful for preparing biodiesel using high-acid-value waste animal/plant oil.    ADVANTAGE - The method does not utilize catalyst and prevents washing process, reduces the usage of devices, separation and reaction steps, discharges less waste water and waste gas and ensures stable product quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for preparing biodiesel using high-acid-value waste oil, comprising: a hydrolysis tower, whose bottom is connected to steam for the hydrolysis of high acid-value waste animal/plant oil; a depressurizing sedimentation tank, where the hydrolysis product obtained in the hydrolysis tower is separated in the depressurizing sedimentation tank to obtain a residue containing non-lipid impurities and glycerol and hydrated fatty acid; a flash evaporation dehydrating tower for dehydrating the hydrated fatty acid; an esterification tower for reacting the dehydrated fatty acid with methanol; and a flash-evaporation dealcoholization tower for removing methanol of esterified reaction product in the flash-evaporation dealcoholization tower to obtain biodiesel.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the device for preparing biodiesel using high-acid-value waste oil.
NOVELTY - Method for preparing dominant population, involves selecting three kinds of cells from Enterobacter cloacae, Gordonia, and Pseudomonas putida, transferring the cells into nutrient solution, culturing each cell, centrifuging the product, cleaning the product using phosphate buffer, dissolving calcium alginate in the deionized water, then uniformly mixing product with the mixed cells in saline suspension, injecting the mixture into the calcium chloride water, and adding calcium alginate immobilized particles to the municipal wastewater.    USE - The method is useful for preparing dominant population for degrading municipal wastewater.    ADVANTAGE - The method improves total organic carbon (TOC) degrading efficiency.    DETAILED DESCRIPTION - Method for preparing dominant population, involves (a) selecting three kinds of cells from Enterobacter cloacae, Gordonia, and Pseudomonas putida, transferring the cells into 20-50 ml of nutrient solution, culturing each cell at 30 degrees C for 1-2 days, and then inoculating the culture in 500 ml of enrichment medium, centrifuging the product at speed of 6000 revolutions/minute (rpm) for 10 minutes, and respectively obtaining the logarithmic growth phase cells, (b) cleaning the product using phosphate buffer for 2-3 times, mixing 20-24% of E.cloacae, 54-58% Gordonia, and 26-18% of P.putida, suspending the product in the physiological saline, and refrigerating the product, (c) dissolving calcium alginate in the deionized water, until concentration reaches 4%, then uniformly mixing product with the mixed cells in saline suspension, injecting the mixture into the calcium chloride water having concentration of 0.1 M, forming the calcium alginate immobilized small balls with mixed cell having diameter of 3 mm, curing the product for 2 hours under the temperature of 20-25 degrees C, and (d) adding calcium alginate immobilized particles to the municipal wastewater.
NOVELTY - The method involves breaking municipal solid waste mixed with glass and non-magnetic metal to separate magnetic particles. The waste is put into solid-liquid separation tank to which corrosive organic solution is added for recycling light material such as plastic bag. The inorganic matter in waste is collected, crushed and graded. The cement building material is added to inorganic matter. The water separated from tank is put into water treatment pool. The solid separated from tank is fed into fermentation tank to obtain biogas. An organic fertilizer is obtained using biogas slurry.    USE - Method of processing mixed municipal solid waste resource.    ADVANTAGE - The municipal solid waste resource in building, chemical industry, agricultural production industry can be processed continuously, automatically and efficiently to obtain useful material, without causing pollution to the environment.    DESCRIPTION OF DRAWING(S) - The drawing shows the flowchart illustrating processing technique of mixed municipal solid waste. (Drawing includes non-English language text)
NOVELTY - The method involves crushing crop straw and rice straw into a crusher. The crop straw is selected from the mixture of wheat straw, corn straw and cotton straw. The mass ratio of the crop straw and rice straw is 2:2.3. The crushed crop straw and rice straw is mixed according to the total weight of the crushed crop straw and rice straw. The obtained crop straw and rice straw is cured through carbon rod by machine pressing block.    USE - Method for processing and solidifying straw carbon stick.    ADVANTAGE - The straw carbon stick can be processed economically. The efficiency, usability, transporting effect and storage capacity of the straw carbon stick can be improved.
NOVELTY - The method involves removing solid material in biomass oil milking. The phospholipid included in the oil is removed using esterification under acid catalyst and presence of alcohol e.g. methanol. The fatty acid less than predetermined content is removed.    USE - Manufacturing method of biodiesel feedstock oil used in production of biodiesel (claimed).    ADVANTAGE - The production efficiency of the biodiesel is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production method of biodiesel.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating manufacturing process of biodiesel feedstock oil. (Drawing includes non-English language text)
NOVELTY - The device has first heat exchanger for removing residual moisture which is positioned in input side, and for supplying heat to biomass. The second heat exchanger is attached to chamber for supplying heat to biomass having residual moisture. The fibrous material component included in the biomass is de-volatilized. The first cooling unit is provided for cooling the biomass de-volatilized from second heat exchanger. The second cooling unit is provided for again cooling the biomass cooled in the first cooling unit.    USE - Biomass fuel torrefaction device.    ADVANTAGE - The dried biomass can be consecutively supplied through feeder. The generated by-products can be reused through the waste-heat recovery process. The heating source is heated after the heat exchange or refrigerant is reused through waste-heat recovery process, so that the efficiency can be raised.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biomass fuel pre-processing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass fuel torrefaction device.
NOVELTY - A system for methane concentration control of biogas has a gas holder for storing biogas, a high calorie gaseous fuel storage tank, a combustor, an exhaust gas storage tank for storing exhaust gas, a base methane concentration biogas storage tank, a biogas and gas mixing chamber, and a gas component analyzer for measuring methane concentration of the biogas. The measured methane concentration is less than tolerance range of the standard fuel. The methane concentration of biogas is controlled such that high calorie gaseous fuel is supplied to biogas mixing chamber.    USE - System for methane concentration control of biogas (claimed).    DETAILED DESCRIPTION - A system for methane concentration control of biogas has a gas holder for storing biogas, a high calorie gaseous fuel storage tank for storing high calorie gaseous fuel, a combustor for combusting biogas and producing exhaust gas, an exhaust gas storage tank for storing exhaust gas, a base methane concentration biogas storage tank for storing biogas of base methane concentration, a biogas and gas mixing chamber for mixing high calorie gaseous fuel, and a gas component analyzer for measuring methane concentration of the biogas. The measured methane concentration is less than tolerance range of the standard fuel. The methane concentration of biogas is controlled such that high calorie gaseous fuel is supplied to biogas mixing chamber. An INDEPENDENT CLAIM is included for method for controlling methane concentration of biogas.
NOVELTY - The system has heat exchanger (100) that circulates heat exchanging medium in a chamber (110). A purification unit (200) condenses tar and particles in the synthetic gas using the heat exchanger. The purification unit has rotation drum (210) and a hollow spindle (220). The hollow spindle rotates the rotation drum. The rotation drum is provided with fixing discs (211,212).    USE - Purification system of synthetic gas from biomass waste.    ADVANTAGE - The tar elimination performance of the system is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the purification system of synthetic gas.    Heat exchanger (100)    Chamber (110)    Purification unit (200)    Rotation drum (210)    Fixing discs (211,212)    Hollow spindle (220)
NOVELTY - A rice-washing waste water is processed by carrying out rice washing process of rice washing of polished rice, concentrating rice washing waste water discharged at rice washing process in which solid content is 10-30 wt.%, waste processing one part or all part of recycled water which spin-dries at concentration process, and recycling concentrate obtained at concentration process as feed, food drinks or fertilizer.    USE - Processing of rice-washing waste water for feed for pigs, food-drinks, cosmetics and fertilizer (claimed).    ADVANTAGE - Digestive efficiency is excellent and has high nutritive value and good nutritional balance.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) rice-washing waste water concentrate comprising rice washing waste water and solid content (10-30 wt.%);    (2) feed comprising rice washing waste water concentrate;    (3) food-drinks comprising rice-washing waste water concentrate;    (4) cosmetics comprising rice-washing waste water concentrate;    (5) fertilizer comprising rice-washing waste water concentrate; and    (6) manufacture of rice-washing waste water concentrate involving rice washing process of polished rice and concentrating rice washing waste water discharged at rice washing process and carrying out solid content of 10-30 wt.%.
NOVELTY - An empty fruit bunch of coconut oil obtained by defruiting fruit from coconut-oil bunch or carbonized raw material is crushed. The crushed empty fruit bunch is dehydrated (d1). The crude oil obtained by pressing fruit formed by defruiting from coconut-oil bunch is washed with warm water, and the washing warm water is hydrated. The empty fruit bunch is press-dehydrated (d2), to obtain pre-processed empty fruit bunch of coconut oil.    USE - Pre-processing of empty fruit bunch of coconut oil during combustion and heat recovery of empty fruit bunch of coconut oil (claimed) for forming carbonized material used for fuel of blast furnace.    ADVANTAGE - The method efficiently and economically reduces the potassium content in empty fruit bunch of coconut oil. The recovered potassium is used in fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for combustion and heat recovery of empty fruit bunch of coconut oil.    DESCRIPTION OF DRAWING(S) - The drawing shows the flowchart of pre-processing of empty fruit bunch of coconut oil.    Preprocessor (10)    Crushing apparatus (11)    Pressing water-removal device (12)    Warm water hydration apparatus (13)    Fruit processing apparatus (20)
NOVELTY - The apparatus has hydrogen-producing tank e.g. electrolytic vessel (6) which electrolyzes water to produce hydrogen gas and oxygen gas. The electrodes (7) are provided in the hydrogen-producing tank. An insulation board is provided with respect to the electrodes.    USE - Water electrolysis function integrated fuel gas generation apparatus for supplying mixed hydrogen and oxygen gas to boiler.    ADVANTAGE - The generation of bubble in the electrolytic vessel is prevented. The fuel gas generation efficiency of the apparatus is improved. The anti-oxidation property of the electrode is improved. The fall of contact area of electrode and water is prevented. The moisture content in mixed gas can be removed effectively. The safety of the apparatus is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the water electrolysis function integrated fuel gas generation apparatus. (Drawing includes non-English language text)    Feed water tank (1)    Feed water pump (2)    Electrolytic vessel (6)    Electrode (7)    Boiler (8)
NOVELTY - The solid oxide fuel cell (1) has a fuel electrode (3) arranged on the first surface of a support substrate (2). A back layer (7) is arranged on the second surface of the support substrate. An electrolyte (4) is arranged on the fuel electrode. An air electrode (6) is arranged on the electrolyte. The fuel electrode and back layer comprise metal and ceramics.    USE - Solid oxide fuel cell for producing electrical energy.    ADVANTAGE - Can effectively prevent deformation of the solid oxide fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view and top view of solid oxide fuel cell.    Solid oxide fuel cell (1)    Support substrate (2)    Fuel electrode (3)    Electrolyte (4)    Air electrode (6)    Back layer (7)
NOVELTY - The assembly has an anode (11) that is formed on one side of solid polymer electrolyte membrane (13). A cathode (12) is formed on another side of membrane. An anode gas diffusion layer (14) is formed on one side of anode so that layer (14) is placed across anode from membrane. A cathode gas diffusion layer (15) is formed on one side of cathode so that layer (15) is placed across cathode from electrolyte membrane. A formic acid oxidation electrode (16) contains palladium and a solid polymer electrolyte and is formed between anode gas diffusion layer and anode.    USE - Membrane electrode assembly for fuel cell such as direct methanol fuel cell and polymer electrolyte fuel cell of fuel cell electric generation system (all claimed).    ADVANTAGE - The membrane electrode assembly can reduce the thickness of the formic acid oxidation electrode, and can reduce the content of palladium on the cathode side. The quantity of formic acid discharged from the fuel cell can be reduced so that the quantity of formic acid discharged from the fuel cell system can be reduced. The efficiency of the fuel cell can be improved. The electrode assembly can generate electricity without large drop in efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the membrane electrode assembly.    Anode (11)    Cathode (12)    Solid polymer electrolyte membrane (13)    Anode gas diffusion layer (14)    Cathode gas diffusion layer (15)    Formic acid oxidation electrode (16)
NOVELTY - An electrode for an electrochemical cell, comprises a carbon-comprising body, where at least a portion of the carbon of the carbon-comprising material consists of more than 99% sp2 hybridized carbons and where the carbon material has been acid treated and has undergone a set of low voltage cathodic cycles to form an electrode for a hydrogen evolution reaction (HER) and a hydrogen oxidation reaction (HOR).    USE - The electrode is useful for an electrochemical cell (claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) an electrochemical device, comprising at least one electrode, where the HER or the HOR can be performed, where the device functions as an electrolyzer or a hydrogen fuel cell; and    (2) an electrical energy generation system comprising: at least one primary energy generator comprising a fuel free natural renewable energy generator; and at least one secondary energy generator comprising one or more electrochemical devices, where the secondary energy generator is coupled to the primary energy generator, where the secondary energy generator functions as an electrolyzer to font hydrogen on demand when powered by the primary energy generator and where the secondary energy generator functions as a hydrogen fuel cell to generate electricity on demand.
NOVELTY - Engineered microalgae that produces lipid during exponential growth, where the microalgae has been engineered to enhance the expression level or activity of a protein that facilitates carbon assimilation or reduce the expression level or activity of a protein that facilitates nitrogen assimilation relative to the wild-type microalgae, is new.    USE - The engineered microalgae are useful for producing bio fuels.    ADVANTAGE - The engineered microalgae enhances the lipid production.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) producing lipids from microalgae comprising growing a culture of the engineered microalgae for a sufficient period of time and under appropriate conditions such that lipid production is enhanced during exponential growth, and harvesting lipids from the microalgae culture; and    (2) an expression vector comprising a nucleic acid sequence encoding pyr-decarboxylase operably linked to a transcription control element.
NOVELTY - The biodiesel manufacturing device has a maintenance storage tank for storing animal oil, fat or vegetable oil, and alcohol storage tank for storing alcohol. A catalyst mixer mixes catalyst with mixing material obtained from storage tanks. A pump is provided to supply mixed product from catalyst mixer to an influx unit (11) of a microwave reactor (16) provided in a microwave reactor module (10), such that esterification reaction is made inside the reactor. A launcher (15) and a plunger are provided in the microwave reactor for enhancing the production of microwave.    USE - Biodiesel manufacturing device.    ADVANTAGE - The simple structured biodiesel manufacturing device is designed easily while improving the yield about 10%. The processing condition according to the raw material or the catalyst can be controlled easily. The biodiesel can be economically manufactured and the production cost is saved.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the microwave reactor module.    Microwave reactor module (10)    Influx unit (11)    Microwave generator (14)    Launcher (15)    Microwave reactor (16)
NOVELTY - The system has a bioreactor (BR) and a tank (TQ1) for preparation of a medium. The tank is equipped with a mechanical stirrer, and microfiltration membrane module (MF1) is provided for adding sterilized culture medium to the bioreactor. An oxygenation module (OX), a reverse osmosis module and a product storage tank (TQ2) are also provided.    USE - System for obtaining bioproducts such as biosurfactants, biofuel, enzymes and chemicals for production of biofuels.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a system.    Bioreactor (BR)    Microfiltration membrane module (MF1)    Oxygenation module (OX)    Tank (TQ1)    Product storage tank (TQ2)
NOVELTY - A process of producing a biofuel while minimizing fossil fuel derived carbon dioxide emissions, involves: providing a renewable feed to an ester degradation zone to produce a first stream comprising at least one alcohol and a second stream comprising at least one acid; providing the first stream to a treatment zone for removing at least one salt and to obtain a treated stream; providing the treated stream to a reforming zone to obtain an effluent comprising hydrogen; and providing the second stream and at least a portion of the effluent to a refining zone for producing the biofuel.    USE - For producing biofuel such as renewable diesel and renewable jet fuel (claimed).    ADVANTAGE - The process produces biofuel while minimizing fossil fuel derived carbon dioxide emissions; provides a higher degree of integration and shared equipment to reduce capital and operating costs while minimizing the carbon usage in producing the biofuel; and minimizes the usage of hydrogen generated from fossil fuel sources.
NOVELTY - Method (M1) for recovering an insoluble element, involves mixing a cell lysis reagent into sludge or effluent, and separating particles of the insoluble element from lysed cells of the sludge or effluent physically.    USE - The method (M1) is useful for recovering insoluble element including selenium, rare earth or heavy metal from bioremediation sludge or effluent, sludge or effluent comprising insoluble element and microorganisms capable of reducing soluble forms of insoluble element. The method (M2) is useful for treating wastewater (claimed). The recovered selenium is used as a pigment in glass, vitamin supplement and fertilizer.    ADVANTAGE - The method is environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method (M2) for treating wastewater, which involves treating the wastewater in a bioreactor containing selenium reducing microorganisms, withdrawing a sludge comprising particles of elemental selenium and microorganisms from the reactor, disintegrating cells of the microorganisms, and passing the sludge through a solid-liquid separation device to remove at least some of the particles of elemental selenium from the remainder of the sludge.
NOVELTY - Catalytic cracking of aquatic microbial biomass, comprises: contacting the aquatic microbial biomass with at least one cracking catalyst at at least 450 degrees C to obtain a product stream; and separating at least one hydrocarbon fraction from the product stream.    USE - The process is useful for catalytic cracking of aquatic microbial biomass to produce carbon fraction, which is useful in gasoline composition (all claimed).    ADVANTAGE - The utilizes the aquatic microbial biomass that has high growth rates, utilizes large fraction of solar energy, can grow in conditions that are not favorable for terrestrial biomass, consumes carbon dioxide at a high rate, and reduce the carbon footprint of the overall process, and thus provides the hydrocarbon fraction having less than 1000 ppmw sulfur, in an economical, efficient and rapid manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a hydrocarbon fraction produced by the above process, comprising amines, pyrroles, pyridines, quinolines, indoles, acridines and carbazoles; and    (2) a gasoline composition comprising the hydrocarbon fraction and at least one additive.
NOVELTY - Preparing biodiesel involves reacting a triglyceride feedstock, alcohol and catalyst in a high-shear reactor to form a first intermediate reacted mixture; reacting the first intermediate reacted mixture in a low-shear reactor to form a second intermediate reacted mixture; and reacting the second intermediate reacted mixture in a second low-shear reactor to form a crude biodiesel reacted mixture.    USE - For preparing biodiesel (claimed).    ADVANTAGE - The process improves the quality of biodiesel using a three-stage transesterification reactor system to increase efficiency and yield and reduces impurities; and produces purified biodiesel product meets the triglyceride feedstock conversion level required by ASTM 6751.
NOVELTY - Production of cellulose based biofuels, involves: pyrolysing a cellulose-containing feedstock to form a slurry of bioliquids and char; hydrocracking the slurry to produce a hydrocarbon gas stream, a hydrocarbon liquid stream, an impurities stream, and a residue stream; distilling the liquid hydrocarbon stream to produce at least a naphtha stream, and a diesel stream; and gasifying the residue stream to produce at least a hydrogen and a carbon monoxide stream.    USE - For production of cellulose based biofuels (claimed).    ADVANTAGE - The process is simple and time saving. The process is also applicable to other solid hydrocarbon based fuels such as lignite and coal dissolved in solvents or liquefied under appropriate process conditions of pressure and temperature.
NOVELTY - The method involves sending biogas to two clandria-tube type exchanger-absorbers (1, 4). Hot water in the exchanger-absorber is cooled to produce purified flow of carbon dioxide relative to feed rate. Hot water is circulated in the exchanger-absorber to desorb impurities retained by absorbent and to regenerate the impurities. The biogas sending step and the hot water circulation step are performed alternatively on the two exchanger-absorbers that are arranged in parallel, where feed rate is sent to one exchanger-absorber when another exchanger-absorber is in a regeneration phase.    USE - Method for purifying biogas rich in methane and containing carbon dioxide and water, for producing liquid methane.    ADVANTAGE - The hot water is circulated in the exchanger-absorber to desorb impurities retained by the absorbent and to regenerate the impurities, thus achieving continuous regeneration of the impurities without a need for the biogas to ensure transfer of energy and without large consumption of utilities.    DESCRIPTION OF DRAWING(S) - The drawing shows a hydraulic circuit diagram of a system for purifying biogas.'(Drawing includes non-English language text)'    Clandria-tube type exchanger-absorbers (1, 4)    Vacuum pump (6)    Hot water exchangers (11, 12)    Compressor (13)    Cool water (15)
NOVELTY - A hydrogen generating apparatus comprises hydrogen generator (1) which produces hydrogen-containing gas by reforming reaction using source gas, source gas flow path (51) where source gas to be supplied to hydrogen generator passes, hydrodesulfurization device (2) which is provided in source gas flow path and removes sulfur compound in source gas, deoxidation device (3) which is provided upstream of hydrodesulfurization device and removes oxygen in source gas by combustion reaction, and cooler (4) which cools source gas flow path from deoxidation device to hydrodesulfurization device.    USE - A hydrogen generating apparatus for fuel cell system (claimed).    ADVANTAGE - Decrease in desulfurization performance of the hydrodesulfurization device is suppressed.    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 generating apparatus. (Drawing includes non-English language text).    Hydrogen generator (1)    Hydrodesulfurization device (2)    Deoxidation device (3)    Cooler (4)    Source gas flow path (51)
NOVELTY - The cell (1) has an oxygen side collector (12) and a hydrogen side collector (13) that are arranged on the surfaces of solid polymer electrolyte membrane (11). A separator (15,17) is positioned on outer side portions of oxygen side collector and hydrogen side collector. The edge of oxygen side collector is located in the outward portion of the edge of hydrogen side collector. The sealing element (22) is connected with the solid polymer electrolyte membrane and is positioned on outer periphery portion of hydrogen side collector.    USE - Hydrogen production cell of hydrogen production apparatus (claimed).    ADVANTAGE - The pressure resistance of hydrogen production cell can be improved. The high pressure hydrogen can be manufactured effectively in simple manner. The reliability of water electrolysis apparatus is improved. The hydrogen production cell is compact and is provided at low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for hydrogen production apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of hydrogen production cell.    Hydrogen production cell (1)    Solid polymer electrolyte membrane (11)    Oxygen side collector (12)    Hydrogen side collector (13)    Separators (15,17)    Sealing element (22)
NOVELTY - Polymer comprising many phosphazenium-containing repeating units (PRU) (I), is new.    USE - The polymer is useful in: a membrane; and a device, which is hydrogen generation device, fuel cell or water purification device (all claimed).    ADVANTAGE - The polymer enables the efficient operation of fuel cells under alkaline conditions in the presence of carbon dioxide, and facilitates the direction of hydroxide ion conduction that opposes that of methanol fuel crossover, thus mitigating or eliminating deleterious process in the fuel cell.    DETAILED DESCRIPTION - Polymer comprising many phosphazenium-containing repeating units (PRU) of formula ((-W1-CH(Z1-N(R1)-P+(NR1R2)(NR1R2)-NR1R2)-Y1-) (X-)) (I), is new.    Either R1, R2 = H, 1-15C alkyl, 5-10C cycloalkyl, or a point of attachment to a bivalent 1-20C hydrocarbyl; or    R1R2 = 5 or 6-membered ring;    W1, Y1, Z1 = direct bond or 1-10C hydrocarbyl; and    X = any counterion.    INDEPENDENT CLAIMS are also included for:    (1) a polymer comprising PRU and optionally random or sequentially placed hydrocarbon repeating units (HRU) of formula (-(-PRU-)n-(-HRU-)1-n-) (II), where the phosphazenium group has the formula ((R1R2N-P+-(NR1R2)3) (X-)) (III);    (2) a fuel cell comprising an anode, a cathode, a catalyst and the polymer;    (3) a phosphazenium compound of formula((R3R4N-P+-(NR3R4)3) (X-)) (IV);    (4) a substituted phosphazenium compound of formula (V); and    (5) an electrocatalyst ink comprising (IV) or (V) phosphazenium compound.    n = 0.05-1, where in (III) at least one of R2 is a point of attachment to a 1-20C hydrocarbyl; either    R3, R4 = H, 1-15C alkyl, 5-10C cycloalkyl, or aliphatic (1-15C) hydrocarbyl containing a double bond in a 5-8C cycloalkene; or    R3R4 = 5 or 6-membered ring, where in (IV) at least one of R3 is an aliphatic (1-15C) hydrocarbyl containing a double bond in a carbocycle; and    Q = 5-8C cycloalkene.
NOVELTY - Synthesis gas conversion catalyst comprises a combination of molybdenum, cobalt, an alkali metal and chromium on a carbon support.    USE - The catalyst is useful for converting synthesis gas to a mixture of alcohols such as ethanol and propanol.    ADVANTAGE - The catalyst provides a greater carbon monoxide conversion than the same catalyst save for replacing the chromium with equal molar amount of cobalt at identical conditions of temperature and gas hourly space velocity.
NOVELTY - A catalyst composition comprises molybdenum, sulfur and alkali metal ion on nanofibrous, mesoporous carbon molecular sieve support.    USE - Catalyst composition is used for converting mixture of hydrogen gas and carbon monoxide gas to higher alcohol (claimed).    ADVANTAGE - The catalyst composition has excellent selectivity with respect to ethanol.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) production of catalyst composition, which involves impregnating nanofibrous, mesoporous carbon molecular sieve support with molybdenum, sulfur and alkali metal ion; and    (2) process for converting mixture of hydrogen gas and carbon monoxide gas to higher alcohol.
NOVELTY - An anaerobic digestion method involves pre-treating livestock excretion by contacting excretion with blade that rotates at speed of 4000-20000 rpm. The pre-treated excretion is passed through orifice under pressure of 20-800 psi, and resulting excretion is subjected to ozone treatment.    USE - Anaerobic digestion method for pre-treating livestock excretion.    ADVANTAGE - The method enables increasing anaerobic digestibility, biogas production and methane content.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an apparatus for pre-treating livestock excretion.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating an anaerobic digestion method.'(Drawing includes non-English language text)'
NOVELTY - Method for producing and supplying biogas, involves providing a biogas supply system equipped with first and second microalgae culture tanks provided with a nutrient source supply unit or carbon dioxide supply unit (4), and methane fermentation tank (8) to which the concentrated microalgae culture solution is supplied for carrying out methane fermentation.    USE - The method and system are useful for producing and supplying biogas (claimed) which is used as fuel.    ADVANTAGE - The method can be performed stably under uniform and efficient conditions.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for system, which comprises first and second microalgae cultivation tank provided with carbon-dioxide supply unit or nutrient supply unit, and methane fermentation tank, concentration apparatus, and biogas holder (15) for storing the biogas emitted in the concentrate tank (7).    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of system for producing and supplying biogas.    Nutrient adjustment supply tank (3)    Carbon dioxide supply unit (4)    Thickener tank (5)    Biogas holder (15)
NOVELTY - The method involves hydrating guest molecule such as carbon dioxide and methane in the gap in stratum (2) in specific temperature and the pressure condition. The liquid of the guest molecule micro particles is smaller than the gap in the stratum. An opening portion (20a) of pressure-resistant container (20) located in the stratum is opened, for inhaling and extruding the fluid from the container. The emitted-heat amount is controlled by changing the mixing rate of the liquid of guest molecule.    USE - Method for generating gas hydrate such as carbon dioxide hydrate and methane hydrate (all claimed).    ADVANTAGE - The gas hydration can be controlled and accelerated artificially by inhaling and extruding the fluid rapidly. The controllability and the operativity of the heat generation Of gas hydrate can be improved. The improvement of the safety of the recovery efforts of gas resources.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for enhanced oil recovery method of the gas resources.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the gas hydrate generation process.    Methane hydrate (1)    Stratum (2)    Carbon dioxide hydrate (5)    Pressure-resistant container (20)    Opening portion of pressure-resistant container (20a)
NOVELTY - Ethane hydrate (1) obtained by reacting ethane gas and pure water is stored under atmospheric pressure at a temperature greater than -20 degrees C and less than 0 degrees C.    USE - Storage of ethane hydrate.    ADVANTAGE - The method enables economical, efficient and safe storage of ethane hydrate at a temperature at which ethane hydrate does not decompose.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view explaining the mechanism of the self-preservation effect of gas hydrate.    Ethane hydrate (1)    Water film layer (2)    Ice film (3)
NOVELTY - Synthesizing a sex attractant pheromone (I) comprises: producing a halo substituted alkanal compound (II) in an oxidation reaction on a halo substituted alkyl alcohol compound (III); producing a halo substituted dialkoxy substituted alkyl compound (IV) in an O-alkylation reaction on (II); and producing (I) in a reduction reaction and a hydrolysis reaction on a dialkoxy substituted diynyl compound (V).    USE - The method is useful for synthesizing sex attractant pheromone (I).    ADVANTAGE - The method provides the highly stable sex attractant pheromone by utilizing less reaction steps and in an environmentally friendly manner.    DETAILED DESCRIPTION - Synthesizing a sex attractant pheromone of formula (R3-R7-R1-Y2) (I) comprises: producing a halo substituted alkanal compound of formula (Y2-R1-X) (II) in an oxidation reaction on a halo substituted alkyl alcohol compound of formula (Y1-R1-X) (III); producing a halo substituted dialkoxy substituted alkyl compound of formula (W1-R1(W1)-X) (IV) in an O-alkylation reaction on (II); and producing (I) in a reduction reaction and a hydrolysis reaction on a dialkoxy substituted diynyl compound of formula (R3-R6-R1-(W1)2) (V).    X = halo;    Y1 = OH;    Y2 = 0;    R1 = (-CH2-)m or alkyl;    R3 = CH3-(CH2)n- or alkyl;    R6 = (-CC-)q or alkynyl;    R7 = -C=C-C=C-, alkenyl, or R8;    W1 = -O-alkyl, -O-R3, or -O-CH2-CH3;    R8 = cis (-CH=CH-CH=CH-);    m = 5-12;    n = 1-3; and    q = 1 or 2.
NOVELTY - A modified compound comprises mixture containing metal complex and carbon carrier modify-processed at greater than or equal to 500 degrees C.    USE - Modified compound for electrode catalyst for fuel cell and metal complex (claimed). Can also be used as modification hydrogen-producing catalyst, oxygen sensor, pharmaceuticals and agrochemicals, and antioxidant of foodstuff.    ADVANTAGE - Oxygen reduction catalyst activity is high.    DETAILED DESCRIPTION - A modified compound comprises mixture containing metal complex which makes compound of formula (1) a ligand, and carbon carrier modify-processed at greater than or equal to 500 degrees C.    R1,R2,R4,R5=H or hydrocarbyl group;    R3,R6=hydrocarbyl group in which R1, R2 and R3 or R4-R6 may be same or different and may combine with each other and form a ring;    Q1=bivalent group of formulae (i) or (ii); and    R4,R5=H or hydrocarbyl group each independently.    INDEPENDENT CLAIMS are included for:    (1) composition comprising modified compound and carbon carrier and/or high molecular compound;    (2) catalyst comprising modified compound and the composition;    (3) electrode catalyst for fuel cell comprising the catalyst;    (4) complex compound of formula (2); and    (5) metal complex comprising the compound of formula (2), and metal atom or metal ion.    R1,R2,R7=H or hydrocarbyl group; and    R3=hydrocarbyl group in which R1-R3 and R7 may be same or different or may combine with each other to form a ring.
NOVELTY - Aerobic-anaerobic treatment of fermentation substrate, preferably in agricultural biogas plants with a high proportion of plant biomass to be fermented, comprises treating the recirculated air, which is pressed within a separate container (2) parallel to the fermentation process and subsequently recycling the process.    USE - The method is useful for aerobic-anaerobic treatment of fermentation substrate, preferably in agricultural biogas plants.    ADVANTAGE - The method accelerates the reaction kinetics by aerobic treatment of the entire process, thus it reduces the residence time and provides the required reactor volume.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the device for carrying out the aerobic-anaerobic treatment of fermentation substrate.    Pump (1)    Container (2)    Pipe connections (3)    Compressor (7)    Pipe system (8)
NOVELTY - Disclosed is process for production of ethanol from lignocellulosic feedstock. Banana pseudostem wastes are hydrolyzed using mild mineral acid which released maximal level of fermentable aqueous material. The hydrolysate for ethanol production is obtained using Saccharomyces cerevisiae (MTCC 170) and Issatchenkia orientalis (MTCC 10641) strains. Ethanol fermentation efficiencies are 69.72% and 84.67%. The two step process on production of ethanol from banana pseudostem waste is separate hydrolysis and fermentation process. The method is simple and cost-effective to produce ethanol by selectively ethanol tolerant yeast utilizing fermentable sugar based solutions, where it results in maximum ethanol yield with a reduced amount of energy utilization. Image 0/0
NOVELTY - Rapidly processing city kitchen garbage, involves collecting, recycling and separating the city kitchen garbage in large scale, crushing the uniform kitchen garbage into fine slurry, extracting the slurry by slurry pump, and the high temperature steam sterilizing and drying to generate non-toxic and dry powder of restaurant garbage bag packing; conveying the dry powder of the garbage without toxic to restaurant, sending the dry powder of restaurant garbage and bagasse, banana rod, peanut shell and agricultural waste together for biological collaborative fermenting and retting; fermenting material as high quality farmyard manure or fertilizer as cultivation economic animal.    USE - For rapidly processing city kitchen garbage (claimed).    ADVANTAGE - The method is simple, low cost, fast processing city kitchen garbage, convenient and practical.
NOVELTY - Production of carboxyl group-containing isothiocyanate compound (II) involves reacting amino compound having carboxyl group (I), thiocarbonyldiimidazole, and base in a solvent.    USE - Production of carboxyl group-containing isothiocyanate compound used for preparing organic material, pharmaceuticals and agrochemicals.    ADVANTAGE - The method efficiently and economically provides high yield of carboxyl group-containing isothiocyanate compound without using toxic chemicals.    DETAILED DESCRIPTION - Production of carboxyl group-containing isothiocyanate compound of formula: (SCN)m-A-B'-(CO2)n (II) involves reacting amino compound having carboxyl group of formula: (H2N)m-A-B'-(CO2H)n (I), thiocarbonyldiimidazole, and base in a solvent.    m,n=1 or 2;    A=6-14C aryl or 1-12C saturated hydrocarbyl (both optionally substituted by halo, nitro, cyano, 1-6C alkyl, hydroxy, protected hydroxy, 1-6C alkoxy, 1-6C dialkylamino, protected amino, protected 1-6C monoalkylamino, 1-6C alkyl carbonyl, or 1-6C alkoxycarbonyl), where methylene group in 1-12C saturated hydrocarbyl is optionally substituted by O, nitrogen atom substituted by 1-6C alkyl or protected nitrogen atom;and    B'=single bond or A.
NOVELTY - A coated slow-release organic fertilizer comprises a core comprising volatile agricultural fertilizer (particularly urea), and a coating layer comprising plant ash/biogas residue mixture and bentonite. The ratio of agricultural fertilizer, plant ash and biogas residue, and bentonite is 20-23:21-21.5:20-21. The plant ash is mixture of plant ashes with sunflower ash content of 50%. The biogas residue is medium-temperature anaerobic fermentation product of animal manure and straw.    USE - Coated slow-release organic fertilizer used for daily fertilization in rural areas.    ADVANTAGE - The slow-release fertilizer is simple to produce; has low cost, improved utilization rate, and no side effects to crops and growth environment; uses local materials; saves fertilizer usage and economic investment of farmer; and will not cause soil compaction.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fertilizer by:    (A) crushing plant ash and screening to obtain 60-120-mesh particles, filtering biogas residue with water content of 80-90% to obtain 60-mesh particles, uniformly mixing biogas residue and plant ash at ratio of 20:1-1.5, and adding water to bentonite and stirring until water content of 50%; and    (B) fully mixing agricultural fertilizer particles with diameter of 2-4 mm, biogas residue/plant ash mixture and bentonite, naturally air-drying, and filtering.
NOVELTY - Production of organic fertilizer involves filtering polyoxin fermentation liquid through a plate frame filter to obtain block-shaped polyoxin residues with moisture content of 60-70%; treating the residues at 120-160 degrees C and 0.100-0.520 MPa for 5-30 minutes; adding monopotassium phosphate and carrier, and uniformly stirring; adjusting pH to 5.5-8 with borax; and drying.    USE - Method for producing organic fertilizer (claimed) used for crops.    ADVANTAGE - The method is simple and pollution-free, and has short processing time and low cost. The fertilizer has organic material content of 63% and is rich in minerals and other plant growth-stimulating substances. Ascarid mortality rate, coliform values and other heavy metal content are in the standard range.
NOVELTY - Quick maturing agent comprises 10-50 parts by weight (pbw) of a biological carbon black, 20-60 pbw of a biological organic matter, 0.01-1 pbw of a probiotic agent, and 2-6 pbw of a synergist, where: e.g. the biological organic matter is cow dung, pig manure, decaying straws and/or bean pulp; the probiotic agent is nitrogen-fixing bacteria, phosphate-solubilizing bacteria, silicate bacteria and/or Bacillus; the synergist is pyroligneous acid, amino acid, humic acid, or natural plant extraction growth agent; and the maturing agent is prepared by mixing the raw material.    USE - The quick maturing agent is useful for carbon based soil.    ADVANTAGE - The quick maturing agent improves the soil quality, creates good ecological environment, and is economic.    DETAILED DESCRIPTION - Quick maturing agent comprises 10-50 parts by weight (pbw) of a biological carbon black, 20-60 pbw of a biological organic matter, 0.01-1 pbw of a probiotic agent, and 2-6 pbw of a synergist, where: the biological organic matter is cow dung, pig manure, decaying straws and/or bean pulp; the probiotic agent is nitrogen-fixing bacteria, bacteria phosphate-solubilizing bacteria, silicate bacteria and/or bacillus; the synergist is pyroligneous, amino acid, humic acid, or natural plant extraction growth agent; and the maturing agent is prepared by mixing the raw material, pelletizing the mixed raw materials through a pelletizing machine with the diameter of 3.5-6.5 mm to form powder, weighing and packing the powder, and storing the packed product.
NOVELTY - Preparing organic inorganic compound fertilizer, comprises: taking the agricultural waste, humic acid, animal excrement, mixing and fermenting and then performing stand placing process; and sieving the material after the stand placing process, adding auxiliary elements and chemical raw material fertilizer in the materials after sieving, mixing and stirring.    USE - The process is useful for preparing organic inorganic compound fertilizer. No biological data given.
NOVELTY - An organic fertilizer comprises phosphorus tail mineral powder (20-35 parts by weight (pbw)), crop straw powder (20-40 pbw), and soy sauce dregs (20-40 pbw).    USE - As a fertilizer (claimed).    ADVANTAGE - The organic fertilizer has characteristics of comprehensive nutrition, and lasting fertilizer effect; increases the soil organic matter; reduces the environment pollution, and provides the necessary element for crops; improves the physical and chemical properties and biological activity of the soil; and reduces the production cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing organic fertilizer by using waste phosphorus tail mineral powder, involving mixing phosphorus tail mineral powder, crop straw powder and soy sauce residue uniformly based on the weight ratio; adding water according to the ratio of material to water of 1:2-1:3; inoculating Aspergillus niger (4-5%), Lactobacillus (2-3%), Acetobacter (3-4%), and Bacillus megaterium (4-6%); fermenting for 3-5 days at 28-32 degrees C; adding water (15-20%); fermenting for 10-15 days at 50-65 degrees C; and drying and packaging to obtain the product.
NOVELTY - Microbial composition comprises (in wt.%): Bacillus subtilis (5-50), Trichoderma atroviride (0.5-30), Saccharomyces cerevisiae (1-35), Aspergillus oryzae (1-30), Penicllium expansum (0.1-20) and Trichoderma viride (0.5-25).    USE - The microbial composition is used for fermenting straw to obtain organic fertilizer (both claimed), where the straw is obtained from rice, wheat and corn.    ADVANTAGE - The microbial composition completely decomposes the crop straw within a week. The nutrient elements in the straw are accelerated to provide more nutrients to the growth of crops at a later stage. The composition maintains and improves soil fertility, enhances soil organic matter, improves physicochemical property of soil and improves crop yield at a rate of more than 5%.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for preparing organic fertilizer, involves fermenting the straw using the microbial composition; and    (2) organic fertilizer obtained by the above-mentioned method.
NOVELTY - Ecological composite shale organic fertilizer used for improvement of soil, eliminating soil compaction and promoting soil nature, comprises composite shale as substrate, and decomposing ecological agent.    USE - The fertilizer is used for improvement of soil, eliminating soil compaction, and promoting soil nature (claimed) , reducing soil pests, activating soil nutrients, nitrogen fixation, supplementing potassium, phosphorus and mineral nutrients, increasing crop nutrient for promoting development of root system, seedling, and promoting flower formation and fruiting, improving the quality of products, promoting precocity, increasing disease resistance, and cold/drought stress, and improving strength of plants.    DETAILED DESCRIPTION - Ecological composite shale organic fertilizer used for improvement of soil, eliminating soil compaction, and promoting soil nature, comprises composite shale as substrate, and decomposing ecological agent. The decomposing ecological agent comprises (in wt.%): saw dust (20), soybean meal (10), chicken manure (30-40), brown sugar (1-2) and fermentation activator (0.5-1) and yeast (0.1-0.2). The composite shale contains black shale (30) and carbonaceous shale (30), whose particle size is 80-100 meshes. The decomposing ecological agent is prepared by mixing uniformly wood chips powder (20) of 30-50 meshes, chicken manure powder (30-40) obtained by adding dry chicken manure powder (2 kg) and preservative, bean cake composed of soybean meal and brown sugar with water, and fermenting using yeast at predetermined temperature.
NOVELTY - Composting treatment method of pathogenic bacterial pollutant, involves burying to-be-processed samples into a base material stockpile to compost and ferment at 50-60 degrees C and in a humidity of 60-70%, fermenting the stockpile for at least 6 days under a pH value of 8.5-9.0.    USE - The method is useful for composting treatment of pathogenic bacterial (Bacillus or Clostridium) pollutant (claimed), and other pollutants including weed seeds. The treated product can be used as fertilizer.    ADVANTAGE - The treated product protects the environment, improves the soil fertility, increases soil water holding capacity, reduces the volume, odor and pathogen of the organic material and realizes the recycling use of resource. The method uses simple equipment, is inexpensive and easy to perform.
NOVELTY - Microecological alginic acid synergist of organic fertilizer, comprises (in wt.%): alginic acid (6-60), mannitol (0.1-5), crude protein (1-20) and composite Bacillus. The composite Bacillus comprises B.licheniformis, B.subtilis, B.brevis, B.megaterium, Sphingobacterium and B.mucilaginosus, and the total number of viable bacteria is 0.1-50 billion cells per ml.    USE - Microecological alginic acid synergist of organic fertilizer.    ADVANTAGE - The microecological alginic acid synergist of organic fertilizer contains complete natural active effective elements in the seaweed, e.g. seaweed polysaccharide, crude protein, and trace elements including nitrogen, phosphorus, calcium, iodine, potassium, magnesium, manganese and selenium.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the microecological alginic acid synergist of organic fertilizer, which involves mixing kelp, sea mustard, gulfweed and cutweed and crushing into seaweed powder of 30-60 meshes, placing the seaweed and performing depolymerization in a reactor, where the dosage of the seaweed is 2-350 g per l of the reactor, the depolymerization temperature is performed at 50-60 degrees C and pH 2-9 for 22-72 hours, obtaining alginic acid solution, sterilizing and then inoculating the composite Bacillus which is 0.2-10% of the amount of the seaweed powder, heating, oxygenating and fermenting to obtain the product.
NOVELTY - Producing N-methyl potassium dithiocarbamate, involves: mixing and reacting carbon disulfide with monomethyl amine at 15-35 degrees C to generate N-methyl dithiocarbamate, and then reacting the N-methyl dithiocarbamate with potassium hydroxide at 35-40 degrees C to obtain the N-methyl potassium dithiocarbamate.    USE - For producing N-methyl potassium dithiocarbamate (claimed), for preventing and treating insect disease, soil transmission disease, and for weed control, for controlling fungus, nematodes, and insect.    ADVANTAGE - The method has low cost, involves easy technique, has control of finished product quality and provides high purity and yield rate. The method is simple. The yield is 98%. The method recycles excessive carbon disulfide thus reduces environmental pollution.    DETAILED DESCRIPTION - Producing N-methyl potassium dithiocarbamate, involves: mixing and reacting carbon disulfide with monomethyl amine at 15-35 degrees C to generate N-methyl dithiocarbamate, and then reacting the N-methyl dithiocarbamate with potassium hydroxide at 35-40 degrees C to obtain the N-methyl potassium dithiocarbamate, preferably the method involves adding the carbon disulfide in one batch and then slowly dropping the monomethyl amine, sufficiently reacting under an agitation condition to obtain the N-methyl dithiocarbamate; adding the potassium hydroxide to neutralize the obtained N-methyl dithiocarbamate; and adding wastewater produced in a postprocessing process into N-methyl dithiocarbamate solution to obtain aqueous solution with mass percentage concentration of 52-60%. The monomethyl amine, the carbon disulfide and the potassium hydroxide are added according to the molar ratio of (0.95-1) to (1-1.2) to (1-1.05).
NOVELTY - Foliar fertilizer comprises (in %mass): decomposition liquid (15-25), amino acid powder (15-20), nitrate of lime (8-10), monopotassium phosphate (3-6), borax (2-5), polyaspartic acid (5-8), chitosan (0.3-1), bacterial agent (0.5-1.5), surfactant (0.2-0.5), and water (23-51). The bacterial agent is the mixture (0.8-1.2 parts mass)of Bacillus thuringiensis and B.subtilis, where the viable count of the B.thuringiensis is greater than 10 billions/g, and the count of the B.subtilis is greater than 30 billions/g.    USE - The foliar fertilizer is useful for field crop, commercial crop and fruit and vegetable crops (claimed).    ADVANTAGE - The fertilizer provides disease resistance to crops.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the above-cited fertilizer, which involves (a) inoculating silicate bacteria strain to sterilized seed culture in flask under aseptic condition, placing the flask in an air table to culture, where the culturing temperature is 28-32 degrees C, the oscillation frequency is 200-240 revolutions per minute (rpm) and the culturing time is 22-26 hours, inoculating the cultured strain in seed culture in flask, culturing the product at 28-32 degrees C for 45-50 hours and fermenting the product, and (b) adding Saccharomycetes, lactic acid bacteria and Bacillus powder in the fermented product, stirring the product for 8-20 hours at 25-35 degrees C, and filtering the product, where the mass ratio of Saccharomycetes, lactic acid bacteria, Bacillus and medical stone powder in the mass ratio of 1:0.001-0.003:0.001-0.003:0.001-0.003:0.3-0.5.
NOVELTY - Method for preparing fertilizer, involves using (in %): cottonseed cake (10), chicken manure (25-35), pig manure (35-45), monoammonium phosphate (5), potassium sulfate (10), bone powder (4) and magnesium amino acid chelate (1) as raw materials to obtain product.    USE - The method is useful for preparing fertilizer for dragon fruit (claimed). The fertilizer preferably as chemical fertilizer is useful for dragon fruit during its blooming and fruiting stage.    ADVANTAGE - The fertilizer enables earlier blooming in dragon fruit and fruiting with lesser fruit drop, as the fertilizer is prepared in accordance with growth requirements of the dragon fruit plant. The fertilizer enables fruit to grow bigger with higher sugar content and good mouth feel. The fertilizer is simple and convenient to prepare in batches at lower production cost. The fertilizer is suitable for providing beneficial effects to dragon fruit plant for period of more than three years.
NOVELTY - Organic fertilizer produced by sludge, comprises (in parts weight): diammonium phosphate (35-39), ammonium sulfate (20-22), potassium chloride (6-7.5), calcium superphosphate (32-35), and fermentated sludge (53-55).    USE - The organic fertilizer is useful for agriculture.    ADVANTAGE - The organic fertilizer has reduced the sludge moisture content, stabilized the sludge stable components and no harmful microorganism, and is prepared by simple method.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of the above-cited organic fertilizer, which involves (a) paving the fresh sludge on the ground, naturally drying for 3-5 days, and stacking until the water is substantially dried, (b) deciding the stacking size according to the ground (where the normal height is 1 m high, the lower bottom is 1x 1 m, and the upper bottom is 1.5x 1.5 m), arranging several air hole pipes on the ground, paving an air supplying pipe on the ground sawdust, stacking for 3-5 days at 55-65 degrees C and drying sludge using a gas pipe and gas pump per day to stack in the oxygen, and again stacking at more than 55 degrees C for more than 3-4 days, spreading and drying for 1-2 days, and (c) adding the fermented sludge, completely and uniformly stirring, and then passing through granulator to obtain the organic fertilizer product.
NOVELTY - A cynarin is prepared by crushing artichoke leaf, adding water, reflux heating, filtering, adding precipitant to the filtrate, filtering, subjecting filtrate to anion resin, washing with sugar aqueous solution until the washing solution turns neutral, eluting with acidic aqueous solution, subjecting eluate to a macroporous resin column, washing column with water until the product is neutral, adding ethanol solution, extracting, filtering, decompressing and concentrating the filtrate.    USE - Method of preparing a cynarin for preparing drug or healthcare product.    ADVANTAGE - The method is simple and environment-friendly, has low energy consumption, and prepares cheap product having good quality.    DETAILED DESCRIPTION - A cynarin is prepared by crushing artichoke leaf, adding water (8-15 crushed material quantity), reflux heating for 1-2 hours for 2-3 times, filtering, adding precipitant to the filtrate, filtering, subjecting filtrate to anion resin, washing with sugar aqueous solution until the washing solution turns neutral, eluting with 0.5-1% acidic aqueous solution (4-6 BV), subjecting eluate to a macroporous resin column, washing column with water until the product is neutral, adding 40-70% ethanol solution (5-8BV), extracting, filtering, decompressing and concentrating the filtrate to obtain extract having density of 1.2-1.4, filtering, adding deionized water and 90-99% ethanol to the filter cake, reflux heating, decompressing, and vacuum drying.
NOVELTY - A Bacillus thuringiensis HSB1001 (KCTC 11719BP), is new.    USE - The B.thuringiensis HSB1001 is useful for preparing compost of livestock waste chosen from cow dung, pig ordure and fowl droppings (claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) microbial inoculum comprises B.thuringiensis HSB1001 strain or its culture medium; method of preparing microbial inoculum involves culturing B.thuringiensis HSB1001; and method of preparing the compost involves mixing livestock waste and microbial inoculum containing B.thuringiensis HSB1001.
NOVELTY - Method for preparing compost involves fermenting to-be-processed raw material for 6 days at 55 plus minus 5 degrees C, humidity of 65 plus minus 5% and pH of 8.5-9.5 using harmless Tilletia controversa Kuhn teleutospore.    USE - The method is useful for preparing compost which is used as fertilizer.    ADVANTAGE - The method reduces the volume of organic material and the compost prepared by the method improves soil fertility, and water holding capacity of the soil.
NOVELTY - A Stevia rebaudiana slag is utilized for cultivating edible fungi.    USE - Stevia rebaudiana slag for cultivating edible fungi.    ADVANTAGE - The slag is inexpensive and eco-friendly, and improves production efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for cultivating edible fungi.
NOVELTY - A microbe biocontrol organic fertilizer preparing method involves preparing solid culture medium of edible mushroom bran. Trichoderma spore suspension is inoculated in the solid culture medium to culture the Trichoderma and obtain Trichoderma culture that is mixed with sludge to aerobically ferment the Trichoderma culture. The fermented mixture is stood to perform secondary fermentation process. The secondary fermented mixture is screened to collect screening substances with e.g. undesirable particles, to obtain microbe biocontrol organic fertilizer.    USE - Method for preparing a microbe biocontrol organic fertilizer.    ADVANTAGE - The method enables reusing edible mushroom bran, reducing environmental pollution and preparing organic fertilizer so as to improve soil fertility, thus preventing and treating plant diseases.    DETAILED DESCRIPTION - A microbe biocontrol organic fertilizer preparing method involves preparing a solid culture medium of edible mushroom bran. Trichoderma spore suspension is inoculated in the solid culture medium of edible mushroom bran to culture the Trichoderma and obtain the Trichoderma culture. The Trichoderma culture is fully mixed with sludge to aerobically ferment the Trichoderma culture. The aerobically fermented mixture is stood to perform secondary fermentation. The secondarily fermented mixture is dried, grinded and screened to collect screening substances with undesirable and desirable particles to obtain microbe biocontrol organic fertilizer. An INDEPENDENT CLAIM is also included for a microbe biocontrol organic fertilizer.
NOVELTY - Method of producing fermented butyl alcohol, involves fermenting Jerusalem artichoke (raw material) using butanol producing strain.    USE - The method is useful for producing fermented butyl alcohol which is used as biofuel.    ADVANTAGE - The method is suitable for industrial production.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) fermentation culture for producing butyl alcohol, comprising (a) Jerusalem artichoke hydrolyzate, and (b) inorganic salt, where pH of the fermentation culture is 5.3-5.8, the Jerusalem artichoke hydrolyzate is hydrolyzed using acid and sugar (45-100 g/l); and    (2) method for preparing the fermentation culture, involves (a) providing the Jerusalem artichoke hydrolyzate, and (b) adding inorganic salt to the Jerusalem artichoke hydrolyzate to prepare the fermentation culture for producing butyl alcohol.
NOVELTY - A composite microorganism seaweed organic liquid fertilizer preparing method involves adding (in weight parts) complex enzyme (0.1-0.6) and biological fermenting agent (0.1-0.4) to seaweed crushing liquid (100) followed by mixing uniformly. The obtained material is loaded to a fermenting tank. A functional fungicide is added to sterilized filter liquid, where the fungicide is nitrogen-fixing bacteria or potassium-decomposing bacteria. Bacillus subtilis and Bacillus licheniformis are added to the filter liquid followed by regulating nitrogen, phosphors and potassium nutrients.    USE - Method for preparing composite microorganism seaweed organic liquid fertilizer.    DETAILED DESCRIPTION - A composite microorganism seaweed organic liquid fertilizer preparing method involves adding (in weight parts) complex enzyme (0.1-0.6) and biological fermenting agent (0.1-0.4) to seaweed crushing liquid (100) followed by mixing uniformly, and carrying aerobically fermenting. The obtained material is loaded to a fermenting tank followed by carrying aerobically fermenting for 5-8 days at pH of 5-7 at 40-60 degrees C, obtaining fermenting liquid, filtering the fermenting liquid, obtaining filter liquid, and sterilizing the filter liquid for 20-40 minutes at 120-125 degrees C. A functional fungicide is added to the sterilized filter liquid, where the fungicide is nitrogen-fixing bacteria, phosphor-decomposing bacteria or potassium-decomposing bacteria. Bacillus subtilis and Bacillus licheniformis are added to the filter liquid followed by regulating nitrogen, phosphors and potassium nutrients.
