NOVELTY - The furnace has a straight-burning semi-gasification mode and a full-gasification mode that are combined seamlessly. Straight-burning semi-gasification function is performed during powerless state and when biomass gas is humid. The biomass gas is dried by a downdraft full-gasification mode when supplied with power. The furnace performs straight-burning semi-gasification and downdraft full-gasification functions. The furnace is formed by a steel plate that is welded at a lower part of a box furnace body (1) provided with four furnace legs (11) to support the furnace body.    USE - Straight-burning semi-gasification and downdraft full-gasification multifunctional straw furnace for use at home.    ADVANTAGE - The furnace designs a tertiary dashing device so as to clean furnace ash conveniently and quickly. The furnace efficiently generates combustible gas by a crop straw. The furnace purifies and filters the combustible gas during circulation, removes impurity and tar, improves gas quality and cooling and heating effects, prevents environmental pollution and easily processes the tar. The furnace realizes stable gas output, better gas quality and realizes the combustible gas without peculiar smell and pollution. The furnace has wide market prospect.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a straight-burning semi-gasification and downdraft full-gasification multifunctional straw furnace.    Box furnace body (1)    Furnace hearth (2)    Fire grate (3)    Rotation handle (4)    Furnace legs (11)
NOVELTY - Hydrocarbon composition comprises: a gasoil component; a gasoline component; and a hydrocarbon component of a biological origin, where the hydrocarbon component of a biological origin is obtained starting from a mixture of a biological origin containing esters of fatty acids, possibly with quantities of free fatty acids, by means of a process comprising hydrodeoxygenation step of the mixture of a biological origin and possibly a hydroisomerization step of the mixture.    USE - The composition is useful as diesel fuels for engines and combustibles for heating (claimed).    ADVANTAGE - The hydrocarbon composition has improved cold properties, high cetane number, high oxidative stability and high content of biological component.
NOVELTY - The current collector (10) has flat nickel coated stainless steel panel (11) including an upper face (12) and a lower face (13), where the upper face of the panel includes a recess (14) in which a catalyst material (25) is arranged. The material includes staggered elements (30-32). A cross-section of the material is matched to a cross-section of the recess. The recess is formed as a channel (22) that consists of large shiftable staggered sections (18-21). The staggered sections include an offset that corresponds to 10 to 70 percent to 20 to 40 percent of width of the staggered sections.    USE - Current collector for a molten carbonate fuel cell for producing electrical energy.    ADVANTAGE - The upper face of the panel includes the recess in which the catalyst material is arranged, where cross-section of the catalyst material is matched to the cross-section of the recess, thus ensuring insetting of the catalyst material in easy and automatic manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for loading a current collector for a fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic top perspective view of a current collector during loading with catalyst material in an avulsion part.    Current collector (10)    Stainless steel panel (11)    Upper face of stainless steel panel (12)    Lower face of stainless steel panel (13)    Recess (14)    Staggered sections (18-21)    Channel (22)    Catalyst material (25)    Staggered elements (30-32)
NOVELTY - A housing accommodates an electrolytic core including an inner cathode concentrically oriented inside an outer anode immersed in electrolyte solution for electrolysis. The anode is concentrically surrounded by vertically oriented separation pipe (112), to form overlap portion (181) between anode and separation pipe extending above an electrolyte level (134). Electrical power is applied to the anode and cathode to create electrolysis to release hydrogen and oxygen gases. The interior and exterior surfaces of anode are coated with platinum and tantalum.    USE - Hydrogen generator for enhancing combustion in internal combustion engine of automobile.    ADVANTAGE - Vent holes are formed at separation pipe to allow for the flow of gases including hydrogen and oxygen trapped in the free space of the central portion. Since the central volume is larger than the lower volume due to the cross-shaped housing to accommodate electrolyte solution reservoir, the replenishment of electrolytic solution can be minimized. The higher sustained input of power into electrolytic cell is ensured. Hydrogen gas is passed through one-way pressure valve the engine to prevent hydrogen gas flowing backwards at increased efficiency and without generation of spark. Hydrogen production can be increased by providing the non-overlap length of cathode.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic cross-sectional view of the hydrogen generator.    Separation pipe (112)    Electrolyte level (134)    Core side (175)    Side wall (177)    Overlap portion (181)
NOVELTY - The reactor has stirring and shell breaking element (2), and internal heat converting unit (3) that are arranged inside tank (1). A feeder (4) is provided with structure for automatically uploading material stored inside pipeline.    USE - Up-flowing type anaerobic reactor for processing livestock waste, organic waste from village and straw.    ADVANTAGE - The reactor is simple, stable and reliable in operation. The investment cost is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the up-flowing type anaerobic reactor for processing livestock waste.    Tank (1)    Stirring and shell breaking element (2)    Internal heat converting unit (3)    Feeder (4)    Barrel (9)
NOVELTY - Method for manufacturing processed material using automatic compressor, involves performing compression solidification, preferably circular round shaped compression molding of metal fragments generated from several metal processings or several waste materials including crushed wood, chaff, dry waterweed and agricultural waste. The compression solidification process is carried out by a pressure applied using push plate board.    USE - The method is useful for manufacturing processed material which is used in preparation of solid biomass fuel.    ADVANTAGE - The method is simple, cost-effective, versatile and environmentally-friendly. The processed material has high density and can be prepared without any special or advanced techniques. The automatic compressor is inexpensive.
NOVELTY - Producing an algal oil, comprises: (a) continuously providing a growth medium and an algal strain to a bioreactor at a predetermined fluid flow rate; (b) illuminating the growth medium and algal strain contained within the bioreactor by a first artificial light source to effect lipid production by the algal strain; (c) continuously withdrawing a portion of the growth medium and algal strain contained within the bioreactor at the predetermined fluid flow rate; and (d) treating the withdrawn portion of the medium and algal strain to produce and isolate a lipid produced by the algal strain.    USE - The algal oil is useful to produce biofuel, glycerol and biodiesel.    ADVANTAGE - The process is economical, scalable and ecofriendly for preparing algal oil. The system can be arranged very compactly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a system for producing an algal oil comprising bioreactors (26) configured to continuously receive a growth medium and an algal strain at a predetermined fluid flow rate and to continuously output a portion of the growth medium and the algal strain at the predetermined fluid flow rate, where each bioreactor comprises an artificial light source comprising a blue light at a wavelength of 420-450 nanometers and a red light at a wavelength of 640-680 nanometers, where the artificial light source has an illuminance of 2500-10000 lux.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic block diagram illustrating a process for producing algal-based biofuel.    Incubation tank (10)    First conduit (12)    Second conduit (14)    Carbonation tank (26) Bioreactor. (16)
NOVELTY - Methanol and ethanol gasoline additive comprises (%) high-carbon isomer alcohol (50-95), antioxidant (3-5), and long-carbon chain alkane (10-50).    USE - Methanol and ethanol gasoline additive used for gasoline added with 20-40 mass% methanol or ethanol.    ADVANTAGE - The additive improves octane value of gasoline and effectively, reduces discharging amount of carbon dioxide and sulfur dioxide in combusting gasoline, and improves clean degree of gasoline combustion.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for applying ratio of the methanol and ethanol gasoline additive comprising (%) methanol or ethanol (20-40), gasoline additive (3-5), and national standard gasoline (55-75).
NOVELTY - The device has feeding gate and discharging gate that are arranged on fertilizing cabinet in sealing manner. A solar water heater is arranged on top of cabinet. The heating plates are arranged in cabinet. The water outlet of solar water heater is connected with water inlet of heating plates while inlet is connected to outlet of plates. A slope-type bottom is arranged on cabinet whose lowest end is connected with solution collecting slot whose bottom portion is slope-shaped. The fermentation tank is connected with lowest end of solution collecting tank.    USE - Ecological fertilizing device for fertilizing organic garbage.    ADVANTAGE - The fertilizing temperature is improved so as to fertilize microorganism and to improve the fermenting and degrading speed of organic garbage. The hot water is supplied to the heating plates via the solar water heater so that the water is used efficiently. Hence the energy consumption can be reduced and the environment can be protected.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the ecological fertilizing device for fertilizing organic garbage.
NOVELTY - An ecological composting device for organic household garbage, comprises a fermentation tank comprising a side wall, a cover plate, a bottom plate, a feeding door, and a discharging door; where the bottom plate is equipped with a leachate slot set with a leachate fermentation tank; the cover plate is formed by two layers of glasses and is shaped like herringbone composed of a left cover plate and a right cover plate; the left cover plate is set with a solar heating board or a solar transparent plate; and the feeding door is arranged on the right cover plate.    USE - The ecological composting device is useful for organic household garbage (claimed).    ADVANTAGE - The ecological composting device has high utilization ratio in winter. Moreover, the solar heating board or the solar transparent plate belongs to the green energy source, where it is unnecessary to consume resources by other heating methods, even to generate the waste and waste gas in other heating methods; thus, the device has environmental protection and energy conservation properties.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the ecological composting device for organic household garbage.
NOVELTY - The reactor has acidification tank that is mounted above straw stacking chamber. The surface of straw stacking chamber is connected to methane reactor (30). A feed liquid filtration timer is provided with floater frame, floater (15) and biogas slurry inlet and outlet pipe. The upper layer of methane reactor is provided with gas liquid separator while lower layer is provided with biogas lifting pipe (22), gas collection cover (23), helical component (25), return pipe (26), feed liquid pipe (24), blade (29) and bottom return pipe (33).    USE - Biogas reactor.    ADVANTAGE - The high gas yield can be achieved at low cost and the time-saving and labor saving can be attained. The guaranteed biogas supply can be attained and the biogas slurry and residues can be removed efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biogas reactor.    Floater (15)    Biogas lifting pipe (22)    Gas collection cover (23)    Feed liquid pipe (24)    Helical component (25)    Return pipe (26)    Blade (29)    Methane reactor (30)    Bottom return pipe (33)
NOVELTY - Manufacturing hydrogen containing water comprises: (a) manufacturing acidic colloid liquid of at least one phosphate of calcium and magnesium; (b) mixing acidic colloid liquid manufactured at (a), and manufacturing dispersion liquid and aqueous alkali solution at pH 5-8; and (c) obtaining hydrogen containing water by electrolyzing water in dispersion liquid manufactured at (b).    USE - The method is useful for manufacturing hydrogen containing water (claimed).
NOVELTY - A sewage processing method comprises (A) removing floating oil, dispersing oil and part of emulsifying oil from sewage; (B) separating suspended material of the sewage from solid particle impurity; (C) degrading petroleum of sewage by microorganism; and (D) nanofiltering sand, bacterium and colloid material, and virus from sewage and degrading petroleum by bacterial strain. The microorganism strain is from nature and is obtained through manual sieving and domestication. The microorganism strain is from nature and is obtained through manual sieving and domestication.    USE - Sewage processing method for returning oil field producing water to low-permeability oil field.    ADVANTAGE - The discharged water quality satisfies demand of water quality returned to low (ultra-low) permeability oil field.    DETAILED DESCRIPTION - Sewage processing method comprises (A) removing floating oil, dispersing oil and part of emulsifying oil from sewage; (B) separating suspended material of the sewage from solid particle impurity; (C) degrading petroleum of sewage by microorganism; and (D) nanofiltering sand, bacterium and colloid material, and virus from sewage. The degradation process includes preparing oil-containing sand oil sample of oil field and pouring 1 g into conical flask containing 500 mg/L of petroleum and 100 mL of distilled water; processing shaker culture and domestication, after processing domestication for 1 month, purifying and separating strain to obtain 1 Bacillus bacterial strain (Bacillus sp. (CGMCC No.3344)); and degrading petroleum by bacterial strain. The microorganism strain is from nature and is obtained through manual sieving and domestication.
NOVELTY - Producing biofuels from algae comprises: cultivating an oil-producing algae by photoautotrophic growth; producing algal oil by heterotrophic growth of the oil producing algae, where the heterotrophic growth is fed by introducing a sugar feed to the oil-producing algae; and extracting an algal oil from the oil-producing algae.    USE - The process is useful for producing biofuels from algae, e.g. biodiesel product, which is a fatty acid ethyl ester or an alkane (all claimed).    ADVANTAGE - The process: produces the biodiesel product which is substantially free of sulfur; is highly efficient and energy-positive i.e. the energy produced in the form of fuels is far in excess of external input energy, because very little fossil energy is used; does not require any heavy machinery, expensive fuels, or chemical fertilizers and pesticides for algae growth; and eliminates the transportation costs since the algae can be processed near the growth ponds in the process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biodiesel product formed by the process.    DESCRIPTION OF DRAWING(S) - The figure shows the process flow of a system for production of biofuels from algae.    Light stage (2)    Dark stage (6)    Nitrogen fixing algae (8)    Cultivation sub-system (10)    Extraction sub-system (20)
NOVELTY - The method involves depositing a conductive powder with a charge relaxation time of less than about 1 second onto a substrate. The conductive powder is mixed with magnetic carrier beads in sump to form a mixture of conductive powder and magnetic carrier beads. The substrate is positioned away from magnetic brush such that an air gap is arranged between substrate and magnetic brush. A large asymmetry is produced between magnetic brush and substrate such that the electric field at magnetic brush is 3.0 times as great as the electric field at such substrate.    USE - Method for manufacturing electrodes for fuel cell such as polymer electrolyte fuel cell (PEFC), phosphoric acid fuel cell (PAFC), alkaline fuel cell (AFC), molten carbonate fuel cell (MCFC) and solid oxide fuel cell (SOFC) used in household and business, power source for automobile and truck, and personal mobile device e.g. cell phone.    ADVANTAGE - The method enables electrostatic multi-layer deposition of non-magnetic conductive powder/blend onto either insulative or conductive substrates.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view illustrating the manufacturing system producing uniform powder coatings.    Single substrate sheet (4)    Substrate-transporting belt (6)    Backing plates (8)    Idler roll (11)    Sintering operation (18)
NOVELTY - The forming method involves combining carbon and binder materials to form a stock mixture (16). The carbon material includes compressible particles, preferably graphite particles, having preset maximum grain size. The stock mixture is resistively and compressively heated to form a partially carbonized preform body. The resistive and compressive heating step includes applying electric current to stock mixture to generate heat within the stock mixture, and applying pressure of 35 kilograms per square centimeters to the stock mixture.    USE - Forming method for carbon body, such as graphite article (claimed) e.g. graphite plate, graphite billet used in e.g. nuclear reactor, electrochemical fuel cell, production of silicon and polysilicon.    ADVANTAGE - The stock mixture is resistively and compressively heated to form a partially carbonized carbon body whose gross dimensions are approximate to desired machined dimensions of final graphitized carbon body, thus shortening process time required to carbonize the stock mixture, while providing an increase in obtainable material yield. The resulting carbon body has desired characteristics in terms of density and composition, since predetermined production parameters are adjusted based on comparison of detected measurements with preprogrammed set of desired values.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a graphite article e.g. graphite plate.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic block diagram of the hot press apparatus used in forming the carbon body.    Hot press (10)    Mold box (12)    Stock mixture (16)    Hydraulic system (30)    Resistive heating system (32)
NOVELTY - Production of biofuels from biomass, involves: depolymerizing a biomass to form a feed, where the feed is provided by autotrophically growing algal biomass and extracting the feed from it by depolymerizing the algal biomass; converting the algal feed to an algal oil by introducing the algal feed to an oil-producing algae under growth conditions to encourage formation of algal oil within the oil-producing algae; extracting the algal oil from the oil-producing algae; and converting the algal oil to biodiesel.    USE - For production of biofuels from biomass (claimed). The biofuels are e.g. biodiesel or bioethanol.    ADVANTAGE - The process is highly efficient and energy-positive, i.e. the energy produced in the form of fuels is far in excess of external input energy, because very little fossil energy is used. The algae growth requires none of the heavy machinery, expensive fuels, or chemical fertilizers and pesticides required by conventional agriculture. The algae can be processed near the growth ponds, eliminating transportation costs.
NOVELTY - A plasma reaction pipe (5) irradiates microwave generated by a microwave generator to organic waste liquid such that the microwave is reacted with the plasma. A reactive-gas supply portion supplies nitrogen or argon to the plasma reaction pipe as a reactive gas. A collection section collects the product of organic waste liquid decomposed with the plasma. The internal atmospheric pressure of the plasma reaction pipe is reduced and fixed at specific pressure suitable for a glow discharge, by a vacuum pump and a pressure gauge.    USE - Processing apparatus of organic waste liquid e.g. insulating oil used for transformer, using microwave non-equilibrium plasma.    ADVANTAGE - The presence of carbon dioxide in the decomposed product is prevented, so that the global warming is prevented. The fall of decomposition ratio of organic waste liquid in the inside of plasma reaction pipe, is prevented. The operational cost of the processing apparatus is reduced.    DETAILED DESCRIPTION - A reflection section (18a) reflects the microwave passed through the inside of a microwave waveguide (2). The reflected microwave is penetrated into plasma reaction pipe through a permeation section (17). An INDEPENDENT CLAIM is included for processing method of organic waste liquid, which involves irradiating microwave in the plasma reaction pipe. The plasmified nitrogen or argon is supplied to organic waste liquid as reactive gas, to decompose the organic waste liquid. The microwave is reflected by irradiating the microwave to the reflection section, and is irradiated to a position spaced apart from the waveguide.    DESCRIPTION OF DRAWING(S) - The drawing shows an enlarged sectional view of the plasma reaction portion of organic waste disposal apparatus.    Microwave waveguide (2)    Plasma reaction pipe (5)    Permeation section (17)    Hollow portion (17a)    Reflection section (18a)
NOVELTY - A microwave is irradiated into a plasma reaction tube. Biomass or organic waste liquid is supplied to reaction tube in a state in which oxygen is supplied as reactive gas is plasmified with microwave nonequilibrium plasma. Biomass or organic waste liquid is decomposed, and combustible gas is produced. The supply rate of oxygen is less than equivalent reaction ratio.    USE - Processing of organic substance and producing combustible gas used for fuel cell.    ADVANTAGE - The organic substance is efficiently, stably and continuously processed and modified into combustible gas.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of processing apparatus of organic substance.    Microwave generator (1)    Microwave guide (2)    Injection portion of organic substance (3)    Reactive gas supply portion (4)    Processing apparatus of organic substance (A)
NOVELTY - The method involves utilizing a micro bubble generator, and increasing aqueous solution temperature by irradiating an ultrasonic wave to an aqueous solution. Electrolytes i.e. sodium hydroxide, and tap water are added in the aqueous solution. Temperature difference is produced between the aqueous solution and normal temperature air. Air fuel mixture of hydrogen and oxygen is sent to an atomic hydrogen gas reservoir tank (6) through an atomic hydrogen gas air pipe (5) from an enclosed gas collecting cover (12) of an atomic hydrogen gas manufacturing plant.    USE - Method for obtaining turning electric power generation or motive power for a turbine of a motor vehicle.    ADVANTAGE - The method allows acquiring non-pollution energy, avoids environmental pollution, and enables actively producing the thermal energy at high temperature and atmospheric temperature from the atomic hydrogen gas manufacturing plant.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an atomic hydrogen gas generation device.    Atomic hydrogen gas air pipe (5)    Atomic hydrogen gas reservoir tank (6)    Pressurization apparatus (7)    Electrolysis electrode (11)    Enclosed gas collecting cover (12)    Automatic water supplying apparatus (13)
NOVELTY - The apparatus (10A) has a laser apparatus (13) that irradiates laser beam (12) with respect to to-be-measured gas (11). A photodetector (17) is provided for measuring the Raman scattered light (16) generated by irradiation of laser beam (14). The plasma emission (19) generated by irradiation of delayed laser beam (12) by laser-beam delay line (18) is measured by time-lag with photodetector.    USE - Gas analysis apparatus used for measuring gas component such as carbon dioxide, nitrogen, hydrogen, water, carbon monoxide, methane and ammonia in to-be-measured gas such as fuel gas and combustion gas.    ADVANTAGE - Since the plasma emission generated by irradiation of delayed laser beam by laser-beam delay line is measured by time-lag with photodetector, effective irradiation of laser beam can be ensured to analyze the as components.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for gas analysis method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the gas analysis apparatus. (Drawing includes non-English language text)    Gas analysis apparatus (10A)    To-be-measured gas (11)    Laser beams (12,14)    Laser apparatus (13)    Raman scattered light (16)    Photodetector (17)    Laser-beam delay line (18)    Plasma emission (19)
NOVELTY - A solid fuel is obtained by mixing wood chip and sawdust, adding the obtained mixture to starch and water, suspending, heating, forming gel-like gelatinized substance and molding obtained substance to desired shape.    USE - Solid fuel is used for wood stove.    ADVANTAGE - The solid fuel having excellent transportability, usability and storage stability is manufactured easily without environmental pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows manufacture of solid fuel. (Drawing includes non-English language text)
NOVELTY - Method for producing ethanol from biomass, involves mixing xylose-utilizing yeast that has been so transformed has to over-express at least one gene for a metabolism enzyme involved in a pentose phosphate pathway with a saccharification biomass and culturing the mixture.    USE - The method is useful for producing ethanol from biomass (claimed) e.g. rice straw, which is used as alternative fuel for fossils.    ADVANTAGE - The ethanol causes no global warming and food problem while used as fuel.
NOVELTY - Processing plant biomass involves grinding plant and extracting juice from the ground product. The obtained material is processed with chemicals.    USE - Method for processing plant biomass used in preparing carbohydrates, enzymes, ethanol (claimed) and food products.    ADVANTAGE - The method requires less energy to process plant biomass.
NOVELTY - A biomass solid forming fuel is prepared by conveying papermaking waste residue sludge and biomass dry powder to mixing box to obtain mixture; conveying the mixture to stirrer, fully stirring and dispersing; conveying the mixture to drying machine; reducing water content and conveying to distribution cabin; conveying the mixture to forming machine, compressing to obtain solid forming fuel, sieving, cooling and drying to further reduce water content; and conveying the solid forming fuel to mechanical packaging machine.    USE - Method for preparing biomass solid forming fuel (claimed).    ADVANTAGE - The method makes use of papermaking waste residue sludge and biomass dry powder, thus producing clean biomass solid forming fuel and consumption of mineral substance energy is reduced.    DETAILED DESCRIPTION - Preparing biomass solid forming fuel comprises conveying papermaking waste residue sludge and biomass dry powder to mixing box to obtain mixture; conveying the mixture to stirrer, fully stirring and dispersing the mixture; conveying the mixture to drying machine via a conveyer; reducing water content of the mixture via the drying machine, and conveying to distribution cabin; conveying the mixture to forming machine, compressing to obtain solid forming fuel, sieving, cooling and drying in air to further reduce water content; and conveying the solid forming fuel to mechanical packaging machine to obtain finished product.
NOVELTY - The pellet has a circular cylinder provided at a base, where the pellet is made of reed crushed particle with 10 mm size. Water content in the finished pellet is set to 17 percent.    USE - Fuel pellet.
NOVELTY - The gas furnace has a main furnace (7) including a hearth (1), a fire grate (6) and a cracking bin (4) on a lower part of the fire grate. A combined purifying furnace (10) comprises a cyclone purifying bin (13) and an ash storage chamber (12). A bottom side of the cyclone purifying bin is connected with the ash storage chamber. The cracking bin is connected with the cyclone purifying bin by a connecting pipe (5). An upper part of the combined purifying furnace is provided with another cracking bin (14) whose inlet is connected with the cyclone purifying bin.    USE - Downdraft centralized biomass gas furnace.    ADVANTAGE - The gas furnace has simple structure, high biomass gas transformation efficiency and low tar content.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a downdraft centralized biomass gas furnace in partial section.    Hearth (1)    Cracking bins (4, 14)    Connecting pipe (5)    Fire grate (6)    Main furnace (7)    Combined purifying furnace (10)    Ash storage chamber (12)    Cyclone purifying bin (13)    Tar purifying chamber (17)
NOVELTY - The system has a fluidized bed gasification furnace provided with an inlet. An outlet of a dust hopper is connected with a feeder. An outlet of the spiral feeder is connected with an air blowing port of a burner. An outlet of a vortex burner is connected with the inlet of the fluidized bed gasification furnace. The biomass coke collected by a dust hopper is input into an air blowing port via the feeder and under the function of wind power. The biomass coke is entered into the vortex burner to carry out pyrolysis so as to complement heat quantity to the fluidized bed gasification furnace.    USE - Two-stage circulating fluidized bed biomass gasification system.    ADVANTAGE - The system ensures that the biomass powder has good pyrolysis effect in the fluidized bed gasification furnace and the fixed carbon in the biomass coke can have fully pyrolysis via the vortex burning room. The heat quantity is provided to the fluidized bed gasification furnace to carry out pyrolysis circularly, thus avoiding wastage of the biomass powder heat energy and the improving thermal efficiency of the gasification system effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a two-stage circulating fluidized bed biomass gasification system.
NOVELTY - The purifier has an impurity discharge port (2) arranged below a shell (3). An air inlet (5) is arranged above a side of the shell, and an air outlet (6) is arranged below another side of the shell. The shell is provided with a purifying device that is composed of upper purifying sheets (1) and lower purifying sheets (4). The upper and lower purifying sheets are respectively connected with an inner upper wall and an inner lower wall of the shell. The upper and lower purifying sheets are arranged in staggering way. Corridor type upper and lower passages are formed in the shell.    USE - Fuel gas purifier for a straw gasification furnace.    ADVANTAGE - The purifier uses the gravity setting and baffling separating principle to remove the moisture and dust in the fuel gas, which solves the problems that the impurity in the straw fuel gas usually blocks the outlet of the fuel gas furnace, ensures the normal running of the fuel gas furnace, saves gas and consumes no energy in the purifying process.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a fuel gas purifier.    Upper purifying sheets (1)    Impurity discharge port (2)    Shell (3)    Lower purifying sheets (4)    Air inlet (5)    Air outlet (6)
NOVELTY - A garbage disposal device comprises a reaction chamber, a combustion chamber, a heat conductive pipe, a collecting pipe, a water cooling condensing tube, an oil gas separator, and a collector; where more than one reaction chambers and more than one combustion chambers are independent mutually and isolated from each other; a fuel inlet is arranged at the lower end of the combustion chamber; the heat conductive pipe is connected with the upper end; and the collecting branch is interconnected with a collecting pipe at the center of the water cooling condensing pipe.    USE - The garbage disposal device is useful for industrial and commercial applications.    ADVANTAGE - The garbage disposal device is set with a temperature controlling valve for controlling high-temperature reaction in order to make the garbage disposal device regenerate tar and bricks. Moreover, the device is environment-friendly and practical.    DETAILED DESCRIPTION - A garbage disposal device comprises a reaction chamber, a combustion chamber, a heat conductive pipe, a collecting pipe, a water cooling condensing tube, an oil gas separator, and a collector; where more than one reaction chambers and more than one combustion chambers are independent mutually and isolated from each other; a fuel inlet is arranged at the lower end of the combustion chamber; the heat conductive pipe is connected with the upper end; the upper end of the reaction chamber is interconnected with the collecting pipe; the collecting branch is interconnected with a collecting pipe at the center of the water cooling condensing pipe; the terminal of the collecting pipe is stretched out from the water cooling condensing pipe and connected with the oil gas separator; the oil gas separator is respectively connected with an air outlet and a liquid outlet; and the collector is connected and sealed with the reaction chamber.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the garbage disposal device.
NOVELTY - The method involves separating bio oil by quickly pyrolyzing biomass in fluidized bed (7), generating condensable bio oil, pyrolysis gas products of pyrolysis gas and solid residue, and quickly separating generated products. The bio oil is condensed by employing organic condensing agent i.e. L-isoparaffin, to quickly condense the separated products, and condensing the condensable bio oil in the products as small liquid drops. The bio oil is collected by separating the condensed bio oil liquid drops, and obtaining the bio oil. The separated pyrolysis gas is used through processing.    USE - Method for efficiently purifying, separating and collecting bio oil.    ADVANTAGE - The method processes condensing for the biomass pyrolysis gas products by using a method of organic solvent direct cooling, and prepares the bio oil, thus avoiding that the bio oil is employed to condense the pyrolysis gas in traditional direct cooling technology, after the bio oil is cycled and condensed for a lot of times, avoiding the increase in the stickiness, avoiding the bad flowing performance, and avoiding the easy clotting of the bio oil and solid particles at a nozzle to cause the nozzle blocking.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for efficiently purifying, separating and collecting bio oil.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a device for efficiently purifying, separating and collecting bio oil. '(Drawing includes non-English language text)'    Bunding filter (1)    Venturi condenser pipe (2)    Gas-liquid separator (3)    Fluidized bed (7)    Oil pump (10)
NOVELTY - A manufacturing plant of solid fuel from sludge comprises rough crusher which crushes waste material, washing dehydrator which washes and dehydrates the roughly crushed waste material, chlorine-containing resin removal apparatus which determines and removes chlorine-containing resin based on the reflectance of electromagnetic waves, crusher which crushes the sludge in which the chlorine-containing resin is removed, pressure reduced fermentation drying apparatus which ferments and dries sludge in a pressure reduced environment, and molding machine which molds the dried sludge.    USE - Manufacturing plant of solid fuel from sludge.    ADVANTAGE - Generation of toxic substances is reduced and is low cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the manufacturing plant of solid fuel. (Drawing includes non-English language text).    Manufacturing plant of solid fuel (1)    Mixed waste process line (2)    Sludge disposal line (3)    Wooden waste treatment line (4)    Solid fuel production line (5)
NOVELTY - The capacitor has a polarizing electrode which is the metal electrode provided with an interface with the base material such as ion exchange resin. The negative electrode of polarizing electrode is an interface with the base material. The lithium alloy formed from metal component contained in the negative electrode, and the lithium ion, are contained in the electrolyte solution.    USE - Capacitor. Uses include but are not limited to electric vehicle, electric wheelchair, notebook computer, palm type personal computer, mobile telephone, packaging case of electric tool, medical device, digital camera, home appliance, electrically-driven toy, de-mineralizer used in manufacturing pure water used in boiler of power station, semiconductor manufacturing process, and fuel cell electric power generation, and display.    ADVANTAGE - The large electrostatic capacitance is achieved by using the electrolyte containing lithium ion. Since the metal electrode is provided, the need for using the collector is avoided. The number of components is reduced, and the size and weight of the capacitor are reduced.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacturing method of capacitor; and    (2) usage method of capacitor.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical view of the repetition characteristic of charging/discharging after the lithium containing negative electrode formation.
NOVELTY - The furnace has a structure of furnace body which is composed of a hearth (1), a water cavity (2), a spiral pipe (3), a water supplying system (4) and a water spraying nozzle (5). The series of devices of natural solar energy are directly used where water is sprayed out, and hydrogen and carbon monoxide gas are produced, and a chemical molecule atomic fission chaining reaction is carried out. A theoretical basis is based on predetermined chemical molecule formula atomic fission chaining reaction.    USE - Furnace for decomposing water into hydrogen and carbon monoxide for treating garbage and sewage used in e.g. rural area.    ADVANTAGE - Provides energy from combustible substance in burned garbage, crop straw, corn straw, wheat straw, branch and leaf and weeds which are crushed and compacted, and are combusted for generating power. Uses waste heat for treating the sewage, and the modern agriculture is developed. Enables production of agricultural product in a non-seasonal manner, and can be cultivated in a soilless manner. The production of the agricultural product is industrialized and automatic.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the furnace for decomposing water into hydrogen and carbon monoxide.    Hearth (1)    Water cavity (2)    Spiral pipe (3)    Water supplying system (4)    Water spraying nozzle (5)
NOVELTY - The furnace has housing (1) whose top portion is provided with a furnace cover (3) for sealing a charge door (2). An air outlet (9) is arranged on the housing. The furnace cover is screwed to a screw rod (4). The lower end of the screw rod is fixed with a pressing spiral disc (5) located in the internal cavity of the furnace housing. The top wall of furnace housing is fixed with a smoke blocking sleeve (6).    USE - Straw gasification furnace.    ADVANTAGE - The straw gasification furnace can be installed in a simple manner. Smoke can be prevented in the straw gasification furnace. Sufficient air supply pressure can be achieved in the gasification furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the straw gasification furnace.    Furnace housing (1)    Charge door (2)    Furnace cover (3)    Screw rod (4)    Pressing disc (5)    Smoke blocking sleeve (6)    Air outlet (9)
NOVELTY - The anaerobic reactor comprises a gas-liquor separator, which is provided with a gas-liquor input hole, a water liquor output hole and a gas output hole. Gas-liquor input hole is connected with a gas delivery pipe of each three-phase separator. Return pipe has upper end connected with the water liquor output hole and lower ends extending to bottom of a containing space of the tower body. Water outlet provided on the tower body is the channel for the processed sewage to flow out of the tower body. Gas outlet is connected with gas output hole for discharging biogas generated by sewage reaction.    USE - Energy-saving type efficient anaerobic reactor.    ADVANTAGE - Contains a large quantity of microorganism for removing pollutant and achieves internal recycle of the water quality processing.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of the energy-saving type efficient anaerobic reactor.
NOVELTY - The ecological filler structure comprises a planting layer (1), a water distribution layer (3), a double oxide layer (6) and a water collection layer (7) that are arranged from top to bottom. Water distribution layer (3) is provided with a ceramsite layer (2). A dephosphorization layer (4) is arranged between the water distribution layer and the double oxide layer, such that double oxide layer, the water collection layer and the dephosphorization layer are evenly doped with an ecological filler (5).    USE - Ecological filler structure for man-made land sewage treatment system.    ADVANTAGE - Improves physicochemical properties of the soil, improves looseness of soil, avoids overquick hardening of soil, provides a good living space for microorganisms, and guarantees treating effect. Provides a ceramsite structure that improves porosity of the soil, avoids overquick blocking of the land treatment system, improves impurity removal efficiency, and prolongs effective working time. Improves dephosphorization rate, reduces the material cost and attains recycling of waste resources.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic cross-section of the ecological filler structure for man-made land sewage treatment system.    Planting layer (1)    Ceramsite layer (2)    Water distribution layer (3)    Dephosphorization layer (4)    Ecological filler (5)    Double oxide layer (6)    Water collection layer (7)
NOVELTY - The cover (2) has a furnace body (5) whose upper end is provided with a V-shaped water trough. An upper plane of the furnace body is 20 mm greater than an upper plane of the V-shaped water trough.    USE - Sealing cover for a straw gasification furnace.    ADVANTAGE - The upper plane is changed into a convex arc-shaped spherical surface for enabling water vapor without discharging into the water trough through flow back by gravity of water, thus avoiding water spot of fuel at the upper part after blowing out and enabling easy start.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a sealing cover.    Sealing cover (2)    Furnace body (5)
NOVELTY - The device has a burning furnace body whose lower part is provided with an air chamber and a middle part is provided with a burning chamber with a water interlayer. An upper part of the body is provided with a smoke collecting chamber. Annular clapboard is arranged on the smoke collecting chamber. Multiple smoke exhaust holes are arranged on the annular clapboard. One end of a gas purifying device is connected to the smoke collecting chamber of the burning furnace body through a pipeline and another end is connected to a stove. A drainage port is arranged below the gas purifying device.    USE - Straw gas device.    ADVANTAGE - The device is simple in structure, convenient to use, high in energy source utilization rate, environment friendly and ensures health benefits to workers.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a straw gas device.
NOVELTY - The furnace has a dust shaving plate pull rod (5) connected on a dust shaving plate. A wind matching chamber is connected below a heating furnace body. The wind matching chamber is provided with a wind supplying chamber (16), an oxygen supplying chamber (15), a wind supply system, a heating furnace door (26) and a fire grate (25). The wind supplying chamber is directly connected with a bottom of a charging basket (17) via the fire grate. The oxygen supplying chamber is connected with an inflaming retarding chamber (8) via an inflaming retarding chamber wind channel (18).    USE - Biomass straw gasification heating furnace.    ADVANTAGE - The furnace has an integrated design. The furnace avoids the peculiar smell and asphalt oil. The furnace cleans the dust at any time, so that the using process is clean and healthy and does not cause pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass straw gasification heating furnace in partial section.    Dust shaving plate pull rod (5)    Inflaming retarding chamber (8)    Oxygen supplying chamber (15)    Wind supplying chamber (16)    Charging basket (17)    Inflaming retarding chamber wind channel (18)    Fire grate (25)    Heating furnace door (26)
NOVELTY - The apparatus has an absorptive tower for selectively absorbing the carbon dioxide from the exhaust gas. A stripper is provided for degassing the carbon dioxide containing ammonia solution. An ammonia removal unit (10) is used for removing ammonia from carbon dioxide. An ammonia reactor (2) is used for spraying sulfuric acid solution to react with the ammonia. A water supply unit (4) is provided for supplying water to the reactor for maintaining the concentration of sulfuric acid regularly.    USE - Apparatus for removing trace amounts of ammonia from gas discharged through carbon dioxide collection process using aqueous ammonia, used in fertilizer factory.    ADVANTAGE - The need of utilizing excess amount of water and energy for processing of ammonia are reduced and also the cost required for ammonia treatment is reduced efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the ammonia removal apparatus.    Ammonia reactor (2)    Water supply unit (4)    Ammonia removal unit (10)    Sulfuric acid container (31)    Valve (41)
NOVELTY - Microbial composition comprises Bacillus subtilis, Streptomyces microflavus, Trichoderma koningii and Chaetomium globosum.    USE - Microbial composition for decomposing agricultural waste.    ADVANTAGE - The microbial composition enables to decompose agricultural waste rapidly and remove gas generated by organic waste.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing microbial composition, which involves:    (A) obtaining potato agar culture medium by sterilizing 15 pounds of mixture consisting of 200 g peeled potato, 20 g glucose and 15-20 g agar for 30 minutes;    (B) obtaining nutrient agar medium by sterilizing 15 pounds of mixture consisting of 10 g peptone, 3.0 g beef extract, 10 g sodium chloride, 15 g agar and 1000 ml distilled water at pH 7.0 for 30 minutes;    (C) obtaining carrier culture medium, which contains 50% of rice hull, 20% of bran, 14% of bone meal, 14% of fish meal and 2% of brown sugar;    (D) inoculating and culturing Trichoderma koningii and Chaetomium globosum to the potato agar medium at 28 degrees C for 7 days to obtain primary inoculants;    (E) inoculating and culturing Bacillus subtilis and Streptomyces microflavus to the nutrient agar medium at 32 degrees C for 7 days to obtain primary inoculants;    (F) inoculating the primary inoculants of Trichoderma koningii and Chaetomium globosum to the potato agar medium at 24 degrees C for 72 hours to obtain the secondary inoculants;    (G) inoculating the obtained primary inoculants of Bacillus subtilis and Streptomyces microflavus to the nutrient agar medium at 32 degrees C for 72 hours to obtain secondary inoculants;    (H) inoculating the secondary inoculants of the four microorganisms to the carrier culture medium at 28 degrees C for 7 days; and    (I) drying the material at 35-40 degrees C to obtain the desired product.
NOVELTY - Actinomucor elegans No.1 strain has preservation number CGMCC No.3881, and is new. The strain is stored in China microbial culture preservation commission common microbial center.    USE - Actinomucor elegans No. 1 strain used in fungicide for degrading and eliminating fungus from kitchen garbage (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing fungicide, which involves:    (A) inoculating Actinomucor elegans CGMCC No.3881 on a potato dextrose agar (PDA) slant;    (B) inoculating Paenibacillus cineris CGMCC No.3881 on a peptone and beef extract;    (C) culturing the microorganisms at 15-43 degrees C for 24-72 hours in a shaker;    (D) rotating the shaker at 100-250 revolutions per minute for 48-120 hours at 15-43 degrees C; and    (E) putting culturing liquid in a fermenter and them fermenting the material for 48-72 hours at 15-43 degrees C to obtain the desired product.
NOVELTY - Pyrene is degraded by adding pyrene into a liquid culture medium solution; adding agricultural waste (5 g/l of medium) as co-metabolism substrate; and stirring at 28 degrees C and speed of 120 revolutions/minute for 20-22 days to degrade.    USE - Method for degrading pyrene.    ADVANTAGE - The method can degrade high-concentration pyrene.    DETAILED DESCRIPTION - Pyrene is degraded by adding pyrene into a liquid culture medium solution; adding agricultural waste (5 g/l of medium) as co-metabolism substrate; and stirring at 28 degrees C and speed of 120 revolutions/minute for 20-22 days to degrade. The white rot fungi is Pseudotrametes gibbosa having a diameter of 10 mm. The liquid culture medium solution comprises white rot fungi (3 pieces) and liquid culture medium (50 ml). The liquid culture medium comprises (g) ammonium chloride (0.44), potassium dihydrogen phosphate (0.2), magnesium sulfate (0.05), calcium chloride (0.01), and Tween 80 (RTM: polyoxyethylene (20) sorbitan monooleate) (1); and further comprises (ml) inorganic solution (1), vitamin solution (0.5), and twice distilled water. The agricultural waste is bran.
NOVELTY - The equipment has a squeezing box (2) comprising a raw material inlet for feeding food waste. A squeezing mechanism (8) and a residue pushing mechanism (9) are arranged inside squeezing box. A residue discharging door (21) is arranged in side wall of squeezing box. An oil-water separating box (4) is interconnected with a filter box (3) for separating oil from filtered oil-water mixed liquid stored in filter box. A reaction box (5) is provided with an additive inlet for feeding additives which enable reaction between separated oil and additives so as to produce biodiesel.    USE - Integrated equipment for transforming food waste into biodiesel.    ADVANTAGE - The biodiesel can be extracted easily from food waste by simple technique.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the integrated equipment for transforming food waste into biodiesel.    Squeezing box (2)    Filter box (3)    Oil-water separating box (4)    Reaction box (5)    Squeezing mechanism (8)    Residue pushing mechanism (9)    Residue discharging door (21)
NOVELTY - The pig house has a reinforced concrete and brick structure wall portion provided with phenyl board outside. The house main portion is provided with a roof made of compound color steel plate, and a light steel structure roof truss. The windows including a south window and a north window are arranged corresponding to each other in position. A fermenting bed is filled with padding which is as high as top of underground groove structure fermenting vat.    USE - Environment-friendly pig house for growing and fattening pigs in northern cold regions.    ADVANTAGE - Pig waste can be rapidly and effectively degraded and digested. Organic padding, sawdust, rice husk, straw in a certain proportion are fermented and created, through fermentation of microbe. Ingredients are partially converted to be feedstuff for pigs. Waste is turned into wealth. Cost of pig house can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of pig house.
NOVELTY - Invention relates to a method of converting methane to ethylene and ethane via oxidative conversion, characterised by that the catalyst used in this process is a mixture of quartz and phthalocyanine complexes of magnesium, aluminium or manganese, where the method is realised at temperature 700-800 degrees C.    USE - Chemistry.    ADVANTAGE - Use of said catalysts increases output of the product. 2 cl, 7 tbl, 7 ex, 2 dwg
NOVELTY - The system has a high temperature heating furnace that carbonizes vegetation raw material filled in biomass retort (1) at high temperature. A water cooling device (3) cools a mixed gas generated in the process of carbonizing the vegetation raw material to obtain mixed fluid. A water washing device (4) washes the mixed gas via water for generating wood gas and a fluid separating device (7) separates pyroligneous and wood tar oil in the mixed fluid. A wood tar oil storing tank (6) and a pyroligneous storing tank (8) stores the wood tar oil and pyroligneous.    USE - Co-production system used for producing e.g. biomass carbon, gas, oil and pyroligneous.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the co-production system.    Biomass retort (1)    Water cooling device (3)    Water washing device (4)    Wood tar oil storing tank (6)    Fluid separating device (7)    Pyroligneous storing tank (8)
NOVELTY - The device has a urea solid storage tank that is installed on pyrolysis furnace through metering material adding device. The bottom of the pyrolysis furnace is sequentially connected with a flow meter and high temperature draught fan. The furnace is provided with electric heater. A photovoltaic generating system with energy storing system is connected with electric heater. The outlet of the pyrolysis furnace is connected with ammonia spraying grating.    USE - Device for making ammonia by urea solid dry-type pyrolysis.    ADVANTAGE - The device saves urea solution and solution storing device. Since pyrolysis energy is provided by photovoltaic generating system energy consumption is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for preparing ammonia.
NOVELTY - Fertilizer comprises (in parts weight): organic fertilizer (20-50), urea (20-50), monopotassium phosphate (20-50), filler (5-10) and plant growth regulator (0.02-0.06).    USE - The fertilizer is useful for growing rice seedlings (claimed).    ADVANTAGE - The fertilizer strengthens seedlings. The fertilizer is suitable for growing rice seedlings in Southern regions.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing the above-mentioned fertilizer, which involves mixing either livestock, or poultry manures, or crop straw or both, fermenting the obtained mixture aerobically at high temperature, drying the fermented mixture, granulating the dried mixture to obtain organic fertilizer, crushing the organic fertilizer, urea, monopotassium phosphate and filler, adding the plant growth regulator to the crushed material, mixing the obtained mixture mechanically, and packaging the obtained product.
NOVELTY - Agent comprises (in %): inorganic fertilizer (10-90), sex attractant (0.2-40), pesticide (2-40), organic substance (5-40) and auxiliary agent (0.1-30).    USE - The agent is useful as fertilizer for promoting growth of plants and as pesticide for controlling injurious insects (claimed) by attracting insects underground and from far away regions. The agent is useful for various vegetables and fruits.    ADVANTAGE - The agent is pollution-free, brightens the color of fruit, reduces use of high toxicity pesticides, improves quality and yield of agricultural products and overcomes the problem that pests naturally avoid smelling medicinal smell.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the above-cited agent, which involves (a) weighing the raw materials, crushing and mixing uniformly and packing the mixture, or (b) weighing materials, mixing, crushing, pelletizing, drying and packing the product.
NOVELTY - Preparation of cinepazide maleate comprises: providing 2-piperazino-1-pyrrolidino-ethanone and 3,4,5-trimethoxy cinnamoyl chloride as starting materials, carrying out N-acylation reaction without an acid-removing agent in a reaction solvent at a certain temperature to obtain cinepazide and treating the cinepazide with maleic acid to prepare cinepazide maleate.    USE - The method is useful for preparing cinepazide maleate.    ADVANTAGE - The method: has less reaction steps and low production cost; is easily controllable; produces the product with high yield and high purity; and is environmental-friendly and thus can be utilized in industries.
NOVELTY - Preparing raw glyphosate ammonium salt comprises: (i) catalytically oxidizing glyphosine to glyphosate and preparing a mixed solution of glyphosate and a solid catalyst; (ii) filling ammonia into the mixed solution reacting, filtering the reacted solution when hot, introducing the filter cakes to the step (i) for recycling and concentrating the filtered solution in vacuum; (iii) filtering the filtrate at 15-20 degrees C, passing the obtained filtrate to the step (ii) and brining the obtained filter cakes; and (iv) using an organic solvent to wash the filter cakes and drying to obtain the product.    USE - The method is useful for preparing raw glyphosate ammonium salt.    ADVANTAGE - The method: has less reaction steps; combines the separation process of the solid glyphosate and the solid catalyst with the preparation of the glyphosate ammonium salt; prepares the product in high yield and high purity, where the product comprises 98.5% of glyphosate with heating loss not greater than 1% and glyphosate content not less than 89.5%; reduces the production cost; recycles the byproduct urotropine; and does not discharge wastewater and thus is environment-friendly.    DETAILED DESCRIPTION - Preparing raw glyphosate ammonium salt comprises: (i) catalytically oxidizing glyphosine to glyphosate and preparing a mixed solution of glyphosate (15-38 wt.%) and a solid catalyst; (ii) filling ammonia into the mixed solution until pH is 6-8, reacting for 20-40 minutes at 60-75 degrees C, filtering the reacted solution when hot, introducing the filter cakes to the step (i) for recycling and concentrating the filtered solution in vacuum until the glyphosate ammonium salt content is 55-65 wt.%; (iii) filtering the filtrate at 15-20 degrees C, passing the obtained filtrate to the step (ii) and brining the obtained filter cakes; and (iv) using an organic solvent to wash the filter cakes and drying to obtain the product.
NOVELTY - The system (10) has a sensor unit for sensing calorie generated in a fuel cell (11) and a reformer (12). Electricity is generated in the fuel cell, and warm water of a hot water tank (14) is provided due to the generated electricity in the fuel cell. The warm water heated up with the fuel cell of a fuel delivery system (13) is supplied to the reformer. A controller controls electric power measurement data e.g. fuel cell loss, of calorimetry data, the calorie and the electricity generated in the fuel cell and the warm water of the hot water tank sensed by the sensor unit.    USE - Home fuel cell system.    ADVANTAGE - The system analyzes load driving condition according to pattern of electricity consumption during summer and winter so as to reduce running cost of the system, thus improving operating efficiency of the system. The system determines optimum operation mode for component modeling of a grid and reduction of driving expense.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a home fuel cell system.'(Drawing includes non-English language text)'    Home fuel cell system (10)    Fuel cell (11)    Reformer (12)    Fuel delivery system (13)    Hot water tank (14)
NOVELTY - The furnace has a tar pyrolyzer (17) designed between dividing wall water tanks. Air flues are remained on bottom parts of high dividing wall water tanks and upper parts of lower dividing wall water tanks. A side wall of the dividing wall water tanks on a water tank upper body (10) of a gasification chamber (21) is provided with a fuel outlet (9). The gasification chamber, a tar pyrolyzer filling gap, high dividing wall water tank lower edge openings, lower dividing wall water tank upper ports and a fuel outlet form a fuel channel.    USE - Steam mixed air medium biomass gasification furnace.    ADVANTAGE - The furnace adopts combination of a water tank of the gasification chamber and multiple dividing wall water tanks, so that temperature by fuel is reduced indirectly, wet steam and air are mixed to be a biomass gasification agent and the tar pyrolyzer is arranged, thus decomposing tar into permanent gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a steam mixed air medium biomass gasification furnace.    Water tank lower body (2)    Fuel outlet (9)    Water tank upper body (10)    Tar pyrolyzer (17)    Gasification chamber (21)
NOVELTY - The device has a cracking furnace (5) whose gas outlet is connected with a gas inlet of a gasification furnace (9). A slag outlet of the cracking furnace is connected with a slag inlet of a slag cooler (6). A slag outlet of the slag cooler is connected with a feed inlet of an ash carbon separator (7). A gas outlet of the gasification furnace is connected with a gas input end of a heat exchanger (11). A gas output end of the heat exchanger is orderly connected with a dust remover (12), an acid removing tower (13) and a drier (14).    USE - Low-temperature cracking and high-temperature gasification device for use in a biomass.    ADVANTAGE - The device is utilized for the biomass gasification by coupling circulating power generation and the biomass liquid fuel preparation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a low-temperature cracking and high-temperature gasification device.    Cracking furnace (5)    Slag cooler (6)    Ash carbon separator (7)    Gasification furnace (9)    Heat exchanger (11)    Dust remover (12)    Acid removing tower (13)    Drier (14)
NOVELTY - The system has an oxidation reduction part provided with an oxidation device and a reduction device that are connected with each other. A gas-solid catalytic part is provided with a gas-solid separating device and a catalytic cracking device. The gas-solid separating device and the catalytic cracking device are connected with each other. A fuel gas processing part comprises a fuel gas cooling device and a fuel gas collecting recycling device, which are connected with each other. The oxidation device is connected with an air guiding device.    USE - Biomass energy balance process control system for use during a gasifying process.    ADVANTAGE - The system controls the gasifying process of biomass and reduces the content of tar generated in the whole gasifying process in an efficient manner. The system is provided with a gasifying furnace whose pressure can be pre-set to micro-negative pressure in a better manner. The feeding amount and valves are adjusted, so as to obtain the gasified fuel gas with lower heat value.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a biomass energy balance process control system.'(Drawing includes non-English language text)'
NOVELTY - The furnace has a shell whose center part is provided with a dewatering cylinder. A draining hole is installed at a bottom part of the shell. A desulfuration cylinder is installed at a center part of the dewatering cylinder and connected with an inlet tube (4). An outlet cylinder is installed at a side part of a casing and connected with an outlet tube. Center part of the outlet cylinder is provided with a blocking cylinder that is connected with an inner wall of the outlet cylinder by a fixing rod. An outlet valve is installed at a bottom part of the casing.    USE - Highly effective low-discharge straw vaporizing furnace.    ADVANTAGE - The furnace outputs pure fuel gas in smooth manner, has easy ignition, and avoids tar generation.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a highly effective low-discharge straw vaporizing furnace in partial section.    Bottom plate (3)    Inlet tube (4)    Fuel gas outlet (11)    Purifier (20)    Air storing tank (21)
NOVELTY - A catalytic combustion agent comprises (%) initiator (3-50), oxidant (4-90), activator (1-20), cleaning agent (0.5-10), and friction reducer (2-30).    USE - Catalytic combustion agent used for fuel comprising large proportion of methanol, particularly mixture of methanol and gasoline, mixture of diesel and methanol, alcohol-based fuel, or mixture of microemulsion, alcohol and biological gasoline (claimed).    ADVANTAGE - The combustion agent improves combustion speed of methanol and promotes quick sufficient combustion of methanol, improves carbon deposit of combustion chamber, cleans and lubricates the engine, saves oil, reduces abrasion of the engine caused by methanol combustion, reduces exhaust of combustion waste gas, inhibits metal corrosion and rubber swelling, and strengthens and improves combustion effect of large proportion methanol fuel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation and utilization of combustion agent by respectively adding initiator, oxidant, activator, cleaning agent and friction reducer to fuel containing large proportion of methanol; or preparing combustion agent product and adding the product (0.1-15%) to fuel comprising large proportion of methanol.
NOVELTY - Coproduction method of glyphosate and glycine, involves concentrating oxidized mother liquid of glyphosate to obtain concentrated mother liquid and diluted mother liquid containing formaldehyde, introducing liquid ammonia to the mother liquid, subjecting the mixture to condensation, maintaining the reaction temperature to obtain diluted solution containing urotropin, subjecting the diluted solution containing urotropin to film treatment to enhance concentration of urotropin from 0.3% to 5-30%, and directly using the obtained solution for producing glycine.    USE - The method is useful for coproducing glyphosate and glycine.    ADVANTAGE - The method is cost-effective and environmentally-friendly.    DETAILED DESCRIPTION - Coproduction method of glyphosate and glycine, involves concentrating oxidized mother liquid of glyphosate by film processing mode to obtain concentrated mother liquid and diluted mother liquid containing formaldehyde, introducing liquid ammonia to the mother liquid until pH value of the mixture reaches 9-10, subjecting the mixture to condensation, maintaining the reaction temperature at 50-70 degrees C to obtain diluted solution containing urotropin, subjecting the diluted solution containing urotropin to film treatment to enhance concentration of urotropin from 0.3% to 5-30%, and directly using the obtained solution for production of aminoacetic acid (glycine).
NOVELTY - Preparing steroid hormone betamethasone ketal intermediate by normal temperature homogeneous reaction comprises condensing (in parts by wt.): a substrate (1), dichloromethane (0.2-14), boron trifluoride etherate (0.04-10), triethyl orthoformate (0.5-12), glycol (1-11) and triethylamine (0.5-18). The substrate is Platts oxide or a semi-reduced product of Platts oxide.    USE - The method is useful for preparing steroid hormone betamethasone ketal intermediate.    ADVANTAGE - The method, in comparison with the conventional process: reduces the reaction time; improves the product content ( not less than 90%) and yield (115-118%); reduces environmental pollution; removes benzene, which damages the health and environment; is eco-friendly; reduces labor; and is good for commercial production.
NOVELTY - System includes processing organic waste to form slurry, and adding microbial enzymes and other additives to the slurry to form a mixture. The mixture is stirred and heated for performing pyrolytic reactions and the mixture is dried and sterilized simultaneously in vacuum to form a solid fertilizer compound.    USE - System for organic waste treatment (claimed).    ADVANTAGE - The system ensures treatment of organic waste in short duration with high efficiency.
NOVELTY - A wood pellet comprises: a lubricant; grape vine particles; and wood particles. The grape vine particles and the wood particles are mixed with the lubricant. The grape vine particles are from grape plant vines of cabernet sauvignon, pinot noir, merlot and/or chardonnay.    USE - As wood pellets (claimed), useful for providing wood flavor during cooking.    ADVANTAGE - The pellet produces a smoked wood and wine flavor that can be transferred to food while cooking. Thus, the pellets provide a wide range of smoked wine flavors to food to satisfy a variety of personal taste preferences.
NOVELTY - The invention relates to a feeding, homogenizing and dosing mechanism meant for the operation of feeding the presses for extruding wood waste as wood dust, which can be used with minor adjustments in both pellets and briquettes presses. According to the invention, the mechanism consists of a dosing device (1), a trough (2), a homogenizing and feeding device (3), a support (4), an atomizing installation (5), a connection trough (6) of the flange-type, a trough support (7) wherein there is mounted a shaft (8) on which a constant-pitch airscrew (9) is fixed, some bearings (10 and 11) and a housing (12) wherein there is mounted, by means of two bearings (13 and 14), an axle (15) on which 26 blades (16) are mounted, being so oriented as to make up a constant-pitch airscrew, 8 blades in the shape of flat plates (17) having the role of homogenizing the wood dust mixture to feed the press.
NOVELTY - The method for producing tar-free synthesis gas (9) and carbon from biomass (1), comprises partially removing the carbon after incomplete gasification, and subjecting the tar-containing pyrolysis gas to a thermal catalytic purification. The process is carried out before the thermal catalytic purification of water vapor, where the purification is carried out by heating the synthesis gas, a catalytic process, and a catalytic process at elevated temperature. The carbon is removed in the form of biomass cokes and is partially removed in the form of carbon black.    USE - Method useful for producing tar-free synthesis gas.    ADVANTAGE - The method ensures economical production of tar-free synthesis gas with high purity.    DETAILED DESCRIPTION - The method for producing tar-free synthesis gas (9) and carbon from biomass (1), comprises partially removing the carbon after incomplete gasification, and subjecting the tar-containing pyrolysis gas to a thermal catalytic purification. The process is carried out before the thermal catalytic purification of water vapor, where the purification is carried out by heating the synthesis gas, a catalytic process, and a catalytic process at elevated temperature. The carbon is removed in the form of biomass cokes, is partially removed in the form of carbon black, and is granulated before discharging wood- and arable soils. Auxiliary material and/or material is added respectively before the granulation that requires the wood- or the arable soils. An INDEPENDENT CLAIM is included for a device for producing tar-free synthesis gas.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of a pyrolyzer.    Biomass (1)    Synthesis gas (9)    Discharge line (13)    Heater battery (27)    Cleaning device. (28)
NOVELTY - Waste wood materials are crushed, cleaned and impurities are removed to obtain raw material. The wood pieces are dried by overheat steam at 300-600 degrees C. The surfaces of the wood pieces are softened, lignin is dissolved, and activity and cementing property of the raw material is increased. The raw materials are molded to obtain biomass fuel product by an extruding apparatus. The obtained product is screened, dried by air current machine, and packed to obtain biomass fuel. The content of water in the obtained product is 5-10%.    USE - Preparation of biomass fuel used as substitute of domestic and industrial coal.    ADVANTAGE - The method provides environmentally-friendly biomass fuel without adding chemical additives as bonding medium to combine the raw material.    DETAILED DESCRIPTION - Waste wood materials are crushed, cleaned and impurities are removed to obtain raw material having granularity of ( phi )0.02-( phi )20 mm. The wood pieces are dried to control the water content to 5-15%. The wood pieces are treated by overheat steam at 300-600 degrees C. The surfaces of the wood pieces are softened and lignin is dissolved to increase activity and cementing property of the raw material. The raw material is molded to obtain biomass fuel product by an extruding apparatus. The obtained product is screened, dried by air current machine, and packed to obtain biomass fuel. The content of water in the obtained product is 5-10%.
NOVELTY - The method involves mixing petroleum distillate material with biomass raw material. The mixed material and hydrogen are guided through a hydrogenation catalyst layer. The hydrogenation catalyst layer is provided with two catalysts under condition of hydrogenation. Reactant is guided through molybdenum-cobalt hydrogenation refining catalyst, molybdenum-nickel hydrogenation refining catalyst, tungsten-molybdenum-nickel hydrogenation refining catalyst or tungsten-molybdenum-nickel-cobalt hydrogenation refining catalyst. The biomass raw material is animal or plant oil and animal or plant fat.    USE - Method for producing mixed diesel oil.    ADVANTAGE - The method enables producing mixed diesel oil in a simple manner, ensuring small side reaction and stable production, reducing production cost of the diesel oil, and broadening material resource of a diesel oil hydrogenation device.    DETAILED DESCRIPTION - The plant oil is bean oil, tung oil, colza oil, arachis oil, manioca fruit oil, palm oil, sunflower seed oil, maize oil, coconut oil or cottonseed oil. The animal oil is lard oil, beef tallow, fish oil, swill-cooked dirty oil or pluck oil. The petroleum distillate material is straight-run diesel oil, catalytic diesel oil, coked diesel oil, viscosity broken diesel oil or cracked diesel oil.
NOVELTY - The furnace has a gasification furnace generator (1) provided with an igniting and ash hole (3). A side of the gasification furnace generator is equipped with an outlet pipe (6) connected with a wind inlet (8). A fan (7) is equipped between the outlet pipe and the wind inlet connected with a purifier barrel (9). The purifier barrel is equipped with an outlet (10). A lower part of a side wall of the purifier barrel is equipped with a water outlet (11). An inner wall of a wind inlet pipe (4) is provided with a spraying hole (5).    USE - Biomass gasification furnace.    ADVANTAGE - The furnace ensures wide range of gas production, small odor, and high burning efficiency, and sufficiently burns material, and saves energy consumption, and is environment-friendly, and has wide application range.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a biomass gasification furnace.'(Drawing includes non-English language text)'    Gasification furnace generator (1)    Igniting and ash hole (3)    Wind inlet pipe (4)    Spraying hole (5)    Outlet pipe (6)    Fan (7)    Wind inlet (8)    Purifier barrel (9)    Outlet (10)    Water outlet (11)
NOVELTY - The method involves allowing an oil-water mixed solution to flow through a reaction container at given flow rate and to flow out from an outlet pipeline. The outlet pipeline is in communication with a separation device to separate molecular oil obtained by cracking from an uncracked oil-water mixed solution in the separation device. The cracked molecular oil is conveyed to an oil storage tank, and the uncracked vegetable oil is returned to a stirring device. The vegetable oil and water in the stirring device are mixed according to volume ratio of 1: 1 to 10, and uniform stirring is performed.    USE - Method for cracking vegetable oil such as rap oil, tung oil, palm oil and linseed oil (all claimed), through oil-water mixing mode based on a high voltage pulse device.    ADVANTAGE - The method enables complete mixing of oil with water through a mixing stirring device such that the mixing of water molecules and oil molecules increase ionization area of oil molecules, so that the oil chain is easy to break, the conductivity of water accelerates the crack of the carbon chain by the pulse field, and the oil chain is continuously cracked so as to separate the cracked small molecular oil having high burning efficiency, thus greatly improving cracking degree of vegetable oil, burning efficiency of oil and enabling complete burning of oil.    DETAILED DESCRIPTION - The vegetable oil is one of rap oil, tung oil, palm oil and linseed oil.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a method for cracking vegetable oil.
NOVELTY - The furnace has a secondary gasifying chamber (20) formed as a T-joint structure, where a rear end of the secondary gasifying chamber is formed with an installing opening of a plasma spray gun (3). A circular gas collecting chamber (38) is connected to an outside part by a synthesis gas outlet (42), and a slag outlet (15) is connected with a slag pond by a water sealing (16). A spiral material pusher is installed in a front part of a horizontal gasifying furnace cavity (18), where a spiral material push head of the pusher stretches to the front part of the gasifying furnace cavity.    USE - Junk biomass plasma gasifying furnace.    ADVANTAGE - The furnace transforms household rubbish into high quality synthesis gas rich in hydrogen, and removes pollution of dioxin. The household rubbish is transformed into methanol product so as to process the household rubbish with zero discharge and without pollution when a gasifying-liquefying production line is formed.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a junk biomass plasma gasifying furnace in partial section.    Plasma spray gun (3)    Slag outlet (15)    Water sealing (16)    Horizontal gasifying furnace cavity (18)    Secondary gasifying chamber (20)    Circular gas collecting chamber (38)    Synthesis gas outlet (42)
NOVELTY - The device has a driving device connected with a rotation shaft. Helix blades are sleeved on the rotation shaft. A feeding pipe is sleeved at an outer side of each helix blade and provided with a feeding hole and a discharging hole. An air hole area is provided with air holes and installed between the feeding hole and the discharging hole. A sealing cover is sleeved at an outer side of the air hole area of the feeding pipe. The sealing cover is provided with an air inlet that is connected with an air outlet of the air delivering device.    USE - Air curtain feeding device for a biomass gasification system (claimed).    ADVANTAGE - The device delivers non-molded crushed wood chips and blows the crushed wood chips to the discharging hole by an air curtain feeding procedure, so that the device has prolonged service life.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biomass gasification system.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of an air curtain feeding device in partial section.
NOVELTY - The method involves accepting a gas stream with low boiling point gases i.e. isobutane. The low boiling point gases are adsorbed with a heated activated carbon fiber material during an adsorption cycle. The fiber material is heated to a desorption temperature to create a desorption gas stream with the boiling gases during a desorption cycle. The desorption gas stream is actively compressed and/or cooled to condense and liquefy the low boiling point gases. A vessel containing the carbon material is purged prior to the desorption cycle.    USE - Gas purification method for recovery and liquefaction of low boiling point gas i.e. isobutane, in an industrial process e.g. manufacturing processing plant (all claimed) such as foam materials packaging manufacturing plant. Can also be used for recovery and liquefaction of methane, propane, carbon dioxide, ammonia, and chlorofluorocarbon, in an oil refining process, power production process and refrigeration system.    ADVANTAGE - The method captures, concentrates, and reuses the low boiling point gases e.g. methane, which are in the effluent gas of industrial processes to increase the sustainability and economics of the industrial processes, provide great environmental benefits and to avoid the need for thermal distribution of the dilute gases in the effluent stream and to reduce potential cost with the avoidance of the cost of thermal destruction and with the reduced need for raw material for input to a dilute gas component gas purification desorption system.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a gas purification system for recovery and liquefaction of low boiling point gases.    DESCRIPTION OF DRAWING(S) - The drawing shows a screen shot of a controller user interface for a dilute gas component gas purification desorption system having a set of vessels for adsorption/desorption.
NOVELTY - The method involves operating an engine (10) by injecting a gaseous fuel and a liquid fuel to an engine cylinder, and diluting a mixture of an engine cylinder. A fraction of gaseous fuel is increased relative to a fraction of liquid fuel that is injected to a cylinder in response to a transient condition i.e. operator tip-out. The gaseous fuel is composed of vaporized alcohol or hydrogen, a carbon monoxide and methane. The fraction of gaseous fuel is injected to an intake manifold (44), and the mixture is diluted with multiple exhaust gas recirculations, camshaft phasing or a valve actuator.    USE - Method for operating an engine of a hybrid vehicle.    ADVANTAGE - The method allows increasing injection of a gaseous fuel during transient engine operating condition, thus reducing engine misfire when the engine is operated at high dilution level to improve the economy and emissions. The method enables increasing combustion during transient engine operating conditions so as to reduce possibilities of poor combustion stability and/or engine misfire, thus improving drivability and decreasing engine emissions. The method enables reducing the injected amount of liquid fuel at a time injection of gaseous fuel begin, so that the engine can continue to operate at a desired air-fuel ratio and a stoichiometric air-fuel ratio.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of an engine.    Engine (10)    Combustion chamber (30)    Intake manifold (44)    Exhaust manifold (48)    Intake cam (51)
NOVELTY - Carboxylic acid is produced by fermenting organic substrate(s) obtained from renewable and natural raw material. The produced carboxylic acid is subsequently subjected to anodic decarboxylation reaction to obtain olefin.    USE - Manufacture of olefin e.g. ethylene, propylene, butylene and pentene used for preparing polyolefin e.g. polypropylene and polyethylene used for diapers, tampons, sanitary/hygiene products, carry bags, trash bags, industrial/agricultural films, nonwoven webs, flexible packages for foodstuffs, cosmetics, perfumes, cleaning products, sunscreen type protectors, jars, lids for vials, kinking glasses, bottles, air ducts, fuel tanks, water tanks, fenders, panels, toys games, electronic equipment, pipes and fittings, flooring, lining, partition, water tanks and cisterns, boats and kayaks, furniture, synthetic grass field and carpets (all claimed).    ADVANTAGE - The method efficiently and economically provides olefin having high yield and productivity by simple method with reduced emission of greenhouse gases of fossil origin.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for polyolefin.
NOVELTY - A molecular reactor core assembly (100) has hermetically sealed outer housing provided with set of apertures for mechanically coupling to fluid flow conduit. Another set of apertures is formed to provide electrical coupling unit. A hollow, cylindrical, fluid skirt is provided at the housing for unidirectional fluid flow. Contact electrodes are electrically coupled to electrically conductive reactor core with inner and outer conductive plate windings, to electrically couple with the power source.    USE - Molecular reactor core apparatus of hydrogen generation system.    ADVANTAGE - The need for installation of electrolytes for producing hydrogen gas can be avoided, so that the hydrogen gas can be generated with easily accessible material without increasing the cost. The design of molecular reactor core apparatus can be simplified. The operational cost of the molecular reactor core apparatus can be reduced. Large amount of energy is concentrated into small dimensional package to produce electro-thermal-chemical force.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for molecular reactor core and control apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the structure of hydrogen generation system.    Molecular reactor core assembly (100)    Molecular reactor core control assembly (200)    Control circuitry (300)    Water replenishment unit (500)    Hydrogen consumption device (2000)
NOVELTY - The method involves hydroprocessing a portion of a bottom fraction (172) under effective hydroprocessing conditions e.g. effective hydrocracking conditions. Hydroprocessed bottom fraction in a volume of a divided wall column (130) is fractionated to produce a first product fraction (174), second product fraction, third product fraction and a common fraction that is passed to the column, where the second product fraction has improved cold flow property relative to the first product fraction, and the third product fraction has an improved cold flow property relative to the bottom fraction.    USE - Method for producing low sulfur distillate products e.g. diesel, arctic diesel and vacuum gas-vegetable oil product.    ADVANTAGE - The method enables producing low sulfur distillate products under effective hydrocracking conditions such as effective hydrocracking conditions and effective catalytic dewaxing conditions, at reduced cost, without requiring additional equipments.    DETAILED DESCRIPTION - The first, second and third product fractions are achieved, where sulfur content of the second product fraction is lower then sulfur content of the first product fraction, and sulfur content of the third product fraction is lower than sulfur content of the first bottom fraction.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a reaction system.    Reactor (110)    Hydrotreatment stage (112)    Hydrocracking stage (114)    Effluent (125)    Divided wall column (130)    First bottom fraction (172)    First product fraction (174)
NOVELTY - An electrode (41) containing carbide material of element of group V is contacted with electrolyte solution (47), carbon dioxide is introduced into the electrolyte solution, and reduced using the electrode. The element of group V is chosen from vanadium, niobium, and tantalum.    USE - Method for reducing carbon dioxide using for forming carbon monoxide, formic acid and methane.    ADVANTAGE - The method enables efficient and economical reduction of carbon dioxide with reduced energy consumption.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) carbon-dioxide reduction catalyst, which contains carbide material of vanadium, niobium and/or tantalum; and    (2) carbon-dioxide reducing device.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of electrochemical cell.    Electrode (41)    Reference electrode (42)    Counter electrode (43)    Solid electrolytic membrane (45)    Electrolyte solution (47)
NOVELTY - The system has main package (1) containing top plate (2). The hydrogen generating apparatus (12) and stack (5) are arranged inside the main package. The detachable pipe (31) is provided above the hydrogen generating apparatus. The space is formed above the burner (4). The detachable pipe is removed from the main package such that the space is larger than or equal to size of burner.    USE - Fuel cell system.    ADVANTAGE - The detachable pipe can be removed from main package and burner can be removed from hydrogen generating apparatus so that the maintainability of burner of hydrogen generating apparatus is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for maintenance method of fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of fuel cell system. (Drawing includes non English language text)    Main package (1)    Top plate (2)    Burner (4)    Stack (5)    Hydrogen generating apparatus (12)    Detachable pipe (31)
NOVELTY - A membrane electrode assembly (50) having anode (10), a polymer electrolytic membrane (20) and a cathode (30) is formed. At least one type of catalyst is introduced into anode and/or cathode by electrochemical deposition method, and fuel cell (100) is manufactured.    USE - Manufacture of fuel cell.    ADVANTAGE - The fuel cell having improved performance is manufactured. The reaction efficiency of catalyst is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows the cross-sectional view of fuel cell.    Anode (10)    Polymer electrolytic membrane (20)    Cathode (30)    Membrane electrode assembly (50)    Fuel cell (100)
NOVELTY - Isomerizing (M1) a saturated hydrocarbon involves: performing the isomerization in the presence of a superacidic ionic liquid comprising an organic cation and inorganic anion, where the anion is a superacidic aluminum trichloride-Lewis base adduct, and of an olefin.    USE - For isomerizing a saturated hydrocarbon (preferably methylcyclopentane to cyclohexane) (all claimed).    ADVANTAGE - The isomerization process increases the research octane number (RON) of gasoline to improve their combustion properties; converts tertiary carbon atom of the hydrocarbon to a secondary carbon atoms, thus affords a less branched saturated hydrocarbon as the product. The method is improved method and economically viable process for isomerization of saturated hydrocarbon. The preparation process is simple and economically viable, and provides the process product (a saturated hydrocarbon with the same empirical formula) in high yield, in high space-time yield. The isomerization of a saturated hydrocarbon can be greatly accelerated when the isomerization is performed in the presence of a superacidic ionic liquid comprising aluminum chloride and in the presence of an olefin as a catalyst. The method is superior to conventional processes because the reaction equilibria are attained significantly more rapidly.
NOVELTY - The water treatment plant has anaerobic tank (1) and aerobic tank (3) between which flow path (2) for reaction liquid to flow along perpendicular direction is provided. A diffuser (21) is provided in bottom portion of the flow path. A gas recovery apparatus (24) is provided to recover gases from the inside of flow path.    USE - Water treatment plant for treating sewage water. Can also be used in treating industrial waste water, etc.    ADVANTAGE - The dinitrogen monoxide gas of high density can be efficiently recovered from the flow path in which reaction liquid flows along perpendicular direction. The motive power required for collection of gas can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the water treatment plant.    Anaerobic tank (1)    Flow path (2)    Aerobic tank (3)    Diffuser (21)    Gas recovery apparatus (24)
NOVELTY - The water content in an electrolytic membrane (1) is adjusted, and a laminated structure (10) is accommodated in a molding die (K). The resin is injected in molding die of high temperature atmosphere, and a gasket is molded to the periphery of a membrane electrode assembly (3). The water content in membrane is adjusted so that the temperature of electrolytic membrane does not exceed the glass softening point temperature by thermal absorption during vaporization, and the volume of air hole of laminated structure is more than that of water vapor.    USE - Manufacturing method of fuel cell e.g. polymer electrolyte fuel cell mounted in electric vehicle, hybrid vehicle, and for use in domestic application.    ADVANTAGE - The fuel cell is manufactured simply at low cost, and the cross leak path of gas can be eliminated effectively. An increase in temperature of electrolytic membrane is suppressed, and the damage of the laminated structure is prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view illustrating the manufacturing process of fuel cell.    Electrolytic membrane (1)    Membrane electrode assembly (3)    Gas diffusion layers (4,4')    Separator (7)    Laminated structure (10)    Molding die (K)
NOVELTY - The system has modifier (4) having burner (5) for generating heat to reform raw fuel into hydrogen rich reformed fuel. A fuel cell main portion (1) produces electric power according to electrochemical reaction using fuel and air reformed with modifier and discharges anode off gas containing hydrogen. The anode off gas is induced towards burner through gas line (2) so as to burn anode off gas. The burner is positioned upwards rather than upper end portion of fuel cell main portion.    USE - Fuel cell system for electric power generation.    ADVANTAGE - The combustion efficiency of modifier and burner can be improved. The moisture content of anode-off gas of main portion can be reduced without lowering the system performance.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of fuel cell system. (Drawing includes non-English language text)    Fuel cell main portion (1)    Gas line (2)    Modifier (4)    Burner (5)    Fuel gas supply piping (30)
NOVELTY - A microbial strain, Alteromonas sp. SN2 (KCTC1170013P) having an activity for degrading polycyclic aromatic hydrocarbon (PAH), is new.    USE - The microbial strain and composition are used for the bioremediation process of PAH contaminants or for purifying PAH contaminants (all claimed).    ADVANTAGE - The strain and bioremediation process can be industrially utilized through low-cost and environment-friendly process, providing a much more economical and efficient process than conventional technologies such as thermal technology, solidification technology, and vapor extraction technology.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) a bioremediation process of PAH contaminants comprising contacting a microbial strain Alteromonas sp. with PAH; and (2) a composition for purifying PAH contaminants comprising the microbial strain Alteromonas sp.
NOVELTY - Treating scattered sewage comprises connecting a sewage inlet pipe (1) with a scattered sewage collecting pipe; delivering the sewage in a regulating pond (2), separating large-grain impurities, and lifting sewage to a non-block biological filter pond (5); uniformly distributing water on a filling module (7); and collecting the filtered water from the non-block biological filter pond, after the filtered water is contacted with a dephosphorization medium (11) to be dephosphorized, and discharging the water.    USE - Method for treating scattered sewage (claimed).    ADVANTAGE - The method saves the sections of secondary precipitation, sludge concentration and sludge treatment in the conventional sewage treatment process, simplifies processing flow, and meets the requirement of microorganism on oxygen by natural ventilation.    DETAILED DESCRIPTION - Treating scattered sewage comprises:    (A) connecting a sewage inlet pipe (1) with a scattered sewage collecting pipe;    (B) delivering the sewage in a regulating pond (2), separating large-grain impurities from a pump grid cover, and lifting sewage to a non-block biological filter pond (5) by a sewage pump;    (C) uniformly distributing water on a filling module (7) mounted on a filling support frame by a water distributor to be fully contacted and purified with a biological film grown and attached on the surface of the filling; and    (D) collecting the filtered water from the non-block biological filter pond by a filter pond water outlet groove before entering a dephosphorization groove, after the filtered water is contacted with a dephosphorization medium (11) to be dephosphorized, and discharging the water from a water outlet pipe.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a device for treating scattered sewage.    Sewage inlet pipe (1)    Regulating pond (2)    Biological filter pond (5)    Filling module (7)    Dephosphorization medium (11)
NOVELTY - An Acidovorax deposited under CGMCC No.3706, CGMCC No.3707, or CGMCC No.3708, is new.    USE - The Acidovorax is useful for processing organic sewage with high concentration and difficult degradation (claimed).    ADVANTAGE - The Acidovorax can efficiently degrade the chemical wastewater microbial culture with high concentration and good biological stability, can process the sewage under the condition of having high mineralization and higher salt content, and can effectively reduce the chemical oxygen demand (COD) in the sewage.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for processing salt content in the organic sewage with high concentration and difficult degradation via the Acidovorax or the Acidovorax preparation, comprising acidizing the sewage to be processed; diluting the acidized sewage; conveying the sewage to a biological reactor; adding the Acidovorax deposited under CGMCC No.3706, CGMCC No.3707, or CGMCC No.3708 or the Acidovorax preparation to the biological reactor; controlling the temperature in the reactor to be 20-40 degrees Ce; and aerating via hydrolysis acidification-contact oxidization process to purify the sewage.
NOVELTY - A hydrogen supply system comprises photocatalyst provided in aqueous solution in container or tube, and light which is applied to photocatalyst to generate hydrogen and oxygen. The hydrogen and oxygen is supplied to fuel cells and internal combustion engine as fuel.    USE - A hydrogen supply system used for fuel cells and internal combustion engine.    ADVANTAGE - The system has improved hydrogen-producing efficiency and simple structure, and improves safety of vehicle.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional schematic diagram of hydrogen supply system.    Water tank (1)    Titanium oxide electrode (2)    Platinum electrode (3)    Xenon lamp (4)    Buoyancy apparatus (5)
NOVELTY - A food steamer type multipurpose solid anaerobic fermentation device, comprises a bottom tank body, a middle tank body that is arranged above the bottom tank body, and a tank cover that is arranged above the middle tank; where the upper edge of a shell of the bottom tank body and the middle tank body is an annular groove; the bottom of the middle tank body is arranged in the annular groove; a sieve plate is arranged in the lower part of the middle tank body; a steam inlet is arranged on the bottom tank body; and an air outlet is arranged on the top of the tank cover.    USE - The food steamer type multipurpose solid anaerobic fermentation device is useful for anaerobic or facultative anaerobic fermentation techniques comprising solid fermentation for producing methane, solid fermentation alcohol, and solid fermentation white liquor.    ADVANTAGE - The food steamer type multipurpose solid anaerobic fermentation device looks like a food steamer and is divided into several segments which are sealed; where the segments can be combined freely according to the production scale to overcome the shortcoming that the solid fermentation is not easy to achieve mechanization and automation when the material is charged or discharged.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the food steamer type multipurpose solid anaerobic fermentation device.
NOVELTY - A straw briquette fuel comprises (wt.%) tobacco straw (70-90), tree bark or corn straw (5-15) and clay (5-15).    USE - Straw briquette fuel for replacing coal to bake tobacco leaf (claimed).    ADVANTAGE - The fuel reduces baking cost, increases yield and saves expenditure for peasant, saves coal, decreases pollution caused by scatted tobacco straw and baked tobacco leaf on rural environment, and cuts off toxic spreading way of tobacco straw.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of straw briquette fuel.
NOVELTY - Batch continuous output arrangement for fatty acid methyl ester transesterification comprises greater than or equal to 3 first unit action grooves, second unit action groove, and third unit action groove, forming a standing pretreatment purification system, and provided with reaction arrangement through which the reaction product after transesterification performs batch continuous feeding, standing, and discharging. The standing pretreatment purification system is used in the production process for producing fatty acid methyl ester; and staggers the feeding, standing, and discharging.    USE - Batch continuous output arrangement for fatty acid methyl ester transesterification useful for producing biodiesel.    ADVANTAGE - The arrangement improves the conversion rate; shortens the work waiting time by continuously outputting and prolonging the standing time. It is capable of producing high purity biodiesel; and improves the yield and market competitiveness.    DETAILED DESCRIPTION - Batch continuous output arrangement for fatty acid methyl ester transesterification comprises greater than or equal to 3 first unit action grooves, second unit action groove, and third unit action groove, forming a standing pretreatment purification system. The first, second, and third action grooves are provided with reaction arrangement through which the reaction product after transesterification performs batch continuous feeding, standing, and discharging. The standing pretreatment purification system is used in the production process for producing fatty acid methyl ester; and staggers the feeding, standing, and discharging according to the standing procedure of transesterification reaction, forming a batch continuous output arrangement of transesterification reaction of feeding, standing, and discharging in synchronous operation, alternative, and independent action at same time.
NOVELTY - Circulation attached-floating microorganism sewage purifying system comprises a pre-treating unit, a microorganism growing unit, a circulating unit, a measuring and controlling unit and a post-processing unit.    USE - System for purifying circulation attached-floating microorganism sewage.    ADVANTAGE - The system has excellent purifying effect.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of the circulation attached-floating microorganism sewage purifying system.
NOVELTY - Device comprises a fermentation chamber, which has an external opening covered by a cover. The fermentation chamber is connected to an air nozzle and an external air pipe. The fermentation chamber contains a material disk and a stirrer, which are arranged below a material inlet.    USE - Device for producing methane.    ADVANTAGE - The device enables to produce methane in a simple and cost-effective manner.
NOVELTY - Increasing hydrophilic properties of crystalline carbon involves use of a surface modifier.    USE - For increasing hydrophilic properties of crystalline carbon, which is useful for preparing Pt/C catalyst. The Pt/C catalyst is useful for preparation of fuel cell electrode for fuel cells (claimed).    ADVANTAGE - The crystalline carbon having increased hydrophilic property enables easier supporting of platinum, thus a high-content, highly dispersed, highly durable Pt nanocatalyst resistant to electrochemical corrosion is suitably prepared. The catalyst when used for an electrode of a fuel cell, the amount of the catalyst suitably coated on the electrode may be decreased. Accordingly, the electrode becomes thinner and has improved fuel transfer efficiency.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a method (M1) for preparing a Pt/C catalyst, involving: increasing hydrophilic property of crystalline carbon using the surface modifier; supporting platinum on the crystalline carbon to prepare a catalyst; and washing and drying thus prepared catalyst to remove unwanted organic materials;    (2) a Pt/C catalyst prepared by using the method (M1);    (3) a fuel cell electrode comprising the catalyst; and    (4) a fuel cell comprising the electrode.
NOVELTY - The processor has a shell (1) which is provided with a water outlet (20) and a residue outlet (21) while a gear (17) is connected with a speed changing box (3) via a transmission shaft (19). A speed changing motor (2) and the speed changing box are fixed in the shell. A transmission gear (7) of speed changing box is engaged with a first transmission chain wheel (8). A second transmission chain wheel (13) is connected with a filter cloth (16) via a chain wheel roller and is in connection with the gears.    USE - Processor for livestock cultivating sewage and poultry and biogas residue slurry.    ADVANTAGE - Provides a processor with rational design, small size, beautiful appearance, practical property, hard structure, quite convenient assembly and maintenance, great processing energy, low operation cost and good safety.    DESCRIPTION OF DRAWING(S) - The drawing shows an internal structure of the processor for livestock cultivating sewage and poultry and biogas residue slurry.    Shell (1)    Speed changing motor (2)    Speed changing box (3)    Transmission gear (7)    First transmission chain wheel (8)    Second transmission chain wheel (13)    Filter cloth (16)    Gear (17)    Transmission shaft (19)    Water outlet (20)    Residue outlet (21)
NOVELTY - The desulfurizer has nutrient solution input and output pipes (6,23) that are connected to biological aerobic marsh gas desulfurization section and are arranged at the bottom of input and output cylinders (7,21) respectively. An overflow pipe (22) is arranged at the upper portion of output cylinder. A disc sprayer (14) is arranged at the upper portion of the biological anaerobic marsh gas desulfurization section. A microporous spray head (13) is arranged on the disc sprayer connected to shower pipe (16), peristaltic pump (17) and water inlet tank (25) in sequence.    USE - Aerobic/anaerobic integrated safe biological marsh gas desulfurizer.    ADVANTAGE - The biological marsh gas desulfurization is safely carried out through biological aerobic marsh gas desulfurization section and based on complete isolation of the biological anaerobic marsh gas desulfurization section form air. The hydrogen sulfide gas in marsh gas is processed under combined action of aerobic and anaerobic desulfurization bacteria, such that the purified marsh gas measures up to the standard for use. Single substance sulfur is formed, which can be recycled, thus the treatment cost of the desulfurizer is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of the aerobic/anaerobic integrated safe biological marsh gas desulfurizer.    Nutrient solution input pipe (6)    Nutrient solution input cylinder (7)    Microporous spray head (13)    Disc sprayer (14)    Shower pipe (16)    Peristaltic pump (17)    Nutrient solution output cylinder (21)    Overflow pipe (22)    Nutrient solution output pipe (23)    Water inlet tank (25)
NOVELTY - Method for producing organic fertilizer using processed sludge, involves adding pulverizing crop stalk, peanut shell and rice shell as auxiliary materials, adding SZ atomic-powered bacterium to the obtained mixture, agitating obtained materials, placing agitated mixture into fermenting pool, fermenting obtained mixture, taking obtained mixture out, stacking obtained mixture in air, turning stacked mixture, controlling fermentation process within 25-35 days, obtaining granules from the fermented mixture and drying the obtained granules at 70-80 degrees C.    USE - The method is useful for producing organic fertilizer.    ADVANTAGE - The method is inexpensive.    DETAILED DESCRIPTION - Method for producing organic fertilizer using processed sludge, involves using human excrement and dewatered sludge as base material, adding pulverized crop stalk, peanut shell and rice shell as auxiliary materials, adding SZ atomic-powered bacterium, agitating the obtained materials, placing the agitated mixture into a fermenting pool, fermenting the obtained mixture for 7-10 days, taking the obtained mixture out, stacking the obtained mixture in air, turning the stacked mixture once every 7-10 days for 2-3 times, controlling the fermentation process within 25-35 days, obtaining granules from the obtained mixture and drying the obtained granules at 70-80 degrees C.
NOVELTY - Agent comprises (in parts): Bacillus subtilis (35-85), photosynthetic bacteria (5-15), actinomycete (5-15), matrine (5) and fermentation bacteria (5). The agent is prepared by pumping the materials into agitating pot using a pump, mixing and agitating the materials at room temperature for 30 minutes, precipitating the mixture, filtering the mixture, bottling the filtrate and packaging the product.    USE - The agent is useful for coating rice seed (claimed).    ADVANTAGE - The agent is environmentally-friendly, promotes early seed germination and produces cold-tolerant seeds.
NOVELTY - Herbal nutritive fertilizer of fructus forysthiae comprises (in g): dried cow dung (15000), dried pig manure (15000), dried dung (15000), dried feces (15000), broomcorn (15000), cornflour (15000), wheat straw powder (15000), peanut flour cake (25000), rice flour (25000), bran flour (25000), nitrogenous fertilizer (25000), manganese fertilizer (25000), methamidophos (10000), ammonium bicarbonate (1000), calcium fertilizer (1000), dipterex (1000), carbendazim (500), glucose powder (1000) and epoxy resin (3000).    USE - Herbal nutritive fertilizer of fructus forysthiae.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fertilizer which is obtained by obtaining the above-mentioned powder materials, adding the materials into a stirrer for 100 minutes, crushing the mixture in a crusher to obtain particles of 80 meshes, adding the crushed powder into a stirrer, stirring the mixture for 160 minutes, obtaining the stirred mixture, adding the mixture into a fermenting pond in a ratio of 1:1.5, stirring the mixture uniformly, adding the stirred mixture into a human feces water, piling the mixture, compacting the mixture using plastic cloth, fermenting the mixture for 28 hours, turning the pile for first time, again adding the mixture into human feces water, stirring the upper and lower portion uniformly, piling the mixture, compacting the mixture using plastic cloth, fermenting the mixture for 48 hours, turning the pile for second time, fermenting the piled mixture for 72 hours, and adding the fermented fertilizer in mould having 35 cm high, 25 cm wide and 45 cm long to otbain product.
NOVELTY - Composite microbial bactericide comprises Bacillus stearothermophilus, Streptomyces hygroscopicus, and coridus versicolor, where content of each bactericide is adjusted according to the component of processed pig manure.    USE - The composite microbe bactericide is used for processing pig manure compost or for preparing microbial organic fertilizer (claimed). It is useful for processing and integrally utilizing pig manure in pig farm of different sizes.    ADVANTAGE - The composite bactericide achieves quick fermentation and heating speed; provides high maintaining temperature for compost and short fermentation period; promotes the pig manure to become thoroughly decomposed; preserves the effective component of the compost; and can solve environmental pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for application of composite microbial bactericide in harmless treatment, reduction, and resource aspects of pig manure comprising respectively culturing and fermenting 3 bactericides to prepare composite bactericide or single bactericide, where when composite bactericide is used, pig manure and saw powder are mixed at 6:1 dry weight ratio, 0.5% B. stearothermophilus, 0.5% S. hygroscopicus, and 0.3% coridus versicolor are respectively added, uniformly agitated, regularly turned over to ventilate, and then B. stearothermophilus, S. hygroscopicus, and coridus versicolor are fermented in aerobic environment at high temperature after 25-30 days to reach the purposes of reduction, harmless treatment, and reclamation.
NOVELTY - An organic fertilizer comprises (pts.wt.) amino acid (10-50), brown coal (10-35), organic fertilizer (20-70), soil bactericide (0.01-6), disinfectant (0.1-8), and plant growth regulator (1-10).    USE - Organic fertilizer used for sterilizing soil of sheltered ground (claimed) or for application to vegetable fields, particularly vegetable fields with relatively long production period, or for reducing disease infestation of crops or enhancing disease resistance of crops.    ADVANTAGE - The fertilizer can provide all nutrient components and increase vegetable yield in sheltered ground by more than 15% and reduce pesticide amount by 50%.
NOVELTY - Use of Asarum extract, is claimed for preventing and/or controlling agricultural mite. The Asarum extract is obtained by drying Asarum, pulverizing the dried Asarum, sieving the pulverized powder, adding 95% ethanol to the sieved powder, extracting the mixture, stirring and filtering the extract to obtain solution, adding 95% ethanol to the residue and extracting for two times, reducing the pressure and condensing the extract to obtain black brown pasty Asarum extract.    USE - The Asarum extract is useful for preventing and/or controlling agricultural mite.    ADVANTAGE - The Asarum extract is highly efficient and environmentally-friendly and has low residue.    DETAILED DESCRIPTION - Use of Asarum extract, is claimed for preventing and/or controlling agricultural mite. The Asarum extract is obtained by cleaning Asarum, drying the cleaned Asarum in shade place, pulverizing the dried Asarum by plant crusher, sieving the pulverized powder with 40 meshes sieve, adding 95% ethanol (2-10 times) to the sieved powder, maintaining the mixture at room temperature, extracting the mixture for 1-7 days, stirring and filtering the extract to obtain solution, adding 95% ethanol (2-10 times) to the residue and extracting for two times, reducing the pressure by rotary evaporator and condensing the extract to obtain black brown pasty Asarum extract.
NOVELTY - Fixing Pseudoalteromonas sp.SP48 using a polyurethane foam, where the Pseudoalteromonas sp.SP48 is preserved in China Center for Type Culture Collection on August 3rd, 2010, comprises: pelletizing the polyurethane foam, boiling and drying and sterilizing an algicidal bacteria culture medium; processing Pseudoalteromonas sp.SP48 using shake culture, where the Pseudoalteromonas sp.SP48 enters or attaches on the inner wall of the polyurethane foam for growing to form the polyurethane foam containing Pseudoalteromonas sp.SP48.    USE - The polyurethane foam fixed Pseudoalteromonas sp.SP48 is useful for red tide treatment.    ADVANTAGE - The method: utilizes convenient and cheap polyurethane foam with a good density and size, strong absorbing ability, non toxic, and mass and energy transferring effect to adsorb immobilized Pseudoalteromonas sp.SP48 and hence improves the applicability in real red tide treatment; and is economical.    DETAILED DESCRIPTION - Fixing Pseudoalteromonas sp.SP48 using polyurethane foam, where the Pseudoalteromonas sp.SP48 is preserved in China Center for Type Culture Collection on August 3rd, 2010 with a preservation number CCTCC NO:M2010194, comprises: pelletizing the polyurethane foam, boiling and drying and sterilizing an algicidal bacteria culture medium; processing the Pseudoalteromonas sp.SP48 using shake culture, where the Pseudoalteromonas sp.SP48 enters or attaches on the inner wall of the polyurethane foam for growing to form the polyurethane foam containing Pseudoalteromonas sp.SP48.
NOVELTY - Preventing and treating plant soil-borne disease comprises: (i) before sowing the crop or transplanting seedlings, applying an organic fertilizer in the soil, (ii) inoculating the beneficial micro-organisms to the base fertilizer, and (iii) sowing crop seeds or transplanting the crop seedling, after sowing, cultivating the micro-organisms in shade and constant-temperature optimal living environment to degrade the organic matter in the fertilizer and propagating, forming a micro-organism film on the surface of plant root skin to degrade the special organic matter secreted by root of the plant.    USE - The method is useful for preventing and treating plant soil-borne disease.    ADVANTAGE - The method does not use pesticides; and utilizes an agricultural product with low residual toxicity and good quality.    DETAILED DESCRIPTION - Preventing and treating plant soil-borne disease comprises: (i) before sowing the crop or transplanting the seedling, applying an organic fertilizer to the soil as a base fertilizer, (ii) inoculating beneficial micro-organisms to the base fertilizer, and (iii) sowing crop seeds or transplanting the crop seedling, after sowing, cultivating the micro-organisms in shade and, minimum and constant-temperature optimal living environment to degrade the organic matter in the fertilizer and propagating rapidly, after the seeds sprout or the seedlings survive, forming a propagated beneficial micro-organism film on the surface of the plant root skin, where the micro-organism film degrades the special organic matter secreted by the root of the plant during the degradation of the organic matter in the fertilizer.
NOVELTY - The power device has conductive wire (4) that is connected with wind power generator (2) and electrolysis water hydrogen maker (5). A hydrogen gas conveying pipe (6) is connected with hydrogen maker and workshop (7). A hydrogen fuel conveying pipe (9) is connected with hydrogen fuel storage container (8) and hydrogen fuel battery (10). The conductive wire is connected with fuel battery and electric motor (11). A power output shaft (12) is connected with electric motor and mechanical transmission device (13) connected with related mechanical components.    USE - Power device of wind hydrogen source for paddy planter.    ADVANTAGE - The electric energy can be efficiently released in the hydrogen fuel battery by the electrochemical reaction.    DESCRIPTION OF DRAWING(S) - The drawing shows a -perspective view of the power device of wind hydrogen source for paddy planter.    Wind power generator (2)    Conductive wire (4)    Electrolysis water hydrogen maker (5)    Hydrogen gas conveying pipe (6)    Workshop (7)    Hydrogen fuel storage container (8)    Hydrogen fuel conveying pipe (9)    Hydrogen fuel battery (10)    Electric motor (11)    Power output shaft (12)    Mechanical transmission device (13)
NOVELTY - Microemulsion comprises (in wt.%): chlorantraniliprole (0.1-45), natural pyrethrin (0.2-30), emulsifying agent (4-26), penetrating agent (2-10), stabilizing agent (2-8), cosolvent (3-16) and deionized water (24-68).    USE - The microemulsion is useful for preventing and controlling beet armyworm and cabbage caterpillar.    ADVANTAGE - The microemulsion does not require use of toxic solvent e.g. dimethylbenzene, thus it is safe to environment, humans, livestock and other beneficial living beings, and does not easily cause phytotoxicity.    DETAILED DESCRIPTION - Microemulsion comprises (in wt.%): chlorantraniliprole (0.1-45), natural pyrethrin (0.2-30), emulsifying agent (4-26), penetrating agent (2-10), stabilizing agent (2-8), cosolvent (3-16) and deionized water (24-68), where the emulsifying agent is chosen from nonylphenol polyoxyethylene ether, sodium dodecyl benzene sulfonate, phenol polyoxyethylene ether and polyoxyethylene, the penetrating agent is chosen from dioctyl sodium succinate, sodium octyl phosphate and organosilicon, the stabilizing agent is chosen from disodium hydrogen phosphate, phenylephrine alcohol and allyl epihydric alcohol, and the cosolvent is chosen from isoamyl alcohol, ethylene glycol, ethyl acetate and isopropanol. An INDEPENDENT CLAIM is included for preparation of the above-cited microemulsion, which involves adding the chlorantraniliprole, natural pyrethrin, emulsifying agent, penetrating agent, stabilizing agent and cosolvent in high-speed shearing machine, uniformly mixing, adding deionized water and mixing, heating at 43-60 degrees C for 4-10 hours and completely mixing the ingredients.
NOVELTY - Composition comprises (in parts weight) gallnut (30-40), Rheum officinale (30-40) and salt (20-40).    USE - The composition is useful for preventing and treating fish bubble disease and promoting growth of fishes.    ADVANTAGE - The composition is environmentally-friendly and economical and improves survival rate of fishes.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the above-mentioned composition, which involves soaking the gallnut and R.officinale in water for 20-30 minutes, extracting the soaked materials twice by existing method with slow fire for 30-40 minutes, filtering the extract, combining the filtrates, concentrating the filtrate until the relative density of the product is 1.05-1.20 under 40-50 degrees C, cooling the concentrated product to room temperature, and adding and dissolving salt to the product, where the weight ratio of gallnut, R.officinale and salt is 1:10:12.
NOVELTY - Purifying butane using chemical separation process by integrally connecting a distilling tower with a phase separation device, a hydrogenation reactor and an extraction distilling tower with pipeline, is claimed.    USE - The method is useful for purifying butane using chemical separation process.    ADVANTAGE - The method is simple and environmental friendly, and provides high purity product.
NOVELTY - High speed organic wastewater and waste substance treatment system using biotechnology, which utilizes microorganisms Saccharomyces, Actinomyces, a photosynthetic bacteria and a nitrogen-fixing bacteria to decompose the organic and inorganic substance in the waste water, which are from poultry manure and detergent for cleaning the manure and manure device, e.g. a liquid detergent and a disinfectant, discharges the pollution-free substance, reduces the discharge amount and changes the product into a fertilizer, which can be recycled to agriculture, is claimed.    USE - The system is useful for treating organic wastewater and waste substance.    ADVANTAGE - The system: is convenient to operate and maintain; occupies less space and reduces the area by 50-70% in comparison with the conventional system; eliminates pollution source; discharges the pollution-free substance; and reduces the discharge amount and converts the manure sewage into the organic fertilizer up to 100% which can be recycled for further use, and thus is economical.
NOVELTY - Method of preparing cefotiam hexetil hydrochloride, involves (1) reacting cefotiam with carbonate to obtain cefotiam salt, (2) esterifying the obtained cefotiam salt with cyclohexyl 1-iodoethyl carbonate, (3) adding mixed solvent to the mixture, extracting mixture, adding hydrochloric acid to the obtained layer containing organic compounds to obtain layer containing hydrochloric acid, and (4) freeze-drying the layer containing hydrochloric acid to obtain the cefotiam hexetil hydrochloride.    USE - The method is useful for preparing cefotiam hexetil hydrochloride which is used in medicine in the form of tablet, capsule or granule (both claimed).    ADVANTAGE - The method is simple and environmentally-friendly, and prepares cefotiam hexetil hydrochloride with high purity and good yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for medicine, which comprises the cefotiam hexetil hydrochloride.
NOVELTY - An organic photoresist stripper composition contains nitrogen-containing compound (A) (I), ether-type compound (B) (II), compound (C) chosen from sugar, 3-10C alkane, cyclohexane, hydroxyl compound, aromatic hydroxyl compound, acetylene alcohol, carboxylic acid compound, carboxylic acid anhydride and triazole compound, and organic solvent (E).    USE - Organic photoresist stripper composition is used for manufacturing flat panel display and semiconductor device.    ADVANTAGE - The flat panel display using organic photoresist stripper composition has excellent corrosion resistance.    DETAILED DESCRIPTION - An organic photoresist stripper composition contains nitrogen-containing compound (A) of formula: (N(-R1)(-R2))n-R3-(R4-OH)m (I), ether-type compound (B) of formula: N(-X)(-Y')-O-R9 (II), compound (D) chosen from sugar, 3-10C alkane, cyclohexane, hydroxyl compound, aromatic hydroxyl compound, acetylene alcohol, carboxylic acid compound, carboxylic acid anhydride and triazole compound, and organic solvent (E).    R1,R2=H, amino or optionally substituted linear or branched 1-10C hydrocarbyl;    R3=bond or linear, branched or cyclic 1-10C hydrocarbyl;    R4=linear, branched or cyclic 1-10C hydrocarbyl;    n,m=1-5;    R5,R6=H, 1-5C hydrocarbyl or linear or branched aromatic hydrocarbyl;    X, Y=H; linear, branched or cyclic 1-7C hydrocarbyl; or    X+Y=ring.
NOVELTY - Organic nutritive medium is prepared by mixing, stacking and fermenting raw materials including manual sludge from urban sewage treatment plants, sawdust and zymophyte in the weight ratio of 40-60:40-60:0.2-0.5.    USE - The organic nutritive medium is useful for roof greening.    ADVANTAGE - The medium is inexpensive and has rich beneficial microorganisms and nutrients and high venting capability, and retains water and fertilizer.
NOVELTY - An undiluted solution including food, food supernatant and/or livestock excretions is ionized, and hexane is produced. Then, dissolved oxygen is added to the solution, ionized and hexane is produced. Further, pH of the resulting solution is adjusted, to obtain fuel. The obtained fuel is electrolyzed and mixed with hydrogen-mixed gas, to obtain hydrogen-mixed fuel gas.    USE - Manufacture of hydrogen-mixed fuel gas.    ADVANTAGE - The hydrogen-mixed fuel gas is manufactured efficiently and economically.
NOVELTY - Preparing pollution-free pesticide for vegetables comprises dissolving white sugar in water, adding 95% of alcohol to the sugar solution, uniformly stirring and adding peracetic acid and uniformly stirring.    USE - The pesticide is useful for preventing bacterial diseases of the vegetable crops, for killing the tiny injurious insects e.g. aphid.    ADVANTAGE - The pesticide is harmless to man and animals.
NOVELTY - Method for producing organic fertilizer, involves (1) milling garden waste and preheating the milled product, (2) adding nutrient liquid to heated product to obtain fermentation substrate, disinfecting the fermentation substrate, (3) spraying lignin and cellulose degrading bacteria culture liquid into the fermenting substrate, (4) fermenting and culturing the obtained product, and radiating the fermented product using low-frequency alternating magnetic field, and (5) composting the obtained product, and disinfecting the composite to obtain the finished product.    USE - The method is useful for preparing organic fertilizer useful for promoting growth of plant.    ADVANTAGE - The fertilizer is environmentally-friendly as it uses garden waste, has high economical value and can be produced simply.    DETAILED DESCRIPTION - Method for producing organic fertilizer, involves (1) milling garden waste and preheating the milled product at 50-80 degrees C, (2) adding 10-25 vol.% of nutrient liquid to heated product to obtain fermentation substrate, disinfecting the fermentation substrate at 120-122 degrees C for 8-25 minutes under wet condition, (3) spraying lignin and cellulose degrading bacteria culture liquid into the fermenting substrate in the volume ratio of 10:1, where the concentration of the bacterial colony in the nutrient liquid is 1x 107- 9x 108 colony-forming unit (cfu)/ml, (4) fermenting and culturing the obtained product for 24-26 hours, radiating the fermented product for 20 minutes using low-frequency alternating magnetic field for 4-6 days, and (5) composting the obtained product for 1-3 days, and disinfecting the composite to obtain the finished product.
NOVELTY - Aqueous phenol is injected at bottom of evaporation furnace as evaporating agent under centrifugal sputtering of using high-speed centrifuge.    USE - Recycling of aqueous phenol for preparation of biomass fuel.    ADVANTAGE - The aqueous phenol is economical recycled with reduced consumption of energy by simple process without polluting the environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus.
NOVELTY - Perovskite catalyst (I), is new.    USE - The catalyst (I) is useful for producing hydrogen from ethanol by autothermal reforming.    ADVANTAGE - The catalyst (I): is resistant to sintering, carbon deposition and oxidation and thus exhibits high activity, in comparison with the conventional catalyst, which gets inactivated due to oxidation and sintering of active component; does not change its structure, during the autothermal reforming process; has reduced acidity, due to the presence of the adjuvant, which is iron or manganese or chromium; and remarkably increases the hydrogen gas yield. The method improves the: reducibility and stability of the active component of the catalyst and the oxygen defect and lattice structure defect of the surface of the perovskite catalyst.    DETAILED DESCRIPTION - Perovskite catalyst of formula (LaaSrbNicXdO3) (I) is new.    X = Fe, Mn or Cr;    a = 0.7-1;    b = 0-0.3;    c = 0.7-0.95; and    d = 0.05-0.3.    INDEPENDENT CLAIMS are also included for:    (1) the preparation of (I); and    (2) use of the catalyst for producing hydrogen from ethanol by autothermal reforming, comprising reducing 50-200 mg of catalyst in hydrogen/nitrogen mixed gas for 4 hours at 650 degrees C, blowing nitrogen gas, filling mixed gas of ethanol, water and oxygen in a molar ratio of 1:1-4:0.4-1 at a speed of 50-200 ml/min, and carrying out autothermal reforming reaction by the catalyst bed at 400-700 degrees C.
