NOVELTY - The system has a heating device connected with a reaction unit. First and/or second reaction devices is/are connected through a high-pressure separator, a stabilizer system and an extracting system. The extracting system is connected with a recovering system, and connected with a residual extracted oil cutting system. The residual extracted oil cutting system is connected with an evaporating dehydration system through a side line. The evaporating dehydration system is connected with third and/or fourth reaction devices and connected with the high-pressure separator.    USE - Naphtha reformed system for producing high-octane petrol and aromatic hydrocarbon in large scale.    ADVANTAGE - The system greatly increases processing capacity, liquid recovery rate, aromatic hydrocarbon yield and hydrogen yield.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a naphtha reformed system.
NOVELTY - The boiler has a fuel gas furnace (1) and a gas generating furnace (2) separated in left and right ends, where a bottom in the fuel gas furnace is provided with a burner (3) without a coal burning hearth. An upper part in the fuel gas furnace is provided with a pipe type fire pipe (4). The fuel gas furnace and the gas generating furnace are integrated into upside and downside in the boiler. A side of the upper part of the gas generating furnace is provided with a hand material twisting feed hopper. The hand material twisting feed hopper is provided with a sealing cover.    USE - Biomass gas generating fuel gas boiler for a home-made burner.    ADVANTAGE - The hand material twisting feed hopper is provided with the sealing cover, so that the boiler is convenient to feed material, and the floor space is saved.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a biomass gas generating fuel gas boiler.    Fuel gas furnace (1)    Gas generating furnace (2)    Burner (3)    Pipe type fire pipe (4)
NOVELTY - The device has a furnace body (13) whose upper end is installed with an upper cover (1). A side of the body is provided with oil-water separator layers (4, 5). The upper cover is provided with a flange plate (2). The oil-water separator layer (4) is provided with an exhaust pipe (3), and the other oil-water separator layer (5) is provided with a furnace connection pipe (6). The oil-water separator layers are respectively provided with an automatic oil-water discharge valve (7). The body is internally installed with a water jacket (9) whose upper end is provided with an upper water pipe (8).    USE - Multi-functional straw heating gasification heating device.    ADVANTAGE - The device has simple structure, rational design, convenient operation, and feeding and ignition at once, heating effect for 24 hours, better heating continuity, good combustion, large heating calorific power, and better energy conservation and wide range of application. The gas can be utilized for both cooking and heating. The furnace is safe, environment conservation, non-pollution, and prolongs the service life.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a multi-functional straw heating gasification heating device.    Upper cover (1)    Flange plate (2)    Exhaust pipe (3)    Oil-water separator layers (4, 5)    Furnace connection pipe (6)    Automatic oil-water discharge valve (7)    Upper water pipe (8)    Water jacket (9)    Furnace body (13)
NOVELTY - The stove has a burning body provided with a smoke passage cover, a smoke passage plate, a hearth, a grate and an ash hopper that are orderly connected up and down. The smoke passage plate is provided with a fire check ring and a smoke gas opening. A fuel door and a secondary air hole are mounted at a lateral surface of the hearth, where the secondary air hole is surrounded by a shield. The ash hopper is internally provided with an adjustable primary air door. A fuel door is provided with a fire observation window i.e. high temperature glass bar.    USE - Biomass fuel gasification combustion domestic stove.    DESCRIPTION OF DRAWING(S) - The drawing shows an exploded perspective view of a biomass fuel gasification combustion stove.
NOVELTY - The furnace has a row material cylinder connected with a separator that is connected with a combustion device, where the separator has a closed cylinder provided with a filtering screen. An oxygen transferring cover is made of fire resisting material and installed on a fire resisting material layer that is provided at a bottom part of the row material cylinder. An oxygen transferring pipe is installed inside the oxygen transferring cover and connected with an air blower. The oxygen transferring pipe is connected with the separator, the combustion device, and the row material cylinder.    USE - Environment-friendly and energy-saving biologic gasification heating stove.    ADVANTAGE - The device has high heat efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial sectional perspective view of an environment-friendly and energy-saving biologic gasification heating stove.
NOVELTY - Methane (134) is manufactured on a large scale by supplying a waste material or biomass (110) to a plasma melter (112); supplying electrical energy to the plasma melter; supplying steam to the plasma melter; extracting a syngas (118) from the plasma melter; extracting hydrogen from the syngas; and forming methane from the hydrogen produced in the extraction of hydrogen.    USE - Method of manufacturing methane on a large scale (claimed).    ADVANTAGE - The method utilizes minimal fossil fuel, and thus produces a minimal carbon footprint when compared to conventional processes. It does not require large electrical generation resources and consumption of natural resources, produces methane inexpensively using hydrogen, and provides a plasma melter to generate large amounts of methane. Further, carbon dioxide is obtained from a renewable energy source, and hence does not constitute an addition to the greenhouse gas carbon base.    DESCRIPTION OF DRAWING(S) - The drawing shows a simplified function block and schematic representation of a method of manufacturing methane on a large scale.    Biomass (110)    Plasma melter (112)    Syngas (118)    Water gas shift process (122)    Carbon dioxide (126)    Sabatier reactor (128)    Methane (134)
NOVELTY - Botanical plants protecting agent is prepared from salicylic acid, cinnamic aldehyde or cinnamon oil, solvent, surfactant, and water at mass-volume ratio of 0.5-1.5:2.0-6.0:5.0-15.0:0.5-1.5:80-220, where 1 part of salicylic acid is equivalent to 1 g and the other raw materials are calculated based on volume ratio, where 1 part is equivalent to 1 ml.    USE - Botanical plants protecting agent used for inducing disease resistance in fruits and vegetables, with sterilizing function.    ADVANTAGE - The protecting agent is a green and environment-friendly plants protecting agent, which is safe to crops, human, and livestock; has simple preparation and low cost; and does not cause drug resistance to pathogenic bacteria.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of botanical plants protecting agent comprising dissolving salicylic acid with organic solvent to prepare salicylic acid solution; adding cinnamic aldehyde or cinnamon oil in salicylic acid solution and stirring uniformly to obtain mixing liquid; preparing surfactant into 0.5-1.0 vol.% emulsion using distilled water or tap water; adding the obtained mixing liquid in the obtained emulsion; and mixing uniformly.
NOVELTY - Recycling glyphosate mother liquor comprises: (a) neutralizing the raw mother liquor produced in the production process of preparing the glyphosate with alkali; (b) infusing hydrogen chloride or adding hydrochloric acid into the concentrated mother liquor; (c) further concentrating the mother liquor obtained in (b), continuously separating out the sodium chloride, centrifuging, removing the settlement, obtaining the mother liquor comprising glyphosate; and (d) adjusting pH value of the mother liquor, and separating out the glyphosate solid, filtering and recycling the glyphosate.    USE - The process is useful for recycling glyphosate mother liquor (claimed).    ADVANTAGE - The process can adequately utilize the effective components contained in the mother liquor, eliminate the pollution to natural environment, and synchronously and effectively reduce the production cost of the glyphosate.    DETAILED DESCRIPTION - Recycling glyphosate mother liquor comprises: (a) neutralizing the raw mother liquor produced in the production process of preparing the glyphosate with alkali, concentrating to obtain the concentrated mother liquor; (b) infusing hydrogen chloride or adding hydrochloric acid into the concentrated mother liquor until the sodium chloride in the mother liquor is separated out, centrifuging, removing the settlement, and storing the mother liquor; (c) further concentrating the mother liquor obtained in (b), continuously separating out the sodium chloride, centrifuging, removing the settlement, obtaining the mother liquor comprising glyphosate; and (d) adjusting pH value of the mother liquor comprising glyphosate obtained in (c) with alkaline substance until the glyphosate is at equivalence point, and separating out the glyphosate solid, filtering and recycling the glyphosate, or adjusting the pH value to be 4-8.5, and preparing the glyphosate aqueous agent.
NOVELTY - A combustion processing method of sludge involves mixing wood chips to the sludge and burning using a sludge combustion furnace.    USE - Combustion processing method of sludge for making fertilizer (claimed).    ADVANTAGE - The process is low cost, carbon dioxide emission is reduced and environmental impact is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fertilizer formation method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of combustion plant of sludge. (Drawing includes non-English language text).    Fluidized bed (1)    Conveyor (11)    Hopper (12, 13)    Sludge combustion furnace (20)    Gas supply section (21)    Plate-shaped unit (21A)
NOVELTY - A herb biomass is saccharified by chemically processing herb biomass with dilute alkali with concentration of 0.01-10 wt.% or dilute acid and organic solvent, and processing herb biomass after chemical processing by Clostridium genus bacteria.    USE - Saccharification of herb biomass for manufacturing alcohol e.g. ethanol and biofuels e.g. bio-butanol, organic acid, amino acid and bioethanol.    ADVANTAGE - The method is inexpensive and efficient.
NOVELTY - The nitro-compound fertilizer production device has a nitric acid waste liquor tank and an ammonium nitrate waste liquor tank. The nitric acid waste liquor tank and the ammonium nitrate waste liquor tank are connected to a neutralizing tank connected to an electrodialysis tank.    USE - Nitro-compound fertilizer production device.    ADVANTAGE - Helps solve problem of environmental pollution caused by nitric acid waste liquor and ammonium nitrate waste liquor. Offers simple and convenient to use production device that conserves energy and provides environmental protection. Recycles available components from industrial waste water. Ensures zero emission of industrial waste water of nitric acid and ammonium nitrate. Carries out comprehensive utilization of resources. Improves performance of enterprises. Improves ability of resisting risks of enterprises.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of a nitro-compound fertilizer production device.
NOVELTY - R-mandelic acid and derivatives production involves taking 10-50 millimoles per liter per l of racemic mandelonitrile compound as substrate and carrying out hydrolysis reaction at the pH value of 8.0-8.5 and at a temperature of 20-60 degrees C in a reaction system to obtain chiral R-mandelic acid and derivatives. The reaction system contains nitrile hydrolase obtained by Bacillus faecalis alcaligenes CCTCC No: M 208168 as catalyst.    USE - Method for producing R-mandelic acid and derivatives (claimed).    ADVANTAGE - The R-mandelic acid and derivatives production method is cost-effective, requires less amount of strain dosage, generates less amount of waste water, generates less pollution, makes use of mild reaction conditions, and ensures low energy consumption and high yield of R-mandelic acid and derivatives having high conversion rate, on industrial scale.    DETAILED DESCRIPTION - The racemic mandelonitrile compound has a chemical formula (I). The chiral R-mandelic acid and its derivatives have a chemical formula (II).    R=H or halogen.
NOVELTY - A biodiesel composition comprises biodiesel and phenol amide compound (I and/or II).    USE - Biodiesel composition.    ADVANTAGE - The biodiesel composition has improved oxidation stability.    DETAILED DESCRIPTION - A biodiesel composition comprises biodiesel and phenol amide compound of formula (I and/or II).    n,q1,q2=1-3;    (CH2)p=alkylene;    p=0-6;    R1,R2,R4,R5=H, -((CH2)xNH)y-R6, -((CH2)x1NH)y1-C(=O)-R7 or group of formula (i);    m=0-6;    R3=H or 1-3C alkyl;    x,x1=2 or 3;    y,y1,y2=0-5;and    R6-R8=1-24C hydrocarbyl.    The hydroxy group in the compound (I) is located at ortho, meta or para position of carbon atom which is linked to alkylene or carbonyl on benzene ring. The hydroxy group in the compound (II) is located at ortho, meta or para position of carbon atom which crosslinks carbon atom between two benzene rings. An INDEPENDENT CLAIM is included for method of improving oxidization stability of biodiesel-containing fuel, which involves adding compound (I and/or II) to biodiesel-containing fuel.
NOVELTY - Invention relates to biotechnology, particularly to biological purification of waste water from oil products using active sludge and a biological preparation Destroyl. The method involves addition of Destroyl biological preparation to waste water before the aerotank and to active sludge before the aerotank, where Destroyl is added to the waste water and active sludge in ratio ranging from 3:4 to 4:3.    USE - Chemistry.    ADVANTAGE - Method increases efficiency of removing oil products. 2 cl, 1 tbl, 10 ex
NOVELTY - There is provided an improved, two-stepwise continuous device which transforms agricultural biomasses into biogas. The device comprises an aerobic/facultative anaerobic and an anaerobic bioreactors. The operative elements in the aerobic/facultative anaerobic reactor are a sealable upper lid and a mechanical stirring apparatus reactor, in which consists of aerobic/facultative anaerobic microorganism such as Trichoderma spp., Bacillus subtitles, Saccharomyces spp., and/or Acetobacterium spp., etc. The microorganism hydrolyses agricultural biomasses and generates organic acids. The anaerobic reactor is designed to contain absolute anaerobic microorganism such as Methanobacterium spp. And/or Methanobacterium spp., etc., so that the reactor may be used for methane production by transformation of organic acids, hydrogen, and carbon dioxide produced by the previous reactor. This new innovative device can effectively transform the agricultural biomasses into biogas, methane.
NOVELTY - A fuel source comprises a fuel object having maximum dimension of 6 cm, a volume of 10-100 cm3, a moisture content of less than 14 wt.%, where fuel object comprising a particulate derived (60-80 wt.%) from corn stover having a particle size of 100-35000 microns; a wood fiber (20-40 wt.%) having a particle size of 100-30000 microns; an inorganic base (1-10 wt.%); and where the fuel source is substantially free of coal as a heat source and the fuel provides at least 7000 BTU-lb-1 (3500 cal.-gm-1).    USE - In large-scale modern combustion energy generating systems.    ADVANTAGE - The fuel source is substantially free of coal as a heat source and the fuel provides at least 7000 BTU-lb-1 (3500 cal.-gm-1); provides high-energy, low-emission solid fuel made from natural renewable feedstocks. The fuel object of fuel source, has a high energy value, low emissions upon combustion, and highly efficient combustion, in a range of commercially available combustion technologies. The fuel object leads to a mechanically stable fuel object that is manufactured, stored, transported and used in modern combustion installations as is or is easily comminuted to a small particle size depending on the nature of the combustion process.
NOVELTY - Bio-reactor high-rate anaerobic lagoons (BLAAT) as improved processing unit for the treatment of biodegradable wastewater comprises: (a) a mixing chamber which is a structure that receives the raw wastewater; (b) a transition zone between the mixing chamber and a settling zone; (c) a collection of biogas structure which lies below and in the top of the zone of transition; and (d) a zone of enhanced sedimentation.    USE - The BLAAT is useful for treating wastewater (claimed).    ADVANTAGE - The BLAAT has simple operation and maintenance, which is reflected in low operating cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for treating wastewater that uses BLAAT comprising: (a) contacting the incoming waste water or substrate with a bed biologically active in a mixing chamber; (b) moving the wastewater to a transition area where you can make a change in the direction of water flow, without disturbing appreciably the kinetic energy; and (c) sediment wastewater from the transition zone in an area that presents enhanced sedimentation rates and a lower horizontal laminar flow.
NOVELTY - The vessel (30) has a syngas collection chamber (31) connected to a diptube (5) via a slap tap (9) that has a tubular part connected to an opening (36) of a frusto-conical part (35) of the chamber. Another tubular part (6) of the tap is connected to the frusto-conical part or to the former part and spaced away from the diptube to provide an annular space. A discharge conduit (19) in the space has a discharge opening located to direct liquid water along an inner wall of the diptube. Half of a vertical length of the former tubular part extends below the discharge opening.    USE - Reactor vessel for preparing a syngas by gasification of an ash comprising carbonaceous feedstock e.g. coal such as lignite, bituminous coal, sub-bituminous coal, anthracite coal and brown coal, petroleum coke, biomass and deasphalted tar sands residues.    ADVANTAGE - The frusto-conical part predicts blockage by the slag by measuring the temperature of the used cooling water or steam make in conduits of the frusto-conical part, and indicates decrease in temperature of the used cooling water or decrease in steam for a growing layer of the slag, thus operating the reactor vessel closer the optimal gasification temperature while simultaneously monitoring the slay layer thickness to minimize blocking risk by the slag.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a reactor vessel.    Diptube (5)    Tubular part (6)    Slap tap (9)    Discharge conduit (19)    Reactor vessel (30)    Syngas collection chamber (31)    Frusto-conical part (35)    Opening (36)
NOVELTY - An electrode has a conductive substrate provided with a superficial coating containing nickel co-deposited with amorphous molybdenum oxide component(s).    USE - Electrode is used as cathode for cell for electrolytic processes for hydrogen evolution (claimed). Uses include but are not limited to cell for producing chlorine and alkali and cell for producing chlorate and hypochlorite.    ADVANTAGE - The electrode has improved hydrogen evolution cathodic potential and high stability under alkaline environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of electrode, which involves adding amorphous molybdenum oxide component containing particles of molybdenum oxide, nickel molybdate and/or partially reduced molybdenum(VI) oxide to galvanic bath containing nickel ions, and carrying out galvanic co-deposition of nickel with the amorphous molybdenum oxide component(s) on cathode substrate. The partially reduced molybdenum(VI) oxide is of formula: HxMoO3, where x is 0-1.
NOVELTY - Preparation of an intermediate material from a lignocellulosic first material, comprises defibrating the first material in an extruder at a temperature of 600-1800 degrees C in the presence of water (200-450 mass% of the first material).    USE - The process is useful for the preparation of the intermediate material for the production of the ethanol (claimed), which is useful as fuel in a gasoline vehicle.    ADVANTAGE - The process is efficient and economical to provide intermediate material from lignocellulosic first material for the production of ethanol.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an intermediate product for ethanol production, obtained by the process.
NOVELTY - Producing fatty acid methyl esters (FAME) from palm fatty acid distillate, comprises: fractionation of the palm fatty acid distillate in a first fraction comprising 16C-free fatty acids (16C-FFA) and a second fraction comprising 18C-free fatty acids (18C-FFA) and a residue-R1; separate esterification of the first and second fractions with methanol in the presence of an acid catalyst to 16C-FAME and/or 18C-FAME; and production of a blend from 16C-FAME and 18C-FAME.    USE - The process is useful for producing FAME, which is useful as biodiesel for combustion engines (claimed).    ADVANTAGE - The process produces FAME in high yield and in an economical manner.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of a process for the production of fatty acid methyl esters (Drawing includes non-English language text).
NOVELTY - The molding apparatus has a processing tank (1) with extrusion screw shafts (2B) that are engaged with spiral tooth (21a,21b). A to-be-treated solid material having thermal melting property is injected and volume reduction compression is performed by rotation of extrusion screw shafts. An extrusion nozzle with nozzle holes (30) is provided to extrude condensate from bottom face of a material pool (4) provided at front-end board (11) of processing tank. The material pool is recessed at depth of 10-50 mm and is provided with nozzle blocks (3A,3B) at bottom face.    USE - Extrusion compression molding apparatus for volume reduction/recycling process of solid waste such as wood chip, paper, waste plastic, waste construction material and municipal solid waste.    ADVANTAGE - The residence time of the to-be-treated material is increased and the to-be-treated material is melted reliably so that favorable extrusion molding property can be obtained and the quality of the extrusion molded component can be improved.    DETAILED DESCRIPTION - The molding apparatus has a nozzle attachment opening (11b) is formed at the front-end board of processing tank and is fitted with the nozzle blocks detachably screwed to the front-end board of processing tank.    DESCRIPTION OF DRAWING(S) - The drawing shows a top view of the principal portion of extrusion compression molding apparatus.    Processing tank (1)    Extrusion screw shaft (2B)    Nozzle blocks (3A,3B)    Material pool (4)    Front-end board (11)    Nozzle attachment opening (11b)    Spiral tooth (21a,21b)    Nozzle holes (30)
NOVELTY - The apparatus has a tank container thermosetting part heating a tank container (10), where a fiber reinforced resin layer is formed in an outer surface of the tank container by winding a fiber. The tank container thermosetting part performs thermosetting process of the fiber reinforced resin layer. An ultrasonic bubble removal part removes the bubble produced on the surface layer of the tank container in the thermosetting process using air. An ultrasonic irradiation part removes the bubble by irradiating an ultrasonic wave to the bubble.    USE - Apparatus for manufacturing a high pressure gas holder for storing gas in a moving body i.e. fuel cell vehicle.    ADVANTAGE - The ultrasonic bubble removal part removes the bubble produced on the surface layer of the tank container in the thermosetting process using air, thus suppressing bubble generation during the thermosetting process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for manufacturing a high pressure gas holder.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic perspective view of a thermosetting processing apparatus.    Tank container (10)    Thermosetting processing apparatus (200)    Base (210)    Partition (215)    Rotational drive part (225)
NOVELTY - The hydrogen generator has several fuel pellets (3) that are installed on a board (16) corresponding to the position of the several blasting machines. Each fuel pellet is surrounded by a heat insulation structure (20). A grid frame formed by a heat leading structure (18) is arranged between two adjacent fuel pellets.    USE - Hydrogen generator for supplying hydrogen gas to hydrogen fuel battery used in portable information device e.g. mobile telephone, personal digital assistant (PDA), digital camera.    ADVANTAGE - Since the grid frame formed by heat leading structure is arranged between two adjacent fuel pellets, the hydrogen can be generated easily and efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows the top view of the hydrogen production unit.    Fuel pellet (3)    Board (16)    Heat leading structure (18)    Connector (19)    Heat insulation structure (20)
NOVELTY - The recuperator (3) has storage tank (10) in which liquid is stored. The liquid is heated by circulating the liquid between the storage tank and power generating unit (2). The amount of liquid circulated is increased when temperature of liquid sent into power generating unit from storage tank is less than predetermined temperature.    USE - Recuperator used in cogeneration system, for collecting heat generated by fuel cell.    ADVANTAGE - The reduction of temperature of liquid during the circulation process can be prevented, circulation time of liquid can be minimized and electric power generation efficiency can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the cogeneration system. (Drawing includes non-English language text)    Cogeneration system (1)    Power generating unit (2)    Recuperator (3)    Heat exchanger (6)    Storage tank (10)
NOVELTY - Preparation of fatty acid alkyl ester (I) from a feed stock containing free fatty acids, and fatty acid triglycerides, fatty acid diglycerides and/or fatty acid monoglycerides, comprises: (a) contacting feedstock with an alkyl alcohol (1-5C-alkyl alcohols), in the presence of one or more acidic catalysts, where the free fatty acid is esterified from the feedstock in order to obtain a reduced to free fatty acid feedstocks; and (b) transesterifying the reduced free fatty acid feedstock.    USE - The process is useful for preparing fatty acid alkyl ester, which is useful as biodiesel.    ADVANTAGE - The method does not generate additional impurities. The initial esterification controls the level, which leads to a reduced formation of soap in the subsequent transesterification step, hence the method is inexpensive, slows the process time, produces high yield and does not require additional purification steps.
NOVELTY - Fuel pellet comprises leaves or a mixture of leaves and shrub cuttings. The leaf comprises leaf blade, branch and/or branch pieces and/or tree residues.    USE - Used as a fuel pellet.    ADVANTAGE - The fuel pellets exhibits: high calorific value; high ash melting point and show a low ash ejection; low humidity, which leads to better flow properties, since the pellets do not stick or undergo clumping and high storage stability. The processing of the leaves into pellets leads to low space per weight ratio of the pellets and thus large quantities of the fuel can be stored in a small area. The use of the purified road leaves leads to the pellets with low mineral content and does not forms harmful contaminants during combustion. The pellets are stable without further additives and allow an even burning.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing fuel pellets made from leaves, comprising (b) drying unpurified leaf litter in a dryer, (c) separating the unpurified, dried leaves in a separation part, where the leaf litter is divided into at least two fractions, of which at least one fraction is a purified leaf fraction, (d) transporting the purified leaf fraction to a crushing device, (e) crushing the purified leaf fraction, preferably in a mill and (f) pressing the crushed and the purified leaves in a press to fuel pellets.
NOVELTY - A sewage treatment system for biogas tank comprises a bottom part of a second-grade settling chamber that is filled with an active carbon layer. The two sides of separating wall between the second-grade settling chamber and third-grade settling chamber are respectively provided with separating plates which are suspended under the top plate of purifying chamber. A macromolecular adsorbing layer is filled between the separating plates. The outer side wall of the upper part of third-grade settling chamber is provided with a water outlet.    USE - Sewage treatment system for biogas tank.    ADVANTAGE - Prevents pollution of environment since the water discharged from the water outlet is clean water.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of the sewage treatment system for biogas tank.
NOVELTY - Process control of a biogas plant comprises: measuring the quantities of organic acids and calcium ions during the operation of the biogas plant in predetermined intervals; determining the ratio of these quantities; and comparing the determined ratio for the respective intervals with the previous intervals. The ratio within the predetermined number of intervals increases at least to a factor of 2.5.    USE - Calcium oxide is useful: for regulating the amount of organic acids and/or the pH in a bioreactor; and for quick increase in the space load of the biogas reactor (all claimed).    ADVANTAGE - Calcium oxide used in the method: regulates the amount of formed organic acids and thus avoids the acidification and increases the production of biogas; and also increases the space load of the biogas plant.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for carrying out the process control of a biogas plant, comprising a bioreactor which comprises: at least one process control unit for the control of bioreactors with at least one input- and/or output unit, at least one sensor unit for the quantitative determination of organic acids and/or calcium, in which the data from the biogas reactor is transmitted to the process control unit, at least one output unit for a sensor unit, where the output unit is coupled to an input unit of the process control unit or may include input unit itself, so that the process control of the biogas plant is controllable; and at least an additional unit for liquid and/or solid, which is controllable by the process control unit, to introduce the liquid and/or solid in the reactor.
NOVELTY - The reactor has a fluidized bed (14) arranged in a reactor container (6) and comprising a base-forming fluidized bed phase (62) in a lower area and an easy fluidized bed phase in an upper area. A heat transport device (60) couples and decouples heat from the base-forming fluidized bed phase within the lower area of the container. A turbulent fluidized bed phase (64) is arranged between the base-forming fluidized bed phase and the easy fluidized bed phase. Primary air outlets (42) supply a primary fluidization medium i.e. air, within the lower area of the base-forming fluidized bed phase.    USE - Fluidized bed reactor i.e. combustion reactor (claimed), for use in a heatpipe reformer for combustion of solids i.e. wood.    ADVANTAGE - The reactor achieves higher efficiency for combustion of the solids and high temperature heat transfer, and prevents a sealing separation of pyrolysis arrears and bed materials.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of a heatpipe reformer with a combustion reactor comprising a laminated fluidized bed.    Reactor container (6)    Base plate (10)    Fluidized bed (14)    Primary air outlets (42)    Heat transport device (60)    Base-forming fluidized bed phase (62)    Turbulent fluidized bed phase (64)
NOVELTY - The method comprises gasifying flowable biomass through partial oxidation with pure oxygen, where the oxygen is obtained by electrolytic splitting of water and the raw gas is cleaned after cooling under heat recovery in a venturi washer. The pure gas is partially supplied to a spark ignition engine power station and the remaining part is transformed through mixing the hydrogen formed during electrolysis to methanol synthesis gas, where raw methanol is synthesized after the process. The raw methanol is temporarily stored in a tank farm.    USE - Method useful for simultaneous production of electric energy, hot gas and fuel for a closed settlement zone.    ADVANTAGE - The method ensures simple and efficient production of electric energy, hot gas and fuel for a closed settlement zone.    DETAILED DESCRIPTION - The method comprises gasifying flowable biomass through partial oxidation with pure oxygen, where the oxygen is obtained by electrolytic splitting of water and the raw gas is cleaned after cooling under heat recovery in a venturi washer. The pure gas is partially supplied to a spark ignition engine power station and the remaining part is transformed through mixing the hydrogen formed during electrolysis to methanol synthesis gas, where raw methanol is synthesized after the process. The raw methanol is temporarily stored in a tank farm. The methane necessary for heating purpose is formed through hydrogenation of raw methanol. The fuel variants are methane through hydrogenation of methanol, high alcohol mixture through oilgomerization of methane (splitting of water) and hydration, liquid gas through formation of low oligomers and hydrogenation, and oilgomerization and hydration to conventional gasolines and diesel fuels.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic flow diagram of a method for simultaneous production of electric energy, hot gas and fuel (Drawing includes non-English language text).
NOVELTY - Spent grain hydrolysis process comprises: (a) mixing the spent grain with waste water and surplus sludge in a container and subjecting to first solid hydrolysis step (2); (b) subjecting a defined amount to a solid-liquid separation (9); (c) adding the removed solids to a solid digesting lye; (d) subjecting to second solid hydrolysis (14); (e) subjecting to solid-liquid separation; and (f) subjecting the obtained liquid phase to third hydrolysis step (17).    USE - The method is useful for hydrolyzing spent grains.    ADVANTAGE - The method: is suitable for practical use; allows a high throughput rate; can be carried out with limited use of devices; and allows for recovery of all components of the spent grains.    DETAILED DESCRIPTION - Spent grain hydrolysis process comprises: (a) mixing the spent grain with waste water and surplus sludge in a container and subjecting to first solid hydrolysis step (2); (b) removing a defined amount from the container and subjecting to a solid-liquid separation (9); (c) adding the removed solids to a solid digesting lye and the mixture is maintained at a temperature; (d) subsequently subjecting the mixture from the solid digestion to a solid-liquid separation, where the separated solids are fed into a second solid hydrolysis (14) and the mixture is maintained at a temperature; (e) subsequently subjecting the mixture from the second solid hydrolysis to a solid-liquid separation; and (f) subjecting a liquid phase that precipitated during the solid-liquid separation to a separate third hydrolysis step (17).    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of spent grain hydrolysis process.    First solid hydrolysis (2)    Solid-liquid separation (9)    Second hydrolysis step (14)    Third hydrolysis step. (17)
NOVELTY - The household multifunction biomass gasifier has the stove body (1) and the filter device (6). A hearth is set inside the stove body. The gas exit at the upper part of hearth is connected to the combustion device (8) by the gas delivery pipe (10). A mini-typed blower (3) is installed at the bottom of stove body. A sealing cover (11) is installed at the upper mouth of stove body. A small hole is set on the sealing cover. A fire-banking device, comprised of compressive bar, fire-banking disk and hand lever, is installed inside the stove body.    USE - Household multifunction biomass gasifier for domestic use.    ADVANTAGE - Provides the household multifunction biomass gasifier which has simple structure, easy to use, has stable and persistent gas production process, high gas production amount, efficiently avoiding the open flame and spark out, high gas purifying quality, easy to get hot water, and can be widely applied to the rural-urban customers. Provides the domestic gasifier which has stable gas production, good condition of low oxygen combustion, high gas production amount, good filter effect, and is equipped with water-heating function.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the household multifunction biomass gasifier.    Stove body (1)    Mini-typed blower (3)    Filter device (6)    Combustion device (8)    Gas delivery pipe (10)    Sealing cover (11)
NOVELTY - A oil-impregnated crushed material obtained by mixing 5-20 parts weight of waste edible oil with respect to 100 parts weight of crushed biomass having moisture content of 5-25 weight%, is molded using a pelletizer, to obtain a pellet fuel.    USE - Manufacture of pellet fuel (claimed). Uses include but are not limited to boiler for heating e.g. green house cultivation, public facility, factory and hotel.    ADVANTAGE - The method provides pellet fuel which has high emitted-heat amount with reduced combustion residue and can replace fossil fuel. The method is easy and does not damage pelletizer and has reduced power consumption while molding.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for pellet fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows the flow chart of manufacture of fuel pellet. (Drawing includes non-English language text)
NOVELTY - A deodorizing decomposition processing material of organic waste is obtained by mixing used coffee powder and compost obtained by fermenting vegetable sediment, and carrying out deposition fermentation.    USE - Deodorizing decomposition processing material of organic waste e.g. excrement and organic refuse.    ADVANTAGE - The processing material efficiently and economically enables deodorization and decomposition of organic waste.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of deodorizing decomposition processing material of organic waste, which involves mixing inoculum, used coffee powder and vegetable sediment, carrying out deposition fermentation, drying, stopping fermentation and continuing re-culture process.    DESCRIPTION OF DRAWING(S) - The drawing shows the structure of portable toilet.    Portable toilet (1)    Deodorizing decomposition processing method (2)
NOVELTY - The suspended biological filler has an outer layer, a middle layer and an inner layer that are connected by strengthening ribs. Connecting fins are installed on the outer layer and middle layer.    USE - Suspended biological filler used in microorganism water treatment field.    ADVANTAGE - Improves specific surface area of the filler under condition of same volume, and improves biological film-hanging rate through specific design structure of the suspended biological filler. Improves oxidization resistance and ultraviolet resistance by using PE material, while prolonging service life.    DESCRIPTION OF DRAWING(S) - The drawing shows the cross sectional view of the suspended biological filler.
NOVELTY - A membrane-type biogas tank convenient to remove residues comprises a membrane-type biogas tank body, a feeding pipe, a material discharging pipe, a gas transferring pipe, and zipper residue removing holes; where the feeding pipe and the material discharging pipe are located on two ends of the biogas tank body; the gas transferring pipe is located on the middle part of the upper part of the biogas tank; and the zipper residue removing holes are located on the upper part of the biogas tank and two ends of the gas transferring pipe and are near to the side of the biogas tank.    USE - The membrane-type biogas tank convenient to remove residues is useful for industrial applications.    ADVANTAGE - The membrane-type biogas tank solves problems of crusting, pipe blocking and floating residue; and it can remove residues conveniently and fast.    DETAILED DESCRIPTION - A membrane-type biogas tank convenient to remove residues comprises a membrane-type biogas tank body, a feeding pipe, a material discharging pipe, a gas transferring pipe, and zipper residue removing holes; where the feeding pipe and the material discharging pipe are located on two ends of the biogas tank body; the gas transferring pipe is located on the middle part of the upper part of the biogas tank; the zipper residue removing holes are located on the upper part of the biogas tank and two ends of the gas transferring pipe and are near to the side of the biogas tank; and the zipper residue removing holes leak neither air nor water.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the membrane-type biogas tank convenient to remove residues.
NOVELTY - A device for producing biogas by organic waste material comprises a material treating and regulating tank (1), a biogas reactor set (2), a biogas storing cabinet (3), and a discharge or contact aerobic treatment tank (4); where the material treating and regulating tank is connected with the biogas reactor set by a pump and a pipe; the biogas reactor set is connected with the biogas storing cabinet by the pipe; and the biogas reactor set is connected with the discharge or contact aerobic treatment tank by the pump and pipe.    USE - The device is useful for producing biogas by organic waste material (claimed).    ADVANTAGE - The device reduces volume of the single biogas reactor, changes the engineering of the whole device to be middle size from big size, changes the middle size to the normal size, and reduces engineering investment and operation cost. Moreover, because multiple biogas reactors are connected in series and then connected in a parallel in a multilevel manner, it prolongs retention period of the material, which arrives at the best, improves reaction speed and utilization rate of the material, and maintains continuous operation of the whole device.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of the device for producing biogas by organic waste material (Drawing includes non-English language text).    Material treating and regulating tank (1)    Biogas reactor set (2)    Biogas storing cabinet (3)    Discharge or contact aerobic treatment tank (4)
NOVELTY - Methane generator, comprises a methane generator main body, where the methane generator main body is composed of at least two separated shell bodies, the adjacent separated shell bodies are connected and fastened with each other in a sealing manner.    USE - Used as the methane generator.    ADVANTAGE - The methane generator: has rational structure, is provided with the long service life, which can reach 20-30 years thus the industrial production and installation on site can be attained; is provide with excellent quality and sealing property and since the main body is plastic alloy, the production cost is low and the change affected by foundation is small.
NOVELTY - A biomass-mineral substance mixed fuel has spherical and hollow type particles provided with micropores.    USE - Biomass-mineral substance mixed fuel.    ADVANTAGE - The biomass-mineral substance mixed fuel has reduced pollutants, and heat value of coal, and is economically and conveniently transported. The fuel is manufactured simply.
NOVELTY - Manual rope traction stirrer of biogas pool (1) comprises an axle seat (2) installed on the bottom part of the biogas pool. The axle seat is provided with a spindle (3), one end of the stirring blade (4) is fixed on the spindle, the other end is connected with a right pulling rope (5) and a left pulling rope (6), and pool walls on two sides of the biogas pool are equipped with a first pulley (7) and a second pulley (8) respectively.    USE - The manual rope traction stirrer is useful for countryside family-used biogas pools and small-medium size biogas projects.    ADVANTAGE - The manual rope traction stirrer of biogas pool saves the loss of electric energy and exhibits simple structure, low manufacturing cost, convenient installation and good stirring effect, improving the yield of the biogas prominently and facilitating material discharge without incrustation and silting of the feed liquid in the biogas pool.    DETAILED DESCRIPTION - Manual rope traction stirrer of biogas pool (1) comprises an axle seat (2) installed on the bottom part of the biogas pool. The axle seat is provided with a spindle (3). One end of the stirring blade (4) is fixed on the spindle, the other end is connected with a right pulling rope (5) and a left pulling rope (6). Pool walls on two sides of the biogas pool are equipped with a first pulley (7) and a second pulley (8) respectively. The top end of the stirring blade is higher than installation positions of first- and second pulley. The left pulling rope is placed outside of the biogas pool through the first- and second pulley and the right pulling rope is placed outside of the biogas pool through the second pulley.    DESCRIPTION OF DRAWING(S) - The figure illustrates a schematic representation of a manual rope traction stirrer of biogas pool.    Biogas pool (1)    Axle seat (2)    Spindle (3)    Stirring blade (4)    Right pulling rope (5)    Left pulling rope (6)    First pulley (7)    Second pulley (8)
NOVELTY - A cellulose is degraded by treating starting material with isolated polypeptide comprising sequence of 957 amino acids fully defined in the specification or their fragment that has cellulase activity.    USE - Method of degrading cellulose (claimed).    ADVANTAGE - The method provides product with more desirable properties such as thermal tolerance, and partial or complete resistance to extreme pH inactivation, proteolytic inactivation, solvent inactivation, chaotropic agent inactivation, oxidizing agent inactivation, and detergent inactivation.
NOVELTY - Gas purification involves reacting impure feed gas comprising methane (CH4) and carbon dioxide (CO2) with solvent to provide CH4-enriched gas and first stage solvent effluent comprising absorbed CH4 and absorbed CO2, and reacting the first stage solvent effluent with recycled vapor fraction of second stage solvent effluent. The second stage solvent effluent is obtained by reacting first stage solvent effluent with recycled vapor fraction.    USE - Method for gas purification to recover purified CO2 product gas used in enhanced oil recovery and purified CH4 product gas from impure feed gas comprising CH4 and CO2 (claimed).    ADVANTAGE - The method produces purified CH4 and CO2 product gases at high purity. At least 99% of CH4 and greater than or equal to 65% of CO2 in feed gas are recovered in the purified CH4 product gas stream and purified CO2 product gas stream, respectively.
NOVELTY - A biomass gasifier comprises a reactor (10) including an inlet for biomass (12), an inlet for an oxygen-containing gas, an inlet for steam, an outlet for reactor product gas, an outlet for ash, a biogas exit conduit (i.e. cyclone (20)) coupled to the outlet for the reactor product gas, and an inlet for a secondary oxygen source. The biogas exit conduit comprises a catalytic partial oxidation unit (30) for restricting the biogas exit conduit.    USE - A biomass gasifier.    ADVANTAGE - The biomass gasifier can provide efficient conversion of tar and produce syngas with less amount of tar, ash and impurities; and has increased operational flexibility in terms of system efficiency and/or throughput, and reduced cost.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a system comprising a biomass feed unit, a biomass gasifier, a gas clean up unit, and a power production unit; and    (2) a method for biomass gasification comprising heating biomass (i.e. non-edible agricultural waste) in the presence of steam and oxygen to produce a biogas, where heating is carried out in a reactor at 300-850 degrees C; flowing the biogas through the catalytic partial oxidation unit at 600-1150 degrees C to produce a reactor product gas (36) comprising 5-45 vol.% hydrogen; and collecting the reactor product gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass gasifier reactor.    Reactor (10)    Biomass (12)    Cyclone (20)    Catalytic partial oxidation unit (30)    Reactor product gas (36)
NOVELTY - Dehydration of a water rich stream comprises providing a process stream to a temperature controlled adsorber (40) having adsorption flow passage(s) (53) containing an adsorptive material coating and a heat transfer flow passage(s); passing the process stream through the adsorption flow passage(s), where water is adsorbed by the adsorptive material coating; generating heat of adsorption; removing heat of adsorption by passing a cooling fluid through the heat transfer flow passage(s); and producing a dehydrated effluent stream.    USE - Method for the dehydration of a water rich stream (claimed), e.g. fermentation beer used for producing motor fuel grade ethanol.    ADVANTAGE - The method reduces purge gas requirements during regeneration, and simultaneously increases potential for recovering high concentrations of water in regeneration gas. Extremely rapid thermal swing adsorption with cycle times at or below current adiabatic pressure swing molecular sieve adsorption separation processes can be achieved, resulting in smaller adsorber systems, thus saving both capital and energy.    DESCRIPTION OF DRAWING(S) - The drawing is a perspective view of the temperature controlled adsorber.    Temperature controlled adsorber (40)    Adsorption layers (50)    Heat transfer layers (51)    Separator plate (52)    Adsorption flow passage (53)
NOVELTY - The method involves forming a fuel anode layer and an electrolyte layer, and forming the fuel anode layer at an upper part of a metal stent. A green cathode layer is formed. An air electrode slurry is coated at an upper part of the electrolyte layer. A metal stent type solid oxide fuel cell is heated. A sheet is transmitted with a pellet type fuel anode layer. An air electrode material contained in a cathode layer is made of a material selected from barium, strontium, carbon monoxide and iron oxide.    USE - Method for manufacturing a metal stent type solid oxide fuel cell in a fuel system.    ADVANTAGE - The method enables avoiding requirement of separate thermal process for manufacturing a cathode layer. The method enables preventing deterioration of the metal stent and reducing manufacturing time and process of the solid oxide fuel cell. The method enables realizing excellent electrochemical characteristic with a surface resistance (ARS).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic illustration of a method for manufacturing a metal stent type solid oxide fuel cell in a fuel system.
NOVELTY - Natural garden fertilizer comprises multiple shifted and chopped horse manure.    USE - Useful as natural garden fertilizer. No biological data given.    ADVANTAGE - The fertilizer has reduced ammonia content and related odor, and burning effect on plants. The natural garden fertilizer is easy to transport and clean.
NOVELTY - An anionic surfactant is mixed with alcohol solution, agitated and dispersed with aluminum precursor, to obtain solution (A). Nickel precursor is dissolved in distilled water, to obtain solution (B). Then, solutions (A and B) are mixed, treated hydrothermally and centrifuged. The obtained solution is heated-treated, washed using distilled water and dried, to obtain mesoporous nickel-alumina composite catalyst.    USE - Manufacture of mesoporous nickel-alumina composite catalyst used for preparing hydrogen (claimed) for polymer electrolyte fuel cell.    ADVANTAGE - The method economically provides mesoporous nickel-alumina composite catalyst having high stability and activity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of hydrogen.
NOVELTY - Acorn is wet processed into acorn starch and mixed uniformly at 30-35 degrees C. The ratio of acorn starch to water is 1:2.0-1:30. Activated strain (10%) and ammonium sulfate (0.2%) are added and the mixture is sealed at 32-34 degrees C and the pH is regulated to 5. Simultaneous saccharification and fermentation is carried out for 84 hours and the fermented substance is distilled and dehydrated to obtain ethanol fuel. The activated strain is composed of Kluveromyces marxinus, Saccharomyces cerevisiae and Rhizopus chinenssis.    USE - Manufacture of ethanol fuel.    ADVANTAGE - The ethanol fuel is manufactured economically and with improved yield by a simple process and using a simple installation.
NOVELTY - An aqueous EDTA free solution comprises meloxicam, meglumin, N,N dimethylacetamide and propylene glycol.    USE - Aqueous EDTA free solution is used for preparing pharmaceutical composition useful for treating pain, inflammation, fever and respiratory complaints in mammals (claimed) preferably farm animals. The solution can also be used for treating acute mastitis, diarrhea, lameness, and problems with locomotor apparatus. The treatment may be given in conjunction with antibiotic therapy.    ADVANTAGE - The solution exhibits good stability, and has long term shelf-life of greater than or equal to 24 months at ambient temperature on its original packaging. The method has short preparation period, is environmental friendly, and does not include a heating step.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the solution comprising addition of meglumin and povidone, addition of propylene glycol and N,N dimethylacetamide, addition of meloxicam, and filtration.
NOVELTY - A composite material comprises a graphene material, and carbon-containing ferromagnetic nanometer metal particles uniformly coated on the surface of the graphene material. The graphene material comprises a single graphite layer that is less than 50 nm thick. The metal particle has a diameter of 2-100 nm. The ferromagnetic metal is iron, cobalt, and/or nickel. The mass ratio of the metal to the carbon is 1-20:1.    USE - A composite material used as a magnetic separation catalyst in wastewater treatment, electromagnetic shielding, and wave absorption.    ADVANTAGE - The composite material has excellent magnetic performance and good conductivity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the composite material, comprising:    (A) ultrasonically dispersing 0.1-10 mg/mL graphite oxide solution for 0.5-5 hours to obtain a graphene oxide dispersing agent;    (B) adding 0.1-5 mol/L ferromagnetic metal salt solution, where the mass ratio of the soluble salt of the ferromagnetic metal to the graphite oxide is 0.1-100:1;    (C) mixing for 0.5-10 hours;    (D) preparing 0.1-5 mol/L solution by using a precipitant with the molar ratio to the soluble salt of the transitional metal of 1-20:1;    (E) adding the solution into the graphite oxide dispersing agent at 10 mL/minute;    (F) drastically mixing, and reacting at 0-100 degrees C for 0.5-10 hours;    (G) filtering, completely washing, and drying the material to obtain a composite powdery body;    (H) heating the powdery body to 500-800 degrees C at 5-50 degrees C/minute at nitrogen or argon atmosphere;    (I) inflating the mixed gas at 10-100 mL/minute for chemical vapor deposition for 1-60 minutes; and    (J) cooling the reactants at nitrogen or argon atmosphere to room temperature.
NOVELTY - A current collector (120) is formed on gas diffusion layer (110) containing conductive materials. Then, the gas diffusion layer is laminated on electrolyte membrane (130), to form fuel cell (100).    USE - Manufacture of fuel cell used as power supply for electronic devices.    ADVANTAGE - The method provides fuel cell with improved efficiency. The contact resistance between current collector and gas diffusion layer is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic cross-sectional view of fuel cell.    Fuel cell (100)    Gas diffusion layer (110)    Current collector (120)    Electrolyte membrane (130)    Catalyst layer (140)
NOVELTY - Foamable composition (C1) comprises antimicrobial amount of thyme oil (0.01-0.5 wt./vol.%); surfactant; and source of divalent copper ions.    USE - For killing methicillin-resistant Staphylococcus aureus on surface contaminated (claimed). Also useful for treating and preventing bacterial infections and drug-resistant bacterial infections, such as methicillin-resistant Staphylococcus aureus (MRSA); skin infections including lesions, sores, rashes, blisters, abscesses, or cracking of the skin, all of which can by accompanied by discoloration, inflammation, swelling, or pain; other skin infections including impetigo, folliculitis, boils, ecthyma, erysipelas, cellulitis, jock itch, acne, and athlete's foot.    ADVANTAGE - The composition is capable of killing greater than 99.9% or 99.99% of methicillin-resistant Staphylococcus aureus in 15 seconds when applied topically. The composition is environmentally friendly and green compositions for killing MRSA on a contaminated surface.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: 1. killing methicillin-resistant Staphylococcus aureus (MRSA) on a surface contaminated (M1) involving applying to the surface a foamable composition (C1), and exposing the surface to the composition for exposure time sufficient to kill methicillin-resistant Staphylococcus aureus. 2. kit comprising antimicrobial foamable composition (C1), and dispenser.
NOVELTY - The device has a fire damper (15) inserted into a fire damper inserting opening (14). An inserting pipe (12) directly reaches a bottom of a gasification kettle (7). A flue (19) is provided at a right side of a central line. A flue water jacket outlet pipe (17) is installed on a double-structured flue water jacket (18). A heat-absorptive cover (11) is equipped in an upper segment, where the cover is a semi-spherical body. A heat-absorptive cover water inlet hose (10) is connected with a gasification kettle combustion chamber water jacket (23) and the outlet pipe.    USE - Four-function straw gasification gas heating device.    ADVANTAGE - The device integrates the functions of cooking, heating water, heating bed and heating air of a renewable energy source and an environment-friendly furnace. The device enables the process of combustion to be free from smoke, smell and dust and the produced tars are combusted with the flame to be changed into heat energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a four-function straw gasification gas cooking device.    Gasification kettle (7)    Heat-absorptive cover water inlet hose (10)    Heat-absorptive cover (11)    Inserting pipe (12)    Fire damper inserting opening (14)    Fire damper (15)    Flue water jacket outlet pipe (17)    Double-structured flue water jacket (18)    Flue (19)    Gasification kettle combustion chamber water jacket (23)
NOVELTY - The heater (1) has an air feeding cover (2) located in center of a tubular heater main body. The cover is connected to a fan (9) outside the heater. An input pipe for supplying heat conducting medium to the interlayers is equipped outside the heater. Inner holes (6) of interlayers (3) are formed on an inner sidewall of the heater and connected to an input end of a circulating pipe (7) e.g. spiral metal pipe. An output end (10) of the pipe is extended to an outer side of a bottom (11) of heater after circulating pipe along upward and downward directions of the heater.    USE - Straw gasification heater.    ADVANTAGE - The heater can be manufactured at low cost with simple structure, reduced energy and consumption and protecting environment. The heater can be manufactured according to living conditions of people. The circulating pipe is added in the heater, so that the heating area is increased and heat energy in the high-temperature area can be directly collected. The circulating pipe is extended to an outer side of the bottom of the heater, so that the internal resistance, temperature of output medium and heat supply performance of the furnace are increased and flowing speed of medium is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross sectional view of a straw gasification heater.    Straw gasification heater (1)    Air feeding cover (2)    Interlayer (3)    Inner holes (6)    Circulating pipe (7)    Fan (9)    Output end (10)    Bottom (11)
NOVELTY - The device has a gas generating box, a gas purifying pot and a gas cooker connected by a soft plastic pipe to transport gas. A lower part of the gas cooker is equipped with a gas storage cylinder and an upper part is equipped with a stove.    USE - Convenient and sanitary straw gasification cooking device.    ADVANTAGE - The gas generating box, the gas purifying pot and the gas cooker are connected by the soft plastic pipe to transport gas, so that the soft plastic pipe has strong plasticity, variable length simple structure and low cost, and is convenient to use and install.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a convenient and sanitary straw gasification cooking device.
NOVELTY - The device has a secondary vortex separator (5) connected with ends of a carbon filter (6) and with a carbon burning furnace (15). The carbon filter is connected with a spraying tower (7). An end of the spraying tower is connected with a liquid storing tank (9) by an oil separator (8), and another end is connected with a gas storing tank (18) by an electric tar catcher (11), a primary partition wall water cooler (12), a secondary partition wall water cooler (13) and a gas filtering device (14). The oil separator is connected with the spraying tower by a spraying medium cooler (10).    USE - Device for producing liquid fuel by self-heating and self-circulating thermal decomposition of biomass.    ADVANTAGE - The device can recycle solid material and carbon effectively by dual stage vortex separators and a carbon filter. The device transforms waste fibrin biomass into different grade of fuel liquid by quick thermal decomposition technique and stage cooling collection process, and can recycle volatilization gas and coke produced in the thermal decomposition process, thus achieving self-heating of the thermal decomposition system and saving cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a liquid fuel producing device.    Secondary vortex separator (5)    Carbon filter (6)    Spraying tower (7)    Oil separator (8)    Liquid storing tank (9)    Spraying medium cooler (10)    Electric tar catcher (11)    Primary partition wall water cooler (12)    Secondary partition wall water cooler (13)    Gas filtering device (14)    Carbon burning furnace (15)    Gas storing tank (18)
NOVELTY - The mechanism has a fan installed on a front fan box, and a back fan box coordinated with the front fan box. The front fan box is opened with an air inlet while the back fan box is opened with a primary air outlet and a secondary air outlet, and shielding areas of the primary air outlet and secondary air outlet are changed by the rotation of the mechanism.    USE - Distributing air regulating mechanism for a biomass semi gasifier.    ADVANTAGE - The mechanism regulates the wind passing through the two air outlets in a simple manner without any difficult to an operator.    DESCRIPTION OF DRAWING(S) - The drawing shows an exploded perspective view of a distributing air regulating mechanism for a biomass semi gasifier.
NOVELTY - The gasifier has a furnace body including an inner cylinder (1) with a base and an outer cylinder (2), where bottom of the furnace body is provided with primary air inlets (3). A lift type furnace bridge (4) is arranged in a furnace cavity, where an upper part of the furnace body is provided with secondary air inlets (5). Top of the furnace body is provided with a double-layer fire blocking ring (6), and a chimney (7) is connected to a fire blocking ring passage. The secondary air inlets are arranged on a wall of the inner cylinder.    USE - Biomass semi gasifier.    ADVANTAGE - The gasifier provides high heat efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a biomass semi gasifier.    Inner cylinder (1)    Outer cylinder (2)    Primary air inlets (3)    Lift type furnace bridge (4)    Secondary air inlets (5)    Double-layer fire blocking ring (6)    Chimney (7)
NOVELTY - The furnace has a barrel (3) comprising a combustion chamber module (4) provided with a combustion chamber (5). A feeding channel (13) is provided on lateral surface of a divided gasification chamber (12). A feeding door (14) is mounted at an outer port of the channel. A slag-off port (15) and a gasification keeping hole (17) are arranged at bottom of the gasification chamber. An oxygen inlet switch (16) is placed below the slag-off port. An ash box (19) is installed in the furnace barrel, and the gasification chamber is fixed with an ash box handle (20). The body is installed on a base (21).    USE - Household gasification biological combustion cooking device.    ADVANTAGE - The device integrates gasification and combustion. The device has high burning efficiency. The furnace conserves energy and is environment-friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a household gasification biological combustion furnace.    Barrel (3)    Combustion chamber module (4)    Combustion chamber (5)    Divided gasification chamber (12)    Feeding channel (13)    Feeding door (14)    Slag-off port (15)    Oxygen inlet switch (16)    Gasification keeping hole (17)    Ash box (19)    Ash box handle (20)    Base (21)
NOVELTY - The generator has a cover board (20) whose top edge is provided with a material loosing motor and gear (25). The material loosing motor and gear are electrically connected to a material loosing timer (26). A filter includes a filter core (13), a filter air inlet pipe (14) and a filter air outlet pipe (15). The filter air inlet pipe is connected to an inner cylinder (2) through a three-way air outlet valve (18), which is connected to an air outlet pipe (19). The filter air outlet pipe is connected to an electric air suction fan (16), a gas outlet (17) and a gas appliance.    USE - Straw gas generator for a gas appliance (claimed).    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a straw gas generator.    Inner cylinder (2)    Filter core (13)    Filter air inlet pipe (14)    Filter air outlet pipe (15)    Electric air suction fan (16)    Gas outlet (17)    Three-way air outlet valve (18)    Air outlet pipe (19)    Cover board (20)    Material loosing motor and gear (25)    Material loosing timer (26)
NOVELTY - The furnace has a cover (2) whose middle part is passed through a feeding rod (1). An internal wall of a wind passage (4) is provided with multiple twice wind feeding holes (5). A wind feeding pipe (8) is provided with a wind feeding pore (9). A middle part of a body (3) is provided with a gas discharging hole (12). The gas discharging hole is connected with a kitchen range (15) by a purifier (11). A middle part of the kitchen range is provided with a cylinder (17). A side wall in an internal part of the kitchen range is provided with a horizontal oblique fuel gas pore (16).    USE - Straw gas furnace.    ADVANTAGE - The furnace can purify the fuel, so that the fuel of the furnace can burn completely. The furnace has reduced pollution, and can reduce the un-symmetric burning of the fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a straw gas furnace.    Feeding rod (1)    Cover (2)    Body (3)    Wind passage (4)    Twice wind feeding holes (5)    Wind feeding pipe (8)    Wind feeding pore (9)    Purifier (11)    Gas discharging hole (12)    Kitchen range (15)    Horizontal oblique fuel gas pore (16)    Cylinder (17)
NOVELTY - The organic compost turning machine has a hopper (5) that is installed above a frame (4). A lower outlet (3) of the hopper is connected with a turning box (2). Several blades (1) are installed on a main shaft (10) that is installed in the turning box. A driven wheel (11) is installed on main shaft outside the turning box. A motor (6) is installed on the frame. A driven wheel is connected with an output shaft (8) of the motor by a transmission device. A discharging hole (13) is installed on the turning box.    USE - Organic compost turning machine.    ADVANTAGE - The simple structured organic compost turning machine can be manufactured easily while reducing the cost.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the organic compost turning machine. (Drawing includes non-English language text)    Blade (1)    Turning box (2)    Lower outlet (3)    Frame (4)    Hopper (5)    Motor (6)    Output shaft (8)    Main shaft (10)    Driven wheel (11)    Discharging hole (13)
NOVELTY - The furnace has fluidized bed (4) in which air-distributing chamber (1) and carbide outlet (23), spiral charging hole (3) and secondary air nozzle (20) are respectively formed on lower, middle and upper portions. A fixed bed (6) has charging hole (7), and cast iron liner (11) and gas outlet (8), and gas inlet nozzle (24) and rotatable grid (16) respectively formed at top, middle and lower portions. The carbon-collecting hopper and carbon-discharging hole (17) are formed under base (14) of rotatable grid. The fluidized and fixed beds are connected by hot smoke channel (5).    USE - Multifunctional carbonizing furnace used for purifying biomass gas used during power generation.    ADVANTAGE - The proportion of gas to carbon can be regulated according to different applications and demands of carbon manufacturing and power generation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of the multifunctional carbonizing furnace. (Drawing includes non-English language text)    Air-distributing chamber (1)    Spiral charging hole (3)    Fluidized bed (4)    Hot smoke channel (5)    Fixed bed (6)    Charging hole (7)    Gas outlet (8)    Cast iron liner (11)    Base (14)    Rotatable grid (16)    Carbon-discharging hole (17)    Secondary air nozzle (20)    Carbide outlet (23)    Gas inlet nozzle (24)
NOVELTY - A hinge mechanism is controlled by a draw rod (2) by longitudinal movement of a main rod so as to control opening and closing of the grab bucket connected with hinge mechanism. A cross rod (13) is fixed in a through hole formed in a split plate (7) of the hinge mechanism. A horizontal shaft (6) is penetrated through the through hole formed on the fixed piece (12) and split plate and is connected with fixed piece and split plate of hinge mechanism. The middle portion of shaft is connected with lower end of draw rod.    USE - Slag separator of biogas tank.    ADVANTAGE - The structure of the slag separator is simplified. The slag separator can be used conveniently. The processing operation can be performed easily. The manufacturing cost of the slag separator can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the slag separator.    Draw rod (2)    Shaft (6)    Split plate (7)    Fixed piece (12)    Cross rod (13)
NOVELTY - The device has solar heating device (1) installed on top of housing (4) of fermentation tank, and crusher (2) installed on ball valve (3) at upper end of a material feeding hole. The housing has double-layer structure which is devoid of vacuum in center region. A material discharging valve (11) is installed between solid-liquid separator (10) and housing of fermentation tank. A fermentation stirring pump (9), heat exchange device, and a control device are installed on the housing.    USE - Device for generating biogas from food waste, installed in hotel, restaurant, and dining hall.    ADVANTAGE - The food waste can be fermented rapidly to produce biogas fuel which reduces pollution, and yield can be improved.    DETAILED DESCRIPTION - The device for generating biogas from food waste has heat exchange device which includes a heat exchanger (5), heat exchanger circulating pump (6), and direct-heating water heater (7) which are connected with each other through a connecting pipe (8). A control device installed on the housing has a vacuum meter (12), pressure meter (13), temperature controller (14), and an electric control cabinet (15).    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the device for generating biogas from food waste. (Drawing includes non-English language text)    Solar heating device (1)    Crusher (2)    Ball valve (3)    Housing (4)    Heat exchanger (5)    Heat exchanger circulating pump (6)    Water heater (7)    Connecting pipe (8)    Solid-liquid separator (10)    Material discharging valve (11)    Vacuum meter (12)    Pressure meter (13)    Temperature controller (14)
NOVELTY - The power device has an electrical source (2), a generator (5), a packet (6), a compressor (7), a water ed chamber (4), and a cooling chamber (10). The carbon electrode of generator is connected with direct current supply. The efferent of generator is connected with compressor by packet. The output of compressor is connected with water ed chamber. The water ed chamber, compressor and cooling chamber are connected with the electrical source.    USE - Power device for making hydrogen-carbon and mono-oxygen.    ADVANTAGE - Provides a new type of power device which can solve existing problems such as poverty of non-renewable fuel resources, high construction cost, and the safety which is not good when using the products made by fuel by ensuring low fuel cost, clean, and big field of application, which can replace routine fuel in current use by making use of new-style fuel made by water and carbon.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the power device for making hydrogen-carbon and mono-oxygen.    Electrical source (2)    Water ed chamber (4)    Generator (5)    Packet (6)    Compressor (7)    Cooling chamber (10)
NOVELTY - A water purification material is manufactured by mixing predetermined amount of zeolite, tobermorite, aluminum and carbon, under pressure.    USE - Manufacture of material for purifying water. Uses include but are not limited to river water, lakes, marshes, industrial waste water and domestic waste water.    ADVANTAGE - The method efficiently provides material. The water purified using the material has improved dissolved oxygen content.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) purification of water, which involves reacting solution containing deuterium sulfate with water, to generate, hydrogen radical, hydroxyl radical, hydrated electron and hydrogen peroxide radical, and purifying; and    (2) solution, which contains deuterium sulfate, which is obtained using hydroxyl catalyst containing calcium chloride, ammonium sulfate, magnesium sulfate, iron sulfate, potassium phosphate, vitamin and succinic acid.
NOVELTY - A ceramic catalyst (1) is manufactured by adding small amount of hydroxyl catalysts, carbons and organic silicons to main material comprising zeolite, tobermorite, magnesium and/or aluminum, and press-molding.    USE - Manufacture of ceramic catalyst used for hydrogen generating apparatus, hydrogen generation charging device, and hydrogen-utilizing apparatus (claimed).    ADVANTAGE - The method obtains ceramic catalyst which can generate hydrogen efficiently.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a hydrogen generating apparatus;    (2) a hydrogen generation charging device; and    (3) a hydrogen-utilizing apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of hydrogen-producing test equipments, and relationship between reaction tank and storage battery.    Ceramic catalyst (1)    Reaction tank (2)    Weighing table (4)    Water flow pipe (5)    Open-close lid (6)
NOVELTY - A synusiologic device comprises anaerobic biochemical system consisting of sewage water storage adjusting pool, pressure water distribution chamber and anaerobic particle mud reaction chamber; earthworm biological degradation triphase separating system consisting of water distributor, air inlet, air collecting cover, and earthworm filter layer; artificial wet soil purification system consisting of water plant purification pool, capillary filter layer and water collecting chamber; and solar thermal-arresting system consisting of transparent glass and frame.    USE - Synusiologic device is used for purifying and recycling rural sewage (claimed).    ADVANTAGE - The device protects and improves ecological environment, increases efficiency of bio-degradation, reduces operation cost, and realizes target of improving quality of yielding water.    DETAILED DESCRIPTION - The synusiologic device comprises anaerobic biochemical system consisting of sewage water storage adjusting pool, pressure water distribution chamber and anaerobic particle mud reaction chamber; earthworm biological degradation triphase separating system consisting of water distributor, air inlet, air collecting cover, and earthworm filter layer; artificial wet soil purification system consisting of water plant purification pool, capillary filter layer and water collecting chamber; and solar thermal-arresting system consisting of transparent glass and frame. The anaerobic biochemical system is connected with triphase separating system by water outlet pipe. The triphase separating system is connected with soil purification system by water outlet pipe.
NOVELTY - Composition comprises 2,6-dimethyl-meta-dioxane-4-ol acetate and an isothiazolinone biocidal compound.    USE - The composition is useful for: controlling microorganisms in an aqueous or water containing system, where the aqueous or water containing system is paints or detergents (both preferred), coatings, latexes, adhesives, inks, pigment dispersions, household and industrial cleaners, dish detergents, mineral slurries, polymer emulsions, metal working fluids, construction products, personal care products, textile fluids, industrial process water, oilfield functional fluids or fuels; and controlling algae growth in a latex (all claimed).    ADVANTAGE - The composition exhibits synergistic activity, which permits reduced amounts of the materials to be used to achieve acceptable biocidal properties, thus potentially reducing environmental impact and materials cost. The composition provides potential for skin sensitization.
NOVELTY - Producing alcohol and biomass by fermentation of agricultural raw materials e.g. fruit, comprises: (a) accomplishing a material separation of the produced wine from the remaining solid body mass, after completion of the fermentation process; (b) introducing the solid body mass in a pumpable state to a device for producing biogas and/or bioenergy; and (c) converting the wine separated from the solid body mass into alcohol by distillation and subsequently feeding as raw material for the production of alcohol-containing products.    USE - The alcohol produced by the distillation of the wine is useful as a raw material for the production of: alcoholic beverages; preservatives for food and luxury foods; alcohol-containing drugs; alcohol-containing cosmetic products; and taste enhancing additives for food. The biomass is useful for the production of biogas and/or bio-energy (all claimed).    ADVANTAGE - The process: avoids the inclusion of the solid materials in the subsequent distillation process; reduces the energy required for production of alcohol; and reduces the cost required for the disposal of non-recyclable waste materials.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the overall process for the production of alcohol and biomass by fermentation of agricultural raw materials e.g. fruit (Drawing includes non-English language text).
NOVELTY - Enzyme composition comprises polypeptide having cellobiohydrolase II activity, polypeptide having xylanase activity, and one or more cellulolytic proteins chosen from endoglucanase, cellobiohydrolase and beta -glucosidase, where one or both of the polypeptide having cellobiohydrolase II activity and polypeptide having xylanase activity are foreign to the one or more cellulolytic proteins.    USE - The enzyme composition is useful for degrading or converting and fermenting a cellulosic material, and producing a fermentation product chosen from alcohol, organic acid, ketone, amino acid and gas (all claimed). Uses include but are not limited to arabinitol, butanol, ethanol used as e.g. fuel ethanol or industrial ethanol, glycerol, acetic acid, adipic acid, citric acid, acetone, aspartic acid, lysine, serine, glycine, methane, hydrogen and carbon dioxide.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) producing fermentation product involves (a) saccharifying a cellulosic material with the above-mentioned enzyme composition, (b) fermenting the saccharified cellulosic material with one or more fermenting microorganisms and (c) recovering the organic fermentation product; and    (2) fermenting a cellulosic material, involves fermenting the cellulosic material with one or more fermenting microorganisms, where the cellulosic material is saccharified with the above-mentioned enzyme composition.
NOVELTY - An integrated hydroprocessing and gasification system (200) comprises an oil processing system (210) which produces a fuel/diesel outlet stream and a heavy product bottom outlet stream from an oil processing feed stream, and a gasification system (290) which produces a hydrogen outlet stream and a high pressure steam outlet stream from a gasification feed stream. The gasification feed stream comprises the heavy product bottom outlet stream. The hydrogen outlet stream and high pressure steam outlet stream are utilized within the oil processing system.    USE - Integrated hydroprocessing and gasification system.    ADVANTAGE - The integrated hydroprocessing and gasification system provides improved refining efficiency, and reduces emission of gas and generation of byproducts.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for operation of integrated hydroprocessing and gasification system, which involves providing oil processing system for producing fuel/diesel outlet stream and heavy product bottom outlet stream, and coupling the gasification system to the oil processing system.    DESCRIPTION OF DRAWING(S) - The drawing shows the flowchart of integrated hydroprocessing and gasification system.    Integrated hydroprocessing and gasification system (200)    Oil processing system (210)    Distillation units (220,230)    Distillate upgrader (240)    Distillate finisher (250)    Bottom upgrader (260)    Deasphalter (270)    Gasification system (290)
NOVELTY - A bone-knitting medicine pressurized spray comprises (pts. wt.): Davallia, radix dipsaci, Notopterygium root, Angelica, rhizoma arisaematis, cortex periplocae, safflower, and dandelion (64 each), and frankincense and myrrh (21.4 each), and borneol and eucalyptus oil (7), and peach kernel (32), camphor (14), methyl salicylate (10.5), and Eupolyphaga (43). The spray is prepared by extracting Eupolyphaga and peach kernel; and crushing rhizome of Davallia, radix dipsaci, Notopterygium root, Angelica, and rhizoma arisaematis.    USE - Bone-knitting medicine pressurized spray.    ADVANTAGE - The pressurized spray has large medicine-loading rate and small skin stimulus; and is convenient to use and environment-friendly.    DETAILED DESCRIPTION - The bone-knitting medicine pressurized spray comprises (pts. wt.): Davallia, radix dipsaci, Notopterygium root, Angelica, rhizoma arisaematis, cortex periplocae, safflower, and dandelion (64 each), and frankincense and myrrh (21.4 each), and borneol and eucalyptus oil (7), and peach kernel (32), camphor (14), methyl salicylate (10.5), and Eupolyphaga (43). The pressurized spray is prepared by: (A) extracting Eupolyphaga and peach kernel with 8-15 times water of, combining extracts, and filtering to obtain water thick paste whose relative density is 1.25-1.27 g/mL for future use; (B) crushing rhizome of Davallia, radix dipsaci, Notopterygium root, Angelica, rhizoma arisaematis, safflower, dandelion, frankincense, myrrh and cortex periplocae into coarse powder, taking 8-15 times 90% ethanol as solvent, percolating powder, collecting collation, and condensing into ethanol thick paste whose relative density is 1.05-1.15 g/mL for future use; and (C) uniformly mixing water thick paste, ethanol thick pate, borneol, camphor, methyl salicylate and eucalyptus oil, adding 80% ethanol, regulating pH to 5.5-6.5 with sodium hydroxide (4.5-5.5 mol/L), uniformly stirring materials, filtering and canning mixture.
NOVELTY - Method for extracting enzyme, involves extracting enzyme from harvested raw material using an osmotic pressure, where the enzyme is useful as fertilizer in local supply and local consumption type agriculture after harvesting a crop.    USE - The method is useful for extracting enzyme, where the enzyme is useful as fertilizer, and in fermentation of foodstuff or chemical compound (all claimed).    ADVANTAGE - The fertilizer does not cause soil failure, environmental disruption and global warming. The foodstuff containing the enzyme is cost-effective and has low calorie content.
NOVELTY - Warm core of biogas generating pit comprises plastic as raw material and made into a tubular radiating net; the radiating net is composed of radiating pipes; a water inlet and a water outlet are installed at two ends; the water inlet is connected with the heat source; and the heat source is residual heat of kitchen range, solar energy and warm air.    USE - The device is useful for producing biogas in winter.    ADVANTAGE - The yield of the biogas is increased and the device can ensure that the biogas generating pit in the cold area produces biogas in winter.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the warm core of biogas generating pit.
NOVELTY - The feces ecological treating system has a sediment delivering device or the sediment inlet valve for sending slurry manure and sediment of the biochemical processing pond into the sediment solidifying system. The sediment solidifying system has an agitating device, a heating device for evaporating moisture and an insulation device. The sediment solidifying system is provided with an organic fertilizer outlet. The odor purifying system comprises an odor filtering device which is equipped on wind outlet of the sediment solidifying system and a suction fan.    USE - Feces ecological treating system for an environment-friendly toilet.    ADVANTAGE - Suits for the position which is not suitable to directly discharge feces, such as the movable toilet which is not connected with downcomer net, the big bus toilet, the ship toilet and the train toilet.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the feces ecological treating system for an environment-friendly toilet.
NOVELTY - A green preparation comprises etoxazole as effective active ingredient and additives. The green preparation is prepared into miscible oil, wettable powder, microemulsion, water dispersible powder or oil suspension.    USE - Green preparation is used for killing pest, Acarus (claimed), Lepidoptera, Homoptera, and insect in vegetable and other crops.    ADVANTAGE - The preparation has low-toxicity and efficiency of more than 90%.
NOVELTY - Special fertilizer (F1) is prepared from (wt.%) grass carbon (35-40), monopotassium phosphate (10-15), diammonium phosphate (5-10), rape residue (10-15), urea (25-30), and collagen (1-25), where total weight is 100 wt.%.    USE - Special fertilizer used for improving fertility of soil for maize (claimed).    ADVANTAGE - Maize yield is increased by more than 10-20%. Water use efficiency is increased by more than 10-20%. The fertilizer (F1) can make arid-semiarid region fully use the natural rain, thus, keeping water and protecting ecological balance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of fertilizer (F1) comprising carrying out ammoniation on grass carbon and rape residue, where amount of raw materials to be ammoniated is 50 kg; melting 2.5 kg urea in 10 kg water; uniformly spraying water on raw materials; covering the raw materials with plastic film for greater than or equal to 7 days; drying the mixture and crushing to less than 1 mm; sieving the mixture by 20-mesh sieve to obtain powder of grass carbon and rape residue; grinding monopotassium phosphate, diammonium phosphate, and urea to less than 1 mm; sieving the mixture by 20-mesh sieve; mixing the crushed raw materials; and uniformly mixing all the materials; pelletizing; and packaging.
NOVELTY - A microorganism degrading hydrogen sulfide and a production process thereof are provided to remove hydrogen sulfide for a long time and maintain degradation efficiency of hydrogen sulfide while the concentration of hydrogen sulfide is increased.    USE - Used for degrading hydrogen sulfide.    DETAILED DESCRIPTION - The microorganism Pseudomonas sp. SUL4-1(KACC-91089) degrading hydrogen sulfide is provided, wherein Pseudomonas sp. SUL4-1(KACC-91089) is isolated from the sludge in a sewage disposal plant or earthworm feces. The process for producing the microorganism Pseudomonas sp. SUL4-1(KACC-91089) degrading hydrogen sulfide comprises the steps of: culturing a mixture of anaerobically cultured sludge and vermicompost in a nutritive medium containing sulfur; separately spreading the cultured medium on sulfur agar medium and Thiobacillus agar medium and culturing them; and selecting a microorganism showing the excellent hydrogen sulfide-degrading activity and growth rate. (C) KIPO 2006Image 1/1
NOVELTY - Provided is an environmentally-friendly mixed refrigerant for ultralow temperature, which substitutes for Freon type refrigerants and accomplishes ultralow temperature at a low ejection pressure.    USE - Refrigerant.    DETAILED DESCRIPTION - The mixed refrigerant for ultralow temperature comprises 50-70 wt% of isobutane, 15-25 wt% of perfluoroethane and 15-25 wt% of trifluoromethane. The mixed refrigerant optionally further comprises 5-15 wt% of teterafluoromethane based on 100 wt% of the total weight of the refrigerant. In the latter case, the mixed refrigerant preferably comprises 54 wt% of isobutane, 18 wt% of perfluoroethane, 18 wt% of trifluoromethane and 10 wt% of tetrafluoromethane. (C) KIPO 2006 Image 1/1
NOVELTY - An apparatus for manufacturing liquid manure is provided to improve the purity of the liquid manure and make the cleaning of the fermentation tank easier.    USE - Used for manufacturing liquid manure.    DETAILED DESCRIPTION - The apparatus for manufacturing liquid manure includes a fermentation tank(10), a material basket(20), a high-speed heating unit, a heating unit, a indirect electric heater, an aeration unit, a photosynthesis facilitating unit and a liquid manure discharge unit(80). The upper surface of the fermentation tank(10) is open. The material basket receiving liquid manure is received inside the fermentation tank. The high speed heating unit installed in the bottom of the fermentation tank heats the material of the liquid manure and water.
NOVELTY - A manufacturing process and device for animal liquid manure are provided to produce liquid fertilizer having large amount of amino acid by collecting blood of livestock.    USE - Used for manufacturing animal liquid manure.    DETAILED DESCRIPTION - The manufacturing device for animal liquid manure includes a crusher(10), a first fermenter(20), a second fermenter(30), a macro element combining unit(40), and a trace element combining unit(50). In the upper part of the crusher(10), a hopper is installed. Crusher is constituted with a crushing tank and a rotation shaft. The rotation shaft having crushing knifes mounted thereon is rotated inside the crushing tank(11), being driven by a motor.
NOVELTY - A method for solubilizing a poorly soluble drug is provided to solubilize the poorly soluble drug through a solid phase dissolution without causing any environmental pollution and effectively improve elution rate of the poorly soluble drug with a simple manufacturing process.    USE - Used for solubilizing a poorly soluble drug.    DETAILED DESCRIPTION - The method for solubilizing a poorly soluble drug comprises a step of solid phase dissolving the poorly soluble drug such as itraconazole, ibuprofen, dexibuprofen, felodipine, fenofibrate, famotidine, and piroxicam in a copolymer. The solubilized composition comprises 1 part by weight of a poorly soluble drug and 0.1-100 parts by weight of a copolymer. 1 part by weight of the composition further comprises 0.1-100 parts by weight of additives.
NOVELTY - Provided are a thymol compound, a carvacrol compound which is used as environmentally-friendly fungicide, their preparation methods, and a fungicide containing the compound as an effective ingredient.    USE - Used as a fungicide.    DETAILED DESCRIPTION - The thymol compound is derived from a thyme oil and is represented by the formula 1, and the carvacrol compound is derived from a thyme oil and is represented by the formula 2, wherein R1 is H, an aliphatic hydrocarbon group comprising a linear or branched C1-C4 alkyl or haloalkyl group, a C1-C4 aliphatic or aromatic hydrocarbon group containing at least one element selected from the group consisting of N, O, P and S, or a hetero ring.
NOVELTY - Provided are an alkylphenol derivative which is used as environmentally-friendly fungicide, and a fungicide containing the alkylphenol derivative as an effective ingredient.    DETAILED DESCRIPTION - The alkylphenol derivative is represented by the formula 1, wherein R1 is H, an aliphatic hydrocarbon group comprising a linear or branched C1-C4 alkyl or haloalkyl group, a C1-C4 aliphatic or aromatic hydrocarbon group containing at least one element selected from the group consisting of N, O, P and S, or a hetero ring; and R2 is H or CH3. Preferably R1 is represented by -C(=O)-Z, -SO2-Z, or -C(=O)-NZ, wherein Z is an aliphatic hydrocarbon group comprising a linear or branched C1-C4 alkyl and haloalkyl group, an aromatic hydrocarbon group, or a hetero ring.
NOVELTY - The technique involves providing a quenching chamber and a high-temperature super-heater on a gasifier of an entrained flow bed. Temperature of synthetic inlet gas of the quenching chamber is ranged from 1000 to 1100 degrees centigrade. Temperature of synthetic outlet gas of the quenching chamber is ranged from 700 to 800 degrees centigrade. A gasifier inner wall of a low-temperature heat exchanger is equipped with optical tube film-type water cooling walls. A low-temperature super-heater and an economizer are provided in the low-temperature heat exchanger.    USE - Gasification technique for a biomass three-stage entrained flow bed in an energy chemical industry.    ADVANTAGE - The technique can be implemented for increasing gasification efficiency of biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic illustration of a biomass three-stage entrained flow bed gasification technique.
NOVELTY - The furnace has an outer wall whose lower part is equipped with a water outlet pipe. An air outlet pipe and the water outlet pipe are stretched out of a furnace body. A tar discharging hole is formed on bottom of an inner wall. An exhaust air outlet is installed at an air collecting region of the furnace chamber, where the exhaust air outlet is provided with an air sealing cover and a threaded rod. A tar discharging threaded rod is installed on the furnace body, where the tar discharging threaded rod is inserted into the tar discharging hole on the inner wall of a closed separation layer.    USE - Downdraft negative pressure straw gasification furnace.    ADVANTAGE - The furnace recovers pyrolysis tar oil and purifying combustible gas, and is simple to operate.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a downdraft negative pressure straw gasification furnace in a sectional manner.
NOVELTY - Biomass energy generator of straws, animal droppings and sewage water, comprises an acid generating tower, a solid/liquid separating tower, a methane generating tower, a fuel battery, a tubular filler, a spherical filler and a corrugated tube battery assembly, which are connected by circuits and mechanisms, where water outlet of the acid generating tower and water inlet of separating tower, water outlet of separating tower and water inlet of methane generating tower, gas outlet of methane generating tower and gas inlet of fuel battery are separately connected into an integer by pipelines.    USE - The biomass energy generator is useful for generating electric power.    ADVANTAGE - The biomass energy generator generates the electric power with high energy, thermal power and methane gas, without generating wastes that pollute the environment.
NOVELTY - Compressed wooden substance (23) obtained by passing a wood chip (19) through a hopper (20) and compressing device (21) which removes micro woody fiber on the surface and heat processing which reduces the moisture content.    USE - Compressed wooden substance for an alternative fuel (claimed).    ADVANTAGE - Inexpensive and contributes to reduction of carbon dioxide production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an alternative fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the manufacture of the compressed wooden substance.    Wood chip (19)    Hopper (20)    Compressing device (21)    Compressed wooden substance (23)    Casing (24)    Wooden chipper (25)
NOVELTY - A biological fast processing device comprises a body, a reaction vessel, a stirring shaft, a sheet stirring blade, a suction pipe, an ejector, a water injection pipe, a large water tank, a small water tank, a stop valve, a water pump, an exhaust pipe, a water outlet pipe, a heating cavity, an oil return pipe, an oil tank, an oil pump, a heat preservation layer, a material discharge pipe, a microcomputer controller, a material inlet hopper, and a maintenance opening.    USE - A biological fast processing device for organic waste (claimed).    ADVANTAGE - The device can treat organic garbage in large-scale industry, can treat 10 tons of organic garbage, enables complete fermentation and decomposition of organic waste within 10 hours, prevents from burning or killing microorganism due to high environmental temperature, and has microorganism detector and can control heating time and temperature by itself.    DETAILED DESCRIPTION - A biological fast processing device comprises a body, a reaction vessel, a stirring shaft, a sheet stirring blade, a suction pipe, an ejector, a water injection pipe, a big water tank, a small water tank, a stop valve, a water pump, an exhaust pipe, a water outlet pipe, a heating cavity, an oil return pipe, an oil tank, an oil pump, a heat preservation layer, a material discharge pipe, a microcomputer controller, a material inlet hopper, and a maintenance opening. The base of the body is connected to the reaction vessel. The stirring shaft is transversely provided in the center of the reaction vessel and provided with sheet stirring blade.
NOVELTY - Manufacturing a fertilizer comprises: (a) mixing an organic medium with a liquid at ratio of 1:1-1:5 parts and agitating for 30-90 minutes to form a mixture; (b) filtering the mixture to form a filtrate containing 3-8% suspended solids; (c) aerating the filtrate with agitation for 12-24 hours to form an oxygenated filtrate having 5-8% dissolved oxygen with respect to the volume of the filtrate; and (d) fermenting the oxygenated filtrate with aeration for 48 hours with continuous supply of oxygen to form the fertilizer. The organic medium is organic wastes after treatment with earthworms.    USE - The method is useful for manufacturing a fertilizer (claimed), which is useful to assist plant growth. No biological data given.    ADVANTAGE - The fertilizer obtained from the method has improved phosphorus and nitrogen contents (more than 2 fold increase) than those from the existing method.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) manufacturing a fertilizer including either steps (a), (c) and (d) as per se or steps (a), (b) and (d) as per se; and    (2) the fertilizer manufactured by the above methods.
NOVELTY - The electrolysis device has an enclosed electrolytic cell internally provided with pairs of electrodes for electrolyzing water to produce hydrogen and oxygen. An enclosed water and gas separator is connected to the electrolytic cell through a first pipeline to infuse hydrogen and oxygen within the electrolytic cell into the water and gas separator through the first pipeline. An enclosed water and gas safety device is connected to the water and gas separator through a second pipeline to infuse hydrogen and oxygen separated in the water and gas separator into the water and gas safety device.    USE - Electrolysis device used in motor vehicle (claimed).    ADVANTAGE - Provides an electrolysis device capable of promoting the combustion of fuel, improving the combustion efficiency of fuel, and removing the carbon deposition generated in the engine cylinder, such that the discharge of tail gas can be reduced, and the pollution of motor vehicle to the environment can be reduced.    DETAILED DESCRIPTION - An energy supply circuit provides electric energy to the electrodes. The lower parts of the electrolytic cell communicate with the lower part of the water and gas separator through a pump, such that the water within the water and gas separator can be transmitted to the electrolytic cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic illustration of the electrolysis device used in motor vehicle. (Drawing includes non-English language text).