NOVELTY - An agriculture and forest biomass secondary process reaction gasification furnace has a rotary ejector connected with a drawing device and a gasification reaction chamber. A top part of the gasification furnace is divided into a preheating drying chamber, a reaction chamber and air inlet pipes. A lower part of the gasification furnace is provided with a large aperture grate and a fixed fire grate. The large aperture grate is provided for covering a carbon inlet and a discharging device. A large aperture furnace is connected to a dust remover by a pipeline.    USE - Agriculture and forest biomass secondary process reaction gasification furnace for use in a steel industry.    ADVANTAGE - The furnace can be completely combusted, and easily purifies gas and avoids polluting environment.    DETAILED DESCRIPTION - An agriculture and forest biomass secondary process reaction gasification furnace has a motor driven to rotate rotary dial feeder using a speed reducer. A rotary ejector is connected with a drawing device and a gasification reaction chamber. A top part of the gasification furnace is divided into a preheating drying chamber, a reaction chamber and air inlet pipes. A lower end of a reduction reaction room is provided with a gas-solid separating chamber. A gasification furnace chamber is set on an outer wall of an insulating layer. A lower part of the gasification furnace is provided with a large aperture grate and a fixed fire grate. The large aperture grate is provided for covering a carbon inlet and a discharging device. A large aperture furnace is connected to a dust remover by a pipeline.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of an agriculture and forest biomass secondary process reaction gasification furnace.
NOVELTY - A quinocetone preparation method involves mixing methanol, tetrahydrofuran, acetylacetone and catalyst K, concentrating resultant mixture and condensing by adding dehydrating agent, to obtain a maquindox reaction mixture. The resultant mixture is cooled to 30 degrees C, and benzaldehyde and catalyst E are directly added and heated at increased temperature to obtain quinocetone. The resultant mixture is cooled to 20 degrees C, followed by filtering, washing by alcohol and/or water, and vacuum drying at 45-60 degrees C to obtain ketene.    USE - Method for preparing quinocetone.    ADVANTAGE - The method enables preparing quinocetone in a simple, economical and eco-friendly manner, and provides product with high quality.
NOVELTY - A method for extracting entacapone from butterfly flower involves adding 50-70 % of ethanol to dry butterfly flower petal, and collecting crude drug weight percolation liquid. 4-8 stages of counter-current extraction are performed with ethyl acetate. Ethyl acetate extraction liquid is collected. A solvent is decompressed and recycled. The obtained solvent is added to a polyamide chromatography column. The solvent is recovered using a polyamide film followed by concentrating, adding methanol crystal, separating, crystallizing, washing and drying to obtain an entacapone.    USE - Method for extracting entacapone from butterfly flower.    ADVANTAGE - The method enables extracting the entacapone with high purity in a simple manner, and realizing industrial production. The method enables reducing generation of pollution and reducing energy consumption.    DETAILED DESCRIPTION - A method for extracting entacapone from butterfly flower involves adding 50-70 % of ethanol to dry butterfly flower petal, and collecting crude drug weight percolation liquid followed by filtering for 3-8 times. 4-8 stages of counter-current extraction are performed with ethyl acetate. Ethyl acetate extraction liquid is collected. A solvent is decompressed and recycled. The obtained solvent is added to a polyamide chromatography column. The solvent is recovered by using a polyamide film followed by concentrating, adding methanol crystal, separating, crystallizing, washing and drying to obtain an entacapone.
NOVELTY - A Fibrauretin preparing method involves adding berberine hydrochloride in an organic solvent in catalysis of Lewis acid. Methylene is removed to obtain an intermediate product of 2,3,9,10-tetrahydroxy berberine hydrochloride. The intermediate product is added in a basic solvent in presence of a methylation reagent and reacted at temperature of 30-40 degrees C for obtaining an intermediate Fibrauretin alkali. The intermediate Fibrauretin alkali is heated and dissolved in distilled water. The obtained solution is added with hydrochloric acid to obtain Fibrauretin.    USE - Method for preparing Fibrauretin that is utilized in chemical synthesis broadspectrum antibiotical medicine.    ADVANTAGE - The method enables preparing the Fibrauretin using less steps, performing operation in a cost effective manner, saving plate resource, protecting ecological environment, utilizing berberine hydrochloride as cheap raw material, and achieving industrial production of the Fibrauretin.    DETAILED DESCRIPTION - A Fibrauretin preparing method involves adding berberine hydrochloride in an organic solvent having reaction temperature of 100-150 degrees C in catalysis of Lewis acid. Methylene is removed to obtain an intermediate product of 2,3,9,10-tetrahydroxy berberine hydrochloride. The intermediate product of 2,3,9,10-tetrahydroxy berberine hydrochloride is added in a basic solvent in presence of methylation reagent and reacted at temperature of 30-40 degrees C for obtaining an intermediate Fibrauretin alkali. The intermediate Fibrauretin alkali is heated and dissolved in distilled water. The obtained solution is added with hydrochloric acid to obtain the Fibrauretin.
NOVELTY - Composition comprises Aneurinibacillus thermoaerophilus KCCM 41604.    USE - The composition is useful for promoting composting of organic wastes.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) method for preparing the composition involves inoculating A.thermoaerophilus KCCM 41604 in the culture medium, mixing the culture with a carrier medium and drying to obtain the microbial fixation, and mixing feed additives to the dried mixture; and (2) method for composting organic waste involves inoculating the obtained microbial formulation in organic waste.
NOVELTY - The method involves forming an electrode catalyst by mixing microbubbles controlled in particle diameter to viscous electrode catalyst slurry, where peak diameter in particle diameter distribution of the microbubbles is within a range of 0.01 to 100 micrometers. The slurry is coated onto a diffusion layer (5) by a screen printing method, and solvent of the slurry is dried for forming an electrode catalyst layer. The electrode catalyst layer is bonded on two sides of a solid polymer electrolyte membrane (2) to form a membrane electrode assembly.    USE - Manufacturing method for a membrane electrode assembly (MEA) i.e. polymer electrolyte fuel cell.    ADVANTAGE - The electrode catalyst layer bonded on the two sides of the electrolyte membrane allows for controlling capillary structure of the electrode catalyst layer, improving the diffusion of matter to be consumed and the rejection of created water in the electrode catalyst layer, and enhancing use efficiency of catalyst metal, thus achieving high power generation.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of a fuel cell.    Separators (1)    Solid polymer electrolyte membrane (2)    Anode (3)    Cathode (4)    Diffusion layer (5)
NOVELTY - The device has a hydrogen half cell including a hydrogen electrode located between inner hydrogen half cell spacer screen and an outer hydrogen half cell spacer screen. An oxygen half cell includes an oxygen electrode located between an inner oxygen half cell spacer screen and an outer oxygen half cell spacer screen. A gas separation membrane (GSM) is located among the inner hydrogen half cell spacer screens of the hydrogen half cell and the two inner oxygen half cell spacer screens of the oxygen half cell to from an electrolyzer.    USE - Alkaline electrolyzer device for use in an extremely affordable high power density uninterruptible power supply (UPS) system for residential, commercial and industrial applications, for use with high performance phase exchange material (PEM) fuel cell stack, and for use as a primary unit for low cost/high power density energy storage for renewable energy power generation, and a refueling station for production and dispensing of very low cost hydrogen fuel for a hybrid vehicle, for storing hydrogen fuel for later use with externally-fired gas turbine generator sets on wind farms and for supplemental or backup power generation when winds are low or nonexistent.    ADVANTAGE - The device has large active area and high power density, and improves the working efficiency by 81 percent and operating pressure capability up to 200 barometric pressure at low cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a front elevational view of an assembled single cell configuration showing tie rod fasteners, single width reinforcement bars and triple width manifold/reinforcement bars.    Tie rod fasteners (15)    Single width reinforcement bars (16)    Triple width manifold/reinforcement bars (17, 18)
NOVELTY - The unutilized biomass (2) is maintained for predetermined time at high pressure. Pressure is released rapidly, and cell of biomass is destroyed. Hydrolysis of water-soluble polymer is advanced. The expansion softening biomass (4) is mixed to sewage sludge (1) containing organic substance, and is transferred to water-removal device (10) for separating dewatering cake (11) and filtrate (12).    USE - Processing apparatus of sewage sludge.    ADVANTAGE - The unutilized biomass can be processed effectively. The dewatering cake obtained from sewage sludge is recycled in short period of time. Reduction of carbon-dioxide generation amount and energy usage-amount is performed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for processing method of sewage sludge.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the processing apparatus.    Sewage sludge (1)    Utilized biomass (2)    Expansion softening biomass (4)    Water-removal device (10)    Dewatering cake (11)    Filtrate (12)
NOVELTY - An organic waste processing apparatus (1, 2) comprises fermenter (10) which produces biogas containing methane (G) and hydrogen sulfide and ferments organic waste, desulfurizing apparatus (20) which obtains sulfuric acid from hydrogen sulfide in the biogas, and decomposition tank (40) which decomposes sulfuric acid obtained with desulfurizing apparatus and returns residue of organic waste to fermenter.    USE - An organic waste processing apparatus (claimed).    ADVANTAGE - Amount of residue produced is reduced, methanation efficiency is improved, and inorganic substance and metal are recoverable.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of an organic waste processing apparatus. (Drawing includes non-English language text).    Organic waste processing apparatus (1, 2)    Fermenter (10)    Desulfurizing apparatus (20)    Decomposition tank (40)    Methane gas (G)
NOVELTY - Wastewater treatment involves performing floatation process by generating fine bubble with pressurization floating or a microbubble production apparatus after adding and mixing chemical agent to wastewater, performing aeration treatment using microorganisms, performing solid-liquid separation, precipitation or membrane separation, purifying the pollutant material during wastewater by separating and removing sludge from the liquid mixture of the treated water aeration treatment.    USE - Treatment of wastewater e.g. foodstuff industrial wastewater, agricultural wastewater, fish processing wastewater, human waste treatment wastewater, and livestock farming wastewater.    ADVANTAGE - The cost for floatation process by fine bubble can be reduced by simple method, and the generation of offensive odor can be avoided.
NOVELTY - A coagulant (4) is added to sludge (1), into sludge concentrate with a sludge concentration of 4-12%, and separated liquid. The sludge concentrate is anaerobically digested and biogas is recovered. The coagulant, and separated liquid or water is mixed with the anaerobically-digested sludge, to obtain digested sludge coagulant. The obtained product is dewatered. Thus, anaerobic treatment method is carried out.    USE - Anaerobic treatment method.    ADVANTAGE - The method is efficiently and economically carried out by reducing generation of phosphorus, siloxane and other precipitates is reduced and efficiently recovering biogas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for anaerobic-treatment apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic structure of anaerobic-treatment apparatus. (Drawing includes non-English language text)    Sludge (1)    Storage tank (2)    Flocculation tank (3)    Coagulant (4)    Sludge flocculation (5)
NOVELTY - A water-splitting dye-sensitized solar cell comprises a working electrode (520) for producing oxygen gas, and a counter-electrode (224) for producing hydrogen gas from water. The first electrode and the second electrode are positioned between a pair of outer polymer layers (130), where a spacer layer(s) (150) is between the polymer layers. The polymer layers are walls of extruded twin-wall sheets provided with ribs. The sheet comprises a nickel metal coating on its internal surface. A solar cell is between the polymer films.    USE - A water-splitting dye-sensitized solar cell.    ADVANTAGE - The water-splitting dye-sensitized solar cell has a relatively high-volume, and is inexpensive.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing the water-splitting dye-sensitized solar cell.    DESCRIPTION OF DRAWING(S) - The drawing is water-splitting dye-sensitized solar cell.    Outer polymer layers (130)    Spacer layer (150)    Titanium foil (211)    Dye layer (213)    Titanium foil (221)    Counter-electrode (224)    Working electrode (520)
NOVELTY - Increasing triacylglycerol production in a cell, comprises modifying the cell to increase phosphatidic acid production.    USE - The methods are useful for increasing triacylglycerol production in a cell; for producing a genetically modified organism; and for producing a biofuel (all claimed).    ADVANTAGE - The methods are highly improved and efficiently generate lipids suitable for biofuel production, and produce plants and microorganisms with characteristics that improve the yield and/or quality of lipids suitable for biofuel production.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a method for producing a genetically modified organism, comprising making at least one genetic modification to a cell of the organism that increases phosphatidic acid production in the cell, where triacylglycerol production in the cell is elevated compared to a corresponding wild-type cell, and the organism is a microorganism or plant;    (2) a method for producing a biofuel, comprising: cultivating the genetically modified organism, isolating triacylglycerols produced by the organism; and transesterifying the triacylglycerols to produce the biofuel; and    (3) use of the genetically modified organism in a process for producing a biofuel.
NOVELTY - Manufacturing of porous carbon material, comprises treating metal carbide with halogen at at least two halogenation temperatures in stepwise manner so that produced material comprise by weight, less than 100 ppm of individual metal, less than 7000 ppm of chlorine and greater than 99% of carbon, is claimed. The first step can be any temperature between 10-800 degrees C, where second and subsequent steps can be any temperature which is at least 50 degrees C higher than at previous step and time of halogenation can be 1-10 hours and second and subsequent halogenation can be between 1 minute to 3 hours.    USE - The method is useful for manufacturing of porous carbon material which can be used as: electrode material in supercapacitor, battery, fuel cells, desalination and as adsorbent in gas sampling, breath analyzer, gas diffusion layer in fuel cell, hydrogen storage, methane storage, chlorine storage, and other gas storage; and sorbent for gas, liquid filtration and/or separation, sorbent for gas storage, sorbent for analytical techniques e.g. gas chromatography and liquid chromatography, sorbent for use in medical applications e.g. hemodiafiltration, enterosorbent, and toxin removal from biological fluids or sorbent for use in electrical energy storage applications e.g. supercapacitor, battery and fuel cell (all claimed).    ADVANTAGE - The method exhibits high purity without sacrificing tunabilty of porosity (pore size, pore volume and surface area).
NOVELTY - The system (900) has conduit with an inlet (901) that receives a premixed, ammonia-rich gaseous mixture containing ammonia and oxygen. The combustion apparatus comprises a heating element that is arranged within the conduit, for heating the mixture to a temperature higher than 1100 degrees C. The heated mixture undergoes a gaseous-phase avalanche of reactions involving water formation and ammonia decomposition. An outlet expels a mixture of gaseous products including non-combusted hydrogen gas from the conduit that results from the reactions.    USE - Ammonia flame cracker system for decomposing ammonia into hydrogen-containing product mixture.    ADVANTAGE - Ammonia flame cracker system is made compact and the system is capable of decomposing ammonia at a high decomposition yield. High overall thermal conversion efficiency and high throughput rate can be achieved, using very little or no catalyst.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) apparatus for cracking ammonia and combusting a fuel in separate loops; and    (2) method of cracking ammonia.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the ammonia flame cracker system.    Ammonia flame cracker system (900)    Inlet (901)    Round tubings (902,903,905,906)    Exit (907)    Igniter (909)
NOVELTY - A diesel fuel composition (C1) derived from oil selected from vegetable oil and/or animal oil comprises: mixture of 14-18C paraffins having a ratio of iso to normal paraffins of 2-8; and sulfur (less than 5 part per million (ppm)).    USE - In blended fuel composition (claimed); and for on road, off road stationary engines and combustion turbines, and for boilers.    ADVANTAGE - The diesel fuel composition has a lubricity of less than 400 mu m or less than 300 mu m or less than 200 mu m according to ISO 12156/1; has a cetane index of greater than 60 as measured according to ASTM D4737; and exhibits on average at least 25% less nitrogen oxide (NOx) emissions than commercial crude diesel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is/are included for a blended fuel composition comprising the diesel fuel composition (C1); and fuel selected from fuel produced from crude oil, synthetic fuel and/or biodiesel.
NOVELTY - Producing isophorone by catalyzed aldol condensation of acetone reactant, comprises processing the reaction product, hydrolyzing the valuable stream and separating into an organic and an aqueous fraction, obtaining isophorone from the organic fraction, distillative processing of the aqueous fraction, and transferring the vapors from the top of the apparatus of the distillative processing in the hydrolysis apparatus.    USE - The isophorone is useful as a high-boiling solvent in coating-, printing ink-, adhesive- and plant protection agent-industry.    ADVANTAGE - The method is produced in a cost efficient manner with selectivity and without causing environmental pollution and forming undesirable condensation products.
NOVELTY - Preparing organic fertilizer, involves (a) preparing fodder by mixing agent which promotes the feeding habits of larvae with the excrement, (b) accommodating the fodder in a processing container, inoculating several eggs of Musca domestica into the fodder accommodated in the processing container, and breeding the larva, and (c) subjecting the fodder to enzymatic decomposition process.    USE - The method is useful for preparing organic fertilizer.    ADVANTAGE - The method is rapid, and enables to convert large quantities of livestock excrement into organic fertilizer.    DETAILED DESCRIPTION - Method for preparing organic fertilizer using excretion of livestock and the larva of Musca domestica, involves (a) preparing fodder by mixing agent which promotes the feeding habits of larvae with the excrement, (b) accommodating the fodder of predetermined amount in a processing container of predetermined volume, inoculating several eggs of M.domestica into the fodder accommodated in the processing container, where the larva hatched from the egg is made to eat the fodder, and breeding the larva, and (c) subjecting the fodder to enzymatic decomposition process, where the enzyme is excreted from the larva and obtaining fertilizer base material.
NOVELTY - Process (M1) of producing one or more alcohols from a gaseous substrate, involves fermenting a gaseous substrate comprising carbon monoxide (CO) in an aqueous medium in a bioreactor, and increasing cell density by adjusting specific CO uptake in the aqueous medium.    USE - The process is useful for producing one or more alcohols from a gaseous substrate. The alcohols include butanol and ethanol. The alcohols are used in biofuel.    ADVANTAGE - The method is rapid.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for gaseous substrate fermentation method (M2), which involves adding gaseous substrate comprising carbon monoxide into an aqueous medium in a bioreactor, selecting target specific CO uptake (0.01-10 mmol/minute/g of dry cell), adjusting flow of gaseous substrate such that specific CO uptake equals the target specific CO uptake (0.01-10 mmol/minute/g of dry cell), adjusting flow of gaseous substrate such that specific CO uptake equals the target specific CO uptake, and repeating the steps until attaining desired cell density (0.1-15 g/l), and upon attaining the desired cell density converting to continuous mode of operation.
NOVELTY - Biogas pressure stabilizing device comprises a material fermentation device, a stored gas pressure stabilizing device, a fermenting tank (7), a gas-guide tube (8), a sealed tube (9), a distributing wall (10), a feeding pipe (12), a discharging pipe (13), a discharging hole (14), a flow-guide pipe (15), a recirculatory pipe (16), a manure storing room (17), a hydraulic pressure room (18), and a feeding pipe (12).    USE - Biogas pressure stabilizing device.    ADVANTAGE - The device guarantees the pressure in gas holder to prevent the biogas from refluxing into fermenting tank. The biogas pressure on supply peasant households still keep unchanged.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing process of preparing gas holder.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of biogas pressure stabilizing device.    Fermenting tank (7)    Gas-guide tube (8)    Sealed tube (9)    Distributing wall (10)    Feeding pipe (12)    Discharging pipe (13)    Discharging hole (14)    Flow-guide pipe (15)    Recirculatory pipe (16)    Manure storing room (17)    Hydraulic pressure room (18)
NOVELTY - The method involves preparing a stack reference unit (40) that is expanded and contracted in a stacking direction. Multiple cells are loaded on the stack reference unit. The stack reference unit is compressed in the stacking direction (YR) such that the stack reference unit and the cell stack are accommodated inside the case main portion (11) of a fuel cell. An end wall element (16) is attached to wall portion (14) so as to maintain the load applied to the cell stack in the stacking direction.    USE - Manufacturing method of fuel cell such as phosphoric acid fuel cell, molten carbonate fuel cell and solid oxide fuel cell.    ADVANTAGE - The cover element is attached to the wall element by removing the stack reference unit, so that the fuel cells are manufactured easily. Since the stack reference unit and the cell stack are accommodated inside the case main portion, the size of the fuel cell is reduced effectively.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacturing apparatus of fuel cell; and    (2) fuel cell.    DESCRIPTION OF DRAWING(S) - The drawings show the sectional view illustrating the manufacturing process of fuel.    Case main portion (11)    Wall portion (14)    End wall element (16)    Stack reference unit (40)    Stacking direction (YR)
NOVELTY - Pigsty padding material formulation comprises (in wt.%) peanut shell (25), corn core (15), plant ash (20), saw dust (28) and plant straw (12). The formulation is uniformly stirred and sprayed in the pigsty twice, once in the morning and once in the night per day.    USE - The pigsty padding material formulation is used as organic fertilizer for crops and as food for multi-livestock.    ADVANTAGE - The pigsty padding material formulation comprises balanced amount of materials, it has strong absorbing and deodorizing effect with quick degradation effect of pig manure, it can purify pig growth environment, and it is suitable for recycling ecologically.
NOVELTY - Invention relates to agriculture and can be used in processing cattle dung. The method involves formation of at least one pile of dung. Inoculating compost is added to the compost mass in amount of 10-15 kg/t. The compost mass is then moistened, biologically heated and periodically mixed. The inoculating compost used is compost based on poultry droppings and a consortium of microbial strains Bacillus subtilis B-168, Bacillus mycoides B-691, Streptomyces sp.Ac-154, Mukor psychrophilus F-1441, Candida utilis Y-2441 in amount of 1.106-1.107 cells per millilitre per ton of poultry droppings.    USE - Chemistry.    ADVANTAGE - High effectiveness of the process, simple preparation of inoculating compost and low consumption of microorganisms. 2 ex
NOVELTY - Edible fungal solid strain culture medium and method for producing the solid strain, is claimed, where the strain solid medium uses disposable chopstick as raw material, followed by cleaning and cutting into strip-shaped materials.    USE - The solid strain culture medium is useful for producing edible fungus.    ADVANTAGE - The solid strain culture medium is capable of producing edible fungus in an economical and environmentally friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a solid strain culture medium for producing edible fungus solid strain comprising soaking the disposable chopsticks formed by dry-product strip with lime water (1%) for 5-7 hours for absorbing water, adding the soaked disposable chopsticks into the clean water to make the pH value to 7-8, putting the inner frame strips through the truss, removing water and drying for further use until the water content is 58%, where the dry strip comprises dry auxiliary material (0.1-0.2 Kg), wooden meal or corn cob (60-75%), bran (15 -25%), corn powder (5-10%), gypsum powder (1%), sugar (1%) and auxiliary material water content (60-65%), mixing the dried straight strip and placed into the glass bottle or special plastic bag, where the auxiliary material is covered on surface with thickness of 0.3-0.6 cm and sealed in the bottle, sterilizing with a pressure of 5-2 kg/cm2 for 3-4 hours and at normal pressure for 12-18 hours, inoculating the edible fungi strain (10-20%) in sterile environment, and placing the culture in a chamber at 20-28 degrees C for 25-35 days.
NOVELTY - Preparing an amino acid organic fertilizer, comprises weighing 5% of animal residual body, 20-30% of plant straw, 15-25% of castor seed cake, 5% of monosodium glutamate, 8% of vinasse, 20% of non-pollution pond sludge, 8% of turf, 3% of organic fertilizer fermenting agent, 4% of sterilization deodorant, and 2% of mixture of amino acid chelate trace element of amino-acid chelate calcium, amino-acid chelate magnesium, amino-acid chelate ferrous, amino-acid chelate copper, amino-acid chelate manganese, amino-acid chelate zinc, and amino-acid chelate molybdenum; and obtaining the product.    USE - The amino acid organic fertilizer is useful for producing the green food. No biological data given.    ADVANTAGE - The amino acid organic fertilizer increases the organic matter, physicochemical property and bioactivity of the soil.
NOVELTY - The device has a refrigeration system provided with a mixed refrigerant circulating compressor (3), a middle circulating compressor (4) and a main heat exchanger (5) i.e. multi-channel plate-fin heat exchanger. A gas-liquid balance tank (10) and the main heat exchanger are connected by a pipeline. A condenser (15) is provided with another condenser (16). An evaporator (19) is connected with an argon rectifying tower (14), the main heat exchanger, a tower (12) and a methane rectifying tower (13) via a pipeline. A cleaning system is provided with two molecular sieve absorbers (1, 2).    USE - Methane and argon gas separating recycling device.    ADVANTAGE - The device utilizes a mixed refrigerant and nitrogen double refrigeration system to separate and recycle synthetic ammonia draining gas, and obtains high purity methane and argon gas and high purity nitrogen gas and hydrogen gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for recycling synthesizing ammonia draining gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a methane and argon gas separating recycling device.    Molecular sieve absorbers (1, 2)    Mixed refrigerant circulating compressor (3)    Middle circulating compressor (4)    Main heat exchanger (5)    Gas-liquid balance tank (10)    Tower (12)    Methane rectifying tower (13)    Argon rectifying tower (14)    Condensers (15, 16)    Evaporator (19)
NOVELTY - Double base liquid fuel comprises (wt.%) water (30-45), methanol (49-64), potassium hydroxide (0.5-1), sodium hydroxide (0.5-1), ethyl acetate (1.5-2), ethanol (1.5-2), and dicyclopentadienyl iron (0.5-1).    USE - Double base liquid fuel.    ADVANTAGE - The double base liquid fuel has low cost, simple production, safe production process, environmental protection, and low carbon emission.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of double base liquid fuel comprising adding water in a container; adding potassium hydroxide, sodium hydroxide, ethyl acetate, and ethanol; stirring at 300-500 revolutions/minute (rpm) for 35-40 minutes; standing for 20-30 minutes to obtain water solution; adding methanol into the water solution; stirring at 300-500 rpm for 20-30 minutes; uniformly mixing for 15-20 minutes to obtain mixed solution; adding dicyclopentadienyl iron to the mixed solution; stirring at 300-500 rpm for 15-20 minutes; and obtaining double-base liquid fuel.
NOVELTY - Electrolyzing device comprises an electrolytic bath (10) internally provided with at least two independent electrolytic chambers (11) and a hydrogen-oxygen output hole. The electrolytic chamber is filled with electrolyte, and is provided with a group of electrolytic pole plates (30), where each electrolytic pole plate of each electrolytic chamber is arranged in serial circuit manner. The electrolytic pole plate comprises at least one anode plate (31) and at least one cathode plate (32). Each anode plate and each cathode plate are arranged in parallel circuit manner, and are arrayed crossly.    USE - The electrolyzing device is useful for producing hydrogen and oxide.    ADVANTAGE - The device provides low voltage and low current for electrolyzing; is safe nad economical; and can improve output of hydrogen and oxygen.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the electrolyzing device.    Electrolytic bath (10)    Electrolytic chambers (11)    Electrolytic pole plates (30)    Anode plate (31)    Cathode plate (32)
NOVELTY - Producing hydrogen using wind energy source comprises generating electricity via wind energy issued by electric energy into a storage battery, injecting water into a sink containing sodium chloride, where the sink comprises two metal electrolytic plates linking with the anode and cathode of the storage battery; providing direct current to storage battery to generate hydrogen and oxygen, collecting oxygen and hydrogen respectively by a gas collector, storing the pressurized hydrogen gas in a hydrogen purifier with hydrogen storage alloy, and depressurizing hydrogen from hydrogen storage alloy.    USE - The method is useful for producing hydrogen using wind energy source.    DETAILED DESCRIPTION - Producing hydrogen using wind energy source comprises generating electricity via wind energy issued by electric energy into a storage battery, injecting water into a sink containing sodium chloride, where the sink comprises two metal electrolytic plates, and the two electrolytic plates is linked with the anode and cathode of the storage battery; providing direct current to the storage battery to generate hydrogen and oxygen, collecting oxygen and hydrogen respectively by a gas collector equipped with electrolytic plates, preparing high purity hydrogen, storing the pressurized hydrogen gas in a hydrogen purifier with hydrogen storage alloy, and depressurizing hydrogen from hydrogen storage alloy to prepare high purity hydrogen, where large scale production of hydrogen adapts refrigeration technology of hydrogen liquefaction separation.
NOVELTY - Carbon dioxide reduction device of dielectric barrier discharge plasma combined biomass comprises plasma reactor, water (H2O) absorption tank, organic gas adsorption tank, pressure swing adsorption device, and air storage tank; plasma reactor comprising inner electrode and provided with insulating medium, insulating medium and inner electrode and outer electrode; and the outer electrode connected with alternating current power supply, grounding electrode, reaction area formed between outer electrode and inner electrode, and reaction area filled with biomass.    USE - Carbon dioxide reduction device of dielectric barrier discharge plasma combined biomass.    ADVANTAGE - The reduction rate of CO2 is high. The device has low cost.    DETAILED DESCRIPTION - Carbon dioxide reduction device of dielectric barrier discharge plasma combined biomass comprises plasma reactor, water (H2O) absorption tank, organic gas adsorption tank, pressure swing adsorption device, and air storage tank; plasma reactor provided with gas inlet and gas outlet, gas outlet connected with H2O absorbing tank, organic gas adsorption tank, pressure swing adsorption device and air storage tank; plasma reactor comprising inner electrode and provided with insulating medium, insulating medium and inner electrode and outer electrode combined to form reaction area between outer electrode two sides of grid electrode; and the outer electrode connected with alternating current power supply, grounding electrode, reaction area formed between outer electrode and inner electrode, and reaction area filled with biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a plan view of the carbon dioxide reduction device of dielectric barrier discharge plasma combined biomass. (Drawing includes non-English language text)
NOVELTY - Synthesis of calcium peroxide involves adding calcium chloride (75-85 g) to reaction bottle, and adding water (45-80 ml), stirring uniformly, adding hydrogen peroxide (250-280 ml), cooling cold dripping ammonia water (50-55 ml) to stir at 0-8 degrees C, then cooling for half an hour, the temperature is maintained at 0-8 degrees C; and putting the reactant after filtering with little cold water to wash 2-3 times, then drying in the constant temperature drying box, to form dehydrate to the oven at 60 degrees C for 0.5 hours and then obtaining anhydrous calcium peroxide in an oven at 140 degrees C for 0.5 hours.    USE - For the synthesis of calcium peroxide (claimed) which is used as bactericide, antiseptic, anti-yeast agent, disinfectant and bleaching agent, and as an inorganic chemical raw material.    ADVANTAGE - The method is rational in technique, easy to obtain raw material, low in cost, and easy for realizing industrial production with free of pollution; and provides environment-friendly multifunctional inorganic chemical product. The obtained calcium peroxide is very stable; and has strong bleaching, sterilizing, and disinfecting effects.
NOVELTY - A bacterial composition (I) is prepared by mixing (pts. wt.) Trichoderma viride (5-15), Bacillus subtilis (10-15), black Rhizopus (20-30), photosynthetic bacteria (10-15), Saccharomyces cerevisiae (7-15), Bacillus licheniformis (10-15), Nitrosomonas europaea (10-20), and Nitrobacter winogradskyi (10-20).    USE - Bacterial composition (I) used for processing kitchen waste percolate (claimed).    ADVANTAGE - The bacterial composition (I) is convenient to use, and has good fermentation degradation effect and low production cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of bacterial composition (I), comprising (1) separately performing high-density cultivation on bacterial spawns of T. viride, B. subtilis, black Rhizopus, photosynthetic bacteria, S. cerevisiae, B. licheniformis, N. europaea and N. winogradskyi; (2) inoculating the bacteria in shake flask filled with 15-30 vol.% of culture medium to perform activation cultivation; (3) inoculating the cultivated bacterial spawns in fermentation tank to perform fermentation amplification cultivation; (4) separately dehydrating and drying the bacteria obtained in step (3) to obtain hypopus microbial dry powder; and (5) mixing the T. viride, B. subtilis, black Rhizopus, photosynthetic bacteria, S. cerevisiae, B. licheniformis, N. europaea and N. winogradskyi obtained in step (4) at predetermined proportion.
NOVELTY - Preparing bis trimethyl silyl acetylene involves adding acetylene second metal suspension in the toluene, where mole ratio of second metal salt and trimethyl silane is 1:2 to 1:2.2; dropping trimethyl silane; finishing dropping, heating up to 60 degrees C for 2 hours, where the metal salt is disodium acetylene and/or acetylene lithium; using water to stop the reaction, extracting, drying, decompressing and concentrating, decompressing and rectifying to obtain bis trimethyl silicon acetylene. The trimethyl silane is trimethyl chlorosilane.    USE - For preparing bis trimethyl silyl acetylene (claimed) used as medical intermediate.    ADVANTAGE - The method is of low cost; is convenient to recycle the toluene replace expensive price, thus greatly reduces the synthesis cost; greatly reduces the generation and discharge of toxic waste, and is good for environment protection.
NOVELTY - Hybrid Pennisetum americanum x Pennisetum purpureum is cultivated by plowing soil in winter, and setting target ground border and ridge width and a field ditch in March to mid-April; close planting hybrid Pennisetum with row space of 120 cm and 60 cm in middle and late of April, sowing seeds, and cutting every 2-3 nodes in stem into one section; and harvesting by mechanical reaping, and mowing stubble of 10-15 cm every 3 months, where harvesting is 3-4 times a year.    USE - Method of cultivating hybrid Pennisetum americanum x Pennisetum purpureum used in producing methane (claimed).
NOVELTY - The device has rectification transformer that converts external 380V alternating current electric supply to 150V direct current. Oxygen generated by electrolysis is allowed to enter buffering pot after removing water by gas-water separating unit. Oxygen is stored in oxygen storage pot after being compressed by oxygen membrane compressor. Hydrogen generated by electrolysis is allowed to enter buffering pot after removing water by gas-water separating unit. Hydrogen is stored in hydrogen storage pot after being compressed by hydrogen membrane compressor.    USE - Device for producing hydrogen.    ADVANTAGE - Hydrogen can be produced reliably.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for producing hydrogen.
NOVELTY - A cell including a metal stent, a fuel anode layer, a solid electrolyte layer, and cathode layer is manufactured without performing high-temperature annealing. Each layer of cell is formed at room temperature.    USE - Manufacture of cell for metal-supported solid oxide fuel cell for fuel cell generation system (claimed).
NOVELTY - Methane from a methane pond is supplied to a buffer tank after gas and water separation, compressed by a methane compressor, and supplied to a transformation absorbing system at constant speed from the bottom portion of the absorption tower of the system. Methane and carbon dioxide are absorbed, separated and purified by voltage transformation. A pressure and flow rate sensor, and a variable frequency transducer are arranged between the gas and water separator and buffer tank.    USE - Absorption, separation and purification of methane and carbon dioxide.    ADVANTAGE - The method is stable, energy-saving, and highly efficient. The utilization of energy source is improved. The method provides methane with high purity and high heat value, and carbon dioxide with high purity.
NOVELTY - Cathode plate comprises a cathode substrate with honeycomb-surface, an active layer on the upper surface of the substrate and cathode substrate and a noble metal layer on the active layer.    USE - Cathode plate for pole plate of power cell.    ADVANTAGE - The cathode is a honeycomb-plate base body, thus increasing the reaction surface area and improving electrolytic performance. Hydrogen potential is applied in consecutive pulses of 1.2 volts, thus extending the service life. The active layer is the middle layer, thus providing good bonding force between substrate and the noble metal material layer.    DESCRIPTION OF DRAWING(S) - The drawing is a cross-sectional view of the cathode plate.
NOVELTY - A Chlorella vulgaris YSW04 strain (KACC93106P) having high lipid content and wastewater tolerance, is new.    USE - The C.vulgaris YSW04 strain is useful in agent removing nitrogen and phosphorus from wastewater and to produce biodiesel (all claimed).    ADVANTAGE - The C.vulgaris YSW04 strain produces biodiesel with improved quality.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) manufacturing method of the biodiesel, involves culturing the C.vulgaris YSW04 strain in culture medium, and isolating lipid from the culture medium; (2) agent comprising the C.vulgaris YSW04 strain or its culture medium; and (3) method of culturing the C.vulgaris YSW04 strain.
NOVELTY - An organic fertilizer preparing method involves crushing horse dung into thickness of 1 to 5 mm. Auxiliary materials are added to the crushed horse dung to prepare a culture material, where the auxiliary materials are feather meal, mixture of meat and bone meal, and spray-dried blood cells. A surface of the culture material is inoculated with boettcherisca peregrina larvae. The culture material is cultured at 25-35 degrees C for 4 to 5 days. The culture material is collected, dried and prepared into the organic fertilizer.    USE - Method for preparing an organic fertilizer by treating horse dung using boettcherisca peregrina.    ADVANTAGE - The method enables preparing the organic fertilizer with high processing capacity using small occupied area, reducing energy consumption in treatment process, obtaining a bio-organic fertilizer containing biological proteins of boettcherisca peregrina maggots, improving resource utilization of the horse dung, and protecting environmental condition.
NOVELTY - Composite microbial inoculum comprises Pseudomonas (10-20%) including P.stutzeri (20-30%), and P.putida (20-30%), and Bacillus subtilis (30-50%).    USE - The composite microbial inoculum is useful degrading halogenated hydrocarbon, phenol, benzene acid, polycyclic compound, heterocyclic compound, and ester in organic pollutant (all claimed).    ADVANTAGE - The inoculum is non-toxic, has excellent stability and can be prepared simply, inexpensively and rapidly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing composite microbial inoculums, involves (in g/l) (a) culturing the above-cited strain in culture medium including beef extract (3 g), peptone (10 g), glucose (10 g), ammonium sulfate (5), dipotassium monohydrogen phosphate (2), sodium dihydrogen phosphate (2), sodium chloride (5 g), water 1000 ml at 112 degrees C for 20 minutes, (b) oscillating the product for 30 minutes, and counting viable bacteria in the product and (c) culturing the product for 32 hours at 18 degrees C, (d) adding 10 ml of inoculum into culture medium, sterilizing the product, shaking the product at 180 revolutions/minute for 32 hours at 18 degrees C, and sterilizing the obtained product.
NOVELTY - An epicatechin gallate preparing method involves taking fresh Yunnan grandifoliate tea, and adding saturated lime water with tea. The added product is placed in a microwave extracting device for microwave extraction. The obtained solution is filtered and concentrated with diluted hydrochloric acid, and pH value of the solution is adjusted. Collected ethanol is decompressed, recycled, concentrated, refrigerated and filtered. The filter residue is taken, and the ethyl acetate is added to the ethanol, separated, crystallized, washed and dried to obtain epicatechin gallate.    USE - Method for preparing epicatechin gallate.    ADVANTAGE - The method enables preparing the epicatechin gallate with simple operation, low pollution, low energy consumption, high product purity and improved productivity.    DETAILED DESCRIPTION - An epicatechin gallate preparing method involves taking fresh Yunnan grandifoliate tea, and adding saturated lime water with the tea for 8-12 times to soak for 12-24 hours. The added product is placed in a microwave extracting device for microwave extraction, where extraction power is 300-600W, and extraction times is 1-3. The extracting solution is combined for 3-8 minutes, and the obtained solution is filtered and concentrated with diluted hydrochloric acid, and PH value of the solution is adjusted to 3-4. The filtered solution is passed through macroporous absorption resin. 50-80% of ethanol is collected for 3-8 times, and the collected ethanol is decompressed, recycled, concentrated, refrigerated and filtered. The filter residue is taken, and the ethyl acetate is added to the ethanol, separated, crystallized, washed and dried to obtain epicatechin gallate.
NOVELTY - A waste recycling method involves carrying out fermentation anaerobic treatment on human and animal manures and crop residue. The obtained marsh gas is stored and provided to farmers. The aerobic treatment is carried out on marsh gas liquid performed with the fermentation anaerobic treatment. The processed marsh gas slag is transformed into an organic fertilizer for farmland. Multi-level delay filter treatment is performed on the marsh gas liquid, and the obtained water is led to field for irrigating purpose.    USE - Method for recycling waste such as human manure, animal manure and crop residue.    ADVANTAGE - The method enables converting the human and animal manures and the crop residue into marsh gas slag, marsh gas liquid, marsh gas and irrigation water, so that minimum use of the renewable resource can be realized, waste recycling rate is made high, processing degree is made high, and production and life condition of the farmer can be improved. The method enables a waste recycling system to have energy-saving property and high yield and to be a biological and environment-friendly system.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a waste recycling system.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a method for recycling waste.'(Drawing includes non-English language text)'
NOVELTY - A microorganism organic fertilizer is prepared by using kitchen garbage as main raw material and additive is added, where the additive contains agricultural waste, inorganic auxiliary material and microorganism composite bacteria. The microorganism composite bacteria comprising (in wt.%) kitchen waste (60-75), agricultural waste (10-30), inorganic auxiliary material (1-10) and microorganism composite bacteria groups (1-5).    USE - Microorganism organic fertilizer.    ADVANTAGE - The fertilizer improves quality of agricultural products and comprehensive fertility.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing microorganism organic fertilizer.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow chart of a microorganism organic fertilizer. '(Drawing includes non-English language text)'
NOVELTY - Method for preparing peptide, involves (a) pulverizing slaughter waste, (b) adding organic acid and protease to the waste to obtain hydrolysate, (c) mixing organic calcium to the hydrolysate to obtain a reactant and performing ultrafiltration, (d) and aging the isolated reactant.    USE - The method is useful for preparing peptide.    ADVANTAGE - The method is environmentally-friendly, and is cost-effective. The prepared peptide enhances calcium content of vegetable by enhancing calcium absorption in crops.
NOVELTY - A sodium carbonate and sodium sulfide byproduct biogas purification performing method involves preparing sodium hydroxide solution, and controlling biogas flow speed at 200-240 cubic meter per hour and pressure in a reaction kettle at 1.2-1.8 mega Pascal to generate calcium carbonate and sodium sulfide, where mass ratio of the calcium carbonate and sodium sulfide is 1:1.61-2.01. The sodium carbonate and sodium sulfide are filtered to obtain clear filtrate. The filtrate is decompressed, distilled and precipitated to obtain sodium carbonate and sodium sulfide mixed product.    USE - Method for performing biogas purification of byproduct of sodium carbonate and sodium sulfide.    ADVANTAGE - The method enables performing biogas purification of byproduct of sodium carbonate and sodium sulfide with simple operation and convenient popularization and application. The method enables effectively absorbing the carbon dioxide in methane and hydrogen sulfide impurity so as to improve the purity and quality of gas.
NOVELTY - A forsythin separation and preparation method involves using high-speed counter current chromatographic technique to forming immobile phase, mobile phase and solvent system. The solvent system is composed of four components. The solvent system is mixed and stood. The resultant product is filled in stationary phase of chromatography separation in a main motor. The mobile phase pump is provided in the pillar or immobile phase in a main motor. A sample is obtained from sampling valve by UV detecting absorption peak receiving component to obtain forsythin.    USE - Method for preparing and separating forsythin.    ADVANTAGE - The method enables preparing forsythin with high purity and high recycling rate and in simple and eco-friendly manner.    DETAILED DESCRIPTION - A forsythin separation and preparation method involves using high-speed counter current chromatographic technique to forming immobile phase, mobile phase and solvent system. The solvent system is composed of four components that component-A, component-B, component-C and component-D, where component-A is normal alkane, cycloalkane or halogenated hydrocarbon and component-B is halogenated hydrocarbon. The component-C is fatty alcohol, and component-D is water. The solvent system is mixed and stood. The resultant product is filled in stationary phase of high speed counter-current chromatography separation in a main motor. The mobile phase pump provided in the pillar or immobile phase in a main motor. A sample is obtained from sampling valve by ultraviolet detecting absorption peak receiving component to obtain the forsythin.
NOVELTY - The method involves performing pre-treating process includes pre-treating, composting, and solid material separating operations. The gas is provided for disassembling organic compound with methane bacteria to methane gas and carbon dioxide, so as to transfer to methane gas-storage tank. The solar energy is collected for fermenting anaerobic waste water. The acid mineral reacting process, neutralizing process, and coagulating-precipitating process are implemented. The coagulation-precipitation-dehydration process is performed, so that the biological wastewater is treated.    USE - Method for treating organic waste such as food waste, wastewater disposal sludge, livestock excretion ejected in slaughter industrial waste, food processing factory waste, marine product waste, and human excrement (all claimed).    ADVANTAGE - The methane gas and compost can be generated as byproducts. The highly efficient anaerobic digesting operation can be implemented, thus the organic waste can be treated effectively by using solar energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for sludge processing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram illustrating the treatment of organic waste. (Drawing includes non-English language text)
NOVELTY - A high-proportional methanol petrol additive is formed by mixing (in vol. %) corrosion inhibitor (10-15), stabilizer (25-30), viscosity modifier (30-35) and pH modifier (28-30).    USE - High-proportional methanol petrol additive.    ADVANTAGE - The additive has high stability, reduced volatilization effect, large viscosity and corrosion resistance.    DESCRIPTION OF DRAWING(S) - The drawing shows a photographic view of a high-proportional methanol petrol additive.
NOVELTY - A container containing waste oil is heated at 100-220 degrees C. Waste plastic is introduced into the heated container and is molten. Sewage sludge which is primarily dehydrated, is added into the molten material. The molten material is introduced into a mold and is cooled, to obtain solid fuel.    USE - Manufacture of solid fuel.    ADVANTAGE - The method efficiently and economically provides solid fuel by recycling waste such as waste plastic, sewage sludge, or waste wood.
NOVELTY - The coal briquette is made of dried product or carbonized product of organic wastes e.g. food waste or organic by-product generated in food factory. The through holes are formed in the coal briquette. The combustion air is supplied to inside of molded product through the through holes. An additive provided in the briquette is selected from disposable edible oil, abandoned mine oil treatment reagent, resin or tar.    USE - Coal briquette.    ADVANTAGE - The environmental pollution is reduced and recycling efficiency of organic wastes can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing device of coal briquette.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the manufacturing device of coal briquette. (Drawing includes non-English language text)
NOVELTY - The cell has an anode (10) for oxidizing a compound i.e. hydrogen, into hydrogen ions. An electrolyte (20) is in contact with the anode for conducting the hydrogen ions. A cathode (50) reduces another compound i.e. oxygen, into oxide ions. Another electrolyte (40) is in contact with the cathode for conducting the oxide ions. A porous central membrane (30) has two opposite faces that are in contact with the former electrolyte and the latter electrolyte, respectively. The electrolytes and the membrane are formed from same material such as ceramic e.g. barium cerate, which conducts both ions.    USE - Fuel cell for producing electrical and heat energy in stationary application and onboard application i.e. automobile application.    ADVANTAGE - The electrolytes and the porous central membrane are made from same material that conducts the hydrogen and oxygen ions, so that an assembly of the electrolytes and the porous membrane is obtained by a single sintering operation, thus simplifying the manufacturing process of the fuel cell, and improving mechanical resistance and durability of the assembly so as to improve the functioning efficiency and the life duration of the fuel cell.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for manufacturing a fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of a fuel cell.    Anode (10)    Electrolytes (20, 40)    Porous central membrane (30)    Cathode (50)    Conductor (90)
NOVELTY - Cellulose-containing biomass is hydrolyzed to produce aqueous sugar solution. Solution is filtered by microfiltration membrane and/or ultrafiltration membrane, and aqueous sugar solution is recovered from permeation side. Solution is filtered by nano membrane filter and/or reverse osmosis membrane, and permeated water is collected from permeation side and concentrated solution is collected from non-permeated side. Portion(s) of permeated water of nano membrane filter and/or reverse osmosis membrane is used as wash water. Thus, aqueous concentrated sugar solution is manufactured.    USE - Manufacture of concentrated aqueous sugar solution.    ADVANTAGE - The concentrated aqueous sugar solution is produced without affecting the environment and using reduced amount of water.    DESCRIPTION OF DRAWING(S) - The drawing shows the flowchart explaining manufacture of concentrated aqueous sugar solution.    Acid treatment tank (1)    Biomass storage tank (2)    Enzyme aqueous solution storage tank (3)    Chemical agent tank (12)    Recycled water tank (18)
NOVELTY - Method for degrading biomass material, involves (a) pretreating biomass material to obtain a solid fraction and a liquid fraction, where at least about 50% of the biomass material in the liquid fraction is hemicellulosic material, (b) separating the liquid fraction from the solid fraction, and (c) saccharifying the liquid fraction with an enzyme composition comprising one or more cellulases and beta - xylosidase.    USE - The method is useful for degrading biomass material.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing a fermentation product, which involves (a) saccharifying biomass material with an enzyme composition, where at least 50% of the biomass material is hemicellulosic material, and the enzyme composition comprises one or more cellulases and beta -xylosidase, (b) fermenting the saccharified biomass material, and (c) recovering the fermentation product from (b).
NOVELTY - The method producing the motor power compensating current, battery system-on-chip (SOC) compensating current, auxiliary machinery consumable current and torque variation compensating current. The fuel cell current command value is produced such that the fuel cell voltage control is performed so as to follow fuel cell current command value using fuel cell controlling current.    USE - Method for allocating power for fuel cell hybrid vehicle.    ADVANTAGE - The accuracy of the fuel cell controlling current can be improved. Efficient power distribution of fuel cell hybrid vehicle can be performed by preventing the battery force-fill.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph showing compensating current conversion ratio. (Drawing includes non-English language text)
NOVELTY - The method involves dividing hydrogen production cell into oxygen gas side and hydrogen gas side by using membrane electrode assembly as diaphragm. Hydrogen gas/oxygen gas is generated in cathode/anode sides respectively by electrolyzing pure water with electric power supplied to production cell. Hydrogen production system (1) supplies hydrogen gas to demand side by predefined high pressure. Supply of electric power to production cell is stopped when pressure of oxygen gas side is normal pressure. Gas of hydrogen gas side is exhausted when stop time reaches predefined value.    USE - Method for manufacturing hydrogen for fuel cell electric vehicle.    ADVANTAGE - Waste of electric energy can be reduced by reducing pressure in oxygen gas side to normal. The size of the system can be reduced and thus the cost of the system can be reduced. Risk of cell damage can be prevented.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for hydrogen production system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen production system. (Drawing includes non-English language text)    Hydrogen production system (1)    Hydrogen production cell stack (10)    Pump (31)    Solenoid valve (50)    Safety valve (52)
NOVELTY - A biofilter comprises a container having an organic waste product in that; a layer of particulate material consisting of rubber in the container which is positioned above or below the organic waste product so that gases emanating from the organic waste product will pass through the layer of particulate material so that a microbial ecosystem will be created within the layer of particulate material which will feed on and break down the odorous pollutant in the gases passing therethrough to remove at least some of the odorous pollutant from the gases before the gases pass from the container.    USE - For removing odorous pollutants (preferably hydrogen sulfide, ammonia, aldehyde, ketone, amine, aliphatic hydrocarbon and aromatic hydrocarbon) from liquid or solid organic waste product (all claimed).    ADVANTAGE - The biofilter is simple and inexpensive to implement; and exhibits a high level of effectiveness over a perpetual lifetime, with minimal maintenance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for removing (M1) an odorous pollutant from gases emanating from an organic waste product involving providing a container having side walls, a perforated bottom wall and an open upper end which is in communication with the atmosphere; placing a layer of particulate material in the container with the layer of particulate material consisting of rubber; passing the gases upwardly through the perforated bottom wall of the container and through the layer of particulate material so that a microbial ecosystem will be created within the layer of particulate material which will feed on and break down the odorous pollutant in the gases passing therethrough to remove at least some of the odorous pollutant from the gases before the gases pass through the open upper end of the container.
NOVELTY - Process-I of removing fluoroalkanes from a fluoroalkane-containing hydrocarbon stream comprised of 3-10C hydrocarbons and 0.01-3 wt.% of 3-5C fluoroalkanes, comprises contacting the fluoroalkane-containing hydrocarbon stream with an adsorbent having strong acid functionality at a temperature of -40 degrees C to 60 degrees C.    USE - The process is useful for removing fluoroalkanes from a fluoroalkane-containing hydrocarbon stream, where the fluoroalkanes are 1-fluoropropane, 2-fluoropropane, 2-fluoro-2-methylpropane, 1-fluorobutane, 2-fluorobutane, 1-fluoro-2-methylbutane, 1-fluoropentane, 2-fluoropentane, 2,2-difluorobutane, 3-fluoropentane, 1,2-difluoropentane, and/or 1-fluoro-3-methylbutane (claimed).    ADVANTAGE - The process is capable of efficiently removing fluoroalkanes from a fluoroalkane-containing hydrocarbon stream in a cost-effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a system for removing fluoroalkanes from a fluoroalkane-containing hydrocarbon stream comprising: (aa) a fluoroalkane-containing hydrocarbon stream comprised of 2-10C hydrocarbons and 0.01-3 wt.% of 3-5C fluoroalkanes; and (bb) an adsorbent having strong acid functionality in fluid communication with the fluoroalkane-containing hydrocarbon stream.
NOVELTY - The device (1) has heating zones (H1-H4) for heating a component (2) of a membrane-electrode-arrangement, and a rotation body (4) for lamination of the heated component. The heating zones and/or cooling zones (K1-K4) for cooling of the component are integrated in a peripheral surface (U1) of the rotation body. A structure is provided in the peripheral surface for transporting and/or positioning of the component and comprises knobs. The rotation body exhibits a cylindrical form, and a counter rotation body (9) is arranged parallel to the rotation body.    USE - Device for manufacturing a membrane-electrode-arrangement for a fuel cell.    ADVANTAGE - The heating zones and/or cooling zones for cooling of the component are integrated in the peripheral surface of the rotation body, thus reducing constructional space required for manufacturing the membrane-electrode-arrangement while manufacturing the membrane-electrode-arrangement for the fuel cell in a continuous manner at reduced time and at using reduced process steps. The design of the device reduces lamination time and/or loading time required for loading the membrane-electrode-arrangement.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic side view of a device for manufacturing a membrane-electrode-arrangement for a fuel cell.    Heating zones (H1-H4)    Cooling zones (K1-K4)    Peripheral surface (U1)    Membrane-electrode-arrangement manufacturing device (1)    Component of membrane-electrode-arrangement (2)    Rotation body (4)    Counter rotation body (9)
NOVELTY - The method involves pre-processing first frame material (R1) and second frame material (R2) in rolls. An ion exchange membrane (I) is laminated between first frame material and second frame material, to form a laminate (L). The laminate is processed in rolls using third stage of the procedure.    USE - Method for manufacturing membrane electrode assembly for fuel cell.    ADVANTAGE - The continuous and/or clocked preparation of the membrane-electrode assembly in several procedural stages is performed efficiently, as the laminate is processed in rolls using third stage of procedure. The simple handling of components is performed by an integrated transport of the components as a roll. The production time and production cost of the membrane electrode assembly is reduced, by the continuous implementation of several process steps of manufacturing, while reducing long loading times of the device with the components and long lamination times.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for device for manufacturing membrane electrode assembly.    DESCRIPTION OF DRAWING(S) - The drawing shows a plan view of the device for manufacturing membrane electrode assembly.    Transport roller (3)    Feeding unit (8)    Ion exchange membrane (I)    Laminate (L)    Frame materials (R1,R2)
NOVELTY - Purification of biodiesel, comprises percolating biodiesel through a percolation system that comprises at least one percolation column comprising thermally activated bauxite and/or chemically activated bauxite.    USE - The process is useful for purifying biodiesel (claimed).    ADVANTAGE - The process is capable of producing biodiesel with a high purity degree within the required specifications and does not present the drawbacks of known processes.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is biodiesel obtained by the process.    DESCRIPTION OF DRAWING(S) - The drawing shows an illustrative flowchart of the process for biodiesel purification.    Tank (1)    Percolation system (2)    Percolation column (3)
NOVELTY - The fertilizer comprises raw materials including palygorskite (40-50 parts by weight (pbw)), chicken excrement (50-60 pbw), and fermenting agent (2.5-3.5 pbw).    USE - The fertilizer is useful for crops. No biological data given.    ADVANTAGE - The fertilizer improves quality of crops.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fertilizer.