NOVELTY - A method of fuel gas production with Hydrogen and water molecule mixed. Including the method of cycle and temperature controlled by infrared ceramics and catalyst of aluminum metal to product the fuel gas for water flowing through the hydrogen and water molecule.
NOVELTY - A wettable phosmet powder comprises (pts.wt.) raw phosmet material (31-71), sodium dinaphthylmethane sulfonate (2-4), sodium dodecylbenzene sulfonate (2-4), sodium butyl naphthalene sulfonate (1-3), fatty alcohol-polyoxyethylene ether (0.5-1.5), light calcium carbonate (7-46), and polyoxyethylene polyoxypropylene styrylphenyl ether (5-6). The wettable powder further comprises 4-10 pts.wt. silica.    USE - Wettable phosmet powder.    ADVANTAGE - The powder has reduced production cost, contains no organic solvent, is environmentally-friendly and easy to be wet, and produces fine uniform sprayed mist with strong adhesion, good wettability, and high suspension rate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of wettable phosmet powder, comprising:    (A) sieving wettable phosmet powder, removing mechanical impurities and other solid impurities, then crushing, and transferring crushed material to a primary mixing kettle;    (B) adding sodium dinaphthylmethane sulfonate, sodium dodecylbenzene sulfonate, sodium butyl naphthalene sulfonate, fatty alcohol-polyoxyethylene ether, silica, and light calcium carbonate to the primary mixing kettle and stirring, then slowly adding polyoxyethylene polyoxypropylene styrylphenyl ether, and continuously mixing for 1 hour;    (C) after mixing, sending material to ultrafine current crusher and crushing to obtain crushed material having grain size of greater than or equal to 450 mesh; and    (D) transferring the material to a secondary mixer and mixing for 30 minutes, then detecting quality, and packing.
NOVELTY - A water dissociation system comprises a substance which can react with water to generate hydrogen with water; nucleus radioactivity or solar energy for improving ionizing level of the product in the water; a dissociator to separate the two ions; and a discharging electrode to remove electric charges of anion and cation. The discharging electrode comprises a heated metal plate, conductor, or semiconductor.    USE - A water dissociation system used for providing energy in vehicles, ships, dynamos, or gas furnaces (claimed).
NOVELTY - A biological sludge organic-inorganic fertilizer is produced by mixing and prilling dehydrated sludge and auxiliary materials to make sludge granules with 60-65% of initial water content; transmitting the sludge granules to a spreader to uniformly spread the sludge granules in a biological-drying bin to obtain biologically dried piled sludge materials; ventilating the piled materials from bottom to top to dry the materials; and mixing the biologically dried sludge materials with inorganic fertilizers, providing nutrition, prilling, and drying to prepare the fertilizer.    USE - Method of producing biological sludge organic-inorganic fertilizer (claimed).    ADVANTAGE - The method has low energy-consumption and low running cost. The biologically dried sludge can be used as auxiliary materials in normally running stage to reduce dependence to exogenous additives. The biologically dried material has loose structure and is good for ventilation and biochemical reaction, in which the biochemical reaction is shorter than 1/3 of manure fermentation time.
NOVELTY - Method for preparing heat-producing fermented material, involves obtaining organic substance as fermentation substrate and spraying fermentation liquid to the fermentation substrate to obtain heat-producing fermented material.    USE - The method is useful for preparing heat-producing fermented material which is used for breeding tobacco seedling.    ADVANTAGE - The fermented material reduces seedling period and increases the temperature of tobacco seedling. The method is cost-effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for heat-producing fermented material, which is obtained by the above-mentioned method.
NOVELTY - Method consists in supply of fuel to diesel generator and conversion of fuel combustion energy to mechanical energy, and then to electric energy. Water gas is used as fuel, which is obtained from tight retorts as a result of pyrolysis of hydrocarbon raw material. Raw material is loaded to tight retorts, and then retorts are heated, and pyrolysis process is performed. Raw material is dried at the first stage in each retort at 150 degrees . . . 220 degrees C till water is completely removed. Resins, acids and alcohol is separated at the second stage by heating each retort to 350 degrees . . . 440 degrees C. At the third stage the retort is heated to 850 degrees . . . 1000 degrees C; at that, superheated steam or air is supplied in turn to the retort. Water gas is removed from the retort, cooled to temperature of not more than 50 degrees C, stored in gas holder, compressed, mixed with air and supplied as fuel to pre-started diesel generator warmed up to normal working temperature. Remained solid fractions of raw materials is removed from the retort and the process is repeated again.    USE - Electricity.    ADVANTAGE - Non-waste production of electric energy from waste wood. 5 cl, 1 dwg
NOVELTY - Method for processing paint booth circulating water, involves adding microorganism capable of degrading organic substance in coating material and capable of producing biosurfactant to the paint booth circulating water.    USE - The method is useful for processing paint booth circulating water.    ADVANTAGE - The method processes solvent-type coating material present in paint booth without using flocculants and maintains biological oxygen demand (BOD) and chemical oxygen demand (COD) in fixed value in the processed water.
NOVELTY - The method involves absorbing and accumulating organic chlorine pesticide from polluted soil by ageratum. The ageratum is repeatedly planted by seedling or transplantation. The ageratum naturally grows in dry land. Plants are removed at fixed time. The ageratum is planted in a cycle manner with purpose of not continuously extracting the organic chlorine pesticide until content of the organic chlorine pesticide in soil accords with safety standard. Weeds are removed before plantation or seeding of the ageratum.    USE - Method for recovering soil polluted by organic chlorine pesticide with ageratum.    ADVANTAGE - The method enables recovering the soil polluted by organic chlorine pesticide with ageratum at low cost in simple manner. The method enables recycling the resources, reducing carbon, realizing environmental friendliness and achieving social, economical and ecological benefits.    DESCRIPTION OF DRAWING(S) - The drawing shows a tabular column illustrating a method for recovering soil polluted by organic chlorine pesticide with ageratum. '(Drawing includes non-English language text)'
NOVELTY - Removal of phenol in a wastewater comprises adding dirhamnolipid and laccase to the wastewater; adjusting pH value of wastewater to 4-7; controlling liquid at 25-50 degrees C; strongly stirring the mixed wastewater for more than 15 minutes, and standing; passing the liquid through a filter film with 0.45 mu m; and removing phenol in the wastewater.    USE - Method for removing phenol in a wastewater (claimed).    ADVANTAGE - The method is simple and inexpensive.
NOVELTY - A non-jammed bio-trickling filter comprises a water inlet tube (1), a water distributor (2), a filler module (3), a supporting bracket (4) of the filler module, and a drainage system (5). The water inlet tube and the water distributor are mounted on an upper portion of the filter. The water is uniformly distributed in the filler module. The drainage system is arranged on a bottom portion for collecting, refluxing, and draining processed water.    USE - A non-jammed bio-trickling filter used for sewage.    ADVANTAGE - The filter increases contact area between a biological film on a surface of a filler layer and a sewage, increases mass transfer efficiency of a pollutant from the sewage to the biological film, has a simplified structure, and is inexpensive.    DESCRIPTION OF DRAWING(S) - The drawing is a sectional view of the non-jammed bio-trickling filter.    Water inlet tube (1)    Water distributor (2)    Filler module (3)    Supporting bracket (4)    Drainage system (5)
NOVELTY - Use of Gynura bicolor, is claimed for treating livestock and poultry breeding wastewater, where the G.bicolor is grown in livestock and poultry breeding wastewater.    USE - The G.bicolor is useful for treating livestock and poultry breeding wastewater.    ADVANTAGE - The G.bicolor is inexpensive and causes no secondary pollution.
NOVELTY - Hydroisomerization process, comprises: contacting a hydrocarbonaceous feed stream containing 4-6C paraffins with a catalyst under hydroisomerization conditions in the presence of hydrogen, where the catalyst comprises an aluminosilicate zeolite comprising CON- and TUN-type aluminosilicate zeolites and at least one Group VIII metal.    USE - The process is useful for isomerizing light paraffins to produce higher octane gasoline fuels, which is useful in modern automobile engines.    ADVANTAGE - The process provides high selectivity for producing high octane isomers of light paraffins. The catalysts are highly active, environmentally benign, and readily regenerable.
NOVELTY - A raw material is contacted with hydrotalcite as catalyst, and oxygen is removed by decarboxylation or decarbonylation to obtain hydrocarbon. The raw material is triglyceride, fatty acid and/or fatty acid derivative obtained from renewable source derived from biological organism.    USE - Manufacture of hydrocarbon used for gasoline or diesel.    ADVANTAGE - The method economically provides hydrocarbon with reduced consumption of energy.
NOVELTY - A household waste is treated by crushing and fermenting waste under normal temperature and pressure; performing sieving process which comprises gravity separation, magnetic separation and manual separation; crushing oversize with medium and large size of crude sieving or inorganic material with large particle to prepare urban coal material; and crushing stone brick in oversize of crude and medium sieving to prepare roadbed material or pavement brick base material.    USE - Household waste treatment for preparing organic composite fertilizer product (claimed).    ADVANTAGE - The method has low construction investment, low operational cost, simple operation, excellent effect in treating, and high degree of resources recycling.    DETAILED DESCRIPTION - Household waste treatment comprises:    (A) crushing and fermenting waste under normal temperature and pressure;    (B) performing sieving process which comprises gravity separation, magnetic separation and manual separation, the gravity separation comprising rough sieving, medium sieving and refined sieving to obtain oversize and siftage of crude sieving, medium sieving and refined sieving and organic material, inorganic material, magnetic materials and organic leavening;    (C) crushing oversize with medium and large size of crude sieving or inorganic material with large particle to prepare urban coal material; and crushing stone brick in oversize of crude and medium sieving to prepare roadbed material or pavement brick base material;    (D) preparing fertilizer with organic material or organic leavening in oversize and siftage in medium and refined sieving;    (E) directly selling sieved magnetic materials with recovery value; and collecting magnetic materials without recovery value for harmless treatment; and    (F) directly selling manually sieved goods with recovery value.
NOVELTY - Microbial organic fertilizer preparation involves mixing (in pts.wt.): composting soil (70-100), rice bran (30-35), bean pulp (10-20), bone meal (5-10) and fish meal (5-8), and then pilling materials at 15-35 degrees C for 5-8 days.    USE - Microbial organic fertilizer.    ADVANTAGE - The microbial organic fertilizer is prepared by simple process.
NOVELTY - Organic fertilizer from municipal sludge is prepared by mixing municipal sludge containing 66-74% water and biological fermenting agent at weight ratio of 1000:5; mixing with sheep manure and wheat bran; putting mixture into a fermentation pool and fermenting naturally while pouring till the temperature of the fermentation product is 1450-1700 degrees C.    USE - Method of preparing organic fertilizer from municipal sludge (claimed) for use on soil and newly deforested land.    ADVANTAGE - The method can obtain organic fertilizer at a reduced cost. The organic fertilizer effectively improves nutrient release efficiency in the sludge, prolongs nutrient release period, improves actual efficiency of the sludge, improves the soil structure effectively, and speeds up soil maturing effect with respect to newly deforested land.
NOVELTY - Bacterial strain has preservation number CCTCC NO: M2010053. The bacterial strain is cultured on nutrient agar medium. The bacterial strain is Gram-positive and oval. The nutrient agar medium has carbon source selected from glycerol, L-arabinose, ribose, D-xylose, dextrose, fructose, mannose, mannitol, sorbierite, alpha -methyl-D-glucoside, amygdalin, esculin, salicin, cellobiose, maltose, lactose, melibiase, canesugar, trehalose, raffinose, starch or glucogen. The GenBank number of the bacterial strain is HM372880.    USE - Bacterial strain for degrading zearalenone toxin in grain selected from corn, wheat, barley, rice, broomcorn and millet (claimed).    ADVANTAGE - The bacterial strain enables to degrade zearalenone toxin in a safe, cost-effective and eco-friendly manner.
NOVELTY - Manufacturing biodiesel involves cleaning waste vegetable oil using 98% sulfuric acid solution (0.2-2 wt.%); esterifying the waste vegetable oil by a mixture of metoxide and methanol; extracting to obtain the upper layer then washing with warm water, sequentially heating for dehydration then filtering to separate two solid phases and biodiesel using a vacuum extractor to obtain biodiesel; mixing the obtained biodiesel with multifunctional amide additive (0.1-1 wt.% or at concentration of 2%), obtained from peanut oil and diethylenetriamine to give finished biodiesel.    USE - For manufacturing biodiesel.
NOVELTY - A bio-oil is prepared by direct catalytic liquefaction process of algae biomass, which is a hydrothermal process with algae biomass as raw material. It comprises pre-processing, catalytic liquefaction and separation. Pre-processing comprises soaking the dried and crushed algae in 0.05-0.15 mol/L of alkali solution or acid solution for greater than or equal to 20 hours, feeding the soaking solution and modified natural mordenite catalyst in pressure kettle, catalytically liquefying, and cooling and decompressing before separating solid from liquid.    USE - Method for preparing bio-oil (claimed).    ADVANTAGE - The method has over 82% of algae liquefaction rate. Oil production is high in quality, and heat value is over 30 MJ/kg. The method uses water phase system, which is energy-saving, environment-friendly, simple to operate, low in preparation cost, mild in reaction condition, easy to realize scale production, and good in market application prospect.    DETAILED DESCRIPTION - Preparing bio-oil comprises direct catalytic liquefaction process of algae biomass, which is a hydrothermal process with algae biomass as raw material. It comprises pre-processing, catalytic liquefaction and separation. Pre-processing comprises soaking the dried and crushed algae in 0.05-0.15 mol/L of alkali solution or acid solution for greater than or equal to 20 hours, in which a mass ratio of material to solution is 1:10-30; feeding the soaking solution and modified natural mordenite catalyst in pressure kettle, catalytically liquefying for greater than or equal to 0.5 hour while stirring with anaerobic and hydrogen atmosphere at 200-400 degrees C and 3-16 MPa, in which a mass ratio of the algae raw material to catalyst is 1:0.02-0.05; and cooling and decompressing before separating solid from liquid, decompressing and dewatering the liquid, and obtaining the bio-oil.
NOVELTY - Continuous drying and utilizing printing and dyeing sludge, comprises (i) introducing the printing and dyeing sludge into a filter by a sludge pump and dehydrating; (ii) conveying the obtained sludge into a spiral feeder by a conveyor belt, feeding into a vertical spiral drying tower by a rotary feeder and drying; (iii) introducing the obtained dried sludge into a cyclone separator for separating gas and solid, de-dusting, desulfurizing, sterilizing and conveying into a chimney to exhaust; and (iv) mixing solid dried sludge with coal to obtain a mixture, which taken as fuel.    USE - The method is useful for continuously drying and utilizing printing and dyeing sludge.    ADVANTAGE - The method: reduces the hazard of the untreated sludge on the environment; produces the sludge having a combustion heat value of 1500-2000 kcal/kg; and reduces coal consumption and cost by mixing the sludge with coal.    DETAILED DESCRIPTION - Continuous drying and utilizing printing and dyeing sludge, comprises (i) introducing the printing and dyeing sludge having a moisture content of 92-99% into a filter by a sludge pump and dehydrating until the moisture content is 80-85%; (ii) conveying the obtained sludge into a spiral feeder by a conveyor belt, feeding into a vertical spiral drying tower by a rotary feeder and drying until the sludge has a moisture content of 10-30%; (iii) introducing the obtained dried sludge into a cyclone separator for separating gas and solid, in which the solid is guided into a hopper at the bottom of the cyclone separator and introducing the gas and dust into a water film de-duster to remove dust and gas, after being de-dusted, desulfurizing, sterilizing and conveying into a chimney by a draught fan to exhaust based on the standard; and (iv) mixing 10-20% solid dried sludge collected by the hopper with coal to obtain a mixture, which is taken as fuel.
NOVELTY - Method of preparing organic fertilizer, involves mixing animal manure, crop straw, and fermenting bacterium.    USE - The method is useful for preparing organic fertilizer.
NOVELTY - Microbial seed coating formulation comprises Bacillus subtilis (40-90), photosynthetic bacterium (5-15), fungus (5) and film forming agent. The microbial seed coating formulation involves adding the above-cited material into agitation tank under normal temperature, filtering the obtained product, encapsulating the filtrate into bottle and packing the bottles in a box.    USE - The microbial seed coating formulation is useful for preventing bacterial infection in corn plant.    ADVANTAGE - The coating formulation is environmentally-friendly, enables early seedling formation in corn, and produces seedling having strong drought resistance and low temperature resistance.
NOVELTY - Highly clean fuel comprises (in wt.%) methanol etherifying liquor (8-12), aromatic hydrocarbon (35-40), 4-5C olefin (20-30) and of 4-5C alkane (20-30).    USE - Used as a highly clean fuel.    ADVANTAGE - The high clean fuel: solves the problem of comprehensive use of 4C and 5C fraction and coarse aromatic hydrocarbon of the factory; is simple to produce with stable quality; is economical; has good inflammability, high octane number and good antiknock performance, which avoids the air pollution caused by adding tetraethyl lead; is a novel alternative fuel; reduces the carbureted hydrogen, carbonic oxide and nitric oxide in the automobile exhaust; maintains the cleanness of the engine fuel system without carbon deposition and mechanical wearing in order to prolong the service life of automobile; has high atomization degree and the gas mixture is fully burnt in order to maximize the power; enables the automobile to be easily started, with stable rotation speed and good acceleration performance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the highly clean fuel, comprising introducing the methanol etherifying liquor, aromatic hydrocarbon, 4-5C olefin and 4-5C alkane into a homogenizer for homogenization.
NOVELTY - Deacidifying biodiesel comprises mixing biodiesel and a deacidification agent including water-soluble alcohol, water-soluble amine, and water; separating oil phase and water phase after layering; and refining the oil phase to obtain biodiesel with qualified acid value.    USE - Method for deacidifying biodiesel (claimed).    ADVANTAGE - The method conveniently removes organic acid in biodiesel, reduces the acid value, and reuses or recycles organic acid and glycerol.
NOVELTY - A catalyst comprising at least one composite metal selected from composite metal of platinum and nickel; and composite metal of iridium and nickel, is new.    USE - In decomposition reaction of at least one compound selected from hydrazine or their hydrate; and for generating hydrogen and supplying to fuel cell (claimed) for automobiles and portable fuel cells.    ADVANTAGE - The method which utilizes the decomposition reaction of hydrazine, efficiently generates hydrogen with improved selectivity. The hydrogen gas is efficiently generated under controllable conditions without heating to a high temperature; and is produced at low cost because the catalyst exhibits high activity even when it contains a low proportion of platinum or iridium.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) generating (M1) hydrogen involving contacting the catalyst with at least one compound selected from hydrazine or its hydrate; and    (2) supplying hydrogen to a fuel cell involving supplying hydrogen generated by the method (M1) as a hydrogen source to a fuel cell.
NOVELTY - At least one type of zirconium salt, scandium salt and/or cerium salt are mixed with distilled water. A precipitating agent is added to the mixed solution and precipitated. The precipitate is filtered from the solution, and precipitate is vacuum freeze-dried to obtain cerium-doped scandium stabilized zirconia.    USE - Manufacture of nano cerium-doped scandium stabilized zirconia powder for electrolyte used for manufacturing solid oxide fuel cell (claimed) .    ADVANTAGE - The nano cerium-doped scandium stabilized zirconia powder is easily manufactured. The solid oxide fuel cell is economically manufactured with high productivity. The interface resistance between fuel anode and cathode is suppressed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of solid oxide fuel cell.
NOVELTY - Pelletized pellet of straw, wood or plastic of any origin and size comprises sodium percarbonate or disodium monohydrogen phosphate, which is added in an adjusted amount during pellet production.    USE - The pellet is useful as a litter in a fattening system for poultry farming.    ADVANTAGE - The pellet: prevents emission of ammonia to the atmosphere either by destroying resulting ammonia chemically and bacteria, which produces ammonia, or by influencing ammonia and the soil substrate environment chemically in such a manner that a weak acid environment is coupled with a chemically safe binding of the resulting ammonia, where a low ammonium substrate or an ammonium salt is respectively obtained at the end of the stabling period, and the substrate or the salt is respectively suitable for biogas production or as a fertilizer; and has simple production.
NOVELTY - Microorganism KSM strain showing 98% or more homology in base sequence of 16S rRNA gene, belonging to alpha-proteobacteria, and having decomposition ability in deoxynivalenol and nivalenol, is new.    USE - The microorganism KSM strain is useful for preparing agent for decomposing deoxynivalenol and/or nivalenol (claimed).    ADVANTAGE - The microorganism KSM strain is stable with heat.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a method for decomposing deoxynivalenol and/or nivalenol comprising using the microorganisms; and    (2) agent for decomposing deoxynivalenol and/or nivalenol comprising microorganisms.
NOVELTY - A protein capable of degrading deoxynivalenol enzyme, comprising (a) a 261 amino acid sequence (SEQ ID NO: 2) fully defined in the specification, (b) amino acid sequence of SEQ ID NO: 2 in which one or more amino acid residues are deleted, substituted or added, and (c) amino acid sequence exhibiting at least 80% sequence homology to SEQ ID NO: 2, is new.    USE - The protein is useful for degrading deoxynivalenol enzyme (claimed) for preventing diseases caused by red mold, preferably Fusarium graminearum in plant, and improving human health.    ADVANTAGE - The protein is stable in heat, and decomposes deoxynivalenol which is hard to decompose.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) gene encoding the above-cited protein, and comprising (i) a 786 base pair sequence (SEQ ID NO: 1) fully defined in the specification, (ii) base pair sequence of SEQ ID NO: 1 in which one or more base pairs are deleted, substituted or added, and (iii) base pair sequence capable of hybridizing with SEQ ID NO: 1 under stringent conditions;    (2) recombinant vector comprising the above-cited gene;    (3) transformant comprising the above-cited gene or vector; and    (4) method for decomposing deoxynivalenol, involves using the transformant.
NOVELTY - Deoxynivalenol degradation enzyme protein comprising any of: (a) amino acid sequence comprising fully defined 426 amino acids (SEQ ID NO. 2) given in the specification; (b) amino acid sequence comprising SEQ ID NO. 2 having one or more amino acids that are deleted, substituted or added, and having deoxynivalenol decomposition activity; and (c) amino acid sequence having at least 90% or more homology with SEQ ID NO. 2 and having deoxynivalenol decomposition activity, is new.    USE - The protein or gene is useful for decomposing deoxynivalenol (claimed).    ADVANTAGE - The deoxynivalenol degradation enzyme protein is stable with heat.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a deoxynivalenol degradation enzyme gene encoding the amino acid sequence in any of (a)-(c) above; or a deoxynivalenol degradation enzyme gene comprising any of: (a) base sequence comprising fully defined 1281 bp (SEQ ID NO. 1) given in the specification; (b) base sequence comprising SEQ ID NO. 2 having one or more bases that are deleted, substituted or added, and encoding protein having deoxynivalenol decomposition activity; and (c) base sequence encoding protein which hybridizes under stringent conditions with base sequence of SEQ ID NO. 1, and has deoxynivalenol decomposition activity;    (2) a recombinant vector comprising the gene;    (3) a transformant comprising the gene or the recombinant vector; and    (4) a method for decomposing deoxynivalenol comprising using the transformant.
NOVELTY - Generating a gas comprising hydrogen or oxygen via an electrolysis reaction comprises: placing an anode and a cathode in aqueous solution, where at least a portion of the aqueous solution adjacent the anode comprises water, cobalt cation and fluoride anion; and driving an electrolysis reaction from the anode and cathode using an external source of electricity, thus generating the gas.    USE - The method is useful for generating a gas comprising hydrogen or oxygen via an electrolysis reaction (claimed), where the hydrogen gas is useful as an alternative fuel source for a vehicle or other device and the oxygen gas is useful for numerous other known purposes e.g. enhancing oxygen content in room air in buildings.    ADVANTAGE - The method: can be conducted in a large scale production facility, via a residential size generation system; utilizes the catalysts/anodes which function efficiently (with comparatively low overpotentials), without requiring highly basic reaction conditions, even at ambient room conditions, and are stable under the highly oxidizing conditions; utilizes the cobalt and fluoride which are available in relatively high quantities at low cost; and provides a more practical way of storing renewable energy.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) the anode suitable for generating oxygen in the electrolysis reaction, comprising a substrate, and a catalytic coating positioned on the substrate that comprises cobalt, oxygen and fluorine, with the catalytic coating comprising two oxygens for each cobalt represent in the catalytic coating; and    (2) forming the anode comprising: positioning the substrate in the aqueous solution comprising cobalt cation and fluoride anion; and conducting the electrolysis reaction using the substrate as an anode in that reaction.
NOVELTY - The reactor has fluidized bed gasifier for gasifying raw material, into which flow medium is introduced. The flow medium and char generated at the time of gasification, are introduced into fluidized bed combustion furnace. The reheated flow medium is circulated through inside of reactor main portion while burning unburnt matter. An L-shaped valve is provided in communicating path of furnace. The adjustment of particle circulating load in furnace is performed by changing nozzle location for aeration of L-shaped valve.    USE - Circulating fluidized bed gasification reactor for exploitation of unused hydrocarbon resources such as biomass, garbage and sewage sludge.    ADVANTAGE - The particle circulating load can be increased or decreased easily. The operation of reactor can be stabilized by simple process. The mixing of flow medium with ash particle can be prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of circulating fluidized bed gasification reactor. (Drawing includes non-English language text)
NOVELTY - Liquid manure comprises organic nitrogen and inorganic nitrogen, which are extracted from soil or organic fertilizer.    USE - The liquid manure is useful for stimulating plant growth (claimed), and suppressing acidification of soil.    ADVANTAGE - The fertilizer provides healthy plant growth even at initial stage of plant, and is environmentally-friendly as it reduces fertilizer usage.
NOVELTY - An aggregate layer consisting of catalyst particles and water repellent material is formed on an electrode base material. An electrode catalyst layer is formed on the electrode base material by performing freezing and drying process and baking process. The freezing and drying process is performed in the state of covering aggregate layer with paper or non-woven fabric with water absorption characteristic and applying load by mounting weight such as aluminum plate on the paper or non-woven fabric.    USE - Gas diffusion electrode manufacturing method for fuel cell.    ADVANTAGE - The generation of crack in the electrode catalyst layer due to volatilization of solution in the aggregate layer and the peeling of electrode catalyst layer from the electrode base material due to floating produced by expansion during the freezing of solution in the aggregate layer are prevented effectively at the time of performing freezing and drying process.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating the gas diffusion electrode manufacturing process.(Drawing includes non-English language text)
NOVELTY - Synthesizing nanoscale particles of molybdenum disulfide involves: mixing molybdenum ethylhexanoate (0.0001-0.1 M), 2-ethylhexanoic acid (0.0001-0.1 M) and lithium sulfide (0.0001-0.1 M), dispersed in at least one organic solvent, in an oxygen and moisture free environment with stirring.    USE - For synthesizing nanoscale particles of molybdenum disulfide (claimed) as single layer transition metal sulfide catalysts (SLTMS) for upgrading heavy petroleum feedstocks and removing sulfur, nitrogen and other pollutants from fuels; for heavy feed upgrading, in-situ catalysis, bio-fuel conversion and coal liquefaction.    ADVANTAGE - The method does not use stabilizing surfactants for synthesizing the nanoscale particles; produces SLTMS catalysts, such as molybdenum disulfide, with potentially greater activity and specificity than those currently available; enables synthesis of primarily SLTMS, such as nanoscale molybdenum disulfide; and uses low cost industrially available precursors, and is readily scalable.
NOVELTY - Device comprises airtight container, and a hollow drum-shaped rotary shaft, which rotates freely and is vertically arranged in the container. Multiple stirring blades are also provided which are extended horizontally from the rotating shaft. An air feeding unit is provided for feeding air to the container, and a vent is provided for passing the air in the container.    USE - Device for fermenting and drying organic waste.    ADVANTAGE - The device enables to ferment and dry organic waste in a simple and cost-effective manner.
NOVELTY - A biomass fuel compact comprises either: a body comprising a combustible biomass composition, and an adhesive additive comprising a starch, and a hydroxide; or a combustible biomass composition, and an adhesive additive comprising at least one of a starch and a hydroxide.    USE - As biomass fuel compact (claimed).    ADVANTAGE - The present composite biomass fuel compact is durable, reduces the amount of dust normally associated with known biomass compositions, that is lower cost, higher efficiency, and reduces and/or improves regulated or unregulated emissions. The innovative adhesive tends to not only bind the composite biomass, but also to form a continuous shell around the exterior of the compact, providing for a highly durable composite biomass fuel compact.
NOVELTY - A solar reclamation device of organic waste resource, comprises a heating water tank, a solar heater, a constant temperature hot water supply tank, and a reaction tank for containing organic waste; where the reaction tank has interlaid tank wall; a snake-shaped water pipe is arranged in the interlayer; the water outlet of the snake-shaped water pipe of the reaction tank is connected to the constant temperature hot water supply tank through an electromagnetic valve; and the water outlet is connected to the heating water tank through the water pipe and the electromagnetic valve.    USE - The solar reclamation device is useful for organic waste resource (claimed).    ADVANTAGE - The solar reclamation device has production process that is more economical and environment-friendly. Moreover, the production cost is reduced.    DETAILED DESCRIPTION - A solar reclamation device of organic waste resource, comprises a heating water tank, a solar heater, a constant temperature hot water supply tank, and a reaction tank for containing organic waste; where the reaction tank has interlaid tank wall; a snake-shaped water pipe is arranged in the interlayer; the water outlet of the snake-shaped water pipe of the reaction tank is connected to the constant temperature hot water supply tank through an electromagnetic valve; the water outlet is connected to the heating water tank through the water pipe and the electromagnetic valve; and the heating water tank is connected to the solar water heater through a water pump.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the solar reclamation device of organic waste resource (Drawing includes non-English language text).
NOVELTY - The device has a gas purification system comprising a venturi dust catcher (12), a cyclone separator (13), a water film dust catcher (14) and a static capturer (20). A feeding system comprises a falling pipe (7) and a lifting material distributor (3). A gas voltage stabilizing system comprises an anti-explosion water seal (21), an empty chimney (22) and a storage cabinet (23). Ash leaking holes are formed on a gear ash leaking disk (4), where the ash leaking holes are uniformly round with diameter of 25-50 mm. An automatic igniting device is arranged above the empty chimney.    USE - Biomass gasification generating device for a fixed bed.    ADVANTAGE - The device delivers clean gas in a low-rotating speed inner combustion engine through a fan so as to generate power in an efficient manner. The gasification furnace and the purification device realize anti-explosion protection by water seal. The device is safe and reliable. The device has stable structure, convenient feeding effect, stable parameter and wide range of application, and effectively processes multiple biomasses.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass gasification generating device.    Lifting material distributor (3)    Gear ash leaking disk (4)    Falling pipe (7)    Venturi dust catcher (12)    Cyclone separator (13)    Water film dust catcher (14)    Static capturer (20)    Anti-explosion water seal (21)    Empty chimney (22)    Storage cabinet (23)
NOVELTY - The artificially-constructed wet land has concrete constructing basin (1) in which lateral wall is arranged with water inlet (2), while its other lateral wall is arranged with water outlet (3). A gravel layer (4) is filled in the concrete constructing basin. The vegetable layer (5) is arranged on the top part of the gravel layer.    USE - Artificially-constructed wet land for use in purifying the sewage.    ADVANTAGE - Provides reasonable structure in purifying the sewage.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of the artificially-constructed wet land.    Concrete constructing basin (1)    Water inlet (2)    Water outlet (3)    Gravel layer (4)    Vegetable layer (5)
NOVELTY - A process involves: passing a feedstock comprising a triglyceride optionally containing a co-feed gas through a metal apparatus, where the temperature in the metal apparatus is 150-550 degrees C, the pressure in the metal apparatus is 50-2000 psig, the residence time for the feedstock in the metal apparatus is 0.001-5 hours, and the gas co-feed rate is 100-10000 standard cubic feet/barrel (scf/b).    USE - For converting triglycerides to fuel range hydrocarbons, particularly diesel boiling range hydrocarbons (claimed), such as gasoline, and naphtha, where triglycerides include vegetable oils including soybean and corn oil, peanut oil, sunflower seed oil, coconut oil, poppy seed oil, almond oil, hazelnut oil, walnut oil, olive oil, avocado oil, tall oil, cottonseed oil, palm oil, rice bran oil, canola oil, and linseed oil; and animal fats such as tallow animal fat, beef fat, and milk fat.    ADVANTAGE - The process produces hydrocarbons from triglycerides such as vegetable oils or fats, with reduced potential corrosion. The process avoids metallurgy upgrading, thus provides a significant contribution to the art and to the economy.
NOVELTY - Purifying sewage of vertical subsurface flow constructed wetland comprises pre-processing raw sewage to reduce chemical oxygen demand (COD) to less than 300 mg/L and inorganic suspended substance (SS) to less than 20 mg/L and leading liquid supernatant to a constructed wetland. The constructed wetland comprises a foundation pit, an enclosure, a water distributing pipe network, a water collecting pipe network, a filler layer composed of a water permeable matrix and having proper structure, a microbe colony adhered on the filler layer, and a vegetation.    USE - Method for purifying sewage of vertical subsurface flow constructed wetland.    ADVANTAGE - The method has low construction cost and good water treatment effect.    DETAILED DESCRIPTION - Purifying sewage of vertical subsurface flow constructed wetland comprises pre-processing raw sewage to reduce COD to less than 300 mg/L and inorganic suspended substance (SS) to less than 20 mg/L and leading liquid supernatant to a constructed wetland. The constructed wetland comprises a foundation pit, an enclosure, a water distributing pipe network, a water collecting pipe network, a filler layer composed of a water permeable matrix and having proper structure, a microbe colony adhered on the filler layer, and a vegetation. Bottom of the foundation pit and enclosure are reinforced and treated in permeability. The water distributing pipe network is composed of a master pipeline and a branch pipeline connected with the master pipeline vertically; where the master pipeline is 1/3-1/2 constructed wetland in length and the diameter is determined by the water amount. A water outlet having 45 degrees with the horizontal direction is processed at both lower sides of each branch pipelines. The water outlet is 10-20 mm in diameter and a distance between the outlets is 5-10 cm.
NOVELTY - An anaerobic solid reactor comprises a reacting tank body (3) having a middle part in column shape, an upper part in tapered platform shape, and a lower part in reversed tapered platform shape. A methane exhausting device and a draining device are arranged on the upper of the reacting tank body. A phase separating device (6), a steady flow device (7), a gas gathering shell breaking device (4), a reflowing agitating device and a water inlet device are arranged in the reacting tank body. A mud discharging device (10) is arranged on the lower part of the reacting tank body.    USE - Anaerobic solid reactor used for producing methane with high consistency solid organic as raw material, processing high solid and high consistency organic wastewater, and recovering energy, particularly waste liquid from beer vat, and waste liquid from livestock and poultry breeding.    ADVANTAGE - The reactor prevents the problem that the mud is hard to mix, that mud can be stopped in short time, and methane exhausting is influenced via the shell formed on the mud layer at the surface.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic perspective view of the anaerobic solid reactor.    Reacting tank body (3)    Gas gathering shell breaking device (4)    Phase separating device (6)    Steady flow device (7)    Mud discharging device (10)
NOVELTY - Purifying a gas stream comprising at least one first compound containing compounds of the first group formed by e.g. water, ammonia, aromatics, hydrocarbons of alkane, alkene or alkyne comprising at least 5C, and at least one second and a third compound containing compounds of the second group formed by e.g. helium, hydrogen, hydrocarbons below C5 comprises using at least one main adsorber comprising at least one contactor having parallel passages, by variable-pressure swing adsorption (PSA), where the first compound is at least partially arrested at the upstream of the main adsorber.    USE - The process is useful for purifying gas stream.    DETAILED DESCRIPTION - Purifying a gas stream comprising at least one first compound containing compounds of the first group formed by water, ammonia, aromatics, hydrocarbons of alkane, alkene or alkyne comprising at least 5C, aldehydes, ketones, halogenated hydrocarbons, hydrogen sulfide, hydrogen chloride and at least one second and a third compound containing compounds of the second group formed by helium, hydrogen, nitrogen, oxygen, argon, carbon monoxide, carbon dioxide, hydrocarbons below C5 comprises using at least one main adsorber comprising at least one contactor having parallel passages, by variable PSA, where the first compound is at least partially arrested at the upstream of the main adsorber.
NOVELTY - Removing high organic pollutant in garbage seeping liquid comprises using Fenton's reagent, adding accelerating agent for generating the synergistic effect; quickening the oxidation reaction at 12-35 degrees C for 1-4 hours, where the pH is controlled at 3-5, the molar ratio of hydrogen peroxide and iron ion is 2.8-4.6:1, and the adding mode is step by step, and the pH is regulated to 4.8-6 after oxidation reaction; and adding the flocculating agent for flocculating and precipitating.    USE - Method for removing high organic pollutant in garbage seeping liquid (claimed).    ADVANTAGE - The method has high efficiency, energy conservation, emission reduction, widely using range for water quality and exhaustive degradation of the organic pollutant in garbage seeping liquid; can process the garbage seeping liquid at lower temperature; reduces the dosage of the chemical oxidation medicine; and reduces environment pollution.
NOVELTY - A system comprises a water distributing system, a tide flow artificial wetland nitrifying system, a horizontal underflow artificial wetland denitrifying system, and a time program controller. Wetland plants of bed bodies of the tide flow artificial wetland nitrifying system and the horizontal underflow artificial wetland denitrifying system comprises Canna, reed, and cattail.    USE - A system for processing sewage on a tide flow and horizontal underflow combined wetland (claimed).    ADVANTAGE - The system is inexpensive, and has good denitrifying effect.
NOVELTY - The system (10) has a pre-heater (30) that includes coils (35a,35b) installed at ends of exterior wall, and high temperature filter (36) installed at the exit. A reservoir (21) stores undiluted solution of glycerol generated in biodiesel production process and dilutes glycerol in treated water storage tank (22). The mass flow controllers (25a) control emission quantity of glycerol from the tank. A runback portion (70) comprises cross beams (42a,42b) for steady discharge of glycerol, and transfers processing water separated by vapor-liquid separation to the tank.    USE - System for producing high concentration hydrogen.    ADVANTAGE - High concentration hydrogen can be produced efficiently at low cost and utilization rate of the glycerol can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing high concentration hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the high concentration hydrogen production system.    High concentration hydrogen production system (10)    Reservoir (21)    Treated water storage tank (22)    Mass flow controllers (25a)    Pre-heater (30)    Coils (35a,35b)    High temperature filter (36)    Cross beams (42a,42b)    Runback portion (70)
NOVELTY - Palm byproduct is dissolved in organic solvent and the solid material is filter-removed. Water in the dissolved product is further removed and the impurities are removed by centrifugation. Bio-bunker C oil is added to the purified palm byproduct to obtain environmentally-friendly bio-bunker C oil with low sulfur content.    USE - Manufacture of environmentally-friendly bio-bunker C oil with low sulfur content.
NOVELTY - Catalyst obtained by immersing on bentonite by potassium nitrate, is claimed. The ratio of the potassium nitrate and the bentonite is 1:1 (volume/mass), and the grain size is 150-250 microns.    USE - The catalyst is useful for preparing biodiesel from drainage oil.    ADVANTAGE - The catalyst is environmental friendly and can be conveniently separated from product.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the catalyst, comprising mixing potassium nitrate and bentonite, with the ratio of 1:1 (volume/mass) and evenly agitating, conveying the mixture into a dry oven and regulating the temperature until it reaches to 115 degrees C, drying for 5 hours and removing, grinding the catalyst particles and screening to have partials with grain size of 150-250 microns and conveying into a muffle furnace, roasting at 600 degrees C for 6 hours and cooling naturally to obtain the catalyst.
NOVELTY - Preparing prinivil via membrane separation technique, comprises extracting hydrolyzate from immiscible organic solvent to obtain aqueous extract of feed liquid comprising prinivil, and utilizing it as raw material, desalting and concentrating the feed liquid comprising prinivil via nanofiltration membrane, distilling at reduced pressure to obtain the concentrated solution, cooling, and crystallizing, where the hydrolyzate is obtained from prinivil ester and alkaline solution, and the feed liquid comprises prinivil, sodium chloride and sodium trifluoroacetate.    USE - The method is useful for preparing prinivil.    ADVANTAGE - The method: has low production cost, low energy consumption and advanced process route; is simple and safe to operate; generates low waste; has reliable production; has high desalting rate; and has socio-economic benefit.
NOVELTY - Preparing biomass briquette, comprises uniformly mixing biomass, poor quality anthracite powder and an additive, and pressing at low pressure in a wet manner to obtain the briquette. The additive comprises sulfur-fixing agent, biomass adhesive, oxidant and waterproof agent.    USE - The method is useful for preparing biomass briquette.    ADVANTAGE - The biomass briquette exhibits low cost, low ignition point, high burn-off rate, less energy consumption and environmental friendly and desulfurization and hydrophobic functions.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biomass briquette prepared by the above method.
NOVELTY - Preparing biodiesel by continuous rectification of oleic acid and low-boiling-point substance, comprises (i) mixing the low-boiling-point substance with methanol according to rationed proportion; (ii) continuously carrying high-temperature and high-pressure esterification; (iii) distilling by scrapper thin film; (iv) distilling short molecules to eliminate residues; and (v) continuously alkali refining and deacidification.    USE - The method is useful for preparing biodiesel.    ADVANTAGE - The method: produces biodiesel that is renewable and environment friendly; and has a low carbon economy.
NOVELTY - Marsh gas is prepared by pre-treating and mixing alligator Alternanthera; adding crushed straw to treated alligator Alternanthera at a ratio of 1:1-5 while controlling carbon and nitrogen ratio at 20-30:1 (preferably 3-11:1); subjecting the mixture to a fermenting device; inoculating a mixed inoculum material (10-30%); sealing the fermenting device; connecting with a gas storage device; fermenting while stirring at 25-35 degrees C for 20-50 days where marsh generation occurs for 1-2 days.    USE - Method of preparing marsh gas (claimed).    ADVANTAGE - The method is simple, environment-friendly and convenient, reduces the risk of the alien plant alligator Alternanthera, and solves insufficient anaerobic fermented raw material.
NOVELTY - Urban household garbage as corruptible organic substance is placed in the fermenting groove with mechanical stirring device. Negative pressure ventilation is implemented for fermenting groove, and material is stirred for 25-40 days to form aerobically treated material. The material is decomposed, screened and slit to remove plastic, sands and glass to produce organic fertilizer. Thus, urban household garbage is treated.    USE - Method for treating urban household garbage.    ADVANTAGE - The urban household garbage is efficiently and economically treated without affecting the environment.
NOVELTY - Extracting aucubin from aucubaceae comprises: crushing the raw materials, adding ethanol, extracting and combining the extracts; decompressing the extract and recovering the ethanol, adding water to dissolve, filtering the insoluble product, adding a macroporous absorption resin column and rinsing the active ingredient; filtering the rinsed solution, adding a nano-filtering film and condensing; and adding ethyl acetate, adding anhydrous sodium sulfate, condensing, crystallizing, filtering the crystal product, rinsing with chloroform and petroleum ether and vacuum drying at low temperature.    USE - The method is useful for extracting aucubin from aucubaceae.    ADVANTAGE - The method: is simple; consumes less energy; easily controls the temperature during the production; exhibits high extraction efficiency; prepares the product with high content; and is suitable for industrial production.    DETAILED DESCRIPTION - Extracting aucubin from aucubaceae comprises: (a) crushing the raw materials to 20-80 mesh, adding 80-95% ethanol (5-15 times) to extract for 1-2 hours and extracting for 2-3 times and combining the extracts; (b) decompressing the extract and recovering the ethanol, adding water to dissolve, filtering the insoluble product, adding a macroporous absorption resin column to absorb and rinsing until the sugar reaction is negative, using 50-70% ethanol solution (4-7 bed volume) to rinse the active ingredient and collecting the rinsed solution; (c) filtering the rinsed solution with a ultra-filtering film and adding a nano-filtering film to condense and obtain the condensed solution; and (d) adding ethyl acetate to extract for 3-6 times, recovering the ethyl acetate to 1 divide by 6-1 divide by 10 of the original volume, adding anhydrous sodium sulfate, condensing and crystallizing, filtering the crystal product, rinsing for 3-5 times with chloroform and petroleum ether and vacuum drying at low temperature to obtain the product.
NOVELTY - Preparing locust glycosides (acaciin, linarin)comprises: providing Robinia pseudoacacia leaves, grinding and adding to a carbon dioxide supercritical extractor for supercritical extraction, extracting for 80-200 minutes to obtain a extract, adding the extract to a polyamide column chromatography and eluting by an eluent, which is ethanol-pyridine solvent, detecting by the polyamide film and eluent, collecting flow parts, where retention factor is 4-4.5 on the polyamide film, recovering the solvent, concentrating, adding water-pyridine solvent for crystallization, washing and drying.    USE - The method is useful for preparing locust glycosides (acaciin, linarin).    ADVANTAGE - The method: is simple, environmental-friendly and suitable for large scale production; consumes less energy; and prepares highly pure product.    DETAILED DESCRIPTION - Preparing locust glycosides (acaciin, linarin) comprises: providing Robinia pseudoacacia leaves, grinding and adding to a carbon dioxide supercritical extractor for supercritical extraction, where ethanol is used as an entrainer (2-8% of the total extraction solvent), extracting under pressure 10-30 MPa at 40-55 degrees C for 80-200 minutes at the carbon dioxide flow of 1-4 ml/g of crude drug per minute to obtain a extract, adding the extract to a polyamide column chromatography and eluting by an eluent, which is ethanol-pyridine solvent in the ratio of 8:1, detecting by the polyamide film and eluent, collecting flow parts, where retention factor is 4-4.5 on the polyamide film, recovering the solvent, concentrating, adding water-pyridine solvent in the ratio of 1:1 for crystallization, washing and drying.
NOVELTY - The hydrogen generator has reaction bath (10) that accommodates magnesium ball (2) and spring catalyst (4). A hydrogen exhaust port (20) of reaction bath, discharges the hydrogen generated in reaction bath. An exhaust pipe (40) connected to bottom reaction bath, discharges magnesium hydroxide sludge from the reaction bath. An implantation unit (30) includes injection nozzle (36) for injecting electrolyte into the reaction bath.    USE - Hydrogen generator.    ADVANTAGE - The hydrogen generation efficiency can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen generator. (Drawing includes non-English language text)    Magnesium ball (2)    Spring catalyst (4)    Reaction bath (10)    Hydrogen exhaust port (20)    Implantation unit (30)    Injection nozzle (36)    Exhaust pipe (40)
NOVELTY - Biomass nanometer gasoline liquid fuel comprises (in wt.%): biomass alcohol (20-94), gasoline (0-50) and combustion-supporting additive (6-35).    USE - Biomass nanometer gasoline liquid fuel used for gasoline motor vehicle (claimed).    ADVANTAGE - The biomass nanometer gasoline liquid fuel has complete combustion without poison and smoke or polluting the environment.
NOVELTY - Biomass liquid fuel comprises (in wt.%): biomass alcohol (40-90), wastewater (0-25) and additive (5-35).    USE - Biomass liquid fuel used in cooking or boiler of hotel, restaurant and canteen (claimed).    ADVANTAGE - The biomass liquid fuel is cost-effective and eco-friendly, and has improved combustion property.
NOVELTY - Biomass fuel combustion-supporting additive comprises (in wt.%): biomass alcohol (40-75), n-octane (5-40), cosolvent (3-15), combustion-supporting catalyst (0.5-3.5) and emulsifying agent (0.5-2.5).    USE - Biomass fuel combustion-supporting additive.    ADVANTAGE - The biomass fuel combustion-supporting additive is cost-effective, safe in use, clean and eco-friendly, and enables to improve the combustion efficiency of fuel and save the fuel.
NOVELTY - A biodiesel is prepared from waste oil material with high acid value by drying the collected waste oil material, adding methanol and concentrated sulfuric acid, pre-esterifying the mixture, adding continuously methanol and solid acid catalyst, esterifying, setting aside, adding potassium hydroxide and methanol, mixing, subjecting to a piston flow reactor for transesterification, centrifuging, filtering, and distilling obtained filtrate.    USE - Method of preparing biodiesel from waste oil material with high acid value.    ADVANTAGE - The method utilizes waste thus reducing pollutants.    DETAILED DESCRIPTION - A biodiesel is prepared from waste oil material with high acid value by:    (A) drying the collected waste oil material until the water content is lower than 0.1%, adding methanol and concentrated sulfuric acid (0.08-1.2 mass%), and pre-esterifying the mixture at 45-65 degrees C for 0.4-0.6 hours;    (B) adding continuously methanol (3-7 mass% of pre-esterified product) and solid acid catalyst to the pre-esterified product, esterifying at 90-100 degrees C for 0.25-1.25 hours, and setting aside for 45-60 minutes;    (C) adding (%) potassium hydroxide (0.6-1.4) and methanol (13-17) to the esterified product, mixing, and subjecting to a piston flow reactor controlled at 35-95 degrees C at a ratio of 5 tons/hour for transesterification; and    (D) centrifuging, filtering, and distilling obtained filtrate.    The mass ratio of methanol and dehydrated waste oil material is 6.7-20.3%.
NOVELTY - Biodiesel comprises (in wt.%): methanol (25-43), diesel oil (18-30), oleic acid (15-26), cosolvent (15-21) and surfactant (5-10).    USE - As biodiesel.    ADVANTAGE - The biodiesel is environmentally-friendly. The biodiesel has high flash point. The diesel oil replacing rate is high. The biodiesel can be obtained simply, can be stored for long period of time and can be used with any diesel oil.
NOVELTY - An alcohol mixed liquid fuel comprises trinitrotoluene and liquid organic alcohol.    USE - Alcohol mixed liquid fuel.    ADVANTAGE - The alcohol mixed liquid fuel is economical and has excellent stability and combustibility.
NOVELTY - Blended gasoline additive comprises (in parts weight): gasoline (35), ethanol (30), sorbitantristearate (Bspen S-802), triethanolamine (2), ethanediamine (1), sodium oleate (2), wool grease (2), ammonia water (3), T18041, tertiary butanol (0.5), benzoic acid (0.2), methyl tertiary butyl ether (8) and triethanolamine (15). The blended gasoline additive is prepared by adding above-mentioned composition in kettle and stirring the obtained product.    USE - Blended gasoline additive.    ADVANTAGE - The additive is energy-saving and reduces mechanical friction.
NOVELTY - An organic photoresist stripper composition contains nitrogen-containing compound (A) (I), ether-type compound (B) (II), compound (C) chosen from sugar, 3-10C alkane, cyclohexane, hydroxyl compound, aromatic hydroxyl compound, acetylene alcohol, carboxylic acid compound, carboxylic acid anhydride and triazole compound, and organic solvent (D).    USE - Organic photoresist stripper composition is used for manufacturing flat panel display and semiconductor device.    ADVANTAGE - The flat panel display using organic photoresist stripper composition has excellent corrosion resistance.    DETAILED DESCRIPTION - An organic photoresist stripper composition contains nitrogen-containing compound (A) of formula: (N(-R1)(-R2))n-R3-(R4-OH)m (I), ether-type compound (B) of formula: R8-O-R7-CO-N(-R5)-R6-OH (II), compound (C) chosen from sugar, 3-10C alkane, cyclohexane, hydroxyl compound, aromatic hydroxyl compound, acetylene alcohol, carboxylic acid compound, carboxylic acid anhydride and triazole compound, and organic solvent (D).    R1,R2=H, amino or optionally substituted linear or branched 1-10C hydrocarbyl;    R3=bond or linear, branched or cyclic 1-10C hydrocarbyl;    R4=linear, branched or cyclic 1-10C hydrocarbyl;    n,m=1-5;    R5,R6=H, 1-5C hydrocarbyl or linear or branched aromatic hydrocarbyl;and    R7,R8=linear, branched or cyclic 1-5C hydrocarbyl.
NOVELTY - 6-Aminopenicillanic acid, hydrobromic acid and sodium nitrite, are reacted to obtain 6-bromo-3,3-dimethyl-7-oxo-4-thia-1-azabicyclo(3.2.0)heptane-2-carboxylic acid which is reacted with hydrogen peroxide, to obtain (4R)-6-bromo-4-hydroxy-3,3-dimethyl-7-oxo-1-azabicyclo(3.2.0)heptane-2-carboxylic acid. The obtained compound is polycondensed with benzophenone to obtain benzhydryl 6-bromo-3,3-dimethyl-4,7-dioxo-1-azabicyclo(3.2.0)heptane-2-carboxylate which is reacted with ammonium chloride, to obtain benzhydryl 3,3-dimethyl-4,7-dioxo-1-azabicyclo(3.2.0)heptane-2-carboxylate.    USE - Preparation of benzhydryl 3,3-dimethyl-4,7-dioxo-1-azabicyclo(3.2.0)heptane-2-carboxylate.    ADVANTAGE - The method economically provides high yield (90%) of benzhydryl 3,3-dimethyl-4,7-dioxo-1-azabicyclo(3.2.0)heptane-2-carboxylate, by a simple and environmentally-friendly process, without using a high-pressure device.    DETAILED DESCRIPTION - 6-Aminopenicillanic acid (APA), hydrobromic acid and sodium nitrite, are reacted (step A) to obtain 6-bromo-3,3-dimethyl-7-oxo-4-thia-1-azabicyclo(3.2.0)heptane-2-carboxylic acid (B) which is then reacted with hydrogen peroxide (step B) in presence of molybdenum acetylacetonate, to obtain (4R)-6-bromo-4-hydroxy-3,3-dimethyl-7-oxo-1-azabicyclo(3.2.0)heptane-2-carboxylic acid (C). The obtained compound is polycondensed (step C) with benzophenone in presence of dicyclohexylcarbodiimide (DCC) and dimethylaminopyridine (DMAP), to obtain benzhydryl 6-bromo-3,3-dimethyl-4,7-dioxo-1-azabicyclo(3.2.0)heptane-2-carboxylate (D) which is reacted with ammonium chloride or ammonium acetate in presence of zinc powder (step D), to obtain benzhydryl 3,3-dimethyl-4,7-dioxo-1-azabicyclo(3.2.0)heptane-2-carboxylate (A).
NOVELTY - The device has a carrier pump that is installed with two fermentors (120,130). A gas collection tub (150) collects the biogas generated in the lower portion of secondary fermentor through the piping structure that is connected with the primary fermentor. A desulfurizer (300) is mounted on rear end of the gas collection tub for removing sulfur compound.    USE - Device for manufacturing biogas fuel.    ADVANTAGE - The gas collection tub collects the biogas generated in the secondary fermentor through the piping structure that is connected with the primary fermentor. Thus the pipe structure utterly and efficiently transfers the fermented solution to the primary fermentor, and the desulfurizer removes the sulfur compound during the fermentation while improving the fermentation efficiency and productivity.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for manufacturing biogas fuel. (Drawing includes non-English language text)    Livestock excretion reservoir (110)    Fermentors (120,130)    Gas collection tub (150)    Desulfurizer (300)
NOVELTY - Aeration treatment of organic wastewater (9) is carried out in an aerator (2) with an activated sludge by biological treatment. A container having sealing structure filled with electron donor substance, a nonporous film and a support which supports microorganism and provided around nonporous film, is arranged. The electron donor substance is sustain-released from nonporous film portion of container and supplied to support. The support is contacted with organic wastewater in aerator, and denitrification of organic wastewater is carried out. Thus, organic wastewater is processed.    USE - Processing of organic wastewater.    ADVANTAGE - The organic wastewater is efficiently and economically processed and nitrogen component concentration in organic wastewater is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for processing plant (1a) of organic wastewater.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of processing plant of organic wastewater. (Drawing includes non-English language text)    Processing plant of organic wastewater (1a)    Aerator (2)    Sedimentation tank (3)    Organic wastewater (9)    Denitrifying module (11)
NOVELTY - Preparing soil additives by biological fermentation (3), comprises adding organic biomass prior to the fermentation of a liquid coal slurry.    USE - The soil additive is useful for improving the cation exchange capacity and the nutrient- and water-holding capacity of soil.    ADVANTAGE - The method: produces the coal material under aqueous conditions, and the obtained coal material exhibits good miscibility, good flowability and small particle size, and is easily mixed with the water-containing biomass, and directly used as the soil additive or supplied for the fermentation without adding other organic biomass or without additional mixing steps, and thus eliminates costly drying steps, crushing, screening and dry-mixing steps; reduces concentration of metals and toxic materials in the soil additive compared to an input material; and allows quantitative determination of air conditioning effect and associated carbon dioxide.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for carrying out the above mentioned method.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the sewage slurry from a storage container fed in to a reactor for hydrothermal carbonization.    Fermentation (3)
NOVELTY - The sewage eliminating device has a timing device which is connected with an inflating device and used for controlling a timed starting of the inflating device and a pipeline extended into the fluid sewage slot by the inflating device. An air scattering disc is disposed at the tail end of the pipeline. The air scattering holes are disposed on the air scattering disc.    USE - Sewage eliminating device for liquid sewage slot disposed at lateral end of liquid sewage slot.    ADVANTAGE - Controls the timed starting of the inflating device through the timing device. Fluids in the liquid sewage slot are stirred to avoid blocking. Decomposers are matched and thrown into the fluids to break down the sewages in the liquid sewage slot. Effectively improves water quality of the sewage slot and sanitation in the surrounded condition and saves cost and manpower resource.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the sewage eliminating device for liquid sewage slot disposed at lateral end of liquid sewage slot.
NOVELTY - The air temperature-controlled straw carbonization furnace has internal air exhaust cooling device comprises metal air exhaust cooling tube (8), internal air exhaust cooling bend (11) and internal air exhaust cooling double pipe (6) connected in turns. The internal air exhaust cooling double pipe is fixed by the reduced bushing (4). The lower end of air cap (10) is connected to second external air inlet pipe bend (12). The metal air exhaust cooling tube is arranged in the air cap in which upper part is formed with a vent hole (9).    USE - Air temperature-controlled straw carbonization furnace.    ADVANTAGE - Distributes air entering the external air inlet tube, and makes the carbon layer in the straw carbonization furnace move down uniformly. Ensures favorable gas-solid contact and operation at high limited temperature. Improves gasification efficiency and carbonization quality. Ensures that practical applicability is strong, consumption of combustible gas is saved, and service life of the air cap is prolonged.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of the air temperature-controlled straw carbonization furnace.    Reduced bushing (4)    Internal air exhaust cooling double pipe (6)    Metal air exhaust cooling tube (8)    Vent hole (9)    Lower end of air cap (10)    Internal air exhaust cooling bend (11)    Second external air inlet pipe bend (12)
NOVELTY - The semi-gasified stove has stove core (2) in which upper part is gasification liner. The top end of gasification liner is provided with secondary air inlet. The stove body (1) is provided with secondary air channel (7) at outer side of stove core. The stove body is provided with stove chamber at the upper part of the stove core. The stove chamber is communicated with a chimney outlet (8). The secondary air inlet of stove core and secondary air channel of stove body are communicated with the stove chamber.    USE - Semi-gasified stove using biomass or coal.    ADVANTAGE - Increases the cooking energy effect, while reducing the harmful gas and dust emissions. Saves energy, and ensures environment friendliness, safe and efficient operation of the stove.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a stove core.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of the semi-gasified stove using biomass or coal.    Stove body (1)    Stove core (2)    Feed inlet (5)    Secondary air channel (7)    Chimney outlet (8)
NOVELTY - The unit has a freezing separating chamber (8) connected with a normal pressure nitrogen storage bag (13), a compressed nitrogen storage tank (7), a liquid carbon dioxide storage tank (12.3), a liquid methane storage tank (12.2), and a liquefied hydrogen sulphide storage tank (12.1). The normal pressure nitrogen storage bag is connected with the compressed nitrogen storage tank through a nitrogen compressing device (5) and a cooler (6). The nitrogen compressing device is connected with a methane electric generator (2) through a gearbox (4).    USE - Vehicle-mounted methane freezing and liquefying segregating unit.    ADVANTAGE - The unit is flexible, light, movable and convenient to operate. The unit reduces the usage of the straw materials and power cost of transporting the methane residue and rubbish. The unit increases the production of processing methane. The unit saves energy and protects environment.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a vehicle-mounted methane freezing and liquefying segregating unit.    Methane electric generator (2)    Gearbox (4)    Nitrogen compressing device (5)    Cooler (6)    Compressed nitrogen storage tank (7)    Freezing separating chamber (8)    Liquefied hydrogen sulphide storage tank (12.1)    Liquid methane storage tank (12.2)    Liquid carbon dioxide storage tank (12. 3)    Normal pressure nitrogen storage bag (13)
NOVELTY - The gasifier has a gasifier body part provided with a furnace (2), a heat insulating layer (3) and a furnace wall (4). An upper part of the gasifier body is provided with a gasifier cover (5) and a water seal groove (11). A lower part of the gasifier body is provided with an air inlet (7), an air distribution hole (9), an ash outlet (10), a fixing furnace bar (13), a movable furnace bar (14) and an ash chamber (17) when the fixing furnace bar is located above the movable furnace bar. The movable furnace bar is provided with a horizontal furnace bar and a vertical furnace bar.    USE - Domestic double-furnace straw gasifier for eliminating coking and burning out phenomenon.    ADVANTAGE - The gasifier is simple in structure, and has reliable work and convenient operation. The fixing furnace bar is located at a bottom part of the furnace, and the movable furnace bar is located below, so that movable furnace bar is pulled, thus eliminating coking and burning out phenomenon when coking the slag or burning out through the straw fuels.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a domestic double-furnace straw gasifier in partial section.    Furnace (2)    Heat insulating layer (3)    Furnace wall (4)    Gasifier cover (5)    Air inlet (7)    Air distribution hole (9)    Ash outlet (10)    Water seal groove (11)    Fixing furnace bar (13)    Movable furnace bar (14)    Ash chamber (17)
NOVELTY - The gasifier has a circulating water jacket (5) mounted between a furnace body outer cylinder (4) and a conical shape furnace body inner cylinder (6). Diameter of small port is not less than 0.3 cm. Height of the small port is not less than 0.8 cm. A vibrator (18) is arranged on an ash box (16). A grate plate (15) is provided in a plate turning-over type connection. The furnace body inner cylinder on the grate plate is uniformly provided with air supply holes (10) on an upper art of the small port. Thickness of a furnace body is 2-3 mm.    USE - Low-value biomass lignite gasifier.    ADVANTAGE - The conical furnace body inner cylinder is cleverly utilized, so that the structure design of the circulating water jacket and the vibrator is increased to ensure fuel layer in the furnace to successfully fall down and sufficiently burn out, thus avoiding generating of scaffold cavity phenomenon, working stably, increasing combustion ratio and increasing gas production rate of the gasifier. The gasifier ensures sufficient aerobic combustion of a biomass fuel layer in the furnace, conveniently removes furnace waste residues to reach to purpose of energy conservation, environment protection, safety, economical and practical performances by design of uniformly arranging the air supply holes and the turning type grate plate.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a low-value biomass lignite gasifier.    Furnace body outer cylinder (4)    Circulating water jacket (5)    Conical shape furnace body inner cylinder (6)    Air supply holes (10)    Grate plate (15)    Ash box (16)    Vibrator (18)
NOVELTY - The generator has a rotary shaft whose two ends are sleeved in relative holes on an inner wall of a material feeding pipe (7) in a matched manner. An end of the material feeding pipe is fixedly connected with a straight rod handle after stretching out from an outer side of a wall of the material feeding pipe. An upper end of the material feeding pipe is fixedly connected with a lower end surface of a reverse conical material feeding hopper (9). A blast pipe (16) is fixedly sleeved in a round hole on a disk board (15) by an orifice after passing through the conical dust collecting hopper.    USE - Plant energy gas generator.    ADVANTAGE - The material is uniformly stirred for combustion, so that the dust is automatically discharged.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a plant energy gas generator.    Support (1)    Material feeding pipe (7)    Reverse conical material feeding hopper (9)    Disk board (15)    Blast pipe (16)
NOVELTY - The gasifier has a pressure lever (3) whose top part is connected with a crank (1) by a feed screw nut (2). A pressure plate (6) is provided with a pressure plate dense lever (7) that is utilized for stretching into a filler bin (8). An air outlet hole (5) is formed on an upper part of a furnace body for being connected with an inner chamber of the furnace body. An igniting and ash drawing opening (10) is formed on a side wall of a furnace bottom for lighting up fire and taking out ash. A bellow (11) is arranged on a bottom part of the filler bin and connected with an air blower (12).    USE - Straw gasifier.    ADVANTAGE - The gasifier is utilized for focusing fuel and kindling point while lighting up the fire, so that overall surface of the furnace body can produce gas. The gasifier is utilized for focusing surrounding fuel based on kindling point, so that the surface of the furnace body produces enough gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a straw gasifier.    Crank (1)    Feed screw nut (2)    Pressure lever (3)    Air outlet hole (5)    Pressure plate (6)    Pressure plate dense lever (7)    Filler bin (8)    Igniting and ash drawing opening (10)    Bellow (11)    Air blower (12)
NOVELTY - The furnace has an air supply device provided with an air supply pipe and an air distributor below a gasification chamber (4). An air distributor is provided with an upper circular plate (7) and a lower circular plate (8). An arc bent air guide plate (9) is formed between the two circular plates. Center of the lower circular plate is provided with through-holes (10) for fixing with air supply pipe mouths and the air guide plates that are uniformly distributed along circumferential direction of the lower circular plates by taking through-holes of the lower circular plates as center.    USE - Discharging-free environment-friendly type biomass gasification furnace.    ADVANTAGE - The furnace has simple and rational structure, special design, continuous and stable use, high gas generation efficiency, better usage effect, and is tar or swage discharging free, environment friendly, pollution free and durable to use.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a discharging-free environment-friendly type biomass gasification furnace.    Gasification chamber (4)    Upper circular plate (7)    Lower circular plate (8)    Arc bent air guide plate (9)    Through-holes (10)
NOVELTY - The device has an external sleeve pipe whose wind inlet interface (5) is linked with an air supply interface (7) by an air inlet through-hole. An air supply through-hole of an internal sleeve pipe is linked. A phase of air inlet and air outlet interfaces (6, 4) of the external sleeve pipe is linked with the air inlet through-hole. An internal cavity and an air outlet through-hole of the internal sleeve pipe are provided. Another phase of the air inlet interface and the wind inlet interface of the external sleeve pipe are linked with the air supply interface by the air inlet through-hole.    USE - Biomass gasification device.    ADVANTAGE - The device is simple in structure and convenient to install and use. The device controls the air inlet amount of each pipeline by the adjustable value.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass gasification device in partial section.    Air outlet interface (4)    Wind inlet interface (5)    Air inlet interface (6)    Air supply interface (7)    Air outlet port (18)
NOVELTY - The furnace has a rotary gear whose lower part is provided with a rotary gear bottom roller. A lower part of the rotary gear bottom roller is provided with a roller track. A lower part of the roller track is provided with a furnace bottom support frame that is connected with a furnace support. Middle and lower parts of a gasification furnace cavity are provided with a fire-resistance lining support coil. The fire-resistance lining support coil is connected with a furnace water sleeve. A lower part of the furnace water sleeve is provided with a furnace support.    USE - Renewable energy gasification furnace.    ADVANTAGE - The municipal domestic wastage in the mixing fuel and the harmful and toxic burnable substance in the organic sludge in the waste water processing factory is cracked at high temperature to reduce atmospheric pollution. The furnace saves energy and protects ecological environment.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a comprehensive gasification furnace.
NOVELTY - The system has a first-stage cyclone separator (4) whose lower ends and a second-stage cyclone separator (5) are connected to first-stage and second-stage air seal machines (7, 8) via a connection pipe. The first-stage and the second-stage air seal machines are connected to a dust removal auger (9). An air pre-heater (6) is located in an interlayer of the first-stage separator. An air inlet device is connected with the pre-heater via a pipeline. A bed material adding port is arranged on a lower part of a fluidized bed gasification furnace (2) and connected to a bed material adding auger.    USE - Biomass gas industrial furnace system for a fluidized bed.    ADVANTAGE - The biomass is converted into clean gas and combusted effectively in the industrial furnace, so as to release heat. The discharge of sulfur dioxide and oxynitride is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass gas industrial furnace system.    Fluidized bed gasification furnace (2)    First-stage cyclone separator (4)    Second-stage cyclone separator (5)    Air pre-heater (6)    First and second stage air seal machines (7, 8)    Dust removal auger (9)
NOVELTY - The chassis has multiple rotating radiation linear projections evenly distributed on an upper end face. Multiple through holes are formed in the projections, where the chassis is made of insulation materials with certain thickness.    USE - Gasification generator chassis for a biomass gasifier.    ADVANTAGE - The chassis ensures enough air inlets. The chassis produced air vortex while blowing, thus ensuring enough burning. The chassis increases fuel utilization ratio of the biomass fuels transformed into gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a top perspective view of a gasification generator chassis.
NOVELTY - The device has a filter tank (1) provided with a gas inlet (7). Another filter tank (2) is provided with a gas outlet (8) and a water tank (10). The former filter tank and the latter filter tank are arranged on above the water tank. The former filter tank is connected to an internal cavity. The former filter tank is provided with a filtering mechanism (5). The latter filter tank is provided with another filtering mechanism (6). A top part of the former filter tank is connected to a top part of the latter filter tank through a pipeline (9). Purified water is accommodated in the water tank.    USE - Device for filtering biomass fuel gas.    ADVANTAGE - The device has filtering efficiency, and is simple to operate. The device reduces tar content in fuel gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a filtering device.    Filter tanks (1, 2)    Filtering mechanisms (5, 6)    Gas inlet (7)    Gas outlet (8)    Pipeline (9)    Water tank (10)
NOVELTY - The modifier has a straw gas pipeline connected between an outlet of a compressor and an inlet of a converter via a preheater. A converted gas pipeline is connected between an outlet of the converter and an inlet of a gas-liquid separator and between an outlet of the gas-liquid separator and an inlet of an absorbing purifier via a condenser. The converter synthesizes carbon dioxide and hydrogen.    USE - Modifier for promoting a calorific value of straw gas.    ADVANTAGE - The modifier is made into a portable movable mode to process the straw gas in a straw gas storage station. The modifier promotes the calorific value of the straw gas in short time with high output efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a modifier.'(Drawing includes non-English language text)'
NOVELTY - The device has a straw gas pipeline connected between a compressor outlet and an absorption purifier inlet. A purified gas pipeline is connected between the absorption purified outlet and a converter inlet via a pre-heater. A converter gas pipeline is connected between a converter and a gas-liquid separator inlet via a condenser.    USE - Device for increasing heat value of straw gas.    ADVANTAGE - The device has high efficiency. The heat value of the straw gas is improved to 5000-8500 Kcl/Nm3 from 2000 Kcl/Nm3 in a short time.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a straw gas heat value increasing device.'(Drawing includes non-English language text)'
NOVELTY - An isolated polypeptide comprising a 116 or 116 amino acid sequence (SEQ ID NO: 37 or 115) fully defined in the specification, is new. The polypeptide is not chosen from one of 18 (226-254) amino acid sequences (SEQ ID NOs: 2, 4, 6, 8, 10, 12, 14, 16, 18, 20, 22, 24, 26, 28, 30, 32, 34, and 36) all fully defined in the specification.    USE - The isolated polypeptide is useful for producing hydrocarbon, chosen from C.sub.13-C.sub.21 alkane and C.sub.13-C.sub.21 alkene (all claimed) used in biofuel.    ADVANTAGE - The prepared hydrocarbon is inexpensive and environmentally-friendly.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) genetically engineered microorganism comprising a nucleic acid sequence encoding the amino acid sequence of SEQ ID NO: 37 or 115, where the nucleic acid sequence is expressed in the microorganism to produce the polypeptide comprising the amino acid sequence of SEQ ID NO: 37 or 115; and    (2) method for producing hydrocarbon, involves (a) expressing a nucleic acid sequence encoding a polypeptide comprising the amino acid sequence of SEQ ID NO: 37 or 115 in a host cell, (b) providing the polypeptide, where the polypeptide interacts with the host cell to produce a hydrocarbon, and (c) isolating the hydrocarbon from the host cell.
NOVELTY - Multi-cellulase enzyme composition comprises a cellobiohydrolase (CBH) enzyme, an endoglucanase (EG) enzyme and a beta-glucosidase (BG) enzyme. The CBH enzyme has at least 90% sequence identity to SEQ ID NO: 2. The EG enzyme has at least 90% sequence identity to SEQ ID NO: 4 or SEQ ID NO: 6. The BG enzyme has at least 90% sequence identity to SEQ ID NO: 8 or SEQ ID NO: 10.    USE - The multi-cellulase enzyme composition is useful for the enzymatic hydrolysis of cellulose substrate to a fermentable sugar to obtain an end product including an alcohol (preferably ethanol), an organic acid, amino acid and a biofuel (all claimed).    ADVANTAGE - The multi-cellulase enzyme composition increases efficiency of producing biofuels and other commercially valuable compounds in a cost-effective manner.    DETAILED DESCRIPTION - Multi-cellulase enzyme composition comprises a cellobiohydrolase (CBH) enzyme, an endoglucanase (EG) enzyme and a beta-glucosidase (BG) enzyme. The CBH enzyme has at least 90% sequence identity to a fully defined sequence comprising 424 amino acids of SEQ ID NO: 2 as given in the specification. The EG enzyme has at least 90% sequence identity to a fully defined sequence comprising 222 amino acids each of any one of SEQ ID NOs: 4 or 6 as given in the specification. The BG enzyme has at least 90% sequence identity to a fully defined sequence comprising 646 amino acids each of any one of SEQ ID NOs: 8 or 10 as given in the specification. An INDEPENDENT CLAIM is also included for hydrolyzing a cellulose substrate to a fermentable sugar, comprising contacting aqueous slurry containing a cellulose substrate with the multi-cellulase enzyme composition, and hydrolyzing the substrate under conditions sufficient to produce a hydrolysis product comprising fermentable sugars comprising glucose.
NOVELTY - The apparatus (1) has an inner cylinder (5) arranged at outer side of heating element (2) of baseplate (6). An inner tube (7) is arranged at outer side of inner cylinder. The modification catalyst (20) is stored in the space formed between inner cylinder and inner tube. A heat insulating material (40) is arranged to face the heating element of the baseplate so that the modification catalyst is circulated between the inner cylinder and inner tube.    USE - Hydrogen gas generating apparatus for fuel cell electric power generation system.    ADVANTAGE - The possibility for heat deformation of inner cylinder can be avoided and the possibility for flow of reformed gas into combustion exhaust gas path can be avoided effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the hydrogen gas generating apparatus. (Drawing includes non-English language text)    Hydrogen gas generating apparatus (1)    Heating element (2)    Inner cylinder (5)    Baseplate (6)    Inner tube (7)    Modification catalyst (20)    Heat insulating material (40)
NOVELTY - The apparatus has reaction liquid container (2) which accommodates reaction liquid in space between accommodating portions (1). A hydrogen supply pipe (4) supplies hydrogen which is generated by the reaction of the reaction liquid and the water-absorption portion (3) in reaction liquid container to the accommodating portion arranged in exterior of the reaction liquid container. The accommodation portion is arranged in specific state such that expansion is not inhibited by inner wall of the reaction liquid container.    USE - Apparatus for producing hydrogen supplied to fuel cell.    ADVANTAGE - The stability and reproducibility of the apparatus is improved. The size of the hydrogen producing apparatus is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a disassembled perspective view of the hydrogen production apparatus.    Accommodating portions (1)    Reaction liquid container (2)    Water-absorption portion (3)    Hydrogen supply pipe (4)    Hydrophobic sheet (23)
NOVELTY - Converting (M1) solid carbonaceous material to a liquid product involves maintaining the solid carbonaceous material in the presence of at least one active source of cobalt and at least one active source of a second metal at a temperature greater than 350 degrees C and a pressure of 300-5000 psig to form a liquid product.    USE - For converting solid carbonaceous material, preferably a coal, to a liquid product (claimed), to form the liquid hydrocarbon products.    ADVANTAGE - The systems and processes can be used to achieve optimization and efficiency in the production of any desired proportions (or yield percentages) of liquid and/or gas products having a variety of desired properties. The process offers flexibility to a user in being able to achieve desired hydroconversion products from any solid carbonaceous material using any of a variety of different combinations of hydrocarbonaceous liquid, catalyst, and/or catalyst precursor, as well as pretreatment and hydroconversion conditions.
NOVELTY - A biomass processing system (A) comprises preprocessor (1) which removes lignin contained in wood type biomass as pre-processing of wood type biomass, decomposition apparatus (2) which produces hydrolysis processed material containing glucose by carrying out hydrolysis process of mixture of processes wood type biomass and solid acid catalyst, and solid-liquid separator (3) which separates hydrolysis processed material into solid and liquid. The solid material contains solid acid catalyst, and liquid material contains saccharide solution which contains glucose.    USE - A biomass processing system.    ADVANTAGE - The system can simplify separation of solid acid catalyst from solid material, and recycle solid acid catalyst easily.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a biomass processing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of biomass processing system. (Drawing includes non-English language text).    Preprocessor (1)    Decomposition apparatus (2)    Solid-liquid separator (3)    Bioreactor (4)    Biomass processing system (A)
NOVELTY - A catalytic converter consists of metal honeycomb base material formed by processing stainless steel foil, and catalyst layer formed on base material. The stainless steel foil contains iron, chromium and aluminum, and has alumina film formed on the surface. The concentration of iron in the oxide film is 0.5-5.0 %mass with respect to the oxide.    USE - Catalytic converter for fuel cell modifiers used for modifying Methane gas and alcohol.    ADVANTAGE - The catalytic converter has excellent high temperature durability, and provides fuel cell with high electric power generation efficiency.
NOVELTY - Producing a soil additive for improving cation exchange capacity, nutrient- and water holding capacity of the soil by biological fermentation, comprises continuously supplying an organic biomass into a reaction vessel for hydrothermal carbonization before the fermentation of a liquid coal sludge, continuously removing the reaction product from the reaction vessel, and then supplying to additional steps of the fermentation.    USE - The additive is useful for improving cation exchange capacity and nutrient- and water holding capacity of the soil by biological fermentation (claimed).    ADVANTAGE - The method: produces the coal material under aqueous conditions, and the obtained coal material exhibits good miscibility, good flowability and small particle size, and is easily mixed with the water-containing biomass, and directly used as the soil additive or supplied for the fermentation without adding other organic biomass or without additional mixing steps, and thus it eliminates costly drying steps, crushing, screening and dry-mixing steps; reduces concentration of metals and toxic materials in the soil additive compared to an input material; and allows quantitative determination of air conditioning effect and associated carbon dioxide.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for carrying out the above method.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic process flow of the method.    Storage container for sewage sludge (1)    Reactor for the hydrothermal carbonization of biomass (2)    Device for mixing sewage sludge with carbonized sewage (4)    Device for analyzing the carbon content of the fermented mixture (6)    Device for determining the mass of the fermented mixture (7)
NOVELTY - Catalytic cracking of a pyrolysis oil derived from material, comprises: (a) subjecting a feed to a hydrodeoxygenation step to obtain a product stream; (b) separating the partially deoxygenated pyrolysis oil from the product stream obtained in (a); (c) contacting the partially deoxygenated pyrolysis oil obtained in (b) in the presence of a hydrocarbon feed with a cracking catalyst under catalytic cracking conditions to obtain a deoxygenated and cracked product stream; and (d) separating at least one product fraction from the product stream obtained in (c).    USE - The process is useful for catalytic cracking of pyrolysis oils for preparing fuel products (claimed) and chemicals.    ADVANTAGE - The process reduces inorganic content in pyrolysis oil and transportation costs by transporting pyrolysis oil instead of biomass.    DETAILED DESCRIPTION - Catalytic cracking of a pyrolysis oil derived from material comprising lignocellulose, comprises: (a) subjecting a feed comprising the pyrolysis oil to a hydrodeoxygenation step to obtain a product stream comprising a partially deoxygenated pyrolysis oil; (b) separating the partially deoxygenated pyrolysis oil having an oxygen content of 5-30 wt.% from the product stream obtained in (a); (c) contacting the partially deoxygenated pyrolysis oil obtained in (b) in the presence of a hydrocarbon feed derived from a mineral crude oil with a cracking catalyst under catalytic cracking conditions to obtain a deoxygenated and cracked product stream; and (d) separating at least one product fraction from the product stream obtained in (c). An INDEPENDENT CLAIM is included for a fuel product obtained from a product fraction, and further containing at least one additive.
NOVELTY - The biomass dry distillation kettle has kettle main body (1), and a kettle cover (4) which is buckled with the kettle main body. A heating cage (2) is arranged in the kettle main body, and comprised of multiple heating rings (10) fixedly connected in the axial direction. The heat conducting rings above the bearing table are connected by the heat conducting rods, and a connection rod (9) is arranged on the heating cage. A flange interface (5) which outputs matter in the kettle main body is arranged on the kettle cover, and a pulling ring (6) is arranged on the kettle cover.    USE - Biomass dry distillation kettle.    ADVANTAGE - Provides biomass dry distillation kettle which can decompose biomass completely with good heat conducting effect, simple structure, convenient use, and wide application.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a biomass dry distillation kettle.    Kettle main body (1)    Heating cage (2)    Kettle cover (4)    Flange interface (5)    Pulling ring (6)    Connection rod (9)    Heating rings (10)
NOVELTY - The connected furnace has furnace with inner layer made of firebricks and outer layer made of common bricks. The inner layer closely touches with the outer layer, and the top portion of furnace is arc. The front end of furnace is provided with a smoke outlet, and the back end of top portion of furnace is provided with a feeding inlet. The front surface of furnace is provided with a discharge outlet, and the connected furnace is formed by furnaces connected in parallel.    USE - Connected furnace for straws carbonization.    ADVANTAGE - Provides connected furnace which can quickly carbonize straws with high carbon content, saves raw materials and creates economic benefits for enterprises.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a connected furnace for straws carbonization.
NOVELTY - The biomass gasification furnace has hearth (1) with middle portion which is provided with grate (2) with upper portion provided with feed advancing mechanism (3). The lower portion of grate is provided with a dust collecting medium warehouse (4), and the outer portion of dust collecting medium warehouse is provided with a filter (5) and circulation pump (6). The outlet of dust collecting medium warehouse communicates with the inlet of filter via a pipeline, and the outlet of filter is communicated with the inlet of dust collecting medium warehouse via the circulation pump.    USE - Biomass gasification furnace.    ADVANTAGE - Provides biomass gasification furnace with stable material gasification rate, and in which the straw dust is effectively retained in the furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a biomass gasification furnace.    Hearth (1)    Grate (2)    Feed advancing mechanism (3)    Dust collecting medium warehouse (4)    Filter (5)    Circulation pump (6)
NOVELTY - The device has a condensation tube (33) arranged in a condensation chamber (3) and communicated with a condensation opening (24) at bottom of a spraying and washing chamber (2) and a filter opening (34) at top of a filter chamber (4). A cooling water inlet (31) and a cooling water outlet (32) are respectively arranged at bottom and top of the condensation chamber. A filter core (43) is formed between an upper filter mesh (41) and a lower filter mesh (42) arranged in the filter chamber. A gas supplying opening (44) is formed at bottom of the filter chamber and connected to a storage pool (6).    USE - Biomass gasifying device.    ADVANTAGE - The secondary product is collected by the separating pool, and the gas is stored by the storage pool, so that the device can steadily and continuously supply the gas. The device increases gas supplying purity, effectively utilizes different biomass resources and increases yields of the biomass gasifying gas and the secondary product and increases source using rate. The device supplies the gas in the region range with sufficient biomass resources. The coke in the gas can be effectively removed in a labyrinth washing way in the spraying and washing chamber.    DETAILED DESCRIPTION - The filter core is made of biomass material.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass gasifying device.    Spraying and washing chamber (2)    Condensation chamber (3)    Filter chamber (4)    Storage pool (6)    Condensation opening (24)    Cooling water inlet (31)    Cooling water outlet (32)    Condensation tube (33)    Filter opening (34)    Upper filter mesh (41)    Lower filter mesh (42)    Filter core (43)    Gas supplying opening (44)
NOVELTY - The furnace has two furnace grate parts connected with an electric motor via a chain of a transmission axis. A furnace top includes a furnace top stirring air allocating device that comprises an electric motor, a speed reducer, a hollow transmission axis and a stirring lamina. An upper end of the hollow transmission axis is connected with the electric motor and the speed reducer of the device. A lower end of the hollow transmission axis is connected with the stirring lamina. A top end of the hollow transmission axis is linked with an air allocating fan via an electric driven valve gate.    USE - Biomass gasification reacting furnace for a positive air allocating device.    ADVANTAGE - The furnace realizes slag breaking via rolling and squeezing. The furnace adjusts height of a firing layer via parameters of material height, material layer, firing layer, restoring layer, dust layer and the furnace bottom negative pressure monitored by a central control system, thus guaranteeing safety of the positive air allocating device.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an automatic control method for a biomass gasification reacting furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a biomass gasification reacting furnace.
NOVELTY - The method involves gasifying raw material using overheated oxygen or oxygen-enriched air and overheated water steam as primary gasification agent and sending raw material into gasification furnace of fluidized bed to generate coal gas. The fuel gas is injected as secondary gasification agent into gasification furnace. The residue ash and dust are separated from coal using cyclone dust collector. The waste heat is recycled using waste heat recycling system, to form feed gas.    USE - Method for preparing feed gas used in manufacturing of fertilizer and methanol, using rubbish and biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating process for preparing feed gas. (Drawing includes non-English language text)
NOVELTY - Reducing carbon dioxide to one or more products, comprises: (a) bubbling the carbon dioxide into a solution of an electrolyte and a catalyst (124) in a divided electrochemical cell; (b) varying at least one of (a1) which of the products is produced and (a2) a faradaic yield of the products by adjusting one or more of a cathode (120) material and a surface morphology of the cathode, the electrolyte and a manner in which the carbon dioxide is bubbled, or a pH level of the solution and an electrical potential; and (c) separating the products from the solution.    USE - The method is useful for reducing carbon dioxide to products.    ADVANTAGE - The method provides high faradaic yields (e.g. greater than 20%) with long life (e.g. improved stability), electrode and cell cycling in an economical manner.    DETAILED DESCRIPTION - Reducing carbon dioxide to one or more products, comprises: (a) bubbling the carbon dioxide into a solution of an electrolyte and a catalyst (124) in a divided electrochemical cell, where the divided electrochemical cell comprises an anode (118) in a first cell compartment and a cathode in a second cell compartment, and the cathode reduces the carbon dioxide into the products; (b) varying at least one of (a1) which of the products is produced and (a2) a faradaic yield of the products by adjusting one or more of a cathode (120) material and a surface morphology of the cathode, the electrolyte and a manner in which the carbon dioxide is bubbled, or a pH level of the solution and an electrical potential; and (c) separating the products from the solution.    DESCRIPTION OF DRAWING(S) - The figure shows a block diagram of a method for reducing carbon dioxide.    Oxygen extractor (112)    Separator or Membrane (116)    Anode (118)    Cathode (120)    Catalyst. (124)
NOVELTY - The method involves changing high concentration organic wastewater (1) into fertilizer (8) and feed additives (11) by evaporation, desalination and drying.    USE - High concentration organic yeast wastewater treatment method.    ADVANTAGE - The method improves the economic benefits of yeast wastewater, reduces the cost of yeast wastewater treatment, and increases potassium in the fertilizer so as to obtain high-grade potash.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of a high concentration organic yeast wastewater treatment method.'(Drawing includes non-English language text)'    High concentration organic wastewater (1)    Evaporator (2)    Catalyst (3)    Fertilizer (8)    Additives (11)
NOVELTY - Wetland brick of sewage and its device comprises a wetland brick, a filtering net, a medium, a vegetation, a surface layer, a filtering tank, a water discharging opening, a direct-flow hole and laminar flow holes. The medium filtering layer is on the upper part, the filtering tank is on the bottom, the wetland brick is in the filtering tank, and the filtering net is fixed on the upper surface of the plane filtering layer. The two wetland bricks are superposed and arranged to form several lines, and the lower surface of the plane filtering layer is connected to the filtering tank.    USE - Used as a wetland brick of sewage and its device.    ADVANTAGE - The device is simple, economical and has strong practicability.    DETAILED DESCRIPTION - Wetland brick of sewage and its device comprises a wetland brick, a filtering net, a medium, a vegetation, a surface layer, a filtering tank, a water discharging opening, a direct-flow hole and laminar flow holes. The medium filtering layer is on the upper part, the filtering tank is on the bottom, the wetland brick is in the filtering tank, and the filtering net is fixed on the upper surface of the plane filtering layer. There are four holes on the wetland brick, and the two wetland bricks are superposed and arranged to form several lines. The lower surface of the plane filtering layer is connected to the filtering tank, and the water discharging opening is located on the bottom of the filtering tank.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the wetland brick of sewage and its device.
NOVELTY - Methane tank heating device comprises a feed port, which is arranged at one side of the methane tank, a gas outlet pipe, which is mounted at the other side, a superconductive heating pipe, which is installed at one side of the bottom of the methane tank. One end of the superconductive heating pipe is inserted into the methane tank and the other end is inserted into the ground.    USE - Used as a methane tank heating device.    ADVANTAGE - The methane produced from the tank can be used in all seasons, therefore can save energy.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of methane tank heating device.
NOVELTY - The apparatus has electrolytic bath (4) that is divided into two electrolysis chambers (2,3). A catalyst electrode (8) is contacted with negative plate (P1) installed at outlet (6), and inlet port (5) formed in bottom surface of electrolytic bath. An anode plate (P2) is installed at other electrolysis chamber to increase electric current density of electrode plate.    USE - Hydrogen formation apparatus.    ADVANTAGE - The hydrogen can be formed effectively by installing anode plate at other electrolysis chamber to increase electric current density of electrode plate.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen formation apparatus.    Electrolysis chambers (2,3)    Electrolytic bath (4)    Inlet port (5)    Outlet (6)    Catalyst electrode (8)    Negative plate (P1)    Anode plate (P2)
NOVELTY - Integrated biological desulfurization device of methane comprises a tower body composed of an upper desulfurization tower (3) and a lower desulfurization tower (16), and a spraying system and a reflux system. The upper desulfurization tower has a methane outlet at the top. The spraying system includes a spray nozzle (2) in the upper half of the cavity of the upper desulfurization tower, and a delivery pipe (23) mounted out of the tower body, two ends of the delivery pipe separately connects with the spray nozzle and the cavity of the lower desulfurization tower.    USE - Used as an integrated biogas desulfurization device.    DETAILED DESCRIPTION - Integrated biological desulfurization device of methane comprises a tower body composed of an upper desulfurization tower (3) and a lower desulfurization tower (16), and a spraying system and a reflux system. The upper desulfurization tower has a methane outlet at the top. The spraying system includes a spray nozzle (2) in the upper half of the cavity of the upper desulfurization tower, and a delivery pipe (23) mounted out of the tower body, two ends of the delivery pipe separately connects with the spray nozzle and the cavity of the lower desulfurization tower. The delivery pipe is provided with a circulating pump (17). The reflux system includes a reflux pipe out of the tower body, whose two ends separately connects with the bottom of the cavity of the upper desulfurization tower and the cavity of the lower desulfurization tower.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the integrated biogas desulfurization device.    Spray nozzle (2)    Upper desulfurization tower (3)    Lower desulfurization tower (16)    Circulating pump (17)    Delivery pipe (23)
NOVELTY - The hydrogen generator has reaction bath unit (10) containing anode electrode (14) and cathode electrode (18). An electrochemical activity element (13) is arranged in the support surface (12) of anode electrode and nano carbon binder (16) containing sulfone group is arranged on support surface (15) of cathode electrode.    USE - Hydrogen generator for bio-electrochemistry application.    ADVANTAGE - The electrode effective area and hydrogen generation amount can be improved. The hydrogen ion generated in anode electrode can be rapidly attracted by binder, hence hydrogen ion transition speed to cathode electrode is increased. The hydrogen generation rate can be improved. The internal resistance and hydrogen transfer resistance can be lowered. The power consumption can be decreased.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for hydrogen generator operation method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of hydrogen generator.    Reaction bath unit (10)    Support surface of anode electrode (12)    Electrochemical activity element (13)    Anode electrode (14)    Support surface of cathode electrode (15)    Nano carbon binder (16)    Cathode electrode (18)
NOVELTY - A nitrogen expander cycle (40) circulates nitrogen refrigerant (50) in cold box (30) for separating carbon dioxide (35) in bio coal stored in buffer tank (20). The impurity components are separated from carbon dioxide of biogas supplied to anaerobic digester. The heat exchange process of carbon dioxide is performed with nitrogen refrigerant. The temperature of carbon dioxide is increased after heat exchange process. The accumulated solid carbon dioxide is passed to heat exchangers (31,33) connected to liquefied biomethane storage tank (60).    USE - Device for preparing liquefied biomethane from processing of livestock waste, food waste and sewage sludge.    ADVANTAGE - The liquefied biomethane can be effectively used as the energy source with an excellent portability through the heat exchange with the super low temperature refrigerant and storage natural material of methane in the biogas in which the impurity among the biogas more specifically generated in the anaerobic digester or the landfill can be removed effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the liquefied biomethane preparation device.    Buffer tank (20)    Cold box (30)    Heat exchangers (31,33)    Carbon dioxide (35)    Nitrogen expander cycle (40)    Liquefied biomethane storage tank (60)
NOVELTY - The apparatus has a screw which is rotated so as to stir the food waste in a fermentor (10). A warm wind supply unit is installed in the diagonal direction on a large-scale fermentation tub. A turn table (20) is inclined and rotated with respect to a circular column (16) placed vertically in a flat center of the fermentor.    USE - Fermentation apparatus for food waste.    ADVANTAGE - The food waste fermentation process is performed in a short time and at low cost. The deformation of the screw is prevented, and the workability of the screw is improved. The acceleration of fermentation is increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a fermentation apparatus for food waste.(Drawing includes non-English language text)    Fermentor (10)    Circular column (16)    Turn table (20)
NOVELTY - Synthesis of azacitidine comprises: (i) reacting bis(trimethylsilyl)amine and 4-amino-1,3,5-triazin-2(1H)-one in presence of methylbenzene and performing silanization reaction in presence of a phase transfer catalyst to obtain N-(trimethylsilyl)-4-(trimethylsilyloxy)-1,3,5-triazin-2-amine; and (ii) condensing (2R,3S,4R)-tetrahydrofuran-2,3,4,5-tetrayl tetraacetate and N-(trimethylsilyl)-4-(trimethylsilyloxy)-1,3,5-triazin-2-amine to obtain (2R,3S,4R,5S)-4-(4-amino-2-oxo-1,3,5-triazin-1(2H)-yl)tetrahydrofuran-2,3,5-triyl triacetate and carrying out alcoholysis in an alkaline environment.    USE - The method is useful for the synthesis of azacitidine.    ADVANTAGE - The method: shortens the silanization reaction time; reduces the waste liquid quantity of the bis(trimethylsilyl)amine; prevents the influence of water in methanol and ethanol during the purification step and prepares highly pure azacitidine product; utilizes low cost reagent; has moderate reaction conditions; and is short and suitable for industrial production.    DETAILED DESCRIPTION - Synthesis of azacitidine comprises: (i) reacting bis(trimethylsilyl)amine and 4-amino-1,3,5-triazin-2(1H)-one in presence of methylbenzene as a solvent under anhydrous conditions and carrying out silanization reaction under the catalysis of a phase transfer catalyst to obtain N-(trimethylsilyl)-4-(trimethylsilyloxy)-1,3,5-triazin-2-amine, where the molar ratio of 4-amino-1,3,5-triazin-2(1H)-one and the phase transfer catalyst is 1:0.005-0.5; and (ii) condensing (2R,3S,4R)-tetrahydrofuran-2,3,4,5-tetrayl tetraacetate and N-(trimethylsilyl)-4-(trimethylsilyloxy)-1,3,5-triazin-2-amine to obtain (2R,3S,4R,5S)-4-(4-amino-2-oxo-1,3,5-triazin-1(2H)-yl)tetrahydrofuran-2,3,5-triyl triacetate and carrying out alcoholysis in an alkaline environment to obtain the azacitidine.
NOVELTY - A microorganism comprising Bacillus subtilis BHf3-4, JhqK9-1 and JhqM8 (CGMCC No: 4046, 4047, 4048), is new.    USE - The microorganism is useful for degrading phenol and cyanogens in coked waste water.    ADVANTAGE - The volatile phenol in coked waste water can be removed at a rate of 99.6-99.9%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for degrading phenol and cyanogens in coke waste water, which involves (a) cultivating the B.subtilis BHf3-4, Bacillus JhqK9-1 and Klebsiella oxytoca JhqM8 until the concentration is 108-109 cfu/l, and mixing the B.subtilis BHf3-4, Bacillus JhqK9-1 and Klebsiella oxytoca JhqM8 to ratio of 2:1:1, and inoculating the mixture with quantity of 1-10% in membrane bioreactor, (b) treating the inoculated mixture to membrane bioreactor at 25-35 degrees C, aerating oxygen to the bioreactor for 2-4 times/day, adding 3.01 m3 of air to each cubic meter of sewage each time, adding nutritional liquid to the membrane bioreactor for every 9 days, subjecting the liquid to degrade phenol and cyanogens in coked waste water for 24-72 hours, where pore diameter of the membrane bioreactor is 0.11 microns, water outlet pressure is 0.12 MPa, and nutritional liquid is 0.5-2% by volume of the membrane bioreactor comprises (in g/l) peptone (10), beef extract (3), sodium chloride (5), dipotassium phosphate (K2PHO4) (1), magnesium sulfate heptahydrate (MgSO4.7H2O) (5) and the pH of the nutritional liquid is 7-7.4.
NOVELTY - The system has multiple small generators (1) with small windmills mounted on a soft hollow insulating string (6), where one end of the string is connected with a hollow telescopic rod (9) and the other end is mounted with a hanger (10). A hollow fixing shaft (15) is mounted with a rain proof wind power spiral generator body (14). A top end of the hollow fixing shaft is mounted with a lightning rod (20), and a water electrolyzer (24) is connected with an oxygen storage tank (25) and a hydrogen storage tank (26).    USE - Hydrogen supply system for combining a long dragon windmill at a residence and a factory.    ADVANTAGE - The system is manufactured in a cost effective manner. The system ensures no pollution and flexible mounting.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic side view of a hydrogen supply system in a long dragon windmill.    Small generators (1)    Soft hollow insulating string (6)    Hollow telescopic rod (9)    Hanger (10)    Rain proof wind power spiral generator body (14)    Hollow fixing shaft (15)    Lightning rod (20)    Water electrolyzer (24)    Oxygen storage tank (25)    Hydrogen storage tank (26)
NOVELTY - Preparation of ethane involves using raw material storage tank, flow meter, primary sulfuric acid absorber, secondary sulfuric acid absorber, sodium hydroxide neutralizer, silica gel dryer, no.1 absorber, no.2 absorber, condenser, steel bottle and vacuum pump which are integrally assembled with each other through connection pipeline. The ethane is obtained by chemical absorption-adsorptive process.    USE - Preparation of ethane.
NOVELTY - Purification and preparation of n-butane is carried out using a left reflowing pump, a left reflowing tank, a left condenser, a raw material pump, a tower for removing butane, an intermediate reflowing pump, an intermediate reflowing tank, an intermediate condenser, a left tower for removing isobutane, a circulating pump, a right tower for removing isobutane, an isobutane reboiler, an n-butane tower, a right condenser, a right reflowing tank, a right reflowing pump, and an n-butane reboiler integrally connected through a connection pipeline.    USE - Purification and preparation of n-butane.    ADVANTAGE - The method enables simple purification and preparation of n-butane with high purity, without environmental pollution.
NOVELTY - Gasoline comprises (in wt.%): methanol (85-90), solvent oil (3-4), national standard gasoline (5-10) and additive (1-2). The additive comprises cetyl trimethyl sodium sulfonate (5-15), cetyl trimethyl calcium sulfonate (5-15), liquid naphthenic acid (5-10), methylal (15-25), nitromethane (5-10) and 3-8C monohydric alcohol (40-60).    USE - The gasoline is useful for vehicles.    ADVANTAGE - The gasoline has high proportion of methanol.
NOVELTY - An organic photoresist stripper composition contains nitrogen-containing compound (A) (I), ether-type compound (B) (II), nitrogen-containing compound (C) (III), compound (D) chosen from sugar, 3-10C alkane, cyclohexane, hydroxyl compound, aromatic hydroxyl compound, acetylene alcohol, carboxylic acid compound, carboxylic acid anhydride and triazole compound, and organic solvent (E).    USE - Organic photoresist stripper composition is used for manufacturing flat panel display and semiconductor device.    ADVANTAGE - The flat panel display using organic photoresist stripper composition has excellent corrosion resistance.    DETAILED DESCRIPTION - An organic photoresist stripper composition contains nitrogen-containing compound (A) of formula: (N(-R1)(-R2))n-R3-(R4-OH)m (I), ether-type compound (B) of formula: R8-O-R7-CO-N(-R5)-R6-OH (II), nitrogen-containing compound (C) of formula: N(-X)(-Y')-O-R9 (III), compound (D) chosen from sugar, 3-10C alkane, cyclohexane, hydroxyl compound, aromatic hydroxyl compound, acetylene alcohol, carboxylic acid compound, carboxylic acid anhydride and triazole compound, and organic solvent (E).    R1,R2=H, amino or optionally substituted linear or branched 1-10C hydrocarbyl;    R3=bond or linear, branched or cyclic 1-10C hydrocarbyl;    R4=linear, branched or cyclic 1-10C hydrocarbyl;    n,m=1-5;    R5,R6=H, 1-5C hydrocarbyl or linear or branched aromatic hydrocarbyl;    R7,R8=linear, branched or cyclic 1-5C hydrocarbyl;    R9,Y',X=H or linear, branched or cyclic 1-7C hydrocarbyl;and    or X+Y'=ring.
NOVELTY - The method involves fixing a hollow fiber membrane bundle within housing (100). Reaction gas is flown with a potting agent (310) in an inlet port, where hardness of another potting agent (330) is lower than the former potting agent. The former potting agent is coated in both end part of a hollow fiber membrane (200). Moisture content unreacting gas is ejected in a vent through another inlet port. Humidified reaction gas is ejected in another vent through the former inlet port. An intermediate layer (320) is formed between the potting agents.    USE - Method for manufacturing a humidifier of a fuel cell e.g. electrolyte fuel cell and polymer electrolyte fuel cell.    ADVANTAGE - The method enables solving conventional problems of the humidifier, and reducing damage of end part of the hollow fiber membrane due to rubbing.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a humidifier.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of a humidifier.    Housing (100)    Humidifier (101)    Hollow fiber membrane (200)    Potting agents (310, 330)    Intermediate layer (320)
NOVELTY - Incense or mosquito coil comprises (in wt.%): mugwort leaf powder (50-95) and Pyrethrum root, stem, leaf and flower or their extract (5-50).    USE - The incense or mosquito coil is useful for disinfecting air and expelling mosquitoes (claimed).    ADVANTAGE - The incense or mosquito coil causes no pollution to environment, soil and air, thus it is environmentally-friendly. The incense or mosquito coil is safe as it is prepared by using natural raw materials.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the above-cited incense or mosquito coil, which involves (a) uniformly mixing mugwort leaf powder and Pyrethrum root, stem, leaf and flower or their extract, and rolling the mixture into column with cotton paper to prepare incense, or (b) mixing mugwort leaf powder and Pyrethrum root, stem, leaf and flower or their extract with water and agitating into paste, using the existing apparatus for preparing mosquito coil, preparing into disc or club-shaped products, and then drying products.
NOVELTY - Method for chemically synthesizing cytarabine, involves reacting spongouridine with hexamethyldisilazane (HMDS) at 70-160 degrees C and at 5-20 kg pressure, cooling the reacted mixture, decompressing and concentrating the reacted mixture, recycling HMDS from the concentrate to obtain an intermediate product, dissolving the intermediate product in solvent, and cooling the mixture to obtain crude product of cytarabine.    USE - The method is useful for chemically synthesizing cytarabine used for preventing and treating cancer.    ADVANTAGE - The method enables synthesis of cytarabine economically under simple reaction conditions using easily available raw materials. The method is environmentally-friendly.
NOVELTY - The apparatus has production unit (400) that produces hydrogen using electricity generated by solar power generation module (100). The solar power generating module is arranged in the lower portion of the apparatus main portion. A propulsion device (200) moves the apparatus main portion comprising water for performing electrolysis. A storage unit (500) stores the produced hydrogen with liquefaction. The production unit, solar power generation module, propulsion device and storage unit are controlled by controller (800) corresponding to operation of the user.    USE - Hydrogen production apparatus.    ADVANTAGE - The amount of sunlight collected by the solar power generating module is improved. The energy generation and hydrogen production are improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of hydrogen production apparatus.    Solar power generation module (100)    Propulsion device (200)    Production unit (400)    Storage unit (500)    Controller (800)
NOVELTY - Landfill method for disposal of livestock flesh waste, involves forming filling hole at an inclination angle of 5% to the underground surface, placing waterproof vinyl sheet in the filling hole, placing rice straw mat on the surface of the vinyl sheet, adding livestock flesh on the rice straw, adding fermenting agent to the waste, covering the filling hole and fermenting the livestock flesh waste.    USE - The landfill method is useful for disposal of livestock flesh waste.    ADVANTAGE - The method reduces the bad odor of livestock flesh waste and is environmentally-friendly.
NOVELTY - Human and animal excreta processing involves using a hydrophobic chemical compound. Toilet discharge material is processed through sewer line to remove water from the discharge material. The material is neutralized with aqueous chemical in a device, where the solid excreta is dissolved, stabilized and separated from the waste material in decanting equipment. The excreta are mixed with powdered charcoal to obtain briquettes excreta, where hydrophobic chemical compound is separated from the mixture.    USE - Method for processing excreta of human and animals for preparing liquid/solid fertilizer and for preparing briquettes (claimed) used as an energy product in industry.    ADVANTAGE - The excreta processing method is eco-friendly and economic, and does not utilize water for sewage material treatment.    DETAILED DESCRIPTION - Human and animal excreta processing involves using a hydrophobic chemical compound. Toilet discharge material is processed through sewer line to remove water from the discharge material. The material is neutralized with aqueous chemical in a device, where the solid excreta is dissolved, stabilized and separated from the waste material in decanting equipment. The excreta are mixed with powdered charcoal to obtain briquettes excreta, where hydrophobic chemical compound is separated from the mixture. The toilet discharge material is reused to obtain briquettes excreta. Chemical compounds and other constituents of urine are transferred to a reservoir, which is connected by tubes. The obtained product is utilized as a liquid fertilizer or mixed with magnesium oxide or other compounds to obtain fertilizer powder. An INDEPENDENT CLAIM is also included for equipment for processing excreta, which comprises two reservoirs, tubes, electric pump and solenoid valve.