NOVELTY - The hydrogen-oxygen machine has an electrolytic cell, an electrolyte collecting groove, a gas-water separator, an electrolyte refluxing pipe (8) and a gas outlet pipe (16). The upper part of the gas-water separator is provided with cooling washing tanks (18). The electrolyte refluxing pipe is provided at the lower part, and extends into the gas-water separator. The outer walls on the lower part of the cooling washing tanks are provided with electrolyte supplement pipe (10). The outer walls of the cooling washing tanks are provided with jackets.    USE - Hydrogen-oxygen machine with cooling washing tank.    ADVANTAGE - Provides a hydrogen-oxygen machine that integrates functions of separating, cooling and washing, ensures improved working reliability, and has reduced size and cost. Prepares hydrogen and oxygen with high purity.    DETAILED DESCRIPTION - Condenser pipes (13) around the cooling washing tanks are arranged in the jackets. The lower parts of the condenser pipes are provided with refrigerating fluid inlet pipe (12). The upper parts of the condenser pipes are provided with refrigerating fluid outlet pipe (11). The upper parts of the jackets are connected to the condensed water feed pipe (14). The upper parts inside the cooling washing tanks are provided with demisters (15). The upper outer walls of the demisters are connected to a washing water inlet pipe (17) and the gas outlet pipe.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the hydrogen-oxygen machine with cooling washing tank.    Electrolyte refluxing pipe (8)    Electrolyte supplement pipe (10)    Refrigerating fluid outlet pipe (11)    Refrigerating fluid inlet pipe (12)    Condenser pipes (13)    Condensed water feed pipe (14)    Demisters (15)    Gas outlet pipe (16)    Washing water inlet pipe (17)    Cooling washing tanks (18)
NOVELTY - An electrolysis cell generates one or more combustion enhancing gases from an electrolytic solution. The housing of electrolysis cell has sloping sides that directs the combustion gases out through an exit port in the housing. A trap fluidly connected to the electrolysis cell collects and holds the solution. The trap is fluidly connected to the intake of the internal combustion engine and electrolysis cell for delivering the solution to the cell.    USE - System for producing gases for internal combustion engine such as petrol and diesel engines. Uses include but are not limited to electric cars and vans, natural gas and propane fuelled vehicles, hydrogen cell vehicles, etc.    ADVANTAGE - The rate of flow of combustion enhancing gases from cell to engine can be increased when engine is operating at higher speed.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view plates placed in recess.    Recess (20)    Portion (22)    Electrode (26b)    Negative terminals (28a,28b)
NOVELTY - An enclosure (14) contains electrolyte solution (23), and is covered by a lid (15). The enclosure is provided with electrolyzer assemblies (1). A supply portion of electrolyte solution is physically separated from electrolyzer assemblies provided with electrodes made of conductive material that are separated from each other by insulating separator. An external pump (26) is provided to pump solution from supply portion to electrolyzer assemblies. The electrical power is supplied to pump for supplying solution from supply portion to electrolyzer assemblies.    USE - Electrolyzer generator apparatus for making hydrogen rich gas comprising hydrogen, oxygen and water through water electrolysis.    ADVANTAGE - The efficiency of water electrolysis process is improved for producing hydrogen rich gas by isolating the electrolyte solution contained in each electrolysis cell from the supply portion of electrolyte solution. The higher efficiency can be aimed by minimizing the wasted current that does not convert water to hydrogen rich gas. The utilization of electrodes coated with electrode specific nano-materials, so that voltage efficiency is improved at higher current densities.    DESCRIPTION OF DRAWING(S) - The drawing shows the side cross-sectional view of hydrogen rich gas generator.    Electrolyzer assembly (1)    Hydrogen rich gas generator (13)    Enclosure (14)    Lid (15)    Electrolyte solution (23)    External pump (26)    Electrolyte tank (35)
NOVELTY - The method comprises introducing a liquid into the septic system. The liquid comprises a cleaning product carrier consisting of dishwasher detergent, toilet bowl cleaner, washing machine detergent, liquid hand or bath soap and shampoo, and a protein component from aerobic fermentation of yeast. The protein component comprises yeast stress proteins resulting from subjecting a mixture obtained from the yeast fermentation to stress and exposing a product obtained from the fermentation of yeast to additional procedures that increase the yield of proteins produced from the fermentation.    USE - The method is useful for cleaning a septic system.    ADVANTAGE - The method effectively and conveniently cleans the septic system using sufficient amount of stress relative to the total wastewater flow through the system thus biologically digesting organic compounds present in the septic system.    DETAILED DESCRIPTION - The method comprises introducing a liquid into the septic system. The liquid comprises a cleaning product carrier consisting of dishwasher detergent, toilet bowl cleaner, washing machine detergent, liquid hand or bath soap and shampoo, and a protein component from aerobic fermentation of yeast. The protein component comprises yeast stress proteins resulting from subjecting a mixture obtained from the yeast fermentation to stress and exposing a product obtained from the fermentation of yeast to additional procedures that increase the yield of proteins produced from the fermentation, and is present in a sufficient amount relative to the total wastewater flow through the septic system. The stress comprises heat shock of the fermentation product, physical and/or chemical disruption of the yeast cells to release additional polypeptides, lysing of the yeast cell, and exposing a product obtained from the fermentation of yeast to heat shock conditions.
NOVELTY - Catalytic pyrolysis of cellulosic biomass comprises heating the cellulosic biomass to a conversion temperature of 200-500 degrees C in the presence of a catalyst system comprising a basic functionality comprising an alkali metal component and a multivalent metal component.    USE - The process is useful for catalytic pyrolysis of cellulosic biomass including cellulosic biomass of aquatic origin, and lignocellulosic biomass (energy crop material, agricultural waste material, and forestry waste material) (all claimed). The process is also useful for converting biomass to liquid fuel.    ADVANTAGE - The process provides conversion of both cellulose and lignin in single reaction step.
NOVELTY - The arrangement (100) has resonator device (30) containing working gas. A valve mechanism controls outflow of an amount of composition including air, methane, carbon dioxide, butane or propane, and working gas to the resonator device. The valve mechanism works synchronously with the generated sound wave, such that the generated sound wave exposes working gas and added amount of composition to pressure and temperature changes. The temperature is increased by gas compression and decreased by gas decompression, and a portion of added composition undergoes phase change.    USE - Acoustical phase conversion arrangement for stack-based thermo-acoustic device used in production of liquefied natural gas (LNG).    ADVANTAGE - The amount of compound substance added to the working gas in the form of particles, drops or gases undergoes phase change and a portion of the added amount of gas can condense. Thus the acoustical phase conversion operation can be efficiently carried out.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the acoustical phase conversion arrangement.    Resonator device (30)    Energy adding device (32)    Container (50)    Acoustical phase conversion arrangement (100)    Openings (A,B)    Inlets (C,D)
NOVELTY - A biomass oil is added to a reactor vessel, and heated at 100-800 degrees C in vacuum under pressure of 2000 psia for certain period of time to crack the biomass oil. The undesired materials, unreacted biomass oil, heavy ends, and light ends are removed from the cracked biomass oil. The cracked biomass oil is extracted to obtain mixture of chemical products containing 5-90 wt.% of cyclic organic compounds.    USE - Manufacture of chemical products containing cyclic organic compounds used as blendstock in United State military fuel e.g. JP-8, JP-4, and JP-5, and used for producing high-octane aviation fuel and turbine fuel (all claimed).    ADVANTAGE - The method provides chemical products containing cyclic organic compound having high purity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of high-octane aviation fuel with low lead content, which involves heating biomass oil at 100-800 degrees C under pressure of 2000 psia in vacuum to crack the biomass oil, separating a middle distillate mixture containing 50 wt.% or more of cyclic organic compounds from the cracked biomass oil, decarboxylating the middle distillate mixture to produce a mixture of chemical products containing 50 wt.% or more of cyclic alkane and alkene compounds, and blending the mixture of chemical products with fuel having octane number of less than 95, and obtaining aviation fuel having octane number of 100 or more, and lead concentration of less than 0.5 g/liter.
NOVELTY - Reactor comprises: a honeycomb-structured reformer (1) having partition walls separating and forming many cells functioning as fluid passages extending through from one end face to the other end face, having a liquid supply hole with an opening portion on a side face, capable of evaporating liquid supplied inside and reforming the evaporated liquid; a liquid supply tube (11) inserted into the liquid supply hole to supply liquid to the reformer; and a heating apparatus (21) for heating the reformer.    USE - The reactor is useful in: reforming reactions to generate hydrogen by reforming a liquid e.g. to obtain hydrogen-containing reformed gas from a liquid containing a hydrocarbon based compound or an alcohol; and hydrocarbon reformulation test.    ADVANTAGE - The reactor: has high hydrogen production rate; and reforms the liquid by saving energy and space, evaporating and reforming the liquid in a reformer.    DESCRIPTION OF DRAWING(S) - The figure shows the perspective view of a reactor.    Reformer (1)    Liquid supply tube (11)    Heating apparatus (21)    Linear electrode (31)    Pulse power source (32)
NOVELTY - Anaerobic processing device, comprises an anaerobic biological reactor (6) comprising waste water distributor (4), filling material acid-producing section, filling material gas-producing section, and water discharging section (12), where: the top of reactor is connected with marsh gas desulfurization tank (9) through collecting pipe (8); the desulfurization tank is connected to the filling material gas producing section through a gas collecting tank and a marsh gas reflowing pump; and the water discharging section has a water outlet and water reflowing opening connected with water distributor.    USE - The anaerobic processing device is useful for processing waste water containing high sulfate radicals and high organic material concentration.    DETAILED DESCRIPTION - Anaerobic processing device, comprises an anaerobic biological reactor (6) comprising a waste water distributor (4), a filling material acid-producing section for contacting with waste water to react to acidify organic material and reduce sulfate radical, a filling material gas producing section for processing contact reaction with the outlet water of the filling material acid producing section to generate marsh gas and a water discharging section (12), where: the top part of the anaerobic biological reactor is connected with a marsh gas desulfurization tank (9) through a marsh gas collecting pipe (8); the marsh gas desulfurization tank is connected to the filling material gas producing section through a gas collecting tank and a marsh gas reflowing pump; and the water discharging section is provided with a water outlet and a water reflowing opening connected with the water distributor by a water reflowing pump.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic diagram of the anaerobic processing device.    Waste water distributor (4)    Anaerobic biological reactor (6)    Gas collecting pipe (8)    Gas desulfurization tank (9)    Water discharging section (12)
NOVELTY - Hydrogen is produced by dehydrogenating organic hydride in supercritical state. Dehydrogenation reaction of organic hydride is not carried out in supercritical state.    USE - Manufacture of hydrogen for fuel cell.    ADVANTAGE - Hydrogen is efficiently manufactured with high purity. The fuel cell utilizing hydrogen has high energy density.
NOVELTY - Producing synthesis gas, liquid raw material and/or energy storage media from biomass and/or waste comprises solvolyzing organic components of the biomass and/or waste in an alkali solution or hydrate melt, where the inorganic components are sedimented; separating the inorganic components from the liquid phase using physical separation methods; transferring the entrained steam obtained from the solvolysis to a rectification column, in which the organic components of the steam can be separated from water; and further separating the organic substances.    USE - The method is useful for producing synthesis gas, liquid raw materials and/or energy storage media from biomass and/or waste.    DETAILED DESCRIPTION - Producing synthesis gas, liquid raw material and/or energy storage media from biomass and/or waste comprises solvolyzing organic components of the biomass and/or waste in an alkali solution or hydrate melt at 150-250 degrees C and 3-12 bar, where the organic components are converted to at least a liquid phase and the inorganic components are sedimented; separating the inorganic components from the liquid phase using physical separation methods; transferring the entrained steam obtained from the solvolysis to a rectification column, in which the organic components of the steam can be separated from water; and further separating the organic substances through rectification, distillation, extraction, sorption and/or thermochemical gasification in fuel or synthesis gas.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a device for producing synthesis gas, liquid raw material and/or energy storage media from biomass/waste.
NOVELTY - Microorganisms fixation carrier comprises unsaturated group containing urethane resin, cyclodextrin polymer, polymerization initiator and aqueous-based composition containing water-soluble high molecular polysaccharide and metal ion, where the water soluble high molecular polysaccharide contacts with metal ion to form granular gel in the aqueous-based medium. The obtained unsaturated group in the granular gel is subjected to photopolymerization and/or thermal polymerization.    USE - The microorganism fixation carrier is useful in waste water treatment (claimed).    ADVANTAGE - The carrier has large contact area of an aromatic compound and cyclodextrin without inhibiting the adhesion of microorganism. The carrier reduces the production of floating sludge.
NOVELTY - A transesterification reaction of alcohol, fat and oil is carried out in the presence of hydrogen sulfate of organic onium compound as catalyst, to manufacture fatty acid ester.    USE - Manufacture of fatty acid ester used as bio-diesel.    ADVANTAGE - The fatty acid ester is manufactured efficiently and economically in higher yield using hydrogen sulfate of organic onium as catalyst instead of conventional triflate salt. Since alkali catalyst is not used, fatty acid soap is not produced. After the reaction, the catalyst remains as residue, hence recovery of the catalyst is not necessary. The method enables use of oil and fat in high concentration.
NOVELTY - A biodegradation processing apparatus (12) processes the to-be-processed water (11) such as waste water or human body effluent water utilized in space station by biodegradation of activated sludge. A product water manufacturing apparatus (18) distills or freezes the separation water (16) in which solid substance (14a) is separated to obtain product water (17). An oxygen supply apparatus (19) supplies oxygen in the case of biodegradation process.    USE - Waste water treatment equipment for carrying out treatment of domestic wastewater and urine in space station.    ADVANTAGE - The disassembly of the organic matter and the oxidation of ammonia can be achieved simultaneously in the biodegradation process and the deterioration factor in the film distillation apparatus can be removed. The solid substance such as microorganisms can be removed effectively. The water can be recycled effectively and lengthier stay of human being in space can be made possible.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for waste water treatment method for space station.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the waste water treatment equipment for space station. (Drawing includes non-English language text)    To-be-processed water (11)    Biodegradation processing apparatus (12)    Solid substance (14a)    Separation water (16)    Product water (17)    Product water manufacturing apparatus (18)    Oxygen supply apparatus (19)
NOVELTY - An apparatus (200) comprises a generator which generates superheated steam, drying apparatus which dries waste material using the superheated steam supplied from the generator and classifying apparatus which classifies dried products as nonflammables and flammables as raw fuel for manufacturing cement.    USE - Apparatus is used for forming raw fuel used in cement manufacturing plant (both claimed).    ADVANTAGE - The processing of waste material is carried out efficiently and economically using the apparatus.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for formation of cement raw fuel, which involves drying waste material by contacting superheated steam and waste material, classifying dried product into flammables and nonflammables and using classified flammables as raw fuel in cement firing installation (100).    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating cement manufacture plant. (Drawing includes non-English language text)    Cement firing installation (100)    Rotary kiln (102)    Clinker cooler (103)    Calcination furnace (104)    Suspension preheater (106)    Apparatus for manufacturing raw fuel (200)    Drum (202a)
NOVELTY - An apparatus has a modifier (1) which generates hydrogen-rich reformed gas from hydrocarbon fuel, a steam generator (2) which generates water vapor for reforming reaction, and a impurity splitter (6) provided in portion where hydrocarbon fuel and water vapor combines.    USE - Apparatus is used for generating hydrogen from hydrocarbon fuel.    ADVANTAGE - The hydrogen generating apparatus has excellent durability, and is cleaned easily without occlusion in gas flow path.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of apparatus. (Drawing includes non-English language text)    Modifier (1)    Steam generator (2)    Heat exchanger (5)    Impurity splitter (6)    Water storage tank (10)
NOVELTY - The apparatus has cutoff valve (21) that is provided between water electrolyzer (1) and water circulation line (5). The cutoff valves (22,23) are provided in hydrogen extraction line (8) and oxygen extraction line (9), respectively. Several measurement apparatus (24-33) are provided for detecting the state of cutoff valves and outputting detection signal to control unit. The control unit is provided to process the detection signal and output the closing signal to cutoff valves at the time of abnormality generation.    USE - Solid polymer type water electrolysis apparatus.    ADVANTAGE - As the cutoff valve is closed at the time of abnormality generation, the inflow of hydrogen to water electrolyzer can be prevented and the mixing of hydrogen and oxygen can be eliminated. Thus, the spreading of fire due to mixing of hydrogen and oxygen can be suppressed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for stop method of solid polymer type water electrolysis apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the solid polymer type water electrolysis apparatus.    Water electrolyzer (1)    Water circulation line (5)    Hydrogen extraction line (8)    Oxygen extraction line (9)    Cutoff valves (21-23)    Measurement apparatus (24-33)
NOVELTY - Nano metal fuel is a group of nano metal added in alcohol, bio-fuel, plant oil and other organic solvents. This nano metal fuel is used for a power of engine of airplanes, cars, ships and heavy machinery or a fuel for generators and boilers use. This nano metal fuel can be replaced for petroleum to reduce the emission of CO2.
NOVELTY - The present invention relates to a synthetic power fuel oil containing fuel oil and isopropanol, wherein the fuel oil is composed of mixing C4~C18 hydrocarbons. The present invention can be burned and exploded in an internal combustion engine to push the cylinder shaft to generate power after adequately mixing and stirring the fuel oil with the isopropanol. Furthermore, the synthetic power fuel oil of the present invention has low sulfur content to provide efficacies of environmental protection, energy saving, and enhancing the mechanical power.
NOVELTY - A through hole is formed in a separator (7) and is fluid connected to the manifold of a gasket. An opening (73a') is formed in a gas distribution hole (73a) facing the through-hole of the separator. A groove (74) is formed in side opposing the gasket of the separator rather than opening. The separator, gas transmission layers (6,6') and membrane electrode assembly (3) are accommodated in molding die. The gasket is molded to the circumference of membrane electrode assembly, gas transmission layer and side portions projected from separator.    USE - Manufacturing method of fuel cell (claimed).    ADVANTAGE - The groove is formed in the side opposing the gasket of the separator rather than opening formed in gas distribution hole such that the resin is allowed to flow into the groove before the resin is injected into the cavity for gasket. Hence the obstruction of opening of the gas distribution hole by the resin is prevented.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the molding die for fuel cell.    Membrane electrode assembly (3)    Gas transmission layers (6,6')    Separator (7)    Gas distribution hole (73a)    Opening (73a')    Groove (74)
NOVELTY - The method involves injecting filler (6) into an edge of MEGA (3) and porous unit (4) so that the porous unit and MEGA are fixed with respect to each other. The gasket molding apparatus (2) is provided with metal molds (20,21) so that a gasket (7) is integrally molded on outer side of filling portion (4a) of porous unit.    USE - Manufacturing method of fuel cell.    ADVANTAGE - Since the filler is injected into edge of MEGA and porous unit so that the porous unit and MEGA are fixed with respect to each other, the porous unit and MEGA can be fixed temporarily with sufficient precision so that the fuel cell can be manufactured easily with high yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing apparatus of fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view illustrating the operation of manufacturing apparatus of fuel cell.    Gasket molding apparatus (2)    MEGA (3)    Porous unit (4)    Filling portion (4a)    Injecting filler (6)    Gasket (7)    Metal molds (20,21)
NOVELTY - A double-screwing straw gasifying furnace comprises furnace body, hearth, furnace cover, and grate which has two layers of air inlet pipes containing upper layer air inlet pipes and lower layer air inlet pipes in lower side. Each layer of air liner pipe has inner ends that penetrate furnace body and outer sides that incline toward one side of furnace body which are installed by multiple branches on tangential direction. The inclining directions of two layers of air inlet pipes are opposite.    USE - Double-screwing straw gasifying furnace.    ADVANTAGE - The double-screwing straw gasifying furnace has high thermal efficiency, and meets requirements of cooking and heating to avoid multiple disadvantages and provide advanced furnace to spread straw gasifying combustion technology.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the double-screwing straw gasifying furnace.    Fuel gas pipe (3)    Fuel gas furnace (4)    Heating unit (5)    Fuel gas stove (6)    Water box (9)
NOVELTY - The apparatus has a solids feed conduit (27) in fluid communication with a top wall (23) with an interior of a cylindrical vessel. A rotor comprises a rotatable shaft coincident with a longitudinal axis of the cylindrical vessel extending through a solids feed opening into the interior of the cylindrical vessel. A blade (28) comprises an edge connected directly and indirectly with the rotatable shaft and an opposite edge spaced apart from a side wall. The blade comprises a solids feed contact surface including a contact surface plane intersecting with and tangential to the rotatable shaft.    USE - Apparatus for performing pyrolysis of solid organic material e.g. wood, agricultural waste and municipal waste.    ADVANTAGE - The apparatus removes char particles from hot pyrolysis vapors, so as to increase the chemical stability of a pyrolysis oil product. The rotation speed of the rotatable shaft can be changed, so as to easily regulate the rate of acceleration of the solids feed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for performing pyrolysis of solid organic materials.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a system for performing pyrolysis of biomass and solid feeds including an ablative pyrolyzer.    Top wall (23)    Solids feed conduit (27)    Blade (28)    Motor (31)    Solids feed system (40)
NOVELTY - A gasification apparatus has a gasifier (1) that receives flow medium heated as thermal medium from a gas reforming furnace (3); a combustion furnace (2) that supplies air and flow medium discharged out of the gasifier; and gas reforming furnace connected to combustion furnace and gasifier. Gas reforming furnace receives the thermal medium heated with combustion furnace while generation gas produced by gasifier is received and generation gas is made to contact with the thermal medium so that thermal medium is returned to the gasifier while modifying the generation gas.    USE - Gasification apparatus for organic matter raw material such as biomass.    ADVANTAGE - Increases gas volume generation and enables utilization of heat amount held by the tar by gasifying tar in the generation gas from gasifier at gas reforming furnace. Prevents trouble in generation gas utilization that prevents increase of tar removal processing and originates in the tar. Ensures stable gasification of the biomass since comparatively small reaction of the distribution of reaction temperature or reaction time is performed by using circulating fluidized bed furnace. Ensures holding time of biomass within the gasifier is easily controllable by water steam flow volume. Heat balance of the whole gasifier is ensured even when gasifying organic matter raw material with small amount of fixed carbon content since flow medium holds heat amount required in order that flow medium may heat organic matter raw material by gasifier, thus reduces tar in the generation gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a gasification method of organic matter raw material.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the gasifier. (Drawing includes non-English language text).    Gasifier (1)    Combustion furnace (2)    Gas reforming furnace (3)
NOVELTY - A peptide molecule with antimicrobial activity comprising doublets of cecropin A, is new.    USE - The peptide molecule is useful for preparing drugs for preventing and treating microbial diseases in humans and animals, where the microbial diseases can be bacterial or fungal origin or can be caused by bacteria Vibrio ordalii, V. mimicus, V. parahaemolyticus, V. anguillarum, V. alginolyticus, Escherichia coli, Enterobacter aerogenes, E. tarda, Bacillus subtilis, Staphylococcus epidermidis, Micrococcus luteus, and fungus Saprolegnia sp. and mining, agriculture and livestock for the control and prevention of fungus (all claimed).    ADVANTAGE - The molecule is environmentally friendly and rich in an antifungal molecule, which enables to drastically reduce the development of the fungus if the fish is subjected to stress during the nursery time, this will increase significantly the number of survivors in the later stages of development.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a method for producing peptide molecule with antimicrobial activity;    (2) a pharmaceutical composition comprising doublets of cecropin A and a pharmaceutically acceptable vehicle; and    (3) an extract of a peptide molecules with antimicrobial activity comprising the doublet of cecropin A.
NOVELTY - Reducing the level of organic contaminants in an industrial effluent where the industrial effluent lacks sufficient dissolved oxygen to support enzymatically catalyzed removal of organic contaminants by an enzyme requiring oxygen for enzymatic activity, involves (a) adding to the effluent at least one enzyme to reduce the level of organic contaminants in the effluent, where enzymes require oxygen for enzymatic activity; and (b) adding an in situ source of dissolved oxygen.    USE - For reducing the level of organic contaminants in industrial effluent selected from petroleum refinery effluent, desalting waste water, effluent from coking operations, waters resulting from direct contact with a hydrocarbon stream and which contain sulfides, ammonia, phenols and other organic chemical constituents of crude oil, wash water, scrubber water (claimed).    ADVANTAGE - The method effectively reduces level of organic contaminants i.e. at least 5 (preferably at least 50, especially at least 90)%.
NOVELTY - A dichloride and iron chloride are mixed, and then aqueous ammonia or sodium hydroxide solution is added to regulate pH to 10-12, subjected to aging process and washed, to obtain magnetic matrix. The resultant matrix is mixed with zirconium oxychloride, and then water is added to dissolve zirconium oxychloride and subjected to aging process, to obtain precipitate which is filtered, washed and immersed in ammonium sulfate, concentrated sulfuric acid solution or ammonium persulfate and filtered, to obtain filter cake which is roasted, to obtain magnetic solid acid catalyst.    USE - Preparation of magnetic solid acid catalyst used for biodiesel (claimed).    DETAILED DESCRIPTION - A dichloride and iron chloride in mol ratio of 1:1-4:1 are mixed, and then aqueous ammonia or sodium hydroxide solution is added to regulate pH to 10-12, subjected to aging process for 2 hours and washed using distilled water, to obtain magnetic matrix. The resultant magnetic matrix is mixed with zirconium oxychloride in ratio of 1:0.5-2, and then water is added to completely dissolve zirconium oxychloride, pH is regulated to 10-12 using aqueous ammonia or sodium hydroxide solution and subjected to aging process, to obtain a precipitate which is filtered, washed using de-ionized water until no chlorine ion exists and immersed in 10-50% of ammonium sulfate, concentrated sulfuric acid solution or ammonium persulfate for 4 hours and filtered, to obtain a filter cake which is roasted in a muffle furnace at 500 degrees C for 3 hours, to obtain magnetic solid acid catalyst.
NOVELTY - A wastewater biological treatment comprises subjecting wastewater into an upflow anaerobic sludge blanket (UASB), recycling effluent having sulfide, subjecting recycled effluent into a first anaerobic baffled reactor (ABR), subjecting processed effluent to a second ABR, draining the effluent, inoculating sulfate reducing bacteria in the UASB to obtain domesticated active granular sludge, inoculating decoloration agent in the first ABR, and inoculating anammox agent in the second ABR.    USE - Method of wastewater biological treatment. The wastewater comprises high-concentration sulfate, ammonia nitrogen and obstinate organic pollutant, or high chromium content. (all claimed)    DETAILED DESCRIPTION - A wastewater biological treatment comprises:    (A) subjecting wastewater into a UASB controlled at 20-35 degrees C and pH value of 6-8 for 24-48 hours, recycling effluent having sulfide, and subjecting recycled effluent into a first ABR controlled at 20-35 degrees C and pH value of 6-8 for 24-72 hours for micro-aeration;    (B) subjecting processed effluent to a second ABR controlled at 20-35 degrees C and pH of 6-8 for 24-72 hours, and draining the effluent, inoculating sulfate reducing bacteria in the UASB to obtain domesticated active granular sludge; and    (C) inoculating decoloration agent in the first ABR and inoculating anammox agent in the second ABR.    The mole ratio of nitrate nitrogen and ammoniacal nitrogen in effluent is 1-1.3:1.    DESCRIPTION OF DRAWING(S) - The drawing is a flow chart of a method of wastewater biological treatment. Drawing includes non-English language text.
NOVELTY - A power-free method comprises pouring domestic sewage directly to a water collection tank, transporting to a sand-gravel biological filter using water intake pipeline, and discharging. The filter layers traversed by sewage comprises a first layer comprising cobble having grain diameter of 3-5 cm and a thickness of 5-20 cm; a second layer comprising fine sand having grain diameter of 0.1-2 mm and a thickness of 70-100 cm; and third layer comprising cobble having grain diameter of 3-5 cm and a thickness of 5-20 cm.    USE - Power-free method (claimed) for treating single-family type rural domestic sewage.    ADVANTAGE - The method is low cost, has high efficiency; discharges water having chemical oxygen demand of less than 100 mg/l thus making the water applicable to vegetables irrigation or toilet flushing; employs device having small floor space, that does not require power, that can be maintained conveniently, that is durable, and that does not require frequent maintenance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for use in power-free method comprising a water collection tank, a sand-gravel biological filter, a water intake tube, and sand-gravel biological filter filled with three layers of spreading materials    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a device for use in power-free method.
NOVELTY - Sludge with heavy metals exceeding standards is treated by mixing (pts.wt.) sludge (2300) having heavy metal contents exceeding standards and water content of less than 80 mass%, aerobic microbial agent (4.6-6.9), additive (690-805), and heavy metal passivator (184-276); and fermenting the mixture for 15-20 days to obtain treated sludge.    USE - Method of treating sludge having heavy metals exceeding standards (claimed).    ADVANTAGE - The method makes sludge stable and safe, does not damage organisms, and makes treated sludge be safely buried and landfill site can be covered with soils and planted with plants to beautify the environment and improve the ecology.    DETAILED DESCRIPTION - Sludge with heavy metals exceeding standards is treated by mixing (pts.wt.) sludge (2300) having heavy metal contents exceeding standards and water content of less than 80 mass%, aerobic microbial agent (4.6-6.9), additive (690-805), and heavy metal passivator (184-276); and fermenting the mixture for 15-20 days to obtain treated sludge. The aerobic microbial agent comprises Bacillus subtilis, Bacillus stearothermophilus, Aspergillus niger, Sporotrichum thermophile and/or Saccharomyces cerevisiae. The additive comprises shale, grass carbon, saw dust, residue and/or manioc waste.
NOVELTY - The device has a pyrolysis reactor equipped with an external heating system e.g. integral electric heating plate, and a heat insulation system, and a rotating shaft provided with a spiral blade. A side wall of a cylinder is provided with a biomass feeding pipe and a pyrolysis product outlet pipe, where the outlet pipe is vertically led to a coke collecting tank of a pyrolysis product collecting system. A side wall of the coke collecting tank is provided with an outgas pipeline that is orderly connected with a condenser, a bio-oil collecting tank and a tail gas exhaust pipe.    USE - Biomass spiral pyrolysis device.    ADVANTAGE - The device can precisely control the pyrolysis time and the pyrolysis temperature by sections, so that the obtained bio-oil is controllable and easy to extract chemicals.    DETAILED DESCRIPTION - The spiral blade, the inner wall of the cylinder, and the surface of rotating shaft are made of corrosion resistant materials. An INDEPENDENT CLAIM is also included for a process for performing pyrolysis on biomass by using a biomass spiral pyrolysis device.    DESCRIPTION OF DRAWING(S) - The drawing shows a side partial sectional view of a biomass spiral pyrolysis device.
NOVELTY - Preparing diesel fuel component by using vegetable oil through catalytic hydrodeoxygenation comprises adding vegetable oil, catalyst, and solvent in a reactor, adding hydrogen gas with 1-10 MPa reaction pressure, reacting for 3-12 hours and stopping reaction, cooling at room temperature, and automatically separating the catalyst and the liquid phase product without the complex after treatment of centrifuging and filtering; where the catalyst is barium sulfate loading palladium catalyst; the concentration of palladium is 1-10 wt.%; and the solvent is n-hexane, n-heptane, n-octane, or dodecane.    USE - The process is useful for preparing diesel fuel component by using vegetable oil through catalytic hydrodeoxygenation (claimed).    ADVANTAGE - The process has simple preparation technique, low reaction temperature, and less usage amount of solvent. Moreover, the carbon chain of grease does not crack; the target product has high combustion heat value; and the catalyst can be recycled.
NOVELTY - A methanol diesel oil compound additive comprises (pts.wt.) diethyl phthalate (1-4), n-butylamine (1-8), isooctyl alcohol (1-9), cyclohexanone (1-6), dodecyl methacrylate (13-42), hard fat (7-30), phenyl propargyl ether (1-5), dihexadecyl dimethyl ammonium chloride (1-8), ethyl formate (2-12), isooctyl nitrate (2-14), and polyoxyethylene hexadecyl phenolic ether (1-6).    USE - The methanol diesel oil compound additive is useful for spreading methanol diesel oil.    ADVANTAGE - The methanol diesel oil compound additive enables the methanol diesel oil to be uniformly mixed and steadily stored for more than 6 months, which effectively improves fire behavior of methanol diesel oil and inhibits volatilization of methanol when the content is higher. Moreover, it has simple producing technique and convenient use.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a preparation method of the methanol diesel oil compound additive comprising: (a) adding diethyl phthalate, n-butylamine, isooctyl alcohol, and cyclohexanone in material mixing tank based on the ratio, uniformly agitating and adding dodecyl methacrylate and hard fat, uniformly mixing, and adding phenyl propargyl ether and dihexadecyl dimethyl ammonium chloride, uniformly mixing, and orderly adding ethyl formate and isooctyl nitrate to agitate for 30-35 minutes; and (b) adding polyoxyethylene hexadecyl phenolic ether to the solution, heating at 45-50 degrees C, agitating for 20-30 minutes under the atmospheric pressure of 80-100, standing them for 24 hours, and filtering to remove deposit.
NOVELTY - A fuel battery system comprises a bioreactor including a cathode chamber and an anode chamber internally provided with microbial active matters, and separated via a proton exchange membrane, where the cathode chamber contains heavy metal ion solution. The anode comprises two crossly connected graphite electrodes while the cathode comprises an inclined graphite electrode(s).    USE - A fuel battery system used for processing sewage to generate electricity and for reducing heavy metal (claimed).    ADVANTAGE - The system has a simple structure, is inexpensive, and convenient to operate without introducing oxygen.
NOVELTY - Digestor comprises storage and recirculation tank (1) to receiving sludge to be subjected to treatment; reactor (2) in which chemical and biological reactions occur under high pressure condition determined by depth of reactor and under uniform temperature; flotation-sedimentation unit in which biological sludges are sedimented and partially recycled within reactor; storage tank (3), where the sludges increase their concentration; and de-hydration unit for the sludges, so that the latter are then disposed of.    USE - For digesting biological sludges (claimed).    ADVANTAGE - The digestor provide very high digestive efficiency; provides operative simplicity of the continuous system; provides cost effective anaerobic system.    DETAILED DESCRIPTION - Digestor comprises a storage and recirculation tank (1) for biological sludges, suitable to receiving sludge to be subjected to treatment; a reactor (2) placed downward the storage and recirculation tank, within which sludge arrives from storage and recirculation tank, and within which a chemical and a biological reactions occur under high pressure condition determined by depth of reactor and under uniform temperature; a flotation-sedimentation unit of the sludges downward reactor, within which biological sludges are sedimented and partially recycled within reactor; a storage tank (3) downward the flotation-sedimentation unit, where the sludges increase their concentration; and a de-hydration unit for the sludges, so that the latter are then disposed of. The digestor comprises at least one diffusers installed within reactor, suitable to separately insufflate air and pure oxygen within reactor.    DESCRIPTION OF DRAWING(S) - The figure shows schematic view of block diagram of system.    Storage and recirculation tank (1)    Reactor (2)    Storage tank (3)    Flotation-sedimentation unit (5)
NOVELTY - A production inhibitor of methane gas from putrefactive-organism aqueous mixture comprises magnesium oxide powder and/or magnesium hydroxide powder.    USE - Production inhibitor of methane gas from putrefactive organism aqueous mixture e.g. swamp soil, paddy soil and livestock excretion (claimed).    ADVANTAGE - The inhibitor can efficiently suppress production of methane gas in anoxia or low oxygen concentration atmosphere.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a production suppression of methane gas from putrefactive organism aqueous mixture.
NOVELTY - Water is electrolyzed in an electrolytic cell bath (1) containing an electrolyte to generate hydrogen gas (2) and oxygen gas (3). The booster pump sucks (4) the generated gas and feeds into pressurization-melting tank (5). The gas is mixed with water and solubility of gas with respect to water is increased by pressurizing. Then, the pressure of resulting water is decreased rapidly through aperture mechanism (6). The water is made to generate micro-bubble (10) in a low-pressure container rather than the pressurization-melting tank.    USE - Generation of micro-bubble used for manufacture of reduced water (claimed). Uses include but are not limited to washing e.g. face, hands and hair, and hospital, catering field and industry.    ADVANTAGE - The method enables the acceleration of floating and gas-liquid cleaning effect of micro-bubble. Since the method is carried out using mixture of oxygen gas and hydrogen gas, diaphragm is not necessary. The reduced water does not induce corrosion of iron and rotting of foodstuff and drink.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) micro-bubble generator; and    (2) reduced water (11).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the micro-bubble generator.    Electrolytic cell bath (1)    Hydrogen gas (2)    Oxygen gas (3)    Booster pump (4)    Pressurization-melting tank (5)    Micro-bubble (10)    Reduced water (11)
NOVELTY - Biofuel production involves volatilizing triglycerides biomass, where the volatilized biomass is processed through thermal cracking process at 500 degrees C for 10-60 seconds. The obtained biomass is processed through condensation or fractionation process.    USE - Method for producing biofuel by thermal cracking (claimed).    ADVANTAGE - The biofuel production method enables to produce the biofuel with high conversion rate and cetane numbers and high purity by using vertical tubular reactor.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an equipment for producing biofuel, which comprises a feeding unit, heating unit, reaction unit, processing unit and instrumentation and controlling unit.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of a pilot plant of thermal cracking of vegetable oil and greasy residue.    Power supply section (1)    Frequency inverter (2)    Tubular reactor (3)    Condensation section (4)    Fractionating column (5)
NOVELTY - The biomass catalytic gasifier has a catalytic reactor (6) with an air inlet (10) connected to a gasification fuel gas outlet (4) at top section of gasification reactor (1). The catalyst reactor is installed with a catalyst feeding port (5), heat conducting sheets (2), and fuel gas spreading plate (7) on top section, inner wall and bottom, respectively. A gas spreading chamber (9) is provided in an inner cavity of the catalyst reactor, at the lower end of fuel gas spreading plate.    USE - Biomass catalytic gasifier for preparing fuel gas from farming and forest waste materials by pyrolysis, gasification and reforming process.    ADVANTAGE - Provides a biomass catalytic gasifier which ensures favorable production continuity, high gas heat value and carbon conversion rate, favorable furnace heat-conducting property and high heat efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass catalytic gasifier.    Gasification reactor (1)    Heat conducting sheets (2)    Gasification fuel gas outlet (4)    Catalyst feeding port (5)    Catalytic reactor (6)    Fuel gas spreading plate (7)    Gas spreading chamber (9)    Air inlet (10)
NOVELTY - Staggered circulating flow type biological filler has trapezoidal corrugated first filler plates (1) and trapezoidal corrugated second filler plates (2) staggered and fixedly adhered at intersection points (7); and fixation frame body surrounded by two horizontal frames (3) and two vertical frames (4). First and second filler plates are embedded in fixation frame body after fixed adhesion and fastened in the fixation frame body by threaded rods (5) and nuts (6). Round, triangular or rhombic holes (8) are formed in the first and second filler plates.    USE - Staggered circulating flow type biological filler for sewage treatment.    ADVANTAGE - Provides biological filler with large filler superficial area, high utilization rate, large turbulent fluctuation of water flow in filler and complete contact of organism and biological film in water, and increased chemical oxygen demand (COD) removal rate by more than 30 percent compared with conventional biological film reaction system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the staggered circulating flow type biological filler.    First filler plates (1)    Second filler plates (2)    Horizontal frames (3)    Vertical frames (4)    Threaded rods (5)    Nuts (6)    Intersection points (7)    Holes (8)
NOVELTY - A volcanic water purifying device has a semi-spherical net shade (1); a planar net shade (2); and volcanic particles (3) located inside the semi-spherical net shade. The grain sizes of volcanic particles are greater than the aperture of net shade. Semi-spherical net shade and planar net shade are connected with each other through a flange. The grain size of volcanic particles is 1.5-5.0 centimeters. Volcanic grains are basically spherical and have surfaces that are coarse and porous.    USE - Volcanic water purifying device for small-sized sewage purifying treatment and landscape water purifying treatment.    ADVANTAGE - Provides volcanic water purifying device with good purifying effect and that effectively adsorbs suspended substances and soluble organic substances in water and uses suspended substances and soluble organic substances as nutrient source of microorganism.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the volcanic water purifying device.    Semi-spherical net shade (1)    Planar net shade (2)    Volcanic particles (3)
NOVELTY - The furnace has material discharge stirrer (2), feeding device (3), double-taper pipe furnace body (4), feeding water sealing portion (5), chimney (6), cone valve (8), fuel gas outlet (9), and furnace wall (10). The feeding water sealing portion and chimney are arranged on top of furnace body. The cone valve is positioned at the neck part. The fuel gas outlet is arranged on top of the lower cone of furnace body. The material discharge stirrer and heating device are arranged at the lower part of furnace based on furnace body. The material discharge stirrer is arranged outside furnace wall.    USE - Continuous numerical control carbonizing furnace for performing carbonization production continuously using biomass fuel.    ADVANTAGE - Ensures double-sealing of the cone valve and water sealing portion so that feeding of material and unloading of material can be performed at the same time so as to reduce the heat loss. Performs continuous carbonization production and increases production efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the continuous numerical control carbonizing furnace. (Drawing includes non-English language text).    Material discharge stirrer (2)    Feeding device (3)    Double-taper pipe furnace body (4)    Feeding water sealing portion (5)    Chimney (6)    Cone valve (8)    Fuel gas outlet (9)    Furnace wall (10)
NOVELTY - The system has a reaction device connected with a heating device and divided into a set of two reaction device parts. An evaporating dehydration system is connected with the device parts via a high-pressure separator, a stabilizer system and an extracting system. Two recovering towers are connected with the extracting system. The evaporating dehydration system is connected with another set of two reaction device parts. The stabilizer system is provided with a side-line extracting hole. The high-pressure separator is connected with the stabilizer system through a pipeline.    USE - Naphtha reformed system for producing residual extracted oil, benzene and mixed aromatic hydrocarbon.    ADVANTAGE - The system has high processing capacity, high liquid recovery rate, and improves aromatic hydrocarbon yield and hydrogen yield.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a naphtha reformed system.
NOVELTY - The system has first reaction device and second reaction device connected with residual extracted oil cutting system through a high-pressure separator, stabilizer system and an extracting system. The extracting system is connected with two recovering towers. Third reaction device and fourth reaction device are connected with a bottom part of the residual extracted oil cutting system for extracting kerosene through a pipeline. The high-pressure separator is connected with the stabilizer system through the pipeline.    USE - Reformed system for producing high-octane petrol through extraction of kerosene.    ADVANTAGE - The system has increased processing capacity, liquid recovery rate, aromatic hydrocarbon yield and hydrogen yield.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a reformed system for producing high-octane petrol.
NOVELTY - The system has a first reaction device and/or a second reaction device connected with a residual extract oil cutting system through a high-pressure separator, a stabilizer system and an extracting system. A bottom part of the residual extract oil cutting system is connected with an evaporating dehydration system and utilized for directly extracting kerosene product through a pipeline. The evaporating dehydration system is connected with a third reaction device and/or a fourth reaction device.    USE - Reforming system.    ADVANTAGE - The system greatly increases processing capacity, liquid recovery rate, aromatic hydrocarbon yield and hydrogen yield.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a reforming system.
NOVELTY - The system has first reaction device and/or second reaction device connected with an evaporating dehydrating system through a high pressure separator, a stable tower system and an extracting system. The evaporating dehydrating system is connected with third and/or fourth reaction device and provided with a side-draw opening. A bottom part of each reaction device is connected with a high pressure separator through a pipeline, and a high pressure separator is connected with the stable tower system through a pipeline.    USE - Naphtha productive arene reforming system.    ADVANTAGE - The system has better treating property, high liquid absorbing rate, improved yield of arene and improved yield of hydrogen.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a naphtha productive arene reforming method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a naphtha productive arene reforming system.
NOVELTY - The device has an ignition port (2) provided on a bottom ash cleaning opening of a furnace body (1) and equipped with a buckle cover (3). An inner side of the ignition port is equipped with an electro-thermal rod (4), and a lower part of the furnace body is provided with an air inlet pipe (5). An end of the air inlet pipe is connected with a blast fan (6).    USE - Ignition device for a biomass gasification environment-friendly energy-saving furnace.    ADVANTAGE - The device ensures convenient starting of ignition by electrifying the electro-thermal rod, burning the rod, inserting the rod in the ignition port, turning on the blast fan to blow for 1 to 5 minutes and drawing out the electro-thermal rod, thus avoiding pollution of the primary ignition soot, increasing gas generating speed and saving labor and time. The device is convenient to operate, and can satisfy production requirements.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of an ignition device.    Furnace body (1)    Ignition port (2)    Buckle cover (3)    Electro-thermal rod (4)    Air inlet pipe (5)    Blast fan (6)
NOVELTY - The structure has a switch board mounted between a smoke chamber and a counter combustion chamber. A gasification ring is installed above a hearth and a secondary air chamber, where the gasification ring is annularly arranged at an outer part of the gasification ring. A secondary air distributing hole is formed between the hearth and the counter combustion chamber. The gasification ring is provided with a fire collecting basin. The counter combustion chamber is provided with a superconducting tube.    USE - Biomass superconducting gasification ring protection structure.    ADVANTAGE - The structure ensures uniform gas production, safety and convenience, and is eco-friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass superconducting gasification ring protection structure.
NOVELTY - The gasifier has a sealed gas tank comprising a receiving cavity, a filling hole and a filling hole sealing cover. A hearth is provided with a gas intake inlet. A blower is provided with a blowing exhaust outlet that communicates with the gas intake inlet. A blowing intake inlet communicates with the blowing exhaust outlet. A press disc cover rotary shaft and a press disc cover rotary shaft handle are arranged on the filling hole sealing cover. A gas exhaust outlet communicates with the gas intake inlet of the hearth.    USE - Biologic straw gasifier.    ADVANTAGE - The biologic straw gasifier efficiently treats tar such that gas purity is higher and combustion effect is better.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biologic straw gasifier.
NOVELTY - The system has a heating device connected with a reaction device, where the reaction device is divided into first and second reaction devices and connected with an evaporating dehydration system through a high-pressure separator, a stabilizer system and an extracting system. The evaporating dehydration system is connected with third and fourth reaction devices. A bottom part of the reaction device is connected with a high-pressure separator through a pipeline. The high-pressure separator is connected with a stabilizer system.    USE - Reformed system for producing aromatic hydrocarbon.    ADVANTAGE - The system can produce aromatic hydrocarbon in large scale. The system increases processing capacity, liquid recovery rate, aromatic hydrocarbon yield and hydrogen yield.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a reformed system for producing aromatic hydrocarbon.
NOVELTY - The device has a furnace body whose bottom part is equipped with a spiral air inlet. An outlet pipeline is equipped at an upper side of the furnace body, where the outlet pipeline is connected to a fuel gas purification device. Bottom of the fuel gas purification device is equipped with a discharge port. A water outlet point of the discharge port is arranged with a water collector. An upper end of the fuel gas purification device is equipped with a smoke removal pipeline, where the smoke removal pipeline is provided with a smoke removal switch.    USE - Straw gasification furnace device.    ADVANTAGE - The device has high utilization ratio of fuel, large fire, low pollution, and better environment protection effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial sectional view of a straw gasification furnace device.
NOVELTY - The biogas tank has a fermenting tank (1) connected to a waste material tank (3) and a gas storage tank (2) which is located on the fermenting tank. A waste material hole (8) is formed at the central position of an arced door (7). A gas outlet (4) is formed at the central position of the top portion of the gas storage tank. An unloading opening (5) is formed at the intermediate portion on one side of the gas storage tank. A discharging opening (9) is formed at the upper portion on one side of the waste material tank.    USE - Rural household biogas tank.    ADVANTAGE - The biogas tank can be produced simply at low cost and energy, so that the energy can be conserved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of the rural household biogas tan.    Fermenting tank (1)    Gas storage tank (2)    Waste material tank (3)    Gas outlet (4)    Unloading opening (5)    Arced door (7)    Waste material hole (8)    Discharging opening (9)
NOVELTY - An aviation fuel oil base is obtained by hydrogenating a raw oil containing mixed oil of oxygen-containing hydrocarbon compound derived from animal of plant oil-and-fat and sulfur-containing hydrocarbon compound, or a raw oil obtained by mixing the mixed oil with petroleum-derived base obtained by refining crude petroleum oil.    USE - Base oil is used for aviation fuel composition for aeroturbine fuel oil (both claimed).    ADVANTAGE - The aviation fuel composition has low environmental load and excellent combustibility, oxidation stability and cyclic characteristics.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for aviation fuel composition, which contains aviation fuel oil base.
NOVELTY - A pharmaceutical composition comprises a dry base comprising a bulk ingredient and a binder; a viscous additive comprising an oily compound; a saline solution comprising an evaporative fluid and a salt; and a preparation comprising methyl farnesoate encapsulated in phospholipids.    USE - A pharmaceutical composition for inhibiting reproductive activity of tadpole shrimp (claimed) for preventing crop loss. No biological data given.    ADVANTAGE - The particles remain structurally and chemically stable in field for 4-14 days after exposure to water. The composition is environmentally friendly, and prevents crop loss due to tadpole shrimp population without the use of copper sulfate.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparation of the composition comprising combining dry base and viscous additive to form homogeneous first mixture, adding first portion of saline solution and salt to form crumbly consistency, and adding a second mixture comprising preparation comprising methyl farnesoate encapsulated in phospholipids to the first mixture; and    (2) inhibiting reproductive activity of tadpole shrimp comprising dispensing particles into a field comprising tadpole shrimp, its eggs and/or its cysts.
NOVELTY - The biomass thermal decomposition apparatus has combustion furnace (1) which receives supply of char (9) or combustible gas, and then burns it. The air flow layer thermal decomposition device (2) which thermally decomposes biomass (7) supplied in air flow layer, includes biomass supply port and steam supply port. A steam (6) supplied from steam supply port is heated up by hot combustion gas supplied from combustion furnace, and forms air flow layer with combustion gas. The air flow layer thermally decomposes the biomass supplied from biomass supply port.    USE - Biomass thermal decomposition apparatus.    ADVANTAGE - Prevents decline in the liquid yield by advancing of a gasification reaction. Obtains tar by a liquid yield equivalent to the liquid yield in another inert gas. Prevents generation of the local hot section by combustion of biomass, while suppressing free oxygen in atmospheric gas which performs the thermolysis reaction of biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of the biomass thermal decomposition apparatus.    Combustion furnace (1)    Air flow layer thermal decomposition device (2)    Loop seal (4)    Steam (6)    Biomass (7)    Char (9)
NOVELTY - The reduction method involves supplying municipal solid waste (110), electrical energy (116), and steam (115) to plasma melter (112). A syngas (118) is extracted from plasma melter. A greenhouse gas (132) that is exhausted by heat-related process of powerplant (122) is recirculated to plasma melter.    USE - Reduction method for cutting down emission of greenhouse gasses e.g. carbon dioxide in large scale waste disposal process.    ADVANTAGE - Provides a method that inexpensively reduces greenhouse gasses by utilizing plasma melter that consumes and uses carbon dioxide that can be emitted into environment.    DESCRIPTION OF DRAWING(S) - The drawing shows the simplified function block and schematic diagram of method for reduces emission of greenhouse gasses e.g. carbon dioxide in large scale waste disposal process.    Waste (110)    Plasma melter (112)    Steam (115)    Electrical energy (116)    Syngas (118)    Heat-related process of powerplant (122)    Greenhouse gas (132)
NOVELTY - A fuel material, electrical energy, and steam (115) are supplied to a plasma melter (112). Syngas (118) is extracted from the plasma melter, and hydrogen and carbon dioxide are extracted from the syngas. At least a portion of extracted carbon dioxide is supplied to a bioreactor for enhancing the growth of algae (142), and ammonia (134) is formed from hydrogen. The algae form at least a portion of the fuel material.    USE - Large-scale manufacture of ammonia.    ADVANTAGE - The method enables usage of exhaust and waste carbon dioxide to enhance the growth of algae as a commercial product and as a feedstock. The system liberates hydrogen on a large scale and does not require large electrical generation resources. The method enables economical manufacture of ammonia.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) large-scale manufacture of ethylene;    (2) large-scale manufacture of methane;    (3) method of reclaiming carbon dioxide in industrial process;    (4) electrical power generating system; and    (5) method of operating electrical power plant.    DESCRIPTION OF DRAWING(S) - The drawing shows a simplified schematic view of ammonia product produced along with algae which is used as fuel.    Plasma melter (112)    Steam (115)    Syngas (118)    Ammonia (134)    Algae (142)
NOVELTY - Method for delivering an agent, involves administering to a subject a nucleated cell bound to a nanoparticle, where the cell does not internalize the nanoparticle, a liposome covalently bound to a nanoparticle, or a tissue homing cell bound to a biodegradable nanoparticle, where the nanoparticle comprises an agent which is released from the nanoparticle in vivo.    USE - The method is useful for delivering an agent to a subject having tumor e.g. lymphoma, autoimmune disease and infection (all claimed). The cancer includes biliary tract cancer, bladder cancer, breast cancer, cervical cancer, choriocarcinoma, central nervous system (CNS) cancer, colon and rectum cancer, and kidney and renal cell cancer. The autoimmune disease includes rheumatoid arthritis, Crohn's disease, multiple sclerosis, systemic lupus erythematosus (SLE), autoimmune encephalomyelitis, myasthenia gravis (MG), Hashimoto's thyroiditis, Goodpasture's syndrome, pemphigus vulgaris and Grave's disease. The infection includes bacterial infection e.g. Klebsiella infection, viral infection e.g. hepatitis C virus infection, fungal infection e.g. candidiasis and parasite infection e.g. Plasmodium infection.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) biodegradable nanoparticle comprising maleimide groups on the exterior surface; and    (2) composition comprising an isolated T cell or isolated hematopoietic progenitor cell containing biodegradable nanoparticle on the cell surface, where the nanoparticle comprises an agent.
NOVELTY - A composition comprises a genetically engineered yeast cell containing a heterologous DNA encoding at least one enzyme required for N-acetylglucosamine (GlcNAc) metabolism, the genetically modified yeast cell being capable of growing on a nutrient medium where the carbon source is GlcNAc such that the yeast cell prior to genetic engineering is not capable of growth on the GlcNAc carbon source.    USE - The composition is used for making a biofuel, i.e. ethanol (claimed).    ADVANTAGE - The genetically modified yeast cell is capable of growing on a nutrient medium where the carbon source is GlcNAc.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for making a biofuel by modifying a yeast cell preparation that naturally does not metabolize GlcNAc by introducing heterologous DNA into the yeast cell, the heterologous DNA encoding at least one protein required for GlcNAc metabolism; providing GlcNAc as a source of nutrient carbon to the modified yeast strain; and permitting metabolic conversion of the GlcNAc to the biofuel by propagation of the modified yeast cell preparation.
NOVELTY - Producing (P1) an alcohol from a lignocellulosic biomass involves providing lignocellulosic biomass; contacting the lignocellulosic biomass with an alkaline composition containing sodium sulfide and sodium carbonate to provide a pretreated lignocellulosic mixture; contacting the pretreated lignocellulosic mixture with an enzyme composition to provide a fermentable sugar mixture; and fermenting the fermentable sugar mixture to provide an alcohol.    USE - For producing an alcohol (i.e. ethanol) from a lignocellulosic biomass (where the lignocellulosic biomass is selected from herbaceous material, agricultural residues, forestry residues, municipal solid wastes, waste paper, pulp, paper mill residues, corn stover, straw, bagasse, miscanthus, sorghum residue, switch grass, bamboo, water hyacinth, hardwood, hardwood chips, softwood chips, hardwood pulp, and softwood pulp) (claimed).    ADVANTAGE - The process is low cost and efficient for providing lignocellulosic ethanol and other biofuel; reduces side product formation and waste issues; reduces the cost and amount of required process equipment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a composition (C1) comprising an alcohol prepared from lignocellulosic biomass using a method that involving pretreatment of the lignocellulosic biomass with an alkaline solution comprising sodium sulfide and sodium carbonate.
NOVELTY - Obtaining a microorganism or its cellular components having an immunoregulatory function derived from the microorganism, which induces production of interleukin-10 (IL-10) from mammalian dendritic or spleen cells, involves co-culturing a bacterium to be tested with the mammalian dendritic or spleen cell; and selecting a microbial strain having an ability of inducing the production of IL-10.    USE - For obtaining a microorganism or its cellular components having an immunoregulatory function derived from the microorganism, which induces production of Interleukin-10 from mammalian dendritic or spleen cells (claimed), useful for prevention or treatment of immune diseases, e.g. allergy and autoimmune diseases; inflammatory bowel diseases (e.g. large-intestinal ulcer), and maintenance of the immunological homeostasis (health maintenance) of mammals, such as human beings, domestic animals, or pet animals. Also useful in the field of biodegradable plastics; medical and/or pharmaceuticals products; and animal feeding stuff.    ADVANTAGE - The Lactococcus and the ingredient derived from it are high in safety and capable of oral administration, and thus are useful in that immunoregulatory cells can be efficiently induced in the body by making use of the microorganism or its ingredient as an active ingredient of a food product or material, and the animal feeding stuff. The method produces the microorganisms, preferably Lactococcus efficiently.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for selecting a microorganism or its cellular components having an immunoregulatory function, which induces the production of IL-10 from a mammalian dendritic or spleen cells, involving co-culturing cells to be tested with an intestinal epithelial cells to induce cells having a low ability of inducing caspase-1 activity and an enhanced ability of inducing the production of IL-18.
NOVELTY - A high flow water purification treatment comprises using chlorine dioxide, ozone and liquid chlorine as preoxidant which forcedly removes algae in water and simultaneously reduces organic pollutants in water.    USE - High flow water purification treatment is used for removing algae and purifying water of pools, reservoirs and rivers.    ADVANTAGE - The method has lower consumption and high efficiency (algae removal is high), and restores ecological environment. The killed algae residues can be used as nutriment for growth of aquatic plant.
NOVELTY - Treating and recycling urban wastewater comprises passing urban wastewater through grid; pumping up to grit basin with wastewater pump; entering into absorbing basin; mixing with sludge from regenerated basin; introducing mixed solution into grit basin to separate water from sewage; mixing outputting water of grit basin with sterilizer; passing through sterilizing contacting basin; recycling as farm-irrigating water; taking other part of sludge as sludge residue; concentrating sludge by concentrating basin; and introducing into sludge drying factory.    USE - Method for treating and recycling urban wastewater (claimed).    ADVANTAGE - The method has simple treating process, occupies small land area, has low expense on basic construction instrument and operation, and has convenient control and management. The output water can meet requirement on water quality standard for irrigating farm land.    DETAILED DESCRIPTION - The treatment and recycling of urban wastewater comprises:    (A) passing urban wastewater through grid;    (B) pumping up to grit basin with wastewater pump; entering into absorbing basin;    (C) mixing with sludge from regenerated basin;    (D) introducing mixed solution into grit basin to separate water from sewage;    (E) mixing outputting water of grit basin with sterilizer;    (F) passing through sterilizing contacting basin; recycling as farm-irrigating water;    (G) entering most of sludge discharged by grit basin into regenerated basin to regenerate sludge;    (H) entering into absorbing basin after recovering its absorption;    (I) taking other part of sludge as sludge residue;    (J) concentrating sludge by concentrating basin;    (K) introducing into sludge drying factory; and    (L) carrying out dried sludge as farm manure.
NOVELTY - A septic system comprises at least three sealed septic barrels (1, 2, 3), feed pipe (7), methane collecting pipe (6) and connection pipes (4, 5). The feed pipe is connected with upper part of septic barrel far away from the top. The excrement enters septic system through feed pipe. The methane collecting pipe is connected with tops of septic barrels to intensively collect methane produced from septic barrels.    USE - Septic system is used for automatic collection of methane in urban residential areas and rural retail areas.    ADVANTAGE - The system is capable of storing water for isolating odor, thus improving rural environment; and ferments excrement to be used as agricultural fertilizer or animal feedstuff. The sizes of septic barrels can be determined according to customer needs, and are transportable and recyclable.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating a septic system.    Sealed septic barrels (1, 2, 3)    Connection pipes (4, 5)    Methane collecting pipe (6)    Feed pipe (7)
NOVELTY - A biomass liquefied oil is prepared by carrying out pyrolysis on mud to obtain liquefied oil.    USE - Method for preparation of biomass liquefied oil is used for biomass fuel oil, diesel fuel, gasoline or kerosene (claimed).    ADVANTAGE - The prepared liquefied oil has high productivity, high heat value, high hydrogen content and low oxygen content.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the biomass liquefied oil prepared by above method.
NOVELTY - In-situ marsh gas utilization involves adding long lasting desulfurizing agent into a marsh gas fermenting installation through a dosing device for synchronously desulfurizing and fermenting. The obtained deposition is discharged along with the outlet materials, such that the in-situ marsh gas i.e. comprehensively desulfurized inside the marsh gas fermenting device is directly used without extra desulfurizing devices.    USE - Method for in-situ utilization of marsh gas (claimed).    ADVANTAGE - The in-situ marsh gas utilization method is simple, ensures convenient operation, improves utilization valve of resources and desulfurizing efficiency, economizes device and operation costs and extends the service lives of the marsh gas fermenting device and output pipelines.    DETAILED DESCRIPTION - In-situ marsh gas utilization involves adding long lasting desulfurizing agent into a marsh gas fermenting installation through a dosing device for synchronously desulfurizing and fermenting. The obtained deposition is discharged along with the outlet materials, such that the in-situ marsh gas i.e. comprehensively desulfurized inside the marsh gas fermenting device is directly used without extra desulfurizing devices. The desulfurizing agent restrains the activity of sulfureted hydrogen producing strain inside the marsh gas fermenting installation and reduces the sulfureted hydrogen production in the marsh gas. The desulfurizing agent reacts with the sulfureted hydrogen inside the in-situ marsh gas produced during the fermenting process. The desulfurizing agent comprises sulfate reducing bacteria suppressor and sulfureted hydrogen remover in a mass ratio of 1-4:19-16. The mass ratio of desulfurizing agent and dry raw material of marsh gas fermentation is 1-35:1000.
NOVELTY - Flexible methane generator comprises pot made from polyvinyl chloride (PVC) film materials, seal pressed on the two ends of the pot, material entrance, material exit, gas-water separation chamber, gas exit, gas-fired heating system, and solar energy superconductive heating system; where the device is made from flexible materials.    USE - The flexible methane generator industrial and commercial applications.    ADVANTAGE - The pot is well sealed, and simple to construct, of high gas productivity, and easy to be industrialized and generalized.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the flexible methane generator.
NOVELTY - The method involves allowing gas to be treated to be in contact with an absorbing solution comprising amines in aqueous solution to obtain gas enriched with acid compounds. A fraction of the absorbing solution is regenerated in a regeneration column (G) to obtain a regenerated absorbing solution and a gaseous effluent. A part of condensates is introduced into the regeneration column, and the gas enriched with acid compounds is allowed to be in contact in a washing section (B3) with a liquid water flow to obtain a cooled effluent. A part of the water enriched in amine is recycled.    USE - Method for capturing acid compound e.g. carbon dioxide and hydrogen sulfide, in a gas to be treated. Uses include but are not limited to natural gas, flue gas, gas obtained from a Claus method, synthesis gas, conversion gas implemented in an integrated power station for combustion of coal, wood, heavy crude or natural gas, gas resulting from fermentation of biomass, and effluent resulting from a cement factory or an iron factory and a steel mill (all claimed).    ADVANTAGE - The method limits the climatic reheating phenomenon, reduces the content of carbon dioxide and sulfurous hydrogen, and improves the calorific value of gas to allow the liquefaction of natural gas. The method performs the water washing of purified gas and recycles the washing water in the process to recover the amine driven by purified gas. The method allows optimization of the operation of the water washing section, limits the consumption of power necessary for carrying out water washing of the purified gas, reduces the amine losses, and reduces the water treatment operations.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a process for capturing acid compound in a gas to be treated.    Absorption section (B1)    Washing section (B3)    Regeneration column (G)    Filter (H)    Discharging pipe (4)
NOVELTY - Microbe domestication device for purifying the sewage comprises a strain culture box, a strain storage box, a nutrient solution storage box, an air pump, and a control system.    USE - The microbe domestication device is useful for purifying sewage (claimed).    ADVANTAGE - After the microbe strains are placed in the microbe strain culture box and cultured for a period of time, microbe strains are bred in large quantities, when expected concentration and activity are achieved, the microbe strain solution with high concentration is doped to the sewage tank body, and consequently it improves survival rate of microbe strains and reaches the aim of reducing the total operating cost of sewage treatment.    DETAILED DESCRIPTION - Microbe domestication device for purifying the sewage comprises a strain culture box, a strain storage box, a nutrient solution storage box, an air pump and a control system, the strain storage box and the nutrient solution storage box are communicated with the strain culture box through pipelines; where the strain storage box, the nutrient solution storage box and the air pump are connected with the control system through signal circuits; the strain culture box is equipped with an aeration device and a constant temperature device, the constant temperature device is connected with the control system through the signal circuit, the aeration device is connected with the air pump through the pipeline; the strain culture box is equipped with a water intake tube and a water discharge tube, the water intake tube is communicated with the external water source, the water discharge tube is communicated with the sewage treatment tank; and the pipelines for connecting the strain storage box and the nutrient storage box with the strain culture box, the water intake tube and the water discharge tube are equipped with a control valve respectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the microbe domestication device.
NOVELTY - A vegetable oil or disposable edible oil, and methanol or mixed alcohol are subjected to alcoholysis reaction under normal pressure in presence of a catalyst, to obtain biodiesel.    USE - Manufacture of biodiesel used as fuel (claimed).    ADVANTAGE - The method efficiently and economically provides biodiesel in high yield with suppressed generation of glycerin.
NOVELTY - An agrochemical composition comprises (wt.%): diethyl aminoethy hexanoate (0.05-2.5), ethephon or paclobutrazol (0.1-3), chlorpyrifos (0.3-3), imidacloprid (0.01-0.09), Aphox (RTM: Pirimicarb) (0.1-0.25) and additives (balance).    USE - Agrochemical composition is used for stunting and killing pest in corn (claimed). The pest is Ostrinia nubilalis, aphid and moth.    ADVANTAGE - The composition can reduce average height of strain of corn by 20-50 cm; has preventing and treating ratio of O. nubilalis moth of more than 80%; and has preventing and treating ratio of aphid of more than 95%; is simple to use, labor saving, drug saving and safe; ensures whole growth period of corn; completely solves prevention and treatment of pest during later stage of corn, thus ensuring increment or corn, and reducing environmental pollution. The corn yield is increased by more than 20-50%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the agrochemical composition comprising mixing auxiliary agent, adding filler and uniformly stirring to obtain mixture; mixing chlorpyrifos, imidacloprid and Aphox (RTM: Pirimicarb) with above mixture; uniformly stirring, adding diethyl aminoethyl hexanoate and ethephon or paclobutrazol and uniformly mixing; and uniformly mixing mixture with medicine carrier.
NOVELTY - Preparation of organic fertilizer from dredged sludge comprises uniformly stirring sludge, rice husk, and pig manure; mixing and composting; covering the outer layer of compost with saw dust to insulate; introducing air to the compost; turning over once per 5-7 days after the compost is in high temperature fermentation stage; uniformly stirring the compost; turning off the ventilation pipe after 25-28 days; and naturally ventilating the compost to obtain organic fertilizer.    USE - Preparation of organic fertilizer from dredged sludge (claimed).    ADVANTAGE - The organic fertilizer has pH of 6.9-7.43, death rate for ascarid egg of 96-98%, coliform of 10-1-10-2, total cadmium of 0.7 mg/kg, total mercury of 0.03-0.07 mg/kg, total lead of 5-7 mg/kg, total cadmium of 0.76-0.87 mg/kg, total arsenic of 7.3-8.1 mg/kg, and germination index of 70-75%, thus, no phytotoxicity.    DETAILED DESCRIPTION - Preparation of organic fertilizer from dredged sludge comprises preparing (pts.wt.) sludge (4), agricultural waste (1-2), saw dust (1-2), and pig manure (1-2); uniformly stirring sludge, rice husk, and pig manure to obtain a mixture; composting the mixture on a platform with ventilation pipeline; controlling water content of the compost at 60-70%; covering the outer layer of compost with saw dust to insulate; obtaining a compost; starting the ventilation pipe after obtaining the compost; introducing air to the compost, where air volume of ventilation pipeline is controlled at 0.05-0.2 m3 air/m3 compost/minute, the ventilation pipe is started once every 2-3 hours, and ventilation time is 30-40 minutes, where after air is introduced to the compost, the compost is in a high temperature fermentation stage; turning over once per 5-7 days; uniformly stirring the compost; turning off the ventilation pipe after 25-28 days; and naturally ventilating the compost to obtain the organic fertilizer.
NOVELTY - Processing straw-dairy manure organic fertilizer comprises mixing straw powder or rice chaff and biogas liquid and preparing mixture of biogas liquid and straw; carrying out moisture adjustment to fresh dairy manure; uniformly mixing the prepared mixture of biogas liquid and straw and dairy manure containing moisture and fermentation microbial inoculum; carrying out first fermentation, turning, carrying out second fermentation, turning, dehydrating, and completing fermentation; and obtaining organic fertilizer by treating, packing, and finishing.    USE - Processing straw-dairy manure organic fertilizer (claimed) useful for corn in the field.    ADVANTAGE - The method carries out safe treatment to biogas liquid; and obtains organic fertilizer using biogas liquid, thus, solving the problem of pollution due to unrestricted discharge of biogas liquid.
NOVELTY - Production of emulsion fuel oil comprises adding methanol or ethanol to oleic acid or fatty acid, agitating to obtain acid phase, controlling mass ratio at 90-50:10-50; adding methanol or ethanol to ammonia, agitating to obtain alkali phase, and controlling mass ratio at 90-50:10-50; adding alkali phase to acid phase agitated to obtain emulsifying agent, and controlling mass ratio at 10-50:90-50; and adding clean water to petrochemical oil product, agitating until milk white, adding emulsifying agent, agitating until transparent liquid, and filtering, with mass ratio of 90-50:5-25:5-25.    USE - Method for producing emulsion fuel oil (claimed).    ADVANTAGE - The emulsion fuel oil production process is simple, utilizes abundant and low cost raw materials; and produces highly stable product mutually soluble with petrochemical oil product.
NOVELTY - Hemispheric water gas transposition biomass pool comprises a feeding tank, a discharging tank and a fermentation tank.    USE - The pool is useful for achieving water gas transposition of biomass and moving the air chamber during the operation.    ADVANTAGE - The pool can break the encrustation formed in the biomass pool and discharge slag automatically. If the volume of the fermentation tank requires increasing, multiple fermentation pools may be connected.    DETAILED DESCRIPTION - Hemispheric water gas transposition biomass pool comprises a feeding tank, a discharging tank and a fermentation tank, where the tank bottoms of the feeding tank and the discharging tank are higher than the top of the biomass pool, the bottom of the feeding tank is higher than the top part of the fermentation tank, the bottom of the discharging tank is lower than the bottom of the feeding tank, and the bottom of the discharging tank and the top of the fermentation tank are on the same horizontal plane, the fermentation tank is a hemispheric type structure, and the discharging port of the fermentation tank is higher than the feeding port.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hemispheric water gas transposition biomass pool.
NOVELTY - A fermenting substance containing nitrogen and carbon is added to nitrogenous fertilizer compound or alkaline compound, and product is made wet. Pre-processed substance is added into a stack retting tank, microbial bacterial fluid is added, water is injected to soak, maintained for a period of time, and pH is controlled to 3-5, to prepare organic acid. Acid is hydrolyzed to form nutritional liquid. Inoculation fungus and nutritional liquid are added to anoxic tank, mixed completely, and pH is controlled to 6.5-7.5. Water sealing is preformed and methane is produced.    USE - Manufacture of methane.    ADVANTAGE - Methane is manufactured with high purity.    DETAILED DESCRIPTION - A fermenting substance containing nitrogen and carbon is added to nitrogenous fertilizer compound or alkaline compound, product is made wet, and maintained for a period of time. The ratio of carbon to nitrogen is adjusted to predetermined value. The pre-processed substance containing nitrogen and carbon is added into a stack retting tank, microbial bacterial fluid is added, water is injected to soak, maintained for a period of time, and pH is controlled to 3-5, to prepare organic acid. The organic acid is hydrolyzed as low-molecular substance to form nutritional liquid. Alternately, the pre-processed substance containing nitrogen and carbon is added into stack retting tank, maintained at liquid state for a period of time, and pH is controlled to 3-5 to obtain organic acid. The organic acid is hydrolyzed as low-molecular substance to form nutritional liquid. Inoculation fungus and nutritional liquid are added to anoxic tank, mixed completely, and pH is controlled to 6.5-7.5. Water sealing is preformed and methane is produced.
NOVELTY - The device has an induction coil (6) that is arranged in the lower portion of a food drying box (1) for heating and drying food waste. Several halogen lamps (10,30) are installed in the upper portion of the food drying box for emitting high temperature infrared ray with respect to the food waste. A reflector (20) is arranged in the vicinity of the halogen lamps to reflect infrared ray emitted by halogen lamp with respect to the food waste in the food drying box.    USE - Device for processing food waste of restaurant.    ADVANTAGE - High temperature infrared ray can be irradiated effectively with respect to food waste. Hence, moisture content in the food waste can be removed effectively and offensive odor emitted from the food waste can be controlled. Drying efficiency of the food waste can be improved and performance of the food waste processing device can be enhanced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the food waste processing device.    Food drying box (1)    Induction coil (6)    Halogen lamps (10,30)    Reflector (20)    Housing (100)
NOVELTY - The device has preheating oven (20) that preheats organic sludge flowed out from a sludge reservoir (10), and heat hydrolyzed tubs (30,40) that hydrolyze the preheated sludge. A steam supply line (L1) supplies steam to the hydrolyzed tubs. A vapor-liquid separation vessel (50) separates steam from the sludge flowed out from the heat hydrolyzed tubs. A steam supply line (L2) supplies the steam ejected from hydrolyzed tub to preheating oven. A heat exchanger (60) controls the sludge flowed-out from the vessel by a high temperature fire extinguishing gun.    USE - Device for processing organic sludge discharged from waste water treatment plant, home, industry and animal husbandry field, used during production of bio-gas.    ADVANTAGE - The organic sludge treatment process can be performed effectively so that bio-gas production rate can be improved, and the cost required for processing the organic sludge can be reduced reliably.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for organic sludge processing method.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the organic sludge processing equipment. (Drawing includes non-English language text)    Sludge reservoir (10)    Preheating oven (20)    Heat hydrolyzed tubs (30,40)    Vapor-liquid separation vessel (50)    Heat exchanger (60)    High temperature anaerobic digester (70)    Steam supply lines (L1,L2)
NOVELTY - The procedure involves temporarily storing sewage sludge (1) and animal manure on the ground near or on a farmland after sanitization, and placing the manure on top of a waterproof membrane (3) or tarpaulin to prevent the ingress of water during rain. The manure is placed over a layer of biodegradable organic material, such as hay, peat, and sawdust.    USE - Procedure for sanitized storage of natural fertilizer such as sewage sludge and animal e.g. cattle, pig, horse, and sheep, manure, for use in agriculture.    ADVANTAGE - The procedure enables better usage of sewage sludge and animal manure, and improves agricultural production yield.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of storage of sanitized natural fertilizer.    Sewage sludge (1)    Water absorbing layer (2)    Waterproof membrane (3)
NOVELTY - An aerosol type foundation cosmetic composition comprises oil-in-water foundation (70-95 wt.%) as crude aerosol liquid and aerosol dispersion agent.    USE - As aerosol type foundation cosmetic composition.    ADVANTAGE - The composition exhibits visual difference, freshness feeling in use, and is convenient to use.
NOVELTY - The apparatus (100) has a gas chamber (120) which is connected to odor generation chamber (110). A purge chamber (150) is arranged in parallel to the gas chamber. The stored water is directed to purge chamber, when odor is discharged to purge chamber through gas chamber. The water is sprayed to circulation pipe (180) through blower (170), when odor is discharged from purge chamber to pipe.    USE - Apparatus for reducing odor generated from waste such as dung and urine of livestock such as pig and cow, in livestock waste fermentation processing facility. Can also be used in agricultural application, stockbreeding field and industrial field.    ADVANTAGE - The generation of the odor can be avoided without using additional chemicals and the cost of the apparatus can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the apparatus for reducing odor.    Apparatus for reducing odor (100)    Odor generation chamber (110)    Gas chamber (120)    Purge chamber (150)    Blower (170)    Circulation pipe (180)
NOVELTY - Preparation of hydrogen from methanol vapor using catalytically burned flue gas as heat source, comprises preheating methanol and desalted water, gasifying, overheating and transforming into air, carrying out pressure swing absorption to air to obtain hydrogen, discharging tail gas, catalyzing tail gas and burning to generate heat, and transferring heat to heat transfer oil in heat transfer oil system. The heat used in transformation process is provided by heat transfer oil system.    USE - Method for preparation of hydrogen from methanol vapor using catalytically burned flue gas as heat source (claimed).    ADVANTAGE - In the method, the generated tail gas is used in preparing hydrogen from methanol vapor, instead of discharging as waste.
NOVELTY - Gram-negative bacteria biocide comprises at least one active ingredient obtainable from extracts of outer sections of Apiaceae vegetables root.    USE - The biocide is useful for selectively inhibiting Gram-negative bacteria contaminating a medium while significantly less inhibiting Gram-positive bacteria in the medium, where the selectivity value is 1.1-20 (all claimed), and the medium is foods and beverages, preferably food of animal/vegetable origin, processed food, dietary foods and meat, human or animal cavities, such as gastro internal tracks and buccal cavity, and human and animal close environment (e.g. dermal system) and remote environment. Tests details are described but no results given.    ADVANTAGE - The biocide is less toxic to good Gram-positive bacteria.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) inhibiting Gram-negative bacteria in a medium, comprising obtaining a biocide from an outer section of a root of Apiaceae vegetables, and effectively contacting the medium to be protected against Gram-negative bacteria growth, with the biocide; and    (2) a high-survivability probiotic food additive comprising extraction from outer sections of Apiaceae vegetables root, characterized by selectively inhibiting Gram-negative pathogenic bacteria while being less toxic to good Gram-positive bacteria.
NOVELTY - The method for producing ethanol from cellulosic component of municipal solid waste, involves (a) shredding the cellulosic component of municipal solid waste,(b) hydrolyzing with acid and the cellulosic component, to obtain soluble component and insoluble component, (c) separating soluble and insoluble components, (d) separating soluble component obtained in step (c) into acid containing solution and sugar containing solution by continuous ion exclusion chromatography, (e) concentrating sugar containing solution to 12-14% of sugar using reverse osmosis filter, (f) adjusting pH of concentrated sugar containing solution obtained in step (e) to 6 with ammonia, (g) fermenting solution obtained in step (f) with yeast at about 25-36 degrees C to obtain beer, (h) removing yeast from beer obtained in step (g), (i) distilling the ethanol from the beer, (j) drying insoluble component obtained in step (c), and optionally mixing dried component with non-chlorinated plastic, and (k) burning insoluble component obtained in step (j) as a fuel to provide heat for distillation of ethanol in step (i) from filtered beer obtained in step (h) and optionally burning dry insoluble component as boiler fuel to provide heat for raising temperature of acid and shredded cellulosic component while hydrolyzing in step (b) and/or for concentrating the acid containing solution obtained in step (d). Image 0/1
NOVELTY - A combined biological and ecological treatment integral sewage treatment reactor has an ecological treatment tank (2) divided into at least two grids by a vertical partition wall to accept and treat the sewage discharged by a biological treatment tank (1); an iron-enriched filler installed in the grid; water-collecting pipe (6) installed at the bottom of ecological treatment tank and connected with a disinfecting tank (3); and disinfecting tank that drains the treated sewage to neighboring water by the water outlet pipe (7).    USE - Combined biological and ecological treatment integral sewage treatment reactor for sewage treatment.    ADVANTAGE - Provides combined biological and ecological treatment integral sewage treatment reactor with impact resistance, strong load capability, high treatment efficiency, low operation energy consumption, small residual sludge amount, short process flow, small floor area, small investment cost, and convenient management operation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the combined biological and ecological treatment integral sewage treatment reactor.    Biological treatment tank (1)    Ecological treatment tank (2)    Disinfecting tank (3)    Water-collecting pipe (6)    Water outlet pipe (7)
NOVELTY - The peat stirrer has a substrate and a stirring barrel (2). The substrate is fixed to the ground. The stirring barrel is bridged on the substrate. The upper end of the stirring barrel is provided with a feeding hole while its lower end is provided with a discharge hole. A stirring central shaft axially penetrates through the stirring barrel, and is provided in the stirring barrel. Stirring blades (4) are provided on the stirring central shaft. One end of the stirring barrel is provided with a motor which is connected to the stirring central shaft by a decelerator.    USE - Peat stirrer used in brick production.    ADVANTAGE - Provides a peat stirrer capable of uniformly stirring peat so as to more adequately mix peat and shale, which improves the quality of the produced brick while recycling waste material and reducing pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the peat stirrer used in brick production.    Stirring barrel (2)    Stirring blades (4)
NOVELTY - The cover has a sealing cover unit (1) connected with a furnace through a screw (2), where a cross rod (5) is fixed on the sealing cover unit. A threaded shaft (6) is installed on the cross rod, where a spanner (7) is fixed on the threaded shaft. The sealing cover unit is formed by double-layer welding. A small column (10) is fixed in center of a plane upper layer and a down tapered lower layer. A ring of iron ribs is placed under the sealing cover unit and a fireproof rope is provided in a sealing tank (11). The sealing cover unit and the sealing tank are made of iron or copper.    USE - Sealing cover for a biomass environment-friendly energy-saving gasifier.    ADVANTAGE - The cover avoids pollution and improves gas quality. The cover is fireproof, durable and stable. The cover does not need water and does not freeze in winter. The cover is easy to open and convenient to operate. The cover saves time and labor and satisfies demand of production and has long service life.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a biomass environment-friendly energy-saving gasifier sealing cover.    Sealing cover unit (1)    Screw (2)    Cross rod (5)    Threaded shaft (6)    Spanner (7)    Small column (10)    Sealing tank (11)
NOVELTY - The furnace has a transverse clapboard separating a cavity of a cylindrical shell into an upper cavity and a lower cavity. A vertical clapboard separates the lower cavity into a left cavity and a right cavity. A reverse U-shaped condensation pipe is provided in the upper cavity, where two ends of condensation pipe pass through the transverse clapboard. An upper part of upper cavity is in communication with a cold water pipe, and a lower part is in communication with a drain pipe. An air outlet pipe is in communication with the left cavity. A gas pipe is in communication with the right cavity.    USE - Straw gasification furnace for a kitchen in a rural area.    ADVANTAGE - The reverse U-shaped condensation pipe is provided in the upper cavity, the air outlet pipe is in communication with the left cavity, and the gas pipe is in communication with the right cavity, thus purifying combustible gas, and improving burning efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a straw gasification furnace.