NOVELTY - System comprises a feed creation unit that mixes rice husks and bean curd lees and increases feeding by larva with excrement to create feed, an unit for housing feed in a feed housing tray, an unit for inoculating house fly eggs in the feed housed in the housing tray, larva raising unit that feeds the feed housed in the housing tray to the larva, and an unit for separating larva and fertilizer base.    USE - The system is useful for preparing fertilizer for livestock, preferably pig and hen (claimed), for soil improvement, and promoting plant growth.    ADVANTAGE - The system changes large amount of livestock excrement into organic fertilizer rapidly. The fertilizer is environmentally-friendly, has excellent antimicrobial activity and improves quality of fruit.    DETAILED DESCRIPTION - System (10A) comprises a feed creation unit that mixes rice husks and bean curd lees and increases feeding by larva with excrement (18) to create feed (19), an unit for housing predetermined volume of feed in a feed housing tray (20), an unit for inoculating house fly eggs (51) in the feed housed in the housing tray, larva raising unit that feeds the feed housed in the housing tray to the larva having hatched from the eggs, and creates a fertilizer base for organic fertilizer by enzymatic degradation of the feed inside the larva and excretion by the larva during larva raising processing, and an unit for separating larva and fertilizer base using peristaltic dispersion behavior which is active in larva that have passed pupa metamorphosis stage.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic block diagram of system for preparing organic fertilizer.    Organic fertilizer (10A)    Excrement (18)    Feed (19)    Feed housing tray (20)    House fly eggs (51)
NOVELTY - The apparatus has a photoelectric conversion portion (2) that is provided with light receiving surface and back surface. The electrodes (4,5) are provided on the back surface of the photoelectric conversion portion. A seal portion (9) is provided on a peripheral portion of the electrodes. The electrolyte solution is electrolyzed using the electromotive force produced from conversion portion. The seal portion is provided with corrosion resistant property so as the flow of electrolyte solution between the electrodes and photoelectric conversion portion is prevented.    USE - Gas manufacturing apparatus.    ADVANTAGE - Since the light enters the light receiving surface of photoelectric conversion portion without the electrolyte solution, the absorption and scattering of incident light by the electrolyte solution is prevented. Since the quantity of the incident light is increased, the optical efficiency is improved. The manufacturing cost of the gas manufacturing apparatus is reduced. The durability and reliability of the gas manufacturing apparatus can be improved. The contact of electrolyte solution with the conversion portion is prevented.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for gas manufacturing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of gas manufacturing apparatus.    Translucent substrate (1)    Photoelectric conversion portion (2)    Electrodes (4,5)    Seal portion (9)    Top plate (14)
NOVELTY - A metal phosphine complex (I) is new.    USE - New metal phosphine complex is used for hydrogen-producing catalyst and hydrogenation reaction catalyst for producing hydrogen used for fuel cell (all claimed).    ADVANTAGE - The catalyst containing metal phosphine complex is manufactured efficiently and economically with excellent catalytic activity.    DETAILED DESCRIPTION - A metal phosphine complex of formula: MHm(CO)Ln (I), new.    M=iridium, iron, rhodium or ruthenium;    m,n=2 or 3;    nL=trisubstituted phosphine of formula: PR1R2R3;and    R1-R3=5-10C alicyclic hydrocarbyl or 6-15C aryl (both optionally substituted).    (i) R1-R3 does not include phenyl or cyclohexyl optionally substituted by linear hydrocarbyl, sulfo or halo; (ii) When M is iridium or rhodium atom, m is 3 and n is 2; and (iii) When M is iron or ruthenium atom, m is 2 and n is 3. INDEPENDENT CLAIMS are included for the following:    (1) hydrogen-producing catalyst, which contains metal phosphine complex;    (2) manufacture of hydrogen, which involves decomposing formic-acid aqueous solution using hydrogen-producing catalyst;    (3) hydrogenation reaction catalyst, which contains metal phosphine complex;    (4) hydrogenation method, which involves reacting unsaturated compound, formic-acid aqueous solution and hydrogen in presence of hydrogenation reaction catalyst; and    (5) fuel cell.
NOVELTY - A non-woven fabric wadding body dynamic film bioreactor comprises a reaction zone (1), flocculation growing region (2) and non-woven fabric film (3) where the inner non-woven cloth film assembly is provided with a non-woven distributor and sewage in the colloid matter generated by condensation flocculation forms the dynamic membrane on the surface and inside the non-woven membrane.    USE - Non-woven fabric wadding body dynamic film bioreactor for sewage treatment (claimed).    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram of the bioreactor.    Reaction zone (1)    Flocculation growing region (2)    Non-woven fabric film (3)    Reactor gas pump (5)    Water inlet pump (7)
NOVELTY - A method comprises culturing the nitrobacteria in the filtering system and nitration sludge in the water system, controlling the temperature and pH value of the water and wastewater system, monitoring chemical oxygen demand and nitrification inhibitory concentration of pollutant and extracting the culture of nitrobacteria from the filtering system of the nitrating treatment of the industrial wastewater if the temperature, pH value, chemical oxygen demand and nitrification inhibitory concentration of pollutant is beyond threshold.    USE - Method for improving industrial wastewater nitrifying process (claimed).    ADVANTAGE - The nitration process is done in real time, thus continuously cultivating new nitrobacteria.    DESCRIPTION OF DRAWING(S) - The drawing is a flowchart of the method for improving industrial wastewater nitrifying process (Drawing includes non-English language text).
NOVELTY - Preparing N-heterocycle (I) comprises cyclizing a compound comprising at least two nitrile functions by contacting the compound with a siloxane or silane hydride and an oxide or a metal amide.    USE - (I) is useful for the synthesis of pharmaceutical active agents.    ADVANTAGE - The process is simple, and suitable for industrial scale production. The process can be carried out with fewer steps. The reagents used in the process are non toxic. The process avoids byproducts.
NOVELTY - Zirconium oxychloride octahydrate and yttrium chloride hexahydrate are dissolved in water. Urea is added and the mixture is heated, aged, filtered and washed with pure water. The filtered material is pulped with pure water and heated. The heating is stopped and the reaction mixture is cooled to room temperature. The cooled product is ground, crushed using a superfine crusher and centrifuged to separate the ions. The separated ions are ground and spray dried to obtain yttria stabilized zirconia powder as solid oxide fuel cell electrolyte material.    USE - Hydrothermal synthesis of solid oxide fuel cell electrolyte material.    ADVANTAGE - The electrolyte material of high quality is manufactured. The electrolyte material provides batteries with high performance.    DETAILED DESCRIPTION - Zirconium oxychloride octahydrate and yttrium chloride hexahydrate are dissolved in water. Urea is added and the mixture is heated to more than 70 degrees C, aged, filtered and washed with pure water. The filtered material is pulped with pure water, loaded into a magnetic stirring high pressure reaction kettle, heated up to 350-420 degrees C and heat-preserved for 3 hours. The heating is stopped and the reaction mixture is cooled to room temperature. The cooled product is ground for 1 hour. The ground product is further crushed using a superfine crusher and centrifuged to separate the ions. The separated ions are ground and spray dried to obtain yttria stabilized zirconia powder as solid oxide fuel cell electrolyte material.
NOVELTY - An artificial medium manufacturing method involves adding soil microbes in paper sludge and fermenting the paper sludge. The fermented paper sludge is dried. The dried fermentation waste is molded. Cocopeat is mixed in selected fermentation waste.    USE - Method for manufacturing artificial medium for gardening.    ADVANTAGE - The method enables manufacturing artificial medium that can be easily recycled in an environment-friendly manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a method for manufacturing an artificial medium. '(Drawing includes non-English language text)'
NOVELTY - The device has alkali powder storing tank for supplying alkali powder to conveyor belt and mixer for mixing scum and alkali powder are installed at one side of scum storing tank. A pulverizing device for transporting non-dried pellets is installed at one side of conveyor belt. A drier for drying the molded pellets are installed at one side of the mixer. A molding device is provided to mix pellets with scum and alkali powder to obtain a mixture. A ventilation pipe is provided to induce even moisture evaporation in the mixture.    USE - Device for making solidity renewable energy from food waste floated scum.    ADVANTAGE - The environmental pollution is reduced during burning process and drying efficiency of the pellet is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for making solidity renewable energy from food waste floated scum. (Drawing includes non-English language text)
NOVELTY - Method for preparing organic fertilizer using activated sludge, involves inoculating bacteria (1.5-7.5 %mass) to activated sludge, where the bacteria are e.g. Bacillus licheniformis, B.megaterium, B.natto, B.subtilis and L.delbrueckii subsp. bulgaricus and (b) adding mixed enzyme mixture (1-6 %mass) and activated sludge containing bacteria to solid-state fermentation tank, adding water (60-100%) and bran (10-30%), fermenting the mixture, drying and crushing obtained sludge to obtain organic fertilizer.    USE - The method is useful for preparing organic fertilizer using activated sludge.    ADVANTAGE - The method is environmentally-friendly and produces fertilizer as it contain activated sludge rich in starch, cellulose, fat, protein and other substances as raw material.    DETAILED DESCRIPTION - Method for preparing organic fertilizer using activated sludge, involves (a) inoculating biological bacteria (1.5-7.5 %mass) to activated sludge, where the biological bacteria are Bacillus licheniformis, B.megaterium, B.natto, B.subtilis, Lactobacillus plantarum and L.delbrueckii subsp. bulgaricus and (b) adding mixed enzyme mixture (1-6 %mass) and activated sludge containing bacteria to solid-state fermentation tank, adding water (60-100%) and bran (10-30%), fermenting the mixture, drying and crushing obtained sludge to obtain organic fertilizer.
NOVELTY - A Chrysomya megacephala utilizing method involves crushing horse manure having thickness of 1 to 5 mm. An auxiliary material is added to the horse manure to prepare a culture medium, where the auxiliary material is feather powder, meat bone powder and albumen powder. Chrysomya megacephala ovum is inoculated on a surface of the culture medium at 25 to 35 degrees C for 4 to 5 days. A culture material is collected, dried and prepared into organic fertilizer.    USE - Method for utilizing Chrysomya megacephala to process horse manure to produce organic fertilizer.    ADVANTAGE - The method enables processing horse manure with small covering filed and less treatment process energy consumption in a strong manner. The method enables obtaining biological organic fertilizer and Chrysomya megacephala biological protein, realizing resource utilization of the horse manure, changing waste into valuable product and improving environment protection.
NOVELTY - A glutaric acid recycling method involves adjusting pH value of 7-aminocephalosporanic acid (7-ACA) solution by hydrochloric acid within a range of 2.0-2.5, where concentration of the hydrochloric acid is 4-6 mole per liter. The 7-ACA solution is concentrated and discolored using condensed liquid. The 7-ACA solution is concentrated, cooled and filtered. PH of the filtered liquid is regulated using inorganic acid. The 7-ACA solution is concentrated from 8-11 percent, and temperature of the solution is adjusted. The solution is filtered and re-crystallized by organic solvent.    USE - Method for recycling glutaric acid in 7-ACA waste solution.    ADVANTAGE - The method enables recycling the glutaric acid with purity of greater than 99 percent and recovering of large amount of ammonium chloride product. The method enables recycling of the glutaric acid in a simple manner without utilizing an additional device and producing a by-product, thus avoiding secondary pollution of environment.    DETAILED DESCRIPTION - A glutaric acid recycling method involves adjusting pH value of 7-aminocephalosporanic acid (7-ACA) solution by hydrochloric acid within a range of 2.0-2.5, where concentration of the hydrochloric acid is 4-6 mole per liter. The 7-ACA solution is concentrated from 20 to-40 percent and discolored using condensed liquid that comprises 0.5-3 volume percent of active carbon. The 7-ACA solution is concentrated from 12-15 percent, cooled and filtered. PH of the filtered liquid is regulated within a range of 1.0-1.5 using inorganic acid with concentration of 4-6 mole per liter. The 7-ACA solution is concentrated from 8-11 percent, and temperature of the solution is adjusted within a range of 0-10 degrees C. The solution is filtered and re-crystallized by organic solvent.
NOVELTY - Producing ethanol from kitchen garbage involves (a) adding microbial liquid (1-5%) and mixed enzyme composition (0.1-0.6%) to garbage, (b) adding the kitchen garbage to fermentation tank and carrying out fermentation at 25-32 degrees C for 48-80 hours to obtain fermented liquid, and (c) adding the fermented liquid to distillation column to obtain alcohol, where the microbial liquid contains Bacillus licheniformis, B.megaterium, and B.natto and the mixed enzyme composition contains amylase, cellulase, lipase, protease and glucoamylase.    USE - The method is useful for producing ethanol used as fuel (claimed).    ADVANTAGE - The method enables effective utilization and recycling of waste material, hence environment pollution is reduced.    DETAILED DESCRIPTION - Method for producing ethanol from kitchen garbage involves (a) adding microbial liquid (1-5%) and mixed enzyme composition (0.1-0.6%) to the garbage, (b) adding the kitchen garbage mixed with microbial liquid and mixed enzyme composition to fermentation tank and carrying out fermentation at 25-32 degrees C for 48-80 hours to obtain fermented liquid, and (c) adding the fermented liquid to distillation column to obtain alcohol, where the microbial liquid comprises Bacillus licheniformis, B.megaterium, B.natto, B.subtilis, Lactobacillus plantarum, L.delbrueckii ssp. bulgaricus, Saccharomyces cerevisiae and Pichia pastoris and the mixed enzyme composition comprises amylase, cellulase, lipase, protease, pectinase and glucoamylase.
NOVELTY - A scavenging agent comprises (in wt.%) calcium acetate (84) and aluminum (16).    USE - Scavenging agent for straw forming fuel coking in a boiler.    ADVANTAGE - The agent has better coking preventing effect, and avoids discharging of the coking from a boiler so as to reduce consumption of fuel and to ensure safe running of the boiler. The agent avoids accident, reduces boiler maintenance cost, saves labor and material resources, and ensures continuity, stability and safety of the boiler.
NOVELTY - A catalyst comprises mordenite type molecular sieve, HZSM-5 type molecular sieve, silicoaluminophosphate-34 type molecular sieve, silicoaluminophosphate-31 type molecular sieve, silicoaluminophosphate-11 type molecular sieve, MCM-22 type molecular sieve, MCM-41 type molecular sieve and SBA-15 type molecular sieve, where mass ratio of the HZSM-5 type molecular sieve to the silicoaluminophosphate-34 type molecular sieve is 0.2-5.    USE - Catalyst i.e. composite molecular sieve catalyst (claimed), for preparing propylene and propane.    ADVANTAGE - The catalyst enables improving total yield of the propylene and the propane, and avoiding hot spot of a catalyst bed layer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a catalyst filling method for producing propylene and propane.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a catalyst.'(Drawing includes non-English language text)'
NOVELTY - The process comprises electrically and mechanically connecting a lithium ion battery to a power plant fixed with respect to an environment, recharging the battery using the power plant, electrically and mechanically disconnecting the battery and power plant to make the battery electrically and mechanically independent, and supplying an electrical power to a system for producing hydrogen and injecting the hydrogen in the combustion chamber to reduce the consumption of the hydrocarbon fuel of the vehicle.    USE - The process is useful for supplying electrical energy to a lithium ion battery, which is useful for a system to produce hydrogen by electrolysis and to inject hydrogen as an additive in a combustion chamber of hydrocarbon fuel of an internal combustion engine vehicle that is movable with respect to an environment.    ADVANTAGE - The process is capable of efficiently supplying the electrical energy to the lithium ion battery thus enhancing the storage capacity, charge and discharge characteristics and lifespan of the battery and increasing the hydrogen production efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for reducing the consumption of hydrocarbon fuel of an internal combustion engine vehicle.
NOVELTY - The system has anode (4) and cathode (8) that are provided on both surfaces of solid electrolytic membrane (10). Flow path is provided between cathode and one of the surface of solid electrolytic membrane for circulating electrolyte solution. The electrolyte solution is provided with chloride ion whose concentration is below 50mg/L or more.    USE - Water electrolysis system.    ADVANTAGE - Suppression of deterioration phenomenon of electrical process is enabled, when water is electrically processed and radical oxygenated water is generated. Production efficiency of radical oxygenated water is raised.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the water electrolysis system.    Water electrolysis apparatus (1)    Anode side flow path (2)    Anode (4)    Cathode (8)    Solid electrolytic membrane (10)
NOVELTY - Livestock excrement deodorization involves neutralizing amines and ammonia compounds by using organic acid of fruit juice in order to reduce bad odor of livestock excrement, where the compounds are generated by livestock excrement.    USE - Method for deodorizing livestock excrement (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for processing fruit skin and fruit pulp, which involves:    (A) absorbing amines and ammonia with reducing bad odor by drying remaining fruit skin and fruit pulp; and    (B) mixing the obtained product with livestock excrement.
NOVELTY - Gas-tight incorporation of at least one adjacent oxygen consumable electrode in an electrochemical half-cell, comprises sealing a bending regions and/or cracking regions of the oxygen consumable electrodes and/or overlapping areas of the adjacent oxygen consumable electrodes which are formed during the incorporation of the oxygen-consuming electrode on the frame of a gas compartment of a cell, using a paste that is based on at least silver oxide and a hydrophobic polymer component, and a perfluorinated-or partially fluorinated solvent.    USE - The electrochemical half-cell is useful in a chlor-alkali electrolysis, preferably sodium-chloride electrolysis (claimed).    ADVANTAGE - The method is simple, and achieves an easy incorporation of the oxygen consumable electrode in the electrochemical half-cell.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) electrochemical half-cell comprising oxygen consumable electrodes that are adjacent to each other, where the bending regions and/or cracking regions of the oxygen consumable electrodes and/or overlapping areas of the adjacent oxygen consumable electrodes which are formed during the incorporation of the oxygen-consuming electrode on the frame of the gas compartment of the cell, are sealed using a sealing paste that is based on at least silver oxide and the hydrophobic polymer component, and a fluorinated solvent; and    (2) electro-chemical half cell incorporated with an oxygen consumption electrodes, according to the procedure mentioned above.
NOVELTY - The device has gas extraction and measurement chambers (10, 12) and an air drying chamber (16) extending into an enclosure. A pump (26) is operated for producing pressure difference across tubes (20, 22, 24) in a controlled manner for transfer of air from the drying chamber toward the extraction chamber and transfer of gas from the extraction chamber toward a gas discharge outlet (8). The pump is operated for producing circulation of air into the drying chamber. A circuit is configured for operating the pump and measuring the quantities of gas detected by a detection unit i.e. sensor.    USE - Device for detecting gas e.g. hydrogen, acetylene, methane, ethane, carbon monoxide and ethylene, to be monitored in fluid i.e. insulating oil emanating from an apparatus i.e. transformer (all claimed).    ADVANTAGE - The device has reduced encumbrance, and can be installed on an equipment to be monitored. The device is constructed in a simple and economic manner, and possesses lifespan of 10 years. The device enables early detection of faults in electric equipment insulated with oil and utilizes principle of gas dissolved in the insulating oil for detecting abnormal concentration of target gas and preventing the electrical equipment from failure.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of detection device.'(Drawing includes non-English language text)'    Gas discharge outlet (8)    Gas extraction chamber (10)    Measurement chamber (12)    Air drying chamber (16)    Tubes (20, 22, 24)    Pump (26)
NOVELTY - The method involves preparing an electric-catalytic-hydrolysis system comprising a solution containing a hydrogen generating catalyst, a light providing device i.e. green LED light, and an electric energy source, where the catalyst contains an aluminum ion, a copper ion and a silver ion. Hydrogen production is optimized by optimizing a reaction condition by maintaining a reactor core pH value below 8.5, maintaining an oxidizer pH value below 11, and maintaining the pH value in range capable of optimizing a hydrogen production rate.    USE - Method for maintaining performance of an electric-catalytic-hydrolysis system in a field. Uses include but are not limited to a fuel technology field, a renewable energy field, a battery industry, a food production industry, a petrochemical industry, a cement industry and a car industry.    ADVANTAGE - The method enables efficient on-demand production of hydrogen and oxygen from water and heat using environmentally safe metals, and enables recycling the metal hydroxides and converting the hydroxide into hydrogen and oxygen.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a device for maintaining performance of an electric-catalytic-hydrolysis system, comprising a solution containing a hydrogen generating catalyst    (2) a method for controlling an electric-catalytic-hydrolysis system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a hydrogen generation system.    Main reactor (102)    Electrodes (102A)    Oxidizer reactor (104)    Computer-control system (106)    Heat source (108)
NOVELTY - The process for producing hydrogen gas (11) and oxygen gas (12) by hydrolysis of water (9), by fragmentation of its impurities that it carries and by observing a degree of water resistivity and conductivity without polarizing the oxygen or hydrogen gas, after cleaning impurities, is claimed. The water is obtained from sea, river or purification center.    USE - The process is useful for producing hydrogen gas and oxygen gas, which are useful as a fuel complement, for oxygen deficiency of people in airplanes or submarines and spacecraft such as space capsules, for the sanitation of health instruments or for uninterrupted surgery (claimed) and for biological or physiological activities.    ADVANTAGE - The process is capable of economically, simply and energy-efficiently producing the hydrogen gas and the oxygen gas with high purity in an environmental friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an apparatus for hydrolyzing water.    DESCRIPTION OF DRAWING(S) - The diagram shows an apparatus for hydrolyzing water.    Electrodes (4, 5, 6, 7)    Water (9)    Container (10)    Hydrogen gas (11)    Oxygen gas (12)    Second chamber. (14)
NOVELTY - Obtaining a solid fertilizing and biocombustible product from sugar-cane vinasse comprises: (a) concentrating liquid vinasse to obtain concentrated vinasse with a solids percentage of at least 50%; (b) mixing the concentrated vinasse with plant compounds; (c) granulating the mixture obtained in step (b) to obtain a granular solid product that can be used as fertilizer and as biofuel.    USE - The method is useful for obtaining solid fertilizing and biocombustible product from sugar-cane vinasse (claimed).    ADVANTAGE - The method allows optimum utilization of resources and provides high energy efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is solid fertilizing and biocombustible product from sugar-cane vinasse obtained by the method.
NOVELTY - Anaerobic-treatment method of water, involves introducing to-be-processed water into a acid generation tank, decomposing macromolecular component into organic acids in the water, flowing out the water from the acid production tank, introducing the water into a methane production tank filled with fluid non-biological carriers, subjecting the water to a methane fermentation treatment, and suppressing the chromium chemical oxygen demand concentration.    USE - Anaerobic-treatment method of water.    ADVANTAGE - The method is rapid, and prevents acid producing reaction in the methane production tank and proliferation of microorganisms due to the acid producing reaction are, hence prevents adhesion and surfacing of the carriers.    DETAILED DESCRIPTION - Anaerobic-treatment method of water, involves introducing to-be-processed water into a acid generation tank, decomposing macromolecular component into organic acids in the water, flowing out the water from the acid production tank, introducing the water into a methane production tank filled with fluid non-biological carriers, subjecting the water to a methane fermentation treatment, where a stable treatment is continuously carried out by preventing surfacing of the carriers in the methane production tank, and suppressing the chromium chemical oxygen demand concentration of the polymer component other than the organic acid in the treated water flowing into the methane production tank from the acid production tank to 300 mg/l or less.
NOVELTY - Method for recovering lipid from microalgae, involves thermally decomposing microalgae at 450-700 degrees C, obtaining thermally decomposed first microalgae biomass, thermally decomposing obtained microalgae biomass at 250-400 degrees C, pyrolyzing the obtained product at 350 degrees C, and collecting only lipid from the obtained product.    USE - The method is useful for recovering lipid from microalgae, which is used as solid fuel (claimed). The microalgae include Chlorella.    ADVANTAGE - The method is easy.
NOVELTY - Method (M1) for increasing epicuticular wax biosynthesis in plant, involves genetically transforming recombinant vector containing Arabidopsis thaliana-derived myb domain protein 96 (MYB96) gene into plant cell and over-expressing the MYB96 gene in the plant cell.    USE - The method (M1) is useful for increasing epicuticular wax biosynthesis in plant. The method (M2) is useful for preparing transgenic plant with increased epicuticular wax biosynthesis which is used for producing biofuel, preferably bioalcohol and biodiesel. The bioalcohol is bioethanol or biomethanol. The transgenic plant is dicotyledonous plant (all claimed).    ADVANTAGE - The method increases biosynthesis and accumulation of epicuticular wax which comprises high content of fatty acid, alcohol or alkane.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method (M2) for preparing transgenic plant with increased epicuticular wax biosynthesis, involves introducing the above-cited vector into plant cell and over-expressing the gene;    (2) transgenic plant with increased epicuticular wax biosynthesis prepared by the above-cited method (M2);    (3) seed of the transgenic plant;    (4) method (M3) for producing biofuel, involves isolating and separating the epicuticular wax from the transgenic plant and purifying the wax; and    (5) composition for increasing epicuticular wax biosynthesis in plant comprising the MYB96 gene.
NOVELTY - Preparing furfural using xylose, comprises: performing liquid phase dehydration reaction on an aqueous solution containing the xylose under a temperature of 190-210 degrees C and a pressure of 2.5-6 MPa without using a catalyst.    USE - The method is useful for preparing furfural (claimed), which is useful as a precursor for nylon of spandex, an adhesive, a pesticide, and synthetic polymers.    ADVANTAGE - The method improves the yield of furfural, stability of products, selectivity of furfural and minimize the generation of by-products during the reaction process. The method provides furfural in a simple and economical manner.
NOVELTY - Preparing gas cracker feedstock, comprises contacting a feed containing one or more paraffins comprising 4-12C with a catalyst comprising at least one zeolite having 10-membered ring channels and at least one group of VIb, VII b and/or VIII metal, in the presence of hydrogen at elevated temperatures and elevated pressures and converting at least 40 wt.% of the paraffins based on the total weight of paraffins in the feed to ethane and/or propane to obtain a hydrocracked gas cracker feedstock comprising ethane and/or propane.    USE - The process is useful for preparing gas cracker feedstock (hydrocracked gas cracker feedstock) comprising ethane and/or propane, which is useful for producing olefins comprise at least ethylene (all claimed).    ADVANTAGE - The process can be operated at high feed conversions, and reduces the need to provide a second or further cracking process. The process provides feedstock for a gas cracker to produce ethylene with a high conversion to ethane and/or propane.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a process for producing olefins, comprising: providing the obtained gas cracker feedstock; and cracking the gas cracker feedstock under cracking conditions to obtain olefins.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of a process for preparing gas cracker feedstock refractory paraffins. This results in a higher ethane
NOVELTY - A hydrogen generator (4) generates hydrogen from water. A water container (6) connected to hydrogen generator over water conduit (60), stores the water. A hydrogen reservoir (7) is connected with hydrogen generator over hydrogen spacer (44). A fuel cell (8) or hydrogen combustion engine is connected to power generator that is connected with hydrogen reservoir over hydrogen spacer (80) and with water container over water conduit (64). A control device (3) is electrically connected with stream generator (1), hydrogen generator and fuel cell and/or hydrogen combustion engine.    USE - Electrical power supply device.    ADVANTAGE - The power generator generates electrical power from the radiation of non-constant bright radiation source such that continuous electrical energy supply can be ensured. The control device can ensure that fuel cell is activated automatically when insufficient or no radiation energy is available. The electrical power generated by power generator and/or by fuel cell is stored in accumulator such that the electrical power in the accumulator is always buffered, in order to be retrieved immediately if necessary.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for operating power supply device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the power supply device.    Stream generator (1)    Control device (3)    Hydrogen generator (4)    Water container (6)    Hydrogen reservoir (7)    Fuel cell (8)    Hydrogen spacers (44,80)    Water conduits (60,64)
NOVELTY - An activated sludge processing system comprises a solid-liquid separation unit (2) for transferring isolated activated sludge (AC) above the water surface of water suspension (W1) and separating water suspension from an aerator (1) into activated sludge and filtered water (W2), a sludge collection unit (3) which collects transferred activated sludge, a sludge return unit (4) which returns activated sludge collected by the sludge collection unit to the aerator, and a surplus sludge extracting unit (5) which extracts activated sludge as surplus sludge (SC).    USE - An activated sludge processing system for processing organic wastewater.    ADVANTAGE - Size of installation space and operating costs can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a system flow diagram of the activated sludge processing system. (Drawing includes non-English language text).    Aerator (1)    Solid-liquid separation unit (2)    Sludge collection unit (3)    Sludge return unit (4)    Surplus sludge extracting unit (5)
NOVELTY - Preparing triclabendazole, comprises: (a) condensing N-(4,5-dichloro-2-nitrophenyl)acetamide to obtain 4-chloro-5(2,3-dichlorophenoxy)-2-nitrophenyl acetamide; (b) hydrolyzing 4-chloro-5(2,3-dichlorophenoxy)-2-nitrophenyl acetamide to obtain 4-chloro-5(2,3-dichlorophenoxy)-2-nitroaniline; (c) reducing 4-chloro-5(2,3-dichlorophenoxy)-2-nitroaniline to obtain 4-chloro-5-(2,3-dichlorophenoxy)benzene-1,2-diamine; (d) cyclizing 4-chloro-5-(2,3-dichlorophenoxy)benzene-1,2-diamine to give 6-chloro-5-(2,3-dichlorophenoxy)-1H-benzimidazole-2-thiol (I); and (e) methylating (I) using methylating agent.    USE - The process is useful for preparing triclabendazole (claimed) which is used in endemic areas of fascioliasis.    ADVANTAGE - The process is eco-friendly, technologically safe, simple and cost effective.    DETAILED DESCRIPTION - Preparing triclabendazole, comprises: (a) condensing N-(4,5-dichloro-2-nitrophenyl)acetamide with 2,3-dichlorophenol to obtain 4-chloro-5(2,3-dichlorophenoxy)-2-nitrophenyl acetamide; (b) hydrolyzing 4-chloro-5(2,3-dichlorophenoxy)-2-nitrophenyl acetamide to obtain 4-chloro-5(2,3-dichlorophenoxy)-2-nitroaniline; (c) reducing 4-chloro-5(2,3-dichlorophenoxy)-2-nitroaniline in presence of Raney nickel to obtain 4-chloro-5-(2,3-dichlorophenoxy)benzene-1,2-diamine; (d) cyclizing 4-chloro-5-(2,3-dichlorophenoxy)benzene-1,2-diamine in presence of carbon disulfide to obtain 6-chloro-5-(2,3-dichlorophenoxy)-1H-benzimidazole-2-thiol (I); and (e) methylating (I) using a methylating agent to obtain triclabendazole.
NOVELTY - Solar fuel generator, comprises: photoanodes (12) extending outward from a first side of a membrane (10), where the photoanodes includes an n-type semiconductor; and photocathodes (14) extending outward from a second side of the membrane, where the photocathodes includes a p-type semiconductor, and the p-type semiconductors are in electrical communication with the n-type semiconductors.    USE - The solar fuel generator is useful for converting the energy from the sun and water into a fuel such as hydrogen fuel.    ADVANTAGE - The solar fuel generator converts the energy from the sun and water into a fuel such as hydrogen fuel, in a simple, cost-effective, and environment friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for forming a solar fuel generator comprising generating an anode precursor that includes photoanodes extending outward from an anode layer, where the photoanodes includes an n-type semiconductor, generating a cathode precursor that includes photocathodes extending outward from a cathode layer, where the photocathodes include a p-type semiconductor, and bonding the anode layer to the cathode layer with an intermediate layer that provides electrical communication between the n-type semiconductors and the p-type semiconductors.    DESCRIPTION OF DRAWING(S) - The figure shows a perspective view of a solar fuel generator.    Membrane (10)    Supports photoanodes (12)    Photocathodes (14)    Anode semiconductor (16)    Cathode semiconductor. (18)
NOVELTY - The element (50) has a sensing electrode (2) formed in a surface of an insulated substrate (1) i.e. silicon substrate. A heating part (3) is spaced apart to the surface of the insulated substrate with the sensing electrode and formed in the sensing electrode. A sensitization part (4) covers the surface of the insulated substrate containing the sensing electrode and the heating part. A detector terminal (21) is connected to an end of the sensing electrode. A pair of heating terminals (31a, 31b) is provided in two ends of the heating part and connected to the heating part.    USE - Element for detecting leakage of to-be-detected gas. Uses include but are not limited to methane, hydrogen, carbon monoxide and ethanol.    ADVANTAGE - The sensitization part covers the surface of the insulated substrate containing the sensing electrode and the heating part, thus achieving a simple structure and cost reduction of the element without reducing detection sensitivity.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a gas detection element.    Insulated substrate (1)    Sensing electrode (2)    Heating part (3)    Sensitization part (4)    Detector terminal (21)    Heating terminals (31a, 31b)    Gas detection element (50)
NOVELTY - The reformer e.g. main steam reformer (102) and auxiliary steam reformer (120), has a reaction chamber (107) surrounding a central chamber (122), where the reaction chamber comprises an inner wall and an outer wall. The central chamber flows feed gas e.g. methane. A recuperative heat exchanger (124) is placed between the inner wall of the reaction chamber and the central chamber. A feed gas inlet is formed at bottom of the central chamber. A feed gas outlet is formed on top of the central chamber. An expansion region is placed at an outlet of the heat exchanger.    USE - Methane steam reformer e.g. main steam reformer and auxiliary steam reformer, for generating hydrogen in a fuel cell in a reformer system (all claimed).    ADVANTAGE - The reformer transfers heat from an exothermic reaction occurring in the reaction chamber to the feed gas flowing through the heat exchanger, so as to cool the reaction chamber and to decrease local hot zones, thus providing the reaction chamber with an increased even temperature distribution, and hence reducing catalyst degradation and size of the reaction chamber and improving the reformer's hydrogen generation efficiency in an effective manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a steam reforming system coupled to a fuel cell stack.    Main steam reformer (102)    Reaction chamber (107)    Auxiliary steam reformer (120)    Central chamber (122)    Recuperative heat exchanger (124)
NOVELTY - The apparatus has several sprays (10,12) to receive and store catalyst slurry. The catalyst slurry injected from the sprays is applied to a pair of metal drums (20,22). A voltage supply source (30) applies a voltage to the sprays and the metal drums. A dry heating unit is provided in the metal drums to dry the catalyst slurry applied to the surface of the metal drums.    USE - Apparatus for manufacturing fuel cell membrane-electrode assembly used in vehicles. Uses include but are not limited to passenger automobiles, sports utility vehicles, buses, trucks, various commercial vehicles, watercraft such as boats and ships, aircraft, hybrid vehicles, electric vehicles, plug-in hybrid electric vehicles, hydrogen-powered vehicles and fuel vehicles.    ADVANTAGE - The dry heating unit is provided in the metal drums to dry the catalyst slurry applied to the surface of the metal drums, so that high uniform distribution and high porosity of the catalyst layer is achieved and further the manufacturing yield of the electrodes is increased. since the membrane-electrode assembly is manufactured by drying the catalyst layer by heating the metal drums to an appropriate temperature and transferring the dried catalyst layer directly to the polymer electrolyte membrane, the bond-ability between the catalyst layer and the polymer electrolyte membrane is improved and the manufacturing process is simplified at low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for manufacturing fuel cell membrane-electrode assembly.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of apparatus for manufacturing fuel cell membrane-electrode assembly.    Sprays (10,12)    Metal drums (20,22)    Pattern (24)    Voltage supply source (30)    Catalyst layer (50)
NOVELTY - A joining method of a gas diffusion layer and an electrode membrane (10) comprising a catalyst layer, a polymer electrolyte membrane, and a sub-gasket involves: forming a groove (24) at a junction portion of the gas diffusion layer (20) with the sub-gasket; and forming a stopper (23) within the groove in order to join the gas diffusion layer with the sub-gasket without hot-pressing the gas diffusion layer and the sub-gasket together. The stopper is coated with an adhesive.    USE - For joining gas diffusion layer and electrode membrane (claimed) for manufacturing fuel cell stack.    ADVANTAGE - The method provides a way to join the gas diffusion layer with the sub-gasket without hot-pressing them together by forming grooves in a region that does not participate in a fuel cell reaction in the gas diffusion layer.    DESCRIPTION OF DRAWING(S) - The figures shows a joining process view of an electrode membrane and a gas diffusion layer.    Electrode membrane (10)    Gas diffusion layer (20)    Stopper (23)    Groove (24)
NOVELTY - The vaginal tablet comprises 0.2 g of tinidazole, 0.08-0.15 g of tartaric acid, 0.10-0.115 g of sodium bicarbonate, 0.15-0.25 g of lactose, 0.08-0.15 g of hydroxypropyl cellulose, 0.05-0.1 g of carboxymethyl starch sodium, 0.008-0.024 g of povidone K30, 0.10-0.20 g of pure water, 0.003-0.008 g of polysorbate-80, 1-3 g of talcum powder, and 0.5-2 g of superfine silica powder.    USE - The vaginal tablet is useful for treating and killing protozoan infection, anaerobic infection, nausea, anorexia, abdomen disease and gastrointestinal tract disease. No biological data given.    ADVANTAGE - The vaginal tablet is safe and non-toxic, and can be easily prepared without stickiness and adverse events in an environmentally friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing vaginal tablet.
NOVELTY - The organic humus exerting controlling fertilizer comprises chicken manure (30 wt.%), rabbit manure (15 wt.%), swine manure (10 wt.%), cow dung (12 wt.%), cake fertilizer (20 wt.%), hyaluronic acid (2 wt.%), straw (2 wt.%), powdered rock phosphate (5 wt.%), and mineral potassium fertilizer (4 wt.%). The fertilizer is bean cake, cottonseed cake, rape seed cake and sesame cake.    USE - Used as organic humus exerting controlling fertilizer. No biological data given.    ADVANTAGE - The organic humus exerting controlling fertilizer can be simply and economically prepared with high nutritional source and long service life.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method preparation of organic humus exerting controlling fertilizer.
NOVELTY - The invention relates to a process for the integrated automated composting of green and domestic wastes in order to produce natural fertilizers by processing the chopped organic residues with sizes of 0.5...1 cm and whose C/N ratio is from 20/1...40/1 whereto there are added biocomposting stimulators, pH regulating agents, 1...10 % biopreparations, 0.1...5% biodynamic preparations, afterwards the mixture is processed in three stages for a total period of 33...62 days in an automated system, at a temperature of 50...65 degrees C, 65% humidity, which finally reaches 40%, final pH between 8.5 and 5.5, to obtain a compost comprising 73...91% organic matter, 1...3% total nitrogen, 0.2...1% potassium and 0.2...0.5 % phosphorus.
NOVELTY - Biotechnological process for preparing a microbial polyssacharide by recycling glycerin, in which, during the fermentation of Pseudomonas sp. microorganism isolated from the natural environment, on a medium containing the glycerin resulting as by-product of biodiesel fuel preparation, and in optimal stirring-aerating conditions, there takes place the biosynthesis of pseudozan polysaccharide, reaching final concentrations of 19...23 g/l with a rate of production of 0.36...0.48g/l/h. After separating the biomass, the cell-free solution is partially purified and concentrated by microfiltration and ultrafiltration, to obtain the raw polysaccharide which is redissoluted, purified and concentrated, thereby obtaining a product with a concentration of over 90% pseudozan.
NOVELTY - A start-up method of a fuel cell power generation system involves producing reformed gas (12) containing hydrogen from raw fuel (24) using modifier (40), supplying reformed gas to carbon monoxide (CO)-modifying device (50) which transforms CO to carbon dioxide and has anode and cathode, detecting temperature rise of CO-modifying catalyst (52), determining necessity of reducing CO-modifying catalyst, and producing reformed gas containing hydrogen using modifier without producing electric power by fuel cell power generation stack (70) when reducing CO-modifying catalyst becomes necessary.    USE - A start-up method of a fuel cell power generation system (claimed).    ADVANTAGE - Reduction operation of CO-modifying catalyst of a fuel cell power generation system is performed easily.    DETAILED DESCRIPTION - A start-up method of a fuel cell power generation system involves producing reformed gas (12) containing hydrogen from raw fuel (24) using modifier (40), supplying reformed gas to carbon monoxide (CO)-modifying device (50) which transforms CO to carbon dioxide and has anode and cathode, detecting temperature rise of CO-modifying catalyst (52), determining necessity of reducing CO-modifying catalyst, producing reformed gas containing hydrogen using modifier without producing electric power by fuel cell power generation stack (70) when reducing CO-modifying catalyst becomes necessary, supplying reformed gas to CO-modifying device, and reducing CO-modifying catalyst. An INDEPENDENT CLAIM is included for a fuel cell power generation system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a fuel cell power generation system. (Drawing includes non-English language text).    Reformed gas (12)    Raw fuel (24)    Modifier (40)    CO-modifying device (50)    CO-modifying catalyst (52)
NOVELTY - The method comprises cutting rice straw and wheat straw into a silage cellar, where the water content of the wheat straw and the rice straw is 68-72%, and fermenting the fermentation medium for 10-15 days and then packaging. The microbes comprise photosynthetic bacteria, line bacteria, saccharomycetes, lactic acid bacteria and Aspergillus.    USE - The method is useful for manufacturing straw feed, which is useful for promoting growth of cattle and sheep and improving metabolism function. No biological data given.    ADVANTAGE - The method is capable of easily manufacturing the straw feed with high nutritional value.
NOVELTY - A hydrogen gas manufacturing apparatus has source gas manufacture device which vaporizes methanol and water to obtain source gas, reactive gas manufacture device connected to source gas manufacture device which reacts source gas and oxygen-containing gas to obtain reactive gas, hydrogen gas splitter which separates hydrogen gas contained in the reactive gas, and combustion equipment for fuel gas having a heat retaining container, which burns residual gas where hydrogen gas was separated from.    USE - Hydrogen gas manufacturing apparatus for manufacturing hydrogen gas from methanol (claimed).    ADVANTAGE - Size of apparatus is reduced, and hydrogen is efficiently manufacture.    DETAILED DESCRIPTION - A hydrogen gas manufacturing apparatus has source gas manufacture device which vaporizes methanol and water to obtain source gas, reactive gas manufacture device connected to source gas manufacture device which reacts source gas and oxygen-containing gas to obtain reactive gas, hydrogen gas splitter which separates hydrogen gas contained in the reactive gas, and combustion equipment for fuel gas having a heat retaining container, which burns residual gas where hydrogen gas was separated from. The heat retaining container is positioned so that the heat produced by burning residual gas may be transmitted. An INDEPENDENT CLAIM is included for manufacturing method of hydrogen gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic explanatory diagram of the hydrogen gas manufacturing apparatus.    Source gas manufacture device (1)    Reactive gas manufacture device (2)    Hydrogen gas splitter (3)    Heat retaining container (4)    Combustion equipment for fuel gas (9)
NOVELTY - Lignin or lignin-containing material is decomposed in presence of solid-acid catalyst in water and alcohol solvent. Thus, solubilization of lignin is enabled.    USE - Solubilization of lignin. Uses include but are not limited to manufacture of cellulose, hemicellulose, bio-chemical products, bio-plastic and chemical products.    ADVANTAGE - The method efficiently and economically enables solubilization of lignin without environmental pollution.
NOVELTY - A kitchen garbage ferment barrel comprises: a barrel body (7) and a barrel cover (2), where the barrel body is divided into an upper part and a lower part by a filter plate (6). The upper part is garbage storage and ferment chamber (3). The lower part is percolate temporary storage chamber (4). The filter plate is provided with holes. The barrel cover and the barrel body can be tightly combined to form a sealed environment. The external barrel body is provided with drain valve (5) or handle (1). The barrel cover and the barrel body can be buckled with no gap.    USE - For processing of the household kitchen garbage; for the treatment of household kitchen garbage; for reducing household kitchen garbage of urban residents and for reducing the kitchen waste to the environment.    ADVANTAGE - The kitchen garbage ferment barrel is provided with portable mounting, and conveniently use with simple operation, uses resource of kitchen wastes and fit for processing of the household kitchen garbage; obtains clean energy, reduces the discharge of pollutant of fermentation product which is used as high quality organic fertilizer feeding animal and cultivate flower.    DESCRIPTION OF DRAWING(S) - The figure shows schematic diagram of the kitchen garbage ferment barrel.    Ferment barrel Handle (1)    Ferment barrel cover (2)    Garbage storage and fermentation chamber (3)    Percolate storage chamber (4)    Drain valve (5)    Filter plate (6)    Barrel body (7)
NOVELTY - A biogas production system has methane fermentation tank which produces biogas by methane fermentation, 1st gas conduit connected to methane fermentation tank and sends out biogas emitted from methane fermentation tank, impurity absorption tank where biogas is supplied to a solution in the tank, and 2nd gas conduit connected to impurity absorption tank which sends out the biogas that passed the solution in the impurity absorption tank.    USE - A biogas production system.    ADVANTAGE - Biogas impurities such as ammonia is recovered efficiently, and high concentration biogas is manufactured.    DETAILED DESCRIPTION - A biogas production system has methane fermentation tank which produces biogas by methane fermentation, 1st gas conduit connected to methane fermentation tank and sends out biogas emitted from methane fermentation tank, impurity absorption tank where biogas is supplied to a solution in the tank, and 2nd gas conduit connected to impurity absorption tank which sends out the biogas that passed the solution in the impurity absorption tank. The 2nd gas conduit is connected to the upper space part of the culture solution surface of the methane fermentation tank, and the biogas sent from the impurity absorption tank is supplied to the space part. An INDEPENDENT CLAIM is included for method to remove ammonia in the biogas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the biogas production system. (Drawing includes non-English language text).    Methane fermentation tank (1)    Impurity absorption tank (2)    Process target object inlet tube (3)    Delivery valve (4)    Discharge line (5)    Gas circulation line (6)    Air supply pipe (7)    Delivery valve (8)
NOVELTY - Anaerobic fermentation method involves reducing size of rice straw to be 9 mm or less, mixing with paddy soil which is in a flooded state, and subjecting to anaerobic fermentation.    USE - The methods are useful for anaerobic fermentation, energy collection, and recovery of under-ground fermentation gas (all claimed).    ADVANTAGE - The method improves the fermentation efficiency of rice straw, can collect high quality biomass energy without mixing an additive to rice straw, and recovers lot of anaerobic fermentation gas. Anaerobic fermentation is started comparatively in short time, and the recovery is inexpensive.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) energy collection method, involves mixing the size-reduced rice straw with the paddy soil which is in a flooded state, subjecting to anaerobic fermentation, and collecting generated fermentation gas using an airtight container installed in the upper surface of the paddy soil; and    (2) recovery of under-ground fermentation gas, involves collecting the anaerobic fermentation gas generated from the paddy soil in a flooded state, circulating the anaerobic fermentation gas in the paddy soil with a piping system, making it blow off, retaining the anaerobic fermentation gas in paddy soil, carrying to the surface above the flood-water, and recovering the gas.
NOVELTY - The invention relates to a technology for preparing bioethanol by converting cellulosic wastes during a simultaneous saccharification and fermentation process, consisting in separating cellulose from hemicellulose by the vapour-phase self-hydrolysis pretreatment method, acid catalyzed at a pH 2, at a temperature of 180...210 degrees C and at a pressure of 50...70 bar, residence time of 10...15 minutes, followed by the enzymatic hydrolysis of the solid cellulosic fraction separated by the saccharification method followed by the fermentation process in order to obtain solubilized monosaccharides and finally to obtain the bioethanol by the fermentation of glucide fractions and hemicellulose fractions with Saccharomyces cerevisiae at a pH of 4...6 and at a temperature of 30...40 degrees C for 24...72 h.
NOVELTY - The porous macromolecule composite carrier comprises a carrier frame (1) having holes (2). The carrier frame has a porous net-like structure (3), and is spherical in shape. The porous net-like structure is interconnected between the holes. A surface of the image carrier is covered with a microbial attaching layer (4), which has affinity for microorganism. The microorganism attaching layer covered a surface of an inner hole of the carrier frame. A density of the carrier frame is 1.1-1.3 mg/litre. The carrier has a porosity of greater than 40%.    USE - The porous macromolecule composite carrier is useful for treating sewage.    ADVANTAGE - The porous macromolecule composite carrier can be economically produced with improved wear resistance, corrosion resistance and impact resistance, good quality, reduced energy consumption, long service life, high mechanical stability and excellent physical and chemical properties, reduces the sewage processing operation management cost, and improves the sewage processing efficiency.    DETAILED DESCRIPTION - The porous macromolecule composite carrier comprises a carrier frame (1) having holes (2). The carrier frame has a porous net-like structure (3), and is spherical in shape. The porous net-like structure is interconnected between the holes. A surface of the image carrier is covered with a microbial attaching layer (4), which has affinity for microorganism. The microorganism attaching layer covered a surface of an inner hole of the carrier frame. A density of the carrier frame is 1.1-1.3 mg/litre. The carrier has: a porosity of greater than 40%; a specific surface area of greater than 6000 m2/m3; a granularity of 10-20 meshes; and grain diameter of less than 3 mm.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a porous macromolecule composite carrier.    Carrier frame (1)    Holes (2)    Porous net-like structure (3)    Microbial attaching layer. (4)
NOVELTY - Anaerobic membrane bio-reactor comprises a closed circulating system comprising a high speed anaerobic bioreactor and a membrane filter tank. An inlet of the high-speed anaerobic bioreactor conveys sewage to the anaerobic bioreactor. A water outlet conveys treated sewage to the membrane filter tank. The membrane filter tank is equipped with a membrane module. The membrane module is vacuum-driven. The water leakage from the membrane is pumped by a pump or by gravity action, and remaining part of water is re-pumped into the high speed anaerobic bioreactor through a circulating pump.    USE - Used as an anaerobic membrane bio-reactor.    ADVANTAGE - The bio-reactor efficiently separates solids and liquids, ensures higher concentration of microorganisms which overcomes low volume load of anaerobic treatment, and ensures longer sludge retention time, low sludge output, high rate of methane conversion, and good water quality.    DETAILED DESCRIPTION - Anaerobic membrane bio-reactor comprises a closed circulating system comprising a high speed anaerobic bioreactor and a membrane filter tank. An inlet of the high-speed anaerobic bioreactor conveys sewage to the anaerobic bioreactor. A water outlet conveys treated sewage to the membrane filter tank. The membrane filter tank is equipped with a membrane module. The membrane module is vacuum-driven. The water leakage from the membrane is pumped by a pump or by gravity action, and remaining part of water is re-pumped into the high speed anaerobic bioreactor through a circulating pump. A compressor pump pumps a part of biogas produced by the bioreactor into the membrane module for scouring the membrane surface, and an interconnected pipeline re-circulates the biogas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the anaerobic membrane bio-reactor.
NOVELTY - For increasing methane production in anaerobic sludge or wastewater treatment processes, an inorganic nitrate solution is used as an additive to the process.    USE - For increasing methane production in anaerobic sludge or wastewater treatment processes, where the anaerobic sludge treatment system is selected from municipal sludge treatment plant, agricultural biogas plant and industrial anaerobic sludge digestion plant; and for the production of methane (claimed).    ADVANTAGE - The use of nitrate for stimulation of anaerobic digestion of organic matter such as sludge from wastewater, results in increased methane production. The addition of small amounts of inorganic nitrate to an anaerobic sludge treatment process facilitates methane production, resulting in an increase in the production of methane. The method provides an improved anaerobic digestion process resulting in high methane yield by adding inorganic nitrate to the anaerobic sludge or wastewater treatment plant. The method provides efficient process for digestion of organic material compared with the prior art processes, resulting in higher methane production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a process for the preparation of methane in an anaerobic sludge treatment process involving adding nitrate salt to an anaerobic digestion process in an amount of 1-4% of the added chemical oxygen demand (COD).