NOVELTY - An organic material chosen from biomass and waste pulp is heated in a heating tank containing oil with defoaming agent. The oil is removed from the organic material discharged from the heating tank. The de-oiled organic material is molded to obtain solid fuel.    USE - Preparation of solid fuel.    ADVANTAGE - The method effectively provides solid fuel with high calorific value.
NOVELTY - A mesoporous nickel-alumina composite catalyst is formed by hydration and thermal processing of mixture containing a block copolymer, an aluminum precursor and a nickel precursor. The atomic ratio of nickel and aluminum is 0.01-1. The catalyst has average pore size of 2-10 nm. The catalyst carries out steam-reforming reaction of liquefied natural gas, and hydrogen is produced.    USE - Mesoporous nickel-alumina composite catalyst is used for producing hydrogen.    ADVANTAGE - The mesoporous nickel-alumina composite catalyst has high catalytic activity and stability, and enables production of hydrogen of high concentration at high yield.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of mesoporous nickel-alumina composite catalyst; and    (2) manufacture of hydrogen.
NOVELTY - Preparing microorganism-decomposing agent by using livestock excrement, involves inoculating Saccharomyces cerevisiae AS1.2414 and S.cerevisiae AS1.1854 into a culture medium containing carbon source, nitrogen source and nutritious substances for fermentation, inoculating Rhodopseudomonas palustris AS1.2349 into culture medium containing nutritious substances for fermentation, mixing fermented liquid of S.cerevisiae and fermented liquid of R.palustris, and absorbing mixture using rice bran and bran.    USE - The method is useful for preparing microorganism-decomposing agent for producing microbial organic fertilizer.    ADVANTAGE - The method improves production of fertilizer with high quality, reduces composting time and enhances compost maturity.    DETAILED DESCRIPTION - Method of preparing microorganism-decomposing agent by using livestock excrement, involves inoculating Saccharomyces cerevisiae AS1.2414 and S.cerevisiae AS1.1854 into a culture medium containing carbon source, nitrogen source and nutritious substances for fermentation, inoculating Rhodopseudomonas palustris AS1.2349 into culture medium containing nutritious substances for fermentation, mixing fermented liquid of S.cerevisiae and fermented liquid of R.palustris, and using mixture of rice bran and bran as carrier to absorb the mixed fermented liquid to obtain solid decomposing agent.
NOVELTY - Production of medical raw material 2,2'-dithiobis(benzothiazole) (DM) comprises adding water and rubber accelerating agent (M) into reaction kettle, adding into sodium hydroxide, adding into M sodium salt liquid, adding into solvent; and at 40-70 degrees C, dripping mixed oxidizing agent solution of sulfuric acid and hydrogen peroxide into solution, controlling flowing rate to 50-110 ml/minute, extracting and filtering, washing with water, filtering and drying to obtain medical raw material DM product.    USE - Method for producing medical raw material 2,2'-dithiobis(benzothiazole) (DM) (claimed).    ADVANTAGE - The method utilizes sodium sulfate in water which can be recycled, water and isopropanol can be recycled, is environment-friendly; and produces 99% pure medical raw material with melting point of more than 178 degrees C.    DETAILED DESCRIPTION - Production of medical raw material 2,2'-dithiobis(benzothiazole) (DM) comprises adding water and rubber accelerating agent (M) at weight ratio of 1-15:1 into reaction kettle, adding into sodium hydroxide at mol ratio of sodium hydroxide to M of 1:1-3, adding into M sodium salt liquid generated in reaction into oxidizing kettle, adding into solvent comprising water, ethanol, methanol, isopropanol, acetone, aniline or toluene, at volume ratio of solvent to M sodium salt liquid of 1 1-10; and at 40-70 degrees C, dripping mixed oxidizing agent solution of sulfuric acid and hydrogen peroxide at weight ratio of 1:1-12 into solution, controlling flowing rate to 50-110 ml/minute, stopping dripping mixed oxidizing agent until pH 4-8, extracting and filtering, washing with water, filtering and drying to obtain medical raw material DM product at more than 95% yield.
NOVELTY - Method (A) of processing a biomass fuel compact comprises: combining a composition of combustible biomass materials; comminuting the composition of biomass materials; adding an adhesive to the biomass materials to form a composite biomass, the adhesive comprising a starch and a hydroxide; and forming the composite biomass into a shapeform.    USE - The methods are useful for processing a biomass fuel compact (claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a method (B) of processing a biomass fuel compact comprising: combining a composition of combustible biomass materials; adding an adhesive to the biomass materials to form a composite biomass, the adhesive comprising a starch and a hydroxide; and forming the composite biomass into a shapeform; and    (2) a method (C) of processing a biomass fuel compact comprising: combining a composition of combustible biomass materials; comminuting the composition of biomass materials; drying the comminuted composition of biomass materials; adding an adhesive to the biomass materials, the adhesive comprising a starch and a hydroxide; adding a silicate to the composition of biomass materials; adding a viscosity agent to the composition of biomass materials to form a composite biomass; forming the composite biomass into a shapeform; and partitioning the composite biomass shapeform into individual pieces that are compatible with existing power-plants, where the processing is performed at lower temperatures such that an endothermic reaction of the biomass materials and adhesive results.
NOVELTY - A drying barn (1) is located at the bottom of a carbonizing pool (2), and is sealed at the periphery. Two opening doors are arranged on the positive surface and the opposite surface of the drying barn. Carbon discharging funnels directly connected to the drying barn are made of double steel plates and are disposed at a 45-degree angle. A wind blowing device (6), a cooling device (7) and a spiral conveyer (8) are arranged on one side of the carbon discharging funnels. Discharging conveying belts (9) are arranged under the spiral conveyer.    USE - Straw continuous carbonizing furnace.    ADVANTAGE - Provides novel structure having strong practical applicability and energy-saving effect. Biomass material for making carbon comprises agricultural waste such as straw or shell, branches and weeds.    DETAILED DESCRIPTION - The carbonizing pool is built from fire-proof bricks, is open at the top, and is provided with venting holes on the periphery. A feeding belt conveyer (3), a baffle plate (4) and a suction hole are provided on the top and bottom sides, and combustible gas outlets (5) are provided on the four walls of the square pool. A thermodetector is provided on the side wall of the carbonizing pool, and the two parallel carbon discharging funnels are disposed at the bottom of the carbonizing pool.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the straw continuous carbonizing furnace.    Drying barn (1)    Carbonizing pool (2)    Feeding belt conveyer (3)    Baffle plate (4)    Combustible gas outlet (5)    Wind blowing device (6)    Cooling device (7)    Spiral conveyer (8)    Discharging conveying belt (9)
NOVELTY - Endothermic reaction of carbon dioxide gas contained in hot waste gas generated from boiler installed in flue of metallurgical furnace, and a reducing agent is carried out, and carburation is performed with heat energy of waste gas. Thus, sensible heat is recovered from hot waste gas.    USE - Recovery of sensible heat of waste gas discharged from metallurgical furnace e.g. converter (claimed), fusion reduction furnace and electric furnace, and iron manufacturing installation e.g. iron mill.    ADVANTAGE - The carbon dioxide gas reforming reaction is efficiently performed without depositing carbon and non-burning component in waste gas processing plant. The discharge reduction of carbon dioxide gas is enabled with carburation of waste gas, and waste gas is effectively cooled. The sensible heat of waste gas is efficiently and economically recovered.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for cooling method of waste gas.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of converter waste gas recovery installation. (Drawing includes non-English language text)    Converter (1)    Skirt (2)    Lower wood (3a)    Top wood (3b)    Primary dust collector (5)    Gas analyzer (6)
NOVELTY - Catalyst comprised of an interstitial metal hydride, is new.    USE - The catalyst is useful for upgrading a hydrocarbon feed stream comprising a biofuel (all claimed).    ADVANTAGE - The catalysts are resistant to the effects of oxidation and can operate efficiently and effectively under hydroprocessing conditions even after exposure to oxidizing atmospheres, thus improving the ease of manufacturing and handling.    DETAILED DESCRIPTION - Catalyst comprised of an interstitial metal hydride of formula (A1-xB1xT((1-y) plus minus d1)C(y plus minus d2)), is new.    A = Zr;    B1 = Ti (preferred) or Hf;    T = Ni;    C = Mn, Fe (both preferred), Cr, Co, or Cu;    x, y = 0.0-1; and    d1, d2 = 0.00-0.2.    An INDEPENDENT CLAIM is included for a process for upgrading a hydrocarbon feed stream comprising contacting a hydrocarbon feed stream with the catalyst in the presence of hydrogen at process reaction conditions of at least 200 degrees C and at least 400 psig, and obtaining an upgraded reaction product stream.
NOVELTY - Catalyst comprised of an interstitial metal hydride is new.    USE - The catalyst is useful for upgrading a hydrocarbon feed stream comprising a biofuel (all claimed).    ADVANTAGE - The catalyst enables improved product conversion, and sulfur reduction in hydrocarbon feed streams.    DETAILED DESCRIPTION - Catalyst comprised of an interstitial metal hydride of formula (A1-xB1xT((2-y) plus minus d1)C(y plus minus d2)), is new.    A = Nd or Zr;    B1 = Ti, Hf, La, Ce, Pr, Gd, Dy, Er, or Ho;    T = Fe or V (preferred);    C = Mn, Fe, Cr, Co, Ni or Cu;    x = 0.0-1, preferably 0.2-0.6;    y = 0.0-0.2; and    d1, d2 = 0.00-0.2.    An INDEPENDENT CLAIM is included for a process for upgrading a hydrocarbon feed stream comprising contacting a hydrocarbon feed stream with the catalyst in the presence of hydrogen at process reaction conditions of at least 200 degrees C and at least 400 psig, and obtaining an upgraded reaction product stream.
NOVELTY - Plant comprises at least one closed rectangular container (1, 2) with an inlet for the untreated residue, an outlet for the treated residue with the means for discharge of biogas, means for heating the residue, means for mixing of the residue in the container, and a power house (3), where a wall of the power house is formed by a wall of the container.    USE - The plant is useful for anaerobic stabilization of pumpable organic residues.    ADVANTAGE - The plant: has a simple design, thus it is easy to manufacture; can be arranged in combination with other buildings of waste-water treatment plant, thus it is space-saving; has reduced heat dissipation, and a stable process control; carries our degradation of organic matter as a single-stage process, and thus it produces higher yield of biogas.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the ground plan of the plant with two containers.    Containers (1, 2)    Power house (3)    Common wall (4)    Slope elements (5)    Agitator (21)
NOVELTY - The sensor (1) has electrical elements spaced at distance from each other and provided with a gas-sensitive porous metal oxide (4). The electrical elements heat the metal oxide and measure conductance of the metal oxide between the electrical elements, and are spatially embedded at the sintered metal oxide. The electrical elements are provided with an electrical energy for heating the metal oxide, and voltage and/or current between the electrical elements is measured. The voltage is applied between connection parts (5, 6), and a current flow is determined between the connection parts.    USE - Heated gas sensor for detecting and/or determining concentration of a gaseous material. Uses include but are not limited to methane, ethane, propane, carbon-di-oxide, or hydrogen.    ADVANTAGE - The sensor is manufactured in a simple and cost effective manner with increased sensitivity and stability under an adverse operating condition.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for manufacturing a heated gas sensor for detecting and/or determining concentration of gaseous material.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a heated gas sensor.    Heated gas sensor (1)    Gas-sensitive porous metal oxide (4)    Connection parts (5, 6)
NOVELTY - A manufacturing apparatus of biomass fuel comprises structure which extracts essential oil from trees which becomes biomass fuel and processes dreg material into block-shaped wooden block fuel.    USE - A manufacturing apparatus of biomass fuel.    ADVANTAGE - The apparatus utilizes forest resources effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of manufacturing apparatus of biomass fuel. (Drawing includes non-English language text).    Heating still (6)    Steam generation pot (7)    Steam cooling device (8)    Steam pipe (9A, 9B)    Pressurization machine (10)
NOVELTY - Producing a biomass-derived pyrolysis oil comprises exposing biomass-derived pyrolysis oil to a reducing gas under pressure, and heating the biomass-derived pyrolysis oil to a temperature of 40-85 degrees C for a time sufficient to stabilize the pyrolysis oil.    USE - The method is useful for producing biomass-derived pyrolysis oil.    ADVANTAGE - The method provides biomass-derived pyrolysis oil with increased phase stability and low viscosity.
NOVELTY - Invention relates to ecological biotechnology and may be used for optimum use of biogas in effluents treatment. Proposed method consists in that biogas is treated by solution of monoethanolamine which absorbs carbon dioxide. Obtained monoethalamine solution is regenerated whereat, on its heating and pressure reduction, carbon dioxide is desorbed. After cooling, carbon dioxide is biologically deodorised and rinsed by oxidiser, while methane extracted from biogas is recovered. Carbon dioxide is biologically deodorised in vortex mass exchange apparatus which comprises cylindrical housing with holes, gas and fluid feed and discharge branch pipes, distribution disk and tangential slits, and adjusting barrel with opening that revolves about the axis. Biological deodorisation is performed by continuous sprinkling of carbon dioxide flow by active sludge produced in secondary precipitation during effluents cleaning, which features density varying from 20 to 45 n3/m2.h and hydraulic drag in gas phase of 400 Pa.    USE - Process engineering.    ADVANTAGE - Efficient deodorisation of carbon dioxide in production of "dry ice" and carbonised drinks. 1 dwg, 1 ex
NOVELTY - Electrolysis unit includes anode and cathode chambers located in common housing and having monopolar electrodes - anode and cathode, which are connected to constant voltage source; at that, anode chamber is separated from cathode one with electrically insulating partition which does not touch the bottom of common housing and on which UV radiation source is installed. Anode and cathode chambers are connected to deionisation chamber by means of pipelines, as well as to dissociation chamber through ion separator with electric gradient field and through intakes of waste water solution of electrolyte from upper layers of electrolyte. In anode and cathode chambers between anodes and cathodes there installed are additional electrodes connected to each other by common conductor which connects plus and minus outputs of both dc power supply units, the other ends of which are connected to anode and cathode respectively; at that, one power supply unit supplies stabilised constant voltage which is minimum required for oxygen separation on the anode, and the other one supplies stabilised constant voltage which is minimum required for hydrogen separation on cathode.    USE - Electricity.    ADVANTAGE - Reducing the costs for electric power supply, eliminating irrational expenses of electric and chemical energy, and providing acceleration of electrolysis processes. 2 cl, 3 dwg
NOVELTY - The boiler has a combustion system provided with an anaerobic combustion chamber. A boiling combustion chamber is arranged at a lower part of the boiler. The combustion chambers are isolated by a fireproof material and reserved with a flame passage. A feeding system is provided with a transmission belt, a hopper and a spiral propeller that are connected together, where the propeller is located below the hopper.    USE - Biomass-fired solid molding fuel boiler.    ADVANTAGE - The boiler is provided with biomass-fired solid molding fuel as raw material to generate power, where the fuel prevents generation of harmful gases or emission of harmful substances, thus protecting the environment from pollution. The boiler reduces the required amount of non-renewable resources such as petroleum and coal. The boiler enables safe and efficient garbage processing and heating.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass-fired solid molding fuel boiler.
NOVELTY - Bioenergetic complex comprises digester with coil, heat insulation, auger intermixing device, loading and unloading branch pipes, conduits of biogas supply, gas holder, and heliocollector with tank-storage battery, where the complex has boiler AoGV for biomass preheating, wind-power plant with thermal electrical heater built into tank-storage battery, which allows to maintain necessary temperature in the period of absence of solar radiation, and a circulating pump, built into conduit of reverse supply of heat-transfer agent, which increases work effectiveness.    USE - The bioenergetic complex is useful for industrial applications.
NOVELTY - The method involves using hot air from primary wind outlet of air pre-heater as main fluidizing wind. The smoke gas from tail portion of boiler is used as auxiliary fluidizing wind. The gases are mixed and conveyed to gasification furnace (7) on condition that total wind volume for fluidization. A straw pack is dispersed by straw pack dispersing device (8) and conveyed to gasification furnace through belt drying conveyor (9) for finishing gasification reaction. The fuel gas is conveyed to furnace wall of boiler for reducing nitrogen oxide (NOx) circulation process.    USE - Method for integrated straw gasification power generation in supercritical coal fired generating unit.    ADVANTAGE - The generating unit is simply modified to effectively integrate biomass gasification furnace for gasifying and reburning the biomass to generate power such that the defect on direct mixed combustion of biomass is reduced and influence of biomass ash to coal ash is avoided. The auger feeding device is not damaged easily such that highly-efficiency utilization of biomass is realized and emission of pollutant of coal fired power plant is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating method for integrated straw gasification power generation.    Cyclone separator (5)    Flying ash hot auger (6)    Gasification furnace (7)    Straw pack dispersing device (8)    Belt drying conveyor (9)
NOVELTY - The steam power unit has a stand, a gasifier, a combustor, a steam generator, a steam turbine and a transmission, where the gasifier is a straw gasifier and the combustor is a gas cooker.    USE - Steam power unit.    ADVANTAGE - The steam power unit is provided with the straw gasifier that can convert plant raw materials into fuel gas instead of petroleum products, so that the steam power unit has energy-saving and waste-using functions, and is used to develop a new energy source.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a steam power unit.
NOVELTY - The furnace has a combustion chamber (2) whose wall is provided with a gas inlet (9), and a gas discharging opening (10) connected with a gas purifier and a chimney (6) via a three-way pipe. An ash outlet (7) is formed at a lower part of a furnace body (1), and a closed door (8) is arranged at the ash outlet. An evaporation pipe is arranged in the gas purifier, and a hole is formed on an upper end of the evaporation pipe. A cooler is provided with a cooling water discharging opening, and a U-shaped pipeline is arranged in the cooler. An end of the pipeline is connected with the gas purifier.    USE - Straw gasification combustion furnace.    ADVANTAGE - The furnace is environment friendly, has high combustion efficiency, and utilizes a straw that can be sufficiently burned.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a straw gasification combustion furnace.    Furnace body (1)    Combustion chamber (2)    Chimney (6)    Ash outlet (7)    Closed door (8)    Gas inlet (9)    Gas discharging opening (10)
NOVELTY - The furnace has an outer furnace wall provided with an air outlet pipe (14) connected with a gas output pipe. A feeding device unit and a hearth upper port sealing device unit are arranged on a top part of the furnace body. The inner and outer furnace walls are provided with an igniting device unit (12) with a sealing cover and a fire observing hole (11) passing through the hearth. Dry and wet slag discharging device units are arranged on a lower part of the furnace body. Multiple thermocouples (6) are arranged on the inner and outer furnace walls.    USE - Rubbish gasifying and purifying reaction furnace.    ADVANTAGE - The furnace processes rubbish so as to convert waste material into useful product. The furnace is simple in structure and convenient to operate, ensures high efficiency and environmental protection functions, and saves energy consumption.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a rubbish gasifying and purifying reaction furnace.    Thermocouples (6)    Fire observing hole (11)    Igniting device unit (12)    Air outlet pipe (14)    Slag discharging water tank (15)
NOVELTY - The device has a gasification furnace whose upper part is connected with a filter system through a gas pipeline. A slag discharging opening is formed at a lower part of the gasification furnace. A filter is connected with the gasification furnace through the gas pipeline. The filter is connected with a water tank through the gas pipeline. The filter system and the filter are connected with each other, where the filter is connected with the gas pipeline for conveying gas. A water gauge measures a water level in the gasification furnace.    USE - Biomass gasification device.    ADVANTAGE - The device is environment-friendly, and the combustible gas generated by the gasification furnace is purified through the filter system, so as to remove dust and tar.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass gasification device.
NOVELTY - A biomass feeding device comprises driver mechanism, material cabin, blade, feeding screw rod and pneumatic feeding pipe. The driver mechanism includes motor, huge flywheel, small flywheel and belt. The pneumatic feeding pipe is placed at the bottom of material cabin. The feeding screw rod is in the center of material cabin, where upper end is coaxially mounted with the huge flywheel, and lower end extends into the pneumatic feeding pipe via the conical outlet. The blade is placed at the lower part inside the material cabin.    USE - A biomass feeding device for fluidized bed.    ADVANTAGE - The device can precisely control the biomass feeding; thus providing more stable feeding process, preventing advanced coking of the material, and increasing reaction working condition of fluidized bed as well as the output rate of the reaction product.    DETAILED DESCRIPTION - Biomass feeding device comprises driver mechanism, material cabin, blade, feeding screw rod and pneumatic feeding pipe. The driver mechanism includes motor, huge flywheel, small flywheel and belt. The motor is placed outside the upper part of material cabin, where small flywheel is coaxially mounted with the output end, and small flywheel is linked with the huge flywheel. The pneumatic feeding pipe is placed at the bottom of material cabin. The feeding screw rod is in the center of material cabin, where upper end is coaxially mounted with the huge flywheel, and lower end extends into the pneumatic feeding pipe via the conical outlet. The blade is placed at the lower part inside the material cabin, and is coaxially mounted with the feeding screw rod.    DESCRIPTION OF DRAWING(S) - The drawing is a perspective view of biomass feeding device.
NOVELTY - A biomass spiral pyrolysis involves flow-splitting biomass material with high-temperature flue gas by entering flue gas branch warehouse chamber from lower part of pyrolytic reactor, and pyrolyzing to obtain biomass carbon and fuel. The entering directions of biomass material and flue gas are opposite.    USE - A biomass spiral pyrolysis.    ADVANTAGE - The method is simple and practical; and has good heat transfer effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a pyrolytic device.    DESCRIPTION OF DRAWING(S) - The drawing is a sectional view of pyrolytic device. Drawing includes non-English language text.
NOVELTY - The combustor has a combustion chamber which is connected with a feeding pipe and an air outlet pipe. An axial inner wall of feeding pipe is tangent to inner wall of cross section of combustion chamber. The wind is sent to combustion chamber with biomass from tangent direction of feeding pipe. The ash is separated by centrifugal force of cyclone to obtain clean biomass gas.    USE - Cyclone dust-separating biomass gasifying combustor.    ADVANTAGE - The dust separating effect can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the cyclone dust separating biomass gasifying chamber.
NOVELTY - The device has a heat accumulating chamber that is provided with the heat accumulating portion processing holes among which the nozzle holes are arranged. The ceramic heat accumulating portions are arranged in the heat accumulating portion processing holes, and a combustor main portion is arranged in the nozzle hole. The combustion-supporting medium and biomass combustible air are combusted at the end portion of device to form flame releasing heat to heat the other mediums.    USE - Air heat accumulating type combustion device for biomass air heating system (claimed).    ADVANTAGE - The high-temperature combustion product and the low-temperature combustion-supporting medium flow pass through the heat accumulating portions to indirectly exchange heat so that heat of fuel gas is effectively utilized. The combustion stability of fuel gas is ensured.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biomass air heating system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of combustion device.
NOVELTY - Preparing (m1) a platinum-cobalt (PtCo) nanocube catalyst involves dissolving a platinum precursor, a cobalt precursor, a surface stabilizer and a reducing agent in a solvent to prepare a solution; heating the solution under an inert gas atmosphere; maintaining the temperature of the solution to obtain PtCo alloy nanocubes; adsorbing the PtCo alloy nanocubes on a carbon support to obtain a catalyst; and optionally removing the surface stabilizer from the catalyst.    USE - For preparing a platinum-cobalt (PtCo) nanocube catalyst which is useful in fuel cell (claimed).    ADVANTAGE - The method produces PtCo nanocube catalyst with superior surface characteristics and activity since the cubic structure is suitably maintained without high-temperature heat treatment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a fuel cell comprising the PtCo nanocube catalyst prepared by the method (m1).
NOVELTY - The apparatus has one or more electrolysis cells in which water is dissociated into constituent gases. A quantity of electrolyte including water to-be-dissociated is contained in the electrolysis cell. An electrical unit is provided to conduct electrical energy from external source to multiple interleaved electrodes of staggered polarity through electrical bussing system such that electrode (4) of neutral charge precedes and follows every anode and cathode of electrode stack. A conduit is provided to exhaust dissociated gases from electrolysis cell.    USE - Electrolytic apparatus for separating water from constituent gases such as hydrogen and oxygen gases.    ADVANTAGE - By using the apparatus, dissociated gases can be effectively produced and maintenance requirement is minimized.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for separating water from constituent gases.    DESCRIPTION OF DRAWING(S) - The drawing shows an exploded perspective view of interface between electrode plates and four electric conductor busses.    Electrode (4)    Electric busses (6)    Aperture (101)    Grooves (102)    Washer (103)
NOVELTY - The apparatus has feeder module (106) that conveys stream of liquid alkali metal (102) comprising molten sodium, to a titration module (108) that contains water (114). The liquid alkali metal and water interacts in the titration module. A main electrode electrically communicates with the stream of liquid alkali metal and an auxiliary electrode electrically communicates with water in the reaction chamber. A terminal is coupled to the electrodes, and connected with hydrogen fuel cell (128) receiving hydrogen (124) generated in the titration module.    USE - Apparatus for producing electric energy.    ADVANTAGE - The hydrogen for fuel cell can be generated without using large amount of energy during the process of generating the hydrogen.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) system for producing energy; and    (2) method for producing energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the system for producing electric energy.    System for producing electric energy (100)    Alkali metal (102)    Feeder module (106)    Titration module (108)    Water (114)
NOVELTY - The system for chemical looping combustion, comprises a molten liquid metal oxide, a fuel source, and a reaction chamber. The molten liquid metal oxide and the fuel source react in the reaction chamber to generate carbon dioxide and reduced species. The molten metal oxide is contained within a melt of other molten species including glass melt and/or ionic melt. The fuel source is renewable from biomass, wood, cellulose, corn stover, waste paper and/or municipal solid waste. The reaction chamber is in direct thermal contact with a closed loop system that contains a heat transfer fluid.    USE - The system is useful for chemical looping combustion of hydrocarbons.    ADVANTAGE - The system ensures economical and energy efficient chemical looping combustion of hydrocarbons without an air separation unit, thermal regeneration step and the need to separate carbon dioxide from hydrogen, mitigates the movement of the metal/metal oxide at very high temperatures, and avoids the mechanical and chemical degradation of the solid oxygen carrier with each cycle.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a process for chemical looping combustion; and    (2) a chemical looping combustion catalyst.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic view of two operating states of chemical looping combustion system.
NOVELTY - The plant for treating vegetable oils (2) for fuel capacity for all conventional motors and diesel power units, is claimed. The pure vegetable oil in the plant is treated as long as with flue gas until changing the nature and the flash point. The flue gas is brought over the flue gas supply in the lower chamber (9) of the plant and passes through the upper chamber by the flue gas outlet (6). The vegetable oil is pumped from the lower chamber by means of a pump (5) into a distributor tube (4) of the upper chamber and again runs over guide plates into the lower chamber of the plant.    USE - Plant for treating vegetable oils useful for the fuel capacity for all conventional motors and diesel power units.    ADVANTAGE - The plant can be economically produced for treating vegetable oils.    DESCRIPTION OF DRAWING(S) - The figure shows a cross-section view of a plant for treating vegetable oils.    Vegetable oils (2)    Distributor tube (4)    Pump (5)    Flue gas outlet (6)    Lower chamber. (9)
NOVELTY - Increasing performance potential of a biogas plant, comprises: introducing hydrogen into a methane fermenter (8) or a post-fermentation system, in which hydrogen is generated by electrolysis of water; feeding generated hydrogen into a hydrogen-metal hydride storage (2) in an air-tight container (3) under a pressure; storing hydrogen atoms in a crystalline metal lattice of the storage; and releasing the atomic hydrogen from an output side of the storage via an anti-biofilm-membrane on a biomass, preferably methane bacteria, which is made to respire in carbon dioxide to form methane.    USE - The method is useful for increasing performance potential of a biogas plant.    ADVANTAGE - The method: allows direct introduction of separately produced hydrogen into the methane fermenter or the post-fermentation system without forming bubbles, where the methane bacteria present in the fermenter absorbs hydrogen to a maximum extent, and thus it increases the methane content and the methane rate steadily during the methane production; does not require a separate hydrogen fermenter, and thus it is cost-efficient, and has low energy consumption; and uses the device, which exhibits low-loss and sufficient supply of hydrogen into methane fermenter or the post-fermentation system.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for performing the method, comprising the methane fermenter or the post-fermentation system, a hydrogen-source, preferably electrolyzer (1), the hydrogen-metal hydride storage in the air-tight container, a gas-dosing device and a control device (5), where the storage is in an active contact with the biomass on the outer side via a hydrogen-permeable biofilm-inhibiting membrane.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the device for performing the method.    Electrolyzer (1)    Hydrogen-metal hydride storage (2)    Air-tight container (3)    Control device (5)    Methane fermenter (8)
NOVELTY - Water-in-oil type emulsification skin cosmetics comprise isostearic acid glycerol (A), aqueous component (B), oil-based component (C) containing less than or equal to 20 carbon containing isoparaffin, and salt (D) chosen from alpha -amino-acid derivative and its salt and beta -amino acid derivative and its salt in which inner water phase ratio obtained by removing mass of (B) by mass of (B) and (C) is greater than or equal to 68%, amount of monoisostearic acid glycerol in (A) is greater than or equal to 85 mass% and amount of (D) is 0.001-5 mass%.    USE - Water-in-oil type emulsification skin cosmetics e.g. cosmetic liquid, milky lotion, cream, pack and ointment for dermatologies. Can also be used for pharmaceutical and quasi-drug.    ADVANTAGE - The cosmetics have high wrinkle improvement effect, favorable emulsion stability and fresh usability.
NOVELTY - The cell (100) has container (110) that accommodates semiconductor electrode (120), counter electrode (130), and the electrolyte solution (140). The band edge levels of conduction band and valence band in n-type semiconductor layer (123) are higher than band edge levels of conduction band and valence band in n-type semiconductor layer (122). The Fermi level of n-type semiconductor layer (122) is higher than that of n-type semiconductor layer (123). The Fermi level of conductor (121) is higher than that of n-type semiconductor layer (122).    USE - Photo-electrochemical cell for energy system (claimed) used for domestic application.    ADVANTAGE - The quantum efficiency of hydrogen generation reaction by irradiation of light can be improved.    DETAILED DESCRIPTION - The cell has electrolyte solution whose pH value is based on vacuum level when temperature is 25 degrees C. The Fermi level of one n-type semiconductor layer is more than -4.44eV and band edge level of valance band in other semiconductor layer is less than -5.67eV. One semiconductor layer is made of titanium oxide and other semiconductor layer is made of oxide nitride and oxy-nitride. A hydrogen reservoir is connected with photo-electrochemical cell using piping. A fuel cell is connected with hydrogen reservoir using other piping. An INDEPENDENT CLAIM is included for energy system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the photo-electrochemical cell.    Photo-electrochemical cell (100)    Container (110)    Semiconductor electrode (120)    Conductor (121)    N-type semiconductor layers (122,123)    Counter electrode (130)    Electrolyte solution (140)
NOVELTY - Method of manufacturing fatty acid ester, involves reacting fats, oil and monohydric alcohol as raw material with water in presence of calcium oxide (1-14 mol) as catalyst.    USE - The method is useful for manufacturing fatty acid ester which is used for manufacturing fuel e.g. biodiesel.    ADVANTAGE - The method activates calcium oxide rapidly and easily, and enables preparation of fuel inexpensively.
NOVELTY - The furnace has a nozzle that is arranged at an upper portion of a furnace main portion, and connected with an inner surface of furnace main portion. A catalyzing device is made from dolomite clinker, and arranged in the furnace main portion.    USE - Biomass solid fuel furnace.    ADVANTAGE - Since the catalyzing device is arranged in furnace main portion, the oil tar in the gas is well decomposed, the number of pyrolyzation portion and space requirement are reduced. Thus the production efficiency is improved, production cost is reduced, and potential safety hazard is avoided.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass solid fuel furnace.
NOVELTY - Combined rural sewage water treatment comprises performing a high-efficiency anaerobic treatment on the wastewater, pretreating wastewater in grit chamber (2) via grid well (1), subjecting to high-efficiency anaerobic reaction treatment in high-efficiency anaerobic pond (3), performing a multi-filler biofiltration treatment, and cleaning the artificial wetland.    USE - Method of combined rural sewage water treatment (claimed).    ADVANTAGE - The wastewater after being processed has removal rate of 80-85% chemical oxygen demand (CODcr), 90-95% biological oxygen demand (BOD5) and 70-80% ammonia-nitrogen (NH3-N).    DETAILED DESCRIPTION - Combined rural sewage water treatment comprises:    (A) pretreating wastewater in grit chamber (2) via grid well (1), subjecting to high-efficiency anaerobic reaction treatment in high-efficiency anaerobic pond (3), processing decomposition, hydrolysis and acidification of hydrolysis acidification bacteria in high-efficiency anaerobic reactor, and converting into methane and carbon dioxide by methane generating bacteria; entering wastewater to multi-filler biological trickling filter (4) to be treated via spraying system under lifting action of pump (7), with biological fillers in the pond; and entering wastewater after multi-filler biofiltration treatment to secondary settling pond (5) such that the suspended matters, shedding biomembranes and zoogloea substances are removed to obtain purified water, and purifying purified water in an artificial wetland.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the combined rural sewage water treatment. (Drawing includes non-English language texts).    Grid well (1)    Grit chamber (2)    High-efficiency anaerobic pond (3)    Multi-filler biological trickling filter (4)    Secondary settling pond (5)    Lifting action of pump (7)
NOVELTY - Preparing a mixed salt of glucosamine sulfate and an alkali metal chloride, involves (A) : suspending glucosamine hydrochloride in a nonaqueous solvent; adding to it a solution of a basic alkali metal salt in water; and adding to it a solution of an alkali metal hydrogen sulfate in water, thus the mixed salt is obtained.    USE - For forming mixed salt of glucosamine sulfate and alkali metal chloride (claimed).    ADVANTAGE - The process is very easy and cost efficient and thus in particular usable for large scale industrial production. The process allows very high yields of more than 90%; and avoids the use of toxic chemicals such as triethyl amine, and also avoids the use of a water removal step such as freeze drying steps, which in general are very costly. According to the present process, exposure of the glucosamine base to extreme pH conditions is avoided by adding a basic alkali metal salt prior to the addition of the alkali metal hydrogen sulfate solution. Thus, the formation of degradation products is vastly decreased.
NOVELTY - Preparing celecoxib polymorphic Form III, comprises: (a) providing a solution of celecoxib in a ketone solvent; (b) heating the solution at a temperature of above 40 degrees C to produce a hot solution; (c) combining the hot solution with water to form a slurry; and (d) recovering the celecoxib polymorphic Form III from the slurry, where the polymorphic Form III of celecoxib is characterized by (i) a powder X-ray diffraction pattern, and an infrared (IR) spectrum as given in the specification.    USE - The process is useful for preparing celecoxib polymorphic Form III for the treatment and/or prevention of disorders or diseases of animals (including humans) mediated at least in part by the cyclooxygenase-2 prostaglandin synthesis enzyme, e.g. painful inflammatory conditions. No biological data given.    ADVANTAGE - The improved, commercially viable, consistently reproducible and environmentally friendly process provides thermodynamically most stable crystalline celecoxib polymorphic Form III having an improved purity of greater than 99.9% as measured by HPLC, and enhanced bulk, flow properties, and compression characteristics in the preparation of tablets and capsules.
NOVELTY - Process (P1) of recrystallization of laquinimod sodium comprises: (a) dissolving laquinimod sodium in water to form an aqueous solution; (b) concentrating the aqueous solution to form a concentrated solution; (c) adding a water-miscible anti-solvent to the concentrated solution to form laquinimod sodium crystals; and (d) isolating the laquinimod sodium crystals.    USE - The process is useful for recrystallization of laquinimod sodium (claimed), which is useful to treat acute experimental autoimmune encephalomyelitis. No biological data given.    ADVANTAGE - The process: is industrially reproducible and provides laquinimod sodium crystals with high yield, high purity, improved crystalline characteristics, increased particle size and higher density; and utilizes water as the primary solvent, thus environmentally friendly.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) laquinimod sodium prepared by the process (P1); and    (2) a process (P2) for making a pharmaceutical composition comprising laquinimod sodium, comprising: obtaining a batch of laquinimod sodium; determining whether insoluble matter is present in the batch by mixing a sample from the batch in deionized water at room temperature at a ratio of at least 110 mg of sample to 1 ml of water, and inspecting the resulting mixture for the presence of insoluble matter; and mixing the batch with at least one carrier, if the insoluble matter is determined to be present below a predetermined amount.
NOVELTY - A purification pool comprises a primary filter pool (1) and a secondary filter pool (2). The primary filter pool is connected with the secondary filter pool through a first passage opening (9) provided with a filter mechanism (8). The purification pool is further provided with a tertiary filter pool (3) connected with the secondary filter pool through the second passage opening (10). Another filter mechanism is mounted at the second passage opening.    USE - Purification pool for biomass gas system.    ADVANTAGE - The purification pool offers a simple structure, strong practicability and safety disposal for polluted liquid of the straw machine set of the biomass gas system.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of a purification pool.    Primary filter pool (1)    Secondary filter pool (2)    Tertiary filter pool (3)    Filter mechanism (8)    First passage opening (9)    Second passage opening (10)
NOVELTY - The barrel has a soot door located in the centre of the bottom of the fuel barrel. A seal cover with handle is arranged on the soot door. The seal cover is moveably connected with a seal cover fixing shaft fixed to the bottom of the fuel barrel by the handle.    USE - Fuel barrel for biomass gasification furnace.    ADVANTAGE - The soot door located in the centre of the bottom of the fuel barrel, so that the main flame area in the fuel barrel is located in the centre of the bottom of the fuel barrel, thus making the fuel in the barrel burnt sufficiently and uniformly, and preventing the corrosion and damage to the wall of the fuel barrel because the main flame area is not in the centre.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a fuel barrel of biomass gasification furnace.
NOVELTY - The device has housing internally mounted with the inner container of the hearth. An air outlet tube is equipped on the side wall of the middle of the housing. The lower end of the air outlet tube is connected to an air inlet of the upper end of a filter. An air outlet in the middle of the filter is connected to a gas pipe. An oil outlet on the lower end of the filter is connected to an oil returning tube. A vortex chassis is equipped at the bottom end of the inner container. An air inlet tube is mounted on the side wall at the bottom of the body and equipped with an air blower.    USE - Gasification generating device for a biomass gasification furnace.    ADVANTAGE - The device can convert the most of biomass fuel as the fuel gas by a structure mode for mounting the inner container of the hearth in the housing and the air inlet tube, the air outlet tube and the filter so as to increase the fuel availability, saves energy, has safety and reliability, convenient use and long service life and fitting for the people in the countryside to expand and use.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a gasification generating device for a biomass gasification furnace.
NOVELTY - The system has a purification system comprising a primary purification unit (1), and an auxiliary purification unit (13), where an upper part of the primary purification unit is connected with the top of the core purification unit (2) by a connection pipe (4). The core purification unit comprises a filter cylinder (6) and a filter barrel. An exhaust pipe (8) is installed in the filter barrel. A filter material (10) is installed in the filter barrel. A filter medium (11) is installed in the filter cylinder. A purification outlet (12) is installed at the top of the filter cylinder (6).    USE - Low-tar biomass gas system.    ADVANTAGE - The system has purification unit and auxiliary purification unit, so the tar content of the terminal gas is reduced drastically and the purification efficiency is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a low-tar biomass gas system.    Primary purification unit (1)    Core purification unit (2)    Connection pipe (4)    Filter cylinder (6)    Exhaust pipe (8)    Filter material (10)    Filter medium (11)    Purification outlet (12)    Auxiliary purification unit (13)
NOVELTY - The device has a main body (1) with a gas inlet (4) and a gas outlet (6), where an inner chamber of the main body is provided with multiple filtering cylinders (2) with different diameters. A middle of the inner chamber of the main body is provided with a cyclone purification passage (3). An outlet of the cyclone purification passage is connected with the gas outlet. Multiple vent holes (5) are on the filtering cylinder. A bottom of the main body is provided with a conical collecting bin (7). A wall of the filtering cylinder is a corrugated structure.    USE - Biomass gas supply device.    ADVANTAGE - The device has high gas purification efficiency, simple operation and low tar content in gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass gas supply device.    Main body (1)    Filtering cylinder (2)    Cyclone purification passage (3)    Gas inlet (4)    Vent hole (5)    Gas outlet (6)    Conical collecting bin (7)
NOVELTY - The purifier has a main purifying room (1), where an upper part of which is provided with a spraying head (5) and a water charging pipe (4). A lower part is provided with an air inlet channel (2) and a water discharge port (3). An air outlet end of the air inlet channel (2) is vertical downwards. An upper part of an assistant purifying room is provided with the spraying head and water charging pipe. The main purifying room is communicated with the assistant purifying room via an air outlet (9).    USE - Straw gas purifier.    ADVANTAGE - The purifier has simple structure, low cost and high purifying efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a straw gas purifier.    Main purifying room (1)    Air inlet channel (2)    Water discharge port (3)    Water charging pipe (4)    Spraying head (5)    Air outlet (9)
NOVELTY - A device for preparing biogas by anaerobic and dry fermentation of silkworm excrement, which is a closed cylindrical or rectangular tank body, comprises a feeding system, a discharge system, and a fermentation chamber; where the feeding system comprises a feeding tube and a movable cover plate; the discharge system comprises a discharge tube and a discharge valve; the feeding tube is sealed and welded with a tank body; and the height of the feeding tube is less than the radius of the tank body.    USE - The device is useful for preparing biogas by anaerobic and dry fermentation of silkworm excrement (claimed).    ADVANTAGE - The device is a harmless fermentation processor with closed and simple structure, which can prevent dispersing and spreading of pathogenic bacteria, improve the cultivating environment of silkworm region, and solve the excrement pathogenic propagation and foul pollution for silkworm raiser.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the device for preparing biogas by anaerobic and dry fermentation of silkworm excrement.
NOVELTY - The furnace has a furnace body externally provided with a fan (14). The furnace body is divided into an upper furnace body (3) and a lower furnace body (5). The upper furnace body is provided with a combustion furnace head (1). An air-wind mixing chamber (23) is arranged below the combustion furnace head and provided with a gas inlet (2) and a secondary air inlet (22). An air outlet hole is formed on an outer ring pipeline between a long tube air outlet and a short tube air outlet.    USE - Household integrated biomass gasification furnace for a stove.    ADVANTAGE - The furnace has high heat transfer gasification efficiency, and is environment-friendly, convenient to use and simple in structure.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a household integrated biomass gasification furnace.    Combustion furnace head (1)    Gas inlet (2)    Upper furnace body (3)    Lower furnace body (5)    Fan (14)    Secondary air inlet (22)    Air-wind mixing chamber (23)
NOVELTY - The vaporizer has a fan (8) connected to a gas furnace (3). A dust discharging opening (6) is formed on a side wall of the gas furnace. An oxygen supply conduction pipe (9) is arranged near the fan. An air outlet end of the oxygen supply conduction pipe is connected to a lower part of a cooker (11). A feeding box (2) is arranged on an upper side of the gas furnace. An upper stirrer handle (1) is arranged on an upper end of the gas furnace. An upper stirring device is connected to the upper stirrer handle and arranged on the upper side of the gas furnace.    USE - Domestic residue mixed stowage vaporizer.    ADVANTAGE - The vaporizer is simple in structure, stable, reliable and convenient to use and operate, has high efficiency for processing domestic residue, high gas yield.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a domestic residue mixed stowage vaporizer.    Upper stirrer handle (1)    Feeding box (2)    Gas furnace (3)    Dust discharging opening (6)    Fan (8)    Oxygen supply conduction pipe (9)    Cooker (11)
NOVELTY - The furnace has a gasification furnace body provided with a hearth tank. An upper end of the furnace body is provided with a sealing ring cover. A side wall of a middle of the furnace body is provided with a gas outlet tube. The gas outlet tube is connected with the hearth tank. A lower end of the gas outlet tube is connected with a gas inlet of an upper end of a filter. The filter is connected with a fuel gas tube. A gas inlet tube is provided with an air blower, where the gas inlet tube is provided with a branch connected with a fuel gas oven.    USE - Biomass gasification furnace for use by rural people.    ADVANTAGE - The furnace effectively converts biomass fuel gas into fuel gas, greatly improves the fuel gas use rate, achieves efficient energy-saving, and is safe, reliable and convenient to use, and has long service life.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass gasification furnace.
NOVELTY - The gas stove has a gas distribution plate (2) placed inside a stove main body (1) to divide the stove main body into a combustion chamber (6) and a purification chamber (7). A purification medium (3) is loaded at bottom of the purification chamber. A gas inlet (4) is connected with the purification medium through an L-shaped pipeline (5). A smoke discharge hole (8) and a supporting bracket (9) are arranged on an upper part of the combustion chamber. An igniter (10) is arranged on the combustion chamber.    USE - Straw gas stove for a biomass gas equipment.    ADVANTAGE - The gas stove is convenient to install and safe to use, and effectively purifies terminal gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a straw gas stove.    Stove main body (1)    Gas distribution plate (2)    Purification medium (3)    Gas inlet (4)    L-shaped pipeline (5)    Combustion chamber (6)    Purification chamber (7)    Smoke discharge hole (8)    Supporting bracket (9)    Igniter (10)
NOVELTY - Delftia tsuruhatensis strain H1 capable of degrading chloroaniline, preserved in China typical culture collection center, which is Wuhan University, Wuhan, China, 430072, CCTCC NO: M209249, with the preservation date of November 4, 2009, is new.    USE - The Delftia tsuruhatensis strain H1 is useful for degrading chloroaniline or its derivative in sewage (claimed), preferably industrial sewage.    ADVANTAGE - The bacterial strain: can degrade chloroaniline pollutants rapidly under aerobic conditions, in high efficiency manner; and is in wild type with clear genetic background, thus making it suitable for genetic improvement.
NOVELTY - Methylobacterium rhodesianum H13 strain for high-efficiency degradation of dichloromethane, preserved at China typical model cultivation center, which is Wuhan University, Wuhan, China, with postal code of 430072, preservation date of May 20, 2010, and preservation number of CCTCC NO: M2010121, is new.    USE - The Methylobacterium rhodesianum H13 strain is useful for degrading dichloromethane in the wastewater and waste gas (all claimed).    ADVANTAGE - The Methylobacterium rhodesianum H13 strain can grow with dichloromethane as carbon source and energy while high-effectively degrading the bottom substance.
NOVELTY - The water purifying device has permeable shell, and a filler which is placed into the shell. The shell is partially or totally provided with permeable holes, and can be integrally formed by combining the shell and shell cover. The shell is triangle, cube, cuboid, polygonal shape, sphere or elliptical shape.    USE - Water purifying device for sewage processing technology.    ADVANTAGE - Provides water purifying device with strong practicality and removes pollutant in the water through mass propagation of microorganism.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a water purifying device.
NOVELTY - A prefabricated methane tank comprises methane tank body comprising an arc upper tank body (3) and an arc lower tank body (5) abutted together; where the upper part of the methane tank body is communicated with a feeding opening tube (6) and a discharging opening tube (2); and the upper part of the methane tank body is communicated with an air outlet (1).    USE - The prefabricated methane tank is useful for generating methane.    ADVANTAGE - The methane tank can be prefabricated in advance, and assembled at scene. Moreover, it has short building time, high strength, large bearing ability, long service life, and good use effect without maintenance, and is not frozen.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the prefabricated methane tank.    Air outlet (1)    Discharging opening tube (2)    Arc upper tank body (3)    Arc lower tank body (5)    Feeding opening tube (6)
NOVELTY - In method, soil is prepared to grow Galega orientalis: acid soils are limed, peat and manure compost is added. Ploughing is carried out, seeds are treated before sowing with the aqueous solution of rizotorfin in amount of 40 divide by 45 g - on a dry basis per 1 kg of seeds; the aqueous solution of boric acid in amount of 12 divide by 20 g per 1 kg of seeds; the aqueous solution of ammonia molybdate in amount of 6 divide by 8 g per 1 kg of seeds. The sowing rate is 25 divide by 27 kg/ha. Vegetating plants are sprayed with the aqueous solution of boric acid in amount of 800 divide by 1000 g per 1 ha of soil in the phase of 5 divide by 7 leaves. In the beginning of growth and after the first hay crop, the plants are sprayed with liquid humic fertiliser from biohumus in amount of 0.10 divide by 0.15 g per 1 ha of soil. At the 5th, 10th and 15th years of life the crops are treated with a disk harrow and are further sprayed with liquid humic fertiliser from biohumus in amount of 0.08 divide by 0.10 g per 1 ha of soil. Green mass is cut in budding phase and is distributed into rolls by forage harvesters. Then the green mass is cured in rolls for 2 divide by 3 days with drying to residual moisture of 60 divide by 65%, the green mass is ground by forage harvesters until the fibre length makes 1 divide by 3 cm. The ground green mass is dried in the drying drum at the temperature of 100 divide by 110 degrees C, granulated, granules are cured for 48 divide by 54 hours until residual moisture makes 9 divide by 12% and packed.    USE - Agriculture.    ADVANTAGE - Method makes it possible to produce ecologically clean biofuel.
NOVELTY - An input reservoir (10) stores food wastes and biochips. A driving unit integrally connected with the reservoir is operated to move food waste and biochip into a reaction bath. A mixing reactor (21) in reaction bath mixes the food waste and biochip. A hot wire heater is installed to the outside of reaction bath for heating the mixed food waste and biochip. A reactive element (20) is connected to the input reservoir and mixing reactor for fermentation of food waste and the end product is formed into biofuel or bio compost.    USE - Food waste processing unit.    ADVANTAGE - The food waste is processed efficiently and generated end product can be utilized as biofuel or bio compost. The temperature of reaction bath is regularly maintained. The food waste processing time is suppressed and generation of bad small is suppressed.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the food waste processing unit.    Input reservoir (10)    Motor (15)    Reactive element (20)    Mixing reactor (21)    Aging tank (22)
NOVELTY - Method for pre-treating organic waste, involves hydrolyzing organic waste by heating under pressure, removing ammonia and collecting ammonia gas from the hydrolyzed material.    USE - The method is useful for pre-treating organic waste for fermenting methane (claimed).    ADVANTAGE - The methane can be fermented with high efficiency.
NOVELTY - The equipment heats up water through various light reflecting concave mirror (3) for reflecting sunlight and generates electricity through high pressure saturated steam obtained by multi-grade heating of boiling furnace driving steam turbine electricity generator. The windmill drives the wind electricity generator to generate electricity. The boiled water or steam residual heats the low boiling point object to generate electricity. A water electrolyzer electrolyses water for producing hydrogen and oxygen.    USE - Multi-source multi-functional electricity generating and hydrogen producing equipment for domestic application and industrial application.    ADVANTAGE - The electricity generating and hydrogen producing equipment is configured with flexible connection, wide application, cleanness, and no pollution. The power supply is performed continuously.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the electricity generating and hydrogen producing equipment.    Concave mirror (3)    High-pressure-proof steam pipeline (9)    Heat gathering bottom seats (14)    Heat preserving bottom cover (15)    Heat preserving water boiling work (122)
NOVELTY - The filter material has a filter material body (1) that has a net-shaped honeycomb hole structure (2). The filter material body is spherical, cylindrical or similarly spherical.    USE - Filter material for processing water.    ADVANTAGE - Quickly degrades organic pollutant in water. Exhibits strong pollutant capacity, high porous ratio, acid and alkali resistance and long service life, not easy to block, and can be washed repeatedly.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the filter material for processing water.    Filter material body (1)    Net-shaped honeycomb hole structure (2)
NOVELTY - A compound anaerobic reacting pool disposed at the front end is composed of various sections of a compound anaerobic processing unit that are connected in series. The compound anaerobic processing unit is provided with a light filtering filter material region at the upper part, and an active mud region at the lower part. A horizontal undercurrent constructed wetland disposed at the rear end, is provided at the lower part with a stuffing layer, and at the upper part with a soil covering layer.    USE - Processing system for treating rural domestic sewage combining compound anaerobic and constructed wetland.    ADVANTAGE - Compound anaerobic reacting pool combines anaerobic active mud method with bio-membrane method, and makes use of anaerobic biochemical reacting and physical intercepting effect, thus organic pollution and floating solid removing effect is good, and usage life of follow-up constructed wetland is prolonged. Constructed wetland mainly removes nitrogen and phosphorus via cooperating effect of plant, microorganism and stuffing, thus quality of outlet water is good. Multi-section compound anaerobic and constructed wetland combining processing technique does not consume power, and allows simple operation and convenient managing.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of the processing system.
NOVELTY - Commercial biomass pool, which uses excrement of human and livestock, organic rubbish and other organic waste as raw materials, is designed as a long tunnel, where the gas-producing raw material is loaded in a material groove, which moves in the pool at an appropriate time and in a fixed direction.    USE - The pool is useful for producing biogas in large scale, commercial fuel gas, generating power and fertilizers.    ADVANTAGE - The environment index in the pool is controllable.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of commercial biomass pool.
NOVELTY - Sugar cane bagasse drying equipment comprises a hollow metallic cylinder, where the bagasse is utilized as fuel substitute. The hollow metallic cylinder contains a helical blade at upper part of the cylinder. The cylinder is comprised of a dome with a gutter, which helps to remove condensate. The cylinder is fixed in a prone position slightly deviated from horizontal to obtain wet bagasse directly from a conveyor belt. The bagasse is deposited back after removing approximately 12% of the moisture. The bagasse is deposited back to the conveyor and then passed through a microwave generator.    USE - Sugar cane bagasse drying equipment.
NOVELTY - The apparatus has an alkali reservoir (10) that supplies alkaline substance e.g. ammonia to a supersonic wave treatment tank (20) to enhance the pH of livestock wastewater flowed into supersonic wave treatment tank using ultrasound. The wastewater is supplied from supersonic wave treatment tank to a mixed tide (30) so as to neutralize pH of wastewater. An anaerobic digester (50) is arranged to perform digesting process to wastewater flowed out from mixed tide. A gas holder (60) is arranged to store biogas generated from anaerobic digester.    USE - Apparatus for digestion processing of livestock wastewater.    ADVANTAGE - The digestion processing can be performed with respect to livestock wastewater easily and efficiently by simple technique.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the apparatus for digestion processing of livestock wastewater. (Drawing includes non-English language text)    Alkali reservoir (10)    Supersonic wave treatment tank (20)    Mixed tide (30)    Anaerobic digester (50)    Gas holder (60)
NOVELTY - Preparing solid waste derived fuel comprises: (i) drying sludge in a dryer, adding quick lime to obtain dried sludge granules, where the weight ratio of the quick lime to the sludge is 1:2.5-5; (ii) drying, and crushing straw agricultural waste by a crusher; (iii) selecting the screened combustible product via a rubbish selecting device and crushing into combustible granules; and (iv) shaping, processing, mixing the dried sludge granules, straw agricultural waste and combustible granules in a weight ratio of 1-3:5-8:5-8 and shaping and squeezing in a shaping machine.    USE - The solid waste derived fuel is useful for cement factory, power generating factory and rubbish processing factory.    ADVANTAGE - The method: prepares the solid waste derived fuel, thus reducing the sludge and rubbish pollution, and soil occupation problem.
NOVELTY - The partitioned methane pond has pond body cover (2), and a fermentation pond body (1) which is divided into dry fermentation region (3) and sewage processing region (4). The dry fermentation region is located at the middle portion of fermentation pond body, and the space between the dry fermentation region and fermentation pond body forms the sewage processing region connected with water inlet (5) and water outlet (6).    USE - Partitioned methane pond for dry-wet fermentation.    ADVANTAGE - Performs solid-liquid partitioning fermentation to the life sewage and garbage, and satisfies the requirements of safety treatment and methane production.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a partitioned methane pond for dry-wet fermentation.    Fermentation pond body (1)    Pond body cover (2)    Dry fermentation region (3)    Sewage processing region (4)    Water inlet (5)    Water outlet (6)
NOVELTY - Methane preparation involves crushing crop straws, adding water, and then stirring the materials uniformly. A microbial inoculum and ammonium hydrogen carbonate are added to the stirred materials, and then the materials are covered by plastic film for 5-7 days at 50 degrees C. The obtained material is put into a tank and water is added into the tank and then the tank is sealed to obtain the desired product.    USE - Method for preparing methane by using crop straws (claimed).
NOVELTY - Premix comprises (in wt. %) pig complex enzyme preparation (1-5), pig multi-vitamin premix (5-10), pig microelement premix (0.2-1), lysine, complex additive premix (5-15) comprising lysine, an antioxidant, choline chloride and an acidulant, calcium hydrophosphate (15-30), stone powder (30-40), edible salt (4-8), Luctarom (RTM: Stevioside) (0.1-0.5), kitasamycin microcapsule preparation (0.2-0.5) having a mass concentration of 50%, a colistin sulfate microcapsule preparation (0.5-2) having a mass concentration of 10%, and zeolite powder.    USE - The premix is useful for: compound pig feed; and improving the immunity of pigs.    ADVANTAGE - The premix: improves the utilization ratio of nutrients in the pig feed for increasing the production; reduces the emission of substances e.g. phosphor and nitrogen into the natural environment by means of the livestock manure; and improves the economic benefits on the feeder.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing the premix, comprising weighing each raw material, adding the weighed raw materials into a mixer by a material conveying system and mixing the raw materials in it for 2-8 minutes to achieve a degrees of homogeneity of 5%, and packaging the mixed powder to obtain the finished product, where the premix comprises (in wt. %) pig complex enzyme preparation (1-5), pig multi-vitamin premix (5-10), pig microelement premix (0.2-1), lysine, complex additive premix (5-15) comprising lysine, an antioxidant, choline chloride and an acidulant, calcium hydrophosphate (15-30), stone powder (30-40), edible salt (4-8), Luctarom (RTM: Stevioside) (0.1-0.5), kitasamycin microcapsule preparation (0.2-0.5) having a mass concentration of 50%, colistin sulfate microcapsule preparation (0.5-2) having a mass concentration of 10%, and zeolite powder.
NOVELTY - Microalgae oil pressure catalytic refining, comprises: (a) adding microalgae mud collected by flocculation into a reaction kettle, adding hydrogen-rich organic solvent and lewis acid catalyst filling carbon dioxide into reaction kettle, agitating and heating, and reacting and cooling; and (b) filtering and centrifugally separating produced crude product to obtain liquid phase product, removing organic solvent phase, and placing aside and layering to remove most of moisture, adding microemulsion assistant into obtained crude biofuel, agitating to mix evenly and obtaining microemulsion biofuel.    USE - The method is useful as a pressure catalytic refining of microalgae oil.    ADVANTAGE - The method: adopts wet microalgae as raw material, and avoids consuming large amount of energy for drying the microalgae oil; produces microemulsion biofuel with fine stability, non-layered, high temperature resistance and easy storage and without precipitate; has high heat value, sufficient burning and less ash content; can replace home fuel and part of industrial fuel; and has wide application range.    DETAILED DESCRIPTION - Microalgae oil pressure catalytic refining, comprises: (a) adding microalgae mud collected by flocculation into a reaction kettle, adding hydrogen-rich organic solvent with mass ratio of 1:1 and lewis acid catalyst with mass ratio of 2.5-7.5%, filling 2-4 MPa of carbon dioxide into reaction kettle, agitating and heating up to 300-450 degrees C and reacting for 30-60 minutes and cooling to room temperature; and (b) filtering and centrifugally separating produced crude product to obtain liquid phase product, removing organic solvent phase by distillation, and then placing aside and layering to remove most of moisture, obtaining crude biofuel, and adding 4 vol.% of microemulsion assistant in the crude biofuel, agitating at 1000-1500 revolutions/minute for 2-5 minutes to mix evenly and obtaining the microemulsion biofuel.
NOVELTY - The invention relates to an installation and process for preparing hydrogen and oxygen and/or a fuel gas by forced pulse electrolysis. The claimed installation comprises a group of gas-generating resonant cells, made as capacitors with water as dielectric, the cells being connected with a high voltage pulse transformer connected, in its turn, with a unit shaping and amplifying the pulse train to be applied to the resonant cells in order to generate gas, the generated gas being collected in a collecting tube, and the flow rate of the gas being monitored by means of a monitoring unit comprising a gas volumemeter, the thus described entire assembly being controlled by a central unit provided with a microprocessor, wherein pre-established pulse trains are generated, said pulse trains being imposed by means of a smart card connected with a central unit, and, depending on the situation, they are corrected on the basis of a feedback signal coming from the monitoring unit, the electric energy necessary to functioning being ensured by a supply source which is also connected with an emergency system which controls the cutting off of the energy supply in certain cases. The central unit also comprises a driver for an LCD display on which there may be visualized, in real time, the functioning parameters. The claimed process consists in treating water by forced pulse electrolysis inside a resonant cell, consisting of a capacitor with water as dielectric, connected to an L-C type electric circuit, on the capacitor armatures a high voltage pulse train being applied concomitantly with the application of a breakdown voltage of up to 1 kV on one of the armatures which has as an effect the breaking of a covalent bond within the water molecule and the release of hydrogen, oxygen and free radicals, and also other chemical elements, depending on the type of treated water.
NOVELTY - Waste edible oil is mixed with water and supplied to a reactor in which pressure is maintained in vacuum condition. A catalyst is loaded in the reactor and reaction is activated by the catalyst. The gas generated in the reactor is separated from liquid product by gasification, and biogas and liquid fuel are recovered from each product, respectively.    USE - Production of biogas and liquid fuel (for use in vehicles and industrial machines) from disposed edible oil.    ADVANTAGE - The method enables efficient recycle of waste edible oil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production apparatus of biogas and liquid fuel from disposed edible oil.
NOVELTY - The device has a reactor (9) with a filling bed (10) for fixing the fiber filling (8), the water distributing head (6) connected with the water pump (2) and an aerating head (7) which is connected with an aerator (5). The water pump, aerator and the valve (4) are connected with a time controller (3). An inner circulating pump (11) is arranged in the reactor, and is connected with an inner circulating pipe (12). A water outlet of the inner circulating pipe is arranged in upper end of the reactor. The water distributing head is connected with the valve and functions as drain.    USE - Biological membrane sewage processing device.    ADVANTAGE - Improves attachment of nitrobacteria and denitrobacteria and shortens water retaining duration by providing abundant nutrition of the filling on the upper layer. Ensures water quality of the water discharged from settlement. Reduces operation and maintenance cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the inner circulating sequential batch type biological membrane sewage processing device.    Water pump (2)    Time controller (3)    Valve (4)    Aerator (5)    Water distributing head (6)    Aerating head (7)    Fiber filling (8)    Reactor (9)    Filling bed (10)    Inner circulating pump (11)    Inner circulating pipe (12)
NOVELTY - The suspending filler is a hollow gridding tubular suspending filler made of macromolecular plastic. The inner and/or outer surface of the filler is provided with a macromolecular villus beard layer. The beard layer is hydrophilic.    USE - Suspending filler.    ADVANTAGE - Achieves large specific surface area and fast adhering speed of biological film. Improves biological adhering amount by about 20 percent.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of the suspending filler.
NOVELTY - This invention relates to a method for producing fatty acid methyl ester from a high fatty acid oil utilizing recycled methanol, including performing at least a first, a second, and a third esterification reactions, and a transesterification reaction. Since this method uses the low cost disposed oil as the raw material and uses the methanol solution recycled from the process as the reactant, the manufacturing cost of the biomass diesel can be reduced. Furthermore, since this method may reduce free fatty acid components in the transesterification reaction, the disadvantage of the low yield of the current transesterification process may be reduced and therefore the manufacturing cost of producing biomass diesel can be reduced.
NOVELTY - The invention relates to a device for carbon dioxide purification and methane gas separation, which includes a blower, a vacuum pump, a valve assembly, and at least a carbon dioxide purification tower which is utilized to remove the carbon dioxide in air and can be further combined with a sulfide purification device to remove the sulfide and carbon dioxide in methane gas, effectively separating methane gas; in addition, also provided is a method for carbon dioxide purification and methane gas separation associated thereto.
NOVELTY - The invention relates to an apparatus for sulfur-containing waste gas purification and methane gas recycling, which includes a blower, a vacuum pump, a valve assembly, and at least a sulfide purification tower which is utilized to remove the sulfide in sulfur-containing waste gas and can be further combined with a methane gas recycling apparatus to remove the sulfide and carbon dioxide in methane gas, effectively purifying the methane gas; in addition, also provided is a method for sulfur-containing waste gas purification and methane gas recycling associated thereto.
NOVELTY - A device has a hydrolyzing acidifying reactor, a solid-liquid separating device, an adjusting sink and an expanded granular sludge bed reactor. The hydrolyzing acidifying reactor is columned complete-mixing type reactor. A cover is arranged on the upper portion of hydrolyzing acidifying reactor. The agitating device is arranged in hydrolyzing acidifying reactor. Anaerobic granular sludge is transformed in the expanded granular sludge bed reactor.    USE - Device is used for processing organic waste (claimed).    ADVANTAGE - The organic waste is efficiently processed using the device with high chemical oxygen demand removing effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for processing method of organic waste, which involves hydrolyzing the organic waste, performing solid-liquid separation, and performing anaerobic reaction.
NOVELTY - Pyrethroid pesticide residue degrading gram negative bacterial strain ZS-S-01 of Stenotrophomonas sp., preserved in China Committee for Culture Collection of Microorganisms, having a preservation number CGMCC M 2010095 and Genbank accession number HM016874 of 16s ribosomal DNA, is new.    USE - The strain is useful for degrading pyrethroid pesticide residue (claimed).    ADVANTAGE - The degrading agent comprising the strain is of low cost, convenient to use and shows good degrading effect; and is suitable for producing fruits and vegetables in large scale.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a pyrethroid pesticide residue degrading agent, which is produced by: (i) inoculating a fenvalerate pesticide residue degrading bacterial strain ZS-S-01 to a Czapek culture medium shake flask and shaking the culture until log phase is reached, (ii) inoculating the cultured strain (8-10% volume ratio) into a seed tank and culturing until log phase is reached, where the medium comprises (in wt.%) sucrose (3), sodium nitrate (0.2), potassium chloride (0.05), magnesium sulfate (0.05), dipotassium phosphate (0.1), ferric sulfate (0.001) and peptone (0.05) of pH 7, (iii) inoculating the log phase seed tank culture (8-10% volume ratio) into a production tank containing the same seed tank culture medium as mentioned above to culture and (iv) controlling the sterile air aeration rate at 0.45-0.6 m3/minute and agitating speed at 200-300 rotations per minute at 30-35 degrees C for 36-48 hours during culturing, and packaging the culture liquid using a plastic barrel or sub-packaging liquid dosage forms in bottles.
NOVELTY - Preparing microbial oil and biodiesel by fermenting cassava starch comprise: using Trichosporon cutaneum B3 as an oil producing strain, using saccharified liquid of cassava starch as a carbon source, fermenting in a batch culturing condition to culture the microbes, drying and extracting to obtain the microbial oil, which is used for trans-esterification reaction under the action of a catalyst to obtain the biodiesel with glycerin as a by-product.    USE - The method is useful for preparing microbial oil and biodiesel.    ADVANTAGE - The method: utilizes cassava starch which serves as a carbon source, which is fully utilized and hence saves raw material cost; is simple, convenient, environment-friendly and easy to control; and has good industrial application.
NOVELTY - In a method which involves exposing an aqueous electrolyte to an electric field through electrodes lying at a certain distance from each other and tapping the dissociation products, exposure of the aqueous electrolyte to the electric field is carried out with calculated resonance frequency on harmonics relative which the fundamental frequency of oscillation of water molecules is a multiple, with separate tapping of dissociation products from each even and odd electrode. The apparatus consists of electrodes which are immersed in the aqueous electrolyte and placed in parallel at a distance from each other and hydraulically linked to form electrolytic sections which are connected into an electrical circuit, and are connected to an alternating current generator, which enables to obtain electromagnetic oscillations at frequency between 10 kHz and 3.2 MHz.    USE - Chemistry.    ADVANTAGE - Design of a simple method for dissociation of water into hydrogen and oxygen and apparatus for realising said method, which are suitable for industrial use, enable to reduce power consumption of the water dissociation process and enable separate tapping of gases. 10 cl, 2 dwg, 1 tbl
NOVELTY - An electricity generating system by using natural climate which synchronously utilizes a wind generator, a solar panel and a rainwater generator to make at least one of these equipments generate electricity all day. The wind generator, the solar panel and the rainwater generator also transmit electric power to a tap water electrolyzing assembly via a main parallel generation controller, so as to electrolyze tap water and produce hydrogen for combusting, thus saving fuel costs.
NOVELTY - Invention relates to organic chemistry, particularly, to direct thermal oxidation of methane to produce heat power and may be used for recovery of well methane in mining. proposed method comprises heating a portion of initial well methane from gas complex treatment unit in furnace at 0.1-1 MPa and gas concentration in initial gas making 20-25 vol. %. Heated gas is fed into tubular cooling zone jacket space and, therefrom, into reaction zone wherein methane gas-phase oxidation occurs at 400-650 degrees C accompanied by reaction mix cooling in reactor tubular zone. Final cooling of reaction mix occurs in refrigerator-condenser whereat cooled reaction mix is separated into off gases and fluid products, and high-pressure and low-pressure steam and heat water are produced. Note here that thermal conditions are adjusted by feeding cold well methane in reactor reaction zone and varying heating temperature of a portion of methane fed to rector tubular cooling zone inlet.    USE - Process engineering.    ADVANTAGE - Higher efficiency of methane oxidation. 2 cl, 2 dwg
NOVELTY - The device has a heater (7) that is installed at a circulating pipe (6), and an aerator (8) that is installed at the bottom portion of a tank (1) having a cover structure (2). A fermentation room (3) is installed at the top of the tank. A water tub (4) is installed at the bottom portion of the fermentation room. The mineral ions are injected into the water tub stored with the to-be-fermented organic waste continuously using a sprinkling guide plate (9), so as to ferment the organic waste.    USE - Vented-type fermenting device for producing fertilizer from organic waste.    ADVANTAGE - The organic waste can be fermented effectively within short period of time.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fermenting device.    Tank (1)    Cover structure (2)    Fermentation room (3)    Water tub (4)    Circulating pipe (6)    Heater (7)    Aerator (8)    Sprinkling guide plate (9)
NOVELTY - Described is a method of converting lignin to liquid and gaseous hydrocarbons and derivatives thereof, involving using lignin in form of insoluble wet hydrolysis lignin, which, in the presence of a catalyst - noble metal salt, is simultaneously treated with water, alcohols and hydrogen at initial pressure of 10-20 atm in an autoclave while heating to 250-350 degrees C, after which sub- or supercritical conditions at pressure 60-90 atm are created, and liquid hydrocarbons are separated from the solid residue by filtering.    USE - Chemistry.    ADVANTAGE - High conversion of lignin to liquid hydrocarbon products with a negligible fraction of solid and gaseous products. 3 cl, 10 ex
NOVELTY - A carbon dioxide recycling method is provided. First, a carbonate electrolyte solution is formed and a solid photo-catalyst is added therein to form a suspension solution. Then, gas phase carbon dioxide is directed into the suspension solution. Then, an electrical current is conducted into the solution and a light which wavelength is from 250 to 760 nm is irradiated to reduce carbon dioxide to form reusable product.
NOVELTY - A system for releasing heat in the hydrogen production method of fuel cell provides reaction heat of hydrogen production. The system comprises a tank, a fuel and air supply, and a combustion catalyst. The fuel comprises an organic compound and water for a combustion reaction. The catalyst for combustion is mounted in the tank, and catalyzes the combustion reaction of the fuel so as to release heat. The mole proportion of the carbon atom in the organic compound to the water molecular is at least less than 3.5. It was also applicable for catalytic combustion of exhaust gas and liquid.
NOVELTY - The device (100) has a kneading section (110) having mixing rooms (120,130) with hopper (113) in which the food waste is shattered. A fermentation portion (210) is provided to perform fermentation of food waste. The top of flanges (144,144a) having separate space portions (145,145a), is fixed to the stationary tubes (147,147a) to motor (M) and lower portion is fixed to frames (142,142a). The stationary tube fixed to lower portion of flange is provided with impellers (140,140a) with screw axis which is protruded from the stationary tube in which impeller wing is fixed.    USE - Device for manufacturing liquid fertilizer using food waste ejected from home and restaurant.    ADVANTAGE - The fermentation of food waste is performed effectively and the liquid fertilizer is manufactured easily without generation of bad smell in the fermentation period, and the contamination of air is prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the liquid manure manufacturing device. (Drawing includes non-English language text)    Liquid fertilizer manufacturing device (100)    Kneading section (110)    Hopper (112)    Mixing rooms (120,130)    Impellers (140,140a)    Frames (142,142a)    Flanges (144,144a)    Separate space portions (145,145a)    Stationary tubes (147,147a)    Motor (M)
NOVELTY - Perovskite type composite oxide catalytic agent doped with halogen (I), is new.    USE - (I) is useful in methane oxidative coupling reaction (claimed).    ADVANTAGE - (I): exhibits good catalytic activity and stability.    DETAILED DESCRIPTION - Perovskite type composite oxide catalytic agent doped with halogen of formula (AB1O3- delta X sigma ) (I), is new.    A = Ba, Sr, Ca, La, Mg, Sm, Y and/or Ce;    B1 = Cr, Co, Fe, Cu, Ga, Al, Zn, Zr, Ni, Mn, Ti, Nb, Sc and/or In;    X = F, Cl, Br or I;    delta = 0-0.8; and    sigma = not less than 0.04 and not greater than 0.16.    An INDEPENDENT CLAIM is also included for the preparation of perovskite type composite oxide catalytic agent doped with halogen (I).
NOVELTY - Gasoline comprises (in %): methanol (85-95) and additive (10-15) and does not contain methyl tertiary butyl ether (MTBE).    USE - The gasoline is useful in engine or burner (claimed).    ADVANTAGE - The gasoline is environmentally-friendly, consumes less energy, exhibits excellent performance and replaces liquid fuel of the current gasoline.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing the above-cited gasoline, which involves adding methyl alcohol to synthetic pot, adding additive to the methyl alcohol and stirring or mixing the mixture by circulating pump.
NOVELTY - Methanol is mixed with epoxy ethane in the weight ratio of 1:8-12, heated at 50-60 degrees C and activated for 2.5-3.5 minutes. The obtained mixture is cooled to less than 25 degrees C and provided into storage tank. The obtained cooled mixture is activated and mixed with gasoline according to a weight ratio to obtain qualified methanol gasoline.    USE - Manufacture of methanol gasoline.    ADVANTAGE - The method is simple and easy, and improves the inter-solubility of methanol gasoline. The methanol gasoline will not corrode the oil supply system, and has improved power performance.
NOVELTY - A safe energy-saving liquid fuel comprises (in parts weight) methanol (1000), acetone (0.5-2.5), ethanol (1-6), camphor (0.1-3), ferrocene (0.01-0.125), potassium permanganate (0.002-0.003), white sugar (0.1-5), sodium chloride (0.1-3), solvent (5-10) and water (250-430). The solvent is solvent oil or petroleum ether.    USE - Safe energy-saving liquid fuel.    ADVANTAGE - The safe energy-saving liquid fuel has no fume, no taste, no toxicity, no scale, and has high heat efficiency, easy extinguishing property and low use cost. The fuel is not influenced by the temperature during use.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of safe energy-saving liquid fuel. Ferrocene is added into a container, and acetone is added under room-temperature agitation, to obtain homogeneous solution (A). Camphor is added to container, and ethanol is added under room-temperature agitation, to obtain homogeneous solution (B). White sugar is added into the container, and water is added in an amount of 4-10 times the weight of white sugar under room-temperature agitation, to obtain a solution (A). Sodium chloride is added into the container, and water is added in an amount of 10-20 times the weight of white sugar under room-temperature agitation, to obtain a solution (B). Potassium permanganate is added into the container, and water is added in an amount of 100-500 times the weight of potassium permanganate, to obtain potassium permanganate solution. Methanol, solvent and homogeneous solutions (A and B) are added into the container, evenly agitated, and solutions (A and B) are added and further agitated. Residual water is added completely, agitated, left for 10-30 hours, and packed the finished product (fuel).
NOVELTY - Microbial preparation comprises Klebsiella pneumoniae DM, Enterobacter caucerogenus DM, Acinetobacter calcoaceticus DM, Pseudomonas stutzeri OX1, Rhodococcus erythropolis and P.putida in the ratio of 1:1:2:2:1:1 or 1:1:3:3:3:1.    USE - The microbial preparation is useful for decontaminating oil pollution of soil.    ADVANTAGE - The microbial preparation has excellent degradability and adaptability for oil component in polluted soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the above-cited microbial preparation, which involves obtaining dried oil contaminated soil, diluting the soil, adding microorganisms chosen from K.pneumoniae DM, E.caucerogenus DM, A.calcoaceticus DM, P.stutzeri OX1, R.erythropolis and P.putida one by one to the diluted soil, measuring aromatic hydrocarbon degradability using biological oxygen demand (BOD) tester, measuring total petrol hydrocarbons (TPH) degradability, measuring hydrophilic character of microorganisms by bacterial adherence to hydrocarbons (BATH) test, measuring the cell wall change of the microorganisms using methyl methane sulfonate (MMS), confirming the cell wall portability of the microorganisms within the soil by measuring zeta potential and confirming maintenance of cell wall property after 100-200 generations, mixing the above-cited microorganisms in the ratio of 1:1:2:2:1:1 or 1:1:3:3:3:1, and subculturing the microbial mixture in a mineral medium containing oil treating agent.
NOVELTY - The system (100) has mixing vessel having accommodation space, which is connected to fuel supply pipe (610), and fuel mixing portion that is installed in accommodation space having drift spaces. A generation unit (200) generates hydrogen by electrolyzing water through electricity generated by sunlight/wind force. The fuel mixing portion mixes fossil fuel and hydrogen, and oxidizer (500) generates heat energy. A spiral tube has inlet hole to spray hydrogen on accommodation space. The hydrogen is passed through drift spaces and fossil fuel is ejected through exhaust pipe.    USE - Hydrogen generation system for welding machine, cutter, soldering machine, brazing machine, chemical food processing and refractory metal manufacture.    ADVANTAGE - The maintenance cost or production cost of hydrogen generation system can be improved. The energy consumption can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of hydrogen generation system.    Hydrogen generation system (100)    Hydrogen generation unit (200)    Hydrogen storage unit (300)    Oxidizer (500)    Fuel supply pipe (610)
NOVELTY - Fermented product is obtained using microorganism chosen from Enterobacter sp., Pseudomonas sp., Rhodotorula sp. and Pichia sp..    USE - The fermented product, preferably wood pellet is useful in fertilizer or solid fuel (both claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of manufacturing wood pellet.
NOVELTY - Hygroscopic agent has multiple terminal structure with porous desiccant comprising (in wt.%) composition (0.0005-0.5) containing methyl violet and quinaldine red in ratio of 1:1-15 as indicators and moisture indicator, where the indicator is distributed in porous desiccant.    USE - The hygroscopic agent is useful for absorbing moisture for preserving foodstuffs and pharmaceuticals from rancidity and degeneration.    ADVANTAGE - The agent is environmentally-friendly as it does not contain harmful chlorinated cobalt base indicator.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of manufacturing the above-cited hygroscopic agent.
NOVELTY - The method involves dividing a coal pile stock into matrix type sections. A sensor is arranged in each matrix type section, and gas density of the coal pile stock is measured by utilizing the sensor. Location information of the sensor is transmitted to a server, and spontaneous ignition of the coal pile stock is progressed. Concentration of methane and carbon monoxide in the coal pile stock is determined, and a global positioning system (GPS) transceiver is connected to the server.    USE - Method for detecting ignition point of a coal pile in a coal yard.    ADVANTAGE - The method enables simplifying the structure of the global positioning system, and reducing the ignition point detecting cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a global positioning system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a global positioning system.'(Drawing includes non-English language text)'
NOVELTY - Method of preparing casting material, involves pulverizing crab shell (60-70 wt.%) and solid fuel ash (20-30 wt.%), mixing pulverized material in weight ratio of 10:20, fermenting the mixture, subjecting the fermented mixture for humidification process and mixing the obtained humidified material with earthworm castings.    USE - The method is useful for preparing casting material (claimed).
NOVELTY - A cobalt-phosphorus-boron/copper catalyst is obtained by washing copper foil, dipping in hydrated tin chloride and palladium chloride, activating, drying, spraying cobalt-phosphorus solution on both sides of activated copper thin plate and plasticizing in electric furnace at specified temperature for specified time. The cobalt-phosphorus solution is obtained by mixing cobalt chloride hexahydrate, sodium phosphate and sodium borate reducing agent in distilled water.    USE - Cobalt-phosphorus-boron/copper catalyst is used for producing hydrogen (claimed) for fuel cell.    ADVANTAGE - The hydrogen can be manufactured effectively using cobalt-phosphorus-boron/copper catalyst.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing hydrogen.
NOVELTY - The sewage and livestock residue fermenting device has a housing (110) accommodating a mixer (150) for mixing residue. A slot (111) is connected to the upper side of housing. A vent (170) is provided at the lower side of housing. The mixer has a stirring shaft (151) and several pairs of shovel shaped blades (152) provided on the stirring shaft along the longitudinal direction of the shaft. An oyster shell supply unit (140) is connected to the top of the housing for supplying powdered oyster shell (141).    USE - Sewage and livestock residue fermenting device for producing mature soil.    ADVANTAGE - The fermenting device disassembles organic compound within the housing, promotes fermentation quickly and reduces bad smell during fermentation. The fermentation time is reduced by reducing the moisture content of residue within the housing. The heavy metal in the soil is absorbed and the acidified soil is alkalized by using oyster shell powder for producing profitable mature soil.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the sewage and livestock residue fermenting device.    Housing (110)    Slot (111)    Oyster shell supply unit (140)    Powdered oyster shell (141)    Mixer (150)    Shaft (151)    Blade (152)    Vent (170)
NOVELTY - Method for preparing compost, involves obtaining sewage and animal waste in a fermenter, drying the waste, adjusting moisture content of the waste to 65%, inoculating microorganisms into fermenter, injecting rice straw and oyster shell powder into the fermentation unit, uniformly mixing the mixture, adjusting the moisture content of the mixture to 45-50%, fermenting the mixture, adjusting the moisture content of the mixture to 40%, and aging the fermented mixture. The waste residues, microorganisms and rice straw are added in the weight ratio of 70:25:5.    USE - The method is useful for preparing compost.    DETAILED DESCRIPTION - Method for preparing compost, involves obtaining sewage and animal waste in a fermenter, drying the waste and adjusting moisture content of the waste to 65%, inoculating microorganisms into fermenter, injecting rice straw of size 5-20 mm and oyster shell powder obtained using mesh of size 200-325 into the fermentation unit, uniformly mixing the mixture, adjusting the moisture content of the mixture to 45-50%, fermenting the mixture and again adjusting the moisture content of the mixture to 40%, and aging the fermented mixture. The waste residues, microorganisms and rice straw are added in the weight ratio of 70:25:5.
NOVELTY - An automated powdered biomass fired stove is meant to use processed biomass such as tree leaves, shrubs, agricultural husks, stalks, saw dust etc as fuel by cutting, drying and pulverizing to 6-8 mm mesh, for thermal energy application for various usages like frying, cooking food, making sweets, making namkeen, generating steam for thermal use or generating electricity. The stove can be used for economical replacement of costly petroleum products, coal and wood etc. The biomass is combusted into circular combustion chamber made of mild steel duly lined with fire cement and having numbers of air nozzles, thus to attain maximum retention time and to provide primary/secondary air and turbulence for smokeless, ash less and efficient combustion. A control panel consists of temperature controller which controls the cooking/frying medium temperature. Image 0/0
NOVELTY - Treatment process for converting in-field straw into organic compost fertilizers for plants: comprises preparing a straw treatment microbial composition (Biomix-straw); collecting, stacking and spraying the composition onto the straw in the field; annealing and mixing the organic annealing ingredients for the plants, where the straw is subjected to annealing for ten days, mixed and continued to anneal for 20-40 days, and then well-decomposed into organic compost fertilizers.    USE - The process is useful for converting in-field straw into organic compost fertilizers, which is useful for plants (claimed).
NOVELTY - The method of generating an electric current from electrons produced by the rupture of hydrogen bonds to oxygen atoms of water molecules during the hydrolyzation of alkaline metals from the surface of a tape passing through a turbulent moving stream of a diffuse mixture of air and water, is claimed. The electrons are statically attracted to the finned surface of an ionic capacitor, which is connected in series with an electrolytic capacitor.    USE - The method is useful for generating an electric current in an electrolytic diffusion fuel cell, which is useful as a mobile source for recharging batteries in an electrical powered vehicle while the vehicle is in motion.    ADVANTAGE - The method is capable of efficiently and economically generating the electric current in the electrolytic fuel cell.    DESCRIPTION OF DRAWING(S) - The diagram shows a side view of a total diffusion cell circuit showing a capacitor.    Magazine cartridge case (10)    Hydrolyzation chamber (20)    Upper continuity terminal (21)    Cell frame (28)    Centrifugal fan air blower. (33)
NOVELTY - An expression cassette comprising a promoter operatively linked to a polycistronic nucleotide sequence capable of encoding a microbial scaffolding protein and at least two enzymes, is new. The scaffolding protein contains at least two receptor sites for binding to ligand sites in at least two enzymes.    USE - The expression cassette is useful for degrading biomass (claimed) into fermentable sugars, and producing biofuels.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) vector comprising the above-mentioned cassette;    (2) host cell comprising the vector; and    (3) method of degrading a biomass, involves contacting a biomass with the host cell.
NOVELTY - A stabilized biodiesel fuel contains phenol-type compound (I) and amine-type compound (II). The total content of amine-type compound and phenol-type compound is 300 ppm or more.    USE - Stabilized biodiesel fuel is used for engines.    ADVANTAGE - The stabilized biodiesel fuel has excellent storage stability and oxygen stability.    DETAILED DESCRIPTION - A stabilized biodiesel fuel contains phenol-type compound of formula (I) and amine-type compound of formula (II) (100-2000 ppm). The total content of amine-type compound and phenol-type compound is 300 ppm or more.    R1=tertiary butyl;    R2=1-4C alkyl;    R3=1-8C alkyl or phenyl;and    R4=1-6C alkyl.
NOVELTY - A gasified gas-purified waste water is processed by cooling gasifiying gas (9) from circulating fluidized bed gasifier (2) with water with water-cooled apparatus (16), removing impurity material in gasifying gas, pressurizing waste water from water-cooled apparatus by booster pump, heating with heater, carrying out pressure reduction flush of waste water, separating into waste water and vaporization component, and supplying separated vaporization component to combustion furnace (1) of circulating fluidized bed gasifier.    USE - Processing of gasified gas-purified waste water.    ADVANTAGE - The method reduces installation area with simple apparatus.    DETAILED DESCRIPTION - A gasified gas-purified waste water is processed by cooling gasifiying gas (9) from circulating fluidized bed gasifier (2) which makes combustion furnace (1) and gasifier circulate through flow medium and is made to gasify raw material (8) by gasifier with water with water-cooled apparatus (16), removing impurity material in gasifying gas, pressurizing waste water from water-cooled apparatus by booster pump, heating with heater, carrying out pressure reduction flush of waste water, separating into waste water and vaporization component, supplying separated vaporization component to combustion furnace of circulating fluidized bed gasifier, inducing waste water to ammonia stripper and activated sludge tank, and detoxifying impurity material. An INDEPENDENT CLAIM is included for a processing facility of gasification gas-purification waste water.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the processing facility of gasified gas-purified waste water. (Drawing includes non-English language text).    Combustion furnace (1)    Gasifier (2)    Raw material (8)    Gasifiying gas (9)    Water-cooled apparatus (16)
NOVELTY - A hydrogen producing apparatus is operated by temporarily stopping air from selective oxidation air supply apparatus in state which continued supply of source gas from source gas supply apparatus (4) and water from water supply apparatus (5) when operation continuation time after starting operation turns into predetermined time.    USE - Operation of hydrogen producing apparatus for operating fuel cell system (claimed) e.g. domestic fuel cell system.    ADVANTAGE - The method reduces carbon monoxide in generated gas from hydrogen producing apparatus.    DETAILED DESCRIPTION - A hydrogen producing apparatus is operated by temporarily stopping air from selective oxidation air supply apparatus in state which continued supply of source gas from source gas supply apparatus (4) and water from water supply apparatus (5) when operation continuation time after starting operation turns into predetermined time. The hydrogen producing apparatus comprises modification part (1) which produces reformed gas containing hydrogen by steam reforming reaction from source gas from source gas supply apparatus with modification catalyst and steam obtained by vaporizing water from water supply apparatus, and selective oxidation part (3) which reduces carbon monoxide in mixed gas containing gas with selective oxidation catalyst and selective oxidation air from selective oxidation air supply apparatus by selective oxidation reaction. An INDEPENDENT CLAIM is included for an operating method of fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the hydrogen producing apparatus. (Drawing includes non-English language text).    Modification part (1)    Transformation part (2)    Selective oxidation part (3)    Source gas supply apparatus (4)    Water supply apparatus (5)
NOVELTY - A blower (40) mixes fuel gas supplied from fuel-supply path (20), and oxidizing agent gas supplied from oxidizing agent supply path (30). A gas flow rate acquisition unit (62) detects flow volume of fuel gas supplied to blower. A modifier temperature sensor (45) detects temperature of modifier. A modification control unit (61a) controls opening degree of flow control valve (24) so that detected temperature turns into preset target temperature while controlling rotational speed of blower, and detected flow volume turns into preset target flow volume.    USE - Modifier.    ADVANTAGE - The layout volume of modifier can be reduced. The supply amount of fuel gas with respect to modifier can be controlled with more precision by performing correction, so that upstream pressure of flow control value is high.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view illustrating the modifier. (Drawing includes non-English language text)    Fuel-supply path (20)    Flow control valve (24)    Oxidizing agent supply path (30)    Blower (40)    Modifier temperature sensor (45)    Modification control unit (61a)    Gas flow rate acquisition unit (62)
NOVELTY - Biological waste treatment of to-be-processed water containing organic substance is carried out by a methane producer. A portion of treated water is recycled to biologically treated water or water before biological treatment, and mixed. Carbon dioxide gas contained in the returned treated water is released before mixing process. Precipitation separation of granule sludge contained in water is carried out. The recycle of supernatant liquid is carried out. Thus, organic wastewater is processed.    USE - Processing of organic wastewater.    ADVANTAGE - The organic wastewater is efficiently processed using reduced amount of alkaline component. The reduction of yield of methane is suppressed.    DETAILED DESCRIPTION - Biological waste treatment of to-be-processed water containing organic substance is carried out by a methane producer. A portion of treated water is recycled to biologically treated water or water before biological treatment, and mixed. Carbon dioxide gas contained in the returned treated water is released before mixing process. The treated water is showered, and carbon dioxide gas is released from treated water during decarboxylation. The showered treated water is introduced into sedimentation tank, and precipitation separation of the granule sludge contained in introduced water is carried out. The recycle of the supernatant liquid is carried out. Thus, organic wastewater is processed. An INDEPENDENT CLAIM is included for processing apparatus of organic wastewater.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of wastewater processing apparatus. (Drawing includes non-English language text)    Biological treatment tank (10)    Collection board (12)    Mixing tank (40)    Stirring blade (41)    Sedimentation tank (50)
NOVELTY - The method involves introducing air or oxygen into biogas stream (4) by an injector (1) i.e. Venturi nozzle, that is utilized as a final structural component before aerobic desulfurization of biogas. The injector is arranged at an intake pore, and is provided with a throttle valve (6) and a non-return valve (5). The injector is made of acid-sensitive and weather- and/or UV-constant material. The injector corresponds to determination of explosion protection.    USE - Method for producing conditions for consecutive desulfurization of biogas.    ADVANTAGE - The method improves economy and ecology of the aerobic desulfurization of the biogas while allowing fast and inexpensive replacement of existing compressors/blowers of the device. The injector is designed such that it is functionally maintenance-free and does not require electrical or mechanical energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for producing conditions for consecutive desulfurization of biogas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a device for producing conditions for consecutive desulfurization of biogas.    Injector (1)    Tube (2)    Biogas stream (4)    Non-return valve (5)    Throttle valve (6)
NOVELTY - The apparatus has stirring blade (98) to stir organic waste accommodated in container (14). A vapor jet pipe (68) and steam generator (70) supply high temperature and high pressure heating steam in container. A pressure reduction pump (78) is arranged for carrying out pressure reduction within container. The stirring blade is operated while supplying heating steam and carrying out pressure reduction of container so that boiling process of organic waste is carried out within container.    USE - Apparatus for processing organic waste. Uses include but are not limited to vegetable debris, excrement, dead fish, offal, shellfish shell, food waste from industrial waste, agriculture, forestry, stock raising industry, fisheries, food processing sector, store, office and house.    ADVANTAGE - The boiling process can be carried out sufficiently and reliably, and organic waste in container can be stirred under sufficient high temperature and high pressure conditions.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of organic waste processing apparatus.    Container (14)    Vapor jet pipe (68)    Steam generator (70)    Pressure reduction pump (78)    Stirring blade (98)
NOVELTY - The furnace has a triple ventilation hole interconnected to a triple ventilation chamber and an inner side of a coal furnace core. Multiple triple ventilation pipes are plugged into a furnace body via a furnace bottom board. The triple ventilation pipes sequentially pass through a core barrel and an insulating material to enter into the ventilation chamber. An oven ring unit is arranged between top of an internal sleeve hole of a water jacket and an oven hole of a furnace surface board. A smoke chamber is arranged around a middle ring of an oven ring unit and connected to a smoke pipe bend.    USE - Two-section firewood and coal biomass gasification furnace.    ADVANTAGE - The furnace forms three ventilations that are rationally distributed, so that flammable gas can be completely combusted. The triple ventilation structure is simple, and has reduced manufacturing cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a two-section firewood and coal biomass gasification furnace in partial section.
NOVELTY - Green organic fertilizer is composed of cow dung, poultry dung, pig dung, microbial inoculum and sodium humate.    USE - Green organic fertilizer.    ADVANTAGE - The green organic fertilizer has double fertilizing efficiency and contains high amount of organic matters, beneficial microflora and active substances e.g. zinc, iron, sulfur, magnesium, calcium and other trace elements. The fertilizer is free from pathogenic bacteria, parasitic ovum and weed seeds, where the fertilizer contains more than 4% of quick-acting nitrogen, phosphorus and potassium and more than 30% of organic matters, and promotes yield of crops and improves the quality of crops.
NOVELTY - An eddy current, laminar current and pulse current type anaerobic bioreactor comprises upper gas collecting cover (13) in tank body (3), lower gas collecting cover inside and below upper gas collecting cover, return tube (17) arranged in center of the lower gas collecting cover (15), and water distributor (1) disposed on the bottom of the tank body to input sewage water.    USE - Eddy current, laminar current and pulse current type anaerobic bioreactor used for treating various organic sewage waters.    ADVANTAGE - The anaerobic bioreactor overcomes existing upflow anaerobic sludge blanket reactors, quickly starts, has high load and low equipment cost, and can produce usable methane and water, thus protecting environment.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the eddy current, laminar current and pulse current type anaerobic bioreactor.    Water distributor (1)    Tank body (3)    Upper gas collecting cover (13)    Lower gas collecting cover (15)    Return tube (17)
NOVELTY - An air permeable porous electrode comprises air permeable base-material surface on which reactive metal microparticle covered with film formed from compound which contains reactive sensitive group in one end and contains thiol group in other end has through-hole through film which is connected and fixed.    USE - Air permeable porous electrode for manufacturing fuel cell used in vehicle (claimed) and mobile telephone.    ADVANTAGE - The air permeable porous electrode is water repellent and oil repellent.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) manufacture of air permeable porous electrode involving coating paste containing solvent and hardening reactive metal formed in porous base material surface which has through-hole from compound containing reactive sensitive group in one end and thiol group in other end;    (2) air permeable porous spacer comprising alkoxy group and electrically insulating microparticles;    (3) manufacture of air permeable porous spacer involving using alkoxy group and electrically insulating microparticles;    (4) fuel cell comprising air permeable porous electrode and/or air permeable porous spacer; and    (5) manufacture of fuel cell involving using air permeable porous electrode and air permeable porous spacer.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the process of coating and hardening paste of catalyst metal microparticle coated with monolayer and of laminated spacer layer.    Air permeable solid electrolyte film (11)    Platinum microparticles (12)    Porous spacer layer (13)
NOVELTY - The modifier (50) has a combustion gas flow path (20) that is equipped with several flow stabilizers (100) mutually arranged by flow direction of combustion gas at predetermined intervals. A truncated-cone-shaped diffusion plate by which the ejection port ejects the combustion gas is provided in the surrounding surface with large diameter top opening end and small diameter lower opening end. A conical baseplate is provided for sealing the small diameter lower opening end of the truncated-cone-shaped diffusion plate.    USE - Modifier for fuel cell power supply devices.    ADVANTAGE - Since the baseplate is provided for sealing the small diameter lower opening end of the truncated-cone-shaped diffusion plate, the modifier can be operated efficiently even if the modifier is in sloped state.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the modifier.    Burner nozzle (2)    Heater (5)    Combustion gas flow path (20)    Modifier (50)    Flow stabilizer (100)
NOVELTY - Transesterification reaction of a lipid and a molar excess of a low molecular mass alkyl ester is carried out with an addition of an alcohol in the presence of an acidic catalyst, preferably toluenesulfonic acid to obtain biofuel.    USE - Manufacture of biofuel used as fuel or additive for petrochemical fuel oil for diesel engine.
NOVELTY - The system (S) has a concentration detection unit (6) that detects the concentration of the nitrous oxide gas (G) emitted from the sewage (W) in the aerobic tank (2). A menthol supply unit supplies menthol (M) in the sewage. A computer (5) controls the amount of menthol supplied to the sewage in the aerobic tank based on the change of the detection concentration.    USE - Generated-gas-amount reduction system.    ADVANTAGE - The generation amount of the nitrous oxide gas from the tank can be finely controlled by the control of the denitrifying reaction within the aerobic tank and generation amount of the nitrous oxide gas can be reduced with high precision.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for generated-gas-amount reduction method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the generated-gas-amount reduction system.    Aerobic tank (2)    Computer (5)    Concentration detection unit (6)    Nitrous oxide gas (G)    Menthol (M)    Generated-gas-amount reduction system (S)    Sewage (W)
NOVELTY - The method involves performing steps of multiphase separation, fermentation, biogas production and biological denitrification and dephosphorization, to translate domestic wastewater (2) and organic rubbish (1) into clear water and biogas (7), organic fertilizer (8) and sand residue, which are discharged directly. A multi-phase separation device is utilized for separating the domestic wastewater, where the device is provided with a domestic wastewater inlet.    USE - Method for integratedly treating domestic wastewater and organic rubbish.    ADVANTAGE - The method allows domestic wastewater and organic rubbish to be treated simultaneously, thus providing minimum pollutant discharge.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of an apparatus for integratedly treating domestic wastewater and organic rubbish.'(Drawing includes non-English language text)'    Organic rubbish (1)    Domestic wastewater (2)    Multiphase separation block (3)    Clear water and biogas (7)    Organic fertilizer (8)
NOVELTY - Pulsed electric field method for the continuous extraction of oil and lipids from small aquatic plants, comprises: providing a continuous flow of a slurry of small aquatic plants; directing continuous flow of small aquatic plants to a treatment zone (16); and applying pulsed electric fields to the treatment zone to lyse cell walls of the small aquatic plants to enhance extraction of oil and lipids from them.    USE - The pulsed electric field method is useful for the continuous extraction of oil and lipids from small aquatic plants including algae or phytoplankton (claimed), which is useful in the production of a biofuel.    ADVANTAGE - The pulsed electric field method: provides enhanced extraction of oil and lipids; minimizes energy consumption while achieving the desired level of lysing of the cells in the slurry; and minimizes the cost of pulsed electric field processing.    DESCRIPTION OF DRAWING(S) - The figure shows the schematic front-view of the primary components used for the method of continuous extraction of oil and lipids from small aquatic plants.    Pulsed electric field system (10)    High voltage electrode (12)    Treatment zone (16)    Ground electrode (20)    Insulator (24)
NOVELTY - The gas sensitivity material has microcrystalline selenium (1) which is positioned between two electrodes (3,4). The microcrystalline selenium responds to the organic gas which is derived from the volatile organic compound having dielectric constant in room temperature in the range of 1.0 to 38.0.    USE - Gas sensitivity material for gas sensor (claimed) for detecting carbon monoxide gas.    ADVANTAGE - The microcrystalline selenium can be easily produced and is less expensive, and can respond to organic gas molecules at a high sensitivity at room temperature without being affected by moisture. The microcrystalline selenium shows a change of different magnitude in the value of current flowing under a definite voltage, depending on the kind of an organic gas perceived, such that the kind of organic gas is determined based on the magnitude of change.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for gas sensor.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of the gas sensor.    Microcrystalline selenium (1)    Gas detection unit (2)    Electrodes (3,4)    Power supply (5)    Variable resistor (6)
NOVELTY - A recombinant microorganism capable of producing alcohol from metabolite comprising 2-keto acid, is new. The alcohol is chosen from 1-propanol, isobutanol (4-4.9 g/l), 1-butanol, 2-methyl 1-butanol, 3-methyl 1-butanol, and 2-phenylethanol. The recombinant microorganism has an increased tolerance to isobutanol compared to Escherichia coli, where the microorganism is isolated from parental Corynebacterium glutamicum.    USE - The recombinant microorganism, preferably C.glutamicum is useful for producing alcohols chosen from 1-propanol, isobutanol, 1-butanol, 2-methyl 1-butanol, 3-methyl 1-butanol, and 2-phenylethanol (all claimed) which is used in motor fuels e.g. cars.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) recombinant C.glutamicum comprising elevated expression or activity of 2-keto-acid decarboxylase, and alcohol dehydrogenase compared to parental microorganism, where the recombinant microorganism comprises at least one gene knockout or disruption encoding enzyme in a ppc, pyc, ldh, any of its homolog and their combinations and the recombinant microorganism produces isobutanol; and (2) method for producing alcohol, involves providing recombinant microorganism, culturing microorganism in the presence of substrate or metabolic intermediate under conditions for conversion of the substrate to alcohol, and substantially purifying the alcohol.
NOVELTY - Fuel additive comprises a synergistic combination of a cetane improver and a mineral oil co-additive.    USE - The fuel additive is useful for incorporating in a middle distillate fuel (which is diesel fuel, fuel oil and/or biofuels) for reducing nitrogen oxides emissions from an engine exhaust of an engine combusting the fuel (all claimed).    ADVANTAGE - The fuel additive: exhibits an unexpected synergistic decrease in nitrogen oxide emissions compared to other additives and additive combinations; and does not exhibit an adverse increase in particulate emissions compared to other additives used to improve nitrogen oxide emissions.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) an additive package for a middle distillate fuel comprising the fuel additive, where a volume ratio of the cetane improver to the mineral oil co-additive in the additive package is 1:1 to 30:1;    (2) a middle distillate fuel comprising the fuel additive or the additive package; and    (3) reducing nitrogen oxides emissions from an engine exhaust of an engine combusting a middle distillate fuel, comprising: incorporating the fuel additive in a middle distillate fuel; and combusting the fuel in the engine.
NOVELTY - Processing biomass comprises: conveying (16) biomass to pile (12) of biomass on platform (14); maintaining biomass in the pile in wetted condition, so that biomass has pH level in predetermined pH range and temperature in predetermined temperature range; applying an enzyme (30) to the biomass in the pile, where the enzyme extracts hemicelluloses from the biomass; draining (18) liquid from the pile of the biomass; removing the extracted hemicelluloses from the drained liquid; and returning to the pile at least portion of the drained liquid after removal of extracted hemicelluloses.    USE - The method is useful for processing biomass.    ADVANTAGE - The method maintains the pH in the desired ranges and prevents or suppresses the growth of unwanted bacteria and fungi in the piles, thus protecting the fibers and carbohydrates in the biomass.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for: apparatus to process biomass comprising: a platform supporting a pile of biomass; a drainage channel in the platform adapted to receive drainage liquid from the pile of biomass; a circulation system for liquid drainage extracted from the pile through the drainage channel, the circulation system including at least one conduits receiving and transporting the liquid drainage to a liquid discharge device proximate to the pile; an enzyme source included in the circulation system and adapted to provide an enzyme to the liquid drainage to be discharged by the liquid discharge device.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic diagram of a system for processing piles of biomass materials.    Pile (12)    Platform (14)    Biomass conveyor (16)    Drainage channel (18)    Enzyme (30)
NOVELTY - Lowering the cloud point of fatty acid esters, comprises: (a) providing fatty acid esters; (b) adding solvent to the fatty acid esters; (c) adding urea to the fatty acid esters; (d) mixing the fatty acid esters, solvent and urea; (e) evaporating substantially all of the solvent, thus forming a clathrate-liquid mixture; and (f) separating substantially all of the clathrates from the liquid in the mixture formed in step (e), thus forming refined fatty acid esters having a lower cloud point than that of the fatty acid esters provided in step (a).    USE - The method is useful for lowering the cloud point of fatty acid esters (claimed).    ADVANTAGE - The method is cost effective, robust and efficient in reducing the cloud point of biodiesel fuel.
NOVELTY - Recovering and purifying liquids used for biomass pretreatment, involves: removing particulate matter from a spent process stream of a biomass pretreatment process; and separating liquids present in the spent process stream of a biomass pretreatment process.    USE - For recovering and purifying liquids used for biomass pretreatment (claimed), which is used for production of biofuels and other biomass based products.    ADVANTAGE - The liquid recovery and purification minimizes waste production and enhances process profitability. The membranes are formed from organic or inorganic materials that provide the required separation characteristics and are stable in the chemical and thermal environment of the process. The incorporation of the membranes in spiral wound or hollow fiber modules permits effective contacting with process streams.
NOVELTY - The unit has furnace that is coated with fireproof and anticorrosive paint, whose lower portion is provided with slag blocking plate. A mobile grate is arranged below plate. An ash discharging gear is arranged below mobile grate. The upper end of furnace is provided with synthesis gas outlets while lower end is provided with gas inlet and oxygen and carbon dioxide agent inlet. The gas outlets are connected to synthesis gas inlet through pipeline. The gas outlets are connected to smoke condensing and purifying equipment through pipeline provided with valve.    USE - Gasification unit for municipal domestic waste.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for gasification method for municipal domestic waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the gasification unit for municipal domestic waste.