NOVELTY - The furnace has a stuffing cover positioned on a stuffing hole (2). Multiple air supplying holes (9) are formed on a furnace body (1) at two sides of a banded-trough shaped carbon-digging hole (4). A carbon-digging cylinder (5) is connected with the furnace body and sleeved with a sealing cylinder (6). An upper end of the sealing cylinder is connected with bottom of the furnace body outside the air-supplying holes. Two ends of the carbon-digging hole are extended out of the sealing cylinder and mounted on a carbon-digging side cover. An inlet is arranged on the sealing cylinder.    USE - Incessant horizontal gasification furnace for a straw.    ADVANTAGE - The furnace solves the problems of frequent gas-cutting and gas-reducing, and reduces gas-producing time.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of an incessant horizontal gasification furnace.    Furnace body (1)    Stuffing hole (2)    Carbon-digging hole (4)    Carbon-digging cylinder (5)    Sealing cylinder (6)    Air supplying holes (9)
NOVELTY - The gasifier has a bottom ash bin (1) arranged at a lower part of a furnace and provided with an ash discharge port (2) at bottom. A furnace plate (3) is arranged above the ash discharge port and fixed with a furnace inner core (4). A gasified gas guide exit (10) is provided on a sidewall of a furnace body whose middle part is provided with an annular wind box (8) with round or polygonal pores. A top part of an air supply port (5) and an ignition tuber (9) are provided with a furnace cover (7).    USE - Small-scale biomass gasifier.    ADVANTAGE - The gasifier reduces usage of fuels, avoids environmental pollution, and improves rural living standard.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a small-scale biomass gasifier.    Bottom ash bin (1)    Ash discharge port (2)    Furnace plate (3)    Furnace inner core (4)    Air supply port (5)    Furnace cover (7)    Annular wind box (8)    Ignition tuber (9)    Gasified gas guide exit (10)
NOVELTY - The gasifier (1) has a fuel gas tube (2) drawn from an upper part and connected to a steam filter (3). The steam filter is connected to a tar and dust filter (4). The steam filter comprises a water-cooled structure. The tar and dust filter includes a water-filter structure.    USE - Biomass gasifier for preventing blockage of a pipeline and a fuel gas stove.    ADVANTAGE - The gasifier prevents blockage of the pipeline and the fuel gas stove in an effective manner. The gasifier is simple in structure, has better tar filtering effect and high combustion efficiency, and reduces air pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass gasifier.    Biomass gasifier (1)    Fuel gas tube (2)    Steam filter (3)    Tar and dust filter (4)
NOVELTY - The hearth has a metal heat conduction inner layer, a metal heat conduction outer layer and a heat insulation layer, which are arranged from inside to outside. An air channel is arranged between the metal heat conduction inner layer and the metal heat conduction outer layer. The metal heat conduction inner layer and the metal heat conduction outer layer are made of steel, and the heat insulation layer is made of fireproof bricks. The metal heat conduction inner layer and the metal heat conduction outer layer are 0.8 mm thick. The heat insulation layer is 3.0 mm thick.    USE - Hearth for a biomass semi-gasifying furnace.    ADVANTAGE - The inner side of the hearth is arranged with the metal heat conduction inner layer and the metal heat conduction outer layer, and the air channel is arranged between the metal heat conduction inner layer and the metal heat conduction outer layer, thus improving the ignition speed and combustion stability. The heat insulation layer is arranged outside the hearth, thus reducing heat loss and energy consumption, and improving energy utilization rate. The hearth is safe to use, simple in structure and inexpensive.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a hearth for a biomass semi-gasifying furnace.
NOVELTY - The mechanism has a screw rod provided with an external thread. An ash basin is connected to a lower end of the screw rod. The screw rod is provided with a volume adjusting assembly that is formed above the ash basin. The volume adjusting assembly is threadedly connected with the external thread of the screw rod. An outer circumference of the volume adjusting assembly is adapted to an inner circumference of a hearth. The volume adjusting assembly is formed with holes. The volume adjusting assembly is equipped with a material putting plate and a lower nut.    USE - Hearth volume adjusting mechanism for a biomass semi-gasification furnace.    ADVANTAGE - The mechanism allows a user to adjust effective volume of the hearth randomly according to different use time, so as to match the different biomass fuel feeding amounts, thus accelerating the fuel to be effectively gasified quickly, and hence guaranteeing adequate combustion of the gasified gas and reducing the resource wastage.    DESCRIPTION OF DRAWING(S) - The drawing shows a top view of a hearth volume adjusting mechanism for a biomass semi-gasification furnace.
NOVELTY - The heater has a furnace body equipped with a gasification chamber (2). A top portion of the furnace body is equipped with a feed inlet (3) and a fuel outlet (4). The feed inlet is equipped with a sealing cover (5). Wind screens (11) are arranged at an upper part of a hurricane piece (10) and placed on an inner circumferential edge of an outer cylinder (7). Hurricane slots (12) are formed between the wind screens and the hurricane piece. An annular hurricane cavity (9) is connected with an air inlet pipe (14) that is connected with an air compressor (13).    USE - High-purity biomass gas producing heater.    ADVANTAGE - The heater has simple structure, simple operation, good practical and stable function, and rapid and pollution-free gas production.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a high-purity biomass gas producing heater.    Gasification chamber (2)    Feed inlet (3)    Fuel outlet (4)    Sealing cover (5)    Outer cylinder (7)    Annular hurricane cavity (9)    Hurricane piece (10)    Wind screens (11)    Hurricane slots (12)    Air compressor (13)    Air inlet pipe (14)
NOVELTY - The method involves converting a hydrocarbon feedstock into a gas mixture, and burning a portion of the gas mixture within a combustion chamber (102). Another portion of the gas mixture is converted into methanol during low demand for the gas mixture within the combustion chamber. Contaminants and particulates are removed from the gas mixture, where the gas mixture is cooled before the contaminants and particulates are removed from the gas mixture. The methanol is stored within a storage tank (92).    USE - Method for producing and storing methanol for use in a power generation system i.e. integrated gasification combined cycle (IGCC) power generation system, by utilizing a methanol generation and storage system (all claimed).    ADVANTAGE - The method enables producing and storing methanol by using the methanol generation and storage system in a cost effective manner. The power generation system is more flexible and self-sustainable. The gasifier unit used during gasification process has reduced size. The gasifier unit runs at a more constant production rate, thus reducing damage of the system.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a power generation system comprising a gas turbine    (2) a methanol generation and storage system comprising a methanol plant.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a coal gasification process for a power generation system including a methanol plant and storage tank.    Gasifier (64)    Air separation unit (70)    Gas cleanup tower (72)    Storage tank (92)    Combustion chamber (102)
NOVELTY - An electrolysis system (4) generates hydrogen and oxygen from water. A combustion chamber (6) processes hydrogen and oxygen, for generating water vapor. An evaporation chamber (12) generates water vapor from water. A condensation chamber (14) receives water vapor from both combustion and evaporation chambers, for condensing water vapor into purified water. A water vapor conduit (16) draws water vapor from evaporation chamber into condensation chamber, when vacuum is generated while water vapor is transferred from combustion chamber to condensation chamber.    USE - Water purification system.    ADVANTAGE - The purified water can be obtained easily and the electric power can be utilized efficiently for electrolyzing water.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for purifying water.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the water purification system.    Electrolysis system (4)    Combustion chamber (6)    Evaporation chamber (12)    Condensation chamber (14)    Water vapor conduit (16)
NOVELTY - The anaerobic reactor has a reactor pot (3) having a biogas outlet at its top wall. The upper part of the reactor pot is provided with a three-phase separator (4) whose upper part is provided with an overflow weir (10). The middle part of the separator is provided with a compressed air washing pipe (7), and the lower part is provided with a mud outlet. The overflow weir is connected to a water outlet (5) on the side wall of the reactor pot. The lower side of the separator is provided with a circulating water collecting pipe (8).    USE - Anaerobic reactor for biological treatment of organic sewage with high concentration.    ADVANTAGE - Provides anaerobic reactor having plane distribution which occupies less area and has high impact load resisting capability. Project construction is fast, biological starting is fast, maintenance cost is low, service life is long, and application range is wide.    DETAILED DESCRIPTION - The circulating water collecting pipe is connected to a water inlet pipe assembly (1) on the bottom of the reactor pot. The water inlet pipe assembly is connected to a reverse washing pipe (11) through an inlet water distributing pipe (2).    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram showing the anaerobic reactor.    Water inlet pipe assembly (1)    Inlet water distributing pipe (2)    Reactor pot (3)    Three-phase separator (4)    Water outlet (5)    Compressed air washing pipe (7)    Circulating water collecting pipe (8)    Overflow weir (10)    Reverse washing pipe (11)
NOVELTY - The biological rope includes a micro-organism carrier composed of a main beam fiber (1) and assisting fibers (2) braided to periphery of the main beam fiber. The assisting fibers are annular, and the main beam fiber and assisting fibers are chemically synthetic fibers.    USE - Biological rope for treating domestic sewage and river water.    ADVANTAGE - Reduces biochemical oxygen demand, chemical oxygen demand and suspended solid of river water and sewage by increasing the capability of micro-organism for treating organic material.    DESCRIPTION OF DRAWING(S) - The drawing is a front view showing the biological rope.    Main beam fiber (1)    Assisting fibers (2)
NOVELTY - Fermenting bed for fully degrading chicken manure at cage culture chicken house comprises fermentation tank, travel tripper, tracks, and idler wheels.    USE - The fermenting bed is useful for fully degrading chicken manure at cage culture chicken house (claimed).    ADVANTAGE - The bed has simple structure, easy operation, convenient use, safety and environmental friendliness. In addition it saves labor, improves the work efficiency and decreases the culture cost. It meets the demand of Development and Construction of State Ecological Agriculture.    DETAILED DESCRIPTION - Fermenting bed for fully degrading chicken manure at cage culture chicken house comprises a fermentation tank (1) filled with fermenting bed materials, where the fermentation tank (1) which is rectangular is arranged on the right lower side of the chicken cage, the opening edge of the fermentation tank (1) is equipped with a travel tripper (2), two sides of the fermentation tank (1) are equipped with tracks (3), the left border end part and the right border end part at the bottom frame (2c) of the travel tripper (2) are equipped with idler wheels (5), and idler wheels (5) located on the bottom frame (2c) of the travel tripper (2) are blocked on tracks (3).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fermenting bed.    Fermentation tank (1)    Travel tripper (2)    Tracks (3)    Working table (4)    Idler wheels (5)
NOVELTY - The gasifier has a furnace (1) equipped with a cover (3), a fuel gas guide pipe (4), a speed reducer (5), a speed-reducing bracket (15), an inner purifier (6), a material-falling plate (7), an isolation plate (8), an upper duct (11), a lower arched air hole (10), a wind head (9), a wind volume distribution valve (19) and a fan (20). An outer purifying body (2) is located at outer side of the furnace. Bottom of a purifying guide pipe (17) is located under a curved purifying piece (16). An oxygen-discharging switch (12) is connected with the furnace by a guide pipe (21).    USE - Biomass energy-saving gasifier.    ADVANTAGE - The gasifier makes the biomass fuel on the material-falling plates to fall down gradually. The gasifier controls the fire layer to raise freely, saves energy ideally, increases gas yield, and can purify the gas uniformly.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of a biomass energy-saving gasifier.    Furnace (1)    Outer purifying body (2)    Cover (3)    Fuel gas guide pipe (4)    Speed reducer (5)    Inner purifier (6)    Material-falling plate (7)    Isolation plate (8)    Wind head (9)    Lower arched air hole (10)    Upper duct (11)    Oxygen-discharging switch (12)    Speed-reducing bracket (15)    Curved purifying piece (16)    Purifying guide pipe (17)    Wind volume distribution valve (19)    Fan (20)    Guide pipe (21)
NOVELTY - The furnace has an exhaust pipe (2) and an air intake pipe (3) located at a bottom part of a furnace body (1). The exhaust pipe is communicated with an application device (4) through a suction fan (12). An external part of the furnace body is fixedly linked with a filter sleeve (7). An upper end part of a sidewall of the furnace body is equipped with an air outlet (8) that is communicated with the filter sleeve. The filter sleeve is externally connected with the air discharge pipe. An upper end of a screw (9) is equipped with a rotary handle (10).    USE - Air draft type straw gasification furnace.    ADVANTAGE - The furnace has better gas production effect, good quality and high purity of gas without pollution. The furnace guarantees uniform inspiration and installs the filter sleeve for purifying the gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of an air draft type straw gasification furnace.    Furnace body (1)    Exhaust pipe (2)    Air intake pipe (3)    Application device (4)    Filter sleeve (7)    Air outlet (8)    Screw (9)    Rotary handle (10)    Suction fan (12)
NOVELTY - The furnace has an outer layer shell (6) hermetically connected and fixed with a furnace top (1). A furnace bottom (2) is arranged outside a furnace shell (3). A cavity formed between the outer layer shell and the furnace shell is a filtering inner layer whose top part is connected with inner side of the furnace. A lower part of the filtering inner layer is connected with an exhaust pipe (5). A bottom side of the filtering inner layer is connected with a drain pipe (7) communicating with outer side of the furnace. A valve (9) is positioned on the drain pipe.    USE - Straw gasification furnace.    ADVANTAGE - The furnace is simple in structure, and has less volume. The furnace requires less space to install, and is inexpensive. The furnace prevents blockage with good purification effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a straw gasification furnace.    Furnace top (1)    Furnace bottom (2)    Furnace shell (3)    Exhaust pipe (5)    Outer layer shell (6)    Drain pipe (7)    Valve (9)
NOVELTY - The device has a purifier whose upper part is provided with a gasifying pipeline that is connected to an upper part of a gasifying chamber. A lower part of the purifier is provided with a refluxing pipeline that is connected to a lower part of the gasifying chamber. A side part of the purifier is equipped with an escape pipe. Multiple transversely arranged screen baffles are provided in a cylindrical cavity of the purifier, and the gasifying chamber is provided with a wind filtering cover whose top part is provided with multiple pores.    USE - Device for cracking and gasifying a straw to produce a fuel gas in a rural area. Uses include but are not limited to boil water, cook, warm and supply heat.    ADVANTAGE - The cavity of the purifier is provided with the transversely arranged screen baffles, thus enhancing the coke removing and water removing effects. The top part of the wind filtering cover is provided with the pores, so as to enhance the gasification effect. The fuel gas produced by the device can be used for boiling water, cooking, warming and supplying heat, so the device has wide application range in the rural areas.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a straw cracking and gasifying device.
NOVELTY - The biogas purifier has a pair of barrel chambers (1) set with a desulfurizing agent feed opening (2) in an upper end, and supported by a hanger frame (7). The desulfurizing agent feed opening is sealed by a sealing cover (5). The lower ends of two barrel chambers are connected with each other through a loose joint construction segment (6) so as to form a U-shaped sulfur removal passage.    USE - Biogas purifier.    ADVANTAGE - The sulfur removal effect is enhanced, and the desulfurizing agent supplied into two barrel chambers can be replaced alternately without disassembling the biogas input pipe and biogas output pipe, so that the desulfurizing agent can be replaced conveniently in a short time. The service lifetime of the biogas purifier is prolonged.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the biogas purifier.    Barrel chamber (1)    Desulfurizing agent feed opening (2)    Biogas input pipe (3)    Biogas output pipe (4)    Sealing cover (5)    Loose joint construction segment (6)    Hanger frame (7)
NOVELTY - Control system for temperature and pressure of chemical reactor, where a reaction takes place biomass hydrothermal carbonization, comprises: (a) deposit with pressure regulation device; (b) union through the reactor tank and deposit; and (c) injection device to the reactor condensate.    USE - The control system is useful for controlling pressure and temperature of chemical reactor and in a vertical reverse-flow reactor, in which: vapors and gases build up and camp out at the top of reactor (all claimed).    ADVANTAGE - The system reduces adverse environmental impacts associated with the continuous industrial development.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a controlling method comprising: (a) pressurizing an aqueous mixture of biomass and catalyst to a pressure of at least 10 bar; (b) feeding the aqueous mixture of biomass and catalyst to a reverse-flow vertical reactor; (c) cooling the third mix of charred biomass together with at least process water in a cooling tube to values lower than its evaporation temperature atmospheric pressure; and (d) depressurizing and extract the aqueous mixture of charred biomass;    (2) a vertical reverse-flow reactor comprising a tube inside the central zone of reactor from the bottom up to 50 to 80% of the height of reactor; and    (3) a reverse-flow vertical reactor comprising a turn to the side and the underside of the tube and promotion, entry for the injection of vapor.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the control system.
NOVELTY - A processing apparatus of purified wastewaters of energy gas comprises pH control part which adjusts basic purified wastewaters, gas-liquid contact part which discharges ammonia that carried out gas-liquid contact of adjusted basic purified wastewaters to atmosphere, and ozone supply part which oxidatively decomposes cyanogen contained in purified wastewater that supplies ozone to atmosphere of gas-liquid contact part.    USE - Processing apparatus of purified wastewaters of energy gas e.g. gasified fuel and biogas fuel.    ADVANTAGE - The apparatus efficiently processes ammonia and cyanogen contained in purified wastewaters of energy gas at low cost using ammonia stripping.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of processing purified wastewaters of energy gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the processing apparatus of energy gas purified wastewater.    Column (3)    Sprinkle nozzle (5)    Distributing pipe (7)    Alkali tank (9)    Airpipe (11)
NOVELTY - The carburetor has a feed device (1) and a supply duct (5), which are brought into a carburetor body (12), and the body has a bottom (4), which ends in a central shaft (6). The body has an insulation space (11), where the feed device, the duct, the shaft and an agitator shaft (14) are guided into the space by a conveyor device (15), so that a carburetor base cover (10) holds the feed device, the duct and the shafts. A carburetor dome (17) is arranged in a carburetor space (A) such that a gap (18) i.e. annular gap, is produced between the dome and a carburetor cover (19) and/or body.    USE - Moving bed carburetor for use in machine and plant engineering, energy conversion and recovery and in an arrangement for energy conversion of carbonic waste products i.e. partially decomposed waste products, during degasification and/or gasification process.    ADVANTAGE - The carburetor dome is arranged such that the gap is generated between the dome and the carburetor cover and/or carburetor body, thus enabling complete degasification and/or gasification of solid materials, and hence sufficiently securing stability of thermal processes by counter current process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for operating a moving bed carburetor in an arrangement for the thermal decomposition of waste products and waste materials.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of a moving bed carburetor.    Carburetor space (A)    Feed device (1)    Carburetor body bottom (4)    Supply duct (5)    Central shaft (6)    Carburetor base cover (10)    Insulation space (11)    Carburetor body (12)    Agitator shaft (14)    Conveyor device (15)    Carburetor dome (17)    Gap (18)    Carburetor cover (19)
NOVELTY - A raw material oil containing oxygen-containing hydrocarbon compound derived from animal and vegetable fats and sulfur-containing hydrocarbon compound is hydrogenated in presence of hydrogen, to obtain an aviation fuel base material.    USE - Manufacture of aviation fuel base material used for aircraft and jet.    ADVANTAGE - The method provides aviation fuel base material having excellent combustibility, oxidation stability, carbon neutral characteristics and durability.
NOVELTY - Method of processing algae, involves harvesting wild algae, preprocessing algal harvest to remove undesirable substances from the harvested algae, and drying the algae with exhaust gases from gas turbine generator.    USE - The method is useful for processing algae which is used in food product, animal feed, fuel e.g. ethanol or biodiesel (all claimed).    ADVANTAGE - The method does not require energy for growing algae and eliminates the undesirable environmental impacts of algal blooms in oceans.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of producing animal feed, which involves harvesting wild algae from Gulf of Mexico, drying algae with exhaust gases from gas turbine generator, milling the algae, and mixing algae with substrate to obtain animal feed.
NOVELTY - Method for operating and controlling a modifier, involves gradually increasing heating temperature of an outflow port as steam-reforming process progresses to reach the optimum temperature.    USE - Method for operating and controlling a modifier for a fuel cell system (claimed) which produces reformed hydrogen-rich gas.    ADVANTAGE - Extends the lifespan of modification catalyst.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) an apparatus for controlling and operating a modifier; a modifier; and a fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the fuel cell system. (Drawing includes non-English language texts).    Fuel cell system (100)    Liquid fuel (111A)    Modifier (141)    Burner (141A)    Oxygen-containing gas supply unit (150)    Fuel cell stack (170)
NOVELTY - The tool has powder stock support structure (40) which is installed in interior space of hopper area (21) that stores powder material (3). A guide portion (22) guides the powder material in hopper area to the cavity (11) of metal mold (10). A vibration portion (24) vibrates the tool to drop the powder material stored by structure to guide portion.    USE - Tool for filling powder material into metal mold used for manufacturing separator for fuel cell (claimed) such as phosphoric acid fuel cell, polymer electrolyte fuel cell (PEFC) and solid oxide fuel cell.    ADVANTAGE - Since the vibration portion which vibrates tool to drop powder material stored by powder stock support structure to guide portion, uniform filling of powder material with respect to the metal mold cavity can be performed easily and rapidly.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) powder material filling method; and    (2) manufacturing method of separator for fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of the tool for filling powder material.    Powder material (3)    Metal mold (10)    Cavity (11)    Hopper area (21)    Guide portion (22)    Vibration portion (24)    Powder stock support structure (40)
NOVELTY - A biomass thermal decomposition apparatus comprises combustion furnace which receives supply of char (8) and combustible gas and generates hot combustion gas, air flow layer thermal decomposition device (2) which has biomass supply port and gas supply port, thermally decomposes biomass supplied in air flow layer and produces combustible gas, tar and char, gas supply port which receives produced gas as circulating gas which is heated by hot combustion gas supplied from combustion furnace and forms air flow layer, and biomass supply port which thermally decomposes biomass (7).    USE - A biomass thermal decomposition apparatus.    ADVANTAGE - The apparatus has high yield of tar, and prevents local hot section by combustion of biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass thermal decomposition apparatus.    Fluidized bed furnace (1)    Air flow layer thermal decomposition device (2)    High temperature cyclone (3)    Biomass (7)    Char (8)
NOVELTY - Manufacture of modifier for fuel cells involves arranging greater than or equal to 2 casings (10) overlapping the collar part (15, 16) of 1st and 2nd flat saucer-shape containers (11, 12) through a partition plate (17), arranging a modification material in the casing, and laser welding the contact surfaces (21, 22) of the collar part and partition plate.    USE - Manufacture of modifier for fuel cells.    ADVANTAGE - Produces modifier with sufficient workability and stable quality.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the modifier. (Drawing includes non-English language texts).    Casings (10)    Flat saucer-shape containers (11, 12)    Collar part (15, 16)    Partition plate (17)    Contact surfaces (21, 22)
NOVELTY - The method involves forming catalyst layer (26) on the surface of electrolytic membrane (50), to laminate a gas diffusion layer (14) with the electrolytic membrane. A visually recognized alignment mark (56) is provided in the peripheral portion of opening (54) of electrolytic membrane. The cell configuration structure is positioned with respect to the electrolytic membrane based on the alignment mark.    USE - Manufacturing method of fuel cell.    ADVANTAGE - The positioning accuracy between cell configuration structures comprising fuel cell is increased by visually recognizing the alignment mark. The fuel cell is manufactured with high precision.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the production line of fuel cell.    Gas diffusion layer (14)    Catalyst layer (26)    Electrolytic membrane (50)    Opening (54)    Alignment mark (56)
NOVELTY - A co-current gasifier comprises fuel silo (14) for storing fuel to be gasified, upper floor (16a) forming the bottom of fuel silo, gasification compartment (20) beneath the upper floor for gasifying fuel, mechanism for conducting gasification air into gasification compartment, and fuel distributor (80). The upper floor has holes (30) for conducting the fuel from fuel silo to the gasification compartment (s).    USE - A co-current gasifier used for damp, air-dried pine, birch, fir or other wood chipped with bark, and biowaste.    ADVANTAGE - The device sets only little requirements on dampness or composition of fuel to be used; generates very little tar, thus providing less purification of product; has low tar content which enables burning of generated product gas in delicate devices, such as engines of vehicles; produces large amount of gas, thus improving use possibilities of gasifier in large power plants; and is functionally reliable.    DESCRIPTION OF DRAWING(S) - The drawing is a vertical cross-sectional view of co-current gasifier.    Fuel silo (14)    Upper floor (16a)    Gasification compartment (20)    Holes (30)    Fuel distributor (80)
NOVELTY - A self-contained system, for treating waste water received from at least first and second utilization apparatus, comprises at least a bioreactor, a reverse osmosis stage and an ion exchange stage, where a first stream of a first purity treated at least by the bioreactor is recycled through the first utilization apparatus and a second stream of higher purity treated at least by the bioreactor, reverse osmosis stage and ion exchange stage is recycled through the second utilization apparatus.    USE - The self-contained system is used for treating waste water received from at least first and second utilization apparatus (claimed).    ADVANTAGE - The present invention provides system for waste management, more particularly a self-contained system for treating and recycling waste water.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a bioreactor provided with means for recirculating water from it into its headspace in the form of a spray for suppressing foam in it.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the self-contained system.    Pan (1)    Wash basin (2)    Spray nozzles (3, 11, 24)    Pump (4, 5, 12, 23, 26, 44)    Membrane bioreactor (6)    Dispensing unit (7)    Sensor (8)    Water heater (9)    Mixing valve (10)    Filter (12a)    Sump (13)    Level sensors (14, 28, 29, 52)    Partition (15)    Perforation (15a)    Waste inlet pipe (16)    Air diffuser (17)    Blowers (18, 19)    Membrane pack (20)    Vent pipe (21)    Pipes (25, 31, 34, 38, 41, 42, 46, 48, 51, 57, 58)    Permeate tank (27)    Filter (32)    Corona discharge ozone generator (33)    Diffusers (35, 43)    Outlet pipe (37)    First branch (37a)    Second branch (37b)    Branch (39)    Spiral wound reverse osmosis filter (45)    Ion exchange resin filter (47)    Tank (49)    Source (50)    Vent/overflow pipes (53, 56)    Conductivity sensors (54, 55)    Pump-out valve (59)    Valves (60, 63, 64)    Fill pipe (61)    Float valve (62)
NOVELTY - A heat exchanger (108) recovers the heat from the combustion exhaust gas emitted from a combustor (104). A pump (112) pumps a liquid medium to flow through a heat path (110) for receiving the heat of the combustion exhaust gas. A heat accumulator (140) stores the recovered heat. A controller (114) supplies air from a combustion fan (106) to the combustor when combustion is not executed during stop process and operates the pump for cooling a reformer (102).    USE - Hydrogen generating apparatus of fuel cell system (claimed) such as polymer electrolytic fuel cell system and solid oxide fuel cell system for distribution type electric power generation system.    ADVANTAGE - Since the controller supplies air from the fan to the combustor when combustion is not executed during the stop process and operates the pump for cooling the reformer, the possibility of occurrence of burn in the person who is in exhaust port vicinity by the hot air discharged from the exhaust port at the time of cooling can be prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the hydrogen generating apparatus. (Drawing includes non-English language text)    Reformer (102)    Combustor (104)    Combustion fan (106)    Heat exchanger (108)    Heat path (110)    Pump (112)    Controller (114)    Heat accumulator (140)
NOVELTY - A pyrophosphoric acid containing tin, zirconium, titanium or silicon and phosphoric acid are mixed, heated at 80-160 degrees C and maintained at 200-400 degrees C, to obtain proton-conducting structure (10).    USE - Proton-conducting structure is used as solid electrolyte for fuel cell used for generating electric power (claimed) and hydrogen sensor.    ADVANTAGE - The structure has excellent proton conductivity.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of proton-conducting structure.    Proton-conducting structure (10)    Core (11)    Coating layer (12)
NOVELTY - The apparatus has a burner (102a) to heat a modifier (16), and a combustion air supply device (117) to supply combustion air to the burner. An abnormality detector (110a) detects abnormality related to fuel cell. A controller (110) controls combustion air supply device so that the cooling amount of modifier is increased more than the time of normal stop process when the abnormality related to fuel cell is detected.    USE - Hydrogen generating apparatus of fuel cell system (claimed).    ADVANTAGE - The cooling operation of the hydrogen generating apparatus can be performed appropriately according to the detection of abnormality related to fuel cell and the fall of starting property of the apparatus can be suppressed efficiently. The energy consumption can be reduced when the amount of cooling between modifier and fuel cell is increased and the maintenance operation of the apparatus can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the hydrogen generating apparatus. (Drawing includes non-English language text)    Modifier (16)    Burner (102a)    Controller (110)    Abnormality detector (110a)    Combustion air supply device (117)
NOVELTY - Producing an alcohol from a lignocellulosic biomass comprises providing lignocellulosic biomass; contacting the lignocellulosic biomass with a first enzyme composition for a first period of time to provide a first hydrolysis mixture; thickening the first hydrolysis mixture to form a second hydrolysis mixture; hydrolyzing the second hydrolysis mixture for a second period of time to provide a fermentable sugar mixture; and fermenting the fermentable sugar mixture to provide an alcohol.    USE - Method for producing an alcohol used in a fuel mixture comprising ethanol and gasoline (claimed).    ADVANTAGE - The method can efficiently hydrolyze lignocellulosic materials at higher fiber concentrations (e.g. greater than 10% K); and can provide higher concentration glucose solutions, resulting in capital and operating savings in alcohol production plants.
NOVELTY - Purifying biodiesel, comprises reacting a crude biodiesel with an adsorbent comprising at least one aluminum oxide containing component having an aluminum content, calculated as aluminum oxide, of more than 40 wt.%; and separating a purified biodiesel from the adsorbent.    USE - The method is useful for purifying biodiesel.    ADVANTAGE - The method is more efficient in removing the impurities from the crude biodiesel. The adsorbent used in the method: removes impurities efficiently at lower concentration; can be introduced in any form e.g. powder or granule; and has high surface area and high pore volume, thus exhibits high adsorption capacity and is suitable for the industrial application.
NOVELTY - The method involves operating a recirculation conveying equipment (7) i.e. blower, during a switching-off process that is started after switching off a fuel cell system (1) when a safety valve is temporarily open. An electrical heater (9) is provided in an area of the recirculation conveying equipment to heat the recirculation conveying equipment in critical phases during the switching-off process and/or a starting process of the fuel cell system. Hot lubricant of the fuel cell system flows through the electrical heater.    USE - Method for operating a fuel cell system i.e. proton exchange membrane (PEM) fuel cell system, in a vehicle (claimed) i.e. motor vehicle. Uses include but are not limited to a trackless land vehicle, rail-bound land vehicle, ship and aircraft.    ADVANTAGE - The electrical heater is provided in the area of the recirculation conveying equipment to heat the conveying equipment during the switching-off process and/or the starting process of the fuel cell system, thus ensuring the switching-off process without additional structural measures and rapid restart of the fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a fuel cell system with associated components.    Fuel cell system (1)    Fuel cell (2)    Cathode region (3)    Anode region (4)    Recirculation conveying equipment (7)    Electrical heater (9)
NOVELTY - Igniter comprises a wax containing combustible carrier material (1). The carrier material is coated with the wax.    USE - The igniter is useful for igniting solid combustible materials e.g. wood, charcoal or coal, preferably in tiled stoves, chimneys and barbecue grills (claimed).    ADVANTAGE - The igniter provides fast and safe ignition of the fire and only the surface of the carrier material is uniformly coated with the wax and not completely filled by the wax and thus the igniter is cost effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing an igniter comprising twisting the carrier material to rope-like structure and spraying with liquid wax, preferably paraffin.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of the igniter in the form of a rope like carrier material with the twisted fibers of wood wool.    Carrier material (1)    Fibers (2)
NOVELTY - The hydrogen generating system (11) has a housing (13) with a reservoir (25) storing an electrolyte solution. An electrode plate assembly with cathode, anode and neutral plates are partially submerged in the reservoir. The anode plate is arranged in spaced relationship with the cathode plate. The neutral plates are arranged in the spaced relationship between the cathode and anode plates. A power source is electrically connected with the electrode plate.    USE - Electrolytic hydrogen generating system mounted on vehicle such as truck and diesel tractor of tractor-trailer combination.    ADVANTAGE - The power supplied to the system is efficiently used and a sufficient supply of gas is generated at low temperatures, since the neutral plates are arranged in the spaced relationship between the cathode and anode plates. Thus, the amperage level of the system can be controlled. The generation of hydrogen and oxygen available at start-up is increased and the usual warm-up period required for the system to full production at optimum temperature is reduced.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for controlling hydrogen generating system;    (2) computer readable medium storing program for controlling hydrogen generating system; and    (3) method for dynamically adding or removing quantity of active plates in electrode plate assembly of hydrogen generating system.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the hydrogen generating system.    Hydrogen generating system (11)    Housing (13)    Reservoir (25)    Panel (43)    Lid (83)
NOVELTY - A solid heterogeneous transesterification catalyst composition comprises calcined calcium carbonate mixture containing (in weight% with respect to total weight of mixture) calcium carbonate (70-95) having mean crystal size of 350-500 Angstrom , calcium oxide (5-25) having mean crystal size of 50-300 Angstrom and calcium hydroxide (5-25) having mean crystal size of 110-300 Angstrom .    USE - Solid heterogeneous transesterification catalyst composition is used for manufacturing fatty-acid ester (claimed) for producing biodiesel used as fuel in diesel engine.    ADVANTAGE - The solid heterogeneous transesterification catalyst composition is continuously manufactured without potentially harming the production equipment. The fatty-acid ester is economically manufactured using the catalyst composition.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of solid heterogeneous transesterification catalyst composition, which involves calcining limestone material containing calcium carbonate (95% or more) at 600 degrees C or more under air for 2 hours or less. The calcination is not performed under inert gas; and    (2) manufacture of ester of fatty acid and glycerin, which involves contacting reaction mixture (a) containing triglyceride and aliphatic alcohol with the solid heterogeneous transesterification catalyst composition. The reaction mixture (a) reacts to form a product containing aliphatic alcohol, biodiesel and glycerol.
NOVELTY - Processing gas containing methane and higher hydrocarbons, comprises partially condensing and expanding gas from a pressure of 70-120 bars to 20-35 bars to obtain at least a 1C fraction (3) and a 2C+ fraction (4), separating the 2C+ fraction from the 1C fraction, and separating the 1C fraction into a first fraction, which is brought to a pressure of 20-40 bars and a second fraction, which is brought to a pressure of 50-70 bars.    USE - The method is useful for processing gas containing methane and higher hydrocarbons, where the gas is natural gas (claimed) e.g. refinery streams.    ADVANTAGE - The method is flexible, and allows efficient processing of natural gas into individual stream for further processing along different paths.    DESCRIPTION OF DRAWING(S) - The figure shows a flow chart for processing gas containing methane and higher hydrocarbons.    Gas stream (1)    Separator (2)    1C Fraction (3)    2C+ Fraction (4)    Splitter (12)
NOVELTY - Reversed lid of inlet of methane pond comprises pinch plate (1), screw (2), fixing rod (3) and nut (4). The edge of the pinch plate (1) is set with the step (5) with the shape matching the inner wall of the connecting part of the inlet (6) and the sealing head (7).    USE - The reverse lid is useful for air- and leak-proofing methane pond.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the reversed lid.    Pinch plate (1)    Screw (2)    Fixing rod (3)    Nut (4)    Step (5)    Inlet (6)    Sealing head (7)
NOVELTY - The method involves supplying water from a water supply source to a steam chamber (30) arranged adjacent to an exhaust conduit (32) of an internal combustion engine (12). Heat from the conduit is conducted to the chamber to produce steam. The steam is flown to a catalytic converter (20). The steam is converted to hydrogen and oxygen, and the hydrogen and the oxygen are flown to an intake port of the engine. The hydrogen and the oxygen are converted to the steam in a combustion process. The steam is recycled to the converter.    USE - Method for supplying gasoline, hydrogen and oxygen fuel for hydrocarbon and water hybrid engine to power a land vehicle.    ADVANTAGE - The method utilizes oxides of elements to be oxidized with the steam and to be reducible back to an original state without requiring a chemical reducing agent, and efficiently produces oxygen gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a hydrocarbon and water hybrid engine.    Hydrocarbon and water hybrid engine (10)    Internal combustion engine (12)    Catalytic converter (20)    Substrate element (22)    Steam chamber (30)    Exhaust conduit (32)    Exhaust conduit (44)
NOVELTY - The device has a shell, central shaft and impellers, where the shell has an import and an export that are distributed axially at sides of the shell. The import is connected with an input tube of fluid. The export is connected with an output tube of the fluid. A central shaft is axially provided in a center of the shell, where the impellers are provided on the central shaft. A thread pitches among the impellers and is gradually reduced along an export direction, where the impellers are unidirectional screw impellers.    USE - Fluid refining device for oxygenizing waste water and sewage, purifying a waste water system, desulfurizing fuel gas, refining of beverage, cosmetic, dope and refinement, and for oxygenizing and fermenting industrial material. Can also be used for refining gas or mixture of liquid and gas.    ADVANTAGE - The design of the device is simple, reduces volume and cost of the device and enables the device to be used in a convenient manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a fluid refining device.
NOVELTY - Agrochemical composition (C1) with biogenic component comprises active components I and II (0.1-60 wt.%), conducting agent, cosolvent, and solvent. The active component I is abamectin; and active component II is dicofol, pyridaben, propargite, or hexythiazox.    USE - Composition (C1) prepared into static oil (claimed) used for preventing and treating red spider of cotton.    ADVANTAGE - The static oil has convenient processing, low cost, long-lasting effect, high work efficiency, capability of reducing environment pollution, improved utilization ratio, and reduced usage amount of active components.
NOVELTY - Compositing is performed by extracting bacteria groups in dominant position from living garbage in high-temperature period of secondary fermenting section; and culturing and introducing to obtain compound bacteria; in the secondary fermenting period, inoculating compound bacteria by inoculating amount of 1-5%, in which the high-temperature period of the secondary fermenting section is brought forward for 5-15 hours and the high temperature lasting time is prolonged to 15-31 hours.    USE - Compositing for inoculating compound bacteria in secondary fermenting section.    ADVANTAGE - The method shortens the time of secondary fermenting and compositing to 4-10 days and improves production efficiency of the compost.
NOVELTY - A furnace comprises a gear chamber, a furnace body, a material transferring pipe, and a material transferring piston. A motor, an air extractor, a regenerated fuel gas storing chamber and a residue discharging pipe are also installed in the garbage cracking furnace. The gear chamber is provided on lower part of the furnace body, where the gear chamber comprises a gear motor, a drive gear and a drive gear shaft.    USE - Furnace for treating garbage.    ADVANTAGE - The furnace ensures high efficiency and energy conservation and can be recover regenerated fuel gas in an eco-friendly manner.
NOVELTY - A methanol gasoline compound additive comprises (parts volume) solvent (30-70), combustion accelerant (10-20), steam inhibitor (2-10), cleaning dispersant (10-20) and surfactant (5-10). The solvent is n-hexane, tert-butanol, acetone or ethyl acetate.    USE - A methanol gasoline compound additive.    ADVANTAGE - The additive has good stability, can be stored conveniently, does not have phase separation; does not produce precipitate after long time storage or storing at low temperature; and has low production cost.    DETAILED DESCRIPTION - A methanol gasoline compound additive comprises (parts volume) solvent (30-70), combustion accelerant (10-20), steam inhibitor (2-10), cleaning dispersant (10-20) and surfactant (5-10). The solvent comprises n-hexane, tert-butanol, acetone or ethyl acetate. The combustion accelerant comprises methyl lactate and ethyl tert-butyl ether. The steam inhibitor is ethyl formate. The cleaning dispersant comprises calcium petroleum sulfonate, magnesium stearate and magnesium isostearate. The surfactant is triglyceryl stearate, glycerin monostearate, ethyl laurate and/or benzoic acid dodecanol. An INDEPENDENT CLAIM is included for preparation of the additive comprising mixing solvent and combustion accelerant; stirring for 15-20 minutes at room temperature and normal pressure; adding cleaning dispersant and steam inhibitor; stirring for 25-30 minutes; adding surfactant; stirring the mixture at a pressure of 40-60 bar for 25-30 minutes; reducing to normal pressure; aging for 24 hours; and filtering.
NOVELTY - An in-situ biogas desulfurizing agent is iron salt comprising ferrous oxalate, ferrous chloride, ferrous sulfate, ferrous nitrate, ferrous carbonate, ferric chloride, ferric sulfate, ferric nitrate and/or ferric citrate. The weight ratio of desulfurizing agent to dry biogas fermentation raw material is 1-30:1000.    USE - An in-situ biogas desulfurizing agent in solid or liquid form, for use in biogas fermentation device in biogas tanks for large-, middle- or small-sized engineering and domestic use, to simultaneously desulfurize and ferment raw material comprising animal feces, straws, highly concentrated industrial and agricultural organic wastewater and organic wastes, where total solid content is not greater than 35% (claimed).    ADVANTAGE - The desulfurizing agent has adequate raw material, greatly enhanced desulfurization rate, convenient operation and low running cost; provides cost saving of desulfurizing device; is directly added into fermentation device to desulfurize in-situ biogas; and solves the problems including short utilization period, frequent replacement, and inconvenient use of agent.
NOVELTY - An environment-friendly cured coal is prepared by mixing materials comprising (wt.%) straws (70-80), powdered coal (18-28), yellow clay (1.20-1.50), slaked lime (0.30-0.60) and aluminum oxide (0.15-0.20), and uniformly blending to obtain mixture; adding water into mixture so that water content reaches 14-18%; and blending and pressing to obtain product.    USE - An environment-friendly cured coal used as fuel for industrial and domestic applications, flue-cured tobacco and biomass power generation.    ADVANTAGE - The fuel fully utilizes renewable resource and solves environmental pollution. When used, cured coal easily catches fire and can be fully combusted. The product has high heat efficiency and low cost; can fix sulfur and emit less dust; and solves the problem that the pure straw pressing blocks have low continuous combustion time and high combustion cost.
NOVELTY - Biodiesel is prepared from waste fat and oil having high acid values, by pretreating waste fat and oil, carrying out acid catalyze esterification reaction, then performing alkali catalyze ester exchange reaction, and carrying out post-treatment to fat and oil comprising separation and purification steps. The catalyst used in acid catalyze esterification reaction is a solid acid catalyst which uses mesoporous molecular sieve SBA-15 as carrier. The catalyst used in alkali catalyze ester exchange reaction is solid alkali catalyst prepared by using oyster shell as raw material.    USE - Method of preparing biodiesel from waste fat and oil having high acid values (claimed).    ADVANTAGE - The catalysts used in the method have better stability, and can be used repeatedly. The method reduces pollutant in the environment by utilizing waste fat and oil.    DETAILED DESCRIPTION - Biodiesel is prepared from waste fat and oil having high acid values, by pretreating waste fat and oil, carrying out acid catalyze esterification reaction, then performing alkali catalyze ester exchange reaction, and carrying out post-treatment to fat and oil comprising separation and purification steps. The catalyst used in acid catalyze esterification reaction is a solid acid catalyst which uses mesoporous molecular sieve SBA-15 as carrier, and is prepared by carrying out phosphotungstic acid, phosphomolybdic acid or sulfonic acid group modification. The catalyst used in alkali catalyze ester exchange reaction is solid alkali catalyst prepared by using oyster shell as raw material.
NOVELTY - Ethyl ester biodiesel is prepared from cotton seed oil by mixing cotton seed oil and absolute ethyl alcohol, performing ester exchange reaction with ethyl alcohol at 60-78 degrees C for 1-1.5 hours in the presence of tetrahydrofuran as cosolvent and potassium hydroxide as catalyst, and performing separation process. The weight ratio of cotton seed oil to tetrahydrofuran is 1:0.75-1. The amount of potassium hydroxide used is 1-1.25% of the weight of the cotton seed oil.    USE - Method of preparing ethyl ester biodiesel from cotton seed oil (claimed).    ADVANTAGE - The cosolvent used in the process changes ester exchange from heterogeneous reaction to homogeneous reaction. The method has fast reaction, and has increased production rate of biodiesel, i.e. 94-98% production rate. The tetrahydrofuran and ethanol used in the process can be recycled.
NOVELTY - Chlorella sorokiniana CS-01 has a preservation number CCTCC M209220, and is new.    USE - Chlorella sorokiniana CS-01 for manufacturing grease (claimed) and biodiesel.    ADVANTAGE - The Chlorella sorokiniana CS-01 has strong environmental suitability, fast growth rate and high grease yield, and is also cultured on a large scale as the material for manufacturing biodiesel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for culturing Chlorella sorokiniana for producing grease, which involves:    (A) selecting individual algae and subjecting to sterilized culturing liquid for index culturing;    (B) inoculating the strain after index culture to BG11 sterilized culture liquid, where the final inoculation concentration is 1x 106-3x 106 pieces per ml;    (C) culturing the strain at a temperature of 25-35 degrees C, where the pH value of the culture medium at 6-10;    (D) adding ethylenediaminetetraacetic acid (EDTA-Fe (III)) having concentration of 1x 10-5-1x 10-3 moles per l at a temperature of 25-35 degrees C and a pH of 6-11;    (E) culturing the mixture for 18-22 days in aerobic conditions and for 28-32 days in anaerobic conditions at a luminous intensity of 6600-10000 Lux and lighting ratio of 14:10;    (F) centrifuging and separating the obtained algae solution; and    (G) freezing and drying the obtained algae mud to extract grease.
NOVELTY - A Bacillus sp. E2-Y preserved in the China center for type culture collection in Wuhan University, Wuhan, China, 430072 with the preservation number is CCTCC No: M 209150 and preservation date is July 15, 2009, is new.    USE - The Bacillus sp.E2-Y is useful for degrading environmental estrogen pollutants and 17beta-estradiol (all claimed).    ADVANTAGE - The specie is extracted from wastewater treatment unit, and it is a dominant strain in the wastewater treatment system. It can be applied to complicated physical condition, and the application prospect is wide.
NOVELTY - Volatile fatty acid production involves taking mixed sludge, which is composed of excess sludge from sewage treatment plant as raw material. Sodium hydroxide is added to the sludge mixture in a mass ratio of 1:0.01-0.3 and is stirred. The sludge mixture is heated at 26-90 degrees C for 5-120 minutes and is naturally cooled to room temperature, and the pH is regulated to neutral with hydrochloric acid. Anaerobic sludge is taken as inoculum, and is stirred under anaerobic condition to carry out anaerobic fermentation for 36-84 hours to obtain volatile fatty acid.    USE - Method for producing volatile fatty acid (claimed).    ADVANTAGE - The volatile fatty acid production method reduces environmental pollution caused by organic material present in the sludge, is cost-effective as it uses a circulating economy mode of the urban sewage treatment plant and reduces investment and operation cost, greatly improves the speed for hydrolyzing and acidifying sludge, cumulates the volatile fatty acid in a short time, greatly improves the hydrolysis speed of sludge, and shortens time of anaerobic fermentation of the sludge.
NOVELTY - The pressure adjustable hydrogen generator has a control module (5) that calculates the current demanded hydrogen producing voltage and sends it to a switch power module (1). The switch power module generates corresponding electrolysis current according to the hydrogen producing voltage signal. A pressure measuring device (4) detects the hydrogen output pressure of a gas storage device (3). The hydrogen output pressure is converted into electric signal and sent out to the control module.    USE - Pressure adjustable hydrogen generator.    ADVANTAGE - Ensures high control precision, convenient operation and stable electrolysis and limiting current to protect electrolysis film from being burnt.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a pressure adjustable hydrogen generator adjusting method.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of a pressure adjustable hydrogen generator. (Drawing includes non-English text).    Switch power module (1)    Electrolysis module (2)    Gas storage device (3)    Pressure measuring device (4)    Control module (5)
NOVELTY - The device has signal transmitters (1) arranged row by row at intervals. A carbon monoxide concentration sensor (a), oxygen concentration sensor (b), a methane concentration sensor (c) and a temperature sensor (d) are connected with a single chip computer (4) by an analogue to digital converter (3). A wireless transceiver module (6) is connected with the single chip computer. Another single chip computer (5) is connected with a display module (7), a 485 communication interface (9) and a functional key (10).    USE - Wireless monitoring device for coal spontaneous combustion of a mined-out space.    ADVANTAGE - The device is equipped with a portable receiver that is connected with an underground sub station by the 485 interface, so that the parameter of the mined-out space can be monitored in a real time by the underground monitor network. The device is simple in structure and easy to operate, and reduces consumption of energy with high measuring precision.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a wireless monitor method for coal spontaneous combustion of mined-out space.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a wireless monitoring device.    Carbon monoxide concentration sensor (a)    Oxygen concentration sensor (b)    Methane concentration sensor (c)    Temperature sensor (d)    Signal transmitters (1)    Analogue to digital converter (3)    Single chip computers (4, 5)    Wireless transceiver module (6)    Display module (7)    485 communication interface (9)    Functional key (10)
NOVELTY - The hearth (19) of fuel producer (1) is big in upper part and small in lower part. A round humectation tube (23) is set in the center of the hearth in a retardant coating (18) disposed around the hearth. One side of the humectation tube is along the upside of the retardant coating and contacts a fuel way (21), while the other side extends along the outside of the hearth to a first cleaning cartridge (8) provided in tandem with a second cleaning cartridge (8'). Each cartridge has a clean room (27,27') in which a purifying net (30,30') and a cleaning net (29,29') are set in different levels.    USE - Fuel and stalk burning producer, e.g., fuel gas stove for family use for, e.g., bath, warming.    ADVANTAGE - Provides structure that improves fuel quality and provides blue flame, high flame current, and vigorous fire power.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the fuel and stalk burning producer.    Fuel producer (1)    First cleaning cartridge (8)    Second cleaning cartridge (8')    Retardant coating (18)    Hearth (19)    Fuel way (21)    Humectation tube (23)    Clean room (27,27')    Cleaning net (29,29')    Purifying net (30,30')
NOVELTY - The device has a retort (1) arranged with a cylinder body and a cover. A discharge hole is formed at a bottom part of the cylinder body. A frame (4) is arranged with a supporting bracket (10) and a ladder (11). A high speed churn-dasher (2) is placed with a motor and a beater. A service platform (3) with a stop hole (12) is formed at a top part of the frame. A programmable logic control system (5) is arranged with a microcomputer and a touch display screen for connecting a solenoid pilot actuated valve (18) and a motor.    USE - Biodiesel producing device.    ADVANTAGE - The control device connects the solenoid pilot actuated valve and the motor to control working operation. The device is simple and reliable. The device has high automatic working level, and the retort can be fixed at a service platform of one frame. The device reduces working intensity of a worker, and utilizes the equipment fully to increase working efficiency. The device utilizes seed fat and animal oil to produce biodiesel.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biodiesel producing device. .    Retort (1)    High speed churn-dasher (2)    Service platform (3)    Frame (4)    Programmable logic control system (5)    Supporting bracket (10)    Ladder (11)    Stop hole (12)    Solenoid pilot actuated valve (18)
NOVELTY - A solar-powered oxyhydrogen production equipment has oxyhydrogen machine with electrolytic bath that holds electrolyte, electrode boards distantly set in electrolytic bath, and aperture formed over the electrolytic bath and connects with electrolytic bath; and solar dynamotor that converts sunlight into electrical energy to supply electric power to the electrode board of oxyhydrogen machine so that each electrode board electrolyzes the electrolyte and produces hydrogen and oxygen.    USE - Solar-powered oxyhydrogen production equipment for generating and supplying hydrogen and oxygen to equipment.    ADVANTAGE - Decreases amount of electric consumption in cities and ensures saving energy based on the needs of protecting environment since solar dynamotor converts sunlight into electrical energy and generates auxiliary electric power to meet the needs for supplying power to the oxyhydrogen machine that produces hydrogen and oxygen for subsequent equipment.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic perspective view of the solar-powered oxyhydrogen production equipment.
NOVELTY - Inside a shell (1) of a gasifier section are a blender (2) and an air pre-heating pipe (6). At the lower part of the shell are a flow-leading unit (3) and a multi-grade oxygen-supplying equipment (4). Outside the shell is a water circulating cover (5). An air pre-heating pipe (6) is connected to a heat exchanger (8). A depurative temperature-adjusting equipment includes a depurating equipment (7) that is connected to the gasifier section and includes the heat exchanger which is connected to a heating appliance (10) through a valve (9).    USE - Late-model biomass gasifier for generating combustible gas using biomass.    ADVANTAGE - Enables use of straw or ruderals while eliminating need for fermenting. Provides simple structure that provides convenience and high production quality. Provides adequate combustion under high temperature, thus enabling use in countryside.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the late-model biomass gasifier.    Shell (1)    Blender (2)    Flow-leading unit (3)    Multi-grade oxygen-supplying equipment (4)    Water circulating cover (5)    Air pre-heating pipe (6)    Depurating equipment (7)    Heat exchanger (8)    Valve (9)    Heating appliance (10)
NOVELTY - The furnace has an airproof furnace portion (16) without grate, and an airproof charge compactor installed on top of the furnace portion. A fuel gas hood (8) is installed on the condenser (21) of the furnace. A gas combustor (6) is installed in the lumen of the fuel gas hood, and is connected by a pipe to a combustor (4). The gas combustor is connected to the blast pipe of the fan. An inlet opening is formed on the outer wall of the fuel gas hood. The combustor is connected to the discharge pipe on top of the fuel gas hood. An outlet discharge pipe (5) is provided on the combustor.    USE - Combustion and heating furnace for use in the countryside and towns to burn e.g. straws.    ADVANTAGE - Provides a new combustion and heating furnace that efficiently burns e.g. straws, has improved thermal efficiency, ensures reduced environment pollution, and is convenient to use. Ensures that the combustion and heating furnace is airproof due to the use of an airproof furnace without grate, and installed airproof charge compactor on top of the furnace.    DETAILED DESCRIPTION - A fan and ash hole cover (20) is provided below of the furnace portion. A fuel gas pipe is installed to connect on the upper side of the furnace portion. The inlet portion of the condenser is connected to the fuel gas pipe of the fuel combustion furnace portion, while the outlet portion of the condenser is arranged downwardly to connect with a dust collecting box (1). The top portion of the condenser is connected to the gas combustor.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic illustration of the combustion and heating furnace.    Dust collecting box (1)    Combustor (4)    Outlet discharge pipe (5)    Gas combustor (6)    Fuel gas hood (8)    Airproof furnace portion (16)    Fan and ash hole cover (20)    Condenser (21)
NOVELTY - The cartridge has an active carbon filter located in an inner ring of a water cooler, and a cyclone dust removal cavity formed in a space between the water cooler and the active carbon filter. A watertight part is formed on a lower part of the water cooler. An escape pipe is located on an upper side of cyclone dust removal cavity that is located far away an inlet branch part. A lower part of the active carbon filter is provided in screen stencil. A cyclone dust removal cavity extended part is extended along a lower part of the inner ring of the water cooler to a lower part of watertight part.    USE - Whirlwind, water-cool, filter cleaning cartridge for straw gasification furnace.    ADVANTAGE - The water cooling effect and impurity i.e. tar, cleaning effect are improved. The peculiar smell can be prevented when the gas is kindled. The gas combustion is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a whirlwind, water-cool, filter cleaning cartridge.
NOVELTY - The furnace has a connecting pipe (8) that is connected with the air reservoir (10). A fixed vent pipe (9) with a vent valve is provided in the middle of air reservoir (10). The top vent-pipe with the vent valve is connected through a tee joint (11) with the connecting pipe. A right gas switch (13) is provided with a fixed special cooker( 14) to which a drain elbow (12) extends. The bottom tee joint with the connecting pipe is connected with the air reservoir (10).    USE - Firewood gasification furnace.    ADVANTAGE - Obtains simple structure, can be used conveniently and has high combustion efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the firewood gasification furnace.    Connecting pipe (8)    Fixed vent pipe (9)    Air reservoir (10)    Drain elbow (12)    Right gas switch (13)    Fixed special cooker (14)
NOVELTY - The boil-off boiler (8) has grates (12) and a dust exit (7) that are set below. The boiler, through the ignition room (6), links with the secondary burning furnace. An inlet pipe (21) is set in the ignition boiler. The equipment (17) for interchanging heat and the hot water pipe are set in the secondary burning furnace. The equipment for interchanging heat connects with the water cover of the boiler. Multiple smoke pipes (10) are set in the equipment. The hot water pipe is set around the boiler and links with the water cover of the boiler.    USE - Boil-off boiler for biomass.    ADVANTAGE - Burns directly without cooling to make less tar. Makes the boil-off room generate carbon monoxide which enters the secondary burning furnace to burn completely after ignition to advance the heat efficiency and save energy. Dust sinks to the bottom of the boiler to decrease pollution through the secondary burning boiler to be departed.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory internal view of the boil-off boiler.    Ignition room (6)    Dust exit (7)    Boil-off boiler (8)    Smoke pipes (10)    Grates (12)    Equipment (17)    Inlet pipe (21)
NOVELTY - The process involves cooling and cleaning a fraction of a raw syngas stream (224), and subjecting the remaining fraction of the raw syngas stream to a shift reaction. The cleaned fraction and the remained fraction of stream are combined to yield a clean syngas flow having specific hydrogen to carbon monoxide gas ratio. Excess syngas is generated, and a primary stream of syngas with non-optimal hydrogen to carbon monoxide ratio is supplied to the chemical process unit. A remaining secondary syngas stream is directed to a hydrogen recovery unit.    USE - Process for manufacturing a syngas stream created by gasification, steam methane reforming (SMR) or high temperature process in field power plants to produce chemicals and fuels.    ADVANTAGE - The process enables providing fuel having high hydrogen content to power island, thus producing fewer carbon-dioxide emissions. The process enables improving production efficiency of products such as electricity and fuels.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic illustration of a process for manufacturing a syngas stream.    Feedstock (220)    Raw syngas stream (224)    Syngas cooler (226)    Boiler feedwater (280)    Steam (290)
NOVELTY - Pressure automatic deslagging marsh gas tank comprises main body (3) which is a horizontal rectangular structure made from reinforced concrete.    USE - The tank is useful for industrial and commercial applications.    ADVANTAGE - The bottom of the marsh gas tank is slope shaped, which makes the slags inclined to flow forwards, thus forming up a dynamic flow process. Two openings are made on the lower part of both the feeding end and the deslagging end. This ensures the gas in the tank to be sealed and makes it convenient for feeding and deslagging. The feeding and deslagging operations can be made continuously, and the flow process of it is stable. It also has a high density of feeding.    DETAILED DESCRIPTION - Pressure automatic deslagging marsh gas tank comprises main body (3) which is a horizontal rectangular structure made from reinforced concrete. One end of the marsh gas tank is connected with the pressure feeding tank (1), and the other is connected with the slag tank (7). The bottom of the marsh gas tank is sloped shaped from the feeding end to the deslagging end. The grade of slope is 1:3-5. The feeding end of the tank is opened with a feeding port (2). The lower opening (6) of the feeding end is connected with the slag tank, which is linked up to the deslagging tank (9). There is a marsh gas outlet (5) on the upper part of the marsh gas tank, and it is connected to the gas storage device by pipelines. A temperature measuring device is set inside the marsh gas tank. Some heat preserving materials are coated over the rim of the marsh gas tank, the top and bottom of which have heat preserving layers.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the marsh gas tank.    Feeding tank (1)    Feeding port (2)    Main body (3)    Marsh gas outlet (5)    Lower opening (6)    Slag tank (7)    Deslagging tank (9)
NOVELTY - The method involves introducing a part of an absorbent solution charged with acidic compounds in a regeneration zone (Z1) to produce a partially regenerated absorbent solution. A part of the partially regenerated absorbent solution is taken from the zone and is separated into a fraction with enriched acidic compounds and a fraction with low acidic compounds. The fraction with enriched acidic compounds is introduced into another regeneration zone (Z2) to produce a regenerated absorbent solution. The fraction with low acidic compounds and the regenerated absorbent solution are recycled.    USE - Method for deacidification of a gaseous effluent such as natural gas, synthesis gas, combustion fume, refinery gas, Claus gas and biomass fermentation gas (all claimed), by absorbent solution.    ADVANTAGE - The method enables removing the acidic compounds such carbon dioxide (C02) and the hydrogen sulfide (H2S) contained in the gaseous effluent. The method separates the absorbent solution in two fractions in order to evacuate a portion of the absorbent solution with low acidic compounds during regeneration, thus reducing the flow rate of absorbent solution, and decreasing the energy necessary to carry out regeneration.    DETAILED DESCRIPTION - The absorbent solution comprises a reactive compound selected from a group consisting of amine, alkanolamine, polyamine, amino acid, alkaline amino acid salt, amide, urea, phosphate, carbonate and alkali metal borate. The acidic compounds comprise formic acid, oxalic acid, acetic acid and propionic acid.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a process of deacidification of a gaseous effluent.    Separation balloon (B1)    Absorption column (C1, C2)    Heat exchanger (E1-E3)    Reboiler (R1)    Regeneration zones (Z1, Z2)
NOVELTY - Metal particles (5) comprises one or more elements comprising group IIIA-VIIB of the periodic table of elements and their mixtures, carrying hydrophobic groups on their surface.    USE - The metal particles are useful for the hydrolysis reaction of a chemical hydride into hydrogen (claimed).    ADVANTAGE - The composition avoids the adhesion of borate on the catalyst surface during the hydrolysis reaction thus provides a good hydrophobic surface, prevents the system crash in the cooling reactor, and allows the hydrolysis reaction of a chemical hydride into hydrogen with very high concentrations of chemical hydrides without additional catalysts.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparing metal particles, where a surface treatment intended to make the hydrophobic catalyst is carried out by plasma-enhanced chemical vapor deposition;    (2) a reaction chamber (1) for implementation of a hydrolysis reaction of a chemical hydride into hydrogen, where the reaction chamber comprises the metal particles; and    (3) fuel cell comprising the reaction chamber.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a reaction chamber.    Reaction chamber (1)    Walls (2)    Ends (3, 4)    Metal particles. (5)
NOVELTY - An organic framework comprises plate-shaped layers (1) formed by successively connecting building blocks arranged in the vicinity of each other. Each building block is formed through a covalent bonding of 2 or 3 6-204C aromatic ring groups to a linear or cyclic boron-containing cluster. A Lewis base (2) is coordinate-covalent-bonded to the boron-containing clusters in the plate-shaped layers.    USE - Organic framework is used for adsorption and desorption of gases, sensors, drying agents, ion-exchange materials, molecule recognizers, materials used for chromatography, molecular selective emitters and absorbers, molecular sieves, nanotubes, nanoreactors, adsorbents used for storing ammonia, carbon dioxide, carbon monoxide, hydrogen, amines, methane, oxygen, argon, and nitrogen, and catalysts (all claimed).    ADVANTAGE - The organic framework enables adsorption of large amount of hydrogen between pores and layers, as the distance between plate-shaped layers is broadened due to covalent bonding of Lewis base.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the organic framework.    Plate-shaped layer (1)    Lewis base (2)
NOVELTY - Producing esters comprises: fermenting a fermentable carbon source in the presence of an organic acid producing microorganism to produce fermentation output comprising an organic acid; extracting the organic acid into an extractant; and esterifying the organic acid in the extractant in the presence of a catalyst and alcohol to produce an organic ester.    USE - The method is useful for producing esters, preferably butyrate ester (claimed), which is useful as a biofuel.    ADVANTAGE - The method significantly improves fermentation rate, reactor productivity and final product concentration by reducing end-product inhibition, thus reducing downstream processing load and recovery costs. The method provides higher product yield with higher purity than batch fermentation. The method reduces the product cost to a competitive level for commercial application, thus benefiting the bio-based industry by providing a viable avenue for better byproduct utilization and high-value products suitable for various markets. The method economically converts fermentation produced butyric acid and ethanol to ethyl butyrate ester.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method of producing esters comprising: fermenting a fermentable carbon source in the presence of an organic acid producing microorganism to produce fermentation output comprising an organic acid; extracting the organic acid into an organic solvent; stripping the organic acid from the organic solvent; and esterifying the organic acid in the presence of a catalyst and alcohol to produce an organic ester.
NOVELTY - A hydrogen generation system has a water-electrolyzing hydrogen production device, a hydrogen storing tank, a hydrogen compressor, and a hydrogen steel container that are orderly connected with each other. The water-electrolyzing hydrogen production device is solid polymer electrolyte (SPE) device for producing hydrogen by electrolyzing purified water.    USE - Hydrogen generation system for producing hydrogen by electrolyzing purified water and storing hydrogen.    ADVANTAGE - Provides hydrogen generation system with simple structure, no corrosion and danger, small occupied space and is easy to operate since water-electrolyzing hydrogen production device, hydrogen storing tank, hydrogen compressor, and hydrogen steel container are orderly connected with each other.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the hydrogen generation system. (Drawing includes non-English language text).
NOVELTY - Wastes and combustible wastes are separated. The combustible wastes are thermally decomposed into gasification synthesis gas. The synthesis gas is purified to obtain (in vol.%) hydrogen (20-30), carbon monoxide (25-40), and methane (5-10).    USE - Transformation of combustible wastes into energy fuel used for generating power in power plants including micro gas turbines, gas engines, and gas turbines.    ADVANTAGE - The method enables production of energy fuel having excellent power generating efficiency, by effectively using combustible waste.
NOVELTY - The heat generating structure (100) has a porous composite element (110) made of material containing silicon carbide and silicone. An electrode (120) is provided in the composite element, such that when electric current is supplied between the electrodes, the composite element generates heat for heating the substances such as particles, fluid in the surroundings of composite element.    USE - Heat generating structure for exhaust purification device of internal combustion engine, and fuel reformer (both claimed).    ADVANTAGE - The heat generating structure of simple structure excellent in energy saving property improves thermal efficiency and removes particulate matter in the exhaust gas efficiently. The clogging of particulate filter can be suppressed without increasing size of exhaust purification apparatus.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) exhaust purification device of internal combustion engine; and    (2) fuel reformer.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the heat generating structure.    Heat generating structure (100)    Porous composite element (110)    Electrode (120)    Connection board (121)    Rod-shaped terminal (122)
NOVELTY - A microecologic preparation comprises (in parts weight) solid photosynthetic bacteria preparation (13-17), solid Bacillus subtilis preparation (12.5-16.5), solid brewing Saccharomyces cerevisiae preparation (10.5-13.3), solid denitrification bacteria preparation (33-37) and microorganic flocculating agent (0.3-0.7).    USE - Microecologic preparation is used for purifying water and accelerating growth of aquiculture animals (claimed).    ADVANTAGE - The microecologic preparation is economical, and increases transparency and dissolved oxygen of water. The microecologic preparation effectively reduces bait coefficient and the content of organic pollutants and harmful substance e.g. nitrite, sulfide, nitrogen and phosphorus in water, and rapidly optimize culture environment. The microecologic preparation enhances the disease-resistant ability of cultured fishes and accelerates the growth of cultured animals.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of microecologic preparation, which involves mixing solid photosynthetic bacteria preparation, solid Bacillus subtilis preparation, brewing Saccharomyces cerevisiae preparation, and denitrification bacteria preparation with the milled organic mixture, to obtain a mixed material, pressing and granulating the mixed material, to obtain living phytoplasma bacteria columnar particles, granulating the microorganic flocculating agent by a round tray, to obtain spherical particles, mixing the living phytoplasma bacteria columnar particles and spherical particles and blending.
NOVELTY - The composition contains water, cane extracts, low-class fatty alcohol and aerosol undiluted solution which comprises a propellant. The aerosol composition is selected from the group in which propellant comprises liquefied petroleum gas and dimethyl ether. The main base of the composition is water.    USE - Composition, particularly aerosol composition for preventing the smell of hair.    ADVANTAGE - The composition contains water, cane extracts, low-class fatty alcohol and aerosol undiluted solution which comprises a propellant, where the aerosol composition is selected from the group in which propellant comprises liquefied petroleum gas and dimethyl ether, and hence effectively removes the off-flavor soaking into hair with convenient use and cost-effective manufacturing of the composition.
NOVELTY - Plant biomass and waste polyester liquefaction involves putting plant biomass, polyester, catalyst and liquefier in a reaction kettle equipped with a stirrer. The liquefier is 1-4C monohydric alcohol. The reaction kettle is heated to 230-280 degrees C and pressurized to 5-8 megapascal, where temperature is maintained at this state for 5-40 minutes. The reaction kettle is cooled to 100 degrees C naturally, and then cooled to room temperature by water. The mixed reactants of reaction kettle are filtered by Buchner funnel, and obtained filtrate and residue are extracted and filtered by organic solvent.    USE - Method for liquefying plant biomass and waste polyester in presence of supercritical fluid (claimed).    ADVANTAGE - The plant biomass and waste polyester liquefaction method improves quality of biological oil and enhances utilization efficiency of the plant biomass and waste polyester.    DETAILED DESCRIPTION - Plant biomass and waste polyester are liquefied by putting plant biomass, polyester, catalyst and liquefier in a reaction kettle equipped with a stirrer. The liquefier is 1-4C monohydric alcohol. The reaction kettle is heated to 230-280 degrees C and pressurized to 5-8 megapascal, where temperature is maintained at this state for 5-40 minutes. The reaction kettle is cooled to 100 degrees C naturally, and then cooled to room temperature by water. The mixed reactants of reaction kettle are filtered by Buchner funnel, and obtained filtrate and residue are extracted and filtered by organic solvent. The obtained extraction liquor and filter liquid are distilled by a rotary evaporator at 35-40 degrees C. The dosage of the catalyst is 1-10% of the plant biomass, and that of the liquefier is 4-8 times of the sum of the plant biomass and polyester by mass. The mass ratio of the plant biomass to the polyester is 2:1-2:4.
NOVELTY - Fuel composition (150) contains petroleum or benzine (50-60 wt.%), animal oil or vegetable oil (20-30 wt.%) and water (20-30 wt.%).    USE - Fuel composition is used for vehicle and boiler.    ADVANTAGE - The fuel composition has high calorific value and reduces amount of petroleum fuel used.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for device for manufacture of fuel composition.    DESCRIPTION OF DRAWING(S) - The drawing shows cross-sectional view of device for manufacture of fuel composition.    Reservoir (100)    Fuel supply portion (110)    Fuel discharge portion (120)    Valve (130)    Motor unit (140)    Fuel composition (150)
NOVELTY - The reactor has rotary cone (3), tray-shaped cover (5), belt wheel (8) and fuel burner (10). The wall of reactor is provided with ring-shaped intermission sand baffle cover (11), adiabatic layer (12) provided with heat-bearer inlet pipe (16). The adiabatic layer is provided smoke outlet (2) in left wall and fuel burner in right wall. A cooler (7) is formed with cover, asbestos filling and main reactor base (704). The lower cover of cool water device is fixed on reactor base. The upper cover is provided with asbestos material to resist thermal radiation.    USE - Reverberation type reactor for producing bio fuel used in bio-fuel equipment.    ADVANTAGE - The bio fuel is produced with high transforming ratio of material and better use ratio of energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the reverberation type reactor.    Smoke outlet (2)    Rotary cone (3)    Tray-shaped cover (5)    Cooler (7)    Belt wheel (8)    Fuel burner (10)    Ring-shaped intermission sand baffle cover (11)    Adiabatic layer (12)    Heat-bearer inlet pipe (16)    Main reactor base (704)
NOVELTY - A hydrogen generator has an electrolytic cell accommodating primary and secondary electrodes and containing an electrolyte aqueous solution, and hydrogen ion supply port for supplying hydrogen ion to aqueous solution.    USE - Hydrogen generator is used in fuel cell (claimed).    ADVANTAGE - The hydrogen generator enables production of hydrogen in a controlled manner by effectively controlling drive of hydrogen ion supply port.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell.
NOVELTY - A biomass mixture contains biomass and mixture of copper and alumina.    USE - Biomass mixture for use in catalyst pyrolysis.    ADVANTAGE - The biomass mixture efficiently performs catalyst pyrolysis process.
NOVELTY - Method for leaching valuable metal from desulfurized waste catalyst involves using metabolic product of sulfated strain.    USE - Method for leaching valuable metal e.g. nickel, vanadium and molybdenum from desulfurized waste catalyst.    ADVANTAGE - The method economically and efficiently enables leaching of valuable metal from desulfurized waste catalyst in high yield by simple process.
NOVELTY - The method involves using disposable edible oil as raw material and performing distillation process with respect to the disposable edible oil. Acid clay is added to the disposable edible oil to remove the impurity present in the disposable edible oil.    USE - Method for manufacturing biodiesel used as fuel for internal combustion engine and diesel engine used for vehicle.    ADVANTAGE - High purity and environment friendly biodiesel can be manufactured. The distillation residue of the disposable edible oil can be used as boiler fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram explaining the manufacturing process of biodiesel. (Drawing includes non-English language text)
NOVELTY - The apparatus has a mixer that mixes the organic waste in storage chamber. A solubilization tank maintains the temperature of the organic waste within the range of 70-75 degrees C in order to improve the biodegradability of the non-degradable organic material of organic waste transferred from mixer. An agitating blade agitates the organic waste after performing fermentation process to organic waste by a fermentation unit. A discharging unit discharges the agitated organic waste through discharge outlet formed in lower portion of fermentation unit.    USE - Anaerobic digestion apparatus for anaerobic digestion of organic waste (claimed) such as food waste, livestock excretion, excrement, sludge, etc.    ADVANTAGE - The anaerobic digestion of organic waste can be performed efficiently and energy consumption by the anaerobic digestion apparatus can be reduced. The efficiency of the anaerobic digestion can be increased and anaerobic digestion apparatus can be installed at low cost. The solubilization rate of the non-degradable organic material can be increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the anaerobic digestion apparatus. (Drawing includes non-English language text)
NOVELTY - The apparatus has a stirrer (300) including a chain for mixing the pulverized organic waste stored in a fermentation drying room (100). An escalator (320) is installed at the bottom side of a base frame, for transferring the stirred waste to an agitating blade (330) installed on the top of escalator for agitating the organic waste. A supporting plate is installed in the bottom portion of escalator for supporting the escalator so that escalator is moved by sliding operation.    USE - Organic waste compositing apparatus.    ADVANTAGE - The compositing apparatus improves the process of sprinkling the organic waste stored in the drying room so that compost is produced easily without increasing load of equipment. Hence, lifetime of compositing apparatus is increased and function of organic waste compositing apparatus is improved, so that operability and productivity of compositing apparatus are improved while reducing manufacturing cost.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view illustrating the operating state of stirrer.    Fermentation drying room (100)    Stirrer (300)    Escalator (320)    Agitating blade (330)    Hydraulic cylinder (360)
NOVELTY - The apparatus has a working coil (42) wound on induction heater (40) installed at the bottom of stirring tube (20). The moisture contained in the air is condensed in an exhaust pipe (16) for ejecting air in the stirring tube. The separation of condensed moisture from air is performed by condensed water separation unit (80). A catalyst filter (50) is arranged for purifying bad smell exhausted from the exhaust pipe with the exhaust fan (14). A halogen heater (30) is arranged at the top of stirring tube, for emitting infrared ray into the stirring tube.    USE - Food garbage disposal apparatus.    ADVANTAGE - The food waste containing bad smell and moisture can be removed effectively, using the vortex of the electromagnetic induction current generated within the stirring tube, so that energy efficiency of the apparatus can be improved. The drying efficiency of food waste can be improved, since moisture contained in the air can be evaporated easily, so that pathogen and harmful bacteria contained in the food waste can be removed, by using the halogen heater.    DESCRIPTION OF DRAWING(S) - The drawing shows a right side sectional view of the food garbage disposal apparatus.    Exhaust fan (14)    Exhaust pipe (16)    Stirring tube (20)    Halogen heater (30)    Induction heater (40)    Working coil (42)    Catalyst filter (50)    Condensed water separation unit (80)
NOVELTY - A controller (400) controls the picker and pre-processor for collecting the product processed through the manufacturing machine for automatically washing a reactor (201). A valve (212) supplies washing solution to reactor. A valve (213) circulates cleaning water within the reactor. The controller controls the valves, heater (215) which heats the reactor.    USE - Automatic washing system of bio-diesel manufacture reactor.    ADVANTAGE - The foreign material in the reactor can be completely removed by automatically washing by bio-diesel. The temperature rise of the heater can be improved. The blockage of filter is prevented.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for automatic washing method of bio-diesel manufacture reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of the automatic washing system.    Reactor (201)    Valve for supplying washing solution (212)    Valve for circulating cleaning water (213)    Heater (215)    Controller (400)
NOVELTY - Preparation of biofuel, involves (a) preparing saccharification liquid from biomass, (b) then fermenting the saccharification liquid to obtain saccharification liquid containing carboxylic acid, and (c) chemically processing carboxylic acid to obtain alcohol.    USE - Preparation of biofuel, preferably butanol (all claimed).    ADVANTAGE - The method improves productivity and yield of biofuel by removing fermentation inhibitor, and is environmental friendly.
NOVELTY - A sulfur free odorant composition comprises 1-5C alkyl isovalate (1), acrylate-based compound(s) (2), and nitrogenous compound(s) (3). The compound (2) is used in the weight ratio of 3-7:7-3 with respect to the alkyl isovalate and the compound (3) is used in the weight ratio of 1:0.01-0.5 with respect to the alkyl isovalate.    USE - Sulfur free odorant composition used in gas e.g. liquefied petroleum gas, liquefied natural gas, methane gas, hydrogen gas, propane gas and butane gas for fuel cell.    ADVANTAGE - The sulfur free odorant composition has excellent chemical stability, odorization performance, enables to detect the gas leak efficiently and does not produce metal corrosion. Since the composition does not contain sulfur, the need for removing sulfur in the fuel cell is eliminated.    DETAILED DESCRIPTION - A sulfur free odorant composition comprises 1-5C alkyl isovalate of formula: R1-O-C(=O)-CH2-CH(-CH3)-CH3 (1), acrylate-based compound(s) of formula: R2-O-C(=O)-CH=CH2 (2), and nitrogenous compound(s) of formula (3). The compound (2) is used in the weight ratio of 3-7:7-3 with respect to the alkyl isovalate and the compound (3) is used in the weight ratio of 1:0.01-0.5 with respect to the alkyl isovalate.    R1,R2=optionally branched 1-5C alkyl;and    R3-R6=H or R1.
NOVELTY - The apparatus (10) has several cylindrical electrodes having different diameter, which are concentrically arranged in a tank (12) in a state immersed in water containing electrolyte stored in tank. The electrodes have an inner electrode having anodic terminal, and outer electrode having cathode terminal, and an intermediate bipolar electrode. One electrode among several electrodes is foraminous and other electrodes are solid.    USE - Electrolytic hydrogen and oxygen generation apparatus.    ADVANTAGE - The gas is generated efficiently at enhanced productive rate and at low production cost, while improving the overall efficiency of the apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the electrolytic hydrogen and oxygen generation apparatus.    Electrolytic hydrogen and oxygen generation apparatus (10)    Tank (12)    Cylindrical sidewall (14)    Cover plate (18)    Threaded rods (22)    Plug (26)
NOVELTY - Invention relates to equipment intended for producing hydrogen by water thermo chemical decomposition and can be used to supply hydrogen fuel to power plants and produce hydrogen for processing purposes. Proposed unit comprises hopper with initial components, water tank, hydrogen tank, oxygen tank, heater to maintain thermo chemical cycles and outer heat source connected thereto by heat lines, as well as oxidation reactor and reduction reactor intercommunicated via system to transfer initial components, thermo chemical decomposition intermediate products and finished product that comprise multipurpose valves and accessories. Note that proposed plant comprises power supply, control and adjustment unit, and electrochemical generator that incorporates battery of fuel elements, thermal control system, electric current inversion and transformation unit connected by pipelines with hydrogen and oxygen tanks to supply unit components via said inversion and transformation unit and power supply furnished with appropriate connector assemblies.    USE - Process engineering.    ADVANTAGE - Higher efficiency due to reduced power consumption. 3 cl, 1 dwg
NOVELTY - A production apparatus comprises a sodium chlorate electrolysis cell (9) to provide sodium chlorate at a product output (14), and to provide a hydrogen-rich gas including oxygen, chlorine and organics at a byproduct output (19); and a phosphoric acid fuel cell (44) for providing electrical power (47, 48, 50, 51) to the electrolysis cell. The byproduct output of the electrolysis cell is provided to a water cooled catalytic reactor (26), and the output of which is applied (42) to the fuel inlet (43) of the phosphoric acid fuel cell.    USE - Apparatus for closed loop fuel cell powered production of sodium chlorate.    ADVANTAGE - The apparatus can assure conversion of all the byproducts while sustaining the reactor temperature in a safe range.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic block diagram of an apparatus.    Electrolysis cell (9)    Product output (14)    Byproduct output (19)    Water cooled catalytic reactor (26)    Application of output of catalytic reactor (42)    Fuel inlet (43)    Fuel cell (44)    Electrical power (47, 48, 50, 51)
NOVELTY - The method involves providing an inlet manifold (20) in fluid communication with a flow field (24) having several channels (36) receiving restricted fluid flow from the inlet manifold when compared to channels (34). A relative pressure drop between the channels is altered with a pressure drop feature. The fluid flow from the inlet manifold is encouraged to the channels having restricted fluid flow in response to the pressure drop feature. A width (W2) of the flow field is greater than a width (W1) of the inlet manifold.    USE - Method of manufacturing fuel cell plate flow field of fuel cell (claimed).    ADVANTAGE - Since the fluid flow from the inlet manifold is encouraged to the channels having restricted fluid flow in response to the pressure drop feature, even flow distribution is provided between the channels and the efficiency of the chemical reaction within the fuel cell is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a plan view of fuel cell plate having a flow field.    Inlet manifold (20)    Flow field (24)    Channels (34,36)    Width of inlet manifold (W1)    Width of flow field (W2)
NOVELTY - Preparation of astaxanthin feed additive comprises wet grinding beer spent grains by grinding machine to obtain coarse pulp fluid; adding water to adjust the solid-to-liquid ratio of fluid to 1:10 to 1:15, controlling pH value to 4.0-5.5, sterilizing and cooling to room temperature to obtain coarse pulp fluid of beer spent grains; adding cellulase to the fluid and performing enzymolysis hydrolyzing; propagating red yeast seed liquid stored at low temperature, inoculating to enzymolyzed fluid, fermenting for 72-96 hours at 18-22 degrees C under aerobic condition and stopping fermenting; and drying.    USE - Method for preparing astaxanthin feed additive (claimed).    ADVANTAGE - The method has high utilization rate of raw material, good quality of product and easy industrialization. It realizes production of astaxanthin feed additive using industrial wastes, particularly beer spent grains, thus achieving the purpose of recycling the wastes.
NOVELTY - The device has an absorption liquid spraying pipe (8) arranged on an upper part of a packing layer (6) of filled towers (1). Separators (4) are mounted between the filled towers. A steam raising pipe (5) is connected with the filled towers and installed through the separators. A liquid dropping hole is formed on the separators and contact with a liquid dropping pipe (9). The liquid dropping pipe is stretched out from bottom sides of the filled towers and equipped with a biogas outlet (3). The filled towers are provided with a lower filled tower part and an upper filled tower part.    USE - Biogas double-stage normal-pressure decarburizing device.    ADVANTAGE - The device has simple structure, and is convenient to manufacture and inexpensive.    DETAILED DESCRIPTION - The lower filled tower part is an alkali decarburizing tower part, and the upper filled tower part is an alcohol amine decarburizing tower part.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biogas double-stage normal-pressure decarburizing device in partial section. '(Drawing includes non-English language text)'    Filled towers (1)    Biogas outlet (3)    Separators (4)    Steam raising pipe (5)    Packing layer (6)    Absorption liquid spraying pipe (8)    Liquid dropping pipe (9)
NOVELTY - The method involves passing biogas into a bubbling column plate absorption oxidation coating, and absorbing sulfureted hydrogen in the biogas using absorption liquid with spray oxidizer, where the absorption liquid is compound liquid of sodium carbonate/sodium bicarbonate and malysite complex compound. Void tower stream velocity speed in the bubbling column plate absorption oxidation coating is 0.2-1.5 meter per second. The biogas absorbed by the absorption liquid is passed to a subsequent dried thionizer, wet thionizer or biological thionizer to remove the sulfureted hydrogen from the biogas.    USE - Method for removing sulfureted hydrogen from biogas.    ADVANTAGE - The method performs desulfurization process in an efficient and fast manner at normal temperature.    DETAILED DESCRIPTION - The oxidizer is selected from a group consisting of ozone, oxyful or potassium permanganate. The viscosity of the ozone is 0.2-10 gram per cubic meter, viscosity of the oxyful is 50-100 milligram per liter and viscosity of the potassium permanganate is 20-200 milligram per liter. An INDEPENDENT CLAIM is also included for a device for removing sulfureted hydrogen from biogas, comprising a bubbling column plate absorption oxidation coating.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a device for removing sulfureted hydrogen from biogas.'(Drawing includes non-English language text)'    Shell (1)    Inlet (2)    Grid plate (3)    Bubbling hood (4)    Shower (5)    Down spout (6)
NOVELTY - The bed has a packing film (1) installed with two packing layers (3, 4) from bottom to top. A cavity i.e. gas proliferation chamber, is formed between the packing film and a drainage board (11). An external source nutrient feed system comprises liquid storage tanks (14) that are inter-connected with each other and a nutrient solution feed system. A reaction tank is connected to the liquid storage tanks by a leakage liquid outlet (12). A liquid outlet end of the nutrient solution feed system is provided with a spray thrower (19) above one of the packing layers.    USE - Biochemical waste gas deodorization and clean-up bed.    ADVANTAGE - The wipe-off ratio of the fetor material in the waste gas that is processed through the clean-up bed is maintained above 85 percent.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for performing biological deodorization by utilizing a deodorization and clean-up bed.    DESCRIPTION OF DRAWING(S) - The drawing shows a hydraulic circuit diagram of a biochemical waste gas deodorization and clean-up bed.    Packing film (1)    Packing layers (3, 4)    Drainage board (11)    Leakage liquid outlet (12)    Liquid storage tanks (14)    Spray thrower (19)
NOVELTY - The mold has a flanging mold including a female mold (2) and a male mold (1). Size of periphery blanking openings is 0.1-0.3 mm greater than size of a finished flow field plate. Periphery stamping flanging openings of the flanging mold and stamping flanging openings of a fluid in-and-out passage at two ends of a flow field plate are provided with same size as the finished flow field plate. The female mold of the flanging mold is stamped with a flow field face of the flow field plate, and the male mold is stamped with a flanged face toward a side of a flow field.    USE - Mold for stamping a thin metal flow field plate for processing a fuel cell.    ADVANTAGE - The mold has simple structure, high metal flow field plate precision and less buckling deformation, and is easy to manufacture.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for stamping a thin metal flow field plate for processing a fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a thin metal flow field plate stamping mold.    Male mold (1)    Female mold (2)
NOVELTY - The method involves directly sending protogenetic domestic wastes to an externally heating cylindrical drier, and transferring air to internal part of the cylindrical drier through a draught fan. The dried domestic wastes are sent into a rotary kiln for pyrolyzation in air-isolating condition. Pyrolyzed gas and pyrolyzed oil are transferred into a smelting entrained flow gasifying furnace, where combustible gas produced in inner side of the furnace is at temperature of 1100 to 1200 degree centigrade. Heat resources are utilized through double-grade heat recovering process.    USE - Method for smelting-gasifying domestic wastes by rotary kiln and smelting entrained flow to prepare combustible gas.    ADVANTAGE - The method allows smelting of heavy metals and inorganic contents inside the domestic wastes at high temperature flame zone, and allows avoiding secondary pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic illustration of domestic wastes smelting-gasifying method.