NOVELTY - The device has a photovoltaic cell (19) submerged in an electrolyte solution (5) and connected to an anode (8) and a cathode (9). A clear UV coating is provided on the cell. A membrane (17) separates a vessel (2) into two independent hydrogen and oxygen chambers (3, 4), where one of the chambers has the anode and the other chamber has the cathode. A hydrogen gas collection area is formed in the former chamber. A hydrogen gas exhaustion arrangement is coupled to the area.    USE - Device for generating hydrogen gas used in fuel cells for electrical generation for residential application or for automobile and lorry.    ADVANTAGE - The device generates the hydrogen gas by using only renewable sources of energy and provides the simple membrane structure for keeping the hydrogen gas separated from the oxygen and other contaminants. The coating protects the cell from the solution and increases electrical efficiency of the cell. The device eliminates the need for an electrolyzer, and provides pure hydrogen gas without complex gas separation equipment.    DETAILED DESCRIPTION - The coating is equivalent to ENVIBAR UV 1244 coating product. The electrolyte solution is a mixture of water and an acid or salt, or a mixture of water and a polymeric gel-type electrolyte, or a mixture of water and a solid electrolyte. The membrane is a proton-exchange membrane. An INDEPENDENT CLAIM is also included for a method for generating hydrogen gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a hydrogen generation system.    Vessel (2)    Hydrogen chamber (3)    Oxygen chamber (4)    Electrolyte solution (5)    Anode (8)    Cathode (9)    Membrane (17)    Photovoltaic cell (19)
NOVELTY - Method for preparing liquid fertilizer using living-system waste material as raw material, subjecting the living-system waste material in aggregated or granular form to fermentation-decomposition process by inoculating non-pathogenic microorganisms on its surface, washing and removing the fermented product formed on the surface of the waste material by contacting with flowing water, and collecting the water containing fermented product as liquid fertilizer.    USE - The method and apparatus are useful for preparing liquid fertilizer which is used for cultivating plants (all claimed), e.g. Brassica campestris.    ADVANTAGE - The method and apparatus prepare liquid fertilizer simply and rapidly without discharging any contaminations to environment.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) liquid fertilizer obtained by the above-cited method; and    (2) apparatus for preparing the liquid fertilizer comprising (a) processing container which accommodates fermentation mixture containing the waste material and non-pathogenic microorganisms, (b) flowing water contact unit to contact flowing water with the fermented product, and (c) liquid fertilizer discharge unit to collect and discharge the liquid fertilizer.    DESCRIPTION OF DRAWING(S) - The drawing shows perspective view of apparatus.    Housing (1)    Liquid fertilizer discharge pipe (10)    Insertion opening (11)    Air hole (12)    Operating panel (13)
NOVELTY - The free-board tar destruction unit comprises a unit for affixing to an inside of a free-board section of a gasifier or a dual bed gasifier affixed to an inside of either a gasifier vessel or a combustor vessel, a catalyst placed within a radial flow catalyst bed, a single compartment axial flow catalyst bed, flow-through horizontal catalyst compartments and bayonet vertical catalyst compartments, and a heating unit. The catalyst and the heating unit are placed within alternating bayonet vertical compartments.    USE - The free-board tar destruction unit is useful for a biomass gasifier (claimed).    ADVANTAGE - The compact free-board tar destruction unit enhances efficiency of the biomass gasifier, saves capital and operating costs by combining several functions within the gasifier vessel, reduces catalytic degradation, and can be easily affixed and removed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a biomass gasifier.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic view of a bench scale biomass gasifier.    Biomass gasifier (20)    Steam (22)    Inert sand (24)    Biomass (26)    Gases (28)    Tars. (30)
NOVELTY - The fermenter (80) has a heating system for heating an inner side floor surface of a fire-extinguishing waste water purge compartment (10) and a top part of an anaerobic digestion fermentation room (20). A dome valve (30) moves from the top part of the room and purifies fire-extinguishing waste water. A dome valve high limit jaw (34) of the valve is mounted on a topmost part of a dome valve flow guide (33). Rollers (35, 36) are arranged in a dome valve seating jaw (31). The compartment and the room are filled with seawater. A sensor unit (43) detects location of a safety valve (41).    USE - Fire-extinguishing fermenter for wet biomass.    ADVANTAGE - The fermenter enhances self-cleaning effect of the waste water, produces biogas energy, protects domestic animals from virus, facilitates fusing of fertilizer effect property of the waste water for reproduction of marine growth, utilizes intrinsic methane bacteria for producing biogas, and separates pathogen from seawater by osmotic pressure.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a fire-extinguishing fermenter.    Fire-extinguishing waste water purge compartment (10)    Anaerobic digestion fermentation room (20)    Dome valve (30)    Dome valve seating jaw (31)    Dome valve flow guide (33)    Dome valve high limit jaw (34)    Rollers (35, 36)    Safety valve (41)    Sensor unit (43)    Fire-extinguishing fermenter (80)
NOVELTY - The discharger has a reservoir provided with a storage part for storing waste that is put into an inlet port of a mixing exhausting part. Cylindrical internal space is formed in a lower part of the reservoir. An evacuated chamber is provided with a vent and a rotating disk in a stirring chamber that is equipped with a rotating blade in a stirring axis. The mixing exhausting part transfers the waste in horizontal direction. An open close detection sensor is connected with an exhaust motor. An aging chamber is arranged in the lower part of the mixing exhausting part.    USE - Storage discharger for an environment-friendly compost manufacturing equipment (claimed).    ADVANTAGE - The discharger reduces compost manutime and ensures that the waste passes through segmented space of a compost manufacturing equipment, thus producing high-quality compost from the waste and removing bad smell and contaminant of the waste.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an environment-friendly mature fermentation fertilizer manufacturing apparatus comprising a deodorizing device.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a storage discharger.
NOVELTY - Manufacture of a hydrogen purifier (100) comprises disposing an intermediate plate(s) (106) on a first end plate (104); disposing a second end plate (108) on the intermediate plate(s); pressing together the first end plate, the intermediate plate(s), and the second end plate to form a hydrogen purifier module (102); and placing clips (110) around the module. The intermediate plates includes a feed plate, and a permeate plate comprising a hydrogen-permeable membrane and a hydrogen-selective membrane.    USE - Method for the manufacture of a hydrogen purifier used in a reformation and hydrogen purification system (claimed).    ADVANTAGE - The clips are coupled to an exterior surface of the plates, allowing the plates to have a smaller overall size as compared to bolted purifiers.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a hydrogen purifier.    DESCRIPTION OF DRAWING(S) - The drawing is a sectional view of the hydrogen purifier.    Hydrogen purifier (100)    Hydrogen purifier module (102)    First end plate (104)    Intermediate plate (106)    Second end plate (108)    Clips (110)
NOVELTY - Aerating a biomass, involves: a) laying a trough lining assembly in a trough having a top, a bottom, a distal end, and a proximal end, where the trough lining assembly comprises: i) a liner and; ii) an aerator; b) depositing the biomass into the trough; and c) injecting an aerating gas into the trough at the proximal end near the bottom of the trough, such that the aerating gas is released through the aerator continuously along the length of the trough.    USE - For aerating a biomass (claimed), for treating wastewater, for stimulating growth of algae, shrimp, fish and other water-based biological products.    ADVANTAGE - The aerator provides continuous aeration of biomass present in the trough by releasing aerating gas into the biomass along the length of the trough. The continuous aeration also churns the biomass, exposing more of it to the aerating gas and to sunlight. The trough lining assembly improves the efficiency of algae production by stimulating photosynthesis and consumption of carbon dioxide. The trough lining assembly has low production, transportation, installation, and maintenance costs.
NOVELTY - An improved manganese peroxidase comprises a polypeptide having at least 80% sequence identity to the 345-388 amino acids (SEQ ID NOS: 1-7 or 8), given in the specification, and improved manganese peroxidase activity compared to a control manganese peroxidase comprising the amino acid sequence of SEQ ID NOS: 1-7 or 8, respectively.    USE - The improved manganese peroxidase, polynucleotide, vector, isolated cell or culture of cells, and method are useful for converting a cellulose-containing biomass feedstock to a sugar or a non-sugar biomass-derived intermediate (claimed).    ADVANTAGE - The improved manganese peroxidase can be efficiently used for converting a cellulose-containing biomass feedstock to ethanol using improved manganese peroxidases.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a polynucleotide comprising a nucleic acid encoding the improved manganese peroxidase;    (2) a vector comprising the polynucleotide;    (3) an isolated cell or culture of cells, where the cells comprise the polynucleotide, where the polynucleotide is heterologous to the cell; and    (4) a method for converting a cellulose-containing biomass feedstock to a sugar or a non-sugar biomass-derived intermediate, comprising treating the biomass with an improved manganese peroxidase, or with a cell that expresses the improved manganese peroxidase.
NOVELTY - Method (M1) for producing one or more fermentation end-products, involves contacting a biomass derived from a genetically modified plant or algae comprising one or more genetic modifications with Clostridium, and an external source of one or more enzymes that are capable of enhancing hydrolysis, and allowing sufficient time for Clostridium to hydrolyze and/or ferment biomass to produce fermentation end-products. At least one of genetic modifications results in altered expression and/or activity of proteins involved in cell wall degradation.    USE - The method is useful for producing one or more fermentation end-products chosen from alcohol (e.g. ethanol, methanol, butanol, propanol), organic acid, carbonyl compound, and saccharide (all claimed).    ADVANTAGE - The method is cost-effective and enables production of product at high yield.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) system for producing one or more fermentation end-products comprising a biomass derived from genetically modified plant or algae, one or more microorganisms, and a vessel; and (2) method (M2) for producing ethanol, involves providing a genetically modified biomass derived from a genetically modified plant or algae, contacting genetically modified biomass with Clostridium strain, allowing sufficient time for Clostridium or its variant to hydrolyze and/or ferment genetically modified biomass to produce ethanol.
NOVELTY - An assemble-on-site system for collecting biogas from digesting sewage comprises: a biogas deflection assembly configured and sized to fit a primary treatment unit; and a collection interface assembly operatively associated with the biogas deflection assembly and configured for connection to a biogas capture or collection system; where, when installed in the primary treatment unit, the biogas deflection assembly is substantially submerged and provides for the deflection of biogas to points of biogas collection in the collection interface assembly.    USE - The systems are useful for collecting biogas from digesting sewage; and for producing and collecting biogas (all claimed).    ADVANTAGE - The system efficiently collects methane-containing biogas from digesting sewage.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a kit comprising one or more components of the system and instructions; and    (2) a system for producing and collecting biogas comprising a primary treatment unit operatively associated with a source of sewage, the system above installed in it and a biogas capture or collection system operatively associated with the system above.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a collector interface assembly.    Primary treatment unit (500)    Biogas deflection assembly (1100)    Collector interface assembly (1200)    Hanger assemblies (1400)
NOVELTY - Method for preparing casing material, involves providing a portion of plant parenchyma tissue extracted from a plant source, mixing the portion with water to provide a starting mixture, and allowing the starting mixture to compost to form the casing material.    USE - The method is useful for preparing casing material for producing mushroom, preferably button mushroom (all claimed) e.g. Agaricus bisporus.    ADVANTAGE - The casing material is cost-effective, and improves yield of mushroom.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) casing material prepared by the above-mentioned method, comprising portion of plant parenchyma tissue extracted from a plant source; and    (2) method of producing button mushrooms, involves providing a growth substrate, seeding the substrate with mushroom spawn, allowing vegetative mushroom growth in the spawned substrate, applying a layer of casing material on top of the growth substrate, allowing the casing material to absorb water, and stimulating mushroom growth to switch from vegetative to reproductive growth, hence producing mushroom pins on top of the casing material.
NOVELTY - The apparatus has electrodes (8) for electrolysis which are arranged on back surface of photoelectric conversion section (2). When electrodes for electrolysis are in contact with electrolyte solution, the electrodes (4,5) are provided to decompose electrolyte solution by electrolysis. When photoelectric conversion section is provided to receive light, the tilt angles of electrode (8) is formed between surfaces that are in contact with electrolysis solution.    USE - Gas manufacturing apparatus for gas manufacturing apparatus array (claimed).    ADVANTAGE - The light can be entered in the light-receiving surface of photoelectric conversion section without electrolyte solution, so that the absorption of incident light and scattering of incident light by electrolyte solution can be prevented. The quantity of incident light can be improved, so that the optical efficiency can be improved. The piping for connecting the recovery opening of gas can be simplified, so that the installation cost of the piping can be reduced and misconnection of piping can be prevented.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the gas manufacturing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the gas manufacturing apparatus.    Board (1)    Photoelectric conversion section (2)    Electrodes (4,5)    Electrode for electrolysis (8)    Sealing material (16)
NOVELTY - Hydrogen and carbon dioxide are reacted in the presence of catalyst containing copper in a reactor (5), and reaction mixture containing methanol is produced. Portion(s) of reaction mixture is circulated, and a portion is burned to produce burned product and energy, when reaction mixture contains 0.1 mol% or more of compound (p) containing carbon, which is not associated with methanol and hydrogen. The methanol-containing component is separated from reaction mixture, and methanol is manufactured.    USE - Manufacture of methanol used as fuel and raw material for dimethyl ether and methyl t-butyl ether.    ADVANTAGE - The methanol is efficiently produced from carbon dioxide and hydrogen, and load on global environment is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows the flowchart of manufacture of methanol. (Drawing includes non-English language text)    Purifier (1)    Compressor (3)    Heating apparatus (4)    Reactor (5)    Cooler (6)
NOVELTY - Yeast cell comprising: an exogenous gene coding for a enzyme with the ability to convert pyruvate and coenzyme-A into formate and acetyl-CoA; a genetic modification that reduces specific nicotinamide adenine dinucleotide (NAD+)-dependent formate dehydrogenase activity in the cell; an exogenous gene coding for an enzyme with acetaldehyde dehydrogenase activity, which gene confers to the cell the ability to reduce acetyl-CoA into acetaldehyde; and a genetic modification that increases the specific activity of NAD+-linked glycerol dehydrogenase, is new.    USE - The yeast cell is useful for producing fermentation product (claimed), e.g. formic acid and ethanol which is useful as a bio fuel.    ADVANTAGE - The yeast cell is capable of producing fermentation product with high yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing a fermentation product comprising ethanol, lactic acid, 3-hydroxy-propionic acid, acrylic acid, 1,3-propane-diol, a butanol and an isoprenoid-derived product, where the process comprises fermenting a medium with a yeast cell, and the medium contains or is fed with a source of glycerol and with a source of at least one of a hexose and a pentose, and the yeast cell ferments the glycerol and the at least one of the hexose and pentose to the fermentation product and formate, and optionally, recovery of at least one of the fermentation product and formate.
NOVELTY - Removing carbon monoxide, hydrogen and methane from an anode waste gas stream from a fuel cell involves: passing the anode waste gas stream comprising carbon monoxide, hydrogen and methane through a catalyst system, where the waste gas stream first contacts a platinum/palladium catalyst and then contacts a copper/manganese catalyst.    USE - For removing carbon monoxide, hydrogen and methane from an anode waste gas stream from a fuel cell (claimed).    ADVANTAGE - The platinum/palladium catalyst effectively operates at temperatures 140-800 degrees C and is primarily utilized to oxidize the CO and H2. By using the combination of the platinum/palladium catalyst and the manganese/copper catalyst, complete conversion of the hydrogen and CO can be achieved at a lower temperature than using only the copper/manganese catalyst.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a catalyst system for removing carbon monoxide, hydrogen and methane from an anode waste gas stream from a fuel cell, comprising a first platinum/palladium catalyst and a second copper/manganese catalyst, where the anode waste stream contacts the first catalyst before contacting the second catalyst.
NOVELTY - The system has an adiabatic pre-reformer or pre-reforming reactor, and an isothermal reformer or reforming reactor. The ethanol is catalytically transformed into methane, hydrogen, carbon monoxide and carbon dioxide in the adiabatic pre-reformer or pre-reforming reactor. The methane provided in the pre-reformed gas stream obtained in the pre-reformer is catalytically converted into hydrogen in the isothermal reformer or reforming reactor. A catalytic combustor provides the thermal energy required by the reformer.    USE - Bioethanol processing system of electric energy generating system for propelling motor vehicle (all claimed).    ADVANTAGE - Since the methane provided in the pre-reformed gas stream obtained in the pre-reformer is catalytically converted into hydrogen in the isothermal reformer or reforming reactor, pollutant emission can be reduced, and gradual generation of coke deposits can be prevented, due to which the deactivation of the catalytic systems in the reformer can be avoided, hence hydrogen gas-rich reformed gas stream can be generated effectively. Since the different reactors form the ethanol processing system, the size of reforming systems can be reduced, collisions and vibrations can be eliminated, and the energy demands in remote or difficult-to-access locations can be satisfied.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for reforming ethanol.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the bioethanol processing system.
NOVELTY - Hydrothermal carbonation of biological material comprises (a) obtaining a biomass, after a fermentation process with subsequent distillation and/or rectification process, and (b) converting the obtained biomass into a carbon-rich product by hydrothermal carbonation process, where the obtained process water of the step (b) is supplied again to the step (a).    USE - The nutrient-containing process water is useful as additive for prepare mash during the fermentation process. The process is useful for hydrothermal carbonation of a biological material, bioethanol (all claimed).    ADVANTAGE - The process is free of expensive and cost-intensive drying methods.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for carrying out hydrothermal carbonation of biological material comprising at least a reactor for mash manufacture, a reactor for fermentation, a distillery with draining devices for the distillate, reactor for the hydrothermal carbonation process, a separation device with draining devices for solid, carbon-rich product, and an interconnector from the separation device to the reactor of the mash manufacture, in the which the process waters is transported.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic overview of the main steps in the hydrothermal carbonation of biological material (Drawing includes non-English language text).
NOVELTY - The apparatus (1) has a modifier (17) having a catalyst heated by a heating portion. A temperature detector (18) with a position regulation unit (19) detects the temperature of the catalyst. A biasing unit (20) provided in the outer periphery of the modifier, biases the temperature detector elastically in insertion direction. The position regulation unit is elastically biased by the biasing unit, and the temperature detector is attached to the modifier.    USE - Hydrogen generating apparatus for use in fuel cell system (claimed) for domestic application and business application.    ADVANTAGE - The temperature detector used under high temperature can be attached and removed easily from/to the modifier.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen generating apparatus. (Drawing includes non-English language text)    Hydrogen generating apparatus (1)    Modifier (17)    Temperature detector (18)    Position regulation unit (19)    Biasing unit (20)
NOVELTY - The apparatus (10) has oxygen and hydrogen discharge communicating holes (50b,50c) that distributes the generated oxygen and hydrogen in a lamination direction, while a water supply communicating hole (50a) distributes the water in the lamination direction in separators (34,36). The oxygen and hydrogen discharge communicating holes are formed in the electric power feeding portions (40,42). An insulating pipe portion (70) sealed the hydrogen discharge communicating hole, and positioned the separator which is arranged by the hydrogen discharge communicating hole.    USE - Water electrolysis apparatus for manufacturing hydrogen gas of fuel cell.    ADVANTAGE - Since the insulating pipe portion is arranged by the hydrogen discharge communicating hole, the positioning of the separator is performed easily. Hence a favorable sealing performance can be ensured.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the water electrolysis apparatus.    Water electrolysis apparatus (10)    Separators (34,36)    Electric power feeding portions (40,42)    Water supply communicating hole (50a)    Oxygen discharge communicating hole (50b)    Hydrogen discharge communicating hole (50c)    Insulating pipe portion (70)
NOVELTY - A waterweeds-shaped floating belt used for sewage treatment comprises a water grass shape floating belt, a connecting layer and a net shaped structure. The grass-floating belt is composed of polyethylene hollow fiber layer and polyurethane glue layer, where at least 2 polyethylene hollow fiber layers are bonded by polyurethane glue layer. The grass-floating belt is connected with at least an opening formed on a lower surface of the connecting layer. The net-shaped structure is provided on upper surface of the connection layer.    USE - A waterweeds-shaped floating belt used for sewage treatment.    ADVANTAGE - The belt has simple structure, and large specific surface area.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating the waterweeds-shaped floating belt.
NOVELTY - The pond has multiple sludge hoppers distributed on bottom of a pond body. An oblique pipe filler layer is paved in the pond body. A water inlet is arranged on an upper left pond wall of the pond body. A water outlet is arranged on an upper right pond wall of the pond body. A water baffling wall is arranged on an upper left part of a pond cavity. Front and back peripheries are connected with front and back pond walls. Upper periphery is jointed with the left pond wall of the pond body. Lower periphery is jointed with an upper layer side of the oblique pipe filler layer.    USE - Biochemical settling pond.    ADVANTAGE - The pond prevents sludge from pilling above the oblique pipe filler layer.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biochemical settling pond in partial section.
NOVELTY - Organic acid is manufactured by contacting lipase derived from Yarrowia lipolytica with biomass containing fats and oil and decomposing fats and oil.    USE - An organic acid manufacturing method (claimed).    ADVANTAGE - Cost of producing organic acid from fats and oil is reduced, and methane gas is efficiently manufactured from fats-and-oil biomass.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) manufacturing method of methane gas from biomass containing fats and oil which involves producing organic acid from biomass and methane-fermenting lipolysis-processed material after producing organic acid by methane producer;    (2) organic acid manufacturing apparatus comprising lipolysis tank containing Yarrowia lipolytica; and    (3) methane gas manufacturing system comprising organic acid manufacturing apparatus consists of methane fermentation tank which methane-ferments lipolysis-processed material by methane producer and biogas storage tank which stores emitted biogas.    DESCRIPTION OF DRAWING(S) - The drawing shows a process flowchart of methane gas manufacturing method. (Drawing includes non-English language text).
NOVELTY - An insulation system comprises a sludge methane pond and a sludge desiccation room, where the wall of sludge methane pond refers to hollow wall (3). The sludge methane pond is provided with a hollow wall inlet (31) and a hollow wall outlet. The hollow wall inlet is connected with a tail gas outlet of the sludge desiccation room by an insulation tube.    USE - Insulation system for biological anaerobic degradation pond of brick production sludge.    ADVANTAGE - The insulation system has low heating cost and can ensure the temperature of the degradation pond because the afterheat hot wind after drying of the produced brick is used for heating the biological anaerobic degradation pond of brick-production sludge.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of an insulation system.    Sludge marsh gas tank (1)    Brick drying system (2)    Hollow wall (3)    Sensor (5)    Hollow wall inlet (31)    Baffle plate (33)
NOVELTY - Biological synergist scene cultivation system for sewage treatment plant comprises expanding culture tank, seed tank, steam generator, pneumatic system, aerobic aeration tank, and multiple pipelines. The steam generator is connected with the jackets arranged on the expanding culture tank and the seed tank through the pipelines. Pneumatic system is respectively connected with the aeration pipes of the expanding culture tank and seed tank. The seed tank is connected with the expanding culture tank through pipeline.    USE - Biological synergist scene cultivation system for sewage treatment plant.    ADVANTAGE - The device has simple and compact structure, scientific design, and high economic efficiency.
NOVELTY - An integrated glass reinforced methane pool comprises a spherical fermenting tank (1) composed of a lower semi-tank body (2) and upper hemisphere cover (3) with feeding pipe (4) on the two sides. The feeding pipe is extended into the lower semi-tank body. The feed pipe and the upper end of the air outlet pipe (5) are connected with the cylindrical water pressure. The gas outlet pipe is connected with the upper part integrated with the spherical tank cover. The spherical fermenting tank is made of glass steel material.    USE - In the production of marsh gas.    ADVANTAGE - The integrated glass reinforced methane pool adopts glass fiber reinforced plastic and integrally shaped in such a way that sealing performance is good, and material of glass fiber reinforced plastic corrosion resistant performance is good, and the production of marsh gas is pure.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic diagram of an integrated glass reinforced methane pool.    Spherical fermenting tank (1)    Lower semi-tank body (2)    Upper hemisphere cover (3)    Feeding pipe (4)    Air outlet pipe (5)
NOVELTY - Biomass energy anaerobic fermentation tank comprises at least one assembly tank bottom and an assembly tank body with at least one layer. The assembly tank body further comprises multiple tank wall assembling plates for connecting tank wall assembling plate connectors. The tank wall assembling plate is provided with mounting parts at upper, lower, left and right sides. The assembly tank body is a circular tank comprising a tank wall assembling plates which are connected by connectors.    USE - Used as a biomass energy anaerobic fermentation tank.    ADVANTAGE - The device is simple in structure and convenient to transport, has anti-corrosive and heat preservation properties, and is suitable for small and medium-sized farm.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the biomass energy anaerobic fermentation tank.
NOVELTY - Producing a biological organic fertilizer involves (a) fermenting microbial bacteria by a fermenting device to obtain a fermentation liquor; (b) spouting and pelletizing lignin back liquor to obtain a lignin organic granular formulation; and (c) inoculating the lignin organic granular formulation by adding the lignin organic granular formulation into stirrer with material continuously and uniformly flow, adding into the fermentation liquor in a spraying manner, then air-drying or drying in the air to obtain a finished product, preferably a compound microbial fertilizer.    USE - For producing biological organic fertilizer (claimed).    ADVANTAGE - The method is cheap, safe and environmental-friendly. The obtained biological organic fertilizer has high biological activity.    DETAILED DESCRIPTION - Producing a biological organic fertilizer by using a lignin organic granular formulation, involves (a) fermenting microbial bacteria for the field of the fertilizer by a fermenting device to obtain a liquid microbial inoculum, namely a fermentation liquor, where the total effective viable count in the fermentation liquor is 2.6-6 billions/g; (b) spouting and pelletizing lignin back liquor to obtain a lignin organic granular formulation; and (c) inoculating the lignin organic granular formulation by adding the lignin organic granular formulation into a stirrer with a material continuously and uniformly flow, adding into the fermentation liquor obtained in step (a) in a spraying manner, then air-drying or drying in the air to obtain a finished product, namely a compound microbial fertilizer, where the added amount of the fermentation liquor is 0.5-1.5% of the total weight of the finished product biological organic fertilizer. The microbial bacteria is selected from at least one of Bacillus subtilis, Bacillus megaterium and Bacillus mucilagimosus krassilm.
NOVELTY - A preparation method for base fertilizer of mature tree of Hongfeng apricot, involves preparing raw materials of plant straw (15%), cotton seed cake (5%), dry pollution-free canal mud (14%), dry chicken manure (20-25%), dry pig manure (30-35%), diammonium phosphate (10%), calcium amino acid chelate (0.5%), zinc amino acid chelate (0.25%) and copper amino acid chelate (0.25%), are sent into a grinder to be ground; feeding ground materials into fermentation tank, then adding organic fertilizer; stirring the materials uniformly with water, and adding the deodorant.    USE - For preparing base fertilizer of mature tree of Hongfeng (Pinyin of Chinese character) apricot (claimed).    ADVANTAGE - The preparation method is simple process, wide sources, low production cost and simple operation.    DETAILED DESCRIPTION - A preparation method for base fertilizer of mature tree of Hongfeng (Pinyin of Chinese character) apricot, involves preparing the raw materials of plant straw (15%), cotton seed cake (5%), dry pollution-free canal mud (14%), dry chicken manure (20-25%), dry pig manure (30-35%), diammonium phosphate (10%), calcium amino acid chelate (0.5%), zinc amino acid chelate (0.25%) and copper amino acid chelate (0.25%), are sent into a grinder to be ground; feeding the ground materials are fed into fermentation tank, then adding the organic fertilizer leaven in the right amount; stirring the materials uniformly with water, then hermetically fermented, for 10 days in summer and 25 days in winter; after the fermentation, adding the deodorant in the right amount and uniformly stirred for deodorization; the deodorized materials are aired and ground to powders.
NOVELTY - Preparation technology of particle carbon, involves using semi-sealed low temperature carbonization-furnace anoxic carbonization decomposition, directly processing low temperature carbonization the waste with different granularities, such as straw, fruit shell, corn core, chicken manure and other raw materials, where carbonized particle completely keeps the original micro-porosity, where the porosity degree is high, so the produced particle of carbon has good absorbing performance and increasing insulating property.    USE - As preparation technology of particle carbon (claimed).    ADVANTAGE - The carbon-based slow release fertile produced by using the preparation technology has the merits of no energy consumption, low cost, high yield, stable quality, and no pollution to the environment.
NOVELTY - A functional fungicide or functional bacterial manure comprises (wt.%): Streptomyces fradiae CGMCC No.5133 and Bacillus mucilaginous (5-70), cake dregs (2-20), humic acid powder (10-50), zeolite powder (5-30), shale (0-20), powdered rock phosphate (0-10) and agricultural rare earth (0-30).    USE - As functional fungicide or functional bacterial manure (claimed).    ADVANTAGE - The functional fungicide improves the production efficiency and save production cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for functional fungicide containing Streptomyces fradiae CGMCC No.5133 and Bacillus mucilaginous is prepared by inoculating liquid seed solution into a solid multiplication culture medium to perform the multiplication culture and drying the solid multiplication culture medium.
NOVELTY - The bacterial strain Perlucidibaca piscinae single nitric acid bacterial colony having preservation number of China general microbial culture collection center (CGMCC) NO. 5281, is claimed.    USE - The bacterial strain is useful for removing nitrite-nitrogen from sewage at low temperature in aerobic condition, where the temperature is 8-12 degrees C (all claimed).    ADVANTAGE - The bacterial strain has improved removal rate of nitrate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an isolated culture method of a bacterial strain.
NOVELTY - The instrument has an oxygen concentration detecting sensing probe and a methane concentration detection sensing probe connected with a central processor through a signal processing circuit, where the central processor is connected with a working power supply circuit, an alarm circuit and a digital tube display i.e. LCD.    USE - Alarming instrument for detecting methane and oxygen.    ADVANTAGE - The instrument has compact structure and small volume, and is provided with the digital tube display without having external light intensity.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of an alarming instrument.
NOVELTY - Reducing hydrogen sulfide concentration in a biogas, involves (a) supplying air in a psychrophilic anaerobic bioreactor producing biogas, where the bioreactor comprises a gas phase, and liquid phase containing an anaerobic sludge, or supplying a first psychrophilic bioreactor with air and biogas, where the biogas is provided from second bioreactor, and the first psychrophilic bioreactor comprising a sludge, or , and (b) removing hydrogen sulfide from biogas by oxidation to elemental sulfur, or removing the converted sulfur from hydrogen sulfide from the bioreactor.    USE - The method is useful for reducing hydrogen sulfide concentration in a biogas.    ADVANTAGE - The method is easy to perform and cost-effective, and causes no pollution.
NOVELTY - A syngas stream composition comprises (vol.%): particulates (up to 50000 mg/Nm3); hydrogen (H2) (5-39); carbon monoxide (CO) (5-39); carbon dioxide (CO2) (15-50); nitrogen (N2) (8-30); argon (0-2); and moisture (15-50 on a wet basis); and where the hydrogen (H2)/carbon monoxide ratio is 0.3-2 and at least 15 wt.% of the particulates have an aerodynamic particle diameter of less than or equal to 1 micron.    USE - As syngas stream, preferably plasma gasified syngas, from gasified municipal solid waste (claimed).    ADVANTAGE - The waste is efficiently gasified to form a high quality syngas using a plasma gasifier. The waste is controllably and efficiently gasified in the presence of oxygen. The method involves shredding of waste without sorting prior to gasification, which reduces or eliminates the need to pre-sort or process waste prior to gasification, which may decrease the cost and energy requirements for the system. The gas stream includes a plasma gasifier that does not require drying, pyrolysis, gasification and combustion zones within gasifier, each zone requiring different temperatures, providing for greater simplification of controls and equipment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for forming a syngas stream involving providing a waste; gasifying the waste under oxygen-fired conditions to form a syngas stream (C1).
NOVELTY - A glycerol containing alkali metal, alcohol, organic fatty acid, and moisture content under is heated under reduced pressure, and alcohol and moisture content are removed. A sulfuric acid is added to glycerol, neutralized and centrifuged. The sulfate and organic fatty acid of alkali metal are separated-removed. The sulfate of alkaline-earth metal is added and mixed with glycerol. The glycerol is centrifuged. The sulfate of alkali metal and alkaline-earth metal salt of organic fatty acid are separated-removed. Thus, the purification of glycerol is carried out.    USE - Purification of glycerol by-produced during manufacture of biodiesel fuel.    ADVANTAGE - The method enables economical purification of glycerol, by suppressing blockage of pipes. The corrosion of supercritical water piping is suppressed.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view explaining the manufacture of biodiesel.    Waste glycerol header (200)    Neutralization tank (206)    Continuous centrifuges (211,231)    Magnesium sulfate screw feeder (222)    Cation exchange tower (241)
NOVELTY - Fertilizer comprises at least one organic fertilizer selected from stable manure, compost and/or peat; at least one calcium mineral fertilizer selected from quick lime with calcium oxide (up to 70 wt.%), slaked lime with calcium oxide (up to 60 wt.%), dolomite; aluminum powder, where the fertilizer is in the form of pellets and pH of the fertilizer is in the alkaline area; and where the moisture content of the fertilizer is reduced to 10-14 wt.%.    USE - As fertilizer (claimed) useful in agriculture.    ADVANTAGE - The fertilizer improves the quality of natural organic fertilizer, and allows for the addition of one or several mineral fertilizers to this mixture such that there is enough of the natural organic fertilizer to carry out its function in the plant and soil and the quantity of mineral fertilizers does not have negative effect on the soil and the long-term of the production of an individual plant culture. The fertilizer solves the problem of nutrient loss, nitrogen in particular, from natural organic fertilizer by adding powdered aluminum and lime (slaked or quicklime) to natural organic fertilizer. The mixture of natural organic fertilizer, aluminum and lime is pelletized in order to facilitate application of this fertilizer product under the root of the plant. The fertilizer allows the plant to extract nutrients directly from the pellet when its roots have grown strong enough to do so. The pellets are durable, do not decompose underground and do not lose nutrients until the plant's roots penetrate them and begin extracting nutrients. A reaction occurs within the pellet between the aluminum and lime that creates hydrogen, which bonds nitrogen to itself, converting into ammonia that remains within the pellet thus significantly reducing the loss of nitrogen from natural organic fertilizer.
NOVELTY - Making a hydrocarbon fuel comprises (a) converting a feedstock containing monosaccharides, oligosaccharides and/or polysaccharides to furfural-ketone adducts and/or hydroxymethyl furfural (HMF)-ketone adducts by reacting the feedstock with one or more ketones in the presence of a bromide or chloride salt, acid and water, and (b) at least partially hydrogenating and dehydrating the ketone adducts to form hydrocarbons or oxygenated hydrocarbons.    USE - The method is useful for making a hydrocarbon fuel.    ADVANTAGE - The method provides hydrocarbon fuel in a simple and cost-effective manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) depolymerizing lignin comprising contacting biomass containing lignin with one or more ketones in the presence of a bromide or chloride salt, acid and water at a temperature of 85-160 degrees C; and    (2) solubilizing at least a portion of the lignin in biomass in a ketone comprising contacting the biomass containing lignin with one or more ketones in the presence of a bromide or chloride salt, acid and water at a temperature of 85-160 degrees C.
NOVELTY - Skeletal isomerization is carried out at 60-110 degrees C with respect to perhydroacenaphthene (1 part weight), using hydrogen fluoride (0.5-1.5 parts weight) and boron trifluoride (0.05-0.5 part weight) as catalyst, to obtain 1,3-dimethyladamantane.    USE - Manufacture of 1,3-dimethyladamantane for use as polymeric raw material and fine chemicals e.g. pharmaceuticals.    ADVANTAGE - The method eliminates the use of a solvent and expensive catalyst, and enables catalyst recovery. The method enables economical and environmentally-friendly manufacture of 1,3-dimethyladamantane with high yield.
NOVELTY - Producing bioethanol and methane gas, involves obtaining crops having high yield as a raw material for producing bioethanol, obtaining mixed waste liquid and unused biomass as a raw material for producing methane gas, where methane gas is produced as countermeasure against waste liquid, the methane gas is utilized as distillation heat source during purification of bioethanol, and the biomass circulation system is used for manuring and managing the crops, and a digestive liquid generated during the methane gas production process is used as liquid fertilizer.    USE - The method is useful for producing bioethanol and methane gas, and digestive liquid (by-product) which is used as liquid fertilizer.    ADVANTAGE - The method is cost-effective, and enables to reuse waste material.
NOVELTY - A solar cell has pattern which is formed on organic thin-film transistor, using compound having linear or branched 3-5C alkyl group, and solvent which is dipropylene glycol dialkyl ether.    USE - Solar cell is used for electronic paper and organic electroluminescent device.    ADVANTAGE - The solar cell has excellent workability.
NOVELTY - Generating hydrogen, comprises: providing a transition metal-carbon nanotube hybrid catalyst comprising a nitrogen-containing carbon nanotube in which transition metal nanoparticles with a uniform size are distributed; and introducing the transition metal-carbon nanotube hydride catalyst to an alkaline sodium borohydride solution to generate hydrogen.    USE - The method is useful for generating hydrogen (claimed) in hydrogen storage systems for fuel cells, fuel storage systems for hydrogen fuel vehicles, electric vehicles and/or as energy sources for electronic devices.    ADVANTAGE - The method: utilizes a transition metal-carbon nanotube hybrid catalyst containing nitrogen in which transition metal powder having high catalytic activity is uniformly distributed in an interval of several nanometers on surface of a carbon nanotube so as to maximize surface area of the catalyst exhibiting catalytic activity; is more simple for hydrogen storage compared to conventional methods; reduces the size of a hydrogen storage tank and/or investment costs because of high storage capacity of hydrogen; and utilizes sodium borohydride existing in an aqueous solution with a very high pH at room temperature and ambient pressure thus it is stable in view of thermodynamics so that sodium borohydride can be stably stored in the air for several months and rapidly react with the catalyst introduced to it to generate hydrogen.
NOVELTY - Forming hydrocarbon fuel compound involves: obtaining quantity of hexose sugar; reacting hexose sugar to form alkali metal levulinate, alkali metal valerate, alkali metal 5-hydroxy pentanoate or alkali metal 5-alkoxy pentanoate; preparing anolyte comprising alkali metal levulinate, alkali metal valerate, alkali metal 5-hydroxy pentanoate or alkali metal 5-alkoxy pentanoate; and decarboxylating alkali metal levulinate, alkali metal valerate, alkali metal 5-hydroxy pentanoate or alkali metal 5-alkoxy pentanoate to form radicals, where the radicals react to form hydrocarbon fuel compound.    USE - For forming hydrocarbon fuel compound such as gasoline additive including octane, 2,7-octadione, 1,8-hydroxy octane, and 1,8-dialkoxy octane (claimed).    ADVANTAGE - The method produces hydrocarbon fuels from biomass such as plant, algal or animal origin.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an electrolytic cell comprising: an anolyte compartment; a catholyte compartment; NaSICON membrane that separates the anolyte compartment from the catholyte compartment; an anolyte is housed within the anolyte compartment, where the anolyte comprises a solvent and a quantity of sodium levulinate, sodium valerate, sodium 5-hydroxy pentanoate, or sodium 5-alkoxy pentanoate; a catholyte is housed within the catholyte compartment; and a voltage supplier that decarboxylates the sodium levulinate, the sodium valerate, the sodium 5-hydroxy pentanoate, or the sodium 5-alkoxy pentanoate, where the decarboxylation forms radicals that react to form a hydrocarbon fuel compound.
NOVELTY - Purified biodiesel fuel obtained by process comprising treating fatty acid alkyl esters utilizing at least one adsorbent column (12) containing an adsorbent material (14) for removing at least one impurity from the fatty acid alkyl esters, is claimed.    USE - The biodiesel fuel is useful in methanol recovery process.    ADVANTAGE - The biodiesel fuel: allows methanol recovery without water washing or adsorptive treatment with filtration; and is free of impurities comprising soaps, metals, free glycerin, sterol glucosides and many other impurities that reduce stability of biodiesel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a system for purification of the fatty acid alkyl esters.    DESCRIPTION OF DRAWING(S) - The figure shows schematic diagram of the system for biodiesel purification using an adsorbent column purification process.    Adsorbent system (10)    Adsorbent column (12)    Adsorbent material (14)    Crude biodiesel (16)    Purified biodiesel (17)
NOVELTY - The apparatus has heavy gas decomposition apparatus (5) that is provided with catalyst made of nickel, alumina or iron for stimulating the decomposition of the heavy gas used as tar substance. The heavy gas is filled at temperature of 500-700 degrees C in the rotary kiln (3). The pyrolysis gas discharged from the heavy gas decomposition apparatus is supplied as supplementary fuel to the burner (12) of the rotary kiln.    USE - Processing apparatus for carbonizing and incinerating hen droppings used as fertilizer and soil conditioner. Can also be used livestock excrement e.g. pig feces.    ADVANTAGE - Since the pyrolysis gas discharged from the heavy gas decomposition apparatus is supplied as supplementary fuel to the burner of the rotary kiln, the fuel consumption is reduced, the discharge of tar substance is reduced and the energy efficiency is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the processing apparatus for carbonizing and incinerating hen droppings.    Hen droppings (1)    Injecting hopper (2)    Rotary kiln (3)    Heavy gas Decomposition apparatus (5)    Burner (12)
NOVELTY - A photo-curing ink composition manufacturing method involves producing photocure dispersion master solution, where the solution is prepared using electromagnetic conductive polymer particle. Light is scattered in the obtained master solution, followed by filtering using a filter to obtain finished product.    USE - Method for manufacturing photo-curing ink composition for use in electronic and electrical components such as secondary battery, solar cell, fuel cell, integrated circuit, large scale integrated circuit, very large scale integration circuit, chemical sensor, DNA chip or electromagnetic wave shielding (all claimed).    ADVANTAGE - The method enables manufacturing photo-curing ink composition in an eco-friendly manner with low energy consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an electronic component and electrical component.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating a method for manufacturing photo-curing ink composition.'(Drawing includes non-English language text)'
NOVELTY - Fuel composition comprises a distillate fuel and an additive comprising the reaction product of an alkyl phenol with an acid or an anhydride comprising optionally saturated dicarboxylic acid, an anhydride of a saturated dicarboxylic acid and/or an anhydride of an unsaturated dicarboxylic acid.    USE - The composition is useful for improving the lubricity and/or anti-corrosion properties of a low-sulfur content middle distillate fuel (claimed). The composition is useful for improving lubricity of a lubricant including a motor oil, a transmission fluid including in an automotive automatic transmission, and in an alcohol including in methanol and/or ethanol when used as a fuel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for improving the lubricity and/or anti-corrosion properties of a low-sulfur content middle distillate fuel, comprising adding the additive to the middle distillate fuel.
NOVELTY - The system has grounded stainless steel electrolyte stabilization tank (24) that is provided with water reservoir, catalytic chemicals of potassium hydroxide and boric acid within water solution, and enclosed fluid pathway. A hydrogen generator (36) is provided with fluid conduit that is in communication with electrolyte stabilization tank, fluid holding space provided between anode plate and cathode plate, and electric power coupling provided between power providing system and anode and cathode plate.    USE - Oxyhydrogen (HHO) generating electrolysis system for combustion engine air supply system.    ADVANTAGE - The electronic control box is provided to control the electrolyte stabilization pump. The stabilization tank is grounded to eliminate a negative build up of electric charge within the tank, thus the overall effectiveness of the apparatus is increased. The water reservoir is fluidly coupled to the electrolyte stabilization tank through conduit so as to maintain the fluid level within the electrolyte stabilization tank. The fill switch is coupled to pump between the water reservoir and electrolyte stabilization tank so as to allow water to flow into the electrolyte stabilization tank when the volume drops below the preset limit.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the improved combustion engine air supply system.    Combustion engine air supply system (20)    Electrolyte stabilization tank (24)    Scrubber (30)    Hydrogen generator (36)    HHO circulation pump (44)
NOVELTY - A compost slaughter by-products manufacturing system has a screening device for selecting by-product generated in slaughter, and a fatty acid decomposition unit disassembling the saturated fatty acid of the by-product. A reducing odor part disassembles animal protein to remove bad smell of the by-product. A microwave oven is set as dryer for drying the by-product. A grinding part pulverizes the by-product to desired size.    USE - Compost slaughter by-products manufacturing system.    ADVANTAGE - The manufacturing system improves fermentation and drying process of by product in a simple, economical and eco-friendly manner.    DETAILED DESCRIPTION - A compost slaughter by-products manufacturing system has a screening device for selecting by-product generated in slaughter in specified condition, and a fatty acid decomposition unit disassembling the saturated fatty acid (R-CCOH) of the selected by-product. A reducing odor part disassembles animal protein in order to remove the bad smell of the by-product, where the saturated fatty acid is disassembled. A microwave oven is set as dryer for drying the by-product. Fermentation is carried out with the aerobic microorganism under aridity condition. A grinding part pulverizes the by-product to desired size. An INDEPENDENT CLAIM is also included for a compost manufacturing process.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of compost slaughter by-products manufacturing system.'(Drawing includes non-English language text)'
NOVELTY - Method for producing homotypic acetogenic bacteria comprises adding sodium formate as carbon source, and 2-bromoethanesulfonate as inhibitor for producing methane, in upward-flow anaerobic sludge blanket reactor, selectively culturing in an acidized anaerobic sludge, where the amount of sodium formate is 1.3-13 g/l, and the dosage of 2-bromoethanesulfonate is 30-50 mmole/l, the initial pH is 7 plus minus 0.5.    USE - The method is useful for producing homotypic acetogenic bacteria.    ADVANTAGE - The method is cost effective and eco-friendly for producing homotypic acetogenic bacteria.
NOVELTY - Microorganism proliferation device wastewater treatment method comprises collecting sewage into adjusting pool, adjusting water quality for 6-8 hours; pumping into a biochemical treatment system through lifting pump, biochemically treating and culturing bacteria through microorganism proliferation; returning ammonia nitrogen in the mixed solution of the anoxic section by adding nitrobacteria, adding nitrate; performing post-treatment, adding domestic sewage to 3/4 capacity in the microorganism proliferation; and discharging or recycling.    USE - A microorganism proliferation device wastewater treatment method.    ADVANTAGE - The method effectively improves the biochemical sewage treatment process, improves the biochemical treatment efficiency, reduces running cost of biochemical treatment, is capable of moving up and down in the biochemical system error or other accident state, quickly recovers the biochemical system, and has simple operation and stable operation.    DESCRIPTION OF DRAWING(S) - The drawing is a flow diagram illustrating the microorganism proliferation device wastewater treatment method (Drawing includes non-English language text).
NOVELTY - A home landscape type kitchen waste earthworm compost reactor comprises miniascape, clapboard with holes, side wall, bottom frame, earthworm compost reaction tank, side wall inserting plate and gas distribution hole. The miniascape is on upper end of the clapboard with holes. The earthworm compost reaction tanks are in the clapboard with holes and are separated from each other by the side wall inserting plate.    USE - A home landscape type kitchen waste earthworm compost reactor.    ADVANTAGE - The reactor can keep indoor air fresh and will not influence family life, has no complicated operation in the process of using, and is simple and convenient to operate.    DETAILED DESCRIPTION - Home landscape type kitchen waste earthworm compost reactor comprises miniascape, clapboard with holes, side wall, bottom frame, earthworm compost reaction tank, side wall inserting plate and gas distribution hole. The miniascape is on upper end of the clapboard with holes. The earthworm compost reaction tanks are in the clapboard with holes and are separated from each other by the side wall inserting plate. Two sides of the clapboard with holes are provided with side walls. The gas distribution holes are on the surface of the side wall, the bottom of the miniascape and the side faces of the earthworm compost reaction tank.
NOVELTY - A plant nutrient brick comprises (wt.%) organic fertilizer (preferably aged fermented chicken manure, pig manure, dairy manure, sheep manure and/or bacterial waste material, 40-60); chemical fertilizer (preferably nitrogenous, phosphate and/or potassium fertilizer, 5-10); starch (10-15); clay (preferably kaolin, 25-35); and water (balance).    USE - Plant nutrient brick, i.e. cube, sphere, or cylinder, used for home greening and public green space.    ADVANTAGE - The brick is easy to use and locks plant nutrients in starch and clay so that fertilizer has long lasting effect, thus saving time and fertilizer.
NOVELTY - The method involves providing a silent low reacting product during ethanol production. The low reacting product is separated into a two fraction parts. One of the fraction parts is thinner than the other fraction part. A portion of the former fraction part is separated by separation of suspended solids in a protein-rich portion. An aerobic conversion of a carbon-rich part of the former fraction part is carried out with formation of biogas. Syrup is combined with the latter fraction part and dried to form deposition of a final protein.    USE - Method for processing a reaction product e.g. cereal during ethanol production. Can also be used for sugar cane, wheat, maize, triticale, rye, barley, and sugar beet.    ADVANTAGE - The method ensures combining of bio-ethanol with biogas, avoiding energy loss during production of the ethanol and adjusting pH with acid drain that is formed in desulfurization of biogas and reducing chemical costs for correcting acidity of anaerobic effluent in a biogas plant.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a system for producing biogas in reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a system for producing biogas in reactor.
NOVELTY - A composition, comprises: graphene or graphene oxide comprising at least one functional group associated with the graphene or graphene oxide.    USE - The composition and method are useful for fabricating a functionalized carbon-based nanostructure; for producing a device, where the device is a capacitor; and for producing a fuel cell, and a photovoltaic cell (all claimed).    ADVANTAGE - The composition efficiently produces an improved functionalized carbon-based nanostructure.    DETAILED DESCRIPTION - A composition, comprises: graphene or graphene oxide comprising at least one functional group associated with the graphene or graphene oxide, where the functional group has the structure of formula (1).    R1, R2, and R3= optionally substituted substituent; and    G = carbon atom of the graphene or graphene oxide.    INDEPENDENT CLAIMS are:    (1) a method for fabricating a functionalized carbon-based nanostructure, comprising: providing a carbon-based nanostructure comprising an allylic functional group; reacting the carbon-based nanostructure with a reactant comprising at least one carbon atom; and causing a carbon-carbon bond to form between the carbon atom within the reactant and a carbon atom within the carbon-based nano structure;    (2) a device, comprising: the composition;    (3) a fuel cell, comprising: the composition;    (4) a method, comprising: reducing water using the composition;    (5) a composite, comprising: the composition; and a matrix material; and    (6) a photovoltaic cell, comprising: the composition.
NOVELTY - The reactor has a reaction bath part (100) connected with an external air supply part (300). A dehydrogenase (DHA) material is installed at an inner side of the reaction bath part. An ultrasonic oscillator (210) irradiates ultrasound to an anaerobic sludge part. An injection nozzle (320) is installed at a lower part of the reaction bath part. An air supply pipe (310) is connected to the injection nozzle. The air supply pipe is equipped with an air pump (330). An anaerobic sludge colony layer is formed on the reaction bath part. A controller (400) controls an operation of the air pump.    USE - Micro-aerator integrated dry anaerobic digestion reactor.    ADVANTAGE - The reactor prevents external air while entering, reduces hydrogen sulfide production amount and increases methane gas product amount. The reactor diversifies concentration of adenosine triphosphate (ATP) and DHA in the anaerobic sludge part by arranging the ultrasonic oscillator at the inner side of the reaction bath part by a dry anaerobic digestion process.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a micro-aerator integrated dry anaerobic digestion reactor.    Reaction bath part (100)    Ultrasonic oscillator (210)    External air supply part (300)    Air supply pipe (310)    Injection nozzle (320)    Air pump (330)    Controller (400)
NOVELTY - The generator has a discharge door ejecting raw material. A generating bath is equipped with the discharge door. Solar energy is collected by a solar collector. A heat insulation cover is provided with transparent material. An inlet pipe is connected to a water tank. A heat exchanging tube is connected to the inlet pipe. Warm water circulation is controlled by a control valve. An end of an exhalant is connected to the heat exchanging tube, and another end of the exhalant is connected to the water tank. The control valve is connected to a circulating pump.    USE - Methane gas generator.    ADVANTAGE - The generator has low energy consumption, and achieves carbon exhaust amount reduction effect and warm-keeping effect according to greenhouse effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross sectional view of a methane gas generator.
NOVELTY - A halogenated catalyst comprises oxidation transition-metal composite body and oxygen.    USE - Halogenated catalyst for manufacture of halogen compound (claimed) used in organic chemistry industry, petrochemical industry, pharmaceutical industry, or agrochemical industry.    ADVANTAGE - The catalyst is highly active and efficiently advances halogenation on moderate conditions and can be easily recovered after reaction.    DETAILED DESCRIPTION - A halogenated catalyst comprises oxidation transition-metal composite body of formula AxMO(2+0.5x), and oxygen.    A=alkali metal;    M=Cr, Mn, Co, Ni and Fe; and    x=0-2.    An INDEPENDENT CLAIM is included for a manufacture of the halogen compound involving making a compound or polymer and halogen which may have substituent and carbon-hydrogen bonding react in presence of halogenated catalyst.
NOVELTY - The system has elongated separator vessel (120) that is mounted upright above the tank bottom, and provided with mid-level inlet (122), upper gas outlet (126) and bottom-opened discharge end (150). The mid-level inlet is communicated with landfill gas collector pipe (104). The bottom-opened discharge end is located vertically above/below the tank bottom/tank leachate level (112) of atmospheric tank respectively. The separator vessel leachate level (152) is located below/above mid-level inlet/bottom-opened discharge end respectively.    USE - System for separating landfill gas in raw multi-phase stream from landfill gas collector.    ADVANTAGE - The pre-treatment of raw multi-phase stream from landfill site can be performed in a continuous manner. The quality of the landfill gas can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for pre-treating raw multi-phase stream from landfill site.    DESCRIPTION OF DRAWING(S) - The drawing shows the cross-sectional view of the separating system.    Landfill gas collector pipe (104)    Tank leachate level (112)    Elongated separator vessel (120)    Mid-level inlet (122)    Upper gas outlet (126)    Bottom-opened discharge end (150)    Separator vessel leachate level (152)
NOVELTY - Waste biomass (1) is mechanically pretreated (2) and anaerobically digested (3) using heated water. The produced sludge is used as bio-fertilizer (4). Methane gas (5) produced during digestion is collected, compressed and stored. The methane gas is combusted to produce energy for generation of electricity. Feed water is preheated in heat exchanger (7) using the produced energy, and heated water is used for anaerobic digestion. Water vapor and carbon dioxide produced in heat exchanger or discharged, and generated electricity (8) is utilized.    USE - Sustainable waste management.    ADVANTAGE - The energy conversion of waste is efficiently and economically enabled without affecting environment at high conversion rate.    DESCRIPTION OF DRAWING(S) - The drawing shows the flowchart of sustainable waste management.    Waste biomass (1)    Mechanical pretreatment (2)    Anaerobic digestion (3)    Bio-fertilizer (4)    Methane gas (5)    Energy conversion (6)    Heat exchanger (7)    Electricity (8)
NOVELTY - Drying residual biomass, involves homogenizing material and feed in a hopper and then drying the material.    USE - Method for drying residual biomass used as fuel for producing cement clinker.