NOVELTY - The system has biomass raw material feeding system that supplies reaction raw material for fluidized bed gasification reaction. A separation device is arranged outside the fluidized bed gasification reactor. A gasification medium supplies gasification medium for fluidized bed gasification reactor. A ash discharge device is connected to the separation devices, which comprises discharge pipe, a valve and an ash conveying device.    USE - Biomass gasification reaction system with ash discharge device.    ADVANTAGE - The valve of ash discharge device can be opened so as to discharge the material of separation device, that ensures the success running of system. The gas combustion efficiency, smoke content is combusted gas and environment pollution can be reduced, so that the siltation process is convenient and easy by saving the maintenance time and avoiding the long-time stopping of system.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the biomass gasification reaction system.
NOVELTY - The method involves passing a hydrogen rich gas through a calcium oxide layer (12), and subsequently passing the gas through a lanthanum oxide layer (14), where one of the layers is supported by a porous material, and a ratio by weight of calcium oxide to lanthanum oxide is within a range of 2 to 3 units of calcium oxide for each unit of lanthanum oxide. A predominant amount of hydrogen sulfide is removed from the gas by the calcium oxide layer, and the remainder of the hydrogen sulfide is removed from the gas by the lanthanum oxide layer.    USE - Method for removing hydrogen sulfide from a hydrogen rich gas at temperatures in the range of 600 to 800 degrees Centigrade, for use in power generation by fuel cell. Can also be used in an emission control system.    ADVANTAGE - The method passes the gas through the calcium oxide layer and the lanthanum oxide layer, thus enabling to effectively and efficiently remove hydrogen sulfide for fuel reformation and fuel cell applications while utilizing a minimal amount of reactants by weight.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a desulfurization assembly for removing hydrogen sulfide from a gas while utilizing a minimal amount of reactants by weight, comprising a stage including a reactant    (2) a filter system for desulfurization, comprising two metal oxides.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic illustration of a bi-layer sorbent assembly.    Bi-layer sorbent assembly (10)    Enclosure (11)    Calcium oxide layer (12)    Lanthanum oxide layer (14)    Inlet (16)    Outlet (17)
NOVELTY - Producing hydrocarbon and hydrogen fuels comprises: (a) fermenting a biomass material containing fermentation medium with an inoculum comprising a mixed culture of microorganisms derived from the rumen contents of a rumen-containing animal and incubating under anaerobic conditions and for a sufficient time to produce volatile fatty acids in the medium; and (b) subjecting the volatile fatty acids or their salts to electrolysis under conditions effective to convert the volatile fatty acids or their salts to hydrocarbons and hydrogen.    USE - The method is useful to produce hydrocarbon and hydrogen fuels simultaneously from biomass by a combination of fermentation and electrolysis, where the biomass is cellulosic biomass, plants, plant parts, plant materials, agricultural crops, forages, grasses, aquatic plants, bagasse, corn stover, corn cobs, dried distillers grains, hay, flax straw, oat hulls, wood, sawdust, paper products, paper processing wastes, cardboard, yard or landscape waste, animal wastes, animal processing wastes, animal carcasses, or spent sausage casings (all claimed).    ADVANTAGE - The method provides an economic solution to biomass waste disposal by utilizing damaged, spoiled, or spent cellulosic commodities to produce hydrocarbon fuels, hydrogen and other chemical products by reprocessing them instead of discarding in landfills.
NOVELTY - Method of producing fatty acid esters, involves (i) culturing an engineered Cyanobacterium in a culture medium, where the engineered Cyanobacterium comprises a recombinant acyl-CoA synthetase and a recombinant wax synthase, and (ii) exposing the engineered Cyanobacterium to light and carbon dioxide, where the exposure results in the incorporation of an alcohol into fatty acid esters produced by the engineered Cyanobacterium.    USE - The method is useful for producing fatty acid esters, which are used in biofuels and chemicals.    DETAILED DESCRIPTION - Method of producing fatty acid esters, involves (i) culturing an engineered Cyanobacterium in a culture medium, where the engineered Cyanobacterium comprises a recombinant acyl-CoA synthetase and a recombinant wax synthase, and (ii) exposing the engineered Cyanobacterium to light and carbon dioxide, where the exposure results in the incorporation of an alcohol into fatty acid esters produced by the engineered Cyanobacterium. The fatty acid esters are chosen from tetradecanoic acid ester, Delta 9-hexadecenoic acid ester, hexadecanoic acid ester, heptadecanoic acid ester, delta 9-octadecenoic acid ester and octadecanoic acid ester. The amount of the fatty acid esters produced by the engineered Cyanobacterium is increased relative to the amount of fatty acid produced by an identical cell lacking the recombinant acyl-CoA synthetase or recombinant wax synthase.
NOVELTY - Method and device for dehydrating partially dehydrated sludge using organic portions, and for providing energy-rich fuel, are claimed. The method comprises adding partially dehydrated sludge in the form of aqueous-wet pellets (3) or in other forms, into hydrocarbon or hydrocarbon mixture.    USE - The method and the device are useful for dehydrating partially dehydrated sludge, and for providing energy-rich fuel.    ADVANTAGE - The method: expels the residual water content of the sludge in energy efficient manner; provides a fuel with high heat value and high fuel value; comprises the heating of the reactant at a temperature that is greater than the boiling point of the water and thus destructs the pathogens, bacteria and viruses; and removes small amount of pollutants present in the sludge in addition to dehydration.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the side view of the device for dehydrating the partially dehydrated sludge and for providing energy-rich fuel.    Feeding device for partially dehydrated sewage sludge (1)    Homogenization unit (2)    Aqueous-wet pellets (3)    Conveyor Chain (4)    Hot oil bath (5)
NOVELTY - Fire extinguishing agent, preferably dry extinguishing powder, comprises 0.0001-18 wt.% of ammonium phosphate and/or ammonium dihydrogen phosphate, 70-95 wt.% of ammonium sulfate and 0.1-9.9 wt.% of other auxiliary agents.    USE - The fire extinguishing agent is useful for the fire classifications of A, B and C (claimed).    ADVANTAGE - The fire extinguishing powder in the class of A, B and C has good extinguishing properties. The fire extinguishing agent: is produced economically and ecologically sensible, and by use of no other disposal costs; and has long shelf life.
NOVELTY - Method for modifying coal using biomass, involves performing dry distillation process of biomass to obtain biomass charcoal, contacting the obtained biomass charcoal and coal, reducing the water content ratio of the coal using sensible heat of the biomass charcoal and adhering tar present in the biomass charcoal to the coal.    USE - The method is useful for modifying coal used for manufacturing of iron and steel.    ADVANTAGE - The method reduces carbon dioxide emission and is environmentally-friendly.
NOVELTY - Method for manufacturing shaped charcoal using biomass, involves dry-distilling the biomass to obtain tar, adding coal and solid binder to the tar, and press-molding the obtained mixture.    USE - The method is useful for manufacturing shaped charcoal which is used in steel industry.    ADVANTAGE - The method is environmentally-friendly and cost-effective.
NOVELTY - The burner has a warming burner body formed by a material storage cylinder, a rectangular shaped empyreumatic oil purifier, a cooking burner head and a water tank. A material feeding barn utilizes a bottom air feeding manner for air feeding. A bottom part of the material feeding barn is provided with a draught fan. A bottom part of a pillar is sealed and welded by steel plate. The draught fan blows air into a cylinder body to form whirlwind, and is directly connected with a cylinder or a hemispheroid.    USE - Cooking type gasification burner for straw fuel.    ADVANTAGE - The burner utilizes empyreumatic oil chemolysis technology, exhaustive empyreumatic oil treatment purified gas and a material that is uniformly coated in a hearth with certain thickness, so that the burner satisfies cooking requirements. The burner is convenient and practical to use.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a cooking type gasification burner.
NOVELTY - A control method of slurry biochemical treatment loop comprises cascade controlling the organic load in the water, controlling food number of biochemically treated microbe, reducing energy consumption of slurry increasing link; cascade controlling the dissolved oxygen concentration in aeration pool, supplying the aeration pool to reduce the energy consumption of wind machine; feedforward-cascade controlling the concentration of the slurry in the aeration pool, controlling number of microbe in the slurry treatment system and reducing energy consumption of the slurry reflux link.    USE - A control method of slurry biochemical treatment loop.    ADVANTAGE - The method effectively controls the slurry increase, wind machine aeration and slurry reflux links, guarantees the stable water outlet and reduces energy consumption of the slurry biochemical treatment process, exerts loop cascade control and artificial intelligent control algorithm and solves the problem of traditional proportional-integral-derivative (PID) single loop that has bad ideal control effect.    DETAILED DESCRIPTION - The organic load setting value is controlled via the water outlet chemical oxygen demand (COD).    DESCRIPTION OF DRAWING(S) - The drawing is a flow diagram view illustrating the control method of slurry biochemical treatment loop (Drawing includes non-English language text).
NOVELTY - Activator for enhancing degradability of oil degrading bacteria comprises microbial activator, vitamin solution and microelement solution at a volume ratio of 1:1:1, where before using, the 3 solutions are stored individually. The microbial activator comprises Tween 80 (RTM: polyoxyethylene (20) sorbitan monooleate), monopotassium phosphate, magnesium sulfate heptahydrate, dipotassium phosphate and cane sugar. The vitamin solution comprises vitamin A, vitamin B and vitamin C. The microelement solution comprises zinc, cobalt, manganese, copper, molybdenum, nickel, selenium and boron.    USE - An activator for enhancing degradability of oil degrading bacteria and for oil sewage treatment (claimed).    DETAILED DESCRIPTION - An activator for enhancing degradability of oil degrading bacteria comprises microbial activator, vitamin solution and microelement solution at a volume ratio of 1:1:1, where before using, the 3 solutions are stored individually. The microbial activator comprises 1.0-10.0 mL/L of Tween 80 (RTM: polyoxyethylene (20) sorbitan monooleate), 0.02-1.0 g/L of monopotassium phosphate (KH2PO4), 0.01-0.5 g/L of magnesium sulfate heptahydrate (MgSO4.7H2O), 0.15-4.5 g/L of dipotassium phosphate (K2HPO4) and 0.5-20.0 g/L of cane sugar. The vitamin solution comprises 0.5-10.0 g/L vitamin A, 10.5-10.0 g/L of vitamin B and 0.5-10.0 g/L of vitamin C. The microelement solution comprises 0.05-0.15 g/L of zinc, 0.02-0.10 g/L of cobalt, 0.15-0.40 g/L of manganese, 0.02-0.20 g/L of copper, 0.04-0.35 g/L of molybdenum, 0.02-0.15 g/L of nickel, 0.04-0.30 g/L of selenium and 0.0007-0.003 g/L of boron.
NOVELTY - The combustor has an air outlet pipe transversally provided in a center part of a hollow cylindrical combustion chamber. A feed pipe and the air outlet pipe are connected with the combustion chamber. A left end of the air outlet pipe is fixed at an internally disposed end of the combustion chamber, and right end is an extension end and extended out of the combustion chamber. An air chamber is formed between a chamber part and the combustion chamber and connected with an air pipe. The air outlet pipe is formed with multiple air outlet holes, and the air chamber is connected with the holes.    USE - High-energy biomass gasification combustor for use in a boiler.    ADVANTAGE - The combustor compensates clean biomass gas to oxygen before entering a boiler to obtain more energy and to promote sufficient combustion of the biomass gas in the boiler, thus obtaining maximum combustion energy of the boiler.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a high-energy biomass gasification combustor for use in a boiler.
NOVELTY - The furnace has an ash discharging chamber (14) formed on a bottom end of a gasification furnace body (1). A side of an upper part of an oven drying section (11) is provided with a gas discharging mouth (2). An upper side of the ash discharging chamber and a lower side of a closed mouth of the furnace body are provided with multiple gas inlets (3). A gas discharging hole (4) is connected with a deformed brick interlayer (5). Multiple small pore diameter water inlets (18) are provided on a throat of the furnace body and directly connected with an inner cavity of the furnace body.    USE - Pyrolysis gasification furnace for urban solid waste.    ADVANTAGE - The furnace utilizes a reactor for effectively treating urban solid waste with low apparatus price, less operation cost and high energy and resource recycling rate.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a pyrolysis gasification furnace for urban solid waste.    Gasification furnace body (1)    Gas discharging mouth (2)    Gas inlets (3)    Gas discharging hole (4)    Deformed brick interlayer (5)    Oven drying section (11)    Ash discharging chamber (14)    Small pore diameter water inlets (18)
NOVELTY - The disk has a left area (1), middle area (2), right area (3), upper area (4) and a lower area (5) respectively formed on cross-shaped left, right, upper and lower parts, where the disc is in cross-shape. The middle area is formed on a cross-shaped central node, and the left area is provided with an air inlet (6). The lower area is close to an ash inlet and an ash outlet. The left area, the middle area, the lower area, right area and the upper area are formed with the Phi 24 millimeters of oxygen supplying holes (8).    USE - Oxygen supplying disk for a straw gasification furnace.    ADVANTAGE - The size of the oxygen supplying holes is determined according to the wind speed to reach the purpose of uniformly supplying oxygen, thus avoiding phenomenon of burning-out and burning in inclined way    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of an oxygen supplying disk for a straw gasification furnace.    Left area (1)    Middle area (2)    Right area (3)    Upper area (4)    Lower area (5)    Air inlet (6)    Oxygen supplying holes (8)
NOVELTY - The system has an indirect cooling tower (7) whose inlet end is connected with a water recycle pool (21). A purification tower (9) is connected to a fine purifier (11) through a root blower (10). A second-stage coarse purification tower (6), the indirect cooling tower, the purification tower and fine purifier are provided with ball valves and connected with a vinegar tar pool (16). Two ends stages of a self-cooling deduster, purification towers, a gas water separation tower (8) and bottom of the purification tower are provided with floss holes (20).    USE - Biomass dry gasification centralized gas supply system.    ADVANTAGE - The system can continuously run a gasification furnace without polluting water. The system avoids need of large-scale gas storage cabinet. The system has high gas quality, high utilization ratio and low manufacturing cost. The system is energy-saving and environment-protecting.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a biomass dry gasification centralized gas supply system.    Second-stage coarse purification tower (6)    Indirect cooling tower (7)    Gas water separation tower (8)    Purification tower (9)    Root blower (10)    Fine purifier (11)    Vinegar tar pool (16)    Floss holes (20)    Water recycle pool (21)
NOVELTY - The device has a gasification reaction chamber (16) and a combustion chamber (3) that are combined into a single structure and separated through a water cooling furnace. The gasification reaction chamber is connected with a gas stove (15). The combustion chamber is connected with a flame-out dust removing chamber (26) through a flame spiral flowing port (24) via a side surface. A heat exchanging unit is arranged between a smoke passage (19) and the flame-out dust removing chamber and mounted on a device cavity.    USE - Multifunctional household biomass gasification heat supplying device.    ADVANTAGE - The device has functions of cooking, warming and bathing. The device has clean combustion effect, strengthened heat transmission effect and high heat efficiency, is inexpensive and easy to popularize.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a multifunctional household biomass gasification heat supplying device.    Combustion chamber (3)    Gas stove (15)    Gasification reaction chamber (16)    Smoke passage (19)    Flame spiral flowing port (24)    Flame-out dust removing chamber (26)
NOVELTY - A compound bacterium comprises bacterium and carrier. The bacterium includes (pts. wt.): Cellulomonas fimi (15-30), Basidiomycetes (10-25), Bacillus (5-15), Aspergillus (15-35), Neurospora (5-35), Trichoderma (8-20), actinomycetes (15-20) and saccharomycetes (5-15). The carrier is chitosan, rice bran, sawdust and/or soil.    USE - Compound bacterium for degrading landscaping garbage (claimed).    ADVANTAGE - The compound bacterium has synergistic effects, increases landscaping garbage degrading efficiency, rapidly rusts organic material and converts into green organic fertilizer for improving soil. The compound bacterium also effectively improves soil occupation caused by landfill or environment pollution caused by burning.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the compound bacterium which comprises inoculating bacterium in culture medium and shaking for 48-72 hours in shaking bed at 35 degrees C and 120 revolutions/minute; diluting to form bacterium solution until per ml of bacterium contains 5000000000; and absorbing bacterium solution to carrier according to 2000000000 bacterium per gram of carrier and obtaining desired compound bacterium.
NOVELTY - Purifying surface water body comprises selecting reed swamp; then using surface root hair of the reed in the swamp to prepare fixed carriers of petroleum degrading bacteria; using the actual petroleum polluted river as the swamp water inlet source; slowly flowing through the surface of the swamp by using the manner of overflowing on the surface according the condition that the water inlet flow rate of unit surface area is not more than 0.0075 m3/hour so as to obtain the removing effect of the petroleum, which meets the index of the national surface water environment quality standard.    USE - Method for purifying surface water body, particularly river polluted by petroleum in the port.    ADVANTAGE - The method is simple, low in cost, and easy to operate.
NOVELTY - The system has a wooden carbon kiln (1) in which the top is connected with the lower portion of a self balancing oil liquid separator (2). One end of the ventilating pipe (4) is connected with one side of a big energy precise smoke processor (7). The big energy precise smoke processor (7) is connected with one end of a drafting and pressure adjusting system (8) by a pipeline at the top, and the other end of the drafting and pressure adjusting system (8) is connected with an air storage jar (9).    USE - Conversion system for preparing carbon, air and oil by biomass.    ADVANTAGE - The system is featured with clear flow process, high generated heat value, and can be convenient used. Long service life and high cost performance are achieved. Environment is not polluted by the products and discharged materials.    DETAILED DESCRIPTION - One end of the self balancing oil liquid separator (2) is connected with one end of a multi-medium smoke and dust processor (3) by a horizontal pipe (6). The other end of the multi-medium smoke and dust processor (3) is connected with the lower portion of a ventilating pipe (4).    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the conversion system.    Wooden carbon kiln (1)    Self balancing oil liquid separator (2)    Multi-medium smoke and dust processor (3)    Ventilating pipe (4)    Horizontal pipe (6)    Big energy precise smoke processor (7)    Drafting and pressure adjusting system (8)    Air storage jar (9)
NOVELTY - The prevention of slagging involves using a mixture of air and vapor as a biomass gasifying agent. Preferably, gasifying waste water is used as a water source, and coal gas heat is used as heat source for producing the vapor. Preferably, the volume ratio of the air with respect to the vapor in the biomass gasifying agent is 1 is to 1 to 12 is to 1.    USE - Prevention of slagging on low-ash-melting-point biomass-raw-material fixing bed of gasifying furnace.    ADVANTAGE - Can effectively relieve the scorification of the furnace, thus guaranteeing the effective and stable operation of the furnace. Provides a simple, rational, energy-saving, and environment-friendly process without other investment costs.
NOVELTY - The biomass gasification power generation involves performing raw material pretreatment, biomass static bed gasification, gas purification, and fuel gas power generation. Preferably, the raw material pretreatment involves biomass collecting, drying and forming operations. Preferably, a biomass raw material comprises crop straw.    USE - Biomass gasification power generation using furnace with scale static bed.    ADVANTAGE - Enables comprehensive utilization of resources while protecting the environment. Enables generation of gas with a high heat value. Allows generated residue and tar to be comprehensively used to save cost. Enables full utilization of generated heat, thus improving heating efficiency and reducing operation cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an assorted equipment for biomass gasification power generation for scale static bed.    DESCRIPTION OF DRAWING(S) - The drawing shows the flow diagram of biomass gasification power generation. (Drawing includes non-English language text).
NOVELTY - The method involves directly washing, cooling and electro fishing the tar at intermediate temperature. The gas is cooled indirectly and electrofishing of tar is performed at normal temperature. Dechlorination and desulfurization is performed.    USE - Biomass gasified fuel gas purifying method.    ADVANTAGE - The obtained purified gas can meet the combustion and generating the requirement, environment can be protected from harmful gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram illustrating the biomass gasified fuel gas purifying process.(Drawing includes non-English language text)
NOVELTY - The pipe type reactor has a plate orifice group that is provided in a reactor pipe having fluid inlet end and outlet end connected with a piston. A reciprocal harmonic movement drive mechanism is arranged for controlling advancement or withdrawal of fluid in the reactor pipe. The drive shafts are attached to the ends of the drive mechanism.    USE - Pipe type reactor for producing biomass diesel oil.    ADVANTAGE - Turbulent flow of fluid can be generated efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the reactor.
NOVELTY - The corn picker has hydrogen manufacturing device (5) that generates hydrogen based on the current generated by wind driven generator (2). The hydrogen is stored in fuel storage container (8) through hydrogen delivery pipeline (6) and is delivered to hydrogen fuel battery (10). A corn delivery device (19) is connected with drying device (20) and corn picking and peeling device (17) mounted behind a hydraulic lifter (16). The hydraulic lifter is mounted behind stalk cutting device (15) for regulating position of stalk cutting device.    USE - Corn picker.    ADVANTAGE - The hydrogen manufacturing device generates hydrogen based on current generated by wind driven generator and stores in fuel storage container such that the electric energy is realized by electrochemical reaction in the fuel battery and the energy is used effectively for corn cutting, corn picking and peeling operations.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the corn picker.    Wind driven generator (2)    Hydrogen manufacturing device (5)    Hydrogen delivery pipeline (6)    Fuel storage container (8)    Hydrogen fuel battery (10)    Stalk cutting device (15)    Hydraulic lifter (16)    Corn picking and peeling device (17)    Corn delivery device (19)    Drying device (20)
NOVELTY - The device has blade (1) which is rotated by wind power, and wind power generator (2) provided on top of hollow strut (3), that is driven to generate current. The current is inputted to electrolysis water hydrogen producing device (5) so as to generate hydrogen by conducting wire (4). A hydrogen fuel battery (10) is connected to hydrogen producing device and motor (11) by conducting wire. A power output shaft (12) of motor, is connected with turntable (14) of cutter (13). A handrail direction handle (20) is arranged on power base flat plate (19) arranged behind cutter.    USE - Power device for supplying hydrogen energy to gardening grass cutter.    ADVANTAGE - The hydrogen energy can be supplied efficiently to cutter, hence over height green grass can be cut easily by using blade. The performance efficiency of power device can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of power device.    Blade (1)    Wind power generator (2)    Hollow strut (3)    Conducting wire (4)    Hydrogen producing device (5)    Hydrogen fuel battery (10)    Motor (11)    Power output shaft (12)    Cutter (13)    Turntable (14)    Power base flat plate (19)    Handrail direction handle (20)
NOVELTY - Low-carbon bio-petroleum product comprises 0.1-50% of bio-petroleum or ammonia and 50-99.5% of acetone or butanol and/or gasoline, diesel oil or coal oil.    USE - Used as a low-carbon bio-petroleum product.    ADVANTAGE - The low carbon in the product is achieved by using carbon absorbing energy plants planted in wind farms and saline-alkali soil; The wind farm, the saline-alkali soil and bio-fuel are interacted to achieve low carbon product through never inexhaustible environmentally friendly oil flied and low carbon oil wells. The damage of rainforests, wet lands and soil can be prevented. The product can improve production efficiency of small scale farmers and change current status of combustion of straws and environmental pollution. The product has economical benefit.
NOVELTY - Hydrogen producing device, comprises a refuse crusher (2), a fluid pump, a fermentation type hydrogen-producing reactor (3) and a photosynthetic type hydrogen-producing reactor (4). The fermentation type hydrogen-producing reactor and a reaction drum of the photosynthetic hydrogen-producing reactor are provided with flow guide drums, whose wall is provided with a light source. The fermentation type hydrogen-producing reactor and a reaction solution inlet pipe of the photosynthetic hydrogen-producing reactor are arranged on the top of the reaction drum.    USE - The device is useful for producing hydrogen using organic household refuse.    DETAILED DESCRIPTION - Hydrogen producing device, comprises a refuse crusher (2), a fluid pump, a fermentation type hydrogen-producing reactor (3) and a photosynthetic type hydrogen-producing reactor (4) connected in sequence. The fermentation type hydrogen-producing reactor and a reaction drum of the photosynthetic type hydrogen-producing reactor are provided with flow guide drums for internally circulating on the same axis. The wall of the flow guide drum in the photosynthetic type hydrogen-producing reactor is provided with a light source. The fermentation type hydrogen-producing reactor and a reaction solution inlet pipe of each set of the photosynthetic type hydrogen-producing reactor are arranged on the top part of the reaction drum and are extended to the flow guide drum after entering the reaction drum. The fermentation type hydrogen-producing reactor and a reaction solution outlet of each set of the photosynthetic type hydrogen-producing reactor are higher than the upper end surface of the flow guide drum.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the hydrogen producing device.    Refuse crusher (2)    fermentation type hydrogen-producing reactor (3)    Photosynthetic type hydrogen-producing reactor (4)    Photocatalytic reactor (5)
NOVELTY - Methylobacterium (1xb-3), which forms small, smooth, non-transparent and light pink colored colonies with regular edges on a beef extract and peptone culture medium, with a preservation number CGMCCNo.3713, is new.    USE - The bacterial strains are useful for degrading high molecular weight PAHs in soil or wastewater, and for environmental remediation (claimed).    ADVANTAGE - The bacterial strains are highly efficient in degrading the PAHs.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for: (1) Burkholderia (1xb-5), which forms white, semitransparent, irregular colonies on the beef extract and peptone culture medium, which are not easy to pick, with a preservation number CGMCCNo.3714; (2) Rhodococcus (1xb-6), which forms large, wetted and regular edged red colonies on the beef extract and peptone culture medium plate, with a preservation number CGMCCNo.3715; (3) Phyllobacterium (1xb-9), which forms milky white, non-transparent, regular edged colonies on the beef extract and peptone culture medium, with a preservation number CGMCCNo.3716; (4) high molecular weight polycyclic aromatic hydrocarbon (PAH) degrading bacterial strains, comprising the above mentioned four bacterial strains; (5) preparing the high molecular weight PAH degrading bacterial strains, comprising: inoculating Methylobacterium (1xb-3), Burkholderia (1xb-5), Rhodococcus (1xb-6) and Phyllobacterium (1xb-9) into the beef extract and peptone culture medium, culturing up to log phase, centrifuging, discarding the supernatant, washing with phosphate buffer, centrifuging, discarding the supernatant to obtain a bacterial suspension, and mixing the four bacterial suspensions; and (6) use of the bacteria or bacterial strains in degrading five high molecular weight PAHs e.g. benzo(a)anthracene, benzo(b)fluoranthene, benzo(k)fluoranthene, benzo(a)pyrene and indeno(1, 2, 3-cd)pyrene in soil or wastewater by biological treatment and environmental remediation.
NOVELTY - Gordonia alkanivorans S104 strain has preservation number CGMCC No.4224, and is new. The strain is preserved in the China common microbial culture preservation center. The strain is Gram-positive bacterium and is rod-shaped.    USE - Gordonia alkanivorans S104 strain used for degrading oils such as raw oil, diesel, soybean oil and olive oil (claimed).    ADVANTAGE - The Gordonia alkanivorans S104 strain can prevent pollution caused by raw oil and diesel.
NOVELTY - Preparing biofuel i.e. ethanol involves utilizing biomass raw material and culturing microbial cell. The cultured cells are saccharified, fermented, distilled and dehydrated. The cell culturing is carried out by using a culture medium containing fungus, bacterium, Actinomycetes and Saccharomycetes. The culture medium contains 3-20 parts carbon sources, 1-15 parts nitrogen sources, 1-10 parts nutritive salts, 1-5 parts growth hormones and 50-94 parts water.    USE - Method for preparing biofuel i.e. ethanol (claimed).    ADVANTAGE - The method enables to prepare biofuel i.e. ethanol in a cost-effective and eco-friendly manner.    DETAILED DESCRIPTION - Preparing biofuel i.e. ethanol involves utilizing biomass raw material and culturing microbial cell. The cultured cells are saccharified, fermented, distilled and dehydrated. The cell culturing is carried out by using a culture medium containing fungus, bacterium, Actinomycetes and Saccharomycetes. The culture medium contains 3-20 parts carbon sources, 1-15 parts nitrogen sources, 1-10 parts nutritive salts, 1-5 parts growth hormones and 50-94 parts water. The culture medium is kept in an incubator in which air enters through an air compressor. The culture medium is kept at 20-39 degrees C and pH 3.0-8.5 for 40-150 hours. The materials are saccharified in the culture medium with distillers yeast. The saccharified materials are then utilized for culturing microbial cell.
NOVELTY - The device has cone reflector (3) through which light is lighted to radiator (4), when sunlight is incident on disc-type reflector (1) vertically and secondary lens (2) collects incident light. A ray emitted on surface of radiator is used for performing photoelectric conversion on photovoltaic cell (5). The generated electricity is stored by storage battery (6). The positive and negative poles (9,10) of polymer electrolytic tank (20), that are formed using multi-hole platinum material are attached to surface of proton exchange film (16).    USE - Device for manufacturing hydrogen using solar thermal photovoltaic system.    ADVANTAGE - The power consumption of device for manufacturing hydrogen is reduced with increased use rate of solar energy. The solar thermal photovoltaic system has higher conversion efficiency. The device is capable of using the electric energy that is generated during the hydrogen manufacturing process and is independent of temperature changes of the environment.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of device for manufacturing hydrogen.    Disc-type reflector (1)    Secondary lens (2)    Cone reflector (3)    Radiator (4)    Photovoltaic cell (5)    Storage battery (6)    Positive pole (9)    Negative pole (10)    Proton exchange film (16)    Polymer electrolytic tank (20)
NOVELTY - Production of hydrogen from anaerobically digested organic materials comprises placing the materials in a reaction zone; and applying an electric potential across the materials; thus producing hydrogen and carbon dioxide where electric potential is applied occasionally after periods without application of the electric potential.    USE - Process for producing hydrogen from anaerobically digested organic materials.    ADVANTAGE - The method does not require the use of fossil fuels, can serve communities that have relatively undeveloped electricity distribution and other energy infrastructures with a system that provides useful energy from collected wastes, and can separate carbon dioxide, nitrogen and other gases from produced hydrogen.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a process for conversion of biomass wastes into useful energy comprising application of intermittent voltage for purposes selected from group including depression of microorganismal activity that produces methane, enhancement of microorganismal activity that produces hydrogen, and creation of an atmosphere within the biomass wastes that is maintained rich in hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing is a flow chart showing both production of hydrogen and suppression of methanogenesis from anaerobically decomposed organic materials in the presence of an applied electropotential, and methanogenesis from anaerobically decomposed organic materials in the absence of an applied electropotential.
NOVELTY - The natural-gas helium extractor has a natural gas feeding pipeline (1) that is connected to heat exchanger (2) and rectifying tower (3). A helium discharging pipeline (5) is provided in the top of rectifying tower. A rectifying liquid pipeline (6) is provided in the bottom of rectifying tower and is led from the heat exchanger to be connected to an expander (4). A tail gas discharging pipeline (7) is provided in the expander.    USE - Natural-gas helium extractor.    ADVANTAGE - The Natural-gas helium extractor eliminates the need for liquid to improve the cooling efficiency of the expander. The separation pressure and temperature of the rectifying tower in the helium extraction technique is improved, hence the power consumption needed in the cooling liquefying separation is reduced. The pressure of the external input natural gas is reduced and the expansion ratio of the external natural gas is improved, hence the cooling efficiency is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the natural-gas helium extractor.    Natural gas feeding pipeline (1)    Heat exchanger (2)    Rectifying tower (3)    Expander (4)    Helium discharging pipeline (5)    Rectifying liquid pipeline (6)    Tail gas discharging pipeline (7)
NOVELTY - A cyclic unit has cyclic pipeline that transmits electrolyte, hydrogen and oxygen. A gas pipeline is connected with temporary storage barrel to output hydrogen and oxygen. A return pipeline is connected with liquid storage barrel and electrolysis bath. A cooling unit has radiation fan corresponding to cyclic pipeline. Each electrode plate of electrolysis unit is formed with cyclic hole and through hole. The cyclic pipeline has inflow port connected to through hole. The return pipeline has backflow port connected through electrolysis bath.    USE - Cyclic electrolysis device.    ADVANTAGE - A cyclic electrolysis device can be provided at low power consumption.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic side view of the cyclic electrolysis device.
NOVELTY - A cyclic calefacient film type biogas tank comprises a film type biogas tank comprising a feeding pipe, a discharging pipe, a biogas conveying pipe, a pressure resistant cyclic heating cushion, and a cyclic tube inlet and outlet; where the film type biogas tank body is compounded by polyvinyl chloride high molecular material; the upper part of the biogas tank is connected to the feeding pipe and the discharging pipe; the upper part of the side surface is connected to the biogas conveying pipe; and the bottom of the tank body is connected to the pressure resistant cyclic heating cushion.    USE - The cyclic calefacient film type biogas tank is useful for industrial and commercial applications.    ADVANTAGE - The cyclic calefacient film type biogas tank solves biogas production in winter in cold area; where the mounting is convenient; and the popularization and use are easy.    DETAILED DESCRIPTION - A cyclic calefacient film type biogas tank comprises a film type biogas tank comprising a feeding pipe, a discharging pipe, a biogas conveying pipe, a pressure resistant cyclic heating cushion, and a cyclic tube inlet and outlet; where the film type biogas tank body is compounded by polyvinyl chloride high molecular material; the upper part of the biogas tank is connected to the feeding pipe and the discharging pipe; the upper part of the side surface is connected to the biogas conveying pipe; the bottom of the tank body is connected to the pressure resistant cyclic heating cushion; the upper part of the pressure resistant cyclic heating cushion is wave-shaped and has large superficial area; the internal is S-shaped cyclic tube structure; the lower part is connected to a cyclic tube inlet and outlet; and the pressure resistant cyclic heating cushion is integrally connected to the biogas tank after processing.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the cyclic calefacient film type biogas tank.
NOVELTY - A sewage water purifier comprises shell, water outlet arranged on shell, water inlet arranged under shell, drain outlet arranged under shell, current amplifying cones arranged at the bottom and top of shell, mineral substance filled in lower part, and vertical porous water guiding pipes arranged at upper part. The lower end of porous water guiding pipe is closed while upper end is opened and arranged under current amplifying cones. The fibers are filled to porous water guiding.    USE - A sewage water purifier.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of sewage water purifier.
NOVELTY - The method involves mixing 1-30 parts by weight of calcium hydroxide, 1-30 parts by weight of soil sugar and 1-30 parts by weight of activated charcoal into a mixer. The carbonized mixture is pulverized to fine particles, and microbe tint coloring is mixed with 1-50 parts by weight of the pulverized mixture. 1-100 milliliter of distilled water is injected in the microbe tint coloring, and the microbe tint coloring is agitated to cultivate the microbe.    USE - Method for blending food and control appointment microbe tint coloring in a home and restaurant.    ADVANTAGE - The method enables providing better annihilation capability, reducing ferment smell, improving the activity of the microbe with long-term maintenance and efficiently removing moisture generated in food waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of a food and control appointment microbe tint coloring blending method.'(Drawing includes non-English language text)'
NOVELTY - Bacillus subtilis culturing involves inducing and culturing Bacillus subtilis containing cetyl in traditional industrial production to prepare petroleum-degrading enzymes (SYM) new strain. A nutrient buffering solution containing carbon and nitrogen is prepared. A culture medium and additive are also provided in a tank for fermenting and culturing petroleum enzyme.    USE - Method for culturing Bacillus subtilis used for decomposing paraffin component of petroleum (claimed).    ADVANTAGE - The method enables to culture Bacillus subtilis which improves decomposition rate of paraffin component of petroleum by reducing viscosity and freezing point of raw oil.
NOVELTY - Using fermented waste solution of nisin as nitrogen source involves dissolving 3.25g/l of sodium dihydrogen phosphate, 3.11g/l of disodium hydrogen phosphate, 2.14g/l of glucose, 20g/l of amylase, 0.13g/l of Tween 80 (RTM: Polysorbate 80), 30-80g/l of corn powder, 0-30g/l of corn starch, 150-700g/l of fermented waste solution of nisin and 0-20g/l of soybean protein to form a culture medium.    USE - Method for using fermented waste solution of nisin as nitrogen source for producing chymosin through fermentation (claimed).    ADVANTAGE - The method enables to use fermented waste solution of nisin in a cost-effective and eco-friendly manner.    DETAILED DESCRIPTION - Using fermented waste solution of nisin as nitrogen source involves dissolving 3.25g/l of sodium dihydrogen phosphate, 3.11g/l of disodium hydrogen phosphate, 2.14g/l of glucose, 20g/l of amylase, 0.13g/l of Tween 80 (RTM: Polysorbate 80), 30-80g/l of corn powder, 0-30g/l of corn starch, 150-700g/l of fermented waste solution of nisin and 0-20g/l of soybean protein to form a culture medium. pH of the culture medium is regulated at 6.7-6.8 by using 5-6% sodium hydroxide. A culture solution is prepared by inoculating Rhizomucor miehei in a culture medium at 37-38 degrees C for 20-24 hours at 260 revolutions per minute. The materials are kept in a 250ml triangular flask at 37-38 degrees C for 96 hours at 260-280 revolutions per minute to obtain chymosin. The corn powder contains 1.075wt.% of nitrogen, fermented waste solution of nisin contains 0.24wt.% of nitrogen, and soybean protein contains 8wt.% of nitrogen.
NOVELTY - A carbon catalyst has a sum total of 0.06 mmol or more per 0.02 g with respect to desorption amount of carbon monoxide and desorption amount of carbon dioxide at 150-400 degrees C in a temperature programmed desorption.    USE - Carbon catalyst is used for electrodes of batteries (both claimed) e.g. polymer electrolyte fuel cells. Can also be used as synthesis catalyst, environmental catalyst, air-cell electrode catalyst, hydrogen-peroxide decomposition catalyst, and as catalyst in oxygen reductive reaction.    ADVANTAGE - The carbon catalyst has improved activity and economical efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of carbon catalyst, which involves carbonizing (S1) a raw material containing an organic compound, a metal, and an electroconductive carbon material as a carbon source to obtain a carbonized material, impregnating (S2) a metal in the carbonized material, and heat-processing (S3) the carbonized material.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of the manufacturing method of carbon catalyst. (Drawing includes non-English language text)    Carbonization (S1)    Impregnation (S2)    Heat-processing (S3)
NOVELTY - Process (I) of converting syngas to a liquid fuel comprises: (a) generating or providing syngas; (b) dividing the syngas into a first syngas stream and a second syngas stream; (c) converting at least some of the first syngas stream to methanol using a methanol-synthesis catalyst; (d) converting at least some of the methanol to at least one gasoline component using a zeolite catalyst; and (e) converting at least some of the second syngas stream to ethanol using a biocatalyst.    USE - The process is useful for converting syngas to a liquid fuel including methanol, ethanol, gasoline, ethanol-containing gasoline blendstock, ethanol-containing gasoline fuel (all claimed), dimethyl ether, and gasoline components including alkanes, cyclic or branched hydrocarbons, olefins, aromatics, alcohols, ethers, ketones and aldehydes.    ADVANTAGE - The process: converts syngas to the gasoline components, which meets the fuel specification of ASTM D 4814-09a; and reduces overall energy intensity and/or number of processing steps in the production of renewable gasoline.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a process (II) of converting syngas to an ethanol-containing gasoline blendstock comprising: generating syngas from gasification of a carbon-containing feedstock; converting at least some of the syngas to methanol using a methanol-synthesis catalyst; converting at least some of the methanol to at least one gasoline component using a zeolite catalyst; converting at least some of the syngas to ethanol using a biocatalyst; and combining the gasoline components with the ethanol, to produce an ethanol-containing gasoline blendstock; and    (2) a fuel composition produced by a process comprising: steps (a)-(e) as above per se; and (f) combining the gasoline components and ethanol, to produce a fuel composition.
NOVELTY - Preparing biological coal comprises processing biomass briquette by drying, carbonizing, and cooling into biological coal through carbonization conversion technology.    USE - The process is useful for preparing biological coal (claimed).    ADVANTAGE - In utilizing the process, the prepared biological coal provides a solution for problems of storage, transportation and fire-prevention in the process of biomass utilization process, and is capable of being burned for electricity directly.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of the process for preparing biological coal (Drawing includes non-English language text).
NOVELTY - Processing method of low-flash-point waste oil involves mixing low-flash-point waste oil and biomass.    USE - Processing method of low-flash-point waste oil used for solid fuel (claimed).    ADVANTAGE - The low-flash-point waste oil is processed efficiently and economically with excellent handling property and improved flash point.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for solid fuel.
NOVELTY - The method involves preheating a metal plate with a heating furnace, and griping the preheated metal plate with a conveying apparatus. The preheated metal plate is conveyed to an injection molding machine. The metal plate is set in a metal mold of the injection molding machine. The conveying apparatus is conveyed while the metal plate is heated with a heating apparatus. A suction-tube (52) is supported by a supporting member (53) and provided in between a pad (51) and a heater (54).    USE - Method for manufacturing a separator of a fuel cell in a motor vehicle.    ADVANTAGE - The conveying apparatus is conveyed while the metal plate is heated with the heating apparatus, thus suppressing temperature variation of the metal plate, and hence improving dimensional accuracy of a resin component.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a holding part of a conveying apparatus.    Holding part (5)    Pad (51)    Suction-tube (52)    Supporting member (53)    Heater (54)
NOVELTY - The cell module (10) has a vaporization part generating raw fuel gas to heat up water content and raw fuel. The vaporization part contains water vapor. A modification part generates fuel gas to reform the raw fuel gas supplied from the vaporization part. The modification part contains hydrogen. Fuel gas flows into an inside part through a fuel gas flow channel when producing electric power with oxidizing agent gas. A combustion part (70) burns the fuel gas discharged from a cell stack (30a) between a modifier (20) and the cell stack.    USE - Fuel cell module.    ADVANTAGE - The fuel cell module uniformly maintains temperature distribution in the modifier.    DESCRIPTION OF DRAWING(S) - The drawing shows a vertical cross-sectional view of a fuel cell module.'(Drawing includes non-English language text)'    Fuel cell module (10)    Storage container (12)    Modifier (20)    Cell stack (30a)    Combustion part (70)
NOVELTY - The method involves coating an electrolyte on a surface of a catalyst-carrying carbon. The catalyst-carrying carbon and a solvent are mixed to produce a catalyst ink by a mixing process. A spray coating of the catalyst ink at a base material is carried out by a spraying process. The solvent is a poor solvent of the electrolyte.    USE - Method for manufacturing a fuel cell supplying an electric power to a load apparatus i.e. motor.    ADVANTAGE - The spray coating of the catalyst ink at the base material is carried out by the spraying process, thus producing uniform thickness in the catalyst layer.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a manufacturing method of a fuel cell for processing a cathode catalyst layer. '(Drawing includes non-English language text)'
NOVELTY - A compost is obtained by mixing organic wastes with ground moisture-absorbing material, charging obtained mixture in fermenter for aerobic composting, and introducing inoculating additive (2-7 mass%) after unloading of mass from fermenter on area. Unloading is produced immediately after beginning of decrease in maximum temperature, and then the mass is maintained in collars for 30 days.    USE - Method for obtaining compost (claimed).
NOVELTY - The method comprises passing vapor in a steam pipeline, subjecting the molecules of vapor to action of electrons flow, and exposing the molecules to high-frequency microwave irradiation. The electrodes are placed inside the steam pipeline.    USE - The method is useful for obtaining hydrogen from vapor.
NOVELTY - A production and utilization method of hydrogen involves generating biogas containing hydrogen and carbon dioxide using biomass by hydrogen fermentation, and separating carbon dioxide from gas derived from biogas.    USE - A production and utilization method of hydrogen.    ADVANTAGE - The method obtains hydrogen efficiently and reduces carbon dioxide emission.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of production and utilization method of hydrogen. (Drawing includes non-English language text).
NOVELTY - An organic sludge generation apparatus comprises dispersion microbe tank (1) which is introduced with solution containing organic substance and thrown with dispersion microbe for decomposing organic substance, and separation apparatus which separates organic sludge from solution processed by dispersion microbe tank. The retention of solution in dispersion microbe tank is completed before microbes other than dispersion microbe become dominant.    USE - Organic sludge generation apparatus for fats and oils manufacturing system (claimed) used for wastewater treatment business and energy business.    ADVANTAGE - The apparatus efficiently generates organic sludge.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) generation method of organic sludge involving introducing solution containing organic substance into dispersion microbe tank into which dispersion microbe which decomposes organic substance is thrown, separating organic sludge from solution processed by dispersion microbe tank, and completing retention of solution in dispersion microbe tank before microbes other than dispersion microbe become dominant;    (2) fats and oils manufacturing system comprising dispersion microbe tank, separation apparatus, culture apparatus which cultures heterotrophic algae by making organic sludge into nutrient and extracting device which extracts fats and oils from heterotrophic algae; and    (3) manufacturing method of fats and oils involving generating organic sludge, culturing heterotrophic algae by making organic sludge into nutrient and extracting fats and oils from heterotrophic algae.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the organic sludge generation apparatus. (Drawing includes non-English language text).    Dispersion microbe tank (1)    Centrifuge (2)    Microbial cell densitometer (3)    Light liquid tank (4)    Heavy liquid tank (5)
NOVELTY - A paper catalyst has sheet-like porous catalyst structure obtained by baking (S5) heat-resistant fiber which holds the catalyst component with an inorganic binder at 1000 degrees C or more. The catalyst component comprises oxide particles containing nickel, or nickel.    USE - Paper catalyst is used as modifier for steam reforming reaction of gas containing methane and hydrogen (claimed) for manufacturing hydrogen used for fuel cell.    ADVANTAGE - The paper catalyst has excellent activity. The hydrogen is efficiently manufactured, using the paper catalyst.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of paper catalyst.    DESCRIPTION OF DRAWING(S) - The drawing shows the flowchart of manufacture of the paper catalyst. (Drawing includes non-English language text)    Slurry production process (S1)    Floc production process (S2)    Sheet forming process (S3)    Drying process (S4)    Baking process (S5)
NOVELTY - Hydrogen production and utilization method involves producing biogas which contains hydrogen by thermal decomposition by using biomass as raw material, separating hydrogen while denaturing biogas to hydrogen rich gas by membrane shift reaction device, and separating carbon dioxide from gas containing concentrated carbon dioxide which is obtained by separating hydrogen.    USE - Production and utilization of hydrogen used for fuel cell.    ADVANTAGE - The method obtains hydrogen efficiently, and reduces carbon dioxide emission.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of hydrogen production and utilization method. (Drawing includes non-English language text).
NOVELTY - Water in oil emulsion comprises: diesel fuel (70-99 wt.%) comprising biodiesel blended fuel (0-50 vol.%); water (0.5-30 wt.%); alkyl amine ethoxylate (0.01-5 wt.%), at least 25 wt.% of the alkyl amine ethoxylate being 10-14C alkyl amine ethoxylate and at least 25 wt.% of the alkyl amine ethoxylate being 16-18C alkyl amine ethoxylate; and product (0.03-1 wt.%) obtainable by reacting a polyisobutylene succinic anhydride of molecular weight 900-2600 with 1-2 moles of a tertiary alkanolamine.    USE - The composition is useful in stabilizing a water in oil emulsion (claimed), which is useful as a biodiesel blended fuel.    ADVANTAGE - The emulsion is stable.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) making the emulsion comprising blending the components of the emulsion; and    (2) a composition comprising alkyl amine ethoxylate (1-500 parts by weight), at least 25 wt.% of the alkyl amine ethoxylate being 10-14C alkyl amine ethoxylate and at least 25 wt.% of the alkyl amine ethoxylate being 16-18C alkyl amine ethoxylate, and the product (3-100 parts by weight) obtainable by reacting a polyisobutylene succinic anhydride of molecular weight 900-2600 with 1-2 moles of a tertiary alkanolamine.
NOVELTY - The device has a power generator connected with a steam turbine and connected with a transformer (1) by a circuit. A biogas pool is connected with an entrance of a gas separator (2) by pipelines, where an exit of the gas separator is connected with a pressurizing gas storing box by the pipelines. A pressurizing gas storing box is connected with the steam turbine by the pipelines. A bottom part of the gas separator is provided with a gas exhaustion tube (3). The pipelines between the biogas pool and the gas separator are provided with a control valve (4).    USE - Biogas power generation device.    ADVANTAGE - The pipelines between the biogas pool and the gas separator are provided with the control valve, so as to control the biogas flow amount. The device is capable of transforming the biogas into electricity without producing secondary pollution, and has environmentally-friendly effect, high electricity generation ratio and simple assembling process.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a biogas power generation device.'(Drawing includes non-English language text)'    Transformer (1)    Gas separator (2)    Gas exhaustion tube (3)    Control valve (4)
NOVELTY - The system has a front storing device provided with a buffer chamber and a working bin, where the buffer chamber and the working bin are provided with a feed opening and a discharge opening, respectively. A front feeder control unit controls feeding frequency of a front feeder according to signals transmitted by a furnace temperature sensor and a furnace pressure sensor. A flame detector senses flame of a feeding radiation device. An ignition control unit controls turn-on state of an ignition device according to a signal transmitted by the flame detector.    USE - Automatic biomass gas feeding radiation control system for controlling a biomass gasification reaction system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of an automatic biomass gas feeding radiation control system.'(Drawing includes non-English language text)'
NOVELTY - The method involves arranging upper material position meter and middle material position meter in buffer warehouse. Materials are conveyed in warehouse by arranging material position meters in working warehouse. Furnace temperature/pressure sensors are arranged into fluidized bed gasification reactor to control feeding frequency of front-furnace feeding device according to measured furnace temperature/pressure. Flame detector is arranged into diffusing device for diffusing, ignition device is automatically ignited when flame of diffusing device quenches.    USE - Automatic control method for controlling biomass gasification reaction.    ADVANTAGE - The flame detector is arranged into diffusing device for diffusing, ignition device is automatically ignited when flame of diffusing device quenches. Thus the biomass raw materials are fully reacted for diffusing the residual fuel gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biomass gasification reaction system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram illustrating the process of controlling biomass gasification reaction. (Drawing includes non-English language text)
NOVELTY - The burner has a gasifying device (1) integrally embedded in a radiator (2). A tail gas exhausting port (20) is connected to outer and inner sides of a heat exchanging channel (15) and arranged on a tail end of the radiator. A tail gas one-way valve (11) is arranged on the tail gas exhausting port. An outer side of the tail gas exhausting port is connected with a strong exhausting fan (13) via a one-way valve (16). Another tail gas exhausting port (21) is provided with a normally opened magnetic baffle (12) and arranged on the top of the gasifying device.    USE - Biomass fuel gasifying and direct spraying burning type hot wind burner.    ADVANTAGE - The burner has better gasifying, carbonizing, burning and heat exchanging functions. The burner achieves non-tar burning in opened way so as to prevent heat loss, thus achieving more than 95 percent of heat efficiency. The burner efficiently utilizes reproduced energy, so that the burner is made environment-friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass fuel gasifying and direct spraying burning type hot wind burner.'(Drawing includes non-English language text)'    Gasifying device (1)    Radiator (2)    Tail gas one-way valve (11)    Normally opened magnetic baffle (12)    Strong exhausting fan (13)    Heat exchanging channel (15)    One-way valve (16)    Tail gas exhausting ports (20, 21)
NOVELTY - The device has a drive motor (2) that is arranged at bottom of a stander. The drive motor is connected with a speed reducer (3) through a triangular belt (8). The speed reducer is respectively connected with a gear box portion (4) and moveable box portion (5) through coupling shaft (7) and triangular belt (9). An output shaft of the gear box portion and output shaft of the moveable box portion are respectively connected with a ring model component (10).    USE - Biomass granule forming device of dual-ring model.    ADVANTAGE - The device is convenient to use at vast rural areas. The device is provided with simple structure and convenient to repair and maintain. The granular fuel with high density and high granule molding ratio are obtained.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass granule forming device of dual-ring model.    Drive motor (2)    Speed reducer (3)    Gear box portion (4)    Moveable box portion (5)    Coupling shaft (7)    Triangular belts (8,9)    Ring model component (10)
NOVELTY - Treating oilfield wastewater containing polymer comprises microorganism aerobic treatment and filtering treatment. The microorganism comprises Bacillus cereus, Bacillus megaterium, Bacillus subtilis, Candida lipolytica short bacillus, Pseudomonas fluorescens. The microorganisms are mixed. Aerobic degradation of the microorganism is carried out, and filtering treatment is performed.    USE - Method for treating oilfield wastewater containing polymer (claimed).    ADVANTAGE - The method is simple, has simplified procedure, convenient operating management, low treating operation cost (0.65-0.7 yuan/ton of water, which is two-thirds of the conventional treatment) and does not need the additional of any medicament. The treatment does not cause secondary pollution. The treating effect is stable, which can ensure that the treating water output achieves 5.5.2. The method has little slurry, and does not need slurry treating system.
NOVELTY - Excrement treatment involves separating excrement into dry excrement and liquid excrement by using a dry and wet separator. The dry excrement is processed by a biochemical processor for generating organic fertilizer by adding effective microorganism and other active substances. The obtained mixture is kept and processed through adjustment of a processing system for performing biological membrane process.    USE - Method for treating excrement (claimed).    ADVANTAGE - The method efficiently treats the excrement with improved processing efficiency in an eco-friendly manner.
NOVELTY - A catcher comprises a main collection tube (1) comprising an upper part which is a taper accumulation tube (3) having a stream guide tube water outlet (6), and a lower part which is a cylinder-shaped catching tube (4) having 2-4 filtering holes (5) on its lower end; and a filtering net (2) on a bottom part of the filtering holes.    USE - A catcher of cyanobacteria recovered from sludge (claimed).    ADVANTAGE - The catcher has a simple construction, and achieves convenient collection.    DESCRIPTION OF DRAWING(S) - The drawing is a sectional view of the catcher.    Main collection tube (1)    Filtering net (2)    Taper accumulation tube (3)    Cylinder-shaped catching tube (4)    Filtering holes (5)    Stream guide tube water outlet (6)
NOVELTY - A fungicide comprises Bacillus stearothermophilus, Streptomyces hygroscopicus and S. microflavus.    USE - Fungicide for compost treatment of household refuse (claimed).    ADVANTAGE - The fungicide exhibits quick fermentation heating, high compost temperature and short fermentation period. It promotes garbage to become thoroughly decomposed and stores available nutrient of the compost; and has no environmental pollution and produces excellent microbial organic fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for application of fungicide, in which the strains are respectively cultured and manufactured after fermentation.
NOVELTY - A device for producing methane from wet garbage, comprises two or more methane ponds that are used alternatively; where each methane pond is set with a heating pipeline, which is connected with a solar heater.    USE - The device is useful for producing methane from wet garbage (claimed).    ADVANTAGE - The device ensures the continuous use; where it produces methane continuously even under the condition of low temperature and unstable temperature.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the device for producing methane from wet garbage.
NOVELTY - Rapid and optimal compost preparation involves mixing 45-75% of dry matter of green plant material (grass) with 25-55% of dry matter of sugarcane bagasse. The mixture is piled up with 1.80m height and required length for 1 day. Gypsum and 8-10% of dry matter are mixed with stack in third day. The stack is mixed and formed again in fifth day. The stack is moistened, mixed and pasteurized in seventh day and then placed into tunnel for next four days. The compost is supplemented for seeding.    USE - Method for preparing compost rapidly and optimally for growing mushrooms e.g. Agaricus bisporus (claimed).    ADVANTAGE - The compost preparing method ensures enormous savings in the use of infrastructure and machinery pertaining to composting and is energy efficient and eco-friendly process that enables to produce compost in short time (i.e. in 10 days) without producing leachate and using dung, where the compost is an organic fertilizer free from foul odor emission and ensures 40-50% reduced emission of carbon dioxide and ammonia.
NOVELTY - Alkylation process comprises contacting at least one 2-6C olefin and at least one 3-6C isoparaffin with a catalytic composition prepared from a hygroscopic catalyst precursor under alkylation conditions, where the catalyst precursor is added in-process to the catalytic composition and the catalyst precursor is at least partially coated with a hydrophobic material prior to addition of the catalyst precursor to the catalytic composition.    USE - The alkylation process is useful for stabilizing catalytic activity.    ADVANTAGE - The catalyst can be efficiently and economically maintained during and/or after catalyst regeneration, and the catalytic activity and composition of the ionic liquid catalyst is stabilized in an economic and efficient manner.
NOVELTY - Method for manufacturing continuous porous material, involves adding molded polymeric material having agrochemical absorption property and containing polymeric material and air hole forming agent in solvent, dissolving air hole forming agent in solvent and obtaining molded polymeric material with open cell.    USE - The method is useful for manufacturing continuous porous material for filtering and removing agrochemicals e.g. insecticide and herbicide in water source.    ADVANTAGE - The continuous porous material is environmentally-friendly as it prevents contamination of river water and underground water by the agrochemical and has high water-permeability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for continuous porous material, which is obtained by the above-cited method.
NOVELTY - Automatic backflow and stirring methane tank for straw dry fermentation, comprises straw methane tank and two tunnel methane tanks arranged aside of the straw methane tank. A sealing film is disposed on an opening of the straw methane tank and a water groove is formed around it. Automatic backflow and stirring device communicating with the tunnel methane tanks is installed in the straw methane tank. The tunnel methane tanks and straw methane tank communicate with a supercharger via pipelines with valves.    USE - Automatic backflow and stirring methane tank for straw dry fermentation.    ADVANTAGE - Because an automatic backflow and stirring device communicating with the tunnel methane tanks is installed in the straw methane tank, when the tunnel methane tanks produce methane, the pressures in the tanks are increased, methane liquid flows to the upper side of straw materials in the straw methane tank from a straw tank liquid inlet tube under the function of barometric pressure, to soak the straw; and when methane in the tunnel methane tanks is used, the pressures are reduced, and the methane liquid flows into the tunnel methane tanks from a backflow tube under the function of barometric pressure. The automatic stirring of methane tank is finished during methane-using process of users and methane-producing process of methane tanks.
NOVELTY - A method (M1) of producing a hydrocarbon product from coal/biomass involves: converting the coal/biomass to coal-oil/bio-oil; optionally processing the coal-oil/bio-oil in a hydroprocessing reaction to remove at least one oxygen, nitrogen or sulfur from hydrocarbon compound in the coal-oil/bio-oil; and using at least a portion of the coal-oil/bio-oil as a feedstock in a cracking reaction to convert hydrocarbon compounds in the feedstock into a mixture of smaller hydrocarbon compounds comprising the hydrocarbon product.    USE - For producing hydrocarbon product such as gasoline, fuel oil, naphtha, naphtha intermediate, methane, ethane, liquid petroleum gas (LPG), and lower olefins (such as ethylene, propylene, and butylenes) (claimed).    ADVANTAGE - The method produces hydrocarbon products such as gasoline and lower olefins from renewable sources; reduces adverse environment effects and/or economic cost compared to existing technologies relying on the extraction and use of crude oil; produces hydrocarbon products of comparable or increased quality to those produced from crude oil and other similar feedstocks.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a hydrocarbon product produced by the process (M1).
NOVELTY - The device has a cylinder shaped water sealing device whose upper part is installed with a coal gas inlet tube, a coal gas outlet tube, a hydraulic hopper, a liquid level valve joint and a draining tube joint. A generating furnace air coal gas burner is provided with a coal gas inlet tube, an air inlet tube, a mixed port and a mixed room. The mixed room is provided with a high voltage igniting device. A shell is installed with a flange, where the device is connected with a biomass fuel coal gas generating furnace coal application system via a coal burner.    USE - Biomass fuel air gas generating furnace device for a thermotechnical device and a boiler sorted device.    ADVANTAGE - The device utilizes a waste wood block, a wood slag, a rice husk, a straw and waste mushroom as materials, so that energy and production cost is saved and discharge of sulfur dioxide is reduced, thus increasing environment protection effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a biomass fuel air gas generating furnace device in partial section.
NOVELTY - The device has a plasma torch heater (5) whose gas discharging hole is formed on a water vapor nozzle. A slag discharging hole of a gasifying furnace (6) is formed on a slag charging hole of a slag cooling device (7). A gas outlet of the gasifying furnace is connected with a gas charging hole of a spraying tower (11). The gas charging hole of the spraying tower is formed on a gas charging end of a heat exchanger (12). The gas discharging end of the heat exchanger is connected with a dust remover (13), an acid removing tower (14) and a drier (15).    USE - Biomass water vapor indirect gasifying device for preparation of a biomass liquid fuel.    ADVANTAGE - The device utilizes the high-temperature overheat water vapor as the oxidant and energy carrier to dry, evaporate, crack and gasify the biomass fuel in the gasifying furnace to generate rough synthesis gas. The rough synthesis gas is quenched with the spraying tower to acquire original synthesis gas without molten slag and alkali metal oxidant. The rough synthesis gas is performed cooling, duct-removing and drying process, so as to acquire high-quality synthesis. The device is suitable for biomass gasifying combination circulation generation and preparation of biomass liquid fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass water vapor indirect gasifying device.    Plasma torch heater (5)    Gasifying furnace (6)    Slag cooling device (7)    Spraying tower (11)    Heat exchanger (12)    Dust remover (13)    Acid removing tower (14)    Drier (15)
NOVELTY - The ureter has a hollow light plastic ball installed in a ureter part. An upper end of the ureter part is connected with a mobile connector. A built-in evacuating catheter is installed in a wall of the ureter part. A marking frame and a digital strip are installed on a surface of the ureter part. Diameter of a neck part of the ureter is less than that of the plastic ball. A urine discharging port is installed on a wide end of the mobile connector, and the built-in evacuating catheter is passed through the wall of the ureter part.    USE - Practical and environment-friendly ureter.    ADVANTAGE - The ureter can be used repeatedly, thus saving cost. The built-in evacuating catheter and the urine discharging port are utilized to prevent redundant urine from overflowing along an outer wall of the ureter, thus avoiding hands of a patient and a doctor from being polluted. The marking frame is convenient to mark patient information in an inerasable manner. The digital strip can prevent mixing of samples. The ureter has automatic sealing function, automatic discharge function, sample reserving function, convenient deposition and transmission function, environment protection and anti-aliasing sampling function.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a practical and environment-friendly ureter.
NOVELTY - Device comprises a tank, an anaerobic digester, a solid-liquid separation room, a methane liquid filter room, a methane liquid distilation room and an overflow tank, where the anaerobic digester is located between the tank and a hopper-shaped bottom board. The tank is connected with an additive tank. A temperature sensor, an additive sensor, a pH sensor, a humidity sensor, a water level limiter, a concentration sensor, a pressure sensor, a methane sensor and a volume sensor are disposed in the anaerobic digester.    USE - Device for generating methane (claimed), carbon dioxide, carbinol, organic composite fertilizer and organic agricultural pesticide.    ADVANTAGE - The device enables to generate methane in an eco-friendly manner.
NOVELTY - Constructing ecological ditch comprises: (i) leveling two dikes of branch ditch and bottom slope, constructing ecological stopping basic weirs, planting plants on two dikes of first section of branch ditch, planting aquatic plants and dirt-resistant plants, and (ii) leveling edge slope of main canal and bottom slope by paving hollow brick on the flat edge slope, filling stones onto the hollow brick and burying to the thickness obtained by reducing the thickness of the filled stone by actual thickness of the hollow brick, flooding and planting emergent aquatic plants and landscape plant.    USE - The ecological ditch is useful for sewage treatment and processing rural life sewage (claimed) and sewage generated by agricultural production activity.    ADVANTAGE - The ecological ditch: has simple construction method; has simple routine maintenance; and is economical.    DETAILED DESCRIPTION - Constructing ecological ditch comprises: (i)leveling two dikes of the branch ditch and bottom slope, constructing ecological stopping basic weirs on the bottom of the ditch at intervals for dividing the branch ditch, planting plants, which are dense and high on two dikes of first section of branch ditch adjacent to the water outlet of the farmland, planting aquatic plants on the bottoms of the other sections of branch ditches and planting 2-3 rows of dirt-resistant plants on the edge slope, and (ii) leveling the edge slope of the main canal and the bottom slope, paving hollow brick on the flat edge slope, filling stones onto the hollow brick, burying the brick to the thickness obtained by reducing the thickness of the filled stone by actual thickness of the hollow brick, flooding and planting emergent aquatic plants on the edge slope and planting landscape plant with developed root on the upper edge slope.
NOVELTY - Producing chemicals in microalgae species using Microalgae genomics technology (RTM: Microalgae-based method) is claimed. The technology manipulates the metabolic pathway in the genome of microalgae species comprising Chlorella vulgaris, to generate novel compounds, which have potential commercial use.    USE - The process is useful: for producing chemicals in microalgae species; in algae and microalgae; to generate novel bioactive compounds in algae which is used in the prevention of oral pathogens and diseases; to generate a broader spectrum of novel chemicals or increase the existing compounds in algae, which has antibacterial activity and could kill a variety of oral bacteria; to generate fatty acids and increase the concentration of existing fatty acids, which are used as biofuel; and to generate compounds with other applications comprising anticancer, antiinflammation and anti HIV, and many other uses; to generate chemicals for drug discovery, pharmaceuticals, nutraceuticals, agricultural chemicals, phytochemicals and nutritional chemicals (all claimed). Test details are described but no results given.    ADVANTAGE - The process: increases the yield of novel compounds and existing compounds; utilizing random activation mutations which induced in a large number of microalgae cells.
NOVELTY - The device has two mixers (1,17) among which mixer (1) has an outlet connected to a stirrer (2). A turning machine (4) is arranged at the back of stirrer. A conveyor (6) is arranged at the back of turning machine. An outlet of air absorbing pipeline (9) is connected to dust removing machine (10) which is connected to a draught fan (11). The outlet of air absorbing pipeline (29) is connected to dust removing machine (30). Another draught fan (47) is connected to dust removing machine (46). The outlet of dryer (44) is connected to a package machine (50).    USE - Combined production device for producing organic particle fertilizer and organic-inorganic mixture particle fertilizer.    ADVANTAGE - The production efficiency of the combined fertilizer production device is improved, by increasing fertilizer crushing quality, and by controlling drying humidity of fertilizer.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the combined production device for producing organic particle fertilizer and organic-inorganic mixture particle fertilizer.    Mixers (1,17)    Stirrer (2)    Turning machine (4)    Conveyor (6)    Air absorbing pipelines (9,29)    Dust removing machines (10,30)    Draught fans (11,47)    Dryer (44)    Dust removing machine (46)    Package machine (50)
NOVELTY - The device has mixer (1) whose outlet is connected with stirrer (2). A turning machine (4) is arranged on rear portion of stirrer. The outlet of conveyor (6) on rear portion of turning machine, is connected with inlet of dryer (8) that is heated by hot air furnace (7). The top of dryer is connected with air sucking pipeline (9) whose outlet is connected with draught fan (11) connected to smoke pipe (12). The fine material of sieving machine is connected with fine grinder (15) whose outlet is connected to mixer (17) connected with packer (19) and pelletizer (21).    USE - Device for producing bulk blending (BB) fertilizer used for producing organic granulated fertilizer and organic-inorganic mix granulated fertilizer.    ADVANTAGE - The grinding process is performed by using fine grinder so that water content rate of fertilizer is 30-40% so that production efficiency is improved. The fertilizer grinding quality can be improved greatly and particle diameter of fertilizer can be controlled to be 1 mm or below.    DETAILED DESCRIPTION - The outlet of dryer is connected with inlet of coarse grinder (13) whose outlet is connected with inlet of sieving machine (14).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of BB fertilizer producing device.    Mixers (1,17)    Stirrer (2)    Turning machine (4)    Conveyor (6)    Hot air furnace (7)    Dryer (8)    Air sucking pipeline (9)    Draught fan (11)    Smoke pipe (12)    Coarse grinder (13)    Sieving machine (14)    Fine grinder (15)    Packer (19)    Pelletizer (21)
NOVELTY - Environmental-friendly production of cold fresh divided fillets comprises: (i) farming fresh live fish in cold water of 0-4 degrees C, opening the neck of the fresh live fish, and then by placing in the cold water; (ii) removing scales, head, tail and viscera from the bled fish at 0-4 degrees C; (iii) cutting into slices and reforming; (iv) dipping the fillets in cold ozone aqueous solution of 1.5-2 mg/kg and sterilizing for 5-10 minutes, introducing to a sterile operating table at 2-6 degrees C, and draining; (v) coating the fillets by an antistaling agent; and (vi) drying and forming the film.    USE - The method is useful for producing cold fresh divided fillets.    ADVANTAGE - The method: doesn't use chlorine dioxide and a preservative and hence is environment-friendly; controls the decomposition of microorganism of the divided fillets, reduces the fatty oxidation and protein decomposition, thus guaranteeing the freshness of the product; and uses a green composite coating antistaling agent coating thus prolonging the quality guarantee period of the cold fresh divided fillets.
NOVELTY - Methane treatment device-equipped pigsty system has pigsty; methane device with anaerobic fermentation pond; and at least two rows of pig fences provided inside the pigsty. Methane device is connected with the pigsty through a feces discharging channel. Feces discharging channel is located under the pig fence. Full-leaking feces floor is located between the pig fence and feces discharging channel.    USE - Methane treatment device-equipped pigsty system for pig breeding.    ADVANTAGE - Provides pigsty system that realizes zero emission since pig fences are communicated with the methane pond under the pig fence through full-leaking feces floor so that pigs are feed, feces are treated, methane and fertilizer are generated while saving the land. Reduces special cleaning operation since feces sewage is directly pushed into the methane pond, thus saves water and labor, improves working efficiency and weather environment, and ensures healthy growth of the pig.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the methane treatment device-equipped pigsty system.
NOVELTY - Environmental friendly complex microbial preparation for removing household sewage, comprises Lactobacillus acidophilus, Candida utilis, Bacillus licheniformis, Streptomyces albus, and Rhodopseudomonas palustris, and the preparation is obtained by complex culturing of bacterial ingredients through anaerobic and aerobic fermentation technique.    USE - The environmental friendly complex microbial preparation is useful for removing household sewage.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the environmental friendly complex microbial preparation, comprising (i) culturing of single-strain Lactobacillus acidophilus, Candida utilis, Bacillus licheniformis, Streptomyces albus, and Rhodopseudomonas palustris in respective culturing medium; (ii) acclimatizing Lactobacillus acidophilus, Candida utilis, Bacillus licheniformis, Streptomyces albus, and Rhodopseudomonas palustris in respective culture medium comprising molasses, adding Candida utilis to the culture medium comprising molasses for complex acclimatization culture of Rhodopseudomonas palustris; (iii) mixing the acclimatized strain liquid seeds for complex culturing.
NOVELTY - The device has combustion chamber whose inner wall is provided with fire-proof layer. A fuel supply unit supplies burnt fuel to combustion chamber. A recycle water shift unit (30) collects burnt fuel from combustion chamber, and blocks injection of outside air into combustion chamber. A top cover is mounted on one end of fuel supply tube (12). One of the hydraulic cylinder (14) moves fuel supply tube forward and backward, and another cylinder (16) operates knife slider (17) so as to seal combustion chamber.    USE - Biomass pyrolysis device for use in manufacture of clean gas.    ADVANTAGE - Since the recycle water shift unit collects burnt fuel from combustion chamber, and blocks injection of outside air into combustion chamber, the temperature of combustion chamber can be maintained regularly and the dust can be removed effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for clean gas manufacturing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of biomass pyrolysis device.    Hopper (11)    Fuel supply tube (12)    Hydraulic cylinders (14,16)    Knife slider (17)    Recycle water shift unit (30)
NOVELTY - The container (110) includes a side portion that is positioned such that top of contents including smoked corn and charcoal are exposed. A ground hole is formed at the center of bottom portion of container. A handle is formed in the side upper portion of container.    USE - Container for controlling combustion of smoked corn and charcoal used during roasting meat with seasonings.    ADVANTAGE - The thermal power and combustion time of corn and charcoal can be adjusted reliably, while preventing generation of unpleasant smell during seasoning process.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the container.    Charcoal (30)    Furnace (40)    Grill (50)    Meat (60)    Container (110)
NOVELTY - The generator has a fuel storage unit (200) that is arranged outside the dry distillation chamber having inner wall formed with fire-proof layer. An air supplying unit supplies external air to a fuel supply unit. The fuel supply unit supplies biomass fuel into dry distillation chamber, for generating combustible gas. The combustible gas is burnt and dried in dry-distillation chamber, and supplied to process chamber.    USE - Biomass gas generator.    ADVANTAGE - Since the fuel storage unit is arranged outside the dry distillation chamber having inner wall formed with fire-proof layer, the lifetime of the fuel storage unit can be improved and the oxide erosion of the fuel storage unit can be suppressed. The amount of necessary oxygen can be controlled easily at the dry-distillation of biomass fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a plan view of the fuel storage unit.    Fuel storage unit (200)    Blower (201)    Damper (204)    Coolant chamber (206)    Nozzle (207)
NOVELTY - Preparing slow-release carbon material using low molecular weight polylactic acid prepared by molten polymerization, comprises: (a) obtaining polylactic acid having 1 to 100000 molecular weight; (b) mixing polylactic acid and amylum in a mass ratio of 1-4 and evenly stirring; and (c) slowly and evenly adding mixed polylactic acid and amylum by injection molding at 100-180 degrees C, extruding and cooling at 10-40 degrees C.    USE - The method is useful for the slow release of pesticides and chemical fertilizers.    ADVANTAGE - The method: utilizes biodegradable and low cost raw materials; provides carbon material having slow release and no secondary pollution characteristics; provides balanced microbial nutrition, and increased metabolic function and treatment efficiency by supplying the carbon source evenly; eliminates the need of other auxiliary substances; and is simple and economical.
NOVELTY - A sludge is treated in recycling manner by (A) mixing sludge with calcium hydroxide (Ca(OH)2), placing it into fermentation reactor, stirring and uniformly mixing and processing anaerobic fermentation; (B) discharging volume of fermentation mixture from reactor at regular intervals and adding sludge having same amount as discharged mixture and Ca(OH)2; and (C) adding iron sulfate (FeSO4) solution into discharged mixture, stirring, adding polyacrylamide, stirring, filter pressing and dewatering, and detecting dewatered filtrate.    USE - Method is used for treating sludge in recycling manner (claimed).    ADVANTAGE - The method improves concentration of short chain fatty acid generated by sludge and fermentation liquor amount, decreases volatile material of sludge, and removes most phosphate in fermentation liquor.
NOVELTY - Extracting polymyxins B and E from a culture in a fermentation extract comprises: adjusting the pH of the culture to 10-14 by an alkali at 0-25 degrees C, stirring the material for 30 minutes, performing solid-liquid separation to collect the residue and obtain polymyxins B and E free alkali sediment, adjusting the pH of the free alkali sediment to 1-6, performing solid-liquid separation to obtain polymyxins B and E concentrated solution after dissolving the polymyxins B and E free alkali sediment, filtering, removing the inorganic salt and spraying the material to obtain the product.    USE - The method is useful for extracting polymyxins B and E from a culture in a fermentation extract.    ADVANTAGE - The method: is simple, convenient, economical, rapid and environmental friendly; extracts the product with high yield; exhibits high extracting rate; and utilizes less amount of the fermenting solution and solvent.
NOVELTY - Preparation of ecological oil comprises: (a) choosing a biomass material, rapidly pyrolyzing the biomass material at 500 degrees C to generate the mixture of pyrolyzed biomass gas and biomass particles; (b) separating solid particles and biomass ash; and (c) rapidly condensing the pyrolyzed biomass gas to be below 80 degrees C and liquefying to generate ecological oil.    USE - The process is useful for preparing ecological oil (claimed).    ADVANTAGE - In the process, the solid thermal medium, liquid thermal medium, and gas cold medium three recycle steps are included; thus, the preparation process can decrease production cost, and has high working process safety, high ecological oil purity, and high thermal value. Moreover, it cannot generate any wastewater, waste gas, and waste slag, which meets strict environment-friendly demands.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of the process for preparing ecological oil (Drawing includes non-English language text).
NOVELTY - Healthcare liquor comprises (in ml): white spirit (1000), ginseng (10-20), Cordyceps sinensis (10-20), Gynostemma pentaphylla (20-30), cortex lycii radicis (10-20), cornua cervi pantotrichum (10-20), Astragalus mongholicus (20-30), Angelica (10-20), safflower (10-20), penisotariae (10-20), yam (40-60), green plum (20-30), medlar (80-100), sea otter (20-30) and Odobenus rosmarus (20-30) and superoxide dismutase (SOD) containing plant extract (200-500).    USE - Healthcare liquor used for resisting fatigue, improving immunity, promoting generation of semen and nourishing kidney, smoothing channel and promoting blood circulation, refreshing and benefiting vital energy, promoting blood circulation and preventing stasis, strengthening bones, promoting metabolism, enhancing emotion, enlarging penis, prolonging sexual intercourse, removing toxin, preventing impotence, premature ejaculation, pain in back and leg, numbness of muscle and bones, and abnormal menstruation and dysmenorrhea of woman.    ADVANTAGE - The healthcare liquor is eco-friendly enables to promote body health, and has high nutrient component and no unpleasant smell.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing healthcare liquor, which involves:    (A) cleaning ginseng, Cordyceps sinensis, Gynostemma pentaphylla, cortex lycii radicis, cornua cervi pantotrichum, Astragalus mongholicus, Angelica, safflower, penisotariae, yam, green plum, medlar, sea otter and Odobenus rosmarus and superoxide dismutase (SOD) containing plant extract;    (B) adding 2000ml of water with the cleaned materials for 20-30 minutes;    (C) filtering the materials for 1-2 hours by 1200 meshes to obtain 1000ml of liquid;    (D) preparing 1000ml of white spirit and adding extracted liquid with it;    (E) mixing and stirring the materials for 10 minutes;    (F) keeping the materials for 10 days; and    (G) filtering the materials to obtain the desired product.
NOVELTY - Wood fiber composite decomposition agent obtaining involves preparing a cow dung culturing substrate by weighing 150g cow dung in 100ml beaker, and then mixing 400ml water. The mixture is stirred for 30 minutes to obtain filtrate. An inoculating agent is also prepared by weighing 20g sieved compost in 100ml beaker and using 50ml water. The mixture is stirred for 30 minutes to obtain the agent. Cow dung culturing substrate and inoculating agent are mixed in 250ml triangular flask at 45 degrees C. The mixture is rotated at a speed of 120 revolutions per minute for 3-5 days.    USE - Method for obtaining wood fiber composite decomposition agent used for fermenting bacterial agent of cow dung and agricultural straw (claimed).    ADVANTAGE - The wood fiber composite decomposition agent obtaining method is simple.    DETAILED DESCRIPTION - Wood fiber composite decomposition agent obtaining involves preparing a cow dung culturing substrate by weighing 150g cow dung in 100ml beaker, and then mixing 400ml water. The mixture is stirred for 30 minutes to obtain filtrate. An inoculating agent is also prepared by weighing 20g sieved compost in 100ml beaker and using 50ml water. The mixture is stirred for 30 minutes to obtain the agent. Cow dung culturing substrate and inoculating agent are mixed in 250ml triangular flask at 45 degrees C. The mixture is rotated at a speed of 120 revolutions per minute for 3-5 days. Phanerochaete chrysosporium, Trichoderma sp., Rhizopus sp., Panaeolus sp. and Coprinus sp. are separated from cow dung and then cultured in a potato dextrose agar culture medium. The potato dextrose agar culture medium is obtained by adding 20g/l glucose and 17-20g/l agar-agar in 200g/l potato leachate. The mixture, which is obtained from cow dung culturing substrate and inoculating agent, is mixed with the cultured material. The obtain material is then dried to obtain the desired product.
NOVELTY - Bacillus subtilis X1 strain has preservation number in CGMCC No. 4037, and is new. Bacillus subtilis X1 strain is Gram-positive bacterium, where the ivory bacterial colony is formed on beef extract-peptone medium.    USE - Bacillus subtilis X1 strain used for preventing soil-borne disease such as ginseng root rot, sclerotiniose and seedling blight.    ADVANTAGE - The Bacillus subtilis X1 strain enables to prepare a microbial inoculum in a safe and eco-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing microbial inoculum of Bacillus subtilis X1 strain, which involves:    (A) culturing Bacillus subtilis X1 strain in nutrient yeast dextrose agar (NYDA) culture medium at -70 degrees C for 18-20 hours;    (B) selecting a single bacterial colony and inoculating it in a liquid culture medium in for 18-20 hours at 30 degrees C;    (C) culturing the obtained material for 18-20 hours at 30 degrees C to obtain the activated strain; and    (D) inoculating the activated strain to a fermentation pot filled with the NYDA culture medium for 24-48 hours at 24.5-25.5 degrees C to obtain the desired product.
NOVELTY - Sphingobacteria DX-T3-03 strain with high resistance to zinc and ability to degrade phenol, comprising 16s ribosomal DNA containing 1391 nucleotides as fully defined in the specification, is new.    USE - The strain is useful for treatment of phenol-containing industrial waste water and heavy metal pollution.    ADVANTAGE - The strain has high resistance to zinc (4 mM/l) and can degrade phenol at a rate of 88% and with a low nutrient need. The extraction of the strain is simple, convenient, cost-effective and environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for the extraction of the sphingobacteria DX-T3-03 strain.
NOVELTY - Ethanol preparation involves culturing microorganism in cell culturing solution. The materials are saccharified, fermented and distilled. The microorganism is fungus, bacterium, Saccharomycetes or Actinomycetes. The culturing solution contains 3-20 pts.wt. of carbon source, 1-15 pts.wt. of nitrogen source, 1-10 pts.wt. of nutritive salt, 1-15 pts.wt. of growth hormone and 50-94 pts.wt. of water. The cell culturing solution is poured into a culturing device, which has an air compressor and a purifying device.    USE - Method for preparing ethanol used as biofuel (claimed).    DETAILED DESCRIPTION - Ethanol preparation involves culturing microorganism in cell culturing solution. The materials are saccharified, fermented and distilled. The microorganism is fungus, bacterium, Saccharomycetes or Actinomycetes. The culturing solution contains 3-20 pts.wt. of carbon source, 1-15 pts.wt. of nitrogen source, 1-10 pts.wt. of nutritive salt, 1-15 pts.wt. of growth hormone and 50-94 pts.wt. of water. The cell culturing solution is poured into a culturing device, which has an air compressor and a purifying device. The materials are cultured in the culturing device at 20-39 degrees C for 40-150 hours and the materials are liquefied at 30-105 degrees C.
NOVELTY - Cellulose recycling involves mixing fresh substrate and immobilized cellobiase in a fermentation section. The immobilized cellobiase is placed in a reactor in which 10-30CBU/g amount of cellulose and processed lignocellulosic material are also added. A culture liquid is also added to the reactor. The materials are processed in the reactor at 50 degrees C for 12-24 hours and then the temperature of the reactor is reduced to 30-3 degrees C. Yeast is also added to the reactor and then the obtained materials are filtered to obtain the immobilized enzyme grain.    USE - Method for recycling cellulose used in fuel ethanol production (claimed).    ADVANTAGE - The cellulose recycling method is simple and cost-effective.    DETAILED DESCRIPTION - Cellulose recycling involves mixing fresh substrate and immobilized cellobiase in a fermentation section. The immobilized cellobiase is placed in a reactor in which 10-30CBU/g amount of cellulose and processed lignocellulosic material are also added. A culture liquid is also added to the reactor. The materials are processed in the reactor at 50 degrees C for 12-24 hours and then the temperature of the reactor is reduced to 30-3 degrees C. Yeast is also added to the reactor and then the obtained materials are filtered to obtain the immobilized enzyme grain. Fresh lignocellulosic material is added to the obtained material and the obtained material is kept for 90 minutes at room temperature, and then the processed product is distilled.
NOVELTY - A Silybin nanocrystal cosmetic comprises 5-50 wt.% of surfactant, 3-30 wt.% of oil, 0.5-3 wt.% of Silybin, proper quantity of essence, and distilled water; where the total amount of the components is 100%.    USE - The Silybin nanocrystal cosmetic is useful for moisturizing, skin whitening, sun blocking, oil control, and removing blackhead and acne (claimed).    ADVANTAGE - The Silybin nanocrystal cosmetic is smooth and soft. Moreover, it has strong effect of anti-wrinkle and smoothing face and good appearance. Additionally, it can moisturize skin for a long time, resist ultraviolet hurt, and improve the skin elasticity.
NOVELTY - The method involves concluding a plasmid that is vaccinated to soil with residual chlorpyrifos. The plasmid is carried by a bacillus latersprorus deoxyspergualin. Organic content of the soil is five to fifty grams per kilogram.    USE - Bioremediation method for soil polluted by chlorpyrifos.    ADVANTAGE - The method enables solving the problem of living difficulty of an exogenetic microbe in the soil and degrading maximal dispersion of the bacterium to degrade the chlorpyrifosas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a bacillus latersprorus deoxyspergualin.
NOVELTY - A crop straw carbide alcohol-carried solid fuel comprises: (a) carrier material: carbide of crop straws; (b) alcohol fuel: industrial alcohol; and (c) gelatinizing agent.    USE - The crop straw carbide alcohol-carried solid fuel is useful for industrial and commercial applications.    ADVANTAGE - The crop straw carbide alcohol-carried solid fuel fully uses the crop straw carbide which has special pore structure and high absorption and storage properties for alcohol fuel; thus, the solid alcohol fuel has composite burning properties of carbon and alcohol. Moreover, it has little dosage of gelatinizing agent, stable flame during combustion process, collapsing or flowing absence, black smoke or peculiar smell absence, long combustion time, less residues, and heat insulation effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for preparing the crop straw carbide alcohol-carried solid fuel, comprising: (a) drying and cutting crop straws into sections, carbonizing the straw sections for 1-4 hours at 250-500 degrees C, and obtaining carbide of crop straws as carrier material for absorbing and carrying alcohol fuel; (b) mixing industrial alcohol of 100 pts.wt. with gelatinizing agent of 1-5 pts.wt. to obtain alcohol solution containing gelatinizing agent; (c) putting the carbide of the crop straws into the alcohol solution containing gelatinizing agent, enabling the carbide of the crop straws to absorb saturated-amount alcohol solution; and (d) taking out the carbide of crop straws absorbing saturated-amount alcohol solution; where the alcohol solution containing gelatinizing agent gradually forms homogeneous gelatin in slots to obtain crop straw carbide alcohol-carried solid fuel; and sealing and packaging the product.
NOVELTY - Producing coal-based fuel carbon comprises: (a) fetching 80-95 pts.wt. of bituminous coal, 0-10 pts.wt. of crop straw, and 4-10 pts.wt. of organic adhesive, uniformly mixing and stirring, adding proper water and uniformly mixing again; (b) pressing the material obtained in (a) on a molding machine to produce a spherical body, and naturally airing the produced green ball in air; and (c) placing the naturally-aired green ball in a carbonizing furnace, carbonizing at 400-700 degrees C for 90-120 minutes, and cooling to obtain the coal-based fuel carbon.    USE - The process is useful for producing coal-based fuel carbon (claimed).    ADVANTAGE - In utilizing the process, the coal-based fuel carbon has cheap materials which are easy to obtain and efficiently utilizes biomass energy; where the compressive strength of every fuel carbon product is greater than 25 kg; the fixed carbon is greater than 75%; the volatile matter is greater than 10%; the ash is less than 10%; the calorific value is greater than 6500 kilocalorie/kg; and the sulfur content is less than 0.4%. Moreover, it has easiness for ignition, combustion resistance, complete combustion, no smoky smell, no spark and soot, high furnace surface temperature, high thermal stability, and no collapse and breakage during combustion process.
NOVELTY - A Bacillus subtilis LBK1 bacterial strain for degrading bifenthrin having the 16Sr-DNA sequence comprising a fully defined 1441 bp sequence (SEQ ID NO. 1) given in the specification, is new.    USE - The bacterial strain is useful for biodegradation of bifenthrin pesticide (claimed), and bioremediation or biological cleaning of water body polluted by pesticide, soil, and farm product.    ADVANTAGE - The degradation rate of the bacterial strain to bifenthrin reaches to more than 80%.
NOVELTY - This invention is about methods and device producing hydrogen and oxygen. This hydrogen, oxygen-producing device contains a bracket, several power packages and one first pressurizer. The bracket comprises a first mid-pressure collecting tube, a low-pressure collecting tube connected to the former, and several gas collecting tubes which gather hydrogen and oxygen to the low-pressure collecting tube. Every power package includes one rotary base with its hinge set on the gas collecting tube and one wind-power generator which allows wind-driven electrolysis of water in the rotary base into hydrogen and oxygen. The first pressurizer forces hydrogen and oxygen to first mid-pressure collecting tube. By minimizing the size of wind-power generator and using the electricity generated this way to electrolyte water directly, the hydrogen and oxygen product turns out to be pollution-free, and meets the demands of environmental protection in energy-saving and carbon reduction.
NOVELTY - Bacterial fungicide (100 wt.%) comprises (in wt.%) Pseudomonas putida (1-2), a surfactant (9-15) and a liquid carrier (83-90).    USE - The bacterial fungicide is useful for controlling pathogenic fungus on root crops infected by Pythium, Rhizoctonia or Fusarium.    ADVANTAGE - The bacterial fungicide: has efficacy on cucumber, tomato, eggplant, green pepper, cotton, watermelon and sesame; is purely natural, safe to human and livestock, environmental friendly and non-resistant; is beneficial for production of pollution-free green vegetables; is economical and ecological with social benefits.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing the bacterial fungicide, comprising: (i) separating Pseudomonas putida and amplifying the unicellular pure bacteria strain of Pseudomonas putida to obtain a seed bacterial solution; (ii) inoculating the seed bacterial solution into a fermenting tank containing a microorganism culturing solution, controlling and regulating the temperature inside the fermenting tank at 30 degrees C and pH 7 and further fermenting for 7-120 hours; (iii) when cell density in the fermented solution is 100000000000 colony-forming unit/ml, filtering and centrifuging the fermented culture solution and drying the fermented culture solution by spraying a powder to obtain a crude bacteria powder; and (iv) uniformly mixing the crude bacteria powder (1-2 wt.%), surfactant (9-15 wt.%) and liquid carrier stuff (83-90 wt.%), and milling the materials into 400 meshes to obtain the bacterial fungicide.
NOVELTY - A flame retardant material comprises (in parts weight) polypropylene (100), modifier (5-16) and complex flame retardant (5-10) comprising octabromo ether and antimony trioxide.    USE - Flame retardant material.    ADVANTAGE - The flame retardant material has excellent flame retarding performance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of the flame retardant material, which involves uniformly mixing the components in a high speed mixer.
NOVELTY - Synthetic methanol is preparing using (in parts weight) methanol (60-80), diesel oil (20-40), anticorrosion adhesive (0.03-0.07), solvent (0.5-2), and octane regulator (0.2-0.8).    USE - Synthetic methanol is used as liquid fuel for industrial and civil applications.    ADVANTAGE - The synthetic methanol has abundant resources of materials, is economical, can be prepared easily and used conveniently, and makes up for supply shortage of natural products.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of synthetic methanol, which involves orderly adding the materials to an agitating container at normal temperature, agitating for 15-30 minutes, and encapsulating them in a bottle.
NOVELTY - The device has heat-changing medium inlet tube (8) connected with heat-changing medium outlet tube (5) through shell and heat-changing tube (10). The inside of lower seal head (3) is provided with lower inner seal head (19), and lower tubular board (12) is connected with lower inner seal head to form lower inner cavity (17). The lower inner seal head is provided with air tube (7), and lower seal head is provided with heat-changing medium inlet tube. The shell (1) is connected with heat-changing medium outlet tube through outer space (9) of heat-changing tube.    USE - Catalysis reaction device for synthesizing methane and methyl ether.    ADVANTAGE - The lower inner seal head is provided with air tube, and lower seal head is provided with heat-changing medium inlet tube, and shell connected with heat-changing medium outlet tube. Hence the catalysis reaction device has great production ability and high contact media activity. The structure of the catalysis reaction device is simple, and the reliability of the reaction device is high and excellent operation of the reaction device is realized.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the catalysis reaction device.    Shell (1)    Lower seal head (3)    Heat-changing medium outlet tube (5)    Air tube (7)    Heat-changing medium inlet tube (8)    Outer space (9)    Heat-changing tube (10)    Lower tubular board (12)    Lower inner cavity (17)    Lower inner seal head (19)
NOVELTY - Invention relates to chemistry. The hydrogen generator has a reaction vessel, a main pipeline for delivering hydrogen with two electrically controlled valves 32, 33 and a hydrogen cleaning apparatus 9, a liquid container 10 for removing the oxide film of the reagent with a concentration measuring apparatus 23 and a level gauge 22 and two electrically controlled valves 30, 31, a drainage tank 11 and two electrically controlled valves 34, 35, a programmed control unit 29, a processing and analysis unit 40 and a measurement unit 42. The housing of the generator has a rectangular shape with two removable covers 4 and three compartments 1, 2, 3. The outermost compartments 1, 2 of the housing are identical and their adjacent parallel walls form the third compartment 3. The housing has a water jacket 7 which is joined to the third compartment and has inlet and outlet pipes. Horizontal partitions 6 are rigidly joined to the removable covers in the outermost compartments of the housing through a supporting arm 5. A reagent in form of a plate 8 is attached to the partitions 6, on which perforations are made around the reagent. The hydrogen generator also includes a filter 12, a liquid flow metre 13, a hydrogen flow metre 14, two pressure sensors 15, 16, two concentration measuring apparatus 24, 25, five temperature sensors 17, 18, 19, 20, 21, two check valves 26, 27, two electrically controlled valves 28, 29 and a comparator 41.    USE - Chemistry.    ADVANTAGE - Invention increases efficiency of the generator and simplifies its design. 1 dwg
NOVELTY - A hollow mesoporous silica capsule consists of nanoparticles dipped in nanoporous carbon.    USE - The hollow mesoporous silica capsule is useful in drug delivery system.    ADVANTAGE - The hollow mesoporous silica capsule is environmentally-friendly, has high specific surface area and is manufactured using simple method.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of the hollow mesoporous silica capsule.
NOVELTY - A waste water treatment equipment comprises dispersion microbe tank (1) into which dispersion microbe which solution containing organic substance is introduced and decomposed organic substance is thrown, and fluidized bed-type bioreactor tank (2) to which solution processed by dispersion microbe tank is introduced and particulate carriers to which microorganisms which decomposed organic substance that remains have adhered and predation living organism which preys on dispersion microbe are injected.    USE - A waste water treatment equipment.    ADVANTAGE - The equipment can process waste water with hardly-decomposable chemical oxygen demand and biological oxygen demand in high load.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a wastewater treatment process.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the waste water treatment equipment. (Drawing includes non-English language text).    Dispersion microbe tank (1)    Fluidized bed-type bioreactor tank (2)    Aerator (3)    Pipe (11)    Oxygen supply blower (21)
NOVELTY - A town sewage treatment comprises using coarse screen, main lift pump, fine screen, and sedimentation basin; building Orbal (RTM: oxidation ditch); eliminating phosphorus, decoloring and dosing; coagulating sedimentation tank; using sludge pump and sludge concentration basin; sludge dehydrating; forwarding mud cake freight; sand filtering; and contacting disinfection tank.    USE - Method for treating town sewage (claimed).    ADVANTAGE - The method has a stable sewage treatment effect and the effluent water quality reaches the demands of national regulation. The capital construction investment and operation cost are low and the benefit is high. The running management is convenient and the operation is flexible. Within a load change range, the running manner and technical parameter can be adjusted according to the different inflow water quality and the influent water quality demands, which exerts the processing ability of processing device and processing structures to the maximum. The method realizes the rational automatic control in the technical process, improves the management level, and reduces the labor intensity and labor cost.
NOVELTY - Biomass pretreatment comprises: (a) heating the biomass to a temperature of at most 110 degrees C in an exchanger H1; (b) heating the biomass obtained in step (a) to a temperature of between 150 and 175 degrees C in a scratched-surface exchanger H2; (c) subjecting the biomass to thermohydrolysis at a temperature of between 150 and 175 degrees C; and (d) cooling the thermohydrolyzed biomass for subsequent biological treatment.    USE - The method is useful for biomass pretreatment (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is installation for carrying out the method comprising: (i) a heat exchanger H1; (ii) a scraped surface heat exchanger H2; (iii) an M1 service area; (iv) a scraped surface heat exchanger H4 or flash tank F1; and (v) exchanger H5.
NOVELTY - Manufacturing method of biomass-to-liquid fuel involves pre-processing cellulose biomass feedstock, adding to organic solvent to obtain cellulose biomass dispersion, and heat-processing in the presence of solid catalyst.    USE - Manufacturing method of biomass-to-liquid fuel for energy manufacture and petroleum plant.    ADVANTAGE - Process is simple, separation of catalyst to biofuel is easy, and enzyme treatment is unnecessary.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biomass-to-liquid fuel manufacturing apparatus comprising pre-processing unit, solid preparation unit where biomass dispersion is prepared, catalyst supply unit and heating unit.
NOVELTY - Mesoporous oxide-catalyst complex comprising a mesoporous metal oxide, and a catalyst metal supported on the mesoporous metal oxide, is new, where the catalyst on the mesoporous metal oxide has a degree of dispersion of 30-90%.    USE - The catalyst mesoporous oxide-catalyst complex is useful: in a fuel processing device for a fuel cell (claimed); and as a catalyst for hydrocarbon reforming.    ADVANTAGE - The mesoporous oxide catalyst complex is prepared at low cost with high efficiency. The mesoporous oxide catalyst complex provides a high degree of dispersion and large pore area.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparation of the mesoporous oxide-catalyst complex; and    (2) a fuel processing device, comprising a hydrocarbon reforming catalyst comprising the mesoporous oxide-catalyst complex.
NOVELTY - Catalyst support comprises a catalyst support material and an active material capable of catalyzing a reverse water-gas shift reaction associated with the catalyst support material.    USE - The catalyst support is useful for supporting a catalyst for hydrogenating carbon dioxide (claimed).    ADVANTAGE - The catalyst support exhibits improved selectivity and yield in reducing carbon dioxide with hydrogen, with less methane formation, and with improved catalyst stability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a catalyst comprising the catalyst support and a catalyst material immobilized on the catalyst support;    (2) making the catalyst support, comprising associating an active material capable of catalyzing a reverse water-gas shift reaction with the catalyst support material; and    (3) hydrogenating carbon dioxides, comprising reacting hydrogen and carbon dioxide in the presence of the catalyst comprising the catalyst support and the catalyst material for catalysis of a hydrogenation reaction located on the coated catalyst support material.
NOVELTY - Creatinol sulfate (I), which is formed by chemically reacting N-methylamino-ethanol and cyanamide, is new.    USE - (I) is useful as important intermediates of organic synthesis. (I) is useful as energy supplements, food additives and plant growth regulator. No biological data given.    ADVANTAGE - The method: provides (I) with high yield and purity; consumes less energy; and is cost-effective. (I) has less toxicity, thus reducing damages of the environments and human bodies.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of (I).    DESCRIPTION OF DRAWING(S) - The figure shows a flow diagram for the process of synthesizing creatinol sulfate.
NOVELTY - The method involves decomposing an organic substance e.g. wood chip, wood powder and agricultural waste material, into a tar containing gas and charcoal-like solid by heating the organic substance. The wood chip is thermally decomposed in the charcoal and tar containing gas. A light oil and water-soluble organic substance are provided in a light organic component. A thermal decomposition apparatus is equipped with a hollow-cylinder shape thermal decomposition reactor. The thermal decomposition reactor is positioned inside a combustion heating furnace.    USE - Method for gasifying an organic substance (claimed) e.g. biomass. Can also be used for a timber, wood powder, paper, excrement, foodstuff waste material, agricultural residue such as sugarcane bagasse, rice straw and chaff.    ADVANTAGE - The method generates the tar without preparing a porous inorganic substance that is decomposed into charcoal-like solid, effectively adsorbs an organic substance, and improves thermal decomposition efficiency and energy density of the organic substance.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a gasifier    (2) an electric power generating apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation illustrating an organic substance gasification method.'(Drawing includes non-English language text)'
NOVELTY - A reactor for fuel cells comprises buffer tank which stores gas supplied to catalyst layer temporarily, catalyst layer (35) provided in annular space between inner pipe (31) and outer pipe (32), double cylinder pipe structure provided in surroundings of high temperature body, pre-heating tank (40) which absorbs heat transmitted from high temperature body to buffer tank, and gas communication opening provided in part which carried out substantially semicircle separation of inside of annular space from gas inlet of pre-heating tank.    USE - A reactor for fuel cells.    ADVANTAGE - The reactor performs catalytic reaction favorably.    DETAILED DESCRIPTION - A reactor for fuel cells comprises buffer tank which stores gas supplied to catalyst layer temporarily, catalyst layer (35) provided in annular space between inner pipe (31) and outer pipe (32), double cylinder pipe structure provided in surroundings of high temperature body, pre-heating tank (40) which absorbs heat transmitted from high temperature body to buffer tank, and gas communication opening provided in part which carried out substantially semicircle separation of inside of annular space from gas inlet of pre-heating tank. The gas inlet of segmentation tank that adjoined segmentation tank is provided in part which carried out substantially semicircle separation of inside of annular space from gas inlet of segmentation tank. The buffer tank is partitioned off into segmentation tanks (39a) so that layer may be formed in pipe-axis direction. The pre-heating tank is provided adjacent to buffer tank.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of carbon monoxide modifying device in vertical direction and horizontal direction.    Inner pipe (31)    Outer pipe (32)    Catalyst layer (35)    Segmentation tanks (39a)    Pre-heating tank (40)
NOVELTY - A powdered coal (4) is blown as an auxiliary reducing material through the tuyeres. Biomass charcoal (3) obtained by dry-distillation of biomass (1) is pulverized to produce ground material. The ground material and powdered coal are blown into blast furnace (8) through tuyeres, and blast furnace is operated.    USE - Method for operating blast furnace.    ADVANTAGE - The emission of carbon dioxide is effectively prevented during operation of blast furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows the explanatory view of operation of method of blast furnace.    Biomass (1)    Dry distillation apparatus (2)    Biomass charcoal (3)    Powdered coal (4)    Mixing apparatus (5)    Blast furnace (8)
NOVELTY - Method for utilizing biomass, involves (a) drying biomass by performing distillation to obtain biomass coal having Hardgrove grindability index of 45 or more, (b) pulverizing the obtained biomass coal together with coal to obtain powder, and (c) blowing the pulverized powder from tuyere as an auxiliary reducing material in blast furnace.    USE - The method is useful for utilizing biomass used as substitute for pulverized coal.    ADVANTAGE - The method is cost-effective, improves air transportability and flammability, and reduces emission of carbon dioxide in iron producing process.
NOVELTY - An acid gas removal system utilizes a cryogenic distillation tower (100) for separating sour gas stream into overhead gas stream comprising methane and liquefied bottom acid gas stream comprising carbon dioxide. A sulfurous component removal system positioned upstream of acid gas removal system receives raw gas stream and separates the raw gas stream into hydrogen sulfide stream and sour gas stream.    USE - System for removing acid gases from sour gas stream.    ADVANTAGE - The contents of hydrogen sulfide and other acid gases can be easily separated from the sour gas stream by cryogenic distillation process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for removing acid gases from sour gas stream.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the cryogenic distillation tower.    Fluid stream (12)    Cryogenic distillation tower (100)    Distillation zone (106)    Freezing zone (108)    Melt tray (130)
NOVELTY - Biologically active water (BW) is saturated melted water containing nanosized gas bubbles. The distance of hydrogen bond of water molecule which exists in interface with bubble is shorter than the distance of hydrogen bond in water at normal temperature and pressure.    USE - Biologically active water is used for biological activation (claimed) of plant, animal e.g. fish and shellfishes and microorganism.    ADVANTAGE - The environmentally-friendly and safe biologically active water is manufactured economically, easily and efficiently. The biologically active water stably activates plant, animal and microorganism for long period of time.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) apparatus (X) used for manufacture of biologically active water; and    (2) biological activation method.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of fish culture. (Drawing includes non-English language text)    Discharge portion (7)    Water tank (50)    Pump (51)    Flow path (52)    Discharge path (53)    Biologically active water (BW)    Apparatus used for manufacture of biologically active water (X)
NOVELTY - Manufacturing fuel form olive pomace comprises roasting olive pomace at 200-320 degrees C.    USE - The method is useful for manufacturing fuel for domestic use, such as coal for cooking and heating, and for industrial application (preferably fuel station) in the form of powder, pellets, granules and sticks.    ADVANTAGE - The temperature range provides specific high power energy, without release of odors and provides stability to the fuel, including protection against biological degradation over time. The roasting step reduces the moisture content and other odorous volatile molecules from the fuel, and increases the proportion of fixed carbon content.
NOVELTY - A catalyst contains active metal separated on carrier containing alumina and having pore volume of 0.2-1.0 ml/g and pore diameter of 50 nm or more. The active metal is rhodium, platinum and/or palladium, and is contained in an amount of 0.3-5 %mass with respect to 100 %mass of the carrier.    USE - Catalyst used in modifier for hydrogen production apparatus (both claimed).    ADVANTAGE - The catalyst has excellent sulfur-proof property.
NOVELTY - An isolated polynucleotide comprising a nucleic acid encoding a cellobiohydrolase or its fragment, is new. The nucleic acid is codon-optimized for expression in a yeast strain and where the cellobiohydrolase is selected from Cochliobolus heterostrophus, Gibberella zeae, Irpex lacteus, Volvariella, or Piromyces sp. cellobiohydrolase.    USE - The polynucleotide, vector, and host cell are used for hydrolyzing a cellulosic substrate and fermenting cellulose (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) a vector comprising the polynucleotide; (2) a host cell comprising a polynucleotide encoding a heterologous cellobiohydrolase or its fragment; (3) a host cell comprising the polynucleotide or the vector; (4) a host cell comprising a heterologous polynucleotide encoding a cellobiohydrolase, where the cellobiohydrolase has a specific activity on Avicel of 0.08 mu mol/mg/minute, and where the host cell is a yeast cell; (5) a co-culture comprising the host cell and a second host cell comprising a heterologous cellulase selected from an endogluconase, a beta -glucosidase, or a cellobiohydrolase; (6) a method for hydrolyzing a cellulosic substrate comprising contacting the cellulosic substrate with the host cell or the co-culture; and (7) a method of fermenting cellulose comprising culturing the host cell or the co-culture in a medium that contains crystalline cellulose under conditions for a period sufficient to allow saccharification and fermentation of the cellulose.