NOVELTY - A methanol diesel fuel comprises (parts volume) diesel oil (50-80), methanol (15-40), surfactant (6-18), cosolvent (3-12), corrosion inhibitor (2-8), and cetane improver (1-4). The surfactant comprises (parts volume) triglyceride (3-10) and glycerin monostearate (3-8). The cosolvent comprises (parts volume) oleinic acid (2-7), and fatty alcohol-polyoxyethylene ether (1-54). The corrosion inhibitor comprises (parts volume) bis(cyclopentadienyl)iron (1-3) and methyl isobutyrate (1-5). The cetane improver comprises (parts volume) 2-ethoxyethyl nitrate (0.5-2), and isooctyl nitrate (0.5-2).    USE - A methanol diesel fuel for use as a clean energy source.    ADVANTAGE - The fuel has excellent intermingle stability and longer service life; can be stored for greater than or equal to 6 months at room temperature and normal pressure without layering; does not cause corrosion and swelling to metal parts, and rubber and plastic elements; reduces discharge of waste gas and particulate after combustion; can be applied directly to the civil and commercial production; and can replace the existing diesel oil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the fuel according comprising:    (A) injecting methanol into a material mixer and dissolving tank at room temperature and normal pressure, adding surfactant, and stirring for 15-20 minutes;    (B) adding diesel oil, stirring for 20-30 minutes, adding cosolvent, and stirring for 30-35 minutes; and    (C) adding cetane improver, stirring for 20-30 minutes, adding corrosion inhibitor, and stirring.
NOVELTY - An ethanol diesel oil comprises (pts.wt.) diesel oil (60-70), ethanol (15-25), cyclohexane (1-4), n-butyl alcohol (1-3), methyl cyclopentene (1-3), isopropyl ether (1-3), dodecyl methacrylate (1-5), sorbitan monooleate (1-4), polyoxyethylene hexadecylphenolic ether (1-3), inositol hexaphosphate (1-3), hexadecyl benzyl dimethly ammonium chloride (1-2.5), and dimethoxypropane (0.5-2).    USE - An ethanol diesel oil.    ADVANTAGE - The oil has excellent stability, free phase separation and deposition after placing for a long time at room temperature; improves corrosion effect of moisture and oxygen molecule to metal or rubber pad; and reduces friction of the movable elements of the engine.
NOVELTY - A high purity methanol gasoline comprises (pts.wt.) number 90 gasoline (60-70), methanol (15-25), dihexylether (1-3), glycol dimethyl ether (2-5), n-heptane (1-4), acetone (2-5), dimethyl carbonate (1-3), octadecacylamino ferrocene (1-2), polyisobutadiene ethylenediamine (0.1-1), polyisobutene isobutyl carbaminate (0.1-1), and methylcyclopentadienyl manganese tricarbonyl (0.1-0.5).    USE - A high purity methanol gasoline.    ADVANTAGE - The gasoline has excellent stability, can be stored and transported conveniently, prevents reduction of the combustion properties of gasoline, can be used directly, and has less discharge of pollutants generated through the combustion of gasoline thus reducing environment pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the gasoline comprising:    (A) mixing dihexylether and glycol dimethyl ether, adding n-heptane and acetone, stirring, adding dimethyl carbonate, and stirring well at room temperature and normal pressure;    (B) adding octadecacylamino ferrocene, olyisobutadiene ethylenediamine, polyisobutene isobutyl carbaminate and methylcyclopentadienyl manganese tricarbonyl;    (C) stirring the mixture at room temperature and normal pressure for 20-300 minutes, adding methanol, and stirring for 20 to 300 minutes; and    (D) adding number 90 gasoline, stirring, and filtering.
NOVELTY - The burner has a material distributor fixed under a feed port of a gasification chamber, where a lower part of the gasification chamber is connected with a mixing combustion chamber. A chain type grate is fixed under the gasification chamber and the mixing combustion chamber. A speed reducer is connected with a motor and a spindle of the chain type grate. A chain wheel on the spindle of the material distributor is placed opposite to the chain wheel on the spindle of the grate. Two side walls of the gasification chamber and the combustion chamber are provided with an air distributor port.    USE - Biomass burner.    ADVANTAGE - The burner allows inflammable biomass press block to continuously burn.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a biomass burner.
NOVELTY - Processing biomass, comprises: reducing one or more dimensions of individual pieces of biomass; and treating the biomass using a treatment method that changes the molecular structure of the biomass, where at least one of the reducing and treating steps comprise treating the biomass with a screw extrusion process.    USE - The method is useful for processing biomass, which is useful for making a product, which comprises a combustible fuel (all claimed), hydrogen, alcohols (e.g. ethanol or butanol), organic acids (e.g., acetic acid), hydrocarbons and co-products (e.g. proteins).    ADVANTAGE - The method is carried out at elevated temperatures. The method provides cellulosic and/or lignocellulosic materials that: have a lower recalcitrance level, a lower molecular weight and/or crystallinity relative to a native material; react more rapidly e.g. with an acid, base, or an enzyme; and/or can be more readily utilized by a variety of microorganisms.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for making a product, comprising: providing a material that includes a carbohydrate produced by a process that includes treating a biomass feedstock with radiation, sonication, pyrolysis, and/or oxidation; subjecting the feedstock to a screw extrusion process; and contacting the material with a microorganism having the ability to convert at least a portion of the material to the product.    DESCRIPTION OF DRAWING(S) - The figure shows a block diagram illustrating conversion of biomass into products and co-products.    System (100)    Feed preparation subsystem (110)    Pretreatment subsystem (114)    Primary process subsystem (118)    Post-processing subsystem. (122)
NOVELTY - The purifying material comprises a porous support having a surface porosity of greater than 10%, a specific brauner-emmett-teller (BET) surface greater than 100 m2/g and an average size distribution of 1-10 nm of bimodal pores. The soot having an average particle size of less than a micrometer covers 10-20% of upper surface of the support. The support is composed of a material that withstands temperatures of 1200 degrees C, and present in the form of grains or beads.    USE - The purifying material is useful in a device to eliminate tars and soot contained in a gas mixture (claimed) such as syngas from the gasification of biomass.    ADVANTAGE - The purifying material ensures rapid, effective, economical and simultaneous elimination of tars and soot contained in the gas mixture thus increasing the yield of overall process of biomass, and does not require frequent cleaning and maintenance.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a process for eliminating tars and soot contained in a gas mixture; and    (2) a device for eliminating tars and soot contained in a gas mixture.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a device for eliminating tars and soot contained in a gas mixture.    Inlet conduit (1)    Pyrolytic chamber (2)    Connection conduit (3)    Purification enclosure (4)    Reservoir. (5)
NOVELTY - Composition comprises 2,3,3,3 - tetrafluoropropene (5-80 wt.%), difluoromethane (5-45 wt.%) and at least a compound (2-50 wt.%) comprising propane, propylene or ethylene.    USE - The composition is useful: for heating and/or cooling of a motor vehicle; as heat transfer fluid; and in replacement of R-22 (chlorodifluoromethane), R-407C (mixture of 1,1,1,2-tetrafluoroethane (52 wt.%), difluoromethane (23 wt.%) and pentafluoroethane (25 wt.%)), and R-404A (mixture of 1,1,1,2-tetrafluoroethane (4 wt.%), trifluoroethane (52 wt.%) and pentafluoroethane (44 wt.%)) (all claimed). The composition is useful in refrigeration, air conditioning and for heating including heat pumps.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) heating and/or cooling of a motor vehicle using a reversible refrigeration loop (16), in which circulates a refrigerant fluid, comprising a first heat exchanger (13), an expander (14), a second heat exchanger (15), a compressor (11) and means of reversing the flow direction of refrigerant fluid, where the refrigerant fluid comprises the composition; and    (2) a device comprising the reversible refrigeration loop.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of a device.    Compressor (11)    First heat exchanger (13)    Expander (14)    Second heat exchanger (15)    Reversible refrigeration loop. (16)
NOVELTY - Composition comprises 2,3,3,3-tetrafluoropropylene (55-75 wt.%), difluoromethane (5-40 wt.%) and at least one compound (5-40 wt.%) comprising propane, propylene or ethylene.    USE - The composition is useful: for heating and/or cooling of a motor vehicle; as heat transfer fluid; and in replacement of R-22 (chlorodifluoromethane), R-407C (mixture of 1,1,1,2-tetrafluoroethane (52 wt.%), difluoromethane (23 wt.%) and pentafluoroethane (25 wt.%)), and R-404A (mixture of 1,1,1,2-tetrafluoroethane (4 wt.%), trifluoroethane (52 wt.%) and pentafluoroethane (44 wt.%)) (all claimed). The composition is useful in refrigeration, air conditioning and for heating, including heat pumps.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) heating and/or cooling of a motor vehicle using a reversible refrigeration loop (16), which circulates a refrigerant fluid, comprising a first heat exchanger (13), an expander (14), a second heat exchanger (15), a compressor (11) and means of reversing the flow direction of refrigerant fluid, where the refrigerant fluid comprises the composition; and    (2) a device comprising the reversible refrigeration loop.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of a device.    Compressor (11)    First heat exchanger (13)    Expander (14)    Second heat exchanger (15)    Reversible refrigeration loop. (16)
NOVELTY - Heating and/or cooling of a motor vehicle body using a reversible refrigeration loop (16), in which a refrigerant fluid is circulated, comprising a first heat exchanger (13), an expander (14), a second heat exchanger (15), a compressor (11) and means for reversing the direction of flow of refrigerant fluid, where the refrigerant fluid comprises 2,3,3,3-tetrafluoropropene (5-80 wt.%) and at least one compound (20-95 wt.%) comprising propane, propylene or ethylene, is claimed.    USE - The composition is useful: for heating and/or cooling of a motor vehicle framework; as heat transfer fluid; and in replacement of R-22 (chlorodifluoromethane), R-407C (mixture of 1,1,1,2-tetrafluoroethane (52 wt.%), difluoromethane (23 wt.%) and pentafluoroethane (25 wt.%)), and R-404A (mixture of 1,1,1,2-tetrafluoroethane (4 wt.%), trifluoroethane (52 wt.%) and pentafluoroethane (44 wt.%)) (all claimed). The composition is useful in refrigeration, cooling and for heating, including heat pumps.    ADVANTAGE - The method prevents the entry of air in the evaporator of the refrigeration loop thus improving the starting of the compressor and/or the performance of the motor vehicle.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a device comprising the reversible refrigeration loop; and    (2) composition comprising the refrigerant fluid.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of a device.    Compressor (11)    First heat exchanger (13)    Expander (14)    Second heat exchanger (15)    Reversible refrigeration loop. (16)
NOVELTY - An ammonia decomposition catalyst comprises a compound formed by substituting a transition metal in specific portion of perovskite-type complex oxide (I).    USE - Ammonia decomposition catalyst is used for decomposition of ammonia for producing hydrogen.    ADVANTAGE - The ammonia decomposition catalyst provides stable catalytic activity for long period of time. The transition metal is fixed in crystal lattice of ammonia decomposition catalyst even at high temperature.    DETAILED DESCRIPTION - An ammonia decomposition catalyst comprises a compound formed by substituting a transition metal in A-site portion or B'-site portion of perovskite-type complex oxide of formula: AB'O3 (I).    A=A-site portion of perovskite-type complex oxide;and    B'=B'-site portion of perovskite-type complex oxide.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of test apparatus for measuring ammonia decomposition activity. (Drawing includes non-English language text)    Reactor (1)    Catalyst filled layer (2)    Heater (3)    Thermocouples (4,5)    Flowmeter (6)
NOVELTY - A gas treating system has a fermenter (1), fermenter (2) including unit (3) for maintaining temperature of tank, and a reactor (4) including combustion unit (5) for combusting methane contained in gas produced from fermenter (1), using biogas emitted from fermenter (2) as fuel. The fermenters (1,2) perform fermentation of organic waste. The fermenter (2) is smaller than the fermenter (1).    USE - Gas treating system is used for processing gas generated during fermentation of organic waste e.g. livestock excrement, organic refuse and sewage-treatment sludge, and is economical.    ADVANTAGE - The gas treating system efficiently performs processing of organic waste, and converts methane in organic waste into biogas with low warming coefficient.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of biogas processing system.    Fermenters (1,2)    Unit (3)    Reactor (4)    Combustion unit (5)    Catalyst filled layer (6)
NOVELTY - The method involves dividing the catalyst layers (12a,12b) in which catalyst is filled, so as to form several layers. The temperature of catalyst in each divided catalyst layer is controlled according to the reaction temperature range of the catalyst.    USE - Method for decomposition of tar contained in combustible gas for gasifying biomass fuel, coal, coke, waste oil and other organic compound in gas engine, gas turbine and boiler. Can also be used in solid fuel, industrial waste and other organic waste.    ADVANTAGE - The decomposition process of tar contained in the combustible gas can be carried out easily and effectively, by using simple technique.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for tar decomposition installation.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view illustrating the decomposition process of tar.(Drawing includes non-English language text)    Reaction container (10)    Catalyst layers (12a,12b)    Catalyst temperature measurement units (14a,14b)    Oxidizing agent supply units (20a,20b)    Catalyst supply units (40a,40b)
NOVELTY - The method involves staking gas diffusion layers (2,3) on both sides of membrane electrode assembly (1). A gasket is integrally formed on circumference of stacked layers. The structural elements of modules other than gasket are stacked, to form fastening portion (200) in lamination direction. The gasket is molded to circumference of fastening portion by module.    USE - Method for manufacturing fuel cell e.g. polymer electrolyte fuel cell.    ADVANTAGE - The adhesion of dissimilar material on electrolytic membrane in prevented effectively. The manufacturing method of fuel cell excellent in efficiency is provided.    DESCRIPTION OF DRAWING(S) - The drawing shows a longitudinal cross sectional view explaining the state of stacking on both sides of insulation plate.    Membrane electrode assembly (1)    Gas diffusion layers (2,3)    Electrode case (4)    Separator (7)    Fastening portion (200)
NOVELTY - The fuel cell (100) has a manifold (M2) for discharging the fuel off-gas such as hydrogen generated by electrochemical reaction. A screw (120) arranged along the manifold is rotated by flow of hydrogen through the manifold. The water in the manifold is discharged to the exterior of fuel cell by the rotation operation of screw.    USE - Fuel cell such as polymer electrolyte fuel-cell.    ADVANTAGE - The water in the manifold is discharged to the exterior smoothly and the discharge of hydrogen from the manifold is suppressed, so that the energy efficiency is improved. Since it is not necessary to use the special apparatus for rotating the screw, the number of component is reduced and the space saving is achieved and the cost is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the fuel cell. (Drawing includes non-English language text)    Fuel cell (100)    Screw assembly (110)    Screw (120)    Bearing (130)    Manifold for hydrogen emission (M2)
NOVELTY - A fuel cell (100) has a manifold (HO) for discharging the fuel off-gas such as hydrogen, and an oxidant-gas supply manifold for supplying oxidant gas. A bypass flow path (510) connects the manifold (HO) and oxidant-gas supply manifold. A control unit opens an interruptible bypass cutoff valve (500) provided in the bypass flow path at the time of scavenging-air process of fuel cell.    USE - Fuel cell system equipped with polymer electrolyte fuel cell and solid oxide fuel cell, for electric power generation.    ADVANTAGE - The scavenging effect of air in the fuel cell is improved. The retaining of water inside the hydrogen discharge manifold is suppressed. The fall of electric power generation efficiency due to the big pressure loss arising within hydrogen discharge manifold can be suppressed.    DESCRIPTION OF DRAWING(S) - The drawing shows an expanded perspective view of the fuel cell. (Drawing includes non-English language text)    Fuel cell (100)    Bypass cutoff valve (500)    Bypass flow path (510)    Hydrogen supply manifold (HI)    Hydrogen discharge manifold (HO)
NOVELTY - System (1) is formed by a set of continuous flow digesters (2), a proportional feeder (3) and a homogenizer. A helical static mixer, a reservoir, a set of metering pumps, an optional reactor (8), another anaerobic reactor (9) and a floc-settling unit (10) are also provided. A physico-chemical equalization reactor (11), a set of filtering and polishing units, a photodynamic ultraviolet sterilizer, electric generators and centrifugal pumps are also included. Drainage and recirculation hydraulic line and a biogas capture and displacement line (18) are also provided.    USE - System for optional digestion of residual, agricultural or industrial organic matter.    ADVANTAGE - The system is eco-friendly, promotes digestion of residual, agricultural or industrial organic matter in continuous flow, saves time, reduces hydraulic retention time of waste, and uses automatic process of photodynamic sterilization.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the system for optional digestion of residual, agricultural or industrial organic matter.    System (1)    Continuous flow digesters (2)    Proportional feeder (3)    Optional reactor (8)    Anaerobic reactor (9)    Floc-settling unit (10)    Physico-chemical equalization reactor (11)    Biogas capture and displacement line (18)
NOVELTY - The device has a furnace body (1), where external part of high temperature zone from combustible zone to dry distillation layer in an inner side of the furnace body is equipped with a round gas-collection sandwich layer (2). Two round pipes (3) are equipped in place, which is provided in an internal wall of the furnace body and has a distance of 5-15 cm connected to a water seal in a top end at interval of 180 degree. The round pipes are guided downward into a top part of the gas-collection sandwich layer. Pipe holes in upper parts of the round pipes are equipped with filter screens (5).    USE - Pre-heating drying pressure stabilization collection device for combustible gas of a biomass gasification furnace (claimed).    ADVANTAGE - The combustible gas is filtered by the water seal, so as to convey the combustible gas to a cooking utensil by a pipeline. The device can make combustible gas to absorb heat of the furnace body, so as to reduce tar yield and moisture content. The gas transmission passage is enlarged to achieve stabilizing atmospheric pressure, so as to guarantee stable firepower in cooking utensil, thus improving heat transformation efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a pre-heating drying pressure stabilization collection device.    Furnace body (1)    Round gas-collection sandwich layer (2)    Round pipes (3)    Filter screens (5)    Hole (6)
NOVELTY - The device has a water seal tanks arranged at an outer side at a bottom of an upper furnace body (3) and an outer side of a top of a lower furnace body (8), where the bodies are connected by water seal tanks. An inner wall of the upper furnace body is inversely conical. Multiple truckles (5) are arranged at an outer side of an outer wall of one of the water seal tanks of the lower furnace body. A disk (7) is arranged above the water seal tank of the lower part of the upper furnace body. Multiple horizontal necks are equably distributed on the disk.    USE - Automatic fuel falling device for use in a biomass gasifier.    ADVANTAGE - The fuel in the furnace leaks automatically. The device avoids the phenomenon of partial combustion, offset combustion, overhead and breakage of the fuel, so that the device ensures the generated gas to combust continuously and steadily.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial section of an automatic fuel falling device for use in biomass gasifier.    Upper and lower furnace bodies (3, 8)    Shifting rollers (4)    Truckles (5)    Disk (7)
NOVELTY - Organic waste containing chlorinated organic compound is supplied as a raw material (20) to a reaction apparatus (21). A superheated steam is supplied from a steam generation apparatus (41) and molecular weight of organic compound contained in raw material is reduced by thermal modification process involving hydrothermal reaction. Chlorine is desorbed, volatilized from chlorinated organic compound and removed by nucleophilic substitution using the steam. Superheated steam is used as fuel for steam generation apparatus.    USE - Fuel formation of waste material.    ADVANTAGE - The fuel formation of waste material is enabled with suppressed generation of alkali metal molten salt, and hence high temperature corrosion of furnace wall is prevented during combustion.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) fuel of waste material; and    (2) fuel formation apparatus of waste material, which has reaction apparatus equipped with steam generation apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows the front view of reaction apparatus. (Drawing includes non-English language text)    Raw material (20)    Reaction apparatus (21)    Reaction container (23)    Insertion opening (24)    Steam generation apparatus (41)
NOVELTY - A biomass liquid recovering apparatus recovers liquid contained in thermal decomposition product obtained by carrying out fast pyrolysis of biomass. The recovering apparatus has an addition unit (42) for adding lower alcohol or acetone to the biomass liquid, and a recovery unit (43) for recovering the liquid to which lower alcohol or acetone is added.    USE - Apparatus is used for recovering biomass liquid (claimed) e.g. tar used as fuel.    ADVANTAGE - The apparatus efficiently recovers high quality tar with improved two-phase compatibility. The phase-separation of water-soluble tar and water-insoluble tar is suppressed, such that tar with uniform phase is obtained. The polymerization of water-soluble tar is suppressed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biomass liquid recovering method.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of biomass liquid recovering apparatus. (Drawing includes non-English language text)    Fast-pyrolysis unit (10)    Biomass supply unit (20)    Tar-processing unit (40)    Addition unit (42)    Recovery unit (43)
NOVELTY - Water is electrolyzed to generate hydrogen and oxygen, and plasma reaction is carried out using obtained hydrogen and oxygen as discharge gas, by mixing with to-be-treated drinking water. The obtained treated water is supplied to water-storage tank, and disinfection byproduct, bacteria and virus in water, are removed. Thus, domestic drinking water is purified.    USE - Purification of domestic drinking water.    ADVANTAGE - The method effectively reduces disinfection byproduct in drinking water, provides purified domestic drinking water having improved oxygen content, and is safe.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus for purifying domestic drinking water.
NOVELTY - The reactor has a sloping board-slot type reactor (4) whose top part is connected with a vertical scroll feeder (3), where section of the sloping board-slot type reactor is a rectangular section. The sloping board-slot type reactor is connected with a series complex thermal medium heater reactor (1) through a thermal medium flow controller (2). A pneumatic trough (6) is connected with the sloping board-slot type reactor. The pneumatic trough is connected with an outer cooler through a gas vent (5). A heat-carrier transfer car (7) is formed under the sloping board-slot type reactor.    USE - Combined reactor for preparing a biofuel by fleetly thermal cracking biomass.    ADVANTAGE - The reactor has complete mixing, small volume, simple structure, and an easy producing and maintaining method, and is inexpensive, saves high energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a combined reactor.    Series complex thermal medium heater reactor (1)    Thermal medium flow controller (2)    Vertical scroll feeder (3)    Sloping board-slot type reactor (4)    Gas vent (5)    Pneumatic trough (6)    Heat-carrier transfer car (7)
NOVELTY - An environmentally friendly insecticide comprises 1 pt.wt. each of mountain pepper, tea seed oil cake and red-knees herb.    USE - Environmentally friendly insecticide used for preventing or killing pest.    ADVANTAGE - The insecticide is safe, non-toxic to human and animal and pollution free; and has easily available materials, low production cost, and low investment, making it suitable for industrialization without using special equipment.
NOVELTY - A passivant comprises zeolite, fly ash and calcium magnesium phosphate fertilizer, where high-temperature composting treatment is performed by pretreating animal dejection and straws or other crop straws, adding the passivant and uniformly mixing.    USE - Passivant is used for reducing bioavailability of heavy metal in animal dejection compost (claimed).    ADVANTAGE - The passivant has simple and easy operation; and can be utilized in organic fertilizer plants. The validity of heavy metal in pig manure compost is reduced.
NOVELTY - A conditioner is prepared by pretreatment livestock manure and straw or other crop straws, and uniformly mixing wt. ratio of 2-8:1, where content of water is 60-65%; and adding conditioner, and uniformly agitating materials to carry out normal high-temperature composting treatment.    USE - Conditioner is used for deodorizing and preserving nitrogen in livestock manure compost (claimed) useful for organic fertilizer.    ADVANTAGE - The compost is thoroughly decomposed after composted for about 30 days; and can reduce odorous substance in pig manure compost and ammonia volatilization. The odor removing time can be more than 10 days ahead. The content of nitrogen nutrient in compost product can be increased by more than 20%. The loss of the nitrogen element in process of composting is reduced by more than 70%. The conditioner exhibits simple usage and operation.
NOVELTY - Aspergillus fumigatus strain NJZ5 is a high-temperature cellulose-decomposing fungi and is preserved in General Microorganisms Centre of China Committee for Culture Collection of Microorganisms with a preservation number CGMCCNO.3309. The Aspergillus fumigatus strain NJZ5 has separated mycelium, smooth and green conidiophore having thorn, and has a spherical tip, with a single-layer bottle-shaped stem, which produces spore.    USE - Aspergillus fumigatus strain NJZ5 for producing microbial inoculum compost from agricultural wastes (claimed).    ADVANTAGE - The Aspergillus fumigatus strain NJZ5 notably improves compost temperature, shortens compost period and controls the compost period to 30 days.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for producing microbial inoculum compost from agricultural wastes, which involves:    (A) fermenting microbial inoculum and inoculating the strain NJZ5 to the potato dextrose agar (PDA) liquid culture medium to a shake flask and culturing it;    (B) carrying out liquid fermentation at a pH of 5-6, a culture temperature of 35-40 degrees C, a liquid-loading amount of 20-50% of the volume of the culture container, and a rotating speed of 170 revolutions per minute (rpm) for 12 hours;    (C) inoculating the strain to 1 ton of a fermentation tank by vacuum inoculating method, where the culture medium in the fermentation tank is PDA liquid culture medium;    (D) culturing the strain colony in an amount of 1x 109 in the fermentation liquid;    (E) stopping fermentation to obtain the fermentation liquid;    (F) absorbing the strain and uniformly mixing the fermentation liquid which cultures 1x 109 of strains and absorbent rice bran in the stirrer in a mass ratio of 1:10-3:10; and    (G) obtaining rapid compost microbial inoculum of agricultural wastes.
NOVELTY - The straw gasification furnace has a middle layer furnace wall (3) and an outer layer furnace wall (4) arranged outside an internal layer furnace wall (2). A top cover plate (6) is arranged between internal layer furnace wall and outer layer furnace wall. A filtering plate (14) is arranged between middle layer furnace wall and outer layer furnace wall. A draining pipe (16) is arranged in the bottom surface and a gas discharging pipe (5) is connected with the upper side of the outer layer furnace wall.    USE - Straw gasification furnace.    ADVANTAGE - Water and oil can be separated effectively. Since the structure of the straw gasification furnace is simplified, space required by straw gasification furnace can be reduced and implementation cost of the straw gasification furnace can be reduced.    DETAILED DESCRIPTION - The straw gasification furnace has a smoke channel (13) whose one end is arranged in the inner side of the internal layer furnace wall. Other end of the smoke channel is penetrated to the internal layer furnace wall and middle layer furnace wall. A water inlet pipe (15) and water discharge pipe (12) are penetrated into the outer layer furnace wall and coupled with middle layer furnace wall. The internal and external layers (9,7) of the cover are arranged at the upside end of the outer layer furnace wall and internal layer furnace wall. A steel wire is penetrated between internal and external layers of the cover.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the straw gasification furnace.    Internal layer furnace wall (2)    Middle layer furnace wall (3)    Outer layer furnace wall (4)    Gas discharging pipe (5)    Top cover plate (6)    External layer (7)    Internal layer (9)    Water discharge pipe (12)    Smoke channel (13)    Filtering plate (14)    Water inlet pipe (15)    Draining pipe (16)
NOVELTY - The apparatus has a dry anaerobic digester (120) to provide a solid material having concentration of about 15% by anaerobic digestion process. A dehydration chamber (111) includes a coherence dehydrating element (112) to separate the dehydrating liquid and solid material provided from the dry anaerobic digester using coagulant. The coherence dehydrating element provides another solid material so as to separate the organic supernatant by receiving the dehydrating liquid.    USE - Apparatus for recycling organic supernatant in food waste, livestock excretion, sewage sludge, etc.    ADVANTAGE - The size of the dry anaerobic digester can be reduced and the dry anaerobic digester which is capable of storing large amount of organic supernatant and biogas can be obtained. The organic supernatant can be recycled effectively by fermenting the digested sludge from the dry anaerobic digester.    DESCRIPTION OF DRAWING(S) - The drawing shows a block flow diagram explaining the organic supernatant recycling process. (Drawing includes non-English language text)    Dehydration chamber (111)    Coherence dehydrating element (112)    Dry anaerobic digester (120)    Biogas collecting tank (140)    Water control agent feeding tank (151)
NOVELTY - The apparatus has a backup dehydration unit (231), dehydration unit (232) and coherence dehydration unit (233) for separating the solid materials from the organic waste. A dry anaerobic digester (240) supplies the total amount of solid material generated from the dehydration units to a compositing tank (273) after performing anaerobic process with respect to the supplied solid material.    USE - Apparatus for recycling organic waste e.g. food waste, livestock excretion and sewage sludge for producing biogas.    ADVANTAGE - The percentage of water content supplied to the dry anaerobic digester can be minimized, and the volume of the digester can be minimized and high organic loading amount can be maintained, so that the biogas can be manufactured efficiently from organic waste.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for recycling organic waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the organic waste recycling apparatus.(Drawing include non-English language text)    Dehydration unit (231)    Dehydration unit (232)    Coherence dehydration unit (233)    Dry anaerobic digester (240)    Compositing tank (273)
NOVELTY - The method involves collecting methane gas generated in anaerobic digestion facility (20), and the sludge generated in a gas preservation facility (22). The collected sludge is allowed to flow into solubilization apparatus (60). The sludge is selectively supplied to a reaction bath of advanced treatment facility (30), after increasing methane gas generation rate of anaerobic digestion facility.    USE - Processing method of high-concentration organic waste water.    ADVANTAGE - The processing of high-concentration organic waste water is performed efficiently, by anaerobic treatment process.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the system for treating high-concentration organic waste water.    Anaerobic digestion facility (20)    Gas preservation facility (22)    Solid-liquid separator (24)    Advanced treatment facility (30)    Solubilization apparatus (60)
NOVELTY - The trees are cut into wooden logs of 10-50 cm length, and the cut logs are immersed in a biodiesel liquid for 6-48 hours, and allowed to soak for 1-3 hours. The soaked logs are sent to pressurization cutter for cutting the coated wooden logs for use as solid fuel.    USE - Method for manufacturing wood fuel used as solid fuel for combustion in stove in house, and for heating effect in crop cultivation.    ADVANTAGE - The generation of disgusting smell or toxic gas can be reduced, and the environment pollution can be prevented. The burning time of the fuel can be increased, and the heating effect can be improved. The wood fuel is safe and harmless to man and crops.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram explaining the manufacturing method of wood fuel. (Drawing includes non-English language text)
NOVELTY - Agent represents a consortium of the following bacteria - Rhodococcus sp.SMB37, Rhodococcus sp.SMB38, Arthrobacter sp.SMB32, Microbacterium sp.SMB33, Thalassospira sp.SMB34, Halomonas sp.SMB31 and "Salinicola socius" SMB35, deposited in collection of Chemical mutagenesis laboratory of Institute of Ecology and Genetics of Microorganisms, Urals department of Russian Academy of Sciences under No. SMB3.    USE - Biotechnologies.    ADVANTAGE - High speed of polycyclic carbohydrates destruction under conditions of high salt concentrations (NaCl to 7%). 2 tbl
NOVELTY - An innovative device for enhancing fuel efficiency of internal combustion engine of vehicles, is disclosed. The device comprises an efficient, compact and low cost electrolysis unit which splits water into a mixture of hydrogen and oxygen gas. The rate of production of the gaseous mixture and its release into the engine is duly controlled by use of appropriate systems. The device can be directly installed into vehicles without any major modifications of existing vehicular design. Image 0/0
NOVELTY - A system for advantageous utilization of electrical power in electrolytic process for production of electrolytic gases, particularly hydrogen and oxygen, comprises an electrolytic capacitor (EC), a single phase transformer (T), rectification diodes (D) connected between electrolytic capacitor and single phase transformer, the power source (PS) and clamps (C) providing power to the electrodes of an electrolytic cell. A capacitor is connected in parallel to the alternating current (AC) power source to step down transformer for maximum utilization of electrical energy. The capacitor has 1000V, 20-25 KVA capacity and is connected in parallel to a 220 volts AC supply with 99.9% pure copper conductor and output is connected to a 5 KW oil cooled step down transformer. the step down transformer has a loading of approximately 1000 amperes/m2 of the electrode surface at 2.5 volts and is connected to diodes for direct current (DC) output. The diodes are connected to electrodes of electrolytic cell. Image 1/1
NOVELTY - The method comprises guiding native fats and/or raw vegetable oils (10) to be cleaned to a strong acid cation exchanger (12), heating the native fats and/or raw vegetable oils to be cleaned and/or the strong acid cation exchanger, and cleaning the fats and/or raw vegetable oils in two-stages, where the electrical conductivity and/or permittivity of the cleaned fats and/or raw vegetable oils are measured after each cleaning stage The fats and/or raw vegetable oils are initially guided through a heat exchanger and then heated, cleaned and subsequently guided again through the heat exchanger.    USE - Method for cleaning native fats and/or raw vegetable oils, and for the esterification of free fatty acids with mono- or polyhydric alcohols such as methyl alcohol or glycerin, where the cleaned fats and/or raw vegetable oils are useful as fuel in an internal combustion engine (all claimed) such as diesel engine and as fuel for mobile purposes.    ADVANTAGE - The method is capable of simply and effectively cleaning the native fats and/or raw vegetable oils with high quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a plant for cleaning native fats and/or raw vegetable oils.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic view of a plant for cleaning native fats and/or raw vegetable oils.    Fats and/or raw vegetable oils (10)    Strong acid cation exchanger (12)    Plant (18)    Inlet (24)    Outlet (26)    Heating device. (28)
NOVELTY - A methane fermentation system comprises organic waste supply installation (2) which supplies organic waste which are carbon source and hydrogen source to underground cavities (1) such as abandoned mine and waste oil rice field, and collection installation (3) which collects methane gas to produce on ground. The organic waste are supplied to underground cavity from organic waste supply installation.    USE - A methane fermentation system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of methane-fermentation apparatus.    Underground cavity (1)    Organic waste supply installation (2)    Collection installation (3)    Monitoring apparatus (4)    Separation unit (5)
NOVELTY - A fuel gas such as hydrogen is generated from water by electrolysis, and the generated fuel gas is filled in collapsible bag, when the bag is not completely full, and allowed to bypass the bag and move towards the internal combustion engine, when the bag is full. Then, the fuel gas is drawn from the bag into the engine, when the engine requires a fuel boost. Thus, method of providing fuel gas for internal combustion engine is performed.    USE - Method of providing fuel gas for internal combustion engine.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) system used for providing fuel gas for internal combustion engine; and    (2) electrolytic tank.
NOVELTY - Producing ethanol, comprises: adding a suspending fluid to a feedstock to produce a fermentation suspension, where the suspending fluid comprises an organic material that is at least partially anaerobically digested; adjusting the pH of the fermentation suspension, if necessary, to a value conductive for fermentation; and fermenting the fermentation suspension to produce ethanol, where the suspending fluid is substantially free of (exogenously added) fresh water or nutrient supplement.    USE - The methods are useful in hydrolyzing the feedstock to yield ethanol (claimed), where the ethanol is useful for combustion as a fuel or a fuel additive.    ADVANTAGE - The methods provide: enhanced or increased ethanol yield compared to an otherwise identical process using fresh water instead of the suspending fluid; cost efficiency; and wet distiller's grains as the remaining portions, which are valuable and palatable as feed for cattle. The methods enable turning anaerobic digest effluent into value-added products and assists bioethanol industry to achieve positive balance on energy consumption, bioethanol production, waste management, and environmental preservation. In the method, suspending fluid is substantially free of non-anaerobic microorganisms, which does not interfere with fermentation processes (e.g. by consuming the feedstock).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for hydrolyzing a feedstock, comprising: adding a suspending fluid to the feedstock to produce a feedstock suspension, where the suspending fluid comprises organic material that is at least partially anaerobically digested; and hydrolyzing the feedstock suspension such that at least a portion of the polysaccharides are converted into simple sugars, where the feedstock comprises polysaccharides and the hydrolyzed feedstock yields more ethanol when fermented than prior to hydrolysis.
NOVELTY - Producing a hydrocarbon comprises two or three carbon atoms from glycerol, involves: providing glycerol; converting glycerol to acrolein through use of a first catalyst, catalyzing dehydration reactions; and converting the formed acrolein to the hydrocarbon, through use of a second catalyst catalyzing de-carbonylation reactions, or through use of a second catalyst catalyzing hydrogenation reactions and a third catalyst catalyzing de-hydration reactions.    USE - For producing hydrocarbon comprises two/three carbon atoms (claimed); as a starting material in chemical industry; as a monomer within the polymer industry; and as a fuel.    ADVANTAGE - The method provides hydrocarbon (preferably ethane) at least 60 (preferably at least 80)% yield from glycerol.
NOVELTY - The gasifier has burners and nozzles whose shape and calibration are varied to optimize the production and combustion of gas produced by gasification, pyrolization of various forms of biomass. The outlet apertures (28) are formed in the inner chamber of gasifier whose sizes are optimized by varying the degree of mixing the gases with air so as to produce and burn the gas produced by gasification. The apertures are connected to the connecting tubes which are connected to the terminal plates, without the need for welding or riveting process.    USE - Gasifier used for small stoves, combustion chambers for pellet, biomass stoves, combustion chambers of gasification system and fuel conversion plant (all claimed).    ADVANTAGE - The gasifier which is operated with a mechanical or electric fan, without requiring additional machining process, improves combustion, gasification and pyrolization, while reducing manufacturing costs efficiently.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) device for coaxial gasification and pyrolysis or vaporization; and    (2) combustion method.    DESCRIPTION OF DRAWING(S) - The drawing shows a longitudinal cross sectional view of the device for coaxial gasification and pyrolysis or vaporization.    Combustor device (10)    Support rod (12)    Base plate (14)    Top plate (16)    Outlet aperture (28)
NOVELTY - Waste material is crushed and deposited to predetermined height. The deposit is subjected to aerobic fermentation and the fermented material is supplied to cement burner (100), and used as raw fuel.    USE - Manufacture of raw fuel for cement manufacture.    ADVANTAGE - The waste material is processed efficiently and economically.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) raw fuel manufacturing equipment (200), which consists of grinder (201) for crushing the waste material, and deposition type fermenter (202); and    (2) cement manufacturing plant, which is equipped with the raw fuel manufacturing equipment.    DESCRIPTION OF DRAWING(S) - The drawing shows the flowchart of the cement manufacturing plant. (Drawing includes non-English language text)    Cement burner (100)    Rotary kiln (102)    Raw fuel manufacturing equipment (200)    Grinder (201)    Deposition type fermenter (202)
NOVELTY - A processing system of organic waste includes a methane fermentation tank in which organic wastes are subjected to high-temperature methane fermentation, and a fermentation-liquid modification component, which is disposed after methane fermentation tank and in which fermentation for improving the water retentivity of fermentation liquid (4) is carried out.    USE - System is used for treating organic waste containing excrement of living organism e.g. livestock (claimed).    ADVANTAGE - The system effectively enables production of fertilizer without generation of offensive odor.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) processing of organic waste, which involves performing primary fermentation process, secondary fermentation process and dispersing slurry of fermentation liquid which passed through secondary fermentation process, on the surface of soil. The primary fermentation process involves performing methane fermentation treatment at high temperature with respect to organic waste. The secondary fermentation process involves performing fermentation process which improves water retention with respect to fermentation liquid produced in methane fermentation treatment; and    (2) modification of fermentation liquid derived from organic waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of system for treating organic waste. (Drawing includes non-English language text)    Livestock barn (1)    Livestock excrement (2)    Methane-fermentation layer (3)    Fermentation liquid (4)    Fermentation liquid modification process component (5)
NOVELTY - The device has a separator located in central part for separating chemicals from fatty water.    USE - Device for producing biodiesel.    ADVANTAGE - The device can work continuously without any external power supply.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a biodiesel producing device.
NOVELTY - A PTU (110) separates sewage into scum layer, liquid layer and sludge layer. The PTU has a settling chamber (112) which receives sewage and outputs liquid effluent, and a digestion chamber (114) receives solid components of sewage from settling chamber. The settling chamber has a headspace (121) configured to vent to atmosphere and to collect biogas. The digestion chamber has headspace (122) which collects methane-containing biogas. The scum layer is retained in settling chamber and sludge layer is retained in digestion chamber.    USE - System for extraction and collection of sewage biogas used for chemical synthesis in chemical industry and for production of electricity in residence.    ADVANTAGE - The collection of methane-containing biogas from sewage is maximized and the interaction between methane-containing biogas and methanotrophs in scum layer is prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the PTU.    PTU (110)    Settling chamber (112)    Digestion chamber (114)    Headspace of settling chamber (121)    Headspace of digestion chamber (122)
NOVELTY - The device has a gasifying furnace (1) whose sidewall is equipped with an ejector (13). Collected tar is injected into the gasifying furnace for continuing combustion. A tar capturer (6) is provided with a cooling device (7), which is arranged with cooling media. A filter dust removal device (3) and airway tubes (4, 5) are made by a set of heat preserving materials. Temperatures of a tar collection groove (9), back flash tubes (10, 12), a liquid seal bent tube (11) and a lighter are controlled based on usage of hot wind or fuel gas.    USE - Fixed bed straw gasifying device.    ADVANTAGE - The device reduces tar content in the fuel gas, realizes automatic back flash of the tar, and improves gasifying efficiency, fuel gas calorific value and fuel gas quality. The device avoids secondary pollution of the tar.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a fixed bed straw gasifying device.    Gasifying furnace (1)    Filter dust removal device (3)    Airway tubes (4, 5)    Tar capturer (6)    Cooling device (7)    Tar collection groove (9)    Back flash tubes (10, 12)    Liquid seal bent tube (11)    Ejector (13)
NOVELTY - The device has an ash storage chamber (9) whose upper and lower parts are equipped with photoelectric ash level controllers, respectively. An upper position switch (9-5) and a lower position switch (9-4) of the ash level controller are mounted on the upper and lower parts of one side of the ash storage chamber, respectively. An upper photoelectric reflection plate and a lower photoelectric reflection plate (9-3) of the ash level controller are mounted on the upper and lower parts of another side of the ash storage chamber, respectively.    USE - Compression self-sealed full-automatic spiral ash discharging device for a biomass fixed bed gasification furnace.    ADVANTAGE - The full-automatic sealed continuous ash discharging device is adopted for making the biomass fixed bed gasification furnace to work continuously. The device guarantees stable pressure and safe circulation in the gasification furnace. The device can realize that the gasification furnace discharges the ash randomly according to ash amount in the ash chamber. The device has high automation degree and better environment protecting effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a compression self-sealed full-automatic spiral ash discharging device.    Ash discharging door (1)    Ash storage chamber (9)    Lower photoelectric reflection plate (9-3)    Lower position switch (9-4)    Upper position switch (9-5)
NOVELTY - The gasifier has a feeding port connected with a gasification chamber through a material storage chamber, where the material storage chamber is arranged on an upper part of the gasifier. The gasifier is provided with a front seal cover and a rear seal cover. Bottom part of a rectangular gasification chamber is provided with a chained grate. The grate is installed on a conveyer belt. A blending device is arranged above the chained grate. Bottom part of a gasifier body is arranged with a pedestal. A set of gas collecting ports is connected with a cyclone separator by a gas pumping pipe.    USE - Grate-type gasifier for gasifying biomass material of agriculture and forestry.    ADVANTAGE - The gasifier has a scientific and rational structure, and is convenient to use and maintain. The gasifier has continuous material feeding and carbon discharging property, and provides stable gas supply by cutting the biomass material of agriculture and forestry into baculiform or flaky material with a specific length without crushing the material into uniform powder such that the biomass material can successfully enter the gasifier.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a grate-type gasifier for gasifying biomass material of agriculture and forestry.
NOVELTY - The compressed material (1) is formed in block-shaped by mixing multiple crushed straw materials. The block-shaped body is rectangular or square with length, width and the height of 5 to 30 cm.    USE - Compressed material for replacing straw energy.    ADVANTAGE - Attains simple structure, avoids pollution caused by the combustion of straw in field and fully utilizes energy source, and conveying and storage are convenient.    DESCRIPTION OF DRAWING(S) - The drawing shows the perspective view of the compressed material in rectangular shape.    Compressed material (1)
NOVELTY - The furnace has a furnace body whose four walls are respectively provided with heat-reservation layers. The furnace body is internally provided with a porous furnace base whose lower part is provided with an air inlet chamber. An upper surface of the porous furnace base is provided with a sealing ash layer. A wind pipe connected with a blower is fixed to an air inlet pipe and a distribution pipe. The air inlet pipe is connected with an air inlet chamber at a lower part of the porous furnace base. The distribution pipe is connected with an air pipe under a burning cooking range.    USE - High-efficiency and clean straw gasification furnace.    ADVANTAGE - The porous furnace base and the sealing ash layer on the furnace base provides multiple holes at any direction for ventilation to realize full burning of a hearth base layer including middle and periphery parts, so that the furnace has obvious saving effect, the air inlet is smooth, and power is increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a high-efficiency and clean straw gasification furnace.
NOVELTY - The system has a cleanout door fixed at a lower end of a tank, and an air inlet pipe connected with a blower. A round exhaust port is connected with channels located at a periphery of the tank. The channels are connected with an air tube. The air tube is connected with a fire spray head that is sealed in a sealing furnace. A sewage settling pool is located at a lower side of a ring-shaped channel, and a pollution discharging port is located at a bottom part of the sewage settling pool. A sewage discharging port is located at one side of the sewage settling pool.    USE - Energy-saving plant gasification system.    ADVANTAGE - The system smoothly discharges gas, and is simple in structure, convenient to operate and inexpensive. The system does not produce smoke, and the gas in the sealing furnace is fired fully. The system is easy for lighting. The firing spray head is firm and durable. The duration of fire of the system is as long as 48 hours.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an energy-saving plant gasification system.
NOVELTY - The machine has two straw gasifying furnaces (2), a heater (1) and a circulating system (3) connected with each other, where the heater is provided with multiple seamless copper pipes. The straw gasifying furnaces are provided with two fans that are controlled by frequency conversion, where one of the fans is utilized for inletting air and the other fan is utilized for adsorbing air.    USE - Highly-efficient and environment-friendly heat supply machine for use in a rural area.    ADVANTAGE - The machine avoids problem caused by the straw in the rural area, saves energy and effectively supplies heat.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a highly-efficient and environment-friendly heat supply machine.    Heater (1)    Straw gasifying furnaces (2)    Circulating system (3)
NOVELTY - Polyimide gas separation membrane is prepared by dissolving aromatic diamine and aromatic dianhydride in polar solvent to prepare a solution. Weight average molecular weight of polyimide gas separation membrane is 80000.    USE - Polyimide gas separation membrane used for separating carbon dioxide and methane, carbon dioxide and hydrogen, and petroleum and natural gas.    ADVANTAGE - The polyimide gas separation membrane is cost-effective and simple, and has strong dissolubility, high molecular weight and good permeability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing polyimide gas separation membrane, which involves:    (A) preparing polyamide acid solution by dissolving aromatic diamine monomer in polar solvent by stirring in presence of nitrogen or argon to obtain a solution;    (B) reacting aromatic dianhydride with solution at -20 degrees C to -23 degrees C for 2-24 hours to obtain polyamide acid solution;    (C) preparing polyimide membrane by chemical imidization;    (D) diluting polyamide acid solution;    (E) forming a membrane on glass plate;    (F) stripping polyimide membrane;    (G) cooling glass plate with polyimide membrane at room temperature; and    (H) boiling cooled glass plate with water.
NOVELTY - A biodiesel is prepared from grease with high acidic value by dripping plant or animal grease with acidic value of 20-200 mg potassium hydroxide/g into reaction kettle; catalytically cracking, in which sodium catalyst carbonate is pre-added into the reaction kettle at 450 degrees C; transferring generated cracking oil vapor to pass a rectifying column at 320-360 degrees C to enter a counterflow reaction filling tower; inputting alcohol vapor into the counterflow reaction filling tower from bottom up to react with the generated cracking oil vapor; and obtaining the biodiesel.    USE - Method for preparing biodiesel from grease with high acidic value (claimed).    ADVANTAGE - The method has simple technique, high acidic value of product as fuel oil, and high conversion rate of product.    DETAILED DESCRIPTION - Preparing biodiesel from grease with high acidic value comprises dripping plant or animal grease with acidic value of 20-200 mg potassium hydroxide/g into reaction kettle; under the blending condition, catalytically cracking, in which sodium catalyst carbonate (5 wt.%) is pre-added into the reaction kettle at 450 degrees C; transferring generated cracking oil vapor to pass a rectifying column at 320-360 degrees C to enter a counterflow reaction filling tower; inputting alcohol vapor into the counterflow reaction filling tower from bottom up to react with the generated cracking oil vapor; and obtaining the biodiesel. The counterflow reaction filling tower is provided with an acidic granular catalyst fixed bed layer and a temperature inside the counterflow reaction filling tower is 60-200 degrees C.
NOVELTY - The air cathode has a base material whose two sides are, respectively coated with a diffusion layer and a catalyst layer. A diffusion layer comprises 1-2 nanometer carbon base layers and 1-5 polyfluortraethylene coating layers from inside to outside. A nanometer carbon base layer is a mixture of a carbon powder with granularity of 20 nm and 40 percentage weight of polyfluortraethylene emulsion according to mixing ratio of 10-50 ml of the polyfluortraethylene emulsion per gram of a carbon powder. A gram of active carbon powder is added with 0.5-4 ml of emulsion and 5-10 ml of isopropanol.    USE - Air cathode for manufacturing microbe fuel cells.    ADVANTAGE - The air cathode has multiple diffusion layers and catalyst layers, so that the air cathode reduces water loss caused by the evaporation and improves the stability of the electrode. A side of the air cathode directly faces to the air, and the oxygen is directly diffused to the cathode catalyst surface in the absence of the additional air supply device and power, so that the air cathode efficiently reduces operation cost of the cell and improves stability. The cathode catalyst material is made of the active carbons with wide source and low cost and without metal catalyst, so that the air cathode efficiently reduces manufacturing cost of the cell. The air cathode is simple in structure, inexpensive and easy in expansion. The air cathode can be utilized for manufacturing the microbe fuel cells with high performance and low cost and can purify waste water.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an air cathode preparation method.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of an air cathode.
NOVELTY - A catalyst support (10) comprises: a base member (11); and several paths (13) extending through the base member in a first direction from a first end of the base member to a second end of the base member, where each path has a first end at the first end of the base member and a second end at the second end of the base member, and the first ends of the paths are disposed at different intervals from a plane that is perpendicular to the first direction.    USE - As a catalyst support in a reformer (claimed); as apparatus to generate high purity hydrogen gas from a hydrocarbon.    ADVANTAGE - The catalyst support may have maximum temperatures beyond which chemical and/or physical degradation may occur; reduce hot spots; having a long life time.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) manufacturing (M1) a catalyst support involving: providing a first base member having a sheet shape; providing a second base member having a ripple shape; forming a spiral structure by overlapping and spirally winding the first base member and the second base member; and offsetting a central portion of the spiral structure by a predetermined interval in a direction parallel to a winding axis of the spiral structure so that a central portion of the spiral structure projects relative to a peripheral edge portion of the spiral structure or is recessed relative to the peripheral edge portion of the spiral structure; and    (2) a reformer comprising: a first chamber for a target reaction; and the first catalyst support disposed in the first chamber.    DESCRIPTION OF DRAWING(S) - The figure shows a catalyst support.    Catalyst support (10)    Base member (11)    First end surface (11a)    Second surface (11b)    Paths (13)
NOVELTY - Detecting (M1) contamination of a gasoline fuel used in an internal combustion engine involves detecting at least one biodiesel chemical components (A1) in an engine oil sample from the internal combustion engine, by separating the sample into a polar component and a non-polar component and analyzing at least one of the polar or non-polar component for the diesel chemical components.    USE - For detecting contamination of gasoline fuel used in internal combustion engine (claimed).    ADVANTAGE - The method is useful for failure analysis techniques, that determines the cause of engine malfunction or failure by taking a sample of engine oil from the subject engine for testing to determine whether a fuel used in the engine is contaminated with an unsuitable fuel. Using the method the contamination of gasoline fuel or engine oil from an engine consuming such biodiesel fuel can be easily determined and analyzed.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) detecting (M2) contamination of a conventional petroleum-based fuel for an internal combustion engine involving detecting biodiesel chemical components (A2) related to the presence of the biodiesel chemical components in a sample of an engine oil used in the internal combustion engine, which is designed to consume a petroleum-based fuel; separating the sample into a polar component and a non-polar component via extraction with a polar solvent having a polarity index of greater than or equal to 5; and analyzing the polar or non-polar component for the biodiesel chemical components; and    (2) detecting (M3) alternative fuel contaminant in a petroleum-based fuel involving detecting at least one biodiesel chemical components (A3) selected from plant sterols, fatty acid methyl esters, and/or cetane related to the presence of biodiesel chemical component in a fuel sample by analyzing the fuel sample via Gas Chromatography and Mass Spectrometry (GC/MS).
NOVELTY - Producing liquid hydrocarbon biofuel, involves identifying genetic material in micro algae Botryococcus braunii encoding cells to produce hydrocarbons, isolating and purifying genetic material from the micro algae, cloning the genetic material into macro algae seaweed species Macrocystis pyrifera to produce genetically modified seaweed, extracting hydrocarbons generated by the genetically modified seaweed through photosynthesis, and processing the extracted hydrocarbons as liquid biofuel.    USE - The method is useful for producing liquid hydrocarbon biofuel, which is useful in transportation vehicles and in chemical feedstock (all claimed).    ADVANTAGE - The method enables production of large amount of hydrocarbon using rapidly growing sea weeds without using large amount of land area, and the method does not utilize energy intensive fertilizer for producing biofuels.
NOVELTY - The method involves preparing gas flow path (20) having a porous portion, and gas diffusion layer (30) having an electroconductive porous base material whose hardness is lower than gas flow path. The gas flow path and gas diffusion layer are laminated by applying preset pressure to produce laminated structure (10). The laminated structure and membrane electrode assembly are laminated by applying pressure different from preset pressure.    USE - Manufacturing method of fuel cell (claimed).    ADVANTAGE - Since the gas flow path and gas diffusion layer are laminated by applying preset pressure to produce laminated structure, the contact property of the gas flow path and gas diffusion layer can be improved, and the number of manufacturing processes can be reduced and the manufacturing time of the fuel cell can be shortened.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell.    DESCRIPTION OF DRAWING(S) - The drawings show the explanatory views illustrating the manufacturing processes of the fuel cell. (Drawing includes non-English language text)    Laminated structure (10)    Gas flow path (20)    Gas diffusion layer (30)    Convex portion (35)    Press apparatus (200)
NOVELTY - The collecting apparatus has a gravity separating unit (42) that separates the liquid, obtained from thermal decomposition product, into water-soluble tar and water-insoluble tar using gravity. The water-insoluble tar has larger specific gravity than water-soluble tar. A polymerization-inhibitor adding unit (43) is provided to add polymerization inhibitor to the water-soluble tar. A collecting unit (45) classifies and collects the water-insoluble tar and the water-soluble tar added with polymerization inhibitor.    USE - Biomass liquid collecting apparatus used in collecting liquid from thermal decomposition product that went through fast biomass pyrolysis.    ADVANTAGE - Prevents the water-soluble tar from getting heavy dye to the addition of polymerization inhibitor to the water-soluble tar. Suppresses change in quality in the water-soluble tar, thus avoiding deterioration of quality of water-soluble tar. Maintains the quality of water-soluble tar and water-insoluble tar as fuel due to the improved collection of water-soluble tar and water-insoluble tar from liquid obtained from thermal decomposition product that went through fast biomass pyrolysis.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for the biomass liquid collection method.    DESCRIPTION OF DRAWING(S) - The drawing is a block diagram showing the structure of the biomass liquid collecting apparatus. (Drawing includes non-English language text).    Tar processing unit (40)    Pump (41)    Gravity separating unit (42)    Polymerization-inhibitor adding unit (43)    Water-removing unit (44)    Collecting unit (45)
NOVELTY - Wet grinding of carbonized material (3) is carried out in the presence of water (6) to obtain ground material (3a). The ground material is dispersed in water in predetermined amount to obtain carbonized material slurry (10). The slurry is boiled and dehydrated after preset time. Carbonized ground material (3c) is recovered. Demineralization of carbonized material is enabled.    USE - Demineralization of carbonized material used as fuel for combustion furnace.    ADVANTAGE - The demineralization of carbonized material is efficiently enabled and demineralized material is obtained with reduced chlorine content.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for demineralizer of carbonized material, which has wet grinding mill (11) for forming carbonized material slurry, carbonized material boiling apparatus (12) for boiling carbonized material slurry, and water removal device for dehydrating carbonized material slurry.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view illustrating demineralization of carbonized material.    Carbonization apparatus (1)    Waste material (2)    Carbonized material (3)    Ground material (3a)    Carbonized ground material (3c)    Water (6)    Carbonized material slurry (10)    Wet grinding mill (11)    Carbonized material boiling apparatus (12)    Dehydration-washing apparatus (13)
NOVELTY - Fuel additive concentrate comprises: (a) an aminotriazole compound comprising a reaction product of hydrocarbyl carbonyl compound and an amine compound (I) or its salts; and (b) a hydrocarbyl-substituted succinimide dispersant, where the ratio of (a) to (b) is 1:10-10:1.    USE - The fuel additive concentrate is useful for improving the antifoam performance of fuel (claimed), preferably diesel fuel, biodiesel, biodiesel-derived fuel, synthetic diesel, jet fuels, kerosene and diesel fuel treated with oxygenates for particulate control. The fuel composition is useful to operate both stationary diesel engines e.g. engines used in electrical power generation installations, pumping stations, and ambulatory diesel engines e.g. engines used as prime movers in automobiles, trucks, road-grading equipment and military vehicles.    ADVANTAGE - The fuel additive concentrate provides mutual compatibility and convenience to the fuel. (I) reduces blending time and lessen the possibility of blending errors.    DETAILED DESCRIPTION - Fuel additive concentrate comprises: (a) an aminotriazole compound comprising a reaction product of hydrocarbyl carbonyl compound and an amine compound of formula (NH2-C(=NR)-NH-NHR1) (I) or its salts; and (b) a hydrocarbyl-substituted succinimide dispersant, where the ratio of (a) to (b) is 1:10-10:1.    R = H or 1-15C hydrocarbyl; and    R1 = H or 1-20C hydrocarbyl.    An INDEPENDENT CLAIM is included for a fuel composition comprising a major amount of a fuel and a minor amount of the additive composition or fuel additive concentrate.
NOVELTY - A green preparation comprises etoxazole and emamectin benzoate complex as active components, and additives. The preparation is prepared into miscible oil, wetting powder, microemulsion, water dispersible powder and/or oil suspension.    USE - Green preparation is used for killing pest, Acarus (claimed), Lepidoptera, Homoptera and coleopteran in vegetable and other crops.    ADVANTAGE - The preparation has high-efficiency of more than 90%, and low-toxicity.
NOVELTY - Regulating acidity and basicity of biogas pool comprises: (a) adding inoculum; (b) adding plant ash; (c) adding limewater; and (d) preventing high basicity.    USE - The method is useful for regulating acidity and basicity of biogas pool (claimed).    ADVANTAGE - The inoculum and plant ash are added to new or old biogas pool to regulate acidity and basicity inside and to ferment materials inside fully so as to meet the demand of biogas users.    DETAILED DESCRIPTION - Regulating acidity and basicity of biogas pool, where inoculum and plant ash are added; the method specifically comprises the following steps: (a) adding inoculum: adding high-quality bacteria when pH value is lower than 6.3 since acidification may happen on newly built biogas pool, stopping supplying material and controlling acid concentration at 6-8%; (b) adding plant ash: adding plant ash or ammonia when fermentation concentration is normal, controlling ammonia concentration at 5% (95 kg of water is mixed with 5 kg of ammonia), and agitating the materials uniformly; (c) adding limewater: agitating 2% clarified limewater with fermenting liquid uniformly, measuring pH value, adding clarified limewater and agitating the materials uniformly if pH value is too low; and (d) preventing high basicity: when the normal working of biogas pool is affected by pH value higher than 8, mixing 2-3 cm long green grass with hog urine or cattle urine, keeping them outside the biogas pool for 2-3 days, putting them into the biogas pool, and agitating them uniformly to make green grass contact fully liquid so that pH value becomes normal gradually.
NOVELTY - A photosensitizing nanomaterial is manufactured by adding solid material to anhydrous aromatic solvent form suspension; saturating suspension with metal complex tetrapyrrole derivative; heating and stirring the suspension under inert atmosphere in the dark; filtering and washing manufactured photosensitizing nanomaterial from suspension; and drying photosensitizing nanomaterial.    USE - Method for manufacture of photosensitizing nanomaterial used for treatment of a biological target particularly bacterium (claimed).    ADVANTAGE - The manufactured photosensitizing material provides targeted and selective treatment mechanism, thus avoiding uncontrolled diffusion of the metal complex tetrapyrrole derivative into environment and/or neighboring tissue.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for treatment of a biological target by photodynamic treatment which comprises irradiating photosensitizing material with light to inactivate biological target in an aqueous medium.
NOVELTY - The manufacturing machine has an electrolyzing unit which is connected with a groove body. The groove body is filled with liquid and a top end of the groove body is provided, in extended state, with a gas outlet pipe. The top side of the internal groove is provided, in extended state, with a gas discharging valve. The gas discharging valve is provided, in extended state, with the gas outlet pipe. The external groove and the internal groove are all filled with liquid. A chamber is kept on the upper section of the external groove.    USE - Manufacturing machine for oxy-hydrogen hydro-fuel energy.    ADVANTAGE - Maintains buffering space on the top of the groove body since the groove body is not filled with liquid. Effectively protects the electrolyzing unit by resisting fire.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the manufacturing machine.
NOVELTY - Nanometer insecticidal aqueous paint comprises (in pts.wt.): vinyl acetate emulsion (VAE) (30-40), deionized water (30-35), hydroxyl cellulose (0.2-0.4), wetting agent (0.2-0.3), antifoaming agent (0.3-0.5), film-forming additive (0.1-1.5), cation generating material (1-2), nanometer silicon dioxide (0.8-1.2), powder material (15-30), pH regulator (0.1-0.2), anti-freezing agent (1-2) and insecticide (1-4).    USE - Nanometer insecticidal aqueous paint.    ADVANTAGE - The nanometer insecticidal aqueous paint is eco-friendly and safe for mammals, purifies air, kills insects, and has less odor.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing nanometer insecticidal aqueous paint, which involves:    (A) adding deionized water to dispersing jar;    (B) adding hydroxyl cellulose and dispersing it at 100-400 revolutions/minute for 2-15 minutes;    (C) adding dispersion wetting agent, antifoaming agent and film-forming additive;    (D) dispersing them again for 5-25 minutes;    (E) adding passive natural cation generating material and nanometer silicon dioxide, and dispersing the mixture at 500-800 revolutions/minute for 5-25 minutes;    (F) adding powder material and dispersing the mixture for 5-40 minutes at 1000-1600 revolutions/minute;    (G) grinding the mixture by sand grinder;    (H) adding vinyl acetate emulsion (VAE), insecticide, pH regulator, anti-freezing agent and dispersing the mixture at 600-900 revolutions/minute for 2-15 minutes;    (I) filtering and filling the mixture; and    (J) obtaining the finished product.
NOVELTY - A carbonaceous solid fuel is injected into a pyrolyzing furnace, external fuel and oxidant are added, and carbon and thermal gas are obtained. The average temperature in the pyrolyzing furnace is 450-550 degrees C, and the outlet temperature of output thermal gas is more than 450 degrees C. Biomass in the pyrolyzing furnace is turned over circumferentially while stirring continuously. The biomass is left for more than 600 seconds and the thermal gas generated from pyrolyzing procedure is left for more than 120 seconds.    USE - Mesothermal rapid pyrolysis and schizolysis of carbonaceous solid fuel.    ADVANTAGE - The method satisfies the material processing requirement of gasification of biomass entrained flow gasifier through mesothermal rapid pyrolysis and schizolysis of carbonaceous solid fuel.    DETAILED DESCRIPTION - A carbonaceous solid fuel is injected into a pyrolyzing furnace, and external fuel and oxidant are added for pyrolysis to obtain carbon and thermal gas. The carbonaceous solid fuel is biomass. Only external fuel is supplied to the pyrolyzing furnace initially, and the heat energy required for pyrolysis is provided by reaction of oxidant and thermal gas generated from pyrolysis in turn. The average temperature in the pyrolyzing furnace is 450-550 degrees C, the outlet temperature of output thermal gas is more than 450 degrees C, and pyrolysis is mesothermal pyrolysis. Biomass in the pyrolyzing furnace is turned over circumferentially while stirring continuously. The biomass is left for more than 600 seconds and the thermal gas generated from pyrolyzing procedure is left for more than 120 seconds, to realize rapid pyrolysis of biomass and schizolysis of thermal gas. The pressure of pyrolyzing furnace is adjusted to 0.1-5.0 MPa according to the output thermal gas.
NOVELTY - The device has a fuel container that is filled with reaction mixture of hydride and activator. A hydrogen outlet is set in the fuel container. A gas flowing pipe and water flowing pipe are arranged on the surface of the fuel container.    USE - Hydrogen generating device.    ADVANTAGE - The efficiency of the hydrogen generating device can be improved reliably, and the structure of the hydrogen generating device can be simplified effectively. The hydrogen generating device can be operated safely and controlled easily.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the hydrogen generating device.
NOVELTY - The stove (1) has a gasifying room (2), gas-water separating room (3), and a cool wind nozzle (5). A firebox is connected with the gas-water separating room through a gas alleyway, and a flaming head is mounted inside the firebox and is connected with the gas alleyway. A grate is formed under the flaming head and a dust-cleaning mouth is formed under the firebox. A firewood-adding mouth is formed at the top of the firebox.    USE - Economical straw gasifying gas-wood dual function service stove.    ADVANTAGE - The stove can be used with or without electricity, and it saves 50% of the floor space. Since the common red brick is used as construction material of the stove, instead of the steel board or the cast-iron board, the cost is reduced and its structure is simplified. The stove can be efficiently used in the impoverished mountain areas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of the stove.    Stove (1)    Gasifying room (2)    Gas-water separating room (3)    Wind-sending pipe (4)    Cool wind nozzle (5)
NOVELTY - Synthesis of butanol involves forming allyl magnesium chloride by reacting chloropropene as raw material with magnesium.    USE - Synthesis of butanol used for preparing cyproconazole.    ADVANTAGE - The method simply and economically provides butanol with high yield, without causing pollution.
NOVELTY - The method involves guiding ventilation air to ventilation air filter through an air inlet using a ventilation air directing pipeline. The filtered ventilation air is pressurized by a ventilation air pressurizing pump at a pressure rate of 0.2-0.4 mega Pascal. The hydrogen sulfide gas is removed from the pressurized ventilation air, and methane is absorbed from the ventilation air after hydrogen sulfide gas is removed. The absorbed methane is collected and stored in a temporary container, and stored methane is utilized as fuel.    USE - Method for collecting and utilizing methane.    ADVANTAGE - The methane can be collected and utilized effectively at reduced cost. The energy required for methane collection and utilization process can be decreased reliably.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram illustrating the process for collecting and utilizing methane.
NOVELTY - Production of high-efficiency bioorganic compound fertilizer involves mixing fresh pig manure, edible bacterium-cultivated waste residue crushed materials, nitrogen-phosphorus-potassium, trace elements and microbial strains at weight ratio of 800:200:9.5:0.5:1, and uniformly stirring; naturally fermenting for 7-15 days, controlling temperature in fermentation process at 45-65 degrees C, and aerating and stirring simultaneously; and discharging fermented mixed material, air-drying, crushing, and packaging.    USE - Method for producing high-efficiency bioorganic compound fertilizer (claimed).    ADVANTAGE - The method maintains original organic materials and protein nutritional components in pig manure, preserves beneficial microorganisms, decomposes nitrite in soil, improves quality of crops and sugar content of fruits, has strong pertinence and low cost, and is simple and convenient to implement and suitable for small and medium pig farm.    DETAILED DESCRIPTION - Production of high-efficiency bioorganic compound fertilizer involves (A) surrounding fermentation tank with brackets and waterproof cloth, and providing rainproof sunshield above the tank; (B) mixing fresh pig manure, edible bacterium-cultivated waste residue crushed materials, nitrogen-phosphorus-potassium, trace elements and microbial strains (preferably composite Azotobacter, phosphate bacteria, potassium bacteria, probiotic, or fiber bacteria) at weight ratio of 800:200:9.5:0.5:1, uniformly stirring, and placing in the tank; (C) naturally fermenting for 7-15 days, controlling temperature in fermentation process at 45-65 degrees C, and aerating and stirring simultaneously; and (D) discharging fermented mixed material, air-drying, crushing, and packaging.
NOVELTY - Green environment-friendly biological organic composite fertilizer comprises AS1.910 Bacillus mucilaginous and AS4.891 Steptomyces miroftauus.    USE - The green environment-friendly biological organic composite fertilizer is useful for increasing yield of crop.    ADVANTAGE - The fertilizer has simple technical method and technology, effectively uses urban garbage and the offal of agricultural product as materials of biological fertilizer, saves the inorganic fertilizer, reduces cost, can be widely applied to additional fertilizer and base fertilizer for crop, fruit-bearing forest, especially greenhouse vent and weather crop at air temperature more than 20 degrees C, and should be applied more popularly in entire country.    DETAILED DESCRIPTION - Green environment-friendly biological organic composite fertilizer prepared by mutagenesis, separation and purification of strain, preparation and fermentation of the strain and microbial inoculum culture medium, preparation and fermentation of bacterial manure culture medium, preparation and processing of organic fertilizer, preparation and formula of inorganic fertilizer, preparation and processing of micro-element, and formula and technology of composite fertilizer, where the strains of the biological composite bacterial manure comprises (a) AS1.910 Bacillus mucilaginous and (b) AS4.891 Steptomyces miroftauus.
NOVELTY - An anti-caking agent comprises (wt.%) organic modifier (0.1-20) and powder material (80-99.9), prepared by wet mixing uniformly to absorb organic modifier on surface of powder material, dehydrating, drying and crushing.    USE - An anti-caking agent used for chemical fertilizer.    ADVANTAGE - The agent has no toxic or side effect and pollution, low cost, low usage amount, excellent anti-caking performance and slow release effect to chemical fertilizer.
NOVELTY - A Alcaligenes xylosoxidans H4-1 (CGMCC No.3252), is new.    USE - The Alcaligenes xylosoxidans H4-1 is useful in solid microbial inoculum for degrading petroleum hydrocarbon and bioremediation of petroleum pollution and soil polluted by petroleum (all claimed).    ADVANTAGE - The Alcaligenes xylosoxidans accelerates the bioremediation of petroleum pollution, thus protects the environment of petroleum fields.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) microbial inoculum for degrading petroleum hydrocarbon, comprising the Alcaligenes xylosoxidans H4-1 as active component; and (2) solid microbial inoculum for degrading petroleum hydrocarbon, comprising the A.xylosoxidans H4-1 (15x 109-20x 109 colony forming units (CFU)), ammonium salt (0.9-1.2 g), soluble magnesium salt (0.02-0.1 g) and carbon source.
NOVELTY - Trans-esterification reaction of oil and methanol is performed in presence of enzymatic catalyst to obtain biodiesel. Methanol is injected into a reactor and a porous material capable of maintaining moisture is further injected. The glycerol is separated from the porous material in the reaction mixture.    USE - Manufacture of biodiesel used as fuel.    ADVANTAGE - The method provides biodiesel in high yield, with reduced consumption of energy.
NOVELTY - A fuel composition comprises component(s) selected from a hydrocarbon substituted sulfonated phenol (i) or its salt, an ethylene oxide/propylene oxide copolymer (ii) and/or a hydrocarbyl substituted phenol (iii), gasoline (2), alcohol(s) (3), and ashless dispersant(s) (4). The weight ratio of at least one component to ashless dispersant is 2:1-1:50, and the amount of alcohol(s) is 0.1-45 weight% of the fuel composition, and remainder of gasoline. Image 0/0
NOVELTY - Household or commercial waste reduced to size of 10-30 cm in dimension(s) is treated. The treated waste is fed into a vessel, such that volume of vessel is set to 70 volume% or more. The vessel is tilted between 10 degrees and 60 degrees from horizontal, and main cooking or steam treatment is carried out. The treated material of vessel is classified into one or more useful fractions. Thus, treatment of waste at elevated temperature and pressure is enabled.    USE - Treatment of waste e.g. municipal solid waste at elevated temperature and pressure.    ADVANTAGE - The waste is economically treated at elevated temperature and pressure, using reduced energy and without requiring pretreatment process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for municipal solid waste treatment system.
NOVELTY - The biological treatment device has a biological degradation unit (1) with a degrading biological bacteria filler layer having volume of 19-25% of that of the biological degradation unit. The volume of the aerobic biological bacteria filler layer of an aerobic unit (2) is 19-25% of that of the aerobic unit. A purification unit (3) has a purification filler layer with a volume of 4-8% of that of the purification unit. Two air pipes (16) are led to the bottom of the aerobic unit.    USE - Biological treatment device for feces sewage in environmental engineering.    ADVANTAGE - Saves treatment time, simplifies treatment process and reduces large amount of discharge. Offers compact and durable biological treatment device modularly designed and manufactured to adapt with wide application. Ensures simple installation. Realizes functions of receiving, degrading, aerobic treating, purifying and recycling in closed state. Can be continuously operated. Recycles first flushing water circularly treated and recycled for more than five years.    DETAILED DESCRIPTION - The design parameters of optimal combination proportion of volume of each unit and total volume of the device are 35-39% for the biological degradation unit, 30-34% for the aerobic unit, 14-18% for the purification unit and 13-17% for a recycling unit (4).    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of a biological treatment device.    Biological degradation unit (1)    Aerobic unit (2)    Purification unit (3)    Recycling unit (4)    Air pipes (16)
NOVELTY - The plant gas generator has a main water tank with pan-shaped bottom surface that is installed at the upper port of a furnace, while a sealing water tank is installed on the upper edge of the furnace. The sealing water tank contacts a sealing sleeve installed on the main water tank. A water inlet pipe and a water outlet pipe are installed on the main water tank. A water-collecting tray is installed at the bottom of the main water tank, penetrates through the furnace via a water pipe, and connected with a drain pipe.    USE - Plant gas generator with water and vapor separating function used in rural energy field.    ADVANTAGE - Enables separating more than 90 percent of water containing tar produced when the fuel burns since cooling water tank and water-collecting tray are both installed on the furnace. Provides plant gas generator with simple structure and safe to use, while prolonging burning time. Offers energy saving and ensures environmental protection.    DESCRIPTION OF DRAWING(S) - The drawing shows the cross sectional view of the plant gas generator.
NOVELTY - The device has a square column draft tube provided at an inner side of a square column outer shell of an airlift three-phase circulation bioreactor, and a square air distributing plate installed at a center part at a bottom part of the outer shell. An aperture of an air hole on air distributing plate is 0.5-4.5 mm, and an upper part of the outer shell is provided with a dismountable pyramid sealing. A water outlet is provided under the outer shell, and distance from a bottom part of a draft tube to a bottom part of the outer shell is half of side length of cross-section of the outer shell.    USE - Device for purifying a methylbenzene waste gas in a bubble tower airlift three-phase circulation bioreactor.    ADVANTAGE - The three-phase of gas-liquid-solid is advanced in regular flow pattern and cycling flow and has low air rising resistance. The device has wide application range in research of using fossilized Pseudomonas putida to purify methylbenzene waste gas in the three-phase bioreactor.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for purifying a methylbenzene waste gas in a bubble tower airlift three-phase circulation bioreactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a device for purifying a methylbenzene waste gas in a bubble tower airlift three-phase circulation bioreactor.'(Drawing includes non-English language text)'
NOVELTY - The device has a water outlet arranged at a position of a lower part of a shell that is placed close to a bottom surface. A bubble tower three-phase bioreactor is utilized as a shell body in the shape of square column. A side length of a square cross section of the shell body is 0.12-0.2 m, and a center position of a bottom part of the shell body is provided with an aeration board. An upper part of the shell body is equipped with a detachable seal in the shape of pyramid. Height-diameter ratio of the shell is 10:1-12:1.    USE - Device for purifying toluene waste gas in a bubble tower three-phase bioreactor.    ADVANTAGE - The bubble tower three-phase bioreactor has no internal constructional elements, thus reducing the resistance for air rise, shortening lingering time and providing better processing effect. The device has wide applications.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for purifying toluene waste gas in a bubble tower three-phase bioreactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a toluene waste gas purification device for a bubble tower three-phase bioreactor. '(Drawing includes non-English language text)'
NOVELTY - Stepped composite sewage treatment device with vertical flow for artificial wetland, is composed of multiple units (1) each composed of an adjacent lower pool (2) and an upper pool (3). The units are separated from each other with baffles (4). The lower pool and the upper pool are filled with substrate layers (6) and soil layers (9) from bottom to top. Water distributing pipes (7) are provided on the soil layers of the lower pool, and plants (8) are planted on the soil layers of the lower pool and the upper pool.    USE - A stepped composite sewage treatment device with vertical flow for artificial wetland.    ADVANTAGE - The device has wide application range for repairing water body, good repairing effect, and low construction cost, low management and maintenance cost, and good fancy property.    DETAILED DESCRIPTION - A stepped composite sewage treatment device with vertical flow for artificial wetland, is composed of multiple units (1). Each of the units is composed of an adjacent lower pool (2) and an upper pool (3), and the units are separated from each other with baffles (4) and their bottoms are communicated with each other. The lower pool is higher than the upper pool, thus, a step is formed. Adjacent two units are separated from each other via a baffle (5). The upper pool of former unit is aligned with the lower pool of the next unit. The lower pool and the upper pool are filled with substrate layers (6) and soil layers (9) from bottom to top. Water distributing pipes (7) are provided on the soil layers of the lower pool, and plants (8) are planted on the soil layers of the lower pool and the upper pool.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view illustrating the stepped composite sewage treatment device.    Units (1)    Lower pool (2)    Upper pool (3)    Baffles (4, 5)    Substrate layers (6)    Water distributing pipes (7)    Plants (8)    Soil layers (9)
NOVELTY - The gasifier has fire grates (13) equipped with through-holes and installed in a furnace body (1). An ash chamber (12) is arranged below the furnace body, where gaps are formed between edges of the fire grates and an internal wall of the furnace body to form ash exhausting holes (2). An ash pushing mechanism is installed on the fire grates and connected with a fire grate driving mechanism in a protective bonnet (5) below the fire grates. The ash pushing mechanism comprises an ash pushing roller (3) and an ash pushing roller rotating shaft (4).    USE - Biomass gasifier.    ADVANTAGE - The ash pushing mechanism can transfer ash from the fire grates into the ash exhausting holes, so that the raw materials or ash dregs on the fire grates are prevented from bridging and accumulating, thus smoothly carrying out chemical reaction of the raw materials and improving the working efficiency. The fire grates are equipped with the through-holes, so that combustible gas can be discharged from the bottom of the furnace body, thus strengthening the gas generating ability of the gasifier.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial sectional view of a biomass gasifier.    Furnace body (1)    Ash exhausting holes (2)    Ash pushing roller (3)    Ash pushing roller rotating shaft (4)    Protective bonnet (5)    Ash chamber (12)    Fire grates (13)
NOVELTY - The device has a tube air inlet device mounted at a lower end of a boiling section of a gasifier. A vibrating device is equipped with a feeding device. The tube air inlet device comprises an air intake pipe, and an annular air bin is mounted at the lower end of the boiling section of the gasifier, which is connected with an air intake pipe. A horizontal air tube is mounted at a top part of the annular air bin in parallel. An air intake pipe of the boiling section of the gasifier is mounted at a top part of a horizontal air tube at intervals.    USE - Device for producing combustible gas from turmeric residue or Chinese medicine residue.    ADVANTAGE - The device enlarges cross area of suspending section to reduce air flow speed. The device is convenient to remove impurity and ballast, thus making the gasifier to operate in a safe manner for a long time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a combustible gas producing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a combustible gas producing device.
NOVELTY - Microbe adhering membrane type anaerobic reactor comprises a reaction container and an organism adhering device in the reaction container. The organism adhering device is composed of a three-dimensional frame and an SDF AquaMats (RTM: Aquatic technology product) biological substrate supported by the three-dimensional frame.    USE - Microbe adhering membrane type anaerobic reactor for fermenting methane (claimed).    ADVANTAGE - The microbe adhering membrane type anaerobic reactor solves the problems of long starting time, low gas yield, high cost and complex technique of methane fermentation.
NOVELTY - A glyceride is hydrolized by mixing and reacting fats and oils containing glyceride, water and enzyme which can catalyze hydrolysis until reaction of glyceride and hydrolysis reaction of glyceride reaches decomposition ratio of greater than or equal to 30%, adding alcohol to reaction liquid, and continuing hydrolysis reaction.    USE - Hydrolysis of glyceride for manufacture of bio diesel fuel (claimed).    ADVANTAGE - The method hydrolyzes glyceride simply and efficiently.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a manufacturing method of free fatty acid or fatty acid ester involving mixing and reacting fats and oils containing glyceride, water and enzyme which can catalyze hydrolysis until reaction of glyceride and hydrolysis reaction of glyceride reaches decomposition ratio of greater than or equal to 30%, adding alcohol to reaction liquid, and continuing hydrolysis reaction;    (2) a manufacturing method of bio diesel fuel involving mixing and reacting fats and oils containing glyceride, water and enzyme which can catalyze hydrolysis until reaction of glyceride and hydrolysis reaction of glyceride reaches decomposition ratio of greater than or equal to 30%, adding alcohol to reaction liquid, and continuing hydrolysis reaction until glyceride, free fatty acid or fatty acid ester content in water-soluble fraction or water-insoluble fraction in reaction liquid reaches to less than or equal to 1 mass%; and    (3) a manufacturing method of free fatty acid and/or fatty acid ester involving mixing and reacting fats and oils containing glyceride, water and enzyme which can catalyze hydrolysis until reaction of glyceride and hydrolysis reaction of glyceride reaches decomposition ratio of greater than or equal to 30%, adding alcohol to reaction liquid, continuing hydrolysis reaction, and collecting glyceride, free fatty acid and/or fatty acid ester from water-soluble fraction or water-insoluble fraction in reaction liquid.