NOVELTY - The apparatus has a culture tank (200) integrated with another culture tank (400). The former culture tank cultivates aerobic micro-organism. The latter culture tank cultivates anaerobe micro-organism. A micro-organism feed port (260) is provided with a water supply part (250). A micro-organism supply tube (262) is connected to the water supply part. A motor fixing plate (222) is connected to the supply tube. An impeller (224) is arranged at upper center of the latter culture tank and fixed to a tank cap (210). A rotation axis rod (223) is connected to a speed reduction motor (221).    USE - Apparatus for cultivating aerobic/anaerobic micro-organisms that are utilized to avoid generation of bad smell in waste dump site of butchery, food and drink.    ADVANTAGE - The apparatus efficiently cultivates the aerobic/anaerobic micro-organisms to avoid generation of bad smell in a waste dump site of a butchery, food and drink. The apparatus has high cultivating efficiency, and is inexpensive.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of an aerobic/anaerobic micro-organisms cultivating apparatus.    Culture tanks (200, 400)    Tank cap (210)    Speed reduction motor (221)    Motor fixing plate (222)    Rotation axis rod (223)    Impeller (224)    Water supply part (250)    Micro-organism feed port (260)    Micro-organism supply tube (262)
NOVELTY - A livestock excretion processing unit comprises: dryer (70) for drying the domestic animals, where the domestic animal within the dryer is dried with the vapor; gasifier (4) for generating combustible gas using the domestic animals dried in the dryer; furnace (10) for burning the combustible gas generated from the gasifier and generates the combustible waste gas; once-through boiler (20) for changing to the superheated steam coil (22) inside circulating water using combustible waste gas, where the steam coil is installed within the once-through boiler.    USE - As livestock excretion processing unit for livestock excretion processing method (claimed) such as for treating feces and urine of domestic animals.    ADVANTAGE - The livestock excretion processing unit provides at the same time drying and processing the domestic animals urine with high energy efficiency and environment-friendly ways.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for livestock excretion processing method involving using the livestock excretion processing unit.    DESCRIPTION OF DRAWING(S) - The figure shows a livestock excretion processing unit.    Gasifier (4)    Furnace (10)    Once-through boiler (20)    Superheated steam coil (22)    Dryer (70)
NOVELTY - Method of sequestering carbon dioxide via manufacture and export of renewable liquid natural gas, comprises: generating electricity in Australia from renewable energy i.e. wind, solar, biomass or geothermal; using this renewably generated electricity to power electrolysis plant in Australia; collecting carbon dioxide from Australian emission source i.e. as fossil fuelled power station, an aluminum smelter, biomass energy plant or liquefied natural gas (LNG) plant; combining carbon dioxide and hydrogen in Sabatier reactor to generate methane gas.    USE - The method is useful for sequestering carbon dioxide via manufacture and export of renewable liquid natural gas.    ADVANTAGE - The method: avoids difficulty of storing and transporting hydrogen; and reduces cost of transporting carbon dioxide and methane; and solves intermittency which attaches to some forms of renewable energy.    DETAILED DESCRIPTION - Method of sequestering carbon dioxide via manufacture and export of renewable liquid natural gas, comprises: generating electricity in Australia from a facility powered by renewable energy i.e. wind, solar, biomass or geothermal; using this renewably generated electricity to power an electrolysis plant in Australia to split water into hydrogen and oxygen; collecting carbon dioxide from Australian emission source i.e. as a fossil fuelled power station, an aluminum smelter, a biomass energy plant or an LNG plant; and combining the carbon dioxide and the hydrogen in a Sabatier reactor in Australia to generate methane gas which is delivered to Australian LNG plant for export overseas.
NOVELTY - The container has lid, floor, wall panel (4), air outlet formed in upper zone (24) and inlet formed in lower zone (22). Several upwardly directed air flow apertures (42) for allowing air to flow through composting mass to outlet are provided. The apertures are set as separate passages like tubes extending from lower zone to upper zone. The floor has central zone (20) which increases the volume of airspace. The apertures extend from raised portion (Incomplete specification, abstract based on available information published by the patent office).    USE - Compost container.    ADVANTAGE - The air flow apertures allow air to comfortably enter and exit the container. The volume of container is reduced and its freight cost is reduced. The container can be easily lifted from the ground and inverted for emptying the container completely. The container can be reassembled and refilled easily at any place. The container can be used easily at the time of transport and storage. The container surfaces can be brushed clean and the ducts are set accessible for prevention of blockage.    DESCRIPTION OF DRAWING(S) - The drawings show the sectional plan and front views of the compost container.    Wall panel (4)    Central zone (20)    Lower zone (22)    Upper zone (24)    Air flow aperture (42)
NOVELTY - Obtaining stabilized biomass for generating thermal energy in boilers, furnaces and burners for domestic, commercial and industrial purpose, involves mixing organic matter and material obtained from sewage treatment plants or activated sludge in the ratio 2:5 and then processing the mixture by using microorganisms for 15-30 days. The organic material is industrial waste material obtained from cereals, vegetable oils and fats, starches, oily sludge, straw, husks, grease recovered during the treatment of domestic wastewater and lignocellulosic materials.    USE - Method for obtaining stabilized biomass for generating thermal energy for boilers, furnaces and burners for domestic, commercial and industrial purpose.    ADVANTAGE - The method enables to obtain stabilized biomass having higher calorific value.
NOVELTY - A phosphorin activator comprises (parts by weight): organic fertilizer (100), humic acid (10-30) and malic acid (10-30). The organic fertilizer is prepared by fermenting livestock manure.    USE - As phosphorin activator (claimed), useful in agriculture technology field.    ADVANTAGE - The phosphorin activator effectively improves the effectiveness of phosphorus in the soil, improves content of rapidly available phosphorus, and reduces the use of the fertilizer. The preparation method is simple, the raw material will not generate secondary pollution, and it is safe and efficient.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the phosphorin activator involving grinding the organic fertilizer, humic acid and malic acid, sieving, and then mixing.
NOVELTY - A bio-butanol manufacturing method involves pre-processing lignocellulosic biomass for separating hemicellulose from the lignocellulosic biomass, and manufacturing material liquid using the hemicellulose. Saccharified liquid is manufactured by using the material liquid, and a culture medium is manufactured. Microorganism is grown in the culture medium and utilized for fermenting the sacchride liquid to manufacture bio-butanol.    USE - Method for manufacturing bio-butanol from lignocellulosic biomass.    ADVANTAGE - The method enables production of the bio-butanol with capacity of about 50 tons/year. The method enables improvement of saccharification ratio of the saccharified liquid by controlling pH of the saccharified liquid without utilizing citrate buffer solution, sulfuric acid and sodium hydroxide.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph illustrating xylose retrieval quantity after saccharification of rice straw.
NOVELTY - System comprises a digester, which contains microalgae and bacteria. A photobioreactor (2) is also provided which contains microalgae for absorbing carbon dioxide and for oxidizing hydrogen sulfide. A column (3) is provided for of purifying biogas, where the column contains an inlet (11) and an outlet (14).    USE - System used for treating industrial effluent and biogas.    ADVANTAGE - The system enables to treat industrial effluent and biogas simultaneously.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a system.    Photobioreactor (2)    Column (3)    Pallets (4)    Effluent (6)    Inlet (11)    Outlet (14)
NOVELTY - Obtaining yeast biomass used in animal feed, involves performing fermentation by using sugarcane molasses.    USE - Method for obtaining yeast biomass used in animal feed.    ADVANTAGE - The method enables to obtain yeast biomass enriched in copper or zinc.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a product for animal feed, which comprises a substrate, molasses, ammonium carbonate, ferrous sulfate, ammonium sulfate and ammonium hypophosphate.
NOVELTY - Domestic composting of worms has a base grating, where a small mesh is installed at bottom of a container (2) of composting display (100). The base contains solid material, where the container has a prismatic shape with lateral openings (4) and protective netting for ventilation and moisture control.    USE - Domestic composting of worms.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the composting display.    Container (2)    Lateral openings (4)    Composting display (100)
NOVELTY - Method for producing granular bioorganic fertilizer, involves producing fermentation liquid containing bacterial strain with an effective viable count of 0.5-4 billions/ml, adsorbing fermentation liquid to humic acid, where the fermentation liquid has an effective viable count of 2-13.5 billions/g, mixing the organic material and auxiliary material, coating the mixture (0.25-1%) and adhesive to the surface of the organic material particle uniformly and quantitatively and packing the mixture to obtain finished bioorganic fertilizer.    USE - The method is useful for producing granular bioorganic fertilizer.    ADVANTAGE - The method increases commercial value of granular bioorganic fertilizer.
NOVELTY - An organic fertilizer comprises (pts. wt.) cogongrass (10-19), cleavers (10-20), Pulsatilla chinensis (1-5), corn straws (20-30), and farmyard manure (30-60).    USE - Organic fertilizer used for corn.    ADVANTAGE - The fertilizer reasonably utilizes waste; has soil repairing function and low carbon content; and fully supplies required nutritional elements of corn.    DETAILED DESCRIPTION - An organic fertilizer comprises (pts. wt.) cogongrass (10-19), cleavers (10-20), P. chinensis (1-5), corn straws (20-30), and farmyard manure (30-60). The fertilizer is produced by: (A) respectively cutting corn straws, cogongrass and cleavers into 1-2 cm; (B) washing P. chinensis 2-3 times with water, drying to wilting state, cutting, boiling in water (P. chinensis/water weight ratio=1:9.5-10.5) for 20-30 minutes, separating, and collecting P. chinensis juice and residue; (C) uniformly mixing cut corn straws, cogongrass and cleavers with farmyard manure and P. chinensis residue, forming composting surface with height of 10-15 cm, and spraying P. chinensis juice to each composting surface until composting process is finished; and (D) covering and sealing the compost with plastic film, and curing (preferably for 45-65 days). The compost is cured when the color is brown or black brown, black liquid is discharged, the volume is reduced to 2/3-1/2 of original volume before composting, and/or the compost is crisp as dry soil when twisting and untwisting with fingers. An INDEPENDENT CLAIM is included for application of fertilizer including applying 65-70% of total amount of fertilizer as base fertilizer; harrowing and preparing soil; and applying remaining fertilizer as top dressing from tillering to spike differentiation period.
NOVELTY - Botanical sterilizing agent comprises amaranth crude extract and sterile water, where the mass of the amaranth crude extract in 1 ml of botanical sterilizing agent is 0.17-0.5 mg.    USE - The sterilizing agent and the amaranth crude extract are useful for preventing and treating bacterial wilt (all claimed).    ADVANTAGE - The amaranth crude extract: is conveniently obtained; can be industrially produced and can be directly applied by a farmer; has an inhibitory concentration EC50 of 0.0415 mg/ml; has a tobacco bacterial wilt treating rate of 77-90.29%, in comparison with the conventional sterilizing agent, e.g. streptomycin sulfate; has low toxicity; and is eco-friendly and safe.
NOVELTY - Promoting decomposition of cotton straw, involves (a) grinding dried cotton straw into fine granule, spraying effective microorganism bacterial liquid on the cotton straw in the ratio of 200-300 ml/ton, (b) stacking the cotton straw and straw decomposing agent in a layered manner, and (c) sealing, stacking and fermenting the processed cotton straw until the stacked material turns black and emits light musty smell and is free of odor, and completing the process when the stacked material appears as loosened granular structure.    USE - The method is used for promoting decomposition of cotton straw.    ADVANTAGE - The bacteria improves decomposing efficiency of the straw and increases nutritive material in the decomposed material.    DETAILED DESCRIPTION - Promoting decomposition of cotton straw, involves (a) grinding dried cotton straw into fine granule, spraying effective microorganism bacterial liquid on the cotton straw in the ratio of 200-300 ml/ton, regulating carbon to nitrogen ratio of the cotton straw to 25:1-30:1 and regulating water content of the cotton straw to 65-70%, (b) stacking the cotton straw and straw decomposing agent in a layered manner, where the amount of straw decomposing agent is 0.4-0.5% of weight of the cotton straw, and (c) sealing, stacking and fermenting the processed cotton straw until the stacked material turns black and has light musty smell and is free of odor, and completing the process when the stacked material appears as loosened granular structure.
NOVELTY - A biological organic fertilizer is prepared by stacking and fermenting materials comprising effective microorganisms (EM) solid fermentation product, chicken manure, and 1% EM stock solution at weight ratio of 5-8:88-92:3-4 for 21-25 days at room temperature, and then drying fermented product, where water content of the finished product is less than or equal to 30%.    USE - Biological organic fertilizer used for organic rice cultivation (claimed).    ADVANTAGE - The fertilizer allows conversion of waste (chicken manure) into non-polluting material, is simple to prepare with fast fermentation time and rich in nutrients, can replace application of chemical fertilizer and pesticide, and improves resistance of rice to insects and rice quality.
NOVELTY - Method for preparing biological organic fertilizer, involves adding magnetized water to bran, boiling the mixture, filtering the product, adding silicon solubilizing bacteria, Bacillus mucilaginosus, phosphorus solubilizing bacteria, potassium solubilizing bacteria, nitrogen-fixing bacteria and Thiobacillus, adding coal gangue powder into the mixture, adding chicken manure powder and pig manure powder into the mixture, drying the product and packaging the product.    USE - The method is useful for preparing biological organic fertilizer.    ADVANTAGE - The biological organic fertilizer has high content of organic matter and improved activity of multiple bacteria, and is cost-effective and utilizes easily available raw materials.    DETAILED DESCRIPTION - Method for preparing biological organic fertilizer, involves adding (in kg) magnetized water (350) to bran (3-5), boiling the mixture, filtering the product, adding (in g) silicon solubilizing bacteria (12), Bacillus mucilaginosus (15), phosphorus solubilizing bacteria (10), potassium solubilizing bacteria (10), nitrogen-fixing bacteria (13) and Thiobacillus (10), pulverizing the coal gangue into a powder with a size of 2 mm, adding the powder into the mixture, crushing (in kg) chicken manure (250) and pig manure (250) into a size of 2 mm or less, adding the powder into the mixture, drying the product and packaging the product in aluminum foil or plastic bag, where each bag comprises 25 kg of product.
NOVELTY - A one-pot method technique for preparing tribenuron, involves reacting 2-sulfamoyl-benzoic acid methyl ester with solid phosgene in the presence of a solvent and catalyst, reacting the resultant product with (4-methoxy-6-methyl-(1,3,5)triazin-2-yl)-methyl-amine to give tribenuron. The catalyst is n-butyl isocyanate, n-butyl formate and benzene sulfonamide. The solvent is xylene.    USE - As one-pot method technique for preparing tribenuron (claimed) used for controlling weeds.    ADVANTAGE - The process simplifies reaction device, shortens the reaction time, reduces energy consumption, and total yield reaches more than 80%. The method reduces the waste of the energy, and reduces the light gas running to leakage. The technique is green new technique of energy-saving, and it is safe and environment-friendly.
NOVELTY - Device comprises a decarburization system, flashing system and an adsorbent regeneration system. The decarburization system comprises a decarburization tower, a check valve, a three-way part, a supercharger, a heat exchanger, a ball valve, a marsh gas flow meter, a decarburization tower safety valve and a pressure gauge. The flashing system comprises a high flashing groove and a lower flashing groove, and the adsorbent regeneration system comprises a regeneration tower, a fan, an adsorbent kettle, an adsorbent flow meter, a preprocessing device, a cooler and a high pressure pump.    USE - The device is useful for separating methane and carbon dioxide in marsh gas.    ADVANTAGE - The device consumes less energy, convenient to disassemble and wash, high processing efficiency and ensures stable operation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the device for separating methane and carbon dioxide in marsh gas.
NOVELTY - The system has a hydrothermal disjoint device (200) that is connected with solid-liquid separator (300). The liquid passing through the anaerobic digestion tub (400) is flowed into reaction bath (500).    USE - System for treating bio organic material.    ADVANTAGE - The bio organic material can be treated efficiently with high energy. The lifetime of hydrothermal disjoint device can be prolonged.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of system for treating bio organic material. (Drawing includes non-English language text)    Hydrothermal disjoint device (200)    Solid-liquid separator (300)    Anaerobic digestion tub (400)    Reaction bath (500)    Denitrification tank (600)
NOVELTY - The reactor has waveguide that is inserted through waveguide inlet hole (210) of vertical reactor. A micro wave generator is installed at outer wall of the reactor. Multiple opening slots are formed on four sides of the waveguide. An inlet port and outlet port are formed in up-down opposite direction on filter tube of the reactor. A filter tube is provided to filter foreign substance or suspended material. A gas exhaust port (220) is formed on top of the reactor.    USE - Vertical type biodiesel reactor of biodiesel manufacturing device (claimed).    ADVANTAGE - The reaction efficiency of the reactor is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biodiesel manufacturing device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the vertical type biodiesel reactor.    Continuous reactors (200a-200n)    Waveguide inlet hole (210)    Gas exhaust port (220)
NOVELTY - A flax stalk, sawdust and effective microorganism stock solution is prepared by crushing flax stalk of 65%, and adding sawdust and effective microorganism stock solution of 34.8-34.9% to the crushed flax stalk. Water is added to the mixture and uniformly stirred in a fermenting tank, where humidity of the fermenting tank is controlled between 50-52.    USE - Flax stalk, sawdust and effective microorganism stock solution for a pig house excrement tank (claimed).    ADVANTAGE - The solution can increase disease resistance of the pig, and save labor and material resources. The solution can be converted into quality organic fertilizer.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a fermenting tank for preparing flax stalk, sawdust and effective microorganism stock solution.
NOVELTY - A titanium-based magnetic solid super acidic catalyst comprises sulfate/titanium oxide as catalytic active component and iron oxide as magnetic matrix of composite catalyst at a mass ratio of 10:1-1:3, and magnetic substrate.    USE - A titanium base magnetic solid super acidic catalyst for catalytic pyrolysis of cellulose or for preparing synthesis gas from biomass left glucose ketone (claimed).    ADVANTAGE - The purity is high. The catalyst can be directly used external magnetic field from the separating and recycling solid residue.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a method for preparing a titanium-based magnetic solid super acidic catalyst comprising preparing a magnetic substrate by configuring the controller into mixed solution and adding into a three-opening bottle, putting in the constant temperature water bath at 65 degrees C, stirring while dripping concentration 0.1 mol/liter sodium hydroxide solution until the pH value of 12, stirring and aging, cooling, separating magnetic substrate and upper layer clear liquid, filtering the magnetic matrix to obtain black solid magnetic substance iron oxide, preparing granular polysilicon by immersing nano titanium oxide (0.02-2 mole/liter) in sulfuric acid solution, drying, baking to obtain nano sulfate/titanium oxide, weighing sulfate/titanium oxide and magnetic substrate iron oxide at a mass ratio of 10:1-1:3, adding not greater than 30 wt.% water, and stirring; and    (2) a method using group magnetic solid super acidic catalyst for catalytic pyrolysis or preparing synthesis gas from biomass left glucose ketone comprising mixing titanium-based magnetic solid super strong acid catalyst, and cellulose or biomass at a mass ratio of 5:1; under oxygen condition, performing pyrolysis reaction at 280-450 degrees C; collecting pyrolysis gas; and condensing to obtain the liquid product rich in left-glucose.
NOVELTY - The method involves using waterless-odorless fertilizer collection tool to store and ferment excrement. The straw charring and reburning furnace is provided to burn organic garbage and straw grains to ash. The organic ash and fermented excrement are mixed and straw grains and organic garbage are provided into the collection tool so as to produce fertilizer such that the fertilizer is collected and transported.    USE - Method for optimally processing urban excrement and garbage.    ADVANTAGE - The flow of excrement and garbage outside can be prevented so that the pollution of environment can be prevented with energy saving effect. The waste can be utilized efficiently as useful product.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of waterless-odorless fertilizer collection tool.
NOVELTY - Ecological organic fertilizer, comprises (in parts weight): organic fertilizer (30-40), urea (30-40), humic acid (10-15), straw ash (15-25), attapulgite (8-12), nanometer calcium carbonate powder (3-8), trace element fertilizer (0.3-0.5) and biological potassium fertilizer (2-5).    USE - Ecological organic fertilizer.    ADVANTAGE - The ecological organic fertilizer provides lodging resistance, disease resistance and drought resistance to the crop, has simple preparation method, improves absorption rate of the crop, and reduces damage to soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the above-cited ecological organic fertilizer, which involves (a) weighing raw materials, and adding the organic fertilizer, urea, straw ash and attapulgite to a stirring machine to mix, (b) adding the humic acid, nanometer calcium carbonate powder, trace element fertilizer and biological potassium fertilizer, uniformly mixing, regulating the moisture content of the mixed material to 45-50% and the acid-base degree to 5.0-6.5, (c) primarily fermenting the mixed material from the step (b) for 4-6 days, and controlling the fermentation temperature to 45-55 degrees C, and (d) stirring the solution of the step (c), then fermenting at second time for 9-11 days, controlling the fermentation temperature to 55-65 degrees C, and finally prilling to obtain the ecological organic fertilizer.
NOVELTY - Synthesizing 2-ethyoxycarbonyl aminosulfonyl-N,N-dimethylnicotinamide comprises: (i) adding 2-aminosulfonyl-N,N-dimethylnicotinamide into acetone aqueous solution; adding ethyl chloroformate and liquid caustic soda into the solution of step (i); (iii) maintaining the temperature for 2-5 hours after dripping; (iv) sampling and detecting; (v) distilling and recycling acetone, then regulating the pH to less than 7 with acid;(vi) filtering, separating and drying to obtain the product.    USE - The method is useful for synthesizing 2-ethyoxycarbonyl aminosulfonyl-N,N-dimethylnicotinamide.    ADVANTAGE - The method: saves energy, and protects environment without generating any pollutants e.g. carbon dioxide or waste saline; and yields high product.    DETAILED DESCRIPTION - Synthesizing 2-ethyoxycarbonyl aminosulfonyl-N,N-dimethylnicotinamide comprises: (i) adding 2-aminosulfonyl-N,N-dimethylnicotinamide into acetone aqueous solution; (ii) regulating the temperature in the reactor at 5-20 degrees C, adding ethyl chloroformate and liquid caustic soda into the solution of step (i) while stirring, where the molar ratio of 2-aminosulfonyl-N,N-dimethylnicotinamide to ethyl chloroformate is 1:1.2-2; (iii) maintaining the temperature for 2-5 hours after dripping; (iv) sampling and detecting, ending reaction when the content of 2-aminosulfonyl-N,Ndimethylnicotinamide in the reaction solution is not greater than 0.1%; (v) distilling and recycling acetone, then regulating the pH to less than 7 with acid;(vi) filtering, separating and drying to obtain the product.
NOVELTY - Eco-friendly reproducible fuel oil active ingredient is biological oil, is claimed.    USE - The biological oil is useful for industrial boiler, industrial furnace and in restaurants for burning stoves.    ADVANTAGE - The biological oil is eco-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the eco-friendly reproducible fuel oil, comprising (i) uniformly mixing the filtered biological oil and acetone to obtain component A; (ii) uniformly mixing the crude methanol and coal tar to obtain component B; (iii) uniformly mixing the component A and component B to obtain component C; and (iv) uniformly stirring the component C with ferrocene, sodium hydroxide and camphor powder to obtain product.
NOVELTY - A biodiesel is prepared by mixing cane residue with sunflower seed scrap at mass ratio of 50:10-50:90, preferably 50:30; adding phosphate buffer solution until humidity is 70-80, preferably 75%; mixing residue, sunflower seed scrap and buffer solution; sterilizing in high pressure boiler, and cooling to obtain fermentation culture medium; adding lipase microbe to culture medium to obtain solid fermentation product containing lipase; freeze drying fermentation product to degrease; and taking dried and degreased solid product as catalyst to prepare biodiesel.    USE - Method for the preparation of biodiesel (claimed).    ADVANTAGE - The method has simple preparation process, low cost and recycles the wastes and does not have pollution. It shows that the solid fermentation product has good catalysis activity and stability, and has more than 86% biodiesel converting rate and 60% of original enzyme activity after being used for three times.
NOVELTY - The device has the metal rod that receives electric energy and sends electric energy to two sealed containers holding water through the anode and cathode of the lead. The oxygen and hydrogen are generated in the sealed containers and provided to the oxygen storage tank and the hydrogen storage tank.    USE - Lightning electric energy absorption-conversion-utilization device.    ADVANTAGE - The device structure can be simplified. The device cost can be reduced. The huge energy can be generated instantly during lightning.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the lightning electric energy absorption-conversion-utilization device. (Drawing includes non-English language text)
NOVELTY - Compound fertilizer comprises (in parts weight): residue (8-10) and mixed fertilizer (3000-4000).    USE - As fertilizer.    ADVANTAGE - The fertilizer contains nitrogen and microelements such as zinc and copper. The fertilizer is released at a sustained rate, and silica gel and active carbon powder particles in the fertilizer improves soil fertility and improves drought resistance. The fertilizer is prepared using melamine waste residues, and thus the method prevents environmental pollution caused by the waste residues.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing the compound fertilizer, which involves (a) reacting (in parts weight): residue (8-10), 35% formaldehyde (2-3) and water (90-100) at 75 degrees C for more than 30 minutes to obtain adhesive slurry (2%), and regulating pH of the solution to 8-8.5 using sodium hydroxide solution, and (b) introducing the slurry through a mortar pump into a injector of a mixed fertilizer, controlling the flow of the slurry in the injector, and spraying the slurry on the surface of the fertilizer to obtain compound fertilizer in the form of granules, where the amount to slurry injected is 30-35 kg/ton of fertilizer.
NOVELTY - A 2-halogenated-5-trifluoromethyl benzyl alcohol compound is prepared by reacting 4-halogenated benzotrifluoride with paraformaldehyde and chlorinating agent to chloromethylation to obtain 2-5-trifluoromethyl-benzyl; providing organic acid and performing esterification reaction under acid-binding agent and the presence of solvent to obtain 2-5-trifluoromethyl-benzyl organic acid; and hydrolyzing with acidic or alkaline solution to obtain the benzyl alcohol compound.    USE - Method for the preparation 2-halogenated-5-trifluoromethyl benzyl alcohol compound (claimed) useful as cholesterol lowering medicine cholesterol ester transfer protein inhibitors intermediate.    ADVANTAGE - The method provides low cost raw material, has good environmental protection and energy saving, process is simple and easy to realize industrialization, and high recycling rate, high purity, stable quality, and completely meets the use requirement of pharmaceutical intermediate.    DETAILED DESCRIPTION - Preparation of 2-halogenated-5-trifluoromethyl benzyl alcohol compound of formula (I) comprises:    (A) reacting 4-halogenated benzotrifluoride of formula (II) with paraformaldehyde and chlorinating agent to chloromethylation to obtain 2-5-trifluoromethyl-benzyl of formula (III);    (B) providing organic acid and performing esterification reaction under acid-binding agent and the presence of solvent to obtain 2-5-trifluoromethyl-benzyl organic acid of formula (IV); and    (C) hydrolyzing with acidic or alkaline solution to obtain compound (I)    The chlorinating agent is hydrogen chloride, chlorosulfonic acid, chloromethylether, bis-methyl ether, chloromethyl ether, chloromethyl silane or methoxyl acetyl chloride. The organic acid is organic acid alkali metal salt of acid-binding agent in formic acid, acetic acid, propionic acid, butyric acid, alkali metal carbonate, triethylamine, pyridine or tributylamine.    X=F, Cl, Br or I; and    R1=H or 1-3C alkyl.
NOVELTY - The apparatus has condenser (1) for condensing livestock excretions gas. The advanced oxidation process (AOP) mine stoker (2) removes the bad smell of the organic compound component of the livestock excretions gas which is not condensed in condenser. An acidity water cleaning station (3) neutralizes the alkaline bad smell material of livestock excretions gas which is not fired from AOP mine stoker, using hypochlorous acid water. An alkaline water cleaning station (4) neutralizes acidity bad smell material of gas which is not fired from acidity water cleaning station.    USE - Livestock excretions removing apparatus used in livestock industry.    ADVANTAGE - The livestock excretions can be processed after photooxidation process for fuel recycling process. The bad smell can be removed with low cost structure.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for livestock excretions removing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of livestock excretions removing apparatus. (Drawing includes non-English language text)    Condenser (1)    AOP mine stoker (2)    Acidity water cleaning station (3)    Alkaline water cleaning station (4)
NOVELTY - Method for treating food waste, involves heating the waste in a heating tank containing wood chips and microorganism, spraying hot water at 50-60 degrees C periodically into the heating tank, stirring the components, subjecting the food waste to decomposition process using microorganism by sealing the tank with cover for 5 hours, spraying hot water to the product through upper nozzle and stirring the waster for 40 seconds-4 minutes, subjecting the waste to aerobic degradation process by culturing the microorganism, and discharging the waste from the tank.    USE - The method is useful for treating food waste.    ADVANTAGE - The method is economical, environmentally-friendly, convenient to perform, rapid, performed under optimal condition, and stable, and maximizes self purification of food waste.    DETAILED DESCRIPTION - Method for treating food waste, involves heating the waste in a heating tank containing wood chips having particle size of 4-8 mm and microorganism at 35-65 degrees C, spraying hot water at 50-60 degrees C periodically into the heating tank, stirring and mixing the components using stirring unit for 8-12 hours, subjecting the food waste to decomposition process using microorganism by sealing the tank with cover for 5 hours, spraying hot water to the product through upper nozzle and stirring the waster for 40 seconds-4 minutes, stirring the decomposed waste for 5-10 minutes, subjecting the waste to aerobic degradation process by culturing the microorganism aerobically, and discharging the waste from the tank after degradation.
NOVELTY - A kitchen garbage anaerobic digestion of hydrogen is improved by removing impurity from the kitchen waste by sorting, crushing, and mixing. The active sludge is marsh gas production system by adding water to dilute to obtain active sludge. The active sludge suspension processed kitchen garbage in volatile solid and active mud solution of volatile solid is 1.9-4.2:1:3. Ammonium chloride is added to the mixture to control the concentration of ammonia nitrogen to 1-4.5 g/liter. After mixing in a closed anaerobic digestion system, the mixture is fermented at 35 plus minus 2 degrees C for manufacturing hydrogen.    USE - Method for improving kitchen garbage anaerobic digestion of hydrogen (claimed).    ADVANTAGE - The method inhibits methane production bacteria and promotes production of hydrogen bacteria to improve the hydrogen yield.
NOVELTY - The system has frame that is hinged in side of the main portion. The combining element fixes the main portion on the process bath wall. The location of the portion is controlled by control unit according to the location of the process bath wall. The engaging element is connected to the rear side of the main portion. The other engaging element is connected to the process bath wall. The intervening element is connected to the combining elements. The combining elements and intervening element are connected and fixed by fastening element.    USE - Odorless treatment system for sewage.    ADVANTAGE - The smell generated in the livestock industry is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows the block flow diagram of the odorless treatment system for sewage.(Drawing includes non-English language text)
NOVELTY - Biological organic fertilizer comprises (in %): bamboo shoot waste (65-70), livestock excrement (30-35), and fermenting microorganisms (2.8-3.2).    USE - Biological organic fertilizer.    ADVANTAGE - The biological organic fertilizer is cost-effective, can be prepared simply, rapidly and cost-effectively using bamboo shoot waste and livestock excrement, and has strong applicability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the above-cited biological organic fertilizer, which involves uniformly mixing bamboo shoot processed waste with livestock excrement, adding calcium superphosphate to the mixture, adjusting pH of the mixture to 7-8, fermenting the mixture at 40-50 degrees C for 4-6 days, and secondarily fermenting the product at 50-60 degrees C for 9-11 days.
NOVELTY - The device has an electrolytic cell that includes electrolysis electrodes in an electrolytic bath. The electrolysis electrode is provided on the outside of the electrolytic bath. The electrolysis electrode is set on one side of electric field cathode. The electrolysis electrode is close to one side of an electric field anode. The pump and valve are provided on a circulating pipeline of electrolyte. The electrolysis electrode is provided with through hole connected with an external circulating pipeline of an electrolytic tank.    USE - Electrolytic hydrogen producing device.    ADVANTAGE - The hydrogen producing rate can be effectively improved. The power consumption for the device can be reduced. The device is convenient to install, and the environment can be protected without pollution. The hydrogen for hydrogenation station can be ensured. The required energy sources can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the electrolytic hydrogen producing device.
NOVELTY - The system has a water inlet pipe which is connected with a main tank (1). A lower portion is provided through a water supply pipe (4). The water supply pipe is connected with a planting box (7) and planting pipe. One end of lower portion is connected with planting box while other end is planting pipe through a water supply pipe and fermentation cylinder (9). A water storage barrel (10) is connected through a water pump (12). The water supply pipe is connected with the main tank.    USE - Roof planting system for agricultural land.    ADVANTAGE - The urban organic waste can be processed easily by roof planting system to improve the environment.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the roof planting system for agricultural land.    Main tank (1)    Water supply pipe (4)    Planting box (7)    Fermentation cylinder (9)    Water storage barrel (10)    Water pump (12)
NOVELTY - The reformer has a microwave generator magnetron (1020) that is transmitted to the liquid fuel and water for a liquid coolant (1006) through a heat exchanger (1007). The liquid fuel and water is entered into an evaporator (1008) for forming steam enters into a microwave resonant cavity (1018). The microwave resonant cavity is connected with a spark ignition device (1017). The chemical materials of reformer chamber are excited by spark ignition device controller. The spark ignition device controller is configured to control on and off operation of the spark ignition device.    USE - Microwave low temperature plasma reformer for production of hydrogen for vehicle.    ADVANTAGE - The chemical pollution of the microwave cavity can be reduced. The reformer is featured with simple structure can be achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the low temperature plasma reformer.    Liquid coolant (1006)    Heat exchanger (1007)    Evaporator (1008)    Spark ignition device (1017)    Microwave resonant cavity (1018)    Microwave generator magnetron (1020)
NOVELTY - The cover structure has sprockets (4,5) that are mounted on the rotary shafts (2,3). The semicircular-shaped structures (12,12') are fixed to the anchoring bolt. A bearing ingression main portion and retainer ingression main portion are installed in the side portion of bearing structure. A circular plate is inserted into screw hole formed in a shape cover structure (26). A round kiln portion is positioned in the inner portion of the semicircular shaped cover (22). The anchoring bolt is fixed with a retainer ingression main portion.    USE - Bearing cover structure for compost mixer.    ADVANTAGE - The maintenance cost of the compost mixer is reduced. The time and labor required for disassembling the bearing cover structure are reduced. The corrosion of the bearing cover structure is prevented. The damage caused to the bearing cover structure is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of bearing cover structure.    Rotary shaft (2,3)    Sprocket (4,5)    Semicircular-shaped structure (12,12')    Semicircular shaped cover (22)    Shape cover structure (26)
NOVELTY - Preparing microbiological feed, involves (a) culturing Bacillus subtilis, yeast and lactic acid Bacillus (1-8) in inclined surface containing peptone, and generating seed culture solution, (b) performing double-screw extrusion technology to the culture solution, and processing fresh rice bran, (c) inoculating the seed culture solution to the sterilized rice bran, and performing solid fermentation, (d) obtaining fermented rice bran, and drying and crushing the rice bran, and (e) mixing rice bran powder and protein feed to obtain the feed.    USE - The method is useful for preparing microbiological feed which is used for improving function of gastrointestinal tract and immunity of animal, preferably livestock and poultry animals.    ADVANTAGE - The feed is harmless and pollution-free.    DETAILED DESCRIPTION - Method for preparing microbiological feed, involves (a) culturing (in parts weight) Bacillus subtilis (1-8), yeast (1-6) and lactic acid Bacillus (1-8) in inclined surface containing peptone at 30-40 degrees C for 2-4 days, and generating seed culture solution, (b) performing double-screw extrusion technology to the culture solution at 125-145 degrees C and 0.5-0.7 kPa for 10-20 seconds, and processing fresh rice bran using microwave sterilization technology for sterilizing rice bran, (c) inoculating the seed culture solution to the sterilized rice bran at 25 degrees C, and performing solid fermentation for 5-7 days, (d) obtaining fermented rice bran, and drying and crushing the rice bran to obtain powder, and (e) mixing rice bran powder and protein feed in the mass ratio of 1:4-6 to obtain the feed, where the protein feed comprises corn, bean pulp or their mixture.
NOVELTY - The apparatus has a rotation power shaft (2) which applies rotation power to agitating blade (3). An oxygen supply pipe (14) is connected to air blower (P). Multiple injection nozzles (151) are installed in bottom surface of oxygen discharge tube (15). A load sensor (42) is mounted in lower surface of fermentation storage tank. A gas exhaust unit (7) exhausts toxic gas generated in fermentation storage tank (1) to the outside. A drive motor (M) is equipped in the elastic support frame (4).    USE - Compost fermentation tank apparatus.    ADVANTAGE - The fertilizer raw material (waste) coherence can be prevented effectively. The occurrence of damage to the agitating blade can be prevented. The fermentation temperature maintenance function, the deodorization function, the load sensing function of the compost fermentation tank can be enhanced.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the compost fermentation tank apparatus.(Drawing includes non-English language text)    Fermentation storage tank (1)    Rotation power shaft (2)    Agitating blade (3)    Elastic support frame (4)    Gas exhaust unit (7)    Oxygen supply pipe (14)    Oxygen discharge tube (15)    Load sensor (42)    Injection nozzles (151)    Drive motor (M)    Air blower (P)
NOVELTY - A sludge organic fertilizer is prepared by adjusting water content to 55-65%, carbon/nitrogen value to 27-33, and carbon composition to 35-45%. Sludge is added into a fermentation device, subjected to fermentation composting and fermented for 65-75 hours at 52-57 degrees C, where pH value of the sludge is 9-11. The sludge is again subjected to fermentation composting and fermented for 55-75 hours at 58-63 degrees C to obtain sludge organic fertilizer, where pH value of the sludge is 7-9.    USE - Sludge organic fertilizer for use in red soil texture.    ADVANTAGE - The fertilizer is suitable for slightly acidic soil, and ensures growth of pitaya on red loam soil.
NOVELTY - An enteromorpha aerobic composting method involves spreading enteromorpha on enteromorpha stacking field upto 20-30 cm thickness, and supplying water (40-60% of weight of enteromorpha). Doping sand (10-40% of weight of enteromorpha) is added to the enteromorpha and stirred uniformly, and aerobic fermentation is performed. The fermented material is passed into a device containing oxidizing agent, where content of oxidizing agent is more than 10%. The resultant product is stacked for 15-25 days.    USE - Method for aerobic composting of enteromorpha for use as organic fertilizer.    ADVANTAGE - The method enables aerobic composting of enteromorpha in an eco-friendly manner.    DETAILED DESCRIPTION - An INDIPENDENT CLAIM is also included for a system for aerobic compost processing of enteromorpha for use as organic fertilizer.
NOVELTY - An organic fertilizer preparing method involves filtering waste slag by using a 2-10 cm mesh screen. Auxiliary material is added to the filtered waste slag to prepare a culture medium, where the auxiliary material is feather powder, meal powder, sawdust and straw powder. A housefly ovum is inoculated on a surface of the culture medium. The culture medium is cultured for 4-5 days at temperature of 25-35 degrees C. The culture material is collected, dried and prepared into the organic fertilizer.    USE - Method for preparing an organic fertilizer by using housefly to process human excrement.    ADVANTAGE - The method enables preparing the organic fertilizer with strong processing ability and low energy consumption using small area, obtaining fly maggot biological protein, realizing resource utilization of waste residue, changing waste into valuable product, and ensuring environment-friendly effect.
NOVELTY - A biological organic fertilizer comprises (in weight parts) lime powder (60-70), ferrous sulfate (13-20), magnesium sulfate (5-8), corn straw powder (10-15), biological organic fertilizer fermenting strain agent (15-25), organic matter-decomposing inoculant (0.2-0.6), lysine (0.2-0.6), defatted rice bran powder (0.1-0.3), bone powder (15-25), ammonium nitrate (12-18) and organic activating agent (0.01-0.03).    USE - Biological organic fertilizer for producing municipal sludge in urban residents, office and school.    ADVANTAGE - The fertilizer enables production of the municipal sludge at low cost with better producing effect and avoids the environmental pollution.
NOVELTY - An organic fertilizer comprises (in weight parts) manure (6.5-8) and crop waste (1).    USE - Organic fertilizer.    ADVANTAGE - The agricultural waste is easy to treat, and prevents environmental pollution. The prepared organic fertilizer has rich organic nutrient, nitrogen, phosphorus, potassium content, fast crops absorbing process and small dosage. The fertilizer can be easily prepared without occupying much human resource, thus saving cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing an organic fertilizer.
NOVELTY - A urea processing water cycling system has first circulating cooler (1), second circulating cooler (2) and ammonium carbonate solution tank (4), where the two circulating coolers are connected to a sucking tower (3) through a pipeline, and are further connected to a liquid inlet of the ammonium solution tank.    USE - Urea processing water cycling system.    ADVANTAGE - The urea processing water cycling system has high recycling rate, and is inexpensive.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a urea processing water cycling system.    Circulating coolers (1, 2)    Sucking tower (3)    Ammonium carbonate solution tank (4)
NOVELTY - A waste alkali liquid humic acid salt preparation method involves collecting alkali or salt water from soluble alkali-containing waste water, cooling and drying to obtain alkali concentration of 18-22 percentage. The alkali is added with coal powder in a ratio of 1:8-10, where the coal powder is prepared by smashing a weathered coal or lignite or peat coal into a smashing machine and crushed into a particle size of 0.2-0.5mm. The mixture is stirred and heated at 89-91 degrees C for 1-1.5 hours in a reaction kettle to obtain a precipitate and clear liquid.    USE - Method for preparing waste alkali liquid humic acid salt during waste water recycling process.    ADVANTAGE - The method enables preparing waste alkali liquid humic acid salt in a simple, economical and eco-friendly manner.    DETAILED DESCRIPTION - A waste alkali liquid humic acid salt preparation method involves collecting an alkali or salt water from soluble alkali-containing waste water, cooling and drying to obtain alkali concentration of 18-22 percentage. The alkali is added with a coal powder in a ratio of 1:8-10, where the coal powder is prepared by smashing a weathered coal or lignite or peat coal into a smashing machine and crushed into a particle size of 0.2-0.5mm. The mixture is stirred and heated at 89-91 degrees C for 1-1.5 hours in a reaction kettle to obtain a precipitate and a clear liquid. The clear liquid is mixed uniformly with hydrochloric acid solution and cooled to pH of 2. The mixture is allowed to stand for 8-12 hours to deposit a supernatant precipitate and dried to obtain an end product, where the precipitate and a raw materials of humic acid are mixed uniformly, allowed to stand for 2-3 hours in the ratio of 1: 0.5-0.8 and followed by pressing the mixture to form granules, which is utilized as a fertilizer.
NOVELTY - A straw biogas residue nutrition preparation method involves discharging residue and transferring to marsh gas pool, drying and crushing the residue. Potassium dichromate is added to residue for nutrient determination, and organic matter content in slag is distilled and measured to find the nitrogen content. Potassium, iron, manganese and boron are measured by flame atomic absorption spectrophotometry. Nutrient is added to plant seedling, and adhesive and press forming mold are added. The seedling is dipped in water and covered with soil. The seedling is planted and tested for plant growth.    USE - Method for preparing straw biogas residue nutrition.    DETAILED DESCRIPTION - A straw biogas residue nutrition preparation method involves discharging the straw biogas residue without adding new reaction material and transferring to marsh gas pool, and drying and crushing the straw biogas residue. Potassium dichromate is added for nutrient determination, organic matter content in slag is distilled and measured to find out the nitrogen content and sodium hydroxide. Sodium bicarbonate extracting molybdenum-antimony anticolorimetry measures efficient phosphorus content, soil quick-acting potassium, microelement iron, manganese, copper and boron are measured by flame atomic absorption spectrophotometry. Nutrient is added to the plant seedling, adhesive and certain proportion of press forming mold are added. The seedling is dipped in water and kept constant for 6 hours by covering hydrophobic soil. Water supply is stopped before 3-4 days of plantation, and seedling is planted and tested for plant growth.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a method for preparing straw biogas residue nutrition.'(Drawing includes non-English language text)'
NOVELTY - Use of acesulfame potassium (AK) sugar crystal mother liquor for producing potassium salt, is claimed.    USE - The AK sugar crystal mother liquor is useful for preparing potassium salt.    ADVANTAGE - The AK sugar crystal is capable of economically and easily producing potassium salt in an environmental friendly manner with high yield and quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing potassium salt using AK sugar crystal mother liquor comprising mixing the acidic solution, cooling, filtering, and re-crystallizing.
NOVELTY - An optical homochiral 2-chloromandelic acid preparing method involves adding a chiral resolving agent, 2-chloromandelic acid and a metal compound to a solvent, heating to dissolve, stirring to cool, filtering after separating the solid out, drying, and collecting the solid. The solid is re-crystallized, pH is regulated by acid solution, and the re-crystallized solid is filtered to recover insoluble substance. Mother liquid by the organic solvent is extracted and dried in spinning manner to obtain the optical homochiral 2chloromandelic acid.    USE - Method for preparing optical homochiral 2-chloromandelic acid in an industry.    ADVANTAGE - The method enables preparing optical homochiral 2-chloromandelic acid with easy availability of raw material and non-toxin resolving agent, low preparation cost and environment-friendly effect.    DETAILED DESCRIPTION - An optical homochiral 2-chloromandelic acid preparing method involves adding a chiral resolving agent, 2-chloromandelic acid and a metal compound to a solvent, heating to dissolve, stirring to cool, filtering after separating the solid out, drying, and collecting the solid, where mol ratio of the chiral resolving agent to the 2-chloromandelic acid is 1:4-2:1, and the mol ratio of a metal ion in the metal compound to the 2-chloromandelic acid is 1:4-2:1. The solid is re-crystallized, pH is regulated to 1-2 by acid solution, and the re-crystallized solid is filtered to recover insoluble substance. Mother liquid by the organic solvent is extracted and dried in spinning manner to obtain the optical homochiral 2chloromandelic acid.
NOVELTY - A nutrition fertilizer is prepared by crushing crop straw, mixing with rabbit manure and mushroom residue, adding urea by adjusting the carbon-nitrogen ratio to 1:20-1:40, stacking and fermenting in a fermentation tank. The fermented product is mixed with monopotassium phosphate, potassium sulfate, zinc sulfate, sodium molybdate, manganese sulfate and ammonia nitrate, tobacco is crushed to 1 cm sections, and coal residue, paclobutrazol, gibberellin and bentonite are added to the mixture, mixed, cooled, dried and granulated to obtain the final mixture.    USE - Nutrition fertilizer for lettuce.    ADVANTAGE - The fertilizer can efficiently prevent sclerotinia and botrytis infection in a lettuce growth process, and improves the quality of the lettuce.    DETAILED DESCRIPTION - A nutrition fertilizer is prepared by crushing (in weight parts) crop straw (11-20), mixing with rabbit manure (30-50) and mushroom residue (15-20), adding the urea (20-25) by adjusting the carbon-nitrogen ratio to 1:20-1:40, stacking and fermenting in a fermentation tank. The moisture of the mixture is 66-70%, fermented at 45 degrees C, stack is mixed at every 3 hours for 18 hours. The fermented product is mixed with monopotassium phosphate (2-5), potassium sulfate, zinc sulfate (3-5), sodium molybdate (1-4), manganese sulfate (2-6) and ammonia nitrate (5-7) for 30 minutes, tobacco (7-10) is crushed to 1 cm sections, and coal residue (5-10), paclobutrazol (2-5), gibberellin (4-7) and bentonite (4) are added to the mixture, mixed for 1-2 hours, cooled, dried and granulated to obtain the final mixture.
NOVELTY - Production of close type anaerobic livestock excrement compost using organic materials including livestock excrement, involves (a) mixing the organic materials with a water control material, (b) conglomerating the mixed organic material in a bale (B) shape, (c) covering and closing the bale (B)-shaped organic materials by vinyl, and (d) installing unit for discharging gas from the inside of the covered bale (P).    USE - Production of close type anaerobic livestock excrement compost.    ADVANTAGE - The method reduces generation of odor and combustion gas, and is cost-effective.
NOVELTY - A three-dimensional fiber/carbon nanotube-reinforced body has carbon nano-tubes (CNTs) with nano-enhancing phase and formed by chemical vapor infiltration (CVI) process in a three-dimensional fiber prefabricate body to obtain a multi-level reinforcing body.    USE - Three-dimensional fiber/carbon nanotube-reinforced body.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing a multi-level reinforcement.
NOVELTY - The method involves preparing substrate for bio-gas production. The anaerobes or reaction solutions containing anaerobes are injected to the substrate. The substrate is cultured under the anaerobic condition at 20-50 degrees C to prepare hydrogen gas or methane gas.    USE - Method for producing bio-gas, using jellyfish such as Nemopilema nomurai, full moon jellyfish, and ghost jellyfish (all claimed).    ADVANTAGE - Since the substrate is cultured under the anaerobic condition at 20-50 degrees C to prepare hydrogen gas or methane gas, the bio-gas can be prepared effectively without consuming more cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical representation illustrating the reaction of bio-gas.
NOVELTY - A ibuprofen intermediate p-isobutyl benzyl ethanol preparation method involves mixing p-isobutyl acetophenone, alcohol comprising 1-7C fatty alcohol or 3-7C alicyclic alcohol, and magnesium oxide, reacting resultant mixture at 50-160 degrees C for 1-24 hours under normal pressure, to obtain p-isobutyl benzyl ethanol. A weight ratio of the p-isobutyl acetophenone to alcohol is 1:1-50. The magnesium oxide catalyst is composed of activated carbon as carrier and magnesium oxide as active component. The loading amount of magnesium oxide is 1-20 wt.% of carrier.    USE - Method for preparing ibuprofen intermediate p-isobutyl benzyl ethanol.    ADVANTAGE - The method enables preparing ibuprofen intermediate p-isobutyl benzyl ethanol in a simple and eco-friendly manner.
NOVELTY - A columbianetin extraction method involves crushing radix peucedani and adding carbon dioxide and ethyl acetate as entrainer for supercritical extraction, where total mass of the entrainer is 1-3%, extracting pressure is 10-30MPa, and temperature is 40-50 degrees C. Ethyl acetate solution is added for 4-8 stages of countercurrent extraction as an extracting agent. The extracting solution is combined. The solvent is decompressed, recycled and concentrated. Absolute ethyl alcohol crystal is added, separated, crystallized, washed and dried to obtain a product.    USE - Method for extracting columbianetin.    ADVANTAGE - The method enables extracting columbianetin in a simple manner with less pollution, low energy consumption and high product purity.    DETAILED DESCRIPTION - A columbianetin extraction method involves crushing radix peucedani and adding carbon dioxide and ethyl acetate as entrainer for supercritical extraction, where total mass of the entrainer is 1-3%, extracting pressure is 10-30MPa, temperature is 40-50 degrees C, carbon dioxide flow rate is 3 ml/g, and extracting time is 120-180 minutes. Ethyl acetate solution is added for 4-8 stages of countercurrent extraction as an extracting agent. The extracting solution is combined. The solvent is decompressed, recycled and concentrated. Absolute ethyl alcohol crystal is added, separated, crystallized, washed and dried to obtain a product.
NOVELTY - A film treatment system has a mixing device for mixing crushed soybean with water to obtain an extract. A water outlet end of an acid leaching tank is linked with a water inlet end of a micro-filter membrane system by a pipeline. A water outlet end of an ultra-filtration membrane system is provided with a penetrating fluid pipeline, and a nanofiltration membrane system is fixed with a water inlet end of a concentrated solution pipe. The concentrated solution pipe provided in a water outlet end of nanofiltration membrane system is fixed to a low temperature treatment device to prepare levodopa.    USE - Film treatment system for preparing levodopa.    ADVANTAGE - The system can prepare the levodopa with high yield and purity, in an environment-friendly manner.    DETAILED DESCRIPTION - A film treatment system has a mixing device for mixing crushed soybean with water to obtain an extract. A water outlet end of an acid leaching tank is connected with a water inlet end of a micro-filter membrane system by a pipeline. The micro-filtration membrane system is connected via an inlet end of an ultra-filtration membrane system. A water outlet end of the ultra-filtration membrane system is provided with a penetrating fluid pipeline, and a nanofiltration membrane system is connected with the water inlet end of a concentrated solution pipe. The concentrated solution pipe provided in a water outlet end of nanofiltration membrane system is connected to a low temperature treatment device to prepare levodopa.
NOVELTY - A biological cold fermentation straw recovery agent comprises (in weight parts) straw fast corrosion agent (2-8), dodecyl sodium sulfate (2-8), dispersing anthraquinone (15-25) and calcium oxide (60-80).    USE - Biological cold fermentation straw recovery agent for producing vegetable fiber.    ADVANTAGE - The agent avoids waste liquid discharge, is inexpensive, and has quick utilization effect and high product performance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for producing vegetable fiber using biological cold fermentation straw recovery agent.
NOVELTY - Method for producing bio-organic fertilizer using water gourd juice and fermentation device, involves (a) crushing the water gourd to obtain juice, (b) adding (in parts weight): the juice (100), sugar (1-5), and molasses (2-10) to the fermenting device, and performing ozone sterilization, (c) adding microbial inoculum comprising anaerobic and facultative microorganisms (1-3) to the fermentation device, fermenting for 72 hours, (d) adding the juice (0.10%) for the production of viable biological agents ( greater than or equal to 20 million/ml).    USE - The method and fermentation device are useful for producing bio-organic fertilizer preferably biological agents (all claimed). The biological agents are probiotics composition.    ADVANTAGE - The method enables effective utilization of the waste water gourd juice, hence secondary pollution is reduced. The fermentation device enables effective utilization of solar energy, hence energy consumption and production cost are reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fermentation device for producing the biological agent, which has fermenting tank (1) on opening of lid (2) hinged with rear portion of the fermenting tank provided with sterilizing device, circulation device, light transmission device (5) installed outside the lid, and heating control unit (6).    DESCRIPTION OF DRAWING(S) - The drawing shows schematic representation of fermentation device used for producing bio-organic fertilizer.    Fermentation tank (1)    Lid (2)    Light transmission device (5)    Heating control unit (6)
NOVELTY - Method for extracting potato based on magnetic beads and deeply processing nucleic acid, involves (a) adding lysis buffer to sample and collecting supernatant, (b) adding binding buffer and silicon dioxide to the obtained supernatant, where nucleic acid is capable of forming compound with magnetic bead and washing residual impurity using 70% washing solution, and (c) adding the obtained nucleic acid complex to tris(hydroxymethyl)aminomethane EDTA (TE) solution.    USE - The method is useful for extracting potato based on magnetic beads and deeply processing nucleic acid.    ADVANTAGE - The method is simple and environmentally-friendly, and enables extraction of potato based on magnetic beads and deeply processed nucleic acid with high purity.
NOVELTY - Purifying butane by rectifying method, comprises hydrogenating 4C hydrocarbon, completely hydrogenating olefin and diolefin to obtain butane and isobutane, and separating the two obtained products by rectifying process to obtain high purity butane, where the molar ratio of 4C hydrocarbon and hydrogen is 1:0.5-5.    USE - The method is useful for purifying butane by rectifying method.    ADVANTAGE - The method is simple and convenient to produce butane.
NOVELTY - Method for cultivating and producing edible mushroom, involves using soy residue, mushroom inoculant and cotton as essential raw materials.    USE - The method is useful for cultivating and producing edible mushroom which is used as feed additive or organic fertilizer and in poultry (claimed).    ADVANTAGE - The soy residue can be recovered and reused for several times. The method is environmentally-friendly, shortens breeding period, and enables production of hypha with uniform growth and high nutritious value. The mushroom contains active polysaccharide and crude fiber.