NOVELTY - A hydrogen production apparatus (10) has a desulfurization portion (11) which removes sulfur compound from a raw material containing hydrocarbon, a modification portion (12) which generates a reformed gas by modifying raw material which passed through desulfurization portion, a modification catalyst containing hydrogen and carbon monoxide, and one or more hydrogen sulfide-removal portion (13,15) which removes hydrogen sulfide which is provided downstream more than the modification portion.    USE - Hydrogen production apparatus is used for fuel cell system (claimed).    ADVANTAGE - The apparatus provides hydrogen, with reduced impurities. The fuel cell system comprising the hydrogen production apparatus is stably operated for a long period of time.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the hydrogen production apparatus.    Fuel cell system (1)    Hydrogen production apparatus (10)    Desulfurization portion (11)    Modification portion (12)    Hydrogen sulfide-removal portions (13,15)
NOVELTY - The apparatus (10) has a hydrogen peroxide vaporization part (20) for evaporating hydrogen-peroxide solution liquid that is fed in an evaporation container (22) using a heating part (24) and generating gas that contains hydrogen peroxide gas. A hydrogen-peroxide solution liquid feeding part (30) feeds hydrogen-peroxide solution in the evaporation container. A waste gas collection part (60) collects waste gas that is discharged from an exposure container.    USE - Chemical-stability evaluation apparatus for a material e.g. fuel cell component, at hydrogen peroxide gas atmosphere. Uses include but are not limited to an electrolytic membrane, a catalyst layer, a membrane electrode assembly and a sealing material.    ADVANTAGE - The apparatus stably exposes a test piece in high concentration hydrogen-peroxide gas when small amount of hydrogen-peroxide solutions are fed, and whole-quantity evaporation is carried out in the evaporation container. The apparatus avoids heating the high concentration hydrogen-peroxide solution. The apparatus generates high concentration hydrogen-peroxide gas, and evaluates chemical stability under low temperature and low humidity of 120 degrees Celsius or less.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a chemical-stability evaluation apparatus.    Chemical-stability evaluation apparatus (10)    Hydrogen peroxide vaporization part (20)    Evaporation container (22)    Heating part (24)    Hydrogen-peroxide solution liquid feeding part (30)    Waste gas collection part (60)
NOVELTY - The system determines the output voltage of vehicle-mounted battery (30) and generates the PWM pulse of preset duty ratio based on duty ratio control map. A switching element (38) converts the output voltage of battery into pulse voltage according to duty ratio by responding to PWM pulse. An electrolytic vessel (36) is made to generate hydrogen oxygen gas and supply to combustion chamber (16) as combustion acceleration gas. The variable control of generation amount of combustion acceleration gas added to main fuel is performed according to determined voltage.    USE - Combustion improvement system for internal combustion engine e.g. diesel engine such as bus and truck. Can also be used in petrol engine, ethanol engine, petrol ethanol mixing engine, light oil and ethanol mixing engine, propane-gas engine or natural gas engine.    ADVANTAGE - The generation amount of hydrogen oxygen gas in electrolytic vessel can be increased and discharge amount of hazardous ingredients accompanying acceleration of vehicle such as black smoke, hydrocarbon, carbon dioxide and carbon monoxide is reduced. The fall in battery remaining capacity is avoided reliably and electrolysis vessel with improved electrolysis efficiency is enabled. The power consumption of electrolytic vessel is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for combustion improvement method.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the combustion improvement system. (Drawing includes non-English language text)    Combustion chamber (16)    Battery (30)    Electrolytic vessel (36)    Switching element (38)    Voltage sensor (52)
NOVELTY - A hydrogen production apparatus (10) comprises modification part (11) which generates reformed gas containing hydrogen and carbon monoxide, and first hydrogen sulfide removal part (12) which removes hydrogen sulfide. The first hydrogen sulfide removal part is more downstream than modification part.    USE - A hydrogen production apparatus used for fuel cell system (claimed).    ADVANTAGE - The apparatus has low maintenance frequency, and operates stably over a long period of time.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of fuel cell system comprising hydrogen production apparatus. (Drawing includes non-English language text).    Fuel cell system (1)    Hydrogen production apparatus (10)    Modification part (11)    First hydrogen sulfide removal part (12)    Shift reaction part (13)
NOVELTY - A polyester fiber raw material is isolated and extracted by removing alkaline solution part after heating polyester and cotton mixed use textiles in aqueous alkali solution ( less than or equal to 5%) at 60-90 degrees C, neutralized washing of polyester and cotton mixed use textiles by acidic electrolyzed water, carrying out enzymatic decomposition of cellulose using cellulase, and carrying out solubilization removal of cotton fiber raw material.    USE - Isolation and extraction of polyester fiber raw material.    ADVANTAGE - The method is simple and efficient.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a recovery of polyester fiber raw material involving adding polyethyleneglycol fatty acid ester to enzyme reaction liquid for decomposing cellulose of polyester and textiles for cotton mixture by cellulase.
NOVELTY - Processing a biomass comprises (a) separating the biomass into a lignin fraction and (hemi)cellulose fraction; (b) processing the (hemi)cellulose fraction; and (c) converting the lignin fraction into an organo-mineral fertilizers.    USE - The process is useful for processing a biomass and for producing an organo-mineral fertilizer (claimed). No biological data given.    ADVANTAGE - The process reduces the release of carbon dioxide in the environment, hence avoids environmental pollution, and provides adequate separation of lignin and (hemi)cellulose, preferably in annual plants and biomass residues.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) an organo-mineral fertilizer comprising ammonium nitrogen, normally hydrolyzable amide nitrogen and fixed organic nitrogen, where the rate of release nitrogen in the fertilizer is adjusted by changing the ratio of ammonium nitrogen:amide nitrogen:solid organically bound nitrogen in the fertilizer; and    (2) a process of producing organo-mineral fertilizer comprising ammoxidation of lignin, where the lignin is obtained from the digestion of biomass.    DESCRIPTION OF DRAWING(S) - The figure shows a flow chart of a method of processing a biomass (Drawing includes non-English language text).
NOVELTY - The system (2) has biomass gasification furnace (3) to gasify biomass (1), and dust removal device (15) to remove gasified char in gasified gas generated in furnace. A gas purifying unit (23) includes gasified gas introduction unit (27) for introducing gasifying gas in which gasified char is removed, into porous particles having fine pores and biomass. A purified gas exhaust unit (29) exhausts the purified gas from gas purification unit.    USE - System for gasifying biomass such as farm product, by-product, timber and plant.    ADVANTAGE - The purification of gasifying gas generated by gasifying biomass in furnace can be performed efficiently. The concentration of hydrogen sulfide in the gasifying gas can be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for gasifying biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass gasification system. (Drawing includes non-English language text)    Biomass (1)    Biomass gasification system (2)    Biomass gasification furnace (3)    Dust removal device (15)    Gas purifying unit (23)    Gasified gas introduction unit (27)    Purified gas exhaust unit (29)
NOVELTY - The system has a thermal medium circuit (8) which is provided with a thermal medium for exchanging the heat with a fuel cell (1). The hot water is circulated through the hot-water storage circulation path (9) by hot-water storage circulation pump (4). A controller (19) is configured to perform a forced circulation operation of stored hot water. The hot-water storage circulation pump is operated at larger operating quantity than the maximum operation quantity when fuel cell generates electricity.    USE - Fuel cell cogeneration system.    ADVANTAGE - The precipitation of the hardness component is suppressed such that the clogging of flow path is suppressed. The destabilization of electric power generation is avoided. The reliability of the fuel cell cogeneration system is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the fuel cell cogeneration system. (Drawing includes non-English language text)    Fuel cell (1)    Hot-water storage circulation pump (4)    Thermal medium circuit (8)    Hot-water storage circulation path (9)    Controller (19)
NOVELTY - An external water source (112) provides water to the arrangement, a water pump (118) pumps the provided water to facilitate water flow, and a steam generator (120) evaporates water from the facilitated water flow for generating pressurized steam having a motive pressure for a steam jet-ejector (122). An entraining portion of the essentially low pressure anode exhaust gas stream in the anode side gas recirculation, compresses the gas mixture to an intermediate pressure of the fuel feed-in stream for controlling O/C relationship in the fuel cell side.    USE - Arrangement for controlling oxygen-to-carbon (O/C) relationship in fuel cell system such as solid oxide fuel cell (SOFC) system for producing electricity with fuel cells. Can also be used in molten carbonate fuel cells (MCFCs).    ADVANTAGE - A practical O/C relationship management in the fuel cell system can be achieved by utilizing conventional system components.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for controlling oxygen-to-carbon (O/C) relationship in fuel cell system for producing electricity with fuel cells.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the SOFC device.    External water source (112)    Condenser (116)    Water pump (118)    Steam generator (120)    Steam jet-ejector (122)
NOVELTY - Fermentation-decomposition treatment apparatus, comprises box-shaped decomposition treatment tank and recessed portion near front and back walls of the decomposition tank. The recessed portion has a trough bottom, which is lower than bottom surface of decomposition treatment tank. When a to-be-agitated substance is added into the decomposition treatment tank, which is agitated by agitation unit, which moves the substance front and back between front and back walls.    USE - The fermentation-decomposition treatment apparatus is useful for processing sludge e.g. organic waste.    ADVANTAGE - The apparatus prevents adhesion of sludge on side walls of the decomposition treatment tank.    DETAILED DESCRIPTION - Fermentation-decomposition treatment apparatus, comprises box-shaped decomposition treatment tank and recessed portion near front and back walls of the decomposition tank. The recessed portion has a trough bottom, which is lower than bottom surface of decomposition treatment tank. When a to-be-agitated substance is added into the decomposition treatment tank, is agitated by agitation unit, which moves the substance front and back between front and back walls. The substance is pushed up against the front and back walls by the agitation unit, which falls into the recessed portion and is discharged outside.
NOVELTY - Converting a hydrocarbon feed comprises: (a) catalytically cracking the feed; (b) separating the mixture into spent catalyst and hydrocarbon product; (c) separating the hydrocarbon product into two or more fractions; (d) further catalytically cracking at least one of the fractions; (e) separating the mixture into used catalyst and hydrocarbon product; (f) subjecting fractions and hydrocarbon product to separation such as to obtain a gas and liquid fractions; (g) increasing the pressure of the gas; (h) separating hydrocarbons; and (i) separating the propane-lean product into a fraction.    USE - The process is useful for converting hydrocarbon feed (claimed), which is useful in a fluid catalytic cracking.    ADVANTAGE - The process provides conventional cracking products.    DETAILED DESCRIPTION - Converting a hydrocarbon feed comprises: (a) catalytically cracking the feed; (b) separating the mixture into spent catalyst and hydrocarbon product; (c) separating the hydrocarbon product into two or more fractions; (d) further catalytically cracking at least one of the fractions; (e) separating the mixture into used catalyst and hydrocarbon product; (f) subjecting one or more fractions and hydrocarbon product to separation such as to obtain a gas and one or more liquid fractions; (g) increasing the pressure of the gas; (h) separating hydrocarbons comprising 3 carbon atoms from the product to obtain propane-lean product; and (i) separating the propane-lean product into a fraction containing hydrocarbons comprising 4 carbon atoms, a fraction containing hydrocarbons comprising 5 or 6 carbon atoms, and a heavy fraction, which process the fraction containing hydrocarbons comprising 5 or 6 carbon atoms is sent as feed to step (d).    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a process flow scheme.    Riser reactor (3)    Stripper/separator (5)    First cyclone (7)    Second cyclone (8)    Regenerator. (11)
NOVELTY - The apparatus has solid and liquid fuel components comprising solid fuel e.g. sodium borohydride, and liquid fuel e.g. water or methanol, respectively, that are mixed to form a fuel mixture, where the fuel mixture is made to react to produce gas i.e. hydrogen, in presence of catalyst. The solid compartment comprises a cover (22) e.g. frangible cover or peelable cover, connected to an actuator placed outside the apparatus, where the actuator is selectively actuated to mix the fuels, and is moved by a user.    USE - Apparatus for generating hydrogen gas use in a fuel cell utilized to directly convert chemical energy of reactant e.g. fuel such as hydrogen and oxidant, into direct current electricity. Can also be used for generating oxygen and ammonia.    ADVANTAGE - The apparatus has improved storage and starting capabilities and prolonged service life, and can efficiently produce hydrogen. The apparatus comprises a starter mechanism to isolate the solid fuel from the liquid fuel, so that pre-mixed fuel can degrade to react slowly with each other in the absence of the catalyst during storage.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of a spring-loaded starter mechanism.    Lock knob (12)    Pull-tab (13)    Seal piston (16)    Chamber (20)    Cover (22)
NOVELTY - Engineered fuel feed stock (I) comprising at least one component derived from a processed municipal solid waste (MSW) stream, comprises a carbon content of 30-80%; a hydrogen content of 3-10%, an ash content of less than 10%; and a sorbent.    USE - (I) is useful for a variety of purposes including as gasification and combustion fuels. (I) is useful for the production of thermal energy, power, biofuels, petroleum, and chemicals.    ADVANTAGE - (I) contains substantially no glass, metals, grit, and noncombustibles. (I), when converted, produces less greenhouse gas (GHG) emissions as compared to the known level of GHG emitted from coal when converted. (I) with added sorbent can mitigate corrosion, improve fuel conversion, extend power generating plant lifetime, reduce ash slagging, and reduced operating temperature. The sorbent in (I) reduces the amount of a variety of pollutants present in traditional fuel and feed stocks, including sulfur and chlorine. (I) has improved reaction kinetics, improved sorbent reactivity, improved pollutant removal efficiency, improved fuel conversion, improved corrosion control, reduced ash slagging, reduced operating temperature, extend power generating facility lifetime, avoid expensive retrofit costs, and reduced operating and maintenance costs. (I) has superior combustion or gasification profiles.
NOVELTY - Bringing small lumpy, mineral carbonates in combustible form, comprises grinding the carbonates to a particle size of less than or equal to 1 mm, adjusting the moisture content of the grounded carbonates to 2-8 wt.%, mixing the grounded, wet carbonates with starch, cellulose and/or their derivatives (the added amount of starch, cellulose and/or their derivatives in total, amounts to 1-10 wt.% of the mass of the grounded carbonates), and compacting the resulting mixture by a roller press.    USE - The small lumpy, mineral carbonates in combustible form is useful as a reducing agent in steel production.    ADVANTAGE - The method: comprises bringing small fractions obtained during the breakage of chalk in to a combustible form, which can be supplied for an industrial re-use; allows the change of the burning performance of small lumps of chalk to obtain briquettes in stable combustible form with desired particle size; and produces the chalk material in the form of granulate or briquettes with good mechanical cohesion, i.e. high mechanical strength.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a briquettes or granulate from essentially calcium carbonate, obtained by the above mentioned method.
NOVELTY - A two-stage dry anaerobic fermentation of traditional Chinese medicinal dregs comprises crushing traditional Chinese medicinal dregs until its granular size is 5-10 mm; adding fresh cow dung and sludge to the granules at a ratio of 2:1:3; hydrolyzing and acidifying the mixture at 55 plus minus 1 degrees C and pH of 5.5 plus minus 0.2; subjecting to aerating tank; and aerating at 35 plus minus 1 degrees C and a pH of 6.8-7.2 in a close sealed condition while stirring for every 2 minutes.    USE - A two-stage dry anaerobic fermentation of traditional Chinese medicinal dregs.    ADVANTAGE - The fermentation is quick and short, high processing efficiency, strong anti-impact load capability, high yield, and stable system operation.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a two-stage dry anaerobic fermentation of traditional Chinese medicinal dregs. Drawing includes non-English language text.
NOVELTY - The furnace has a furnace cover provided with a guide rod hole. A guide rod penetrates through the guide rod hole. A lower end of the guide rod is fixed with a material spreading machine i.e. material pressing disk. The material spreading machine is arranged in a furnace cylinder. A steel pipe, a metal flat washer and a heat resistant rubber flat washer are orderly penetrating through the guide rod. The heat resistant rubber flat washer is tightly in contact with a top out part of the furnace cover. An upper end of the guide rod is provided with a handle.    USE - Straw gasification furnace.    ADVANTAGE - The material spreading machine of the furnace stirs or presses a straw in a furnace body, and is beneficial for fully burning and generating the gas. The machine is beneficial for controlling the firepower and the burning time. The furnace has artful design, complete combustion, easily controlled burning time, difficult flameout and energy-saving performance, is convenient to use, and simple to operate.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a straw gasification furnace in partial sectional.
NOVELTY - The gasifier has a material pressing lever device located on an upper part of a furnace body (10). A low-temperature gas guiding device is located on a middle part and an upper part of the furnace body. A high-temperature gas guiding device is located under the furnace body. An ash discharging device is located on a furnace bottom part. A movable connector (a) is connected with a lower end of a draw rod (2). Another movable connector (b) on an upper end of the draw rod is connected with a horizontal pressing rod (1).    USE - Material-added, ash-discharged and continuous gas-produced straw gasifier for converting agricultural and forestry residues into combustible gas and use in restaurants and boilers.    ADVANTAGE - The gasifier provides better troubleshooting functions, better gas production efficiency and continuous gas production. The gasifiers avoids stopping the fire while adding firewood to the gasifier or discharging the ash, occurring flameout caused by burning out and partial combustion, causing secondary pollution of tar and applicable to restaurants and boilers.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a material-added, ash-discharged and continuous gas-produced straw gasifier.    Movable connectors (a, b)    Horizontal pressing rod (1)    Draw rod (2)    Spring (4)    Furnace body (10)
NOVELTY - The gasifier has a material feeder connected with middle furnace structure. An operation platform is mounted on middle furnace structure. A power gate is connected with lower furnace structure and middle furnace structure. A sealing cabin of lower furnace structure is mounted under power gate. An electric dust remover is connected with fan. A lower gate is mounted at distance 20 cm away from furnace structure.    USE - Compound gasifier for producing biomass fuel.    ADVANTAGE - The production of biomass fuel is performed continuously. The convenient and safe operation of the compound gasifier and anti-explosion production are achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the compound gasifier.
NOVELTY - The device has a gasification furnace (4) whose air outlet is connected with a high-temperature input end of a heat exchanger (14). A low-temperature air output end of the exchanger is connected in series with a dust remover (17), an acid eliminating tower (18) and a drier (19) in a sequential manner. A dreg discharging hole of a cracking furnace (6) is formed with a material inlet of a particle separator (7). A dreg outlet of the separator is connected with a dreg inlet of a dreg cooler (8). A dreg outlet of the cooler is connected with the material inlet of an ash coke separator (9).    USE - Biomass double-furnace conjoined cracking gasification device for producing pure synthetic gas.    ADVANTAGE - The device obtains the pure synthetic gas with high quality after cooling, removing dust and acid and drying the primary synthetic gas. The device ensures low energy consumption, low manufacturing cost, high efficiency of cold gas and high heat value of the generated synthetic gas. The device eliminates tar and alkali metal compounds, and can be applied to continuous production of the pure synthetic gas in large scale.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a biomass double-furnace conjoined cracking gasification device.    Gasification furnace (4)    Cracking furnace (6)    Particle separator (7)    Dreg cooler (8)    Ash coke separator (9)    Heat exchanger (14)    Dust remover (17)    Acid eliminating tower (18)    Drier (19)
NOVELTY - The tank has a biomass gasification furnace (1) whose gas inlet (2) is connected to an air compressor (3). A gas outlet (4) of the furnace is connected with a water filtering chamber (7) via a pipeline (5). Upper and lower parts of the water filtering chamber are provided with a purifying tube (9) and a drain opening (8), respectively. The water filtering chamber is connected with another drain opening. The tank (6) is connected with a third drain opening, where upper face of the tank is connected to the gas outlet.    USE - Gas-storage tank for a biomass gasification furnace.    ADVANTAGE - The tank has burnable gas that is generated by the biomass gasification furnace. The furnace is convenient to clean, and is wide in application range.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a gas-storage tank.    Biomass gasification furnace (1)    Gas inlet (2)    Air compressor (3)    Gas outlet (4)    Pipeline (5)    Tank (6)    Water filtering chamber (7)    Drain opening (8)    Purifying tube (9)
NOVELTY - The processing device has a crushing machine, densifying machine and pelletizer which are installed on a tractor. The crushing machine, densifying machine and pelletizer are integrally moved as the tractor is moved.    USE - Mobile processing device for densifying biomass solid fuel.    ADVANTAGE - The device enables recycling and palletizing of straws.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the mobile processing device.
NOVELTY - The device has belt conveyors that are arranged between the garbage selection device, iron-removal devices, crushing device and garbage crushing device. A belt transportation packing machine is arranged between mixing stirring device and grinding shaping device. The garbage crushing device and mixing stirring device are connected together by conveying cylinder.    USE - Device for producing organic composite fuel using household garbage.    ADVANTAGE - The device is simple in structure. The crushing device, iron removal device and shaping device are connected by belt conveyor to form closed garbage fuel production line, so that manufacturing cost of the device is reduced. The device can be operated automatically during whole production, so that man power required for operating the device is reduced. The product can be produced based on the user requirement.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the device for producing organic composite fuel using household garbage.
NOVELTY - The system has a sludge delivery device (2) whose output end is arranged above the inlet of airflow type dryer (1). The cylinder of the dryer is connected with supercharging pipe (6) whose backside is respectively connected with high-pressure air blower (5) and smoke filter separator (4). The dryer has outlet which is connected connecting funnel (7) whose upper end is connected with smoke pipe (3). The air outlet (23) and air inlet (22) of smoke pipe are connected with smoke exhausting system (15) and heat source (14), respectively.    USE - System for manufacturing fuel through drying waste sludge.    ADVANTAGE - The system is simple in structure, safe and reliable, efficient and energy saving, and has good drying effect and high mechanical degree.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of system for manufacturing fuel through drying waste sludge.    Airflow type dryer (1)    Sludge delivery device (2)    Smoke pipe (3)    Smoke filter separator (4)    Air blower (5)    Supercharging pipe (6)    Connecting funnel (7)    Heat source (14)    Smoke exhausting system (15)    Air inlet of smoke pipe (22)    Air inlet of smoke pipe (23)
NOVELTY - The system has combustion material extraction device provided with feeding opening. The discharged material of the combustible material discharging opening of the combustible material extraction device is conveyed to the feeding opening of the crushing device. The crushed discharged material of the discharging opening of the crushing device is conveyed to the feeding opening of the extrusion forming device. The discharging opening of the extrusion forming device is served as the outlet of RDF finished product.    USE - System for manufacturing RDF.    ADVANTAGE - The material of refuse derived fuel can be extracted from household waste so that RDF can be manufactured with excellent purity and heat value. Excellent economic benefit and social effect can be achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of system of manufacturing RDF.
NOVELTY - A methane preparation device with double anaerobic fermentation spaces, comprises an upper tank that is a facultative tank, a water inlet/outlet system of a movable cover, and a main body of a methane tank; where the methane preparation device with double anaerobic fermentation spaces is divided to the upper tank and a lower tank; the upper tank is the facultative aerobic tank and shared by the water pressure space and pre-fermentation space; the lower tank is an absolute anaerobic methane ferment tank; and the facultative tank and the methane tank are connected by a top water returning hole.    USE - The methane preparation device with double anaerobic fermentation spaces is useful for industrial applications.    ADVANTAGE - The methane preparation device with double anaerobic fermentation spaces has simple structure and good methane generation effect.    DETAILED DESCRIPTION - A methane preparation device with double anaerobic fermentation spaces, comprises an upper tank that is a facultative tank, a water inlet/outlet system of a movable cover, and a main body of a methane tank; where the methane preparation device with double anaerobic fermentation spaces is divided to the upper tank and a lower tank; the upper tank is the facultative aerobic tank and shared by the water pressure space and the pre-fermentation space; the lower tank is an absolute anaerobic methane ferment tank; the facultative tank and the methane tank are connected by a top water returning hole; and the methane preparation device with double anaerobic fermentation spaces cancels the water inlet port and the water outlet port of the traditional methane tank, and adds a material inlet/outlet spare device on the window, which is taken as a spare system device.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the methane preparation device with double anaerobic fermentation spaces.
NOVELTY - Conversion of organic biowaste to biocrude oil comprises: providing concentrated biosolid fraction and bypass liquid fraction obtained from organic biowaste; subjecting the biosolid fraction to hydrothermal process under conditions to obtain a biocrude oil product, aqueous residual product and gaseous residual product; cultivating an organism in a culturing media to obtain a cultivated mixture; recovering a concentrated cultivated organism fraction from the cultivated mixture; and introducing the cultivated organism fraction and optionally the biosolid fraction to hydrothermal process.    USE - The process is useful for conversion of organic biowaste to biocrude oil.    ADVANTAGE - The process: allows multiple use cycles for aqueous residual product which comprises the nutrients for organism growth thus eliminating or reducing the cost; does not require high oil content algae; provides cost-effective extraction of oil from wet algae biomass without drying (i.e. increases algae oil production capabilities and reduces the energy inputs required for extracting algae biofuel products); and provides environmental benefits including improving water quality, conserving fresh water resource, sequestering carbon dioxide, reducing solid waste quantities, and destroying residual pharmaceuticals and antibiotic resistance genetic materials in human and animal wastes.
NOVELTY - The furnace has a gasifying furnace body provided with an antiseptic liner. An upper part of the gasifying furnace body is an inverted taper structure. A gasifying furnace feeder is set on the upper part of the gasifying furnace, and includes a feeding box, an upper turning plate valve and a lower turning plate valve. The upper turning plate valve and the lower turning plate valve are automatically driven and controlled by an electric hydraulic rod computer. An antiseptic film structure in an inner surface of the gasifying furnace body.    USE - Mass biomass fixed bed gasifying furnace i.e. biomass straw gasifying furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial sectional view of a mass biomass fixed bed gasifying furnace.
NOVELTY - The furnace has a body (3) placed on an end of a shell (1). The body with a water sleeve interlayer (2) is fixed on an outer surface. A storage box with an automatic feeding device is installed on another end of the shell. A secondary wind blowing oxygen supply device (5) is equipped on a middle part of the body. The body above the secondary wind blowing oxygen supply device is provided with a triple wind blowing oxygen supply atomizing device (6). An upper end of the body is allocated with a flame combustion chamber (11).    USE - Dust removal combustion assisting straw gasification combustion furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a dust removal combustion assisting straw gasification combustion furnace.    Shell (1)    Water sleeve interlayer (2)    Body (3)    Secondary wind blowing oxygen supply device (5)    Triple wind blowing oxygen supply atomizing device (6)    Flame combustion chamber (11)
NOVELTY - The furnace has a material inlet with an upper cover (3) placed at a top part of a sleeve structure shell (2). An air outlet (14) is coupled with a stove (10) via a pipeline (13). An air inlet (12) is furnished at an upper part of a gas chamber (4). An elastic pressing-material device (7) is arranged between an upper cover of the feed inlet and fuels (6) in the gas chamber. Upper and lower parts of the pressing-material device are respectively placed against to a lower part of the upper cover and an upper part of the fuels. An ignition mouth (9) is mounted at a lower part of a burning chamber (5).    USE - Multi-functional plant gasification furnace.    ADVANTAGE - The furnace prevents smoke leakage to avoid polluting the environment by the negative-pressure firing. The elastic pressing-material device is utilized, so that the fuel stays at the extruded state in the burning process. The furnace avoids the opening the upper cover of the feed inlet to press to prevent the gas from being leaked and avoid polluting the environment so as to save energy and reduce working intensity. The furnace is simple, convenient and easy to use.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a multi-functional plant gasification furnace in partial section.    Sleeve structure shell (2)    Upper cover (3)    Gas chamber (4)    Burning chamber (5)    Fuels (6)    Elastic pressing-material device (7)    Ignition mouth (9)    Stove (10)    Air inlet (12)    Pipeline (13)    Air outlet (14)
NOVELTY - The furnace has a water jacket furnace body provided with a combustion chamber (8). A lower side of the combustion chamber is an ash storage chamber (1). A water pipe type fire grate is arranged between the combustion chamber and the ash storage chamber. The combustion chamber is provided with vertical water pipes (6) vertically, annularly arrayed and connected with a water jacket at two ends. A fuel cabin is provided with air supply passages at bottom and lateral side and is formed by the vertical water pipes and the water pipe type fire grate.    USE - High-efficiency and energy-saving cooking and heating furnace.    ADVANTAGE - The furnace can burn the biomass fuel or the coal, and has large heated area, high thermal efficiency, fast heating and temperature rise and convenient use. The furnace is clean and sanitary.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a high-efficiency and energy-saving cooking and heating furnace.    Ash storage chamber (1)    Furnace slag outlet (5)    Vertical water pipes (6)    Combustion chamber (8)    Cylindrical fire gathering hood (10)
NOVELTY - A city household garbage processing system, comprises a garbage storage pit, a garbage sorting system, an anaerobic fluid container, an anaerobic organism reactor, a burning system, a methane generator, a percolate storage pool, and a garbage percolate post-processing system; where a transferring channel is arranged between the garbage storage pit and the sorting system; a leakage pipeline is arranged between the garbage storage pit and the anaerobic fluid container; and a transferring channel is arranged between the garbage sorting system and the anaerobic organism reactor.    USE - The city household garbage processing system is useful for industrial applications.    ADVANTAGE - The city household garbage processing system is highly efficient and environment-friendly. Moreover, it saves the land and can generate a large quantity of renewable energy.    DETAILED DESCRIPTION - A city household garbage processing system, comprises a garbage storage pit, a garbage sorting system, an anaerobic fluid container, an anaerobic organism reactor, a burning system, a methane generator, a percolate storage pool, and a garbage percolate post-processing system; where a transferring channel is arranged between the garbage storage pit and the sorting system; a leakage pipeline is arranged between the garbage storage pit and the anaerobic fluid container; a transferring channel is arranged between the garbage sorting system and the anaerobic organism reactor; the anaerobic organism reactor is connected with the percolate storage pool by a pipeline; and the percolate storage pool is connected with the anaerobic fluid container by a pipeline.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the city household garbage processing system.
NOVELTY - Constructed wetland sewage purification system comprises a wetland bed and water plants, where the water plants are equipped on the wetland bed. The wetland bed is orderly divided into three layers from bottom to top i.e. a gravel layer, a blend layer and a coil layer. The blend layer is formed by lime stone, waste steel sludge, waste slag and soil.    USE - Constructed wetland sewage purification system.    ADVANTAGE - The constructed wetland sewage purification system is cost-effective and has good processing efficiency.
NOVELTY - A fuel gas discharging pipe is arranged between a helix sealed material conveyor (1) and a hollow-core rotating shaft head (4). A horizontal columnar pipe heat exchanger arranged in a destructive distillation pipe is provided with multiple heat exchanging pipes distributed in the destructive distillation pipe. The multiple heat exchanging pipes are fixed through a pipe plate (9). The heat exchanging pipe passing through an inserting hole is formed on pipe plate, and an overflow opening is formed on the pipe plate close to a jetting burner.    USE - Solid biomass internal combustion dry distillation gasification furnace.    ADVANTAGE - The heat exchanging pipe passing through inserting hole is formed on pipe plate, and overflow opening is formed on pipe plate close to jetting burner. Hence the destructive distillation rate of drying on the gasified materials is enhanced, and the heat energy utilization is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the solid biomass internal combustion dry distillation gasification furnace.    Helix sealed material conveyor (1)    Hollow-core rotating shaft head (4)    Pipe plate (9)    Gas input pipe (13)    Helix slag discharger (17)
NOVELTY - The method is carried out by rotating the working chamber (4) containing the electrolyte in a centrifugal inertial force and magnetic fields. The electrolyte is circulation in the first working circuit causes its rotation in a stationary chamber located in orthogonal electric and magnetic fields so that the magnetic field is directed parallel to the electrolyte rotation axis and the electric field is directed radially from the periphery to the centre of the chamber. Thus due to the vector sum of the Lorenz force and the centrifugal inertia force, due to charge and mass difference, the negatively charged heavy ions, anions, are displaced to the chamber periphery and positively charged light hydrogen ions, cations, are displaced to the centre to the axis rotation zone. Thus a magnito-hydrodynamic separation of ions into two isolated streams takes place. The electrolysis, ions charge neutralization, takes placed in the working chamber and the discharge chambers (5,6) due to current flow in the external electric circuit and eliminating shunting by the working chamber walls. The gas is dried in tow separators (7,8). The energy consumption during the electrolysis endothermic reaction, converted to hydrogen and oxygen potential energy is compensated in the heat exchanger (1) due to environmental heat energy.    USE - Hydrogen production for use in stationary and mobile power supply units in transport, chemical industry, power production, engineering etc.    ADVANTAGE - Production costs are reduced while reducing formation of hazardous waste and global warming effect.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for    (A) Electric unit for hydrogen production    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the heat pump producing hydrogen    Working chamber (4)    Discharge chambers (5,6)    Separation drying chambers (7,8)
NOVELTY - Upgrading an organic acid comprises neutralizing the organic acid to form a salt and thermally decomposing the resulting salt to form an energy densified product.    USE - The process is useful for: upgrading an organic acid (claimed); and producing high energy density fuels, which is useful as diesel and jet fuels.    ADVANTAGE - The process is economic and eco-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a process-I for dimerization of levulinic acid into a 9C tri-ketone using either a calcium or magnesium salt of levulinic acid.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a process for energy densification of biomass-derived organic acids.    Neutralization reactor (12)    Dryer (14)    Furnace (16)    Kiln (18)    Condenser. (20)
NOVELTY - The apparatus has mass-flow controller (10) that controls gas supply volume into gas-dissolving membrane module (2). A gas filter (11) is provided in gas supplying pipe (8) between electrolyzer (3) and mass-flow controller.    USE - Apparatus of manufacturing gas-dissolved water used for cleaning of glass substrate for LCD.    ADVANTAGE - The condensed water produced in gas supplying pipeline is removed by gas filter provided in gas supplying pipe between electrolyzer and mass-flow controller.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for gas-dissolved water manufacturing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the apparatus of manufacturing gas-dissolved water. (Drawing includes non-English language text)    Gas-dissolving membrane module (2)    Electrolyzer (3)    Gas supplying pipe (8)    Mass-flow controller (10)    Gas filter (11)
NOVELTY - A household garbage composting device comprises a sealing box body and a feeding port installed on the box body. A composting room is installed in the box body. The feeding port is communicated with the composting room. A discharging port is arranged on the composting room. A ventilation helical stirring propeller is installed in the composting room. A water bath groove is arranged on lower part of the composting room. A heating device is connected on the water bath groove. A secondary composting room is on lower part of the composting room in the box body.    USE - Household garbage composting device.    ADVANTAGE - The device supplies heat energy to accelerate speed for fermenting and degrading kitchen waste and other organic household garbage, provides environment for moving microorganism, and optimizes usage rate of heat energy. It uses solar for heating, which is safe to the environment and which reduces normal energy consumption. Further, the secondary composting room can greatly shorten longitudinal length of integral composting device, saves occupying area of the compost, and further improves fermentation degree of the compost and reduces work intensity.
NOVELTY - The furnace has a gas generating room whose right side is provided with a gas generating wind machine. The machine is accessed to a lower part of a heating tube via a wind tube. A top part of the room is provided with a double layer furnace cover and a feeding port. A middle part of a gas transporting tube is provided with smoke flue. A crossed part of the flue and the tube are provided with a changing door. The flue is connected with an interlayer of a gas generating room top double layer furnace. An outer wall of a furnace body is provided with an igniting switch and a comprehensive switch.    USE - Injector type gasifying furnace for use in rural home.    ADVANTAGE - The furnace has high thermal exchange efficiency of gasifying gas or natural gas furnace and a gas generator.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an injector type gasifying furnace.
NOVELTY - Methane recovery and utilization device comprises a methane pool (1), and a feeding pipe (2) passing through the upper end face of the methane pool and inserted into the lower part of methane pool. The lateral wall of bottom part of methane pool is equipped with drainage pipe (3). The upper end face of methane pool is equipped with gas storage room (4) communicated with internal part of the methane pool. The gas storage room is connected with air outlet pipe (5). The methane pool is equipped with heating pipe, and outer wall of methane pool is assembled with solar energy heat collection plate.    USE - Used as a methane recovery and utilization device.    ADVANTAGE - The device: has compact structure, high heating temperature in pool and small effect of external environment to methane output; is relatively stable; does not lose heat; and cleans the residual slag conveniently.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the methane recovery and utilization device.    Methane pool (1)    Feeding pipe (2)    Drainage pipe (3)    Gas storage room (4)    Air outlet pipe (5)
NOVELTY - Method for producing fuel using waste material, involves fermenting waste material, crushing fermented material into coarse powder having predetermined size, drying obtained powder, crushing the dried product, and blowing the crushed product into cement kiln or calcination furnace.    USE - The method is useful for producing fuel used for cement firing.    ADVANTAGE - The obtain fuel is inexpensive and has excellent combustibility.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus for producing fuel, which comprises fermentation processing apparatus for fermenting waste material, primary crusher for crushing the fermented material, selected for removing coarse material having predetermined size, drying machine for drying the selected material, crusher for crushing dried product and blowing apparatus for blowing the crushed material.
NOVELTY - The machine has a sealable vessel (1) that is provided with multiple mutually connected air distribution pipes (2) on the inner layer. Multiple air exhaust holes are provided with the air distribution pipes. A master air inlet of distribution pipe is connected with an air intake and exhaust pipe (3) outside the vessel. The air intake and exhaust pipe is divided into two branches, one of which is connected with an air pump (4) by a valve for filling air into the vessel and other is connected with vacuum pump (6) by the valve to exhaust air from vessel.    USE - Organic fertilizer composting machine.    ADVANTAGE - The organic fertilizer composting machine controls the fermentation temperature and air, hence the fermentation speed is increased, while providing capability for selecting anaerobic fermentation and aerobic fermentation. The organic fertilizer composting machine reduces the labor intensity.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional block diagram of the organic fertilizer composting machine.    Sealable vessel (1)    Air distribution pipe (2)    Intake and exhaust pipe (3)    Air pump (4)    Vacuum pump (6)
NOVELTY - The furnace has a gasification furnace wall made of a steel plate. The steel plate is sealed to form a cavity that is filled with water. An upper end of a furnace body is provided with a smoke exhaust and a filling orifice. The smoke exhaust is provided with a turnover heat insulating plate. The smoke exhaust is internally provided with a smoke insulating plate. An oven head is arranged above the filling orifice. The oven head is connected with a reaction chamber through a channel. A control valve is arranged on the channel.    USE - Biomass gasification furnace for use in a rural area.    ADVANTAGE - The furnace is simple in structure and inexpensive. The furnace enables direct-fired combustion, thus improving gasification efficiency of the furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass gasification furnace in partial section.
NOVELTY - The system has a post-processing equipment that produces organic material compost. A food waste reservoir (110) stores the food waste. A sample reduction reservoir (120) performs sample reduction with respect to the food waste. A conveyor (190) conveys the food waste to a fermentation unit (310). The fermentation unit ferments the food waste, to remove the bad odor of food waste.    USE - Non-wastewater and non-odor organic material composting installation system.    ADVANTAGE - The installation cost of non-wastewater and non-odor organic material composting installation system can be reduced. The wastage of water resource can be prevented. The generation of bad odor can be prevented. The salinity of water can be reduced. The fermentation of food waste can be performed efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the non-wastewater and non-odor organic material composting installation system. (Drawing includes non-English language text)    Food waste reservoir (110)    Sample reduction reservoir (120)    Water control agent reservoir (130)    Conveyor (190)    Fermentation unit (310)
NOVELTY - A watercourse purification system for processing rural domestic sewage, where water flow rate in the watercourse is 1 m/s, uses a discarded watercourse or bottomland similar to the watercourse to structure a processing unit. According to the direction of the water flow, a plant grid sedimentation unit, an artificial biomimetic material contact oxidation unit, a vertical flow artificial wet land unit and a floating plant unit are sequentially disposed from upstream to downstream.    USE - A watercourse purification system for processing rural domestic sewage.    ADVANTAGE - Removal rates of the chemical oxygen demand (CODcr), suspended solids (SS), ammonia-nitrogen (NH3-N), total nitrogen (TN) and total phosphorus (TP) in the domestic sewage entering the system are respectively 77.1%, 84.1%, 70%, 68% and 58.8%. The system reduces pollution load and improves the water quality, which can guarantee the improvement of water environmental quality of downstream river.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for watercourse purification processing method comprising    (A) planting good-sized aquatic plant in the watercourse to form the plant grid sedimentation unit, so as to block floater with large size and sand in the domestic sewage or surface runoff, then settle part of suspended matter;    (B) using high-performance contact filter material, i.e. biomimetic material biological rope, fixing to the watercourse to form the contact oxidation unit, decomposing the organic matter in the sewage and removing the nitrogen in the sewage;    (C) building the vertical flow artificial wet land unit, treating the nitrogenous and phosphorus pollutional material in the sewage; and    (D) using floating plant to further process the sewage.    DESCRIPTION OF DRAWING(S) - The drawing is a block diagram illustrating the watercourse purification system (Drawing includes non-English language text).
NOVELTY - A sewage reinjection processing method of low-permeability/special low permeability oil reservoirs, comprises making the processing water pass through aerobic microorganism integrated bacteria to degrade organic pollutant, separating films and refine filtering. The aerobic microorganism integrated bacteria which remove oil are Zoogloea sp, Bacillus cereus, and Pseudomonas alcaligenes, and those which degrade organic contaminant are Brachybacterium collins, Bacillus licheniformis, Bacillus subtilis, and Pseudomonas sp.    USE - A sewage reinjection processing method of low-permeability/special low permeability oil reservoirs    ADVANTAGE - The method greatly improves the fore-processing effect. Separating the follow-up film can adopt normal and economic separation processing method, such as hollow fiber film, vacuum film, or gas stripping film or vibration film, or filtering by silicon soil. Compared with existing technology, the method has shorter processing time, less investments and lower processing costs.    DETAILED DESCRIPTION - A sewage reinjection processing method of low-permeability/special low permeability oil reservoirs, comprises making the processing water pass through aerobic microorganism integrated bacteria to degrade organic pollutant, separating films and refine filtering. The aerobic microorganism integrated bacteria which remove oil are Zoogloea sp, Bacillus cereus, and Pseudomonas alcaligenes, and those which degrade organic contaminant are Brachybacterium collins, Bacillus licheniformis, Bacillus subtilis, and Pseudomonas sp. These bacteria are separately loaded in suspension fillings with 65-85 (preferably 75-85) V/V% filling density in an aeration pool and/or the suspension fillings, and organic aeration filtering pool fillings. The separation film is a fiber film with a bore diameter meeting the filtering requirement or vacuum film or gas stripping film or vibration film. Delicate filter is filter by silicon soil.
NOVELTY - The present invention relates to a vertical type twin tank processor for organic waste and kitchen waste, mainly comprising a first fermentation tank that receives the introduced from a blender and a second fermentation tank that receives the introduced from a first fermentation tank, so that the organic waste and kitchen waste can be fed through the blender into the first fermentation tank for heating, oil filtering, dehydration, and fermentation, and then introduced into the second fermentation tank for ripening. A part of the fermentation products in the second fermentation tank is allowed to flow back into the first fermentation tank to increase the fermentation speed.
NOVELTY - The present invention is a soot extraction and biological treatment method, particularly referring to lead soot and exhaust gas to an extraction unit and wash with a detergent of non-ionic surfactant. By using the detergent to wash soot and exhaust gas and effectively emulsify soot and exhaust gas to produce wastewater containing emulsified oil, the emulsified oil in the wastewater is next degraded into carbon dioxide and water solution using oil splitting bacteria. The degraded water solution is then directed to the extraction unit and mixed with detergent for continuously washing soot and exhaust gas. As such, it forms a repeated circulatory system, making oil degradation rate over 99%.
NOVELTY - The method involves providing water storage tank storing organic waste and measuring the ammonium concentration of the organic waste by measuring sensor. The fermentation process is performed using methane gas which is supplied with respect to organic waste and processing water supplied from water feeding unit. The digestive fluid generated after fermentation process is filtered and is stored in gas holder. The concentration of ammonia is maintained at fixed range during the fermentation process.    USE - Organic waste processing method.    ADVANTAGE - The pH concentration can be adjusted to the specified range during fermentation process. The denitrification effect at the anoxic chamber is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating the method of organic waste processing. (Drawing includes non-English language text)
NOVELTY - The present invention is related to a method of producing bioenergy by laccase, which mainly adds laccase to generate a biological reaction during the process of manufacturing biofuels from oils of plant or animal origin, and through sedimentation separation in a separation tank and performs a post processing procedure so as to produce biofuels.
NOVELTY - Processing waste frying fats and oils by transesterification, where the process does not supersede food production, as primary agricultural activity by energy production, is disclosed.    USE - The process is useful for producing engine fuel by transesterification of waste frying fats and oils.
NOVELTY - Plant straw material is recycled by crushing plant straws and putting the crushed straws in pig raising beds as padding; adding effective microorganisms (EM) flora into the straws; regularly finding excrement of pigs in the straws; after three years, taking out straws and excrement of pigs in the raising beds and uniformly stirring, adding nitrogen, phosphate and potash fertilizer, and filling the product in cultivation beds for planting fruits or vegetables; and after another three years, taking out the padding in cultivation beds and spreading it on saline-alkali soil to plant grain crops.    USE - Method for recycling plant straw material useful for saline-alkali soil close to agricultural area (claimed).    DETAILED DESCRIPTION - Recycle of plant straw material comprises:    (A) crushing plant straws and then putting the crushed straws in pig raising beds as padding;    (B) adding EM flora into the straws and uniformly stirring;    (C) regularly finding excrement of pigs in the straws;    (D) after three years, taking out the straws and excrement of pigs in the raising beds and uniformly stirring, adding nitrogen, phosphate and potash fertilizer, and then filling the product in cultivation beds for planting fruits or vegetables; and    (E) after another three years, taking out the padding in the cultivation beds and spreading it on saline-alkali soil to plant grain crops.
NOVELTY - An anaerobic treatment device comprises a first reaction chamber, a second reaction chamber, and a gas-liquid separator, where the second reaction chamber is arranged on an upper part of the first reaction chamber.    USE - An anaerobic treatment device used for a high concentration wastewater (claimed).    ADVANTAGE - The cyclic flow when treating low concentration wastewater can be 2-3 folds of flooding velocity, and the cyclic flow when treating high concentration wastewater can be 10-20 folds of flooding velocity.    DETAILED DESCRIPTION - An anaerobic treatment device comprises a first reaction chamber, a second reaction chamber, and a gas-liquid separator, where the second reaction chamber is arranged on an upper part of the first reaction chamber. The two reaction chambers are in communication with each other. The top of the first reaction chamber and the second reaction chamber are provided with conical gas collecting hoods. The first reaction chamber is provided with a biogas raising pipe connected to the internal of the gas-liquid separator. The second reaction chamber is provided with a gas collecting pipe connected to the internal of the gas-liquid separator. A return pipe is lead out from the internal of the gas-liquid separator to the internal of the first reaction chamber.
NOVELTY - Method for increasing productivity of methane, involves producing acetic acid by synthesizing gas using biomass or combustible material, and fermenting the mixture using acetic acid producing bacteria.    USE - The method is useful for increasing productivity of methane.    ADVANTAGE - The method reduced wastage and saves energy.
NOVELTY - Ultra-fine fiber three-dimensional artificial waterweeds comprise a central rope grass stem leaf, floating grass head, and an anchoring root. The central rope grass stem is fixedly inserted with synthetic leaves. An upper part of the central rope grass is connected to the floating grass head. A lower part of the central rope grass stem is connected to the anchoring root. The synthetic leaves are ultra-fine fiber yarn strips.    USE - Ultra-fine fiber three-dimensional artificial waterweeds used as microorganism filler (claimed) for a sewage treatment device, and for a polluted river, lake, and pond water.    ADVANTAGE - The filler has enormous microorganism adhesion superficial area, and achieves improved water purifying.
NOVELTY - Strengthened ecological wetland treatment facility comprises precipitation tank, vertical flow and horizontal flow combined filter bed, sludge drying bed and secondary ecological wetland. A sewage outlet of the precipitation tank is connected to the vertical flow and the horizontal flow combined filter bed. The water outlet of vertical flow and horizontal flow combined filter bed is in communication with the secondary ecological wetland.    USE - Strengthened ecological wetland facility for treating sewage, particularly rural domestic wastewater, city landscape water and river polluted water.    ADVANTAGE - The facility effectively treats the polluted water and reduces the cost for treating sludge.    DETAILED DESCRIPTION - A strengthened ecological wetland treatment facility comprises a precipitation tank, a vertical flow and a horizontal flow combined filter bed, a sludge drying bed and a secondary ecological wetland. A sewage outlet of the precipitation tank is connected to the vertical flow and the horizontal flow combined filter bed. The water outlet of vertical flow and horizontal flow combined filter bed is in communication with the secondary ecological wetland. The secondary ecological wetland discharges natural water. The sludge discharging port of the precipitation tank is in communication with the sludge drying bed and the filtrate of sludge drying bed is connected to the precipitation tank.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of the strengthened ecological wetland treatment facility for treating sewage.
NOVELTY - Preparing anthraquinone from Damnacanthus, comprises crushing the medicinal herb, using alkaline solution to slightly wet the material, placing in a percolator, percolating and extracting, adding an anion exchange resin, stirring, filtering, concentrating the filtrate until it has a constant weight, washing the crude extract with water, adding the extract into a reaction kettle and carrying out supercritical extraction, separating to obtain anthraquinone, allowing the extract to pass through a medicinal active carbon column, collecting a decolorized liquid, concentrating and drying.    USE - The method is useful for preparing anthraquinone from Damnacanthus.    ADVANTAGE - The method: produces a high content of anthraquinone (more than 90%) with high efficiency and good quality; and utilizes all the solvents which are non-toxic and safe; and is environmental-friendly.    DETAILED DESCRIPTION - Preparing anthraquinone from Damnacanthus, comprises: (i) crushing the medicinal herb to 20-60 mesh, using alkaline solution to slightly wet the material, placing the materials in a percolator, percolating and extracting using an alkaline solution; (ii) adding an anion exchange resin to the extract, stirring for half an hour, filtering, concentrating the filtrate at low temperature until it has a constant weight, washing the crude extract with water for several times; (iii) adding the above extract into a reaction kettle and carrying out supercritical extraction under a pressure of 12-36 MPa at 32.5-58 degrees C, separating under a pressure of 4-7 MPa at 45-58 degrees C to obtain anthraquinone; (iv) allowing the extract to pass through a medicinal active carbon column and collecting a decolorized liquid; and (v) concentrating and drying the decolorized liquid.
NOVELTY - A composite additive comprises (pts.wt.) benzene (2-3.5), acetone (2-3.5), ferrocene (0.5-2), solvent oil (20-40), silicone oil (0.5-1.5), triethanolamine (0.5-1.5), trihydroxypropane (1-2), dimethyl carbonate (0.5-1) and/or methyl tert-butyl ether (2-7). The material are added into reactor, stirred for 10-15 minutes and filtered; and impurities are removed, and the product is pumped to finished product tank to obtain composite additive.    USE - A composite additive used for alcohol-ether composite gasoline for vehicle (claimed).    ADVANTAGE - The composite gasoline uses no gasoline and completely replaces gasoline, saves energy and protects environment, will not delaminate after 3 years of storage, and has good stability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an alcohol-ether composite gasoline for vehicle, comprising (wt.%) methanol (80-95) and composite additive (5-20), or alcohol-ether mixed solution (85-95) and composite additive (5-15). The materials are added into reactor and uniformly stirred; and impurities are removed to obtain alcohol-ether composite gasoline for vehicle. The methanol is not less than 95%.
NOVELTY - The device has multiple array-type pyroltic pipes (9) which are vertically inserted in the middle of a furnace chamber (4), and provided with a reaction section (2) and a balancing section (3). A smoke inlet (1) is provided in the lower portion of outer side of the chamber. A smoke outlet (7) is placed on the outer side of the chamber. A feeding system (6) is arranged below the chamber and communicated with the reaction section. A material store chamber (5) is communicated with the feeding system. A gas chamber (8) is arranged below the chamber and pyrolytic pipes.    USE - Array type fluidization fast pyrolytic reaction device.    ADVANTAGE - The production is easy and the whole reaction can be controlled easily. The reactors can be amplified easily and reliable at the same time. The distribution of the pyrolytic circulating gas in each pyrolytic pipe is uniform so as to reach a state of spraying fluidization. Energy consumption is low.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the array-type fluidization fast pyrolytic reaction device.    Smoke inlet (1)    Reaction section (2)    Balancing section (3)    Furnace chamber (4)    Material store chamber (5)    Feeding system (6)    Smoke outlet (7)    Gas chamber (8)    Array-type pyrolytic pipe (9)
NOVELTY - Method for producing of refuse derived fuel using microbial materials, mixing dehydrated sludge and food waste with microbial agent, fermentation the obtained mixture, degrading the fermented product using microorganisms, drying obtained product, fermenting the obtained mixture using solid fuel boiler, drying the product, crushing the dried product, and molding the crushed product to form solid fuel.    USE - The method is useful for producing of refuse derived fuel using microbial materials.    ADVANTAGE - The refuse derived fuel has excellent combustibility.    DETAILED DESCRIPTION - Method for producing of refuse derived fuel using microbial materials, mixing dehydrated sludge and food waste with microbial agent until the mixture reaches 50-60% of total water content, and total carbon nitrogen ratio of 30-50, fermentation the obtained mixture, degrading the fermented product using microorganisms, drying obtained product until the moisture content reaches 40%, fermenting the obtained mixture using solid fuel boiler, drying the product until the moisture content reaches 10% or less, crushing the dried product, and molding the crushed product to form solid fuel.
NOVELTY - A biofuel preparation device comprises a gas carrying system, a feeding system, a fluidized bed reactor, a cyclone separator, a hot vapor filter, a biofuel collecting system, sensing mechanisms, and a data collection controlling system. The feeding system is connected with the fluidized bed reactor. The cyclone separator, the hot vapor filter and the biofuel collecting system are connected in series by a pipe. The gas carrying system is connected with the fluidized bed reactor, the hot vapor filter and the feeding system.    USE - Biofuel preparation device.    ADVANTAGE - The device has simple structure, can continuously and steadily feed biomass, and is fast in cracking biomass to produce biofuel having improved quality.    DETAILED DESCRIPTION - A biofuel preparation device comprises a gas carrying system, a feeding system, a fluidized bed reactor, a cyclone separator, a hot vapor filter, a biofuel collecting system, sensing mechanisms, and a data collection controlling system. The feeding system is connected with the fluidized bed reactor. The cyclone separator, the hot vapor filter and the biofuel collecting system are connected in series by a pipe. The gas carrying system is connected with the fluidized bed reactor, the hot vapor filter and the feeding system. The sensing mechanisms are arranged on test points of the fluidized bed reactor, the cyclone separator and the hot vapor filter. The data collection controlling system is connected with the sensing mechanisms to collect temperatures and pressures of the test points. The gas carrying system is nitrogen source divided into three branches which are connected with bottom input end of fluidized bed reactor, upper input end of hot vapor filter, and feeding system.
NOVELTY - Soil modifier comprises (in parts): humic acid (5-10) and fermented and decayed excrement (90-95).    USE - The soil modifier is useful for modifying salinity and alkalinity of marine soil (claimed).    ADVANTAGE - The soil modifier can be obtained simply and cost-effectively. The soil modifier polymerizes soil salinity and prevents aggregation of salt on the surface layer and increases the soil cationic exchange property. The soil modifier improves organic matter and beneficial microorganisms of soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing the above-cited soil modifier, which involves mixing and agitating the fermented and decayed excrement with solid humic acid uniformly by disc agitator, conveying the agitated mixture to extrusion granulator by transmission belt and extruding and granulating the mixture to obtain the product.
NOVELTY - The desulfurizer has elementary sulfur settling region that is equipped with inverted tape sulfur discharge funnel (2) and sulfur discharge pipe (1). The aerobic methane biologic desulfuration section is equipped with tray air exposure device (5), dissolved oxygen probe (24), taper gas collector (18), annular air baffle inclined plate (8) and air guide pipe (20). The anaerobic methane biologic desulfuration section is equipped with tray air distributor (10), biological padding layer (12) and methane collection pipe (15).    USE - Aerobic/anaerobic integral methane security biologic desulfurizer.    ADVANTAGE - The security of methane biologic desulfuration is ensured and vulcanized hydrogen in methane can make purified methane reach standard. The methane is used for common action of aerobic/anaerobic desulfuration germ. The elementary sulfur is formed and recoverable portion processes the expense.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the aerobic/anaerobic integral methane security biologic desulfurizer.    Sulfur discharge pipe (1)    Inverted tape sulfur discharge funnel (2)    Tray air exposure device (5)    Annular air baffle inclined plate (8)    Tray air distributor (10)    Biological padding layer (12)    Methane collection pipe (15)    Taper gas collector (18)    Air guide pipe (20)    Dissolved oxygen probe (24)
NOVELTY - Method of producing fatty acid from domestic sewage, involves sterilizing wastewater by performing first-grade treatment, adding the wastewater to bioreactor, inoculating microalgae in the bioreactor, culturing microalgae using carbon dioxide as aeration air source, allowing the microalgae to grow up to logarithmic phase, controlling the pH of the effluent at 5-10 after the microalgae reaches logarithmic phase, collecting the microalgae from obtained effluent, and dehydrating the effluent to extract the fatty acid.    USE - The method is useful for producing fatty acid which is used in biodiesel.    ADVANTAGE - The method emits less carbon, and is cost-effective.
NOVELTY - Composite acid catalyst, acid oil and methanol are added into a closed reaction container. The excess methanol is distilled and recovered. Dilute sodium carbonate solution is added to neutralize the composite acid catalyst. Aqueous industrial salt solution is added, washed by water, kept stand to obtain upper layer of fatty acid methyl ester and lower layer of glycerol salt water. The glycerol salt water is discharged, flashed, fatty acid methyl ester is dewatered, entered into molecular rectifying tower to obtain biodeisel (refined fatty acid methyl ester).    USE - Manufacture of biodiesel.    ADVANTAGE - The method economically provides biodiesel having high conversion rate, by simple process with excellent operativity and reduced energy consumption.    DETAILED DESCRIPTION - Composite acid catalyst, acid oil and methanol are added into a closed reaction container at 65-75 degrees C for 2-6 hours. The excess methanol is distilled and recovered. Dilute sodium carbonate solution (2-10%) is added to neutralize the composite acid catalyst. Aqueous industrial salt solution (0.5) is added, washed by water for 2-3 times till being neutral, kept stand to obtain upper layer of fatty acid methyl ester and lower layer of glycerol salt water. The glycerol salt water is discharged, flashed, fatty acid methyl ester is dewatered, entered into molecular rectifying tower to obtain biodeisel (refined fatty acid methyl ester). The content of composite acid catalyst is 1-5% of oil weight. The content of methanol is 15-50% of oil weight. The composite acid catalyst comprises concentrated sulfuric acid, concentrated phosphoric acid and straight-chain alkyl benzene sulfonic acid in the mass ratio of 2-4:1:1.
NOVELTY - The electrolyzer has a permanent magnet (4) that is located at lower end of container case (8). The bottom portion of container case is provided with armature channel (9) with concave insulator (12). The electrodes (11) are located at two sides of lower end of inner portion of container case. The strong electrolyte aqueous solution (13) is on concave insulator. The gas chambers (14) are on strong electrolyte aqueous solution. The armature channel, electrodes, and strong electrolyte aqueous solution form a close circuit to electrolyze.    USE - Energy saving electrolyzer for hydrogen production.    ADVANTAGE - The energy saving electrolyzer exerts supers low voltage to electrolysis circuit with small length and large cross section to produce hydrogen, hence super-low voltage large-current electrolysis is achieved to produce hydrogen at reduced consumption of energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the energy saving electrolyzer.    Permanent magnet (4)    Container case (8)    Armature channel (9)    Electrodes (11)    Concave insulator (12)    Strong electrolyte aqueous solution (13)    Gas chambers (14)
NOVELTY - The device has anode and cathode chambers that are provided with inlet and wiring pillar respectively. The oxygen outlet and hydrogen outlet are mounted in oxygen and hydrogen separator respectively and lower ends are provided with electrolyte outlet. The ion exchange film is mounted between chambers. The anode outlet is connected with hydrogen separator through pipeline. The electrolyte outlet and other end of hydrogen separator are connected with circulating system and anode chamber inlet by pipeline.    USE - Device for preparing hydrogen and oxygen by circulating alkaline seawater electrolyte.    ADVANTAGE - The device electrolyte alkaline seawater to generate clean oxygen by anode chamber and to generate hydrogen by cathode chamber, so that poisonous chlorine in seawater can be prohibited and dialyzing of seawater can be performed effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing method of device for preparing hydrogen and oxygen by circulating alkaline seawater electrolyte.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of device preparing hydrogen and oxygen by circularity alkaline seawater electrolyte.
NOVELTY - The tank has separating cavity (9) whose inlet and outlet are respectively provided with circulating boost pump (1) and pressure regulating valve (3). The hydrogen cavity (5) is separated from separating cavity via selecting film (8) which allows hydrogen ion to pass through. The hydrogen cavity is provided with negative electrode (7) and filled with sulfuric acid. The positive electrode (4) is arranged in separating cavity and positioned opposite to negative electrode. A circulating pipeline (2) closing to regulating valve is provided with oxygen hole (10).    USE - Membrane electrode electrolytic tank.    ADVANTAGE - The membrane electrode electrolytic tank can effectively electrolyze and prepare hydrogen and oxygen. The electrolysis is carried out under very low electrolysis voltage. The safety of the tank is increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the membrane electrode electrolytic tank.    Circulating boost pump (1)    Circulating pipeline (2)    Pressure regulating valve (3)    Positive electrode (4)    Hydrogen cavity (5)    Negative electrode (7)    Selecting film (8)    Separating cavity (9)    Oxygen hole (10)
NOVELTY - The removal device comprises a medicine feeder, a reduction reactor and a residual chlorine remover, which are orderly connected via connection pipeline. A water distributor, a water discharger and an automatic venting valve are arranged on the residual chlorine remover. An active carbon and a solid catalyst particle are arranged on the lower part of the residual chlorine remover. Water distributor is installed in the active carbon and the solid catalyst particle on the lower part of the residual chlorine remover via connection pipeline.    USE - Removal device of residual chlorine in sewage.    ADVANTAGE - Can be continuously operated and useful for return water procedure in oil field.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of the removal device of residual chlorine in sewage.
NOVELTY - Ecological integration of aerobic-undercurrent type wetland combined sewage processing system comprises a grate pool, a sediment adjusting pool, a lift pump, an embedded integrated aerobic processing system and an undercurrent type artificial wetland processing system, where the grate pool is connected with the sediment adjusting pool through pipeline. The sediment adjusting pool is further connected with the embedded integrated aerobic processing system through pipeline, and the sewage in the adjusting pool is pumped into the embedded integrated aerobic processing system by the lift pump.    USE - Used as an ecological integration of aerobic-undercurrent type wetland combined sewage processing system.    ADVANTAGE - The sewage processing system: has extended service life, low cost, simple operation process, easy management and less power consumption; avoids chemical usage; prevents secondary pollution and has good effect on removing nitrogen and phosphorus. The plants can be grown on artificial wetland and has better landscape.    DETAILED DESCRIPTION - Ecological integration of aerobic-undercurrent type wetland combined sewage processing system comprises a grate pool, a sediment adjusting pool, a lift pump, an embedded integrated aerobic processing system and an undercurrent type artificial wetland processing system, where the grate pool is connected with the sediment adjusting pool through pipeline. The sediment adjusting pool is further connected with the embedded integrated aerobic processing system through pipeline; the sewage in adjusting pool is pumped into the embedded integrated aerobic processing system by the lift pump, and the integrated aerobic processing system is connected with the undercurrent type artificial wetland processing system by pipeline.
NOVELTY - A raw material aromatic compound is reacted with oxidizing agent in presence of electron donor-receptor molecular assemblage in electron-transferred state, and oxidized to obtain oxidation reaction product of aromatic compound.    USE - Manufacture of oxidation reaction product e.g. bromobenzene used as pharmaceutical intermediate.    ADVANTAGE - The method economically provides oxidation reaction product of aromatic compound without polluting environment.
NOVELTY - Method for preparing biodiesel, involves pulverizing Salicornia herbacea, heating pulverized material, supplying carbon dioxide to the material, adding methanol, ethanol, ethylene glycol, propylene glycol, 1,3-butyl glycol, glycerol and vegetable oil to the mixture, passing the mixture through separator, extracting oil, mixing the oil with alcohol, adding oil mixture to mixture of sodium hydroxide, potassium hydroxide and base catalyst, esterifying the mixture, separating glycerol and alcohol from the mixture and washing ester compound.    USE - The method is useful for preparing biodiesel.    ADVANTAGE - The biodiesel is environmentally-friendly and cost-effective.    DETAILED DESCRIPTION - Method for preparing biodiesel, involves pulverizing Salicornia herbacea to 0.5-5 mm, steaming the pulverized material at 80-100 degrees C or 120-200 degrees C for 20-40 minutes, roasting the steamed material for 20-60 minutes, supplying carbon dioxide to the roasted material in the weight ratio of 1:50-100 at 30-80 degrees C under 20-30 MPa, adding methanol, ethanol, ethylene glycol, propylene glycol, 1,3-butyl glycol, glycerol and vegetable oil to the mixture, passing the mixture through separator at 10-50 degrees C under 10-20 MPa for 30-120 minutes, extracting oil by separating S.herbacea, bleaching the oil, mixing the oil with alcohol in the molar ratio of 1:3-10, adding oil mixture to mixture of sodium hydroxide, potassium hydroxide and base catalyst in the weight ratio of 1:0.005-0.01, stirring the mixture at 40-70 degrees C in 200-400 revolutions/minute, esterifying the stirred mixture, separating glycerol and alcohol from the mixture and washing ester compound.
NOVELTY - The device has an air separating tower (1) whose liquid oxygen outlet (E) is connected to a liquid oxygen inlet (e) of methane removing tower (2). A liquid nitrogen outlet (B) of air separating tower is connected to a liquid nitrogen inlet (b) of high purity oxygen tower (3). An oxygen outlet of heat exchanger (K702) is connected to an oxygen gas inlet of air separating tower. An oxygen flow inlet of the heat exchanger is connected to the high purity oxygen tower that is provided with high purity oxygen gas outlet.    USE - High purity oxygen extraction device.    DESCRIPTION OF DRAWING(S) - The drawing shows a circuit diagram of the high purity oxygen extraction device. (Drawing includes non-English language text)    Air separating tower (1)    Methane removing tower (2)    High purity oxygen tower (3)    Liquid nitrogen outlet (B)    Liquid oxygen outlet (E)    Heat exchanger (K702)    Liquid oxygen inlet (b)    Liquid oxygen inlet (e)
NOVELTY - The device has pressing load screws (51,52) which are vertically arranged in the pressing cabin (3). The pressing lead screws are horizontally provided with supporting platforms which are capable of lifting on the pressing lead screws. A control cabin (10) controls supporting platforms to lift and descend on reverse direction. The supporting platforms are horizontally provided with pressing claw which is synchronously stretched out of the supporting platforms or synchronously folded in the supporting platforms.    USE - Biomass gasifier pressing device.    ADVANTAGE - The pressing device has good continuous working performance, stable feeding of combustion chamber, and good biomass gasifying effect and good stability in producing and supplying gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass gasifier pressing device.    Gasifier (1)    Opening (2)    Pressing cabin (3)    Control cabin (10)    Pressing load screws (51,52)
NOVELTY - The mixer has main tube (1) whose inner diameter is 300 mm. The secondary tube (2) is vertically inserted into main tube from right half round of cross section of the main tube. The inner diameter of secondary tube is 50 mm. The eight blades (3) are mounted in main tube. The inclination angle of blade is denoted as alpha of 16-20 degrees , and rotation angle is denoted as beta of 16-20 degrees . The wall thickness of main tube and secondary tube is 5-10 mm. The width of wedge-shaped outlet is 5-10 mm.    USE - Static mixer used in Claus technique for purifying natural gas and recycling sulfur.    ADVANTAGE - The static mixer can prolong residence time of gas in the mixer and can improve turbulent flow intensity of gas, so as to improve mixing rate of mixed gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the static mixer.    Main tube (1)    Secondary tube (2)    Blade (3)
NOVELTY - Funnel-shaped biogas tank and mechanical manuring are claimed.    USE - The tanks is useful for generating: biogas by fermenting organic rubbish in the tank for generating power, bio-liquid for culturing Chlorella pyrenoidosa and residual remains for mechanical manuring.    ADVANTAGE - The residual remains replace the traditional fertilizer, and are applied mechanically while spreading the fertilizer, which improves working efficiency and improves air quality, and fully uses organic rubbish, which makes a great contribution to the agriculture.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the funnel-shaped biogas tank.
NOVELTY - The tank has anaerobic bacteria that multiplies rapidly under great pressure and high temperature, so that fermenting cycle is short and gas is abundant. Switch is automatically opened to let gas automatically flow into methane liquid-methane residual separation room under great pressure after fermenting and gas generation. High pressure is given on the separated methane residual for dewatering and adding multiple kinds of trace element such as nitrogen, phosphorus and potassium.    USE - Urban large-scale booster methane gas fermenting tank used in organic fertilizer production line.    ADVANTAGE - The high pressure is given on the separated methane residual for dewatering and adding multiple kinds of trace element such as nitrogen, phosphorus and potassium for manufacturing high efficiency organic fertilizer by a fully automated processing line.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view illustrating the process of manufacturing high efficiency organic fertilizer. (Drawing includes non-English language text)
NOVELTY - The electrolytic bath cell has porous carrier that includes micropore for providing the flow path of reactant of electrolysis. An electrolyte is provided between the carrier for separating the hydrogen and oxygen. An electrode is formed in partial layer of carrier. An inter-connector is provided for connecting the unit cells consisting of carrier, electrolyte and electrode.    USE - Electrolytic bath cell for high temperature water electrolysis, for use in industrial chemical production field.    ADVANTAGE - The overvoltage of cathode and anode is reduced and the polarization loss can be reduced by increasing the electric current density. The hydrogen and oxygen production efficiency can be raised. The chronic problem of high temperature electrolytic bath can be eliminated by fluid passage of micropore of porous carrier. The electrolysis efficiency and capacity of water electrolysis can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for electrolytic bath stack manufacturing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the electrolytic bath cell. (Drawing includes non-English language text)
NOVELTY - Electrode structure comprises several electrodes arranged on flat electrode plate and the electrodes are separated with each other by component having insulating property. The electrode plate has several electrodes arranged on its surface. The electrodes are connected using component having insulating property. The component is inserted into holes present in the flat electrode plate. The anode of the electrode plate is platinum or titanium.    USE - The electrode structure is useful for electrolysis of water.    ADVANTAGE - The hydrogen blister and generated oxygen bubble can be easily separated from the electrode plate. The electrode plate reduces loss of power and heat generation, and can be used for long period of time.
NOVELTY - The barge-mounted fuel cell generating plant (1) has multiple assembling blocks (11), in which air chamber (13) is formed in the inner side. The assembling blocks are made of steel material. A gasifier is equipped for gasifying coal to produce synthetic gas. A carbon dioxide collecting unit is equipped for collecting the carbon dioxide incidentally generated in the gasifying process at the rear end of a separator.    USE - Barge-mounted fuel cell generating plant.    ADVANTAGE - The gasifier is equipped for gasifying coal to produce synthetic gas, where a carbon dioxide collecting unit is equipped for collecting the carbon dioxide incidentally generated in the gasifying process at the rear end of a separator, and hence ensures minimizing environmental contamination in a cost-effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for installing a barge-mounted fuel cell generating plant.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a barge-mounted fuel cell generating plant.    Barge-mounted fuel cell generating plant (1)    Barge (10)    Assembling blocks (11)    Air chamber (13)    Fuel cell generation system (20)
NOVELTY - The system has a feed port of a combustible extracting device that can be used for introducing the waste into a domestic refuse processing plant. The discharged material from a discharge port of the combustible extracting device is conveyed to a feed port of the crushing device. The crushed material from the discharging port of the crushing device is conveyed to a feed port of the extruding and molding device. A discharging port of the extruding and molding device is served as an outlet for the finished product of the refuse derived fuel.    USE - System for producing refuse derived fuel.    ADVANTAGE - The discharging port of extruding and molding device that is served as outlet for finished product of refuse derived fuel. Hence the problem of extracting combustible from the current domestic refuse processing plant for preparing refuse derived fuel and selecting the device and technique is solved. The raw material of the refuse derived fuel can be extracted from the domestic refuse waste. The refuse derived fuel with good purity and high heat value can be prepared. The economic and social benefits are good.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing refuse derived fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the system for producing refuse derived fuel.
NOVELTY - A (2E)-1-(4-(2-oxo-2-(piperidin-1-yl)ethyl)piperazin-1-yl)-3-phenylprop-2-en-1-one, or its salt is new.    USE - New (2E)-1-(4-(2-oxo-2-(piperidin-1-yl)ethyl)piperazin-1-yl)-3-phenylprop-2-en-1-one is useful in medicine for treating cardiovascular and cerebrovascular diseases (claimed).    ADVANTAGE - The (2E)-1-(4-(2-oxo-2-(piperidin-1-yl)ethyl)piperazin-1-yl)-3-phenylprop-2-en-1-one is environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of (2E)-1-(4-(2-oxo-2-(piperidin-1-yl)ethyl)piperazin-1-yl)-3-phenylprop-2-en-1-one. A cinnamic acid is mixed with methylene dichloride, and dimethyl formamide is added to obtain reaction mixture. The obtained reaction mixture is dipped in thionyl chloride and methylene dichloride under ice bathing, reacted at room temperature and distilled methylene dichloride at normal pressure to obtain cinnamoyl chloride. A piperazine is added into methylene dichloride, dipped in cinnamoyl chloride under ice bathing, reacted at room temperature, extracted, washed organic layer using water, dried and depressurized to obtain oil cinnamoyl piperazine. A piperidine is mixed with toluene, and chloroacetic chloride and toluene is added, reacted at room temperature, filtered, concentrated and dried to obtain light yellow 2-chlorine-N- piperidine acetamide. A 2-chloro-N-piperidinacetamide and methylene dichloride are mixed at 5-10 degrees C, and triethylamine, bucinnazine and methylene dichloride are added, reacted at room temperature, extracted, separated and washed to obtain white crystal of 1-(cinnamoyl)-4-(piperidine acetyl) piperazidine. The obtained crystal is melted at 116-118 degrees C. A 1-(cinnamoyl)-4-(piperidine acetyl) is dissolved in piperazidine, and 1-(cinnamoyl)-4-(piperidine acetyl)piperazidine is added, extracted and filtered to obtain white 1-(cinnamoyl)-4-(piperidine acetyl)piperazidine maleate.
NOVELTY - A synthesized methane catalyst (in %mass) contains aluminum oxide (0-70), zirconium oxide (5-85), nickel oxide (12-30), lanthanum oxide (0.5-10), cerium oxide (0.1-5), calcium oxide (0-3) and barium oxide (0-1).    USE - Synthesized methane catalyst.    ADVANTAGE - The synthesized methane catalyst has excellent thermal stability, catalytic activity and selectivity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation for catalyst, which involves mixing aluminum source, zirconium source, nickel salt, lanthanum salt, cerium salt, calcium salt and barium salt, neutralizing and precipitating with sodium salt.
NOVELTY - The equipment has circulating tank that is formed by connection of several cylinders for circulating the wastewater. An intake and discharge unit performs the collection and exhaustion of gas by metabolism of microorganism. An impeller circulates the wastewater in cylinders. The air is supplied to wastewater through venture-pipe or diffuser.    USE - Aerobic treatment equipment for livestock excretion, domestic wastewater, and industrial wastewater (all claimed).    ADVANTAGE - The reduction of air in wastewater can be prevented so that aerobic pressurizing amount can be reduced. Hence highly efficient aerobic treatment of wastewater can be ensured.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the aerobic treatment equipment. (Drawing includes non-English language text)
NOVELTY - A domestic waste is crushed with primary crest crusher, and domestic waste combustible material is separated. The reclaimed waste is then crushed independently with secondary crest crusher, and reclaimed waste combustible material is separated. The separated combustible materials are stored in mixing reservoir. The mixture and reclaimed waste combustible material controlled with product life cycle measure are mixed with calcium hydroxide, and mixed solid fuel is produced from domestic waste and landfilled waste.    USE - Manufacture of mixed solid fuel.    ADVANTAGE - The mixed solid fuel having high quality and calorific value is economically manufactured.
NOVELTY - The generator has input portion (163) in inner side of process bath (100). The high rating board (157) and fixed partition wall (155) having constant height, are connected to upper and lower sides of process bath respectively. A slope portion (110) at lower surface of process bath, is gradually inclined downwards. A liquid fertilizer vent (109) is provided at upper portion of liquid fertilizer storage area (210). A gas generation space (160) is separated from material input space (120) in a state of controlling input portion through variable partition wall (161).    USE - Methane gas generator for generating methane gas from food waste, human or animal waste.    ADVANTAGE - The organic waste can be completely decomposed and methane gas can be collected and used as an energy source. The methane gas processing efficiency can be enhanced.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of the waste disposal unit.    Process bath (100)    Liquid fertilizer vent (109)    Slope portion (110)    Material input space (120)    Fixed partition wall (155)    High rating board (157)    Gas generation space (160)    Variable partition wall (161)    Input portion (163)    Liquid fertilizer storage area (210)
NOVELTY - Fuel composition contains organic binder and coal filler. The organic binder used is a fermentation residue formed during anaerobic fermentation of organic animal wastes, with the following ratio of components in wt %: fermentation residue 10-90, crushed coal filler - the rest.    USE - Chemistry.    ADVANTAGE - Improved technology of preparing the composition for producing moulded solid fuel, high environmental friendliness of the process and low financial expenses. 1 ex
NOVELTY - A microbial fuel cell comprises anode tank (9) which is separated by diaphragm (1) which is ion-permeable separation film and has electrolytic solution which suspends microorganisms (2) which can disperse oil component, electron transport substance and oil component and can be decomposed in anode electrode (6) and liquid, and cathode tank (10) which consists of electrolytic solution in which cathode electrode and catalyst are dissolved.    USE - Microbial fuel cell for moving body engine e.g. motor vehicle, truck and motorcycle.    ADVANTAGE - The microbial fuel cell can use oil as fuel and can produce electric power.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the oil utilization type microbial fuel cell.    Diaphragm (1)    Microorganisms (2)    Anode electrode (6)    Anode tank (9)    Cathode tank (10)
NOVELTY - A hydrogen production apparatus comprises catalyst which carries out steam reforming of raw material containing hydrocarbon, modification part which produces reformed gas containing hydrogen and carbon monoxide, and hydrogen sulfide removal part which removes hydrogen sulfide.    USE - A hydrogen production apparatus used for fuel cell system (claimed).    ADVANTAGE - The apparatus has low maintenance frequency, and operates stably over a long period of time.    DETAILED DESCRIPTION - A hydrogen production apparatus comprises catalyst which carries out steam reforming of raw material containing hydrocarbon, modification part which produces reformed gas containing hydrogen and carbon monoxide, and hydrogen sulfide removal part which removes hydrogen sulfide. The catalyst for steam reforming comprises rhodium, platinum and/or palladium which is supported in alumina containing support in ratio of 0.3-5 mass% with respect to 100 mass% of alumina containing support. The alumina containing support comprises 2-25 mass% of rare-earth elements oxide and 0.1-15 mass% of alkaline-earth elements oxide supported with respect to 100 mass% of alpha -alumina with pore volume of 0.2-1.0 ml/g and hole diameter of greater than or equal to 50 nm.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of fuel cell system comprising hydrogen production apparatus. (Drawing includes non-English language text).    Fuel cell system (1)    Hydrogen production apparatus (10)    Modification part (11)    Hydrogen-sulfide removal parts (12, 14)    Fuel cell part (20)
NOVELTY - The method for the emission-free transformation of solar energy into electrical energy, comprises generating power in a closed cycle process and closing all material circulation. The exhaust heat of the power generation remains in the circulation process thus enabling the optimization of the growth conditions of microorganisms in bioreactor and is present in harvest unit for the treatment of biomass for the disposal. A system of centrifugal- and jet pumps is used in the mixing unit.    USE - Method useful for the emission-free transformation of solar energy into electrical energy.    ADVANTAGE - The method ensures effective, economical and emission-free transformation of solar energy into electrical energy.    DETAILED DESCRIPTION - The method for the emission-free transformation of solar energy into electrical energy, comprises generating power in a closed cycle process and closing all material circulation. The exhaust heat of the power generation remains in the circulation process thus enabling the optimization of the growth conditions of microorganisms in bioreactor and is present in harvest unit for the treatment of biomass for the disposal. A system of centrifugal- and jet pumps is used in the mixing unit, and a closed flat channel-bioreactor is used in such a way that transparent multilayer film tubes are construed in a flat channel system that flows into the harvest channel, and in which the microorganisms are supplied and moved by mixing nozzles.    DESCRIPTION OF DRAWING(S) - The figure shows a block diagram of a method for the emission-free transformation of solar energy into electrical energy (Drawing includes non-English language text).
NOVELTY - The system has individual low-boiling-point heater (19), and water boiler (29) are arranged in each focusing point of sunlight reflected by concave reflecting mirrors (17), and linked to turbine generator, respectively. The heater heats different media directly or indirectly to produce different steams so as to push the turbine generator to generate the power. A water electrolyzer (41) is linked to turbine generator, to electrolyze the water so as to prepare hydrogen and oxygen.    USE - Multifunctional solar energy power generation hydrogen production system installed in residence and plant.    ADVANTAGE - High power generation, low cost and flexible installation of hydrogen production system can be ensured.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the multifunctional solar energy power generation hydrogen production system.    Rotating plate (10)    Concave reflecting mirror (17)    Low-boiling-point heater (19)    Water boiler (29)    Water electrolyzer (41)
NOVELTY - Producing ethane gas comprises: (a) obtaining Y-grade liquids from the field; (b) adding pressure to the liquids; (c) adding heat to the liquids; (d) passing the heated liquid through a de-ethanizer tower; (e) extracting the ethane gas; and (f) adding pressure to the ethane gas.    USE - The method is useful for producing and utilizing ethane gas (all claimed), and in landfill industry.    ADVANTAGE - The method is simple and eco-friendly, and provides ethane in an economical manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) utilizing ethane gas comprising: step (a) as above per se, separating the ethane gas from the Y-grade liquids, maintaining the pressure of the ethane gas at 200-215 pounds per square inch, and sending the ethane gas to a landfill site flare to incinerate landfill waste;    (2) an apparatus for producing ethane gas comprising a means for obtaining ethane and other natural gasses from ground wells, a means for separating ethane from the other the natural gasses, and a means for burning landfill materials with the ethane; and    (3) an apparatus for producing and utilizing ethane gas comprising a means for obtaining ethane and other natural gasses from ground wells, a means for separating ethane from the other the natural gasses, a means for mixing the ethane with methane to obtain an acceptable British thermal unit (BTU), and a means for selling the mixture to customers.
NOVELTY - The apparatus (100) has oxide nano wires (130) that are formed between two conductive plates (110,120) to decompose the water. The nano wires are electrically connected to the two conductive plates. The nano wires are converted from a stoichiometric state into non-stoichiometric state by the current supplied through the conductive plates. The nano wires are converted from a non-stoichiometric state into stoichiometric state by reacting with water to generate hydrogen.    USE - Hydrogen-generation apparatus.    ADVANTAGE - The nano wires between conductive plates are converted from non-stoichiometric state into stoichiometric state by reacting with water to generate hydrogen such that hydrogen production efficiency is increased. The nano wire is more easily heated to diversify to non-stoichiometric state.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the hydrogen-generation apparatus.    Hydrogen-generation apparatus (100)    Conductive plates (110,120)    Nano wire (130)    Water supply unit (160)    Power supply device (190)
NOVELTY - A photoelectrode material consists of composition including silicon oxide (27) as main component.    USE - Photoelectrode material is used for photoelectric cell (claimed).    ADVANTAGE - The photoelectrode material is economical and has excellent stability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for photoelectric cell.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of photoelectric cell. (Drawing includes non-English language text)    Glass substrate (21,23)    Taking-out electrode (22,24)    N-type semiconductor layer (25)    Platinum film (26)    Silicon oxide (27)
NOVELTY - Method comprises: providing a mixture comprising fecal waste and a bacterium, where the bacterium is a type that produces 5-32C fatty acid in the presence of any microbes in the fecal waste; incubating the mixture to produce a fatty acid enriched mixture; removing water from the fatty acid enriched mixture to produce a dried mixture; and pyrolyzing the dried mixture in an inert atmosphere to produce an alkane from the 5-32C fatty acid.    USE - The method is useful for producing alkane (claimed), which is useful as a fuel.    ADVANTAGE - The method provides alkane with lower carbon emissions and minimal energy input in an economical manner.
NOVELTY - Method for fermenting methane from organic waste, involves subjecting organic waste to ultra high solubilization process using protease producing microbe to obtain methane.    USE - The method is useful for fermenting methane.    ADVANTAGE - The fermented methane has high proteolytic ability.
NOVELTY - Inflammable waste material e.g. wood chips, waste thread, rice bran, fallen leaves, rubber and plastic material, starch resources, and aqueous adhesive are mixed with waste oil at 80 plus minus 10 degrees C, and added to a formwork. The mixture is roasted, cooled and dried to obtain activated carbon and fuel.    USE - Manufacture of activated carbon and fuel.    ADVANTAGE - The method safely and economically provides activated carbon and fuel by simple method without affecting the environment.
NOVELTY - A medium-heat biomass fuel gas preparation device, comprises a furnace body (20), a feeding device, a high-temperature smoke gas inlet (23), a discharging device (13), and a dry distillation gas outlet (26); where the furnace body (20) is inclined towards one side of the discharging end from one side of the charging end; and the outer side wall of the furnace body (20) is equipped with a drive mechanism for the furnace body (20).    USE - The medium-heat biomass fuel gas preparation device is useful for straw and wood crushed materials comprising cotton firewood, corn straw, and wheat straw.    ADVANTAGE - The medium-heat biomass fuel gas preparation device can achieve direct dry distillation and gasification under high pressure and high temperature of 700-1000 degrees C. Moreover, it has thermal efficiency of more than 85%. Additionally, it is simple in operation, convenient in maintenance, stable in operation, and low in noise.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the medium-heat biomass fuel gas preparation device.    Discharging device (13)    Furnace body (20)    Gear ring (21)    High-temperature smoke gas inlet (23)    Dry distillation gas outlet (26)
NOVELTY - Use of Aeropyrum pernix culture supernatant is claimed in degradation of prion protein and/or protein deposits, where the A.pernix culture supernatant comprises A.pernix serine protease or its active fragment, or protein having at least 80% homology with A.pernix serine protease, or its active fragment.    USE - The A.pernix culture supernatant is useful for degradation of prion protein and/or protein deposits in surgical equipment, textiles, food, waste, and solid material surface (all claimed). The surgical equipment is chosen from scissors, forceps, needles, needle holders, retractors, scalpels, lancets, endoscopes, towel clamps and drills.    ADVANTAGE - The method is environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of degrading prion protein and/or protein deposits, which involves incubating the prion protein and/or protein deposits with A.pernix culture supernatant.
NOVELTY - A dispersion comprises zinc oxide or titanium oxide (60 %mass or more), isoparaffin having a polymerization degree of 3-10, and a polyether-modified silicone having a hydrophilic-lipophilic balance value of 3-10 as a dispersing agent.    USE - Dispersion is used for cosmetics (claimed) e.g. sunscreen and foundation.    ADVANTAGE - The dispersion contains high pigment concentration of zinc oxide or titanium oxide, and does not contain volatile silicone, which prevents environmental pollution. The dispersion provides non-sticky cosmetics.
NOVELTY - A container type anaerobic reaction chamber comprises a reaction chamber (1), an insulating layer (2) and a biogas slurry refluxing system. Main body of the reaction chamber is a waste container. Upper top plate of the waste container is provided with a biogas outlet tube (3) and a waste gas discharging pipe (5). Two thermometers (4) are mounted on side surface of the waste container. End surface of the waste container is provided with a sealed chamber door (6).    USE - A container type anaerobic reaction chamber used for fermenting solid dung and sewage by dry method to produce biogas.    ADVANTAGE - The chamber has low consumption, high reliability, high biogas quality, high yield, and low production cost.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating the container type anaerobic reaction chamber.    Reaction chamber (1)    Insulating layer (2)    Biogas outlet tube (3)    Thermometers (4)    Waste gas discharging pipe (5)    Chamber door (6)
NOVELTY - The circulation system has a power generator connected to gas turbine for converting mechanical work of gas turbine to electric energy. An evaporator connected to liquid carbon dioxide booster pump and working substance mixer realizes refrigeration output while realizing heat absorption gasification of liquid carbon dioxide. The pump is connected with a carbcondenser for boosting low-pressure LNG from an LNG accepting station to a pressure of 7.35 megaPascal. An outer network cold supplier is connected to an LNG gasifier, using low temperature natural gas as a cold source for outer network.    USE - Regenerating Brayton-Rankine compound thermal circulation system using liquefied natural gas (LNG) cryogenic energy.    ADVANTAGE - The thermal performance of the thermal circulation system is greatly improved and can realize, at the same time, carbon dioxide zero emission by a pure oxygen combustion method. The thermal circulation system has good economical efficiency, environmental conservation and wide engineering application possibility.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow circuit diagram of the thermal circulation system. (Drawing includes non-English language text).
NOVELTY - An alloy metallic nanostructure is obtained by dipping supported metal precursor in glycerol solution.    USE - Alloy metallic nanostructure e.g. platinum-palladium/carbon nanostructure is used as catalyst for manufacturing electrode for fuel cell.    ADVANTAGE - The electrode manufactured using the alloy metallic nanostructure has high durability, strength and decomposability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of alloy metallic nanostructure.
NOVELTY - The method involves loading thermophilic bacteria agent containing multiple thermophilic bacteria on the padding. The dense oil sewage and the thermophilic bacteria loaded on padding are accommodated in the reaction unit. The treatment performed on dense oil sewage is finished, if dense oil sewage in the reaction unit reaches the drainage standard.    USE - Method for treating dense oil sewage using thermophilic bacteria such as Geobacillus stearothermophilus, Bacillus caldolyticus and thermophilic Bacillus (all claimed).    ADVANTAGE - The sewage treatment process can be simplified and the cost required for sewage treatment process can be reduced, by applying thermophilic bacteria to high temperature dense oil sewage.    DESCRIPTION OF DRAWING(S) - The drawing shows the flow diagram illustrating the method for treating dense oil sewage. (Drawing includes non-English language text)
NOVELTY - The reactor composting device has a fermentation system that is composed of the rectangular fermenting pool (3) and a tapered gas collection pool (8). The gas collection pool (8) is installed under the fermenting pool (3) and is connected with the fermenting pool. The gas processing system is composed of the sucking pump (5) and the ammonia absorbing tank (6). The bottom of the gas collection pool (8) is communicated with the sucking pump (5). The sucking pump (5) is communicated with the ammonia absorbing tank (6).    USE - Reactor composting device for aerobic fermentation.    ADVANTAGE - The temperature of the composting portion is kept for the aerobic composting. The composting process is little impacted by the external lower temperature so as to achieve the annual production. The reactor is good for sending out the foul smell in the process of collecting the compost and effectively collecting the ammonia produced in the process of composting.    DETAILED DESCRIPTION - The bottom of the fermenting pool (3) is equipped with a padding layer (7) and a stainless steel screen (4). The middle is equipped with the gas guiding pipe (1). The bottom of the gas guiding pipe (1) is fixed on the stainless steel screen (4) by passing through the padding material (7). A gas collection processing system is composed of the gas collection pool (8) and the gas processing system.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the reactor composting device.    Gas guiding pipe (1)    Rectangular fermenting pool (3)    Stainless steel screen (4)    Sucking pump (5)    Ammonia absorbing tank (6)    Padding material (7)    Tapered gas collection pool (8)
NOVELTY - Alcohol-type biological fuel oil comprises (in %mass) refined biological diesel oil (20-50), industrial methanol (40-80), and additive (5-30) comprising co-solvent (5-20), auxiliary surfactant (1-15), stabilizer (0.2-2) and corrosion inhibitor (0.1-1).    USE - Alcohol-type biological fuel oil.    ADVANTAGE - The alcohol-type biological fuel oil is safe, economical and environmentally-friendly, and can be manufactured by simple method with reduced consumption of energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of alcohol-type biological fuel oil. Co-solvent and auxiliary surfactant are added to the additive, agitated evenly, and industrial methanol or refined biological diesel oil is added to obtained solution. The resultant mixture is agitated, and stabilizer and corrosion inhibitor are added. The obtained mixture is agitated and dissolved to obtain alcohol-type biological fuel oil.
NOVELTY - Method for solving fermentation and suspension problems of straw in methane tank, involves (a) placing iron or rattan into basket capable of containing 10 kg dry weight of straw in each frame, and (b) filling pretreated straw into the frame, feeding 4-8 basket in each feeding pool, and depositing the basket to methane tank while the methane solution immerses 20-30 cm of the basket.    USE - The method is useful for solving fermentation and suspension problems of straw in methane tank.    ADVANTAGE - The method is convenient to perform and manage.
NOVELTY - Waste residue from iron reduction is added to waste acid obtained by phosgene cyclization. The added materials are mixed, reacted, and settled to obtain supernatant. Chlorine is introduced to the supernatant, or hydrogen peroxide is added for oxidization. The obtained reaction solution is condensed and the solvent is removed. Thus, recycling of waste acid and waste residue is carried out.    USE - Recycling method of waste acid and waste residue discharged during production of weedicide oxadiazon used for preparing ferric chloride.    ADVANTAGE - The method is environmentally-friendly, and economically provides ferric chloride with reduced consumption of energy.
NOVELTY - The machine has frame whose end is movably connected with one end of swing oil cylinder. The other end of swing oil cylinder is fixedly installed on cart traveling mechanism. The lower frame is rotated on cart traveling mechanism along supporting shaft under driving of swing oil cylinder. The hook chain-plate sludge turning-spreading mechanism and driving mechanism are installed in frame. The chain of hook chain-plate sludge turning-spreading mechanism is connected with driving end of driving mechanism to drive chain plate and hook on chain moving circularly.    USE - Sludge turning machine.    ADVANTAGE - The weight, energy consumption, manufacturing, operation and maintenance cost of the sludge turning machine are reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the sludge turning machine.
NOVELTY - The method involves providing displacement sensor (A), transmissive photo-electronic sensor (B), charged coupled device sensor (C) and reflection type photo-electronic sensor (D) for detecting defect of single cell (1) for fuel cell. The thickness of single cell is 100-2000 mu m and planar area of single cell is 10-1000cm2.    USE - Method for detecting defect in fuel cell material for manufacturing process of fuel cell (both claimed).    ADVANTAGE - The defect of single cell can be detected effectively by providing displacement sensor, transmissive and reflection type photo-electronic sensors and charged coupled device sensor for detection.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) fuel cell material; and    (2) manufacturing method for single cell for fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fuel cell material defect-detection system.    Single cell (1)    Displacement sensor (A)    Transmissive photo-electronic sensor (B)    Charged coupled device sensor (C)    Reflection type photo-electronic sensor (D)
NOVELTY - Production of transportation fuel involves providing a feedstock containing mineral oil, and lipid material (preferably triglycerides and/or fatty acid alkyl esters); and hydroprocessing the feedstock in a hydroprocessing zone which is maintained at conditions that promote conversion efficiency of the feedstock, preferably maintained at not greater than 1000 vppm carbon monoxide, based on total vapor content of the hydroprocessing zone.    USE - For production of transportation fuel (claimed), such as gasoline, kerosene, jet fuel, and diesel.    ADVANTAGE - The method produces fuel, particularly high quality transportation fuels, from biological material, e.g. lipid material. By increasing the amount of lipid or bio-material in feedstock that is converted to transportation fuel, particularly by hydroprocessing, the method limits undesirable side reactions that causes increase in heat of reaction and produce compounds which negatively impact catalyst efficiency.
NOVELTY - The furnace has a gasification furnace portion (71), a composite filter (74), an air exhauster (45), a coalescence filter (62), a generator set (66), a gas storage tank (53), an air exhauster (56) of the gas storage tank and a cooking stove (49).    USE - Thermal cracking furnace.    ADVANTAGE - The furnace has an energy conversation, environmental protection and stable performance. The furnace can be pressed into the biomass fuel without environmental pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the thermal cracking furnace.    Air exhauster (45)    Cooking stove (49)    Gas storage tank (53)    Air exhauster (56)    Coalescence filter (62)    Generator set (66)    Gasification furnace portion (71)    Composite filter (74)
NOVELTY - A palm-oil waste water treatment equipment (100) comprises aerator (2) which biologically treats by introducing palm-oil waste water after methane fermentation, coagulant supply unit (10) which supplies coagulant to biologically treated palm-oil waste water from aerator, and sludge flocculation process unit (4) which separates coagulant containing palm-oil waste water after coagulant supply into treated water and sludge flocculation.    USE - A palm-oil waste water treatment equipment.    ADVANTAGE - The equipment can fully reduce biological oxygen demand (BOD) component and suspended solid (SS) component.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of palm-oil waste water treatment equipment. (Drawing includes non-English language text).    Methane fermentation equipment (1)    Aerator (2)    Sludge flocculation process unit (4)    Coagulant supply unit (10)    Palm-oil waste water treatment equipment (100)
NOVELTY - The gasifier has a furnace bar (13) installed in a furnace (1), and an ash chamber (12) located under the furnace. Through holes (13a) are distributed on the furnace bar. A gap is existed between an edge of the furnace bar and an inner wall of the furnace to form an ash discharging hole (2). An ash-poking mechanism is installed on the furnace bar, and is connected with an ash-poking driving mechanism. The ash-poking driving mechanism is installed in a protection cover (5) under the furnace bar. An ash-poking rod (3) is installed on a rotation shaft (4) and located above the furnace bar.    USE - Multi-furnace bar biomass gasifier.    ADVANTAGE - The gasifier avoids a material or ash on the furnace bar from bridging, prevents a slag from bonding, thus improving working efficienc. The gasifier is convenient to lead a combustible gas from bottom of the furnace to strengthen gas production ability of the gasifier.    DESCRIPTION OF DRAWING(S) - The drawing shows a artial sectional view of a multi-furnace bar biomass gasifier.    Furnace (1)    Ash discharging hole (2)    Ash-poking rod (3)    Rotation shaft (4)    Protection cover (5)    Ash chamber (12)    Furnace bar (13)    Through holes (13a)
NOVELTY - The furnace has a furnace grid installed in a furnace body, and an ash chamber located beneath the furnace body, where middle of the furnace grid is a pore-free flat plate. Ash outlets are formed on an edge of the furnace grid connecting an inner wall of the furnace body, and an ash shifting mechanism for inputting ash from the furnace grid into an ash discharging mechanism is installed on the furnace grid. The ash shifting mechanism is connected with an ash driving mechanism, which is located in a protective cover beneath the furnace grid.    USE - Biomass gasifying furnace.    ADVANTAGE - The ash shifting mechanism is driven by the ash driving mechanism so as to make the ash on the furnace grid continuously discharged, so that the chemical reaction of biomass material operates smoothly to improve the working efficiency of the furnace. The pore-free flat plate in the middle of the furnace grid prevents the defect of existing furnace grid such as leakage. The protective cover in the ash chamber beneath the furnace grid can protect the ash driving mechanism.    DESCRIPTION OF DRAWING(S) - The drawing shows a side partial sectional view of a biomass gasifying furnace.
NOVELTY - The furnace has tubes (6, 16) connected on a generator (1), where the tube (16) is located below the tube. A valve (13) is arranged in a tube (10). A blower (7) is respectively connected with the generator and a filter tank (5) by tubes (17, 18). An exhaust tube (19) is connected on the tube (6). Another valve (14) is mounted in the exhaust tube. A water sleeve (11) is arranged in the generator, and is respectively provided with a water inlet (8) and a water outlet (9). An edge of a cover body is embedded with an asbestos ring (3).    USE - Gasification generating furnace for straws that is utilized in a family, canteen and a restaurant.    ADVANTAGE - The furnace greatly increases output quantity of combustible gases, and greatly decreases proportion of the mixture gases of a moisture and a carbon dioxide, so as to ensure that the combustible gases can be continuously delivered to a combustion device, greatly improve energy source utilization rate of the combustible gases, and decrease environmental pollution. The furnace overcomes problems that the furnace delivers too heavy gas moisture to the combustion device, can not preferably generate continuous combustible gases, and greatly waste energy sources.    DESCRIPTION OF DRAWING(S) - The drawing shows a side perspective view of a gasification generating furnace.    Generator (1)    Asbestos ring (3)    Filter tank (5)    Tubes (6, 10, 16, 17, 18)    Blower (7)    Water inlet (8)    Water outlet (9)    Water sleeve (11)    Valves (13, 14)    Exhaust tube (19)
NOVELTY - Producing biogas by dry fermentation, comprises aerating the fermenter with the biogas or the combustion product of the biogas.    USE - The biogas or the combustion product of the biogas is useful for aerating the fermenter during the production of biogas by dry fermentation (claimed).    ADVANTAGE - The method: does not affect the quality of the produced biogas and the efficiency of the biogas production; and produces the biogas with economically usable methane content even with low dry matter content.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biogas plant for producing the biogas by dry fermentation, comprising a device for recirculating the biogas from the fermenter or a biogas storage tank, into the fermenter, and/or a device for recirculating the biogas combustion product from a combustion motor into the fermenter.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the block diagram of control lines and line connections of individual components of the biogas plant comprising eight dry fermenters.    Pressure container (1)    Booster (4)    Butterfly valve (6)    Rubber compensator (9)    Pipe (12)
NOVELTY - Reacting chemical compounds by biotransformation, preferably whole cell biotransformation, comprises adding alginite as reaction additive to the reaction medium.    USE - The alginite is useful: as reaction additive in the biotransformation reaction, preferably whole cell biotransformation reaction; and for degrading environmental pollutants. The method is useful for: degrading environmental pollutants (all claimed), preferably chemical pollutants; and microbial production of chiral intermediates for pharmaceutical industry.    ADVANTAGE - The method: produces the product with enhanced diastereomeric and/or enantiomeric purity, preferably greater than or equal to 91%; exhibits high conversion rate, preferably greater than or equal to 98%; and completely degrades the chemical environmental pollutants.
NOVELTY - Producing 3-chloro-4,5-difluorbenzotrifluoride comprises reacting 3,4,5-trichlorobenzotrifluoride with at least one fluoride source in the presence of at least one catalyst and distillatively separating the obtained 3-chloro-4,5-difluorbenzotrifluoride from the reaction mixture.    USE - The process is useful for producing 3-chloro-4,5-difluorobenzotrifluoride, which is useful as an important intermediate for the production of biologically active substances for pharmaceutical and agricultural chemical applications.    ADVANTAGE - The improved process produces 3-chloro-4,5-difluorobenzotrifluoride in high yield, in an environmental and safe manner.
NOVELTY - The process involves passing a portion of an effluent originating through a hydroconversion reaction zone (6) with moving-bed and three-phase reactors (2) in presence of hydrogen. A catalyst bed of hydroconversion catalyst is contained in the reactor. The reactor is operated in an ebullating-bed mode and provided with ascending current of liquid and gas. The catalyst is withdrawn out of the reactor by using a withdrawing unit. A fresh catalyst is added to the reactor by using an adding unit to obtain a liquid feed with reduced content of Conradson carbon, metals, sulfur and nitrogen.    USE - Process for conversion of heavy hydrocarbon feed e.g. petroleum residue, and derivatives originating from biomass, coal, to upgradeable lighter products such as fuel.    ADVANTAGE - The moving-bed reactor is installed upstream of the three-phase reactors that are operated in an ebullating-bed mode so as to maximize the refining of the feed while increasing the conversion of the feed to upgradeable lighter products and improving properties and stability of the unconverted heavy residues.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of a process for conversion of heavy hydrocarbon feed to upgradeable lighter products.    Pipes (1, 3, 4)    Moving-bed and three-phase reactors (2)    Hydroconversion reaction zone (6)    Naphtha (15)    Vacuum distillate (17)
NOVELTY - The system has reformer (11) that produce reformed gas by reforming raw fuel using burner (15). A carbon monoxide transformer (12) has cylindrical shape portion and is integrally formed with reformer so that the reformer is positioned within the cylinder portion. The carbon monoxide transformer decreases carbon monoxide concentration in reformed gas that is produced by reformer.    USE - Fuel cell system.    ADVANTAGE - Since the temperature of transformer can be reduced by heating transformer with exhaust gas of burner, the need for heating transformer can be avoided, thus reducing size and cost of fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of fuel cell system. (Drawing includes non-English language text)    Reformer (11)    Transformer (12)    Burner (15)    Heat exchanger (19)    Reformed gas introducing unit (23)
NOVELTY - A hydrogen production apparatus (10) consists of a modification portion (11), a honeycomb structure installed in the modification portion, and a modification catalyst supported by the honeycomb structure. A raw material (AA) for hydrogen production containing a hydrocarbon is reformed using the modification catalyst.    USE - Hydrogen production apparatus is used for producing reformed gas containing hydrogen and carbon monoxide in fuel cell systems (claimed) e.g. domestic fuel cell systems.    ADVANTAGE - The hydrogen production apparatus enables manufacture of hydrogen with low energy consumption and pressure loss.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen production apparatus and fuel cell system. (Drawing includes non-English language text)    Fuel cell system (1)    Hydrogen production apparatus (10)    Modification portion (11)    Hydrogen-sulfide removal units (12,14)    Raw material (AA)
NOVELTY - The syngas production system has parallel reactors each defining internal passage, and compacting unit for compacting loose biomass material and introducing compacted biomass material into entrances of internal passages of reactors. A heater is configured to heat compacted biomass material within reactors to temperature at which organic molecules within compacted biomass material break down to form ash. The gas passages are formed within internal passages of reactors, and conduct carbon monoxide and hydrogen gases through reactors. A removing unit is configured to remove ash from reactors.    USE - Syngas production system using biomass materials.    ADVANTAGE - Eliminates the need for lock hopper system to mitigate the ingress of air into the reactor tubes or unwanted leakage of syngas from ash removal section by ensuring that the system operates within inlet and outlet pressures within certain limits. Minimizes heat loss to promote process efficiency and reduce hazard risks. Minimizes backflow of syngas through the tubes by promoting compaction of the biomass as it enters the tubes, as well as to allow creation of the interstices between the individual reactor tubes to accommodate heating elements.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a syngas production method.    DESCRIPTION OF DRAWING(S) - The drawing shows the perspective view of the syngas production system using biomass materials.    Tubes (12)    Interstices (18)    Deflector (20)    Throats (22)
NOVELTY - An alcoholysis process (M1) for producing dialkyl carbonates involves: either process (A): feeding reactants and a trace amount of soluble organometallic compound to a reactor comprising a solid alcoholysis catalyst, where the soluble organometallic compound and solid alcoholysis catalyst each comprise Group II to Group VI element; or process (B): feeding alcohol, and alcoholysis reactant comprising at least one of urea, organic carbamate, and cyclic carbonate to first reaction zone of solid alcoholysis catalyst; and feeding soluble organometallic compound to the first reaction zone.    USE - For producing dialkyl carbonates selected from diethyl carbonate or dimethyl carbonate (claimed), biodiesel, carboxylic esters or organic carbamates.    ADVANTAGE - The soluble organometallic compound is continuously fed to the reaction at very low levels to sustain the solid catalyst activity for an extended cycle length.