NOVELTY - Method for in situ biomineralization of a soil contaminant, involves (a) providing several bacteria to a soil comprising at least one contaminant, where at least one bacterium expresses phosphatase, (b) providing a phosphate-rich material to the soil, (c) reacting at least one bacterium expressing a phosphatase with the phosphate-rich material in the presence of the contaminant, and (d) immobilizing the contaminant in the soil.    USE - The method is useful for in situ biomineralization of a soil contaminant such as metal, radionuclide and uranium (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) substantially purified nucleic acid derived from Rahnella sp. Y9602, encoding an enzyme exhibiting phosphatase activity, where the nucleic acid is substantially homologous to a 738 base pair sequences (SEQ ID NO: 1) fully defined in the specification; (2) expression vector for the enzyme exhibiting phosphatase activity comprising the nucleic acid, operatively linked to at least one controlled sequence compatible with a suitable bacterial host cell; (3) bacterial cell transformed with the expression vector, where the bacterial cell can express the enzyme exhibiting phosphatase activity in a detectable quantity; and (4) system for the production of reactive phosphate, comprising a bioreactor having a chamber, several bacteria disposed within the chamber, and a phosphate-rich material disposed within the chamber, where at least one bacterium expressing a phosphatase enzymatically liberates a reactive phosphate group.
NOVELTY - Esterification of free fatty acids in triglycerides with methanol involves contacting heterogeneous esterification catalyst in a reactor with reaction mixture comprising methanol and triglyceride mixture containing 70-99.8 wt.% triglycerides and 0.2-30 wt.% free fatty acids, under esterification conditions to produce product stream; separating water and methanol from product stream to produce dried product stream; contacting dried product stream with methanol to produce methanol-rich phase and triglyceride-rich phase; and separating methanol-rich phase and recycling it to the reactor.    USE - For the esterification of free fatty acids in triglycerides with methanol (claimed) to produce fatty acid methyl esters used as biodiesel fuels in diesel engines.    ADVANTAGE - The water content of the product stream is reduced by at least 70 wt.%. The method is capable of esterifying free fatty acids efficiently to the desired low levels of residual fatty acids.
NOVELTY - A wind-to-hydrogen system (100) comprises a ship (104) configured and arranged to carry one or more wind machines (102); one or more wind machines disposed on ship and configured and arranged to produce electricity in response to movement of turbine blades; an electrolysis tank including pairs of cathode and anode electrolysis plates and disposed on the ship, where electrolysis tank is configured and arranged to receive electricity from wind machines for electrolysis; and a hydrogen storage system configured and arranged to receive hydrogen from the electrolysis tank and store hydrogen.    USE - The wind-to-hydrogen system is useful for converting wind energy to hydrogen fuel (claimed).    ADVANTAGE - The invention implements alternative energy resources such as wind energy in ways that are not disruptive to established communities.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method of converting wind energy to hydrogen fuel, comprising providing one or more wind machines to a sea going vessel; providing a tank to the vessel for holding water during an electrolysis process, where the tank includes one or more pairs of electrolysis plates for splitting water into oxygen and hydrogen; using electricity from the one or more wind machines to perform electrolysis of water in the tank; and collecting hydrogen produced from the electrolysis of water.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of vessel-deployed wind-to-hydrogen system.    Vessel-deployed wind-to-hydrogen system (100)    Wind machines (102)    Ship or vessel (104)
NOVELTY - Organic waste is heated and gasified in a biomass gasifier in a reduced atmosphere. While gasifying the organic waste and producing biogas by using the biomass gasifier and dry-type methane fermentation apparatus, the fermentation residue produced after biogas production is injected into the biomass gasifier. The fermentation residue is then gasified in the biomass gasifier, to produce biogas.    USE - Recycling of organic waste and paper garbage e.g. newspaper, corrugated cardboard, and office automation paper, discharged from buildings and redevelopment blocks.    ADVANTAGE - The method enables efficient and economical in-situ recycling of organic waste, with reduced generation of carbon dioxide. The produced biogas can be utilized for electric-power generation or air conditioning in buildings and redevelopment blocks.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of the recycling method of organic waste. (Drawing includes non-English language text)
NOVELTY - Gas separation membrane comprises polyimide with certain repeating unit.    USE - Gas separation membrane for selective separation of mixed gases (claimed) such as oxygen gas, nitrogen gas and helium gas, nitrogen gas and hydrogen gas, methane gas and carbon dioxide gas, and methane gas.    ADVANTAGE - Has excellent mechanical properties.    DETAILED DESCRIPTION - Gas separation membrane comprises polyimide with repeating unit of formula (1).    B=tetravalent group; and    A=bivalent aromatic group of formula (2).    An INDEPENDENT CLAIM is included for a selective separation of mixed gas involves permeating to the gas separation membrane.
NOVELTY - A reformer consists of a thermally-conductive component (2), a catalyst layer (1) formed on the surface(s) of thermally-conductive component, and a flow path (4) in which produced carbon dioxide circulates. The reformer produces hydrogen or hydrogen-containing compound from a compound containing carbon in a molecule, and steam.    USE - Reformer is used in electric-power generation systems, distributed power supplies, and motor vehicles (all claimed).    ADVANTAGE - The reformer accelerates reaction which produces hydrogen or hydrogen-containing compound. The reformer provides compact and highly efficient power generation systems, distributed power supplies, and motor vehicles. Local temperature rise in the catalyst layer is prevented, which suppresses powdering of catalyst material by heat distortion.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) distributed power supply consisting of the reformer, and a power engine or generator chosen from fuel cell, turbine, and engine; and    (2) motor vehicle consisting of the reformer, and a power engine or generator chosen from fuel cell, gas turbine, and internal combustion engine.    DESCRIPTION OF DRAWING(S) - The drawing shows an external view of the reformer. (Drawing includes non-English language text)    Catalyst layer (1)    Thermally-conductive component (2)    Heater (3)    Flow path (4)    Cooler (5)
NOVELTY - Waste edible oil for biodiesel fuel is received from a supply source, and biodiesel fuel is manufactured as follows by using the received waste edible oil. The waste edible oil is transesterified with a lower alcohol, and the obtained fatty-acid ester is purified. The purified ester is mixed with light oil, to obtain biodiesel fuel. The biodiesel fuel is supplied to a vehicle, and advertisement of the supply source of waste edible oil is published on the vehicle.    USE - Promotion of utilization of waste edible oil for biodiesel fuel used in diesel engines of vehicles. Uses include but are not limited to cars, buses, trucks, and rail vehicles.    ADVANTAGE - The method enables manufacture of biodiesel fuel without precipitation. Since an in-vehicle advertisement is provided, the advertisement can be read by traveling passengers.
NOVELTY - The power generation apparatus (1) has a heating apparatus (14) that heats the water supplied from a water storage apparatus (13) to form steam. A steam electrolyzer (5) electrolyzes the steam and generates hydrogen and oxygen while storing the oxygen and hydrogen in oxygen tank (17) and hydrogen tank (16) respectively. A hydrogen-oxygen engine (8) generates motive power based on the reaction of the hydrogen and oxygen supplied from the tanks respectively while recovering the exhaust heat from steam, in waste heat recovery equipment (2).    USE - Power generation apparatus mounted in motor vehicle.    ADVANTAGE - The cleanliness of the power generation apparatus can be improved and the energy efficiency of the power generation apparatus can be improved while using appropriate amount of hydrogen and oxygen.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the power generation apparatus. (Drawing includes non-English language text)    Power generation apparatus (1)    Heat recovery equipment (2)    Steam electrolyzer (5)    Hydrogen-oxygen engine (8)    Water storage apparatus (13)    Heating apparatus (14)    Hydrogen tank (16)    Oxygen tank (17)
NOVELTY - A fuel cell system has a fuel cell (1) which uses liquid fuel as fuel, a fuel circulation path (5) for circulating liquid fuel through anode side catalyst electrode (3a) of fuel cell, and an evaporation unit. The fuel cell has a pair of anode side catalyst electrode (3a) and cathode side catalyst electrode (3b) formed on electrolytic membrane (2) capable of permeating anion. The boiling point of fuel is more than that of water. Evaporation unit evaporates generated water in liquid fuel by heating fuel flowing through path (5) at temperature less than boiling point of fuel.    USE - Fuel cell system.    ADVANTAGE - The fuel cell system has favorable electric power generation efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of fuel cell system.    Fuel cell (1)    Electrolytic membrane (2)    Anode side catalyst electrodes (3a)    Cathode side catalyst electrode (3b)    Fuel circulation path (5)    Heat exchanger (7)
NOVELTY - The method involves positioning two electrodes in respective surfaces of an electrolytic membrane. The distribution of electrolyte of thickness direction of electrode is estimated based on the alternating current impedances measured at each frequency. Another electrode containing specific electrolyte is manufactured at adjusted manufacturing conditions, based on the electrolyte distribution estimation result.    USE - Method for manufacturing solid polymer type fuel cell.    ADVANTAGE - The distribution state of electrolyte in thickness direction of electrode is estimated correctly, so that the manufacturing of fuel cell is performed easily.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart explaining the manufacturing process of fuel cell. (Drawing includes non-English language text)
NOVELTY - Producing secondary energy source from shock-treated biomass, comprises completely or partially, mechanically and/or chemically pre-treating the biomass (1, 2) of same or different type, decomposing the biomass by shock-like pressure- and/or temperature treatment (either by increasing or reducing the temperature and pressure) and removing soluble substances present in the biomass.    USE - The method is useful for producing secondary energy source from shock-treated biomass, preferably for producing gaseous- and/or liquid fuel, which are used as universal- or customized fuel e.g. biogas, biodiesel, ethanol fuel and bioactive coal.    ADVANTAGE - The process: consumes less time and less investment; avoids one-sidedly designed procedure techniques; allows the conversion of different types of biomass and shows improved recovery of fuel-pellets.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of a process flow for the production of fuels from shock-treated biomass.    Biomass (1, 2)    Fertilizer substrate (20)    Solid energy carrier (21)    Absorbent materials (22)    Bioactive coal (23)
NOVELTY - The gasifier has a tar filter installed on a gas outlet (5) and provided with a box (6) and thin tar filter plates (4). The gas outlet is installed on an upper part of the box. A gas inlet is connected to the gas outlet and installed on a lower part of the box. The tar filter plates are provided with filter holes. Neighbor filter holes are formed on a thin metal plate. The tar filter plates are overlapped in positive and opposite directions alternately in the box.    USE - Straw gasifier.    ADVANTAGE - The straw gasifier filters tar, and directly returns gas to fuel for cracking and burning process. The gasifier reduces water-vapor content in combustible gas when tar in the combustible gas is filtered.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a straw gasifier.    Cover (1)    Thin tar filter plates (4)    Gas outlet (5)    Box (6)    Furnace (7)    Air inlet (18)
NOVELTY - The grate has a grate body (2) installed with metal water-supply pipes, where two sides of the grate body are respectively provided with a water inlet tube (4) and a water outlet tube (1). Ends of the water inlet tube and the water outlet tube are provided with connection flanges (5), where length of the water inlet tube and the water outlet tube are greater than length of connection pipes of the grate body. A connection plate (3) is fixed on extending parts of the water inlet tube and the water outlet tube, where an inner side of the grate body is cambered.    USE - Straw gasification furnace grate.    ADVANTAGE - The grate has long service life, and guarantees reliable operation and gas supply of the gasification furnace. The grate improves gas calorific value and gas conversion rate.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a straw gasification furnace grate.'(Drawing includes non-English language text)'    Water outlet tube (1)    Grate body (2)    Connection plate (3)    Water inlet tube (4)    Connection flanges (5)
NOVELTY - A fats-and-oils decarboxylation decomposition catalyst (3) and fats-and-oils (I) are contacted at 350-475 degrees C to obtain biodiesel fuel containing 8-24C hydrocarbon.    USE - Manufacture of biodiesel fuel.    ADVANTAGE - The biodiesel fuel having excellent storage stability is manufactured economically and with improved productivity by a simple process using a simple apparatus. Since glycerin is not produced as a byproduct, impurities such as dienes do not remain in the product. The amount of coke generated during the process is low. The fuel has low pour point and does not produce odor or blackening.    DETAILED DESCRIPTION - A fats-and-oils decarboxylation decomposition catalyst and fats-and-oils of formula: CH(-CH2OC(=O)-R1) (-CH2OC(=O)-R3)-OC(=O)-R2 (I) are contacted at 350-475 degrees C to obtain biodiesel fuel containing 8-24C hydrocarbon of formulae: R1H, R2H, R3H and CxHy comprising major amount of 3C propane and reduced amounts of methane, ethane and butane.    R1-R3=alkyl groups comprising fats and oils, and show chain-shaped paraffin and olefin.    INDEPENDENT CLAIMS are included for the following:    (1) apparatus (1) used for manufacturing biodiesel fuel, which consists of reaction container (2) comprising the catalyst, heater (4) which heats the catalyst, the fats-and-oils, or extraction raw material, injection portion (5) which supplies an extraction raw material and fats-and-oils into the reaction container, and gas derivation portion which derives the produced gas from the reaction container; and    (2) fats-and-oils decarboxylation decomposition catalyst.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the apparatus used for manufacturing the biodiesel fuel. (Drawing includes non-English language text)    Apparatus (1)    Reaction container (2)    Fats-and-oils decarboxylation decomposition catalyst (3)    Heater (4)    Injection portion (5)    Gas introducing portion (6)
NOVELTY - An oil adhesion floor-surface purification facility comprises water supply pipe (2) which has sprinkle hole in predetermined space and is laid by upper surface of floor surface (1), water collection part (3) which can collect water that flows over surface of floor surface and is equipped with wastewater part in which wastewater flows in into exterior of floor surface and separates oil and water, oil-water separation tank which connects water tank (51), and microbial bed part in which microorganisms can live and propagate.    USE - Oil adhesion floor-surface purification facility for engine dissection of motor vehicle.    ADVANTAGE - The facility rapidly biodegrades oil and can efficiently proliferate microorganisms and the floor surface can be maintained at cleaning.    DETAILED DESCRIPTION - An oil adhesion floor-surface purification facility comprises water supply pipe (2) which has sprinkle hole in predetermined space and is laid by upper surface of floor surface (1), water collection part (3) which can collect water that flows over surface of floor surface and is equipped with wastewater part in which wastewater flows in into exterior of floor surface and separates oil and water, oil-water separation tank which connects water tank (51) in which wastewater flows in into water supply tank through water supply part and has closed circulating water system, and microbial bed part in which microorganisms can live and propagate and is provided at floor surface, water supply pipe and water collection parts.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic explanatory view of the purification facility. (Drawing includes non-English language text).    Floor surface (1)    Water supply pipe (2)    Water collection part (3)    Water tank (51)    Aeration apparatus (52)
NOVELTY - The device has a control and protection circuit provided in a load output control unit computing a conversion target value of a semi-bridge isolated direct current (DC)/direct current (DC) conversion circuit according to a loading instruction set by a computer. The control and protection circuit transmits a computed target value to a driving circuit. The driving circuit controls output of the DC/DC conversion circuit. Output power of a fuel cell generating system is loaded on a large-power non-inductive resistor by DC/DC conversion circuit.    USE - Load testing device for a fuel cell generating system.    ADVANTAGE - The driving circuit controls the output of the direct current (DC)/direct current (DC) conversion circuit, and provides the output current or output power of the fuel cell generating system to meet current or power demand of the computer. The device realizes output control of the fuel cell generating system by controlling current of an input end of the DC/DC conversion circuit, and consumes the output power of the fuel cell generating system by the large-power non-inductive resistor, so that the device is inexpensive and easy to realize, and has better adjustability.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a load testing device for a fuel cell generating system.'(Drawing includes non-English language text)'
NOVELTY - Circumfluent landscape constructed wetland without terminal comprises a main body, wetland units and wetland plants. The main body is elliptical, square or circular and is formed by connecting single wetland unit in series, which are separated from each other via partition boards. The first wetland unit has a water inlet pipe and a water distribution pipe net. The final wetland unit has a water outlet pipe. The wetland plants are planted on substrate layers of wetland units.    USE - Circumfluent landscape constructed wetland without terminal.    ADVANTAGE - The wetland saves the covering area, adds a sewage treatment flow, extends the residence time of water power, is difficult to block, has simple structure and convenient operation and maintenance, has low investment and operation costs, and has landscape effect.    DETAILED DESCRIPTION - Circumfluent landscape constructed wetland without terminal comprises a main body, wetland units and wetland plants. The main body is elliptical, square or circular and is formed by connecting single wetland unit in series, which are separated from each other via partition boards. The first wetland unit has a water inlet pipe and a water distribution pipe net. The final wetland unit has a water outlet pipe. Each unit is undercurrent constructed wetland, surface current constructed wetland or formed by arraying the undercurrent constructed wetland and the surface current constructed wetland alternately. The substrate layer of undercurrent constructed wetland comprises gravel and field soil. The surface current constructed wetland is the mixture of field soil and yellow sand. The wetland plants are planted on substrate layers of wetland units. The heights of wetland units are gradually reduced in sequence.    DESCRIPTION OF DRAWING(S) - The drawing is a perspective view of a circumfluent landscape constructed wetland without terminal.
NOVELTY - Converting methane to methanol and its derivative comprises oxidizing under the effect of an oxidant and a catalyst in 90-100 wt.% sulfuric acid at 40-400 degrees C and 0.1-15 MPa. The oxidant and the catalyst are iodine monochloride.    USE - Method for converting methane to methanol and its derivative including methanol or dimethyl ether (claimed).    ADVANTAGE - The method reduces water quantity produced during the reaction, and is inexpensive.
NOVELTY - Transforming methane to methanol and its derivatives comprises oxidizing methane under 90-100 wt.% sulfuric acid environment using oxidants and catalysts at 40-400 degrees C and 0.1-15 MPa, where the oxidants and catalysts are iodine monobromide.    USE - Method for transforming methane to methanol and its derivatives including methanol and dimethyl ether (claimed).    ADVANTAGE - The method reduces water quantity in reaction, and is inexpensive.
NOVELTY - The micro-refinery system (101) comprises a distillation tube (131) that is vertically arranged. A guide wire is provided vertically within the distillation tube. A float surrounds a portion of the guide wire and includes a magnet. A magnetometer sensor is mounted on an external surface of the distillation tube for detecting the vertical position of the float.    USE - Micro-refinery system for producing hydrocarbon such as ethanol and petrol used as fuel in internal combustion engine of motor vehicle.    ADVANTAGE - The mass and friction of the guide wire are reduced hence the obstruction of the float movement due to the fluid can be prevented. The measurement resolution of the magnetometer sensor is improved. The damage of the magnetometer sensor due to the harsh internal base column environment is prevented. The operation efficiency of the micro-refinery system is improved. The hydrocarbon production performance is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the micro-refinery system.    Fermentation tank (103)    Lid (111)    Thermoelectric mechanism (113)    Distillation tube (131)    System controller (151)
NOVELTY - Process comprises contacting a hydrocarbon feed stream comprising paraffins having at least seven carbon atoms per molecule with a composition comprising an ionic liquid supported on silica to produce a product stream comprising 4-6C light paraffins.    USE - The process is useful for producing product stream comprising 4-6C light paraffins.    ADVANTAGE - The ionic liquid is effective at mildly cracking paraffins at moderate conversion conditions.    DETAILED DESCRIPTION - Process comprises contacting a hydrocarbon feed stream comprising paraffins having at least seven carbon atoms per molecule with a composition comprising an ionic liquid supported on silica to produce a product stream comprising 4-6C light paraffins, where the ionic liquid has the structure of formula (AB1).    A = a cation capable of forming an ionic liquid; and    B1 = an anion containing aluminum and a halogen which is capable of forming an ionic liquid.
NOVELTY - Controlling pests comprising termites, fire ants and carpenter ants in an area, comprises applying at least one compound comprising 1-carvone, 1-linalool, styralyl alcohol and tetrahydrolinalool to an environment, where it is desired to control at least one of such pests.    USE - The method is useful for controlling pests comprising termites (Formosan subterranean termites), fire ants and carpenter ants in an area (claimed). Tests details are described but no results given.    ADVANTAGE - The composition is non-toxic to humans, biodegradable and environmentally safe. The method/composition provides at least 50% of mortality of termites in 2 days and up to 100% of mortality of termites in 1 day.
NOVELTY - An electrode (120) has a conductor (121) and n-type semiconductor layer (122) to which light is irradiated to generate hydrogen. Size of band edge levels of conduction band and valence band in surface vicinity region of semiconductor layer is larger than that of junction surface vicinity region between semiconductor layer and conductor. Fermi level of junction surface vicinity region of semiconductor layer is larger than that of surface vicinity region of semiconductor layer. Fermi level of conductor is larger than that of junction surface vicinity region of semiconductor layer.    USE - Photoelectrochemical cell used in energy system e.g. domestic-use electric power generation system.    ADVANTAGE - Since the charge separation of the electron and hole are produced by light excitation, the quantum efficiency of hydrogen produced due to irradiation of light on semiconductor layer, can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for energy system.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the photoelectrochemical cell.    Photoelectrochemical cell (100)    Electrode (120)    Conductor (121)    Semiconductor layer (122)    Electrolyte (140)
NOVELTY - A micro-oxygen biotreatment of honey alcohol wastewater by supplying oxygen from air, comprises establishing a micro-oxygen reactor; applying an oxidation-reduction potential controller and a blast blower to control oxidation-reduction potential of liquid in a reflux barrel; making liquid reflow into the micro-oxygen reactor to form the micro-oxygen environment; and then using active sludge in micro-oxygen reactor to remove organic substance and sulfate from wastewater.    USE - Micro-oxygen biotreatment of honey alcohol wastewater.    ADVANTAGE - The method simultaneously realizes the sulfate reduction, the sulfide oxidation and methane production in the same reactor.    DESCRIPTION OF DRAWING(S) - The drawing is a block diagram of a micro-oxygen biotreatment technique of honey alcohol wastewater (Drawing includes non-English language text).
NOVELTY - The science tool comprises a main body, in which multiple wheels are installed at the lower part. A bio-reactor (2) is installed on the top of the main body for mixing the yeast with the food waste put inside the bio-reactor for fermentation. An evaporator (3) is connected to one side of the bio-reactor, which separates the ethanol generated in the bio-reactor. A heater (4) is connected to the bio-reactor, which heats the water flowed in through a circulating pump (7). A cooling device (5) is connected to the evaporator for cooling the gaseous ethanol disappearing due to heating of the heater.    USE - Science tool for environment-friendly education of food waste fermentation process.    ADVANTAGE - The bio-reactor is installed on the top of the main body for mixing the yeast with the food waste put inside the bio-reactor for fermentation, where an evaporator is connected to one side of the bio-reactor, which separates the ethanol generated in the bio-reactor, and a cooling device is connected to the evaporator for cooling the gaseous ethanol disappearing due to heating of the heater, and thus enables an easy and efficient way of education with direct experience of the food waste fermentation process with yeast, and production of ethanol.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a science tool.    Bio-reactor (2)    Evaporator (3)    Heater (4)    Cooling device (5)    Circulating pump (7)
NOVELTY - Processing a carbohydrate/hydrocarbon-containing material, comprises irradiating a combination formed by combining a carbohydrate/hydrocarbon-containing material with an inorganic material.    USE - The method is useful to produce a fuel, such as ethanol and/or butanol (e.g. n-butanol) by fermentation, pharmaceuticals, and/or food products.    ADVANTAGE - The method is eco-friendly.
NOVELTY - Preparing kerosene fraction comprises: performing hydrotreating/hydrocracking operated under a pressure of 20-120 bars and at 250-500 degrees C, preferably 350-400 degrees C, of a hydrocarbon charge comprising a charge of petroleum origin and a charge of biological origin having vegetable oils and/or animal fats; and splitting for recovering the kerosene fraction, where the fraction has a boiling point of less than 300 degrees C, preferably less than 240 degrees C.    USE - The process is useful for the preparation of the kerosene fraction, which is useful: for the formulation of a jet fuel so that it meets the specifications of JetAl; as charge for petrochemical processes, such as steam cracking; and for formulating specialty products, such as solvents, ink diluents and paints, thinners and pesticides.    ADVANTAGE - The process provides kerosene fraction with good quality and high yield. The process is cost effective and rapid to prepare the kerosene fraction.    DETAILED DESCRIPTION - Preparation of kerosene fraction comprises: performing a hydrotreating or hydrocracking operated under a pressure of 20-120 bars and at a temperature of 250-500 degrees C, preferably 350-400 degrees C, of a hydrocarbon charge comprising a charge of petroleum origin and a charge of biological origin comprising vegetable oils and/or animal fats of which at least 5 wt.% of fatty acid has a chain length of less than or equal to 14 carbon atoms with respect to the total weight of triglycerides, preferably at least 20 wt.%, or at least 50 wt.%; and splitting for recovering the kerosene fraction, where the fraction has a boiling point of less than 300 degrees C, preferably less than 240 degrees C.
NOVELTY - Method for biologically degrading microcystin (MC) with microorganisms, involves using high cell concentration of cultured Sphingomonas sp. strain USTB-05 solution, or enzyme extracted from cell as biocatalyst, removing MCs in water by adding the biocatalyst, or applying the biocatalyst to sewage containing MCs to degrade and remove MCs.    USE - The method is useful for biologically degrading microcystin with microorganisms.    ADVANTAGE - The method is safe, economical and efficiently degrades and removes MCs generated by cyanobacterial bloom.
NOVELTY - A raw material containing carbon dioxide and hydrogen is pre-processed to obtain mixed gas. Additive chosen from propane, sulfur hexafluoride and tetra-n-butyl ammonium bromide is added to the obtained mixed gas, reacted and cooled to obtain carbon dioxide hydrate. Thus, method of pre-combustion decarbonization is carried out.    USE - Method of pre-combustion decarbonization used for carbon capture storage field for power generation.    ADVANTAGE - The pre-combustion decarbonization method is carried out economically and efficiently.
NOVELTY - The device has column-tapered tank main portion (1) provided with stirring devices (2,3). The water inlets (a) and sludge discharging holes (c) are uniformly distributed at the bottom portion of the tank. An umbrella-shaped baffle plate (4) is arranged under the biogas outlet formed at the top portion of the tank main. The water feeding pipe (5) and sludge discharging pipe (6) are connected with the water inlet and sludge discharging hole.    USE - High-temperature anaerobic fermentation device for biogas purification treatment.    ADVANTAGE - Water can be distributed uniformly at the bottom of the tank and the homogenizing effect of the tank is improved. The discharge of sludge and water through gas outlet is suppressed, so as to improve the subsequent biogas purification treatment. The safety of the tank unit is ensured by suppressing the interference of loads of tanks in the tank unit. The average chemical oxygen demand (COD) removal rate can be maintained stable at more than 85% when the high-temperature anaerobic fermentation device works normally, and the coarse biogas yield of a single device can be made 30000 cubic meter. The device can be utilized to build large scale of tank units to save 10-30% of the total investment.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the high-temperature anaerobic fermentation device.    Tank main portion (1)    Stirring devices (2,3)    Umbrella-shaped baffle plate (4)    Water inlet (a)    Sludge discharging hole (c)    Water feeding pipe (5)    Sludge discharging pipe (6)
NOVELTY - Microbial preparation comprises culture medium and strain, where the strain comprises Bacillus licheniformis, B.subtilis, B.pumilus, B.coagulans, Saccharomyces cerevisiae and Streptomyces chingyangensis. The total viable count of each gram of the microbial preparation is 0.5-1x 1010. The viable count of B.licheniformis is 10-20%, B.subtilis is 10-20%, B.pumilus is 10-20%, B.coagulans is 10-20%, S.cerevisiae is 5-15%, and S.chingyangensis is 5-15%.    USE - The microbial preparation is useful in preparation of fermented base material that is useful in poultry and livestock growing regions for processing livestock and poultry manure, where the livestock and poultry includes pig, cow, sheep, rabbits, and birds (all claimed).    ADVANTAGE - The microbial preparation rapidly decomposes the organic matter in livestock and poultry manure, effectively removes the stink in livestock and poultry manure, and decreases the content of hazardous substance in the excrement. The microbial preparation processed manure is utilized as raw material for producing organic fertilizer and thus environmental pollution is not caused by livestock and poultry manure.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) method for preparing microbial preparation, involves inoculating B.licheniformis, B.subtilis, B.pumilus, B.coagulans, S.cerevisiae and S.chingyangensis to culture medium, and then culturing to obtain microbial preparation; and (2) method for processing livestock and poultry manure, involves inoculating the microbial preparation into the base material, fermenting the base material, and contacting the fermented base material with livestock and poultry manure.
NOVELTY - An agrochemical composition comprises humic acid (8-12%), validamycin (3-5%), ethiofencarb (80-90%), and imidacloprid (5-9%).    USE - Agrochemical composition for preventing Cnaphalocrocis medinalis, rice planthopper, banded sclerotial blight, snout moth larva, false smut and panicle blast.    ADVANTAGE - The composition is environment friendly and has effective rate of 92.3% against Cnaphalocrocis medinalis, 98.3% against rice planthopper and 85.2% against banded sclerotial blight.
NOVELTY - Healthcare pillow comprises upper woven layer and lower woven layer, where multiple medicine bags are equipped between the upper woven layer and lower woven layer according to positions of acupuncture points on the rear part of human head. The sizes of the upper and lower woven layers match with the size of the pillow towel.    USE - The healthcare pillow is useful for massaging and lowering blood pressure (claimed), and for treating dizziness, headache, tonsillitis, toothache, aphasia, epilepsy, cervical spondylosis, panasthenia, stroke, insomnia, cough, asthma, and brain ischemia.    ADVANTAGE - The medicine bag of healthcare pillow is non-toxic, convenient to use and eco-friendly, and does not cause side effects.
NOVELTY - A water treatment comprises adding perferrate to slightly polluted water for 5-30 minutes of pre-oxidation while controlling addition amount of perferrate to 0.3-1.5 mg/L; and flowing water subjected to pre-oxidation treatment in biological active filter tank from top and flowing water out from bottom, where upper layer of biological active filter tank is active carbon layer that is 60-80 cm high, while lower layer is quartz sand layer, and filtering speed is 6-9 m/hour.    USE - Method for treatment of water.    ADVANTAGE - The method conserves energy, and eliminates organic pollutants without changing conventional process flow or increasing large devices.
NOVELTY - Biological ball for purifying water and improving water quality, is prepared using raw materials comprising (in %mass) seaweed processed by bacteria (10-15), various auxiliary materials (60-96) and various additives (10-30).    USE - The biological ball is useful for purifying water and improving water quality (claimed) by decomposing impurity in sewage, degrading harmful amino nitrogen in sewage, removing harmful ammonia and harmful sulfureted hydrogen, removing unpleasant smell, improving dissolved oxygen concentration and removing underwater pollution.    ADVANTAGE - The biological ball purifies water rapidly and is prepared by simple process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparation of the above-cited biological ball, which involves (a) obtaining the bacterial strain preserved in refrigerator and culturing in seaweed slurry at not greater than 35 degrees C for 3-5 days, (b) sterilizing wood fiber, mineral powder, sand, wheat husk, bean pulp and zeolite powder into a sterilizer at high temperature for 24 hours, (c) mixing molasses, water, salt, amino acid, cultured bacterial liquid and the mixture sterilized in step (b), pouring the mixture into a stirring tank and stirring the mixture, reacting at normal temperature and normal pressure after the mixture is stirred, and (d) using pelletizer to prepare the obtained mixture into elliptic ball with even shape and smooth surface, and then packing the elliptic balls using a vacuum packing machine to obtain finished product.
NOVELTY - Methane is reacted with hydrogen bromide/water, and oxygen in presence of primary catalyst, to obtain alkyl bromide. The primary catalyst is composite catalyst obtained by mixing metal compound precursor and silicon precursor, hydrolyzing, drying and calcinating.    USE - Preparation of alkyl bromide used for preparation of 3-13C higher hydrocarbon, and methanol and dimethyl ether (both claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparation of 3-13C higher hydrocarbon; and    (2) preparation of methanol and dimethyl ether, which involves reacting alkyl bromide with water in presence of secondary catalyst.
NOVELTY - A drain deblocking and/or freshening agent comprises enzyme(s) including peptidase, endopeptidase or proteinase; bacterial strain(s) from genus Bacillus; and a fragrance. It further comprises water softener and carrier medium.    USE - Drain deblocking and/or freshening agent in tablet form for shower drainage systems.    ADVANTAGE - The drain deblocking and/or freshening agent can prevent the build up of hair and other waste products within the drain, and is environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a drain deblocking and freshening dispenser (2) comprising a housing for receiving a drain deblocking and/or freshening agent. The housing has a mechanism to allow fluid flow and locatable in the wastewater outlet that is above standing water.    DESCRIPTION OF DRAWING(S) - The drawing shows a plan view of a dispenser.    Dispenser (2)    Receptacle (4)    Oval formations (8)
NOVELTY - The chromatograph has an organic gas analyzing system provided with a six way valve, and an alumina capillary column connected to a hydrogen flame detector. An inorganic gas analyzing system is provided with a ten-way valve and a pin-shaped valve, and pre-truncating filling column is connected with a thermal conductivity detector. A data processing system i.e. chromatogram data collecting station computes collected data of different channels in the organic gas analyzing system and inorganic gas analyzing system.    USE - Gas chromatograph for analyzing inorganic gas and organic gas such as oxygen, nitrogen, carbon monoxide, carbon dioxide, methane and ethane gas.    ADVANTAGE - The chromatograph can analyze more than 20 kinds of organic gas, and is convenient to operate and inexpensive. The chromatograph reduces system error.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a gas chromatograph. '(Drawing includes non-English language text)'
NOVELTY - The suspension is pre-treated by mild dewatering and then subjected to vibrating membrane filtration.    USE - For generating green electricity from manure and other organic waste.    ADVANTAGE - The heat generated during biogas combustion is sufficient to be able to dry and sterilise the solid fraction.    DETAILED DESCRIPTION - A process for separating an aqueous liquid suspension of organic material into a concentrated solid fraction and a liquid fraction with a low solids content comprises an optional coagulation and flocculation step, a preliminary mechanical separation step comprising at least one so-called mild dewatering stage, and a subsequent membrane filtration step comprising vibrating membrane filtration. INDEPENDENT CLAIMS are also included for the following:    (1) Apparatus for carrying out this process;    (2) Energy-efficient integrated treatment method for manure and/or at least one organic waste stream, comprising bio-fermentation of the waste and recovering the biogas; burning the biogas in a motor to produce electricity and heat; separating the sludge from the bio-fermentation step into a wet solid fraction and a liquid fraction with a low solids content using a preliminary mechanical separation step comprising at least one mild dewatering stage, followed by vibrating membrane filtration; and drying the solid fraction using the heat generated during burning of the biogas; and    (3) Installation for performing this treatment method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram representing the separation process.
NOVELTY - A composite methanol gasoline comprises (wt.%) methanol (65-75), coal oil (20-24), ether (3-5), auxiliary agent (0.8-1), high corrosion inhibitor (0.4-0.6), detergent (0.2-0.4), and combustion improver (0.5-0.7).    USE - A composite methanol gasoline.    ADVANTAGE - The gasoline can be prepared using stable and simple method, and is inexpensive.    DETAILED DESCRIPTION - A composite methanol gasoline comprises (wt.%) methanol (65-75), coal oil (20-24), ether (3-5), auxiliary agent (0.8-1), high corrosion inhibitor (0.4-0.6), detergent (0.2-0.4), and combustion improver (0.5-0.7). It is prepared by mixing the auxiliary agent, high corrosion inhibitor, detergent, combustion improver, coal oil, and ether; uniformly stirring at normal temperature and normal pressure; and adding methanol, and uniformly stirring at normal temperature and pressure.
NOVELTY - Microorganisms including Microbacterium oxydans M101 (KCTC 11366BP), Rhodobacteraceae bacterium M116 (KCTC 11367BP) and Pseudomonas marincola M157 (KCTC 11368BP) capable of decomposing oil, are new.    USE - The microorganisms are useful in agent for decomposing oil in marine water (claimed).    ADVANTAGE - The oil can be decomposed by a cost-effective process.
NOVELTY - A gas liquid two-phase cultivation comprises using solution simulating the components of targeted waste gas or mixture of the solution and gas as a nutrition source to domesticate and cultivate a strain for 5-20 days; and spraying directly the mixed strain liquid obtained from cultivation on the biological packing in a biological reactor to start immediately the biological reactor used for treating the targeted waste gas.    USE - Method of gas liquid two-phase cultivation (claimed) for biological treatment of waste gas.    ADVANTAGE - The method removes pollutants, saves cultivation cost, directly uses liquid matters with the same property as substrate thus eliminating the difficulty on the operation caused by the toxic and harmful gas during the cultivating process; and employs microorganisms having the desired activity and a simple device having flexible operation and strong adaptability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a cultivation device comprising:    (1) a cultivation jar;    (2) an analog waste gas distribution system;    (3) an electrical control device;    (4) a liquid adding system;    (5) a nutrition liquid adding system;    (6) a tail gas purifying system;    (7) a strain inlet;    (8) a liquid adding port;    (9) a tail gas discharging port;    (10) a temperature probe;    (11) a pH probe;    (12) a heater;    (13) a micropore gas distributor; and    (14) a waste gas inlet and outlet.
NOVELTY - Method of producing straw bacterial manure, involves inoculating Trichoderma spp. to potato dextrose agar (PDA) culture medium, culturing, inoculating culture to seed bacterial culture medium and fermenting (F1) to obtain seed bacterial fermented liquid, inoculating the seed bacterial fermentation liquid to solid culture medium and fermenting (F2) to obtain solid fermented substance, drying, mixing plant straws with dried solid fermented substance, and fermenting (F3) to obtain the straw bacterial manure.    USE - The method is useful for producing straw bacterial manure (claimed).    ADVANTAGE - The straw bacterial manure can be obtained rapidly with controlled quality.    DETAILED DESCRIPTION - Method of producing straw bacterial manure, involves inoculating Trichoderma spp. to a potato dextrose agar (PDA) culture medium, culturing, inoculating the culture to seed bacterial culture medium and fermenting (F1) to obtain seed bacterial fermented liquid, where the seed bacterial culture medium comprises (in g) potato (200), glucose (20), magnesium sulfate heptahydrate (0.5), ferrous sulfate heptahydrate (0.0075), manganese sulfate (0.0025), zinc sulfate (0.002), potassium dihydrogen phosphate (3.83), sodium nitrate (1.42), ammonium sulfate (1.1), calcium chloride (1), and water (1000 ml), inoculating the seed bacterial fermentation liquid to solid culture medium and fermenting (F2) to obtain solid fermented substance, drying, where the solid culture medium is obtained by mixing rice straw powder with wheat bran at weight ratio of 9:1 and adding ammonium sulfate (1 g), Tween 20 (RTM: polysorbate 20) (0.1 g) and water (100 ml) to every 100 g of mixture to obtain the solid culture medium, mixing plant straws with dried solid fermented substance, and fermenting (F3) to obtain the straw bacterial manure.
NOVELTY - A process for preparation of fuel briquettes from agricultural waste comprises pulverizing agricultural waste, adding binder such as cow dung, clay, molasses or starch to the pulverized agricultural waste and then subjecting the same to the step of briquetting in a screw extruder, at a pressure of 4-10 kg/cm2. Image 1/1
NOVELTY - A desulfurization system (10) comprises desulfurizer (11) which heats and de-sulfurizes introduced lamp oil with heater and produces de-sulfurized lamp oil, heater (13) which power-receives electric power and heat-generate from main power supply (99), de-sulfurized lamp oil tank (15) which stores de-sulfurized lamp oil, and control apparatus (81) which controls desulfurizer to perform desulfurization in predetermined time slot when electric power load of mains power supply is small.    USE - A desulfurization system used for fuel cell system (claimed).    ADVANTAGE - The desulfurization system can contribute to leveling of electric power load of main power supply, and reduces influence of power consumption of heater at the time of desulfurization to external electric power load.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a systematic diagram of fuel cell system containing desulfurization system. (Drawing includes non-English language text).    Desulfurization system (10)    Desulfurizer (11)    Heater (13)    De-sulfurized lamp oil tank (15)    Control apparatus (81)    Main power supply (99)
NOVELTY - The method involves removing particulate matter contained in fat and oil by using a filter (A) or a settling tank (B). Fatty acid included in raw material is removed by removing phospholipid inclusion and metal component through vacuum and steam distillation process. Residue fatty acid remaining behind after reaction is removed by mixing the residue fatty acid with alkali after distillation process. Soap generated in the residue fatty acid is removed through a centrifuge (F). Water contained in the raw material is removed.    USE - Method for manufacturing a bio-diesel raw material (claimed). Uses include but are not limited to manufacturing bio-diesel raw material from disposable edible oil, distillers dried grains with soluble (DDGS) corn oil, Jatropha stock, lard, tallow, and chicken fat.    ADVANTAGE - The particulate matter contained in fat and oil is removed by processing regularly using a chemical method so as to produce biodiesel raw material effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic illustration of a bio-diesel raw material manufacturing method.'(Drawing includes non-English language text)'    Filter (A)    Settling tank (B)    Centrifuge (F)    Mixer (J)    Extractor (L)
NOVELTY - The method involves passing a product gas such as hydrogen or oxygen through a gas pressure booster. The gas pressure booster is powered by using a drive substance such as water or a drive gas such as oxygen or hydrogen produced at a pressure of at least 10 bar by a self-pressurized electrolyzer. The pressure of the product gas in a product gas line is increased by the powered gas pressure booster.    USE - Method of increasing pressure of product gas such as compressed natural gas (CNG), oxygen or hydrogen for hydrogen internal combustion engine of motor vehicle.    ADVANTAGE - The energy demand is reduced and the balance of a plant is simplified, since the gas pressure booster is powered by using drive substance or gas produced by the self-pressurized electrolyzer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for combination of gas pressure booster powered by drive gas and electrolyzer.
NOVELTY - The drying and carbonization apparatus has a drying chamber (2) with a cylinder (6) that is arranged with a screw conveyor (12) along the vertical direction. A discharge port is extended towards the cylinder outside the drying chamber, and an exhaustion branch pipe (9) connected with a meander exhaust pipe (10) is attached to the cylinder along the length direction.    USE - Apparatus for drying and carbonizing water organic refuse, hen droppings and soybean curd residue.    ADVANTAGE - The to-be-burned materials can be burned easily and the carbonized efficiently while reducing the fuel cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of the drying and carbonization apparatus. (Drawing includes non-English language text)    Drying chamber (2)    Cylinder (6)    Exhaustion branch pipe (9)    Meander exhaust pipe (10)    Screw conveyor (12)    Air supply piping (18)
NOVELTY - The sensor has a power-down signal output circuit connected with a corresponding port of a single chip. A carbon monoxide detecting circuit, a signal magnify circuit and an analog to digital (A/D) convertor are connected with each other. The A/D convertor, an outside memorizer, the carbon monoxide signal display circuit, the carbon monoxide signal output circuit and a key board and remote control receiving circuit are connected with a corresponding port of the single chip. The detecting element of the carbon monoxide detecting circuit is connected with the electrode protecting device.    USE - Methane and carbon monoxide combination sensor.    ADVANTAGE - The sensor is simple in structure, and monitors concentration of methane and carbon monoxide. The sensor is inexpensive, consumes less power with higher price ratio and convenient in scene construction.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a methane and carbon monoxide combination sensor.'(Drawing includes non-English language text)'
NOVELTY - A Briquetting machine has a jumper head inserted into the working room on a stander; feed-in equipment set over the working room; a shaping mold that corresponds with the jumper head set in the working room. Shaping mold is formed as taper with large inlet and small outlet. The outlet end of shaping mold is connected with a typing sleeve set with heating equipment. The outlet end of typing sleeve is set with a freezing mechanism.    USE - Briquetting machine for pressing biomass such as agricultural and forestry waste into solid fuel blocks used as source of fuel of e.g. boiler, cooker.    ADVANTAGE - Increases heat energy, decreases waste, ensures saving of energy, and prevents contamination of the environment by processing biomass such as agricultural and forestry waste into solid fuel blocks.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the briquetting machine.
NOVELTY - Treatment of rice flour wastewater comprises dropping effective microorganisms (EM) in the wastewater; uniformly stirring and mixing; feeding the wastewater into an aeration tank; continuously dropping EM in the aeration tank; hanging EMX ceramic in the wastewater; aerating the wastewater for 6-12 hours in an intermittent manner; and depositing the wastewater in a deposition tank; continuously hanging EMX ceramic in the deposition tank; depositing the water; and feeding the water into a clean water tank; filtering the water through the EMX ceramic; and dropping EMX in the filter tank.    USE - Method for treatment of rice flour wastewater (claimed).    ADVANTAGE - The method is simple and low cost. The discharged water is accordant with the level of running water. The processed water can be drunk, irrigated, or used as clean water for further use. The clean water is free from odor smell, slurry, mosquito and fry; and is beneficial for environment beautifying.    DETAILED DESCRIPTION - Treatment of rice flour wastewater comprises:    (A) dropping EM in the wastewater which is held in an original water regulation tank at a volume ratio of 1: 500-2000; uniformly stirring and mixing; feeding the wastewater into an aeration tank;    (B) continuously dropping EM in the aeration tank at EM to slurry volume ratio of 1: 200-2000; hanging 500-1000 g EMX ceramic in the wastewater in terms of 1 ton of water; aerating the wastewater for 6-12 hours in an intermittent manner; and depositing the wastewater in a deposition tank;    (C) continuously hanging 500-1000 g EMX ceramic in the deposition tank in terms of 1 ton of water; depositing the water from the deposition tank; and feeding the water into a clean water tank; and    (D) filtering the water through the EMX ceramic in the clean water tank; dropping EMX in the filter tank at EMX to water volume ratio of 1: 5000-10000; and discharging or using the water till satisfying the standard of regenerated water.
NOVELTY - A microbial fuel cell (100) for generating electrical power comprises a chamber that defines an inlet (130) and an outlet and having a top side defining a horizontal plane, and an anode and a first cathode (114) associated with the chamber. The anode is defined in part(s) from granular activated carbon.    USE - A microbial fuel cell for generating electrical power from fluid source, preferably wastewater (claimed).    ADVANTAGE - The fuel cell can convert the potential energy inherently present in wastewater into useful electrical energy while treating the wastewater for subsequent use.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for generation of electrical power from fluid source.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a single-chamber microbial fuel cell.    Fuel cell (100)    Cathode (114)    External resistor (122)    Electrical circuit (124)    Inlet (130)
NOVELTY - A polymer electrolyte membrane is manufactured by preparing an emulsion polymerization solution by mixing a vinyl-based monomer, an anionic surfactant, and a radical polymerization initiator in water; dipping a proton-conductive polymer membrane in the emulsion polymerization solution to swell the membrane; and performing an emulsion polymerization of the monomer embedded inside the swelled proton-conductive polymer membrane to form a polymer micelle (100).    USE - Method of manufacturing a polymer electrolyte membrane for a fuel cell (claimed).    ADVANTAGE - The method manufactures a membrane having smaller, but more densely distributed internal channels thus having improved proton conductivity to suppress cross-over of a fuel through the polymer electrolyte membrane.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for membrane-electrode assembly for a fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a polymer micelle included inside a hydrophilic channel of a polymer electrolyte membrane.    Polymer micelle (100)    Vinyl-based polymer (110)    Anionic surfactant (120)    Hydrophobic part (121)    Hydrophilic channel (130)
NOVELTY - Mixed phase, non-stoichiometric titania photocatalyst material as deposited on a substrate, is claimed, where the material is responsive to UV and visible illumination, and is non-stoichiometric in terms of its oxygen content.    USE - The photocatalyst material is useful for the photocatalytic reaction of a reactant, preferably the photoreduction of carbon dioxide to methane (all claimed).    ADVANTAGE - The mixed-phase titanium dioxide material enhances photoactivity largely due to the synergistic interactions between anatase and rutile phases, which serve to extend their photoresponse to longer wavelengths of light. The material is a highly reactive and a UV and visible light responsive photocatalyst as deposited on a substrate (i.e. without the need for a subsequent thermal treatment). The material shows a marked red-shift in photoresponse. The sputtering creates metastable structures that are not possible by equilibrium based chemical processes and also creates stabilized interfacial defect sites, obviating the need for anion/cation dopants in so much as they are used to create a population of defects such as vacancies.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) method-1 of photocatalytically reacting a reactant, comprising contacting the reactant and the photocatalyst material under UV or visible light illumination;    (2) method-2 of photoreduction of carbon dioxide to methane, comprising contacting the carbon dioxide and the photocatalyst material under UV or visible light illumination; and    (3) making the titania photocatalyst material, comprising removing titanium atoms from a target in the presence of oxygen whose concentration is limited in a manner to deposit a mixed phase, non-stoichiomeric titania material on a substrate.    DESCRIPTION OF DRAWING(S) - The figure shows deposited nanocomposite titania film structure (plan view and cross-sectional view) of low angle deposited film (normal oxygen content).
NOVELTY - A wastewater-processing apparatus consists of a wastewater-treatment tank (2) for purifying wastewater containing organic matter using useful microorganisms and silicon coagulant, an active-oxygen supplier (3) for supplying active oxygen, such as superoxide anions, and a filter (4) for filtering the treated wastewater.    USE - Apparatus is used for processing organic wastewater (claimed) e.g. sewage, human waste, and other organic wastewater.    ADVANTAGE - The apparatus is compact, and effective in reducing the amounts of consumable supplies for use in water treatment, such as coagulant and filtration film, and in shortening the time necessary for wastewater treatment. The apparatus enables economical processing of organic wastewater. Clogging of filter by floc is prevented. Thus, by decomposing the organic matter taken in by the floc, discarded sludge is reduced and discarding of silicon coagulant with the sludge is prevented. The usage amount of silicon coagulant is reduced. Superoxide dismutase can be supplied by a simple and reliable method.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for organic-wastewater processing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the organic-wastewater processing apparatus.    Natural-water tank (1)    Wastewater-treatment tank (2)    Active-oxygen supplier (3)    Filter (4)    Discharge tank (9)
NOVELTY - Process auxiliary material for introducing into a substrate of a biogas plant comprises trace elements, preferably iron(III) chloride.    USE - The process auxiliary material is useful in the production of biogas.    ADVANTAGE - The process auxiliary material is an acidic medium which increases the solubility of the trace elements allowing their optimal dispersion within the substrate, thus significantly improving the availability of the essential trace elements for the microorganisms resulting in an increased methane production and increased efficiency of the biogas plant. The addition of the auxiliary material based on the substrate analysis avoids fluctuations in the efficiency of the biogas plant providing an optimized and stable fermentation process with high methane yield and high use of the digestate as a fertilizer. The iron (III) chloride helps in the precipitation of sulfur, thus improving the availablity of the trace elements.
NOVELTY - Preparing an electrode comprises: (i) preparing a dispersion of a polyoxometalate and a conductive material having a positive charge in a solvent; (ii) depositing the obtained suspension on a carbon support; (iii) drying the suspension; and (iv) applying a binder to the dried suspension to obtain an electrode.    USE - The electrode is useful for the production of hydrogen.    ADVANTAGE - The raw materials used in the process are inexpensive, hence cost effective.
NOVELTY - Method for isolating wooden component, involves subjecting biomass resources as starting material to microbial cell treatment process using Basidiomycete and wood-rotting fungi, subjecting the processed material to high pressure hydrothermal processing process by hot water at high pressure, and separating wooden component from the processed material of the high pressure hydrothermal processing process as a solid residue.    USE - The method is useful for isolating wooden component such as lignin (claimed), cellulose and hemicellulose that are useful as raw material in foodstuff and pharmaceuticals.    ADVANTAGE - The lignin, cellulose and hemicellulose are obtained without using chemicals such as strong acid and without production of fermentation inhibitory byproducts such as furfural and monosaccharides such as glucose and xylose, cellooligosaccharide and xylo oligosaccharide. The method recycles biomass resources from agriculture and fermentation brewing industry.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) wooden component obtained by the above-mentioned method;    (2) industrial material comprising the wooden component; and    (3) apparatus for separating wooden component, comprising microbial cell processing apparatus accommodating Basidiomycete and wood-rotting fungi, high pressure hydrothermal processing apparatus for processing the processed material of microbial cell processing apparatus by hot water, and separation apparatus for separating a solid residue from the processed material high pressure hydrothermal processing apparatus.
NOVELTY - A fluidity improver consists of ( alpha )-olefin polymer having weight average molecular weight of 50000-500000 obtained by polymerizing ( alpha )-olefin mixture of 8C ( alpha )-olefin and 14-18C ( alpha )-olefin. The molar ratio of 8C ( alpha )-olefin with respect to 14-18C ( alpha )-olefin is 10/90-60/40.    USE - Fluidity improver is used for biodiesel fuel oil composition (claimed) for gasoline-powered car and diesel car.    ADVANTAGE - The fluidity improvers has excellent stability improvement effects in low temperature such as clogging point improvement effect and pour point improvement effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biodiesel fuel oil composition containing 10-10000 ppm of fluidity improver.
NOVELTY - The method involves filling fine granular biomass particles (11) from hopper (3) in reaction container (2) which is heated to obtain a solid substance at specific pressure range. The pressurization piston (6) is slid up and down along internal peripheral surface of reaction container from upper portion of hopper so as to maintain desired pressure in reaction container. Filling of fine granular particles is stopped only if detected pressure value and height position of the pressurization piston are in preset range.    USE - Manufacturing method of biocoke for use as fuel in iron manufacturing industry and electric power generation plant using boiler. Can also be used in casting production, cupola furnace, blast furnace as reducing agent, baking fuel, slaked lime, etc.    ADVANTAGE - Filling time of granular particles can be shortened and filling efficiency can be improved. Size and cost reduction of manufacturing installation can be attained.    DETAILED DESCRIPTION - The biocoke manufacturing method involves obtaining solid substance by heating fine granular biomass particles before half carbonization. The molded object is allowed to cool while reducing the pressure in the reaction container. The cooled molded object is discharged. An INDEPENDENT CLAIM is included for biocoke manufacturing apparatus.    DESCRIPTION OF DRAWING(S) - The drawings show the sectional views of the biocoke manufacturing apparatus.    Reaction container (2)    Hopper (3)    Piston (6)    Fine granular biomass particles (11)    Conveying section (15)
NOVELTY - A solution (A) (11) containing silver ion and rhodium ion, and solution (B) (12) containing reducing agent are prepared. Then, any one solution (A or B) (21) is sprayed on other solution (22), to obtain silver-rhodium alloy microparticles.    USE - Manufacture of silver-rhodium alloy particles used for catalyst for synthesis of organic compounds, and electrode catalyst for fuel cell.    ADVANTAGE - The method provides silver-rhodium alloy particles in which silver and rhodium forms into a solid solution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for silver-rhodium alloy particles.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view explaining the manufacture of silver-rhodium alloy particles.    Solution A (11)    Solution B (12)    Solution (21)    Other solution (22)
NOVELTY - The engine has an engine main body (5) provided with a spark plug (13) to ignite supplied fuel, where base fuel is changed to reformation fuel using heat and dehydrogenation catalyst of exhaust gas. Exhaust gas is discharged from the engine main body. A reactor (6) generates hydrogen, and drives the engine main body by supplying the base fuel and reformation fuel to the engine main body. Hydrogen supplied to the engine main body is burned. Fuel and the air-fuel mixture of air are compressed.    USE - Gasoline engine i.e. spark-ignition type gasoline engine, for use in a motor vehicle. Can also be used for a spark ignition direct injection type gasoline engine and a homogeneous charge compression ignition type gasoline engine.    ADVANTAGE - The reactor generates hydrogen, and drives the engine main body by supplying the base fuel and reformation fuel to the engine main body, so that heat of exhaust gas can be used effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a gasoline engine.'(Drawing includes non-English language text)'    Base fuel tank (1)    Pump (2)    Injection valve (3)    Engine main body (5)    Reactor (6)    Spark plug (13)
NOVELTY - Fuel cell system comprises modifier, carbon monoxide reduction apparatus (6), anode pole, case body (61), heat exchanger tube (62), gas diffusion chamber (63), catalytic reaction chamber connected to the gas diffusion chamber through a 1st dispersing plate (64), gas convergence chamber with an outflow port connected to the catalytic reaction chamber through 2nd dispersing plate, and flow-hole which distributes reformed gas into clearance gap between support plates and case body.    USE - A fuel cell system.    ADVANTAGE - Implements efficient catalytic reaction.    DETAILED DESCRIPTION - Fuel cell system comprises modifier which generates reformed gas with a modification catalyst, carbon monoxide reduction apparatus with a carbon monoxide reduction catalyst, anode pole which produces electric power by electrochemical reaction, case body, heat exchanger tube which cools or heats the modification catalyst or carbon monoxide reduction catalyst, gas diffusion chamber with a inflow port, catalytic reaction chamber connected to the gas diffusion chamber through a 1st dispersing plate, gas convergence chamber with an outflow port connected to the catalytic reaction chamber through 2nd dispersing plate, and flow-hole which distributes reformed gas into clearance gap between support plates and case body.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the carbon monoxide reduction apparatus.    Carbon monoxide reduction apparatus (6)    Case body (61)    Heat exchanger tube (62)    Gas diffusion chamber (63)    1st dispersing plate (64)
NOVELTY - A fuel cell has an air electrode for reducing oxygen, a fuel electrode for oxidizing hydrogen, a membrane electrode assembly (11), a pair of mask with opening (17,20), and a hydrogen producing substance accommodating portion (22) provided at space formed at side of fuel electrode sealed with membrane electrode assembly and housing (21). The membrane electrode assembly consists of solid electrolyte arranged between positive electrode and negative electrode, and in which water or water vapor is impregnated and ion conductivity is produced.    USE - Fuel cell e.g. polymer electrolyte fuel cell is used as power supply for portable electronic device.    ADVANTAGE - The fuel cell has excellent output characteristics and simple structure.    DETAILED DESCRIPTION - A fuel cell has an air electrode for reducing oxygen, a fuel electrode for oxidizing hydrogen, a membrane electrode assembly, a pair of mask with opening which clamps membrane electrode assembly from both sides of positive electrode and negative electrode, and controls passage of water vapor, and a hydrogen producing substance accommodating portion provided at space formed at side of fuel electrode sealed with membrane electrode assembly and housing. The membrane electrode assembly consists of solid electrolyte arranged between positive electrode and negative electrode, and in which water or water vapor is impregnated and ion conductivity is produced. Hydrogen producing substance (23) is used as fuel and reacted with water to form hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of fuel cell. (Drawing includes non-English language text)    Membrane electrode assembly (11)    Solid electrolytic membrane (12)    Opening (17,20)    Housing (21)    Hydrogen producing substance accommodating portion (22)    Hydrogen producing substance (23)
NOVELTY - The method for producing a polymer electrolyte membrane (16), comprises producing a polymer solution of polyazol in a solvent mixture, transferring the polymer solution in a flat structure, and dropping the polymer solution that is transferred in the flat structure with liquid water at room temperature by immersing, pouring or spraying to form a polymer electrolyte membrane. An additive component is added to the polymer solution before dropping. The polymer electrolyte membrane is packed and is built in a fuel cell (10).    USE - Method for producing a polymer electrolyte membrane, which is useful for fuel cells (claimed), for electrochemical applications and for the construction of a membrane electrode assembly.    ADVANTAGE - The method is capable of economically, rapidly and simply manufacturing the polymer electrolyte membrane with good mechanical and electrochemical properties, good proton conductivity, improved long-term stability, improved thermal stability, optimized material properties and less technical effort thus increasing the efficiency and performance of the fuel cell.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a polymer electrolyte membrane; and    (2) a fuel cell.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of a fuel cell comprising individual cells.    Fuel cell (10)    Individual cell (12)    Membrane electrode assembly (14)    Polymer electrolyte membrane (16)    Electrodes. (18, 20)
NOVELTY - Composite raw material for biogas, where stack retting, drying and pulverizing of poultry droppings and crop straws are performed; biological germ and additives are added, and a product is obtained through mixing and stirring. Poultry droppings, crop straws, biological germ and additives are mixed in the weight percentage of 70-80%, 15-25%, 3-6% and 0.001-1%.    USE - The composite raw material is useful for biogas (claimed).    ADVANTAGE - The stack-retting time of the crop straw and poultry dropping is 3-5 days. It avoids shortage of raw materials for biogas fermentation and it produces high quality bioenergy; the poultry droppings and crop straws are easy to obtain; and it has waste recycling, low production cost, clean environmental sanitation and satisfactory effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a preparation method of a composite raw material for biogas comprising the following that stack retting, drying and pulverizing of poultry droppings and crop straws are performed; biological germ and additives are added, and the composite raw material for biogas is obtained through mixing and stirring.
NOVELTY - A botanical green solvent (no units given) comprises pinene (10-40), D-limonene (10-40), longifolene (5-15), camphene (5-15), dehydroabietic acid (3-15), pinane (1-10), and antioxidant (0-2).    USE - Botanical green solvent for pesticide.    ADVANTAGE - The solvent has low cost raw material, and has simple and environment-friendly preparation. The preparation has low power consumption, and provides safe and low product cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparation of botanical green solvent, comprising:    (A) taking rosin, crushing, and dehydrating;    (B) performing dry distillation on the dehydrated rosin separating from air for 5-20 hours at 200-500 degrees C, condensing gas product generated from pyrolysis, and collecting it together with liquid product generated from pyrolysis to obtain pyrolysis liquid;    (C) washing the pyrolysis liquid with alkali liquor (3-6 mass%) until there is no acidity, standing and separating oil from water, fractionating the separated oil phase, and collecting fraction at 80-260 degrees C;    (D) dehydrating, and controlling mass percentage of water in the fraction to be less than or equal to 0.4 mass%; and    (E) adding antioxidant to the dehydrated fraction, dissolving uniformly to finally prepare the botanical green solvent containing 0-2% of antioxidant.
NOVELTY - A nicotine/phosphorelated chitosan nanoparticle water dispersible preparation is prepared by dissolving nicotine in neutral water, and preparing it into nicotine aqueous solution; dissolving phosphorelated chitosan into neutral water, and preparing it into phosphorelated chitosan aqueous solution; under stirring condition, dipping the nicotine aqueous solution into the phosphorelated chitosan aqueous solution, and obtaining the preparation.    USE - Method for preparing nicotine/phosphorelated chitosan nanoparticle water dispersible preparation for agrochemical preparation (claimed).    ADVANTAGE - The method provides environment-friendly agrochemical preparation with slow-release function.
NOVELTY - A two-phase distribution bioreactor comprises a tank body (13), in which filter mesh (3) is arranged. A solid phase extracting agent bed layer (4) and an immobilized microorganism carrier bed layer (5) are arranged alternately among all filter meshes from bottom to top. Lower part of the tank body is provided with a water aerating system and an aeration system. Upper part of the tank body is provided with a water outlet (2).    USE - Two-phase distribution bioreactor used for treating organic wastewater that has high concentration and is difficult to degrade (claimed).    ADVANTAGE - The bioreactor is capable of effectively improving tolerance and extraction phase property of microorganisms to organic pollutants. Problems that the organic extraction phase can be biodegraded, growth of microorganism is inhibited and the micro organism is lost due to large number of bubbles produced in aeration process are solved. The solid extracting agent has large adsorption amount and high adsorption speed, and can be used for mixing floras and treating complex wastewater.    DESCRIPTION OF DRAWING(S) - The drawing is a cross-sectional view illustrating the two-phase distribution bioreactor.    Water outlet (2)    Filter mesh (3)    Solid phase extracting agent bed layer (4)    Immobilized microorganism carrier bed layer (5)    Tank body (13)
NOVELTY - The method involves passing hydrocarbons through grinding, drying, and primary and secondary reaction processes. Grinding bodies are formed as molded bodies made from glass or ceramic material. The hydrocarbons and a catalytically active material are brought into contact with each other, and the processes are carried out simultaneously, while organic solid matter in the hydrocarbons is dried and ground. A solid-solid reaction of the matter and solid catalyst is carried out, and the developing gaseous or liquid products are cleaved and/or converted in secondary reactions on a catalyst surface.    USE - Method for catalytic conversion of solid-like hydrocarbon for material usage of brown coals and/or biomass and/or plastics such as thermoplastics, and/or oil coke and/or oil sands and/or oil shale in a refining plant.    ADVANTAGE - The method carries out the solid-solid reaction of the organic solid matter and solid catalyst and cleaves and/or converts the developing gaseous or liquid products in secondary reactions on the catalyst surface, thus providing a high yield of base materials for the refining plant, without the need for additional usage of materials. The energy and separation expenditure can be hence reduced.    DETAILED DESCRIPTION - The catalytically active material consists of acid zeolite or acid zeolite-based materials. The primary and secondary reaction processes are controlled by inert or reaction gases e.g. methanol and hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a rotating tube reactor with an inner worm gear.'(Drawing includes non-English language text)'    Material and sphere feed (AA)    Nitrogen (BB)    Pyrolysis vapor (CC)    Pyrolysis residue (DD)
NOVELTY - Method involves preparation of raw material, heating with subsequent treatment and obtaining fuel. The prepared material is heated at 55-60 degrees C, with subsequent separation of moisture and impurities, and the material is treated in a reaction vessel through simultaneous esterification and trans-esterifiction while mixing the material with alcohol in ratio 5:1-7:1 respectively and addition of a heterogeneous acid catalyst in amount of 5-10% to the mass. The process is carried out at 120-150 degrees C for 60-120 minutes with turbulent stirring at 1200-1500 rpm and at atmospheric pressure. 5% glycerin is added 15 minutes before the end of the process. The process is stopped and the heterogeneous catalyst is extracted. The obtained substrate is put into a settling tank and kept for 6 hours. Biodiesel and glycerin in the settling tank are separated by draining the formed bottom glycerin phase. Excess alcohol is distilled off. The biodiesel is purified with magnesium silicate for 30 minutes. Magnesium silicate is extracted and reduced. The raw material used is raw fat containing 10-100% free fatty acids and/or plant material of oil-bearing crops, and the heterogeneous acid catalyst used is lanthanum diphosphate and/or magnesium silicate and/or aluminium diphosphate and/or sulphated zirconium.    USE - Chemistry.    ADVANTAGE - Invention increases output of the product with improved ecological index. 1 dwg, 3 ex
NOVELTY - The process involves separating liquid and gaseous phases using a gas/liquid separator (4). The methane enriched gaseous phase is introduced into a cryogenic separation device, where the separation device comprises a freezing zone and a distillation zone positioned below the freezing zone. A bottom stream rich in liquid phase contaminant and lean in gaseous product and a top stream rich in gaseous product and lean in gaseous contaminant e.g. hydrogen sulfide, are removed from the cryogenic separation section.    USE - Process for removing gaseous contaminants e.g. carbon dioxide and hydrogen sulfide from a feed gas stream i.e. natural gas (all claimed). Can also be used for carbon oxysulfide, mercaptans, sulfides and aromatic sulfur.    ADVANTAGE - The method enables improving the removing gaseous contaminants from gas streams and energy efficiency of the overall processing in an efficient manner. The method enables eliminating the need for separate treatment for the secondary gas and the liquid removed in the centrifugal separator.    DETAILED DESCRIPTION - The feed gas stream comprises 20 to 80 volume percent of methane. The feed gas stream has temperature between minus 20 and 150 degrees centigrade and pressure between 10 and 150 bara.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a gas/liquid separator.    Conduits (3, 5, 6)    Gas/liquid separator (4)    Gas inlet (34)    Housing (35)    Separating body (36)    Disks (36a-36f)    Ducts (37)
NOVELTY - The coalescer (10) has an elongated, closed, vertically arranged vessel (12) including a fluid inlet and a fluid outlet located at a lower portion of the vessel. A power supply external to the vessel is in communication with an electrode surface (70). The electrode surface, another electrode surface (72) and an electrode e.g. cylindrical wire screen, establish a voltage field around a perimeter portion of the vessel and in a center portion of the vessel, where the voltage field serves to coalesce glycerin in the stream to augment separation from the stream.    USE - Vertical electrostatic coalescer for promoting glycerin coalescence in a biodiesel stream.    ADVANTAGE - The electrode surfaces and the electrode e.g. cylindrical wire screen, effectively establish the voltage field around the perimeter portion of the vessel and in the center portion of the vessel. The coalescer has small size, and promotes separation of glycerin from alkyl fatty acid esters during continuous production of biodiesel in an effective manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of a vertical electrostatic coalescer including a circular conduit for distributing an inlet stream of biodiesel and glycerin and employing an electric field to coalesce the glycerin droplets in biodiesel.    Vertical electrostatic coalescer (10)    Elongated closed vertically arranged vessel (12)    Contact rod (18)    Support leg (26)    Electrode surfaces (70, 72)
NOVELTY - The system (1) has dispatch controller (10) connected to power determination and monitoring unit (3), and electrolyzer module controller (9). An alternative load (11) is connected to transmission line (4), low voltage side of central step down n-pulse transformer, and n-pulse direct current (DC) bus (7), to demand any electric power from wind farm (2) which is not demanded by electrolyzer modules (5). An alternative power source (12) is connected to high and low voltage sides of the transformer, and bus, to supply any of the electric power demanded by modules.    USE - System for distributing electric power generated by wind farm to electrolyzer module for producing hydrogen.    ADVANTAGE - Maximization of hydrogen production and minimization of energy losses can be easily achieved, while achieving sufficient on-demand power supply and maintaining stability when power imbalances are occurred.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for distributing electric power from wind farm generating medium to high voltage alternating current (AC) electricity to several electrolyzer modules for producing hydrogen; and    (2) method for control distribution of electric power from wind farm generating medium to high voltage alternating current (AC) electricity and medium voltage DC electricity to several electrolyzer modules for producing hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the system used for distributing electric power generated by wind farm.    System for distributing electric power generated by wind farm (1)    Wind farm (2)    Power determination and monitoring unit (3)    Transmission line (4)    Electrolyzer module (5)    DC bus (7)    Electrolyzer module controller (9)    Dispatch controller (10)    Alternative load (11)    Alternative power source (12)
NOVELTY - Production (m1) of fatty acid ethyl esters involves reacting a substrate comprising triglycerides, diglycerides, monoglycerides and/or free fatty acids, with at least one immobilized lipolytic enzyme, to provide a reaction mixture where the enzyme loading is below 30 wt/wt.% with respect to the substrate, and the molar ratio of ethanol to fatty acid (EtOH:FA) is at least 3 equivalents; separating the immobilized lipolytic enzyme from the resulting reaction mixture; and subjecting the immobilized lipolytic enzyme to at least one further reaction directly without modifications.    USE - For production of fatty acid ethyl esters used in a composition for refined fuel (claimed).    ADVANTAGE - The lipolytic enzymes immobilized on a hydrophilic carrier material in the presence of high amounts of ethanol can effiently be re-used for production of fatty acid ethyl esters directly without modifications.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) re-use of at least one lipolytic enzyme immobilized on a hydrophilic carrier in the production of fatty acid ethyl esters obtained by reacting ethanol with a substrate; and which enzyme after use in a conversion reaction is separated from the resulting reaction mixture and re-used directly without modifications in the next conversion reaction;    (2) composition obtained by the method (m1) where the composition comprises at least two of the following components selected from fatty acid ethyl esters; triglyceride; diglyceride; monoglyceride; glycerol; and water.
NOVELTY - The method involves operating a superheating boiler (50) exclusively with one or more by-products generated when producing the liquid hydro carbonaceous product (1). The by-products preferably include tail gas (9) generated in Fischer-Tropsch synthesis applied onto purified synthesis gas (4), filtered ash (49) removed from raw synthesis gas (3), ultra-purification by-product gas (48) generated in an ultra-purification unit (23), and product upgrade by-product fractions (47) generated by product upgrading of the hydro carbonaceous product using a product upgrading unit (32).    USE - Method for producing liquid hydro carbonaceous product, such as liquid biofuel, from solid biomass.    ADVANTAGE - The superheating boiler superheats the saturated steam produced in the cooling step, enhancing total efficiency of process for producing the liquid hydro carbonaceous product such as liquid biofuel. The by-products resulting from producing the hydro carbonaceous product ensures that the synthesis gas or any other product gas or liquid generated in the process is not used for superheating, maintaining overall yield of the process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an apparatus for producing liquid hydro carbonaceous product from solid biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic flowchart of a method for producing liquid hydro carbonaceous product from solid biomass.    Liquid hydro carbonaceous product (1)    Raw synthesis gas (3)    Purified synthesis gas (4)    Tail gas (9)    Ultra-purification unit (23)    Product upgrading unit (32)    Product upgrade by-product fractions (47)    Ultra-purification by-product gas (48)    Filtered ash (49)    Superheating boiler (50)
NOVELTY - The device has channels (12) connected to lines for feeding of water and electrolyte (13) and withdrawal of electrolysis products (10,22,23). An electrolyzer (1) with upper cover (3) and lower cover (4) made of electrically conducting material is mounted on a shaft (5) having the channels. One short circuited electrode (11) is located centrally in electrolyzer. Other electrode is formed by inner surface of electrolyzer. An electromagnetic system has electromagnets (26,27) mounted above the upper and under the lower covers of electrolyzer that rotates relative to electromagnets.    USE - Device for electrolytic production of hydrogen and oxygen by electrolysis of water, for use with internal combustion engines of transport mechanism, steam turbines of thermal/nuclear power stations, for utilization of industrial heat in metallurgy etc.    ADVANTAGE - The rotation speed of electrolyzer is reduced and the productivity of the electrolyzer is improved by the usage of the electromagnetic system without need for complicated design. The volume of electrolyte solution is decreased and concentration of electrolyte solution is increased during production time by rotating electrolyzer relative to magnets. The surfaces of the electrolyzer in contact with the electrolyte are covered with the special coatings, so that the electrical properties of the electrically conductive portions are improved and the materials are protected from corrosion.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device used for electrolytic production of hydrogen and oxygen.    Electrolyzer (1)    Drum (2)    Upper cover (3)    Lower cover (4)    Shaft (5)    Electrolyte solution or water (9)    Electrolysis products (10,22,23)    Short-circuited electrodes (11)    Channels (12)    Electrolyte (13)    Upper fixed magnets (26)    Lower fixed magnets (27)
NOVELTY - A hydrogen-producing agent is a lithium alloy containing lithium, and aluminum, magnesium and/or zinc.    USE - Hydrogen-producing agent is used for supplying hydrogen for fuel cell (claimed), and gas chromatography.    ADVANTAGE - The hydrogen-producing agent stably and efficiently provides highly purified hydrogen.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for hydrogen-producing method.
NOVELTY - A front side catalyst layer (2) consisting of water vapor modification catalyst is provided. A back side catalyst layer (3) is provided on either sides of the hydrogen separation membrane (4). Cross sectional area of the back side catalyst layer is 65% or less of the cross sectional area of the front side catalyst layer.    USE - Membrane separation type hydrogen production apparatus.    ADVANTAGE - Decline in hydrogen permeation efficiency can be suppressed by increasing the flow rate of reformed gas in the back side catalyst layer. Fall of hydrogen concentration in the hydrogen separation membrane can be prevented. Hydrogen can be separated and refined efficiently and so, hydrogen production efficiency can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the membrane separation type hydrogen production apparatus. (Drawing includes non-English language text)    Inlet portion (1)    Front side catalyst layer (2)    Back side catalyst layer (3)    Hydrogen separation membrane (4)    Exit portions (5,6)
NOVELTY - The apparatus (20) processes the elongated bio-coke by pressure, while heating biomass feedstock at specific temperature. Several parallel teeth (21A,21B) and inclined teeth (22) are arranged in bio-coke dropping position at regular intervals. Two inclined teeth are positioned at both sides of parallel teeth in linear symmetry.    USE - Apparatus for cracking bio-coke used as alternate fuel for coal coke. Uses include but are limited to fuel for boiler used in raw material processing and electric power generation application, casting production, heat source, and used as reducing agent in iron manufacture, etc.    ADVANTAGE - The cracking of hard bio-coke to desired length is performed easily in short duration, by the arrangement of parallel and inclined teeth.    DETAILED DESCRIPTION - The parallel teeth are inclined so that the expanded helical side is lowered. The helical angle with respect to parallel teeth is set about 5-45 degrees . The inclination angle with respect to horizontal direction of parallel teeth is set about 5-30 degrees . The cross-section of the parallel and inclined teeth is formed in triangular shape.    DESCRIPTION OF DRAWING(S) - The drawing shows a top view of the arrangement configuration of bio-coke cracking apparatus.    Bio-coke cracking apparatus (20)    Parallel teeth (21A,21B)    Inclined teeth (22)
NOVELTY - An electric power generation system which uses organic wastes has waste treatment apparatus (1) where organic wastes are contacted with high pressure, high temperature steam (0.2-3 MPa, 130-250 degrees C) and discharged as dried material, coal boiler (3) which converts the heat, used to dry the organic waste, into steam and discharge it to the waste treatment apparatus and generator (4) driven with steam emitted from coal boiler.    USE - Electric power generation system which uses organic wastes.    ADVANTAGE - Energy recovery from organic wastes is raised, amount of coal in coal boiler is reliably decreased, carbon dioxide emission amount is reduced, electric power generation is efficient, energy balance is favorable and excessive electric power is produced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of electric power generation system. (Drawing includes non-English language text).    Storage tank (2)    Coal boiler (3)    Generator (4)    Grinder (5)
NOVELTY - An internal modification-type solid oxide fuel cell has cathode, anode (12), solid oxide electrolyte (11) interposed between cathode and anode and collector (16) in contact with anode. The collector contains catalyst current collection element (61) provided with a film containing modified catalyst and electron-conductive substance which produces hydrogen from hydrocarbon formed on the surface of a base material.    USE - Internal modification-type solid oxide fuel cell is used for fuel cell system (claimed).    ADVANTAGE - The usage amount of modification catalyst and electron-conductive substance in internal modification-type solid oxide fuel cell is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of anode vicinity of internal modification-type solid oxide fuel cell.    Solid oxide electrolyte (11)    Anode (12)    Collector (16)    Catalyst current collection element (61)
NOVELTY - The method involves operating an air processing system (APS) (12) including an air blower (16) and a fuel processing system (FPS) (38) including a fuel recycle blower (64) to respectively deliver oxidant air and hydrogen fuel to cathode and anode catalysts of a fuel cell (32). The fuel cell is passivated with the hydrogen fuel by shutting off the air processing system. The hydrogen fuel is transferred from the FPS to the APS and circulated between and through the FPS and a portion of the APS excluding the air blower, by using the fuel recycle blower.    USE - Method for operating fuel cell power plant for transportation applications, stationary power plants and automotives.    ADVANTAGE - The fuel cell stack is passivated during shutdown and shutoff conditions without using a combustible gas fuel certified air blower, by circulating the hydrogen fuel between and through the fuel and air processing systems using fuel recycle blower. Thus the fuel cell is efficient and light weight. The efficiency of the system is increased and the amount of potentially combustible fuel exhausted to the external environment is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell having a cathode catalyst and anode catalyst.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fuel cell power plant.    Fuel cell power plant (10)    APS (12)    Air blower (16)    Fuel cell (32)    FPS (38)    Fuel recycle blower (64)
NOVELTY - A reformation module (1) comprises a heat exchanging device (14), in which heat is transferred from a combustion exhaust gas (55) to water (30). The water flow rate in the heat exchanging device is variable via a controlling unit, so outlet temperature of the heat exchanging device depends on adjustable water flow rate. Another heat exchanging device (11) is also designed in the reformation module, in which the heat is transferred from a hydrogen-rich process gas (25) to water.    USE - Reformation module for producing hydrogen-rich process gas.    ADVANTAGE - The reformation module ensures a high degree of compactness, quick and reliable adjustment of the outlet temperatures and minimum thermal stresses.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for operating reformation module for producing a hydrogen rich process gas, which involves using heat exchanging device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the reformation module.    Reformation module (1)    Heat exchanging devices (11,14)    Hydrogen-rich process gas (25)    Water (30)    Combustion exhaust gas (55)
NOVELTY - The handler has magnetizers selectively magnetizing a particle attractor (140) into attraction mode and non-attraction mode, where the particle attractor is provided with permanent magnets. The particle attractor exhibits regions of increased magnetic field gradients in the attraction mode to attract super paramagnetic particles suspended in carrier fluid received by precipitation cavity (130) of a main body (110) via a set of openings (131, 132). The particle attractor engages with corresponding portion of an inner wall of the precipitation cavity.    USE - Submicron-sized particle handler for handling submicron-sized particle e.g. super paramagnetic nano-particle such as cellular sample, organic material, micron-sized magnetic bead and biologic debris, in waste treatment application. Can also be used for drug delivery application, gene delivery application, hyperthermia treatment application and MRI's contrast enhancement application.    ADVANTAGE - The handler significantly increases the speed of collecting submicron-sized particle on biological assays in a cost effective manner by effectively attracting the submicron-sized particle, thus reducing the loss of carrier fluid during handling of the submicron-sized particle. The handler selectively changes direction of flow of the carrier fluid in precipitation cavity from an opening to another opening, thus increasing the probability of the exposure of the submicron-sized particle to the particle attractor to increase the probability of attraction of the super paramagnetic particles.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for manufacturing a particle handler.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a main body of a submicron-sized particle handler.    Main body (110)    Lower body (111)    Upper body (112)    Precipitation cavity (130)    Openings (131, 132)    Particle attractor (140)
NOVELTY - Heat-treating a flowable suspension comprises: (a) pressurizing the suspension; (b) heat-treating the pressurized suspension; and (c) depressurizing the heat-treated suspension using a fixed flow rate pump, where the fixed flow rate pump is controlled to keep the pressured suspension essentially within a pre-determined pressure range.    USE - The method and device are useful for heat-treating a flowable suspension (all claimed). It can be used for sterilizing biogenic material or for subjecting the flowable suspension to a temperature hydrolysis, for example in order to pretreat biogenic or other organic material in the production of fuels such as ethanol or biogas.    ADVANTAGE - In the fixed flow rate pump, the volumetric flow rate is essentially independent of the pressure of the suspension before and/or after the pump. It essentially lacks the volume-pressure-elasticity observed in common kinetic pumps such as eductor-jet pumps. The pressure of the suspension can be kept within a pre-determined range. The pressure can be kept high enough to avoid vaporization of a liquid component of the suspension. It is achievable to keep the pressure low enough to ensure the safety of the device and avoid a waste of energy. Clogging can also be avoided. Abrasion as observed in the valves of the prior art devices can also be avoided, thus reducing maintenance costs.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for heat-treating a flowable suspension comprising means for pressurizing the suspension, an hydrolysis reactor for heat-treating the pressurized suspension and a fixed flow rate pump for depressurizing the suspension, where the device comprises control means for controlling the depressurizing pump so that the pressure of the pressurized suspension is kept within a pre-determined pressure range.
NOVELTY - Hydrogen-producing apparatus (30) for fuel cells, comprises water accommodating part (31), hydrogen producing agent (32) which reacts with the water vapor and produces hydrogen and ventilation unit (33) to make the water vapor flow.    USE - Apparatus for producing hydrogen for fuel cells (claimed).    ADVANTAGE - The amount of hydrogen produced is controlled.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for producing hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows a top view and a cross-sectional side view of the hydrogen-producing apparatus.    Hydrogen-producing apparatus (30)    Hydrogen producing agent (32)    Ventilation unit (33)    Water absorbing sheet (34)    Wind adjustment cover (37)
NOVELTY - A water outlet pipe for circulating water of an electrolytic cell is connected to a water inlet pipe of a radiator having a water outlet pipe connected to a water inlet pipe of an ultrasonic activator. The water outlet pipe of the ultrasonic activator is connected to the water inlet pipe of a magnetic activator having a water outlet pipe connected to the water inlet pipe of the electrolytic cell. A circulation pump is arranged between the water outlet pipe of the electrolytic cell and the water inlet pipe of the radiator.    USE - Oxy-hydrogen machine for activated water.    ADVANTAGE - Ultrasonic oscillation of water breaks chain connection structure among water molecules, and activated water with small molecular groups can be obtained by activating water with magnetic activator, thus improving efficiency of producing hydrogen and oxygen from activated water, reducing electric energy consumption, and saving cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the oxy-hydrogen machine.