NOVELTY - The device has conveying pump (1), feeding valve (2), flash evaporation tower (3), cup (4), discharging check valve (5), methanol condenser (6) and vacuum device, in which flash evaporation tower is provided with multi-layer tower distribution disc (32) and tower plate (33). The outlet of conveying pump is connected with the feeding valve through pipeline. A flash tower top low-boiling outlet (31) is connected with methanol condenser through cup. A flash tower bottom discharging outlet (34) is connected with the discharging check valve through pipeline.    USE - Bio-diesel oil methyl estered dealcoholization device.    ADVANTAGE - The methanol in the bio-diesel oil is removed through fatty acid methyl ester, without influencing the dissolving of glycerol and depositing of soap. The bio-diesel oil can be dealcoholized rapidly and efficiently through bio-diesel oil methyl estered dealcoholization device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the bio-diesel oil methyl estered dealcoholization device.    Conveying pump (1)    Feeding valve (2)    Flash evaporation tower (3)    Cup (4)    Discharging check valve (5)    Methanol condenser (6)    Flash tower top low-boiling outlet (31)    Multi-layer tower distribution disc (32)    Tower plate (33)    Flash tower bottom discharging outlet (34)
NOVELTY - A 3-substituted phenyl-5-hydroxymethyl oxazolidine-2-ketone compound (I) preparing method involves condensing substituted aniline compound (II) with epihydric alcohol, to obtain (R)-(+)-3-substituted phenylamino-1,2-propylene glycol. The obtained (R)-(+)-3-substituted phenylamino-1,2-propylene glycol is reacted with 3-phenylamino-propane-1,2-diol compound (III) and carbonyl compound.    USE - Method for preparing 3-substituted phenyl-5-hydroxymethyl oxazolidine-2-ketone compound.    ADVANTAGE - The method enables preparing 3-substituted phenyl-5-hydroxymethyl oxazolidine-2-ketone compound with simple process at mild reaction condition, improved production energy consumption and safe production coefficient and reduced production cost. The method enables preparing 3-substituted phenyl-5-hydroxymethyl oxazolidine-2-ketone compound in an environment-friendly manner.    DETAILED DESCRIPTION - A 3-substituted phenyl-5-hydroxymethyl oxazolidine-2-ketone compound of formula (I) preparing method involves condensing substituted aniline compound of formula (II) with epihydric alcohol, to obtain (R)-(+)-3-substituted phenylamino-1,2-propylene glycol. The obtained (R)-(+)-3-substituted phenylamino-1,2-propylene glycol is reacted with 3-phenylamino-propane-1,2-diol compound of formula (III) and carbonyl compound of formula (X2-C(=O)-X3).    R1, R2=heteroaryl ring (optionally substituted), halo, piperidine group of formula (a) or 2,4,5,6-tetrahydro-pyrrolo(3,4-c)pyrazole group of formula (b);    Z1=O, S or NR4;    R4=amine protection group;    R3=1-4C alkyl, aryl ring or phenyl group of formula (c);    Z2=CH2 or N;    R5=2H-tetrazole group of formula (d) or 3H-(1,2,3)triazol-4-yl-methylamine group of formula (e).    R6=1-6C alkyl, and    R7, R8=amino protecting group.
NOVELTY - A fuel production method involves hydrolyzing lignocellulosic material to obtain liquid lignin-containing phase and solid phase of cellulosic material, and fermenting hydrolyzate from cellulosic material in presence of ethanol. Lignin in lignin-containing liquid phase is reprocessed by subjecting to catalytic pyrolysis or depolymerization.    USE - Method for producing fuel such as gasoline and diesel utilized in internal combustion engine.    ADVANTAGE - The method enables producing fuel in a simple manner    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating a method for producing fuel. '(Drawing includes non-English language text)'
NOVELTY - Organic fertilizer is obtained by (a) adjusting the water content of sludge to 55-65%, carbon/nitrogen content to 27-33% and total carbon content to 35-45%, (b) fermenting compost at first time for 65-75 hours at 50-52 degrees C and pH of 7-11, and (c) fermenting the compost at second time for 55-75 hours at 53-55 degrees C and pH of 7-9.    USE - The organic fertilizer for afforestation is useful for promoting the growth of Eucalyptus and Zoysia matrella (claimed).    ADVANTAGE - The organic fertilizer is prepared with reduced composting period of 30-40 days, at low temperature and low energy consumption and thus is cost-effective. The fertilizer enriches soil with more organic matters and maintains ecological balance.
NOVELTY - Culture substrate comprises peat, agriculture and forestry waste compost, pyrolysed agricultural and forestry wastes and bactericide.    USE - The culture substrate is useful for cultivating plants (claimed).    ADVANTAGE - The culture substrate is rich in nutrition, stable and convenient for foliage plant, and improves survival rate and ornamental effect of the plant.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the above-mentioned culture substrate, which involves uniformly mixing the above-mentioned raw materials.
NOVELTY - Preparation of ibuprofen methyl pyridine, involves dissolving ibuprofen and 2-hydroxymethylpyridine in organic solvent to obtain mixture, esterifying mixture at room temperature for 1-24 hours in presence of dehydrating agent and catalyst to obtain product, filtering the product, washing the product using 5% sodium bicarbonate solution, neutralizing the product using water, adding desiccant to product, recovering solvent from product, reducing pressure of the product and distilling product to obtain ibuprofen methyl pyridine.    USE - The method is useful for preparing ibuprofen methyl pyridine which is used in pharmaceutical composition for preventing and treating infectious disease, pain and inflammation.    ADVANTAGE - The method is environmentally-friendly, and prepares large amount of ibuprofen methyl pyridine simply, safely and cost-effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for pharmaceutical composition in the form of paste or ointment, where paste comprises (in g): ibuprofen methyl pyridine (50), albolene (95), octadecanol (85), liquid paraffin (57), sodium lauryl sulfate (10), glycerol (47), ethyl parahydroxybenzoate (1) and distilled water (655), and ointment comprises ibuprofen methyl pyridine (50), albolene (350), ethyl parahydroxybenzoate (1), stearic acid (299) and glycerin monostearate (300).
NOVELTY - Biological composite diesel oil comprises (in wt.%) diesel oil (40-80) and an emulsifier (20-60). The emulsifier comprises (in wt.%) methanol (40-55), oleic acid (35-40), ethanolamine (3-10) and cyclohexylamine (7-10).    USE - Used as a biological composite diesel oil.    ADVANTAGE - The product saves energy, protects environment, reduces corrosion and abrasion on cylinder and it is convenient for transportation and storage.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the biological composite diesel oil, comprising (i) preparing emulsifier by adding methanol, oleic acid and cyclohexylamine into a container, mixing and stirring for 30 minutes to obtain emulsifier and (ii) adding emulsifier into the diesel oil and stirring for 5-10 minutes at 45-70 degrees C.
NOVELTY - Biological composite alcohol oil emulsifier comprises (in parts by wt.): methanol (45-70), fuel grade regulator ferrocene (2-5), viscosity regulator glycerine (15-20), cosolvent zinc oxide (1-4), combustion improver soda ash (2-6) and water (10-20).    USE - Used as a biological composite alcohol oil emulsifier.    ADVANTAGE - The composition is a stable, energy saving, economical and eco-friendly composition.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) preparing the biological composite alcohol oil emulsifier, comprising: (a) adding (in parts by wt.): ferrocene (2-5) and methanol (10-15) into a container A, uniformly mixing and soaking for 4-5 days, (b) adding (in parts by wt.): zinc oxide (1-4), soda ash (2-6) and methanol (10-15) into a container B, and mixing, (c) adding (in parts by wt.): glycerine (15-20) and methanol (25-40) into a container C and stirring, (d) transferring the stirred mixture in the container C to the container A, and adding water (10-20 parts) and uniformly stirring, and (e) transferring the stirred mixture in the container B to the container A, and uniformly mixing, and    (2) preparing a biological composite alcohol oil, comprising adding (in parts by wt.): biological composite alcohol oil emulsifier (1-5), diesel oil (1-3) and water (10-25) into methanol (67-88), and uniformly mixing.
NOVELTY - The facility has ribbon shaft that is installed inside a brass rice-bowl (50) to mix livestock excretion. The heat nozzles are installed at exterior of the ribbon shaft. A microorganism fermentation unit is equipped between the brass rice-bowl and arrangement fermentation unit. A mixing unit is provided to deliver the livestock excretion to excretion storage (12) through an outer tube. A delivery section (70) delivers the fertilizer to vehicle.    USE - Fertilizing facility of livestock excretion of pig.    ADVANTAGE - The livestock excretion is fermented effectively to produce fertilizer consecutively with reduced time such that inhalation of bad smell by the operator during delivery of fertilizer is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fertilizing facility of livestock excretion.    Warehousing unit (10)    Excretion storage (12)    Preparation fermentation unit (20)    Brass rice-bowl (50)    Delivery section (70)
NOVELTY - Method of producing organic fertilizer, involves collecting and storing blood obtained from slaughter process of animals, pulverizing the blood, precipitating plasma protein, disassembling the plasma protein, inoculating Lactobacillus plantarum and Saccharomyces cerevisiae (5-15 parts weight) in the disassembled plasma protein (100 parts weight), controlling the mixture at 25-40 degrees C and pH of 6.5-8.5, fermenting the mixture at 25-40 degrees C for 48-96 hours, and blending the fermented mixture with oil meal and fish meal.    USE - The method is useful for producing organic fertilizer for improving yield of crops.    ADVANTAGE - The fertilizer prevents acidification of soil, is environmentally-friendly and rich in amino acids, and overcomes problems of existing chemical fertilizers.
NOVELTY - Method for treating various waste materials including sewage, involves extracting phosphorus and/or nitrogen from the waste using struvite, and testing the waste to determine whether the waste contains high phosphorus content relative to rate and/or nitrogen content, where the nitrogen and/or phosphorus can be fixed.    USE - The method is useful for treating various waste materials including sewage, agricultural waste, manures and restaurant wastes for producing biofuels including methane and biogas.    ADVANTAGE - The method enable to increase growth of algae including glucose fermenting algae without sunlight.
NOVELTY - A catalyst comprises central metal palladium. The central metal palladium is combined to the bivalent counter anion. The center of the auxiliary ligand is coordinated to the metal palladium. The counter anion is boron fluoride anion, antimony fluoride anion and phosphorus fluoride anion.    USE - Catalyst is used for dehydrogenating metal hydride.    ADVANTAGE - The catalyst has high efficiency, and excellent regenerative.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of hydrogen.
NOVELTY - A sodium risedronate synthesizing method involves adding pyridine derivative in presence of methanol and hydrochloric acid to obtain 2-pyridin-3-yl-acetimidic acid methyl ester, which is reacted with methanol in microwave to obtain 3-(2,2,2-trimethoxy-ethyl)-pyridine. The obtained pyridine compound is subjected to further reaction to obtain dimethyl ester derivative, which is reacted with sodium hydroxide and refluxed with water for 4 hours to obtain sodium risedronate, where the molecular formula of sodium risedronate is C7H15NNaO9.5P2, and the molecular weight is 350.12.    USE - Method for synthesizing sodium risedronate.    ADVANTAGE - The method enables preparing sodium risedronate in a simple and ecofriendly manner with high yield and without complicated reaction and special agents.    DETAILED DESCRIPTION - A sodium risedronate synthesizing method involves adding pyridin-3-yl-acetonitrile in presence of methanol and hydrochloric acid at 10 degrees C for 12 hours to obtian 2-pyridin-3-yl-acetimidic acid methyl ester. The obtained 2-pyridin-3-yl-acetimidic acid methyl ester is reacted with methanol in microwave at 100 degrees C for 3 hours to obtain 3-(2,2,2-Trimethoxy-ethyl)-pyridine. The obtained 3-(2,2,2-trimethoxy-ethyl)-pyridine is further reacted with phosphorus trichloride, added with methylbenzene and cooled to 0 degrees C, reacted for 2 hours to obtain (1-(dimethoxy-phosphoryl)-1-hydroxy-2-pyridin-3-yl-ethyl)-phosphonic acid dimethyl ester. The obtained (1-(dimethoxy-phosphoryl)-1-hydroxy-2-pyridin-3-yl-ethyl)-phosphonic acid dimethyl ester is reacted with sodium hydroxide and refluxed with water for 4 hours to obtain sodium risedronate, where the molecular formula of sodium risedronate is C7H15NNaO9.5P2, and the molecular weight is 350.12.
NOVELTY - A pressure swing adsorption and cryogenic combination method involves filling raw coal-bed methane into a pressure swing adsorption unit, and concentrating and evacuating the methane to obtain intermediate gas. The gas exchanged with the heat is fed and cooled into a cryogenic separating unit to obtain liquid methane in a reactor of a fractionating tower. Heat of the waste gas produced from an upper part of the fractionating tower is exchanged via the freezing unit and recycled. The waste gas is passed into a pressure swing adsorption unit to dilute and absorb air discharged from the tower.    USE - Pressure swing adsorption and cryogenic combination method for separating methane from low concentration coal-bed methane.    DETAILED DESCRIPTION - A pressure swing adsorption and cryogenic combination method involves filling raw coal-bed methane with less than 30% concentration of methane into a pressure swing adsorption unit, and concentrating and evacuating the methane to obtain 40-60% of intermediate gas. The intermediate gas is decarburized and dried with a purification unit to purify the intermediate gas. The purified intermediate gas is fed into a freezing unit for exchanging heat with a refrigerant and producing waste gas by a fractionating tower to cool the intermediate gas. The intermediate gas exchanged with the heat is fed and cooled into a cryogenic separating unit to obtain liquid methane with purity greater than 99% in a reactor of a fractionating tower. Heat of the waste gas produced from an upper part of the fractionating tower is exchanged via the freezing unit and recycled. The waste gas is passed into a pressure swing adsorption unit to dilute and absorb air discharged from the tower.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a pressure swing adsorption and cryogenic combination method.'(Drawing includes non-English language text)'
NOVELTY - A catalyst comprises iron hydroxide and precious metal iridium as double active components, where the iridium content is 0.1-5% of total quantity of the catalyst.    USE - Catalyst for use in a proton exchange membrane fuel cell generating system to selectively remove micro toxic carbon monoxide from hydrogen-rich atmosphere.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a method for preparing a catalyst    (2) an application of a catalyst.
NOVELTY - Method for producing organic fertilizer, involves pulverizing passion flower-fruit peel, adjusting pH value of the product to 5.5-7.5, mixing cow dung as conditioner to obtained product, adding organic matter-decomposing inoculant to the product, and composting and fermenting the product, where the mass ratio of cow dung and passion flower-fruit peel is 1:9-4:6.    USE - The method is useful for producing organic fertilizer (all claimed).    ADVANTAGE - The fertilizer has organic content up to 35% and nitrogen, phosphorus, and potassium content up to 5%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for organic fertilizer produced by above-cited the method.
NOVELTY - The hydrodynamic friction reducer has a polymer, particularly ethylene oxide and a biofuel, particularly ethanol, where the polymer is added with a concentration of 15 parts per million. The magnitude of the friction reduction is expressed in percentage that is determined by a turbulence level in an operating range of a rheometer.    USE - Hydrodynamic friction reducer for biofuels.    ADVANTAGE - The hydrodynamic friction reducer has a polymer, particularly ethylene oxide and a biofuel, particularly ethanol, where the polymer is added with a concentration of 15 parts per million, and thus ensures efficient and improved hydrodynamic friction reducer.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical representation of viscosity between ethanol and polymer. (Drawing includes non-English language text).
NOVELTY - A 3-hydroxymethyl tetrahydrofuran synthesizing method involves reacting gamma -butyrolactone with substituted propanone compound (I) or formaldehyde in presence of strong alkali and performing substitution reaction to obtain alpha -substitutive gamma -butyrolactone. The alpha -substitutive gamma -butyrolactone is subjected to a reduction reaction with metal boron hydride below -5-50 degrees C in the presence of catalyst-I to obtain the reduced product. The reduced product is reacted with metal boron hydride in the presence of catalyst-II to generate 2-hydroxymethyl-1,4-butanediol.    USE - Method for synthesizing 3-hydroxymethyl tetrahydrofuran.    ADVANTAGE - The method enables synthesizing 3-hydroxymethyl tetrahydrofuran with high yield in a simple, inexpensive and eco-friendly manner, and suitable for industrial production.    DETAILED DESCRIPTION - A 3-hydroxymethyl tetrahydrofuran synthesizing method involves reacting gamma -butyrolactone with substituted propanone compound of formula (I) or formaldehyde in the presence of strong alkali and performing substitution reaction to obtain alpha -substitutive gamma -butyrolactone. The alpha -substitutive gamma -butyrolactone is subjected to a reduction reaction with metal boron hydride below -5-50 degrees C in the presence of catalyst-I to obtain the reduced product. The reduced product is reacted with metal boron hydride in the presence of catalyst-II to generate 2-hydroxymethyl-1,4-butanediol. The 2-hydroxymethyl-1,4-butanediol is added with acid for neutralization, filtered, the solvent is removed from the filtrate and rectified to obtain 3-hydroxymethyl tetrahydrofuran.    R=H, Cl, Br, 1-5C alkoxy or benzyloxy;and    R1=1-5C alkyl or benzyl.
NOVELTY - Method for preparing sodium cantharidinate, involves mixing cantharidin extract and sodium hydroxide solution in the ratio of 1:2-3, heating and dissolving the product, adding activated carbon to the product, reflowing and decoloring the product for 0.5-1 hours, thermally filtering, washing, decompressing and concentrating the product, adding ethanol to the product, cooling the product to room temperature, separating out the solid from the product, and drying the product to obtain sodium cantharidinate, where the weight ratio of cantharidin and ethanol is 1:3-10.    USE - The method is useful for preparing sodium cantharidinate which is used in medicine or health food for treating tumor.    ADVANTAGE - The method is simple, rapid, environmentally-friendly, inexpensive, convenient for usage and suitable for industrial production, utilizes reduced amount of acetone and isopropanol, has improved production efficiency, and provides high yield up to 89%.
NOVELTY - An inhibitor comprises (in wt.%) lime (80), magnesium oxide (5), alumina (6) and silica (9).    USE - Inhibitor for preventing straw forming fuel material from coking during combustion process.    ADVANTAGE - The inhibitor is inexpensive and simple to prepare, and avoids the problem of lack of straw combustion during coking.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a method for preparing an inhibitor    (2) a method for processing straw forming fuel raw material.
NOVELTY - The fuel cell includes a separator (15) provided with a thick peripheral portion that contacts the outer side of a sealing material (17). The sealing material includes a thick portion which contacts the inner side of the separator.    USE - Fuel cell for producing electric power.    ADVANTAGE - Prevents the sealing material from moving towards the outer peripheral side of the fuel cell even when a high pressure is transferred from the inner side of the fuel cell to the sealing material, thus preventing leakage of reactive gas. Provides a simple and high-quality fuel cell with a favorable battery characteristic.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic sectional view of a fuel cell.    Electrolyte layer (11)    Gas diffusion layer (13)    Electrode (14)    Separator (15)    Sealing material (17)
NOVELTY - The device has a cathode pipe (4) connected to a positive electrode (1) and fixed above with a hexagon honeycombing-like positive electrode. The cathode pipe is provided with multiple saw-tooth shaped metal conductive tips (5), where one end of the cathode pipe is arranged in a middle part of the hexagon honeycombing-like positive electrode. Another end of the cathode pipe is fixed on a cathode frame that is arranged in a box body via an insulating support. The positive electrode is matched with the cathode pipe to form an exhaust gas treatment unit.    USE - Tip corona discharge low temperature plasma waste gas treating device.    ADVANTAGE - The device can efficiently and quickly remove pollutant in waste gas in an inexpensive manner, and can process large quantity of wind industrial waste gas. The device has stable operation, and is suitable for industrial production in large scale.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a tip corona discharge low temperature plasma waste gas treating device.    Positive electrode (1)    Cathode pipe (4)    Saw-tooth shaped metal conductive tips (5)
NOVELTY - A coating cathode functional layer is formed on a cathode support by coating slurry solution containing solvent on support, vacuum dried, and plasticized after removing the solvent on support and coating layer, to form solid oxide fuel cell.    USE - Manufacture of solid fuel cell (claimed).    ADVANTAGE - The method efficiently and economically provides solid oxide fuel cell having excellent crack resistance.
NOVELTY - A polymer electrolytic membrane fuel cell bulk metal glass bipolar plate comprises zirconium-based bulk metal glass consists of zirconium, niobium, copper, nickel and aluminium as elemental compound, where thickness of a fuel cell is 0.1-3 mm, the purity of each element of zirconium, niobium, copper, nickel and aluminium is no less than 99.95 wt.%, the zirconium-based bulk metal glass contains 95 volume % of amorphous phase with corrosion speed of less than or equal to 16 micro amps/square.cm and conductivity of greater than or equal to 5000 specific conductivity/cm.    USE - Polymer electrolytic membrane fuel cell bulk metal glass bipolar plate for use in fuel cell manufacturing field.    ADVANTAGE - The bipolar plate has high conductivity and corrosion resistance, and is inexpensive.    DETAILED DESCRIPTION - A polymer electrolytic membrane fuel cell bulk metal glass bipolar plate comprises a zirconium-based bulk metal glass consists of zirconium, niobium, copper, nickel and aluminium as elemental compound (Zr60-xNbxCu20Al10Ni10), where x is 0-20, thickness of a fuel cell is 0.1-3 mm, the purity of each element of zirconium, niobium, copper, nickel and aluminium is no less than 99.95 wt.%, the zirconium-based bulk metal glass contains 95 volume.% of amorphous phase with corrosion speed of less than or equal to 16 micro amps/square.cm and conductivity of greater than or equal to 5000 specific conductivity/cm. An INDEPENDENT CLAIM is also included for a method for preparing a polymer electrolytic membrane fuel cell bulk metal glass bipolar plate.
NOVELTY - The method involves forming the air electrode in the multiple air channel inner surface. The multiple slits are formed by cutting the short-side portion of the other supporter in the module and sidewall portion of the supporter. The multiple fuel channels are formed in the upper side and lower side of the multiple slits of the supporter. The connecting electrode in each module is connected.    USE - Manufacturing method of fuel cell of solid electrolyte.    ADVANTAGE - the fuel cell can be lightened by improving the capacity per unit volume.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the fuel cell of solid electrolyte. (Drawing includes non-English language text)
NOVELTY - An article of manufacture which comprises a combustible article of manufacture, comprises torrefied biomass having a combustible oil entrained in it.    USE - As combustible article of manufacture (claimed), particularly torrefied wood, which is useful as a combustible fuel.    ADVANTAGE - The waste wood and other normally unused biomass could be put to a practical use instead of being placed in landfills or incinerated or left to decay where it returns carbon dioxide, methane and other gasses to our air. The farmers could put to use large areas of near worthless land and restore it to grow energy biomass crops for energy production. The switch grass may be one of the most energy efficient biomass crops to grow for energy use. It may produce 2 to 3 times the energy of corn to developing a new processing method that is simple, safe, efficient and practical for major commercial use, has been a driving force leading to the development of this substantial improvement over the prior art. The present apparatus and method overcomes all the previous problems that prevented torrefied wood from becoming a practical coal replacement fuel.
NOVELTY - A thermophilic microorganism having a deodorizing ability for short chain fatty acid, which belongs to Bacillus licheniformis, is new.    USE - The thermophilic microorganism is useful for producing deodorizer and compost (all claimed).    ADVANTAGE - The production of short chain fatty acids, which are the offensive odor components, can be reduced, thus deodorization is achieved in the process of composting.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a deodorizer comprising the microorganism as an active ingredient; and    (2) a method for producing compost comprising adding the microorganism or the deodorizer to an organic remnant.
NOVELTY - The manufacturing apparatus (10) has a press molding component that presses a flat metal plate (30) arranged between upper and lower molds, while a stamper forms the external shape of a punch separator for a flat metal plate. The surface of the lower mold (14) is rougher than the surface of the upper mold (12).    USE - Manufacturing apparatus for fuel cell separator.    ADVANTAGE - Suppresses the ball up to the upper mold since a molded article is reliably fixed to a lower mold at the time of mold opening after press molding, thus preventing the damage by the fall of the molded article from the upper mold as well as the damage by interference with the scrap after a punch.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a manufacturing method of the fuel cell separator.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of the manufacturing apparatus.    Manufacturing apparatus (10)    Upper mold (12)    Lower mold (14)    Extraction blade (16)    Flat metal plate (30)
NOVELTY - Ceria group electrolyte arranged on a metal support (10) is baked in atmosphere having oxygen partial pressure less than atmospheric pressure, during manufacture of fuel cell (100). Thus, fuel cell is manufactured. The expansion difference is maintained at specific condition during baking.    USE - Manufacture of fuel cell.    ADVANTAGE - The generation of crack and peeling is suppressed during manufacture of fuel cell.    DETAILED DESCRIPTION - Ceria group electrolyte arranged on a metal support is baked in atmosphere having oxygen partial pressure less than atmospheric pressure, during manufacture of fuel cell. Thus, fuel cell is manufactured. The expansion difference is maintained at condition given by: expansion difference=(coefficient of thermal expansion of metal support-coefficient of thermal expansion of electrolyte)x (calcination temperature-room temperature)x 100-(reduction expansion coefficient of electrolyte) more than 0, during baking.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view explaining manufacture of fuel cell. (Drawing includes non-English language text)    Support (10)    Hole (11)    Anode (20)    Anode material (21)    Electrolyte layer (30)    Fuel cell (100)
NOVELTY - The apparatus has gasification reforming furnace (10) to reform the gas which partially oxidizes and thermally decomposes the waste material, to produce reformed gas. A connector pipe (30) connects cooling unit (20) which receives the reformed gas from the gasification reforming furnace, and cools reformed gas. A burner (41) blows oxygen containing gas in the connector pipe, and burns a portion of reformed gas.    USE - Waste material gasification processing apparatus.    ADVANTAGE - The adhesion of dust to the inner wall of connector pipe can be prevented. The waste material gasification processing apparatus can be operated stably irrespective of the property of waste material.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the waste material gasification processing apparatus.    Gasification reforming furnace (10)    Cooling unit (20)    Connector pipe (30)    Burner (41)    Temperature sensor (51)
NOVELTY - The furnace has fireproof sleeve (3) that extends outwards, and is set on the bottom plate. An air outlet (4,7) is provided under the fireproof sleeve that is provided with water seal cover. The upper cover plate (1) is provided with water seal tank, and the upper portion of tank is covered.    USE - Biomass gasification furnace.    ADVANTAGE - The biomass gasification furnace provides stable combustion for long time, safety and good reliability.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass gasification furnace.    Upper cover plate (1)    Furnace cover (2)    Fireproof sleeve (3)    Air outlet (4,7)    Air inlet (9)
NOVELTY - The method involves taking biomass and a coal material as raw materials. A synthetic gas rough product is supplied in a fixed bed pressure gasification unit and removed from a condensing separating unit. A tar component of the synthetic gas rough product is condensed to obtain a purified synthesis gas rough product. The purified synthesis gas rough product is cracked, hydrogenated and transformed into a catalytic-free partial oxidation unit. Carbon monoxide and hydrogen are added into the oxidation unit to obtain converted synthesis gas that is post processed to obtain a synthetic gas product.    USE - Method for preparing synthesis gas by a fixed bed pressing gasification process.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a structure used for preparing synthesis gas by a fixed bed pressing gasification process.'(Drawing includes non-English language text)'
NOVELTY - The device has a pressurizing gasification furnace provided with a synthetic gas crude product by taking a mixture of biomass and optional coal material as a raw material. Synthesis gas is removed by a condensing separating unit under a crude product solid phase condition. The synthesis gas crude product is cracked, hydrogenated and transformed to generate a main component. The main component is divided into carbon monoxide and a non-catalytic partial oxidation unit of hydrogen. The synthesis gas is passed via a processing unit. A chilling washing unit is provided with a quench washing tower.    USE - Static bed pressing gasification synthesis gas device.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a static bed pressing gasification synthesis gas device.'(Drawing includes non-English language text)'
NOVELTY - Bio-diesel solid acid catalyst bearing mold, comprises a bearing template (1) and a solid acid support (2). The bearing template is equipped with the solid acid support. The solid acid support is equipped with a filtrate tank.    USE - Used as a bio-diesel solid acid catalyst bearing mold.    ADVANTAGE - The mold recycles catalyst; performs solid-liquid separation without multi-step filtration process; and prevents loss of product.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the bio-diesel solid acid catalyst bearing mold.    Bearing template (1)    Solid acid support (2)
NOVELTY - The furnace has a furnace body divided into an upper furnace body (1) and a lower furnace body (5). The upper furnace body and the lower furnace body are respectively formed on an upper hearth (11) and a lower hearth (51). A burner (3) is fixed on the lower hearth. The burner is provided with multiple secondary air inlet holes (31) and a furnace bridge (6). An upper surface of the lower hearth is provided with an exhaust pipe (2). The exhaust pipe is arranged in the upper furnace body. An air inlet (4) is arranged on the lower furnace body and connected with a lower end of the lower hearth.    USE - Biomass energy-saving furnace.    ADVANTAGE - The furnace has high heat efficiency and low manufacturing cost. The furnace is simple in structure, and avoids smoke pollution and occupies less space.    DESCRIPTION OF DRAWING(S) - The drawing shows a side perspective view of a biomass energy-saving furnace.    Upper furnace body (1)    Exhaust pipe (2)    Burner (3)    Air inlet (4)    Lower furnace body (5)    Furnace bridge (6)    Upper hearth (11)    Secondary air inlet holes (31)    Lower hearth (51)
NOVELTY - The system has a flue gas treatment device that is connected with a fuming device. The fuming device is comprised of combustion chamber (5) having feeding device and grooves. A smoke outlet pipe is passed through a flue gas component detecting device (18) connected with a fume processing device. An upper portion of the purifying chamber (30) is provided with a tube (19), while a lower portion is provided with an air outlet (32). An automatic control system is connected with feeding device, discharging device, blast device and flue gas component detecting device.    USE - Garbage fuel gasification smoke treatment system.    ADVANTAGE - The garbage fuel gasification smoke treatment system is provided to ensure the obvious economic and social benefits. The cause of pollution to the external environment can be prevented. The production efficiency of the garbage fuel gasification smoke treatment system can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for garbage fuel smoke gasification process control method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the connection configuration of the garbage fuel gasification smoke treatment system.    Combustion chamber (5)    Flue gas component detecting device (18)    Tube (19)    Purifying chamber (30)    Air outlet (32)
NOVELTY - The furnace has a furnace body, a sealed boiler bracket, a combustion chamber (1), a smoke exhaust smoke channel (15), a feeding hopper (6), a hearth (12), a fire grate (7), ash bin (9) and an ash bucket (8). The hearth is equipped with a cracking tube neck. Another hearth is provided inner side or outer side of a fire device (11). One side of the former hearth is connected with a feeding hopper. The furnace body is provided with a secondary air inlet passage (10) and a secondary air pre-heating chamber (13).    USE - Biomass low carbon furnace.    ADVANTAGE - The furnace builds up a condensed deposition so as to block a pipe and furnace eye for realizing full combustion, thus solving tar and pollution problem of condensed water, improving heat efficiency and reaching an uncovering cover feeding. The furnace provides energy conservation, emission reduction and low carbon life.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a biomass low carbon furnace.    Combustion chamber (1)    Feeding hopper (6)    Fire grate (7)    Ash bucket (8)    Ash bin (9)    Secondary air inlet passage (10)    Fire device (11)    Hearth (12)    Secondary air pre-heating chamber (13)    Smoke exhaust smoke channel (15)
NOVELTY - A high solid content biomass fuel comprises 60-80 mass% wood-type material (A) and plastics (B).    USE - A high solid content biomass fuel (claimed).    ADVANTAGE - Hazardous substances during combustion are not produced, and high solid content biomass fuel is stably produced with high emitted-heat amount.
NOVELTY - Recovering and purifying liquids used in biomass treatment processes, involves: processing a stream obtained from a biomass treatment process through membrane filtration; processing the filtered stream through an electro dialysis device; and separating liquids present in the stream by passing the stream through a membrane.    USE - For recovering and purifying liquids used in biomass treatment processes (claimed), which is useful for production of biofuels, chemicals, and other biomass-based products.    ADVANTAGE - The ionic liquid recovery and purification minimizes waste production and enhances process profitability. The process recovers ionic liquid at least 97 wt.%.
NOVELTY - Biofuel and/or biochemical are synthesized from pyrolysis oil which is not pretreated or upgraded by hydrotreatment and/or hydrodeoxygenation. Pyrolysis oil is contacted with a catalytic cracking catalyst at 400 degrees C or more in the presence of a hydrocarbon co-feed to produce cracked product(s). The cracked product(s) is fractionated to produce product fraction(s), which are used to produce biofuel and/or biochemical.    USE - Preparation of biofuel and/or biochemical from pyrolysis oil.    ADVANTAGE - The method uses pyrolysis oil which is sufficiently miscible with hydrocarbon co-feed such that co-processing is feasible. Catalytic cracking of pyrolysis oil in the presence of hydrocarbon co-feed leads to a synergistic effect, where the coke make during the catalytic cracking is less than what would be expected on the basis of the sum of coke make for each feed when catalytically cracked separately. The method is simple and economical as no upgrading by hydrotreatment is required.
NOVELTY - A liquid combustion catalyst composition includes a mixed metal-complex ionic compound formed by dissolving mixed metal-complex chelate compound or mixed metal-complex ionic hydrate comprising metal chosen from magnesium, calcium, manganese, zinc and aluminum and one or more alkali metal compounds chosen from lithium, potassium and sodium in a solvent (soluble liquid).    USE - Liquid combustion catalyst composition is used in combustion engine for burning hydrocarbon fuel, fossil fuel and biomass fuel.    ADVANTAGE - The liquid combustion catalyst composition has improved formation and ionicity of ionic complex salt, burning promotion, and removal efficiency of fouling and clinker. The combustion efficiency of combustion engine is improved using the liquid combustion catalyst composition, with reduced usage amount of fuel.
NOVELTY - Environmental conservation type organic-refuse compost bag comprises bag which provides opening in upper portion, and opening-and-closing unit on the opening, and partition compression-bonded line which partitions off the organic-refuse portion provided inside of the bag, and accommodates an organic refuse for the bag, and liquid which accommodates the organic-refuse water content located in the lower portion and through which the organic-refuse water content is made to flow into the liquid portion having at least one hole.    USE - As environmental conservation type organic-refuse compost bag (claimed).    ADVANTAGE - The compost bag improves fermentation rate of organic manure and maintains moisture content of organic manure, has excellent transparency, and can be prepared simply, inexpensively, conveniently and environmentally-friendly.
NOVELTY - Method for performing saccharification of high solids, involves (a) obtaining cellulosic biomass, (b) pretreating the cellulosic biomass, (c) adjusting the pretreated cellulosic biomass to solid concentration of 6-35 weight/weight% and starting pH of 5-7, and (d) hydrolyzing the pretreated biomass with at least one aqueous hydrolyzing liquid comprising cellulase and/or saccharification enzyme to obtain cellulosic hydrolyzate which comprises fermentable sugar.    USE - The method is useful for saccharifying cellulosic biomass (claimed) chosen from corn stover, agricultural residues, municipal solid waste, industrial solid waste, yard waste, wood and forestry waste, sugar cane, switchgrass, wheat straw, hay, barley, barley straw, rice straw, grass, waste paper, sludge from paper industry, corn grain, corn cobs, corn husks, sugar cane bagasse, Sorghum, soy, trees, branches, wood chips and sawdust, used for producing ethanol, butanol, acetic acid or butyric acid.    ADVANTAGE - The method improves saccharification yield to 50-70% or more, cost-effectively.    DETAILED DESCRIPTION - Method for performing saccharification of high solids, involves (a) obtaining cellulosic biomass, (b) pretreating the cellulosic biomass to obtain pretreated cellulosic biomass, (c) adjusting the pretreated cellulosic biomass to solid concentration of 6-35 weight/weight% and starting pH of 5-7, and (d) hydrolyzing the pretreated biomass with at least one aqueous hydrolyzing liquid comprising at least one enzyme chosen from cellulase, saccharification enzyme and their combinations for certain period of time to hydrolyze at least a portion of the pretreated cellulosic biomass to obtain cellulosic hydrolyzate which comprises fermentable sugar.
NOVELTY - The system has solar power generation device (2) that is installed in artificial pond (1) for storing water. The circulating lines (18) makes methane fermentation tank (17) to circulate through water of the artificial pond. A methane gas refiner (19) is provided to separate carbon dioxide from methane gas discharged from methane fermentation tank. A transfer unit (21) is provided to supply the separated carbon dioxide to the artificial pond.    USE - Renewable energy multistage utilization system.    ADVANTAGE - Since the methane gas refiner is provided to separate carbon dioxide from methane gas discharged from methane fermentation tank, the reproducible energy total amount obtained from unit area can be increased efficiently without increasing the discharge amount of the carbon dioxide.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the renewable energy multistage utilization system.    Artificial pond (1)    Solar power generation device (2)    Methane fermentation tank (17)    Circulating line (18)    Methane gas refiner (19)    Transfer unit (21)
NOVELTY - The apparatus has storage unit (12) and fuel cell power generation unit (13) that are Installed in base portion (14). A seawater electrolysis unit (11) electrolyzes seawater and extracts hydrogen using the electric power supplied from solar panel. A storage unit stores the hydrogen extracted in the seawater electrolysis unit. A fuel cell power generation unit generates electric power using hydrogen stored in storage unit and electrically feeds to supply object on land.    USE - Marine solar electric power generating apparatus.    ADVANTAGE - Since the fuel cell power generation unit is provided to generate electric power using hydrogen stored in storage unit and electrically feeds to supply object on land, the stable supply of the clean energy generated using sunlight can be supplied to the urban areas adjacent to the sea.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the marine solar electric power generating apparatus. (Drawing includes non-English language text)    Energy plant (10)    Seawater electrolysis unit (11)    Storage unit (12)    Fuel cell power generation unit (13)    Base portion (14)
NOVELTY - The system (101) has a fuel concentration detection apparatus detecting fuel concentration of fuel i.e. methanol, supplied to a fuel cell (102). A concentration detection element (112) in the apparatus has a proton electroconductivity solid polymer film arranged between electrodes. A polar switching unit (114) switches a polarity of a voltage applied to the detection element. A current measurement unit measures oxidation current of the fuel produced by applying the voltage to the detection element. A concentration sensor controls a methanol concentration in a preset range.    USE - Fuel cell system i.e. direct methanol fuel cell system, for use as a portable type power supply for an electric motorcycle, an assist type bicycle, a wheelchair for medical nursing care and a senior car.    ADVANTAGE - The system improves stability of the concentration sensor using the oxidation current of the fuel, and stably uses the concentration sensor in long run.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for operating a fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a fuel cell system.    Fuel cell system (101)    Fuel cell (102)    Gas-liquid separation film (110)    Air supply unit (111)    Concentration detection element (112)    Polar switching unit (114)
NOVELTY - The microaerobic gas desulfurization device comprises a micro peristaltic pump (1), a computer (2), a biogas tank (3), a discharge hole (4), a stirring blade (5), an exhaust pipe (6), and a stirring motor. The micro peristaltic pump is connected with the computer. A guide tube is connected to the biogas tank. A lower part of the biogas tank has a discharging opening with an inside of the tank. An upper part of the discharge port is connected with the stirring blade. The stirring blade is connected with the stirring motor. An upper part of the biogas tank is provided with a feed inlet.    USE - The device is useful for desulfurization of microaerobic gas.    ADVANTAGE - The microaerobic gas desulfurization device can be simply and effectively manufactured in an economical manner.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic view of a microaerobic gas desulfurization device.    Micro peristaltic pump (1)    Computer (2)    Biogas tank (3)    Discharge hole (4)    Stirring blade (5)    Exhaust pipe. (6)
NOVELTY - The composite bacteria comprises raw materials consisting of trichoderma viride (15%), Bacillus subtilis (10-15%), black Rhizopus (25-40%), photosynthetic bacteria (25-40%), Candida lipolytica (5-10%), Bacillus licheniformis (10-15%), nitrosated hair bacteria (5-15%) and Vickers nitrate bacteria strains (5-15%).    USE - The composite bacteria is useful for degreasing food waste.    ADVANTAGE - The composite bacteria is capable of rapidly, economically, easily and effectively degreasing the food waste in an environmental friendly manner, and ensures rapid degradation of the lipid composition of food waste.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of preparing composite bacteria for degreasing food waste.
NOVELTY - Wheat straw and cow dung mixed compost is fermented by building low bank having height of 25-35 cm on periphery of ground; mixing and piling wheat straw and fresh cow dung at volume ratio of 4-6:6-4, where the pile is 2 m in width and 1 m in height; piling eight ridges of compost, where the interval between ridges is 0.5 m; and after piling, spreading a layer of straw on the compost.    USE - Method of fermenting wheat straw and cow dung mixed compost (claimed).    ADVANTAGE - The method has simple operation, does not cause stinking, provides thorough sterilization and short thorough decomposing time, and can satisfy fast composting requirement.
NOVELTY - Positive electrode (15) comprises a carbonaceous material doped with a non-metallic element.    USE - The positive electrode is useful in lithium air battery (claimed).    ADVANTAGE - The positive electrode provides: high energy efficient lithium air batteries with high charge and discharge capacity without utilizing complicated process and expensive material.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) preparing the positive electrode comprising: mixing a non-metal precursor and a mesoporous material with a solvent to prepare a slurry; drying the slurry and calcining the dried product under an inert atmosphere to produce a calcined product; and contacting the calcined product and a hydrogen halide; and    (2) a lithium air battery (10) comprising: a negative electrode (13) enabling intercalation and deintercalation of lithium ions; an electrolyte; and the positive electrode using oxygen as a positive electrode active material.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of the lithium air battery.    Lithium air battery (10)    First current collector (12)    Negative electrode (13)    Positive electrode (15)    Catalyst (17)
NOVELTY - Liquid fuel composition, comprises a liquid fuel, and a sublimatable organic compound, where sublimatable organic compound has a sublimation point lower than 45 degrees C at atmospheric pressure, and includes a skeleton comprising bicycloheptane, indane, pyrone, cyclopropane, cyclobutane, cyclopentane, cyclohexane, cycloheptane, cyclooctane, and benzene.    USE - The liquid fuel composition is useful for enhancing combustion efficiency of liquid fuel, where the liquid fuel is gasoline, diesel, alcohol, biomass fuel, and/or organic hydrogenated fuel oil (all claimed). The liquid fuel composition is useful in vehicles.    ADVANTAGE - The liquid fuel composition can raise the running mileage of the vehicles. The liquid fuel composition is environmental friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for enhancing combustion efficiency of a liquid fuel, comprising adding the sublimatable organic compound in the liquid fuel.
NOVELTY - A unit cell has a current collector layer provided with a porous structure, and a tape cast in an outer surface of a cathode.    USE - Unit cell for electrical energy producing fuel cell.    ADVANTAGE - The cell enhances current collecting ratio of a current collector and performance of a fuel cell, and prevents conductivity degradation caused by poor contact through the current collector layer in warpage generation of the cell.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a unit cell manufacturing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a unit cell.
NOVELTY - Production of organic fertilizer from household waste involves crushing organic waste until diameter of 20-40 mm; conveying crushed materials to organic material degradation device; adding acid (preferably inorganic acid, 0.5-1 wt.%), uniformly stirring, putting in stirred high-pressure degradation reactor and pressurizing to 1-1.2 MPa by steam, and maintaining pressure for 1-1.5 hours; separating degraded organic materials from non-degradable materials; preparing degraded organic materials into organic fertilizer; and recovering waste gas.    USE - Method for producing organic fertilizer from household waste (claimed).    ADVANTAGE - The method produces organic fertilizer from household waste, without obnoxious odor; and allows recycling of non-degradable organic materials.
NOVELTY - A fuel reformer (R) has a desulfurizer (2) with which a desulfurization catalyst (2a) for removing a sulfur compound from hydrocarbon-type raw fuel gas, is filled, a modifier (3) for carrying out steam reforming of raw fuel gas and producing reformed gas containing hydrogen, a hydrogenation unit (7), and an oxidation-reduction reaction device (1) filled with an oxidation-reduction reaction agent (1a) for exhibiting oxidation-reduction reaction which repeats reaction reversibly between oxidation state and reduction state between the desulfurizer and addition portion (8) of reformed gas.    USE - Fuel reformer used for producing hydrogen gas used for fuel cell.    ADVANTAGE - The fuel reformer is compact. The sulfur content in the raw fuel gas after desulfurization is reduced to low level.    DETAILED DESCRIPTION - A fuel reformer has a desulfurizer with which a desulfurization catalyst for removing a sulfur compound from hydrocarbon-type raw fuel gas, is filled, a modifier for carrying out steam reforming of raw fuel gas de-sulfurized with desulfurizer, and producing reformed gas containing hydrogen as a main component, a hydrogenation unit in which a portion of reformed gas is added to the raw fuel gas flowing into the desulfurizer, and an oxidation-reduction reaction device filled with an oxidation-reduction reaction agent for exhibiting oxidation-reduction reaction which repeats reaction reversibly between oxidation state and reduction state between the desulfurizer and addition portion of reformed gas.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of fuel reformer. (Drawing includes non-English language text)    Oxidation-reduction reaction device (1)    Oxidation-reduction reaction agent (1a)    Desulfurizer (2)    Desulfurization catalyst (2a)    Modifier (3)    Hydrogenation unit (7)    Addition portion (8)    Fuel reformer (R)
NOVELTY - System for producing biodiesel by waste cooking oil comprises: an oil storage device, a washing tower, a dehydrating tower, a reaction device, a rectifying tower, a washing device, a dehydrating device and a high temperature distillation device which are orderly connected, where the rectifying tower is connected with the reaction device through the return pipe.    USE - Used as a system for producing biodiesel by waste cooking oil.    ADVANTAGE - The system has simple structure, high production efficiency, is simple to operate, and carry out harmless treatment for waste cooking oil.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of the system for producing biodiesel by waste cooking oil (Drawing includes non-English language text).
NOVELTY - Producing fatty acid esters of lower alcohols from fatty acids contained in fatty acid triglycerides or fatty acid esters of lower alcohols, comprises esterifying free fatty acids present with lower alcohols; optionally recovering and reusing the catalysts proceeds by distilling off the lower alcohol present in excess and the reaction water; and subsequently alkali-catalyzed transesterification of the triglycerides with lower alcohols at a purity necessary for use as fuel for diesel engines.    USE - The fatty acid esters of lower alcohols are useful as fuel for diesel engines.    ADVANTAGE - The process provides fatty acid esters with high purity and without using costly raw materials.    DETAILED DESCRIPTION - Producing fatty acid esters of lower alcohols from fatty acids contained in fatty acid triglycerides or fatty acid esters of lower alcohols, comprises esterifying free fatty acids present with lower alcohols at atmospheric pressure and temperatures in the boiling range of the lower alcohols and in the presence of acid homogeneous catalysts and optionally a solvent; optionally recovering and reusing the catalysts proceeds by distilling off the lower alcohol present in excess and the reaction water; and subsequently alkali-catalyzed transesterification of the triglycerides with lower alcohols at a purity necessary for use as fuel for diesel engines, where dibasic aliphatic or aromatic sulfonic acids are used as homogeneous esterification catalysts and the solvent acts as carrier material for the acid catalysts and is insoluble in the fatty acid triglycerides or fatty acid esters.
NOVELTY - Preparing ammonium phosphate compound fertilizer involves either adding ammonium sulfate (2-18 parts) into 75-95% phosphoric acid (3-15 parts) at 120-140 degrees C stirring and mixing until it is completely dissolved to obtain uniform ammonium sulfate phosphate eutectic material; feeding resulting material into a granulating device to pelletize to obtain granular ammonium phosphate compound fertilizer. The fertilizer can be optionally mixed/melted together with ammonium nitrate or ammonium chloride to obtain ammonium nitrate or ammonium chloride particle compound fertilizer.    USE - For preparing ammonium phosphate compound fertilizer capable of decomposing phosphorus and potassium in soil (claimed).    ADVANTAGE - The method uses low temperature melting this simplifies production process, and saves energy consumption. The method reduces the production cost; and produces ammonium phosphate compound fertilizer which improves crop yield, and is safe, reliable and convenient for use.    DETAILED DESCRIPTION - Preparing ammonium phosphate compound fertilizer involves either adding ammonium sulfate (2-18 parts) into 75-95% phosphoric acid (3-15 parts) at 120-140 degrees C stirring and mixing until it is completely dissolved to obtain uniform ammonium sulfate phosphate eutectic material; feeding resulting material into a granulating device to pelletize to obtain granular ammonium phosphate compound fertilizer; or adding sulfuric acid to monoammonium phosphate or diammonium phosphate to generate phosphoric acid and ammonium sulfate, and adding ammonium sulfate (0-300 parts) according to weight, heating at 120-140 degrees C to obtain ammonium sulfate eutectic material, cooling the eutectic material cooling, granulating to obtain granular ammonium phosphate compound fertilizer. The fertilizer can be optionally mixed/melted together with ammonium nitrate or ammonium chloride to obtain ammonium nitrate or ammonium chloride particle compound fertilizer.
NOVELTY - Organic wheat fertilizer, comprises Rhododendron molle (10-20 parts by weight (pbw)), earthworm (6-10 pbw), wheat straw (15-25 pbw), and farmyard manure (35-65 pbw), where the organic wheat fertilizer is prepared by e.g. (a) cutting the wheat straw, and (b) mixing the straw and the Rhododendron molle to 2-3 times of water, and then boiling for 20-30 minutes in the water, where the mass ratio of the Rhododendron molle and water is 1:2-3, separating and collecting Rhododendron molle juice and Rhododendron molle residue.    USE - Used as an organic wheat fertilizer.    ADVANTAGE - The organic wheat fertilizer is eco-friendly, inexpensive, provides rich nutrition to soil e.g. reduces the agricultural chemical, improves the crop stress resistance, and can be prepared with high quality in a simple manner. Tests details are described but no results given.    DETAILED DESCRIPTION - Organic wheat fertilizer, comprises Rhododendron molle (10-20 parts by weight (pbw)), earthworm (6-10 pbw), wheat straw (15-25 pbw), and farmyard manure (35-65 pbw), where the organic wheat fertilizer is prepared by (a) cutting the wheat straw, (b) mixing the straw and the Rhododendron molle to 2-3 times of water, and then boiling for 20-30 minutes in the water, where the mass ratio of the Rhododendron molle and water is 1:2-3, separating and collecting Rhododendron molle juice and Rhododendron molle residue, (c) cutting the wheat straw of earthworm, farmyard manure and Rhododendron molle residue fully and uniformly stirring after compost, and repeating until compost is finished, and (d) covering the compost and sealing the compost by plastic film till the compost is mature.
NOVELTY - Micro-emulsified biodiesel comprises (in wt %) biodiesel (65-90), emulsifier (2-12), cosolvent (3-8) and water (5-15).    USE - Used as a micro-emulsified biodiesel.    ADVANTAGE - The micro-emulsified biodiesel: is clear, transparent and uniformly dispersed, and has stable thermodynamics; is beneficial for storing and transporting without stratification; can not only be used as a renewable energy source, but also reduces the emission of harmful nitrogen oxide (NOx) gas and carbon smoke while burning the biodiesel; is economical and can be stored and transported stably for a long time. The preparation method is simple without causing any pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the micro-emulsified biodiesel, comprising: uniformly mixing fatty alcohol-polyoxyethylene ether AEO-3 and fatty alcohol polyoxyethylene ether AEO-7 to obtain the emulsifier; mixing the biodiesel, emulsifier, cosolvent and water, and uniformly stirring; and obtaining the transparent mixing liquid, namely micro-emulsified biodiesel.
NOVELTY - A fermentation tank filler formulation comprises (wt.%) corncob grain (60) having particle size of 2-3 mm, sawdust (39.8-39.9), and effective microorganisms (EM) stock solution (0.1-0.2). The materials are added and uniformly stirred at controlled humidity of 48-50%.    USE - Fermentation tank filler formulation used in pig pen excrement pool (claimed) to convert pig excrement to high quality organic fertilizer.    ADVANTAGE - The filler formulation can increase pig disease resistance and save labor and material with no pollutant discharge.
NOVELTY - The torch has a cathode provided with a flat lower surface. A top cover is formed in around an upper end of the cathode. A body part is arranged in a lower part of the top cover. An anode is arranged inside the body part, and covers a lower part of the cathode. A cathode cooling hole is formed inside the cathode. A fluid path is connected with the cathode cooling hole. The body part is provided with an outlet to eject cooling water outside. The anode is provided with a parasitic production part.    USE - Plasma torch for treating waste air during chemical vapor deposition process.    ADVANTAGE - The torch can effectively remove fluorinated inundation in the waste gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of a plasma torch.
NOVELTY - An animal excrement biological conversion method involves sealing animal waste in a collecting tank by using a conveying belt. The animal waste is cured. House fly, oxygen and maggot are added into a culture medium. Earthworm is collected and added into the culture medium. The animal waste is cultured using the culture medium. A substrate or base containing the processed animal waste is sterilized, dried, packed and entered into a warehouse.    USE - Animal excrement biological conversion method for preparing an organic fertilizer (claimed).    ADVANTAGE - The method enables utilizing breeding industry animal excrement as raw material, and converting the animal excrement into processed material with low investment cost, easy operation and quick conversion effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating an animal excrement biological conversion method.'(Drawing includes non-English language text)'
NOVELTY - An organic fruit and vegetable substrate cultivating method involves obtaining rural waste such as crop straw, mushroom residue, sawdust and farm fertilizer such as cattle, chicken, quail, river sand, and stirring. Water is injected for composting, and a film is covered. Organic substrates are fermented for 40-50 days, and coarse sand is filled to layers of bricks. A micro-spraying thin wall hose is paved, and micro-spraying thin-wall soft pipes are laid. Different crops are planted according to different conditions, and a seed is soaked in warm water. The seed is taken out and washed.    USE - Method for cultivating organic fruit and vegetable substrate.    ADVANTAGE - The method enables providing simplicity, effectiveness and ecological, saving energy, and protecting environment.    DETAILED DESCRIPTION - An organic fruit and vegetable substrate cultivating method involves obtaining rural waste such as crop straw, mushroom residue, sawdust and farm fertilizer such as cattle, chicken, quail, river sand, and stirring evenly. Water is injected for composting, and a film is covered. Organic substrates are fermented for 40-50 days, and coarse sand is filled to layers of bricks. A micro-spraying thin wall hose is paved, and micro-spraying thin-wall soft pipes are laid. Different crops are planted according to different conditions, and a seed is soaked in warm water at 55 degrees C for 15-25 minutes. The seed is taken out and washed at 25-30 degrees C.