NOVELTY - The system (100) has a salt material (112) including sodium chloride, and a heating apparatus (116) which generates sufficient heat to melt the salt material. A hydrogen production subsystem (190) includes a left side production chamber (140) which receives and reacts aluminum and sodium hydroxide to form hydrogen and aluminum sodium hydroxide (AlNa(OH)4). A right side production chamber (144) receives and react aluminum and hydrochloric acid to form hydrogen and aluminum chloride (AlCl3). A hydrogen flow system delivers the hydrogen to a power generating apparatus.    USE - System for generating hydrogen on demand for use with fuel cell and power generating apparatus of transportation vehicle (claimed) such as car, truck, airplane, boat and train, for delivering power. Can also be used in hydrogen flame, motor and home.    ADVANTAGE - The volume and the pressure of the hydrogen storage tank in the system can be reduced, since the storing of the hydrogen is not necessary. The variability in the heat source can be smoothed out by allowing temporary storage. The environmental impact that the system imposes on our environment can be reduced.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for generating hydrogen on demand; and    (2) system for on-demand production of sodium hydroxide.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram for system for generating hydrogen.    System for generating hydrogen (100)    Salt material (112)    Heating apparatus (116)    Left side production chamber (140)    Right side production chamber (144)    Hydrogen production subsystem (190)
NOVELTY - The separation process involves passing a first product stream to a second separation unit containing an oxygen-selective adsorbent and operated with a pressure swing so as to preferentially adsorb oxygen to produce a low pressure gas stream enriched with oxygen and produce a higher pressure second product stream enriched with methane. The natural gas feed stream is passed to a first separation unit to separate oxygen from the feed stream and produce the first product stream enriched with methane and a waste stream having a higher molar concentration of oxygen than the feed stream.    USE - Separation process for separating oxygen from natural gas feed stream from landfill gas, coal mine methane, coal bed methane, natural gas wells, or biogas.    ADVANTAGE - Achieves low oxygen levels in natural gas stream without use of catalytic system. Ensures cost-effective separation of oxygen from natural gas feed stream.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the removal process of oxygen from contaminated methane feed gas using carbon molecular sieve pressure swing adsorption.    Pre-treat (26)    Membrane (32)    Removal system (41)    Recycle stream (44)    Removal system (49)
NOVELTY - The system (100) has solar cell raft mother vessel (4) which is equipped with seawater electrolysis device for converting electric energy generated by solar cell unit (20) into hydrogen. A liquid hydrogen tank stores hydrogen obtained by the conversion. A recovery vessel (6) has hydrogen recovery unit for recovering hydrogen stored in liquid hydrogen tank. A hydrogen recovery tank (9) recovers hydrogen from the recovery vessel and stores hydrogen. A power plant (10) converts hydrogen stored in the hydrogen recovery tank into electric energy.    USE - Solar energy power generation system for motor vehicle.    ADVANTAGE - The recovery vessel is provided with hydrogen recovery unit for recovering hydrogen stored in liquid hydrogen tank such that long distance conveyance of sunlight energy can be carried out efficiently at low cost. The energy for movement of solar cell raft mother ship can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the solar energy power generation system. (Drawing includes non-English language text)    Solar cell raft mother vessel (4)    Recovery vessel (6)    Hydrogen recovery tank (9)    Power plant (10)    Solar cell unit (20)    Solar energy power generation system (100)
NOVELTY - The device (10) has a feed device (30) and a rotationally symmetric furnace pipe (20) with a rotational axis (R). An elongated resistance heater (23) protrudes from an outer side (A) of the furnace pipe into an inner side (I) of the furnace pipe and a hot zone (H1) and a less hot zone (H2). The hot zone (H1) follows the less hot zone (H2) as viewed from an inlet side (E). The resistance heater is designed in such a manner that temperature in the inner side of the furnace pipe in range of the hot zone is 1200 degree Celsius.    USE - High-temperature device for converting organic starting material e.g. waste material, residual material and biomass, into synthese gas.    ADVANTAGE - The device provides efficient stability against the aggressive material even during high temperature and effective conversion of the starting material to the synthese gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for converting starting material into a gaseous product in a high-temperature device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of a high-temperature device.    Outer side (A)    Inner side (E)    Hot zone (H1)    Less hot zone (H2)    Inner side (I)    High-temperature device (10)    Furnace pipe (20)    Elongated resistance heater (23)    Feed device (30)
NOVELTY - The device has a wave guide (1) connected to a gas excitation unit having a part (11) forming a moveable element e.g. strip type movable element, that is in contact with the gas and is vibrated by the impact of the molecules of excited gas. A sensor (4) measures the vibration of the element. The sensor and the element form a detecting unit that detects the excitation of the gas. The gas excitation unit is constituted by a laser.    USE - Gas detecting device for detecting the gas e.g. carbon dioxide, carbon monoxide or methane, to avoid domestic accident by oxygen deficiency.    ADVANTAGE - The device is compact. The utilization of the sensor and movable element allows the device to provide accurate detection of gas, and allows the device to be utilized in a simple manner for domestic applications.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a gas detecting device.    Wave guide (1)    Sensor (4)    Part (11)    Moveable element's proximal end (110)    Free space (114)
NOVELTY - The fuel cell system has a poisoning determination device (120a), which determines poisoning of polymer electrolyte form fuel cell of fuel cell stack (101); and a controller (120), which controls a switching device (104,105) in the generating mode of fuel cell stack to interrupt supply of reactive gas to a second reference cell (103). The fuel cell system determines poisoning of polymer electrolyte form fuel cell is carried out when voltage or electric current value of first reference cell (102) is smaller than voltage or electric current value of second reference cell.    USE - Fuel cell system.    ADVANTAGE - Deterioration by the catalyst poisoning of the fuel cell stack which produces electric power is suppressed. Fuel cell system performs poisoning recovery processing of fuel cell stack at an appropriate timing.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an operating method of a fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of schematic structure of the fuel cell system. (Drawing includes non-English language text).    Fuel cell stack (101)    First reference cell (102)    Second reference cell (103)    Switching device (104,105)    Controller (120)    Poisoning determination device (120a)
NOVELTY - The stack has an anode opposition plate (42) connected with hydrogen supply ports (422i) and an opening part (422o). An intermediate plate is connected with flow-path formation parts for forming a flow path for inducing hydrogen containing water content in the opening part to the hydrogen supply ports. The hydrogen supply ports are arranged in a thickness direction of the anode opposition plate.    USE - Solid polymer type fuel cell stack for a separator (claimed).    ADVANTAGE - The stack allows self-humidification of the electrolytic membrane.    DESCRIPTION OF DRAWING(S) - The drawing shows a top view of a component of a fuel cell module. '(Drawing includes non-English language text)'    Anode opposition plate (42)    Hydrogen supply port (422i)    Opening part (422o)    Through-hole (424a)
NOVELTY - Method for processing waste gas containing non-halogenated aliphatic hydrocarbon and halogenated aliphatic hydrocarbon, involves (a) contacting catalyst (a1) containing metal of platinum and/or palladium, or its oxide with the waste gas at 275-475 degrees C, (b) contacting catalyst (a2) containing titanium oxide and tungsten oxide with the gas obtained from process (a) at 300-550 degrees C, where the catalyst (a2) does not contain noble metal and (c) contacting catalyst (a3) containing palladium metal or its oxide with the gas obtained from process (b) at 300-550 degrees C.    USE - The method is useful for processing waste gas containing non-halogenated aliphatic hydrocarbon and halogenated aliphatic hydrocarbon.    ADVANTAGE - The method suppresses generation of halogen gas.
NOVELTY - Biogas slurry processing device comprises first sand settling tank, a liquid storage tank, a second sand setting tank and two biogas slurry channels. The first and second sand settling tanks are respectively connected with the liquid storage tank by the two biogas slurry channels, and the liquid storage tank is arranged between the first and second sank setting tank. The first sand setting tank is provided with a biogas slurry inlet, while the second sand setting tank is provided with a processed biogas slurry outlet.    USE - Used as a biogas slurry processing device.    ADVANTAGE - The device adopts natural ecological processing process of three-level delay filtration and aerobic storage of a circle containing multiple biologic chains so as to realize flow-dividing irrigation of biogas slurry and fresh water.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of the biogas slurry processing device.
NOVELTY - A biomass energy combustor comprises a combustion chamber with a charge hole and a carbon discharge hole; where the carbon discharge hole is set with a carbon discharge auger; and the pitch of the spiral blade of the carbon discharge auger is gradually reduced along a carbon discharge direction.    USE - The biomass energy combustor is useful for automatically discharging carbon.    ADVANTAGE - The biomass energy combustor can compress combustion substrate while discharging carbon and further carbonize the combustion substrate to increase product carbon content. Moreover, the combustion chamber sucks air in multiple angles via main air hole and air distribution holes, which changes the airflow direction in the combustion chamber, increases the contact time and contact surface of combustion-supporting air and combusting material, and improves combustion-supporting effect. Additionally, the combustion-supporting air is preheated for multiple times by the heat of the combustion chamber, which reasonably utilizes heat and reduces heat loss.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the biomass energy combustor.
NOVELTY - The generator has a vertical hydraulic oil cylinder arranged at a top part of a furnace body. A material inlet piston cylinder is horizontally arranged at the side of the furnace body. An air outlet pipe port is externally connected with an upper part of a ring-shaped gas collecting chamber. Refractory bricks are arranged from a lower part of the gas collecting chamber to an inner wall of an upper furnace body of a fire bar. A slag chamber is arranged at a lower part of the fire bar. A slag outlet and an air inlet pipe port are arranged on the furnace body located at the slag chamber.    USE - Environment-friendly household rubbish fuel gas generator.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial sectional view of an environment-friendly household rubbish fuel gas generator.
NOVELTY - The boiler has encircling secondary air bellows that are installed at the four sides of the arch portion of the furnace tank (8). A limestone powder hopper (5) with control material valve is installed at secondary wind header pipe (4). A shaft flue (14,29) are installed at the high-temperature smoke outlet (13) of the furnace tank in sequence. A convection low and high temperature super heater pipe (18,22) are installed in the shaft flue (25). The distance between the front and rear arches of furnace tank and 20t biomass and rubbish power generation boiler are 1.1m.    USE - Biomass and rubbish power generation boiler for preventing the corrosion of super heaters.    ADVANTAGE - The biomass and rubbish power generation boiler prevents the corrosion of super heaters so that the service life of the super heater can be improved. The cost of biomass and rubbish power generation boiler can be reduced by providing simple construction and maintenance.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the biomass and rubbish power generation boiler. (Drawing includes non-English language text)    Secondary wind header pipe (4)    Limestone powder hopper (5)    Furnace tank (8)    High-temperature smoke outlet (13)    Shaft flue (14,25,29)    Low temperature super heater pipe (18)    High temperature super heater pipe (22)
NOVELTY - The furnace has a straw furnace body whose side part is provided with a fuel feeding suspension crane. An upper part of the furnace body is connected with a fuel gas clean room via a fuel gas transport pipe. A lower part of the fuel gas clean room is connected with a fuel gas cooker via a gas pipe. The fuel gas transport pipe is connected with a steam condensing box and a tar collecting box. The tar collecting box is connected with the fuel gas transport pipe via a spiral coil pipe.    USE - Multifunctional straw gasification furnace.    ADVANTAGE - The furnace is simple in structure and suitable for the occasions of many people having dinner such as large-scale hotel, outdoor food and beverage plaza, and satisfies the firepower demand of large-scale cooking.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a multifunctional straw gasification furnace.
NOVELTY - Apparatus comprises stirring unit for mixing animal and plant organic waste with deodorizing liquid having denitrifying effect including photosynthesis microbe, first detection unit for detecting predetermined biological oxygen demand (BOD) of the mixture by stirring the mixture until it reaches predetermined value, and controlling unit for separating solid and liquid portion from the stirred mixture obtained from the first detection unit.    USE - The apparatus is useful for processing animal and plant organic waste which is used as fertilizer or fuel.    ADVANTAGE - The apparatus is environmentally-friendly and reduces the offensive odor of the waste material.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) method for processing animal and plant organic waste, involves performing the above-mentioned steps; and (2) processing apparatus for performing the above-cited method comprising deodorizing liquid containing alkali proof photosynthetic microorganism chosen from Synechococcus having beta -carotene and Rhodopseudomonas, preferably Rhodopseudomonas A and Rhodopseudomonas B having bacterial chlorophyll and neurosporene.
NOVELTY - Enhancing the biofuel potential of an algal culture comprises: providing a culture of at least one algal species; contacting the algal culture with a composition to enhance the biofuel potential of the algal culture; and allowing the algal culture to for a time period, where the potential of the algal culture to provide a biofuel product or be processed to the biofuel product is enhanced compared to when the algal culture is not in contact with the composition.    USE - The method is useful for enhancing the biofuel potential including biomass or lipid content of the algal culture (claimed).    ADVANTAGE - The method is: simple, safe and eco-friendly as compared to conventional genetic and metabolic engineering; and suitable for use in both open ponds and closed photobioreactors.
NOVELTY - A calcium salt is added to a process liquid containing organic substance, which is pre-treated by adding sulfuric acid, and neutralized. Anaerobic treatment is then carried out using microorganism, and metabolites are recovered. Anaerobic treatment is carried out by a sulfate reducer, and calcium sulfate precipitated during neutralization is recovered. Calcium carbonate precipitated during sulfuric acid reduction process is recovered and supplied to neutralization process as calcium salt. Thus, organic substance is processed.    USE - Processing of organic substance for producing bioethanol.    ADVANTAGE - The organic substance is efficiently and economically manufactured.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for processing apparatus (1) of organic substance, which has a neutralization unit (3), metabolite recovery unit (4), sulfuric acid reduction unit (5) and neutralization agent supply portion (6).    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of bioethanol manufacturing apparatus. (Drawing includes non-English language text)    Processing apparatus (1)    Pre-processing unit (2)    Neutralization unit (3)    Metabolite recovery unit (4)    Sulfuric acid reduction unit (5)    Neutralizing agent supply unit (6)
NOVELTY - The system has an air blower (7) connected with a polymer collapsible gas storing device (10) that is connected with a user source (19). A combustible gas valve (8), a de-air valve (9) and a vacuum pump (12) are connected between the air blower and the polymer collapsible gas storing device. A user conveying valve (11) is installed between the gas storing device and the user source. A lower side of a vapor gasification device (1) is equipped with a residue extracting mouth (18). An oxygen valve (14) is connected with a draught fan valve (16) and a ventilation opening three-way valve (17).    USE - Domestic rubbish thermal pyrolysis application system.    ADVANTAGE - The system generates combustible gas and oil tar by thermal pyrolysis, where the gas can be used as fuel and the oil tar can be used as a chemical raw material.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a domestic rubbish thermal pyrolysis application system.'(Drawing includes non-English language text)'    Vapor gasification device (1)    Air blower (7)    Combustible gas valve (8)    De-air valve (9)    Polymer collapsible gas storing device (10)    User conveying valve (11)    Vacuum pump (12)    Oxygen valve (14)    Draught fan valve (16)    Ventilation opening three-way valve (17)    Residue extracting mouth (18)    User source (19)
NOVELTY - The device has an iron casting tower board (2) whose lower part is arranged with a fan (7) and a uniform distribution device (13). An upper terminal of a waste processing tin (8) is connected to a ceramic dust-removing device (11) through a gas conveyance tube (10). A connection part of the gas conveyance tube and an inner wall of the waste processing tin is provided with a coke-removing device (9). A lower part of the ceramic dust-removing device is arranged with a water seal security device (12).    USE - Plant waste material gasifying burning device.    ADVANTAGE - The device is environment-friendly, simple in structure and safe to use, and saves energy resource.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a plant waste material gasifying burning device.    Iron casting tower board (2)    Fan (7)    Waste processing tin (8)    Coke-removing device (9)    Gas conveyance tube (10)    Ceramic dust-removing device (11)    Water seal security device (12)    Uniform distribution device (13)
NOVELTY - The furnace has a furnace cover (1) inlaid in a peripheral water groove (5) on an outer side of a feed port at an upper end of a furnace drum (4) and supported by a bracket (14). A lower end of the furnace drum is inlaid in a peripheral water groove (10) at an upper end of a furnace base (7), where the furnace base is fixedly connected to a lower part of the bracket supporting a furnace body. An ash and slag outlet is arranged at a lower end of a drum body (8) of an intake device and sealed by an ash baffle (13).    USE - Biomass gasification furnace.    ADVANTAGE - The furnace can continuously smash fuel at an upper end of a hearth in the internal high-temperature area of the furnace drum by a material feeding shovel fixed to an intake pipe in the furnace base so as to generate gas continuously and stably and prolong combustion time.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a biomass gasification furnace.    Furnace cover (1)    Furnace drum (4)    Peripheral water grooves (5, 10)    Furnace base (7)    Drum body (8)    Ash baffle (13)    Bracket (14)
NOVELTY - The furnace has a material feeding opening (6) opened on an upper end of a furnace body (3). An upper suction chamber (2) is arranged around the material feeding opening. An upper suction opening (1) is opened on the upper suction chamber. A lower end of the furnace body is arranged in a lower suction chamber (5). A lower suction opening (4) is opened on the lower suction chamber.    USE - Compound suction straw gasification furnace.    ADVANTAGE - The furnace reduces waste gas discharge amount and increases fuel production rate.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a compound suction straw gasification furnace.    Upper suction opening (1)    Upper suction chamber (2)    Furnace body (3)    Lower suction opening (4)    Lower suction chamber (5)    Material feeding opening (6)
NOVELTY - The furnace has a gas generation furnace part (2) whose upper part is provided with a gas generation tube (4) and connected with a cooling separation barrel (5). A gas delivery tube (6) on the cooling separation barrel is connected with an impurity gas separation device. A gas outlet tube (9) is mounted on the impurity gas separation device. The impurity gas separation device is arranged with a water tank (10) and an impurity gas separation barrel (8) arranged on the water tank. The gas delivery tube and the gas outlet tube are connected on the impurity gas separation barrel.    USE - Biomass gasification furnace.    ADVANTAGE - The furnace is simple in structure and inexpensive, and makes full utilization of rural bamboo joints, bamboo poles, leaves, branches, firewood and wood processing leftover materials as fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial sectional view of a biomass gasification furnace.    Gas generation furnace part (2)    Gas generation tube (4)    Cooling separation barrel (5)    Gas delivery tube (6)    Impurity gas separation barrel (8)    Gas outlet tube (9)    Water tank (10)
NOVELTY - The device has a generating furnace (2) connected with a material transferring device (1) and a dust collector (3). A spraying tower (5) is connected with a filter (6) and arranged between the dust collector and a gas storing cylinder (9). The dust collector, a dust collecting air cooler (4), the spraying tower, the filter, and an electric tar collector (8) are formed in a four-grade purifying system. The dust collecting air cooler is arranged between the dust collector and the spraying tower. The electric tar collector is arranged between the filter and the gas storing cylinder.    USE - Biomass fluidized bed device.    ADVANTAGE - The device utilizes waste biomasses as fuel and utilizes air as a gasifying agent, thus reducing production cost of fuel gas. The device purifies the fuel gas to improve cleanness of the fuel gas and to protect the environment.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass fluidized bed device.    Material transferring device (1)    Generating furnace (2)    Dust collector (3)    Dust collecting air cooler (4)    Spraying tower (5)    Filter (6)    Electric tar collector (8)    Gas storing cylinder (9)
NOVELTY - The boiler has transverse baffle boards (3) arranged in a biomass gasification chamber (6) to form a positive pressure combustion gasification smoke channel (5). A lower part of the chamber is fixed with a side face boiler door (14). A side of a furnace body is fixed with a water return interface (16). An ashbin is fixed with a boiler base below the chamber. An inner part of the chamber is fixed with a primary wind channel (10) that is provided with a bottom wind ring with holes. The bin is placed below a ground surface that is lower than a leg (15). A basic pit is sealed by water.    USE - Underlying transverse combustion biomass gasification boiler.    ADVANTAGE - The primary wind channel changes way of introduction of combustion wind to the boiler, thus preventing the fire from being set out. The boiler allows changing the combustion manner along with a boiler structure to achieve complete combustion and better fire frame effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an underlying transverse combustion biomass gasification boiler.    Transverse baffle boards (3)    Positive pressure combustion gasification smoke channel (5)    Biomass gasification chamber (6)    Primary wind channel (10)    Side face boiler door (14)    Leg (15)    Water return interface (16)
NOVELTY - The furnace has a furnace internal buckle (11) installed in a furnace external buckle (12). A gas outlet tube on an upper part of the furnace external buckle is connected with an air distribution knob and a reversed cone safety device (4). The gas outlet tube is connected with an adjustable speed draught fan (5), a valve (8) and a flame arrestor (6). An upper part between the furnace internal buckle and the furnace external buckle are provided with a porous ring tube (1). A porous furnace cover device (2) is installed above a biomass fuel (9) in the furnace internal buckle.    USE - Negative pressure gasification furnace.    ADVANTAGE - The steam and nitrogen available in furnace is discharged from the holes, and tar is recycled as biomass for combustion, thus reducing the tar from being discharged to the atmosphere.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a negative pressure gasification furnace.    Porous ring tube (1)    Porous furnace cover device (2)    Reversed cone safety device (4)    Adjustable speed draught fan (5)    Flame arrestor (6)    Valve (8)    Biomass fuel (9)    Furnace internal buckle (11)    Furnace external buckle (12)
NOVELTY - The hydrogen fuel cell harvester (1) has a hydrogen fuel cell (4) producing electricity as result of electrochemical reaction of hydrogen fuel. The electricity is input to the electric motor (6) via electric lead (5). The torque produced by the motor is transmitted to a mechanical transmission device (8) via power output shaft (7). The transmission device drives a rotatable eccentric plucking wheel (12) for plucking grain crops. The fuel cell is a proton exchange membrane, alkaline, or phosphoric acid type hydrogen fuel cell.    USE - Hydrogen fuel cell harvester for grain crops.    DESCRIPTION OF DRAWING(S) - The drawing shows the side view of a hydrogen fuel cell harvester.    Hydrogen fuel cell harvester (1)    Hydrogen fuel cell (4)    Electric lead (5)    Electric motor (6)    Power output shaft (7)    Mechanical transmission device (8)    Eccentric plucking wheel (12)
NOVELTY - Method (M1) for extracting at least one lipid components from aqueous algal suspension or slurry, comprises: (a) saturating anion-exchange resin in column or container with algal suspension or slurry; (b) removing any excess water of liquids from column or container by applying gas pressure or vacuum, air drying column or container, or using combination of other drying techniques; (c) flowing eluent through algae saturated column to elute algae off column; and (d) collecting eluted algae in a receiver connected to the column or container, where eluted algae comprises components and eluent.    USE - The method is useful for extracting at least one lipid component from an aqueous algal suspension or slurry, where the lipid components are further converted into FAMEs or biodiesel (all claimed).    ADVANTAGE - The method: does not require prior drying of the algae; utilizes minimum solvent, which can be reused, hence simple and economical; and does not destroy the algal biomass which can be used for other purposes.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method (M2) of extracting at least one lipid components from an aqueous algal suspension or slurry, comprising: saturating a lipid binding column or a container comprising a lipid binding hydrophobic resin with the algae; stopping the flow of the algae at the saturation point of the column or the container; applying a gas pressure or a vacuum to the column or the container to remove any residual algae from the column or the container; passing a solvent through the column or the container to extract the bound lipid components and the oils, where the solvent is hexane or other alkanes, chloroform or other halogenated solvents, ether, ketone, or other aromatic solvents; collecting the solvent comprising the dissolved lipid components and the oil in a separate receiver; and removing the solvent to obtain a concentrate comprising the lipid components and the oil.
NOVELTY - The livestock excretion dryer has an input unit (210) that transfers the livestock excretion supplied from a hopper bottom furnace. An exhaust gas outlet (500) discharges the exhaust gas. An agitator agitates the livestock excretion. An exhaust gas feed port (400) supplies the exhaust gas to a drying element (200). The drying element is allowed to remove the moisture content from the livestock excretion.    USE - Livestock excretion dryer for livestock excretion solid fuel producing apparatus (claimed).    ADVANTAGE - Since the exhaust gas is supplied to drying element, the livestock excretion drying effect can be improved. The livestock excretion can be dried quickly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for livestock excretion solid fuel producing apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the livestock excretion dryer.    Drying element (200)    Input unit (210)    Exhaust gas feed port (400)    Exhaust gas outlet (500)    Auxiliary drying unit (600)
NOVELTY - The system (200) has pyrolysis device (120) which decomposes thermally the volatile component and organic compound in predetermined temperature. The pyrolysis/gasification process is performed with respect to the waste comprising wood composite, waste plastic, organic sludge, food waste and livestock excretions.    USE - Fuel cell electric power generation system.    ADVANTAGE - The electric power generation efficiency is improved. The fuel cell electric power generation system is environmental friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for power generation method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fuel cell electric power generation system. (Drawing includes non-English language text)    Combustion waste (100)    Pyrolysis device (120)    Gas purifier (130)    Heat exchanger (140)    Current converter (170)
NOVELTY - A continuous discharge-type pyrolytic carbonizer comprises a pyrolysis tank (1), a controllable oxygen supply pipeline (2), and a movable transverse stop (3). Lower part of the pyrolysis tank has a U-shaped guide tank (4) and a screw discharger (5). One side of the guide tank is fixed to inner wall of pyrolysis tank. The screw discharger has a feed port communicated with bottom of the pyrolysis tank, and a discharge port arranged outside of the pyrolysis tank.    USE - Continuous discharge-type pyrolytic carbonizer used for processing crop stalks.    ADVANTAGE - The carbonizer is capable for quick feeding and discharge, has high efficiency, and is safe to use and reliable, and suitable for local operation in fields.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the pyrolytic carbonizer.    Pyrolysis tank (1)    Oxygen supply pipeline (2)    Movable transverse stop (3)    Guide tank (4)    Screw discharger (5)
NOVELTY - Biofilter comprises a bucket body (1) made of glass fibr reinforced plastic, and a water inlet tube (2) via which the sewage can enter into the bucket body is transversally installed on top of the bucket body. A water outlet tube (3) via which sewage flows out along the bottom of the bucket body after being filtered is installed on the bottom side surface, and an oxygen tube (4) for introducing the oxygen is installed on one side surface of the upper part and located below the water inlet tube. An oxygen layer (5) for storing oxygen is disposed on the lower part of the bucket body.    USE - Used as a biofilter.    ADVANTAGE - The biofilter: uses Nitrobacter and de-nitrifying bacteria to reduce ammonia nitrogen content and maintain water quality in a stable state for a long time; and is simple with long service life and capacity of purifying sewage.    DETAILED DESCRIPTION - Biofilter comprises a bucket body (1) made of glass fiber reinforced plastic, and a water inlet tube (2) via which the sewage can enter into the bucket body is transversally installed on top of the bucket body. A water outlet tube (3) via which sewage flows out along the bottom of the bucket body after being filtered is installed on the bottom side surface, and an oxygen tube (4) for introducing the oxygen is installed on one side surface of the upper part and located below the water inlet tube. An oxygen layer (5) for storing oxygen is disposed on the lower part of the bucket body, and biological balls which are not uniformly distributed and have different sizes are placed from the oxygen layer to the bucket top.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of the biofilter.    bucket body (1)    Water inlet tube (2)    water outlet tube (3)    Oxygen tube (4)    Oxygen layer (5)
NOVELTY - The method involves drying combustible organic material. Inorganic compounds provided with aluminum and iron metals. Starch-based materials such as dextrin and cellulose processed with liquid products such as crude oil, acrylates, amides and phenols.    USE - Method for producing charcoal for a power equipment by treating waste water.
NOVELTY - Warehouse for dried, pre-fermented low-carbon livestock manure comprises an upper baffle, a lower baffle, a bottom side, a framework and a transparent plastic film enclosing to form an enclosed space, where the upper baffle and the lower baffle are connected with two sides of the bottom side, two ends of the framework are connected with the upper baffle and the lower baffle, and the transparent plastic film is covered on the framework.    USE - The warehouse is useful for dried, pre-fermented low-carbon livestock manure.    ADVANTAGE - The warehouse: has simple structure; saves energy; utilizes solar energy, wind energy and biological energy produced during fermentation; and is economical, environment-friendly and not affected by weather.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the warehouse.
NOVELTY - A solid fuel contains coal powder, petroleum coke powder, biomass fuel powder and fuel additive. The fuel additive comprises silica and calcium carbonate or calcium oxide.    USE - Solid fuel is used for smelting glass (claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparation of solid fuel, which involves sieving coal powder which passes through 170 meshes, sieving petroleum coke powder which passes through 140 meshes, sieving biomass fuel powder which passes through 50 meshes and sieving fuel additive, grinding the sieved coal powder, petroleum coke powder, biomass fuel powder and fuel additive, and mixing; and    (2) device for preparing the solid fuel, which has a grinding device, four constant weight feeding machines and a mixing device connected with all the constant weight feeding machines, and optionally, a conveying device connected with the mixing device and the dilute phase gas conveying device.
NOVELTY - A methanol fuel comprises (in wt.%) methanol (less than 50), aromatic hydrocarbon (more than 45) and fluxing modifier (more than 5).    USE - Methanol fuel used for vehicles.    ADVANTAGE - The methanol fuel is directly used without doping with gasoline or changing gasoline engine, and has favorable dynamic property and reduced oil consumption. The synthesizing device has simple structure, and quickly and economically enables to manufacture methanol fuel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for synthesizing device of methanol fuel, which has a methanol raw material conveying device, a fluxing modifier raw material conveying device, an aromatic hydrocarbon raw material conveying device, a synthesizing device and a filling device of product tank.
NOVELTY - The electrolytic hydrogen generator has a hydrogen generation chamber connected with the bottom of hydrogen washing device by a hydrogen guide pipe. The washing device is connected with a hydrogen acid-alkali neutralizing device and a hydrogen purifying device by a guide pipe. The acid-alkali is dried by a drying device, and the upper portion of oxygen generation chamber is connected with liquid-adding and oxygen pressure-regulating barrel by an oxygen pipe and provided with water adding hole and oxygen outlet.    USE - Electrolytic hydrogen generator.    ADVANTAGE - The exhaust pressure is controlled by a pressure-reducing valve and oxygen pressure detector, so that the hydrogen exhaust pressure is equal to the oxygen exhaust pressure in order to ensure pressure balance between two sides of conductive membrane. The mixing of hydrogen and oxygen gas is prevented, so that purity of hydrogen is maintained for a long time.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the electrolytic hydrogen generator.
NOVELTY - Preparation of cefpodoxime acid of formula (I) using aqueous monoglyme or aqueous diglyme as a solvent in a very safe, simple, economical, environmentally-friendly manner, is disclosed. Image 0/0
NOVELTY - Domestic organic waste is selected, and inflammable articles are sampled. The sampled material is added to anoxic pyrolysis tank and decomposed at 200-450 degrees C. Carbide discharged from obtained process is pulverized, and evaporation gas of organic component produced during cracking is condensed to produce emulsified gasoline. Carbide and gasoline are mixed at constant rate to produce bio powder. The bio powder is compressed to manufacture solid bio-charcoal.    USE - Manufacture of solid bio-charcoal.    ADVANTAGE - The solid bio-charcoal is manufactured without affecting the environment by a simple method.
NOVELTY - Water is added to biomass materials provided on a loading platform. The biomass materials are ground using a splitting machine, and rough fiber is separated from the materials. The material is mixed in fluid, using a milling machine, and slag mud with diameter of 100 microns or less is separated. The water (10-20%) is separated from fluid by a separator, and separated water is supplied to a liquid storage tank. The slug mud and rough fiber are molded in an extrusion molding machine, to obtain single-component and multicomponent biomass solid-liquid fuel.    USE - Production of single-component and multicomponent biomass solid-liquid fuel.    ADVANTAGE - The method enables economical production of single-component and multicomponent biomass solid-liquid fuel with high yield, without environmental pollution.    DETAILED DESCRIPTION - Water is added to biomass materials provided on a loading platform. The weight ratio of solid portion of biomass materials and water is 1:0.2-0.7. The biomass materials are ground using a splitting machine, and rough fiber is separated from the materials. The material is mixed in fluid, using a milling machine, and slag mud with diameter of 100 microns or less is separated. The water (10-20%) is separated from fluid by a separator, and separated water is supplied to a liquid storage tank. The slug mud and rough fiber are molded in an extrusion molding machine, to obtain single-component and multicomponent biomass solid-liquid fuel. An INDEPENDENT CLAIM is included for device for producing single-component and multicomponent biomass solid-liquid fuel, which has loading platform, splitting machine, milling machine, separator, a liquid storage tank and extrusion molding machine.
NOVELTY - The heat exchanger (100) has a heat exchange coil connected to two paths and arranged in a thermal storage tank (22). The thermal storage tank stores heat generated in a fuel cell system (21) through a thermal medium. The thermal medium flow warm water/hot-water heats up with a heat exchange action. A heating water inlet and a heating water outlet are installed on a top part of the thermal storage tank. Multiple branched ducts (51, 52) are mounted on the heat exchange coil at a vertical state. The branched ducts are made of steel material.    USE - Heat exchanger for a thermal storage tank of a fuel cell system.    ADVANTAGE - The heat exchange coil can be formed and connected with two paths so as to ensure effective heat exchange action. The heat exchanger utilizes waste heat generated in the fuel cell system so as to saves energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a heat exchanger.'(Drawing includes non-English language text)'    Circulating pump (6)    Fuel cell system (21)    Thermal storage tank (22)    Branched ducts (51, 52)    Heat exchanger (100)
NOVELTY - The organic waste gasifier (100) has main portion having barrier (130) for partitioning main portion into gasification reactor (110) and combustion reactor (120) such that double-reactor type sewage sludge portion is formed. The gasification reactor gasifies the organic waste and ejects material. The combustion reactor increases the temperature of material and air spray unit sprays the air towards gasification reactor and material in combustion reactor. The sewage sludge portion has baffle (140) for circulating material among gasification reactor and combustion reactor.    USE - Organic waste gasifier for fluidized-bed gasification apparatus used in chemical process field.    ADVANTAGE - The material can be circulated smoothly among gasification reactor and combustion reactor. The gasification and combustion efficiency are improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of organic waste gasifier.    Organic waste gasifier (100)    Gasification reactor (110)    Combustion reactor (120)    Barrier (130)    Baffle (140)
NOVELTY - An ortho-phenylenediamine and phenylacetic acid is dissolved in low-grade saturated ethanol solvent. A dehydrating agent is added at 100-130 degrees C, and constant-temperature reaction is performed to obtain reaction liquid. The obtained reaction liquid is cooled at room temperature and filtered to obtain bendazol salt. The obtained salt is decompressed and dried. The obtained dried material is dissolved in water, and pH value is adjusted. An active carbon is added decolored, filtered, cooled, crystallized and dried to obtain bendazol hydrochloride.    USE - Preparation of bendazol hydrochloride.    ADVANTAGE - The method economically provides bendazol hydrochloride with short period of time.    DETAILED DESCRIPTION - An ortho-phenylenediamine and phenylacetic acid is dissolved in low-grade saturated ethanol solvent. A dehydrating agent is added at 100-130 degrees C, and constant-temperature reaction is performed to obtain reaction liquid. The obtained reaction liquid is cooled at room temperature and filtered to obtain bendazol salt. The obtained salt is decompressed and dried. The obtained dried material is dissolved in water, and pH value is adjusted. An active carbon is added decolored, filtered, cooled, crystallized and dried to obtain bendazol hydrochloride. The dehydrating agent is dicyclohexylcarbodiimide, 1-ethyl-3-(3-dimethylaminopropyl)carbodiimide hydrochloride, N,N-carbonyl diimidazole or n-propyl phosphoric anhydride. The solvent is recovered.
NOVELTY - A biomass gasification method involves supplying biomass slurry to thermal decomposition reaction apparatus and thermally decomposing biomass by supercritical state, supplying product produced in thermal decomposition process and oxidizing agent to oxidation reaction apparatus, retaining solid polymer substance contained in product for greater than or equal to 20 seconds and oxidatively decomposing by oxidizing agent, supplying product produced at oxidative-degradation process to catalytic reaction apparatus and generating gas composition, and lowering temperature and pressure of gas composition and vaporizing.    USE - A biomass gasification method used in energy industry field.    ADVANTAGE - The method gasifies biomass in low-temperature region of 400 degrees C efficiently event if concentration of biomass in slurry is increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of biomass gasification method. (Drawing includes non-English language text).
NOVELTY - Device for processing by-products of poultry and stock raising with the use of heat of exothermic reactions, includes biofermenter(s) having pressure and exhaust fans. The biofermenter has a housing with internal cavity for fermentation of mixture of carbon-containing raw material and phosphorus-containing complexones of microcells by layer, which does not exceed 1.5 m. The housing has a bottom, longitudinal walls, and cover, where bottom is made in the form of aeration grid using grid with cells, and fixed between longitudinal or transverse walls of housing with support to foundation beams.    USE - Device for processing by-products of poultry and stock raising with the use of heat of exothermic reactions.    DETAILED DESCRIPTION - Device for processing by-products of poultry and stock raising with the use of heat of exothermic reactions, comprises biofermenter(s) having pressure and exhaust fans; and air duct and aeration grids installed at the bottom of biofermenter via longitudinal supports. The biofermenter has a housing with internal cavity for fermentation of mixture of carbon-containing raw material and phosphorus-containing complexones of microcells by layer, which does not exceed 1.5 m. The housing has a bottom, longitudinal walls, and cover, where bottom is made in the form of aeration grid using grid with cells, which do not exceed 5 mm, and fixed between longitudinal or transverse walls of housing with support to foundation beams. Foundation beams are placed along any pair of longitudinal walls to the entire length of housing with formation of space under the bottom of housing and have a height of greater than or equal to 70 cm and width of 15-25 cm. Air ducts are formed by parallel channels between foundation beams. They are placed in immediate proximity or connected with blower fan(s), which ensures temperature of exothermic reactions of 70-80 degrees C.
NOVELTY - Preparing bio-fuel, comprises: (i) crushing the biomass into fragments, washing for removing impurities and dehydrating the washed fragments; (ii) arranging the dehydrated biomass fragments in a vapor explosion device, feeding vapor and carrying out instantaneous vapor explosion and solid-liquid separation of vapor explosion products; (iii) rinsing the solid substances separated in step (ii) with water, then washing with hot water at 70-90 degrees C and dehydrating the washed solid matter; and (iv) extruding the dehydrated solid matter into block-shaped bio-fuel and crushing into a granular bio-fuel.    USE - The method is useful for preparing bio-fuel.    DETAILED DESCRIPTION - Preparing bio-fuel, comprises: (i) crushing the biomass roughly into fragments, washing the fragments for removing the impurities and dehydrating the washed fragments till the water content is 25-45 wt.%; (ii) arranging the dehydrated biomass fragments in a vapor explosion device, feeding vapor at 150-350 degrees C, maintaining a pressure of 0.5-3 MPa for 3-10 minutes, carrying out instantaneous vapor explosion and solid-liquid separation of the vapor explosion products; (iii) using clean water to rinse the solid substances separated in the step (ii) for 5-15 minutes, then using hot water at 70-90 degrees C to wash for 30-60 minutes and dehydrating the washed solid matter till the water content is 5-20 wt.%; and (iv) extruding the dehydrated solid matter in the step (iii) into block-shaped bio-fuel at a pressure of 15-75 MPa or extruding the solid matter and crushing them into a granular bio-fuel with a particle diameter of 0.1-15 mm.
NOVELTY - A device comprises a force material feeding device, a carbonizing chamber, a heat exchanger, a purifier, a carbon filter and water sealing flame arrestor orderly connected with each other through air conveying pipes. The force material feeding device consists of a material hopper, fan, a material conveying pipe, a cyclone separator and an air sealing machine. The material outlet of the material hopper is connected with the former cyclone separator through the material conveying pipe.    USE - Device used for preparing biomass and for recycling fuel waste heat.    ADVANTAGE - The device efficiently changes high-temperature combustible gases into clean combustion gases through cooling process in an eco-friendly manner.    DETAILED DESCRIPTION - A device comprises a force material feeding device, a carbonizing chamber, a heat exchanger, a purifier, a carbon filter and water sealing flame arrestor orderly connected with each other through air conveying pipes. The force material feeding device consists of a material hopper, fan, material conveying pipe, a cyclone separator and an air sealing machine. The material outlet of the material hopper is connected with the former cyclone separator through the material conveying pipe. Upper side of the former cyclone separator is connected with an exhaust pipe, where lower side is connected with the air sealing machine. The fan is arranged on the material conveying pipe, where the material inlet is provided at top of the carbonizing chamber with the material outlet of the air sealing machine.
NOVELTY - The system has a tar collecting tower whose outlet is connected with a liquid tar conveying device. The liquid tar conveying device is connected with a gasifying stove. The liquid tar conveying device includes a base. A tar pump, tar heating container and an insulating layer are arranged on the base. The tar pump is positioned at a side of the tar heating container. An insulating pipe connects an end of the tar pump with the tar heating container. Another end is connected with a Venturi nozzle inlet of the gasifying stove.    USE - High temperature cracking system for biomass fuel gas tar.    ADVANTAGE - The system recycles the waste tar intensively with improved operating factor of the tar and can be manufactured in a cost effective manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a high temperature cracking system.
NOVELTY - A cooking straw carbonizing stove comprises a carbonizing stove body, a charcoal box body, a feed port, a fire room and a steamer, where the fire room is provided with highest temperature faces to furnace mouth. A steel wok is installed on the furnace mouth for the high temperature needed by cooking, where a water layer is designed outside of the carbonizing stove body with water compensating port and a steam pipe. The carbonizing stove body is connected with a steamer by the steam pipe.    USE - Cooking straw carbonizing stove.    ADVANTAGE - The cooking straw carbonizing stove enables to achieve cooking and carbonizing processes.    DETAILED DESCRIPTION - A cooking straw carbonizing stove comprises a carbonizing stove body, a charcoal box body, a feed port, a fire room and a steamer, where the fire room is provided with highest temperature faces to furnace mouth. A steel wok is installed on the furnace mouth for the high temperature needed by cooking, where a water layer is designed outside of the carbonizing stove body with water compensating port and a steam pipe. The carbonizing stove body is connected with a steamer by the steam pipe. The charcoal box body is equipped with a grate, where a box cover plug plate is installed on the grate. The box cover plug plate is taken out during cooking process, where the water layer is watered by the water compensating port.
NOVELTY - A sludge turning-throwing roller with built-in power transmission device for sludge turning-throwing machine for treating the sludge in a harmless, recycling, and environment-friendly manner, comprises a connection and supporting device (IV), a turning-throwing device (III), a cooling system (V), a power transmission device (I), and a concentric location device (II).    USE - The sludge turning-throwing roller with built-in power transmission device is useful for sludge turning-throwing machine for treating the sludge in a harmless, recycling, and environment-friendly manner (claimed).    ADVANTAGE - The sludge turning-throwing roller with built-in power transmission device has advanced and reliable technology, compact and rational structure, smooth and stable operation, low transmission power loss, high production efficiency, alternate working of the fermentation tank by one machine, and high promotion value.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the sludge turning-throwing roller with built-in power transmission device for sludge turning-throwing machine for treating the sludge in a harmless, recycling, and environment-friendly manner.    Installation and connection hanging frame (1)    Refrigerator (2)    Turning-throwing motor (12)    Fixed inner roller (14)    Installation fixed tray (17)
NOVELTY - A device for preparing liquid manure by organic waste, comprises a fermenting bucket having a lower part that is equipped with a spaced filtering mesh; where the inner wall surface of the fermenting bucket is equipped with an electric heating sheet; the bottom part of the fermenting bucket is equipped with an oxygen transportation pipe; the oxygen transportation pipe is connected with an air outlet of an oxygen machine out of the fermenting bucket; and the fermenting bucket on lower part of the spaced filtering mesh is equipped with a liquid outlet tap.    USE - The device is useful for preparing liquid manure by organic waste (claimed).    ADVANTAGE - The device has simple structure, low cost, and high liquid manure yield rate. Moreover, the oxygen fermenting is more exhaustive. Additionally, the device has no secondary pollution and is more environment-friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the device for preparing liquid manure by organic waste.
NOVELTY - The system has a bucket elevator (7), a falling pipe and a lift charge distributor (3) that are provided in a feeding system. A dust hopper (2), a helical conveyor (24), an air seal machinery (17), a cyclone separator (18), an air seal machinery (19), a weighing machine (20), a dust hopper (21), a draught fan (22) and a cyclone separator (23) are provided in a carbon conveying system. A Venturi dust collector (12), a cyclone dust collector (13) and a water film coke cutter (14) are provided in a gas purification system.    USE - Fixed bed biomass gas industrial boiler system for treating biomass raw material e.g. rice husk, straw and sawdust.    ADVANTAGE - The system can be operated in a stable manner, and is convenient to use. The device does not pollute the environment during working process. The system can treat multiple types of biomass raw materials.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a fixed bed biomass gas industrial boiler system.    Dust hopper (2)    Lift charge distributor (3)    Bucket elevator (7)    Venturi dust collector (12)    Cyclone dust collector (13)    Water film coke cutter (14)    Air seal machinery (17)    Cyclone separator (18)    Air seal machinery (19)    Weighing machine (20)    Dust hopper (21)    Draught fan (22)    Cyclone separator (23)    Helical conveyor (24)
NOVELTY - An outdoor hydraulic glass steel methane tank capable of being embedded, comprises an upper hemisphere, a lower hemisphere, a sealing bar, a feed hopper, and a hydraulic pressure room; where the punches (11) for separately mounting the feed hopper (1) and the hydraulic pressure room (4) are arranged at two sides of the upper hemisphere (2); an edge is arranged at the connection of the upper hemisphere (2) and the lower hemisphere (5); and the edge is fixed and sealed by the sealing bar (6).    USE - The outdoor hydraulic glass steel methane tank capable of being embedded is useful for industrial and commercial applications.    ADVANTAGE - The outdoor hydraulic glass steel methane tank capable of being embedded has compact structure, easy manufacturing, stable methane generation, high heat value, light weight, and corrosion resistance.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the outdoor hydraulic glass steel methane tank capable of being embedded.    Feed hopper (1)    Upper hemisphere (2)    Air outlet pipe (3)    Hydraulic pressure room (4)    Lower hemisphere (5)    Sealing bar (6)
NOVELTY - Fuel composition comprises at least one herbaceous plant of Poaceae family having 4C photosynthesis and at least one vegetable wax mainly formed from hydrogenated oil of at least one plant, where the plant is in chopped form    USE - The composition is useful for ignition of combustible materials and for the preparation of the fire lighter (claimed).    ADVANTAGE - The composition is: easily malleable; non toxic; devoid of risk of gastrointestinal and lung problem and devoid of risk of suffocation or poisoning, preferably for children; and is more stable. The composition: reduces the risk of aspiration if accidentally swallowed, preferably by children; easy and simple to manufacture even at room temperature. The preparation of the composition: does not require a high power pressure; and inexpensive.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a fire lighter, which is present in the form of a solid substance, where the substance comprises the composition; and    (2) a preparation of the fuel composition comprising at least one step of mixing herbaceous plants of the Poaceae family in chopped form with the vegetable wax consists mainly of hydrogenated oil of at least one plant and a shaping by compression of the obtained mixture, preferably in the form of pellets.
NOVELTY - The device has a filtrate collecting groove and a compost cabin provided with radiator, feeding valve and discharging valve. A solar energy water heater is arranged at the top of compost cabin. The water outlet of solar energy water heater is communicated with water inlet of radiator. The water outlet of radiator is communicated with the water inlet of the solar energy water heater. The extreme lower end of the compost cabin is communicated with the filtrate connecting groove. The extreme lower end of the filtrate collecting groove is connected with a ferment pond.    USE - Ecological compost device of organic garbage.    ADVANTAGE - Improves the compost temperature of the compost, and builds micro environment which is good for activity of the microbe. Accelerates the fermenting speed of the organic garbage, and provides hot water for the radiator through the solar energy water heater, recycles water, and greatly reduces energy consumption. Provides an environment friendly ecological compost device.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the ecological compost device.
NOVELTY - Use of waste residue of Stevia rebaudiana monosaccharide in preparing biomass forming fuel rod, is claimed.    USE - The waste residue of Stevia rebaudiana monosaccharide is useful in preparing biomass forming fuel rod (claimed).    ADVANTAGE - The biomass forming fuel rod: has large capacity, has high calorific value, is environmental friendly, achieves less discharge of sulfur dioxide and generates less nitrogen oxides (NOx) being a green energy resource.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing biomass forming fuel rod comprising fermenting and heating the waste residue of Stevia rebaudiana monosaccharide, removing water, baking at 150-300 degrees C, crushing by a crusher after the moisture reaches 13-30%, cooling, reducing the temperature to 17-45 degrees C, and compressing to mold under 80-100 MPa to prepare a rod shaped product.
NOVELTY - Biochar, comprises (in wt.%) waste bacteria residue (50-75), gangue (10-40) and water (10-15).    USE - Used as a biochar.    ADVANTAGE - The method: conserves energy and soil resource; is economical; and has high socioeconomic value.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing the biochar, comprising: (i) crushing gauge into powder, and crushing waste bacteria residue containing water content of 35-50% into grains; (ii) mixing uniformly, agitating water-containing waste bacterial residue grains (60-90%) and gauge powder (10-40%); (iii) sterilizing and drying, heating the mixture for killing the mycelium and water content of the mixed material to decreases to 10-15%; and (iv) transferring the sterilized and dried mixed material to a high-pressure compression molding machine to compress and shape.
NOVELTY - A catalyst system (S1) for processing a reactant comprising at least some sulfur, comprises praseodymium in the form of a mixed phase of tri- and tetra-valent praseodymium; and a catalyst material. The mixed phase of praseodymium inhibits sulfur poisoning of the catalyst material.    USE - As a catalyst system for processing a reactant, preferably a fuel for a fuel cell, or hydrocarbon in a hydrocarbon reformation device (preferably a hydrogen generator), comprising at least some sulfur (all claimed), without sulfur poisoning of the catalyst material.    ADVANTAGE - The praseodymium in the catalyst material inhibits sulfur poisoning of the catalyst material, thereby improving the sulfur tolerance of the catalyst system.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a hydrogen generator comprising the catalyst system (S1) for processing a sulfur-containing hydrocarbon.
NOVELTY - The method involves ablating and pyrolizing a biomass material (2) between counter-rotating crunching rollers (3, 4), and turning the rollers at slightly different speeds. The rollers having circumferential surfaces, where the circumferential surfaces are heated with a highly heated fluid e.g. super-heated gas. A cylindrical body is housed within the rollers. Vaporized fluids are condensed in an enclosure (5). The biomass material is feed to the rollers through a chute (6). Hot dry steam is injected into the chute to preheat the biomass material.    USE - Pyrolytic method for converting biomass material such as paper, wood chips and vegetation debris, into useful byproducts. Uses include but are not limited to oils, liquids, carbon particles and solids.    ADVANTAGE - The method formulates and adjusts atmosphere to achieve a specific chemical reaction during processing, and facilitates ablation of a tire. The rollers avoid need of pre-shredding tires and other such items prior to feeding into a pyrolysis apparatus.    DETAILED DESCRIPTION - The highly heated fluid is taken from a group consisting essentially of superheated steam, highly heated molten salts, highly heated oils, combustion gasses, plasma and open flame.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of a pyrolysis machine.    Biomass material (2)    Counter-rotating crunching rollers (3, 4)    Enclosure (5)    Chute (6)    Trough (34)
NOVELTY - Removing carbon dioxide from a carbon dioxide containing gas stream, involves: providing an ion exchange resin, contacting the ion exchange resin with the carbon dioxide containing gas stream; sorbing a portion of the carbon dioxide from the carbon dioxide containing gas stream by the ion exchange resin, thereby forming a carbon-dioxide-form ion exchange resin; and desorbing the attached carbon dioxide from the carbon-dioxide-form ion exchange resin, thereby increasing the capacity of the resin to re-adsorb carbon dioxide.    USE - For removing carbon dioxide from a carbon dioxide containing gas stream comprising industrial gas and/or industrial gas stream selected from flue gas streams, hydrocarbon combustion gas streams, natural gas, produced gas, cracked gas, and synthesis gas streams (claimed); and in general carbon dioxide removal applications.    ADVANTAGE - The method utilizes effective ion exchange material comprising an aminoalkylated bead polymer in the removal of carbon dioxide from industrial applications, as compared to other materials often used in general carbon dioxide removal applications. The method increases the capacity of ion exchange resin to re-adsorb carbon dioxide. The method of carbon dioxide reduction of natural gas avoids introducing water vapor to the treated natural gas.
NOVELTY - A gas oil composition comprises: at least one gas oil; at least one dialkyl carbonate; where the dialkyl carbonate is obtained from bioalcohol.    USE - As fuel for burners, or for heating boilers, as fuel for diesel engines (claimed).    ADVANTAGE - The gas oil has a density, at 15 degrees C, of 780-845(preferably 800-840) kg/m3, determined according to the standard EN ISO 12185:1996/01:2001; has a flash point of greater than or equal to 55 (preferably 65) degrees C, determined according to the standard EN ISO 2719:2002; has a cetane number of greater than or equal to 47 (preferably greater than or equal to 51), determined according to the standard EN ISO 5165:1998; and has a cetane number of greater than or equal to 47 (preferably greater than or equal to 51) according to the standard ASTM D6890:2008. The process uses urea as carbonylating agent, which is a non-toxic, inexpensive and easily available product. The possibility of recycling the ammonia, makes the synthesis process highly sustainable as it uses bioalcohol and carbon dioxide.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for use of dialkyl carbonate obtained from bioalcohol as component for gas oil.
NOVELTY - System for processing wet organic waste comprises (i) fermentation apparatus for fermenting the wet organic waste by microbial process and (ii) combustion furnace for combusting the fermented material. The fermentation apparatus supplies carbon dioxide produced during fermentation to the combustion furnace. The carbon dioxide in the high temperature exhaust gas evolved during combustion in the combustion furnace is recovered and stabilized.    USE - The system is useful for processing wet organic waste.    ADVANTAGE - The system emits carbon dioxide is utilized for cultivating plant.
NOVELTY - Water is initially allowed to pass through an ion-exchange resin, and then through one of tourmaline and rocks, and then through the other, to obtain a particular type of water (75). The temperature is set to 30 degrees C or more and less than the boiling point of the particular type of water, in a state in which the particular type of water and aluminum (77) are put into the container (60), and the particular type of water is contacted with aluminum within the container. The particular type of water and aluminum are reacted to produce hydrogen.    USE - Manufacture of hydrogen for use as fuel gas in motor vehicles.    ADVANTAGE - The method enables easy and continuous extraction of hydrogen from a particular type of water and aluminum.    DETAILED DESCRIPTION - Water is initially allowed to pass through an ion-exchange resin, and then through one of tourmaline, and rocks containing silicon dioxide consisting of liparite and/or granite (65-76%), and then through the other, to obtain a particular type of water. The temperature in the container is set to 30 degrees C or more and less than the boiling point of the particular type of water, in a state in which the particular type of water and aluminum are put into the container, and the particular type of water is contacted with aluminum within the container. The particular type of water and aluminum are reacted to produce hydrogen. An INDEPENDENT CLAIM is included for hydrogen manufacturing apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the hydrogen generating apparatus.    Container (60)    Lid (61)    Heater (69)    Particular type of water (75)    Aluminum (77)
NOVELTY - Directly converting methane to methanol, comprises: (a) creating an oxygen-activated catalyst by heating a catalyst at a first temperature in an oxidizing environment; and (b) passing a methane-containing gas stream at a second temperature over the oxygen-activated catalyst to directly form methanol; where the first temperature and the second temperature are less than 300 degrees C.    USE - The method is useful for directly converting methane to methanol (claimed).    ADVANTAGE - The method efficiently and effectively converts methane to methanol.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a composition of matter suitable for direct conversion of methane to methanol, comprising an oxygen-activated catalyst with at least one active site, where the active site comprises a mono-( mu -oxo)dicupric core;    (2) a method of creating an oxygen-activated catalyst suitable for direct conversion of methane to methanol, comprising: (a) pre-treating a catalyst by heating the catalyst in a gaseous environment with continuous gas flow at a pre-treatment temperature range of about 370-750 degrees C, where the gaseous environment comprises less than 10 ppm water or less than 3 ppm water; and (b) heating the pre-treated catalyst at a temperature less than 300 degrees C in an oxidizing environment to form the oxygen-activated catalyst; and    (3) a chemical processing plant for direct conversion of methane to methanol comprising: (a) a storage unit comprising methane gas; (b) a storage unit comprising oxygen-activated catalyst, where the oxygen-activated catalyst comprises at least one active site, where the active site comprises a mono-( mu -oxo)dicupric core; and (c) a unit for passing the methane gas over the oxygen-activated catalyst from the respective storage units at a temperature of less than 300 degrees C and an ambient pressure for the direct conversion of the methane gas into the methanol.
NOVELTY - Processing of slightly saponifiable crude oil from plant or animal origin, comprises: (a) degumming of crude oil with the addition of an acid, carrying out partial neutralization of the acid by adding a base and separating the resulting gums and soaps by a mechanical separation process; and (b) further reducing the content of aromatic substances and free fatty acids in the oil by stripping with inert gas or water vapor and/or applying a vacuum.    USE - The method is useful for processing of Jatropha oil (claimed), which is used as a raw material for production of biodiesel by a transesterification process.    ADVANTAGE - The method: is easy; produces the purified oil with high yield and good quality; reduces the thermal load of the oil; includes limited addition of the base; and requires simple equipment.    DETAILED DESCRIPTION - Processing of slightly saponifiable crude oil from plant or animal origin, comprises: (a) degumming of crude oil with the addition of an acid, carrying out partial neutralization of the acid by adding a base and separating the resulting gums and soaps by a mechanical separation process; and (b) further reducing the content of aromatic substances and free fatty acids in the oil by stripping with inert gas or water vapor and/or applying a vacuum. The degumming, partial neutralization with the base and separation of gums are carried out in a first temperature range, and the stripping and/or the vacuum treatment are carried out in a second temperature range. The distance between an upper limit of the first and a lower limit of the second temperature range is at least 100 K, and not greater than 220 K.
NOVELTY - The method involves drying wet fuel in an indirectly heated fluidized bed (6) at pressure larger than 1 mega Pascal, and redensifing cleaned exhaust vapor at a pressure higher than the pressure in the bed. The redensified vapor is supplied to fluidized bed driers (11) for heating such that the vapor is condensed. The vapor condensate is discharged into a preheater (3) such that the fuel is preheated in the preheater. The dried fuel is supplied to a gasification reactor (20) over a pressure conveying and dosing system (13), and the fuel is gasified by an oxidizing agent at a system pressure.    USE - Method for combined drying and gasification of wet fuel e.g. coal, peat, wastes and residues with increased cellulose content and primary and secondary biomasses (all claimed).    ADVANTAGE - The dried fuel is supplied to the gasification reactor over the pressure conveying and dosing system, and the fuel is gasified by the oxidizing agent at the system pressure, thus drying and gasifying the wet fuel at uniform pressure level without using synthetic gas with reduced oxygen content.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic flow diagram of an entrained flow gasification process with an integrated fluidized bed drying process.    Preheater (3)    Indirectly heated fluidized bed (6)    Separator (8)    Fluidized bed driers (11)    Pressure conveying and dosing system (13)    Gasification reactor (20)
NOVELTY - Ignition agent for solid fuels including wood, charcoal and coal for using in stoves, fireplaces and grills, comprises a wax-containing flammable main body (3), where the main body consists of dried straw (1).    USE - The ignition agent is useful for solid fuels including wood, charcoal and coal for using in stoves, fireplaces and grills.    ADVANTAGE - The ignition agent: has simple composition and low production cost; and exhibits improved functions.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing the ignition agent with the wax- or paraffin-containing main body.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the ignition agent in the form of bundled and combined straws of the rice straw in two bundles.    Straw (1)    Bundle (2)    Main body (3)
NOVELTY - This invention relates to a batch continuous production mode of fatty acid methyl ester (biodiesel) transesterification reaction providing at least three or more than three first unit effect tank, second unit effect tank and third unit effect tank to form a standing treatment purification system. The first unit effect tank, the second unit effect tank, and the third unit effect tank of the standing treatment purification system is respectively provided with a reaction mode for a batch of continuously feeding, standing and discharging the reacted product after performing transesterification reaction so that the standing treatment purification system is applied in the process flow of producing fatty acid methyl ester (biodiesel) to effectively stagger the standing procedure of transesterification reaction based on feeding, standing, discharging operation. The production operations that perform the division of labor in multistep alternation at the same time and that may not interfere with each other are formed to fulfill the purpose of continuous production and enhancing the conversion rate due to the prolonged standing time and reducing operation waiting time.
NOVELTY - Hydrogen production involves performing conversion an alcohol to hydrogen by steam reforming in a fixed bed reactor at 723-823K and atmospheric pressure for 4-72 hours. A catalyst of mixed oxides is used in the conversion an alcohol to hydrogen. The mixed oxides have perovskite structure (I).    USE - Method for producing hydrogen (claimed) used in fuel cell such as a polymer electrolyte membrane (PEM) fuel cells.    ADVANTAGE - The method enables to produce hydrogen with reduced emissions of greenhouse gases and air pollution.    DETAILED DESCRIPTION - Hydrogen production involves performing conversion an alcohol to hydrogen by steam reforming in a fixed bed reactor at 723-823K and atmospheric pressure for 4-72 hours. A catalyst of mixed oxides is used in the conversion an alcohol to hydrogen. The mixed oxides have perovskite structure of formula La1-xMxNiO3 (I).    x= 0.0-1.0; and    M=alkaline earth metals or elements of lanthanide group.
NOVELTY - A fuel cell system (100) has modifier (50) for producing fuel gas by steam reforming reaction, fuel cell (70) operating using fuel gas and oxidizing agent gas, combustion chamber (60) for burning off gas of fuel cell and heating modifier, sensor (81) for detecting temperature of modifier directly or indirectly, and control portion (10). Control portion controls feed rate of modification water with respect to raw fuel of modifier. Feed rate of modification water is increased, when detection temperature is changed from positive to negative.    USE - Fuel cell system.    ADVANTAGE - The fuel cell system efficiently controls feed rate of raw fuel and modification water without using detector.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for operating method of fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of fuel cell system. (Drawing includes non-English language text)    Control portion (10)    Modifier (50)    Combustion chamber (60)    Fuel cell (70)    Sensor (81)    Fuel cell system (100)
NOVELTY - A hydrogen storage alloy contains rare earth element containing yttrium (excluding lanthanum), and cobalt, manganese, zinc, iron, lead, copper, tin, silicon and/or boron. The concentration ratio (%) of aluminum and nickel in bulk layer with respect to surface layer of alloy is 0.36-0.84.    USE - Hydrogen storage alloy used for alkaline storage battery used as power supply for hybrid vehicles, pure electric vehicles, etc.    ADVANTAGE - The hydrogen storage alloy provides alkaline storage battery with excellent output characteristics and durability. The penetration of aluminum to positive electrode is suppressed.    DETAILED DESCRIPTION - A hydrogen storage alloy has compositional formula: LaxReyMg1-x-yNin-m-vAlmTv, where Re is chosen from rare earth element containing yttrium (excluding lanthanum), T is cobalt, manganese, zinc, iron, lead, copper, tin, silicon and/or boron, preferably copper or tin, x is 0.17-0.64, n is 3.5-3.8, m+v is 0.1-0.22, and v is 0 or more. The alloy has A5B19 type main structure. The concentration ratio (%) of aluminum and nickel in bulk layer with respect to surface of alloy is 0.36-0.84.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of alkaline storage battery.    Hydrogen storage alloy electrode (11)    Electroconductive core (11a)    Active material layer (11b)    Core exposure portion (11c)    Nickel positive electrode (12)    Separator (13)
NOVELTY - Preparation of methanol comprises heterolytic cleavage of hydrogen by a frustrated Lewis pair comprising a Lewis acid and a Lewis base; and hydrogenation of carbon dioxide with the heterolytically cleaved hydrogen to form methanol.    USE - The frustrated Lewis pair is useful for the production of methanol (claimed). The methanol is useful as a precursor to many useful organic chemicals (e.g. formaldehyde and acetic acid), a substitute for traditional fossil fuels, and in the generation of electricity in fuel cells.    ADVANTAGE - The process: utilizes the abundant carbon dioxide resource available; provides the methanol in a pure form (i.e. without other d by-products); can be operated at relatively low temperatures and pressures; avoids the use of transition metal catalysts; and is specific for the production of methanol (i.e. no other 1C by-products are formed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for methanol obtained by the process.
NOVELTY - A method of analyzing biodiesel content in a fuel sample, involves: mixing a predetermined amount of solvent with a fuel sample including at least one of a biodiesel and other diesel fuel, where the fuel sample is soluble in the solvent; mixing a predetermined amount of water with the fuel sample; analyzing the fuel sample for a change in clarity; and associating the change with a biodiesel content in the fuel sample.    USE - For analyzing biodiesel content in fuel sample (claimed).    ADVANTAGE - The method is simple, accurate, and provides on-site biodiesel concentration quantification test for blended biodiesel and ULSD or other non-ULSD diesel fuels.
NOVELTY - The device has a liquid guiding cover is mounted in the front of the horizontal mixing tank. A central rotating shaft is arranged in the horizontal mixing tank in radial direction. A louver rotating wheel and porous guiding rotating impellers are fixed on the central rotating shaft. The integration sequencing mixing chamber is mounted above the horizontal mixing tank and is connected with the methanol porous annular layer.    USE - Automatic type methanol gasoline mixing and regulating device.    ADVANTAGE - A regulating device which mixes the methanol uniformly in the storage process which enables high precision can be provided.    DESCRIPTION OF DRAWING(S) - The drawing shows the perspective view of automatic type methanol gasoline mixing and regulating device.
NOVELTY - The kettle has a feed port inserted on the kettle cover which is connected with a guide pipe. The kettle cover and the feed port are inserted with a kettle injection port. The injection port is connected with a guide pipe. The kettle cover is connected with the liquid phase platinum resistor temperature measuring meter and full-automatic type monitoring liquid indicator. The sandwich kettle structure is formed with a stirrer which is arranged at the center of the outer portion of the kettle.    USE - Reaction kettle of bio-diesel production.    ADVANTAGE - A reaction kettle having sandwich structure that avoids the phenomenon of liquid hanging and which enables the uniform liquid and that ensures safety can be provided, while improving production efficiency and reducing the labor cost.    DESCRIPTION OF DRAWING(S) - The drawing shows the perspective view of reaction kettle of bio-diesel production.
NOVELTY - Circular marsh gas generator comprises a feed opening (3), a discharge opening (7), a desulfurizer (6), a marsh gas stove (11) and a gas duct, and a fermenting tank (10) buried underground and connected with bottom part and upper part of a fermenter, which is installed on the ground through a pipeline. A submersible pump is installed on lower part of the fermenting tank and its water outlet pipe is connected with a pipeline through a valve, where if the valve is opened and the submersible pump is connected, the fermentation liquor in the fermenting tank and the fermenter forms circular flow.    USE - Used as a circular marsh gas generator.    ADVANTAGE - The marsh gas generator improves the gas generation efficiency and processing efficiency of the fermenting tank, and it has easy cleaning, convenient sewage discharging and high marsh gas generation efficiency, thus it solves the problems of low marsh gas generation efficiency, floating residue incrustation and sewage discharge difficulty of the current water pressure type biomass pool.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the circular marsh gas generator.    Feed opening (3)    Desulfurizer (6)    Discharge opening (7)    Fermenting tank (10)    Marsh gas stove (11)
NOVELTY - Producing short chain carboxylic acids by controllably photocatalytically degrading lignin residues in aqueous solution comprises treating the lignin residues in the presence of a titanium dioxide nanocatalyst with ultraviolet radiation.    USE - The process is useful for the preparation of short chain carbon compounds, where the short chain carboxylic acid comprises a 2-10C linear or branched alkyl or alkenyl group, and the short chain carboxylic acid is formic acid, acetic acid, succinic acid, maleic acid, and/or fumaric acid (all claimed), the succinic acid is a high-value chemical in the bio-based economy, and a precursor for many industrially important chemicals in food, chemical and pharmaceutical industries, including 1,4-butanediol, gamma -butyrolactone, tetrahydofuran and methylpyrrolidone, the maleic acid is hydrogenated to 1,4- butanediol, and a precursor for biodegradable polymers, and acetic acid is useful as feedstock chemical for microbial fuel cell.    ADVANTAGE - The process provides short chain carbon compounds with high purity. The process reduces the hazard of recalcitrant waste stream on the environment; and converts the recalcitrant and toxic organic compounds into chemicals which are of commercial value. The process is eco-friendly and inexpensive    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) an aqueous solution comprising the short-chain fatty acid produced by the process; and    (2) a short-chain fatty acid isolated from the solution.
NOVELTY - Ground-placed solar constant temperature sewage gas generating tank comprises a tank body, an upper semicircle, a lower semicircle, a sealing cover and a solar heat absorbing plate. The tank body is poured into two semicircles by glass plastic steel. The two semicircles are correspondingly provided with fixing tank eaves. The top of the upper semicircle (1) is provided with a feed port sealed by the sealing cover (3). The sealing cover is provided with a gas outlet (2). The solar heat absorbing plate (4) is installed on the outer layer of the upper semicircle.    USE - Used as a ground-placed solar constant temperature sewage gas generating tank.    ADVANTAGE - The device has simple structure, easy construction, low cost, stable gas and high heating value and produces environmentally-friendly energy source.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of the ground-placed solar constant temperature sewage gas generating tank.    Upper semicircle (1)    Gas outlet (3) Sealing cover (2)    Solar heat absorbing plate (4)
NOVELTY - An energy recyclable household garbage disposal machine comprises solid combustible garbage disposer, casing, solid food garbage disposer, motor, and rotating component provided inside two disposers and coaxially linked with motor. The gas processing system is installed under garbage disposer and is connected with combustible garbage disposer pipe. An electric device control box is connected with solid combustible garbage disposer, solid food garbage disposer, motor, and gas processing system by conductive wires. The electric device control box detect safety and control actions of components.    USE - An energy recyclable household garbage disposal machine.    ADVANTAGE - The machine is capable of changing solid combustible substance in household garbage into combustible gas for recycling and grinding food garbage to discharge through discharge holes.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of energy recyclable household garbage disposal machine.
NOVELTY - Torrefied biomass material comprises at least 1 wt.% of bio-liquid.    USE - The torrefied biomass material is useful as: an oil absorbent; an activated carbon for water filtration; a soil modifier; a chemical or mercury absorbent; an industrial thermal generation material; torrefied fire logs or wood pellets; or wood-based charcoal (all claimed).    ADVANTAGE - The torrefied biomass material has an enhanced mass energy density of at least 10000 British thermal units (btu)/lb, preferably 12500-14000 btu/lb.
NOVELTY - Manufacturing apparatus of biomass fuel carries out grinding of waste material including wooden crushed material, chaff, dry water plant, and agricultural waste, and produces refuse-derived fuel.    USE - Apparatus is used for manufacturing biomass fuel (claimed).    ADVANTAGE - The biomass solid fuel is easily and economically manufactured.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of biomass fuel, which involves processing livestock feed chosen from waste rice, waste soybean, agricultural waste and compost, crushing, and producing fuel accompanying generation of light and heat, and germination suppression of weeds.
NOVELTY - Process (A1) for the preparation of polymorphic form I of clopidogrel hydrogen sulfate comprises: (a) dissolving clopidogrel base in an organic solvent comprising ether and/or ester; (b) mixing the resulting solution with sulfuric acid and alcoholic solvent and; (c) isolating clopidogrel hydrogen sulfate form I.    USE - The processes are useful for the preparation of polymorphic form I of clopidogrel hydrogen sulfate (claimed).    ADVANTAGE - The processes: are commercially viable, economical and environment friendly; are free from the contamination of form II or other existing polymorphic forms of clopidogrel hydrogen sulfate; provide free flowing, non-sticky and easily filterable solid on commercial scale, to improve the isolation of clopidogrel hydrogen sulfate form I; and provide clopidogrel hydrogen sulfate form I in high yield and high polymorphic purity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for process (A2) for the preparation of polymorphic form I of clopidogrel hydrogen sulfate comprises: (d) dissolving clopidogrel hydrogen sulfate in an alcoholic solvent; (e) adding anti-solvent comprising ether and/or ester; and (f) isolating clopidogrel hydrogen sulfate form I.
NOVELTY - Phosphate compound containing tetravalent metallic element and alkali metal is new.    USE - As inorganic proton conductor (claimed) useful in fuel cells including electrodes and electrolyte; and in electrochemical devices e.g. hydrogen generators and exhaust gas purifying apparatuses.    ADVANTAGE - The inorganic proton conductor (I) exhibits excellent proton conductivity.    DETAILED DESCRIPTION - Phosphate compound containing tetravalent metallic element and alkali metal having formula (M)1-a(N1)aP2O7 (I) is new.    M=a tetravalent metallic element;    N1=alkali metal;and    a=0.01-0.7.    An INDEPENDENT CLAIM is included for preparing (I) involving adding a solvent to a mixture of tetravalent metallic element precursor, an alkali metal precursor and phosphoric acid to give a composition; stirring the composition; and heat treating the stirred composition to form (I).
NOVELTY - A sewage processing apparatus comprises crushing device for crushing solids in sewage, cross flow filter device for filtering crushed solid sewage, UV sterilizing device for sterilizing filtered liquid and control cabinet for setting and controlling other devices. The deposition outlet and supernatant outlet are formed on crushing device input end. The first output end is used for outputting filtered liquid and second output end is used for outputting retained substances. The residual liquids are arranged on cross flow filter device.    USE - Sewage processing apparatus. The processed sewage can be directly used in industrial applications of culturing alga.    ADVANTAGE - The apparatus has tight structure and high processing efficiency and has convenient management maintenance.    DETAILED DESCRIPTION - Sewage processing apparatus comprises crushing device for crushing solids in sewage, cross flow filter device for filtering crushed solid sewage, UV sterilizing device for sterilizing filtered liquid and control cabinet for setting and controlling other devices. The deposition outlet and supernatant outlet are formed on crushing device input end. The first output end is used for outputting filtered liquid and second output end is used for outputting retained substances. The residual liquids are arranged on cross flow filter device. The input end is connected to supernatant outlet of crushing device through pipeline. The first output end is connected with UV sterilizing device.
NOVELTY - Anaerobic fermentation method for acidulating and separating cow dung, involves separating fibers in cow dung which are acidulated at middle temperature and fermented using liquid raw materials by spiral squeeze solid-liquid separating machine. The acidification process is performed for 3-4 days by heating cow dung and water, where content of the total solid is 10-12% at 33-37 degrees C, separating acidulated liquid by solid-liquid separating machine, where the total solid content of the separated solid materials is 38-45%.    USE - The method is useful for fermenting and separating cow dung for producing methane gas and fertilizer (claimed).    ADVANTAGE - The method enables improved production of methane gas.    DETAILED DESCRIPTION - Anaerobic fermentation method for acidulating and separating cow dung, involves separating fibers in cow dung which are acidulated at middle temperature and fermented using liquid raw materials by spiral squeeze solid-liquid separating machine. The acidification process is performed for 3-4 days by heating cow dung and water, where content of the total solid is 10-12% at 33-37 degrees C, separating acidulated liquid by solid-liquid separating machine, where the total solid content of the separated solid materials is 38-45%. The productions of organic compound fertilizer and microbial organic fertilizer are performed using the acidulated liquid. The solid content of the separated liquid 6.6-7.4%. The separated liquid is used for performing anaerobic fermentation of methane at 33-37 degrees C, where 1/7 volume (30%) of methane is added to methane producing reactor everyday. The water is added to the reactor for 7 days. The liquid discharged from the methane producing reactor is fermented for one day, hence the productive methane in the liquid can be substantially fermented and the yield of the methane in sewage gas reaches up to 65-75%.
NOVELTY - The gas water sealing device includes pulling rod with a bottom end connected to the top of the trumpet shaped cover. The pulling rod passes through the through hole on the top of the external shell. A second trumpet shaped cover is connected to the pulling rod and covered on the top end of the pipeline of the second water container. The bottom end of the second trumpet shaped cover is arranged below the water level in the second water container. The outlet end of the gas pipeline is arranged in a space surrounded by the primary water container and the external shell.    USE - Biomass flammable gas water sealing device for biomass gasifying reaction system (claimed).    ADVANTAGE - An explosion and leakage of the biomass is prevented from being easily generated as a result of poor stability of gas pressure and poor stability of gas outlet, making the biomass flammable gas water sealing device most effective and safe to ensure reliable operation of the biomass gasifying reaction system.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biomass gasifying reaction system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass flammable gas water sealing device.
NOVELTY - The furnace has a furnace cover (3) mounted on a top part of a furnace body (7), and a water seal ring (17) mounted on the cover. An air inlet tube (6) is connected with a blower fan (8), and an air homogenizing hat (11) is mounted on an end of the tube. An ash outlet (9) is mounted on one side of bottom of the body, and the tube is connected with an oxygen supply tube (5) and a hearth chamber (4). A filter hat (15) is mounted on an outer end of a splitting converter (22), and a nickel base tablet (14) and an active alumina molecular sieve (13) are orderly mounted in the furnace.    USE - Nickel base catalyst biomass gasification furnace.    ADVANTAGE - The device can split the waste gas, which cannot be directly combusted into combustible gas, and can increase the combustion efficiency. The device reduces the energy consumption, and avoids generation of the tar. The device has compact structure, simple operation and low manufacturing cost. The device occupies small area, and has long lasting effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial sectional view of a nickel base catalyst biomass gasification furnace.    Furnace cover (3)    Hearth chamber (4)    Oxygen supply tube (5)    Air inlet tube (6)    Furnace body (7)    Blower fan (8)    Ash outlet (9)    Air homogenizing hat (11)    Active alumina molecular sieve (13)    Nickel base tablet (14)    Filter hat (15)    Water seal ring (17)    Splitting converter (22)
NOVELTY - Deoxygenating feedstock comprising materials of biological origin, comprises contacting the feedstock with carbon monoxide in the presence of a catalyst and water under alkaline conditions at 150-350 degrees C and under a pressure of 0.1-150 bar to produce hydrocarbons. The catalyst comprises a metal which is ruthenium, manganese, rhodium, rhenium, osmium, iridium, molybdenum, copper, zinc, palladium, platinum or cobalt.    USE - The method is useful for: deoxygenating feedstock comprising materials of biological origin, where the feedstock is fats and oils originating from plants, animals, fish or insects, fats and oils obtained from microbiological processes utilizing algae or microbes, fats and oils contained in plants bred by means of gene manipulation, recycled fats of the food industry, and/or biomass originating from Fischer-Tropsch products and fractions, or carboxylic acids, esters of carboxylic acids, alcohols, aldehydes and/or ethers of 3-70C (preferably 3-40C); and producing hydrocarbons (preferably paraffinic hydrocarbons) which are useful as diesel, gas, gasoline, aviation fuel and solvents (all claimed).    ADVANTAGE - The method produces high quality biofuels.
NOVELTY - Organo metal-oxo complex (I), is new.    USE - (I) is useful for generating hydrogen gas from water (claimed).    ADVANTAGE - (I) has high catalytic activity and long-term stability. (I) is inexpensive, and earth-abundant elements.    DETAILED DESCRIPTION - Organo metal-oxo complex of formula (((PY)5W12)MO)2+) (I), is new.    PY5W12 = (NC5XY1Z)(NC5H4)4C2W12;    M = high oxidation state metal; and    W1, X, Y1, Z = H, R, halide, CF3 or SiR3;    R = alkyl or aryl group; and    R3 = not defined.    INDEPENDENT CLAIMS are included for:    (1) generating hydrogen gas from water, comprising dissolving (I) in a water bath containing both an anode and a cathode and an electrolyte, applying a negative potential to the cathode, and (I) picking up electrons at the negative electrode, and then reacting with water to release hydrogen; and    (2) an organo metal salt dissolvable in water, where the salt includes a pyridine metal-oxo complex of formula (A).    A2- = Cl-, I-, PF6- or CF3SO3-.
NOVELTY - The evaporator has main container (0100) in which cylindrical heat generating element (0200) is arranged inside. The liquid diffused layer (0300) and liquid evaporation layer (0400) cover top and side portions of heat generating element. A gas supply line (0500) introduces carrier gas inside container. A liquid supply pipe (0600) supplies liquid to liquid diffused layer from main container upper portion. A mixture-of-gas discharge port (0700) discharges mixture of gas of carrier gas and emission of liquid evaporated by liquid evaporation layer to container exterior.    USE - Evaporator for fuel cell.    ADVANTAGE - Since the heat generating element is arranged inside main container, the liquid in gas can be evaporated efficiently by evaporating a liquid from the liquid evaporation layer which covers heat generating element. The liquefying and adhering to the outer periphery of liquid supply pipe can be prevented as emission condenses by making into a double-pipe structure the pipe which supplies gas and liquid to the inside of main container.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the evaporator.    Main container (0100)    Heat generating element (0200)    Liquid diffused layer (0300)    Liquid evaporation layer (0400)    Gas supply line (0500)    Liquid supply pipe (0600)    Mixture-of-gas discharge port (0700)
NOVELTY - The sensor has a spacer (4) that supports out lead (5a-5c), while penetrating multiple electrode pins to the protrusion side (11b) of a mount base. A pressing structure covers the whole surface of the side supporting each out lead of spacer. A pressing structure locking component (12b) presses and latches the pressing structure to the spacer side.    USE - Gas sensor e.g. contact combustion type gas sensor used in boiler apparatus, for detecting leakage of poisonous gas, exhaust gas and air pollutant. Can also be used in semiconductor type gas sensor for detecting leakage of combustible gas such as hydrogen gas, methane or carbon monoxide gas from fuel cell electric vehicle.    ADVANTAGE - Since out lead is supported firmly by spacer, stress in out lead can be avoided while preventing the damage of out lead and connection portion of the electrode pin. Since the pressing structure increases/decreases the surface area for external air, thermal radiation effect can be improved while providing reliable gas sensor.    DESCRIPTION OF DRAWING(S) - The drawings show the perspective view of the gas sensor.    Holder (1)    Spacer (4)    Out leads (5a-5c)    Protrusion side of mount base (11b)    Pressing structure locking component (12b)
NOVELTY - A hydrogen storage alloy electrode is a metal hydride electrode having a conductive substrate filled with hydrogen storage alloy powder, a water-soluble binder, fluorine oil and a surfactant. The surfactant is polyoxyethylene alkyl ether having clouding point of 45 degrees C or more.    USE - Hydrogen storage alloy electrode is used for alkaline storage battery used as power supply for portable equipment and hybrid electric vehicles.    ADVANTAGE - The hydrogen storage alloy electrode has excellent oxidation resistance, and provides alkaline storage battery having excellent cycle characteristics.
NOVELTY - A hydrogenation catalyst contains modified inorganic oxide particles obtained by supporting nickel oxide or chromium oxide and/or copper chromite on surface of inorganic oxide particles. The modified inorganic oxide particles have specific surface area of 200-300 m2/g and average particle diameter of 10-50 mu m.    USE - Catalyst is used for hydrogenation of hydrocarbon e.g. olefin hydrocarbon, aromatic compound e.g. toluene and benzene, and petroleum resin.    ADVANTAGE - The hydrogenation catalyst having excellent sulfur-proof property is manufactured economically. Generation of waste water and waste gas is prevented during manufacture of catalyst.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of hydrogenation catalyst, which involves pulverizing slurry containing inorganic oxide carrier, nickel-containing compound and chromium oxide and/or copper chromite in liquid phase, adjusting pH of slurry, aging at 40-95 degrees C, spray-drying slurry and granulating.
NOVELTY - Storing an electrical energy, comprises: splitting water in an electrolyzer (E) with the electrical energy; passing the obtained hydrogen in a storage container (S), and removing hydrogen from the storage container when needed; and supplying hydrogen as a fuel (7) to a fuel cell (B) for generating the electrical energy. A hydrogen source is supplied as a waste heat obtained during the method to meet the existing heat requirement, and a hydrogen-containing insert (5) is implemented in an endothermic reaction under the production of hydrogen.    USE - The method is useful for storing an electrical energy.    ADVANTAGE - The method maintains balance between the power supply and the power requirement, and thus improves storage of the electrical energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an apparatus for storing the electrical energy, comprising: the electrolyzer, in which hydrogen is obtained from water with the electrical energy; the storage container, in which hydrogen recovered from the electrolyzer is temporarily stored; the fuel cell; the hydrogen source, in which the hydrogen-containing insert is implemented; and a device, through which the hydrogen source is supplied as the waste heat obtained during the operation of the apparatus.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the apparatus.    Hydrogen-containing insert (5)    Fuel (7)    Fuel cell (B)    Electrolyzer (E)    Storage container (S)
NOVELTY - An odorization agent contains mercaptan and saturated aliphatic hydrocarbon as active ingredients.    USE - Odorization agent is used for fuel e.g. town gas, liquefied natural gas, industrial gas, liquefied petroleum gas, industrial gas, dimethyl ether, hydrogen gas, fuel cell gas, gasoline, naphtha and kerosene (all claimed).    ADVANTAGE - The odorization agent has excellent storage stability, chemical stability and handleability, and reduced freezing point and sulfur content. Generation of nitrous acid gas during combustion is reduced.
NOVELTY - The combined system has a substitute fuel that heats a fluidized bed reactor system which converts processed biomass to a synthesis gas after formality of the sustained energy bill. The synthesis gas is tarless till 900 degree Celsius.    USE - Combined system for energy generation through thermal waste treatment for generation of process energy for the heating of a fluidized bed reactor for bio-hydrogen production as fuel input for the comprehensive operation of fuel cell.    ADVANTAGE - The combined system has a substitute fuel that heats a fluidized bed reactor system which converts processed biomass to a synthesis gas after formality of the sustained energy bill, and hence ensures improved and cost-effective energy generation.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of production of synthesis gas. (Drawing includes non-English language text).
NOVELTY - The method involves conveying the wood chip using roller (13) through conveyor belt (14), to lower portion of the wood chip storage section (10). The metal contained in the conveyed wood chip is removed using magnetic separator (16) and the wood chip is stored in the wood chip repository (30). The wood chip having constant size after performing metal extracting process is selected using standard wood chip separator (18).    USE - Method of transferring biomass fuel e.g. refuse-derived fuel (RDF) to biomass fuel bunker.    ADVANTAGE - The conveying amount of the wood chip can be controlled and standard wood chip can be selected easily.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the process for transferring biomass fuel.    Wood chip storage section (10)    Roller (13)    Conveyor belt (14)    Magnetic separator (16)    Standard wood chip separator (18)    Wood chip repository (30)
NOVELTY - A discharge tube discharges air to incinerator (3) at top of RDF production chamber (4) with waste transfer screw conveyor (43) injected with waste (T) containing food waste and pulverized waste. Waste is passed from exit of waste feeding hopper (42) connected to inlet end (42a) of waste transfer screw conveyor. The RDF (F) is injected through the RDF input hopper (1) to reproduce RDF through pyrolysis process for burning the RDF. A burner (7) is installed between air discharger tube and transfer screw conveyor to burn the gas heated with air inside incinerator.    USE - Apparatus for reproducing refuse derived fuel (RDF) by using food waste and combustion waste.    ADVANTAGE - The burning process of solid fuel processed from the domestic waste can be performed effectively with reforming, so that the reproduction process of RDF through pyrolysis can be performed effectively at reduced fuel cost. The food waste and combustible waste can be heated effectively with the heat of combustion of the utilized gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the structure of RDF reproduction apparatus.    RDF input hopper (1)    Incinerator (3)    RDF production chamber (4)    Burner (7)    Waste feeding hopper (42)    Inlet end of waste feeding hopper (42a)    Waste transfer screw conveyor (43)    RDF (F)    Waste (T)
NOVELTY - Method of decomposing unsaturated aliphatic aldehyde, involves using aldehyde dehydrogenase derived from microorganism.    USE - The method is useful for decomposing unsaturated aliphatic aldehyde, preferably acrolein (claimed) which is used in chemical industry as detection agent, disinfectant, coating material, textile finishing agent and refrigerating agent.    ADVANTAGE - The method reduces toxicity of acrolein hence prevents plants, environment and animals from disease e.g. necrosis of hepatocytes caused by acrolein.
NOVELTY - An alloy consists of solidified alloy obtained by heating aluminum, metal (A) and low melting metal having melting point of 230 degrees C or less to the temperature which is higher than the temperature of aluminum, obtaining melted alloy, contacting obtained melted alloy with water and cooling. The metal (A) is zinc, magnesium, and/or silicon. The content of metal (A) is 0.1-10 weight% with respect to content of aluminum. The content of low melting metal is 0.1-50 weight% with respect to content of aluminum.    USE - Alloy is used for generating hydrogen (claimed) used for internal combustion engine e.g. hydrogen fueled engine.    ADVANTAGE - The alloy efficiently and safely generates hydrogen by simple method.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for generation method of hydrogen.
NOVELTY - The device has a left-side mixing tank (4) and a right-side mixing tank (5) which are arranged between the alkaline methanol preparing tanks (2) and a pipeline reactor (3). The two left and right mixing tanks are in parallel connection and the outlet ends are connected with a conveying pump (6) and pipeline reactor. The left and right mixing tanks are connected with the alkaline methanol preparing tanks.    USE - Transesterification device for preparing biodiesel.    ADVANTAGE - The device has an independently arranged mixing tank, so that the pre-processed waste grease, methanol and alkaline catalyst are completely mixed and conveyed to pipeline reactor through pump. Hence the pipeline reactor is difficult to block.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic circuit diagram of transesterification device.    Alkaline methanol preparing tanks (2)    Pipeline reactor (3)    Left-side mixing tank (4)    Right-side mixing tank (5)    Conveying pump (6)
NOVELTY - The device has a container into which waste food material is injected. The injected food material is heated by a heating unit which is connected to the container, so that the moisture content is removed. The food material is compressed and cut. The cut food material is cooled and condensed by the refrigeration unit, such that carbide is discharged.    USE - Device for generating carbide from waste food material.    ADVANTAGE - The moisture content can be removed easily from the food material without contamination of the food material and carbide generation efficiency can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the carbide manufacturing device.    Drying unit (100)    Compression unit (200)    Transfer screw (210)    Housing (230)    Coking chamber (310)
NOVELTY - A courtyard device of seesaw type for composting organic garbage, comprises a primary fermenting chamber set with a material inlet on the upper part and a second fermenting chamber which is a barrel shape with an arc bottom; where the two lateral sides are equipped with ventilating holes and the bottom is equipped with a pulling and pushing plate equipped with a liquid outlet; one lateral side of the bottom is set with a material outlet and the ventilating hole; and the seesaw opposite to an opening on the bottom of the primary fermenting chamber is correspondingly equipped with the opening.    USE - The courtyard device of seesaw type is useful for composting organic garbage (claimed).    ADVANTAGE - The courtyard device can achieve fast fermentation of domestic and agricultural garbage into organic fertilizer.    DETAILED DESCRIPTION - A courtyard device of seesaw type for composting organic garbage, comprises a primary fermenting chamber set with a material inlet on the upper part and a second fermenting chamber which is a barrel shape with an arc bottom; where the two lateral sides are equipped with ventilating holes and the bottom is equipped with a pulling and pushing plate equipped with a liquid outlet; one lateral side of the bottom is set with a material outlet and the ventilating hole; the primary fermenting chamber is fixed upon the middle part of a seesaw, and the second fermenting chamber is fixed under the middle part of the seesaw; the seesaw opposite to an opening on the bottom of the primary fermenting chamber is correspondingly equipped with the opening; and the primary fermenting chamber is connected with the secondary fermenting chamber through the opening of the seesaw.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the courtyard device of seesaw type for composting organic garbage.
NOVELTY - A transfer slide machine of chicken manure turning device, comprises a bracket (1) and two parallel sliding rails (3) for supporting a chicken manure turning device; where the sliding rails (3) are fixed to the ends of two parallel rails for supporting the chicken manure turning device; the bottom of the bracket (1) is equipped with a roller (2) that is matched with the two sliding rails (3); and the bracket (1) is equipped with two parallel guide rails (4) having the space that is the same as the space of the rollers (2).    USE - The transfer slide machine of chicken manure turning device is useful for industrial and commercial applications.    ADVANTAGE - The transfer slide machine of chicken manure turning device saves the equipment investment and reduces the production cost.    DETAILED DESCRIPTION - A transfer slide machine of chicken manure turning device, comprises a bracket (1) and two parallel sliding rails (3) for supporting a chicken manure turning device; where the sliding rails (3) are fixed to the ends of two parallel rails for supporting the chicken manure turning device; the bottom of the bracket (1) is equipped with a roller (2) that is matched with the two sliding rails (3), where the bracket (1) can move horizontally along the sliding rails (3); and the bracket (1) is equipped with two parallel guide rails (4) having the space that is the same as the space of the rollers (2), where the chicken manure turning device can move to the bracket (1).    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the transfer slide machine of chicken manure turning device.    Bracket (1)    Roller (2)    Sliding rails (3)    Guide rails (4)
NOVELTY - A methane flower and tree bottle for the urban and rural greening, comprises a bottle cover, a funnel bottle, and a water storing bottle which are in sequence connected from top to bottom; where the methane flower and tree bottle is a monomer methane flower and tree bottle.    USE - The methane flower and tree bottle is useful for the urban and rural greening (claimed).    ADVANTAGE - The methane flower and tree bottle can greatly extend the period of watering and fertilizing of the flower vase. Moreover, the other good growing conditions like penetrating irrigation can be supplied by bottle; thus, it has economic and social benefits.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the methane flower and tree bottle for the urban and rural greening.
NOVELTY - The furnace has a water jacket arranged in a furnace wall of a round drum-shaped hearth. A water inlet pipe and a water outlet pipe connected with the water jacket and an external heat diffuser are arranged on a furnace body. An inner wall of the hearth around a combustor is provided with a smoke backflow pipe. Pipe ports of the smoke backflow pipe are arranged opposite to a smoke vent, which is provided with a filter screen. A lower part of the round drum-shaped hearth is provided with an ash outlet. An upper part of the round drum-shaped hearth is provided with a feed port.    USE - Furnace i.e. direct-combustion gasification furnace, for gasifying biomass and cooking and heating application.    ADVANTAGE - The furnace has excellent combustion effect, high efficiency, and energy-saving and environment-friendly functions. The furnace provides high temperature of the hearth. The fire power can be regulated and controlled effectively. The furnace can be applied in cooking, heating and supplying hot water. The furnace can fully utilize waste heat of the smoke.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a furnace.
NOVELTY - The furnace has an ash outlet (1) arranged under a burning region (2). An outer layer of an upper part of a fuel barrel is connected with a pyrolysis furnace head. A back part of the fuel barrel is provided with a water tank that is provided with a water jacket having a heat exchanger. An upper part of the water jacket is equipped with a water tank water outlet, while lower part of the water jacket is equipped with a water tank water inlet. Pearl sand (4) is filled between annular heat exchange tubes (5).    USE - Tar-free straw gas heating furnace.    ADVANTAGE - The furnace effective improves heat utilization rate, thus meeting warming demands of users.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a tar-free straw gas heating furnace.    Ash outlet (1)    Burning region (2)    Pearl sand (4)    Annular heat exchange tubes (5)    Blanking device (7)
NOVELTY - A traditional Chinese medicinal composition comprises (pts.wt.) Astragalus root (100-300), capillary Artemisia (200-400), honeysuckle (100-300), and rhubarb (100-300). The composition is prepared by crushing the materials and passing through 60-mesh sieve; and then mixing (pts.wt.) bile acid (10-30), taurine (10-30) and starch (200-500) with the crushed and screened materials, and uniformly mixing them.    USE - Traditional Chinese medicinal composition used for preventing and treating grass carp diseases (claimed).    ADVANTAGE - The composition has reasonable formulation and simple preparation, and is safe and environmentally friendly.
NOVELTY - Disposal of rural waste by biological microbial inoculum for compost manufacturing comprises crushing biological microbial inoculum into waste of 2-3 cm; blending and piling at 1:5 weight ratio; adjusting the water content to 52-57% and the pH to 6.8-7.2; fermenting while adjusting carbon/nitrogen ratio at 30:1; fermenting and raising temperature; overturning for the first time; overturning once in each day; raising temperature to more than 45 degrees C; keep overturning for 3-6 days for 3-4 times in each day, where total fermentation time is 10-30 days; and obtaining compost.    USE - Disposal of rural waste by biological microbial inoculum for compost manufacturing (claimed).
NOVELTY - Regenerative environment-friendly industrial coal is produced by uniformly stirring 30-40-mesh regenerative household garbage (60-100 wt.%) and 35-45-mesh high-performance optimized material (35-80 wt.%) to obtain combustible base material (95-180 wt.%); and mixing with transforming agent (5-20 wt.%) to obtain industrial coal (100-200 wt.%).    USE - Regenerative industrial coal used for power generation and industrial application.    ADVANTAGE - Original coal is saved to 60-80%. Harmful substance and gas are reduced to 60-80%. Use ratio of industrial garbage and building waste is improved to 90-99%. Original coal resource is protected, utilization rate of coal is improved, and living environment is protected. Self heat quantity (1800-3000 kcal) of garbage is improved to industrial coal standard (4500-6000 kcal).
NOVELTY - The method involves sorting collected kitchen trash according to organic and inorganic matters. The separated organic matters are crushed and trash particle mixture is obtained. A fermenting agent is added to the crushed trash particle mixture for obtaining fermented product. A grease substance is separated in fermentation solution and dry substance is separated from wet substance in fermented product. Solid and liquid organic matters are obtained and prepared to produce a respective solid fertilizer and liquid fertilizer.    USE - Kitchen trash treatment method used for producing fertilizer.    ADVANTAGE - Since the method can use the nutrient substance, the more environment-friendly fertilizer can be produced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for kitchen trash treatment system.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram explaining the process for kitchen trash treatment. (Drawing includes non-English language text)
NOVELTY - Compound fertilizer comprises (in %): brewing residue, nitrogen, phosphorus pentoxide, potassium oxide and trace element. The fertilizer is obtained by separating solid and liquid using horizontal spiral centrifuge, drying solid waste residue, adding nutritional element to the dried solid waste powder and granulating the residue with the nutritional element, airing the mixture, and packaging the obtained product.    USE - As compound fertilizer.    ADVANTAGE - The fertilizer has excellent applicability and is environmentally-friendly.    DETAILED DESCRIPTION - Compound fertilizer comprises (in %): brewing residue (60-70), nitrogen (10-20), phosphorus pentoxide (10-20), potassium oxide (5-10) and trace element (0.1-1.5). The fertilizer is obtained by separating solid and liquid using horizontal spiral centrifuge until the water content in the brewing residue is reduced from 95-98% to 50-70%, drying solid waste residue to 50-70%, and further drying the solid residue using rotary cylinder dryer until the water content is reduced 50-70% to 10% to obtain the solid powdered waste residue, adding nutritional element to the dried solid waste powder having 10% of water content and 50-70% of brewing residue based on different soils and different seasons in different areas of our country to obtain the organic compound fertilizer for different areas and granulating the residue with the nutritional element, airing the mixture, and packaging the obtained product based on the different requirement of the user, such as 5 kg per bag, 10 kg per bag, 25 kg per bag and 50 kg per bag. The nutritional element is chosen from nitrogen, phosphorus pentoxide, potassium oxide, and one or more of calcium, magnesium, sulfur, iron and zinc.
NOVELTY - Special fertilizer comprises (in %mass): nitrogen (12.5), phosphorus (6), potassium (10) and microbial organic fertilizer (20).    USE - The special fertilizer is useful for controlling insect pest and reducing plant diseases.    ADVANTAGE - The fertilizer saves labor cost, improves soil fertility, increases yield of rice crops and content of organic substance, and implements sustainable development of rice field ecosystem.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the above-cited fertilizer, which involves crushing the raw materials, mixing the raw materials uniformly, and pelletizing the mixture using a disc.
NOVELTY - Special biological nitrogen-fixing fertilizer for non-glutinous rice.    USE - The special biological nitrogen-fixing fertilizer is useful for improving growth, blooming, maturity and photosynthesis of non-glutinous rice (claimed).    ADVANTAGE - The fertilizer provides nitrogen and potassium for growth of the non-glutinous rice and improves beneficial microorganism, improves the action of the nitrogen-fixing bacteria for long period of time, promotes metabolism of the non-glutinous rice and increases yield of the non-glutinous rice. The fertilizer is environmentally-friendly and can be obtained simply and cost-effectively.
NOVELTY - The device has a water grease pre-treating device (3) which is connected a micro-algae culturing device (1) and a drier (4). A methanol storage tank (12) is arranged between an esterification reaction kettle (5) and a methanol distillatory (7). A micro-algae high-speed centrifugal separator (2), a glycerin separator (8) and a water washing tower (9) are connected with the micro-algae culturing device by a pipe.    USE - Device for producing bio diesel from waste grease and engineering micro-algae.    ADVANTAGE - The culturing cost of the micro-algae can be reduced, pollution during production of diesel can be avoided and utilization efficiency of grease contained in micro-algae can be enhanced.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the device for producing bio diesel from waste grease and engineering micro-algae. (Drawing includes non-English language text)    Micro-algae culturing device (1)    Micro-algae high-speed centrifugal separator (2)    Water grease pre-treating device (3)    Drier (4)    Esterification reaction kettle (5)    Methanol distillatory (7)    Glycerin separator (8)    Water washing tower (9)    Methanol storage tank (12)
NOVELTY - The straw extrusion pelletizer has a feed inlet that is mounted on the protecting cylinder and the granulator comprises a metal cylinder, an extrusion wheel, a pressure shaft and a discharging mould disc. The upper port of the material cylinder is connected with the bottom of the protecting cylinder. The discharging mould disc is installed on the lower port of the material cylinder and the extrusion wheel corresponds to the discharging mould disc.    USE - Walking type straw extrusion pelletizer used in mechanical applications.    ADVANTAGE - The walking type straw extrusion pelletizer can directly palletize the straw in the field to become the plant fuel, so that straw treatment problem is effectively avoided by protecting the environment.    DESCRIPTION OF DRAWING(S) - The drawing shows the perspective view of the walking type straw extrusion pelletizer.
NOVELTY - The reactor has a riser (10) which is located in a down comer (11). A feeding hole (5) and catalyst inlet (6) are installed on upper end of down comer. A light-phase liquid level meter (12.2) and methyl ester outlet (12.3), glycerol discharging hole (12.6) and heavy-phase liquid level meter (12.5) are located on upper and lower ends of tank (12.1) respectively. A cleaning outlet (12.7) is installed at bottom of tank. The height-diameter ratio of down comer is 10.7 and diameter ratio of riser and down comer is 0.60.    USE - Air-lifting bio-diesel ester exchange reactor.    ADVANTAGE - The reaction speed during the production of bio-diesel is improved, the material conversion rate and yield are improved, and the cost is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the air-lifting bio-diesel ester exchange reactor.    Feeding hole (5)    Catalyst inlet (6)    Riser (10)    Down comer (11)    Tank (12.1)    Light-phase liquid level meter (12.2)    Methyl ester outlet (12.3)    Heavy-phase liquid level meter (12.5)    Glycerol discharging hole (12.6)    Cleaning outlet (12.7)
NOVELTY - The cell has a reactor that includes outer glass cylinder (5), inner porous plastic cylinder (6), and titanium cathode cylinder (7) coaxially distributed. A bottom end of glass cylinder is provided with water inlet (17), and upper end provided with water outlet (1) and connected to gas collecting bag (10). The graphite materials are filled between glass cylinder and plastic cylinder. A positive pole of power supply (12) is directly inserted into graphite particles via titanium line, while negative pole is connected to cathode cylinder.    USE - Electrolytic cell for preparing hydrogen.    ADVANTAGE - The manufacturing cost of the system is reduced. The production rate of the hydrogen is fast. The electrode is provided with long service life.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the electrolytic cell.    Water outlet (1)    Outer glass cylinder (5)    Inner porous plastic cylinder (6)    Titanium cathode cylinder (7)    Gas collecting bag (10)    Power supply (12)    Water inlet (17)
NOVELTY - Thermophilic fermentation process for treating municipal sludge, involves removing impurities from municipal sludge (total solid content is 15 plus minus 2%), adding water to adjust concentration of total solid to 4-8%, processing the sludge in pre-treatment tank, pyrohydrolysing sludge with the industrial waste heat of 102-105 degrees C for 30-60 minutes, cooling the material to 50 degrees C, subjecting the sludge to anaerobic fermentation tank and fermenting at 50-52 degrees C for 7-14 days, collecting biogas containing 60-80% of methane and subjecting the biogas to disulfite treatment.    USE - The thermophilic fermentation process is useful for treating municipal sludge. The municipal sludge is sedimentary sludge in the septic tank of the town draining system (claimed).    ADVANTAGE - The method is environmentally-friendly, simple and economical and yields biogas with high content of methane.
NOVELTY - The bath has an oxygen cavity (4) and a hydrogen cavity (5) that are installed and separated by a selection membrane (6). The membrane allows a hydrogen ion to pass through and hydroxyl ion and gas molecular having large diameter not to pass through. An inlet of oxygen cavity is connected with a circulation boost pump (8) and an outlet is connected with a reaction valve (7). A hydrogen cavity is directly connected with circulation pipeline (1). A positive electrode (2) is installed inside oxygen cavity and a negative electrode (3) is installed inside hydrogen cavity.    USE - Electrolysis bath with membrane technology.    ADVANTAGE - The water is electrolyzed effectively by using electrolysis bath with membrane technology, so as to obtain the hydrogen and oxygen. Moreover the provided bath has high safety and can be operated under very low electrolysis voltage.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the electrolysis bath with membrane technology.    Circulation pipeline (1)    Positive electrode (2)    Negative electrode (3)    Oxygen cavity (4)    Hydrogen cavity (5)    Selection membrane (6)    Reaction valve (7)    Circulation boost pump (8)
NOVELTY - The device has a nitrogen gas expansion freezing separation chamber (8) connected with a normal pressure nitrogen gas bag (13), a compressed nitrogen gas kettle (7), a liquefied hydrothion kettle (12.3), a liquid methane kettle (12.2) and a liquid carbon dioxide kettle (12.1). The normal pressure nitrogen gas bag is connected with the compressed nitrogen gas kettle via a cooler (6) by a nitrogen gas compressor (5). The nitrogen gas compressor is connected with a methane generator (2) by a transmission unit (4).    USE - Vehicular methane freezing liquefying separation device.    ADVANTAGE - The device is flexible and portable to operate. The device reduces straw raw materials and cost for conveying wastages, realizes low carbon agricultural development, saves energy and protects environment.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a vehicular methane freezing liquefying separation device.    Methane generator (2)    Transmission unit (4)    Nitrogen gas compressor (5)    Cooler (6)    Compressed nitrogen gas kettle (7)    Nitrogen gas expansion freezing separation chamber (8)    Liquid carbon dioxide kettle (12.1)    Liquid methane kettle (12.2)    Liquefied hydrothion kettle (12.3)    Normal pressure nitrogen gas bag (13)
NOVELTY - The device has a gas chamber (8) provided with two plane reflecting flash grids (3, 4), where an upper end of the gas chamber is provided with two heat release electrical detectors (5, 6). The heat release electrical detectors are connected with a signal processing circuit (7). The heat release electrical detectors transmit test signals to the signal processing circuit. The signal processing circuit judges whether methane and carbon monoxide in sampling gas are above a certain limit to produce an alarm.    USE - Spectral infrared absorption mash gas detecting device.    ADVANTAGE - The device can detect mash gas selectively, rapidly and stably, and can realize detection of the methane and the carbon monoxide in the sampling gas in a cost effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a mash gas detecting method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a spectral infrared absorption mash gas detecting device. '(Drawing includes non-English language text)'    Parallel optical assembly (2)    Plane reflecting flash grids (3, 4)    Heat release electrical detectors (5, 6)    Signal processing circuit (7)    Gas chamber (8)
NOVELTY - The furnace has a material inlet that is opened on upper portion of furnace case. A gas outlet is located on top of furnace case. An electric heater is arranged at bottom of furnace case. An agitating vane is installed above the electric heater, and is connected with a power device on top of furnace case. A feeding hopper is arranged at the material inlet.    USE - Pyrocrack furnace for biomass material.    ADVANTAGE - The natural gas and heat can be gained effectively from agricultural waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the pyrocrack furnace for biomass material.