NOVELTY - Alcohol ether substitutive fuel for vehicle comprises the following parts of components by weight: 75 to 85 parts of methanol, 10 to 15 parts of coking light oil, 3 to 4 parts of dimethyl ether, 0.08 to 0.12 parts of dimethyl sulfoxide, 0.04 to 0.06 parts of butyl amine, 0.2 to 0.4 parts of N,N'-disalicylic acid-1,2-propylene diamine, 0.3 to 0.4 parts of 2,6-ditertiary butyl paracresol.    USE - The alcohol ether substitutive fuel is useful for vehicle (claimed).    ADVANTAGE - The product has strong commonality and suitable for wide models of cars, and will not be influenced by air temperature. It can replace petroleum fuel completely, saving the petroleum resource and purifying air environment.
NOVELTY - The gasification unit has a support provided between a furnace body and a water tank that is equipped with an inlet port, inlet valve, drain outlet and a drain valve. A space of the water tank above liquid level is connected with an end of a high-temperature gas pipeline. The high-temperature gas pipeline is provided with a draught fan, and two thermometers are, respectively installed on the gas pipeline and behind the draught fan. The gas pipeline is provided with a pressure meter and a flow meter, where end of the gas pipeline is directly connected to an industrial coal boiler.    USE - Industrial gasification unit for continuous production of straw gas for an industrial coal boiler (claimed).    ADVANTAGE - The gasification unit performs continuously deashing process in the liquid-sealed manner, and directly burns high-temperature gaseous tar with straw gas, which avoids decocking, simplifies technique, increases heat, reduces emissions, relieves secondary pollution, improves conversation ratio of straws, provides remarkable comprehensive economic benefits and improves immeasurable environmental benefits.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of an industrial gasification unit for continuous production of straw gas for an industrial coal boiler.
NOVELTY - Production of biodiesel through in-situ transesterification of Xanthoceras sorbifolia comprises putting nut of X. sorbifolia and low-carbon alcohol in ultrasonic reactor at a ratio of 1 g:15-40 mL, adding catalyst (1.5-5 wt.%), reacting at 50-70 degrees C for 6-10 hours under 200-1000 W, taking out product from the reactor, distilling off unreacted methanol in the liquid, and layering, where the lower layer is crude biodiesel and upper layer is crude glycerin.    USE - Method of producing biodiesel through in-situ transesterification of Xanthoceras sorbifolia (claimed).    ADVANTAGE - The method has high yield of oil having high quality. It is simple and safe, and has low cost. It can also produce glycerin having high purity.
NOVELTY - The gasifier has a charging device and a firing hole provided at sides, where a filler valve hole (12) formed with a filler valve (13) is placed on a lower end of the gasifier. An air-blasting device is connected with the filler valve hole, and an air delivering pipe is connected to a dust separator (2) i.e. cyclone dust separator or bag-type dust separator, provided with an outlet pipe. One end of a biomass pushing device (6) provided in the charging device is connected with a hopper (5) and another end is connected with a furnace (1).    USE - Biomass circulating fluidized-bed gasifier for coal and oil boilers.    ADVANTAGE - The gasifier can quickly pyrolyse a biomass material whose granularity is less to generate carbon monoxide, Hydrogen and methane of other alkane gases. Environment polluting sulfur and ash are not produced. Heat value of the gasifier is 5 - 8.6 mega joules per meter cube.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass circulating fluidized-bed gasifier.    Furnace (1)    Dust separator (2)    Hopper (5)    Biomass pushing device (6)    Filler valve hole (12)    Filler valve (13)
NOVELTY - The sewage treatment equipment includes a raw water box (1), an anaerobic reactor (2), a phosphor-removing reactor, a middle settling tank (4), a semi-short-range nitrification reactor (5), a secondary settling tank (6), a middle water tank (7), and an anaerobic ammoxidation reactor (8). The anaerobic reactor has an anaerobic biological filter tank filled with the sponge filling (2.1). A first zone of the phosphor-removing reactor is an anaerobic reaction zone, and its other four chambers are aerobic zones.    USE - Urban sewage treatment equipment for anaerobic generation of methane and removal of organic matter and denitrification of autotroph.    ADVANTAGE - Provides urban sewage treatment equipment having simple structure and high efficiency, and employs advanced technique.    DETAILED DESCRIPTION - A first chamber of the semi-short-range nitrification reactor is an anoxic zone and the other four chambers are aerobic zones. The anaerobic ammoxidation reactor is provided with a columnar reaction body (8.1) and a water bath sleeve (8.10).    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram showing the urban sewage treatment equipment.    Raw water box (1)    Anaerobic reactor (2)    Sponge filling (2.1)    Middle settling tank (4)    Semi-short-range nitrification reactor (5)    Secondary settling tank (6)    Middle water tank (7)    Anaerobic ammoxidation reactor (8)    Columnar reaction body (8.1)    Water bath sleeve (8.10)
NOVELTY - The hydrogen-oxygen fuel generating device has an oxyhydrogen gas generating unit having an electrolytic cell for holding brine. A first pipeline is communicated to the electrolytic cell for conveying oxyhydrogen gas, and a second pipeline is communicated to an oxygen-containing gas generating unit for conveying oxygen-containing gas. A third pipeline mixes and outputs the oxyhydrogen gas conveyed by the first pipeline and the oxygen-containing gas conveyed by the second pipeline.    USE - Hydrogen-oxygen fuel generating device.    ADVANTAGE - Reduces hydrogen content of output gas by mixing and outputting oxygen-containing gas and oxyhydrogen gas, thus spontaneous combustion caused by high content of hydrogen can be reduced, and generation rate of tempering can be controlled.    DETAILED DESCRIPTION - Electrode plates are continuously provided on the electrolytic cell at intervals and dipped in the brine. A power supply is electrically connected to the electrode plates for electrifying the brine so as to electrolyze and to obtain oxyhydrogen gas.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram showing the hydrogen-oxygen fuel generating device.
NOVELTY - Treatment of agricultural residue into a pumpable slurry, comprises: reducing the particle size of the agricultural residue to form a pumpable slurry; introducing the pumpable slurry to the base of a digester using a mud pump or sludge pump; and stirring the floating slurry for removing tiny air bubbles in it, by results in sinking of the floatated agricultural residue for ensuring a continuous good contact between the agricultural residue and the microbial culture medium.    USE - The agricultural residue is useful as feeds in the biogas plants for producing biogas.    ADVANTAGE - The method ensures: appropriate contact between the biomass and the microbial culture medium; and that any scum formed on the surface is made to sink, by continuous contact of the biological matter forming the scum with the microbial consortia. The method reduces the capital cost of the equipment. The method utilizes any conventional digester for the production of biogas without requiring specific design (screw conveyers). The method simplifies further processing of microbial digestion. The method reduces retention time of the feed stock and biogas plant size.
NOVELTY - An electrolysis cell (11) has a lower portion that is provided with lower tube and lower plate. An upper portion has upper tube and upper plate. The upper and lower portions are made of stainless steel material. The lower portion and upper portion are arranged such that a hollow cavity for containing electrolytic fluid is formed between lower and upper portions. An electric current source is connected between upper and lower portions. A pump (15) is connected to electrolyte tank (13) and electrolysis cell so as to force the electrolytic fluid from tank into cell.    USE - Water electrolysis system for fuel/air mixture system of internal combustion engine such as petrol engine and diesel engine mounted in motor vehicle.    ADVANTAGE - The output efficiency of electrolysis cell is improved, by preventing the generation of gas bubbles in the electrolytic fluid supplied from electrolyte tank. The combustion performance of engine is improved and amount of exhaust emissions from the engine is reduced reliably. The fuel consumption of engine is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the water electrolysis system.    Current controller (10)    Electrolysis cell (11)    Electrolyte tank (13)    Pump (15)    Relay (19)
NOVELTY - Producing biodiesel, involves reacting the refined oil obtained from Hevea brasiliensis berries with mixture of basic substances and alcohol.    USE - The method is useful for producing biodiesel.    ADVANTAGE - The productivity of biodiesel is increased.
NOVELTY - The device has a reaction tank (1) whose upper part is connected with a hot saline water sprayer (4) that is connected with a hot saline water tank (3). A lower part of the reaction tank is provided with a waste water outlet (9) and a coarse product outlet (10), where the coarse product outlet is connected with a centrifugal machine (5) that is provided with a piece of filter cloth (6). The centrifugal machine is connected with a buffer tank (7) that is connected with an oil pump (8). The reaction tank is made of carbon steel, stainless steel and enamel material.    USE - Impurity removing device for bio-diesel production.    ADVANTAGE - The device separates moisture from stock oil, and removes impurities such as colloid, protein and argil, from the stock oil, so that impurity content in the stock oil is reduced from 2 to 10 percentage to make convenience for next esterification process. The reaction time for the next esterification reaction is shortened to be 6 hours, so as to save steam by 12 Renminbi per ton of raw materials and to increase conversion efficiency by 2 percentage, thus increasing income of per ton of raw materials by 180 Renminbi, and improving economic benefits.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of an impurity removing device.    Reaction tank (1)    Hot saline water tank (3)    Hot saline water sprayer (4)    Centrifugal machine (5)    Filter cloth (6)    Buffer tank (7)    Oil pump (8)    Waste water outlet (9)    Coarse product outlet (10)
NOVELTY - Fuel processing in solid oxide fuel cell (SOFC) system involves removing sulfur from hydrocarbon-based fuel by using a desulfurizer (20) and obtaining hydrogen-rich reformed gas by using a primary reformer (10); and selectively decomposing low carbon 2-5C hydrocarbon compound contained in desulfurized reformed gas and converting it into hydrogen and methane by using a post-reformer (30).    USE - Method for fuel processing in SOFC system.    ADVANTAGE - The method efficiently removes non-converted 2-5C hydrocarbon compounds, thus, preventing deterioration of SOFC performance and increasing stability of SOFC and fuel cell system for a long time; and is thermally independent without external heat.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic block diagram of a fuel processing apparatus.    Injection nozzle (11)
NOVELTY - Coal entirely without wood, where the coal is obtained from a raw material composed of residues from olive oil extraction, where the material is crushed kernels, is claimed.    USE - The coal is useful for cooking in barbecue.    ADVANTAGE - The coal: has high heat capacity and rapid ignition capacity i.e. 3 minutes; and is devoid of wood.
NOVELTY - The fuel cell has reinforcement layer (150) which is positioned inside electrolytic layer (100). The thickness (L1) of electrolytic layer existed in cathode gas inlet side rather than reinforcement layer at cathode side, is larger than thickness (L2) of electrolytic layer existed in anode gas outlet side rather than reinforcement layer at anode side. The thickness (L3) of electrolytic layer in anode side rather than reinforcement layer at anode gas inlet side, is larger than electrolytic layer in cathode side rather than reinforcement layer at cathode gas outlet side.    USE - Fuel cell e.g. polymer electrolyte fuel cell for generating electric power.    ADVANTAGE - The reinforcement layer is provided with low water flow resistance portion, hence drying of electrolytic layer can be suppressed. The water content/moisture can be eliminated from electrolytic layer.    DESCRIPTION OF DRAWING(S) - The drawing shows a structural view of electrolytic layer. (Drawing includes non-English language text)    Thickness of electrolytic layer (L1-L3)    Electrolytic layer (100)    Reinforcement layer (150)    Catalyst layer (200)
NOVELTY - A biomass is subjected to acid hydrolysis in presence of aqueous solution of organic acid chosen from 7-20C alkyl- and aryl-sulfonic acids and/or halogenated carboxylic acid at 800-1600 degrees C, to obtain primary mixture comprising primary solid phase and primary aqueous phase. The primary mixture is subjected to enzymatic hydrolysis to obtain secondary mixture comprising secondary solid phase and secondary aqueous phase. The secondary aqueous phase is subjected to fermentation in presence of oleaginous yeast, to obtain oleaginous cellular biomass-comprising lipids.    USE - Production of lipids used for producing biodiesel and green diesel (both claimed) used as fuel for motor vehicle.    ADVANTAGE - The lipids are produced economically in high yield.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating the production of lipid from biomass.
NOVELTY - High energy biofuel composition comprising ethanol and butanol is produced by performing fermentation of a sugar bearing media using Clostridium sporogenes (MTCC 5469).    USE - High energy biofuel composition comprising ethanol and butanol.    ADVANTAGE - The method is integrated with recovery of the high energy biofuel periodically to overcome the toxicity, thus higher concentration of high energy biofuel is produced at a titer of 50-90 g/l of fermentation media comprising sugars bearing media and other nutrients minimally required for growth.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of the above-cited high energy biofuel composition, which involves fermenting sugar bearing media with C.sporogenes (MTCC 5469) in a fermenter, periodically adding an extractant to the fermenter, extracting a fermentation broth comprising the high energy biofuel from the fermenter, separating the high energy biofuel from other constituents in the fermentation broth, and purifying the high energy biofuel.
NOVELTY - A polymer having a sulfonic acid group and sulfonyl halide group in a molecule is maintained at 0 degrees C or less in the presence of a base. Crosslinking reaction of the polymer thus produced is carried out using a crosslinking agent having functional group(s) chosen from disulfonylamide group, diamine group, diol group, and dithiol group in an organic solvent, to obtain a polymer electrolyte.    USE - Synthesis of polymer electrolyte for use in solid polymer electrolyte membranes of polymer electrolyte fuel cells (both claimed) used as power supply for electric vehicles. Can also be used for electrodialysis, diffusion dialysis, battery diaphragms, hydrohalic acid electrolysis, water electrolysis, brine electrolysis, humidity sensors, gas sensors, and oxygen enrichers.    ADVANTAGE - The method enables synthesis of polymer electrolytes having high ion-exchange capacity and which improve ionic conductivity by having a more uniform crosslinking point than existing electrolytes.
NOVELTY - Producing an agent comprises: (a) a microbial digestion of biomasses performed through at least one inoculation with a consortium of microorganisms susceptible of activating the above digestion to obtain a solid digested fraction; (b) a vermicomposting of the digested solid fraction obtained in phase (a); and (c) a fungal-bacterial metabolization of the solid fraction obtained in phase (b).    USE - The method is useful for producing the agent for treating agricultural soils starting from biomasses of animal origin. No biological data given.    ADVANTAGE - The method improves the health status of depleted soils and the productive capacities of the soils.    DETAILED DESCRIPTION - Producing an agent comprises: (a) a microbial digestion of biomasses performed through at least one inoculation with a consortium of microorganisms susceptible of activating the above digestion to obtain a solid digested fraction; (b) a vermicomposting of the digested solid fraction obtained in phase (a); and (c) a fungal-bacterial metabolization of the solid fraction obtained in phase (b), where the fungal-bacterial metabolization envisions: (c1) at least one inoculation of the solid fraction with a consortium of microorganisms susceptible of activating a further enzymatic digestion; (c2) movement and oxidation of the inoculated solid fraction; (c3) at least one injection of the solid fraction with aeriforms, preferably air.
NOVELTY - A disposal method of urban garbage comprises classifying the urban garbage by proportional air classification and magnetic separation into ironwork, waste plastic, organic garbage and inorganic matters; sieving the organic matters; crushing the inorganic matters to be building material products; preparing the waste plastic into plastic raw material; naturally fermenting the organic garbage, sterilizing, drying, crushing and directly pelletizing to be organic fertilizer; and cooling the gas produced in the fermenting and drying process and preparing to be air fertilizer.    USE - A disposal method of urban garbage (claimed).    ADVANTAGE - The method reduces the work intensity of worker, is clean and sanitary, and has good sorting effect, so that the utilization rate of the sorted garbage is high and without residue. The organic garbage is naturally fermented, so that the cost is low. The produced waste gas is prepared into air fertilizer, so that secondary pollution is avoided.    DETAILED DESCRIPTION - A disposal method of urban garbage comprises:    (A) classifying the urban garbage by proportional air classification and magnetic separation in sorting machine into ironwork including steel bar, waste plastic, organic garbage and inorganic matters;    (B) sieving the organic matters in sieving machine to sieve out the inorganic matters such as sandy soil and bricks, where the inorganic matters such as bricks are crushed to prepare to be building material products;    (C) preparing the waste plastic into plastic raw material by extruding machine after being washed;    (D) naturally fermenting the organic garbage in fermenting tank and then sterilizing and drying in oven after being fermented for several days; then crushing the organic garbage and directly pelletizing to be organic fertilizer; and    (E) cooling the gas produced in the fermenting and drying process in cooling tower and then canning and preparing to be air fertilizer.
NOVELTY - Biogenic production of ethanol, comprises culturing an engineered cyanobacterium in a culture medium in the presence of light and carbon dioxide. The cyanobacterium comprises at least two copies of a recombinant alcohol dehydrogenase gene, where at least one copy of the recombinant alcohol dehydrogenase gene is extrachromosomal.    USE - The method is useful for producing ethanol and increasing ethanol production (all claimed), where the ethanol is useful as biofuel. The method is also useful for producing other carbon-based products e.g. propanol, isopropanol, butanol, fatty alcohols, fatty acid esters, wax esters, propane, octane, diesel, polymers e.g. terephthalate, 1,3-propanediol, isoprene, caprolactam and rubber.    ADVANTAGE - The method utilizes engineered cyanobacterium Synechococcus strain, which enables the efficient and increased production of ethanol and thus eliminates the time-consuming and expensive processing steps required to generate biofuels from biomass sources by conventional methods.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) increasing the production of ethanol by an engineered cyanobacterium, comprising varying the activity of recombinantly expressed alcohol dehydrogenase and pyruvate decarboxylase in the cyanobacterium; and    (2) an engineered cyanobacterium comprising alcohol dehydrogenase activity adhA(M) under the control of the lambda cI promoter.
NOVELTY - A hydrogen is produced by gasifying fuel into raw synthesis gas comprising carbon monoxide, hydrogen, steam, sulfur, and halide contaminants; passing the raw synthesis gas through water gas shift reactor into which calcium oxide and steam are injected, the calcium oxide reacting with the shifted gas to remove carbon dioxide, sulfur, and halides in solid-phase calcium-containing product; separating the solid-phase calcium-containing product from enriched gaseous hydrogen product; and regenerating calcium oxide by calcining the solid-phase calcium-containing product in the presence of steam.    USE - Method for producing hydrogen (claimed).    ADVANTAGE - The method is capable of producing high purity hydrogen gas, into which capture of carbon dioxide, sulfur and halides are integrated.    DETAILED DESCRIPTION - Producing hydrogen comprises gasifying fuel into raw synthesis gas comprising carbon monoxide (CO), hydrogen, steam, sulfur, and halide contaminants in form of dihydrogen sulfide (H2S), COS, and HX, in which X is halide; passing the raw synthesis gas through water gas shift reactor (WGSR) into which calcium oxide (CaO) and steam are injected, the CaO reacting with the shifted gas to remove carbon dioxide (CO2), sulfur, and halides in solid-phase calcium-containing product comprising calcium carbonate (CaCO3), calcium sulfide (CaS), and CaX2; separating the solid-phase calcium-containing product from enriched gaseous hydrogen product; and regenerating CaO by calcining the solid-phase calcium-containing product in the presence of steam, in the presence of CO2, in the presence of synthesis gas, in the presence of hydrogen and oxygen gas, and/or under partial vacuum.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of carbon capture and sequestration in fossil fuel based power plants.
NOVELTY - Feedstock is contacted with carbon monoxide in presence of catalyst comprising metal chosen from ruthenium, manganese, rhodium, rhenium, osmium, iridium, molybdenum, copper, zinc, palladium, platinum and cobalt, and water under alkaline condition at 150-350 degrees C under pressure of 0.1-150 bar, to obtain hydrocarbon. Thus, deoxygenation of feedstock of biological origin is carried out.    USE - Deoxygenation of feedstock of biological origin used for producing hydrocarbon e.g. paraffinic hydrocarbon used as diesel fuel, gas, gasoline and aviation fuel, and as solvent (all claimed).    ADVANTAGE - The deoxygenation of feedstock of biological origin produce high quality hydrocarbon.
NOVELTY - A methanol purifying process involves making methanol absorb carbon dioxide, hydrogen sulfide and sulfur at low temperature. The methanol solution can absorb 160-180 m3 of carbon dioxide at 2.1 MPa.    USE - A methanol purifying process for large industrial devices of ammonia synthesis, methanol synthesis, hydroxyl synthesis, industrial production of hydrogen, city gas production, and purification of natural gas.    ADVANTAGE - The purifying process has big absorbing capacity, good selectivity, high purifying degree, and low manufacturing cost.
NOVELTY - A coloring agent comprises (pts.wt.) humate (40-50), carbon black (0.1-3), erie black (2-4), acid scarlet (1-2), sodium hexametaphosphate (0.2-1), and water (40-56.7).    USE - A coloring agent for diammonium phosphate compound fertilizer (claimed).    ADVANTAGE - The fertilizer is inexpensive, environmentally friendly, and pollution-free. It is liquid so it can be conveyed in a sealing state, and used conveniently.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing the coloring agent, comprising adding humate, carbon black, erie black, and acid scarlet to water in a reaction tank; uniformly stirring; and adding sodium hexametaphosphate, and uniformly stirring for 6090 minutes.
NOVELTY - Fish oil is separated from fish, and content of free fatty acid in fish oil is increased by pretreatment. The fish oil is then mixed with alcohol as solvent and a catalyst, and supplied to a reactor. Carbon dioxide of high pressure is injected into reactor, and esterified at 30-100 degrees C and 80-500 bar in supercritical phase. The esterified reaction product is separated from reactor. The alcohol is then separated, and fatty acid alkylester type biodiesel is manufactured.    USE - Manufacture of fatty acid alkylester type biodiesel.    ADVANTAGE - The biodiesel is quickly manufactured at low temperature conditions.    DESCRIPTION OF DRAWING(S) - The drawing shows the flowchart for manufacture of biodiesel. (Drawing includes non-English language text)
NOVELTY - A gas from a gas-forming section is further compressed by a low-pressure cylinder of a synthesis-gas compressor after being decarburized. The gas is then flown into an isothermal purifier, and methylated and methanized to obtain a purified gas whose content of carbon monoxide and carbon dioxide is below 10 ppmv. The purified gas is transferred to the next purifying section to be dried and purified.    USE - Once-through isothermal purification.    ADVANTAGE - The method enables simple, economical and environmental-friendly isothermal purification in an energy-saving manner. The quality of purified gas meets the conditions of ammonia synthesis catalyst. The method also reduces the content of carbon monoxide and carbon dioxide to less than 10 ppmv.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for once-through isothermal purification device arranged between a low-pressure cylinder and a high-pressure cylinder of a compressor. The device consists of isothermal methylating reactor(s) and an insulation methanation reactor which are connected in series. The gas flows into the methylating reactor for methylation via the low-pressure cylinder after decarburization, then into the insulation methanation reactor for methanation, and then output.
NOVELTY - A heat recovery system for the conservation of biomass and extraction of heat from the flue gas obtained from the burning of biomass in large cooking stoves, is disclosed. It facilitates the recovery of waste heat in the flue gas which does not deliver to the vessel but come out without adversely affecting the other functions of the stove. This device is a vessel that is inserted in the path of spent flue gases and accompanying change in stove design to allow the additional component. This is provided with a spiral baffle to ascertain better contact between the vessel and hot flue gases, and an additional tapered block is introduced to resist the flow of flue gases and ensures more residence time in the stove. Image 0/0
NOVELTY - Manufacturing biofuel comprises providing a microorganism and fermenting the microorganism to allow degeneration of the biomass to biofuel.    USE - The method, primer pairs, and probes are useful for manufacturing biofuel (all claimed).    ADVANTAGE - The method provides a simple and fast method of manufacturing biofuel.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) a primer pair comprising gccaaaggatttattcgctatga (SEQ ID NO. 1) and gccttggtgagccgttacc (SEQ ID NO. 2) specific in the 16s rDNA of Clostridium acetobutylicum; (2) a probe which is used with primer pair in (1), where the probe comprises acccgcggcgcattagcttgt (SEQ ID NO. 3); (3) a primer pair comprising cgaattcttctgactggtggctat (SEQ ID NO. 4) and tttgaaatcatcgtaactcccaagt (SEQ ID NO. 5) specific in the pSOL1 plasmid of C. acetobutylicum; and (4) probe which is used with primer pair in (2), where the probe comprises cagccaaccaatcaagctataggaaatgctc (SEQ ID NO. 6).
NOVELTY - Treating rice and wheat straws comprises cutting the wheat straws into the wheat straw grains; cutting the rice straws into the rice straw grains; mixing the wheat straw grains and the rice straw grains according to a ratio; and compressing the mixed wheat straw grains and the rice straw grains into the finished product of straw blocks or grain finished product.    USE - The process is useful for treating rice and wheat straws (claimed).    ADVANTAGE - The process uses the complementarity of performance of the wheat straws and rice straws; where they are mixed and compressed into the finished product of straw blocks; they make up the defects of each other with good forming effect; and they are easy to completely burn. Moreover, the manufacturing cost is low; and any additive is not needed.
NOVELTY - Catalyzing reduction reaction of organic substance via plant biological catalyst comprises: (a) forming a plant catalyzing reaction system; (b) putting the plant catalyzing reaction system in the magnetic field to obtain a magnetized plant catalyzing reaction system; (c) putting the magnetized plant catalyzing reaction system in an oscillation device so that the magnetized plant catalyzing reaction system is catalyzed to obtain the reaction product; and (d) separating and extracting the reaction product to obtain the purified reaction product.    USE - The methods are useful for catalyzing reduction reaction of organic substance via plant biological catalyst (claimed).    ADVANTAGE - The method can improve the enzymatic activity of the plant biological catalyst so that the percent conversion of the reduced product is improved to satisfy the industrial application demand.    DETAILED DESCRIPTION - Catalyzing reduction reaction of organic substance via plant biological catalyst comprises: (a) adding the plant biological catalyst to the reaction solution with substrate to form a plant catalyzing reaction system; (b) putting the plant catalyzing reaction system in the magnetic field to be magnetized under the condition of controlling the magnetic induction intensity and magnetic processing time to obtain a magnetized plant catalyzing reaction system; (c) putting the magnetized plant catalyzing reaction system in an oscillation device to oscillate and culture so that the magnetized plant catalyzing reaction system is catalyzed to obtain the reaction product; and (d) separating and extracting the reaction product to obtain the purified reaction product.
NOVELTY - The apparatus has a hopper (14) that supplies chaff to the interior space (2c) of a kiln (2) through an inlet port. A combustion chamber (3) supplies external heat to the inner portion of the kiln to heat chaff indirectly so that the chaff with high moisture content remains in the kiln for longer period of time than chaff with less moisture content. A dryer is provided with stirring blade arranged between spiral portions for performing drying process with respect to the chaff in the kiln.    USE - Apparatus for performing carbonization of organic matter containing waste material such as livestock excrement such as cattle and pig feces, sludge, coffee-bean dregs, apricot seed and soybean residue.    ADVANTAGE - Chaff inside the kiln can be heated indirectly using external heat. Hence, carbonization process of the chaff can be performed effectively and regenerated carbon can be obtained efficiently. Since the water vapor in the kiln is drained through distributing pipe, moisture content of the organic matter can be reduced at earlier stage. Carbonization time of the organic matter can be shortened and self-sustained combustion process can be promoted.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for performing carbonization of organic matter containing waste material.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the apparatus for performing carbonization of organic matter containing waste material.    Kiln (2)    Interior space (2c)    Combustion chamber (3)    Exhaust port (5)    Hopper (14)
NOVELTY - The thermodynamic system (120) has a fluid pump for pumping working fluid (122) through a power cycle. A thermal input supplies heat to the working fluid. A turbine (130) placed downstream of thermal input calculates engine efficiency based on motion of working fluid. A heat pump (136) pumps heat from one portion of working fluid to another portion of working fluid.    USE - Thermodynamic system used for engine such as aircraft engine, land-based vehicle engine and vehicle engine (all claimed). Can also be used in electric generating power plant, jet engine, petrol engine, diesel engine, geothermal engine, refrigerator and air separation plant.    ADVANTAGE - Since the heat pump pumps heat from one portion of working fluid to another portion of working fluid, the waste heat produced by the engine can be removed so that the thermodynamic efficiency of the engines can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing engine efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the thermodynamic system.    Thermodynamic system (120)    Working fluid (122)    Turbine (130)    Cooling medium (133)    Heat pump (136)
NOVELTY - A ladder device has a bio-membrane band (1); a cross bar (2); suspending ropes (3); a pendant (4); and a hanging rod. The top and both sides of bio-membrane band are provided with a sleeve respectively. Sleeve at the top of bio-membrane band is penetrated by hard cross bar while the sleeves at both sides of bio-membrane band are penetrated by suspending ropes. The top portions of suspending ropes are connected with the hanging rod while bottom portions are connected with the pendant.    USE - Ladder device for hanging and fixing sewage purification bio-membrane band.    ADVANTAGE - Provides ladder device that establishes or improves anaerobic tank, anoxic tank and aeration tank of the sewage treatment plant for sewage treatment, increases the biomass of micro-organisms in the system by folds and effectively removes the pollutants, especially the nitrogen, thus water purification effect of the device is good, treatment efficiency of the system is increased, energy consumption of the system is lowered, and at the same time, greatly reduces the sludge yield of the system and saves the treatment cost of sludge.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the ladder device for hanging and fixing sewage purification bio-membrane band.    Bio-membrane band (1)    Cross bar (2)    Suspending ropes (3)    Pendant (4)
NOVELTY - A unified fuel processing reactor has a primary reformer (110) for reforming a hydrocarbon-base fuel, a desulfurizer (120), and a post-reformer (130) for selectively decomposing a low carbon hydrocarbon compound. The primary reformer, desulfurizer and post-reformer are isolated from each other by internal partition walls. The primary reformer is provided at center portion of reactor, and post-reformer and desulfurizer are concentrically disposed in turn outside of primary reformer.    USE - Unified fuel processing reactor is used for solid oxide fuel cell.    ADVANTAGE - The unified fuel processing reactor has improved reaction stability, and enables miniaturization of fuel cell system.    DETAILED DESCRIPTION - A unified fuel processing reactor has a primary reformer for reforming a hydrocarbon-base fuel and generating hydrogen-rich reformed gas, a desulfurizer for removing sulfur component from the reformed gas, and a post-reformer for selectively decomposing a low carbon (2-5C) hydrocarbon compound contained in desulfurized gas into hydrogen and methane. The primary reformer, desulfurizer and post-reformer are isolated from each other by internal partition walls except a passage for conveying fluid. The primary reformer is provided at center portion of the reactor, and post-reformer and desulfurizer are concentrically disposed in turn outside of primary reformer.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of unified fuel processing reactor.    Inlet port (101)    Outer wall (102)    Primary reformer (110)    Desulfurizer (120)    Post-reformer (130)
NOVELTY - Intensification of biogas production from sewage involves taking crude sewage sludge from upper part of cylindrical container (5) and then forcing it by force pump (2, 9) to a spear cavitator (7), following expansion delivering it back by duct (1, 8) from down into the container, while the sludge flows upwards and then collecting it in the upper part of the container and transmitting to a reactor for methane production.    USE - For intensification of biogas production from sewage through cavitation in spear cavitator (claimed).    ADVANTAGE - The rate of flow of sewage sludge through a spear cavitator is several times higher (preferably at least 5-times higher) then the rate of sludge (particularly fresh sludge) delivery to the container. The method increases efficiency of methane production from communal sewage sludge with concurrent decrease of the organic mass content in the fermented sludge.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for intensification of biogas production from sewage sludge, containing cylindrical container, which in its lower side part is connected with the supply duct (4), which is connected with drum sieve (3) connected with the force pump and a duct which delivers crude sewage sludge to the container, while in the upper side part the container is connected by duct through force pump and spear cavitator and a duct (10) supplying from down to the container, and the outlet of supply duct is directed to a disk (11) having conically edged furrows cut out, where in the upper part of the container there is a duct (6) for transferring sludge to the methane fermentation reactor.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a device for intensification of biogas production from sewage sludge.    Duct (1, 6, 8)    Force pump (2, 9)    Drum sieve (3)    Supply duct (4, 10)    Cylindrical container (5)    Spear cavitator (7)    Disk (11)
NOVELTY - The hydrogen based fuel without wood and other biomass, is obtained from the extraction of olive oil by crushing. The residues from crushing are purified by pyrolysis at 510 degrees C thus forming a carbon mixed with a gas. The mixture is passed through a water-gasification phase to obtain a mixture of hydrogen and carbon monoxide.    USE - The hydrogen based fuel is useful in engines, power plants and batteries (claimed), and as an energy source in power vehicles, buildings and homes.    ADVANTAGE - The hydrogen based fuel can be easily and economically fabricated.
NOVELTY - A porous electrode base material is manufactured by dispersing carbon short fiber and binder short fiber and producing carbon fiber paper, producing precursor sheet by immersing in water and solidifying polyacrylonitrile as resin after impregnating dimethylacetamide solution of polyacrylonitrile as poor solvent into carbon fiber paper, obtaining precursor sheet from which solvent is removed, and carbonizing polyacrylonitrile as resin in precursor sheet and obtaining porous electrode base material. The actual carbon ratio after carbonization in precursor sheet is greater than or equal to 20%.    USE - Manufacture of porous electrode base material for membrane electrode assembly used for polymer electrolyte fuel cell (claimed).    ADVANTAGE - The method obtains porous electrode base material with high water content management function, few battery performance variation by variation of humidification conditions, and sufficient gas air permeability, thickness and penetration direction resistance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a porous electrode base material.
NOVELTY - A gas holder (12) has a storage unit (14) which expands and contracts the stored low calorie gas under atmospheric pressure. A level indicator (34) detects the expansion direction of stored calorie gas and measures the internal volume of storage unit. A gas booster (44) is started when the expansion amount is beyond a constant value and is stopped when the expansion amount is less than the constant value. A controller (66) increases the introductory flow volume of high calorie gas according to decrease of introductory flow volume of low calorie gas.    USE - Fuel gas mixing apparatus for mixing high calorie gas e.g. town gas and low calorie gas e.g. biogas obtained organic refuse, for mixed gas combustion type power generation equipment (claimed).    ADVANTAGE - The mixed gas can be stored in the state near to normal pressure and the supply of mixed gas is steady. The storage unit of gas holder is formed with a simple structure. A favorable combustion state can be achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic block diagram of fuel gas mixing apparatus. (Drawing includes non-English language text)    Gas holder (12)    Storage unit (14)    Level indicator (34)    Gas booster (44)    Controller (66)
NOVELTY - Hydrothermal treatment of biomass comprises obtaining reaction mixture having biomass and enhancing additive, reacting reaction mixture in supercritical or near-critical state of water, and using black liquor as enhancing additive for obtaining reaction mixture.    USE - Method for hydrothermal treatment of biomass (claimed) used for treating waste, or low-value, and streams of biomass converting into gaseous or liquid fuels or base components for further refining.    ADVANTAGE - The method uses low cost black liquor, which makes the reaction mixture easier to process, because it reduces the biomass particle size and tendency of biomass fibers to bond into agglomerates. The reaction mixture has a slippery character due to which higher dry matter contents are achievable, thus leads to decrease of excess water in the process and, and reduces energy needed for heating the reaction mixture. The method gives higher gas yields at shorter reaction times, eliminates or reduces char and tar production, and eliminates or reduces production of carbon monoxide.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for 10. An apparatus for hydrothermal treatment of biomass comprising reaction section (7) for reacting reaction mixture having biomass and enhancing additive in supercritical or near-critical state of water, and feeding unit (12) for feeding black liquor as enhancing additive to the reaction mixture.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the apparatus for hydrothermal treatment of biomass.    Mixing equipment (3)    Reactor system (5)    Heating section (6)    Reaction section (7)    Feeding unit (11, 12)
NOVELTY - A microorganism grease is produced by sorting kitchen waste materials, classifying and recycling non-biomass, removing non-biomass waste, mixing the rest of kitchen waste materials and water, adding composite enzyme preparation, heating the mixture, subjecting to centrifuge, filtering, sterilizing the filtrate; testing sugar degree and pH value, sterilizing, inoculating Geotrichum to the sterilized solution; fermenting, subjecting to centrifuge, filtering, and leaching centrifuged precipitate using organic solvent.    USE - Method of producing microorganism grease (claimed).    ADVANTAGE - The method has mild reaction condition and low energy consumption, does not produce pollutants, is hazard-free, and reduces pollution.    DETAILED DESCRIPTION - A microorganism grease is produced by sorting kitchen waste materials; classifying and recycling non-biomass; removing non-biomass waste; mixing the rest of kitchen waste materials and water; adding composite enzyme preparation; heating the mixture at 50-60 degrees C for 2-4 hours; subjecting to centrifuge; filtering to separate formed precipitate and enzyme digestion solution as filtrate; sterilizing the filtrate; testing sugar degree at 7-10% and pH value at 5.5-6 of the filtrate; sterilizing; inoculating Geotrichum to the sterilized solution; fermenting at 28-30 degrees C for 5-7 days; subjecting to centrifuge; filtering; and leaching centrifuged precipitate using organic solvent. The composite enzyme preparation comprises amylase, diastatic enzyme, protease and cellulase.
NOVELTY - Electrolysis cell or fuel cell comprises a membrane between an anode and cathode, each of which comprises a nonwoven titanium fabric on the side facing the membrane.    USE - The cell is especially useful as a hydrogen-generating electrolysis cell in which a voltage is applied between the anode and cathode, water is supplied to the anode side of the membrane, oxygen or an oxygen/water mixture is withdrawn from the anode side of the membrane and hydrogen or a hydrogen/water mixture is withdrawn from the cathode side of the membrane, or as an electricity-generating fuel cell in which the membrane is wetted, oxygen is supplied to the anode side of the membrane, hydrogen is supplied to the cathode side of the membrane and water is withdrawn from the anode side of the membrane (all claimed).    ADVANTAGE - The titanium nonwovens provide capillary flow of fluids and minimize the risk of damage to the membrane.
NOVELTY - Liquid chainsaw fluid composition comprises 1-30 wt.% of water, up to 0.5 wt.% of methanol, 50-95 wt.% of glycerol, up to 1.5 wt.% of surfactant, up to 20 wt.% of pressure sensitive adhesive, optionally up to 2 wt.% of corrosion inhibitor and/or optionally up to 1 wt.% of perfume.    USE - The composition is useful for the production of biodiesel.    ADVANTAGE - The composition is environmentally harmless and biodegradable. The composition is stable against UV radiation and is not oxidized even when used over a period of 18 months. The cost of the composition is reduced by 50% than conventional chain saw oils.
NOVELTY - The technique involves fully mixing crushed and magnetically separated household waste materials and NaY type molecular sieve catalyst in a closed feeding machine. Products of catalyst cracking are condensed through a condenser pipe, and bio-oils are collected and stored in an oil storage tank. Carbon residues produced in the catalyst cracking reaction are collected with a carbon residue collector, and are utilized as an adsorbent for treating sewage. Gas produced in the catalyst cracking reaction is burned and exhausted through a gas combustion pipe.    USE - Thermal cracking resourcfulization technique for household waste of a ship at sea.    ADVANTAGE - The technique ensures that the bio-oil obtained from the garbage splitting decomposition is utilized for production or livelihood so as to realize the efficient utilization of the energy, and the solid contents of the by-product are mainly carbon residues that can be utilized as an adsorbent for treating the sewage. The technique efficiently prevents the ocean environment from being polluted by the ship, thus ensuring wide market prospect.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a thermal cracking resourcfulization technique.'(Drawing includes non-English language text)'
NOVELTY - Water and acid removal involves utilizing molecular distillation method, where biological oil is distilled at -15 to 5 degrees C of cooling-surface temperature and 20-90 degrees C of thermal-surface temperature. The distillate of the cooling surface is removed and residual liquid of the thermal surface is collected. The distance between thermal surface and cooling surface is 15-60, preferably 15-25 millimeter, and distilling pressure is 10-1000 Pascal.    USE - Method for removing water and acid from biological oil (claimed).    ADVANTAGE - The water and acid removal method is eco-friendly, improves thermal value and lowers acidity and water content of the biological oil by removing water and acid successfully.
NOVELTY - Immobilized microorganism rubber particle filler comprises rubber particles as carrier, an embedding agent and a microorganism enzymatic preparation. All components are interacted to each other to produce high molecular gel, where microorganism is embedded and fixed in the gel network.    USE - Immobilized microorganism rubber particle filler used in sewage treatment (claimed).    ADVANTAGE - The immobilized microorganism rubber particle filler enables to produce internal circulating fluidization of bioreactor easily, and ensures good bio-membrane stability and high association between sewage and immobilized microorganism filler.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing immobilized microorganism rubber particle filler, which involves:    (A) preparing the embedding agent solution;    (B) preparing the microorganism enzymatic preparation solution;    (C) mixing both solutions with continuous stirring to obtain colloid; and    (D) preparing rubber particles and mixing with colloid in cross-linking form to obtain the product.
NOVELTY - Heat of biomass pyrolyzing furnace is directly burnt and dispersedly supplied by using a heat supplying burning device comprising burning devices which are radically dispersed at the upper part of the pyrolyzing furnace, and controlling the highest temperature in the burning area of the furnace at less than 1600 degrees C.    USE - Method of directly burning and dispersedly supplying heat of biomass pyrolyzing furnace.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a method of directly burning and dispersedly supplying heat of biomass pyrolyzing furnace.
NOVELTY - The method involves milling carbon to obtain carbon powder, and conveying carbon powder to an entrained bed by pyrolysis gas. Oxygen is utilized as oxidant in the pyrolysis gas to carry out mixing suspension combustion gasification process. Maximum temperature of a furnace wall of the entrained bed is maintained to be 50 degrees centigrade that is lower than ash melting point of a raw material to provide ash particles on the furnace wall and an outlet of a synthesis gas unit for finally obtaining the synthesis gas by discharging the slag as solid.    USE - Gasification method for high-temperature entrained bed to discharge slag as solid.    ADVANTAGE - The method can be implemented for gasification of biomass and for avoiding changing of the biomass into waste, thus improving environment-friendly effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of a high-temperature entrained bed gasification method. '(Drawing includes non-English language text)'
NOVELTY - Combustion charcoal includes 50-70 pts.wt. of straw, 3.5-4 pts.wt. of sodium nitrate, 25-30 pts.wt. of barium nitrate and 2.5-3.5 pts.wt. of starch. 0-20 pts.wt. of gagate, 5-8 pts.wt. of bentonite and 2.5-3.5 pts.wt. of lime powder are included.    USE - Combustion charcoal.    ADVANTAGE - The combustion charcoal is eco-friendly as it is prepared by utilizing crop straw as main raw material, reduces discharge amount of sulfur dioxide and thus ensures customers safety.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing combustion charcoal, which involves:    (A) crushing straw by fast carbonizing furnace and carbonizing straw;    (B) leading combustible gas generated by carbonizing process of straw into combustible gas hot air furnace of drying line and recovering tar and wood vinegar;    (C) adding raw materials into dosing system connected to a cyclone separator, a cloth bag dust remover and an air transfer pipe and mixing;    (D) transferring the mixed raw materials into forming system by belt conveyor;    (E) transferring the formed product into solar drying line and drying in air;    (F) transferring the product into drying line and drying at 100-120 degrees C; and    (G) weighing, packing and storing products.
NOVELTY - Method for treating lignocellulosic material, involves (a) steam pretreating a lignocellulosic material, (b) subjecting the pretreated lignocellulosic material to biological conversion to yield one or more soluble products and lignin, and (c) separating the one or more soluble products from the lignin to yield substantially pure lignin.    USE - The method is useful for treating lignocellulosic material to produce substantially pure lignin which is useful as feedstock for the production of fuels chosen from synthesis gas, liquid fuel, solid fuel and specialty chemicals (all claimed).    ADVANTAGE - The produced pure lignin is at least 50% pure, preferably 90% pure.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for lignin product produced by performing above-cited method.
NOVELTY - The method involves applying voltage between photocatalyst electrode (2) and metal electrode (3) immersed in hydrogen-sulfide containing liquid (10) using solar cell (5), so that hydrogen is generated and electric power is produced by solar cell, while exposing photocatalyst with respect to light (L). Green laser beam is irradiated to photocatalyst containing metal sulfide material.    USE - Method for processing hydrogen-sulfide containing liquid.    ADVANTAGE - Recovery of hydrogen from hydrogen-sulfide containing liquid using photocatalytic reaction can be easily achieved at low cost in a highly efficient manner, while achieving effective utilization of light.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for processing apparatus of hydrogen-sulfide containing liquid.    DESCRIPTION OF DRAWING(S) - The drawing shows the perspective view of the processing apparatus of hydrogen-sulfide containing liquid.    Photocatalyst electrode (2)    Metal electrode (3)    Solar cell (5)    Hydrogen-sulfide containing liquid (10)    Light (20)
NOVELTY - Preparation of oxidation catalyst comprising cerium oxide (21) and metal i.e. gold (22, 23, 24), platinum palladium, tin, ruthenium or nickel, comprises sputtering cerium oxide and metal from target to substrate. The cerium oxide and metal material are sputtered to substrate concurrently from target(s) to form layer of cerium oxide including dispersed atoms of metal.    USE - Method for preparation of oxidation catalyst comprising cerium oxide and metal i.e. gold, platinum palladium, tin, ruthenium or nickel (claimed) used in fuel cells for producing hydrogen, reforming exhaust of combustion engines and catalyzing other chemical reactions.    ADVANTAGE - The method allows continuous doping of cerium oxide thin layer with metal atoms during its growth on substrate, allows dispersion of metal within cerium oxide layer at atomic level, and leads to presence of metal in ionic form. By the method, an interaction of metal atoms with cerium oxide, its high catalytic activity and high resistance against catalytic poisoning is achieved, i.e. high tolerance for the presence of carbon monoxide in hydrogen during reactions inside fuel cell. The catalytic activity of catalyst is improved. By using catalyst, specific output power of fuel cell is enhanced by 3 orders of magnitude, and high tolerance of catalyst to carbon monoxide content in hydrogen is expected.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a gold-cerium oxide catalyst, comprising 25-99 wt.% gold in the form of gold cations (Au+1 and Au+3); and    (2) a platinum-cerium oxide catalyst, comprising 30-100 wt.% platinum cations (Pt+2 and Pt+4).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of metal atoms within cerium oxide layer.    Cerium oxide (21)    Gold (22, 23, 24)    Clusters (44)
NOVELTY - Producing ethanol and 2-propanol from syngas, comprises: (a) converting syngas into methanol in the presence of a methanol-synthesis catalyst; (b) converting at least some of the methanol from step (a) into a composition including ethylene and propylene in the presence of a methanol-to-olefins catalyst; and (c) hydrating at least some of the ethylene into ethanol and at least some of the propylene into 2-propanol.    USE - The process is useful for producing ethanol and 2-propanol, which are useful to power an internal combustion engine to power a transportation vehicle.    ADVANTAGE - The process provides high selectivites for producing ethanol and 2-propanol from syngas. The process is economical and cost-effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for separating one or more olefins from one or more alcohols, comprising: (a1) providing a feed stream comprising one or more olefins and one or more alcohols; (b1) contacting the feed stream with dimethyl ether, under conditions for absorption of at least one of the alcohols into the dimethyl ether, to generate a solution of dimethyl ether and at least one of the alcohol; and (c1) removing dimethyl ether from the solution from step (b1), to generate a purified alcohol stream comprising the alcohol.    DESCRIPTION OF DRAWING(S) - The figure shows a block-flow diagram for depicting variations of converting syngas into ethanol and 2-propanol.
NOVELTY - A metal-organic framework building block (B1) comprises a tetratopic carboxylic acid and a metal. The metal-organic building block is robust, non-catenated, 3-dimensional, and permanently microporous.    USE - For gas adsorption separation (claimed) e.g. carbon dioxide, hydrogen, nitrogen, and methane from the gas mixture; and also for catalysis, gas storage, sensing, biological imaging, and drug delivery.    ADVANTAGE - The metal-organic building block is robust, non-catenated, 3-dimensional, and permanently microporous. They have low density, high internal surface areas, and uniformly sized pores and channels, thus have high adsorption selectivity for adsorption of gases.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) new 1,2,4,5-tetrakis(4-carboxyphenyl)benzene or their salts;    (2) gas adsorption separation process (M1) involving selectively removing at least one gas from a gas mixture by contacting the gas mixture with block; and    (3) preparing metal-organic framework of formula (Zn 2(A')(B') 2) n involving solvothermal reacting of the tetratopic carboxylic acid and Zn(NO 3) 26H 2O in N,N-dimethylformamide (DMF); optionally heating the product under reduced pressure to remove the DMF; and optionally soaking the product in a tetratopic carboxylic acid containing solution.    n=25-100;    A'=tetratopic carboxylic acid;    B'=R'-pyridin-4-yl or N,N-dimethylformamide;    R'=H, methyl, ethyl, ethenyl or CF 3.
NOVELTY - A photoanode is formed by providing a solution comprising metal ionic species and anionic species; providing a photoactive electrode (130); and causing the metal ionic species and the anionic species to form a catalytic material associated with the photoactive electrode by application of a voltage to the photoactive electrode.    USE - Method for forming a photoanode for the catalytic production of oxygen from water. The photoanode is also used in photoelectrochemical device for electrolysis of water. (all claimed)    ADVANTAGE - The method can form photoanode which can operate with increased energy conversion efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for producing oxygen from water, comprising:    (A) providing a photoelectrochemical cell comprising a photoactive electrode (130); an electrolyte (132); and a catalytic material integrally connected to the photoactive electrode the catalytic material comprising metal ionic species and anionic species, and where the catalytic material does not comprise metal oxide or metal hydroxide; and    (B) illuminating the photoelectrochemical cell with light to produce oxygen from water.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a photoelectrochemical cell.    Chamber (128)    Photoactive electrodes (130, 134)    Electrolyte (132)    Resistor (136)    Power source (138)
NOVELTY - Marsh gas production involves adding water, active mud and solid alkali to broken plant straw, which are anaerobically fermented in the sealed container to produce the marsh gas. The solid alkali is selected from organic solid alkali, inorganic solid alkali or organic and inorganic composite solid alkali. The organic and inorganic composite solid alkali is molecular sieve loaded with organic amine and quaternary amine alkali.    USE - Method for producing marsh gas.    ADVANTAGE - The marsh gas production method has low technical operation demand and low marsh gas production cost, which uses superior strain of flora used in anaerobic active mud for producing greatly improved gas yield, where 10g of plant straw can produce 2760ml of gas in 15 days and the gas producing speed rate is 18.4ml/gram/day.
NOVELTY - The coking furnace has a separating wall (7) in the hearth which is immovably connected to furnace top and furnace walls on two sides of furnace body (15), and is parallel with a garbage baffle (6). The hearth is set between the garbage baffle, the separating wall, and a round flue (9) at central place of furnace top combined the garbage coking room on a furnace bed face (19). The hearth is also set between the separating wall and front wall of furnace body, and a round flue (10) at central place of furnace top combined the garbage coking combustion room on the furnace bed face.    USE - Secondary-burning coking furnace for burning domestic garbage.    ADVANTAGE - Avoids the smoke gas pollutes the atmosphere since the garbage coking by the high temperature oxidation brings small number of non-toxic smoke gas which vents from the flue of the garbage coking chamber. Avoids the acid matter from polluting the atmosphere when the garbage coking brings the combustible gas to fire since the powdery quicklime comes into the garbage layer of the garbage coking chamber oxygen-poor pyrogenation and the acid matter for the high speed airflow which is supplied by the oxygen of the garbage layer. Avoids the furnace bed and the hot straining of the fire grate since the heat insulation stuff layer protects the furnace bed and the fire grate is not protected by the high temperature in the firing space.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic illustration showing the structure of the secondary burning domestic garbage coking furnace.    Garbage baffle (6)    Separating wall (7)    Round flue (9)    Round flue (10)    Furnace body (15)    Furnace bed face (19)
NOVELTY - A movable stirrer is provided in the fermentation vat (5). The movable stirrer has main pipeline (6), sub pipelines (7) transversely connected to main pipeline. A vertical slideway (1) and horizontal slideway (2) are provided in the fermentation vat so that movable stirrer slides left and right or up and down through the slideways.    USE - Device for fermenting animal stool.    ADVANTAGE - Simple, lightweight and energy saving fermenting device can be obtained.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic perspective view of the device for fermenting animal stool.    Vertical slideway (1)    Horizontal slideway (2)    Fermentation vat (5)    Main pipeline (6)    Sub pipelines (7)
NOVELTY - The method involves putting the household garbage into a fermentation tank for primary digestion. The pre-processed fermentation liquid is delivered to an anaerobic reactor for generating the biogas. The biogas is desulfurized using a desulfuration device and is delivered to a combustion stove. A portion of material liquid in the anaerobic reactor is discharged to the fermentation tank for pre-processing and the biogas sludge is discharged from the bottom portion of the reactor directly.    USE - Method for producing biogas using household garbage in cities and towns and wastes in rural areas as raw material.    ADVANTAGE - The biogas containing high concentration of methane and low concentration of hydrogen sulphide can be produced efficiently using household garbage in cities and towns and wastes in rural areas as raw material. The automatic washing of the reactor, reflowing of the material fluid in the reactor to the fermentation tank and automatic draining and pollution removal are performed efficiently. The organic loading rate and processing efficiency of the reactor are improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for device for preparing biogas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for generating biogas. (Drawing includes non-English language text)
NOVELTY - Biomass gasification tar cracking catalyst comprises 10-30 wt.% of nickel oxide, 3-8 wt.% of lanthanum oxide, 1-3 wt.% of magnesium oxide and gamma -aluminum oxide.    USE - Biomass gasification tar cracking catalyst.    ADVANTAGE - The biomass gasification tar cracking catalyst has high intensity and excellent activity and selectivity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing biomass gasification tar cracking catalyst.
NOVELTY - Rupturing a microalgae cell wall, involves providing a continuous flow of a fluid medium comprising at least one microalgae to a hydrodynamic cavitation device; applying hydrodynamic cavitation to rupture at least one microalgae cells, where microalgae oil is released from the microalgae into the medium and extracting the microalgae oil from the medium.    USE - For rupturing a microalgae cell wall to release the microalgae oil useful for biofuel i.e. biodiesel production (claimed).    ADVANTAGE - The methods enables a continuous production of microalgae oil and thus significantly reduces the cost of producing finished biofuels or other products. The current extraction technologies greatly inhibit diatom cultivation for oil production and favor organic wall microalgae cultivation. The use of hydrodynamic cavitation can be applied effectively to both organic and silica wall photosynthetic organisms. The method not only increases the quality and quantity of pure biodiesel fuel output but also its production rate. The method eliminates the need for dewatering steps and harvesting steps required in other extraction processes. The hydrodynamic extraction enables the production of low-cost biofuels from microalgae oils because it is easily integrated into an economic and continuous process. The cost of hydrodynamic extraction using a 10 gallon/minute reactor is approximately 0.002 dollars per gallon of fluid processed which is several orders of magnitude smaller than the alternative combined costs of harvesting, de-watering, and existing extraction technologies. Furthermore hydrodynamic extraction does not require the addition and subsequent removal of costly additives or chemicals and the hydrodynamic extraction also enhances the adoption of diatoms for microalgae oil production.
NOVELTY - Method of generating power, comprises: providing fuel cell (14) that operates using hydrogen gas and hydrocarbon fuel (16); reacting hydrocarbon fuel with water vapor in heated environment to produce reactant gases include hydrogen gas; providing hydrogen separator (24) containing support tube and hydrogen permeable tube that are coaxially aligned so that gap exists between support tube and permeable tube; passing reactant gases through gap in separator, where hydrogen gas permeates through permeable tube and separates from reactant gases; and supplying hydrogen gas to fuel cell.    USE - The method is useful in producing pure hydrogen gas which is used to power a fuel cell.    ADVANTAGE - In the method, power generation system takes hydrocarbon fuel and converts most of the chemical energy in the hydrocarbon fuel into purified hydrogen and produces electricity and water that can be recycled back into the system. The method provides power in a highly efficient, single-step process.    DESCRIPTION OF DRAWING(S) - The figure is a schematic representative of power generating system.    Fuel processor (12)    Fuel cell (14)    Hydrogen fuel (16)    Hydrogen separator (24)
NOVELTY - A 20% amitraz cream is produced by using (kg/ton): raw amitraz (202), emulsifier (120), dimethyl formamide (100), synergistic agent (10) and dimethylbenzene.    USE - Method for producing 20% amitraz cream (claimed) for treating harmful acari on crops, and preventing homoptera pests.    ADVANTAGE - The produced cream is free from environment pollution; improves quality of fruit and level of sanitation, quality and safety; and exhibits fumigating functions.
NOVELTY - A 5% hexaconazole suspension is produced by using (kg/ton): hexaconazole (50.3), special auxiliary agent (120), xanthan gum (3), dimethyl formamide and water.    USE - Method for producing 5% hexaconazole suspension (claimed) used for preventing and treating rice sheath blight, epiphyte diseases of cereal crops, powdery mildew, gray mold of grape and other cash crops.    ADVANTAGE - The method exhibits prevention effect of more than 80%; and can relieve environment pollution.
NOVELTY - A synthetic power fuel comprises (vol.%) power fuel (92.6-99.26) that is formed by mixing hydrocarbons containing 4-18 carbon atoms and 0.74-7.4 vol.% of isopropyl alcohol.    USE - The synthetic power fuel is useful for an internal-combustion engine.    ADVANTAGE - In utilizing the synthetic power fuel, the combustion and the explosion of the fuel and the isopropyl alcohol push an air cylinder shaft to produce power. Moreover, the synthetic power fuel has low sulfur content; where it is environment-friendly, energy-saving, and relatively improved in mechanical power.
NOVELTY - A environment-friendly sludge solid fuel comprises (wt.%) sludge (45-70), potassium permanganate (0.01-3.5), industrial salt (0.1-8) containing sodium chloride, biomass adsorbent (20-50) comprising sawdust, bamboo dust and scrapes or powder of other plants, ash removal anti-coking agent (0.1-3), and hogwash oil (1-10).    USE - The environment-friendly sludge solid fuel is useful for industrial and commercial applications.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a preparation method of the environment-friendly sludge solid fuel comprising: (a) adding potassium permanganate and agitating in a sealed pot for not less than 5 minutes to have the functions of sterilizing and deodorizing; (b) adding industrial salt and biomass adsorbent and respectively agitating for more than 5 minutes; uniformly agitating and adsorbing; (c) processing two times of spiral mechanical pressure dehydration and one time of double-circulated heat parching; where the parching temperature is 100-180 degrees C; or processing one time of spiral mechanical pressure dehydration; where the cost of heat parching will be increased; (d) producing the shape of the product to solid cylinder shape or hollow cylinder shape or the mixture of the two shapes; and (e) cooling the finished products in a cooling system at 22-35 degrees C, packing to sell it; or cooling the products naturally and packing; where the time for cooling will be prolonged.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the device used for preparing the environment-friendly sludge solid fuel.
NOVELTY - A control process for reducing ash content of gasified coal comprises using biomass carbon powder to replace raw coal powder used for producing the gasified coal in proportion to turn it into mixed carbon powder; and regularly adding binder to produce the gasified coal.    USE - The control process is useful for reducing ash content of gasified coal (claimed).    ADVANTAGE - The control process can regulate and control the proportion of anthracitic gasified coal; where the relative decreasing range is 2-8%; thus, the increase of ash content caused by the addition of inorganic binder into the anthracitic gasified coal is completely eliminated and the ash content of the anthracitic gasified coal is reduced to an index lower than inherent ash content of the raw coal powder.
NOVELTY - The furnace has an air outlet pipe (3) whose one end is connected with an upper end side of the furnace and another end is connected with a purifier (4). A flue (6) is placed at the air outlet pipe, and a secondary air supply pipe (7) is installed at an air inlet pipe and connected with a gas output pipe (8) of the purifier. Valves (9, 10, 11, 17) are respectively placed at an air inlet pipe (2), the air outlet pipe, the secondary air supply pipe and the flue. A medium (16) e.g. wooden meal/active carbon/slaked lime, is equipped on layers of a clapboard.    USE - Efficient energy-saving gas furnace.    ADVANTAGE - The furnace is environment friendly, effectively utilizes burnable domestic garbage as fuel, efficiently saves energy, ensures high combustion efficiency, and avoids smoke dust.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of an efficient energy-saving gas furnace.    Air inlet pipe (2)    Air outlet pipe (3)    Purifier (4)    Flue (6)    Secondary air supply pipe (7)    Gas output pipe (8)    Valves (9, 10, 11, 17)    Medium (16)
NOVELTY - The device has a coal gas generator (1) i.e. multi-matter energy coal gas generator, whose wind inlet is connected with gas outlets of a coal gas generator steam pocket (2) and an aquae phenolata evaporator (3). A gas outlet of the coal gas generator is connected with an inlet of a coal gas compressor (8) by an afterheat-recycling dust collector cyclone part (4), a natural wind cooling machine (5), an indirect cooler (6) and an electro-fishing oil lightening machine (7). A gas outlet of the coal gas compressor is connected with a dry-type thionizer (9).    USE - Multi-matter energy environment-friendly air-cooling type coal gas production device.    ADVANTAGE - The device uses inexpensive agricultural waste materials such as straw and wooden meal, organic home scrap combined bales and coal pieces as fuel to produce the purified coal gas in an effective manner. The production cost of the purified coal gas is 0.2-0.35 Yuan, so the purified coal gas has wide range of application.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a multi-matter energy environment-friendly air-cooling type coal gas production device.'(Drawing includes non-English language text)'    Coal gas generator (1)    Coal gas generator steam pocket (2)    Aquae phenolata evaporator (3)    Afterheat-recycling dust collector cyclone part (4)    Natural wind cooling machine (5)    Indirect cooler (6)    Electro-fishing oil lightening machine (7)    Coal gas compressor (8)    Dry-type thionizer (9)
NOVELTY - Starch is manufactured by culturing algae which releases starch extracellularly, leaving the culture still to separate starch and algae and collecting separated starch.    USE - Manufacture of starch for manufacture of ethanol (claimed) such as bioethanol used as fuel for internal combustion engines in motor vehicles.    ADVANTAGE - Starch is manufacture without annihilating the algae cell, ethanol and starch can be obtained continuously and the process is inexpensive.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) manufacture of ethanol which involves saccharifying the obtained starch and performing alcoholic fermentation; and    (2) manufacture of starch and ethanol which involves culturing algae by photoautotrophy using carbon dioxide gas and light irradiation.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of the manufacture of bioethanol. (Drawing includes non-English language text).
NOVELTY - An electrolytic cell has flanged stainless steel cylinder (1) with both ends sealed with stainless steel disc cover (4) and insulated with rubber-made packing (3). The interior portion of the bath is segmented into several chambers with several stainless steel electrode discs (5). The circumference of the cylinder is electrically insulated by plastic insulation cylinder (6) made of polypropylene or Teflon (RTM: PTFE). A ring-shaped electrode plate insulation support frame (7) is fixed to electrode discs.    USE - Oxyhydrogen gas generator for welding, cutting and thermal spraying applications.    ADVANTAGE - A reliable and efficient oxyhydrogen gas generator is realizable. Immediate utilization of generated gas is achievable and the explosion of gas to environment is suppressed.    DESCRIPTION OF DRAWING(S) - The drawings show the sectional view of the stainless steel cylinder, perspective view of the electrode plate insulation support frame and front view of the stainless steel disc cover of oxyhydrogen gas generator. (Drawing includes non-English language text)    Stainless steel cylinder (1)    Rubber-made packing (3)    Stainless steel disc cover (4)    Stainless steel electrode disc (5)    Plastic insulation cylinder (6)    Electrode plate insulation support frame (7)
NOVELTY - The "DENSIFIED PALM FUEL" products compressed into different shapes and size made out of Diological parts of Arecaceae family plants having scientific classification, Kingdom: Plantae, Order: Arecales, Family: Arecaceae, which is a natural redeemable resource. The coconut palm (Cocos nucifera), substance of the family Arecaceae (palm family), in particular having high compressive strength, having less ash content, low moisture, uniformity in size and with low dust content and its simple method for manufacturing. The product comprises particles of coconut palm (frond, fruit bunches, husks inclusive of shells, trunks) organic binders, in the ratio of 99:1. The natural densified palm fuels are prepared by adjusting the particle size of coconut palm to not more than about 70-90% of the minimum dimension of the natural densified palm fuels to be produced, adjusting the moisture content of the coconut palm particles to about 16-28 wt.%, densifying the particles into substantially symmetrical densified palm fuel having dimension between 3-25 mm diameter for pellets, 25-100 mm diameter for briquettes, length generally varies between 25-100 mm, lumps of assorted size from 10-40 mm, bales of 2\asterisk2\asterisk2 or any measure as per requirement, balls of 10-50 mm diameter spherical at a pressure, where constituents of the particles exude and form a coating of wax-like material on the surface of the products, and adjusting the moisture of the products to a content which is in equilibrium with the atmosphere. The natural densified palm fuels product is adapted to be used as fuel in burning of industrial/domestic/commercial thermal applications. Image 0/0
NOVELTY - An apparatus has electrolysis tank containing vertical anode chamber (1) provided with water-permeable plate-type anode pole (4-1), and vertical cathode chamber (6) provided with plate-type cathode pole (9). The anode chamber and cathode chamber are separated from each other using barrier membrane containing fluorine-type cation exchange membrane. The water-permeable plate-type anode pole is in contact with barrier membrane. The space between barrier membrane and cathode pole is filled with ion exchange resin (10).    USE - Apparatus is used for producing hydrogen-dissolved drinking water (claimed).    ADVANTAGE - The apparatus economically provides water having high dissolved hydrogen concentration.    DETAILED DESCRIPTION - An apparatus has electrolysis tank containing vertical anode chamber provided with water-permeable plate-type anode pole and vertical cathode chamber provided with plate-type cathode pole. The anode chamber and cathode chamber are separated from each other with barrier membrane containing fluorine-type cation exchange membrane. The water-permeable plate-type anode pole is in contact with barrier membrane. The space between barrier membrane and cathode pole is filled with ion exchange resin. Highly pure water having electric conductivity of 50 mu S/cm or less is supplied to electrolysis tank, to obtain drinking water having dissolved oxygen concentration of 0.1 ppm or more at pH of 2.5-8.5, preferably 5.8-8.5. An INDEPENDENT CLAIM is included for production of hydrogen-dissolved drinking water.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of electrolysis tank.    Anode chamber (1)    Anode pole (4-1)    Diaphragm (5-1)    Cathode chamber (6)    Cathode pole (9)    Ion exchange resin (10)
NOVELTY - Producing biodiesel fuel, comprises direct conversion of triglycerides (I) into methyl esters (II)-(IV) of the respective acids by cleaving between the consecutive carbon atoms of the glycerol portion.    USE - The method is useful for the production of biodiesel fuel (claimed).    ADVANTAGE - The method: produces biodiesel fuel of high quality, which: is feasible at the industrial level and dispenses the use of alcohol for the production of fatty acid esters to afford a reduction of costs related to the acquisition of raw materials; transforms the fats and oils of vegetable or animal origin into methyl esters; and produces biodiesel that might not generate glycerol as a co-product or by-product.    DETAILED DESCRIPTION - Producing biodiesel fuel, comprises direct conversion of triglycerides of formula ((R1-COO)CH2-CH(COO-R2)-CH2(COO-R3)) (I) into methyl esters of formula (CH3-COO-R1) (II), (CH3-COO-R2) (III) or (CH3-COO-R3) (IV) of the respective acids by cleaving between the consecutive carbon atoms of the glycerol portion.    R1-R3 = not defined.    DESCRIPTION OF DRAWING(S) - The figure shows the schematic diagram of the production of biodiesel fuel.
NOVELTY - A microbial electrolytic cell (100) has a reservoir (110) containing a fluid (140), an organic donor material contained in reservoir, an anode (120) submerged in the fluid, anode-respiring bacteria (125) proximal to the anode, and a cathode (130). The cathode is located above the anode and proximal to an upper level of the fluid contained in reservoir.    USE - Microbial electrolytic cell is used for producing hydrogen (claimed).    ADVANTAGE - The microbial electrolytic cell efficiently enables production of hydrogen.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of microbial electrolytic cell.    Microbial electrolytic cell (100)    Reservoir (110)    Anode (120)    Anode-respiring bacteria (125)    Cathode (130)    Fluid (140)
NOVELTY - An odor assimilating (decomposing) bacteria is manufactured by aerobically culturing odor assimilating (decomposing) bacteria by liquid medium or solid medium for aerobic microbes (bacteria).    USE - Manufacture of odor assimilating (decomposing) bacteria.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a manufacturing method of compost; and    (2) a utilization method of compost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of relationship of fermentation temperature and elapsed time in sludge-disposal method which performs organic-fertilizerization of raw sludge on aerobic conditions. (Drawing includes non-English language text).
NOVELTY - Processing method of drainage liquid involves removing nitrogen component of drainage liquid by supplying to a hydroponics bed (10) having a culture medium (12) with Bacillus subtilis, performing hydroponics, supplying to a process tank (1) which decolorize, aggregates and precipitates pollutant material and removes phosphoric acid component, removing phosphoric acid component, supplying to a processing tank (3) filled with porous materials (4) where B. subtilis cultured in the fine spaces.    USE - Processing method of drainage liquid such as agricultural drainage liquid.    ADVANTAGE - Nitrogen component and phosphoric acid component are efficiently removed and also decolorizes drainage liquid.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a hydroponics apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the processing method of drainage liquid. (Drawing includes non-English language texts).    Process tank (1)    Supplying to a processing tank (3)    Porous materials (4)    Hydroponics bed (10)    Culture medium (12)
NOVELTY - The filter (1) has a main portion (10) provided with a filter layer (12). A to-be-processed water supply unit supplies to-be-processed water to the main portion. An oxygen-containing gas supply unit supplies the oxygen-containing gas to the to-be-processed water in the main portion in upper direction of filter layer. A water level measuring device (40) adjusts the water level of to-be-processed water in the main portion.    USE - Filter used for biological treatment for removal of iron, manganese and ammonia in underground water and river water using microorganism such as nitrifying bacteria, manganese bacteria, oxidation bacteria and iron bacteria. Can also be used in industrial water treatment, sewage treatment and waste water treatment.    ADVANTAGE - The dissolved oxygen concentration of to-be-processed water is controlled easily such that the iron, manganese and ammonia are removed efficiently from the to-be-processed water.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the filter. (Drawing includes non-English language text).    Filter (1)    Main portion (10)    Filter layer (12)    Treated water discharge pipe (20)    Water level measuring device (40)
NOVELTY - The gasifier has a lower part pilot burner (240) connected to a top fire grate (110) that is provided in a bottom air supply tube (230). A combustion zone is formed on a top part of a lower part fire grate (210), and a gasification sphere part is formed on a top part of the combustion zone. A lower part reaction chamber (200) is formed between the bottom air supply tube and the lower part fire grate, and a synthetic gas collecting tube (260) is connected to the lower part reaction chamber for collecting combustibility synthetic gas.    USE - Up down vented type complex gasifier. Uses include but are not limited to up down vented type complex gasifier for converting combustible waste, biomass, dried wastewater sludge and fuel resource into gaseous fuel.    ADVANTAGE - The gasifier increases quality of synthetic gas, improves remaining carbon ratio rate, minimizes residual char, and prevents environmental pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of an up down vented type complex gasifier.'(Drawing includes non-English language text)'    Top fire grate (110)    Lower part reaction chamber (200)    Lower part fire grate (210)    Bottom air supply tube (230)    Lower part pilot burner (240)    Synthetic gas collecting tube (260)
NOVELTY - Generation of hydrogen comprises: producing a hydride slurry by reacting a powder metal with a compound comprising water, hydroxide, and aqueous hydrochloric acid (HCl), where the reaction is a low temperature process performed in a sealed inert gas flushed reaction chamber heated at 100-400 degrees C; reacting the hydride slurry with a compound comprising water or water with aqueous HCl to provide hydrogen; and recycling the metal by reduction of the oxide with sodium or sodium hydride.    USE - The method is useful for preparing hydrogen, which is useful in an engine.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a reactor apparatus for the process of generating hydrogen.    DESCRIPTION OF DRAWING(S) - The figure shows the process of hydride synthesis.
NOVELTY - A large-sized metal separator manufacturing apparatus comprises low dies having a predetermined pattern formed on an upper surface; a transferring mechanism for pitch-transferring the lower dies in directions opposite to each other; and a pressing mechanism for compression-molding a metal plate placed on the upper surface of each of the lower dies and pitch-transferred in which the entire area of the metal plate is divided into unit areas and the compression molding process is performed on the respective unit areas.    USE - A large-sized metal separator manufacturing apparatus for a fuel cell.    ADVANTAGE - The apparatus can prevent spring-back, recoiling, excessive local thinning, and tool wear thus ensuring the dimensional accuracy of a fine pattern of a large-sized separator thus increasing manufacturing speed and yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing of a large-sized metal separator for a fuel cell using an incremental rubber molding process.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic perspective view of a completely sealed retainer.    Retainer (54)    Compression rubber (56)
NOVELTY - Decontaminating syngas, comprises: (a) contacting syngas with one or more sorbents, in which the contacting is upstream of a catalytic candle filter, to form decontaminated syngas; and (b) passing the decontaminated syngas through a candle filter containing a mixed cracking catalyst, where ammonia and tars are removed thus producing a purified syngas.    USE - The process is useful for decontaminating syngas, which is produced by gasification of coal or biomass comprising municipal waste solids or sludges, switch grass, forest litter, wood chips, algae, corn stover and rice straw (all claimed).    ADVANTAGE - The process is simple, compact, and effective process for treating syngas to reduce the levels of tars, metals, ammonia, halides, particulates and sulfur contaminants. The process provides highly pure syngas with less negative effects.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of generic modified gasification apparatus for using nitric oxide as a method for removing ammonia contaminants.    Generic, modified coal or biomass gasification unit (100)    Modified gasification unit (110)    Fuel inlet (120)    Oxygen/steam inlet (130)    Slag outlet and/or recycle outlet. (140)
NOVELTY - The method involves measuring consumption current of kneading machine (54) which kneads the slurry. The viscosity of slurry kneaded with kneading machine is adjusted according to the consumption current. The slurry is formed with the constituents such as coal, limestone and water. The viscosity of slurry is adjusted by adjusting the quantity of water added to slurry. The quantity of water added to slurry is increased, when measured consumption current exceeds preset value and the quantity of water is decreased, when measured current is less than preset value.    USE - Viscosity management method of slurry prepared from sewage sludge, in slurry supply apparatus (claimed) used for supplying slurry to fluid bed boiler as fuel.    ADVANTAGE - The viscosity of slurry can be adjusted to fluid bed boiler exactly and rapidly, irrespective of constituent material of slurry supplied as fuel. Thus the fluid bed boiler can be driven stably.    DETAILED DESCRIPTION - The slurry is prepared from the sewage sludge produced in sewage works. An INDEPENDENT CLAIM is included for slurry supply apparatus (40) which supplies slurry to fluid bed boiler as fuel. The apparatus has an ammeter (60) which measures the consumption current of kneading machine. A valve (52w) controls the flow of water into slurry during adjustment of slurry viscosity and a viscosity control apparatus (62) adjusts the opening degree of valve for water flow.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic block diagram of slurry supply apparatus. (Drawing includes non-English language text)    Slurry supply apparatus (40)    Flow control valve (52w)    Kneading machine (54)    Ammeter (60)    Viscosity control apparatus (62)
NOVELTY - The system (100) has the solid-polymer electrolyte fuel cell (110) that is provided with the anode and cathode catalyst layers. An electrolyte layer is formed between the anode and cathode catalyst layers so as to form the membrane electrode assembly. An enzyme supply unit (130) is connected with the oxidizing agent gas supply line (161) to supply the enzyme (132) to a fuel gas supply pipe (152) so as to disassemble the hydrogen peroxide produced in the fuel cell while detecting the control stop operation of fuel cell.    USE - Fuel cell system for fuel cell electric vehicle (claimed).    ADVANTAGE - Since the hydrogen peroxide produced in the fuel cell is disassembled while detecting the control operation of fuel cell, the deterioration of the electrolyte layer of the fuel cell of the fuel cell system is prevented. Thus, the electric power generation performance of the fuel cell system is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of fuel cell system.    Fuel cell system (100)    Solid-polymer electrolyte fuel cell (110)    Enzyme supply unit (130)    Enzyme (132)    Fuel gas supply pipe (152)    Oxidizing agent gas supply line (161)
NOVELTY - A fuel cell apparatus comprises fuel cell aggregate with fuel cells arranged in module, modifier which is arranged in combustion part of upper part of fuel cell aggregate in module and modifies fuel, fuel supply unit which supplies fuel to modifier, air supply unit which supplies air for electric power generation to fuel cell aggregate, control unit which controls fuel supply unit and air supply unit and fuel utilization change unit which lower high-load area which outputs big electric current value in low-load are which outputs small electric current value.    USE - Fuel cell apparatus for producing electric power.    ADVANTAGE - The apparatus can maintain combustion stability of combustion part even when load following operation is performed.    DETAILED DESCRIPTION - A fuel cell apparatus comprises fuel cell aggregate with fuel cells arranged in module, modifier which is arranged in combustion part of upper part of fuel cell aggregate in module and modifies fuel, fuel supply unit which supplies fuel to modifier, air supply unit which supplies air for electric power generation to fuel cell aggregate, control unit which controls fuel supply unit and air supply unit and fuel utilization change unit which lower high-load area which outputs big electric current value in low-load are which outputs small electric current value. The fuel or air for electric power generation is supplied in flow path of fuel cell of fuel cell aggregate and other fuel and air for electric power generation is supplied outside the flow path of fuel cell. The residual fuel and residual air for electric power generation which are not used for power generation reaction in combustion part.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph of the relationship between electric current value at time of generating mode in fuel cell apparatus and fuel utilization. (Drawing includes non-English language text).
NOVELTY - The method comprises photocatalytically desulfurizing biogas under supply of pure oxygen, and separating carbon dioxide present in the biogas by adsorption means (8), which comprises a carbon molecular sieve. A condensation of biogas is carried out between the desulfurization process and the adsorption process. The biogas is cooled after the desulfurization process and introduced into a provision system after cleaning. The adsorption means is exposed to reduced pressure condition after the carbon dioxide adsorption process. The desorbed gas is introduced to a biogas plant.    USE - Method for cleaning biogas.    ADVANTAGE - The method ensures simple and efficient cleaning of biogas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for cleaning biogas.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of a device for cleaning biogas.    Desulfurization unit (2)    Oxygen source (3, 4)    Adsorption means (8)    Condensation arrangement (9)    Oxygen producing device. (25)
NOVELTY - In a device for thermolysis of a carbonized charge (1), in which the charge is dried and introduced (6, 7) into the thermolysis system (4, 5), a rewetting system (9) for the charge (8) is located in the introduction system.    USE - For thermolysis of a carbonized solid charge (e.g. domestic garbage, car crushing residues, used tires, noxious industrial waste or green waste), to produce a combustible gas and a combustible solid (both of which are useful as energy source).    ADVANTAGE - Rewetting of the charge (generally in compressed bale form) before thermolysis ensures that (especially during shut-down phases) the charge remains moist, does not contract in the introduction channel and maintains a seal to prevent atmospheric from penetrating into the oxygen-free environment within the thermolysis furnace. Risks of burning of the charge and formation of explosive air-combustible gas mixtures in the thermolysis furnace are thus eliminated. Thermal deformation of the loading piston within the channel (which can prevent sliding of the piston and necessitate replacement of the piston) is also prevented.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a corresponding thermolysis method for a carbonized charge, in which the charge is rewetted during introduction into the thermolysis system (specifically by spraying, injection, nebulization or vaporization), preferably to decrease the temperature of the charge during the introduction stage.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic diagram of a carbonized charge thermolysis plant.    Waste to be treated (1)    Loading funnel (2)    Thermolysis furnace (4, 5)    Charge introduction channel (6)    Charge introduction piston (7)    Bales of compressed charge to be treated (8)    Water injectors, as rewetting system (9)
NOVELTY - The method involves trapping carbon dioxide by a thermochemical cycle that comprises a combustion reactor (8) and an oxidation chamber (9) connected together. Metal oxides are circulated in the thermochemical cycle, where the metal oxides are alternately oxidized and reduced, and ensure oxygen supply for combustion. Biomasses are dried by air-lean fumes output from the oxidation chamber of the thermochemical cycle.    USE - Method for extracting carbon dioxide from atmosphere air, by thermochemical conversion of biomasses e.g. agricultural residues, logging residues and sorted household wastes, into energy and synthetic fuel such as methanol and dimethyl ether.    ADVANTAGE - The method can treat the biomasses in proximity of biomass sources, by using small size and large scale installations, and enables the extraction of the carbon dioxide gas in a selective and inexpensive manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for extracting carbon dioxide from atmosphere air comprising a drying reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block representation of a device for extracting carbon dioxide from atmosphere air.    Drying reactor (1)    Paralysis reactor (2)    Thermochemical converter (3)    Combustion reactor (8)    Oxidation chamber (9)
NOVELTY - The method involves using biomasses in a thermochemical converter (3) with trapping of carbon dioxide for producing energy and/or fuels. Curing, pyrolytic gas production, and thermochemical conversion of carbon residue are performed for producing vapor. The carbon residue is transferred to towards converter fuel (8). Air and water/carbon dioxide vapor (9) are used for oxidizing and reducing metallic oxides.    USE - Method for extracting carbon dioxide from atmospheric air.    ADVANTAGE - The method extracts the carbon dioxide from the atmosphere air in a selective manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram illustrating a carbon dioxide extracting method.'(Drawing includes non-English language text)'    Curing reactor (1)    Thermochemical converter (3)    Converter fuel (8)    Water/carbon dioxide vapor (9)    Gaseous flow (10)
NOVELTY - A Paenibacillus THU0001 strain (FERM P-21614) exhibiting organic waste decomposition effect, is new.    USE - The Paenibacillus THU0001 strain is useful for decomposing organic waste and for manufacturing compost (all claimed), where the organic waste is chosen from foodstuff residues such as vegetable debris, fish waste material, fallen leaves, wood chip and excrement.    ADVANTAGE - The microorganisms decompose organic waste stably in a short period of time, and suppresses offensive smell such as ammonia smell.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) composition having organic waste decomposition effect, comprising Paenibacillus sp. THU0001 strain (FERM P-21614), and Bacillus sp. THU3710 strain (FERM P-21616); and (2) method for decomposing organic waste or manufacturing compost, involves mixing the microorganisms or the composition with organic waste, and maintaining warm at 50-75 degrees C.
NOVELTY - A Bacillus sp. strain THU3710 (FERM P-21616), B.ginsengihumi strain THU4501 (FERM P-21617) and Bacillus sp. strain THU0021 (FERM P-21615) capable of decomposing organic waste, are new.    USE - The microorganisms are useful for decomposing organic waste. Can also be useful for decomposing foodstuff residues such as vegetable debris, fish waste material, fallen leaves and wood chip.    ADVANTAGE - The microorganisms decompose organic waste rapidly and produces less offensive odor.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) microbial composition useful for decomposing organic waste, comprising Paenibacillus sp. strain THU0001 (FERM P-21614), Brevibacterium sp. and the above-mentioned bacteria; and (2) method for decomposing organic waste or manure, involves mixing the organic waste with Bacillus sp. strain THU3710 or the above-mentioned microbial composition, and maintaining the mixture at 50-75 degrees C.