NOVELTY - 2-bromo-4,5-dimethoxy benzoic acid is mixed with 1,2-dichloroethane and thionyl chloride, heated and refluxed for 1 hour. Zinc chloride and 3,5-dimethoxyphenol is added, stirred, heated at 40-80 degrees C for 2-4 hours, and 1,2-dichloroethane solvent, and sodium hydroxide aqueous solution with 10-30% are added, heated and refluxed for 2-3 hours to obtain 1,3,6,7-tetramethoxide xanthone. The obtained 1,3,6,7-tetramethoxide xanthone is mixed with glycol solvent and hydrochloric acid, heated and refluxed for 3-5 hours, to obtain norathyriol.    USE - Preparation of norathyriol.    ADVANTAGE - The method economically provides norathyriol with excellent safety by a simple process, without polluting the environment.
NOVELTY - Dehydrated sludge (100 parts), cottonseed shell residue (15-25 parts), mashed sugar (5-10 parts), xylitol slag (25-35 parts), and furfural slag (20-25 parts) are mixed, stirred, composite microbial halophilic bacterial strain is sprayed, uniformly mixed, fermented for 5 days, left, fermentation is again continued for 5 days, sulfur powder (120 meshes) (12-18 parts), lanthanum oxide (5-10 parts), calcium carbonate (4-7 parts), and ferrous sulfate (2-6 parts) are added. Thus, production of saline-alkali soil improving agent is carried out.    USE - Production of saline-alkali soil improving agent.    ADVANTAGE - The salinity of the saline-alkali soil is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of saline-alkali soil improving agent.
NOVELTY - Method for turning wastes remained after forestry-paper integration into energy, involves subjecting the wastes to fermentation process for production of energy.    USE - The method is useful for turning wastes remained after forestry-paper integration into energy chosen from methane, highly concentrated methane gas and dimethyl ether and agricultural fertilizer (claimed).    ADVANTAGE - The method enables effective utilization of wastes which causes secondary pollution, hence environment is protected, pollution is reduced and ecological balance is maintained.
NOVELTY - Biologically preprocessing strengthened rice straw, involves removing roots and panicle from hollow paddy rice, drying with wind and crushing, sieving through 40-60 mesh sieve, preparing culture medium containing peeled potato material, regulating pH to 4.5 with hydrochloric acid, sterilizing at 121 degrees C for 20 minutes, inoculating Phanerochaete chrysosporium strain into the culture medium, obtaining seed liquid and fermenting the strengthened rice straw using the seed liquid.    USE - The method is useful for biologically preprocessing strengthened rice straw to produce methane by fermentation with white rot fungus (claimed).    ADVANTAGE - The method has good lignin degradation effect to shorten anaerobic fermentation period, and improve the methane conversion efficiency and conversion rate of the straw resource.    DETAILED DESCRIPTION - Method for biologically preprocessing strengthened rice straw to produce methane by fermentation with white rot fungus, involves removing roots and panicle from hollow paddy rice, drying with wind and crushing, sieving through 40-60 mesh sieve, preparing culture medium comprising (in g): peeled potato material (200), glucose (10), yeast extract (3), trace element solution (2), agar (20) and distilled water (1000 ml), regulating pH to 4.5 with hydrochloric acid, sterilizing at 121 degrees C for 20 minutes, where the trace element solution comprises glycine (0.5 g/l), and the peeled potato material is obtained by cutting into blocks, boiling in water for 30 minutes, adding glucose and agar, quantifying with distilled water to make the volume to be 1000 ml, and regulating the pH to 4.5 with hydrochloric acid, and inoculating Phanerochaete chrysosporium strain into the culture medium, obtaining seed liquid and fermenting the strengthened rice straw using the seed liquid.
NOVELTY - Nonionic alcohol ether type vehicle fuel active agent comprises (in wt.%) ethyl ether (9-15), isopropyl ether (6-16), petroleum ether or vinyl ether (3-6), isopropyl alcohol (8-16), tertiary butyl alcohol (7-15), dimethyl carbonate (5-9), antioxidant (2-3.5) anti-corrosion agent (2-3), stabilizing agent (2-5), n-butyl alcohol (17-25), isobutyl alcohol (10-19).    USE - The vehicle fuel active agent is useful for preparing 10-85% of methanol gasoline, ethanol gasoline and ethanol diesel oil.    ADVANTAGE - The vehicle fuel active agent exhibits low temperature resistance and stable performance.
NOVELTY - A lasofoxifene midbody (IV) preparation method involves performing grignard reaction on a bromine substituted phenyl compound (I) in presence of magnesium. The substituted phenyl compound (I) is reacted with 6-methoxyl tetralone to obtain nitrogen substituted phenyl compound (II) or inorganic acid salt. The nitrogen substituted phenyl compound (II) is dissolved in organic solvent. Bromination is performed in presence of bromating agent to obtain bromine substituted phenyl compound (III) or inorganic acid salt. The bromine substituted phenyl compound (III) is dissolved in organic solvent.    USE - Method for preparing lasofoxifene midbody.    ADVANTAGE - The method enables preparing lasofoxifene midbody in a low-cost and eco-friendly manner, and is suitable for mass production.    DETAILED DESCRIPTION - A lasofoxifene midbody of formula (IV) preparation method involves performing grignard reaction on a bromine substituted phenyl compound of formula (I) in the presence of magnesium. The substituted phenyl compound of formula (I) is reacted with 6-methoxyl tetralone to obtain nitrogen substituted phenyl compound of formula (II) or inorganic acid salt. The product is dissolved in organic solvent, where the organic solvent is tetrahydrofuran or 1,4-dioxane. Bromination is performed in presence of bromating agent to obtain bromine substituted phenyl compound of formula (III) or inorganic acid salt. The bromine substituted phenyl compound of formula (III) is dissolved in the organic solvent. Coupling reaction is performed with phenylboronic acid in presence of inorganic alkali to prepare compound of formula IV or inorganic acid salt, where the inorganic acid is hydrochloric acid or hydrobromic acid..
NOVELTY - Foliar organic fertilizer is prepared by mixing (in wt.%): biological amino acid (10-15), biological protein mixture (30-35), EM mixture (10-15) and JS-activator (5-10), and fermenting and chelating the mixture. The biological protein mixture is prepared by mixing marine algae extract (20-30), soybean extract (60-70) and animal protein (5-10). The EM mixture is prepared using 10-15 kg of EM primary liquid, 5-10 kg of brown sugar, secondary macro nutrients (10-15) and chelated micronutrients (3-6).    USE - The foliar organic fertilizer is useful for promoting root formation, sprout formation and fruit formation, strengthening seedling and protecting fruit (claimed).
NOVELTY - Treating waste, comprises obtaining landfill and/or fuel from fed waste material by: separating the waste material into at least one first fraction having waste portions above predetermined waste portion size, and into a second organic rich fraction having waste portions below the predetermined waste portion size; separating the second fraction into at least one organic rich fine and coarse fraction; fermenting the organic rich coarse fraction by dry fermentation; and further treating the fermented residue of the dry fermentation, together with previously separated organic rich fine fraction.    USE - The method is useful for treating waste.    ADVANTAGE - The method: is simple; produces reusable biogas in a cost-efficient manner; and does not requires energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic flow diagram of treating waste. Drawing includes non-English language text.    Fraction rich in organic material (AA)    Fraction for further treatment or processing (BB)    Coarse fraction rich in organic material (CC)    Fine fraction rich in organic material (DD)    Fermentation residue (EE)
NOVELTY - Fuel composition comprises 50-99% fuel formed by four-carbon-atom alcohols like n-butanol, isobutanol, secondary-butanol or tert.-butanol, 0.5-5.0% of one or multiple additives like triethylene glycol dinitrate (TEGDN), tetraethylene glycol dinitrate or their mixture. 0.005-1.0% of one or multiple additives selected from carboxylic acid, amine and oleic acid-based mixed ethoxylated amine, carboxylic acid ester, polyethylene glycol or polypropylene glycol or their mixture are also included.    USE - Fuel composition for diesel-cycle motors (claimed) in urban transport or motorway vehicles.    ADVANTAGE - The fuel composition ensures improved security and reduced evaporation losses, replaces fossil fuels, reduces emissions of carbon compounds, adequate intake and competitive cost and maintains life of system components. The fuel composition can be produced from a renewable biological source using biotechnology methods, including fermentation of sugars or materials available in sugar-alcohol manufacturing plants.    DETAILED DESCRIPTION - Fuel composition comprises 50-99% fuel formed by four-carbon-atom alcohols like n-butanol, isobutanol, secondary-butanol or tert.-butanol, 0.5-5.0% of one or multiple additives like triethylene glycol dinitrate (TEGDN), tetraethylene glycol dinitrate or their mixture. 0.005-1.0% of one or multiple additives selected from carboxylic acid, amine and oleic acid-based mixed ethoxylated amine, carboxylic acid ester, polyethylene glycol or polypropylene glycol or their mixture are also included. 0.0005-1 0% of a stabilizer additive is selected form ethanolamine, diphenylamine, diphenylurea or morpholine, and 0.0005-1.0% of one or multiple additives selected from polyether based mixed carboxylic acid amides, are also included in the fuel composition.
NOVELTY - The chamber (16) has a pyrolysis reaction zone positioned upstream of a combustion reaction zone and including a plasma torch (22). The combustion reaction zone is positioned upstream of a carbon layer support that is positioned upstream of a synthesis gas (syngas) collection chamber. A syngas heater in an inlet in fluid communication with the syngas collection chamber. The syngas heater is positioned in the pyrolysis reaction zone such that heat from the pyrolysis reaction zone heats syngas flowing through the syngas heater.    USE - Plasma assisted gasification reaction chamber for a modular, syngas powered, power generation system (claimed) to produce clean synthetic gas using waste products as petroleum based fuel within an internal combustion engine e.g. turbine engine and diesel engine.    ADVANTAGE - The chamber is designed such that cooling systems within a gasification system are operated until the chamber is cold to prevent damage and filters can be replaced. The chamber is designed such that household rubbish can be used as shredded fuel to create syngas, thus reducing diesel fuel consumption in power generation, and eliminating rubbish with minimal contaminant discharge in air while allowing the gasification system to reduce contaminates in the syngas, and hence producing the syngas that requires less filtering and is more readily usable in an engine without requiring extensive filtering and with fewer contaminates while improving the work efficiency of the engine without negatively impacting the chamber.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a plasma assisted gasification system.    Plasma assisted gasification system (10)    Controlled zone gasification reactor (12)    Plasma assisted gasification reaction chamber (16)    Plasma torch (22)    Fuel dryer (130)    Flare (140)
NOVELTY - Isolation of highly pure potassium sulfate from potassium sulfate-containing sludge during the treatment of residues from biodiesel production, where the method is performed in two spatial and/or time separate steps, comprises heating potassium sulfate-containing sludge in the first step under non-oxidizing conditions at a material temperature of 400-700 degrees C; and in a second step heating the product from the first Step under oxidizing conditions at a material temperature of 700-900 degrees C.    USE - The method is useful for the isolation of highly pure potassium sulfate from potassium sulfate-containing sludge during treatment of residues from biodiesel production.    ADVANTAGE - The organic constituents from the sludge residue can be completely separated from the biodiesel production, and at the same time the degradation of sulfate present in the treated fuel mixture is prevented.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for the isolation of highly pure potassium sulfate from potassium sulfate-containing sludge during the treatment of residues from biodiesel production.    DESCRIPTION OF DRAWING(S) - The figure shows a flow diagram of the procedure for obtaining potassium sulfate from biodiesel production (Drawing includes non-English language text).
NOVELTY - Process intensification of biogas plant, preferably for increasing loading rate, comprises adding adaptation triggering substrates for controlled replication of acetogenic microorganisms, which causes the degradation of inhibiting higher molecular weight carboxylic acids with 3-6C, and thus accelerates a process adaptation of the biocoenosis in the subsequent high-load range of the fermentation.    USE - The method is useful for process intensification of the biogas plant, preferably for increasing loading rate.    ADVANTAGE - The method: operates at higher loading rates than the conventional methods; exhibits improved space-time yield; and can be carried out in devices exhibiting small dimensions.
NOVELTY - Sludge resource treatment process comprises conveying sludge to drying machine to dry at low temperature; separating sludge and smoke via gas-solid separator; drying separated sludge; keeping retort furnace temperature at 150-800 degrees C, under oxygen or no oxygen distillation; conducting cracking reaction to organic sludge to generate high heat value of combustible gas; and after distilling by slag, cooling the rest solid to 50 degrees C to obtain carbon.    USE - Sludge resource treatment process.    ADVANTAGE - The method uses sludge drying and distilling technology to make sludge into biological carbon for improving soil, thus thoroughly solving difficult sludge treatment. The method does not need post treatment requirement and secondary pollution, has low treatment cost, can thoroughly change the sludge waste into treasure, and realizes the resource recycling.    DETAILED DESCRIPTION - Sludge resource treatment process comprises:    (A) conveying sludge to a drying machine to dry at low temperature;    (B) separating the sludge and smoke from drying machine via gas-solid separator;    (C) drying separated sludge;    (D) keeping retort furnace temperature at 150-800 degrees C, under oxygen or no oxygen distillation;    (E) conducting cracking reaction to organic sludge in sewage treatment process to generate high heat value of combustible gas, where combustible gas is used as fuel, and discharging dry product produced by flue gas via waste heat and purifying; and    (F) after distilling by slag, cooling the rest solid to 50 degrees C to obtain carbon.    DESCRIPTION OF DRAWING(S) - The drawing is a block diagram of a sludge resource treatment process (Drawing includes non-English language text).
NOVELTY - A recombinant mutant ketol-acid reductoisomerase (KARI) enzyme of a 491 amino acid sequence (SEQ ID NO: 63) fully defined in the specification, is new. The enzyme has a ketol-acid reductoisomerase HMM search profile E-value of less than 10-3 using hidden markov model (HMM) search program and comprises at least one mutation within phosphate binding loop, where at least one mutation comprises a substitution at Thr residue at position 52 of a 338 (SEQ ID NO: 17) fully defined in the specification.    USE - The recombinant mutant KARI enzyme is useful for producing isobutanol (claimed) which is used as fuel or fuel additive.    DETAILED DESCRIPTION - A recombinant mutant ketol-acid reductoisomerase (KARI) enzyme of a 491 amino acid sequence (SEQ ID NO: 63) fully defined in the specification, is new. The enzyme has a ketol-acid reductoisomerase HMM search profile E-value of less than 10-3 using hidden markov model (HMM) search program and comprises at least one mutation within phosphate binding loop, where at least one mutation comprises a substitution at Thr residue at position 52 of a 338 (SEQ ID NO: 17) fully defined in the specification. The Thr residue is substituted to a polar, negatively charged amino acid. INDEPENDENT CLAIMS are included for the following:    (1) host cell comprising the recombinant mutant KARI enzyme; and    (2) method for producing isobutanol, involves (a) providing a recombinant yeast microorganism comprising an engineered isobutanol biosynthetic pathway comprising the recombinant mutant KARI enzyme, and (b) culturing the recombinant yeast microorganism under conditions for producing isobutanol.
NOVELTY - A sewage purifying device comprises cylinder (1), sewage inlet pipe and N layer resin curing laccase filter layer (4). The filter layer is composed of a filter screen inside for resin curing laccase. The filter layer has a circular shape. Sewage inlet pipe of the main body is provided with purifying barrel, and the sewage inlet pipe of the water purifying barrel is higher than top of the box body.    USE - Device used for purifying sewage, particularly textile dyeing wastewater or papermaking industry wastewater.    DETAILED DESCRIPTION - A sewage purifying device comprises cylinder (1), sewage inlet pipe and N layer resin curing laccase filter layer (4). The filter layer is composed of a filter screen inside for resin curing laccase. The filter layer has a circular shape. Sewage inlet pipe of the main body is provided with purifying barrel, and the sewage inlet pipe of the water purifying barrel is higher than top of the box body. A sewage water inlet pipeline of the water purifying barrel from bottom surface of the box is d, where d is a positive number. Each layer of filter layer is located in purifying barrel. The N layers of filter layer is sleeved and fixed on the sewage inlet pipe (2). The filter layer is solidified laccase filter layer with bottom surface of purifying barrel N layer between the water pipe and water seal connected with N layer resin curing the outer edge of the purification cylinder laccase of the filtering layer in sealing connection with inner ring wall located at the most upper layer of the filter layer and connected with purifying cylinder of purifying column between top box side wall of purified water outlet, where N is a positive integer.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of sewage purifying device.    Cylinder (1)    Sewage inlet pipe (2)    Purified water outlet pipe (3)    Laccase resin filter layer (4)
NOVELTY - A municipal solid waste is processed by pretreatment and hydrothermal steps in which the original domestic garbage is sieved after removing large block garbage, and placed into garbage wet microwave sample preparation system for high-temperature high-pressure hydrothermal treatment for 1-2 hours at 160-230 degrees C; and dehydrating; passing bulky garbage through magnetic separation machine to separate non-ferrous metal; performing pyrolysis and gasification step; and removing generated biomass gas tar.    USE - Method for comprehensive processing for municipal solid waste (claimed).    ADVANTAGE - The method is harmless and is capable of preventing generation of dioxin. It does not need additional fuel, thus reducing burning cost.    DETAILED DESCRIPTION - Comprehensive processing for municipal solid waste comprises:    (A) pretreatment and hydrothermal steps in which the original domestic garbage is sieved after removing large block garbage, and placed into garbage wet microwave sample preparation system for high-temperature high-pressure hydrothermal treatment for 1-2 hours at 160-230 degrees C; and dehydrating;    (B) passing bulky garbage through magnetic separation machine to separate non-ferrous metal;    (C) performing pyrolysis and gasification step, in which the sieved material is placed into pyrolysis gasification furnace and dried at 120 degrees C;    (D) removing generated biomass gas tar, and performing desulfurization through fume purifying device; and    (E) supplying gas turbine generator with power.
NOVELTY - The method involves measuring the photodiode output signal at a first concentration and a different second concentration of the analyte gas within a gas sample receiving chamber (4). The photodiode calibration data and LED calibration data are determined.    USE - Method of calibrating optical absorption gas sensor for detecting analyte gas e.g. carbon dioxide. Can also be used for carbon monoxide, methane and water vapor.    ADVANTAGE - By determining photodiode calibration data and LED calibration data , the analyte gas can be detected with high efficiency. The process effectively reduces the cost.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method of operating optical absorption gas sensor;    (2) method of measuring concentration of analyte gas; and    (3) optical absorption gas sensor.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the optical absorption gas sensor.    Optical absorption gas sensor (1)    Main portion (2)    Gas sample receiving chamber (4)    Aperture (6)    LED (8)
NOVELTY - The apparatus (10) has a tank that generates hydrogen and oxygen gas in water e.g. tap water (11). The inlet and ejection opening portions (22,23) of a container (12) are connected with each other through a circular flow path (24). The water is circulated between container and circular flow path through a rotodynamic pump (25). A porous element is formed at the edge portion of circular flow path while connecting tank with the circular flow path. The hydrogen and oxygen gas mixed in an electrolytic vessel (13) is supplied to the container through a supply flow path (26).    USE - Hydrogen-dissolved water manufacturing apparatus for dissolving hydrogen gas in water used in medical and household applications.    ADVANTAGE - The dissolving efficiency of hydrogen gas in water can be improved effectively, since hydrogen and oxygen gas mixed in electrolytic vessel is supplied to the container through supply flow path. The power consumption of hydrogen-dissolved water manufacturing apparatus can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the hydrogen-dissolved water manufacturing apparatus. (Drawing includes non-English language text)    Hydrogen-dissolved water manufacturing apparatus (10)    Water (11)    Container (12)    Electrolytic vessel (13)    Inlet and ejection opening portion (22,23)    Circular flow path (24)    Rotodynamic pump (25)    Supply flow path (26)
NOVELTY - A hydrogen gas manufacturing apparatus (10D) comprises a carbonization furnace (3) which heats and thermally decomposes biomass and produces hydrogen, carbon dioxide, and carbon monoxide and a shift reaction part (4) sent out to the hydrogen gas user side with hydrogen and carbon dioxide produced from the carbonization furnace. Carbon monoxide produced from the carbonization furnace and supplied water vapor are made to react to produce carbon dioxide and hydrogen.    USE - A hydrogen gas manufacturing apparatus (claimed).    ADVANTAGE - Hydrogen can be manufactured without releasing carbon dioxide, power consumption is reduced significantly, and cost of hydrogen production is decreased.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a hydrogen gas manufacturing apparatus. (Drawing includes non-English language text).    Carbonization furnace (3)    Shift reaction part (4)    Hydrogen gas manufacturing apparatus (10D)
NOVELTY - An environment-friendly liquid insecticidal fertilizer comprises (parts): solid potassium hydroxide (7-12), triglycolamic acid (1-3), isopropanol (30-35), tea oleic acid (40-45), monopotassium phosphate (5-7) and water (30-38).    USE - As a liquid insecticidal fertilizer, used to kill pest selected from leaf pest such as aphid, trialeurodes vaporariorum, and red; and lawn pest such as ants, slug and other soft insect.    ADVANTAGE - The liquid insecticidal fertilizer is environment-friendly; has high pesticidal efficiency without toxicity to human and plants; has easy operations; is easy to manufacture; is safe to use; and exhibits synergistic effect.
NOVELTY - Producing bio-charcoal based slow-release nitrogen fertilizer involves thermally cracking or gasifying dry sawdust of maize straws or waste apple tree branches to obtain the bio-charcoal; feeding hot water (100 parts) at 80-100 degrees C to ammonium nitrate (200 parts) to prepare an ammonium nitrate solution with a concentration of 22%; and mixing bio-charcoal (100 parts) with ammonium nitrate (63-82 parts) solution, stirring them uniformly, and drying the mixture to obtain the finished products.    USE - For producing bio-charcoal based slow-release nitrogen fertilizer.    ADVANTAGE - The process is simple, and has low cost. The nitrogen of the nitrogen fertilizer loaded by the bio-charcoal has a release slowing effect, reduces nitrogen loss, and improves the utilization rate of the nitrogen fertilizer. The bio-charcoal is detained in the soil that plays the role of carbon fixation and carbon emission reduction, thus relieves climate warming, and provides real green fertilizer. The ammonium nitrate provides prolong fertilizer nutrient period, and reduces the nutrient loss. The process provides fertilizer that is low cost, reproducible, and rich resource. The fertilizer improves soil fertility; makes biological fixation of atmospheric carbon dioxide which is difficult to degrade; and decreases the temperature of the gas emission room, and climate warming.
NOVELTY - Cosmetic preparation (A) comprises (a) bis-ethylhexyloxyphenol methoxyphenyl triazine and (b) propane and/or butane.    USE - (b) is useful to reduce textile staining cosmetic preparations containing (a) (claimed). (A) is useful as sunscreen.    ADVANTAGE - (A) easily washes the textiles, preferably T-shirts, bath sheets and towels without any yellow color.
NOVELTY - A pressure swing adsorption (PSA) apparatus is operated by removing unnecessary gas containing carbon monoxide (CO) from hydrogen-containing gas (A) by supplying hydrogen-containing gas into adsorption tower (1, 1a-1c) from CO adsorption agent layer (3) side of each adsorption tower, wherein adsorption agent bed (2) adsorbs by pressure-reducing the inside of an adsorption tower from CO adsorption agent layer side of each adsorption tower to less than the atmospheric pressure, and manufacturing highly purified hydrogen gas (B).    USE - An operating method of pressure swing adsorption apparatus for highly purified hydrogen gas manufacture used for fuel cells.    ADVANTAGE - Impurity in manufactured hydrogen gas and loss of hydrogen gas product are reduced.    DETAILED DESCRIPTION - A pressure swing adsorption (PSA) apparatus is operated by removing unnecessary gas containing carbon monoxide (CO) from hydrogen-containing gas (A) by supplying hydrogen-containing gas into adsorption tower (1, 1a-1c) from CO adsorption agent layer (3) side of each adsorption tower, wherein adsorption agent bed (2) adsorbs by pressure-reducing the inside of an adsorption tower from CO adsorption agent layer side of each adsorption tower to less than the atmospheric pressure, and manufacturing highly purified hydrogen gas (B). The inside of greater than or equal to 3 adsorption towers has pressure greater than atmospheric pressure, and greater than or equal to 1 adsorption tower stops the operation of PSA apparatus in the state of adsorption pressure of unnecessary gas from hydrogen-containing gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a PSA apparatus which employs an adsorption tower. (Drawing includes non-English language text).    Adsorption tower (1, 1a-1c)    Adsorption agent bed (2)    CO adsorption agent layer (3)    Hydrogen-containing gas (A)    Highly purified hydrogen gas (B)
NOVELTY - Integrated domestic sewage treatment device comprises a box body (1), where the two ends of the box body are respectively provided with an inlet (2) and an outlet (3). The box body is provided with a first clapboard (4) and a second clapboard (5), where the first clapboard and the second clapboard divides the box body into the first chamber, the second chamber and the third chamber. The first and the second chambers are provided with a first circulating pipe. The second and the third chambers are provided with a second circulating pipe. The top of the box body is provided with vent holes.    USE - Used as an integrated domestic sewage treatment device.    ADVANTAGE - The device: is simple with mobile installations; has low operating costs; is acid and alkali resistant and leak proof.    DETAILED DESCRIPTION - Integrated domestic sewage treatment device comprises a box body (1), where the two ends of the box body are respectively provided with an inlet (2) and an outlet (3). The box body is provided with a first clapboard (4) and a second clapboard (5), where the first clapboard and the second clapboard divides the box body into the first chamber, the second chamber and the third chamber. The first chamber and the second chamber are provided with a first circulating pipe. The second chamber and the third chamber are provided with a second circulating pipe. The first chamber and the second chamber are respectively provided with a biochemical treatment filling material. The top of the box body is provided with vent holes.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of the integrated domestic sewage treatment device.    Box body (1)    Inlet (2)    Outlet (3)    First clapboard (4)    Second clapboard (5)
NOVELTY - Kitchen waste processing system comprises e.g. a feeding device, a crushing device, a box body, a magnetic separation device, a mounting device, a fermentation device, an electric control device and an exhaust device, where the feeding device is connected with the crushing device, which is connected with the magnetic separation device, and the magnetic separation device is connected with the mounting device. The electric control device is respectively connected with feeding device, crushing device, magnetic separation device, mounting device, fermentation device and exhaust device.    USE - Useful as kitchen waste processing system.    ADVANTAGE - The system processes kitchen waste in presence of microorganisms, and thus it prevents kitchen waste pollution.    DETAILED DESCRIPTION - Kitchen waste processing system comprises a feeding device, a crushing device, a box body, a magnetic separation device, a mounting device, fermentation device, an electric control device and an exhaust device, where the feeding device is connected with the crushing device, which is connected with the magnetic separation device, the magnetic separation device is connected with the mounting device, and the mounting device is connected with the fermentation device. The electric control device is respectively connected with the feeding device, the crushing device, the magnetic separation device, the mounting device, the fermentation device and the exhaust device.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of the kitchen waste processing system.
NOVELTY - An amount of biologically-derived oil comprising triglycerides is provided. The biologically derived oil is processed so as to transesterify (102) at least some of the triglycerides to yield saturated monoesters and unsaturated monoesters. At least some of the unsaturated monoesters is oligomerized (103) to obtain fatty acid ester oligomer. At least some of the saturated monoesters is separated (104) from the fatty acid ester oligomer. At least some of the fatty acid ester oligomer is hydrotreated to obtain alkane.    USE - Manufacture of fuel and base oil blendstock.    ADVANTAGE - The fuel and base oil blendstock is manufactured at high yield.    DESCRIPTION OF DRAWING(S) - The drawing shows the flowchart of manufacture of fuel and base oil blendstock.    Providing biologically derived oil (101)    Transesterification (102)    Oligomerization (103)    Separation (104)    Conversion (104a,105)
NOVELTY - A Bacillus sp. Q2 (CCTCC M2011239) capable of degrading quinoline, is new.    USE - The Bacillus sp. Q2 is useful for degrading quinoline in industrial wastewater, preferably refinery wastewater, coking wastewater and coal tar processing wastewater (all claimed).    ADVANTAGE - The Bacillus sp. Q2 degrades 500 mg/l of quinoline completely within 30 hours, exhibits tolerance with respect to 1400 mg/l of quinoline, and has wide application.    DETAILED DESCRIPTION - A Bacillus sp. Q2 (CCTCC M2011239) capable of degrading quinoline, is new. The Bacillus sp. Q2 comprises rDNA which has GenBank (RTM: National institute of health nucleotide sequence database) number (JN132107). The Bacillus sp. Q2 is Gram-positive, comprises milky, tidy, circular, smooth and wet colony and convex centre. The Bacillus sp. Q2 exhibits positive in hydrogen sulfide test, V-P test and nitrate reduction test, and negative in indole test, methyl red test and starch hydrolysis test. The Bacillus sp. Q2 is capable of using the quinoline as carbon source, nitrogen source and energy source to grow and proliferate.
NOVELTY - The device has a hand wheel (3) connected with a stirring impeller extending in an anaerobic reaction tank (1). A movable air chamber is located in channel with vertical penetrating opening formed by steel made air chamber containing box (2) and anaerobic reaction tank. The outer side wall surface of movable air chamber is slidingly contacted with the edge of internal channel. The air chamber is connected with top cavity of anaerobic reaction tank. The air chamber and anaerobic reaction tank are provided with a locating guide device for lifting air chamber.    USE - Organic garbage biological treatment device.    ADVANTAGE - No energy is consumed by the organic garbage biological treatment device. The structure of the organic garbage biological treatment device is simplified. The manufacturing cost of the organic garbage biological treatment device is reduced. The application range of the organic garbage biological treatment device is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the organic garbage biological treatment device.    Anaerobic reaction tank (1)    Air chamber containing box (2)    Hand wheel (3)    Baffle (9)    Gas-water separator (10)
NOVELTY - The method involves filling light granular filter medium in a biochemical system to form a filter material layer in a filter area, where the biochemical system is divided into a filtering zone, a mixing zone and a sludge accumulation area. A water discharge pipe is connected in an upper side of the filter material layer. A lower part of a filter material layer mixing zone is connected with a sewage inlet pipe system. The sewage inlet pipe system is equipped with a sullage pipe. Accumulation area sludge is exhausted from a bottom portion of a slag part.    USE - High-effective energy-saving light particle medium filtering method.    ADVANTAGE - The method enables processing high turbidity sewage in an effective manner, thus providing better quality to water discharged from the biochemical system.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biochemical system.
NOVELTY - A Bacillus stearothermophilus strain A11 (CGMCC 5309) is used in producing hydrogen by sludge or organic waste fermentation which comprises sludge or organic waste pretreatment and hydrogen generation method. The sludge or organic waste pretreatment step comprises inoculating thermophilic Bacillus strain in the sludge or organic waste at 50-70 degrees C for 2-24 hours to obtain thermophilic Bacillus hydrolyzed sludge or organic waste.    USE - Bacillus stearothermophilus strain A11 (CGMCC 5309) used in producing hydrogen by fermenting sludge or organic waste (claimed).    ADVANTAGE - The thermophilic Bacillus strain allows effective filtration of sludge for efficient production of hydrogen and can also inhibit growth of bacteria and kill pathogen in sludge or organic waste. The produced hydrogen has high purity and high yield and short production period.
NOVELTY - Fuel ethanol is produced by pretreating corn straw with propionic acid in presence of catalyst and digesting corn straw for 90 minutes, then filtering, and washing filtered slag using water and acetone until the pH value is neutral to obtain cellulose material; inoculating cellulose using Trichoderma reesei strain TJ'K-108 spore suspension liquid and performing solid culturing for 7 days at 30 degrees C; and using the processed corn straw as substrate and mixing with cellulose, adding water, then inoculating using saccharomycetes, and fermenting for 60-72 hours at 32-36 degrees C to obtain ethanol.    USE - Method of producing fuel ethanol (claimed).    DETAILED DESCRIPTION - Production of fuel ethanol comprises: (A) air-drying corn straw and crushing; (B) pretreating the corn straw with propionic acid (900 g/L) in presence of catalyst (3 g/L) and digesting the corn straw for 90 minutes, where material to liquid ratio is 1:12, then filtering, and washing filtered slag using water and acetone until the pH value is neutral to obtain cellulose (90.68%), hemicellulose and lignin; (C) inoculating cellulose using Trichoderma reesei strain TJ'K-108 spore suspension liquid (1.8x 10 colony forming unit/g substrate) and performing solid culturing for 7 days at 30 degrees C; and (D) using the processed corn straw as substrate and mixing with cellulose, adding water, then inoculating using saccharomycetes, and fermenting for 60-72 hours at 32-36 degrees C to obtain ethanol (0.326 g/g substrate).
NOVELTY - The chamber has a plate valve connected with a high and low position level detector. The high and low position level detector is fixed with a rubbish storage bin. A primary gasification zone is provided a scrapping-type grate, a chain furnace and an automatic leveling device. Three plasma torches are mounted on a gas purifying device. The plasma torches and the gas purifying device are located on a same horizontal plane to form gas refining area. The horizontal plane and a ground surface are inclined together at an angle of 45-120 degrees. Diameter of the gas refining area is 100-200 mm.    USE - Horizontal plasma rubbish gasification reaction chamber.    ADVANTAGE - The plasma torches are utilized for generating gas and slag by utilizing rubbish heat value gas, thus removing harmful gas generating and increasing product yield. The chamber reduces residue wastage and processing and operating cost and purifies gas in an effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a gasification method for a horizontal plasma rubbish gasification reaction chamber.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial sectional side view of a horizontal plasma rubbish gasification reaction chamber.'(Drawing includes non-English language text)'
NOVELTY - A domestic waste wet treatment and resource utilization method involves taking gas and water as work medium water for mixing and pre-treating household waste, and removing large specific gravity impurity. The household waste is hydraulic crushed, filtered and washed for separating the household waste into waste, organic slurry and brick block type particles. The obtained component is treated and recycled.    USE - Method for wet treating and resource utilizing domestic waste.    ADVANTAGE - The method enables quickly and effectively processing domestic waste treatment and resource utilization, thus preventing serious environment pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a domestic waste wet treatment and resource utilization method.'(Drawing includes non-English language text)'
NOVELTY - A celastrol is used for preparing medicine to treat cerebral gliomas.    USE - Celastrol used for preparing medicine to treat cerebral gliomas, for restraining endogenous cannaboid hydrolase fatty acid amide hydrolase and monoglyceride lipase level, for increasing N-arachidonylethanolamine and 2-arachidonoylglycerol content of endogenous cannaboid, for restraining expression of cannabinoid type 1 and promoting expression of cannabinoid type 2, and inducing cell apoptosis of multiple cerebral gliomases (claimed).    ADVANTAGE - The use of celastrol has high raw material utilization rate, low cost and high product purity. Preparation of celastrol is environment-friendly and simple, and suitable for industrial production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of celastrol comprising:    (A) mixing and crushing ground vine part and underground root part of celastrol, ethanol refluxing and extracting, filtering and decompressing. and condensing;    (B) mixing condensed ethanol extract with ethanol by ultrasonic wave, and standing and pouring supernatant;    (C) separating supernatant using absorbing resin, rinsing with ethanol and water, and collecting rinsing solution;    (D) decompressed condensing the rinsing part, purifying with silica gel column chromatography, recovering solvent, and drying to obtain red powder extract; and    (E) dissolving the extract into saturated or unsaturated solution using hot ethanol, standing and separating the red crystal, and drying.
NOVELTY - An aminophenol calcium fertilizer preparing method involves concentrating coenzyme Q10 fermentation liquor using a polyethylene (PE) device. The fermentation liquor is nano-filtered. The coenzyme Q10 yeast waste liquid is adjusted to pH value of 6-8.0 to remove large flocculant precipitate. Fibroin powder is added in concentrated solution Q10 coenzyme and uniformly stirred to obtain needed amino acid calcium fertilizer.    USE - Method for preparing aminophenol calcium fertilizer.    ADVANTAGE - The method enables reducing pollution of waste liquor to environment, promoting seed germination, increasing crop output and improving stress resistance of crops.
NOVELTY - An earthworm breeding method involves constructing an earthworm shed similar to a vegetable greenhouse with 5m wide, 30-60m long, middle path of 0.7-1m, and 2m wide for two sides of an earthworm bed. Pig dung and cow dung of 5-10wt.% are crushed and uniformly mixed with grass. The mixed dung is continuously fermented for 7-10 days to obtain fermented pig manure that is utilized for feeding earthworm. The prepared manure is poured into the earthworm bed. The earthworm with excrement material is stacked in a plastic film that is subjected to light for 15-20 minutes to obtain clean earthworm.    USE - Method for breeding earthworm in a greenhouse.    ADVANTAGE - The method enables realizing the breeding of earthworm by feeding the pig and cow dung as the manure for the earthworm.
NOVELTY - A method for comprehensively utilizing water in ammonium sulfate involves utilizing a vacuum pump for sulfur and phosphorus content as a secondary water cooling pump, where the amount of sulfur and phosphorus content is 10-30 mg/l. Sealing water is utilized as circulating water that is complemented water. Circulating water, ammonium sulfate and waste water are utilized as supplementary of washing water.    USE - Method for comprehensively utilizing water in ammonium sulfate for use in an ammonium sulfate production enterprise.    ADVANTAGE - The method enables realizing better draining effect, avoiding generation of pollution, saving fresh water, efficiently recycling waste nitrogen element-contained substance in the water, improving the ammonia nitrogen utilization rate, and saving cost. The method enables satisfying requirements of recycling economy.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic illustration of a method for comprehensively utilizing water in ammonium sulfate.'(Drawing includes non-English language text)'
NOVELTY - An aerobic compost air distributing device has a transverse ventilation pipe (6) provided with a compost bed body (5) and formed with air outlet holes (7). An air distributing groove (1) of the ventilating pipe is connected with an outer wall of a supporting leg (3). The supporting leg is connected with the ventilation pipe. The air distributing groove is provided with an air-permeable layer (4) and filled with aerobic compost. The air distributing groove is formed parallel to the compost bed body.    USE - Aerobic compost air distributing device.    ADVANTAGE - The device increases a contact area of gas and a stack material from an outlet, so that gas from the ventilating pipe provides high wind speed to prevent deposition of material blockage, and the gas enters into a composting material, improves compost efficiency and reduces energy consumption by a large diffusion surface. The device has reasonable structure, low production cost and operation cost, and is convenient to install and easy to operate.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial sectional view of an aerobic compost air distributing device.    Air distributing groove (1)    Supporting leg (3)    Air-permeable layer (4)    Compost bed body (5)    Transverse ventilation pipe (6)    Air outlet holes (7)
NOVELTY - Dry aerosol shampoo comprises (in mass%) normal butane (14-18), dimethyl ether (12-16), isobutane (18-22), modified corn starch (10-14), propane (12-16), absolute ethanol (15-19), cyclo methyl silicone (0.1-0.3), octadecyl dimethyl ammonium chloride (0.2-0.4) and essence (0.1-0.3).    USE - Used as a dry aerosol shampoo.    ADVANTAGE - The shampoo has corrosion action to the tin and aluminum container. The method is simple and has good cleaning phenomenon.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing dry aerosol shampoo, comprising (i) mixing normal butane, isobutane, propane and dimethyl ether in a gas tank to prepare propellent; (ii) taking the absolute ethanol, and adding the modified corn starch, octadecyl dimethyl ammonium chloride and essence, stirring, and feeding them into a packaging machine via a 25 mu filtering net, packaging according to the pre-determined packaging quantity, and loading, sealing the tank and filling the propellent obtained in step (i) to obtain the dry aerosol shampoo.
NOVELTY - Method for preparing salicylamide involves adding methyl salicylate and toluene in the ratio of 1:2.8-3.2 in reactor, heating the mixture at 40-45 degrees C, continuously injecting ammonia in the reactor and performing amination reaction at 0.25-0.35 mPa and 40-45 degrees C for 5-6 hours, recycling toluene and byproduct (methanol), cooling residual material to 20-25 degrees C, crystallizing the material at 40-45 degrees C and centrifuging the material to obtain salicylamide.    USE - The method is useful for preparing salicylamide.    ADVANTAGE - The method is environmentally-friendly as it does not produce wastewater and produced toluene and reaction by-product can be recycled and enables production of pure and colorless salicylamide at high yield.
NOVELTY - Composite biodiesel comprises (in wt.%) waste plant and animal oil (10- 45), crude methanol (5-30), a surfactant (5-25), mixed aromatics (5-20), petroleum diesel oil (10-60), acetic acid sec-butyl ester (0.05-2.5) and tert-amyl methyl ether (0.01-2.5).    USE - Used as a composite biodiesel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the composite biodiesel, comprising adding the waste plant and animal oil, crude methanol, surfactant, mixed aromatics, acetic acid sec-butyl ester and tert-amyl methyl ether into a reactor, agitating and mixing, adding the petroleum diesel oil, agitating for 10 minutes, and then adding the reacted materials into a high-energy static mixer and a nano-emulsifying machine for processing.
NOVELTY - An immunogenicity reinforcement method involves connecting a micro-molecule organic matter with protein carrier through a crossing connector, where the crossing connector comprises a linear polymer decorated with active groups and molar mass of the linear polymer is 500-10000 kilo Dalton.    USE - Method for reinforcing immunogenicity of a micro-molecule organic matter (claimed).    ADVANTAGE - The method enables connecting the micro-molecule organic matter with the protein carrier through the crossing connector, so that immunogenicity of the micro-molecule organic matter can be reinforced in an efficient manner. The method enables simplifying reinforcement process and reducing reinforcement cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a reinforced micro-molecule organic matter.
(ES2368314-A1)   NOVELTY - Use of sulfonic acid is claimed for capturing compounds having isonitrile (I).    USE - Used for capturing compounds having isonitrile group (claimed).    ADVANTAGE - The sulfonic acid efficiently synthesizes organic compounds, chemical and pharmaceutical industry with environment characteristic of green chemistry.    DETAILED DESCRIPTION - Use of sulfonic acid is claimed for capturing compounds having isonitrile of formula (I).    R2=independently selected from a group consisting of single bond, substituted or unsubstituted alkyl, substituted or unsubstituted cycloalkyl, substituted or unsubstituted alkenyl, substituted or unsubstituted alkynyl, substituted or unsubstituted aryl, substituted or unsubstituted heterocyclic, -(Ra)N-, -(XCH 2CH2)p-, -(XCH(CH3)CH2)p-;    X=selected from oxygen, sulfur or (R)N;    p=1-5;    Ra=hydrogen, unsubstituted or substituted alkyl or aryl group; and    R3=organic or inorganic polymer matrix, a cationic structure or a perfluoro structure.    An INDEPENDENT CLAIM is also included for a method for preparing organic compound of formula (II), which involves reacting compound of formula (I) with compound of formula (III).
NOVELTY - Fruit and vegetable ecological matrix is claimed.    USE - The ecological matrix is used in formulation (claimed) for organic cultivation of living fruit and vegetable and controlling pathogenic microorganisms and parasites.    ADVANTAGE - The ecological matrix contains no chemical pesticide and no substances harmful to environment and human, comprises necessary balancing nutritive elements for living fruit and vegetable, improves quality and yield of fruit and vegetable and income of farmers, and is cost-effective and suitable for large scale industrial production.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) formulation comprising (in %) the above-cited matrix as main raw material (10), earthworm manure and maggot (89), composite biological agent (0.9) and trace elements (0.1); and    (2) method for producing the above-cited matrix, involves post-fermenting humus organic fertilizer using high protein containing recombinant earthworm and maggot and earthworm and maggot (10).
NOVELTY - The method involves mixing fats and oils with biomass and supplying the biomass mixture obtained by the mixing process on the decomposition catalyst accommodated in the catalytic cracking furnace. The heat stirring of decomposition catalyst is carried out by the catalytic cracking process. The cracked gas produced by catalytic cracking is cooled by performing liquefaction process, and the cooled cracked gas is collected as a cracked distillate.    USE - Biomass oil formation method.    ADVANTAGE - The quick catalytic cracking speed of the biomass can be attained. The thermal polymerization of the produced cracked gas can be suppressed. The liquid fuel of the fuel oil can be obtained with high yield. The size reduction and cost reduction of the biomass oil formation apparatus can be realized.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biomass oil-formation apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass oil formation apparatus.    Biomass oil-formation apparatus (1)    Mixer (4)    Fat-and-oil supply unit (5)    Heating unit (10)    Cracked gas pipe (15)
NOVELTY - The gasifier (10) has a punching plate (11) that partitions gasifer interior into top and bottom. A biomass resource supply port (1Oa) supplies biomass resource over punching plate. The oxidation agent supply ports (10c,10d) supply oxidation agent into gasifier. An oxidation agent supply path distributes and supplies oxidizing agent to locations within predetermined range in vicinity of punching plate. A gas discharge port (10b) discharges dry distillation gas generated by the partial oxidation of biomass resource on punching plate to outside.    USE - Gasifier of gasification system (claimed), for gasifying biomass resources.    ADVANTAGE - The gasifier can effectively gasify the biomass resource with low quantity of tar or clinker. The dry distillation gas generated from biomass resources can be discharged effectively to outside. The temperature of the gasifier can be minimized. The gasifier can be manufactured with reduced cost.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) gasification system; and    (2) reformation system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the gasifier of the gasification system.(Drawing includes non-English language text)    Gasifier (10)    Biomass resource supply port (10a)    Dry distillation gas discharge port (10b)    Oxidizing agent supply ports (10c,10d)    Punching plate (11)
NOVELTY - A reactive evaluation method in methane fermentation treatment involves performing methane fermentation treatment of to-be-processed object containing organic substance on anaerobic conditions, producing methane gas, performing methane fermentation treatment of reference material on the same conditions as the methane fermentation treatment of to-be-processed object, and evaluating effectiveness of methane fermentation property about the to-be-processed object with respect to the reference material.    USE - A reactive evaluation method in methane fermentation treatment of organic refuse and sewage sludge.    ADVANTAGE - Reactivity of methane fermentation can be evaluated simply and precisely.
NOVELTY - The pulverization device (10A) has water-content provision unit (13) that supplies the water (12) to biomass pellet (11). A coarse pulverization unit (14A) pulverizes the moistened biomass pellet (11A) to fine powder (11C). The biomass pellet is temporarily stored in hopper (16). The coal (30) is mixed with the biomass pellet by mixing unit. The mixed coal and pellet are conveyed by conveying unit (17,18,27). The granule ground material separated by isolation unit is conveyed to the boiler side by transportation line.    USE - Biomass-pellet pulverization device of biomass/coal mixed combustion system (claimed).    ADVANTAGE - The pulverization can be performed easily and the mixed fuel burning ratio improvement with the coal is attained.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the pulverization device. (Drawing includes non-English language text)    Pulverization device (10A)    Biomass pellet (11)    Moistened biomass pellet (11A)    Fine powder (11C)    Water (12)    Provision unit (13)    Pulverization unit (14A)    Hopper (16)    Conveying units (17,18,27)    Coal (30)
NOVELTY - Fuel additive composition (I) produced by: (a) mixing together, (i) fruit juice containing (x) moles of sugars with cellulose composition, (ii) dilute volume of hydrogen peroxide containing (y) moles of hydrogen peroxide, (iii) iron(II) catalyst, and (iv) diluted sulfuric acid to turn the green iron(II) catalyst solution to yellow/brown iron(III) solution at a pH of approximately 5.5; and (b) holding the solution for greater than or equal to 48 hours in dark at pH of 5-6.5 until the sugars crosslink forming hydroxide, oxygen double bonds and carbonyl groups to produce a dark brown fuel additive, is claimed.    USE - (I) is useful for solid and liquid carbon based fuels (claimed) to improve combustion burning or as a fuel or electrolyte for a fuel cell or battery to produce electricity.    ADVANTAGE - (I) provides a sugar based solution suitable for use with liquid as well as solid carbon based fuels to improve combustion burning, and can be used with or without catalysts, and as a stand alone fuel for fuel cells.    DETAILED DESCRIPTION - Fuel additive composition (I) produced by: (a) mixing together, (i) a given volume of fruit juice containing (x) moles of sugars with cellulose composition, (ii) a dilute volume of hydrogen peroxide containing (y) moles of hydrogen peroxide, where the ratio of moles of sugars to moles of hydrogen peroxide (x/y) selected to provide the desired combustion properties of the resultant fuel additive (iii) an iron(II) catalyst which turns green in the presence of the hydrogen peroxide solution, (iv) sufficient volume of diluted sulfuric acid to turn the green iron(II) catalyst solution to a yellow/brown iron(III) solution at a pH of approximately 5.5; and (b) holding the yellow/brown iron(II) solution for greater than or equal to 48 hours in the dark at a pH of 5-6.5 until the sugars crosslink forming hydroxide, oxygen double bonds, and carbonyl groups to produce a dark brown fuel additive, is claimed.
NOVELTY - The fuel body (10) for burning in a fuel boiler with movable grate, comprises a peelable plant material (95-98 wt.%) such as oats, spelt, paper and/or wood pressed in the fuel body, and additives (2, 3) for reducing slag formation such as lime and/or kaolin pressed with the plant material in the form of cut up particles. The plant material is softened by water vapor. The pressed components of the fuel body are held together by the binding effect of the peelable material.    USE - The fuel body is useful for burning in a fuel boiler with movable grate (claimed).    ADVANTAGE - The fuel body can be economically manufactured with good burn performance.    DETAILED DESCRIPTION - The fuel body (10) for burning in a fuel boiler with movable grate, comprises a peelable plant material (95-98 wt.%) such as oats, spelt, paper and/or wood pressed in the fuel body, and additives (2, 3) for reducing slag formation such as lime and/or kaolin pressed with the plant material in the form of cut up particles. The plant material is softened by water vapor. The pressed components of the fuel body are held together by the binding effect of the peelable material. INDEPENDENT CLAIMS are included for:    (1) a method for preparing the fuel body; and    (2) a device for preparing the fuel body.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a device for preparing the fuel body.    Plant material (1)    Additives (2, 3)    Supply material (5)    Fuel body (10)    Pressing device. (21)
NOVELTY - Composition in dried powder form to improve the composting process of organic waste, to abate the development of unpleasant smells and to obtain a final composted product with enriched fertilizing capacities, comprises one or more nitrogen-based components in the form of nitrate, between 50-90% in weight, except for ammonium-based components, such as ammonium nitrate or ammonium sulfate, urea or other components the decomposition of which leads to the development of ammonia, one or more phosphorus-based components, and one or more potassium-based components.    USE - The composition is useful for improving the composting process of organic waste (claimed).    ADVANTAGE - The composition abates the development of unpleasant smells and the proliferation of insects, and obtains a final composted product with enriched fertilizing capacities.    DETAILED DESCRIPTION - Composition in dried powder form to improve the composting process of organic waste, to abate the development of unpleasant smells and to obtain a final composted product with enriched fertilizing capacities, comprises one or more nitrogen-based components in the form of nitrate, between 50-90% in weight, except for ammonium-based components, such as ammonium nitrate or ammonium sulfate, urea or other components the decomposition of which leads to the development of ammonia, one or more phosphorus-based components, between about 2% and about 18% in weight, and one or more potassium-based components, with the provision that the potassium-based components can coincide, or not, with the one or more nitrogen-based components.
NOVELTY - Utilizing distillation fractions obtained from distillation of tall oil (18) in a biomass-to-liquids (BtL) plant, comprises: utilizing tall oil obtained from cellulose plants; and processing into different fractions and passing the fractions to different points of the BtL process.    USE - The method is useful for producing biofuels, which is used in the gasification step and/or energy generation of the BtL process (claimed).    ADVANTAGE - The method provides high-quality biofuels, and is economical.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for use of tall oil as feedstock in a BtL plant for production of a synthetic biofuel and utilization the biofuel in the gasification step (2) of the BtL process and/or in energy generation (16).    DESCRIPTION OF DRAWING(S) - The figure shows some process diagrammatic view of arrangements for implementing the method.    Gasification step (2)    Fractionating distillation column (12)    Heavier bottoms fraction (15)    Energy generation (16)    Tall oil (18)
NOVELTY - The device has a main exhaust passage provided with an air inlet end and an air outlet end. The air inlet end is connected with a battery cabinet. The battery cabinet generates low density gas exhausted to outer side of a passage. The air outlet end is connected with a part between two air inlets of a supplementary exhaust passage. An auxiliary exhaust channel is provided with an inlet end and an outlet end. The outlet end of the auxiliary exhaust channel is arranged with an exhaust unit for discharging low density gas through the main exhaust passage to external air.    USE - Battery cabinet exhaust device for discharging battery cabinet low-density gas generated by a fuel battery.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a battery cabinet exhaust device.
NOVELTY - A biomass pyrolysis steam condensation system comprises a first stage spraying tower (1), a second stage spraying tower (3) and a bio-oil collecting tank (2). The first stage spraying tower is provided with a biomass pyrolysis steam inlet (4) and a cooling medium high voltage spray nozzle (5), inlet of the bio-oil collecting tank with bio-oil mixture and cooling medium outlet and bio-oil and cooling medium mixture collecting storage tank inlet.    USE - A biomass pyrolysis steam condensation system.    ADVANTAGE - The system has improved bio-oil yield, compact structure and easy arrangement.    DETAILED DESCRIPTION - A biomass pyrolysis steam condensation system comprises a first stage spraying tower (1), a second stage spraying tower (3) and a bio-oil collecting tank (2). The first stage spraying tower is provided with a biomass pyrolysis steam inlet (4) and a cooling medium high voltage spray nozzle (5), inlet of the bio-oil collecting tank with bio-oil mixture and cooling medium outlet and bio-oil and cooling medium mixture collecting storage tank inlet flows into the bio-oil collecting tank from the oil, oil of high density deposition collecting storage tank bottom of the bio-oil, a spraying cooling medium of low density through circulating pump from the oil collection storage tank outlet, arranged in the bio-oil collecting tank top of pyrolysis steam outlet is connected with the second stage spraying tower, a condensing of the bio-oil into bio-oil collecting tank bottom of the second stage spraying tower non-condensed gas outlet.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram of the biomass pyrolysis steam condensation system.    Spraying towers (1, 3)    Bio-oil collecting tank (2)    Biomass pyrolysis steam inlet (4)    Cooling medium high voltage spray nozzle (5)    Cooling medium inlet (8)
NOVELTY - The method involves filling biomass fuel in a cabin when a ball valve is opened. An inlet of an air storage tank is provided with a thermometer. Air adjusting valves and a pressure gauge are arranged in an outlet of the tank. Combustion temperature of a liquid ring compressor is reduced to a lower limit temperature when the adjusting valve is adjusted to a preset size. An opening is formed in a secondary oxidation section air belt. An electric catching focus device is utilized to monitor oxygen content in an oxygen analyzer. Secondary oxidation sections are connected with the adjusting valve.    USE - Method for controlling a biomass gasification device.    ADVANTAGE - The method ensures controlling a biomass gasification device that is inexpensive with high accuracy, high automation degree and safe locating effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a method for controlling a biomass gasification device.'(Drawing includes non-English language text)'
NOVELTY - A tar collecting device comprises pipe, tar collecting tank and smoke pipe. Tar collecting box includes tar collecting pool and smoke box storing tar collecting pool. Cigarette storage box is provided with clapboard. Top and two sides of clapboard are respectively connected with top and side wall of smoke box. A gap is provided between liquid level of clapboard and tar collecting tank. Clapboard separates smoke storage box into smoke chamber and smoke chamber. Inner chamber is provided with 3 layer window.    USE - Tar collecting device for biomass carbonizing furnace.    ADVANTAGE - The furnace has simple structure, convenient operation, and low cost.    DETAILED DESCRIPTION - Tar collecting device comprises pipe, tar collecting tank and smoke pipe. Tar collecting box includes tar collecting pool and smoke box storing tar collecting pool. Cigarette storage box is provided with clapboard. Top and two sides of clapboard are respectively connected with top and side wall of smoke box. A gap is provided between liquid level of clapboard and tar collecting tank. Clapboard separates smoke storage box into smoke chamber and smoke chamber. Inner chamber is provided with 3 layer window, where top part is respectively provided with smoke inlet and smoke is respectively connected with smoke inlet tube and smoke outlet. Carbonization chamber is connected with a combustion chamber.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating a tar collecting device.