NOVELTY - Biofuel mixture preparation involves performing transesterification of a vegetable oil or animal oil with alcohol and glycerol fatty acid ester in presence of catalyst, preferably strong solid Bronsted acid catalyst by absorbing ammonia to obtain a product. Etherification of the obtained product is performed with alcohol in presence of catalyst, where transesterification and etherification are performed simultaneously.    USE - Method for preparing biofuel mixture (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biofuel mixture, which comprises glycerol fatty acid ester and ethanol.
NOVELTY - A catalyst comprises cobalt-nickel complex oxide and activated carbon.    USE - Catalyst is used for removing carbon monoxide from hydrogen-rich gas (claimed) for hydrogen fuel used for fuel cell.    ADVANTAGE - The catalyst is manufactured efficiently, easily and economically with excellent catalytic activity and selectivity.    DETAILED DESCRIPTION - A catalyst comprises cobalt-nickel complex oxide (nCoO-mNiO, where n:m is 4:1-1:4) and activated carbon. An INDEPENDENT CLAIM is included for manufacture of catalyst, which involves dissolving cobalt salt and nickel salt in distilled water, adding activated carbon particles to the solution, and drying at 353K for 10-24 hours.
NOVELTY - The system has a heating device and a reaction device which are connected to the heating device. The first and/or second reaction device are/is connected with raffinate oil cutting system through a high pressure separator, a stabilization tower system and an extraction system. The extraction system is connected with recycling towers. The top of the raffinate oil cutting system is connected with third and/or second reaction device.    USE - Reforming system for producing large quantity of arene from naphtha.    ADVANTAGE - The reforming system processes the reforming efficiently. The reforming system yields large quantity of liquid efficiently. The yield of arene and hydrogen are raised to larger amount effectively by using the reforming system.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for reforming method for producing large quantity of arene from naphtha.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the reforming system.
NOVELTY - Method for producing methanol involves (1) mixing ethanolamine and naphthenic acid with industrial methanol to form denatured methanol, (2) adding oleic acid, petroleum acid and naphthenic acid to obtained mixture, (3) adding alkylphenol ethoxylates, dimethyl carbonate, ethyl oleate and butyl phenol to obtained mixture to form diesel fuel modifier, stirring the mixture for 20-30 minutes to form diesel fuel mixture, and mixing obtained diesel fuel mixture, denatured methanol, and diesel fuel modifier to form product.    USE - The method is useful for producing methanol.    ADVANTAGE - The obtained methanol is inexpensive, has stability, noncorrosive property, non-swelling property, non- emulsifying property, and strong explosive force and can be easily prepared.    DETAILED DESCRIPTION - Method for producing methanol involves (1) mixing ethanolamine (0.5-1.5%) and naphthenic acid (0.2-1%) with industrial methanol to form denatured methanol, (2) adding 5-15% or more of oleic acid, petroleum acid and naphthenic acid to mix up equally to obtained mixture, and (3) adding alkylphenol ethoxylates (54-64%), dimethyl carbonate (10-30%), ethyl oleate (5-10%) and butyl phenol (1-6%) to obtained mixture to form diesel fuel modifier, stirring the mixture for 20-30 minutes to form diesel fuel mixture, and mixing obtained diesel fuel mixture (70%), denatured methanol (25%), and diesel fuel modifier (5%) to form product.
NOVELTY - A clean fuel contains (in wt.%) cow dung (48-60), high refined coal (20-38), middle coal (5-15), gangue (0-8), coal tar (0.5-4), potassium permanganate (0.5-4), quick lime (1-4), industrial alkali (0.8-3), diamine (1-4), industrial salt (1-5), methanol (0.6-2.5), potassium nitrate (0.8-2) and borax (0.2-0.8).    USE - Clean fuel.    ADVANTAGE - The clean fuel is efficiently produced without affecting the environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of clean fuel, which involves drying cow dung until the water content is 10-14%, placing the cow dung into the powder crusher to crush until the granularity is 8-10, placing the high refined coal and middle coal into the powder crusher to crush until the granularity is 8-10, mixing the coal tar, potassium permanganate, quick lime, industrial alkali, diamine, industrial salt, methanol, potassium nitrate and borax, adjusting water, making the humidity of the finished product to 20-40%, agitating for 5-15 minutes, molding and extruding.
NOVELTY - A catalyst contains sulfoacid ion liquid comprising sulfo group(s).    USE - Catalyst is used for manufacture of biodiesel (claimed).    ADVANTAGE - The catalyst has high catalyst activity and recycling property.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biodiesel, which involves uniformly mixing fatty acid, alcohol and catalyst and esterifying at 60-120 degrees C.
NOVELTY - Slow release fertilizer comprises polyhydroxyalkanoates, diatomite and humic acid.    USE - The slow release fertilizer is useful for preventing soil from heavy metal pollution.    ADVANTAGE - The fertilizer is environmentally-friendly, provides nutrient to soil microorganism, and promotes fast growth of plants.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of recovering soil pollution, which involves (a) adding the fertilizer to the soil, and mixing the fertilizer with the soil, (b) selecting one or more remediation plants according to kind of heavy metal pollution in the soil, (c) cultivating the plant in the soil, and recycling the fertilizer.
NOVELTY - alpha -Bromo-hydroxyacetophenone is added to solvent, stirred and dissolved. Then, ethylamine is added to mixture, reacted, and hydrochloride solution is added to mixture. The temperature of reaction mixture is reduced to less than 10 degrees C, separated and washed, to obtain alpha -ethylaminohydroxyacetophenone hydrochloride. The obtained product is added to alcohol solvent, heated, and then catalyst is added to mixture. Then, the mixture is hydrogenated, crystallized, separated and washed, to obtain etilefrine hydrochloride.    USE - Preparation of etilefrine hydrochloride.    ADVANTAGE - The method economically and efficiently provides etilefrine hydrochloride without causing pollution.    DETAILED DESCRIPTION - alpha -Bromo-hydroxyacetophenone is added to solvent, stirred and dissolved. Then, ethylamine is added to mixture, reacted at 10-20 degrees C for 3-6 hours, and hydrochloride solution is added to mixture to adjust the pH value of solution to 0.5-1.5. The temperature of reaction mixture is reduced to less than 10 degrees C, separated and washed, to obtain alpha -ethylaminohydroxyacetophenone hydrochloride. The obtained product is added to alcohol solvent, heated, and then catalyst is added to mixture. Then, the mixture is hydrogenated by supplying hydrogen after nitrogen displacement at 30-40 degrees C for 12-24 hours when relative pressure of reaction system is 0.05 MPa or less. The obtained product is crystallized, separated and washed, to obtain etilefrine hydrochloride.
NOVELTY - Agent comprises (in wt.%): bactericide, growth regulating agent, film-forming agent, suspension, seedvax (5-11), thiram (5-12), chlorpyrifos (6-12), humic acid (10-20), xanthan gum (6-12), bentonite (6-15), defoaming agent (1-6), warning color (0.5-2) and water (remainder).    USE - The agent is useful for controlling corn disease and insect.    ADVANTAGE - The agent is environmentally-friendly and inexpensive, promotes germination rate of corn and increases yield of crops, and has controlling rate of 85%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the agent, which involves adding the humic acid, xanthan gum and bentonite to water, dissolving the mixture, adding seedvax, thiram, chlorpyrifos, defoaming agent and warning color, stirring the mixture at high speed, and roughly pulverizing the mixture to obtain the final product.
NOVELTY - Method for producing ethanol and methane involves mixing monosodium glutamate waste liquid and paper-making sludge, preparing nutrient solution, inoculating Saccharomyces cerevisiae into nutrient solution, culturing the above nutrient solution, adding nutrient solution to the obtain fermentation medium, inoculating the obtained culture liquid into the above medium, fermenting the above medium, distilling fermentation substrate to obtain ethanol and subjecting the remaining distillate to anaerobic digestion process to obtain methane.    USE - The method is useful for producing ethanol and methane (claimed).    ADVANTAGE - The method can improve survival environment of microbe from nutrient structure and productivity of ethanol and methane. The method is simple and cost-effective.    DETAILED DESCRIPTION - Method for producing ethanol and methane by mixed fermentation of paper-making sludge and monosodium glutamate waste liquid, involves (a) mixing monosodium glutamate waste liquid and paper-making sludge at a ratio of 3-10:100 to obtain raw material mixture, (b) preparing nutrient solution, (c) obtaining the prepared nutrient solution, inoculating Saccharomyces cerevisiae into nutrient solution, culturing the above nutrient solution to obtain S.cerevisiae culture liquid, (d) adding cellulose, nutrient solution and water to the obtained raw material mixture, adjusting pH value of the mixture to acidic to obtain fermentation medium, inoculating the obtained S.cerevisiae culture liquid into the above fermentation medium, fermenting the above medium, (e) distilling the fermentation substrate to obtain ethanol, and (f) subjecting the remaining distillate residues to anaerobic digestion process to obtain anaerobic digested sludge, adjusting pH value of the above sludge to alkali and carrying out anaerobic digestion reaction to obtain methane.
NOVELTY - Method of producing methane by anaerobic fermentation of waste vegetables and fruits, involves crushing vegetable and fruit waste, soaking vegetable and fruit waste in methane liquid, fermenting the liquid, adding plant ash or quick lime to regulate the pH value of the fermented liquid to 7-8.5, transferring the pre-treated raw material into an anaerobic reactor or methane tank for anaerobic fermentation, adding methanogenic bacteria to the anaerobic reactor and fermenting the mixture anaerobically.    USE - The method is useful for producing methane by anaerobic fermentation of waste vegetables and fruits (claimed).    ADVANTAGE - The method enables to increase the production rate of methane.    DETAILED DESCRIPTION - Method of producing methane by anaerobic fermentation of waste vegetables and fruits, involves (a) crushing vegetable and fruit waste, (b) soaking vegetable and fruit waste in methane liquid, fermenting the liquid and adding plant ash or quick lime to regulate the pH value of the fermented liquid to 7-8.5, (c) transferring the pre-treated raw material into an anaerobic reactor or methane tank for anaerobic fermentation, and (d) adding methanogenic bacteria to the anaerobic reactor containing 0.08-0.1 km/cubic meter of fermentation liquid and fermenting the mixture anaerobically, where the fermentation period is 60-92 days.
NOVELTY - Agent comprises (in wt.%): Cycocel (RTM: Chlormequat) (50-55), hexanoic acid 2-(diethylamino) ethyl ester (DA-6) (0.4-0.5), emulsifier (8-10), surfactant (2-6), stabilizer (2-6) and deionized water, where the emulsifier is acidic emulsifier AEO-5, the surfactant is OP-10 and the stabilizer is urea.    USE - The agent is useful for regulating growth of sweet potato, controlling the growth of the ground portion of the sweet potato, promoting the assimilation of substance on the ground portion to transfer to the root and reducing the usage of the nitrogen fertilizer (claimed).    ADVANTAGE - The agent improves the yield, and is low in cost and environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the above-cited agent, which involves heating the deionized water to 40-55 degrees C, adding the Cycocel (RTM: Chlormequat) and DA-6 into the water, uniformly stirring the aqueous mixture, then adding emulsifier, surfactant and stabilizer and mixing uniformly the ingredients.
NOVELTY - A device for compounding (S)-5-chloro-2-(cyclopropylethyl)-2-amino-2-(trifluoro) benzoic acid (sic) comprises reaction kettle (1), buffer kettle (2), cooling tank (3), and vacuum pump (4). The air vent of reaction kettle is connected to inlet of buffer kettle, and outlet of buffer kettle is connected to inlet of cooling tank. The inlet and outlet of cooling tank are connected with vacuum pump. The cooling tank is saline jacket cooling tank.    USE - A device for compounding (S)-5-chloro-2-(cyclopropylethyl)-2-amino-2-(trifluoro) benzoic acid (sic).    ADVANTAGE - The device prolongs service life of vacuum pump, improves stability of production, reduces environmental pollution, improves solvent recovery ratio, and saves cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of device for compounding (S)-5-chloro-2-(cyclopropylethyl)-2-amino-2-(trifluoro) benzoic acid.    Reaction kettle (1)    Buffer kettle (2)    Cooling tank (3)    Vacuum pump (4)
NOVELTY - Fertilizer is prepared using crotonylidene diurea mixed solution, urea, monoammonium phosphate, potassium chloride and borax, preparing mixed solution of urea and aldehyde, mixing urea, monoammonium phosphate and potassium chloride, subjecting obtained mixture for amino acid process, adding the prepared mixed solution of urea and aldehyde, and ammonia into pelleting machine, reacting the obtained mixture, and drying and sieving the obtained material.    USE - Controlled-release fertilizer.    ADVANTAGE - The fertilizer is cost-effective, environmentally-friendly, improves solubility of inorganic salt in the fertilizer, controls release of nitrogen, potassium and phosphorus and can be produced with improved utilization rate of nutrient.    DETAILED DESCRIPTION - Fertilizer is prepared using (in wt.%): crotonylidene diurea mixed solution (10-15), urea (25-28), monoammonium phosphate (30-38), potassium chloride (20-28) and borax (1-2), preparing crotonylidene diurea mixed solution by conveying urea, aldehyde and concentrated sulfuric acid in a ratio of 20-22:33-35:1 into a reactor containing nitrogen, stirring the mixture, heating the stirred mixture to 80-90 degrees C, and reacting the heated mixture for 90-120 minutes, (b) mixing with monoammonium phosphate and potassium chloride, performing amino acid process to the obtained mixture, reacting the obtained mixture, and heating the material in the pelleting machine at 60-80 degrees C, where the pH of the material is regulated using ammonia to 6.0-6.5, (c) adding the reacted material into a rotary drum machine for drying, and sieving the dried material.
NOVELTY - Treating waste, comprises (a) separating the waste material into at least one first fraction, preferably with waste parts above a predetermined size of waste parts, and into a second organic-rich fraction, preferably with waste parts below the specified size of waste parts (S1), (b) separating the second fraction in at least an organic-rich fine fraction and an organic-rich coarse fraction (S2), (c) fermenting the organic-rich coarse fraction by dry fermentation (S3), and (d) further treating the digestate together with the previously separated organic-rich fine fraction (S4).    USE - The process is useful for the treatment of waste (claimed) preferably of domestic or household waste.    ADVANTAGE - In the process, using the dry fermentation, a part of the organic-rich load can be removed to yield reusable biogas energy.    DETAILED DESCRIPTION - Treating waste, in which deposit and/or fuel is obtained from conducted waste material by downstream treatment steps, comprises (a) separating the waste material into at least one first fraction, preferably with waste parts above a predetermined size of waste parts, and into a second organic-rich fraction, preferably with waste parts below the specified size of waste parts (S1), (b) separating the second fraction in at least an organic-rich fine fraction and an organic-rich coarse fraction (S2), (c) fermenting the organic-rich coarse fraction by dry fermentation (S3), and (d) further treating the digestate from the dry fermentation together with the previously separated organic-rich fine fraction (S4).    DESCRIPTION OF DRAWING(S) - The figure shows a flow diagram of a process for the treatment of waste (Drawing includes non-English language text).    Waste parts (S1)    Organic-rich coarse fraction (S2)    Dry fermentation (S3)    Organic-rich fine fraction. (S4)
NOVELTY - Zinc aluminate-based catalyst, which is devoid of zinc oxide, alumina and zinc aluminate, is new, where the zinc aluminate phase is a single phase of zinc superstoichiometric spinel type in which the atomic ratio of zinc to aluminum is 0.53-0.60.    USE - The catalyst is useful in the preparation of a composition of alcohol esters of linear 6-26C monocarboxylic acid and glycerin (claimed) and the obtained esters are useful as diesel fuels.    ADVANTAGE - The catalyst: is stable and recyclable; is compatible with continuous industrial processes e.g. the catalyst can be used in the fixed bed for a very long time without loss of its activity; allows for obtaining the esters in high yield; and avoids the problems associated with leaching due to the absence of zinc oxide and thus increases the quality of the obtained esters. The method of preparing the composition does not include the step of purification for removing the catalyst or its residue.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) the preparation of the catalyst; and    (2) preparing a composition of alcohol esters of linear 6-26C monocarboxylic acid and glycerin comprising reacting fat of vegetable or animal origin with 1-18C aliphatic monoalcohol in the presence of the above catalyst.
NOVELTY - Producing distillate from hydrocarbon charge containing olefins, comprises treating charge comprising at least one step of oligomerization of the charge in an oligomerization reactor, where the charge is oligomerized in the presence of at least 0.5 wt.% of an oxygenated organic compound comprising oxygen atom and at least two carbon atoms, where the oxygenated organic compound is of plant origin.    USE - The process is useful for preparing distillate, preferably middle distillate which is useful as jet fuel and diesel.    ADVANTAGE - The process: reduces the amount of olefin having chain length too short (10C or less) and increases the yield of C10+ molecules, while controlling the exothermicity of oligomerization reaction; increases the yield of distillates, including middle distillates; provides the resulting product having a high cetane number; and is cost effective for preparing distillate. The process avoids the side reactions.
NOVELTY - This invention relates to a glycerin electric separation device of biomass diesel, mainly including: disposing a first and a second electrode of different length in an electric separation chamber. Through the control of a power distribution control device, high voltage AC can be applied between the first electrode and the second electrode. When a solution obtained from an ester exchange reaction is injected into the electric separation chamber and power has be applied to the first and second electrodes, the solution is facilitated to separate into glycerin and biomass diesel. The separated glycerin will deposit toward the bottom of the electric separation chamber and the biomass diesel of lighter weight and higher impedance gradually aggregates at the top of the electric separation chamber, therefore the impedance of solution at the top of the electric separation chamber increases. When the impedance of the solution does not increase any more, it shows that the separation is completed. The power distribution control device will detect this situation and will stop to apply power to the first and the second electrodes.
NOVELTY - This invention relates to a biomass fuel coal, the components including biomass fiber materials and coal materials, in which the content of the biomass fiber materials is between 70% to 90% by weight of the total components; the content of the coal material is 1% to 20% by weight of the total components. Through the aforementioned component ratios of the biomass fiber materials and coal materials, the discharging amount of green house gasses and pollutant gasses decrease, and the total thermal energy generated by the biomass fuel coal can meet demands of industrial activities and has the benefit of high combustion efficiency.
NOVELTY - A method for producing biodiesel is provided. The step of the method includes filtrating the oil; esterifing fatty acids of the oil into esters by hydrochloride and methanol; heating the esterified oil; transesterifiing triglycerides of the oil by an alcohol and an alkali catalyst; neutralizing the alkali catalyst by an acid; washing a primary biodiesel; heating the primary biodiesel; and collecting a final biodiesel. The oil including a plurality of impurity and fatty acids is converted to biodiesel directly by foregoing method.
NOVELTY - Disclosed is 100% eco-friendly and 100% biomass/herbal composition based fuel bio-additive, which when mixed with fuel, breaks hydrocarbon and improves combustion and removes carbon and hence reduces friction, removes black smoke by a large extent particularly 80%, reduces engine noise to a large extent particularly 20%, saves fuel vaporization to a large extent particularly 5-10%, increases power to a large extent particularly 20% and increases the fuel efficiency to a large extent particularly up to 60%. It easily gets dissolved in any fuel and prevents the vaporization of the fuel. It increases the average of the engine or any appliances and increases life of the engine or any appliances and is authenticated for national standard safety by the test and evaluation methods for fuel bio-additive in respect of Indian Standard 27096-2000 and as per Petroleum Conservation Research Association (PCRA) of India. The fuel efficiency is enhanced by mixing purely biomass/herbal extracts with or without any of the biomass/herbal oils for various applications namely fossil-based engines/appliances/systems of any type or any design, automotive, transportation (rail, road, sea and air), domestic, industrial and other thermal processes, crematoriums, power generation, cooking, lighting, surface treatment, lubrication, aviation, space mission, marine, defense activities etc. The fuel is used in solid, liquid or gaseous forms, resulting in improved combustion, reduction of friction, noise and emission characteristics. Image 0/0
NOVELTY - The method involves producing a fuel mixture consisting of a polar component, and an amphiphilic component, and an auxiliary component in the high pressure of the injection system of the internal combustion engine. The polar component is selected from oxygen-containing molecules, including water, mono-and polyhydric alcohols such as ethanol, ethylene glycol and glycerin, water-soluble peroxides such as hydrogen peroxide and percarbonates, combustion-enhancing salts such as ammonium nitrate, or biocides.    USE - Method for operating an internal combustion engine or a nozzle.    ADVANTAGE - The method involves producing a fuel mixture consisting of a polar component, and an amphiphilic component, and an auxiliary component in the high pressure of the injection system of the internal combustion engine, and thus ensures an improved operating method.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an additive composition.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a high pressure hydraulic test bench. (Drawing includes non-English language text).
NOVELTY - Additive comprises microorganism capable of decomposing polysaccharide. The additive is added to activated sludge when processing organic wastewater using membrane bioreactor.    USE - The additive is useful for processing organic wastewater (claimed) chosen from activated sludge, soil, lakes and marshes water and river water, foodstuff industrial wastewater, sugar factory wastewater, detergent industrial wastewater, starch industrial wastewater and tofu industrial wastewater.    ADVANTAGE - The additive decomposes the polysaccharide which is a causative agent of clogging of the film in a membrane bioreactor and is stable for long period of time.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for processing organic wastewater; and    (2) apparatus for processing the organic wastewater.
NOVELTY - Preparation of cefotaxime acid involves condensing 7-amino-3-acetoxymethyl-3-cephem-4-carboxylic acid with 2-mercaptobenzothiazolyl-(Z)-2-(2-aminothiazol-4-yl)-2-methoxyiminoacetate in the presence of a base in an alcoholic solvent at a lower temperature; adding water to the obtained reaction mass and filtering the solution; adjusting the pH of obtained solution with an acid; and isolating cefotaxime acid in pure form.    USE - For the preparation of cefotaxime acid (claimed) which is useful for treating bacterial infections.    ADVANTAGE - The present method is very safe and yields higher purity and greater yield of the compound (I); avoids excess usages of reagent(s) and organic solvent(s), thus promoting green chemistry and ensuring a cleaner surrounding by putting lesser load on environment; avoids the use of solvents e.g. carbon tetrachloride, N,N-dimethylformamide which are harmful for the environment and very hazardous in nature; uses a solvent (such as alcohol having remarkably lower toxicity than the other solvents) which is recycled and reused and thus makes the process more economical and industrially and commercially viable; and is a simple process, which avoids more number of operations, thus resulting in shortening of reaction time and lowering of labor.
NOVELTY - Method of treating wastewater containing organic compound, involves subjecting wastewater to anaerobic biological treatment process, carrying out primary treatment process by adding mixed gas containing organic compound methane and carbon dioxide to anaerobically treated water, performing secondary treatment process by passing the treated water into solid-liquid separation unit and carrying out tertiary treatment process by passing the treated water into a reverse osmosis (RO) membrane separator and separating the secondary treated water.    USE - The method is useful for treating wastewater discharged from chemical processing plant, petroleum plant and petrochemical plant (claimed).    ADVANTAGE - The method is simple and cost-effective.    DETAILED DESCRIPTION - Method of treating wastewater containing organic compound, involves (a) subjecting the wastewater to pretreatment process by adding compound containing a nitrogen component and phosphorus component to wastewater and subjecting the pretreated water to anaerobic biological treatment process, (b) carrying out primary treatment process by transferring the treated water into an anaerobic-biological-treatment tank and performing anaerobic-biological-treatment process by adding mixed gas containing organic compound methane and carbon dioxide to anaerobically treated water, (c) performing secondary treatment process by passing the treated water into solid-liquid separation unit and performing aerobic biological treatment process, and (d) carrying out tertiary treatment process by passing the secondary treated water into a reverse osmosis (RO) membrane separator and separating the secondary treated water into RO permeated water and RO concentrated water.
NOVELTY - Production of alcohol and other bioproducts from power boiler woody biomass extract containing hemicelluloses involves combining power boiler woody biomass extract containing hemicelluloses with extract from wood prior to Kraft cooking.    USE - For production of alcohol such as ethanol and butanol, and other bioproducts from power boiler woody biomass extract containing hemicelluloses (claimed).    ADVANTAGE - The process is integrated with the host Kraft pulp mill plant process, thus minimizes the heat loss from extracting hemicelluloses, minimizes energy used in the process, and minimizes water consumption.
NOVELTY - Pretreating, fractionating, and converting lignocellulosic material to sugar and lignin derivatives involves using alcohol, sulfur dioxide, enzymes and micro-organisms.    USE - For pretreating, fractionating, and converting lignocellulosic material to sugar and lignin derivatives (claimed).    ADVANTAGE - The process is rapid and offers simple, efficient recovery of cooking chemicals. This is achieved through cooking lignocellulosic material with sulfur dioxide and alcohol in a continuous process. The wash filtrate is stripped of alcohol, sulfur dioxide and volatile impurities, including methanol, furfural and acetic acid.    DESCRIPTION OF DRAWING(S) - The figure shows the flow sheet of biorefinery process.
NOVELTY - The method involves forming a photoresist film in the surface of a substrate (21) and forming a flow path molding pattern on the photoresist films (25a,25b). A conductive resin material (22) containing electroconductive filler made of mixture of carbon fiber and electroconductive powder is coated so that convex portion and recessed portions (25A,25B) of flow pattern are covered. The coated resin material on the top of convex portion and photoresist film comprising convex portion are removed so as to expose the top portion.    USE - Method of manufacturing separator for fuel cell (claimed) used as electric power supply of portable electric equipment, warm water feeder for cogeneration and fuel cell electric vehicle.    ADVANTAGE - The separator exhibiting electroconductivity characteristics, high corrosion resistance, mechanical strength characteristics is manufactured stably at low cost.    DESCRIPTION OF DRAWING(S) - The drawings show the sectional views illustrating the manufacturing process of separator.    Substrate (21)    Conductive resin material (22)    Reactive gas flow path (23)    Recessed portions (25A,25B)    Photoresist films (25a,25b)
NOVELTY - The mold side of intaglio plates (27,28) is filled with conductive resin (22), solvent and conductive resin ink containing electroconductive filler. The solvent is removed from conductive resin ink. The intaglio plates are joined to surface of substrate (21) by thermo compression process. The intaglio plates are peeled from resin. The convex portion and recess portion of intaglio plates are positioned opposite to surface of conductive resin.    USE - Method for manufacturing separator for fuel cell such as solid polymer fuel cell, phosphoric acid fuel cell, molten carbonate fuel cell, solid oxide fuel cell and alkaline fuel cell.    ADVANTAGE - The electroconductivity, corrosion resistance, mechanical strength of fuel cell are improved, by forming the resin layer mixed with electroconductive filler in substrate surface easily at low cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view illustrating the manufacturing process of separator.    Separator (10)    Substrate (21)    Conductive resin (22)    Concave grooves (23,24)    Intaglio plates (27,28)
NOVELTY - Method of processing organic material containing liquid having at least one organic substances of alcohol and amine compound, involves using microorganisms capable of surviving in activated sludge in presence of at least one metal ion and sulfide ion. The microorganisms are bacteria chosen from Hyphomicrobium, Thauera, Leptothrix, Lysobacter, Legionella and Pandoraea.    USE - The method is useful for processing organic material (claimed), waste liquid, printed circuit board washed liquid, food processed waste liquid, domestic waste water, excrement and chemical waste water.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for processing agent for organic material, which comprises the above-mentioned microorganisms.
NOVELTY - A fuel cell separator (A) is manufactured by molding composition for molding which contains thermosetting resin containing epoxy resin, hardening agent containing phenol type compound and graphite particles, and processing surface of obtained molded material (1) by sulfur trioxide. The equivalence ratio of epoxy resin with respect to phenol type compound is 0.8-1.2.    USE - Manufacture of fuel cell separator.    ADVANTAGE - The method obtains fuel cell separator which can maintain hydrophilicity for a long period of time, prevent channel for gas supply discharge being obstructed by water droplet, and maintain high electric power generation efficiency of fuel cell. The fuel cell separator has high hydrophilicity on surface of separator.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a fuel cell separator.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of fuel cell separator in unit cell. (Drawing includes non-English language text).    Molded material (1)    Convex part (1a)    Channel for gas supply discharge (2)    Solid polymer electrolyte membrane (4)    Fuel cell separator (A)
NOVELTY - The device has guidance for a bond wire and a melt that is provided with a device for melting the surface of a definite region of the bond wire surface. The bond wire guidance guides the definite region of the bond wire into a bonding area (1) and connects it to one bond pad. The bonding area has a process gas inlet (3) that is connected to an on-site gas generator (5) which generates a process gas. Gas purifier e.g. de-oxo purifier, purifies the process gas or a portion of process gas (4) prior to being directed into the bonding area.    USE - Device for processing wire bonding with electronic components such as microelectronics with processed gas stored in on-site gas generator.    ADVANTAGE - The bonding area with process gas inlet connected to the on-site gas generator which generates the process gas. Thus the safety of the device is improved by omitting the hydrogen reservoir, the users of the wire bonding machine do no longer need to handle hydrogen or hydrogen containing mixtures which are potentially flammable and explosive. The movement or piping covering longer distances of hydrogen or hydrogen containing gas mixtures is needed which leads to a reduced need of space, handling, administration and safety efforts, and the delivery needs and connected energy consumption are reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for wire bonding.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of device for processing wire bonding.    Bonding area (1)    Gas inlet (3)    Gas (4)    On-site gas generator (5)
NOVELTY - Agent is prepared by mixing stabilized chlorine dioxide and cationic surfactant.    USE - The agent is useful for removing moss (claimed) and controlling algae, bacteria, preferably Salmonella, Vibrio parahaemolyticus, Staphylococcus aureus, Pseudomonas and virus, preferably influenza virus in vegetation, lawn, artificial lawn, tennis court, baseball field and living environment chosen from school, garden, kindergarten, sand pit, footpath, park and street.    ADVANTAGE - The agent prevents unpleasant odor for long period of time, preferably two months or more, and maintains external appearance of lawn, and does not cause any side effect to humans and is environmentally-friendly.
NOVELTY - A solid fuel is obtained by compression-molding mixture containing wood scrap having size of 1-50 mm, paper scrap having size of 1-50 mm, binder, form-retaining agent and heat amount-enhancer. The content of wood scrap and paper scrap with respect to 100 parts weight of the mixture is 15-45 parts mass. The total content of binder, form-retaining agent and heat amount-enhancer is 55-85 parts weight. The weight ratio of wood scrap to paper scrap is 20:80-80:20.    USE - Solid fuel is used as energy source for thermal power generation (claimed).    ADVANTAGE - The solid fuel is manufactured by generating reduced amount of toxic gas and toxic residue and without generating carbon dioxide.
NOVELTY - Method for water treatment, involves eluting minerals from natural minerals, supplying mineral into cultivation tank in which the microorganisms are cultured, discharging micro/nanobubbles into the cultivation tank, adding microorganisms in the cultivation tank and culturing to obtain culture solution, adding the culture solution into the water treatment unit, and then adding and processing to-be-treated water in water treatment unit.    USE - The method is useful for treatment of water (claimed), preferably wastewater (containing organic substances e.g. persistent chemical substances) e.g. foodstuff industrial wastewater and chemical industrial wastewater.    ADVANTAGE - The method maintains biological oxygen demand, chemical oxygen demand, suspended solids and normal hexane at predetermined amount in the processed water.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for water treatment apparatus.
NOVELTY - Biomass fuel comprises solid combustible fuel. The solid combustible fuel is obtained by cultivating Parachlorella sp. binos (FERM ABP-10969) and drying the cultivated cells.    USE - The biomass fuel is useful for generating electric power.    ADVANTAGE - The biomass fuel is inexpensive, easy to preserve and use, and has higher hydrophobicity and calorific value, and generates power with reduced emission of carbon dioxide.
NOVELTY - The bag has a cylindrical drum portion (1) that is made of raw material having air and water permeability. An upper cover (2) is provided to open or close upper face opening of drum portion. A door (7) is arranged in lower edge of peripheral surface of the drum portion, whose one side forms an opening corresponding to the lower edge. The door opening is opened or closed with U-shaped fastener (8). The bearing bars (5) are attached to peripheral surface of drum portion and self-supported by hoop rings (3,4) in the upper and lower edges of drum portion.    USE - Composting bag installed in park and playground of school.    ADVANTAGE - Since the opening is formed corresponding to the lower edge of drum portion, the lower layer of compost formed by dead or fallen leaves can be taken out easily and user convenience can be improved. Hence, the amount of garbage can be decreased and the compost can be utilized for promoting growth of trees. Also, durability of the bag can be improved and garbage disposal cost can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the composting bag.    Cylindrical drum portion (1)    Upper cover (2)    Hoop rings (3,4)    Bearing bar (5)    Door (7)    U-shaped fastener (8)
NOVELTY - Preparing a biofuel comprises disrupting a fatty acid metabolism pathway in a plant cell or fungus by contacting the plant cell or fungus with an inhibitor of fatty acid metabolism to promote accumulation or storage of fatty acids; collecting the fatty acids from the plant cell or fungus; and processing the fatty acids to produce a biofuel.    USE - The method is useful to prepare biofuel.    ADVANTAGE - The method: increases accumulation or storage of fatty acids; and produces biodiesel having slightly higher energy content than the alkyl esters, degrades more slowly, does not attract water and has other desirable chemical properties.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) producing fatty acids comprising: disrupting a fatty acid metabolism pathway in a plant cell or fungus by contacting the plant cell or fungus with an inhibitor of fatty acid metabolism to promote accumulation or storage of fatty acids; and collecting the fatty acids as a source of biofuel;    (2) producing a syngas comprising: disrupting a fatty acid metabolism pathway in a plant cell or fungus to promote accumulation or storage of fatty acids; subjecting the plant cell or fungus to a gasification process; and collecting syngas produced by the gasification process;    (3) a syngas comprising a gaseous mixture of hydrogen and carbon monoxide produced from a plant cell or fungus in which a fatty acid metabolism pathway has been disrupted;    (4) the biodiesel comprising a liquid diesel fuel produced from a plant cell or fungus in which a fatty acid metabolism pathway has been disrupted; and    (5) an algae or a plant cell comprising a stably-integrated polynucleotide encoding RNA interference (RNAi) construct, where the RNAi construct is complementary to a portion of a target gene, and the target gene participates in fatty acid storage or metabolism.
NOVELTY - Composition comprises a solution comprising (a) an ionic liquid (IL) or ionic liquid-aqueous (ILA) phase and (b) an organic phase, where the solution comprises a sugar and a boronic acid.    USE - (I) is useful for removing a sugar from a solution (claimed). (I) is useful in biomass processing or biofuels and other biomaterials, paper recycling and pulp processing for paper manufacturing.    ADVANTAGE - The ionic liquids are environmentally friendly solvents.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for removing a sugar from a solution, comprising: (a) providing a solution comprising the composition; (b) contacting the sugar with the boronic acid to form a sugar-boronic acid complex; (c) separating the organic phase and the aqueous phase, where the organic phase contains the sugar-boronic acid complex; and optionally (d) separating the sugar from the organic phase.
NOVELTY - Leachate and manure treatment involves utilizing methane containing biogas, sludge, water, anhydrous ammonia, dissolved ammonia and ammonia gas. The materials are processed in a tank and decanter (04) with polyelectrolytes. The processed materials are transferred to an evaporator tank through a slurry pump (02). The evaporator tank contains sensors and valve. The slurry is sterilized in the evaporator tank. The obtained product is transferred to a combustion chamber and processed by pyrolysis.    USE - Method for treating leachate and manure by pyrolysis and fractionation.    DETAILED DESCRIPTION - Leachate and manure treatment involves utilizing methane containing biogas, sludge, water, anhydrous ammonia, dissolved ammonia and ammonia gas. The materials are processed in a tank and decanter with polyelectrolytes. The processed materials are transferred to an evaporator tank through a slurry pump. The evaporator tank contains sensors and valve. The slurry is sterilized in the evaporator tank. The obtained product is transferred to a combustion chamber and processed by pyrolysis. The obtained product is processed in an inductors (11), chiller (12) and then in an expansion tank (13). The processed product is processed by heat treatment, thermal induction and fractional distillation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of leachate and manure treatment method.    Slurry pump (02)    Decanter (04)    Inductors (11)    Chiller (12)    Expansion tank (13)
NOVELTY - Improving the resistance to one or more of corrosion, oxidation, sludge and deposit formation of lubricating oil used to lubricate engines run on biodiesel fuel, comprises adding to the lubricating oil or biodiesel fuel an additive amount of a premix of one or more organic bases, one or more detergents and one or more antioxidants.    USE - The method is useful for: improving the resistance to one or more of corrosion, oxidation, sludge and deposit formation of lubricating oil used to lubricate engines run on biodiesel fuel; and improving the resistance to oxidation of biodiesel fuel (claimed).    ADVANTAGE - The addition of premix increases the total base number of the lubricating oil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an additive premix comprising a combination of one or more organic bases, one or more detergents and one or more antioxidants in a weight ratio of 0.5-10:0.5-10:2-80.
NOVELTY - A rubber composition contains (in parts weight) epihalohydrin-type rubber (100), copper salt of dithiocarbamic acid (0.01-0.5), acid receiving agent and curing agent. The vulcanized material containing the rubber composition directly contacts with biodiesel fuel.    USE - Rubber composition is used for forming vulcanized material used for rubber material for motor vehicle (both claimed), fuel hose and air hose.    ADVANTAGE - The vulcanized material formed using the rubber composition has excellent biodiesel-proof property, oil resistance and tensile strength.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for vulcanized material, which is formed by vulcanizing the rubber composition.
NOVELTY - Facilitating removal of a bio-organic stain from a surface comprises: (a) providing a curable polymeric coating comprising a polymer resin, a surfactant, a non-aqueous organic solvent, or a cross-linker; and (b) associating an amylase or its analog with the coating so that the amylase or its analog is capable of enzymatically cleaving a component of a bio-organic stain following curing of the curable polymeric coating to form a surface.    USE - The method is used for facilitating removal of a bio-organic stain from a surface (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a protein-polymer composite material comprising one or more amylases or analogs dispersed in a two component solvent-borne polymer resin, where the average particle size of particles of amylases or analogs in the protein-polymer composite material is 1 nm to 10 mu m (average diameter).
NOVELTY - The device has a charging device part i.e. cylinder, provided with a barrel (1) and a furnace cover. The furnace cover is installed on the barrel. Multiple teeth (3) are uniformly distributed on four walls of the barrel. Multiple contact parts (4) are uniformly installed at top of the device. Two of multiple contact parts are symmetrically installed inside the furnace cover. The contact parts are placed vertical to an axial line of the barrel.    USE - Charging device for a biomass gas furnace.    ADVANTAGE - The device can fill the fuel into the barrel without opening the furnace cover, so that the dust scale at bottom of the barrel is removed and the burning process is completed.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a charging device.    Barrel (1)    Teeth (3)    Contact parts (4)
NOVELTY - A steel is heated by using biomass forming fuel gasification reaction system to prepare biomass gas, and directly transmitting biomass gas to steel heating furnace.    USE - Heating of steel.    ADVANTAGE - The method saves fuel transmitting cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the device for steel heating process using biomass gas.
NOVELTY - A biomass fuel comprises 100-120 pts.wt. of Eupatorium adenophorum, 80-160 pts.wt. of straw and 5-25 pts.wt. of combustion improver, where the combustion improver is tapioca flour.    USE - Biomass fuel.    ADVANTAGE - The biomass fuel saves energy, protects environment, and has low cost and high heat value.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for producing biomass fuel, which involves:    (A) harvesting Eupatorium adenophorum, and airing, crushing and rubbing for later use;    (B) crushing and rubbing straw;    (C) mixing 100-120 pts.wt. of Eupatorium adenophorum, 80-160 pts.wt. of straw and 5-25 pts.wt. of combustion improver; and    (D) pressing and densifying to form Eupatorium adenophorum blocks.
NOVELTY - The furnace has a gasification generating chamber (2) whose top part is provided with a clapboard (3). A gas burning chamber (5) is placed at an upper side of the clapboard. A gas supply device is utilized for supplying supporting gas for the gas generating chamber and the gas burning chamber. The gas supply device comprises a two-time air inlet channel arranged in a gasification furnace body (1). An outlet of the two-time air inlet channel stretches in fuel of the gas generating chamber, where the gas is supplied to the gas generating chamber by the two-time air inlet channel.    USE - Gasification furnace for fire coal and biomass.    ADVANTAGE - The furnace is energy-saving and environment-friendly, and has uniform wind feed and high thermal efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a gasification furnace.    Gasification furnace body (1)    Gasification generating chamber (2)    Clapboard (3)    Burner port (4)    Gas burning chamber (5)
NOVELTY - The furnace has an oxygen feeding pipe (10) connected with an oxygen feeding annular passage (20) that is connected with a furnace hearth (18) by an oxygen feeding hole (21). A top part of the furnace is provided with a sealing groove (2) that is connected with an air blower (4) by an air inlet pipe (3). An air inlet (6) of the air inlet pipe is arranged in a furnace cover outer edge (7) when a furnace cover (5) is covered. An air inlet passage (9) is reserved between an inner ring (8) of the sealing groove and a top part of the furnace cover.    USE - Biomass gasification furnace.    ADVANTAGE - The furnace utilizes air pressure sealing, avoids need of water and tar smell and facilitates operation. The furnace can reduce tar emission and increase gas making time.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a biomass gasification furnace.    Sealing groove (2)    Air inlet pipe (3)    Air blower (4)    Furnace cover (5)    Air inlet (6)    Furnace cover outer edge (7)    Inner ring (8)    Air inlet passage (9)    Oxygen feeding pipe (10)    Furnace hearth (18)    Oxygen feeding annular passage (20)    Oxygen feeding hole (21)
NOVELTY - Treating rubbish percolate by using microbial fuel cell, comprises e.g. injecting a glucose simulating waste water into a microbial fuel cell, connecting an external 1000 ohms resistor, starting the microbial fuel cell using anaerobic sludge as inoculation liquid, then starting the microbial fuel cell successfully when the load voltage is stabilized at above 400 mV, and then injecting mixed solution of glucose and rubbish percolate, measuring the chemical oxygen demand for every two days, and when the removal rate of chemical oxygen demand reaches above 80%, changing the mixed solution.    USE - The method is useful for treating rubbish percolate by using microbial fuel cell.    ADVANTAGE - The method has simple technique, easy implement, low cost, high efficiency and high removal rate of chemical oxygen demand, it converts the organic pollutant in waste water into electric energy, and it is less affected by temperature of treating effect and electricity output.    DETAILED DESCRIPTION - Treating rubbish percolate by using microbial fuel cell, comprises: (i) injecting a glucose simulating waste water into a microbial fuel cell, connecting an external 1000 ohms resistor at a reaction temperature of 29.9-30.1 degrees C, starting the microbial fuel cell using anaerobic sludge as inoculation liquid, when the voltage of the cell is reduced to below 50 mV, changing the glucose simulating waste water in the anode chamber, the microbial fuel cell being successfully started when the load voltage is stabilized at above 400 mV; and (ii) after the microbial fuel cell is successfully started, changing the glucose waste water in the anode chamber into a mixed solution of glucose and rubbish percolate, recording the voltage of the cell every minute, measuring the chemical oxygen demand every two days and, when the removal rate of chemical oxygen demand reaches above 80%, changing the mixed solution of glucose and rubbish percolate.
NOVELTY - Mixed microbial inoculum with high denitrification efficiency comprises nitrifying bacteria (CCTCC No: M2010001) and nitrosobacteria (CCTCC No: M2010002).    USE - The mixed microbial inoculum is useful for treating waste water containing ammonia and nitrogen (claimed).    ADVANTAGE - The mixed microbial inoculum: has high denitrification efficiency and hence can greatly improve water treatment efficiency, improves ecological environment, and does not cause any secondary pollution.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for: a nitrifying bacteria Sundawater X-5, Nitrobacter sp., which is preserved in China Center for Type Culture Collection, Chinese Wuhan University, 430072 on 8th January 2010 with a preservation number CCTCC No: M2010001; and #a nitrosobacteria Sundawater X-6, Nitrosomonas sp., which is preserved in China Center for Type Culture Collection, Chinese Wuhan University, 430072 on 8th January 2010 with a preservation number CCTCC No: M2010002.
NOVELTY - The method involves crushing the inputted food waste using the crushing blade. The crushed food waste is conveyed to the screw mechanism for compressing the food waste. The compressed food waste is conveyed to the reverse screw mechanism for recompressing the food waste. The compressed food waste is heated using the heating unit and the heated food waste is cooled. The carbide extracted from processed food waste is collected.    USE - Method for producing carbide using food waste.    ADVANTAGE - The food waste can be processed efficiently without polluting the environment and the carbide can be produced efficiently from the processed food waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart explaining the process for producing carbide using food waste. (Drawing includes non-English language text)
NOVELTY - Treating rural domestic sewage, by performing anaerobic hydrolysis pre-treatment to domestic sewage, decomposing carbohydrate into fatty acid, performing artificial wetland treatment to the pre-treated sewage, converting granular matters and micromolecular organic matters into organic matters by plants and microorganism, performing shallow ecological pond aerobic bioremediation to water, planting aquatic crops in shallow ecological pond to carry out aquatic product waterfowl cultivation to form artificial ecological system, and recycling purified sewage.    USE - The method is useful for treating rural domestic sewage.    ADVANTAGE - The method is simple, inexpensive and environmentally-friendly.    DETAILED DESCRIPTION - Method for treating rural domestic sewage, involves (1) performing anaerobic hydrolysis pre-treatment to domestic sewage, decomposing carbohydrate into fatty acid, decomposing solid matters into soluble organic matters, and decomposing macromolecular organic matters into micromolecular organic matters, (2) performing artificial wetland treatment to the pre-treated sewage, and converting the granular matters and micromolecular organic matters into organic matters like carbon dioxide and water by adsorbing and decomposing effects of plants and microorganism, and (3) performing shallow ecological pond aerobic bioremediation to the water treated by artificial wetland, planting aquatic crops in the shallow ecological pond to carry out aquatic product waterfowl cultivation to form an artificial ecological system, and decomposing and converting the organic matters and nutrients entering the pond using substance transporting and conversion of multiple food chains and stage-by-stage transmission and conversion of energy in the shallow ecological pond, and recycling the purified sewage as renewable water resource. An INDEPENDENT CLAIM is included for ecological green space treatment system for treating rural domestic sewage.
NOVELTY - Method for increasing biogas production, involves using microorganism for anaerobic fermentation and additive.    USE - The method is useful for increasing biogas production.    ADVANTAGE - The biogas can be produced environmentally-friendly.
NOVELTY - Method for producing ammonia and calcium chloride, involves grinding or crushing a mixture of calcium-containing substance and ammonium chloride in a ratio of 1:0.5-2 at -20 to 200 degrees C for 1-500 minutes using a ball mill or crusher or grinder, and decomposing ammonium chloride by chemical reaction to obtain ammonia gas and calcium chloride.    USE - The method is useful for producing ammonia and calcium chloride.    ADVANTAGE - The ammonia and calcium chloride can be produced rapidly by simple process. The method is inexpensive and environmentally-friendly.
NOVELTY - Polyurethane-fixed nitrobacteria is formed by fixing method which involves embedding and adsorption to fix nitrobacteria on soft polyurethane foam carrier, and polyurethane-fixed nitrobacteria is added into fluidized bed reactor. Interval culture method is performed during initial operation period of reactor. Domestic sewage wastewater to which nutrient is added, is added to reactor. After 10 days, when polyvinyl alcohol is dissolved in water, operation of wastewater treatment system is started for wastewater nitrogen removal process.    USE - Method for treating nitrogen wastewater from power plant with polyurethane-fixed nitrobacteria.    DETAILED DESCRIPTION - Polyurethane-fixed nitrobacteria is formed by fixing method which involves embedding and adsorption to fix nitrobacteria on soft polyurethane foam carrier, and polyurethane-fixed nitrobacteria is added into fluidized bed reactor. The amount of nitrobacteria is 25-35 volume% of reactor. The amount of nitrobacteria is 1 g of wet nitrobacteria per 150 mL of filling material. Interval culture method is performed during initial operation period of reactor. Domestic sewage wastewater to which nutrient is added, is added to reactor. The mass ratio of carbon, nitrogen and phosphorus is 100:15-20:1. After 10 days, when polyvinyl alcohol is dissolved in water, operation of wastewater treatment system is started for wastewater nitrogen removal process.
NOVELTY - A leek soil modifier comprises (in wt.%) rabbit manure (60-78), pig manure (13-26), plant ash (4-6), crop straw (3-6), and quick lime (1-3).    USE - Leek soil modifier.    ADVANTAGE - The leek soil modifier is environmentally-friendly and prevents usage of pesticide to prevent leek insect disease.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of leek soil modifier, which involves cutting crop straw into length of 9-10 cm in winter, uniformly mixing rabbit manure, pig manure, plant ash, and crop straw, placing in a container, placing container in a refrigerating chamber at -10 degrees C for more than 48 hours, placing the material in a sealed container, adding quick lime and placing in a heat insulation chamber at 10-15 degrees C for aerobic fermentation for more than 96 hours, and placing the sealed container in the heat insulation chamber at 35-39 degrees C for high-temperature fermentation for more than 148 hours.
NOVELTY - The apparatus has pyrolysis gasification chamber (1) and catalytic cracking chamber (3) arranged in thermal cracking reaction kettle main body. The upper portion of cracking chamber is provided with fuel gas output pipe (6). The interior of cracking chamber is provided with catalyst bed layer (15) located on filtering mesh (12). A combustion chamber (2) is arranged in main portion and located between gasification and catalytic cracking chambers. The upper portion of chamber (2) is provided with fuel waste gas outlet (10) while lower portion is provided with fuel inlet.    USE - Clock-type biomass thermal cracking integral apparatus.    ADVANTAGE - The pyrolysis gas of apparatus is directly introduced into the cracking chamber, so that the thermal efficiency is improved. The generation of loss during operation of apparatus is prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the clock-type biomass thermal cracking integral apparatus.    Pyrolysis gasification chamber (1)    Combustion chamber (2)    Catalytic cracking chamber (3)    Vapor conveying pipe (4)    Fuel gas output pipe (6)    Fuel waste gas outlet (10)    Filtering mesh (12)    Catalyst bed layer (15)
NOVELTY - The method involves manufacturing an end cell of a solid oxide fuel cell. First air pole (10) is made of rare earth metal such as lanthanum, yttrium, scandium, praseodymium, neodymium, samarium and gadolinium. 50 mole percentage of transition metal such as cobalt, manganese, nickel, copper and iron is doped and dried without thermal process under temperature less than 200 degree Celsius for 10 minutes. The former air pole and another air pole (11) are coated in an upper part that is transmitted through screen printing or tape casting.    USE - Method for preparing air electrode of a solid oxide fuel cell (claimed).    ADVANTAGE - The method enables improving long-term performance, reducing economic cost and solving problems indicated in solid oxide fuel cell due to hermetic sealing and mechanical strength. The method enables obtaining high mechanical strength and current collect ability improvement.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a solid oxide fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram illustrating an air electrode preparing method.    Air pole (10, 11)    Air electrode buffer layer (12)    Fuel anode (14)
NOVELTY - A normal carbon molecular sieve is prepared. The obtained normal carbon molecular sieve is chambered with secondary activating process, and modified through adjusting the pore. Thus, carbon molecular sieve is obtained.    USE - Preparation of carbon molecular sieve used for absorbing nitrogen molecule, separating methane from nitrogen, and extracting methane from coal directly (all claimed).    ADVANTAGE - High concentration methane is efficiently separated from coal using the carbon molecular sieve.
NOVELTY - The aeration or agitation process of the sewage and sludge is executed in oxygen tank to form mixed solution. The portion of mixed solution is allowed to flow into secondary sedimentation tank. The mixed solution is allowed to flow into third-stage sewage treatment unit and the sludge from bottom of secondary sedimentation tank is discharged to sludge concentration unit. The concentrated sludge is discharged to anaerobic sludge digestion unit for digesting sludge under an anaerobic condition to produce biogas containing methane and to produce digested sludge.    USE - Urban sewage de-nitrification treatment method.    ADVANTAGE - The sludge is digested under anaerobic condition to produce biogas containing methane and to produce digested sludge such that the energy consumption is reduced and the biogas output is improved while reducing emission of digested sludge.    DESCRIPTION OF DRAWING(S) - The drawing shows a block flow diagram explaining the urban sewage de-nitrification treatment process.(Drawing includes non-English language text)
NOVELTY - A porous rare-earth metal organic framework material has composition (I) containing amine, fluorine, chlorine, bromine or iodine.    USE - Porous rare-earth metal organic framework material used for storing natural gas e.g. methane (both claimed) used for vehicles.    ADVANTAGE - The porous rare-earth metal organic framework material has excellent thermal stability, excellent pour gas performance and natural gas storing performance.    DETAILED DESCRIPTION - A porous rare-earth metal organic framework material has composition of formula (I).    RE3+=scandium ion, yttrium ion, ytterbium ion or lutetium ion;and    X=H, amine, fluoro, chloro, bromo or iodo.    INDEPENDENT CLAIMS are included for the following:    (1) manufacture of the porous rare-earth metal organic framework material, which involves mixing nitrate or halide of rare-earth metal and organic ligand (BTC) (1x 10-2-10 mol/l) in the molar ratio of 0.2-5:1 in mixed solvent of organic solvent and water used in the molar ratio of 5-10:1, reacting the contents at 4-180 degrees C for 1-72 hours, washing with ethanol and drying at 20-150 degrees C to obtain colorless crystals of the rare-earth metal organic framework material, activating obtained crystals with a saturated metal site and an open pore canal and without terminal coordinated water to obtain the porous rare-earth metal organic framework material; and    (2) use of the porous rare earth metal organic framework material, which involves vacuumizing the activated porous rare-earth metal organic framework material for 4-24 hours at 120-250 degrees C with a common oil pump, setting the vacuum degree to less than 10-3 mm mercury, and testing the ability of the material in storing methane at 20-30 degrees C and 1-100 bar pressure.
NOVELTY - Compound premix feed comprises (in wt.%): mustard pollen extract (0.1-5), antioxidant accelerating agent (6-30), biological antioxidant (8-18), and carrier (50-80).    USE - The compound premix feed is useful for promoting stable growth in livestock.    ADVANTAGE - The compound premix feed is environmentally-friendly, and residue free, and improves lean meat rate, meat quality and flavor.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the compound premix feed, which involves (a) crushing the cell wall of mustard pollen by ultralow temperature wall-breaking method and condensing the crushed powder to obtain the mustard pollen extract, (b) dissolving derivatized cysteamine in ethanol (90 %mass), adding croscarmellose sodium and povidone to the solution, and preparing hydrophilic cysteamine particles by granulating method, coating the granules using dihydropyridine ester to obtain antioxidant accelerating agent in the form of microcapsule, (c) adding mustard pollen extract, antioxidant accelerating agent and biological antioxidant in a mixer and mixing for 3-10 minutes, and (d) adding half of the amount of carrier into the mixer and mixing for 8-15 minutes, adding remaining carrier into the mixer and continuously agitating for 15-30 minutes to obtain the product.
NOVELTY - The water tank has water inlet arranged at upper portion of box structure, while the water outlet is arranged at lower portion of box structure. A gas outlet is arranged at upper portion of anti-overflowing plate. The anti-overflowing plate is arranged in inner portion of box structure, and provided at lower portion of gas outlet.    USE - Water tank for water-electrolyzing hydrogen oxygen generating apparatus used in automobiles and ships.    ADVANTAGE - A water tank having simpler structure can be provided.    DESCRIPTION OF DRAWING(S) - The drawing shows the front view of water tank.
NOVELTY - Organic and inorganic combined method for fertilizing soil biologically, involves culturing soil microorganisms (edaphon) indirectly using fertilizer, inoculating and proliferating microorganism which is effective to soil, intercropping legumes, mulching, regulating moisture in soil, and improving conditions and procedures in applying fertilizer.    USE - The organic and inorganic combined method is useful for fertilizing soil biologically.    ADVANTAGE - The method replaces chemical pesticide. The microorganisms in soil can be increased by the method, and the fertility of soil can be increase year by year.
NOVELTY - A biomass, an oxygen-containing organic solvent and a catalytic cracking catalyst are added to a reactor and reacted, to obtain biomass transformed product including biomass oil.    USE - Formation of biomass transformed product (claimed) for chemical raw material, fuel oil and macromolecular polymer.    ADVANTAGE - The biomass transformed product having high quality is prepared.
NOVELTY - Agent comprises insecticide, solvent, emulsifying agent (2.7-3.3%), auxiliary potentiating agent and propellant. The insecticide is (in %): tetramethrin (0.45-0.55), rich-dallethrine (0.22-0.3) or permethrin (0.45-0.55). The solvent is deodorized kerosene (4.2-4.8) or purified water (45-55). The auxiliary potentiating agent is essence (1.2-1.3). The propellant is butane gas (38-42).    USE - The agent is used as an insecticide for controlling mosquitoes, flies and cockroach.    ADVANTAGE - The agent is environmentally-friendly and safe to transport and store.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for method for preparing the above-cited agent, which involves (a) adding deodorized kerosene in a reactor, heating the mixture at specific temperature, adding tetramethrin, rich-d allethrine and permethrin to the mixture, and dissolving the mixture completely, (b) cooling the reactor, adding emulsifying agent to the reactor, stirring the mixture uniformly, adding purified water to the mixture and simultaneously stirring the mixture, and adding essence to the mixture, (c) adding the solution in a bottle, and fixing aerial valve at the opening of the bottle, and sealing the bottle, and (d) filling butane gas into the bottle by gas-filling machine, and packaging and storing the bottle.
NOVELTY - Aquatic weed simulative biological carrier comprises a polyurethane layer, a fiber mesh layer and a fiber yarn layer, where the polyurethane layer is located at inner layer. Two fiber mesh layers cover upper and lower surfaces of the polyurethane layer. Two fiber yarn layers cover outer surfaces of the fiber mesh layers.    USE - Aquatic weed simulative biological carrier.    ADVANTAGE - The aquatic weed simulative biological carrier enables to purify water by removing organic pollutants in cost-effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for purifying water, which involves:    (A) performing water purifying treatment by using a submersible photo-electro-magnetic river/lake water purifier and aquatic weed simulative biological carrier;    (B) utilizing a sewage sucker, an ozone generator, a vapor-water mixer, a purifier and a submersible electric control box in the submersible photo-electro-magnetic river/lake water purifier;    (C) arranging sewage sucker, vapor-water mixer and purifier orderly on bottom of a river, lake, an artificial lake, a fountain or a landscape fishpond;    (D) providing sewage sucker with a water inlet and water outlet in submersible photo-electro-magnetic river/lake water purifier;    (E) arranging vapor-water mixer with a gas mixing chamber on the surface of water; and    (F) connecting gas mixing chamber with water inlet of the purifier.
NOVELTY - 1-(4-Benzyoxy-3-nitrophenyl)-2-(1-(4-methoxyphenyl)-2-propyamino)ethanol, Raney-nickel and formic acid are reacted, to obtain N-(2-benzyloxy-5-(1-hydroxy-2-(1-(4-methoxyphenyl)-2-propylamino)ethyl)phenyl)formamide (foradil intermediate).    USE - Preparation of foradil intermediate.    ADVANTAGE - The method economically provides foradil intermediate by simple process in high yield without environmental pollution.
NOVELTY - Biodiesel, emulsifying agent, and formic acid are added to a reactor and temperature is controlled to 55-65 degrees C. 30% Hydrogen peroxide is slowly dripped and heat is retained for 8-10 hours. After reaction, the reaction product is allowed to stand and separated into layers. The upper ester layer is washed with hot water until pH of wash water solution is 7. The ester layer is decompressed and distilled, and the product is cooled and filtered to obtain epoxy biodiesel plasticizer.    USE - Preparation of epoxy biodiesel plasticizer.    ADVANTAGE - The method provides epoxy biodiesel plasticizer with an epoxy value of more than 4.5%.    DETAILED DESCRIPTION - Biodiesel, emulsifying agent, and 88 %mass formic acid are added to a reactor in a weight ratio of 1:0.005-0.035:0.05-0.15. The temperature of reaction pot is controlled to 55-65 degrees C, and 30% hydrogen peroxide is slowly dripped in an amount of 0.3-0.7 times the weight of biodiesel. Heat is retained for 8-10 hours. After reaction, the reaction product is transferred to a refining pot. The reaction product is allowed to stand and separated into layers to separate a lower layer water phase. The upper ester layer is repeatedly washed with hot water until pH of wash water solution is 7. The ester layer is decompressed and distilled in vacuum to remove material with low boiling point generated by reaction, and residual water. The product is cooled and filtered to obtain epoxy biodiesel plasticizer.
NOVELTY - A Fructose-bisphosphate aldolase gene isolated from Thermococcus onnurineus and comprising a 708 base pair sequence (SEQ ID NO: 1) fully defined in the specification, is new.    USE - The fructose-bisphosphate aldolase gene is useful for producing recombinant fructose-bisphosphate aldolase (claimed) which is useful for producing 2,4,6-tri-deoxyhexamethylose compound.    ADVANTAGE - The compound is environmentally-friendly.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) heat-proof and organic solvent resistant fructose-bisphosphate aldolase encoded by the above-cited gene;    (2) recombinant vector comprising the above-cited gene;    (3) recombinant engineered bacteria transformed by the above-cited vector; and    (4) use of fructose-bisphosphate aldolase gene for producing recombinant fructose-bisphosphate aldolase.
NOVELTY - A lye inlet is installed near water outlet of water pump, installed in positive electrode room in water splitting groove, or provided in positive electrode recycling water channel connecting water pump and water splitting groove.    USE - A lye inlet used in preparation of hydrogen by recycling water.    ADVANTAGE - The lye inlet reduces cost of hydrogen production.
NOVELTY - Composition comprises (in parts): Hibiscus trionum (1-7), Cynanchum auriculatum (1), solvent, co-solvent, emulsifier and water.    USE - The composition is useful for controlling pests.    ADVANTAGE - The composition has synergistic effect between effective components to improve pesticidal effect, has rapid effect, and environmentally-friendly as it does not cause harm to livestocks and human.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the composition, which involves (a) pulverizing the H.trionum, and C.auriculatum into 20-40 meshes grains, and mixing the powders in ratio of 1-7:1, soaking the mixture in alcohol (95%) for 12-36 hours at room temperature, extracting the mixture ultrasonically, filtering the extract and collecting filtrate for further use, (b) concentrating the filtrate into an extract, and (c) preparing the extract using solvent, co-solvent, emulsifier and water into solution.
NOVELTY - Active component containing cobalt is loaded on silica gel used as carrier by immersion method, and silica gel carrier is subjected to hydrothermal treatment for 0.5-20 hours using 50-100% of steam at 150-600 degrees C. Thus, cobalt-based Fischer-Tropsch synthesis catalyst is manufactured.    USE - Manufacture of cobalt-based Fischer-Tropsch synthesis catalyst used for manufacturing methane and 5C hydrocarbon.    ADVANTAGE - The catalyst provides product with high conversion rate and methane with high selectivity.
NOVELTY - Method for producing furfural with bagasse, involves drying bagasse, delivering the bagasse into spherical boiler to form an aldehyde steam stock solution, delivering rough furfural into water scrubber for washing acetic acid and methanol, refining the obtained product in a rectifying tower to obtain finished product furfural, processing wastewater separated by the water scrubber using light component removing tower for recycling methanol, and adding cellulase into the furfural residues and fermenting the obtained product to obtain acetone and butanol.    USE - The method is useful for producing furfural with bagasse.    ADVANTAGE - The method is simple.    DETAILED DESCRIPTION - Method for producing furfural with bagasse, involves drying bagasse until the water content is 30 plus minus 1%, adding the dried bagasse in dilute sulfuric acid (0.5-0.7 weight/weight%), delivering the bagasse into spherical boiler for hydrolyzing for 2 hours to form an aldehyde steam stock solution, delivering the obtained aldehyde steam stock solution into primary distillation tower for distilling over water, delivering the aldehyde water azeotropic mixture into an aldehyde separating tank after condensing aldehyde water azeotropic mixture for delaminating process, delivering rough furfural into water scrubber for washing acetic acid and methanol, refining the obtained product in a rectifying tower to obtain finished product furfural, processing wastewater separated by the water scrubber using light component removing tower for recycling methanol, and adding cellulase into the furfural residues after separating aldehyde steam in the furfural residues and fermenting the obtained product to obtain acetone and butanol.
NOVELTY - The device has a solar battery plate on top of electric vehicle, and a torque sensor that is installed on output shaft of engine. The solar battery plate and torque sensor are connected with control circuit board whose output is connected with water electrolyzing device. An oxygen supply pipe and hydrogen supply pipe of electrolyzing device are connected with gas intake pipe of engine.    USE - Solar electrolysis oil saving device for vehicle.    ADVANTAGE - The simple structure oil saving device can be obtained without changing internal structure of vehicle.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of oil saving device.
NOVELTY - The hydrogen machine has gas outlet that is located above electrolytic water liquid level in water tank (3). A gas pipe is connected between gas outlet of water tank and gas inlet of air-water separator (4). Another gas pipe is connected between a gas outlet of air-water separator and gas inlet of engine and allocated with stopper (5) for passing through gas and stopping backfire. The pulse width modulator is provided with double-grid gold oxygen half-field effect transistor. A diaphragm is one of high density polyethylene, silica gel, rubber and porous metal piece.    USE - Hydrogen machine for providing auxiliary fuel for vehicle engine.    ADVANTAGE - As the generated hydrogen is passed through three backfire preventing lines of the water tank, the air-water separator and the stopper before entering the engine can effectively avoid the explosion problem caused by the backfire. The air-water separation is performed for the hydrogen before entering the engine without generating adverse effect on the engine. The added oxygen sensing regulator can make the computer in the vehicle control the accurate oil jet so that the oil consumption is reduced, effectively energy is saved and emission effects is reduced with high safety.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen machine.    Hydrogen generator (1)    Accumulator (2)    Water tank (3)    Air-water separator (4)    Stopper (5)
NOVELTY - The device has the hydrogen and oxygen alkali liquor inlets and outlets that are arranged on an end pressing plate. The hydrogen and oxygen alkali liquor outlets are connected with hydrogen and oxygen alkali liquor inlets of hydrogen separator. The conductors are connected between the hydrogen and oxygen alkali liquor inlets, the hydrogen and oxygen alkali liquor outlets, and the hydrogen and oxygen alkali liquor inlets of hydrogen and oxygen separators. The conductors are connected with a ground wire.    USE - Electrolytical hydrogen production device.    ADVANTAGE - The device uses proximity equipotential connection between the hydrogen and oxygen alkali liquor pipes, so that the electrochemical corrosion of electrolytical hydrogen production device can be avoided or reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the electrolytical hydrogen production device.
NOVELTY - Fertilizer is obtained by mixing e.g. dry human excrement and dry duck excrement, pulverizing obtained mixture into powders, adding the obtained powder into fermentation tank, piling mixture, covering mixture with a plastic cloth cover, fermenting mixture, turning the mixture for first time, adding human excrement water (1:0.6) during turning process, turning mixture, spraying the human excrement on the mixture, immediately covering the mixture, covering the mixture after the mixture is turned for 70 hours, and fermenting mixture.    USE - The fertilizer is useful for planting Platycodon grandiflorum (claimed).    DETAILED DESCRIPTION - Fertilizer is obtained by mixing (in parts weight): dry human excrement (8-12), dry duck excrement (14-18), vegetable seed cake powder (10-14), rice bran (12-16), broom corn powder (10-14), organic compound fertilizer (6-10), plant ash (2-4), caraway seed powder (2-6), yellow tung oil tree powder (1-3), peach tree powder (2-6), radix aconiti agrestis powder (4-8), dry Camellia sinensis powder (1-3), nux vomica powder (2-6), copper sulfate (1-2) and Salvia miltiorrhiza powder (1-2) using stirring machine for 70 minutes, pulverizing obtained mixture into powders, adding the obtained powder into fermentation tank, piling mixture, covering mixture with a plastic cloth cover, fermenting mixture for 70 hours, turning the mixture for first time, adding human excrement water (1:0.6) during turning process, turning mixture, spraying the human excrement on the mixture, immediately covering the mixture, covering the mixture after the mixture is turned for 70 hours, and fermenting mixture, where the turning process is then performed for every 70 hours for 7 continuous turnings.
NOVELTY - Preparing special fertilizer by heating complexing agent and catalytic carrier, adding boric acid and/or sodium borate into mixture, stirring mixture to obtain compound containing organic boron element (C1), (2) uniformly mixing one or two of peat, cow dung and chicken manure containing water with industrial bentonite, industrial attapulgite powder and industrial zeolite powder based on ratio of 30-50:25-35:15-30:5-20 to obtain mixture (M2), and (3) mixing compound (C1) (0.5-8%), mixture (M1) (1-10%) and chemical fertilizer (82-95%) to obtain the end product.    USE - The method is useful for preparing special fertilizer for controlling plant diseases caused by lack of boron, and stimulating growth of plants.    ADVANTAGE - The fertilizer improves boron content in artificial soil slope.    DETAILED DESCRIPTION - Method of preparing special fertilizer, involves (1) heating (in wt.%) complexing agent in a reaction kettle (10-35) at 35-65 degrees C, adding catalytic carrier (10-35) to the mixture, dissolving the complexing agent and catalytic carrier in the mixture, adding boric acid and/or sodium borate (25-65) into mixture, stirring mixture for 0.5-5 hours at 50-105 degrees C to obtain compound containing organic boron element (C1), (2) uniformly mixing one or two of peat, cow dung and chicken manure containing water (1-15%) with industrial bentonite, industrial attapulgite powder and industrial zeolite powder based on ratio of 30-50:25-35:15-30:5-20 to obtain mixture (M2), and (3) mixing compound (C1) (0.5-8%), mixture (M1) (1-10%) and chemical fertilizer (82-95%) to obtain the end product. The complexing agent is chosen from diethanolamine, ethanolamine, diglycolamine and diethylene glycol amine. The catalytic carrier is chosen from water, ethylene glycol, propylene glycol and ethyl alcohol.
NOVELTY - Special biological liquid fertilizer comprises (in parts weight): biogas liquid (687-707), photosynthetic bacterial strain (0-3), chitosan (0-15), synergistic agent (0-5), mixture containing trace elements (0-40), urea N46 (0-80), phosphoric acid P50 (0-50), potassium sulfate K50 (0-50), potassium chloride K60(0-100) and natural plant essence (20-50).    USE - The special biological liquid fertilizer is useful for growing flowers with disease resistance, cold resistance and drought resistance characteristics.    ADVANTAGE - The fertilizer is cost-effective, environmentally-friendly and effective even at less amount of dose, improves soil structure of potted flower, improves fertility of soil, fixes nitrogen in the soil, promotes amplification of beneficial microorganism of soil, and has rapid and long lasting effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing the liquid fertilizer, which involves (1) separating biogas residues from biogas slurry obtained by fermenting livestock excrement using methane tank, aging mixture, and degrading and filtering the biogas liquid to obtain clear liquid, (2) adding photosynthetic bacteria to the clear liquid, and culturing mixture, (3) adding a certain amount of marine organism and chitosan to the amplified clear liquid, adding the trace elements, synergistic agent, nitrogen, phosphorus, potassium sulfate and natural plant essence to stirrer and stirring mixture, (4) controlling pH of the mixture to 6.3-6.5, and (5) packing the obtained product to aluminum-plastic container bottle (0.2-0.5 kg).
NOVELTY - Biological organic-inorganic fertilizer comprises (in parts weight): fermented livestock manure and/or biogas residue (345-545), nitrogen-fixing agent (0-10), phosphate-dissolving and potassium-dissolving composite bacteria, humic acid (0-200), solid amino acid (100-200), synergistic agent (0-5), trace element mixture (0-40), urea (0-100), monoammonium phosphate (0-100) and potassium sulfate (0-100).    USE - The biological organic-inorganic fertilizer is useful for promoting growth and resistance to cold, drought and diseases of fruit tree.    ADVANTAGE - The biological organic-inorganic fertilizer can be used with low quantity, has long persistence and increased water-retaining property, and granulates and loosen soil, releases the nutrients slowly, strengthens nutrient absorption of fruit tree, promotes root development, protects flower and fruit, and improves quality and prolongs preservation ability of fruit. The fertilizer is obtained by recycling waste resources and hence protects ecological environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparation of the biological organic-inorganic fertilizer, which involves (i) fermenting the livestock manure in the biogas tank anaerobically or aerobically, (ii) mixing the fermented livestock mature with humic acid, nitrogen-fixing agent, phosphate-dissolving and potassium-dissolving composite bacteria, synergistic agent, trace element and nitrogen-phosphate-potassium inorganic nutrient, and (iii) stirring the mixture and crushing the mixture.
NOVELTY - Producing biological organic fertilizer, by decomposing dining table garbage, pulverizing garbage, pulverizing plant residues and animal excrement, culturing composite biological bacteria, mixing the pulverized garbage and animal excrement with biological bacteria, fermenting mixture, adding the plant residues into decomposed and deodorized garbage and animal excrement, mixing and fermenting mixture, adding nitrogen, phosphorus, potassium and microelements into the fermented mixture, drying mixture naturally, and pulverizing and sieving mixture.    USE - The method is useful for producing biological organic fertilizer for controlling soil damages.    ADVANTAGE - The fertilizer is environmentally-friendly, reduces farm chemical residues and prevents soil acidization.    DETAILED DESCRIPTION - Method of producing biological organic fertilizer, involves (1) separately collecting and decomposing dining table garbage, pulverizing garbage, and pulverizing plant residues and animal excrement, (2) culturing deodorized composite biological bacteria, (3) mixing the pulverized garbage and the animal excrement with the composite biological bacteria, and heating and fermenting mixture to decompose and deodorize the garbage and animal excrement, (4) adding the pulverized plant residues into the decomposed and deodorized garbage and animal excrement, and mixing, heating and fermenting mixture completely, and (5) adding nitrogen, phosphorus, potassium and microelements into the fermented mixture, drying mixture naturally, and pulverizing and sieving mixture to obtain finished product.
NOVELTY - A tocopheryl polyethylene glycol 1000 succinate (TPGS)-b-(polycaprolactone (PCL)-ran-polyglycolic acid (PGA)) copolymer (I) or (II) is new.    USE - TPGS-b-(PCL-ran-PGA) copolymer used as medicinal auxiliary material in medicine used for treating tumor (all claimed).    ADVANTAGE - The TPGS-b-(PCL-ran-PGA) copolymer has excellent bio-compatibility and bio-degradability, and can be prepared in a simple and eco-friendly manner.    DETAILED DESCRIPTION - A tocopheryl polyethylene glycol 1000 succinate (TPGS)-b-(polycaprolactone (PCL)-ran-polyglycolic acid (PGA)) copolymer of formula (I) or (II).    n=20-140;    e=5;    (A+B+...)=2-490; and    (a+b+...)=2-900.    An INDEPENDENT CLAIM is also included for a method for producing TPGS-b-(PCL-ran-PGA) copolymer.
NOVELTY - Formulation comprises mixture of cotton seeds, turf and vermiculite in the weight ratio of 1:1:1.    USE - The formulation is useful for culturing solanaceous seedlings without soil.    ADVANTAGE - The formulation is inexpensive and environmentally-friendly, has sustained release property, and improves seedling culture quality.
NOVELTY - Water dispersible granule comprises (in wt.%): pymetrozine (5-80), dispersant (2-25), disintegrating agent (2-20), wetting agent (1-15), adhesive (0.1-10) and stuffing agent (100).    USE - As water dispersible granule.    ADVANTAGE - The granule is inexpensive, environmentally-friendly and free from organic solvent, has stable physical and chemical property, and does not decompose, combust and explode easily. The granule contains no petroleum products, and releases less dust.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the above-cited granule, which involves crushing pymetrozine, dispersant, disintegrating agent, wetting agent and stuffing agent, stirring the mixture, sieving the mixture using mesh size of 1000, adding adhesive and granulating agent to the mixture, and sieving the mixture using vibration sieve to obtain finished product.
NOVELTY - Nutrient solution, comprises (in mg/l): 5 mol/l of potassium (K+) (195), 4 mol/l of calcium (Ca2+) (160), 2 mol/l magnesium (Mg2+) (48), 9 mol/l of nitrate (NO3-) (558), 3.17 mol/l of sulfate (SO4-) (304) and 0.9 mol/l of phosphorus (P) (27.8).    USE - The nutrient solution is useful for cultivating tomato (claimed).    ADVANTAGE - The nutrient solution is environmentally-friendly as it does not contain agricultural pesticide and plant growth regulator and safe as it does not cause any harm to humans and animals.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the above-cited nutrient solution, which involves testing water quality to determine calcium (Ca2+) content and magnesium content (Mg2+) content in water, comparing dosage of the Ca2+ content and Mg2+ content in the nutrient solution with the Ca2+ content and Mg2+ content existing in the water for preparing the nutrient solution, and adding fertilizer as supplement if the Ca2+ content and Mg2+ content existing in the water are less than the Ca2+ content and Mg2+ content in the nutrient solution or not adding fertilizer if the contents are equivalent.
NOVELTY - A diesel composition comprises base diesel and additives. The base diesel comprises biodiesel. The additives comprises component A comprising Mannich base ashless dispersant, and a component B comprising arylamine antioxidant and/or hindered phenol antioxidant.    USE - A diesel composition.    ADVANTAGE - The composition has good oxidization stability, cleaning performance, and good dispersibility.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for improvement of oxidization stability of the biodiesel comprising adding additive to base diesel.
NOVELTY - Isolated and biologically pure strain of microalgae belonging to Scenedesmus obtusus for bioremediation and degradation of hydrocarbons from petroleum, is new.    USE - The strain is useful for bioremediation and degradation of hydrocarbons from petroleum. It can also be used for degrading benzene, toluene, ethylbenzene and xylenes (BTEX); and for degrading at least one or more hydrocarbons from oil present in oil derivatives such as liquefied gas, gasoline, solvents such as white spirit, high-grade fuel, gasoline, jet fuel, kerosene, domestic fuel oil, motor oil, paraffin, heavy fuel oils, base oils, waxes and asphalts (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are: (1) a device for degrading petroleum hydrocarbons, comprising at least one strain of Scenedesmus obtusus for degrading petroleum hydrocarbons, contained in a space or hardware; and (2) a method for bioremediation of petroleum hydrocarbons, comprising using at least one strain of Scenedesmus obtusus for degrading petroleum hydrocarbons.
NOVELTY - Slurry containing dispersed zeolite particles as seed particles, is made to flow down along the surface of a substrate by means of weight of slurry, and zeolite particles are adhered to the substrate. Zeolite particles-adhered substrate is immersed in a sol, and hydrothermal synthesis is performed to form a zeolite film on the substrate.    USE - Manufacture of zeolite film used for permeation vaporization film and gas separation membrane for separating carbon dioxide, methane and ethane.    ADVANTAGE - The method efficiently provides zeolite film having reduced defects.
NOVELTY - The electrode has an electrode active material that coats an electrically conductive metal. One component is selected from metal cerium, a cerium oxide and a cerium hydroxide and metal platinum. The electrode active material is provided with enormously cerium-rich composition that is molar fractions of platinum and cerium are 15 to 30 mol% and 70 to 85 mol% respectively.    USE - Electrode for producing hydrogen.    ADVANTAGE - The increase in the electrolysis voltage is prevented even when an electrolysis current density is high, and the energy cost is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for electrolysis method.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical representation of platinum-cerium ratio in the electrode active material. (Drawing includes non-English language text)    Hydrogen generation over-voltage (AA)    Current density (BB)    Electrodes (CC-EE)
NOVELTY - Oils and fats are transesterified with methanol using lipase (enzyme) which is active at low temperature and room temperature.    USE - Enzymatic biodiesel production.    ADVANTAGE - The method efficiently provides enzymatic biodiesel using liquid carbon dioxide. The enzymatic biodiesel is economical and environmentally-friendly.
NOVELTY - Improving resistance of biodiesel fuels or lubricating oils (used to lubricate engines run on biodiesel fuels) to oxidation, comprises adding to the biodiesel fuel or lubricating oil a combination of at least one detergent (which is alkali metal salicylate, alkali metal phenate, alkaline earth metal salicylate, alkaline earth metal phenate, hydrocarbyl salicylate or hydrocarbyl phenate) and at least one antioxidant (which is hindered phenolic antioxidants, aminic antioxidants or organo metallic antioxidants), where weight ratio (active ingredient) of detergent to antioxidant is 1:99 to 99:1.    USE - The method is useful for improving resistance of biodiesel fuels or lubricating oils (used to lubricate engines run on biodiesel fuels) to oxidation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a mixture comprising a combination of the detergent and the anti-oxidant.
NOVELTY - Upgrading bio-oils to less recalcitrant fuels, comprises esterifying the bio-oil, where the bio-oils are raw bio-oil or pyroligneous bio-oil or a mixture of raw bio-oil and pyroligneous bio-oil.    USE - The method is useful for upgrading bio-oils to less recalcitrant fuels (claimed) or as biocrude, where the bio-oils is useful as a boiler fuel, a turbine fuel or as a fuel to power a slow diesel, or as any combustion fuel for which a mildly upgraded bio-oil is adequate.    ADVANTAGE - The method is cost-effective and less time consuming, provides bio-oils with high yield, and is capable of reducing water content of olefinated product, thus provides bio-oils with improved properties such as higher heating value (HHV).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device (28) for upgrading bio-oil, comprising a tank for containing reactants, a sprayer configured to apply its contents directly to pyrolysis vapor stream, a pump for providing pressure to the sprayer and a controller for controlling the pump pressure and rate of liquid application.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of the pyrolysis reactor injection device.    Pyrolysis reactor (25)    Heated pipe (26)    Condenser(s) (27)    Device (28)    Three spray nozzles. (29)
NOVELTY - Method-1 for fractionating pyrolysis vapors derived from a feedstock into separate fractions comprises manipulating the temperature of at least one condenser.    USE - The method is useful for increasing the anhydrosugar content within a pyrolysis vapor stream, derived from a feedstock, which is biomass or derived from biomass that is derived from an organic source, where the anhydrosugar-rich aqueous fraction or pyroligneous fraction is useful to produce fuel, biochemical or bioproduct (all claimed).    ADVANTAGE - The pretreatment optimizes the efficacy of the catalyst; and increases the production of anhydrosugars content by removing hemi-cellulose from the feedstock. The method is economical. The method reduces the reaction time and the amount of catalyst required for demineralization of the biomass.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a method-2 for increasing the anhydrosugar content within a pyrolysis vapor stream, derived from a feedstock, comprising injecting a liquid or gas into the pyrolysis vapor stream; and    (2) a device for upgrading bio-oil comprising a tank for containing reactants; a sprayer configured to apply its contents directly to pyrolysis vapor stream; a pump for providing pressure to the sprayer; and a controller for controlling the pump pressure and rate of liquid application.
NOVELTY - A system for producing biodiesel includes a reactant supply unit, a transfer unit connected with the reactant supply unit, a static mixing unit connected with the transfer unit, a reaction unit connected with the static stirring unit, a product separation unit connected with the reaction unit, and a purification unit connected with the product separation unit wherein the reactant supply unit provides a liquid reactant including fatty oil, alcohol compounds and catalysts, and the liquid reactant is transferred by the transfer unit to flow through the static mixing unit and the reaction unit to form a product stored by the product separation unit. The product is separated into biodiesel and glycerol in the product separation unit by a static separation method. The biodiesel in the product separation unit is then purified by the purification unit.
NOVELTY - The present invention relates to a method of producing solid state fuels by controlling the water content of agricultural wastes and adapting with forming temperature and pressure, which is mainly performed by controlling the water contents of agriculture wastes such as rice husks, rice stems, hay or any vegetable roots, stems, leaves, and adapting with the forming temperature and pressure, to produce the solid state fuels. Firstly agriculture wastes such as rice husks, rice stems, hay or any vegetable roots, stems, leaves are dried to an average water content of 18 to 30%, then crushing and mixing, as well as adding additives of clay components, adapting with the level of the average water content, extruding and forming at a temperature of 150 to 210 degrees Celsius, and a pressure of 300Psi/cm.sup.2 to 600Psi/cm.sup.2, to form block-shaped solid state fuels.
NOVELTY - An electrode catalyst layer is provided with a catalytic substance having oxide-based non-platinum catalyst, an electroconductive substance and a polymer electrolyte. The electroconductive substance is arranged on the surface of catalytic substance having electroconductivity. A catalyst ink is then produced and applied to form electrode catalyst layer on a base material that is selected from gas diffusion layer transfer sheet and polymer electrolyte membrane.    USE - Manufacturing method of electrode catalyst layer for solid polymer electrolyte fuel cell (claimed) used in vehicle and home.    ADVANTAGE - The electroconductivity of the catalytic substance is improved at the time of formation of an electrode catalyst layer since the electroconductivity is provided to the surface of catalytic substance, thus increasing the reaction activity point and improving the output performance of electrode catalyst layer.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) fuel cell electrode catalyst layer; and    (2) membrane electrode assembly.
NOVELTY - By-product material treatment involves forming a treated material (m) by filtration and centrifugation processes in a tank (4). The obtained treated material includes 0.1-20% of ethanol, 0.1-5% of citric acid, baking soda and 0.1-1% of fluidizing additive in every 10000 liters of the obtained material.    USE - Method for treating by-product material of biodiesel plants or processing equipment of soybean oil, castor oil, Jatropha oil, palm oil and other species of plants (claimed).    ADVANTAGE - The method enables to treat the by-product material in an eco-friendly manner by drastically reduction of emission of pollutants and contaminants, and provides clean burning oil having high calorific value in a cost-effective manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the by-product material removal process in biodiesel processing equipment.    Tank (4)    Heating system (A)    Centrifugal unit (C)    Mixer (MI)    Treated material (m)
NOVELTY - An electrode of a fuel cell including a gas diffusion layer having a carbon fiber and a catalyst layer is provided. The catalyst layer is disposed on the gas diffusion layer. The catalyst layer includes a carbon nanotube, an adhesive layer and a catalyst. One end of the carbon nanotube is connected with the carbon fiber of the gas diffusion layer. The adhesive layer is disposed on the surface of the carbon nanotube. The catalyst is disposed on the adhesive layer.
NOVELTY - A biomass fuel generator including a first moving granular bed, a second moving granular bed, bed materials and a separation device is provided, wherein the first moving granular bed includes a first bed body, a fist bed material entrance, a first bed material outlet, a biomass entrance and a synth-gas outlet, and the second moving granular bed includes a second bed body, a second bed material entrance, a second bed material outlet, a synth-gas entrance and an air entrance. The fist bed material entrance is connected with the second bed material outlet, and the synth-gas entrance is connected with the synth-gas outlet. The bed materials pass through the second bed material entrance to enter the second bed body. Then, the bed materials are guided into the first bed body to heat the biomass. The biomass is transformed to the biomass fuel via heating, and discharges the synth-gas. The synth-gas is guided into the first bed body, and burns in the bed materials inside the second bed body with the air which pass through the air entrance to enter the second bed body. The separation device is suitable for separating the bed materials and the biomass fuel.
NOVELTY - Composition (I) comprises: at least one fluorinated olefin (a) having an magnetic resonance imaging value of less than ethane; and at least one additional component (b) comprising hydrofluorocarbons, ethers, alcohols, aldehydes, ketones, methyl formate, formic acid, water, trans- 1,2-dichloroethylene, carbon dioxide, dimethoxymethane and/or a second fluoroalkene different than the first fluoroalkene.    USE - (I) is provided as a blowing agent, aerosol, solvent, or heat transfer agent (claimed). (I) is useful in numerous applications, preferably heat transfer systems, such as refrigeration systems, blowing agents, fire extinguishing/suppression compositions, foamable compositions, foams and articles made with or from foams, solvents, aerosols, propellants and cleaning composition and compatabilizing agents. (I) is useful in sterilization applications, sprayable composition applications, inflating agent applications and fragrance and flavor applications.    ADVANTAGE - (I) is environmentally friendly. (I) has lessened negative effects on ozone levels in the troposphere. (I) utilizes a lower mass of volatile organic compounds. (I) exhibits: chemical stability; no substantial ozone depleting potential; relatively high degree of miscibility with common contaminants, particularly mineral oil and/or silicone oil; low or no flammability; low or no toxicity; and low or no global warming potential.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a solvent extraction method comprising solvent extracting a material by contacting the material with (a); and    (2) depositing catalyst on a solid support, comprising precipitating particles of the catalyst from (a).
NOVELTY - Microorganism reactive system comprises cascade of two anaerobic bioreactors, where a water outlet pipe on the top of the primary anaerobic bioreactor is in connection with a water inlet pipeline of the secondary anaerobic bioreactor, the anaerobic bioreactor is up flow anaerobic sludge blanket reactor, the water inlet pipe of the primary anaerobic bioreactor is provided with a functional strain feeding unit, and a filler zone is arranged in the secondary anaerobic bioreactor.    USE - The microorganism reactive system is useful for treating waste water and pollutants, and for producing clean energy source.    ADVANTAGE - The microorganism reactive system reduces the domestication time of sludge and shortens production time.    DESCRIPTION OF DRAWING(S) - The figure represents a schematic view of the microorganism reactive system.
NOVELTY - Method for pressing oil and fat from Scenedesmus microalgae, involves separating and obtaining wet algal bodies of Scenedesmus from culture medium, adjusting moisture content of collected microalgae to 5-96 %mass, and squeezing the wet algae.    USE - The method is useful for pressing fat and oil from Scenedesmus microalgae used as fuel and raw material for chemical product and for producing fatty acid alkyl ester and/or glycerol and feed using residues remained after the process (all claimed).    ADVANTAGE - The method produces high yield of fat and oil. The fat and oil as little impact on environment when utilized as fuel. The chemical products are produced without using fossil fuel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing fatty acid alkyl ester and/or glycerol, which involves transesterifying alcohol using the obtained fat and oil.
NOVELTY - Method for extracting oil and fat from Scenedesmus micro algae, involves adjusting the moisture content of Scenedesmus to 5-96 %mass, destructing cell wall of the Scenedesmus, and extracting oil and fat from the processed material.    USE - The method is useful for extracting oil and fat used in fuel, chemical goods and feed (all claimed).    ADVANTAGE - The oil and fat can be extracted in high amount.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for manufacturing fatty acid alkylester and/or glycerol, which involves subjecting the obtained oil and fat tom transesterification reaction using alcohol.
NOVELTY - The method involves circulating inert gas with oxygen concentration of 5-13 volume% for piping between thermal decomposition gasifier (11) and combustion furnace (13). The thermal decomposition attachment adhered to inner wall of piping under conditions of gas temperature of 500 degrees C is burned and removed.    USE - Method for removing biomass thermal decomposition product e.g. sewage sludge and woody biomass adhered to pipe used in petroleum refining industry and petrochemical industry.    ADVANTAGE - The biomass-derived thermal decomposition is safely removed in short time, and life cycle cost of gasification system is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for thermal decomposition gasification system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass thermal decomposition gasification system.    Biomass thermal decomposition gasification system (10)    Thermal decomposition gasifier (11)    Piping (12)    Combustion furnace (13)    Fan (14)
NOVELTY - The apparatus (1) has inside portion (2) in which waste material is stirred, and outside portion (3) in periphery of inside portion. A trolley (5) is arranged above inside portion, such that direction of central line of trolley mutually corresponds to stirring apparatuses (4) in inside portion. The waste material in inside portion is processed by stirring apparatuses rotated by angular movement of trolley along forward and reverse directions. The processed waste material is sent out from inside portion to outside portion via opening (203), and then discharged out.    USE - Fermentation apparatus for aerobic compositing of waste material such as domestic refuse and farm-and-livestock waste material.    ADVANTAGE - The application of stronger angular moment force on the rotating shaft can be avoided by using trolley which can rotate stirring apparatuses, so that damage caused on the stirring apparatuses can be reduced. The efficiency of fermentation apparatus can be improved.    DETAILED DESCRIPTION - An air injection system (11) is provided in inside portion, so as to inject air into waste material in inside portion.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the fermentation apparatus.    Fermentation apparatus (1)    Inside portion (2)    Outside portion (3)    Stirring apparatus (4)    Trolley (5)    Air injection system (11)    Opening (203)
NOVELTY - The carbonization installation has drying apparatus (1), and dry distillation apparatus (2) and dry distillation gas combustion apparatus (4). Dry distillation gas piping (27) guides the dry distillation gas emitted with the dry distillation apparatus to dry distillation gas combustion apparatus. A combustion gas piping (28) guides the combustion gas of dry distillation gas combustion apparatus to drying apparatus. A dry-gas piping (32) guides the dry gas containing a large amount of water vapor generated with drying apparatus to dry distillation gas combustion apparatus.    USE - Carbonization installation of organic wet waste such as sewage sludge, organic refuse and food residue.    ADVANTAGE - Organic waste which contains the moisture content abundantly can be dried, carbonized, and deodorized except the time of start-up of installation, without using fossil fuel. The usage-amount of dry biomass can be lessened, even dry biomasses such as chaff are utilized as auxiliary material. Since the odor generated at the time of drying is thermally decomposed by the secondary combustion of dry distillation gas, a perfect deodorizing can be performed. A dry gas with a possibility that the odor component and hazardous ingredient which are generated with the drying apparatus can be included is exposed to the high temperature of the dry distillation gas combustion apparatus which performs deodorizing and detoxifying process. The deodorizing by the waste gas processing facility and the burden of harmful gas process are eased.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the carbonization installation of organic wet waste.    Drying apparatus (1)    Dry distillation apparatus (2)    Dry distillation gas combustion apparatus (4)    Distillation gas piping (27)    Combustion gas piping (28)    Dry-gas piping (32)
NOVELTY - A metal complex contains dicarboxylic acid compound (I) chosen from dicarboxylic acid compound (Ia) and dicarboxylic acid compound (Ib), metal chosen from magnesium, aluminum and elements of groups 4-12 of periodic table, and organic ligand in which bidentate coordination with respect to metal is possible.    USE - Metal complex is used for material for separating methane, carbon dioxide, carbon dioxide and hydrogen, carbon dioxide and nitrogen, and air and methane (all claimed). Can also be used for separating methanol, benzene, toluene, acetone, methyl ethyl ketone, methyl chloride, chloroform, noble gas, hexamethyl cyclotrisiloxane, nitrogen oxide, etc.    ADVANTAGE - The metal complex has excellent gas-separation performance.    DETAILED DESCRIPTION - A metal complex contains dicarboxylic acid compound of formula (I) chosen from dicarboxylic acid compound of formula (Ia) and dicarboxylic acid compound of formula (Ib), metal chosen from magnesium, aluminum and elements of groups 4-12 of periodic table, and organic ligand in which bidentate coordination with respect to metal is possible.    X=carbon atom or nitrogen atom;    Y'=electron-donating group;and    R1-R3=alkyl optionally substituted by halo.    (i) When X is carbon atom, Y' is alkyl, alkoxy, formyl, acyloxy, alkoxy carbonyl, nitro, amino or amide optionally substituted by halo; (ii) When X is nitrogen atom, Y' does not exist; (iii) When X is carbon atom and Y' is electron-donating group, dicarboxylic acid compound (I) is of formula (Ia); and (iv) When X is carbon atom or nitrogen atom and Y' is electron-attractive group dicarboxylic acid compound (I) is of formula (Ib). An INDEPENDENT CLAIM is included for manufacture of metal complex.
NOVELTY - A hydrogen-producing catalyst is obtained by carrying out reduction-activation process of active metal and perovskite-type complex oxide (I) at 300 degrees C or more.    USE - Hydrogen-producing catalyst is used for manufacture of hydrogen-containing gas used for fuel cell system (both claimed). Uses include but are not limited to internal combustion engine, gas turbine, rocket fuel, heat engine and car.    ADVANTAGE - The hydrogen-producing catalyst has excellent catalytic activity.    DETAILED DESCRIPTION - Hydrogen-producing catalyst is obtained by carrying out reduction-activation process of active metal and perovskite-type complex oxide of formula: AB'O3 (I) at 300 degrees C or more.    A=lanthanum or alkaline-earth metal element;and    B'=metal.    INDEPENDENT CLAIMS are included for the following:    (1) manufacture of hydrogen-producing catalyst;    (2) manufacture of hydrogen-containing gas;    (3) manufacture apparatus of hydrogen-containing gas; and    (4) fuel cell system (10).    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of fuel cell system.    Fuel cell system (10)    Hydrocarbon gas supply device (12)    Oxygen supply device (13)    Modifier (14)    Reformed gas (15)
NOVELTY - Producing butanol comprises: using Clostridium genus microorganisms which can assimilate Glucide/carbohydrate and 0.5-30 g/L of lactic acid; and using the microorganisms which belong to the Clostridium (Clostridium) genus as substrate in butanol production which is possible in an environment (medium) which includes the substrate.    USE - The method is useful for producing butanol (claimed).    ADVANTAGE - The method efficiently produces butanol and effectively utilizes lactic acid and/or an acetic acid in producing bio-butanol.
NOVELTY - Emulsifying composition comprises: N-oleyl-1,3-propylene diamine (5-40 wt.%); N,N',N'-polyoxyethylene-N-tallow propylene diamine (50-95 wt.%); and solvent (5-40 wt.%).    USE - (I) is useful for homogenizing and reemulsifying fuel and for fabricating a fuel (all claimed).    ADVANTAGE - (I) is: stable at low temperatures; stable to sudden temperature changes; oxidation-stable and resistant to bacterial contamination. The mineral oil and/or plant fuel has improved storage stability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) fuel comprising at least one mineral oil, vegetable oil and water, where the fuel further comprises (I);    (2) preparation of (I) comprising: reheating N-oleyl-1,3-propylene diamine and N,N',N'-polyoxyethylene-N-tallow propylene diamine to obtain a first liquid mixture; and adding the solvent to first mixture and stirring; and    (3) fabricating a fuel comprising adding 3-48 wt.% of (I) to a base fuel comprising 0-99 wt.% of a vegetable oil, 0-99 wt.% of mineral oil and 0.01-8 wt.% of water.
NOVELTY - Converting carbonaceous material into methane-rich fuel gas comprises simultaneously heating the carbonaceous material in the presence of both hydrogen and steam in a hydrogasification reactor, at a temperature and pressure sufficient to generate a stream of methane and carbon monoxide rich product gas, where 0.2-60% of methane on a dry mole basis is generated.    USE - The process is useful for converting carbonaceous material into methane-rich fuel gas (claimed), which is useful as a clean burning fuel i.e. a transportation fuel.    ADVANTAGE - The process: generates methane without using further downstream processing or methanators; produces hydrogen, which can be recycled back into the steam hydrogasifier and uses recycled hydrogen as feed, thus eliminating the hydrogen supply problem; provides high concentration and high quantity of methane; simplifies feedstock processing since drying the feed is not necessary; produces methane from abundant domestic feedstocks e.g. sub-bituminous and low grade coal in a cost effective manner; and uses biomass co-mingled with coal, which results in reduced greenhouse gas emissions compared to a coal based methane production plant.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an apparatus for converting carbonaceous material into methane-rich fuel gas, comprising a steam hydrogasification reactor, where the steam hydrogasification reactor is capable of generating 0.2-60% methane on a dry mole basis, without any downstream processors.    DESCRIPTION OF DRAWING(S) - The figure shows the process configuration involving the innovative steam hydrogasification reaction gasification to produce a high methane containing syngas.
NOVELTY - The device has dehydration unit that dehydrates sludge and processes the organic sludge. The dehydrated sludge is pulverized with the centrifugal force by sludge coal assembly unit, so that sludge coal is prepared. The sludge is supplied to multiple extractors between drum and endless track during electric infiltration dehydration mode.    USE - Device for treating sludge in sewage treatment facility and wastewater disposal facility.    ADVANTAGE - The environmental contamination due to ocean dumping of sludge is reduced. The crushing of sludge by centrifugal force of sludge coal assembly unit is facilitated. The problem caused by adhesion of sludge to rotator is suppressed. The drying efficiency is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating the sludge treatment process. (Drawing includes non-English language text)
NOVELTY - The bin has a storage bin main body whose top part is provided with a feeding opening and bottom part is provided with a discharging opening. The main body comprises an upper cylinder body and a lower conical body, and is provided with rotating shafts. Each rotating shaft is sleeved with multiple spiral blades. One of the shafts is arranged in a lower conical body close to an upper side of the discharging opening. The lower conical body is an inclined conical body, and a center line of the discharging opening is biased from a center line of the upper cylinder body.    USE - Biomass storage bin for a biomass gasification furnace.    ADVANTAGE - The bin destroys the internal stress balance of the material through outer side force disturbance. The bin prevents the material with large natural piling angle from being arched while entering the bin. The bin can be favorable to materials with different piling angles, and can enlarge the raw material adaptability of a biomass gasification furnace using the bin.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass storage bin.
NOVELTY - The system has a generator (5) that is driven by a steam turbine. Multiple stages of low pressure heaters and high pressure heaters and a deaerator (12) are connected with a steam extraction unit of the steam turbine. A cascade auxiliary system comprises a biomass gasification device (20) and a paraboloid slot shaped solar energy heat collector (21), where the gasification device and the heat collector are connected in series and arranged between an exit of a feed pump (13) and a steam extraction inlet of one of the stages of the high pressure heaters.    USE - Biomass and solar energy auxiliary fire coal cogeneration system.    ADVANTAGE - The system reduces coal consumption, optimizes utilization structure of an energy source and avoids pollution to a large degree to achieve environment protection.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass and solar energy auxiliary fire coal cogeneration system.    Generator (5)    Deaerator (12)    Feed pump (13)    Biomass gasification device (20)    Paraboloid slot shaped solar energy heat collector (21)
NOVELTY - The technique involves closing a discharge hole valve of a next layer of temporary storage bins. A biomass material is entered into a layer of the temporary storage bins orderly. A charge hole valve of a bottom layer of the temporary storage bins is closed. A discharge hole valve of the bottom layer of the temporary storage bins is opened. The biomass material is entered into a furnace front feeding device i.e. spiral delivery device.    USE - Furnace front feeding technique for a biomass gasification system.    ADVANTAGE - The technique obtains the reverse jump phenomenon of the gas generated by a biomass gasification furnace via the furnace front feeding device, and reduces the danger of casing bin to be fired or exploded due to fuel reverse jump.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of a furnace front feeding technique for a biomass gasification system. '(Drawing includes non-English language text)'
NOVELTY - The technique involves mounting two fluidized bed gasifying reactors in a parallel manner. A biomass raw material and a gasifying medium are added in each fluidized bed gasifying reactor. The fluidized bed gasifying reactor is enabled to independently react to generate gas. A heavy material flow is returned back in a separating device to the fluidized bed gasifying reactor for reacting. A light material flow is entered in the separating device into another separating device or a gas branch pipeline.    USE - Biomass gasifying parallel reacting technique.    ADVANTAGE - The technique provides flexibility for fitting different yield requirements and independent maintenance.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a biomass gasifying parallel reacting technique.'(Drawing includes non-English language text)'
NOVELTY - The process involves feeding a biomass raw material and a gasification medium into a fluidized bed gasification reactor. The biomass raw material and the gasification medium are made to react to produce gas. A material flow in a separation device is separated into light material flow and a heavy material flow. The heavy material flow is returned to the fluidized bed gasification reactor. Another material flow is passed into the separation device or directly into a gas pipe.    USE - Multistage circulation gasification process for biomass.    ADVANTAGE - The process enables complete reaction between the biomass raw materials and improves gasification efficiency so to reduce generation of tar and dust.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of a multistage circulation gasification process for biomass. '(Drawing includes non-English language text)'
NOVELTY - The system has fluidized bed gasification reactors arranged in parallel for preparing biomass fuel gas. Two stages of separation devices are installed at an outer side of the gasification reactors for separating reaction products. A biomass raw material supplying system provides a reaction raw material to the gasification reactors. A gasification medium supplying system provides gasification media for the gasification reactors. A feeding opening of the gasification reactors is engaged with the biomass raw material supplying system.    USE - Biomass gasification parallel reaction system.    ADVANTAGE - The parallel fluidized bed gasification reactors can react at the same time. The system increases the yield of the fuel gas, lifts the fuel gas yield about multiple times, and controls the output fuel gas flow by controlling on-off of each fluidized bed gasification reactor. The system avoids influencing the normal circulation of other reactors when one reactor or the accessory device has a fault to maintain.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass gasification parallel reaction system.
NOVELTY - The device has a rotary shaft installed in a cylinder body. The rotary shaft is sleeved with a spiral blade. An end of the cylinder body is provided with a slag feeding opening and another end is provided with a slag discharging opening. The cylinder body is obliquely arranged. The slag discharging opening is higher than the slag feeding opening. The slag feeding opening of the cylinder body is connected with a waste outlet of a bottom part of a biomass gasifying furnace. The slag discharging opening is connected with a water box.    USE - Closed slag discharging device for a biomass gasifying furnace.    ADVANTAGE - The device utilizes the propelling force of the spiral blade to stably discharge the ash slag, and has inclined structure to prevent the smoke or the reaction gas from being leaked by the slag discharging device.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial sectional view of a closed slag discharging device for a biomass gasifying furnace.
NOVELTY - The system has a biomass raw material supplying system for providing reaction raw material to a fluidized bed gasifying reactor. Two grades of separating devices are installed beyond the fluidized bed gasifying reactor. The grades separate a reaction product of the fluidized bed gasifying reactor. The grades of the separating devices are provided with two separating devices. A gasifying medium supply system provides a gasifying medium to the fluidized bed gasifying reactor. A feeding port of the fluidized bed gasifying reactor is connected to the biomass raw material supplying system.    USE - Biomass gasifying reaction system.    ADVANTAGE - The system utilizes biomass forming fuel such as wood dust, wood powder, rice husk or crushed biomass materials, to produce biomass combustible gas in the system. The biomass forming fuel can be utilized in an industrial boiler and kiln to perform clean burning of fossil fuel such as natural gas and diesel, and as domestic use gas, so that biomass waste can be utilized efficiently. The system is environment-friendly, and obtains clean renewable energy resource.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass gasifying reaction system.