NOVELTY - The algae culture apparatus (30) stores water into which gas emitted from a methane fermentation equipment (10) performing methane fermentation of to-be-processed object containing organic matter, is mixed. The emitted gas including carbon dioxide and methane gas is mixed with water so as to purify the methane gas by dissolving and supplying carbon dioxide in the water containing algae.    USE - Apparatus for culturing microalgae e.g. Chlorella, Botryococcus, Haematococcus and Spirulina for use as health food and raw material of liquid fuel, used in organic waste processing facility.    ADVANTAGE - The carbon dioxide discharged during methane gas production from methane fermentation equipment is easily dissolved in water and is effectively supplied for algae while reducing environmental pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for algae cultivation method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the methane gas manufacturing equipment. (Drawing includes non-English language text)    Methane gas manufacturing equipment (1)    Sewage treatment installation (2)    Methane fermentation equipment (10)    Methane gas purifier (20)    Algae culture apparatus (30)
NOVELTY - Producing fuel, preferably diesel fuel from plant or animal oils or fats, comprises transesterifying oils or fats containing fatty acids by glycerol esterification under the addition of an alcohol and a catalyst, and subjecting the reaction product to a sedimentation, where the transesterified oil or fat is settled from the other components of the reaction product, the catalyst is an alkaline catalyst and the transesterification reaction is terminated by the addition of water.    USE - The method is useful for producing fuel, preferably diesel fuel.    ADVANTAGE - The method avoids saponification and emulsion formation, and prevents the separation of esters of glycerol, hence provides high quality and inexpensive fuels.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of a device for transesterification of pretreated plant oils or fats.    Mixing vessel (7)    Reactor (8)    Storage containers (9, 10, 11)    Sedimentation tank. (12)
NOVELTY - The hydrogen production apparatus (22) has a water supply amount control apparatus (24) that controls the amount of water supplied from a water supply system (1). A hydrogen mixer (3) mixes the water vapor and hydrogen. A source gas pre-heater (4) pre-heats the mixed gas. A cell container (6) has a cell (7) that electrolyzes the pre-heated gas, to produce hydrogen. A cell performance monitoring apparatus (23) monitors the performance of the cell. A hydrogen flow control apparatus (25) controls the flow volume of hydrogen.    USE - Hydrogen production apparatus installed in nuclear power plant.    ADVANTAGE - The cell container has cell that electrolyzes the pre-heated gas, to produce hydrogen. Hence the hydrogen can be produced efficiently. The energy required for hydrogen production can be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for hydrogen production method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the hydrogen production apparatus.    Water supply system (1)    Hydrogen mixer (3)    Source gas pre-heater (4)    Cell container (6)    Cell (7)    Hydrogen production apparatus (22)    Cell performance monitoring apparatus (23)    Water supply amount control apparatus (24)    Hydrogen flow control apparatus (25)
NOVELTY - The straw energy-saving gas furnace has a purifier assembly which is a cylinder for containing water that is installed a primary, a secondary, and a third purifiers. The primary purifier is connected with a right flue tube by the outlet pipeline of a top end. The third purifier is connected with a hearth by a gas pipeline. A pyrolyzing chamber is connected with the hearth by a blast pipeline. The blowing pipes of the primary oil-water separator, the primary purifier, and the secondary purifier are connected with the secondary oil-water separator.    USE - Straw energy-saving gas furnace for cooking range.    ADVANTAGE - Provides a straw energy-saving gas furnace that can be conveniently used and exhibits cleanliness while protecting the environment.    DESCRIPTION OF DRAWING(S) - The drawing shows a explanatory perspective view of the straw energy-saving gas furnace.
NOVELTY - Biofuel composition (I) comprises normal chain alcohol(s) (A) (1-24% v/v) having greater than 3C but not more than 21C, natural oils (B) (1-24% v/v) and diesel (C) (52-98% v/v) optionally along with fuel additive(s).    USE - (I) is useful for fueling applications (space heating, lighting, cooking, running of engines in automobiles, running of motor pumps and generators) (all claimed).    ADVANTAGE - (A) stabilizes the natural oil blend. (A) is cheap, safe and environmental friendly. The method of preparing (I): reduces the pollution and carbon dioxide emissions; decreases byproduct toxicity; and does not require heat input from environment, due to the use of (A).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) the preparation of (I) comprising mixing (A) with a blend comprising (B) and (C) optionally along with fuel additive(s); and    (2) a method of fueling (I) comprising fueling (I) for fueling applications.
NOVELTY - A hydrogen-generating apparatus comprises a material supply device (4) which supplies raw material containing sulfur component, a hydrogen supply device (5) which electrolyzes water to generate hydrogen, a hydrodesulfurization device and a modifier (1). The hydrodesulfurization device removes sulfur component in the raw material by using hydrogen generated by hydrogen supply device. The sulfur component-removed raw material is subjected to reforming process in modifier, to generate hydrogen.    USE - Hydrogen-generating apparatus is used for fuel cell system (claimed).    ADVANTAGE - The fuel cell system including hydrogen-generating apparatus exhibits high power generation efficiency. The reduction of heat energy in hydrogen-generating apparatus due to methanation reaction of carbon monooxide or carbon dioxide is suppressed.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) fuel cell system; and    (2) operation of hydrogen-generating apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of hydrogen-generating apparatus. (Drawing includes non-English language text)    Modifier (1)    Heater (2)    Material supplying device (4)    Hydrodesulfurization device (5)    Raw material feed line (6)
NOVELTY - The method involves mixing solid fuel (17) with heavy oil (40) to obtain fuel-oil slurry. Hydro-liquefying process of the slurry at low or middle pressure is performed after performing heating and dewatering process to obtain light oil (25), slurry of heavy oil and residue. Light oil is hydro-refined to obtain refined oil. Slurry of heavy oil and residue are gasified in a gasifier (11) to produce Fischer-Tropsch (F-T) synoil with syngas (47). Hydro refining and hydro cracking processes are performed with respect to F-T synoil to obtain refined oil.    USE - Method for multistage liquefying of carbonaceous solid fuel e.g. coal such as lignite and biomass using suspending bed reactor.    ADVANTAGE - Refined oil can be obtained by performing hydro refining and hydro cracking processes with respect to Fischer-Tropsch synoil. High quality oil of low sulfur and ammonia and other chemical products can be obtained by mixing refined oil obtained by processing F-T synoil and refined oil obtained from hydro-refining process.    DETAILED DESCRIPTION - The method involves mixing refined oil obtained by processing F-T synoil with refined oil obtained from hydro-refining process to produce high quality oil of low sulfur and ammonia. An INDEPENDENT CLAIM is included for system for multistage liquefying of carbonaceous solid fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the system for multistage liquefying of carbonaceous solid fuel.    Gasifier (11)    Solid fuel (17)    Light oil (25)    Heavy oil (40)    Syngas (47)
NOVELTY - Methane and carbon dioxide are purified and recycled from landfill gas by separating methane and carbon dioxide from pretreated landfill gas through one-stage pressure swing adsorption, thoroughly purifying separated methane by two-stage or multi-stage pressure swing adsorption, and purifying separated carbon dioxide through liquefied flash evaporation or rectification.    USE - Method of purifying and recycling methane and carbon dioxide from landfill gas (claimed).    ADVANTAGE - The method prevents environmental pollution and greenhouse effect caused by discharging landfill gas into air. It is highly automated, has good desulfurization, dehydration and purification effects. The device used in the method has zero discharge of waste gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for purifying and recycling methane and carbon dioxide from landfill gas comprising a pretreatment unit, a one-stage pressure swing adsorption unit, a two-stage or multi-stage pressure swing adsorption unit and a carbon dioxide purifying unit.
NOVELTY - Catalytic cracking of tar comprises adding (pts.wt.) a de-tarring catalyst (0.1-5) and biomass (100) in a biomass gasifier at a pyrolyzation temperature of 700-1000 degrees C, and gasifying, where the de-tarring catalyst reacts with a biomass thermal gas at high temperature. The de-tarring catalyst is attapulgite clay, dolomite attapulgite clay, calcinate baudisserite, calcinate limestone, iron oxides ore, manganese oxides ore, and/or alkaline matter.    USE - Method for the catalytic cracking of tar (claimed).    ADVANTAGE - The method has reduced tar content in the gasifier gas, an increased production rate, and is inexpensive.
NOVELTY - The furnace has a reaction hearth (4) whose upper left side is provided with a hot water valve (23), a safety valve (24), a steam valve (25), a temperature resistant hose (26) and a steam intake pipe (27) in a sequence. A ring-shaped air flue (9) is connected to a lower side of the reaction hearth. A right upper side of the reaction hearth is provided with a ring-shaped water tank (2). A vent (17) is arranged between the reaction hearth and the ring-shaped air flue. A ring-shaped air distributor (16) is arranged below the vent that is arranged on the ring-shaped air flue.    USE - Downdraft biomass gasification furnace for heating water to bath and cooking and warming purposes.    ADVANTAGE - The furnace is inexpensive, and the need for coal, oil and gas is prevented, thus avoiding pollution. The furnace has high efficiency. The furnace obtains materials from the local resources.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a downdraft biomass gasification furnace in partial section.    Ring-shaped water tank (2)    Reaction hearth (4)    Ring-shaped air flue (9)    Ring-shaped air distributor (16)    Vent (17)    Hot water valve (23)    Safety valve (24)    Steam valve (25)    Temperature resistant hose (26)    Steam intake pipe (27)
NOVELTY - An ethanol gasoline additive is prepared from organic fatty acids containing-carboxylic acids including (wt.%) palmitic acid (2-40), stearic acid (1-15), oleic acid (3-25), linoleic acid (0-25), linolenic acid (2-20), sinapic acid (0-50), palmitic acid (0-15) and dodecenoic acid (4-13).    USE - Additive used for ethanol gasoline (claimed).    ADVANTAGE - The additive can achieve the full mix of the mixed fuel and retains long-term stability without layering of the mixed fuel, with fuel value of mixed system increased by 10-15%. The vehicles do not require change and are only adjusted in applicability and can be used.
NOVELTY - Decoloring a biodiesel comprises adding 3-15 mass % mixture of active carclazyte and bentonite to biodiesel, controlling temperature at 90-130 degrees C, stirring for 20-60 minutes, filtering or centrifuging after standing for 0.3-1 hour, adding 3-15 mass % hydrogen peroxide, controlling temperature at 80-100 degrees C, stirring for 20-40 minutes, and filtering or centrifuging after standing for 0.3-1 hour.    USE - Method for decoloring a biodiesel (claimed).    ADVANTAGE - The method is pollution-free, does not require normal pressure distillation or vacuum distillation, simple, inexpensive, and achieves high refining speed.
NOVELTY - Production of biodiesel comprises adding waste residual oil of plant oil in a reactor, adding methanol and iodine in the reactor, cooling and separating liquid; distilling upper layer of solution to obtain grease product; and adding the grease product, methanol and iodine in the reaction kettle, performing reflux reaction, cooling and separating liquid, washing upper layer of oil phase by hot water with 50-60 degrees C until the upper layer of oil phase is neutral, dewatering and drying.    USE - Method for producing biodiesel (claimed).    ADVANTAGE - The method is simple in technique and low in device investment, which avoids using a lot of strong acid and strong alkali; and is suitable for industrialization. The environment is less polluted. The methanol used in the reaction can be further recycled.    DETAILED DESCRIPTION - Production of biodiesel comprises:    (A) adding waste residual oil of plant oil in a reactor, taking the weight of the waste residual oil as standard, adding 1.5-2.5 (preferably 1.75) times weight of methanol and 0.5-2 (preferably 1.5)% iodine in the reactor, performing refluxing reaction for 0.5-2 (preferably 2) hours at 50-100 (preferably 80) degrees C, cooling and separating liquid, taking upper layer of solution;    (B) reducing pressure and distilling the upper layer of the solution, removing the methanol and the water produced by the reaction, obtaining grease product; and    (C) taking the weight of the grease product as standard, adding the grease product, 1.5-2.5 (preferably 1.75) times weight of methanol and 0.5-2 (preferably 1.5)% of iodine in the reaction kettle, performing reflux reaction for 0.5-2 (preferably 2) hours at 50-100 (preferably 80) degrees C, cooling and separating liquid, taking upper layer of solution, washing the upper layer of oil phase by hot water with 50-60 degrees C until the upper layer of oil phase is neutral, dewatering and drying, obtaining biodiesel product.
NOVELTY - Method for using carapace solid base catalyst to prepare bio-diesel comprises preparing carapace solid base catalyst through incomplete carbonization, chemical modifying agent dipping and activation treatment; preparing reaction raw material comprising methanol and rape seed oil at a mol ratio of 3:1 to 18:1, where the carapace solid base catalyst is 1-7% of the base oil weight, stirring and reacting for 1-5 hours, filtering the reaction liquid while the liquid is hot, distilling the filtrate, recycling the methanol, and obtaining bio-diesel and glycerol.    USE - Method for using carapace solid base catalyst to prepare bio-diesel (claimed).    DETAILED DESCRIPTION - Method for using carapace solid base catalyst to prepare bio-diesel comprises:    (A) carbonizing the carapace through high-temperature treatment and adsorbing chemical modifying agent solution, and performing activation treatment to the incompletely carbonized carapace adsorbed with the chemical modifying agent to obtain carapace solid base catalyst; and    (B) preparing reaction raw material comprising methanol and seed oil at a mol ratio of 3:1 to 18:1, where the carapace solid base catalyst is 1-7% of the base oil weight, putting the reaction raw material in a reacting device under 0.1 MPa and at 40-80 degrees C, stirring and reacting for 1-5 hours, filtering the reaction liquid while the liquid is hot, distilling the filtrate and obtaining the methanol, recycling the methanol, and obtaining bio-diesel and glycerol.
NOVELTY - Neem biodiesel production involves using byproduct of azadirachtin containing 5% of neem oil as raw material, where ultraphosphate is used as catalyst. The raw material and anhydrous low-carbon alcohol are placed into a microwave reactor under microwave radiation to perform ester exchange reaction. The ester exchange reaction is accomplished at 40-85 degrees C at normal pressure for 10-240 minutes, where methanol is recycled through decompression and distillation processes. The residual mixture is kept to form a layer, where lower layer includes glycerin and upper layer provides neem biodiesel.    USE - Method for producing neem biodiesel (claimed).    ADVANTAGE - The neem biodiesel production method is featured with mild reaction condition, easy operation, easy controlling and high transformation rate, and produces the neem biodiesel in an eco-friendly and cost-effective manner by low energy consumption.
NOVELTY - The method involves suspending an ion collection device having a high density of points per area from a support structure, and electrically connecting the ion collection device connected to the support structure by a connecting wire e.g. Teflon (RTM: PTFE) impregnated wire. A load (150) is provided in an electrical connection to the collection device to draw current, where the device comprises a diode (310) connected between a collection fiber e.g. carbon fiber, and the load. An electrical energy provided to the load is stored in a charging capacitor (410) or an inductor.    USE - Method for collecting electrical energy generated in atmosphere for powering a generator and a motor and for driving a fuel cell to produce hydrogen and oxygen (all claimed).    ADVANTAGE - The method allows efficient collection of the energy in the atmosphere. The diode prevents the collected energy from discharging into the atmosphere through the collection fiber.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an energy collection system comprising a switch.    DESCRIPTION OF DRAWING(S) - The drawing shows a circuit block diagram of an energy collection circuit.    Load (150)    Diodes (310, 440)    Storage circuit (400)    Charging capacitor (410)    Rectifier (450)
NOVELTY - A soft methane tank which contains methane chamber, where the methane chamber is soft fermentation vessel (1), air exhaust pipe (2), feeding pipe (3) are equipped on the upper part of the soft fermentation vessel, and drain pipe (4) is equipped on its lower part, is new.    USE - The methane tank is useful for producing methane.    ADVANTAGE - The device can completely ensure the consistency of the generated methane, and the methane which is produced burn stably, and the burning quality of methane is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the methane tank.    Soft fermentation vessel (1)    Air exhaust pipe (2)    Feeding pipe (3)    Drain pipe (4)    Protecting cover (5)    Automatic discharging pipe (6)
NOVELTY - Buried methane generation tank comprises a tank body (1), a feed opening (2) and a discharge opening (3) at the two sides of the tank body (1) and an air-out opening at the top of the tank body. An endothermal plate (5) is fixed at the bottom of the tank body. There are several radiation pieces (6) on the endothermal plate (5).    USE - The methane generation tank is useful for producing methane.    ADVANTAGE - The tank enhance methane production and does not influence normal production of methane in summer.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the buried methane generation tank.    Tank body (1)    Feed opening (2)    Discharge opening (3)    Endothermal plate (5)    Radiation pieces (6)    Endothermal pipe (7)
NOVELTY - A vehicle aluminum-water hydrogen producing device has backwater cabin (17) linked with a reaction chamber (4) through a drainpipe (18) with drain valve (16); and water tank (1) connected with each reaction chamber respectively through conduit pipes (15). Each reaction chamber is connected with gas-liquid separator (7) respectively through gas pipes (5) set on top of reaction chamber. The lower portion of gas-liquid separator is connected with a filter chamber (12) while upper portion is connected with a gas storage container (8).    USE - Vehicle aluminum-water hydrogen producing device for producing substitute of vehicle fuel.    ADVANTAGE - Provides vehicle aluminum-water hydrogen producing device that is simply structured, economical and environment-friendly, and is an ideal device for producing substitute of vehicle fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of the vehicle aluminum-water hydrogen producing device.    Water tank (1)    Reaction chamber (4)    Gas pipes (5)    Gas-liquid separator (7)    Gas storage container (8)    Filter chamber (12)    Conduit pipes (15)    Drain valve (16)    Backwater cabin (17)    Drainpipe (18)
NOVELTY - A regulating straw gasification furnace comprises a furnace component (1), hearth (2) provided inside the furnace component and a furnace cover (4) provided on the hearth. The hearth is connected with a purifier (7) through a gas pipe (5). The purifier is connected with kitchen component (9) through gas pipe (8). The furnace has through-hole provided on the furnace cover and adjuster (3) provided inside the through-hole. At least two layers of dust removing flaming sheet are provided inside the kitchen component.    USE - Regulating straw gasification furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of regulating straw gasification furnace.    Furnace component (1)    Hearth (2)    Adjuster (3)    Furnace cover (4)    Gas pipes (5,8)    Purifier (7)    Kitchen component (9)
NOVELTY - The mobile work station has a water-energy collecting system that constitutes two half-moon-shaped bases (1) linked through an axis (5). An electricity-generating system comprises a dynamotor (3) installed on the axis. The electricity-generating system, an electric-energy conserving system and an electrolysis device are linked in order. The electrolysis device is linked with a hydrogen and oxygen gas conserving and transferring system (2) through a tube.    USE - Mobile work station for producing hydrogen energy.    ADVANTAGE - Ensures high recycling property, flexible operation, special design for ship body, low production cost and little influence on ecologic environment.    DESCRIPTION OF DRAWING(S) - The drawing shows the explanatory view of a mobile work station.    Half-moon-shaped bases (1)    Hydrogen and oxygen gas conserving and transferring system (2)    Dynamotor (3)    Airtight electrolysis groove (4)    Axis (5)
NOVELTY - A solid fuel contains dehydration agent which reacts with water containing organic waste, water containing adsorbent which has water absorptivity, calcium oxide and manganese dioxide, manganese sulfate and/or cobalt sulfates, combustion improver which contains oil and mineral type waste oil which carried out heating purification of fats and oils separated by grease trap, dryer which reacts with water containing sulfuric acid, hydrochloric acid and/or nitric acid, and plant type waste oil.    USE - A solid fuel used as alternative fuel such as coal and petroleum.    ADVANTAGE - The solid fuel has sufficient heat amount, and can suppress low energy consumed at the time of manufacture.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a manufacturing method of solid fuel involving mixing water containing adsorbent with organic waste in required ratio, transpiring and drying water content with heat reaction, mixing dehydration agent in required ratio, mixing dryer in required ratio, mixing combustion improver in required ratio, carrying out compression-molding, and solidifying.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of manufacturing method of solid fuel. (Drawing includes non-English language text).    Stirring processing tank (1)
NOVELTY - The apparatus has height adjustment devices provided at bottom portion of main section. A food insertion hole is provided at the top of main section. A blower supplies external air into a case. The discharge pipe is connected to air diffuser. A drive motor (41) rotates the stirrer (30). A deodorizing device (90) is filled with deodorizing material such as activated charcoal or hardwood charcoal. The deodorizing device deodorizes the tank. A control unit controls the deodorizing device. A discharge pipe (81) discharges the air within fermentation tank to exterior.    USE - Food garbage disposal apparatus for use in restaurant and home.    ADVANTAGE - The processing efficiency of food garbage can be improved. The discharge of harmful gas from the fermentation tank can be prevented. The growth of microorganism inside the fermentation tank is suppressed.    DETAILED DESCRIPTION - Thermal medium is filled in space provided in heating apparatus. An agitation blade (32) is provided in the stirrer so as to mix the food garbage stored inside the fermentation tank. The heating apparatus heats the fermentation tank.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view showing internal structure of food garbage disposal apparatus.    Stirrer (30)    Agitation blade (32)    Drive motor (41)    Discharge pipe (81)    Deodorizing device (90)
NOVELTY - Self-started oxidative steam reforming of methanol (OSRM) process at room temperature for hydrogen production, comprises: pre-mixing an aqueous methanol and oxygen to obtain a mixture; feeding the mixture to a copper (Cu)/zinc oxide (ZnO)-based catalyst at room temperature, where the catalyst comprises a copper palladium (CuPd)/ZnO catalyst or a copper rhenium (CuRh)/ZnO catalyst; catalyzing an OSRM process and raising a reaction temperature; and yielding hydrogen at the reaction temperature substantially equal to or greater than 140 degrees C.    USE - The process is useful for hydrogen production, which is useful in fuel cells that are useful as potential power supply for notebooks, cellular phones and digital camera.    ADVANTAGE - The hydrogen produced by the method contains substantially less than or equal to 1 mole% carbon monoxide. In the process, no external heat is required for initiating the OSRM process. The process can be carried out at low temperature. In the process, the hydrogen production rate R(H2) is high, preferably greater than 2. The catalyst used in the process has higher methanol conversion rate and lower carbon monoxide selectivity at a lower reaction temperature. The process provides high yield of hydrogen.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a catalyst used in a self-started OSRM process at room temperature for hydrogen production, comprising: the Cu/ZnO-based catalyst, where the catalyst is a supported copper catalyst prepared with a co-precipitation method; a copper content in the catalyst is substantially 10-35% (w/w); and a zinc oxide content in the catalyst is substantially greater than 60% (w/w).    DESCRIPTION OF DRAWING(S) - The figure shows a schematic diagram self-started oxidative steam reforming of methanol for hydrogen production.    Thermally-insulated reactor (100)    Catalyst bed (200)    Reactant (300)    Product. (400)
NOVELTY - Lipids are produced by receiving a feedstock including biological matter. The feedstock is exposed to microbes which are capable of converting the feedstock into lipids and the produced lipids are extracted.    USE - Method of producing lipids including triacylglycerides, free fatty acids, wax esters, straight chain hydrocarbons, or branched chain hydrocarbons, useful for producing fuel including biodiesel, diesel, gasoline, or jet fuel (all claimed).    ADVANTAGE - The method can produce liquid fuel from low-value or waste starting materials of biological origin. The microbial conversion processes can suffice to convert agricultural and municipal waste originating from plant matter into all the components of fuel. Further, there is no net carbon added to the atmosphere when the fuel is burned because the feedstock is originally produced by photosynthesis.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a system for producing triacylglycerides comprising a fermentor, and a controller in communication with the fermentor for providing operating instructions to the fermentor, where the fermentor yields the triacylglycerides.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow chart of a cellulosic feedstock pretreatment process.    Receiving stage (110)    Mechanical pretreatment stage (120)    Thermal-chemical pretreatment stage (130)    Water (134)    Nutrients (138)    Liquid phase (144)    Solid phase (148)
NOVELTY - The apparatus has a thin flexible power source providing power to external components e.g. mixers, and comprising metallization layers, where one of the layers is configured as a miniature powered antenna (100) for transmitting or receiving wireless signals. The power source has a lithium aluminum hydride-based hydrogen generator for producing hydrogen gas, and a proton exchange membrane (PEM) fuel cell for generating an electrical current using the hydrogen gas. The generator has fuel (102) for producing the hydrogen gas and a permeable membrane (104) surrounding the fuel.    USE - Wireless communications apparatus for a wireless communications system e.g. wireless radio, navigation system i.e. global positioning system (GPS) system, and computer system (all claimed), that is utilized for transmitting and receiving a wireless signal.    ADVANTAGE - The antenna, the power source and integrated circuitry are integrated to increases wireless communication range, and to reduce the weight, size and cost of the apparatus.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a wireless communications system    (2) a wireless communications method.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a miniature powered antenna.    Miniature powered antenna (100)    Fuel (102)    Permeable membrane (104)    Electrode (108)    Proton exchange membrane (110)    Cover (112)
NOVELTY - Producing liquid fuel from synthesis gas involves reacting the gas at 500-3000 psi and 200-400 degrees C over a catalyst which is copper, zinc, and potassium on a substrate.    USE - For producing liquid fuel, such as methanol, ethanol, propanol, butanol, hydrocarbons (claimed), which is also known as pioneer synthetic fuel (PSF) useful in automobiles.    ADVANTAGE - The catalyst is inexpensive (no precious or exotic metals were used) and gave no sign of deterioration over the course of the experiment. The method increases the energy content of the fuel. The liquid fuel, i.e. PSF have an advantage relative to ethanol in that it contains about 11% more energy per gallon, and thus is a higher quality fuel. Butanol is better still, having over 20% more energy per gallon than ethanol, but its qualitative advantages are even greater than such a comparison implies.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) producing mixture of butanol, higher alcohols and hydrocarbons from synthesis gas, involving reacting the gas at 500-3000 psi and 200-400 degrees C over a catalyst comprising copper, zinc, and potassium on a substrate, to yield a mixture of alcohols and hydrocarbons comprising methanol, ethanol, propanol and butanol, as well as other alcohols and hydrocarbons; and reacting the methanol with the ethanol and/or propanol to produce butanol under 3000 psi at 200-400 degrees C using catalyst comprising copper on hydrotalcite; and    (2) catalyst comprising copper, zinc, and potassium deposited on a substrate.
NOVELTY - A molecule deposition apparatus (10) has a vacuum chamber (11), controllable matrix translation apparatus for controlling position of solvent-free matrix material, sublimation apparatus for sublimating molecules from matrix material, one or more solvent-free matrices (17), one or more samples (20) separated from the one or more solvent-free matrices, condensation apparatus for individually cooling the samples to deposit the sublimated molecules on the samples, and controllable sample translation apparatus for controlling the position of the samples within the chamber.    USE - The molecular deposition apparatus is useful in imaging mass spectrometry for peptide/protein, lipid and metabolite analysis, biomarker discovery, drug biodistribution monitoring and molecular mechanism investigation.    ADVANTAGE - The apparatus enables to deposit molecules on sample surface with high sensitivity and reproducibility.    DETAILED DESCRIPTION - A molecule deposition apparatus has a vacuum chamber, controllable matrix translation apparatus for controlling position of solvent-free matrix material whose molecules are to be deposited within the chamber, sublimation apparatus for sublimating the molecules from the solvent-free matrix material, one or more solvent-free matrices whose position is controllable by the controllable translation apparatus, one or more samples separated from the one or more solvent-free matrices, condensation apparatus for individually cooling the samples to deposit the sublimated molecules on the samples, and controllable sample translation apparatus for controlling the position of the samples within the chamber. An INDEPENDENT CLAIM is included for molecule deposition method.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of molecule deposition apparatus.    Molecule deposition apparatus (10)    Vacuum chamber (11)    Solvent-free matrix (17)    Sample (20)    Vacuum control dosing system (32)
NOVELTY - Metal complex (I) comprising: at least one metal comprising essential trace metallic element for the development of plants; at least a first ligand comprising lignosulfonate, modified lignin, tannins and derivatives of the compound resulting from biological transformation or chemicals, e.g. by oxidation, reduction, or composting; and at least a second ligand comprising organic polydentate ligand, are new.    USE - (I) are useful in agriculture. (I) are useful for the treatment of metal deficiency. (I) are useful for treating iron deficiency. Tests details are described but no results given.    ADVANTAGE - (I) have good stability and solubility for all types of soils, including basic and limestone, which have a high efficiency without affecting environmental and health.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a composition comprising (I) in combination with carrier or vehicle.
NOVELTY - The system (10) has electrolysis cell (30) that includes negatively-charged electrode plate (32) spaced away from the positively-charged electrode plate. Several neutrally-charged electrode plates (33) which are acting as the outer electrode plates of the electrolysis cell are provided in the space between the positively-charged and negatively-charged electrode plates. An insulating sleeve is provided surrounding and contacting the outer periphery of the electrolysis cell, for intensifying the electric output produced by the electrolysis cell.    USE - Hydrogen generator system for internal combustion engine of vehicle.    ADVANTAGE - The system can include compact electrolysis cell so that system can be used for vehicle of different sizes. The system includes array of positively, negatively, and neutrally charged plates arranged away from each other to maximize the overall efficiency of the system. Electric charge can be directly applied to outermost and inner electrode plates so as to increase operation efficiency. Electrodes are connected in such a way that the electric current flow through the cell is enhanced.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the hydrogen generator system.    Hydrogen generator system (10)    Electrolysis cell (30)    Negatively-charged electrode plate (32)    Neutrally-charged electrode plate (33)    Connection arm (41)
NOVELTY - A hydrogen generation vessel comprises a hollow container including a reduction plate which is disposed inside the hollow container and that produces hydrogen by electrolysis of a flowing conductive water, and opening(s) at predetermined locations in the lower 50% of the hollow volume of container so that water inside the hollow container and water outside the hollow container are in fluid contact and pressure inside the hollow container and pressure outside the hollow container are equalized.    USE - A hydrogen generation vessel for generating hydrogen gas from flowing conductive water at a pressure greater than one atmosphere and for collecting hydrogen gas.    ADVANTAGE - The vessel has minimized hollow container cost and complexity, reduces maintenance cost, and utilizes ocean current thus not harming marine life.    DETAILED DESCRIPTION - A hydrogen generation vessel comprises:    (1) a hollow container including a reduction plate which is disposed inside the hollow container and that produces hydrogen by electrolysis of a flowing conductive water, and opening(s) at predetermined locations in the lower 50% of the hollow volume of container so that water inside the hollow container and water outside the hollow container are in fluid contact and pressure inside the hollow container and pressure outside the hollow container are equalized;    (2) a conductive wire that attaches to the reduction plate; and    (3) a mechanism for holding greater than or equal to 80% of the hollow volume of the container beneath the surface of the flowing conductive water.    An INDEPENDENT CLAIM is included for generation and collection of hydrogen at a pressure of more than one atmosphere.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a basic hydrogen generating station.    Basic hydrogen production station (1)    Rotating disk (2)    Current catcher (3)    Restraint (4)    Ocean current (5)
NOVELTY - The alarm unit has gas sensor which outputs electric signal according to concentration of detected gas. A calculation unit (29) calculates level variation quantity of electric signal with respect to predetermined time. A determination unit determines whether level of electric signal of sensor and level variation quantity of electric signal are more than threshold value. A detection unit (6) confirms leakage of gas, when level of electric signal of sensor, is more than threshold value and when level variation quantity of electric signal, is more than threshold value.    USE - Gas alarm unit for detecting leakage of gas such as methane, carbon dioxide, isobutane and liquefied petroleum gas.    ADVANTAGE - The generation of incorrect warning and misreport can be suppressed. The reliability and operability of alarm unit can be improved. The level variation quantity of electric signal of gas sensor can be calculated efficiently. The alarm unit with efficient fire detection function can be ensured.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of gas alarm unit. (Drawing includes non-English language text)    Main power supply unit (1)    LED (3)    Gas detection unit (6)    Speaker (8)    Variation quantity calculation unit (29)
NOVELTY - A baffle plate (30) has a baseplate portion (32) and the vertical plate portions (33-36) having the clearance gap. A zigzag-shaped flow path (29) is formed in the baffle plate. The vertical plate portions and baseplate portion are arranged alternately from the both end portions of a rectangular metal plate by bending the rectangular regions formed of cuttings in same direction in halfway position at right angle to the base.    USE - Modifier for fuel cell.    ADVANTAGE - The baffle plate is manufactured easily by cutting the metal plate. The number of components is reduced and the need for the tool for attaching the vertical plate portion is eliminated hence the production yield of the modifier is improved. The operability at the time of assembling of the baffle plate is improved. The leakage of the exhaust gas from the flow path is prevented.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing method of baffle plate.    DESCRIPTION OF DRAWING(S) - The drawings show the front, sectional side and rear views of the modifier for fuel cell.    Casing (10)    Flow path (29)    Baffle plate (30)    Baseplate portion (32)    Vertical plate portions (33-36)
NOVELTY - The system (10) has a modifier (20) that produces reformed-gas (g) containing hydrogen, and a fuel cell (30) such as polymer electrolyte fuel cell and phosphoric acid-type fuel cell to receive the reformed-gas to generate electric power. A control apparatus (36) restarts the fuel cell system, when an abnormality detected while stopping the fuel cell system, is related with a predetermined small failure.    USE - Fuel cell system for use in house.    ADVANTAGE - The abnormality detected while stopping the fuel cell system, can be eliminated by restarting the fuel cell system when the detected abnormality is related with the predetermined small failure. The fuel cell system is stopped when the abnormality is not eliminated, so as to enhance the safety operation of the fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fuel cell system.(Drawing includes non-English language text)    Fuel cell system (10)    Modifier (20)    Fuel cell (30)    Power conditioner (34)    Control apparatus (36)    Reformed-gas (g)
NOVELTY - A pulp-type wastewater containing resin component is contacted with magnesium silicate compound and performing anaerobic treatment.    USE - Method used for processing pulp-type wastewater discharged from kraft pulp manufacturing process. Uses include but are not limited to paper manufacturing industry, foodstuff industry, medical industry, chemical industry and steel industry.    ADVANTAGE - The processing of pulp-type wastewater is carried out stably and efficiently. During anaerobic treatment, the fermentation-inhibition effect of the resin component is suppressed by the addition of magnesium silicate compound, without requirement of special installation for pre-processing of floatation separation. The by-product obtained in anaerobic treatment is methane which can be used as energy source in pulp plant and as biogas utilized in recovery boiler, kiln etc.
NOVELTY - An aqueous solution of formic acid containing a catalyst of a compound chosen from rhodium mononuclear metal complex (I), or its tautomer, stereoisomer or salt, formic acid and water is prepared. At least one of formic acid and the water is deuterated. The formic acid is decomposed by process of leaving the aqueous solution of formic acid still, process of heating the aqueous solution and/or process which light-irradiates the aqueous solution to obtain deuterium and/or deuterated hydrogen.    USE - Manufacture of deuterium and deuterated hydrogen, Uses include but are not limited to fuel cell, synthesis of organic compound, determination of hydrogen position by structure analysis, hydrogen isotope, and hydrodesulfurization and hydrocracking of petroleum.    ADVANTAGE - The method enables manufacture of deuterium and deuterated hydrogen simply, efficiently and economically.    DETAILED DESCRIPTION - An aqueous solution of formic acid containing a catalyst of a compound chosen from rhodium mononuclear metal complex of formula (I), or its tautomer, stereoisomer or salt, formic acid and water is prepared. At least one of formic acid and the water is deuterated. The formic acid is decomposed by process of leaving the aqueous solution of formic acid still, process of heating the aqueous solution and/or process which light-irradiates the aqueous solution to obtain deuterium and/or deuterated hydrogen.    Ar'=optionally substituted ligand having aromaticity;    R1-R5=H or substituent;    L=ligand, or does not exist;and    m=positive integer, 0 or negative integer.    An INDEPENDENT CLAIM is included for catalyst for decomposition of formic acid.
NOVELTY - The apparatus has a hen-droppings continuous supply apparatus comprising a hen-droppings supply conveyor (4), a supply portion and an injection portion provided with a detector. The gasifiers are provided with gasifier main portion (7) comprising an air nozzle, a cutting-out rotor (34) and a cutting-out screw conveyor (8) that is provided with a detector. The supply portion is provided with chambers comprising dampers and detectors.    USE - Apparatus for manufacturing fuel gas from hen-droppings.    ADVANTAGE - The deflagration prevention is achieved by the gasifier. The combustible gas can be collected continuously and efficiently. The high sealing performance of the gasifier is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a longitudinal cross-sectional view of the fuel gas manufacturing apparatus. (Drawing includes non-English language text)    Hen-droppings supply conveyor (4)    Gasifier main portion (7)    Cutting-out screw conveyor (8)    Damper (31)    Cutting-out rotor (34)
NOVELTY - A selective adsorption agent contains silver-carrying zeolite.    USE - Agent is used for selective adsorption of cyclohexene from fuel gas used for producing hydrogen for polymer electrolyte fuel cell and solid oxide fuel cell (claimed). Uses include but are not limited to town gas, liquefied petroleum gas, gasoline and kerosene.    ADVANTAGE - The agent efficiently adsorbs and removes cyclohexene from fuel gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus for removing cyclohexene, which has container filled with selective adsorption agent.
NOVELTY - A nano-nickel fuel additive comprises (wt.%) metal nickel nanometer powder (0.3-0.8), methyl tertiary butyl ether (5-10), C5 alcohol (10-15), C6 alcohol (5-10), methanol (53.2-72.7), rocket propellant (5-8), and metallic oxide or metal inorganic salt (2-3).    USE - The nano-nickel fuel additive is useful in various kinds of fuels comprising gasoline, diesel fuel, composite fuel, heavy oil and biological oil for automobile, heavy vehicle, train, steamer and boiler.    ADVANTAGE - The nano-nickel fuel additive has good catalyzing and cracking effects and can make the fuel be in full and uniform combustion; thus, it improves the unit fuel calorific value, reaches the best combustion effect, reduces the pollution discharge, removes the inner carbon distribution of the engine, improves the power, reduces the noise, and reaches the effects of energy conservation and emission reduction.
NOVELTY - Electrolyzing water and aqueous solutions comprises providing an anode, a cathode, and an aqueous hydroxide electrolyte in a reaction chamber, elevating the temperature of the electrolyte to greater than or equal to 280 degrees C, elevating the pressure of the electrolyte to greater than or equal to 2 atm, and providing an electrical voltage across the anode and cathode.    USE - Method for electrolyzing water and aqueous solutions (claimed).    ADVANTAGE - The method uses an electrolysis cell that reduces electrode polarization, enhances surface reaction rates, and minimizes corrosion.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an apparatus for dissociating water    DESCRIPTION OF DRAWING(S) - The drawing is a schematic drawing of an alkaline electrolysis cell.
NOVELTY - Reducing the concentration of sulfur and/or sulfur-containing compound in a biochemically prepared organic compound, involves bringing the respective organic compound into contact with an adsorbent, where the adsorbent is clay doped with silver and/or silver compound.    USE - For reducing the concentration of 2-10C dialkyl sulfides, 2-10C dialkyl disulfides, 2-10C dialkyl sulfoxides, 2-10C alkyl mercaptans, 3-methylthio-1-propanol and/or S-containing amino acids (preferably dimethyl sulfide, dimethyl disulfide and/or n-propyl mercaptan). The method provides ethanol useful as solvent, disinfectant, as component in pharmaceutical or cosmetic products or in foodstuffs or in cleaners, as feed in steam reforming processes for the synthesis of hydrogen or in fuel cells as component in fuels for the operation of internal combustion engines or as building block in chemical synthesis (claimed).    ADVANTAGE - The method reduces the concentration of sulfur and/or sulfur-containing compounds by greater than or equal to 90 (preferably greater than or equal to 95, especially greater than or equal to 98) wt.% (calculated as S), or to less than 2 (preferably less than 1, especially less than 0.1) parts per million by weight (calculated as S).
NOVELTY - An asymmetrical gas separation membrane is formed using soluble aromatic polyimide having repeating unit (1) containing specific tetravalent group.    USE - Asymmetrical gas separation membrane used for selectively separate-recovering specific gas from mixture of gases containing hydrogen gas, helium gas, carbon dioxide gas, methane, ethane, oxygen gas and nitrogen gas, and manufacturing oxygen-enriched air or nitrogen-enriched air (both claimed).    ADVANTAGE - The asymmetrical gas separation membrane having improved gas separation performance and mechanical properties is manufactured using a simple installation.    DETAILED DESCRIPTION - An asymmetrical gas separation membrane is formed using soluble aromatic polyimide having repeating unit of formula (1).    B'=10-70 mol% tetravalent group of formula (B1) and 90-30 mol% of tetravalent group of formula (B2);    A=10-50 mol% of bivalent group (A1) of formula (A1a or A1b) having phenyl group optionally substituted by hydroxy and 90-30 mol% of bivalent group (A2) of formula (A2a or A2b);    r=0 or 1;    Y'=O or single bond;    R,R'=H or organic group;    n=0, 1 or 2;and    X=-CH2- or -CO-.    An INDEPENDENT CLAIM is included for method for selectively separate-recovering specific gas from mixture of gases, which involves using the asymmetrical gas separation membrane.
NOVELTY - A biological fuel is obtained by collecting rice husk, wood meal, branch, straw, wheat straw, peanut shell, tobacco straw, dregs of decoction, rice straw and all combustible biological wastes, crushing by directly compressing rice husk and wood meal, drying, screening and compressing to shape. The ash after burning is directly used as fertilizer or used for processing organic fertilizer after being recovered by chemical enterprise.    USE - Biological fuel for boiler used in power generation and heating, replacement of coal and fuel oil (all claimed), and environment-friendly charcoal.    ADVANTAGE - The biological fuel has long burning time, high heating quantity (reaching 3800 kilocalorie), low use cost, regenerating performance and no environment pollution after being treated.
NOVELTY - The sparger (3) has multiple rotating vanes (301) formed on a central shaft (304). A central hole is formed in the rotating vane, in right angle direction with respect to the central shaft. An adhesive plate (302) is coupled to the rotating vane such that the adhesive plate is protruded outside the rotating vane, by passing a bolt through the central hole.    USE - Sparger of equipment for manufacturing compost from organic waste.    ADVANTAGE - Since the adhesive plate is coupled to the rotating vane such that the adhesive plate is protruded outside the rotating vane, the adhesive plate closely adheres to the inner surface of the reservoir accommodating the organic waste. The spread of the organic waste can be controlled easily by regulating the speed of rotation of the sparger.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the operation of the sparger in the compost manufacturing equipment.    Reservoir (2)    Sparger (3)    Rotating vane (301)    Adhesive plate (302)    Central shaft (304)
NOVELTY - The method involves selecting inputs for a biomass feedstock (26) and a landfill gas feedstock containing moisture, and cooling synthesis gas. The synthesis gas is directed to a water gas shift reactor, and carbon monoxide is converted to mixture of carbon dioxide and additional hydrogen. The mixture of the carbon dioxide and the hydrogen are directed to a pressure swing adsorption unit with outlets for a final gas separation and purification stage. High purity hydrogen gas and a stream of offgas being utilized as fuel in a reformer burner are collected from the outlets, respectively.    USE - Method for producing hydrogen and carbon dioxide by an integrated closed-loop processing of landfill gas and biomass feedstock such as citrus waste, sugarcane bagasse, wood, agricultural waste, animal waste, solid municipal biological waste and vegetative waste (all claimed).    ADVANTAGE - The method enables facilitating hydrogen production by an integrated closed-loop processing of landfill gas and solid biomass feedstocks with minimal environmental impact, thus increasing energy efficiency by producing high purity hydrogen. The method allows a biomass gasifier to utilize a surplus steam being generated during landfill gas processing using a closed-loop integrated process, thus avoiding the usage of a special energy-intensive steam generator, and hence reducing the cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a system for producing hydrogen by an integrated closed-loop processing of landfill gas and biomass feedstocks.    DESCRIPTION OF DRAWING(S) - The drawing shows a simplified schematic view of a hydrogen production system for integrated closed-loop processing of landfill gas and citrus waste.    Biomass gasifier (21)    Fresh charcoal (24)    Specialized facility (25)    Biomass feedstock (26)    Citrus fruit (28)
NOVELTY - Bioremediation process uses waste from wineries as carbon and energy source for sulfate-reducing bacteria, where carbon and energy source is ethanol. Calcite and marble sludge are provided for maintaining pH of waste wineries containing medium.    USE - Bioremediation for treating and decontaminating water and effluents containing metals and sulfate.    ADVANTAGE - The bioremediation process enables to reduce sulfate into metal sulfides on large scale in a cost-effective manner.
NOVELTY - An aluminum alloy contains electrochemical noble element, and generates hydrogen by performing hydrolysis reaction in alkaline water.    USE - Aluminum alloy is used for generating hydrogen used as power source of fuel cell for portable electronic instrument e.g. mobile telephone and notebook personal computer, household appliances and vehicle, and heat source of boiler (all claimed).    ADVANTAGE - The aluminum alloy has excellent designability, and is economically manufactured. The aluminum alloy rapidly and safely generates hydrogen.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for manufacture of aluminum alloy.
NOVELTY - A biogasoline is prepared by hydrolyzing biomass of lignocellulose to obtain hydrolyzed raw material liquid; conveying the hydrolyzed raw material liquid into low-temperature reforming reactor filled with catalyst nickel/silicon dioxide-aluminum oxide to react at 160-210 degrees C and 4-6 MPa; conveying the reaction materials form the low-temperature reforming reactor into high-temperature reforming catalyst filled with nickel/HZM-5 to react at 210-270 degrees C and 2-5.6 MPa; and performing gas-liquid separation on the reaction materials.    USE - Method for preparing biogasoline (claimed) for car-carried engine system.    ADVANTAGE - The method is capable of separating layers automatically and it avoids technique of rectifying and purifying the product. The source of raw material is wide and the cost is low.    DETAILED DESCRIPTION - Preparing biogasoline comprises:    (A) hydrolyzing biomass of lignocellulose to obtain hydrolyzed raw material liquid;    (B) conveying the hydrolyzed raw material liquid into low-temperature reforming reactor filled with catalyst nickel/silicon dioxide-aluminum oxide to react at 160-210 degrees C and 4-6 MPa;    (C) conveying the reaction materials form the low-temperature reforming reactor into high-temperature reforming catalyst filled with nickel/HZM-5 to react at 210-270 degrees C and 2-5.6 MPa; and    (D) performing gas-liquid separation on the reaction materials from the gas-liquid separation after the reaction materials are condensed, absorbing the uncondensed biogasoline by 6C alkyl hydrocarbon after being decompressed, and performing phase separation on the liquid by a phase separator to obtain the biogasoline on upper layer of the phase separator.
NOVELTY - Organophosphorus derivative preparation involves reacting 3,5-pentadecylphenol derivative with sodium hydroxide, in presence of chloroform to obtain sodium salt of 3,5-pentadecylphenol derivative. The obtained sodium salt of 3,5-pentadecylphenol derivative is reacted with a dialkyl or diaryl phosphate to obtain the organophosphorus derivative.    USE - Method for preparing organophosphorus derivative for use in petrochemical industry for synthetic oils and mineral oils preparation, and biomass for biofuel preparation.    ADVANTAGE - The organophosphorus derivative preparation method is cost effective and enables to prepare organophosphorus derivatives with high purity, and is eco-friendly.    DETAILED DESCRIPTION - Organophosphorus derivative preparation involves reacting 3,5-pentadecylphenol derivative having chemical formula (I) with sodium hydroxide, in presence of chloroform to obtain sodium salt of 3,5-pentadecylphenol derivative having chemical formula (II). The obtained sodium salt of 3,5-pentadecylphenol derivative is reacted with a dialkyl or diaryl phosphate to obtain the organophosphorus derivative having chemical formula (III).    R1=pentadecyl group;    R2=H, tert.-butyl group or sec-butyl group; and    R3=diethyl phosphite, diphenyl phosphite or diethoxy phosphorus group.
NOVELTY - Excrement and domestic organic waste collection includes using movable toilet bowl, paper-like excrement containing bag and an excrement collector. Polyvinyl chloride (PVC) pipe unit including elbow, three-way element, four-way element and five-way element and new exhaust fan are also included. A sewage discharging system structure and a deodorizing structure are also provided. A movable toilet bowl and an excrement collector are installed.    USE - Method for collecting excrement and domestic organic waste for generating biogas.    ADVANTAGE - The excrement and domestic organic waste collection method is cost-effective, eco-friendly and controllable, and ensures easily operated water-free collection of urine, excrement and domestic organic wastes to generate biogas.
NOVELTY - Treating environment, and regenerating and utilizing energy sources comprises classifying, recovering, and processing garbage into energy sources, such as in vacant lots beside rivers and roads, on mountains and scattered plots of unutilized land and crops in countryside.    USE - The method is useful for treating environment, and regenerating and utilizing energy sources (claimed).    ADVANTAGE - The method overcomes the following problems: (a) larger amount of land is occupied and an increased cost is incurred if the garbage is buried; (b) serious pollution; (c) valuable resources are wasted; (d) when garbage is burned, lots of land is occupied; (e) the investment, project, and cost are huge; (f) the resources utilizing rate is lower; and (g) the energy consumption is great and the effect is not ideal. The method provides the following advantages: (a) the operation is convenient; (b) the participating activity of the people is developed; (c) available resources, such as water and land, are used more effectively; (d) both environment treatment and energy source-regeneration and utilization are achieved; and (e) provides significant improvement in environmental protection and long-term development and harmony between human and nature are cultivated (claimed).
NOVELTY - The generator has solar regenerator which is connected with fermentation reaction chamber through radiator. A sealed feeding port and water discharge port are attached with upper and lower portion of fermentation reaction chamber, respectively. A methane storing chamber is set on the fermentation reaction chamber. A feed liquid recycling and stirring unit is set under the fermentation reaction chamber. A water discharge port is connected with pressure door discharge port.    USE - Solar powered methane generator.    ADVANTAGE - The methane production efficiency can be improved. The methane can be discharged easily from generator and leakage of methane can be reduced. The reliability and performance efficiency of generator can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of solar powered methane generator.
NOVELTY - The electrolysis bath has electrolysis slots connected through end clamp plate (4), disk spring (3), nut (2) and tightening bolt (1) to form a complete electrolysis bath. Each electrolysis slot is provided with oxygen pole frame, hydrogen pole frame, supporting net, electrode, membrane, sealing pad and pole plate. The oxygen pole frame and hydrogen pole frame are integrated, in which the pole plate embedded while the pole plate, oxygen pole frame and hydrogen pole frame are tightly connected.    USE - Electrolysis bath for producing hydrogen and oxygen by water electrolysis.    ADVANTAGE - Provides a novel electrolysis bath that uses non-metal pole frame, ensures reduced weight and cost, and at the same time solves the problem of pole frame corrosion encountered in the conventional electrolysis bath.    DETAILED DESCRIPTION - The oxygen pole frame, pole plate and hydrogen pole frame form double-pole frame components on the two sides of the double-pole plate area. The supporting net provides supporting electrode and flow field. The conducting electrode, membrane and sealing pad form the cathode slot and anode slot.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the novel electrolysis bath.    Tightening bolt (1)    Nut (2)    Disk spring (3)    End clamp plate (4)
NOVELTY - The methane generator has a tank whose bottom is provided with a residue chamber. The top of the residue chamber has isolation net. The bottom of residue chamber has a slag-drip hole that is connected with a residue circulation and removal system. The arc shaped main slag-drip pipe of the residue circulation and removal system is made of soft rubber.    USE - Methane generator.    ADVANTAGE - The simple structured methane generator is constructed easily and efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of the methane generator.
NOVELTY - The device has an upper cover and a lower cover fixed together by a fastening portion which is covered with a resin glass fiber reinforced plastic. The upper cover is provided with a slag breakage hole, a feed inlet, a discharge hole, and a vent for externally connecting a gas input pipe. The lower cover is provided with a taphole, and the slag breakage hole and the taphole are provided with a movable sealing cover.    USE - Methane production device.    ADVANTAGE - The sealing property and the safety of the device can be improved, and it can be used conveniently.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the methane production device.
NOVELTY - The present invention is related to a method of inhibiting egg hatch of apple snail and composition thereof, wherein a spray agent is manufactured by various ratios of a vegetable oil with natural ingredients (including any one of salad oil, peanut oil, sunflower oil, olive oil and so on several vegetable oil) and the composition thereof (including emulsifier, camphor oil, and water). The gap between egg and egg is filled with the spray agent when spraying on the egg of apple snail directly to form a thin film over the egg mass, so that the air hole of the egg is completely sealed to isolate air. Thereby, the embryo is suffocated to death, so that the hatch rate of the egg decreases to zero. The preferred embodiment of the present invention is: forming the spray agent with mixing 80% vegetable oil with 5% emulsifier and 15% water, or mixing 40% vegetable oil with 5% camphor oil, 5% emulsifier and 50% water, which both can inhibit hatch of the egg of apple snail completely. The composition ratio of the present invention has low cost, fit for economic efficiency; reach the object of getting rid of bugs and without the problem of environmental pollution and ecological unbalance.
NOVELTY - This invention provides a manufacturing method of eco-friendly dining utensils, which comprises preparing 40% of coarse husk powder or various bean pod powder, 40% of rice stem powder and 20% of binder, sticky rice thick liquid; mixing, heating and stirring the above-mentioned materials into a pasty state; using a production machine tool to inject mold the mixture into dining utensils such as a bowl, a plate, a spoon, chopsticks, etc.; spraying edible gelatin onto the product surface to reduce its water absorption and thus obtain an eco-friendly dining utensil product. The raw materials used in this invention are obtained from agricultural grain wastes and the eco-friendly utensils are provided for disposal purpose. The disposed eco-friendly dining utensils, after use, can be piled up, softened and fermented to form organic fertilizers for total utilization, which further improve their practical application value.
NOVELTY - A composition contains crystal violet lactone (I).    USE - Composition is used for identifying petroleum products e.g. gasoline, light oil, heavy oil and kerosene, and biodiesel and bioethanol (both claimed).    ADVANTAGE - The composition has excellent durability, and identifies petroleum products using simple process.    DETAILED DESCRIPTION - A composition contains crystal violet lactone of formula (I).    R1,R2=H or linear 1-6C alkyl.    An INDEPENDENT CLAIM is included for identifying petroleum products, which involves using composition.
NOVELTY - The floating cover has a gas-proof sheet (3) supported by several floating edge elements (1), which extends by a skirt. Several cables (2) arranged radially, connect the floating elements to one another. The skirt is fixed to the bottom of said floating elements so as to constitute together with the liquid contained in the tank (100). A perimetral hydraulic guard is provided for keeping gases and volatile substances underneath the sheet.    USE - Floating cover for tank for storing residential sewage and industrial sewage.    ADVANTAGE - The impermeable seal of cover is guaranteed by skirt which does not rise from liquid contained in the tank such that installation is enabled directly on the bottom of the tank and the recovery of rain water is enabled effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the floating cover.    Floating edge element (1)    Cable (2)    Gas-proof sheet (3)    Central floating element (4)    Tank (100)
NOVELTY - A bio-membrane carrier has spacers (4,5) arranged along radial direction of cylindrical barrel (2,3) with respect to the inner cylindrical barrel (1). The cylindrical barrels are arranged with axial lines set in superposed manner, at an angle of 45 to 90 degrees.    USE - Bio-membrane carrier for use in sewage water treatment.    ADVANTAGE - Provides a carrier having good structural design, has good microorganism adhesive performance, has good water flow control performance, and has high bio-membrane function to treat sewage water reliably.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the carrier.    Inner cylindrical barrel (1)    Cylindrical barrel (2,3)    Spacers (4,5)    Rib (6)
NOVELTY - The fuel cell system has fuel cell stack (1) that generates electric power. The temperature of the fuel cell stack is detected by a temperature sensor (43). The target electric power of the fuel cell stack is calculated. The fuel cell stack is controlled based on difference between generated electric power and target electric power, so that target electric power is generated from the fuel cell stack.    USE - Fuel cell system mounted in vehicle.    ADVANTAGE - The target electric power can be generated from the fuel cell stack and the fall of output performance of the fuel cell system can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the fuel cell system. (Drawing includes non-English language text)    Fuel cell stack (1)    Fuel tank (10)    Hydrogen circulation pump (12)    Radiator (30)    Temperature sensor (43)
NOVELTY - Method for increasing ratio of Bacillus with respect to all bacteria in sludge of biotic waste water treatment, involves forming bacterial spores in sludge and disinfecting sludge after sporulation.    USE - The method is useful for increasing ratio of Bacillus with respect to all bacteria in sludge for treating biotic waste water (all claimed).    ADVANTAGE - The number of Bacillus in the sludge is measured rapidly and accurately by a simple and cost-effective process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for method for measuring the number of Bacillus in the sludge of biotic waste water treatment.
NOVELTY - Decomposition of carbon dioxide gas contained in carbon dioxide gas-containing gas is carried out by reacting in presence of a reducing substance capable of reacting with oxygen atom of carbon dioxide gas, and a decomposition reaction substance capable of accelerating decomposition of carbon dioxide gas. Carbon is adhered on decomposition reaction substance, and substance is reduced by decomposition of carbon dioxide gas.    USE - Decomposition of carbon dioxide gas contained in exhaust gas of converter and reduction furnace of iron mill.    ADVANTAGE - The carbon dioxide gas is efficiently decomposed using sensible heat of carbon dioxide gas-containing 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)    Dust collector (5)    Gas analyzer (6)    Controlling valve (7)    Switching valve (8)
NOVELTY - The device has a direct current (DC) voltage converter for converting DC generated by a fuel cell into output power. An output current regulation module regulates current of the output power according to voltage of the DC. A voltage protection module closes the DC voltage converter when the voltage of the fuel cell is lower than protection voltage of the fuel cell. A protection timing module calculates protection time when the voltage of the DC surpasses the protection voltage. A restart module restarts the DC voltage converter after the protection time.    USE - Fuel cell stabilizing device.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a fuel cell stabilizing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow chart illustrating a fuel cell stabilizing method.'(Drawing includes non-English language text)'
NOVELTY - The generator (1) has a Peltier element (11) supplying water, and a high voltage application member (15) applying high voltage. A discharge electrode (10) has higher ionization tendency than hydrogen, and is provided with electrostatic atomizing function to generate electric field when high voltage is applied and water is supplied, and atomizes the water to produce microparticulated water. The electrode includes hydrogen molecule generating function that produces a molecular hydrogen, and generates hydrogen water mist (M) that contains the hydrogen in the microparticulated water.    USE - Reduced water mist generator for use in an article to impart antioxidative effect to a target article such as human skin and hair, food product, metal. Uses include but are not limited to shower head, facial massager, sauna suit, hair dryer, hair brush, hair iron and curling iron, air conditioner, sauna equipment and prefabricated bath unit.    ADVANTAGE - The generator allows a metal mesh to secure large contact area for contacting a hydrogen radical that is to be removed, so that large amounts of the radical can be removed. The generator provides cooling effect due to cooling side of the Peltier element to result in conversion at the cooling side of moisture when the Peltier element is energized.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for producing reduced water mist.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a reduced water mist generator.    Hydrogen water mist (M)    Reduced water mist generator (1)    Discharge electrode (10)    Peltier element (11)    High voltage application member (15)
NOVELTY - A particulate fuel additive composition comprises a reaction product of an active metal salt and an organic acid, where the particles have a particle size below 200 nm.    USE - For treating carbon-based fuels such as coal, selected from bituminous, sub-bituminous, anthracite, lignite, peat, bagasse, wood chips and/or other solid fuels (preferably petroleum derived fuel) (claimed); for treating fuel-burning boilers to control emissions and deposits; the high flash point products are used in coal fired boilers or other types of combustion equipment and industrial combustion.    ADVANTAGE - The composition provides convenient production of fuel products with higher flash points to reduce emissions and deposits. The method improves the safety aspects of products especially when used in, around and near high temperature combustion equipment and due to decrease in size of particles, the fuel treatment is improved. The products are inherently safer to use in potentially dangerous environments.
NOVELTY - The bio-membrane belt frame device includes a frame (1) which has cubic structure and empty periphery. The upper fixing rods are arranged in parallel and are set at the upper section of the frame. The lower fixing rods are arranged in parallel and are set at the lower section of the frame. A bio-membrane belt (4) is fixed in the frame vertically and in parallel. The upper and lower ends of the bio-membrane belt are fixed on the upper fixing rods and the lower fixing rods of the frame. The side length of the frame is 1 to 5 meters, and the side length of the bio-membrane belt is 1 to 5 meters.    USE - Bio-membrane belt frame device for purifying sewage.    ADVANTAGE - Reduces sludge yield of the system, saves sludge treatment cost, improves treatment efficiency of the system, and increases biomass of the microorganisms in the system by predetermined number of times.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the bio-membrane belt frame device filled with bio-membrane belts.    Frame (1)    Bio-membrane belt (4)
NOVELTY - Methane tank provided with internal circulation in vertical direction comprises a fermentation tank (1), a feeding pipe (2) and a discharging pipe (3).    USE - The tank is useful for producing methane.    ADVANTAGE - The tank is sanitary and advantaged in high degree of automation, beautiful appearance, safe use, high gas density, long service life, and small size.    DETAILED DESCRIPTION - Methane tank provided with internal circulation in vertical direction comprises a fermentation tank (1), a feeding pipe (2) and a discharging pipe (3), the feeding pipe (2) is connected to the lower part of the fermentation tank (1), where the top of the fermentation tank (1) is provided with an outlet pipe (4), an annular internal circulating tank (5) is set above the fermentation tank (1), the fermentation tank (1) is in communication with the internal circulating tank (5) through a discharging channel (6), the discharging channel (6) is connected to the discharging pipe (3).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the methane tank.    Fermentation tank (1)    Discharging pipe (2)    Outlet pipe (3)    Annular internal circulating tank (4)    Discharging channel (5)    Movable cover plate (6)    Sand precipitation tank (7)
NOVELTY - The dryer (100) has a heat exchanger (200) that performs heat-exchange process with respect to the air within a heating jacket (120) provided in a drying tank (110). A heating unit (140) is installed in the vicinity of the heat exchanger and operated to increase temperature of the air in the drying tank by supplying thermal medium of high temperature. A microwave generator is arranged in the drying tank to irradiate microwave with respect to the organic waste in the drying tank.    USE - Dryer for processing organic waste e.g. food waste received from home and food industry.    ADVANTAGE - Moisture content in the organic waste provided in drying tank can be removed by irradiating microwave using microwave generator. Hence, fermentation process of the organic waste can be done easily and drying process of the organic waste can be performed within short period of time. Energy consumption of the dryer can be reduced effectively by utilizing energy obtained from condensed water so that the necessity of using bio fuel or oil in the dryer can be eliminated. Structure of the dryer can be simplified at low cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of the dryer. (Drawing includes non-English language text)    Dryer (100)    Drying tank (110)    Heating jacket (120)    Heating unit (140)    Heat exchanger (200)
NOVELTY - The turner has traveling devices i.e. helical auger or helical reamer, installed on a machine frame, and one row or more than one row of turning devices that are installed under the machine frame. The shaft line portion between the adjacent two turning devices on the same row is vertically and symmetrically installed with two rows of branch vent pipes, which extend into the bottom of the fermented material. The supplying device is connected with branch vent pipes by a main vent pipe. A driving device of the helical augers is linked by the helical augers.    USE - Helical fermentation turner for turning organic material e.g. fertilizer and fodder.    ADVANTAGE - The helical turner can guarantee the impulsive ventilation and oxygenation. The stability and safety of the turner are increased. The fermentation period is shortened by more than 70 percentage and the turnover rate of the fermentation workshop is increased by more than 50 percentage. The energy consumption during the fermentation production process is reduced by more than 50 percentage. The economic benefit of the turner is obviously improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a helical fermentation turner.
NOVELTY - A low-content methanol diesel comprises (mass%) diesel (50-80), methanol (10-30), jet fuel (5-10), and additive (5-15). The additive comprises (wt.%) oleic acid (3-8), naphthenic acid (0.3-3), emulsifying agent (0.6-2.5), ethanolamine (0.8-3), and solubilizer (0.1-1). The solubilizer is polyether. The emulsifying agent is fatty alcohol-polyoxyethylene ether, n-octyl alcohol, isooctanol, n-dodecyl alcohol, and/or polyethylene glycol. The ethanolamine is monoethanol amine, diethanolamine, and/or triethanolamine.    USE - Low-content methanol diesel for vehicle (claimed).    ADVANTAGE - The diesel is inexpensive and has good water solubility.    DETAILED DESCRIPTION - Low-content methanol diesel comprises (mass%) diesel (50-80), methanol (10-30), jet fuel (5-10), and additive (5-15). The diesel is number 0 diesel and -10 diesel. A water content of the methanol is less than 0.1%. The jet fuel is No. 2 jet fuel or No. 3 jet fuel. The additive comprises (wt.%) oleic acid (3-8), naphthenic acid (0.3-3), emulsifying agent (0.6-2.5), ethanolamine (0.8-3), and solubilizer (0.1-1). The solubilizer is polyether having hydrophobic lipophilic balance value of 9-12 and molecular weight of 2000-5000. The emulsifying agent is fatty alcohol-polyoxyethylene ether, n-octyl alcohol, isooctanol, n-dodecyl alcohol, and/or polyethylene glycol. The ethanolamine is monoethanol amine, diethanolamine, and/or triethanolamine. An INDEPENDENT CLAIM is included for a method for preparing the low-content methanol diesel comprising mixing all components of the additive except the emulsifying agent; mixing the diesel and jet fuel, and adding methanol into the mixture; adding the mixture of the components of the additive except the emulsifying agent into the mixture of diesel and jet fuel and methanol; and adding emulsifying agent, and stirring for 60 minutes to obtain uniform transparent mixture.
NOVELTY - Inserting piece of culture medium comprises a frame (1) set in the sewage to be treated; the upper end of the frame (1) is connected with a floating element (2); and the inner side of the frame (1) is provided with a carrier (3) for absorbing culture medium.    USE - The inserting piece of culture medium is useful for microbial strain extraction device for biologically treating polluted water and industrial sewage and purifying water by cultivating the extracted microbe bacteria strains.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the inserting piece of culture medium.    Frame (1)    Floating element (2)    Carrier (3)
NOVELTY - Invention is related to chemical industry and may be used to produce hydrogen-methane mixture used for production of hydrogen, alcohols, ammonia, dimethyl ether, ethylene, for Fischer-Tropsch processes. Flow containing low alkanes, having from one to four atoms of carbon, mixed with water vapour and/or carbon dioxide, passed through heating heat exchanger, where it is heated up to temperature in the range of 650 degrees C-700 degrees C. Heated flow for conversion of low alkanes is passed via adiabatic reactor, filled with catalyst packing. Conversion in adiabatic reactor is carried out until methane content is not more than 33%.    USE - Technological processes.    ADVANTAGE - Invention makes it possible to simplify hardware equipment of the process, to reduce heat inputs and to increase serviceability of catalyst. 11 cl
NOVELTY - Method of producing healthcare foods, marsh gas and fertilizer, involves washing kudzuvine root, processing starch and producing the product.    USE - The method is useful for producing healthcare foods, marsh gas and fertilizer (claimed).    ADVANTAGE - The process is configured with self-control operating system and production automatic operation monitoring system having high degree of mechanization. The method enables to use kudzuvine root as raw material instead of other energy resources for producing products, thus effectively saves energy resources and promotes sustainable development.
NOVELTY - The method involves venturi washing gasoloid flue gas, washing a primary spray tower and a secondary spray tower and processing the flue gas by using an electrostatic treater. The venturi washing is performed to directly wash the flue gas with fermented waste liquid. A hexagonal honeycomb-type anode high-voltage electric field with 250-600 mm homopolar distance is applied in an electrostatic treatment, and the electrostatic treater is made from conductive non-metallic composite materials.    USE - Industrial gasoloid flue-gas processing method for processing fermented waste-liquid gunite and granulation in monosodium glutamate industry.    ADVANTAGE - The method realizes resource utilization of the fermented waste liquid without pollution to achieve high profit. The method increases the processing efficiency of organic matters of the gasoloid flue gas to above 95 percent. The method enables processing fermented waste-liquid gunite with high efficiency at low energy consumption with simple operation.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of an industrial gasoloid flue-gas processing method.
NOVELTY - The gasifier has a hearth having a high-pressure sealing base cover at its upper end. The upper part of the hearth is a drying zone, the middle part is an oxidizing zone, and the lower part is a de-oxidizing zone. The lower end of the hearth has an ash-wood cleaning cartridge. The upper end of the cover has a material inlet. The upper cover of the material inlet has an inlet secure cover and a high-pressure sealing ring. A secure valve is installed on the secure cover. A wind duct is installed in the middle of the hearth.    USE - Flammable waste air-blasting dripping atomizing combined gasifier.    ADVANTAGE - Provides gasifier having novel structure, reasonable design, high efficiency, convenient use and reliable technical performance.    DETAILED DESCRIPTION - An end of the wind duct is connected to a firm high-temperature resistance nozzle. The outer part of the wind duct is connected to an oxygen-increasing machine adjusting switch. A fuel-gas separating chamber is provided in the lower side of the ash-wood cleaning cartridge, and is connected to the cleaning cartridge outside the stove body through pipe-line. A fuel-gas outlet is provided at the upper end of the cleaning cartridge.    DESCRIPTION OF DRAWING(S) - The drawing is a side cross-sectional view showing the flammable waste air-blasting dripping atomizing combined gasifier.
NOVELTY - Water-retaining organic and enzymatic active bacterial granular fertilizer, comprises (in %): enzymatically active bacteria (5-15), organic fertilizer (80-90) and water-retaining agent (3-5).    USE - The water-retaining organic and enzymatic active bacterial granular fertilizer is useful for providing drought tolerance, pest and disease damage resistance, and preventing continuous cropping resistance.    ADVANTAGE - The organic fertilizer rapidly absorbs irrigational water or rain water and maintains partial constant temperature for a long period of time. The organic fertilizer retains nutrient and improves the acidity and alkaline of soil, thus improves soil texture and increases soil fertility.
NOVELTY - The generator electrolyzes electric energy of preset value for generating hydrogen and oxygen. The muzzle brake is located at the end of vehicle motor, so that the crude oil mixed with air is heated at preset temperature. The vapor is generated by the heating process of crude oil mixed with air. The automatic control units such as air inlet modulator and end gas detection device are collocated to modulate and control the proportion of air and gas, to realize controlled combustion process.    USE - Generator for generating electric power using hydrogen and oxygen, for petrol/diesel vehicle.    ADVANTAGE - Since air inlet modulator and end gas detection device are collocated to modulate and control proportion of air and gas for combustion process, the vehicle control performance is improved. The fuel consumption and environmental pollution are reduced. The mass kinetic energy required by the motor is improved with reduced oil consumption.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the structure of generator for generating electric power using hydrogen and oxygen.
NOVELTY - This invention provides a method of two stages compost store and the application of the same. The method is characterized by that inoculate beneficial gertm prior to composting and re-inoculate microorganism once more under a proper temperature range while composting. By the second inoculation of microorganism during composting process, the method of this invention may improve compost maturity and increase nutrients composition in the compost, and at the same time, obtain a higher concentration product, And therefore it may apply to improve the effect of biological compost.
NOVELTY - The hydrogen lighter has a cell that supplies power of an electrolysis electrode. The upper ends of a hydrogen cabin and an oxygen cabin are connected to a pressure limiter through an air current elbow. The upper end of the pressure limiter is connected to a unit-directional air valve for outputting air. The unidirectional air valve is provided at one side. A silicon photocell board, connected to the cell, is provided at the outer layer of a machine shell.    USE - Hydrogen lighter.    ADVANTAGE - Uses clean and inexpensive fuel obtained from raw material.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of a hydrogen lighter.
NOVELTY - The method involves preparing a flat and heavily dried field block with fine drainage property into a ground bed with width of 0.4-1.2 m from south to north, and spraying 0.5 percentage of limewater on a bed surface for disinfection. Prepared straw is insulated for 3 days, and 0.05 percentage of mepartricin is added to 4-6 percentage of limewater to dip the straw in a pond for one night. The straw is taken out, and 10-60 percentage of disinfected soil and 20-80 percentages of animal manure are mixed with the straw. A fungus wall is built.    USE - Exposed wall-type method for planting coprinus comatus by using prepared straw and animal manure.    ADVANTAGE - The method can be implemented in simple and easy manner, and the raw materials required can be easily obtained, so that the mushroom can be planted in a better manner.
NOVELTY - Preparation of biodiesel using in-situ transesterification intensively and quickly with solvent, and using cosolvent to improve leaching speed of grease in oil material and quickening transesterification, comprises: (a) adding cosolvent, raw material containing grease, lower alcohol and catalyst based on certain ratio; (b) reacting and separating the solid and liquid; (c) distilling and recycling the lower alcohol and cosolvent in liquid-phase layer to obtain the biodiesel; and (d) recycling the lower alcohol and cosolvent in solid residue.    USE - The process is useful for preparing biodiesel (claimed).    ADVANTAGE - The process improves leaching speed of the grease, reduces resistance of mass transfer of the grease and lower alcohol, and quickens speed of the in-situ transesterification. Moreover, it saves refining processes of the grease; and the time for common in-situ transesterification is shortened to about ten minutes from several hours at normal temperature and under normal pressure.
NOVELTY - The device has a sealed case body connected with a flue gas inlet pipe, air inlet pipe, and a flue gas output pipe.    USE - Flue gas conversion device.    ADVANTAGE - The device exchanges recycled flue gas with air to produce combustible gas such as methane and ethylene.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a flue gas conversion device.
NOVELTY - An anaerobic reactor has middle gas collector at position connecting upper reaction chamber with lower reaction chamber of shell with lifting pipe and refluxing pipe. The lifting pipe lifts biogas produced in lower and upper reaction chambers, and sludge-water mixed solution to the gas liquor separator. The refluxing pipe refluxes sludge-water mixed solution in gas liquor separator to bottom of lower reaction chamber in which water distributor is mounted. An external circulator is installed outside the shell to pump sludge-water mixed solution in shell to gas liquor separator.    USE - Anaerobic reactor.    ADVANTAGE - Allows anaerobic reactor to have inner circulator and an external circulation in which circulation amount of sludge-water mixed solution is large and can be adjusted so that anaerobic reactor will have stronger capability of resisting impact load and buffering change of potential of hydrogen (pH) value. Allows removal of organic substances at high removal rate.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic of the anaerobic reactor.
NOVELTY - A wetland device is divided into three layers, namely first grade wetland, second grade wetland and third grade wetland. A honeycomb permeable cement plate in each layer of wetland, is provided with cobble stones, broken stones and yellow sand. Yellow calami and scirpus Tabernaemontana are planted on first and third grade wetlands while reed is planted on second grade wetland. A water flow channel is formed between first and second grade wetlands while water outlet channel is formed under the cement plate of the third grade wetland.    USE - Wetland device for treating cultivation waste water of pond.    ADVANTAGE - Enables to treat the cultivation waste water of the pond.    DESCRIPTION OF DRAWING(S) - The drawing illustrates the structure of the wetland device.
NOVELTY - A glass or steel made domestic sewage treatment tank has water inlet, water outlet and sewage outlet installed on upper part of cylindrical tank. A choke treatment device is installed on shifting board separating inner part to sedimentation basin. The sedimentation treatment tank and treatment tank are installed in the cylindrical tank. Front end of choke treatment device and sewage channels at two side walls are connected with sewage hole formed at the middle of the shifting board. A rubbish hole is formed under the choke treatment device.    USE - Domestic sewage treatment tank.    ADVANTAGE - Provides a domestic sewage treatment tank that is higher than the traditional sewage treatment tank. Provides a domestic sewage treatment tank that does not create blocking and pollution at time of treating of domestic waste. Enables organic suspended matter to be completely precipitated and thoroughly degraded.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic illustrating the internal structure of the domestic sewage treatment tank.
NOVELTY - A system for treating landscape water involves setting physical treatment system below one side ground (2) of landscape water (1) integrally, pumping liquid medicines in liquid medicine mixing device (5) of treatment system to pipe mixer through pipe by dosing pump, pumping landscape water to pipe mixer (4) through pipe by water pump (3), forming flocculating substance by making landscape water mixed with liquid medicines to enter and precipitate in high-efficient precipitator, and pumping out flocculating substance in high-efficient precipitator and treating centrally by sludge-draining pump.    USE - A system for treating landscape water.    ADVANTAGE - The system effectively removes pollutants such as organic substance, inorganic substance and bacteria.    DETAILED DESCRIPTION - A system for treating landscape water involves setting physical treatment system below one side ground (2) of landscape water (1) integrally, pumping liquid medicines in liquid medicine mixing device (5) of treatment system to pipe mixer through pipe by dosing pump, pumping landscape water to pipe mixer (4) through pipe by water pump (3), forming flocculating substance by making landscape water mixed with liquid medicines to enter and precipitate in high-efficient precipitator, setting filter at the back of high-efficient precipitator, setting sludge-draining pump under high-efficient precipitator, and pumping out flocculating substance in high-efficient precipitator and treating centrally by sludge-draining pump.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of system for treating landscape water.    Landscape water (1)    Ground (2)    Water pump (3)    Pipe mixer (4)    Liquid medicine mixing device (5)
NOVELTY - Forming a metal-polymer composite comprises: providing a thermally-cured dense polyaniline substrate; contacting the thermally-cured dense polyaniline substrate with an acid dopant to form a doped substrate; providing a solution comprising a metal ion; and contacting the solution comprising a metal ion with the doped substrate, where metal nanostructure deposits are formed on the doped substrate, and the deposits have a morphology which is dependent upon the acid dopant.    USE - The method is useful in surface enhanced Raman scattering applications. The composite materials is useful in surface processing catalysis e.g. fuel cells or other chemical reactions, as modified surface electrodes, for anticorrosion and biosensors.    ADVANTAGE - The method is inexpensive. The method provides good catalytic activity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) performing surface-enhanced Raman spectral analysis of an analyte comprising providing a thermally-cured dense polyaniline substrate, where a surface of the substrate comprises metal nanostructure deposits and an acid dopant, bringing an analyte into effective contact with the metal-polyaniline (PANI) composite, illuminating the metal-PANI composite with radiation of at least one wavelength for causing elemental-state particles to produce a plasmon field and for causing the plasmon field to interact with molecules of the analyte, in such a manner, so as to produce Raman photons; and collecting scattered radiation emitted from the metal-PANI composite for spectral analysis; and    (2) a metal-polymer composite comprising a thermally-cured dense polyaniline substrate, an acid dopant, and metal nanostructure deposits.
NOVELTY - A catalyst comprising alumina support and titanium dioxide and sodium and/or aluminum ions is new. The active sites of the catalyst forms a structure having overall surface area of 62 to 73 m2/g comprising titanium dioxide clusters (4.3-5.5 wt.%). The titanium dioxide clusters are enriched with aluminum ions and/or sodium ions with Al+3 to titanium dioxide weight ratio and Na+ to titanium dioxide of 2:1 each.    USE - For the synthesis of methanol and its derivatives (claimed).    ADVANTAGE - The new catalyst prevents recombination of charge carriers and can be used in the liquid phase of synthesis reactions, in particular the synthesis of methanol and its derivatives, advantageous due to its kinetics and high carbon dioxide conversions toward methanol, under economically viable industrial conditions. The catalyst enables management of carbon dioxide so as to lead to reduction of global greenhouse gas emission and coupling carbon dioxide and water to methanol.    DETAILED DESCRIPTION - A catalyst (C1) comprising alumina support and titanium dioxide and sodium and/or aluminum ions is new. The active sites of the catalyst forms a structure having overall surface area of 62 to 73 m2/g comprising titanium dioxide clusters (4.3-5.5 wt.%). The titanium dioxide clusters are enriched with aluminum ions and/or sodium ions with aluminum to titanium dioxide weight ratio and sodium to titanium dioxide of 2:1 each. The clusters are deposited onto a previously oxidized aluminum surface (preferably onto the internal aluminum surface of a tube reactor or onto alumina supports prepared during the process). An INDEPENDENT CLAIM is included for the synthesis of methanol and its derivatives, consisting in a reaction of carbon dioxide with water in presence of photocatalyst (C1).
NOVELTY - An improved process for oxidation of methane to 2C or more hydrocarbons, is disclosed. The process involves passing continuously a gaseous reactant mixture comprising methane and oxygen (or air) optionally with steam over an improved lithium-promoted magnesium oxide catalyst, in a fixed bed reactor at pressure of 1u50 atmosphere, at 500u1000?oC, methane/oxygen ratio in feed in the range of 15u100, and gas hourly space velocity of 500u300000 cm^3.g^-^1.hour^-^1, and separating the water, oxides of carbon, 2C or more hydrocarbons from the product stream. Image 0/0
NOVELTY - Method for generating methane from carbonaceous feedstock with simultaneous sequestration of carbon dioxide, comprises: anaerobically incubating a particulate alkaline earth metal salt in contact with a particulate and/or dissolved carbonaceous feedstock in neutral or alkaline aqueous culture medium containing a culture of methanogenic bacteria consortia; and collecting methane, where at least a portion of carbon dioxide produced during the incubation reacts with the alkaline earth metal salt to form alkaline earth metal carbonate, thus sequestering the carbon dioxide.    USE - The method is useful for generating methane from carbonaceous feedstock (including coal, tar sand, municipal waste, a leachate from a municipal waste, manure, bio-solids from waste water treatment and agricultural residues) with simultaneous sequestration of carbon dioxide (all claimed).    ADVANTAGE - The method provides five-times increase in methane production in the presence of alkaline earth silicates relative to the amount of methane produced in the absence of the silicates. The method provides methane with lower carbon dioxide content hence decreases the subsequent purification of the biological methane required to achieve a pipeline quality natural gas.
NOVELTY - A sulfoalkyl ether cyclodextrin (SAE-CD) composition comprises a sulfoalkyl ether cyclodextrin and a phosphate (less than 100 ppm), where the SAE-CD composition has an absorption of less than 0.2 A.U. due to a drug-degrading agent, as determined by UV/visible spectrophotometry at a wavelength of 245-270 nm for an aqueous solution containing 300 mg of the SAE-CD composition per ml of solution in a cell having a 1 cm path length.    USE - For preparing a product of sulfoalkyl ether cyclodextrin composition (claimed); to stabilize an active agent in an aqueous medium and to increase the solubility of an active agent in an aqueous medium; as analytical reagents, food and cosmetics adjuvants and/or additives, and as environmental clean-up agents in a pharmaceutical dosage form.    ADVANTAGE - The SAE-CD composition provides enhanced solubility and/or enhanced chemical, thermochemical, hydrolytic and/or photochemical stability of other ingredients in a composition.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing a sulfoalkyl ether cyclodextrin (SAE-CD) composition involves: (a) mixing in an aqueous medium a cyclodextrin with a sulfoalkylating agent in the presence of an alkalizing agent to form an aqueous reaction milieu comprising the SAE-CD, at least one unwanted components, and at least one drug-degrading impurities; (b) conducting at least one separations to remove at least one unwanted components from the aqueous milieu to form a partially purified aqueous solution comprising the SAE-CD and at least one drug-degrading impurities, where at least one separations include a process selected from ultrafiltration, diafiltration, centrifugation, extraction, solvent precipitation, and dialysis; and (c) treating the partially purified aqueous solution with a phosphate-free activated carbon at least two times to provide the SAE-CD composition comprising the SAE-CD and phosphate (less than 100 ppm).
NOVELTY - Controlling a reaction between a catalyst and a feedstock, comprises: contacting the catalyst with the feedstock to form a catalyst-feedstock mixture; applying radio frequency (RF) or microwave energy to at least one of the catalyst, feedstock, and catalyst-feedstock mixture, where RF or the microwave energy has a frequency, a power density, and a field strength; and controlling at least one of the frequency, the power density and/or field strength to increase the distribution of middle distillate products from the reaction.    USE - The method is useful for: controlling a reaction between a catalyst and a feedstock; and producing hydrocarbons as biofuels, which is useful in transportation and heating applications.    ADVANTAGE - The method exhibits increased production of hydrocarbons in 6-18C compared to methods in which the RF or microwave energy is not applied. The catalyst exhibits reduced coking as compared to methods in which the RF or microwave energy is not applied.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the production of hydrocarbons as biofuels, comprising: heating at least one of a plant oil and/or an animal oil to a temperature of at least 250 degrees C with conventional heating; contacting at least one of the plant oil and/or animal oil with a catalyst comprising an acid or a solid acid, to produce a catalyst-oil mixture; applying RF or microwave energy to at least one of the catalyst, plant oil, and/or animal oil, and the catalyst-oil mixture; and cracking at least one of the plant oil and/or animal oil to produce hydrocarbons as biofuels, where less than 10% (wt/wt) of the plant oil and/or animal oil is converted to a hydrocarbon off-gas.