NOVELTY - A guide device comprises cylindrical shell body, where 2 ends of shell are provided with a cover. Center of the shell vertical to surface of side part is provided with inlet orifice. Center of shell vertical to the surface of lower side part is provided with outlet. Shell is provided with rotating shaft along axial direction. Two ends of rotating shaft are respectively arranged the central part of cover, where one end of rotating shaft is connected with driving device. Rotating shaft is provided with blade. Amount of feed is not greater than blade rotating one circle to form the volume.    USE - Guide device for biomass carbonizing furnace.    ADVANTAGE - The device can prevent outer air from entering into coking chamber from material inlet and material outlet of carbonization chamber, thus ensuring oxygen-free or oxygen-poor environment in carbonization chamber. It effectively improves biomass raw material in effect and carbonization quality when carbonizing.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating a guide device.
NOVELTY - The method involves carrying out catalytic reaction under the existence of organic solvent and catalyst when the crude biological oil is contained in an omega water system. The reaction temperature is 250-350 degrees centigrade, and the reaction pressure is 16Mpa. Rotating speed of the omega water system is 250750r/min. Oil-water mixture and oil-water separation are mixed to obtain refined oil. Weight of the catalyst is 2 to 20 percent of crude biological oil by weight. The organic solvent is tetrahydronaphthalene or decahydronaphthalene.    USE - Bio-oil refining method.    ADVANTAGE - The method enables reducing water level in the reaction system, thus improving refining effect and refining oil yield.
NOVELTY - Producing pyrolysis oil product from biomass feedstock involves a) subjecting biomass feedstock to thermal treatment in reactor A under torrefaction reaction condition to produce solid and gaseous products; b) subjecting the solid product in reactor B under pyrolysis reaction condition to produce pyrolysis oil; c) subjecting gaseous product in reactor C under combustion reaction condition to produce carbon dioxide, water and heat; and d) recovering/feeding the heat to heat object (O1) selected from e.g. biomass feedstock.    USE - For producing pyrolysis oil product from biomass feedstock selected from wood, paper, crops, animal and plant fats, biological waste and/or algae (claimed).    ADVANTAGE - The process is energy saving; and improves quality of pyrolysis oil.    DETAILED DESCRIPTION - Producing pyrolysis oil product from biomass feedstock involves a) subjecting biomass feedstock to thermal treatment in a reactor A under torrefaction reaction condition to produce mixture product having solid product and gaseous product; b) subjecting the solid product in a reactor B under pyrolysis reaction condition to produce product having pyrolysis oil product; c) subjecting the gaseous product in a reactor C under combustion reaction condition to produce product having carbon dioxide, water and heat; and d) recovering and feeding the heat from step c) to heat an object (O1) selected from biomass feedstock, solid product, gaseous product, pyrolysis products, reactor A, and/or reactor B.
NOVELTY - The gas detector (100) has a light source (102) for emitting a wavelength-modulated light beam (110) into a target region (106). A scanning device (104) scans the light beam emitted by the light source through the target region. A light sensor (112) receives the light returning from the target region via the scanning device. An indicator (124) cooperates with the scanning device to indicate a position of the gas in the target region. A controller (108) detects presence of gas on a path of the light beam based on returning light sensed by the light sensor.    USE - Gas detector for remote detection of gas in target region. Uses include but are not limited to methane, carbon dioxide, carbon monoxide, nitrous oxide, or ethanol.    ADVANTAGE - Provides gas detector that allows for more reliable detection of gas and has potential of reducing time needed for scanning target region by performing automatic scan of target region.    DESCRIPTION OF DRAWING(S) - The drawing is a block schematic diagram of a gas detector.    Gas detector (100)    Light source (102)    Scanning device (104)    Target region (106)    Controller (108)    Light beam (110)    Light sensor (112)    Indicator (124)
NOVELTY - Well-drilling wastewater comprises dosing a composite microbial inoculum in a well-drilling wastewater biochemical reactor (19). The potential of microorganism can be adequately exerted, the biological treatment effect of refractory organic compounds can be improved, and the treatment capacity of a wastewater treatment system can be enhanced.    USE - Method for well-drilling wastewater (claimed).    ADVANTAGE - The method has low cost, fast treatment speed, and simple operation.    DESCRIPTION OF DRAWING(S) - The drawing is a sectional flow diagram of the method for well-drilling wastewater.    Sewage pool (1)    Sewage pump (2)    Coagulant groove (3)    Metering pump (4)    Wastewater biochemical reactor (19)
NOVELTY - Promoting surplus sludge anaerobic digestion comprises gravity concentrating remaining sludge in a sewage treatment plant, adding hydrogen peroxide, and mixing; adding hydrogen peroxide to the excess sludge for ultrasonic processing in ultrasonic reactor; and after the ultrasonic irradiation into the anaerobic digestion reactor, carrying out the subsequent medium temperature anaerobic digestion to produce biogas by gas collecting device for collecting and measuring the methane content.    USE - Method for promoting surplus sludge anaerobic digestion (claimed).    ADVANTAGE - The method improves biogas yield by 17.40%-55.37%, where the biogas methane content is 10%-20%, and reduces energy consumption of ultrasonic treatment.
NOVELTY - Sludge pyrolysis digestion technology includes carrying out aerobic treatment of residual sludge in each group of hydrolysis reactor, heating and pressurizing; reducing the hot steam to the hydrolysis reactor unit pre-hydrolyzed sludge, and further releasing the pressure to the hot steam to the group pre-hydrolysis reactor to finish hydrolysis reaction, returning the hot steam to the first group of reactor; and further releasing pressure in the flash tank, discharging the sludge into the anaerobic digestion tank, and collecting the biogas.    USE - Sludge pyrolysis digestion technology for recycling heat.    ADVANTAGE - The method has high efficiency for recycling steam, and can save energy consumption.    DETAILED DESCRIPTION - Sludge pyrolysis digestion technology comprises:    (A) carrying out aerobic treatment of residual sludge in each group of hydrolysis reactor, heating and pressurizing the first group of hydrolysis reactor injecting hot steam when set thermal hydrolysis reaction;    (B) reducing the hot steam to the hydrolysis reactor unit pre-hydrolyzed sludge to 0.2-0.3 MPa of the pressure spraying flash tank, and further releasing the pressure in the flash tank to the hot steam to the group pre-hydrolysis reactor to finish hydrolysis reaction, returning the hot steam to the first group of reactor, reducing the hydrolyzed sludge to 0.2-0.3 MPa of the pressure spraying flash tank; and    (C) further releasing pressure in the flash tank, the steam flow to a first set of pre-hydrolysis reactor, discharging the sludge via heat exchanger at 50-55 degrees C, using water to dilute till water content is 88%-92%, high temperature anaerobic digestion in the anaerobic digestion tank controlled at 50-58 degrees C, and collecting the biogas.
NOVELTY - Use of butyl rubber or silicone rubber, preferably fluorine-free silicone rubber for producing a sealing element at a proportional valve for controlling a gaseous medium, preferably hydrogen, is claimed.    USE - The butyl rubber or silicone rubber, preferably fluorine-free silicone rubber is useful for producing a sealing element at a proportional valve for controlling a gaseous medium, preferably hydrogen.    ADVANTAGE - The sealing element: exhibits improved elasticity and thus it exhibits excellent sealing effect; is elastically deformable even at low temperatures; provides improved tightness in vehicles with fuel cell propulsion; and ensures accurate metering of hydrogen, preferably prevents inaccurate opening and closing of proportional valve.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) the proportional valve for controlling the gaseous medium, preferably hydrogen, comprising the sealing element containing butyl-rubber or silicone-rubber, preferably fluorine-free silicone-rubber or is produced completely from butyl-rubber or silicone-rubber, preferably fluorine-free silicone-rubber;    (2) producing the sealing element at a component of the proportional valve of a spray material, containing butyl-rubber or is produced completely from butyl-rubber, comprising applying an injection molding die on a surface area of the base surface of the component, and spraying the sealing material on the base surface bounded by the injection molding die; and    (3) producing the sealing element at a component of the proportional valve of a spray material, containing silicone-rubber or is produced completely from silicone-rubber, comprising vulcanizing the silicone-rubber on a surface of the component of the proportional valve.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of the proportional valve.    Nozzle body (2)    Closing element (4)    Base surface (4a)    Flat gasket (5)    O-ring (20)
NOVELTY - A hydrogen generating apparatus (1) comprises reaction container containing modification part which makes raw material and water react and produces hydrogen-containing-gas, and carbon monoxide reduction part (B) which reduces carbon monoxide contained in hydrogen-containing-gas, heating part which heats modification part and carbon monoxide reduction part, heat insulating material (12) which is arranged so that outer periphery of reaction container may be covered, and convection prevention part which is arranged between heat insulating materials.    USE - Hydrogen generating apparatus for supplying fuel gas to fuel cell.    ADVANTAGE - Thermal radiation of the modification part is suppressed, fall of the carbon monoxide reduction performance of carbon monoxide reduction part can be suppressed, and the high temperature deterioration of the catalyst of carbon monoxide reduction can be prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the hydrogen generating apparatus. (Drawing includes non-English language text).    Hydrogen generating apparatus (1)    Fuel cell (3)    Conversion catalyst layer (7)    Heat insulating material (12)    Carbon monoxide reduction part (B)
NOVELTY - The method involves calculating pressure of hydrogen generated in the cathode side that computes the pressure rise time of back pressure valve. The pressure of hydrogen with the pressure gauge positioned in the upstream of the back pressure valve is measured. The pressure of the measured hydrogen and setting pressure of the back pressure valve are computed, after the pass of computed pressure rise time. System breakdown process is performed, when the pressure of compared hydrogen is less than setting pressure.    USE - Method for controlling high-pressure water electrolysis system.    ADVANTAGE - The failure of relief valve can be easily detected, by comparing measured and setting pressure of back pressure valve. The hydrogen getting waste from the relief valve can be prevented. The economical electrolytic treatment can be performed efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the high-pressure water electrolysis system. (Drawing includes non-English language text)    High-pressure water electrolysis system (10)    Pure-water supply apparatus (12)    High-pressure water electrolyzer (14)    Hydrolyzing cell (16)    Electrolysis power supply (20)
NOVELTY - Concentrating methane or other combustible gases from gas mixtures, such as biogas, comprises: removing burning gas-rich product gas stream located at elevated pressure level of the permeator from the retentate side of the permeator; supplying a compressed gas scrubber to a gas inlet at an increased pressure level; obtaining burning gas-poor waste gas stream of the permeator in variable concentration; and igniting the waste gas stream by the addition of air or by a gas burner.    USE - The process is useful for concentrating methane or other combustible gases from gas mixtures, such as biogas.    ADVANTAGE - The process provides highly concentrated methane or other combustible gases from gas mixtures at reduced operating costs.    DETAILED DESCRIPTION - Concentrating methane or other combustible gases from gas mixtures, such as biogas, consisting of a carbon dioxide (CO2)-selective permeation process, a CO2-selective gas scrubber, a gas burner and a recuperator for energy recovery, comprises: removing burning gas-rich product gas stream located at elevated pressure level of the permeator from the retentate side of the permeator; supplying a compressed gas scrubber to a gas inlet at an increased pressure level; obtaining burning gas-poor waste gas stream of the permeator in variable concentration; and igniting the waste gas stream by the addition of air or by a gas burner, where the igniting step is used to provide the required heat energy, and the process can be processed at smaller gas flow rates of 100 standard cubic meters per hour.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of a process for concentrating methane or other combustible gases from gas mixtures (Drawing includes non-English language text).    Compressor (2)    Permeate stream (3)    Retentate stream (4)    Membrane module (5)    Compressed gas scrubber. (6)
NOVELTY - Producing (M1) synthesis gas from biomass involves grinding biomass feedstock to produce ground biomass particles; dispensing the ground biomass particles into thin sheets; subjecting the thin sheets of ground biomass to a treatment including sequential ramps of temperature followed by pressure shocks or pressure shocks concurrent with ramps of temperature; and recovering residual non-volatile biomass component from the treatment and reacting the component with at least one of methane, oxygen, steam, and carbon dioxide, at high temperatures.    USE - For producing synthesis gas from biomass (claimed).    ADVANTAGE - The method produces high purity synthesis gas via conversion of biomass fractionated (BMF) char; and is ultimately generating value added chemicals and renewable fuels.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for adjusting (M2) the ratio of hydrogen to carbon monoxide in synthesis gas, involving grinding biomass feedstock to produce ground biomass particles having diameters of 0.001-1 inch; dispensing ground biomass into thin sheets having thickness that is multiple of the ground biomass particle diameter; subjecting the thin sheets of ground biomass to a treatment including sequential ramps of temperature followed by pressure shocks or pressure shocks concurrent with ramps of temperature; selectively collecting various groups of volatile compounds as they are released from the biomass; collecting remaining non-volatile component of the thin sheets; reacting the non-volatile component with one of oxygen, methane, steam, and carbon dioxide; and adjusting a ratio of reacted oxygen, methane, steam, or carbon dioxide to produce synthesis gas having hydrogen/carbon ratio of 0 to 100.
NOVELTY - The device has a gas inlet, cyclone dust collector, cyclone inertial dust separator, multi-tubular condensation separator, multistage folded filter, negative pressure roots blower, gas-liquid separator, gas water seal and a gas outlet that are connected in series.    USE - Dry type multi-level fuel gas purifying device for a biomass generating furnace.    ADVANTAGE - The device allows passage of gas generated by a biomass gasification generating furnace so as to improve efficiency of straw gasifier by 20 percent and avoid secondary environmental pollution. The device can generate 300 to 3000 cubic meter of gas and generate combustible gas with high quality.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a dry type multi-level fuel gas purifying device.'(Drawing includes non-English language text)'
NOVELTY - System useful for producing biodiesel by animal carcass, comprises orderly connected a feeding device, a steaming tower, a grinding tower, a washing tower, a dehydration tower, a synthesizing tower, a phase separation tower and a first rectification tower. The synthesizing tower is connected to a second rectification tower.    USE - The system is useful for producing biodiesel by animal carcass.    ADVANTAGE - The system is simple and convenient to operate; and has high production efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the system for producing biodiesel by animal carcass (Drawing includes non-English language text).
NOVELTY - Marsh gas pool comprises a digestion chamber whose upper part comprises a sewage inlet (812) and a biogas outlet; an inclined clapboard (830) that carries out digestion and divides the pool into upper (801) and lower chambers (828), where one end of the clapboard from the sewage inlet close to the first distance is higher than the sewage inlet far away from an air outlet and lower end of clapboard is provided with a connection port to connect upper and lower chambers.    USE - As marsh gas pool for performing biological treatment to the domestic sewage (claimed).    ADVANTAGE - The marsh gas pool has simple structure, low construction cost, has stable output pressure; and greatly reduces marsh gas pool operation energy consumption.    DESCRIPTION OF DRAWING(S) - The figure shows digestion tank.    Upper chamber (801)    Device chamber (804)    Sewage inlet (812)    Lower chamber (828)    Inclined clapboard (830)
NOVELTY - The electrolyzer generates mixed gas of hydrogen and oxygen and discharges mixed gas into an electrolytic vessel. Multiple electrode plates are accommodated in the electrolytic vessel. An electrolyte solution temperature detection sensor is provided to detect the temperature of electrolyte solution. Multiple sheets of electrode plates that contribute to electrolysis are increased or decreased based on electrolyte solution temperature detected by the electrolyte solution temperature detection sensor. The changeover switch (153) is installed in control unit (71).    USE - Water electrolyzer of fuel supply apparatus (claimed).    ADVANTAGE - Electrolysis efficiency can be improved. The processing capacity of the water electrolyzer can be improved. Extension and enlargement of the electrolytic vessel can be performed. The cooling efficiency of the cooling device can be improved. Fuel consumption can be reduced. The elastic deformation can be performed smoothly and reliably. The electrolyzer has simple structure so that the cost can be reduced. The combustion and electrolysis efficiency can be improved. The processing capacity of the electrolyzer can be improved. Safe and environmentally friendly fuel supply apparatus can be obtained. Since combustion flame can be stabilized, the discharge of combustion flame can be prevented and the safety can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel supply apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the water electrolyzer.    Control unit (71)    Power supply terminal (141)    Changeover switch (153)    Nuts (177,179)    Sleeve (181)
NOVELTY - Preparing a catalyst comprises: (i) impregnating a calcined support comprising a metal aluminate with a solution comprising nickel acetate at a temperature of greater than or equal to 40 degrees C and drying the impregnated support; (ii) calcining the dried impregnated support, to form nickel oxide on the surface of the support; and (iii) optionally repeating steps (i) and (ii) on the nickel oxide coated support.    USE - The catalyst is useful in number of industrial processes, including methanation and steam reforming processes, such as pre-reforming, primary reforming and secondary reforming.    ADVANTAGE - The method is capable of preparing a catalyst with improved strength and catalyst activity with reduced metal loadings.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) an eggshell catalyst material obtainable by the method;    (2) a process for the steam reforming of a hydrocarbon comprising contacting a mixture of hydrocarbon and steam at elevated temperature and pressure with a catalyst; and    (3) a process for the methanation of a hydrogen gas stream gas stream containing carbon monoxide and carbon dioxide in amounts of 0.1-0.5 vol.%, comprising contacting the hydrogen gas stream at a temperature of 230-450 degrees C with the catalyst.
NOVELTY - The system (100) has a hydrogen supply unit that supplies hydrogen generated by a hydrogen generating apparatus (30). An electric power supply unit is provided to supply electric power produced in a photoelectric conversion unit (2). A control apparatus (40) is provided to control supply of hydrogen, and supply of electric power used for generation of hydrogen. An electrical storage apparatus (70) is connected to control apparatus and hydrogen generating apparatus to exchange electric power.    USE - Solar energy power generation system.    ADVANTAGE - The generation and supply of electric power can be performed stably and efficiently. The independent dispersion electric power supply can be performed without using system electric power while ensuring safety.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the solar energy power generation system. (Drawing includes non-English language text)    Photoelectric conversion unit (2)    Hydrogen generating apparatus (30)    Control apparatus (40)    Electrical storage apparatus (70)    Solar energy power generation system (100)
NOVELTY - An alkaline storage battery (10) has an electrode group formed from a negative electrode (11) essentially containing hydrogen storage alloy (I), a positive electrode (12) essentially containing nickel hydroxide, and a separator (13) containing electrolyte enclosed in an exterior can (17).    USE - Alkaline storage battery is used as power supply for hybrid electric vehicles.    ADVANTAGE - The alkaline storage battery has high output stability and reduced size, and suppressed memory effects. The alkaline storage battery is economical.    DETAILED DESCRIPTION - An alkaline storage battery has an electrode group formed from a negative electrode essentially containing hydrogen storage alloy of formula: LaxNdyRe1-x-y-zMgzNin-m-vAlmTv (I), a positive electrode essentially containing nickel hydroxide, and a separator containing electrolyte enclosed in an exterior can, where Re is rare-earth elements other than lanthanum and neodymium, or yttrium, T is cobalt, manganese or zinc, x is 0.13-0.34, y is 0.14-0.6, z is 0.1-0.15, n=3.5-3.75, m=0.13-0.22 and v is 0 or more.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of alkaline storage battery.    Alkaline storage battery (10)    Hydrogen storage alloy negative electrode (11)    Nickel positive electrode (12)    Separator (13)    Negative electrode collector (14)    Positive electrode collector (15)    Exterior can (17)
NOVELTY - The system has a discharge pipe (50) positioned at a lower side portion of a block member (40). A water-level detection opening includes a top water-level detection section and a top portion that is coupled to an upper portion of a gas-liquid separation opening. The upper portion communicates with a hydrogen pipe (20) positioned at an upper portion of the block member. An inlet hole of the block member is introduced with hydrogen from a high-pressure water electrolysis device and positioned at an upper side portion of the block member and above the top water-level detection section.    USE - Water electrolysis system for a fuel cell vehicle.    ADVANTAGE - The inlet hole is introduced with high-pressure hydrogen from the high-pressure water electrolysis device and positioned above the top water-level detection section of the water-level detection opening, so that the water level in the gas- liquid separation opening can be maintained at a position below the inlet hole during normal operation, thus preventing the hydrogen from flowing into water stored in the gas-liquid separation opening, and hence reducing water droplets and air bubbles occurring in the top water-level detection section and the bottom water-level detection section while ensuring that high- pressure hydrogen containing moisture can be satisfactorily separated into the hydrogen and water and sufficient strength can be achieved with accurate measurement of water level and reduced manufacturing cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a gas-liquid separation device in a water electrolysis system.    Hydrogen outlet path (16)    Gas-liquid separation device (18)    Hydrogen pipe (20)    Block member (40)    Discharge pipe (50)
NOVELTY - Producing hydrogen comprises electrolysis of an aqueous solution that comprises at least one organic product selected from a residual product originating from industry and a biomass-derived product, and also its combinations.    USE - The method is useful for producing hydrogen (claimed).    ADVANTAGE - The method avoids the generation of products of combustion such as dioxins or furans produced in incineration, thus, it is environment-friendly. Additionally, the method provides high purity hydrogen, where the purity exceeds 99%.
NOVELTY - The device has a section reaction chamber of the furnace main portion is provided with inlet. The side portion of the reaction cavity wall of feeding port is covered with sealing cover. The air outlet of the washing purifier is connected with the gas inlet of the chemical cleaner. The air outlet of chemical cleaner is connected with an air inlet end of the air suction pump through the pipeline. The gas pre-processing device, bottom of washing purifier and the cleaner are provided with pipe. The outlet of water pipe is located above the water tank to form water seal.    USE - Device for generating combustible gas using garbage.    ADVANTAGE - The carbon black dust, tar, impurities and other gas can be separated, while removing peculiar smell and reducing pollution to the environment.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for generating combustible gas.
NOVELTY - Electrode comprises a volumetrically compressed and structurally stable mixture (224) of reactive metal particles (228) having substantially high reactive surface area, and metal substrate particles (226) having lesser surface area than the reactive metal particles, and the quantity of the metal substrate particles is to provide structural stability to the electrode upon compression, where the electrode is volumetrically compressed to a percentage of the mixture's original volume to minimize volume while still permitting sufficient permeability to maintain high catalytic efficiency.    USE - The electrode is useful: in at least one electrochemical or catalytic application; in electrochemical sensor, which is configured to detect an analyte capable of undergoing electrochemical reaction at the sensor (all claimed); and in fuel cells and electrolysis devices to generate hydrogen and oxygen.    ADVANTAGE - The electrode: exhibits metal high electrical conductivity and electrochemical stability, and metal mesh screen with high surface area; provides structural integrity; prevents permeation of gasses and thus avoids mixing of hydrogen and oxygen gas, and allows aqueous electrolyte flux; and provides composition which maintains mechanical stability and provides sufficient permeability to reacting species.    DESCRIPTION OF DRAWING(S) - The figure shows a side view of the electrode.    Sintered electrode (220)    Current collector (222)    Compressed mixture (224)    Metal substrate particles (226)    Reactive particles (228)
NOVELTY - System comprises sludge fermentation device, methane collecting device and methane processing device which are orderly connected together. The sludge fermentation device comprises fermentation pool and methane chamber above the fermentation pool. The methane collecting device comprises gas-guide tube connected to the methane chamber, and gas storing pot connected to the gas-guide tube. The methane processing device comprises methane compressor and supercharger orderly connected together.    USE - The system is useful for preventing methane generated by sludge in brick production.    DETAILED DESCRIPTION - System comprises sludge fermentation device, methane collecting device and methane processing device which are orderly connected together. The sludge fermentation device comprises fermentation pool and methane chamber above the fermentation pool. The methane collecting device comprises gas-guide tube connected to the methane chamber, and gas storing pot connected to the gas-guide tube. The methane processing device comprises methane compressor and supercharger orderly connected together. The methane compressor is connected to the gas storing pot. The exhaust port of the supercharger is connected to the brick making furnace.
NOVELTY - A biodiesel is denitrided by contacting the biological diesel oil and organic carboxylic acid containing nitrogen to obtain layered product comprising biodiesel phase and organic carboxylic acid, and recycling the nitrogen contents of the biological diesel oil. The organic acid is carboxylic acid with 1-7C.    USE - Method for denitriding biological diesel oil (claimed).    ADVANTAGE - The method can reduce nitrogen content of diesel to improve the quality of the biodiesel product.
NOVELTY - The present invention relates to a process for producing a preparation based on lactobacilli having a strictly determined microbiological and chemical composition with application in pharmaceutical and nutritional supplements industry. According to the invention, the process consists in the static submerged cultivation of a strain of Lactobacillus in a discontinuous system on a nutritive system containing 1...2% glucose, 0.5...1% peptone, and 1...3% yeast extract thereby resulting a dry biomass preparation. The parameters indicated for growing the biomass are: a temperature of 37...40 degrees C, the pH resulting after sterilizing the medium, duration of 46...48 h, static culture in Erlenmayer flasks. The microbial preparation is obtained after three centrifugation steps, the first having a duration of 40...60 min at a speed of 3000 rpm and a temperature of 4...6 degrees C, and the next two having a duration of 40...60 min at a speed of 5000 rpm and temperature of 4...6 degrees C, the sediment of interest being washed with distilled water between the centrifugation steps.
NOVELTY - Method for pre-treating organic domestic garbage by xylanase to anaerobic fermentation process, involves adding hydrolysate in organic domestic garbage; adding xylanase (150000-200000 U) according to volatile solid quantity in each gram of organic domestic garbage; adding xylanase in the organic domestic garbage; pre-treating at 50-70 degrees C for 8-20 hours, and adding the inoculums in the pre-treated organic domestic garbage; adding water or biogas slurry to form mixture with fermentation concentration of 4-8%; sealing; and then processing anaerobic fermentation at 34-36 degrees C to collect biogas.    USE - As method for pre-treating organic domestic garbage by xylanase to anaerobic fermentation process (claimed).    ADVANTAGE - The method improves the accumulation gas and the accumulation methane; improves the using rate of the raw material; and also improves the limitation of the hydrolysis acidification step during the anaerobic fermentation process so as to solve the problems of hysteretic fermentation speed existed in the normal anaerobic fermentation and low efficiency.    DETAILED DESCRIPTION - Method for pre-treating organic domestic garbage by xylanase to anaerobic fermentation process, involves taking the organic domestic garbage; adding hydrolysate in the organic domestic garbage, where the volatile solid quantity density is 10-14%; adding xylanase (150000-200000 U) according to the volatile solid quantity in each gram of the organic domestic garbage; adding the xylanase in the organic domestic garbage; pre-treating at 50-70 degrees C for 8-20 hours; adding the inoculums in the pre-treated organic domestic garbage, where the ratio of the organic domestic garbage to the volatile solid content of the inoculums is 2 to 2.5:1; adding water or biogas slurry to form mixture with the fermentation concentration of 4-8%; sealing; and then processing anaerobic fermentation at 34-36 degrees C to collect biogas.
NOVELTY - Producing methane comprises (i) feeding and pre-treating the material, where the material do not need to be cut or crushed, adding inoculums or conditioner, mixing and stacking in an anaerobic tank, partially degrading the wax and the pectin of the material; (ii) injecting the water or the biogas slurry to the material stacked in the anaerobic tank, fermenting and sealing; (iii) flowing back the biogas slurry or replenishing water to control the water level in the anaerobic tank, sealing, stirring, and collecting methane; and (iv) terminating the operation of anaerobic tank, and discharging.    USE - The method is useful for producing methane.    ADVANTAGE - The method prevents material from sculling, and has high material degrading rate and methane converting rate.    DETAILED DESCRIPTION - Producing methane comprises (i) feeding and pre-treating the material, where the material do not need to be cut or crushed, adding inoculums or conditioner, mixing and stacking in an anaerobic tank until the fiber of the mixed material is softened, partially degrading the wax and the pectin of the material to reach certain temperature; (ii) injecting the water or the biogas slurry to the material stacked in the anaerobic tank, where the water level is on the basis of submerging the material in the tank, and the total solid content in the anaerobic tank is 10%-20%, fermenting and sealing; (iii) flowing back the biogas slurry or replenishing water for every 1-10 days to control the water level in the anaerobic tank and sealing before the fermentation water level is plus minus 5% to ensure that the total solid content in the anaerobic tank is 10%-20%, stirring, and collecting methane; and (iv) terminating the operation of anaerobic tank, and discharging.
NOVELTY - Methane is prepared by crushing air dried asparagus straw and controlling the grain diameter of the straw at 0.1-5 cm, acclimating the asparagus straw powder for 3 months through seed sludge, adding sodium hydroxide solution to the asparagus straw powder and sealing for 5-25 days, controlling the pH value at 7-7.5, sealing in fermenting device at 30-45 degrees C, oscillating, performing complete mixed wet type fermentation reaction to generate methane after 1-2 days, and fermenting for 20-60 days to convert the degradable organic substance in the asparagus straw into methane.    USE - Method for preparation of methane (claimed).    ADVANTAGE - The method damages the inside tissue of the lignocellulose by carrying out sodium hydroxide pre-treatment on the agricultural waste, thus the cellulose is released from the lignin and semicellulose, the cellulose degradation is accelerated, and the biological digestion performance, gas output potential, economical efficiency, and feasibility of the asparagus straw are improved.    DETAILED DESCRIPTION - Preparation of methane involves:    (A) gathering underground root stock generated in spring and over-ground halm haulm generated in autumn in planting asparagus, spreading on space, and air drying;    (B) crushing the dried asparagus straw and controlling the grain diameter at 0.1-5 cm;    (C) acclimating the asparagus straw powder for 3 months through the seed sludge;    (D) adding sodium hydroxide solution to the asparagus straw powder, stirring, and sealing for 5-25 days;    (E) controlling the pH value of the fermented mixture at 7-7.5; and    (F) sealing in fermenting device at 30-45 degrees C, stirring at real time, oscillating, performing complete mixed wet type fermentation reaction to generate methane after 1-2 days, and fermenting for 20-60 days to convert the degradable organic substance in the asparagus straw into methane with the help of microorganism.
NOVELTY - A Rhizopus oryzae TY GF1 is used in silkworm oil in preparing biodiesel via whole-cell catalysis.    USE - Rhizopus oryzae TY GF1 used in silkworm oil in preparing biodiesel via whole-cell catalysis (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an application of Rhizopus oryzae TY GF1 comprising producing intracellular lipase by Rhizopus oryzae TY GF1, inoculating bacterium in culture medium at 25-40 degrees C, and culturing in shake flask for 1-3 days, with pH of culture medium of 5-7, with each liter of culture medium comprising (g) sucrose (5-20), peptone (20-70), canola oil (5-20), sodium nitrate (0.8-1.4), magnesium sulfate heptahydrate (0.2- 0.8), potassium dihydrogen phosphate (0.8-1.4) and Vaseline (RTM: petroleum jelly based product) (0.5-2%); and vacuum filtering cultured mixed fermentation liquor, freeze drying obtained mycelium for 8-12 hours, and preparing ester exchange reaction system comprising in 100 mL of conical flask comprising (g) silkworm oil (6), methanol (0.35), whole-cell mycelium (0.2-0.8) and 0.2 M sodium acetate buffer solution (0.1-0.4 mL) with pH 5-7, adding methanol every 24 hours for three times, and reacting for 47-72 hours at 24-40 degrees C and at rotating speed of 120-200 revolutions/minute to obtain biodiesel.
NOVELTY - A sludge fermenting method involves adjusting water content of sludge to 55-65% and carbon/nitrogen value of the sludge to 27-33%. The sludge is uniformly stirred in a ferment device built fermentation stack, where fermenting temperature is 52-57 degrees C, pH value is 7-8 and fermenting time is 60-80 hours. The sludge is fermented at temperature of 58-63 degrees C, where pH value of the sludge is 7-8 and fermenting time is 50-80 hours.    USE - Method for fermenting sludge that is utilized for preparing organic fertilizer (claimed).    ADVANTAGE - The method enables reducing the fermentation period, improving compost efficiency and increasing processing capacity of the sludge. The method enables reducing secondary pollution and transportation process and preparing organic fertilizer with sanitary standard quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing organic fertilizer.
NOVELTY - Composite biological enzyme composition comprises (in parts): protease (25-30), laccase, polyphenol oxidasen and manganese peroxidase (20-25), xylanase, pentosanase and mannose (17-21), cellulose, pectinase and hemicellulase (20-25), lipase (10-15), and amylase (12-16).    USE - The composite biological enzyme composition is useful for treating domestic sludge. The composition is in the form of solid or solution (all claimed).    ADVANTAGE - The method is environmentally-friendly, reduces total suspended solids, biochemical oxygen demand and chemical oxygen demand and removes hydrogen sulphide gas and bad odor from sludge.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing composite biological enzyme composition, which involves collecting and extracting bacteria from domestic sludge using bioenzyme, culturing the product in the culture medium, fermenting the product, separating the product by physical or chemical process, centrifuging the product, fermenting the product, filtering the product and drying the product.
NOVELTY - An organic fertilizer preparation method involves filtering waste slag by using a 2-10 cm mesh screen, and adding auxiliary material to prepare culture medium. Sarcophaga peregrina is inoculated in the culture medium for 4-5 days at 25-35 degrees C to prepare culture material. The culture material is collected and dried to obtain organic fertilizer, where the auxiliary material is feather powder, meal powder, sawdust and straw powder.    USE - Method for preparing organic fertilizer for processing human excrement.    ADVANTAGE - The method enables preparing organic fertilizer with strong processing ability, less area occupation and low energy consumption in an ecofriendly manner.
NOVELTY - A fuel preparing system has a sludge conveying device whose output port is arranged on an airflow drier (1) that is connected with a pressure pipe (6). A smoke pipe (3) and a smoke filtering separator are connected to a hopper (7). The hopper is connected with a dust remover of a smoke exhausting system (15). The hopper is provided with a dry mud outlet (35). The smoke pipe is connected with a heat source (14).    USE - System for preparing fuel by drying waste sludge.    ADVANTAGE - The system is safe and reliable to use, and has high working efficiency, energy-saving effect, better drying effect, high product yield and simple structure.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a system for preparing fuel.    Airflow drier (1)    Smoke pipe (3)    Pressure pipe (6)    Hopper (7)    Heat source (14)    Smoke exhausting system (15)    Dry mud outlet (35)
NOVELTY - A straw fermenting cabin has a circular cabin body arranged on a pedestal, and a ventilating device i.e. ventilating tube, equipped in the cabin body and passing through the cabin body, where the top part of the cabin body is provided with a top cover. The ventilating device at the lower part of the top cover is provided with a rain sheltering part. The pedestal comprises a fence made of bricks. A cross beam is arranged on the fence, where one face of the pedestal is provided with a feeding port.    USE - Cabin for fermenting straw that is utilized as feed or organic fertilizer. Uses include but are not limited to withered or fresh sorghum straw, corn straw, wheat straw, canola straw, tobacco straw, and beans straw.    ADVANTAGE - The cabin can save labor, transform by-product of crops and effectively improve additive value of farm product. The cabin realizes environment protection.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for manufacturing a straw fermenting cabin.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a straw fermenting cabin.
NOVELTY - A methane producing method involves mixing manure, crop straw and rice hull, and stirring uniformly to prepare an organic fermentation material. A soft fermenting bag is arranged around a poultry waste water injection soft fermenting bag, and biogas is generated by spraying a fermentation product. The biogas is added to the fermentation product and heated after period of time.    USE - Method for producing methane.    ADVANTAGE - The method enables synchronously carrying out organic fertilizer production, saving the space, conveniently processing the methane liquid and methane slag, and ensuring continuous production of methane during winter in northern area.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a methane producing method.
NOVELTY - Production of immobilized lipase for producing biodiesel, involves reconstructing gene target using reverse transcription product cDNA of oil plant total RNA, introducing the gene target into lipase producing microorganism genome and then into expression vector, introducing the vector into prokaryotic host bacteria Escherichia coli strain BL21 (DE3), obtaining transformant capable of expressing fusion protein (protein-lipase), immobilizing fusion protein on a substrate with lipophilic organic solvent and using immobilized product for biodiesel production.    USE - Production of immobilized lipase used for producing biodiesel.    ADVANTAGE - The method enables purification and immobilization of fusion protein synchronously, and solves the problem in existing enzyme method for producing biodiesel process, that is immobilized lipase is high cost and low efficiency. The method is simple, inexpensive, and improves stability of lipase.    DETAILED DESCRIPTION - Production of immobilized lipase for producing biodiesel, involves performing PCR and automatically reconstructing gene target using reverse transcription product cDNA of oil plant total RNA, introducing the gene target into lipase producing microorganism genome and then into expression vector pET32(+)-0-Lipd25AB, introducing the expression vector into prokaryotic host bacteria Escherichia coli strain BL21 (DE3), obtaining transformant capable of expressing fusion protein (protein-lipase) that is involved in transesterification reaction, immobilizing the fusion protein on a substrate with lipophilic organic solvent and using the immobilized product for biodiesel production.
NOVELTY - Separation device for producing biodiesel comprises a heating device (2), a buffer tank (4), a separator (5), and a centrifuge (6). The centrifuge is provided with a third heavy phase outlet (7). The device further comprises a return pipe. One end of the return pipe is connected with the third heavy phase outlet, and the other end is connected with the inlet of the buffer tank.    USE - The device is useful for producing biodiesel.    ADVANTAGE - The device: can continuously carry out separation of biodiesel, glycerol, and methanol with high separation degree; and is suitable for large-scale production of biodiesel.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the separation device for producing biodiesel.    Heating device (2)    Buffer tank (4)    Separator (5)    Centrifuge (6)    Third heavy phase outlet (7)
NOVELTY - Preparing ammonium potassium polyphosphate comprises: (i) mixing water and phosphoric acid, passing ammonia gas and adding potassium hydroxide, maintaining reaction temperature at 50-100 degrees C, adding potassium hydroxide and dissolving completely to obtain the reaction solution; and (ii) cooling the obtained reaction solution at 0-30 degrees C for crystallizing and performing solid-liquid separation to obtain ammonium potassium polyphosphate crystals.    USE - The method is useful for preparing ammonium potassium polyphosphate.    ADVANTAGE - The method utilizes raw materials with low cost, consumes less energy; does not discharge waste residue and waste water; is safe and eco-friendly; and is suitable for industrialized production.
NOVELTY - The tank has a stirring blade (10) that is provided in the inner cavity of inner tank main portion (5) made of stainless steel vortex. An electric controller (4) is connected with power frequency induction coil winding (6). A cooling device is provided between outer shell (3) and inner tank main portion. The stirring blade and a temperature blade (9) are set on vertical rotating shaft (8) passing through outer shell and inner tank main portion. The rotating shaft is provided with a belt transmission mechanism (23) that is connected with power output shaft of motor (22).    USE - Synthesizing tank for modulating biological ethanol fuel.    ADVANTAGE - The environment-friendly effect of the synthesizing tank is improved. The synthesizing tank can be used in cold and hot environment effectively. The quality of the product synthesized by the synthesizing tank is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for modulation method of biological ethanol fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of the synthesizing tank.    Outer shell (3)    Electric controller (4)    Inner tank main portion (5)    Power frequency induction coil winding (6)    Vertical rotating shaft (8)    Temperature blade (9)    Stirring blade (10)    Motor (22)    Belt transmission mechanism (23)
NOVELTY - Preparation for nutrient fertilizer, involves using raw materials comprising (in wt.%): luffa powder (2-4), corn powder (3-5), straw powder (2-4), broadleaf wooden (6-8), buckwheat shell powder (10-12), wood ash powder (4-6), snail shell powder (18-22), shrimp shell powder (11-13), dried rabbit droppings (6-10), dried sheep droppings (3-5), barley straw powder (6-8), bran powder (7-9), rapeseed cake powder (1-3), cottonseed powder (4-6), nux vomica powder (0.2-0.4), neem leaf powder (0.1-0.3), balsam pear powder (0.2-0.4), and common three wingnut root (0.1-0.3).    USE - Preparation for nutrient fertilizer for used Begonia (claimed) for preventing disease, accelerating the growth ofBegonia, and inducing generation of large sized and bright flowers.    ADVANTAGE - The method prepares hyacinth fertilizer by simple and inexpensive process using easily available raw materials. The prepared fertilizer is rich in nutrients.
NOVELTY - Method for preparing fertilizer for sweet potato, involves using (in wt.%): cottonseed powder (5-10), cake flour (10-15), rabbit manure (20-23), mushroom powder (8-11), barley straw powder (10-15), gourd leaves powder (3-7), sesame straw powder (14-22), straw powder (5-8), pumpkin stem leaves powder (3-5), garlic powder (1-2), and fennel (1-2).    USE - The method is useful for preparing fertilizer for sweet potato.    ADVANTAGE - The fertilizer improves yield and growth of sweet potato, and enables to prevent sweet potato from diseases.
NOVELTY - The reformer (100) has a reforming unit with a first reaction part (150) placed around heating units (140, 145). A second reaction part (170) is placed around the former reaction part. A donut-shaped space mixing-reaction part (160) connects an outlet end of the former reaction part with an inlet of the latter reaction part such that fluid flows between the end of the former reaction part and the inlet of the latter reaction part. The mixing-reaction part with a mixed catalyst simultaneously performs a reforming reaction and a reduction reaction of carbon monoxide.    USE - Reformer for use in a fuel cell for receiving reformation fuel and converting the reformation fuel into reformate that is used for electric generation by the fuel cell.    ADVANTAGE - The mixed catalyst can simultaneously perform reforming and reduce an amount of carbon monoxide, thus increasing the generation amount of hydrogen to 1805, and reducing the generation amount of carbon monoxide to about 50 percentages. The reformer allows oxidation fuel to be supplied to generate heat, and anode off gas to be supplied as another oxidation fuel into the reformer, thus improving efficiency of the reformer. The reformer can be equipped with an integrated reactor for carrying out a reforming reaction and reducing carbon monoxide to maintain durability of the reformer for a long period of time.    DETAILED DESCRIPTION - The heating units are hollow cylinders and hollow polygonal cylinders.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic longitudinal cross-sectional view of a reformer.    Reformer (100)    Fuel distributor (120)    Heating units (140, 145)    Reaction part (150, 170)    Donut-shaped space mixing-reaction part (160)
NOVELTY - A biomass particle carbonization machine comprises an air heating furnace (1) having an air outlet; a carbonization boiler heating chamber (7) connected to the air outlet; a carbonization boiler (2) located on top part of the carbonizing pot heating chamber, and having a safety protective cover (6) provided with an exhaust port; a feeder (3); a material stirring and grease component; a granule cooling conveyor extending towards the carbonization boiler; an end product barn; and a clapboard on the middle of the carbonization boiler.    USE - A biomass particle carbonization machine.    ADVANTAGE - The machine has high degree of automation, is environment-friendly, can perform carbonization without tar emission, and realizes zero emission discharge.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a biomass particle carbonization machine.    Air heating furnace (1)    Carbonization boiler (2)    Feeder (3)    Safety protective cover (6)    Carbonization boiler heating chamber (7)
NOVELTY - A straw carbonizing furnace comprises a carbonizing chamber having a carbonizing auger, and a burner for providing heat energy to the carbonizing chamber. The carbonizing auger has a feeding opening, a discharging opening, and having a wall provided with gas guide tubes for transporting combustible gas out of the carbonizing chamber.    USE - A straw carbonizing furnace.    ADVANTAGE - The straw carbonizing furnace has improved energy utilization rate and carbonizing yield in unit time, reduces energy consumption and energy loss, and can maintain high temperature.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a straw carbonizing furnace.
NOVELTY - The method involves submitting an organic material to an anaerobic digestion process in an apparatus to produce methane. The produced methane is pressurized for conveying organic material through apparatus. The organic material is chosen from wood particles, straw, hay, manure, sphagnum moss, and peat moss.    USE - Method for producing biogas such as methane from organic material (all claimed) e.g. animal manure, crop residue, domestic waste, sludge and biosolids.    ADVANTAGE - The purification efficiency for producing biogas from organic material can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus for producing biogas from organic material.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the apparatus for producing biogas from organic material.    Solid waste transport pipe (3)    Compressed biogas pipe (4)    Solid outflow pipe (10)    Biogas outflow pipe (16)    Compressor (17)
NOVELTY - The fuel prevents phase separation comprising 45 to 55 volume percent of methanol, 25 to 35 volume percent of naphtha, 20 to 40 volume percent of aromatic hydrocarbon, and 0.001 to 13 volume percent of phase-separation prevention agent.    USE - Economic alternative methanol fuel for an internal-combustion engine.    ADVANTAGE - The fuel can replace gasoline, so that air pollution is reduced. The fuel is directly utilized in the internal-combustion engines without modifying existing engines.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph obtained based on characteristics of economic alternative methanol fuel.'(Drawing includes non-English language text)'
NOVELTY - A process for wet torrefaction of a biomass involves establishing a temperature and pressure within a reaction chamber that is at or above a desired reaction condition, where the desired reaction condition is sufficient to increase the energy density of a reacted biomass; introducing a biomass into the reaction chamber such that the desired reaction condition is maintained or equilibrates to it; and subjecting the biomass to the desired reaction condition for an amount of time effective to increase the energy density of the reacted biomass relative to the biomass prior to reaction.    USE - For wet torrefaction of a biomass, which is used as fuel.    ADVANTAGE - The process increases mass and energy densities of a biomass; and increases bulk density of lignocellulosic biomass while preserves sufficient levels of natural binding agents. The wet torrefaction process is completed in a very short period of time, i.e. less than 5 (preferably less than 2, especially 1) minutes, thus decreases the level of byproducts sludge as compared to biomass reacted in older process utilizing longer reaction time.
NOVELTY - System (S1) comprises: a first cross-flow filter configured to remove at least a first portion of a liquid from a fuel slurry to increase a concentration of a solid fuel in the fuel slurry; and a gasifier (106) configured to generate a syngas from the fuel slurry.    USE - The system is useful for concentrating a solid fuel in slurry (claimed), where the solid fuel includes coal, petroleum coke, biomass, wood-based materials, agricultural wastes, tars, asphalt, or other carbon containing items.    ADVANTAGE - The method provides higher concentrations of solid fuel in the slurry, thus improving carbon conversion and cold gas efficiency in the gasification of the fuel slurry, while avoiding the problems associated with pumping higher concentrated slurries.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a system (S2), comprising: a slurry concentration controller (16) configured to control a concentration of a solid fuel in a fuel slurry for gasification, where the slurry concentration controller is configured to adjust removal of a liquid from the fuel slurry via a cross-flow filter; and    (2) concentrating a solid fuel in slurry, comprising: controlling a concentration of a solid fuel in a fuel slurry at least partially by adjusting removal of a liquid from the fuel slurry via a cross-flow filter; and gasifying the fuel slurry in a gasifier downstream from the cross-flow filter.    DESCRIPTION OF DRAWING(S) - The figure illustrates a schematic block diagram of an integrated combined cycle power plant utilizing a filter to increase solid fuel concentration in a slurry.    Controller (16)    Fuel source (102)    Slurry preparation unit (104)    Gasifier (106)    Gas cleaning unit (110)
NOVELTY - Producing molded bodies of fuel from biomass comprises: grinding the biomass; drying the biomass by circulating process air; extracting ammonia and/or hydrogen sulfides bound in the biomass by introducing microorganisms; and transforming the biomass into fuel moldings.    USE - The method is useful for producing molded bodies of fuel from biomass.    ADVANTAGE - The method requires less energy and is simple to produce fuel without pollutants such as ammonia and hydrogen sulfide, and thus the power recovered from the biomass fuel is much less affected by the pollutants.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device to produce fuel moldings from biomass, comprising: a container for drying and size reduction of biomass; connections to closable supply and discharge of process air; openings for filling and removal of biomass; and a spray device for delivering effective microorganisms.
NOVELTY - Preparing renewable p-xylene, involves: (a) treating biomass to form a feedstock; (b) fermenting the feedstock with at least one species of microorganism, thus forming at least one renewable 4-5C molecule; (c) reacting the renewable 4-5C molecules to form at least one renewable 2,5-dimethyl substituted-6C olefin; (d) dehydrogenating and aromatizing at least a portion of the renewable 2,5-dimethyl substituted-6C olefin in the presence of a dehydrocyclization catalyst to form a mixture of comprising p-xylene and hydrogen; and (e) optionally isolating the renewable p-xylene.    USE - For preparing renewable p-xylene (claimed).    ADVANTAGE - The method selectively converts biological 4-5C molecules to specific xylene isomers especially p-xylene and the isolated p-xylene has a purity of greater than 90% and high overall yield.
NOVELTY - The machine has a sealed charring processing tank (1) in which the rice straw bales are placed without cutting. The sealed charging processing tank is placed inside the Biochar unit for charring. The rice straw is ground during the charring process by agitators (4) inside the Biochar unit. The Biochar is cooled by water to reduce the cooling time and increase productivity.    USE - Biochar machine for treating rice straw bales.    ADVANTAGE - The agriculture waste can be grinded so that the material Biochar can be obtained by burning in isolation from the air inside the oven.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the Biochar machine.    Sealed charring processing tank (1)    Ventilator (2)    Agitator (4)    Burner (5)    Chimney (6)
NOVELTY - Degrading a cellulosic material, comprises (a) pretreating the cellulosic material with a composition comprising one or more glycoside hydrolase Family 61 (GH61) polypeptides; and (b) saccharifying the GH61 polypeptide pretreated cellulosic material with an enzyme composition.    USE - The methods are used for degrading a cellulosic material, producing a fermentation product, and fermenting a cellulosic material (all claimed).    ADVANTAGE - The present invention provides improved pretreatment of a cellulosic material for the production of ethanol.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a method of producing a fermentation product; and    (2) a method of fermenting a cellulosic material, by fermenting the cellulosic material with one or more fermenting microorganisms, where the cellulosic material is pretreated with a composition comprising one or more GH61 polypeptides and is saccharified with an enzyme composition.
NOVELTY - Treating biomass to produce materials useful for biofuels comprises: (a) providing a biomass containing polysaccharides; (b) contacting the biomass with a solution containing at least one alpha -hydroxysulfonic acid thus hydrolyzing the biomass to produce at least one fermentable sugar containing product; and (c) optionally removing the alpha -hydroxysulfonic acid in its component form from the product by heating and/or reducing pressure to produce an acid-removed product containing at least one fermentable sugar substantially free of the alpha -hydroxysulfonic acid.    USE - The method is useful for treating biomass to produce materials useful for biofuels (claimed).    ADVANTAGE - The alpha -hydroxysulfonic acid can be easily removed from the product and recycled.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a method comprising: (a) providing a biomass containing polysaccharides; (b) contacting the biomass with a solution containing at least one alpha -hydroxysulfonic acid thus hydrolyzing the biomass to produce at least one fermentable sugar containing product; (c) heating at least one fermentable sugar containing product to a temperature of at least 110 degrees C thus producing furfural containing stream; and (d) removing the alpha -hydroxysulfonic acid in its component form from the furfural containing stream by heating and/or reducing pressure to produce an acid-removed product containing furfural substantially free of the alpha -hydroxysulfonic acid; and(e) optionally recycling the removed alpha -hydroxysulfonic acid as components or in its recombined form to step (b); and    (2) a composition comprising: (a) biomass containing polysaccharides, (b) at least one alpha -hydroxysulfonic acid; and (c) water.
NOVELTY - Derailment prevention structure has a main rail provided on a rail installation structure part which is formed to an open state such that at least one end portion of the longitudinal direction of metal main rails driving a wheel permit the expansion and contraction of the longitudinal direction of a main rail based on the air temperature, and long hole extended in the longitudinal direction of a main rail which is formed in multiple numbers by the main rail in the longitudinal direction at predetermined intervals.    USE - The structure is useful in organic composting fermentation apparatus for preventing derailment (claimed).    ADVANTAGE - The structure prevents meander formation of the main rail, and allows expansion-contraction of rail based on change in air temperature.    DETAILED DESCRIPTION - Derailment prevention structure has a main rail provided on a rail installation structure part which is formed to an open state such that at least one end portion of the longitudinal direction of metal main rails driving a wheel permit the expansion and contraction of the longitudinal direction of a main rail based on the air temperature, and long hole extended in the longitudinal direction of a main rail which is formed in multiple numbers by the main rail in the longitudinal direction at predetermined intervals, where the hole has tool for regulating the movement of the width direction of a main rail in one side of each long hole inserted in a main rail, and tool immobilized on other side of the installation structure part.
NOVELTY - Method for preparing chaff pellet, involves pelletizing the chaff obtained from agricultural waste resources.    USE - The method is useful for preparing chaff pellet which is used as fuel.    ADVANTAGE - The method is cost-effective, simple, stable, rapid and environmentally-friendly, and ensures mass production of the chaff pellet.
NOVELTY - The device has a heat exchanging chamber placed on top of a biogas outlet. A side wall of a high temperature mixed gas inlet is connected with a counter carbon gasification furnace (105) that is connected with the heat exchange chamber. A clapboard divides a standing separation chamber into left and right chambers. A lower part of a biological mixed liquid inlet is located on the left chamber. A side wall of the mixed liquid inlet is provided with a biological acid outlet. The standing separation chamber is provided with a biological heavy tar outlet.    USE - Heating biomass waste resource pyrolytic carbon gasification heating device.    ADVANTAGE - The device utilizes the biological waste into resource for residential purpose, thus saving energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a heating biomass waste resource pyrolytic carbon gasification heating device.    Heating carbon gasification furnace (1)    High temperature mixed gas separator (2)    Water storage buffer tank (3)    Boiler (4)    Counter carbon gasification furnace (105)