NOVELTY - The device has multiple parallel independent buffer cabins provided with a feeding port. A bottom part of a work cabin is provided with a discharging port. The buffer cabins are installed on an upper part of the work cabin. The buffer cabins and the work cabin are connected via gas locking devices e.g. narrow passage. The discharging port at the bottom part of the work cabin is provided with a valve, where the valve is a roller valve or a ball valve.    USE - Biomass furnace material storing device for a biomass gasifying reaction system (claimed).    ADVANTAGE - The device has gas locking structure, which can prevent the leakage of the reaction gas in a reaction system such as the fluid bed gasifying reactor when the outer side feed is smooth.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biomass gasifying reaction system comprising a fluid bed gasifying reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass furnace material storing device for a biomass gasifying reaction system.
NOVELTY - The device has a drive device connecting a rotating axis that is sleeved with a spiral lamina. An external circumference of the rotating axis is sleeved with a feeding pipe. An airlock structure is provided between a feeding device and a martial outlet port. The airlock structure makes intensity at a biomass raw material in the feeding pipe that is higher than that of an adjacent biomass raw material to form a relatively hermetic structure. The airlock structure is provided with a final end of the rotating axis.    USE - Airlock feeding device for a biomass gasifying reacting system (claimed).    ADVANTAGE - The device prevents the production of the fluidized bed gasifying reactor fuel gas from leaking into the air or the material storing device in the front part of the furnace via the feeding device, and avoids the dangers of the self-burning, exploding and stuff poisoning that is caused by the fuel gas leaking, thus protecting the safeties of the equipment, the raw material and the working stuff.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial sectional view of an airlock feeding device for a biomass gasifying reacting system.
NOVELTY - The device has a water sealing device for controlling pressure in biomass combustible gas pipes. A diffusing pipe discharges superfluous biomass combustible gas. An end of the diffusing pipe is connected with the water sealing device. A biomass combustible gas portfire inflames the superfluous biomass combustible gas, where the portfire occurs at an outlet end of the diffusing pipe. The water sealing device is provided with a water container, outer cover, inner cover and a pull rod. A bottom part of the water container is opened with a through hole.    USE - Biogas diffusing device for a biomass gasification reaction system (claimed).    ADVANTAGE - The device can be utilized within a short term, and increases the internal pressure in the pipe of the whole biomass fuel gas system when the biomass is not discharged timely. The device can stop when fault is occurred, and avoids big accident such as explosion.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biogas diffusing device for a biomass gasification reaction system.
NOVELTY - The method involves entering cooled flammable gas into a tar separator after being mixed with a biomass raw material through a Venturi tube. A biomass raw material is utilized as an absorption medium. An adhering carrier for tar liquid is utilized to allow condensed tar liquid drops to absorb and adhere to a surface of the biomass raw material. Purified flammable gas is entered into a filter. Tar in flammable gas is condensed after arriving in the tar separator, where the tar is absorbed and bonded by the biomass raw material.    USE - Separation method for depriving tar from biomass gasified flammable gas.    ADVANTAGE - The method enables controlling secondary pollution of the tar, ensures separation of the tar and continuous long-term operation of the system without generation of sewage. The method allows reducing the load of the filter and the time of replacing filtration medium of the filter so that a device for implementing separation method can be operated continuously for a long time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for implementing separation method for depriving tar from biomass gasified flammable gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic illustration of separation method for depriving tar from biomass gasified flammable gas. '(Drawing includes non-English language text)'
NOVELTY - A composite diesel oil comprises (pts.wt.) methanol (76-82), diesel oil (8-11), gasoline oil (5-7), ethanol (3-6), ferrocene (0.02), and cerium nitrate (0.08).    USE - A composite diesel oil.    ADVANTAGE - The composite diesel oil is cheap, and has simple preparation method and high methanol content.
NOVELTY - The furnace has a gasifying agent T-shaped pipe whose end is connected to a fan air feeding port and another end is connected to an air feeding end of a secondary air distributing pipe of a combustion stove. A third end of the T-shaped pipe is fixed to a flame stove secondary air distributing pipe with a flame stove adjusting valve. An air outlet end of a gasifying feeding pipe is penetrated through a dust case and a soleplate shell of a gasifying device and communicated with inside of a gasifying agent configuring device. A gasifying agent adjusting valve is placed on an air feeding pipe.    USE - Integrated biomass burning and gasifying furnace.    ADVANTAGE - The biomass can be directly burned in the furnace body. The furnace has wide raw material, full combustion, environmental protection, saved energy and rational structure, and is safe and convenient to use.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of an integrated biomass burning and gasifying furnace.
NOVELTY - This invention is a method of producing bodiesel, and more particularly to provide a method that produces extremely high purity biodiesel at low costs mainly comprising steps of mixing vegetable oil, animal oil with methanol, uniformly mixing the extremely fine molecules by passing a ultrasonic vibrator, then performing a transesterification reaction induced by the mixing of a slow- flow mixer and a high speed vortex device for many times to produce glycerol and methanol, then mixing them with water and separating impurities, water, high purity methanol from the mixture through a high speed contrifugal machine, and finally performing heating distillation to obtain the pure biodiesel.
NOVELTY - An apparatus to extract biodiesel from chicken fat, is provided. The apparatus includes a stirrer (222) to process a mixture of chicken fat oil with a standardized solution, to form a reaction mixture (202). The standardized solution is a combination of methanol in 20-50% by volume and at least one of sodium hydroxide and potassium hydroxide in 0.1-3% by volume, and hydrochloric acid catalyst in 0.1-3% by volume. The chicken fat oil is obtained by heating the chicken fat. The reaction mixture forms two distinct layers of an impure biodiesel and a glycerol. The reaction mixture is kept below the boiling point of the alcohol. A separating funnel is used to separate the impure biodiesel and the glycerol. The biodiesel is extracted, by refining the impure biodiesel with hot water. The biodiesel is heated to remove traces of moisture. Image 0/1
NOVELTY - A solid oxide fuel cell comprises fuel electrode (2) which is arranged at one surface side of solid electrolyte (1), air electrode (3) which is arranged at other surface of solid electrolyte, and porous reformation material (4) which contacts with fuel electrode and has steam reforming catalyst.    USE - A solid oxide fuel cell.    ADVANTAGE - The solid oxide fuel cell has improved performance.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the solid oxide fuel cell.    Solid electrolyte (1)    Fuel electrode (2)    Air electrode (3)    Reformation material (4)
NOVELTY - A to-be-processed gas is preheated through a heat exchanger (3), and methane is subjected to catalytic oxidation using an oxidation catalyst (2). The gas is again passed through heat exchanger and heat is recovered by heat exchange with unreacted gas. The flow rate of to-be-processed gas with respect to oxidation catalyst is varied based on methane concentration of gas. The flow rate of gas to catalyst is increased when methane concentration is high, with respect to flow rate of gas to catalyst when methane concentration is low.    USE - Method for removing low concentration methane from to-be-processed gas discharged from ventilation of pit (claimed) of gas engine and turbine.    ADVANTAGE - The low concentration methane is stably and economical removed from the to-be-processed gas for long period of time using catalyst having high durability and inexpensive piping and heat exchanger.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for removal apparatus (100) of low concentration methane, which has heat exchanger for heat exchanging between air blower (1) for introducing gas, and oxidation catalyst, a detection unit (4) of methane concentration, and a control unit (5) for increasing flow rate of gas.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of apparatus used for removing low concentration methane. (Drawing includes non-English language text)    Air blower (1)    Oxidation catalyst (2)    Heat exchanger (3)    Detection unit of methane concentration (4)    Control unit (5)    Removal apparatus of low concentration methane (100)
NOVELTY - Denitrifying reactor capable of producing methanol, using hydrogen donor or nitrite nitrogen obtained from wastewater is performed by denitrifying bacteria. The performance of denitrifying reactor is decreased when activity of microorganism is increased. The activity of microorganism is decreased using hydrogen donor as organic substance. The performance of denitrifying reactor is improved and thus reactor is recovered.    USE - The denitrifying reactor is useful for producing methanol.    ADVANTAGE - The performance of denitrifying reactor can be recovered within short period of time.
NOVELTY - The method involves mixing a wood vinegar and a biomass with grain size less than 80 meshes, carrying out reaction in a slurry bed reactor in reducing gas e.g. carbon monoxide, and controlling liquefaction temperature to be 300-450 degrees centigrade, where a metal ion of the wood vinegar is more than 0.3 percent. and is selected from potassium, sodium, calcium, magnesium, iron, chromium and nickel.    USE - Method for preparing fuel oil using a wood vinegar.    ADVANTAGE - The method uses the wood vinegar to prepare fuel oil, which reduces production cost, and improves yield of oil product with better environment and economic benefits.
NOVELTY - The system has multiple combustion devices that are located in a heating furnace and a fuel gas pipeline for transporting biomass gas. The combustion devices are respectively mounted at two sides of a furnace wall and a discharging end of the heating furnace. The fuel gas pipeline comprises a fuel gas main and fuel gas branches. An inlet of the fuel gas main is installed above a tail part of the heating furnace. The combustion device is connected to the fuel gas main through the fuel gas branches.    USE - Biomass gas combustion system.    ADVANTAGE - The system is designed such that even temperature in the heating furnace is guaranteed by a cross array process of combustion devices on a kiln wall, thus increasing combustion efficiency of biomass gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass gas combustion system.
NOVELTY - The system has a biomass fluidized-bed gasification reactor preparing biomass gas. A biomass material supply system supplies reaction material to the biomass fluidized-bed gasification reactor. A separating device separates a reaction product of the biomass fluidized-bed gasification reactor. A gasification medium supply system supplies a gasification medium to the fluidized-bed gasification reactor. Feed inlets are arranged in intermediate area. A gasification medium inlet and a waste outlet are mounted on bottom part of the intermediate area.    USE - Biomass gas metallurgical iron and steel heating furnace system.    ADVANTAGE - The system produces combustible biomass gas by using the biomass gasification reaction system. The gasification reaction systems are connected in parallel so as to supply air to heating furnace, thus saving transportation cost, and reducing environmental pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass gas metallurgical iron and steel heating furnace system.
NOVELTY - An ecological floating island carrier comprises an upper plant supporting layer, a middle cultivation layer and a bottom supporting layer from the top to bottom.    USE - Ecological floating island carrier for sewage treatment and water body restoration.    ADVANTAGE - The carrier can prevent plants from tilting and keep sprout growth state.    DETAILED DESCRIPTION - An ecological floating island carrier comprises an upper plant supporting layer, a middle cultivation layer and a bottom supporting layer from the top to bottom. The upper plant supporting layer is polyethylene net or stainless steel screen. The middle cultivation layer sequentially comprises composite elastic padding and a steel wire net framework from the top to bottom. The composite elastic padding is fixed on the steel wire net framework; the bottom supporting layer is sequentially composed of composite elastic padding, a steel wire net framework and a polyethylene net, the composite elastic padding is fixed on the steel wire net framework, the steel wire net framework is fixed on the polyethylene net; the distance between the middle layer and the bottom layer is 2-3 times as large as that of the upper layer and the middle layer; 4-8 locating ropes are arranged on the outer edges of the four surfaces of the upper, middle and bottom layers for connecting the three layers into a whole.
NOVELTY - Liquid fuel preparation involves pretreating collected sandy shrubs and then pouring pretreated sandy shrubs into a high-pressure reaction kettle to form a mixed solution in a certain solid-liquid ratio. Inert gases are introduced with a certain pressure into the reaction kettle. The mixture is stirred and heated at 200-450 degrees C for 5-120 minutes and then the mixture is cooled to room temperature. The obtained reaction mixture is collected and then extracted by using an organic solvent, where the organic phase is separated and filtered to remove the organic solvent to obtain bio-oil.    USE - Method for preparing liquid fuel by performing hydrothermal liquefaction of sandy shrubs (claimed).    ADVANTAGE - The method is suitable to prepare liquid fuel by performing hydrothermal liquefaction of various sandy shrubs in a simple and cost-effective manner.
NOVELTY - Solid biofuel preparation involves utilizing two bins (1,2), where first bin is used for vegetable carbon, mineral carbon or artificial carbon and the second bin is used for biomass. Two conveyor belts (3,4) are used for conveying their respective carbon content and biomass into a tape (5). A collecting hopper (6), a feeder (7), a mouthpiece (8), an oven dryer (9) and a generator (10) are also used in the preparation of solid biofuel. The feeder is used for transferring the material into the mouthpiece.    USE - Method for preparing solid biofuel used for producing energy (claimed).    ADVANTAGE - The method enables to prepare solid biofuel with low emission of carbon dioxide.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the solid biofuel preparation method.    Bins (1,2)    Conveyor belts (3,4)    Tape (5)    Collecting hopper (6)    Feeder (7)    Mouthpiece (8)    Oven dryer (9)    Generator (10)
NOVELTY - Preparing ibuprofen degrading microbial inoculum comprises (i) inoculating activated slurry obtained from secondary depositing basin of sewage processing plant into a culture medium, culturing by gradient pressure method, standing, collecting the upper layer water sample, gradient dilution and marking to separate, culturing and purifying, inoculating the separated bacterial strain into beef extract peptone culture medium, vibration-culturing, and (ii) inoculating the cultured bacterial strain into a culture medium and culturing; the bacterial number after fermenting is more than 1 billion/ml.    USE - The method is useful for preparing ibuprofen degrading microbial inoculum.    ADVANTAGE - The method is simple and low in cost. The ibuprofen degrading microbial inoculum is easy to use, highly efficient for degrading ibuprofen, easy to inactivate bacterial strain and can remove ibuprofen in water treatment process.    DETAILED DESCRIPTION - Preparing ibuprofen degrading microbial inoculum comprises (i) inoculating activated slurry obtained from secondary depositing basin of sewage processing plant into a culture medium, in which the inoculating amount is 5-10 %, culturing by gradient pressure method, in which the ibuprofen concentration is 10-35 mg/l, standing, collecting the water sample at the upper layer, gradient dilution and marking to separate, culturing for 48-60 hours at 30-35 degrees C and purifying, inoculating the separated bacterial strain into beef extract peptone culture medium, vibration-culturing to exponential phase, and (ii) inoculating the cultured bacterial strain into a culture medium, in which the inoculating amount is 10-20 %; in the culturing process, the output of sterile air is 1:0.6-1.2, the stirring speed is 180-240 revolution/minutes, the culturing temperature is 30-35 degrees C, the culturing time is 48-60 hours and the bacterial number after fermenting is more than 1 billion/ml.
NOVELTY - The device has pre-treatment unit which is divided into left and right regions provided with aerator (14) and biological filter (15). The water outlet pipe (16) is inserted into an open trench and wet land system. The open trench and wet land system has permeating plate (22) which is vertically positioned to form a front region filled with gravel and a back region filled with natural soil and coal slag.    USE - Dispersive sewage disposal device.    ADVANTAGE - The device is economic and convenient to use. Treatment of dispersive sewage in wide rural region can be facilitated. Biological pre-treatment process can be enhanced so that operation load can be suppressed and long-term steady operation can be ensured.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the dispersive sewage disposal device. (Drawing includes non-English language text)    Pre-treatment device housing (11)    Water inlet pipe (12)    Aerator (14)    Biological filter (15)    Water outlet pipe (16)    Permeating plate (22)
NOVELTY - The reacting device has a feeding inlet that is provided at the top portion of casing. A material hopper is connected at the lower region of casing. A discharging outlet is provided at bottom region of the material hopper. A hollow chamber is provided in the casing while casing is connected with stirrers. The ventilating pipelines are fixedly connected with the casing to connect inner and outer portions of the casing.    USE - Vertical biochemical reacting device.    ADVANTAGE - The continuous processing of the organic waste is realized dynamically and the odor is processed integrally and conveniently. The occupied area of the reacting device is saved and industrial processing of organic waste is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the vertical biochemical reacting device.
NOVELTY - The method involves changing vapor into steam by utilizing a waste heat boiler (6), and discharging water coal gas from top of the waste heat boiler. The water coal gas is mixed with the purified coal gas discharged from a raw coal gas purifying device (3). Steam produced in a coke powder boiler (8) is discharged from a side surface of the waste heat boiler. Water passed in the coke powder boiler is heated to generate the steam and ash. Part of the steam is mixed with the steam discharged from the waste heat boiler. The ash is discharged from a lower part of the coke powder boiler.    USE - Method for preparing coal tar, coal gas and steam through pulverized coal comprehensive utilization.    ADVANTAGE - The method enables saving energy, reducing the production cost for the coal tar, the coal gas and the steam and deeply processing the coal tar product to produce fine chemical engineering product such as benzene and naphthalene. The coal gas product can be utilized for producing the synthesized ammonium and the synthesized methanol, and can be utilized as the cleaning fuel for electricity generation, industrial boiler and civil use. The ash can be utilized for producing building material.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic illustration of a coal tar, coal gas and steam preparing method. '(Drawing includes non-English language text)'    Raw coal gas purifying device (3)    Airflow pyrolyzing pipe (4)    Waste heat boiler (6)    Part gasifying pipe (7)    Coke powder boiler (8)
NOVELTY - The gasifier has an umbrella-shaped ash-unloading disc placed on an upper part of a rotary shaft, and an ash scraper placed on a lower part of the umbrella-shaped ash-unloading disc. A rotary bearing and a rotary gear base are placed on a middle part and a lower part of the rotary shaft, respectively. A rotary gear is placed on a periphery of the rotary gear base. A fireproof lining support ring is placed on a middle-lower part of a gasifier cavity. A furnace body support is placed on a lower part of a furnace body water jacket.    USE - Renewable energy comprehensive gasifier for producing combustible gas.    ADVANTAGE - The gasifier can crack the municipal domestic waste in mixed fuel and harmful and poisonous combustible substance generated in the sewage treatment plant at the high temperature in an inexpensive manner, reduces atmospheric pollution, saves energy and protects ecological environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for producing a combustible gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a renewable energy comprehensive gasifier.
NOVELTY - The cracking furnace has a boiling gasifying furnace (2) obliquely placed on an upper side of a fuel gas primary purifying chamber (14) whose upper part is provided with an inserting plate fire grate (9), where a bottom of the boiling gasifying furnace is provided with a gasifying agent inlet (4). A fixed bed catalytic cracking section (15) is arranged from a lower side of a central line of a gasifying agent nozzle (6) to an upper side of the inserting plate fire grate. An upper part of the boiling gasifying furnace is provided with a material inlet (3) and an igniting hole (13).    USE - Pyrolyzing and gasifying cracking furnace for solid biomass.    ADVANTAGE - The cracking furnace improves quality of the fuel gas, prevents generation of harmful gas such as dioxin, reduces carbon dioxide emission, and increases the output of the combustible gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of a pyrolyzing and gasifying cracking furnace.    Boiling gasifying furnace (2)    Material inlet (3)    Gasifying agent inlet (4)    Gasifying agent nozzle (6)    Inserting plate fire grate (9)    Igniting hole (13)    Fuel gas primary purifying chamber (14)    Fixed bed catalytic cracking section (15)
NOVELTY - The process involves performing a dry distillation process on solid biomass to form biological coke and dry distillation gas, and conveying the biological coke and dry distillation gas to a thermal cracking gasification furnace to perform high-temperature splitting process on the biological coke and the dry distillation gas. A catalytic pyrolysis process is performed on the dry distillation gas in a fixed bed composed of metallurgical coke block catalyst. Solid biomass is dried.    USE - Solid biomass gasifying and splitting process.    ADVANTAGE - The process enables splitting the tar completely by the dry distillation gasification or thermal cracking gasification, thus preventing and treating tar sewage, and preventing heavy metal salt from polluting the environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a solid biomass gasification pyrolysis system comprising a dry distillation furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a solid biomass gasification pyrolysis system. '(Drawing includes non-English language text)'
NOVELTY - A packaging flat film bio-reactor for sewage treatment comprises film bracket (7) with flat film elements consists of supporting plate (1) and film (2). The films are arranged on 2 lateral surfaces of the supporting plate. The supporting plate is fixed to the lateral edges of the films through pressing plates (3). The thickness of the pressing plates on 2 sides is larger than the pressing plates at upper and lower sides. The upper pressing plate has a pumping tube (4), and the suction tubes on the multiple flat film elements are connected to a general suction tube (8) through water tubes.    USE - Packaging flat film bio-reactor for sewage treatment of city, industrial and domestic waste water.    ADVANTAGE - The bio-reactor has good backwashing efficiency, strong anti-pollution capacity, large film flux, long service life, high water yield, sufficient and uniform aeration, cleaning is convenient, and operation is simple, long and low cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-section of the packaging flat film bio-reactor.    Supporting plate (1)    Film (2)    Pressing plates (3)    Pumping tube (4)    Film bracket (7)    Suction tube (8)
NOVELTY - A deep separating type outside loop biological film reactor comprises inner chamber (1) which is column-shaped, outer chambers (2) which are arranged at outside of inner chamber, padding for bearing biological film which is installed in outer chamber, jet aerator (6) which is arranged at the bottom of inner chamber, and round holes (4) located in same horizontal plane which are arranged at the upper part and bottom part of side wall between inner chamber and outer chamber.    USE - A deep separating type outside loop biological film reactor.    ADVANTAGE - The reactor can effectively degrade bacterium of harmful substance in sewage to improve processing effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of deep separating type outside loop biological film reactor.    Inner chamber (1)    Outer chambers (2)    Round holes (4)    Baffle plates (5)    Jet aerator (6)
NOVELTY - Solar sewage treatment system for artificial wetland comprises: a settling tank respectively connected to a grid tank and an undercurrent artificial wetland by a pipe, a solar off-grid generation system electrically connected with a sewage submersible pump for providing power. The bottom part of the settling tank comprises the sewage submersible pump. The sewage in the settling tank is pumped into the pipe connected with the undercurrent artificial wetland by the sewage submersible pump to flow to the undercurrent artificial wetland.    USE - Used as a solar sewage treatment system for artificial wetland.    ADVANTAGE - The solar sewage treatment system utilizes the solar off-grid generation system to convert the solar energy into the electric power for purifying the sewage in remote areas and countries, which have power difficulty and thus saves resources.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the solar sewage treatment system.
NOVELTY - The device has a biomass powder supply device (5) whose conveying pipe outlet is connected with a combustion material inlet of a composite oxygen-enrichment biomass gasification furnace (8). A conveying pipe outlet of a gasification material supply mechanism (7) is connected with a gasification material inlet of the furnace. A gasification chamber spiral and crushing device (9) is placed at bottom of a gasification chamber in the furnace. A three-stage oil and gas separating system (16) is connected with a constant pressure gas storage cabinet (21) by a Roots blower (19) and a water seal (20).    USE - Biomass gas preparation device.    ADVANTAGE - The device can supply large-scale industrial gas and urban gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass gas preparation device.    Biomass powder supply device (5)    Gasification material supply mechanism (7)    Composite oxygen-enrichment biomass gasification furnace (8)    Gasification chamber spiral and crushing device (9)    Three-stage oil and gas separating system (16)    Roots blower (19)    Water seal (20)    Constant pressure gas storage cabinet (21)
NOVELTY - A methane generation device comprises a cylinder formed by a cellar type cylindrical container made by the reinforced concrete, a top cover, and a sealed air pressure reservoir; where the top cover is arranged on the top opening of the cylindrical container in a sealed manner; the top cover is set with an exhaust port for connecting a gas pipeline; the upper part of the sidewall of the cylindrical container is set with a feed inlet; the lower part of sidewall is set with a slag outlet; and the bottom of air pressure reservoir is connected with lower part of cylindrical container by a pipeline.    USE - The methane generation device is useful for industrial and commercial applications.    ADVANTAGE - The methane generation device is convenient to use; and the sealing performance of the reinforced concrete is reinforced and the service life is long.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the methane generation device.
NOVELTY - The system has fan that is fixed on ground. An air outlet of fan is connected with air inlet of main pipeline. The main pipeline is provided with outlets which are respectively connected with grade pipelines. Each grade pipeline is provided with outlets connected with another grade pipelines, so that the air ventilation between fan and grade pipeline is performed. The bottom lateral wall of grade pipeline is provided with a ventilating port.    USE - Vertical gas-distributing system for aerobic composting material fermenting cabin.    ADVANTAGE - The cleaning and maintaining cost of gas supply system is reduced. The cost can be efficiently reduced. The stacked material inside the fermenting cabin can be prevented from accumulating during gas supply process. The material discharge fermenting cabin can be prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the vertical gas-distributing system.
NOVELTY - The device comprises a fermenting kettle and cover board (6) fixed on top of kettle by a bolt (7). An agitating device has a shaft sleeve (12) that is welded on the cover board and an agitating shaft (9) vertically installed on the kettle by the shaft sleeve with lower end located inside the kettle and upper end located outside the kettle. The handle (10) is arranged on upped end of the agitating shaft. The impeller component (8) is arranged on lower end of agitating shaft.    USE - Methane preparation device for producing methane using plant straw and livestock manure as raw materials.    ADVANTAGE - Methane preparation device is capable of sufficiently agitating fermentation material, eliminates a dross layer of liquid material, prevents air exhaust blockage and improves accuracy and security of experiment. Methane preparation device is simple in structure, occupies less space and ensures reliability.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the methane preparation device.    Cover board (6)    Bolt (7)    Impeller component (8)    Agitating shaft (9)    Handle (10)    Shaft sleeve (12)
NOVELTY - The indigenous flora block is formed by taking 61 to 65 wt% indigenous flora cultivation mud containing 48 to 55% water, 23 to 28 wt% calcium hydroxide, 2 to 3 wt% granular sugar, 1.5 to 3 wt% calcium peroxide and 4 to 5.5 wt% sticky rice paste, mixing and agitating materials and pressing in mould. The flora cultivation is formed by extracting river and lake bottom mud sample. A facultative anaerobic cultivation is performed for strain and reproducing flora. The flora is put in hibernation by adjusting through anaerobic treatment to obtain flora cultivation mud.    USE - Indigenous flora block for processing river and lake pollution.    ADVANTAGE - The indigenous flora is convenient to stacked and transported, and when thrown into river or lake, the contained indigenous flora can rapid reproduce and decompose organic pollutant in the water portion of river and lake, so as to eliminate the black and smelly water.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating indigenous flora block for processing river and lake pollution. (Drawing includes non-English language text)
NOVELTY - The method involves building a tunnel and installing a methane tank in tunnel. The methane generated by methane tank is used as energy to preserve heat of methane tank by tunnel in winter. The carbon dioxide (CO2) generated by combustion of methane is collected in a living quarter by a gas collecting device. The CO2 is released into tunnel according to proportion by a gas releasing device in order to increase CO2 content in tunnel and yield of crops. The straw and residual leaves of crops are used in tunnel as a raw material of fermentation in methane tank.    USE - Combination method of methane tank-tunnel in country side for energy utilization aspects.    ADVANTAGE - The rational allocation and the utilization of the resources are achieved. Moreover the problem heat preservation of the methane tank is solved with lowest energy consumption. Since the CO2 is collected by the gas collecting device the emission of CO2 is reduced at the same time CO2 content in the tunnel s improved. Hence the prominent effect is achieved in increasing the yield.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the methane tank-tunnel during combination process.
NOVELTY - Preparation of 4,5-dihydroxy-9,10-dioxo-9,10-dihydro-anthracene-2-carbaldehyde from 1,8-dihydroxy-3-hydroxymethyl-anthraquinone comprising of aerial oxidation of 1,8-dihydroxy-3-hydroxymethyl-anthraquinone at oxygen pressure of 1-2 bar in presence of a transition metal complex, a co-catalyst and optionally an oxidizing agent in an organic solvent such as 1,4-dioxane, water or mixtures at a temperature of 25-100 degrees C, isolation by appropriate process and optional purification of the product.    USE - The process is useful for preparing 4,5-dihydroxy-9,10-dioxo-9,10-dihydro-anthracene-2-carbaldehyde from 1,8-dihydroxy-3-hydroxymethyl-anthraquinone (claimed).    ADVANTAGE - The process is economical, eco-friendly and hazard free.
NOVELTY - Biomass residue is prepared by burning the bagasse of sugar cane.    USE - Biomass residue used for generating energy and used as an agent for absorbing sulfur gas, preferably exhaust gas (claimed).    ADVANTAGE - The biomass residue has improved exhaust gas absorbing efficiency.
NOVELTY - A combustible solid fuel source comprises a base material containing cellulosic or fibrous organic material, and combustible oil (less than 50 weight%) absorbed into the base material. The base material is arranged, such that the content of ash during combustion of combustible solid fuel source is less than 10 weight%. The base material has density of 50 lba/ft3 or more.    USE - Combustible solid fuel source is used in power station.    ADVANTAGE - The combustible solid fuel source is manufactured efficiently without affecting the environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of combustible solid fuel source, which involves compressing the base material containing cellulosic or fibrous organic material, reducing the moisture content of the base material to less than 15%, and contacting the base material with combustible oil.
NOVELTY - Animal fat recovering involves heating animal fat in a furnace with a combustion unit (3) for obtaining a mixture of oil and water. The obtained mixture is processed for separating oil and water by using separators or decanters, where separated oil is stored in a tank. The stored oil is used as heating medium in combustion equipment system for heating and melting more fat, where the rest oil is transferred to make biodiesel fuel.    USE - Method for recovering animal fat from waste of slaughterhouses and animal processing industry for power generation or oil production for industrial use (claimed).    ADVANTAGE - The method provides animal fat easily in a cost-effective and eco-friendly manner by using the animal waste materials.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an animal fat recovering system, which comprises a food supply unit, a combustion furnace and a separator or decanter outlet to separate oil and water.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram depicting components, equipment or devices of the animal fat recovering system. (Drawing includes non-English language text).    Tank (1)    Oven (2)    Combustion unit (3)    Burner (4)    Separator or decanter (5)
NOVELTY - A solid fuel product comprises ground particulate form biomass material (1), bituminous material (4) (less than 10 %mass) and recycled rubber material (2) (less than 40 %mass) which binds the biomass material and the bituminous material, and has moisture content of less than 10%. The biomass material is contained in major amount.    USE - Solid fuel product for use in energy facility, industrial boiler, pulp and paper industries, and cement industry.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing the solid fuel product, which involves grinding biomass material, drying biomass material, grinding recycled rubber material, mixing ground material with bituminous material, and heating obtained mixture.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the rubber recycling process into biomass fuel.    Biomass material (1)    Recycled rubber material (2)    Petroleum coke (3)    Bituminous material (4)    Drum dryer (11)
NOVELTY - Pellet comprises (in wt.%): cellulosic material (25-75) and waxed cellulosic material (14-75).    USE - The pellet is used in fuel.    ADVANTAGE - The pellet has excellent combustible property and can be prepared in any size and shape.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing pellet, which involves crushing cellulosic material, waxed cellulosic material and liquid, measuring humidity content of the mixture, regulating the humidity content of the mixture, and forming a pellet.
NOVELTY - System comprises a tank, where domestic or industrial sewage and pollutant gases are introduced into the tank. The mixture of industrial sewage and pollutant gases is treated with reagents and required components to optimize process.    USE - System for producing biogas and used in multiple industrial processes such as electricity, steam, lime, cement, pig iron, steel and methane production, where methane is used as fuel for steam turbine and an electrical generator (all claimed).    ADVANTAGE - The system ensures improved biogas production.
NOVELTY - Briquettes manufacturing involves agglomerating renewable source of plant material including extract of Syagrus fruits. The extract clumps, hardens and binds the charcoal briquettes without altering the physical-chemical aspects of original coal.    USE - Method for manufacturing briquettes from charcoal (claimed).    ADVANTAGE - The method provides charcoal briquettes with 5 mm diameter central hole, uniform drying and improved quality in an eco-friendly manner. The method also allows reuse of waste charcoal generated from coal bunker, transport, storage and cleaning of coal.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for manufacturing briquettes, which comprises a pulper for pulping disks of fruit.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of charcoal briquettes drying process. (Drawing includes non-English language text).
NOVELTY - Production of molecular sieve dewaxing material involves providing coked light distillate and hydrogen through a molybdenum-nickel hydrogenation catalyst bed layer under hydrogenation refining condition, separating gas and liquid from hydrogenated product, and distilling at initial temperature of 30-70 degrees C, and final temperature of 245-370 degrees C, and obtaining kerosene fraction. The catalyst carrier contains 1-10 weight% of nano-silicon dioxide.    USE - Production of molecular sieve dewaxing material.    ADVANTAGE - The method effectively and economically provides molecular sieve dewaxing material with high adaptability, product additional value, and flexibility, by a simple process.
NOVELTY - The method involves feeding domestic sewage to the anaerobic hydrolysis pond through a water distributor for performing hydrolysis acidification treatment process. The processed domestic sewage is collected and poured into the aerobic biochemical pond for performing aerobic treatment process. The wastewater is collected and fed to the concrete structure, for discharging water. The concrete structure is formed from glass fiber reinforced plastic and reinforced concrete.    USE - Low-power distributed domestic sewage treatment method.    ADVANTAGE - The sewage treatment effect can be improved and residual mud generated during the domestic sewage treatment process can be reduced, while enabling efficient removal of nitrogen and phosphorus contained in the domestic sewage, without requiring more energy, much cost and more area.
NOVELTY - The device has a box main structure and a power supply control box. The air inlet and outlet pipes are arranged on the box main structure. A treating air course arranged in the box main structure, is connected with air inlet and outlet pipes. One row electrode discharging disc comprising a quartz glass pipe, is arranged in the treating air course. The air flowing in the treating air course is made to flow in from one side of the row electrode discharging disc and flow out from the other side.    USE - Industrial waste gas treating device using lower row electrode type low-temperature plasma discharge.    ADVANTAGE - Industrial waste gas treating device is simple in structure, convenient for maintenance, small in volume, small in air resistance loss, excellent in treating air input and low in manufacturing cost. The interception rate of electrons on waste gas is improved, and the waste gas processing efficiency is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the industrial waste gas treating device.
NOVELTY - The device has a ground pool, a storing tank, a pre-treatment tank, a dirt collecting well and a distributing pool which are connected through a pipeline. Hoisting pumps are connected between the ground pool and the storing tank, between the storing tank and the pre-treatment tank. The hoisting pumps are connected between the pre-treatment tank and an iron carbon electrolysis unit and between the dirt collecting well and the distributing pool. An inner wall of a pool housing of a micro-organism purifying system is provided with a flow selecting plate.    USE - Device for processing waste emulsion.    ADVANTAGE - The device with small floor area, low investment, low running cost and low energy loss is achieved. The waste oil resource can be recycled and the oil content in the wastewater can reach the national comprehensive sewage discharging standard.    DESCRIPTION OF DRAWING(S) - The drawing shows a structural block diagram of the device for processing waste emulsion.
NOVELTY - Ruthenium or osmium complexes (I) are new.    USE - (I) is useful as a catalyst, which is useful in an electrode, a photo-electrochemical cell, and photoelectrolytic device. The catalyst is useful for generating hydrogen and/or oxygen gases, and methanol, hydrocarbons and/or oxygen gases (all claimed). (I) is useful for catalytic water oxidation. (I) is useful for the electrolysis or photo electrolysis of water to obtain hydrogen or water reduction of carbon dioxide to obtain affordable and sustainable alternative source of energy.    DETAILED DESCRIPTION - Ruthenium or osmium complexes of formula (L1-M(L3)-L2) (I) are new.    M = Ru or Os;    L1 = bidentate ligand;    L2 = tridentate ligand; and    L3 = monodentate ligand; and    n = 1 or 2.    INDEPENDENT CLAIMS are included for:    (1) a catalyst comprising the complex (I);    (2) an electrode comprising the complex (I), and a supporting substrate on which the catalyst is supported;    (3) a photo-electrochemical cell comprising the catalyst;    (4) a photoelectrolytic device comprising the catalyst and a supporting substrate on which the catalyst is supported;    (5) method-1 of generating hydrogen and/or oxygen gases, comprising: providing the catalyst; and adding the catalyst to an electrolytic media under a conditions to generate hydrogen and/or oxygen; and    (6) method-2 of generating methanol, hydrocarbons and/or oxygen gases comprising providing the catalyst and adding the catalyst to a electrolytic media under a condition effective to generate methanol, hydrocarbons and/or oxygen.
NOVELTY - The method involves hydrolyzing the biomass using catalyst. The biomass is recirculated. The biodiesel is manufactured at a temperature of 150 degree Celsius. Hydrogen and lactic acid are generated in the hydrothermal reaction.    USE - Method for manufacturing biodiesel.    ADVANTAGE - The method involves hydrolyzing the biomass using catalyst, where the biomass is recirculated, and hence ensures improved and efficient manufacturing of biodiesel.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow chart of the biodiesel manufacturing method. (Drawing includes non-English language text).    Biomass (1)    Disintegration reaction device (2a)    Hydrolysis reactor (2b)    Hydrogenation reaction (3)    Hydrothermal reaction (4)
NOVELTY - Yield increasing fertilizer comprises (in wt.%) maize flour (10-14), beanstalk flour (8-10), Sorghum flour (4-6), nitrogenous fertilizer (10-12), potassium chloride (6-8), dry duck manure (18-20), dry cow dung (11-15), wheat straw flour (2-4), plant ash (4-6), superphosphate (4-6), glucose powder (3-5), paclobutrazol (1-3), triple superphosphate powder (1-3) and phenolic resin (2-4).    USE - The fertilizer is useful for Apocynum venetum Chinese herbal medicine.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the yield increasing fertilizer, comprising: mixing above raw material, placing into a stirrer to stir for 90 minutes, taking out and placing into a grinder to grind into the particles of about 80-mesh, then placing into the stirrer to stir for 160 minutes, taking out and pouring into a fermenting pool; adding manure water with ratio of 1:1.5, uniformly mixing up and down and piling up, tamping a plastic cloth to cover and press and fermenting for 28 hours and turning for the first time; then adding manure water again with ratio of 1:1.5, uniformly mixing up and down and piling up, tamping the plastic cloth to cover and press and fermenting for 58 hours and turning for the second time; and piling up and fermenting for 72 hours, and placing fermented yield increasing fertilizer into a die with the height of 35 cm, width of 25 cm, and length of 40 cm to tamp into yield increasing fertilizer block to obtain qualified yield increasing fertilizer.
NOVELTY - Cultivation fertilizer comprises (in %) dried human excrement (8-12), dried duck excrement (14-18), dried cow excrement (6-10), maize powder (2-6), kaoliang powder (6-10), wheat straw powder (4-8), organic fertilizer (6-10), Coptis chinensis powder (2-6), Strophanthus divaricatus branch and leaf powder (4-8), pine needle powder (11-13), sulfur powder (1-3), licorice powder (2-4), lucid ganoderma powder (4-6) and fennel powder (2-6).    USE - Cultivation fertilizer used for planting wild leek (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the above-cited cultivation fertilizer, which involves combining the above raw materials, stirring the mixture in a stirrer for 80 minutes, then pulverizing the mixture into powder by a pulverizing machine, piling the pulverized mixture into a fermentation unit, covering with plastic cloth, pressing compactly, fermenting the mixture for 72 hours after sealing, overturning for the first time, spraying 1/0.6 of human excrement water while overturning, overturning the lower material to the upper place, the inside material to the outside, the outside material to the inside and the upper material to the lower place, spraying the human excrement water uniformly, immediately covering with the plastic cloth after overturning, pressing compactly, fermenting for 72 hours continuously at a temperature of more than 80 degrees C, and then continuously performing process of overturning, adding human excrement water and fermenting for 7 times.
NOVELTY - Method for preparing biodiesel, involves (a) adding isostearic acid, alcohol and catalyst (5-20%) into reactor, and reacting the obtained mixture at 65-85 degrees C for 6-20 hours to obtain isostearic acid ester, and (b) adding the isostearic acid ester to biodiesel, and mixing isostearic acid ester and biodiesel to obtain product.    USE - The method is useful for preparing biodiesel.    ADVANTAGE - The biodiesel is prepared inexpensively by simple method with high productivity and enables biodiesel to crystallize easily at low temperature and thus improves low-carbon fluidness property.
NOVELTY - Methanol diesel microemulsion comprises (in parts weight): modified methanol (15-50), surfactant (0.1-5), diesel oil (40-60) and cosolvent (8-20).    USE - Methanol diesel microemulsion.    ADVANTAGE - The microemulsion can be prepared by simple process, and has combustion performance and standard emission index and thus satisfies environmental requirement.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the methanol diesel microemulsion, which involves (a) adding (in parts weight) methanol (70-96) into a reactor, dissolving hexadecyl modifier (3-10), flash point improver (1-7), inflaming additive (0.01-1), lubricant (0.001-1), anti-wear agent (0.001-1), antioxidant (0.001-1) and anticorrosive agent (0.001-1), agitating the dissolved materials to obtain modified methanol, adding diesel oil and surfactant to the agitated mixture, and adding cosolvent at high agitation speed until transparent state is observed.
NOVELTY - Methanol diesel oil comprises (in parts weight): methanol (30-80), diesel oil (20-60) and additive (10-50).    USE - As methanol diesel oil.    ADVANTAGE - The oil has excellent stability and flammability, and combustion property, and can be stored for long period of time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of manufacturing the above-mentioned oil, which involves (a) mixing the additive components into a reactor, stirring the mixture for 10-50 minutes to obtain mixed additive, (b) mixing the above-mentioned components in the reactor, stirring the mixture, (c) adding mixed additive (10-50 parts) to the mixture obtained in process (b), and (d) stirring the mixture and stabilizing the mixture for 10-20 minutes to obtain the oil.
NOVELTY - Carbinol and grease are added to a static mixer. The carbinol and grease are mixed by static mixer and reacted. The mixture is separated in a gas-liquid separator, and the gas-phase on upper layer of gas-liquid separator contains carbinol. The intermediate layer of gas-liquid separator comprises crude biodiesel. The crude biodiesel is decompressed and distilled in rectifying tower. The tower top and side lines of rectifying tower comprise biodiesel. The tower bottom of rectifying tower comprises fuel oil. The lower layer of the gas-liquid separator contains crude glycerin.    USE - Preparation of biodiesel.    ADVANTAGE - The method enables economical preparation of biodiesel having high quality and yield of 96% or more within short period of time, using device having excellent durability.    DETAILED DESCRIPTION - Carbinol and grease are added to a static mixer in molar ratio of 24:1-42:1 by a metering pump. The carbinol and grease are mixed by static mixer and reacted in a pipe-type reactor at supercritical state. The temperature of a heating furnace burner is automatically controlled to 240-320 degrees C. The pressure is controlled using a sensor and an automatic valve to 15-29 MPa. The reaction time is controlled using metering pump by adjusting flow to 4-15 minutes. The mixture is separated in a gas-liquid separator, and the gas-phase on upper layer of gas-liquid separator contains carbinol. The intermediate layer of gas-liquid separator comprises crude biodiesel. The crude biodiesel is decompressed and distilled in a rectifying tower. The tower top and side lines of rectifying tower comprise biodiesel. The tower bottom of rectifying tower comprises fuel oil. The lower layer of the gas-liquid separator contains crude glycerin.
NOVELTY - Soil matrix comprises 90% of pure sheep stable manure obtained from inner Mongolia grassland and 10% of cow dung obtained from grassland. The soil matrix is prepared by mixing the components, crushing the mixture, agitating the mixture, fermenting the mixture, airing the fermented product, and packaging the product in a bag, where the granularity of the mixture is 50 meshes.    USE - The soil matrix is useful for planting garden, preferably greenhouse for cultivating crops, and preventing diseases and insects in crops chosen from vegetable, fruit and tobacco crops.    ADVANTAGE - The soil matrix has improved ground temperature, saves water and improves crop quality and is convenient to use.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for using soil matrix, which involves stacking the packed bag using red brick, cement brick or cinder brick, designing the bag into a rectangle with a width of 0.6m, height of 0.45m and length of 8m, adding sterilized sand to the matrix and mixing with matrix, and transferring obtained grove.
NOVELTY - A collected waste oil material with low acid value is dewatered. The dewatered waste oil material, methanol and concentrated sulfuric acid are subjected to esterification reaction. The mixture after esterification reaction is settled. The obtained ester is added to mixing kettle, and potassium hydroxide and methanol are added to mixture. The resulting material is added to a piston flow reactor and transesterified to obtain crude product of biodiesel. The crude product of biodiesel is centrifugally separated, and evaporated through film evaporator to obtain biodiesel.    USE - Preparation of biodiesel.    ADVANTAGE - The method enables efficient preparation of biodiesel, without environmental pollution.    DETAILED DESCRIPTION - A collected waste oil material with low acid value is dewatered to reduce water content to 0.1% or less. The dewatered waste oil material, methanol and concentrated sulfuric acid are added to an esterification reaction kettle, and carrying out esterification reaction at 55-75 degrees C for 0.4-0.6 hour. The mass ratio of dewatered waste oil material is 6.7-20.3 %mass. The dosage amount of concentrated sulfuric acid is 0.8-1.2 %mass with respect to mass of waste oil material. The mixture after esterification reaction is settled to remove water and concentrated sulfuric acid. The obtained ester is added to mixing kettle, and potassium hydroxide (0.6-1.4 %mass) and methanol (13-17 %mass) are added to mixture. The resulting material is added to a piston flow reactor and transesterified at 35-95 degrees C to obtain crude product of biodiesel, and the reaction flow rate of piston flow reactor is controlled to 5 ton/hour. The crude product of biodiesel is centrifugally separated, to obtain semi-product of biodiesel. The crude product of biodiesel is evaporated through film evaporator to obtain biodiesel.
NOVELTY - A Methylocystis sp. M6 (KCTC BP-11519), is new.    USE - The Methylocystis sp. M6 is used in methane reduction composition for reducing methane (claimed) in landfills.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) composition for reducing methane comprising the above-cited strain;    (2) biocover for methane reduction;    (3) methane reduction system; and    (4) method for reducing methane.
NOVELTY - The large or medium-sized biogas producing system device has fermentation system (1) which is connected with input end of anaerobic reactor (2) by feeding pipe (21). The output end of anaerobic reactor is connected with desulfurizing tank by biogas pipe (5). A manure-collecting tank (10) is provided with one end connected with material mixing tank while other end is connected with input end of anaerobic reactor by feeding pipe.    USE - Large or medium-sized biogas producing system device.    ADVANTAGE - The bio-gas can be produced quickly and effectively at low cost. The system is simple so that cleaning is performed conveniently.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the large or medium-sized biogas producing system device.    Fermentation system (1)    Anaerobic reactor (2)    Biogas pipe (5)    Manure-collecting tank (10)    Feeding pipe (21)
NOVELTY - A water leaking and discharging pipe (2) is arranged between an anti-leakage layer and a supporting layer. The pipe has a water leading and discharging hole which penetrates through a rapid infiltration pond. The supporting layer has a screen layer (6) located under a porcelain granule layer (7). A processing layer (8) arranged on upper side of supporting layer is a sand and soil mixing layer formed by soil and river sand. The surface of processing layer is planted with plant (11) and a water distributing system is arranged on surface of rapid infiltration pond.    USE - Rapid infiltration sewage disposal device of artificial soil bed.    ADVANTAGE - The device is provided with strong reoxygenation effect, high rate of removing ammonia nitrogen, good quality of discharged water, low investment, low energy consumption and simple operation and management. And also the device is applicable to soil and climatic condition of mountain area and hilly small town.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of the rapid infiltration sewage disposal device.    Water leaking and discharging pipe (2)    Screen layer (6)    Porcelain granule layer (7)    Processing layer (8)    Plant (11)
NOVELTY - The lower portion of fuel gas suction pipe orifice is equipped with furnace unit connecting flange whose lower portion is provided with water sleeve of carbonizing chamber equipped with fireproof lining. The lower portion of carbonizing chamber is provided with exhaust ring inside furnace, and lower portion of exhaust ring inside furnace is provided with carbon collecting chamber equipped with carbon outlet on lower portion. The lower portion of water sleeve of carbonizing chamber is provided with carbonizing chamber furnace seat.    USE - Straw gasifying furnace.    ADVANTAGE - The lower portion of water sleeve of carbonizing chamber is provided with carbonizing chamber furnace seat. Hence the furnace directly applies heat energy of carriers in the fuel gas to dryly distil and carbonize the straw during gasification process, and produces biomass carbonized fuel gas to replace liquefied petroleum gas. A clean and cheap gas fuel is provided to rural areas, and there is no need to wash, cool and purify the produced fuel gas by water. The industrial materials are separated from the fuel gas, and there is no discharge of wastewater, and associated products of high additional value are produced during the straw gasification process such as distilled carbon, wood vinegar, wood tar and acetic acid used as industrial materials.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the straw gasifying furnace.
NOVELTY - A gas purification and separation absorbent comprises cerium(IV) oxide (CeO2) distributed into porous carrier loaded with main active components, clay and binder.    USE - Gas purification and separation absorbent used for absorbing and separating carbon monoxide (CO) and unsaturated hydrocarbon from mixed gas; purifying industrial waste gases including burner gas in steel and aluminum production in metallurgical industry; removing CO and ethylene in carbon dioxide used in food industry; or removing CO impurities and unsaturated hydrocarbon from high-purity gases including nitrogen or methane (all claimed).    ADVANTAGE - The absorbent has high strength, and utilizes CeO2 to form silicon and hydroxy-aluminum network on the carrier, the clay and the binder and to promote close integration of the main active component metal ions, the carrier and the binder. Thus, bonding of silicon and hydroxy-aluminum is strengthened.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of gas purification and separation absorbent, comprising:    (A) dispersing monovalent copper ion or cupric ion as main active component into porous carrier; or mixing main active component with carrier, clay and binder using precursor compound of monovalent copper ion;    (B) directly adding precursor compound of CeO2 into the carrier, the clay and the binder, or firstly steeping CeO2 solution on the carrier, then mixing them with other components; and    (C) heating the obtained absorbent for 0.5 to 10 hours at 100-800 degrees C, and heating for 1-6 hours at 300-700 degrees C.
NOVELTY - Method for producing organic liquid fertilizer, involves crushing or pulping artificially water hyacinth, adding the crushed water hyacinth in sealed container, performing hydrothermal degradation reaction to the obtained mixture, separating solid and liquid from the mixed solution degradation reaction using residue as compost catalyst, and preparing liquid into organic liquid fertilizer or plant nutrient solution or special fertilizer.    USE - The method is useful for producing organic liquid fertilizer.    ADVANTAGE - The method is simple and rapid, and can recycling water hyacinth. The organic liquid fertilizer has high nutrient content and reduces pollution.    DETAILED DESCRIPTION - Method for producing organic liquid fertilizer by degradating water hyacinth, involves crushing or pulping artificially water hyacinth, adding the crushed water hyacinth and juice in a sealed container, maintaining temperature of the sealed container at 50-300 degrees C under pressure of 0.1-5 MPa, performing hydrothermal degradation reaction to the obtained mixture for 30 minutes to 3 hours, separating solid and liquid from the mixed solution degradation reaction, using residue as compost catalyst, and preparing liquid into organic liquid fertilizer or plant nutrient solution or special fertilizer.
NOVELTY - Method for producing organic fertilizer by water hyacinth, involves crushing the water hyacinth, dehydrating the crushed hyacinth, mixing the dehydrated component with fermented animal waste, performing composting fermentation to the obtained mixture in fermentation tank, performing acid regulation when ammonium smell is generated, crushing the fermented material, packaging the material, and palletizing to obtain the organic fertilizer.    USE - The method is useful for producing organic fertilizer.    ADVANTAGE - The organic fertilizer can be produced easily without environmental pollution. The fertilizer is feasible.    DETAILED DESCRIPTION - Method for producing organic fertilizer by water hyacinth, involves crushing the water hyacinth in a vessel, dehydrating the crushed hyacinth in extruding crusher to decrease water content to 55-75%, mixing the dehydrated component with fermented animal waste (5-50%) to obtain water hyacinth mixture, performing composting fermentation to the obtained mixture in fermentation tank, increasing the temperature to 40-70 degrees C, supplying oxygen and dehydrating the fermented material at 60-70 degrees C for two times/day, performing acid regulation when ammonium smell is generated, decreasing the composting temperature to 60-70 degrees C until fermented material has no peculiar smell and color is brown, crushing the fermented material, packaging the material, and palletizing to obtain the organic fertilizer.
NOVELTY - The tower has a fermenting and drying chamber (3) is internally provided with horizontal ventilated pipes (4) and upright ventilated pipes (5) which are connected through a clamped wall wind channel (6) and chimney (7) to compose radiating, ventilation and exhaust channels of fermenting material (8). The ventilated pipes are connected to channel, backflow wind pipe, fan, backflow wind channel and horizontal ventilated channel to compose hot air backflow system.    USE - Static aerobic fermenting and drying tower for producing high-quality organic fertilizer.    ADVANTAGE - High production, less secondary pollution, high resource utilization, small organic raw material volume and convenient conveyance of the static aerobic fermenting and drying tower can be achieved. Since the fermenting and drying tower is built on minimum requested height for traveling of forklift truck, the accumulated temperature effect is generated by integrated fermentation, so that investment is saved, high efficiency and low production cost can be obtained.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the static aerobic fermenting and drying tower.    Fermenting and drying chamber (3)    Horizontal ventilated pipe (4)    Ventilated pipes (5)    Clamped wall wind channel (6)    Chimney (7)    Fermenting material (8)
NOVELTY - A waste chosen from life waste, industrial waste, construction waste, agricultural waste, fishery waste and/or livestock is mixed with components chosen from organic compound, combustibles, inorganic material and recycling material. Life waste is waste generated in human life. Industrial waste is waste generated in industrial site. Construction waste is waste generated in construction site. Agricultural waste is waste generated in agriculture field. Fishery waste is waste generated in fishery field. Livestock waste is waste generated in livestock industry field.    USE - Recycling of waste material.    DETAILED DESCRIPTION - A waste chosen from life waste, industrial waste, construction waste, agricultural waste, fishery waste and/or livestock is mixed with components chosen from organic compound, combustibles, inorganic material and recycling material. Life waste is the waste generated in the human life. Industrial waste is the waste generated in the industrial site. Construction waste is the waste generated in the construction site. Agricultural waste is the waste generated in the agriculture field. Fishery waste is the waste generated in the fishery field. Livestock waste is the waste generated in the livestock industry field. The organic compound is anaerobic, and recycles to biofuel. The combustibles recycles to solid fuel, and used for fracturing, crushing or molding. The inorganic material is chosen from soil, sand, aggregate, waste concrete and rock. The recycling material is chosen from domestic appliance material, timber material, bimetal, iron material.
NOVELTY - Chinese herbal medicine nutritional fertilizer containing red peony comprises dried cow dung, dried pig manure, dried goose manure, bean meal, corn meal, kaoliang powder, wheat powder, green grass powder, wheat straw powder, monopotassium phosphate, triple superphosphate, potassium sulfate, nitramine fertilizer, phosphate fertilizer, teschemacherite, Dipterex (RTM: Trichlorfon), carbendazim, glucose powder and phenolic resin.    USE - As Chinese herbal medicinal nutritional fertilizer.    DETAILED DESCRIPTION - Chinese herbal medicine nutritional fertilizer containing red peony comprises (in g): dried cow dung (30000), dried pig manure (30000), dried goose manure (30000), bean meal (30000), corn meal (30000), kaoliang powder (30000), wheat powder (50000), green grass powder (50000), wheat straw powder (50000), monopotassium phosphate (20000), triple superphosphate (10000), potassium sulfate (5000), nitramine fertilizer (5000), phosphate fertilizer (5000), teschemacherite (3000), Dipterex (RTM: Trichlorfon) (3000), carbendazim (2000), glucose powder (5000) and phenolic resin (15000).
NOVELTY - Preparation of a mildronate intermediate compound comprises adding methylacrylate and alcohol as a solvent to a three-opening flask having a mechanical stirrer and a dripping bucket. The hydrazine hydrate (5-50%) is dripped, and the mixture is continuously stirred. The solvent is distilled at normal pressure, and the pressure is reduced to distill 3-methyl carbazate. The obtained distillate is dissolved using ethanol. The excess methylated agent (5-30%) and acid acceptor are added. The mixture is filtrated, washed using ethanol and dried to obtain mildronate intermediate compound.    USE - Preparation of mildronate intermediate compound.    ADVANTAGE - The method enables safe and economical preparation of mildronate intermediate compound, without environmental pollution.    DETAILED DESCRIPTION - Preparation of a mildronate intermediate compound comprises adding methylacrylate and alcohol as a solvent to a three-opening flask having a mechanical stirrer and a dripping bucket, and the temperature is controlled to 0-50 degrees C. The hydrazine hydrate (5-50%) is dripped for 1-3 hours, and the mixture is continuously stirred for 1-3 hours. The solvent is distilled at normal pressure, and the pressure is reduced to distill 3-methyl carbazate. The obtained distillate is dissolved using ethanol, and the temperature is controlled to 0-50 degrees C. The excess methylated agent (5-30%) and acid acceptor are added. The mixture is filtrated, washed using ethanol and dried to obtain mildronate intermediate compound.
NOVELTY - Compost processing method for solid waste in pig farm, involves (a) uniformly mixing fresh pig waste, coal ash, sawdust and water, preparing into stockpile, and regulating the pH of the stockpile to be 7.5-8.0 with acidic liquid or alkali liquid, and (b) dividing the stockpile into stocks with a bottom area of 3x 5-4x 5 m2 and volume of 10-20 m3, and piling up until the materials are completely fermented.    USE - The method is useful for processing solid waste in pig farm and obtaining compost used as fertilizer.    ADVANTAGE - The method provides high yield of compost fertilizer, is simple, easy to perform, and has high composting efficiency. The fertilizer has high agricultural utilization ratio and causes less harm to the soil after repeated usage. The absorption amount of the fertilizer is higher.    DETAILED DESCRIPTION - Compost processing method for solid waste in pig farm, involves (a) uniformly mixing fresh pig waste, coal ash (where the concentration of coal ash is 1-1.5% of the weight of the fresh pig waste), sawdust (with a particle diameter of 100-180 meshes) and water, preparing into stockpile (having 71-75 %mass of moisture content and carbon and nitrogen ratio of 25-30), and then regulating the pH of the stockpile to be 7.5-8.0 with acidic liquid or alkali liquid, and (b) dividing the stockpile into stocks with a bottom area of 3x 5-4x 5 m2 and volume of 10-20 m3, and piling up until the materials are completely fermented to obtain compost, where the fermentation is high temperature fermentation, the stockpile is turned over once every 5 days, and the stockpile is turned over once every 7-8 days after the temperature of the stockpile is reduced in post-fermentation stage.
NOVELTY - Method of treating kitchen garbage, by modifying kitchen garbage into biochemically-treatable kitchen garbage, crushing the biochemically-treatable kitchen garbage into mixture, subjecting the mixture to centrifugation to separate light phase and heavy phase of mixture, preparing light phase into grease and high-concentration solution, modifying the heavy phase and the solution into thick pulp, hydrating and acidifying the thick pulp to obtain base material, subjecting the base material to anaerobic fermentation with sludge to obtain methane and carbon dioxide.    USE - The method is useful for treating kitchen garbage for preparing methane and carbon dioxide.    ADVANTAGE - The method increases yield of organic material with low impurities.    DETAILED DESCRIPTION - Method of treating kitchen garbage, involves (a) dividing kitchen garbage, and removing metal, plastics and glass bottles from garbage and obtaining biochemically-treatable kitchen garbage, (b) crushing the biochemically-treatable kitchen garbage into mixture having particle diameter of 8 mm or less, (c) subjecting the mixture to centrifugation to separate light phase containing water and heavy phase containing oil, (d) preparing light phase into grease and high-concentration solution, (e) modifying the heavy phase and the high-concentration solution into thick pulp, having solid grain diameter 0.1 mm or less, hydrating and acidifying the thick pulp for base material, and (f) subjecting the base material to anaerobic fermentation by contacting the base material with sludge of the upflow anaerobic sludge blanket and decomposing organic materials of the base material and sludge using microorganism to obtain methane and carbon dioxide.
NOVELTY - Methanogen comprises composite bacteria as functional microorganism. The methanogen is prepared by activating the bacteria, subjecting the bacteria to first expansion and secondary expansion process, absorbing the obtained bacteria, extracting the obtained bacteria, and packaging the obtained bacteria.    USE - The methanogen is useful for producing biogas.    ADVANTAGE - The methanogen can be preserved for 2 years at normal temperature, and has wide adaptability to temperature.
NOVELTY - Reducing coal compounded ammonia comprehensive energy consumption comprises using reproducible energy biomass carbon block to replace the smokeless coal as the compounded ammonia raw material, preparing hydrogen via water gas generating furnace, mixing hydrogen and nitrogen according to the volume ratio of 3:1, and forming the compounded ammonia raw material gas.    USE - The process is useful for reducing coal compounded ammonia comprehensive energy consumption (claimed).    ADVANTAGE - The indirect gasifying of the biomass carbon block can obtain the cleaner compounded ammonia raw material gas with the same valid component as the smokeless coal product compound gas and few sulfur polar; where the biomass carbon block can directly match with the subsequent technical apparatus of coal compounded ammonia to prepare the compounded ammonia and the terminal fertilizer product; thus, achieving the zero discharging of carbon dioxide in compounded ammonia producing technique.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of the process for reducing coal compounded ammonia comprehensive energy consumption (Drawing includes non-English language text).
NOVELTY - Agent comprises dexpanthenol, buffer solution having pH of 4-6 and osmotic pressure regulator.    USE - The agent is useful for treating intestinal paralysis, intestinal infraction, intestinal atony, flatulence after surgery or delivery and restoring intestinal motility after surgery.    ADVANTAGE - The agent is environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing the above-cited agent, which involves weighing acetic acid and sodium acetate, mixing weighted mixture with water for injection to form buffer solution having pH 4-6, adding isotonic regulator having osmolality of 280-315 mosmol/kg to obtained mixture, and dissolving the mixture completely until the 80% of dexpanthenol in present in the total quantity.
NOVELTY - The method involves filling rubbish into composite reactor, and hydrolyzing rubbish by using hydrolyzing solution to generate methane. The rubbish after hydrolyzing is aerobically stabilized. The flow of hydrolyzing solution is stopped after finishing hydrolyzing process. The reactor filled with rubbish is ventilated after finishing aerobically stabilizing process. The rubbish in the reactor after stabilization is removed, and is then vibrated to separate the substance which is used as derivative fuel.    USE - Method for processing domestic rubbish by phase-split aerobic and anaerobic techniques.    ADVANTAGE - The generation of bad smell can be prevented. The rubbish can be processed efficiently.
NOVELTY - Preparing traditional Chinese medicinal cinnabar powder, involves (a) removing foreign materials from raw material, absorbing iron dust from materials, and filtering the mixture, (b) transferring the filtered cinnabar to a ball mill pulverizing machine, obtaining pulverized medium as magnetic ball, and pulverizing the mixture, and (c) filtering the suspended liquid, centrifuging the mixture, placing the mixture, and drying the product.    USE - The method is useful for preparing traditional Chinese medicinal cinnabar powder.    ADVANTAGE - The method is cost-effective, environmentally-friendly, rapid, less labor intensive, suitable for industrial production, convenient to perform and improves purity of traditional medicine.    DETAILED DESCRIPTION - Method of preparing traditional Chinese medicinal cinnabar powder, involves (a) removing foreign materials from raw material, adding the materials in a magnetic selecting machine, absorbing iron dust from the materials, adding the materials in a clean container, stirring the materials, washing the mixture using clean water, and filtering the mixture using sand filter, (b) transferring the filtered cinnabar to a ball mill pulverizing machine, obtaining pulverized medium as magnetic ball, adding clean water to the mixture, and pulverizing the mixture for 60 minutes to form suspended liquid, where volume ratio of cinnabar to water is 1:2, and (c) filtering the suspended liquid using sand like filtering device, dewatering the mixture, centrifuging the mixture for 30 minutes, placing the mixture on cotton cloth or water absorbing paper, and drying the product hot air circulating oven at 40 degrees C.
NOVELTY - Chelate release controlled compound fertilizer, comprises (in parts weight): urea (200-250), monoammonium phosphate (300-350), potassium chloride (230-260), pulverized pumice (50-70), swelling and moisture soil (70-90), concave-convex soil (8-12), liquid polymer resin (6-10) and concentrated sulfuric acid (0.1-1). The fertilizer further comprises moderate and micro elements chosen from zinc sulfate (5-6), manganese sulfate (3.5-4), ferric sulfate (1.3-1.6), magnesium sulfate (1.8-2) and copper sulfate (2.0-2.2).    USE - The chelate release controlled compound fertilizer is useful for preventing diseases caused by deficiency of microelements in plants.    ADVANTAGE - The fertilizer has stable molecular structure, is nutritious and environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves mixing the above-mentioned components excluding zinc sulfate and the liquid polymer resin, coating the zinc sulfate and the liquid polymer resin on the surface of mixture, drying the coated product and processing the coated product into grains having size of 90% or less.
NOVELTY - Ecological organic fertilizer comprises (in wt.%): compound strain (3-5), solid europium nitrate (0.3-0.5), organic substance (84-85) and water (9.5-12.7).    USE - As ecological organic fertilizer containing compound strain.    ADVANTAGE - The fertilizer is environmentally-friendly as it does not cause damage to humans and environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the above-mentioned fertilizer, which involves (1) culturing six beneficial microorganisms including nitrogen-fixing bacteria, associative bacteria, nodule bacteria, Actinomycetes, effective bacteria and bacteria used in fermentation under sterile condition at suitable temperature, extracting the bacteria from the obtained culture when the content of the active bacteria in the culture more than 1.8-2.5000000000 colony forming units (CFU)/g, subjecting the mixture to fermentation to obtain the compound strain for future use, (2) mixing the obtained compound strain with dried tobacco stem or tobacco powder and poultry manure, agitating mixture uniformly, and fermenting and overturning mixture in fermentation tank to obtain the organic substance for future use, and (3) uniformly mixing the compound strain, solid europium nitrate, organic substance and water and packaging the mixture to obtain the product.
NOVELTY - The method involves scattering garbage, and separating massive inorganic matter, plastic product and plastic bag from the garbage. The waste other than the inorganic matter, plastic product and plastic bag is separated from the garbage by a vibration grid, and separated garbage is conveyed to a conveyor belt using a magnetic sucking device which is arranged under vibrating grid. The organic matter in the separated household garbage is crushed by a rotating blade. The separated garbage is dried after breaking and crushing processes are completed, to prepare fertilizer.    USE - Method for performing automatic classification of household garbage, for preparing fertilizer.    ADVANTAGE - The recycling of the useful matter from the garbage can be effectively achieved reliably within a small area and environmental pollution can be avoided effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for device for automatic classification of household garbage.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the household garbage classifying device.
NOVELTY - Biological organic fertilizer is produced by mixing (in %) traditional Chinese medicine residues (70-74), processed sewage from brewery wastewater (10-14), bacterium utilized for fermentation, micro-fertilizer (0.1), phosphate fertilizer (2-4) and urea (3-5), fermenting mixture, post-fermenting mixture, air-drying mixture, granulating mixture at 60 degrees C or less, and drying mixture.    USE - As biological organic fertilizer.    ADVANTAGE - The fertilizer is cost-effective and environmentally-friendly.
NOVELTY - Fertilizer is obtained by adding azophoska and soil activator to high-concentration organic liquid, and aging the mixture, where the high-concentration organic liquid is prepared by biologically fermenting natural organic and agricultural waste.    USE - The fertilizer is useful for activating soil.    ADVANTAGE - The fertilizer is environmentally-friendly, and has long-lasting effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves (a) mixing (in parts): natural organic (0.2-0.5) with agricultural waste (1.7-2.4), fermenting the mixture in fermentation tank at normal temperature for 45-80 days to form dark brown thick organic liquid with fish alcohol smell, filtering the liquid to obtain supernatant organic liquid, and (b) aging the organic liquid, adding azophoska and soil activator to the liquid, and stirring the mixture for 2 days at normal temperature and 900-1200 revolutions/minutes for every 1 hour to obtain the final product.
NOVELTY - Bacterial liquid composition comprises Alcanivorax 97C0-5, Alcanivorax 97C0-6, and Marinobacter PY97S.    USE - The bacterial composition solution is useful for co-degrading oil, and biologically repairing sea line or biologic polluted by sea oil spilling (all claimed).    ADVANTAGE - The bacterial composition solution: can biodegrade the oil pollutant at low temperature; can completely degrade the paraffin components and aromatic hydrocarbon components in oil; and has high rate of oil degrading effect than the single degrading bacterium liquid.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the bacterial liquid composition, comprising inoculating the Alcanivorax 97C0-5 and Alcanivorax 97C0-6 (2%) stored at lower temperature in M8 culture medium, inoculating Marinobacter PY97S (2%) stored at lower temperature in sodium acetate culture medium, culturing at 25 degrees C and preparing the seed solution by mixing at a speed of 150 revolutions/minute under the condition of 0.25 m3/hour of venting quantity, inoculating the seed liquids of 97C0-5 and 97C0-6 in M8 culture medium according to 5% of inoculation quantity, inoculating the seed liquid of PY97S in sodium acetate culture medium according to 5% of inoculation quantity and culturing at 25 degrees C and mixing speed of 150 rotations/minute under the condition of 0.25 m3/hour of venting quantity, adding defoamer and culturing until the cell concentration of the cell is 108-109 colony forming unit/ml, stopping fermentation and preparing the fermented culture solution, mixing the fermented culture solution to obtain the product.
NOVELTY - The equipment has filtered biogas slurry that is conveyed along biogas slurry supply pipeline through biogas slurry supply pump and biogas slurry filter. Clean water is conveyed along clean water supply pipeline through clean water supply pump converged on connection portion of biogas slurry/ supply clean water pipeline and mixed output pipeline. Clean water and biogas slurry is mixed according to needed proportion so as to obtain fertilizer liquid, and obtained fertilizer liquid is conveyed through mixed output pipeline to irrigation device to irrigate crop.    USE - Fertilization equipment for biogas slurry sediment, aeration, filtering, proportioning and dissolved oxygen increment uses biogas slurry to fertilize and irrigate.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the fertilization equipment using biogas slurry. (Drawing includes non-English language text)
NOVELTY - Agent comprises (in parts weight): benzaldehyde (10-100), benzpyrole (1-20), linalool (5-90) and slow-releasing portion comprising silica, methylcellulose and sodium benzoate. The amount of silica is 2.5-3.5 times, methylcellulose is 0.45-0.55 times, and sodium benzoate is 0.45-0.55 times with respect to total weight of the total weight of the benzaldehyde, benzpyrole and linalool.    USE - The agent is useful for controlling Cyrtotrachelus buqueti in bamboo forests.    ADVANTAGE - The agent is inexpensive, environmentally-friendly, non-toxic and harmless to animals and humans, and has excellent durability and slow-release property.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the agent, which involves (a) weighting above-mentioned raw materials, and mixing the materials at normal temperature and normal voltage condition in clean environment, (b) adding silica, methylcellulose and sodium benzoate to the mixture, (c) grinding the mixture using a sand mill for 0.5-1 hours to obtain the powder having diameter of 70 mu m, and screening the powder using a sieve of mesh of size 200, and (d) adding clean water into the obtained powder (20%) to obtain final product.
NOVELTY - Method of preparing monosialotetrahexosylganglioside, involves (a) weighing animal brain tissue, extracting tissue using water solution of detergent, and removing precipitate to obtain extract, and (b) concentrating the extract to obtain extract of monosialotetrahexosylganglioside.    USE - The method is useful for preparing monosialotetrahexosylganglioside.    ADVANTAGE - The method is simple, cost-effective, environmental-friendly and enables preparation of monosialotetrahexosylganglioside having purity of 97% or more, without using organic solvent.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for injection, which comprises the monosialotetrahexosylganglioside prepared by the above-cited method.
NOVELTY - Micro-ecological fungicide comprises Bacillus subtilis fermenting liquid, where the cultivation medium for fermenting liquid comprises corn meal, starch, sucrose or molasses (0.1-10 wt.%) and bean pulp, soybean meal, bran or beef extract (1-10 wt.%) and water (1000 ml); the pH of cultivation medium is 6-9 and performing high-pressure sterilization of the cultivation medium for 30 minutes at 121 degrees C.    USE - The micro-ecological fungicide is useful for resisting Fusarium wilt disease of banana.    ADVANTAGE - The micro-ecological fungicide utilizes raw materials of low cost. The cultivation medium has suitable concentration, inoculation quantity and bottling quantity and the product is low in cost. The detection method is fast and convenient, and can obtain direct and clear result.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing micro-ecological fungicide, comprising (i) taking raw materials (in wt.%) corn meal, starch, sucrose or molasses (0.1-10), and bean pulp, soybean meal, bran or beef extract (1-10) and water (1000 ml), (ii) activating the Bacillus subtilis strain and inoculating into culture medium; placing in incubator shaker at 25-35 degrees C and rotating at 100-200 revolution/minute; performing vibration cultivation for 10-50 hours, where the cultivation medium is beef extract peptone, (iii) inoculating into Bacillus subtilis fermentation cultivation medium, where the inoculation quantity is 1-10% (vol./vol.); cultivating for 10-50 hours at 20-30 degrees C, (iv) performing fermentation and collecting the Bacillus subtilis fermentation liquid.
NOVELTY - A diesel composition comprises a base diesel and an additive. The base diesel comprises biodiesel. The additive comprises a component A that is obtained by mixing alkenyl butanimide, phenyl-containing organic acid and solvent at 60-200 degrees C for 0.5-20 hours. The mole ratio of phenyl-containing organic acid and polyene polyamine in the alkenyl butanimide is 0.5-5:1.    USE - A diesel composition.    ADVANTAGE - The composition has good oxidization stability, cleaning performance, and dispersibility.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for improvement of oxidization stability of the biodiesel comprising adding additive to base diesel.
NOVELTY - A diesel combination comprises a base diesel and additive. The base diesel comprises biodiesel. The additive comprises a component A comprising alkenyl butanimide and/or alkenyl butanedioic acid amide; and a component B comprising arylamine antioxidant and/or hindered phenol antioxidant.    USE - A diesel combination.    ADVANTAGE - The composition has good oxidization stability, cleaning performance, and good dispersibility.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for improvement of oxidization stability of the biodiesel comprising adding additive to base diesel.
NOVELTY - A biomass thermal cracking oil is refined by mixing biologic oil and isooctanol, adding zeolites, distilling to obtain obtained biologic oil, mixing the obtained biologic oil and isometric acetylchloride, adding water to neutralize, removing formed bubbles to obtain anhydrous biologic oil, adding acetic acid and alcohol to the oil, adding toluenesulfonic acid catalyst and activated carbon solid carrier, heating, esterifying, adding anhydrous magnesium sulfate, dehydrating, and filtering.    USE - Method of refining biomass thermal cracking oil.    ADVANTAGE - The method is simple, and has good dehydration effect and high yield.    DETAILED DESCRIPTION - A biomass thermal cracking oil is refined by:    (A) mixing biologic oil and isooctanol at a volume ratio of 5:1, adding zeolites (2-10 pts.wt.), distilling at 80 degrees C and vacuum pressure of 0.02 MPa to obtain biologic oil having less water;    (B) mixing the biologic oil and isometric acetylchloride, adding water to neutralize, and removing formed bubbles to obtain anhydrous biologic oil;    (C) adding acetic acid and alcohol having a molar ratio of 1:2.8 to the oil, adding toluenesulfonic acid catalyst and activated carbon solid carrier, heating at 80 degrees C, reflux-heating, and esterifying; and    (D) adding anhydrous magnesium sulfate, dehydrating, and filtering;    (E) subjecting to neutral buffer solution comprising quat. ammonium salt as surfactant, adding diesel oil, adjusting the pH to 6.27-7, reducing pressure, and filtering.    The ratio of catalyst and anhydrous biologic oil is 1:35. The ratio of anhydrous magnesium sulfate and esterified biologic oil is 1:5. The quat. ammonium salt is formed by mixing hydrogen chloride and triethylamine.
NOVELTY - Biological drying of a domestic garbage comprises sieving out sundries, uniformly mixing domestic garbage, garbage biological-dried products, and crushed straw to obtain a mixed material, placing the mixed material in a groove-type compost reactor to obtain 1.6-2 m high pile body, inserting a temperature sensor, and covering 20 cm thick straw pads on the surface to fill the garbage pile body; biologically drying the garbage pile body by intermittently ventilating at 1-3 m3/minute; and removing straw pads, removing the dried garbage from the reactor, and sorting.    USE - Method for biological drying of domestic garbage used as a soil opsonizing agent and a derived fuel (claimed).    ADVANTAGE - The lower heat value of the dried garbage is improved to 100% and sorting index is improved to 140%, thus improving domestic garbage burn and sorting resource value.    DETAILED DESCRIPTION - Biological drying of a domestic garbage comprises:    (A) sieving out sundries with a grain diameter of greater than 20 cm in a mixed garbage to obtain a domestic garbage with a grain diameter of lesser than 20 cm, uniformly mixing domestic garbage, garbage biological-dried products, and crushed straw at a ratio of 7:2:1 to obtain a mixed material, placing the mixed material in a groove-type compost reactor to obtain 1.6-2 m high pile body, inserting a temperature sensor at 0.4 m, 0.9m, and 1.4m of the pile body from bottom to top to measure temperature of the pile body, and covering 20 cm thick straw pads on the surface to fill the garbage pile body;    (B) biologically drying the garbage pile body by intermittently ventilating at 1-3 m3/minute; and    (C) removing straw pads on the surface of the garbage, removing the dried garbage from the reactor, and sorting the dried garbage by a vibration sieve.
NOVELTY - An energy-saving environment-friendly fuel comprises fuel heavy oil, biomass fuel and fuel additive having a weight ratio of 5-7:3-2:2-1. The fuel is prepared via a combustion engine in an online manner during combustion.    USE - An energy-saving environment-friendly fuel.    ADVANTAGE - The fuel reduces fuel cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a fuel combusting engine comprising:    (A) a fuel mixer;    (B) a combustion engine;    (C) an automated combustion-stabilizing control system;    (D) a mixing cavity arranged in the fuel mixer;    (E) a biomass fuel pipeline;    (F) a heavy oil pipeline;    (G) a fuel additive pipeline;    (H) an oil spraying gun installed on the combustion engine;    (I) a fan;    (J) a cyclone plate installed on the combustion engine;    (K) a heating device installed on the fuel circulating pipeline;    (L) an oil returning pipe;    (M) an electric valve arranged on the oil inlet pipe; and    (N) a unidirectional electric proportional valve arranged on the oil returning pipe; the fuel combusting engine.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a fuel combusting engine.
NOVELTY - A (1S,2R,5R)-6-(4-methoxyphenyl)-2-methyl-4,7-dioxo-3-oxa-6-azabicyclo(3.2.0)heptane-5-ethyl carboxylate is new.    USE - A (1S,2R,5R)-6-(4-methoxyphenyl)-2-methyl-4,7-dioxo-3-oxa-6-azabicyclo(3.2.0)heptane-5-ethyl carboxylate.    ADVANTAGE - The compound can be prepared at low cost using easily obtained raw materials. The method has high yield and simple operation, is environment friendly, and is easy for mass-production.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) an intermediate compound of formula (I) for synthesizing (1S,2R,5R)-6-(4-methoxyphenyl)-2-methyl-4,7-dioxo-3-oxa-6-azabicyclo(3.2.0)heptane-5-ethyl carboxylate (II); and    (2) a method for preparing compound (II).
NOVELTY - Prednisolone hydrate is obtained by mixing acetone and water in a ratio of 7:3 in solvent (15 times), dissolving prednisolone at 15-20 degrees C for 5-10 minutes, diluting the solution using water (80-100 times), filtering, drying the solution at 90-100 degrees C, and controlling water content below 7%.    USE - Production of prednisolone hydrate useful in pharmaceuticals.    ADVANTAGE - The method replaces dimethylformamide having high boiling point with acetone having low boiling point, and solves problems of existing technique such as unqualified solvent and non-recyclable solvent.
NOVELTY - An industrial fuel gas comprises industrial propane gas with purity higher than 95% and liquid-phase synergistic additive which is 0.3-1% of the industrial propane gas.    USE - An industrial fuel gas.    ADVANTAGE - The fuel gas contains little amount of liquid-phase synergistic additive added into propane gas, thus increasing burning temperature and improving burning efficiency of the gas. The liquid-phase synergistic additive has less corrosive action on a vessel and has good volatility.
NOVELTY - A liquefied natural gas is prepared from methyl alcohol purge gas by decompressing methyl alcohol purge gas to 2-6.5 MPa, and pre-heating to 250-350 degrees C; under the action of methanation catalyst, performing methanation reaction to make hydrogen gas in the purge gas react with carbon monoxide and carbon dioxide; and using cryogenic separation technology to obtain liquefied natural gas and by-product of hydrogen-rich gas.    USE - Method for preparing liquefied natural gas (claimed).    ADVANTAGE - The method can obtain liquefied natural gas with high content of methane, non impurity and high heat value. It protects the environment, saves energy and breaks a new path for clean energy.
NOVELTY - A vehicle fuel comprises (wt.%) liquefied petroleum gas (LPG) (20-90) and absolute methanol (10-80). The fuel further comprises 10-800 ml of organic solvent comprising petroleum ether, dimethylbenzene, ethanol, and methyl t-butyl ether. A pressure gauge tank is filled with the mixture of the LPG, absolute methanol, and organic solvent.    USE - A vehicle fuel.    ADVANTAGE - The fuel avoids mechanical stirring technique of product, improves using function of the fuel, saves the fuel, and reduces exhaust gas and pollutant emissions. The raw materials are featured by vast sources and low costs.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for mixture-spraying technique.
NOVELTY - The AS-system comprises an activation camera (2), a classifier (3), a drive shaft (4), an activator, and a channel to supply hot air.    USE - The AS-system is useful for: drying and grinding of biomass in the production of solid bio flues such as pellets and briquettes; blade grinding of woods and other plant materials during production of liquid bio fuels and solvents such as acetone bio butanol and hydrogen; preparation of biomass such as wood waste, lignin, peat and agricultural waste including manure and dry powdered flour for high-efficiency dust burners, boilers, power plants and thermal power plants; and drying and milling of herbs and an another vegetable raw materials in pharmaceuticals.    ADVANTAGE - The AS-system is capable of adjusting a fraction size without stopping the drying and grinding process and effectively, rapidly, easily, reliably and economically drying and grinding the biomass in less consumption of electricity and thermal energy.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic view of an AS-system.    Frame (1)    Activation camera (2)    Classifier (3)    Drive shaft (4)    Feed unload. (5)
NOVELTY - Preparing a product mixture of hydrocarbon from plant triglycerides comprises: providing the plant triglyceride at 320-495 degrees C in a melt of alkali hydroxide, which is movably present in a reaction container (1); discharging the resulting gaseous reactant product containing short chain hydrocarbons; and removing the obtained condensate containing saturated 5-19C hydrocarbon from the reaction container.    USE - The method is useful for preparing a product mixture of hydrocarbon from plant triglycerides.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of a device for preparing a product mixture of hydrocarbon from plant triglycerides.    Reaction container (1)    Heating jacket (2)    Stirrer (3)    Mixture of triglyceride/alkali hydroxide (4)    Inlet. (5)
NOVELTY - Biotechnologically produced bioproduct formulation made of white-rot fungi mycelia, immobilized on pressed and/or powdered renewable raw materials for fungal exolytic degradation of biogenic heterogeneous ligno-cellulosic materials to increase the bacterial bioconvertibility of such complex substrates, is claimed.    USE - The formulation is useful for: fungal exolytic degradation of biogenic heterogeneous ligno-cellulosic materials to increase the bacterial bioconvertibility of such complex substrates; and the pretreatment of poorly fermentable biogenic lignocellulose substrates in biogas production and the compost production (claimed).    ADVANTAGE - The bioproduct formulation increases the biogas yield to 10-30%.
NOVELTY - A conversion battery comprises conversion battery unit which electrically stores electrical energy by converting relative low energy substance such as ethanol (alcohol) into relatively high energy substance such as hydrogen.    USE - A conversion battery used for home-use heating, cooking, wash, cleaning, or miscellaneous business.    ADVANTAGE - The conversion battery has high energy efficiency, and low impact to environment.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of conversion battery. (Drawing includes non-English language text).
NOVELTY - The method involves stacking several fuel cells to form a cell laminated structure. The cell laminated structure is compressed from the direction orthogonal to cell lamination direction. A gas flow path hole (8) is extended in a gas diffusion layer by performing compression at the surface direction.    USE - Manufacturing method of fuel cell (claimed).    ADVANTAGE - The gas flow path hole is extended in the gas diffusion layer by performing compression at the surface direction so that burr produced in machining stage is eliminated without damaging gas diffusion layer and gas flow path layer and physique miniaturization of the fuel cell can be achieved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a longitudinal cross-sectional view illustrating the manufacturing process of fuel cell.    Membrane electrode assembly (3)    Separator (6)    Gasket (7)    Gas flow path hole (8)    Fuel cell (200)
NOVELTY - The device has a gasifying boiler arranged with an air inlet pipe (7) on a side. A lower part of a shell body of the gasifying boiler is provided with a ring-shaped tar processing device that is orderly equipped with a drying layer, a dolomite catalytic cracking layer (2) and a charcoal catalytic cracking layer (1) from up to down. The ring-shaped tar processing device is communicated with the air inlet pipe, and an ash outlet (4) is arranged below a combustion section (3). An air supply pipe (8) is arranged on a bottom part of the device.    USE - Decoking device for a household biomass gas making boiler.    ADVANTAGE - The device integrates gasifying and thermal cracking functions, so that tar is decomposed into permanent gas via making produced gas to pass through the catalytic cracking layer in a circulating manner, thus reducing the content of the tar during gasifying the biomass in an effective manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a decoking device.    Charcoal catalytic cracking layer (1)    Dolomite catalytic cracking layer (2)    Combustion section (3)    Ash outlet (4)    Air inlet pipe (7)    Air supply pipe (8)
NOVELTY - The electrochemical mercury-free hydrogen cell comprises a metal anode, an electrolytes and a gas diffusion electrode, where the metal anode comprises zinc as main ingredient with additives of indium and bismuth. The electrolyte comprises materials such as corrosion inhibitors, surface-active substances, and viscosity formers. An inner surface of a current conductor directed to the metal anode comprises a coating with copper/zinc- and/or copper/tin- and/or a copper/zinc/tin alloy. The indium and bismuth has a concentration of 100-1000 ppm and grain sizes of 1-500 mu m.    USE - Used as an electrochemical mercury-free hydrogen cell.    ADVANTAGE - The electrochemical mercury-free hydrogen cell has improved corrosion resistance.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of an electrochemical mercury-free hydrogen cell.    Cup (4)    Lid (6)    Seal (8)    Coat (9)    Zinc anode. (10)
NOVELTY - The method involves realizing partial solidification of intermediate fluid i.e. liquefied natural gas (LNG), by heat exchange with liquid nitrogen to form partially solidified intermediate fluid, and realizing heat exchange between gaseous effluent and the partially solidified intermediate fluid to obtain partially condensed gaseous effluent including a gas phase and a condensate. The gas phase and the condensate are separated in a separation tank (34). The gas phase is evacuated to outer side of the separation tank to form treated gaseous effluent to be conveyed towards atmosphere.    USE - Method for treating gaseous effluent from a natural gas liquefaction assembly in a floating type liquefied natural gas liquefaction installation and a floating type natural gas producing, storing and unloading installation in an oil refinery industry, a gas industry or oil producing site.    ADVANTAGE - The method enables treating the gaseous effluent from the natural gas liquefaction assembly in an effective and inexpensive manner, and reducing harmful gas emissions to the environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an installation for treating gaseous effluent from a natural gas liquefaction assembly, comprising solidification partial units of intermediate fluid.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a gaseous effluent treating installation.    Separation tank (34)    Column (44)    Nozzle diffuser (50)    Conduit (52)    Drain pipe (66)
NOVELTY - The method involves circulating raw gaseous effluent through a heat exchanger (34) e.g. serpentine type heat exchanger, for being condensed partially by heat exchange with liquid refrigerant, and conveying the partially condensed effluent from the heat exchanger to a separation container (36). The liquid refrigerant is circulated via the heat exchanger for being evaporated partially by the heat exchange with the gaseous effluent. A portion of thermal power necessary for condensation of the gaseous effluent in the heat exchanger is provided by reheating of liquid nitrogen stream in circulation.    USE - Method for treating gaseous effluent from a natural gas liquefaction assembly in a floating type liquefied natural gas liquefaction installation and a floating type natural gas producing, storing and unloading installation in an oil refinery, a gas or oil producing site.    ADVANTAGE - The method enables treating the gaseous effluent from the natural gas liquefaction assembly in an efficient and inexpensive manner. The hydrocarbon content of the purified effluent circulating in a pipe is not greater than 5 percent in moles, thus reducing harmful gas emissions during the passage of hydrocarbon content in a flare.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an installation for treating gaseous effluent from a natural gas liquefaction assembly, comprising a heat exchanger.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a gaseous effluent treating installation.    Flare (32)    Heat exchanger (34)    Separation container (36)    Pipe (44)    Tank (50)
NOVELTY - Recycling of rubber to produce fuel oil, combustible gases and carbon black powder and steel, is disclosed. A heating system which generates electromagnetic wave, is also provided. The direct exposure of rubber to the electromagnetic wave is performed. While allowing direct heating of rubber, the size is reduced using shredder and pulverizer. The heat energy which can be consumed captively for pre-heating the rubber, is also generated. The process is also environmentally-friendly which does not emit hazardous gases. Image 1/1
NOVELTY - Producing a fatty acid derivative comprises culturing a host cell in the presence of a carbon source, where the host cell is genetically engineered to express or overexpress a gene encoding an ester synthase, and isolating the fatty acid derivative, or culturing a genetically engineered microorganism in the presence of an alcohol.    USE - The method and microorganism are used for producing a fatty acid derivative such as a fatty ester. The fatty acid derivative is used in a biofuel composition (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a fatty acid derivative produced by the method above;    (2) a fatty ester produced by the method above;    (3) a genetically engineered microorganism comprising a gene encoding an ester synthase, where the gene encoding the ester synthase is overexpressed relative to a wild-type ester synthase, and where the microorganism produces an increased level of a fatty ester relative to a wild-type microorganism;    (4) a genetically engineered microorganism comprising an exogenous control sequence stably incorporated into the genomic DNA of the microorganism upstream of a gene encoding an ester synthase, where the microorganism produces an increased level of a fatty ester relative to a wild-type microorganism; and    (5) a biofuel composition comprising the fatty acid derivative.
NOVELTY - The gasifier has a combustion zone, where gas is introduced and fuel i.e. pellet fuel, is combusted. A sensor i.e. pressure sensor, measures a preset condition e.g. pressure indicating potential updraft condition, in the gasifier. A grate subsystem for containing the fuel has a grinding mechanism. A controller controls the grinding mechanism in response to the sensor, and activates the grinding mechanism when the preset condition exists to reduce the collection of non-fuel products e.g. glass, metal and ceramic materials, on the grate subsystem.    USE - Gasifier for use in a waste-to-energy system, to produce gas to generate electricity using a feed stock i.e. post consumer waste including food products discharged from cafeterias and food service establishments and to provide heat.    ADVANTAGE - The gasifier utilizes the grate subsystem containing fuel feedstock to automatically reduce or eliminate the grate of clinkers and maintain correct pressure drop along a reactor while maintaining better pressure in the gasifier and minimizing waste of the feedstock.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method of controlling a gasifier including a grate.    DESCRIPTION OF DRAWING(S) - The drawing shows a top perspective view of a gasifier.    Housing (40)    Grate area (48)    Temperature sensor (52)    Conduit system (54)    Fixed grates (62a-62d)
NOVELTY - Converting lipids to alkyl esters, comprises: (a) receiving a reactant comprising one or more lipids; (b) mixing the reactant with an alcohol to form a mixture; (c) adding an acidic catalyst to the mixture; (d) heating the mixture to 50-350 degrees C; (e) controlling a pressure above the heated mixture to be 1-200 bar; and (f) converting at least a portion of the reactant to one or more alkyl esters.    USE - The method is useful for converting lipids to alkyl esters.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a biofuel comprising esters made by the method, where the biofuel has an ester profile indicative of the free fatty acids and the triglycerides, or lipid profile associated with the lipids from the one or more algae; and    (2) a reactor (100) for converting lipids to esters, comprising: one or more inlets to receive any of a reactant (110), and alcohol (120), and an acidic catalyst (130) into a sealed volume; mixing means to mix the reactant, alcohol, and catalyst; and a heater (170) to heat the mixture.    DESCRIPTION OF DRAWING(S) - The figure shows a diagrammatic representation of a reactor.    Reactor (100)    Inlet to receive reactant (110)    Inlet to receive alcohol (120)    Inlet to receive acidic catalyst (130)    Gas inlet (160)    Heater. (170)
NOVELTY - Production of butanol from lignocellulosic feedstocks comprises depolymerizing pentose from a lignocellulosic feedstock to form a remainder, where the depolymerizing step results in a stream comprising primarily pentose, and converting the pentose to butanol.    USE - The process is useful for preparing butanol (1-butanol, 2-butanol or iso-butanol) from lignocellulosic feedstocks comprising bagasse, rice straw, corn stover, Miscanthus, switchgrass, wheat straw, wood, wood waste, paper, paper waste, agricultural waste, municipal waste, sugarcane, energy cane, corn, maize, Sorghum, sweet Sorghum and/or sugar beet (all claimed), where the butanol is useful in biofuel applications.    ADVANTAGE - The process is less expensive and more efficient than known processes. The method includes a pentose only conversion process, such as without a substantial amount of hexose.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) the butanol made by the process; and    (2) a butanol plant (210) for producing butanol from a lignocellulosic feedstock, comprising: a lignocellulosic feed system (214); a pentose depolymerization unit (218) for removing pentose from the lignocellulosic feedstock to form a remainder, where the depolymerization results in a stream comprising primarily pentose; and a pentose conversion unit (224) for converting pentose to butanol.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a butanol plant with a hexose conversion unit.    Butanol plant (210)    Feed system (214)    Pentose depolymerization unit (218)    Pentose conversion unit (224)    Steam line. (230)
NOVELTY - Method for deodorizing sludge odor using metal oxide, involves mixing silicon oxide, potassium oxide, titanium oxide, calcium oxide, magnesium oxide, sodium oxide, manganese oxide, trace amount barium oxide, chromium oxide, and phosphorus oxide to form geopolymer, filling the obtained mixture into cylindrical mesh, injecting the mixture into bad odor generating object including waste sludge, and excrement of livestock, and decomposing the bad odor in the waste material to form biogas.    USE - The method is useful for deodorizing sludge odor using metal oxide (claimed).    ADVANTAGE - The method is simple, inexpensive as the production cost is reduced up to 1/30 and expense for industrial base is reduced up to 1/50, improves operation rate up to 70% or more and does not require any heating process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for decomposing sludge.
NOVELTY - Preparing olmesartan medoxomil from alkaline earth metal salts of trityl olmesartan, comprises: reacting alkaline earth metal salts of trityl olmesartan and 4-chloromethyl-5-methyl-2-oxo-1,3-dioxolene in water miscible organic solvent in the presence of base; extracting the obtained product in water immiscible solvent; and treating the obtained product with an acid to obtain a precipitate, where the precipitated product is isolated by filtration, washing and slurring to obtain olmesartan medoxopil.    USE - The process is useful for olmesartan medoxomil (claimed), which is useful for lowering blood pressure. No biological data given.    ADVANTAGE - The olmesartan acid impurity in the final product is not more than 0.3%. The process is efficient, robust, cost effective and environmental friendly. The process can use minimal acid and other solvents that are easier to handle during large scale production.
NOVELTY - The system has a hydrogen generation device comprising an oxidation gas supply unit that supplies oxidation gas to carbon monoxide removal device. A controller controls a manipulated variable of oxidation gas supply unit before and after halting the power-generating operation in a manner such that amount of oxidation gas supplied to removal device is larger than last supply amount of oxidation gas during the power-generating operation. The controller performs a purge operation within the hydrogen generation device after controlling manipulated variable of oxidation gas supply unit.    USE - Fuel cell system.    ADVANTAGE - The dew condensation by carbon monoxide removal device can be suppressed, while reducing the energy consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for operating method of fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows the flowchart illustrating the stop method of fuel cell system.
NOVELTY - The apparatus (13) has upflow anaerobic sludge blanket (UASB) reactor (7) that performs denitrifying process of nitrogen containing waste water. A liquid cyclone apparatus (17) collects the suspended particle-like organic substance contained in nitrogen containing waste water, and supplies the suspended particle-like organic substance to UASB reactor as nucleus of granule sludge (29).    USE - Denitrifying apparatus for biological nitrification denitrifying apparatus (claimed) of circulation upflow anaerobic sludge blanket (UASB)-siphon sponge batch (SSB) system, used for purifying water in large sized water tank, pond and home-use small water tank.    ADVANTAGE - Since the liquid cyclone apparatus is provided, the growth of granule sludge can be stabilized and granule sludge can be maintained in appropriate quantity. Denitrifying performance of reactor can be stabilized and size of apparatus can be reduced. The denitrifying apparatus can be manufactured at low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biological nitrification denitrifying apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biological nitrification denitrifying apparatus. (Drawing includes non-English language text)    Biological nitrification denitrifying apparatus (1)    UASB reactor (7)    Conveying pump (11)    Liquid cyclone apparatus (17)    Granule sludge (29)
NOVELTY - Pelleting press (3) for producing pellets (10) from a biomass (1), comprises: at least one matrix (4) with many holes for pressing the biomass; at least one roller (5) rolling on a rolling surface of the matrix; at least one driving device for the matrix and/or the roller; a flat carrier plate adjacent to the matrix for storing the matrix in a passing direction of the biomass after the matrix; and at least one opening in the carrier plate for releasing the holes of the matrix. The biomass consists of cellulose- and/or lignocellulose-containing fibers, chips or particles.    USE - The pellets are useful as a fuel in fireplaces.    ADVANTAGE - The pelleting press allows using the matrix with the lowest possible height, and thus the holes have the smallest possible length.    DESCRIPTION OF DRAWING(S) - The figures 1 and 2 show a top view of the rectangular segmented matrix and the underlying carrier plate in the pelleting press with the reversing roller, and a sectional view of the matrix along a sectional line through the segmented matrix and the carrier plate, respectively.    Biomass (1)    Pelleting press (3)    Matrix (4)    Roller (5)    Pellets (10)
NOVELTY - Composition comprises at least one polyalkyl (meth) acrylate polymer having a number average molecular weight Mn of from 1000 to 10000 g/mol and a polydispersity Mw/Mn of from 1 to 8 and at least one ethylene vinyl acetate copolymer comprising units being derived from at least one alkyl (meth) acrylate having 1 to 30 carbon atoms in the alkyl residue.    USE - The composition is useful as flow improvers in fuel compositions (claimed), preferably for improving cold flow properties of fossil fuel oil and/or biodiesel fuel oil.    ADVANTAGE - The invention provides additives that are producible in a simple and inexpensive manner. It further provides composition with a high efficiency as cold flow improvers over a large concentration range.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method of using the composition comprising at least one polyalkyl (meth) acrylate polymer having a number average molecular weight Mn of from 1000 to 10000 g/mol and a polydispersity Mw/Mn of from 1 to 8 and at least one ethylene vinyl acetate copolymer comprising units being derived from at least one alkyl (meth) acrylate having 1 to 30 carbon atoms in the alkyl residue as flow improvers in fuel compositions.
NOVELTY - Organic waste processing apparatus comprises fermenter in an airtight state, bucket pump for pumping up process liquid containing methanogenic bacteria which is utilized for fermenting organic waste in anaerobic condition to obtain methane (biogas) in upper portion of fermenter, nozzle for injecting process liquid from upper portion of fermenter, floor substrate having multiple pores in upper position positioned from bottom wall of fermenter, air supplying unit and suction blower for emitting gas within fermenter.    USE - The apparatus is useful for fermenting organic waste for producing biogas.    ADVANTAGE - The apparatus can continuously ferment organic waste without separate process liquid tank and drain passage. The apparatus has simplified structure and reduced size.    DETAILED DESCRIPTION - Organic waste processing apparatus comprises fermenter in an airtight state, bucket pump for pumping up process liquid containing methanogenic bacteria which is utilized for fermenting organic waste in anaerobic condition to obtain methane (biogas) in upper portion of fermenter, nozzle for injecting process liquid from upper portion of fermenter, floor substrate having multiple pores in upper position positioned from bottom wall of fermenter, air supplying unit and suction blower for emitting gas within fermenter, where the organic waste is deposited on floor substrate for carrying out fermentation, process liquid is stored by downward space of floor and fermenter is heat insulation tank provided with rotational shaft and stirring blade at periphery of shaft. The fermentation process is carried out by driving the bucket pump and suction blower in presence of aerobic microorganism including Geobacillus thermo denitrificans and/or G.caldoxylosilyticas. An INDEPENDENT CLAIM is included for method of fermenting organic waste using the above-mentioned apparatus.
NOVELTY - Woody biomass agricultural method, involves mixing wooden soil conditioner and processed organic substance, and applying the mixture to surface or surface layer of soil of target location, preferably field or artificial cultivation container. The wooden soil conditioner is obtained from base material of processed wood. The processed organic substance is prepared by obtaining organic waste chosen from agricultural residue, weeds and foodstuff residue, decomposing the obtained material, and fermenting the decomposed material using microorganisms.    USE - The woody biomass agricultural method is useful for improving soil fertility (claimed) and increasing yield of agricultural products.    ADVANTAGE - The method is cost-effective and reduces use of chemical fertilizer and chemosynthesis agrochemical, and improves quality of agricultural product.    DETAILED DESCRIPTION - Woody biomass agricultural method, involves mixing wooden soil conditioner and processed organic substance, and applying the mixture to surface or surface layer of soil of target location, preferably field or artificial cultivation container. The wooden soil conditioner is obtained from base material of processed wood, preferably pulverized timber or chopped timber. The processed organic substance is prepared by obtaining organic waste chosen from agricultural residue, weed and foodstuff residue from a living environment, preferably home, decomposing the obtained material, and fermenting the decomposed material using microorganisms, where the microorganisms are chosen from Aspergillus, Bacillus natto, lactic acid bacteria and yeast.
NOVELTY - Method (M1) for marking a petroleum product, involves adding a covert dye to petroleum product. The covert dye is chosen from boron azadipyrromethene dye, boron dipyrromethene dye and their mixture.    USE - The methods are useful for marking and identifying counterfeit or adulterated petroleum product chosen from gasoline, diesel fuel, biodiesel fuel, kerosene, liquefied petroleum gas, ethanol and industrial solvent (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method (M2) for identifying a petroleum product, involves spectroscopically analyzing a portion of the petroleum product for presence of a convert dye;    (2) method (M3) for detecting a counterfeit or adulterated petroleum product, involves repeating the above-cited method (M2), determining concentration of at least one convert dye in the portion of the product, and comparing the determined concentration with a target concentration; and    (3) marked petroleum product comprising mixture of a fluid petroleum product and the dye.
NOVELTY - A hydrogen generator contains a solid fuel mixture, a liquid reactant, a liquid delivery medium, a movable boundary interface, a reaction zone, and a product separation medium fluidly coupled to the reaction zone by a fluid junction, and degassing the product. The movable boundary interface provides constant contact between reacting surface of solid fuel mixture and liquid reactant delivered by liquid delivery medium to form the reaction zone.    USE - Hydrogen generator.    ADVANTAGE - The hydrogen generator stably and efficiently enables production of hydrogen.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for filter conditioning method of hydrogen generator.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of hydrogen generation system.    Hydrogen generation system (100)    Storage for liquid reactant (102)    Pump (104)    Reaction chamber (106)    Product separation medium (108)
NOVELTY - Method for treating organic wastewater, involves processing organic waste using microorganisms in an aerator, which maintains dissolved oxygen concentration to 10 mg/l or more. The microorganisms are chosen from Xanthomonas, Ralstonia, Flavobacterium, Desulftalea, Polaromonas and Stenortophomonas.    USE - The method is useful for treating organic wastewater and suppressing production of surplus sludge (claimed).
NOVELTY - Method for purifying soil contaminated with dioxin, involves maintaining activity of dioxin decomposition microorganism in soil and adding product of Italian ryegrass or Aloe to the soil.    USE - The method is useful for purifying soil contaminated with dioxin.    ADVANTAGE - The method is environmentally-friendly.
NOVELTY - The furnace has carbonizing roller and jet fluid burner (11) that is provided in the outlet port of fuel gas input pipeline (13). The roller ends are sleeved at empty core rotating axis head (4) is provided in input pipeline and spiral sealed material sender (1). The outlet pipe is provided between sender and head. The horizontal type tabulation heat exchangers (7) are fixed with roller and heat is distributed in roller. The heat exchanging pipe passes heat through inserting holes of pipe boards are connected with burner which is provided with overflow port (16).    USE - Solid biomass inner combustion carbonizing gasifying furnace.    ADVANTAGE - The high temperature flame of the fuel gas is jetted directly contacting the material to heat the material rapidly, so that moisture and volatilizing substance in the material can be rapidly distilled out. The hot smoke gas and the distilled substance pass the heat exchanging tabulation through overflow port to indirectly transmit partial heat energy to gasified the substance through pipe wall for combining the direct carbonizing and indirect carbonizing, so that drying gasified substance is improved, time for carbonizing the material and power consumption for carbonizing are reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows sectional view of solid biomass inner combustion carbonizing gasifying furnace.    Spiral sealed material sender (1)    Empty core rotating axis head (4)    Horizontal type tabulation heat exchanger (7)    Jet fluid burner (11)    Overflow port (16)
NOVELTY - Diesel comprises (in %): methanol (85-90) and additive (10-15).    USE - The diesel is useful in current engine and combustor (claimed).    ADVANTAGE - The diesel is environmentally-friendly and has excellent dynamic property. The liquid fuel of the diesel oil can be replaced.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) additive comprising (in %): isobutyl nitrate (35-40), naphthenic acid (10-20), 2-ethyl alcohol (10-15), plant oleic acid (20-30), ethyl nitrate (10-20), cobalt acetate (1000-2500 ppm) and antiseptic (1-3); and    (2) method of manufacturing the above-cited diesel, involves adding methanol into synthesis tank, adding additive to the methanol and stirring the mixture by circulating pump.
NOVELTY - Biomass granular fuel comprises (in wt.%): plant straw (50-60), anthracite (2-5), coal slime (15-20), yellow mud (2-5), waste oil (2-5), food waste (8-12), water (8-12) and animal manure (10-15), where the total content of all the components is 100 wt.%.    USE - As biomass granular fuel.    ADVANTAGE - The biomass granular fuel is environmentally-friendly and can be obtained cost-effectively. The utilization rate of heat energy, combustion time and air permeability of the biomass granular fuel can be increased.
NOVELTY - Use of a room temperature curable coating agent for cathodic corrosion protection in the form of an aerosol spray or a color paint, produced by mixing metal alkoxide (5-95 wt.%) having metal pigment (5-95 wt.%), and adding a solvent and up to 10 wt.% (based on the solid amount) of a catalyst, is claimed.    USE - The cathodic agent is useful for cathodic corrosion protection.    ADVANTAGE - The coating agent: with stain resistant and hydrophobic and oleophobic properties exhibits controlled reduction in activity by covering individual metal particles with a conductive or semi-conductive metal oxide coating, thus protects the cathodic corrosion; is scratch resistant and abrasion resistant; and provides a good adhesion surface for polyurethane and silicone sealants.