NOVELTY - A screw conveyor (1) has an insertion opening (2) of organic waste at one end, and a discharge port (3) of carbonized material at other end. The throw-in organic waste is transferred from insertion opening to discharge port in an airtight state. The screw conveyor is heated over full length by blowing hot air from waste oil burner (4). Several dry distillation gas flutes (5) are arranged standingly in the route of the screw conveyor.    USE - Organic-waste carbonization apparatus. Uses included but are not limited to carbonization of organic-waste such as livestock dung e, cow dung, pig dung and hen dung, foodstuff residue, vegetables residue and fiber residue such as sawdust, coffee dregs and used tea leaves.    ADVANTAGE - The generation of offensive odor during carbonization process can be prevented, compactization of installation can be attained without vast installation space and the carbonized products can be utilized as moisture-content preparation agents, soil conditioner and deodorizing and odor adsorption agent. High thermal efficiency, energy consumption and excellent versatility of the apparatus can be obtained by simple structure.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of the organic-waste carbonization apparatus.    Screw conveyor (1)    Insertion opening (2)    Discharge port (3)    Waste oil burner (4)    Dry distillation gas flute (5)
NOVELTY - Catalytic material (I) comprises at least one metal-carbon compound or metal oxide-carbon compound.    USE - (I) is useful as electrodes in electric energy producing fuel cells (claimed).    ADVANTAGE - The fuel cells produced using (I), have a 10% higher efficiency than existing fuel cells. (I) provides large scale production of fuel cells. (I) enhances oxygen-reduction activity in the production of fuel cells. (I) can be prepared in a cost-effective manner.    DESCRIPTION OF DRAWING(S) - The figure shows a principle structure of an electrode from the catalytic material.
NOVELTY - Wash solution (I) comprising an aqueous solution of several amines, comprises: an absorber component (A) based on a tertiary amine or a mixture of several tertiary amines (30-60 wt.%); a first activator comprising monoalkylamines and/or dialkylamines (1-10 wt.%); a second activator comprising a piperazine compound or its derivatives with at least one free hydrogen atom at one of the two nitrogen atoms (0.01-10 wt.%); and the balance water, where the level of water is not higher than 60 wt.%, based on the total weight of (I).    USE - (I) is useful for removing carbon dioxide from biogas or sewage gas (claimed).    ADVANTAGE - (I) has a very good reaction speed and provides high washing performance. (I) achieves an effective separation of carbon dioxide at low temperature (20-30 degrees )C as compared to a washing solution based on N-methyldiethanolamine single component. (I) can be regenerated and has longer service life.
NOVELTY - A component comprises first metal layer (1), first metal oxide layer (4), second metal layer (2), second metal oxide layer (5), and base material. The oxidation potential of first metal layer differs from second metal layer.    USE - A component for catalytic reaction devices such as hydrogen supply response exposed to high temperature.    ADVANTAGE - The component can produce anodic oxidation material uniformly in non-uniform surface, prevents damage to oxide film, and improves adherence force of film.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a supporting catalyst;    (2) a catalyst body comprising platinum, nickel, rhodium, ruthenium and supporting catalyst; and    (3) a hydrogen supply system.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of substrate for supporting catalysts before anodic oxidation and after anodic oxidation.    First metal layer (1)    Second metal layer (2)    Laminated substrate (3)    First metal oxide layer (4)    Second metal oxide layer (5)
NOVELTY - A methane gas recovery method involves raw material liquid filling process in which sealable fermentation tank is filled with organic raw material liquid, fermentation process in which the organic raw material liquid is fermented in anaerobic conditions in the sealed fermentation tank, continuing fermentation while pressurizing the inside of the fermentation tank with the pressure of a biogas which contains methane gas and carbon dioxide produced by fermentation, adding an alkaline substance in order to neutralize the liquid and collecting gas from the air layer in the fermentation tank.    USE - Methane gas recovery method for energy conversion system (claimed) used in industrial waste, foodstuff factory, livestock farming waste material, organic refuse or sewage sludge.    ADVANTAGE - Carbon dioxide is dissolved in liquid layer to obtain biogas with high methane gas concentration.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for energy conversion system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of methane gas collecting system. (Drawing includes non-English language text).    Fermentation tank (1)    Raw material liquid supply line (2)    Alkaline substance supply line (3)    Gas recovery line (4)    Fermentation residue (5)
NOVELTY - A catalyst support substrate (10) has a projection portion (12) or a groove portion, and a catalyst supported to a surface of projection portion or groove portion. The catalyst support substrate is heated in an organic liquid containing hydrogen element, and catalyst degradation of the organic liquid is carried out to obtain hydrogen gas.    USE - Catalyst support substrate is used for hydrogen production apparatus (claimed).    ADVANTAGE - The catalyst support substrate has excellent hydrogen production efficiency. The hydrogen production apparatus formed using the catalyst support substrate has excellent lightweight property, and is compact.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for hydrogen production apparatus, which has a container in which organic liquid is accommodated, catalyst support substrate which is immersed in the organic liquid in the container and is maintained, and an unit to heat the catalyst support substrate.    DESCRIPTION OF DRAWING(S) - The drawings show the sectional view of the catalyst support substrate.    Catalyst support substrate (10)    Substrate (11)    Projection portion (12)    Nano carbon material (13)
NOVELTY - A hydrogen production method involves forming filled layers by filing ceramic type absorber which absorbs carbon dioxide generated by catalyst (201) for reformation into space partitioned off with louver (101) wall, carrying out reforming reaction and carbon dioxide absorption reaction repeatedly by turns, and carrying out cross flow of each filled layer through louver by hydrocarbon fuel.    USE - A hydrogen production method.    ADVANTAGE - The method obtains hydrogen with high yield and sufficient thermal efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of internal structure of water vapor reformer. (Drawing includes non-English language text).    Louver (101)    Partition (103)    Combustion gas exit header (110)    Catalyst (201)    Carbon dioxide absorber (301)
NOVELTY - The apparatus (1) has a cyclone (42) connected to cooling unit (3) that sprays water with respect to carbonized material (T) obtained by heating the organic waste in carbonization generation unit (2), through a piping (41). A powdered coal collection unit (4) sends the powdered coal (H) whirled upward with water vapor generated inside the cooling unit, to the cyclone, so that powdered coal is separated from the water vapor.    USE - Apparatus for manufacturing carbonized material using organic waste such as excrement and urine of livestock, etc.    ADVANTAGE - Efficient collection of powdered coal can be easily achieved, and occurrence of dew condensation inside the cyclone can be prevented, by providing heat insulating material and heater inside the cyclone. Maintenance operation due to clogging of piping can be reduced, without the need of reducing the collection capability of powdered coal by the cyclone.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the apparatus used for manufacturing carbonized material. (Drawing includes non-English language text)    Apparatus for manufacturing carbonized material (1)    Carbonization generation unit (2)    Cooling unit (3)    Powdered coal collection unit (4)    Piping (41)    Cyclone (42)    Powdered coal (H)    Carbonized material (T)
NOVELTY - A fat, oil and alcohol are transesterified in the presence of calcium-type catalyst to obtain reaction mixture. A chelating agent is added to the obtained reaction mixture, phase-separated the reaction mixture into light liquid and heavy liquid, and isolated to obtain fatty acid alkyl ester.    USE - Manufacture of fatty acid alkyl ester used as biodiesel fuel for internal combustion engine.    ADVANTAGE - The method economically provides fatty acid alkyl ester with high purity.
NOVELTY - A biomass fuel is obtained by adding wood-type waste material as moisture control agent to dechlorinated organic waste, and fermenting. The dechlorinated organic waste is obtained by removing chlorine and/or chloride compound in high-moisture content organic waste containing livestock excretion and/or foodstuff waste material. The content of wood-type waste material is 10-70 %mass with respect to total biomass fuel. The biomass fluid has chlorine concentration of 4000 ppm or less and moisture content of 40% or less.    USE - Biomass fuel is used as fertilizer.    ADVANTAGE - The biomass fuel has excellent combustion efficiency, and is economical and environmental friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of biomass fuel, which involves preparing dechlorinated organic waste by dehydrating high-moisture content organic waste and removing chlorine and/or chloride compound, adding wood-type waste material to the obtained dechlorinated organic waste, and fermenting.
NOVELTY - Producing biodiesel from plants or animal fats and oils, used fats and oils or fat-separator fats and oils, comprises: (a) hydrolytically cleaving fats and/or oils to obtain alcohol (glycerol) and free fatty acids; (b) separating the free fatty acids from the mixture (separation of the glycerol phase); (c) fractionating the free fatty acids producing different fractions of fatty acids depending on the boiling point of the fatty acids; and (d) esterifying the fraction or a mixture of the fraction of step (c) with carbon 1-5 alkyl alcohols, preferably methanol, ethanol, propanol or isopropanol.    USE - The biodiesel is useful as a fuel in diesel engines.    ADVANTAGE - In the method, wide range of raw materials can be used for the production of standardized biodiesel. Also the process offers the possibility to use even contaminated fats and oils, e.g. specified risk material. The process is economically better because of the use of low cost raw materials. The process allows the production of a tailor made methyl or ethyl ester, which are adjusted according to the required winter stability.
NOVELTY - A high calorific value solid fuel producing device has a fat/oil storage tank (10), a hydrocarbon compound storage hopper (20) for storing a lower organic hydrocarbon compound, a burner (11) for heating fat or oil and producing liquid, a water-in-oil evaporative dryer (30), a molding device (40) and a malodorous gas separator (50). The dryer receives the fat or oil and the hydrocarbon compound from the hopper (20) and tank (10), and dries water fraction contained in the hydrocarbon compound to produce an organic hydrocarbon compound substituted with fat or oil.    USE - Device is used for producing high calorific value solid fuel.    DETAILED DESCRIPTION - A high calorific value solid fuel producing device has a fat/oil storage tank for storing animal or vegetable fat or oil, a hydrocarbon compound storage hopper for storing a lower organic hydrocarbon compound, a burner for heating the fat or oil stored in tank and producing liquid, a water-in-oil evaporative dryer, a molding device and a malodorous gas separator. The dryer receives the fat or oil and the hydrocarbon compound from the hopper and tank, and dries water fraction contained in the hydrocarbon compound to produce an organic hydrocarbon compound substituted with fat or oil. The molding device molds and supplies organic hydrocarbon compound substituted with fat or oil, in a predetermined form. The separator (50) carries out separation of malodorous gaseous substances, fat or oil droplets and evaporated water vapor.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of high calorific value solid fuel producing device.    Fat/oil storage tank (10)    Burner (11)    Hydrocarbon compound storage hopper (20)    Water-in-oil-evaporative dryer (30)    Molding device (40)    Malodorous gas separator (50)
NOVELTY - The screw conveyor (16) that receives raw material from a volumetric feeder (17) has a trough (14) with the inner and outer cylinders (14a,14b) and screws (15). The screw is provided with intermediate portion that is wider than the entrance and exit sides. The screw conveyor is provided with a squeezing portion (31), an evaporation portion (32), a solidification portion (33) and a molding portion (18) for compressing, drying, compressing and solidifying, and cutting the raw material respectively.    USE - Apparatus for manufacturing biomass fuel by drying waste culture medium used in mushroom cultivation.    ADVANTAGE - The raw material is compressed, dried and solidified by passing the raw material through the screw conveyor. The structure of the apparatus is simple and the size reduction of the apparatus is achieved. The manufacturing cost of the apparatus is reduced. The biomass fuel with improved quality is obtained by performing sterilization treatment of the culture medium.    DETAILED DESCRIPTION - A raw material adjusting device mixes the waste culture medium with the deodorizer and adjusts the content of the raw material. The raw material from the raw material adjusting device is supplied by the volumetric feeder to the screw conveyor from a hopper. An introducing portion is provided for introducing the thermal medium between the cylinders, and an evacuation unit is provided for evacuating the inside of the inner cylinder of the screw conveyor.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of the biomass fuel manufacturing apparatus.    Trough (14)    Inner cylinder (14a)    Outer cylinder (14b)    Screw (15)    Screw conveyor (16)    Volumetric feeder (17)    Molding portion (18)    Squeezing portion (31)    Evaporation portion (32)    Solidification portion (33)
NOVELTY - Methane gas generator comprises aqueous solution containing a nutrient (2), coliform group (3) cultured in the aqueous solution containing a nutrient, and component containing cellulose (4) which is decomposed by coliform group and produces methane gas (7).    USE - The generator is useful for producing methane which is useful as a fuel.    ADVANTAGE - The methane gas can be generated easily without emitting carbon dioxide.    DESCRIPTION OF DRAWING(S) - The drawing shows the model of methane gas generator.    Aqueous solution containing a nutrient (2)    Coliform group (3)    Component containing cellulose (4)    Methane gas collection container (6)    Methane gas (7)
NOVELTY - Method for producing a fermentation end-product, involves contacting a carbonaceous biomass with (i) a microorganism that hydrolyzes and ferments the biomass, and (ii) an external source of one or more enzymes that are capable of enhancing the hydrolysis; and allowing sufficient time for the hydrolysis and fermentation to produce a fermentation end-product. The one or more enzymes comprise cellulase, and the cellulase and the microorganism act synergistically to enhance hydrolysis.    USE - The method is useful for producing fermentation end-product chosen from alcohol, ethanol, lactic acid, acetic acid and formic acid (claimed), which is useful as e.g. biofuel, chemical additive, processing aid and food additive. Can also be used for producing other fermentation end-product e.g. succinic acid, pyruvic acid, fucoidan, iodine, chlorophyll, carotenoid, calcium, hydrogen, magnesium, iron, sodium, potassium and phosphate.    ADVANTAGE - The method enables efficient hydrolysis and fermentation of biomass containing cellulose and hemicellulase using low concentration of enzyme having enhanced hydrolysis activity, and inexpensive production of fermentation end-products.    DETAILED DESCRIPTION - Method for producing a fermentation end-product, involves contacting a carbonaceous biomass with (i) a microorganism that hydrolyzes and ferments the biomass, and (ii) an external source of one or more enzymes that are capable of enhancing the hydrolysis; and allowing sufficient time for the hydrolysis and fermentation to produce a fermentation end-product. The one or more enzymes do not include xylanase, hemicellulase, glucanase or glucosidase and the external source is not the microorganism. The one or more enzymes comprise cellulase, and the cellulase and the microorganism act synergistically to enhance hydrolysis.
NOVELTY - Preparation of slurry feed involves pyrolyzing biomass to form biomass pyrolysis oil and biomass char, and mixing biomass pyrolysis oil and biomass char with solid carbonaceous particles.    USE - Process for preparing slurry feed, i.e. complex plastic slurry, for gasification to synthesis gas (claimed) which is used for preparing liquid transportation fuels such as gasoline, road diesel, aviation turbine fuel and lubricants.    ADVANTAGE - The process enables biomass to be fed into gasifier using existing types of feed transfer and feed injection equipment without encountering delivery problems commonly associated with handling solid biomaterials.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for cogasification of solid carbonaceous particles and biomass by preparing slurry feed (i.e. complex plastic slurry of pumpable viscosity), pumping the slurry into mixing zone of gasifier where it is mixed with oxygen-containing gas, passing the mixture of slurry and oxygen-containing gas through a feed injector into a gasifier reactor, and gasifying the mixture to form synthesis gas.
NOVELTY - Producing a fermentation product from a lignocellulose-containing material, comprises: combining lignocellulose-containing material and distillers dried grains with solubles (DDG/S); pre-treating the combined lignocellulose-containing material and DDG/S; exposing the pre-treated combined lignocellulose-containing material and DDG/S to hydrolyzing enzymes; and fermenting with a fermenting organism.    USE - The method is useful to produce fermentation products e.g. renewable fuels and chemicals.    ADVANTAGE - The method: enhances enzymatic hydrolysis of a lignocellulose-containing material; reduces the cost of subsequent enzymatic hydrolysis and fermentation processes; reduces the detrimental effects e.g. adverse affect on enzyme performance, yeast growth and fermentative capacity; and provides high sugar (fermentation product) yield by inhibiting the detrimental effects.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a method for enhancing enzymatic hydrolysis of a lignocellulose-containing material, comprising: introducing an effective lignin-blocking amount of DDG/S to the lignocellulose containing material prior to pre-treatment, and exposing the pre-treated lignocellulose-containing material and DDG/S to hydrolyzing enzymes;    (2) a method of reducing the detrimental effect of lignin on hydrolysis of lignocellulose containing material comprising adding DDG/S to the lignocellulose-containing material prior to pre-treating the lignocellulose-containing material; and    (3) a fermentation product made by the method of producing fermentation product.
NOVELTY - Preparing a bio-oil from lignocellulosic matter, comprises: (a) solvating hemicellulose from the lignocellulosic matter using a solvent; (b) removing solvated hemicellulose from solid matter remaining after step (a); and (c) solvating lignin and cellulose from the solid matter remaining after step (a) using a solvent to form the bio-oil.    USE - The method is useful to prepare bio-oil product, which is useful as biofuel, or biofuel additive.    ADVANTAGE - The bio-oil product is stable. The method does not require saccharification and fermentation steps.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the bio-oil from a material comprising lignin and cellulose, comprises treating the material with an aqueous alcohol at a reaction temperature of 180-350 degrees C and a reaction pressure of 8-26 MPa to form the bio-oil.
NOVELTY - The process comprises crushing the whole fruit in a crusher (1) to create a paste, conveying the ground material using a worm (2) in which the hot oil is injected to cause extraction and dilution, conveying the paste in a centrifugal separator (4) for separating the liquid (oil) and solids (cake) by a pump (3), deriving a fraction of oil towards the heater and then injecting it in the mixer, centrifuging the other fraction of oil present in the separator, and recovering solids, which is used as green manure, from the separator.    USE - The process is useful for producing biodiesel and an ecological fertilizer from jatropha curcas, where the biodisel is useful for operating a self-powered generator for the production of electrical energy (claimed).    ADVANTAGE - The process is capable of economically and energy efficiently producing biodiesel and an ecological fertilizer from jatropha curcas in an environmental friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for producing biodiesel and an ecological fertilizer from jatropha curcas.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a device for producing biodiesel and an ecological fertilizer from jatropha curcas.    Crusher (1)    Worm (2)    Pump (3)    Centrifugal separator (4)    Self-powered generator. (7)
NOVELTY - An alkali secondary battery consists of positive electrode (3), negative electrode (4) containing hydrogen storage alloy (14) and alkali electrolyte solution. The hydrogen storage alloy has composition comprising rare earth metal, magnesium, nickel and zinc.    USE - Alkali secondary battery e.g. nickel hydride secondary battery.    ADVANTAGE - The alkali secondary battery with high capacitance is provided by using the hydrogen storage alloy having high hydrogen storage capacity at room temperature. The hydrogen storage alloy has excellent corrosion resistance. The battery has improved oxidation resistance, cycle characteristics and discharge characteristics.    DETAILED DESCRIPTION - An alkali secondary battery consists of positive electrode, negative electrode containing hydrogen storage alloy and alkali electrolyte solution. The hydrogen storage alloy has composition of formula: M1-bMgbNic-d-eZndTe, where M is lanthanum, cerium, praseodymium, neodymium, promethium, samarium, europium, gadolinium, terbium, dysprosium, holmium, erbium, thulium, ytterbium, lutetium, calcium, strontium, scandium, yttrium, titanium, zirconium and/or hafnium, T is element chosen from aluminum, vanadium, niobium, tantalum, chromium, molybdenum, manganese, iron, cobalt, gallium, tin, indium, copper, silicon, phosphorus and/or boron, b is 0.05-0.15, c is 2.8-4.0, d is 0.1-1.0 and e is 0-0.25. The alloy contains 2 or more types of elements containing samarium, preferably lanthanum and cerium containing samarium.    DESCRIPTION OF DRAWING(S) - The drawing shows the partial notch perspective view of nickel hydride secondary battery.    Electrode group (2)    Positive electrode (3)    Negative electrode (4)    Hydrogen storage alloy (14)    Binder (16)
NOVELTY - A mixed paste containing mixture comprising complex oxide and oxide having ionic conductivity, is produced and the mixed paste is provided on electrolyte layer surface in a laminate form to obtain a laminated material. The laminated material is baked to obtain a sintered compact and the sintered compact is reduced to obtain hydrogen electrode.    USE - Manufacture of hydrogen electrode for electrochemical cell e.g. solid oxide fuel cell and high temperature steam electrolysis cell.    ADVANTAGE - The hydrogen electrode having high activity and stability is manufactured economically. The hydrogen electrode provides electrochemical cell having excellent durability and output characteristics.    DESCRIPTION OF DRAWING(S) - The drawing shows the flowchart of the manufacture of the hydrogen electrode. (Drawing includes non-English language text)
NOVELTY - A reaction apparatus comprises reaction apparatus main body (30) which has reaction part that reacts reaction material react and produces product, board (80) arranged in one end side of reaction apparatus main body which supports reaction apparatus main body, connection part arranged at part(s) of area corresponding to board top which connects one end part and board of reaction apparatus main body, and heating part (11) which heats connection part.    USE - A reaction apparatus for electronic device (claimed) e.g. portable electronic devices e.g. notebook-type personal computer, personal digital assistant (PDA), electronic notebook, digital camera, mobile telephone, wristwatch, game machine device, resistor and projector.    ADVANTAGE - The production amount of product produced in reaction part and temperature of reaction part are stabilized.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an electronic device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of the board and container of reaction apparatus.    Vaporization part (3)    Container (10)    Heating part (11)    Reaction apparatus main body (30)    Board (80)
NOVELTY - A fuel formation of water containing organic waste involves making dechlorinated organic waster by removing chlorine and chloride compounds contained in water containing organic waste in slurry or washing process water containing water containing organic waste and dehydrating, adjusting moisture content of dechlorinated organic waste to less than or equal to 85% by drying or heat drying and moisture content adjustment material, and fermenting dechlorinated organic waste with adjusted moisture content in which chlorine concentration becomes less than or equal to 4000 ppm and moisture content is less than or equal to 35 mass%.    USE - Fuel formation of water containing organic waste for biomass fuel (claimed).    ADVANTAGE - The method forms dry dechlorinated organic waste with high combustion efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a biomass fuel comprising fermented dechlorinated organic waste in which chlorine concentration is less than or equal to 4000 ppm and moisture content is less than or equal to 35 mass%.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the demineralization/fuel formation installation used for fuel formation of water-containing organic waste. (Drawing includes non-English language text).    Discharge source (1)    Demineralization installation (2)    Fuel formation installation (3)    Primary tank (11)    Primary solid-liquid separation device (12)
NOVELTY - Waste biomass reusing includes depositing waste and transferring it to a covered place, where the waste is kept in cells. The processing machines are equipped with aeration accessory in which the waste is sprayed. The waste is extracted, composted and aerated by successive cycles until it reaches a temperature of 30-75 degrees C. The waste is finally collected in the form of pellets.    USE - Method for reusing waste biomass for use in producing energy, burning in industrial boilers and supplying fuel for central heating.
NOVELTY - The system has an electromagnetic valve (10) placed in a microcomputer control acquisition device (III). An air inlet (A) of an animal respiratory apparatus (I) is connected to a head end of the electromagnetic valve. A microcomputer (16) in the microcomputer control acquisition device is connected with the electromagnetic valve and another electromagnetic valve (9). The microcomputer acquires and stores electric signals output by a carbon dioxide sensor (11), a methane sensor (12) and an oxygen sensor (13) in an air analyzer group (II).    USE - Multifunctional respiratory metabolism analytical system for an animal such as mouse, rabbit, dog and primate. Can also be used for analyzing respiratory metabolism of a human being.    ADVANTAGE - The system is multifunctional to perform mobile respiratory calorimetric method in different requirements for the animal having weight of 10 to1000 kg. The system analyzes converted quantity of air in the animal respiratory chamber by using an analyzer and acquires converted quantity of air according to time sequence. The system has high precision, stability and repetition function in the test of oxygen, carbon dioxide and methane.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a multifunctional respiratory metabolism analytical system.'(Drawing includes non-English language text)'    Animal respiratory apparatus (I)    Air analyzer group (II)    Microcomputer control acquisition device (III)    Air inlet (A)    Animal respiratory apparatus loose joints (7, 8)    Electromagnetic valves (9, 10)    Carbon dioxide sensor (11)    Methane sensor (12)    Oxygen sensor (13)    Microcomputer (16)
NOVELTY - Treatment of sludge resource comprises: (a) uniformly mixing crushed and dried plant waste produced in industrial and agricultural productions and sludge cake having water content of 80-85% to make the water content of the mixture be equal to less than 55-60%; (b) heating the mixture until the water content of the mixture is 20-25%; (c) producing fuel particles by a granulator; and (d) supplying heat to dry by the fuel particle.    USE - The process is useful for treating sludge resource (claimed).    ADVANTAGE - In the process, by mixing the sludge cake and the plant waste with low water content produced in industrial and agricultural productions, the mixture has quicker dehydrating speed than that of the pure sludge cake in a drier; and the drying temperature is low and the heat consumption is less.
NOVELTY - Method for removing methane in environment, involves adding soil sample of coal mine or refuse landfill into NMS culture medium and culturing in a sealing bottle, replacing with methane for every 24-72 hours in the sealing bottle, inoculating the culture solution into new NMS culture medium every 8-12 days, repeating the process for several times and obtaining methane oxidizing bacteria, and culturing the methane oxidizing bacteria in the environment containing methane to remove methane in environment.    USE - The method is useful for removing methane in environment, preferably from coal mine and refuse landfill (claimed).    ADVANTAGE - The method removes methane by a simple process.    DETAILED DESCRIPTION - Method for removing methane in environment, involves (a) collecting soil sample of coal mine or refuse landfill, (b) adding the soil sample into NMS culture medium and culturing in a sealing bottle, where initially in the sealing bottle, the ratio of NMS culture medium to methane to air is 5-30:5-40:30-80, replacing with methane for every 24-72 hours in the sealing bottle, such that the volume ratio of NMS culture medium to methane to air in the sealing bottle is 5-30:5-40:30-80, (c) inoculating the culture solution in new NMS culture medium every 8-12 days, where the volume ratio of the culture solution in step (b) to the NMS culture medium is 5-15:95-85, repeating the process for several times and obtaining methane oxidizing bacteria, and (d) culturing the methane oxidizing bacteria in the environment containing methane to remove methane in environment.
NOVELTY - A dephosphorizing denitrifying marsh filling comprises cement, lime stones, polyferric sulfate grains, polyacrylic resin, water and water glass. The ratio of cement/lime stones/polyferric sulfate grains is 1:3-10:0.02-0.07. The adding amount of the polyacrylic resin is 0.01-0.05 wt.%.    USE - Dephosphorizing denitrifying marsh filling.    ADVANTAGE - The method provides a high-efficiency inexpensive dephosphorizing denitrifying marsh filling.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of dephosphorizing denitrifying marsh filling including mixing cement, lime stones and polyferric sulfate grains and adding clean water to blend to form slurry; adding polyacrylic resin grains into the slurry and blending uniformly; pouring the slurry into a mold; and spraying water glass on surface of the product inside the mold to fast coagulate.
NOVELTY - The device has an air inlet tube (12) installed in middle of an internal part of a furnace (1). An annular flow guide cap (3) is installed at an outer side of a middle part of the furnace. The flow guide cap and the periphery of the middle part of the furnace are averagely equipped with multiple air outlets (4). An annular filter net (2) is assembled at an internal side of each air outlet, and a flow guide room (13) is formed between the flow guide cap and the furnace. A periphery of a lower part of the air inlet tube is equipped with multiple air inlets.    USE - Device for preparing combustible gas through gasifying biomass. Uses include but are not limited to boiler, industry, generation field, heating field and civil area    ADVANTAGE - The device has simple operation, and can produce gas continuously with high purity and yield and less tar oil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing gas through gasifying biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a combustible gas preparing device.    Furnace (1)    Annular filter net (2)    Annular flow guide cap (3)    Air outlets (4)    Air inlet tube (12)    Flow guide room (13)
NOVELTY - The device has a reducing motor (1) contacted rotationally with a transmission shaft (4) through a coupling band (3). A pressure adjusting bush (8) is fixed on a material pressing blade rotating shaft (7) through a screw thread and a fastening screw. A lower part of the rotating shaft is equipped with a pressure floating bush (10). A material pressing spring (9) is installed on the pressure floating bush. A sleeve connection block (12) is fixed on the rotating shaft through a key and nuts. A material pressing blade (13) is fixed on the sleeve connection block through a post rod (11).    USE - Constant-pressure material densification device for a biomass fixed bed gasification furnace.    ADVANTAGE - The device provides required compactness of the material according to demands of the gasification process for different piling density material. The device avoids burning of the material layer and prevents the furnace from being blasted, thus guaranteeing the safe and stable operation of the gasification furnace. The device has wide adaptability to raw materials.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a constant-pressure material densification device in partial section.    Reducing motor (1)    Coupling band (3)    Transmission shaft (4)    Material pressing blade rotating shaft (7)    Pressure adjusting bush (8)    Material pressing spring (9)    Pressure floating bush (10)    Post rod (11)    Sleeve connection block (12)    Material pressing blade (13)
NOVELTY - The device has tapered ash storing chamber (9), a crank rocker type multilink baffle plate ash storing door (8), a V-shaped feeding hole (7) and a sealed spiral high-temperature resistant conveyer (4) installed at lower part of an inner wall (9-1) of a gasification furnace. A super-ordination switch (9-5) and a lower-ordination switch (9-4) of a photoelectric type ash level controller are respectively set at upper and lower parts of a side of the chamber. Upper and lower photoelectric reflection plates (9-3) are respectively installed at upper and lower parts of another side of the chamber.    USE - Compression sealing type full-automatic spiral ash discharging device for a biomass fixed bed gasification furnace.    ADVANTAGE - The device enables the biomass fixed bed gasification furnace to continuously work, and guarantees that pressure in the furnace is stable and the furnace can securely operated. The device realizes discharging ash randomly according to amount of ash in the ash chamber during the running process of the furnace at high ash discharging speed, high automation and better environmental protection effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a compression sealing type full-automatic spiral ash discharging device.    Sealed spiral high-temperature resistant conveyer (4)    V-shaped feeding hole (7)    Crank rocker type multilink baffle plate ash storing door (8)    Tapered ash storing chamber (9)    Inner wall (9-1)    Upper and lower photoelectric reflection plates (9-3)    Lower-ordination switch (9-4)    Super-ordination switch (9-5)
NOVELTY - A fuel of natural-gas grade is economically produced by using compound fractional separation to refine marsh gas. The separation is capable of removing hydrogen sulfide in the marsh gas based on nano and micro-absorption material and combination optimizing configuration technique, is capable of removing carbon dioxide and residual hydrogen sulfide in the marsh gas by the multi-stage membrane separation technique, and is capable of removing water in the marsh gas.    USE - Method for producing fuel of natural-gas grade (claimed).    ADVANTAGE - The method is capable of clarifying, purifying, and deeply processing marsh gas to convert conventional marsh gas into refined marsh gas. The produced marsh gas has high caloric value and clean quality identical to that of natural gas.
NOVELTY - A straw particle fuel is produced by crushing crop straws to obtain cotton-shaped material by a crusher, mixing prepared cotton-shaped material and sawdust at a weight ratio of 8:2, transporting the mixture to a particle shaping machine, and extruding to obtain cylindrical particle material having a width of 5-10 mm and length of 10-20 mm long.    USE - Method of producing straw particle fuel (claimed).    ADVANTAGE - The method produces fuel having long burning time and small volume thus making transportation and storage of the material easy.
NOVELTY - A household waste fuel comprises raw materials from recycled and treated household waste, that is obtained from manufacturing household waste, and that can burn directly in regular condition.    USE - A household waste fuel.    ADVANTAGE - The fuel is safe, conserves energy, has low running cost, and requires only approximately 10% of investment as compared to using imported equipment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing of household waste fuel comprising subjecting recycled household waste to a first physical process of force dehydration by pressing and using hydraulic pressing machine, roller machine and centrifugal dehydration to reduce water content; and subjecting further to a secondary physical process of force dehydration by baking.
NOVELTY - The tank positioned under ground, has a bottom portion (6) whose height is higher at one end than at the other end. The bottom portion is provided with an open grid structure. The lower side of the bottom portion is provided with an air insulating layer (8) and the cooling water pipe and ventilation pipe arranged at equal interval on the air insulating layer.    USE - Organic matter fermentation tank.    ADVANTAGE - The circulating water adjusts the fermentation temperature and recycles the excess heat. The structure of the tank is simple. The cost of the tank is reduced. The absorbed heat can be used for supplying hot water to bathrooms.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the organic matter fermentation tank.    Bottom portion (6)    Air insulating layer (8)
NOVELTY - The method involves sending lean krypton-xenon liquid into an assistant air separation tower. Liquid oxygen is led to an upper part and a lower part of the assistant air separation tower to form air-liquid convection. The lean krypton-xenon liquid is preliminarily purified at bottom of the assistant air separation tower, and a lean krypton-xenon concentrate is obtained. The lean krypton-xenon concentrate is pressurized through a liquid oxygen pump. Volatile methane is removed from tower top, and a high-concentration krypton-xenon concentrate is obtained by a tower kettle.    USE - Rectifying method for removing methane in lean krypton-xenon liquid.    ADVANTAGE - The method enables providing high methane removing efficiency, precise control, safe operation and wide application, and can be implemented to obtain energy-saving effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a high-purity krypton-xenon extracting device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic illustration of a rectifying method for removing methane in lean krypton-xenon liquid. '(Drawing includes non-English language text)'
NOVELTY - The device has an Ethernet interface arranged on an industrial personal computer data processing and a displaying device i.e. industrial personal computer. Two peripheral component interconnect extended interface (PXI) bus interfaces are arranged on the simulation working condition processing device. The simulation working condition processing device controls a fuel cell power generation system and a loading control system according to downloaded working condition procedure.    USE - Device for testing simulation working condition of a fuel cell power generation system.    ADVANTAGE - The device is applicable for the state monitoring, the performance test, the reliability test or the service life test of the fuel cell power generation system with better real time performance. The device utilizes software that is developed and conveniently maintained, so that the test capability can be increased, and the cost of test and validation can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a simulation working condition testing device.'(Drawing includes non-English language text)'
NOVELTY - The device has a load output control unit provided with an interface that is connected with a high power non-inductive resistor. The interface of the load output control unit connected with a fuel cell generating power system is an input end of a direct current/direct current (DC/DC) converting circuit i.e. semi-bridge isolating type DC/DC converting circuit, in the load output control unit. An output power source of the fuel cell generating power system is loaded in a high power non-inductive resistor by the converting circuit.    USE - Load test device for a fuel cell generating power system.    ADVANTAGE - The device is simple in structure, inexpensive and better in adjustability.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a load test device.'(Drawing includes non-English language text)'
NOVELTY - The hydraulic pressure-type miasma septic tank has through holes (6), and buffer well (1) equipped in front part of first stage septic tank (9). The first stage septic tank and second stage septic tank (8) are internally equipped with discharge pipe (2) communicated to outside of tank. The top part of tank has sealed pyramid-shaped gas holder (3) and gas pipeline (4). The sewage draining port (5) of third stage septic tank is connected to the pipe net of urban sewage.    USE - Hydraulic pressure-type miasma septic tank.    ADVANTAGE - Provides simple structure, low investment, high-efficiency and high-quality organic fertilizer while obtaining marsh gas using the hydraulic pressure-type miasma septic tank. Controls the cleanliness and safety of the environment by killing various deleterious germina and parasitic ovum.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of the hydraulic pressure type miasma septic tank.    Buffer well (1)    Discharge pipe (2)    Sealed pyramid-shaped gas holder (3)    Gas pipeline (4)    Sewage draining port (5)    Through holes (6)    Second stage septic tank (8)    First stage septic tank (9)
NOVELTY - Methane tank comprises a fermentation tank (1) and a predecomposition tank (2) that is provided with a material liquid outlet (3); where the material liquid outlet (3) communicates with the fermentation tank (1).    USE - The methane tank is useful for producing methane.    ADVANTAGE - The fermentation tank (1) will not crust, the predecomposition tank (2) is installed above the fermentation tank (1) or around the fermentation tank (1) so as to keep and increase the temperature of the fermentation tank (1), and the methane tank can work normally at low temperature without additional heating device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the methane tank.    Fermentation tank (1)    Predecomposition tank (2)    Material liquid outlet (3)    Filtering devices (6, 7)
NOVELTY - The compost mat has a woven fabric provided with holes, where the woven fabric is made of polypropylene. Warp threads are made of high strength material such as ultra high molecular weight polyethylene, high-density polyethylene or aramid material. Warp threads have thickness ranging from 5-50 decitex. Weft threads have thickness ranging from 2.500-7.500 decitex.    USE - Compost mat for tunnel composting.    ADVANTAGE - The dirt falls through the holes, thus enabling the tunnel openings to be easily cleaned. The compost mat has high tensile strength. The woven fabric is made of low cost polypropylene, thus making the compost mat inexpensive. The air permeability of compostable material is improved. The mat reduces friction.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a compost mat and compostable material combination.    DESCRIPTION OF DRAWING(S) - The drawing shows a top view of a compost mat for tunnel composting.
NOVELTY - Briquettes production involves removing plants and organic waste from stomachs and intestines of ruminant animals and herbivores. The animal organs are collected in abattoirs and slaughterhouses, and transferred in frills or decanters. Solid waste in the organs is removed and deposited in bins, for draining the fluid from solid waste, to obtain a pre-dried solid waste. The pre-dried solid waste is dried in a dryer, by using air from fan and heat produced by boiler, to reduce moisture contents of the waste to 15-20%, to obtain a dried solid waste.    USE - Method for producing briquettes for use as wood in boilers to produce heat and/or steam for industries.    ADVANTAGE - The briquettes production method enables to produce briquettes having high calorific value, and is eco-friendly.    DETAILED DESCRIPTION - Briquettes production involves removing plants and organic waste from stomachs and intestines of ruminant animals and herbivores. The animal organs are collected in abattoirs and slaughterhouses, and transferred in frills or decanters. Solid waste in the organs is removed and deposited in bins, for draining the fluid from solid waste, to obtain a pre-dried solid waste. The pre-dried solid waste is dried in a dryer, by using air from fan and heat produced by boiler, to reduce moisture contents of the waste to 15-20%, to obtain a dried solid waste. The dried solid waste is transferred to a silo feeder machine briquetter, for performing briquetting. The briquetter compresses the waste by the mechanical force produced by piston driven by two wheels, and thus the briquetting is performed on the solid waste to obtain hot briquettes. The obtained hot briquettes are cooled and then packed in raffia bags of 600 kg of capacity, and finally stored.
NOVELTY - A microbiological fuel cell comprises an anode, a cathode, an electrode chamber and a reaction medium. The cathode is placed in the center of the electrode chamber. Both ends of the cathode are contacted with wall of the electrode chamber. The cathode divides the electrode chamber into anode and cathode reaction chambers. The anode is placed in the anode reaction chamber; and the cathode, anode and external circuit are connected via conducting wires.    USE - Microbiological fuel cell for use in treatment of soy sauce brewing wastewater and similar high-concentration organic wastewater.    ADVANTAGE - The fuel cell is reasonable in structure without the adoption of a proton exchange membrane, and is capable of improving coulomb efficiency and organic pollution removal ratio via the optimization and improvement in microorganism collection, microorganism domestication, and starting condition. In no need of any other external energy source, the fuel cell can design processing capability according to different requirements and be adapted to batch processing, continuous flow processing, and distributed processing.    DESCRIPTION OF DRAWING(S) - The drawing is a perspective view of a microbiological fuel cell with a cathode placed in the center.
NOVELTY - A continuous deodorization method of active sludge ferment gas comprises an exhaust fan, a washing tower, a distribution plate, a recycle pump, a shower pipe and a liquid removing net. The active sludge ferment gas is washed by medicine liquid, and the tower is emptied after the ferment smell is removed. Medicine liquid is used circularly by the pump. The washing medicine liquid is prepared by adding 3-5 kg sodium chlorite in 100 kg tap water, then adding a little sodium chlorite liquid until the pH value of the medicine liquid is 8.5-9.0, adding 0.3-0.5 kg activated zinc oxide, and stirring.    USE - A continuous deodorization method of an active sludge ferment gas (claimed).    ADVANTAGE - The method solves the problem that the active sludge ferment gas needs continuous deodorization; has simple apparatus, easy operation, continuous, fast, and clean deodorization of the active sludge ferment gas; and widely used in the deodorization of the active sludge ferment gas.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating an apparatus for continuous deodorization of active sludge ferment gas.
NOVELTY - A catalyst comprises ZSM molecular sieve, its modified components and binder. The modified components comprise lanthanide series metal oxides, alkali metal oxides and phosphorus oxides. The catalyst comprises (wt.%) ZSM molecular sieve (25-85), binder (15-75), lanthanide series metal oxides (0-10), alkali metal oxides (0.001-5) and phosphorus oxides (0.1-10).    USE - Catalyst for making propylene and ethane.    ADVANTAGE - The catalyst can improve the yield coefficients of the propylene and the ethane and at the same time largely reduce the yield coefficient of the by-product 1-3C alkane during the process of catalyzing the mixed 4C olefin to make the propylene and the ethane.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the application of the catalyst comprising filling the catalyst into a reactor. The water and the mixed 4C raw material are conveyed into the reactor for catalyzing to convert the catalyzing into the reaction for making the propylene and the ethane at 460-600 degrees C and 0.05-0.3 MPa. The weight ratio of water and the mixed 4C raw material is 0-1. The hourly space velocity of the mixed 4C olefin is 1-20 hours-1. The mixed 4C raw material is the mixed 4C fractions of the catalytic cracking device of an oil refinery or the steam cracking device of an ethylene plant.
NOVELTY - Invention refers to a consortium of microbial strains of Candida sp. fungi 616 and Rhodococcus AC-1258 (ver.16-a) bacteria for hydrocarbon removal from environmental objects.    USE - Medicine.    ADVANTAGE - Application of said consortium of bacterial strains improves efficiency of environmental removal. 4 ex
NOVELTY - The apparatus has a settling tank (3) for precipitating sludge from wastewater and an aeration basin (4) for aerating contaminated water from the settling tank. Several filter tubs are arranged in the tank, for filtering aerated water mixed with air. A separation wall (3-4) is formed in the tank and inclined at a predefined angle, for separating heavy precipitate and accommodating the precipitate in the lower portion of the wall. The circular-shaped biological filtration reaction baths (7,9) are arranged in parallel with respect to the aeration basin.    USE - Waste water filtration apparatus.    ADVANTAGE - The processing capability and energy saving effect of the filtration apparatus can be improved by using a simple arrangement.    DESCRIPTION OF DRAWING(S) - The drawing shows a structural view of the waste water filtration apparatus.    Settling tank (3)    Separation wall (3-4)    Aeration basin (4)    Aerobic bioreactor (5)    Biological filtration reaction baths (7,9)
NOVELTY - Fast conversion of livestock and poultry manure into high-efficiency fertilizer comprises hydrolyzing livestock and poultry manure under acidic condition to produce amino acid and obtain high-efficiency fertilizer. An acidic hydrolysis agent (5-8 pts.wt.) and treatment agent are added during hydrolysis. The treatment agent comprises (pts.wt.) dispersing agent (2-5), odor absorbent (2-5), adhesion agent (0.1-0.5), wrapping agent (1-3), pH adjusting agent (0.5-1) and filling agent (10-30).    USE - Method for fast conversion of livestock and poultry manure into high-efficiency fertilizer for crops (claimed).    ADVANTAGE - In the method, the ova and bacteria are completely killed. The fertilizer is beneficial to proliferation of microbes in soil; can avoid killing of beneficial microbes in soil, accumulation of salts and hardening of soil caused by abusing fertilizers; and is suitable for pollution-free ecological agricultural production and large scale industrial production.
NOVELTY - Bromine oxidation of methane is performed by recycling carbon monoxide and carbon dioxide to reactor during reaction. The carbon monoxide and carbon dioxide are side products generated in the reaction and/or added externally.    USE - Method for bromine oxidation of methane for preparing high hydrocarbon, methanol or dimethyl ether (claimed).    ADVANTAGE - The method has zero discharge of waste gas (carbon monoxide and carbon dioxide) without reducing yield of main product.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing high hydrocarbon, methanol or dimethyl ether, comprising reacting methane with oxygen and hydrogen bromide/water in the presence of catalyst to obtain bromomethane and dibromomethane; and reacting bromomethane with dibromomethane in the presence of catalyst to obtain hydrocarbon, in which carbon monoxide and carbon dioxide are recycled to primary reactor before or after the secondary reaction.
NOVELTY - Colloidal-printed carbon structure component has honeycomb structure. The colloidal-printed carbon structure component has meso-pores and/or macro-pores having uniform average diameter of 5-500 nm and Brunauer-Emmett-Teller surface area of 100-1500 m2/g.    USE - Colloidal-printed carbon structure component is used for manufacture of colloidal-printed carbon supported catalyst (claimed) used for fuel cell electrode.    ADVANTAGE - The colloidal-printed carbon supported catalyst formed using colloidal-printed carbon structure component has excellent activity and electroconductivity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of colloidal-printed carbon structure component; and    (2) manufacture of colloidal-printed carbon supported catalyst.
NOVELTY - Hydrogen and oxygen obtaining involves utilizing methane gas, which is obtained from biogas by aerobic process. The methane gas is introduced into a generator to produce electric energy. The electric energy is supplied into water to produce hydrogen and oxygen by electrolysis.    USE - Method for obtaining hydrogen and oxygen from water by electrolysis.    ADVANTAGE - The hydrogen and oxygen obtaining method is eco-friendly and provides hydrogen and oxygen with high purity.
NOVELTY - The kit has a case (900) for surrounding a fan (800) and made of transparent material, and an effluent storage tank (500) for storing effluent coming from a fuel cell portion. A display unit (700) indicates the electricity generated with a central control part (600) that controls a fuel pump (100) and an air pump (200). Fuel and air pump LED displays (101, 201) indicate flow of air-supply and fuel. A feeder tube is connected to the case, and supplies the fuel from the fuel pump. A motor operates a fan (800) by using the generated electricity.    USE - Educating kit for a fuel cell generating system.    ADVANTAGE - The kit enables a user to understand an electro production process of a fuel cell through a basic concept of a fuel cell generation system, thus improving the learning effect of the user. The kit enables the user to understand the fundamental concept of the electrical property of the fuel cell. The case is made of the transparent material, so that the circulation of air and fuel can be visually confirmed.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an education kit.'(Drawing includes non-English language text)'    Fuel pump (100)    Fuel pump LED display (101)    Air pump (200)    Air pump LED display (201)    Effluent storage tank (500)    Central control part (600)    Display unit (700)    Fan (800)    Case (900)
NOVELTY - A cell structure containing a gas flow path is formed of the expanded metal (28) positioned between cell configuration pieces. The front and rear surfaces of the expanded metal are discriminated using a handheld front and back determination unit provided near the outer periphery end of the expanded metal, the discrimination unit having a visual-observable and confirmable three-dimensional features such as marking, hole (28a), protrusion and corner chamfer (28b).    USE - Manufacturing method of fuel cell e.g. polymer electrolyte fuel cell.    ADVANTAGE - The front and rear surfaces of the expanded metal can be discriminated correctly and easily when laminating the cell configuration pieces, thus improving the manufacturing efficiency and reliability of the fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram explaining the manufacturing process of the fuel cell, and a top view of the expanded metal positioned between cell configuration pieces.    Expanded metal (28)    Hole (28a)    Corner chamfer (28b)    Flat raw material (42)    Roller (43)
NOVELTY - The heat exchanger (10) has heat exchanger tube having linear portions (22), circular-arc-shaped folding portions (24) and cylindrical connecting end portion (12) provided at ends. The heat exchanger tube has petal-shaped portion (18) that is separated by forming grooves (14) in outer surface of tube, and is positioned symmetrically with surroundings of shaft hole (16) formed in inside of the tube when tube is viewed along horizontal direction.    USE - Multitubular heat exchanger for carrying out cooling condensation of water vapor generated in fuel cell.    ADVANTAGE - The size reduction of the multitubular heat exchanger can be carried out easily and effectively, and the folding portion can be formed easily without crushing the heat exchanger tube.    DESCRIPTION OF DRAWING(S) - The drawing shows the partial side and sectional views of the multitubular heat exchanger.    Multitubular heat exchanger (10)    Connecting end portion (12)    Groove (14)    Shaft hole (16)    Petal-shaped portion (18)    Linear portion (22)    Folding portion (24)
NOVELTY - The device has a speed reduction motor (1) connected with a transmission shaft (4) through a coupling sleeve (3), where the shaft is connected with a material compacting blade rotary shaft (7) through a screw thread. An upper part of the rotary shaft is connected with a pressure regulation sleeve (8), and a lower part of the rotary shaft is fixed with a pressure floating bush (10). A sleeve connecting block (12) is placed on the rotary shaft through key and nuts. A material compacting blade (13) is placed on the sleeve connecting block through a post rod (11).    USE - Constant pressure material compacting device for a biomass fixed bed gasifier.    ADVANTAGE - The device ensures materials with different accumulation densities to reach required material compactness according to requirements of gasification technique, and avoids burning through material layer, coking caused by excess temperature and furnace explosion, thus providing safe and stable operation of a gasifier. The device can be applied to wide range of raw materials.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial sectional view of a constant pressure material compacting device.    Speed reduction motor (1)    Coupling sleeve (3)    Transmission shaft (4)    Material compacting blade rotary shaft (7)    Pressure regulation sleeve (8)    Material compacting spring (9)    Pressure floating bush (10)    Post rod (11)    Sleeve connecting block (12)    Material compacting blade (13)
NOVELTY - The furnace has an electric motor (10) mounted on an outer side of a furnace hearth (1), where the electric motor drives an upper furnace hearth (5) to rotate along a seal groove (7). A gap (16) is formed between inner wall of a lower furnace hearth (6) and a lower edge of the upper furnace hearth. An annular escape channel (15) is mounted between an outer wall of the upper furnace hearth and the inner wall of the lower furnace hearth. Air holes (12) are provided at middle lower part of the lower furnace hearth. An annular intake channel (9) is mounted on bottom part of the furnace hearth.    USE - Automatic fuel blanking biomass gasification furnace.    ADVANTAGE - The furnace realizes automatic blanking of fuel in the furnace hearth, is convenient and sanitary to operate, effectively prevents burning hole from appearing at the bottom part of the furnace hearth, and stably and uniformly produces gas.    DETAILED DESCRIPTION - The upper furnace hearth is in shape of a table with a small upper part and a big lower part.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of an automatic fuel blanking biomass gasification furnace.    Furnace hearth (1)    Upper furnace hearth (5)    Lower furnace hearth (6)    Seal groove (7)    Annular intake channel (9)    Electric motor (10)    Air holes (12)    Annular escape channel (15)    Gap (16)
NOVELTY - The furnace has a gasification barrel whose bottom part is equipped with a spiral ash discharge rod. An end of the spiral ash discharge rod is connected to a motor, where another end of the spiral ash discharge rod is extended to an ash discharge port. A side of an upper part of the barrel is equipped with a fuel gas outlet pipe, and another side of the barrel is equipped with a charging barrel. A lower part of the charging barrel is connected to a charging port of the barrel, and a position of the charging port of the barrel is equipped with an automatic charging device.    USE - Gasification furnace for producing high-temperature anaerobic combustible gas by gasifying biomass.    ADVANTAGE - The furnace has large gas production rate and long combustion time. The furnace is safe, protects environment, and is free from smoke and waste gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a gasification furnace.
NOVELTY - The device has a heating device body (5) whose lower part is equipped with a sealed lighting port. An ash discharging port is equipped below the lighting port, and points of internal furnace wall corresponding to the lighting port and the ash discharging port are equipped with an upper fire grate (5.1) and a lower fire grate (5.2). A double fire grate structure is provided between the upper and lower fire grates, and a heating device wall between the upper and lower fire grates is equipped with a gasification gas outlet (7) i.e. lower gas discharging structure.    USE - Biomass fuel gasification device.    ADVANTAGE - The device has simple structure, high gasification rate, continuous production, energy-saving property and environmental protection property, and is convenient for lighting and safe to utilize.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass fuel gasification device.    Feeding port (4)    Heating device body (5)    Upper fire grate (5.1)    Lower fire grate (5.2)    Gasification gas outlet (7)
NOVELTY - A precipitant is added to a mixed solution of a nickel compound and a magnesium compound, and co-precipitation of nickel and magnesium is carried out to obtain a deposit. The alumina powder, water or alumina sol is added and mixed with deposit to obtain a mixture. The mixture is dried and baked to obtain a catalyst.    USE - Manufacture of catalyst used for modification of tar-containing gas e.g. dry distillation gas discharged during carbonization of coal and dry-distillation of wood-type biomass and foodstuff waste material-type biomass, and coke oven gas discharged from coke oven (all claimed).    ADVANTAGE - The method enables manufacture of catalyst having high activity and excellent carbon precipitation resistance, stably.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for modifying tar-containing gas; and    (2) regeneration of catalyst, which involves contacting steam and/or air with catalyst, when catalyst carries out degradation by carbon decomposition and/or sulfur poisoning by implementation of modification of tar-containing gas, and regenerating catalyst.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view explaining the modification of the tar-containing gas.    Raw material hopper (5)    External heating rotary kiln (7)    Catalyst tower (8)    Water scrubber (9)    Oil bubbler (10)
NOVELTY - The system has a water intake pipe and a water discharge pipe provided with an electric butterfly valve and a manual butterfly valve. A water storage tank is provided with a submerged pump. A water exhaust pipe of the pump is connected with a top part of a water tank. A fuel gas connection pipeline is equipped with an electromagnetic valve (49) provided at a back side of an opening of a water seal explosion release device (47). A front end of a burner (55) is provided with a fuel gas wind allocation machine (56). A lower end of a raw material cabin (4) is equipped with a belt conveyer (5).    USE - Tobacco stalk waste gasification system.    ADVANTAGE - The system carries out continuous operation without secondary pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a tobacco stalk waste gasification system in partial section.    Raw material cabin (4)    Belt conveyer (5)    Water seal explosion release device (47)    Electromagnetic valve (49)    Burner (55)    Fuel gas wind allocation machine (56)
NOVELTY - The gasifier has a furnace disk (1) installed at an upper end of a furnace body (3). A charge hole (2) is formed at a center position of the furnace disk. An air distribution tube (5) is installed in a lower end of the furnace body. Multiple air distribution holes (6) are formed in the air distribution tube. An ash outlet (4) is installed in bottom of the furnace body. A smoke outlet (7) is installed in one side of the furnace body.    USE - Straw gasifier for use in a bungalow resident.    ADVANTAGE - The gasifier is simple in structure and reasonable in design. The gasifier has uniform air distribution, stable flame and better combustion quality, and is pollution-free, and reduces consumption of energy, thus reducing cost of the gasifier.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a straw gasifier.    Furnace disk (1)    Charge hole (2)    Furnace body (3)    Ash outlet (4)    Air distribution tube (5)    Air distribution holes (6)    Smoke outlet (7)
NOVELTY - The furnace has an upper cover provided with a cooking bench and a secondary air connecting pipe (16). An ash removing chamber is assembled below a grate and a sealing ash removing door is assembled. The ash removing chamber is externally connected to a primary air pipe (23) that is connected to a fan (22). A lower furnace body (4) and an upper furnace body (9) are fixedly integrally assembled and connected to a base (1). An upper cover plate (13) is provided with a furnace ring cover, where a gasification stove is assembled on the upper cover plate.    USE - Integrated furnace-stove biomass fuel gasification direct combustion furnace.    ADVANTAGE - The furnace is inexpensive and simple in structure, and the furnace is pollution emission-free.    DESCRIPTION OF DRAWING(S) - The drawing shows an integrated furnace-stove biomass fuel gasification direct combustion furnace.    Base (1)    Lower furnace body (4)    Upper furnace body (9)    Upper cover plate (13)    Secondary air connecting pipe (16)    Fan (22)    Primary air pipe (23)
NOVELTY - The device has a fuel gas output pipe and a waste gas exhaust valve provided at an upper part of a fuel barrel. The gas output pipe is connected with a gas inlet pipe at an upper part of a purifier. An air inlet pipe is connected with an air feeder i.e. 12 W dual-purpose fan. Waste liquid discharge pipe and a discharge valve are located at a lower part of the purifier. The purifier and the air feeder are fixed on a steel rack at a lower part of a device base. An infrared furnace head is fixed on surface of an upper part of the device base.    USE - Biomass gasification heating device.    ADVANTAGE - The furnace is simple in structure, convenient to use and inexpensive, and utilizes wide fuel source. The furnace is safe and environment friendly. The fan can be utilized during power cut.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a biomass gasification heating device.
NOVELTY - Device comprises at least one carbon nanotube in many layers of graphene, on which at least one molecule is grafted bearing a group G1 reacting with the chemical compound or a precursor of such a group G1.    USE - The device or a system is useful for detecting and optionally quantifying many gaseous chemical compounds, where the gaseous chemical compound is volatile organic compounds, hydrogen, carbon monooxide, carbon dioxide, chlorine and chlorine compounds, ammonia, organophosphorated gas, hydrocyanic acid, thionyl chloride, phosphine, tetrahydrofuran, methane and dimethyl methylphosphonate (all claimed).    ADVANTAGE - The device: is selective and very sensitive, even at room temperature; is simple to format and cost effective; and has large surface area, which can reach 1500 m2/g and thus ensures a high surface of interaction with the surrounding atmosphere. The carbon nanotubes have very high electrical conductivity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a system comprising at least two devices; and    (2) the preparation of the device to detect at least one chemical compound comprising laying at least one carbon nanotube in many graphene layers, on which at least one molecule is grafted bearing a group G1 for reacting with the chemical compound or precursor of such a group G1, on two electrodes, so that the carbon nanotube provides an electrical contact between the electrodes.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the device.    Support (1)    Electrodes (2)    Carbon nanotubes (3)    Means to monitor changes in the resistance of the nanotubes. (4)
NOVELTY - Use of superabsorbers for promoting root growth of plants, is claimed.    USE - The superabsorber is useful for promoting root growth of plants, for crop cultivation, Lawns, golf courses, vegetable cultivation, cotton plantations, reforestation, ornamental plant cultivation, and greenhouse cultures, or culture with cantilever substrates (claimed). The ability of the superabsorber to increase root growth of Terminalia superba Limba belonging to Myrtales was tested in clay type soil. The result showed that the superabsorber increased the root growth of the plant to 87%.    ADVANTAGE - The superabsorber increases the root growth of the plant after a short time, i.e. after one or two months, and is eco-friendly and cost-effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for promoting root growth of the plants, comprising growing the plant in the growth medium and adding the superabsorber to the growth medium.
NOVELTY - Use of superabsorbers for promoting aboveground growth of plants, is claimed.    USE - The superabsorber is useful for promoting above ground growth of plants, for crop cultivation, Lawns, golf courses, vegetable cultivation, cotton plantations, reforestation, ornamental plant cultivation, and greenhouse cultures, or culture with cantilever substrates (claimed). The ability of the superabsorber to increase aboveground growth of Terminalia superba Limba belonging to Myrtales was tested in clay type soil. The result showed that the superabsorber increased the root growth of the plant to 87%.    ADVANTAGE - The superabsorber increases the aboveground growth of the plant after a short time, i.e. after one or two months, and is eco-friendly and cost-effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for promoting aboveground growth of the plants, comprising growing the plant in the growth medium and adding the superabsorber to the growth medium.
NOVELTY - An environment-friendly refrigerant composition comprises propane (10-90 wt.%), and fluoroethane (10-90).    USE - An environment-friendly refrigerant composition (claimed) for replacing R22 refrigerant.    ADVANTAGE - The composition has low slippage temperature, and is compatible with pipes and parts of existing R22 system. When used as replacement to R22 system, it has high refrigerating effect and good energy-saving effect. It does not damage ozone layer and has low latent energy of greenhouse effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing the environment-friendly refrigerant composition comprising mixing propane and fluoroethane in liquid phase state.
NOVELTY - Inoculation and domestication launching method of microorganism fuel cell to energize organic wastewater, comprises adding microorganism nutrient fluid in anode chamber and inoculating the mixed culture fluid as launching anode fluid; processing multiple changes to switch anode fluid into microorganism nutrient fluid, where battery steadily outputs stable voltage to accomplish enrichment of electricity generation; and increasing switch to replace anode fluid with mixed fluid of microorganism nutrient fluid and organic wastewater to be processed, thus domesticating the electricity generation.    USE - Inoculation and domestication launching method of microorganism fuel cell to energize organic wastewater, particularly domestic sewage (claimed).    ADVANTAGE - The method recycles the chemical power from organic contamination in the form of electric power, is strongly operable, has gradual progress in the domestication process, and has stable performance.    DETAILED DESCRIPTION - Inoculation and domestication launching method of microorganism fuel cell to energize organic wastewater, comprises:    (A) adding microorganism nutrient fluid in anode chamber and inoculating the mixed culture fluid as launching anode fluid, while cathode chamber employs sodium nitrate fluid as cathode fluid;    (B) processing multiple changes to switch anode fluid into microorganism nutrient fluid, where after multiple electricity generation cycle, the battery steadily outputs stable voltage to accomplish the enrichment of electricity generation in the anode chamber; and    (C) then processing multiple changes and increasing switch to replace the anode fluid with the mixed fluid of microorganism nutrient fluid and organic wastewater to be processed, thus domesticating the electricity generation, till the nutrient fluid is fully replaced by organic wastewater to be processed to be the anode fluid and the stable voltage is steadily output to accomplish the domestication launching.
NOVELTY - Methane generating device is formed by using an automatically discharging system, heat generating system and automatically methane storing system. The heat generating system generates heat from solar energy which controls and preserves temperature. Sediment is formed due to gas exceeding in a gas storage tank.    USE - Methane generating device.    ADVANTAGE - The methane generating device provides high-temperature effectively, and is automatically controlled, and enables to generate methane for long duration.
NOVELTY - Method of producing biogas by anaerobic co-fermentation of Enteromorpha and other biomasses, involves pretreating Enteromorpha at 30 degrees C or less for 48 hours or more, mixing the pretreated Enteromorpha with other biomasses to obtain mixture, performing fermentation in an anaerobic fermenting device to obtain biogas, where the mixture contains 30-70 vol.% of Enteromorpha.    USE - The method is useful for producing biogas (claimed).    ADVANTAGE - The method enables to obtain biogas simply, easily, conveniently, rapidly and cost-effectively. The biogas can be obtained in large quantities.
NOVELTY - The boiler has a secondary wind port provided on an upper part of a wind distributing plate. Secondary wind ports lean to lateral and lower sides of a secondary wind inlet direction. A primary wind port includes straight wind ports on a lower part of the wind distributing plate. Oblique wind ports are provided in middle of the distributing plate. Projection of the straight wind ports is provided on plane in central axis of a combustion chamber. Shape and arrangement of the oblique wind port are same as the secondary wind port.    USE - Biomass vaporizing combustion boiler for generating combustible gas e.g. carbon monoxide, dimethylmethane and methane.    ADVANTAGE - The boiler generates a large amount of combustible gas e.g. carbon monoxide, dimethylmethane methane on adopting fluidized combustion theory without adding any chemical combustion improver through thermal reaction. The boiler converts biomass into high-grade combustible gas through pre-heating and dry distillation. The primary wind, secondary wind and wind port are designed in the boiler to fully mix the gas with air, so as to intensify combustion. The boiler discharges dust and harmful gas without smoke, thus providing improved design to the boiler, and reducing labor intensity of a worker, and improving the working environment.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass vaporizing combustion boiler.
NOVELTY - The barrel has an inner barrel (1) with a cylinder composed with a bottom, a secondary air distribution combustion barrel (5) and a fire baffle ring (9).    USE - Integrated inner barrel for use in a biomass semi-gasification furnace.    ADVANTAGE - The barrel uses good manufacturing technique, saves labor, time and material. The barrel is easy to use at low cost with high thermal efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an integrated inner barrel.    Inner barrel (1)    Secondary air distribution combustion barrel (5)    Fire baffle ring (9)
NOVELTY - The method involves cooling down carbon dioxide (CO2) separated from mixed gas to specific degrees centigrade, and separating gas and liquid using a gas-liquid separator. The separated CO2 is pressurized to 80-153 bars by a pump. The heat is exchanged with the mixed gas by the separated liquid CO2 after pressurized by the pump to return a part of cool energy to cool the mixed gas. The temperature of the CO2 is increased higher than 31.3 degrees centigrade. The separated CO2 is output from a system at a high-pressure supercritical state.    USE - Method for integrally separating and compressing carbon dioxide.    ADVANTAGE - The method enables utilization of multi-stage compression, multi-stage cooling and multi-stage separation processes so as to increase the phase-transition temperature of carbon dioxide (CO2) by increasing mixed gas pressure and ensure a certain separation rate. The CO2 in the mixed gas is separated in the form of liquid state at a relatively high condensing temperature such that the CO2 condensing separation method is improved at low-temperature and large reduction of the CO2 recovered energy consumption is realized. The method avoids the need of chemical solvent during CO2 separating and compressing process. The method can be implemented at low maintenance cost and high safety with low operation. The method can be widely applied to separate CO2 from the mixed gas, and can generate pure CO2 product and reduce emission of greenhouse gas so as to protect human habitat.    DETAILED DESCRIPTION - The mixed gas is a mixture composed of gases such as hydrogen, nitrogen, oxygen and methane.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic illustration of a carbon dioxide separating and compressing method. '(Drawing includes non-English language text)'.
NOVELTY - A tert-butyl alcohol (1-10 %mol) is added to water, and methane gas is added to the mixed solution containing water and tert-butyl alcohol, to manufacture methane gas hydrate containing tert-butyl alcohol.    USE - Manufacture of methane gas hydrate containing tert-butyl alcohol.    ADVANTAGE - The methane gas hydrate containing tert-butyl alcohol is manufactured efficiently at high temperature and low pressure conditions in short period of time, and has high gas preservation efficiency and storage stability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for storage method of methane gas.
NOVELTY - The method involves introducing an organic feed material into a fluid bed. An inorganic heat source is mixed with the feed material in the fluid bed. Gas is released from the feed material in the fluid bed by vaporizing free water from the feed material and cracking organic molecules in the feed material into shorter chain molecules. The released gas is utilized as a transport stream to entrain solids remaining from the feed material and the inorganic heat source. Cross-sectional area of the transport stream is decreased to ensure that the solids are entrained.    USE - Method for producing gaseous and condensable fuels from an organic feed material e.g. coal and biomass such as switch grass, elephant grass and woody material, waste material such as saw dust or wood chip, and animal waste material, using a fluid bed reactor.    ADVANTAGE - The method enables utilizing transport gas to obtain initial transport of post-reaction solids from a mixing zone and reducing usage of the transport gas when a reactor is hot and in steady-state operation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a fluid bed reactor for producing gaseous and condensable fuels from an organic feed material.    Fluid bed reactor vessel (10)    Mixing zone (12)    Fluidizing gas plenum (14)    Feed material inlet (16)    Transport gas inlet (17)    Fluidizing gas inlet (18)    Inert hot solids inlet (20)
NOVELTY - An electric power generation system (1) comprises hydrogen producing apparatus (2) which is equipped with metal type hydrogen producing agent, water-permeable accommodating part which is filled with metal type hydrogen producing agent and water tank which stores water supplied to metal type hydrogen producing agent, and fuel cell (3) which generates hydrogen supplied from hydrogen producing apparatus as fuel.    USE - Electric power generation system.    ADVANTAGE - The electric power generation system efficiently generates hydrogen as fuel for efficiently producing electric power.    DETAILED DESCRIPTION - An electric power generation system (1) comprises hydrogen producing apparatus (2) which is equipped with metal type hydrogen producing agent, water-permeable accommodating part which is filled with metal type hydrogen producing agent and water tank which stores water supplied to metal type hydrogen producing agent, and fuel cell (3) which generates hydrogen supplied from hydrogen producing apparatus as fuel. The metal type hydrogen producing agent contains fine powder of mixture of iron, magnesium, aluminum, calcium, sodium, zeolite and/or cordierite. The zeolite and cordierite of predetermined amount are contained with respect to total weight of mixture. INDEPENDENT CLAIMS are included for:    (1) hydrogen producing apparatus; and    (2) fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the electric power generation system. (Drawing includes non-English language text).    Electric power generation system (1)    Hydrogen producing apparatus (2)    Fuel cell (3)    Electrical storage part (4)    Inverter (5)
NOVELTY - The reaction apparatus (2) has a heat insulation package (12) that accommodates the apparatus main structure (20) for performing chemical reaction of reaction material. The exterior regions of apparatus main structure, are connected to exterior surfaces of heat insulation package by using flow paths (42,52,133a-135a). The flow paths for coolant gas and oxidizing agent gas are opened or closed by using valves (43,53,64). The electric power is generated from electric power generation cell (11) by reaction of oxidizing agent gas, and supplied fuel.    USE - Reaction apparatus of electric power generation system for electronic device. Uses include but are not limited to electronic device such as notebook type personal computer, mobile telephone, personal digital assistant (PDA), electronic notebook, wristwatch, digital still camera, digital camcorder and game machine, etc.    ADVANTAGE - The flow paths for oxidizing agent gas and coolant gas, for connecting exterior regions of apparatus main structure and heat insulation package are operated by valves. Hence the amount of heat generated at the heat insulation package can be increased during shutdown operation of electric power generation cell. The time required for performing shutdown operation of electric power generation cell can be reduced. The reliable electrochemical reaction can be performed at the electric power generation cell of the reaction apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the structure of electric power generation apparatus including reaction apparatus. (Drawing includes non-English language text)    Reaction apparatus (2)    Electric power generation cell (11)    Heat insulation package (12)    Apparatus main structure (20)    Flow paths (42,52,133a-135a)    Valves (43,53,64)
NOVELTY - A catalyst contains a metal complex comprising rhodium, ruthenium or iridium as a metal component and a nitrogen containing polycyclic compound or carbon monoxide as a ligand.    USE - Catalyst is used for electrochemical oxidation of hydride e.g. borohydride compound of alkali metal for anode pole of direct-type fuel cell and hydrogen-producing apparatus (all claimed).    ADVANTAGE - The catalyst has high activity with respect to electrochemical oxidation of hydride. The hydrogen-producing apparatus formed using the catalyst has self-electric power generation property.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) anode pole of direct-type fuel cell, which contains catalyst for anode poles and borohydride compound as fuel; and    (2) hydrogen-producing apparatus (1), which has a portion of an anode side electrode (2) to which a solution containing hydride and hydroxide is supplied, a portion of a cathode side electrode (3) which is arranged opposingly with the anode side electrode portion and generates hydrogen by reduction reaction of a proton, and an ionic-permeability diaphragm (4) provided between the anode side electrode portion and cathode side electrode portion. The anode side electrode comprises catalyst.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the hydrogen-producing apparatus.    Hydrogen-producing apparatus (1)    Anode side electrode (2)    Cathode side electrode (3)    Ionic-permeability diaphragm (4)    External circuit (5)
NOVELTY - The reaction apparatus (2) has reaction units (21,22) performing different reactions, which are connected by connection structures (23,24). A plate is joined to the reaction units by welding for blocking an internal flow path. The connection structures are connected such that a predetermined space is formed between the reaction units along the height direction.    USE - Reaction apparatus for performing reforming reaction and selective oxidation reaction of carbon monoxide, used in electric power generation system (claimed) of notebook-type personal computer, personal digital assistant (PDA), electronic notebook, wristwatch, digital still camera, digital camcorder and game machine. Can also be used in performing combination reaction, cyclization reaction, decomposition reaction, condensation reaction, polymerization reaction, reductive reaction and rearrangement reaction.    ADVANTAGE - The position shift of the reaction units can be regulated effectively even when the connection structures are deformed due to the heat generated at the time of welding the plate.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) electric power generation system; and    (2) manufacturing method of reaction apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows the top view and side view of the reaction apparatus.    Reaction apparatus (2)    Heat exchanger (10)    Reaction units (21,22)    Connection structures (23,24)    Heat insulation package (30)
NOVELTY - A modification catalyst carries out steam reforming of source gas supplied from supply unit (9), to generate hydrogen rich reformed gas that is made to pass through shift catalyst layer (6) for reduction of carbon monoxide. A filter (27) provided in discharge portion (21), prevents infiltration of water into the shift catalyst layer, while preventing the passage of the powder produced when a portion of the shift catalyst of the granular form or in the shape of a tablet gets destroyed. The reformed gas from catalyst layer is discharged through discharge pipe (20).    USE - Modifier for use in supplying hydrogen rich reformed gas to fuel cell such as solid polymer electrolyte fuel cell.    ADVANTAGE - The obstruction of a reformed gas pipeline by the catalyst powder and the excessive rise in the pressure of the system due to this can be prevented reliably, and the spreading of water in the shift catalyst layer can be prevented, while preventing the deterioration of the catalyst. The resistance force of the filter with respect to the impacts from the outside can be improved.    DESCRIPTION OF DRAWING(S) - The drawings show the fragmentary sectional views of the expanded portions of the discharge portion in the modifier. (Drawing includes non-English language text)    Shift catalyst layer (6)    Supply unit (9)    Discharge pipe (20)    Discharge portion (21)    Filter (27)
NOVELTY - An alternative fuel comprises ethanol and aromatic furan added with respect to gasoline.    USE - Alternative fuel for spark-ignition engines.    ADVANTAGE - The phase separation of water in air is suppressed by the addition of ethanol to gasoline. The alternative fuel has high octane number.
NOVELTY - A fluidized bed-type gasifier (3) thermally decomposes the thrown-in waste material for generating pyrolysis gas. A plasma furnace (4) thermally decomposes the tar and unreacted residue in the pyrolysis gas for generating reformed gas. A heat exchanger (5) generates the water vapor supplied to the gasifier using the heat of the reformed gas. A scrubber (7) condenses the water vapor contained in the reformed gas to separate water vapor from reformed gas.    USE - Combustible gas generating apparatus for decomposing and gasifying waste materials such as municipal solid waste and industrial waste, used in waste material power generation equipment.    ADVANTAGE - The ratio of the flammable component in the reformed gas can be raised by using water vapor for thermal decomposition of the waste material in the gasifier and the water vapor in the reformed gas is condensed to separate water vapor from the reformed gas, so that the emitted heat amount of the reformed gas can be raised. The energy recovery is raised by using the effective heat amount of the reformed gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for combustible gas manufacturing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the waste material power generation equipment provided with combustible gas generating apparatus. (Drawing includes non-English language text)    Fluidized bed-type gasifier (3)    Plasma furnace (4)    Heat exchanger (5)    Bag filter (6)    Scrubber (7)
NOVELTY - An organic waste is thermally decomposed and a portion of chlorine is removed as gas, and carbide is generated. The waste gas containing portion of chlorine is dechlorinated and dry-distilled into gas and tar. The carbide and tar are mixed to obtain a carbonized fuel (32).    USE - Manufacture of carbonized fuel from chlorine-containing organic waste e.g. foodstuffs residue from beverage manufacturing factory, garbage from restaurant, organic refuse and sewage sludge.    ADVANTAGE - The method enables manufacture of carbonized fuel with reduced chlorine content and high yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus for manufacturing carbonized fuel, which has a carbonization furnace (10) to generate carbide, a separation tank (20) to divide dry distilled gas and tar, and a mixing unit (30) to mix carbide and tar.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the apparatus for manufacturing carbonized fuel. (Drawing includes non-English language text)    Carbonization furnace (10)    Separation tank (20)    Chemical solution tank (22)    Mixing unit (30)    Carbonized fuel (32)
NOVELTY - A hydrogen-producing material contains microparticles of aluminum or its alloy (1) with fine cracks (2). The microparticles of non-spherical form occupy portion or more than half the weight of hydrogen-producing material. The aluminum alloy contains aluminum and gallium as main element.    USE - Material for producing hydrogen gas used as fuel for fuel cell and hydrogen fueled car.    ADVANTAGE - The hydrogen-producing material is economically and easily manufactured even at normal temperature.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of hydrogen-producing material.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of microparticle of hydrogen-producing material.    Aluminum or its alloy (1)    Crack (2)
NOVELTY - Solid fuel contains liquor lees as active component.    USE - As solid fuel e.g. biomass fuel.    ADVANTAGE - The solid fuel effectively reduced the consumption of fossil fuel. The solid fuel is cost-effective and eco-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of solid fuel, which involves drying liquor lees under reduced pressure by heating and molding.
NOVELTY - Producing biofuel feedstock involves culturing algae (201) in an aquatic composition that comprises fish (202), where the aquatic composition is controllably modified by the fish to promote algal growth, harvesting the algae from the aquatic composition, and extracting lipids from the algae, where lipids are used as biofuel feedstock.    USE - For producing biofuels or liquid fuels comprising diesel, biodiesel, kerosene, jet-fuel, gasoline, JP-1, JP-4, JP-5, JP-6, JP-7, JP-8, Jet Propellant Thermally Stable (JPTS), a product of the Fischer-Tropsch process, an alcohol-based fuel, an ethanol-containing transportation fuel, algae cellulosic biomass-based liquid fuel, or pyrolysis oil-derived fuel from algae (claimed).    ADVANTAGE - The method to produce biofuel is cost effective and energy efficient. Recycling and recovery of nutrients from the environment and/or other sources is advantageously adopted for culturing algae to reduce the cost of nutrients. To boost the yield of biofuel, the algae are exposed to stress that induces the production and accumulation of lipids.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for system (100) for culturing algae involving a growth enclosure comprising aquatic composition in which algae and the fish are cultured, where at least one condition of the aquatic composition is controllably modified by the fish to promote algal growth, an induction enclosure (304) where the algae is induced to accumulate lipids by a stressor, a foam fractionation unit (303) for concentrating the algae, unit(306) for harvesting the algae, and unit for extracting the lipids from the algae.
NOVELTY - Production of chlorine dioxide (ClO2) involves reacting alkali metal chlorate, mineral acid and reducing agent. The reducing agent is waste liquid containing glycerol derived from biodiesel production.    USE - Process for producing chlorine dioxide (claimed).    ADVANTAGE - The use of waste glycerol from biodiesel plant helps Kraft mills reduce the cost of ClO2 production. Kraft mills using hydrogen peroxide as reducing agent in the generator reduces the cost ClO2 production by switching to waste glycerol. The use of untreated glycerol in ClO2 production saves treatment expenses associated with purification of waste glycerol and partially addresses surplus issue that may arise from the spread of biodiesel plants. The presence of methanol and/or sodium chloride in waste glycerol enhances ClO2 generation.
NOVELTY - The heat-transfer plates and heat exchanger tubes are arranged inside a reaction container. The heat medium is supplied to heat exchanger tube. The supplied gas is discharged to the clearance gap between adjacent plates. The heat exchange tubes are connected through connection portion. The catalyst is filled in clearance gap between adjacent plates. The leakage of heat medium between adjacent heat exchanger tubes is prevented by using the plate-shaped connection portion. The length of connection portion in flow direction of the reaction source gas is 0.05-40 mm.    USE - Plate-type reactor is used for manufacture of methacrolein, acrolein, methacrylic acid, acrylic acid, maleic acid, phthalic acid, styrene, n-butene, isobutene, n-butane, isobutane, butadiene and ethylene oxide (all claimed).    ADVANTAGE - The leakage of the heat medium between adjacent heat exchanger tubes is prevented by using the connection portion. The target object can be steadily obtained at high efficiency.    DETAILED DESCRIPTION - The convex edge of surface of the heat-transfer plate is arranged opposing the connection portion of surface of another heat-transfer plate. The cross-sectional portion of the heat exchanger tube is in circle, ellipse or polygon shape. The distance between adjacent heat-transfer plates satisfies the specific condition relating the distance between the heat exchanger tubes, maximum width of the heat exchanger tube and thickness of the heat transfer plate.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the plate-type reactor.    Reaction zones (61-63)
NOVELTY - Water treatment apparatus (4) comprises reaction tank (7) which carries out aeration treatment of to be processed water using a microorganism support, membrane separation tank with an immersion membrane separator which separates treated water, partitions (11), and diffuser (10) in the front area (5) of the reaction tank.    USE - Apparatus for water treatment (claimed) for river water, lakes and marshes water, underground water, and organic wastewaters such as sewage and industrial effluent.    ADVANTAGE - Has high decomposition efficiency and is energy saving.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a water treatment method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the water treatment apparatus.    Water treatment apparatus (4)    Front area (5)    Reaction tank (7)    Diffuser (10)    Partitions (11)
NOVELTY - A three-cavity serial plasma on-vehicle hydrogen-rich gas generator comprises a cylindrical plasma reaction part comprising reaction cavity and generation cavity that are separated by an insulate gland bush (4); a plasma generation part (2) comprising three generation cavities which are connected in series, uniformly distributed, and formed by a metal pedestal (6), the insulate gland, and ceramics outer cylinder (5); and an inlet (7) and an outlet (11).    USE - The three-cavity serial plasma on-vehicle hydrogen-rich gas generator is useful for rapid preparation of hydrogen-rich gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the three-cavity serial plasma on-vehicle hydrogen-rich gas generator.    Plasma regeneration part (2)    Electrode (3)    Insulate gland bush (4)    Ceramics outer cylinder (5)    Metal pedestal (6)    Inlet (7)    Outlet (11)    Arch side wall (15)
NOVELTY - Preparing polymerization solvent-grade isobutane comprises: (a) mixing hydro-cracking liquefied petroleum gas with hydrogen according to a volume ratio of 1:80-100, and pre-heating at 220-280 degrees C; (b) sending into a hydrogenation reactor, and hydrogenating in the presence of hydrogenation catalyst; (c) sending into a desulfurization reactor, desulfurizing in the presence of desulfurization agent; and (d) separating liquid from gas, separating C3 and C4 components from the separated butane gas, and separating C4 component from the isobutane, dehydrating, and obtaining the product.    USE - The process is useful for preparing polymerization solvent-grade isobutane (claimed).    ADVANTAGE - Compared with the traditional process, the isobutane product having purity of 99.5-99.9% is obtained; and total sulfur and total olefin contents of the isobutane can satisfy requirements of polymerization solvent grade.    DETAILED DESCRIPTION - Preparing polymerization solvent-grade isobutane comprises: (a) mixing hydro-cracking liquefied petroleum gas with hydrogen according to a volume ratio of 1:80-100, and pre-heating at 220-280 degrees C; (b) sending into a hydrogenation reactor, and hydrogenating in the presence of hydrogenation catalyst; where the reaction temperature is 200-250 degrees C; the reaction pressure is 2.0-2.8 MPa; and the reaction space velocity is 1-2 hour-1; (c) sending into a desulfurization reactor, desulfurizing in the presence of desulfurization agent; where the reaction temperature is 200-400 degrees C; the reaction pressure is 2.0-2.8 MPa; and the reaction space velocity is 0.4-1 hour-1; and (d) separating liquid from gas to the product obtained in (c), separating C3 and C4 components from the separated butane gas, and separating C4 component from the isobutane, dehydrating the separated isobutane, and obtaining the product.
NOVELTY - Separation process for reducing ethylene loss and energy consumption of demethanizing column comprises: (a) condensing the compressed pyrolysis gas, sending the condensed gas-liquid mixture to the gas-liquid flashing tank to separate the gas and the liquid; (b) sending the liquid phase as feed material to the demethanizing column; washing the gas phase to separate methane, hydrogen and ethylene; and (c) using the gas phase, using hydrogen after being washed as fuel directly sent to the fuel gas system, and using the washed liquid phase recycled ethane and recycled propane absorbing ethylene.    USE - The separation process is useful for reducing ethylene loss and energy consumption of demethanizing column (claimed).    ADVANTAGE - In utilizing the separation process, the uncondensed ethylene is recovered by absorbing, and the cold energy obtained by high pressure recycling ethane and throttling expanding propane achieves pre-separation of part of hydrogen-methane and ethylene. Moreover, the process effectively reduces load of demethanization and separation energy-consumption.    DETAILED DESCRIPTION - Separation process for reducing ethylene loss and energy consumption of demethanizing column comprises: (a) condensing the compressed pyrolysis gas, sending the condensed gas-liquid mixture to the gas-liquid flashing tank to separate the gas and the liquid; (b) sending the liquid phase as feed material to the demethanizing column; washing the gas phase by recycled ethane and recycled propane mixture to separate methane, hydrogen and ethylene; and (c) using the gas phase with main components as methane, using hydrogen after being washed as fuel directly sent to the fuel gas system, and using the washed liquid phase recycled ethane and recycled propane absorbing ethylene as another liquid phase feed material as the demethanizing column.
NOVELTY - A fuel composition comprises a fuel which is liquid at room temperature and comprising a blend of hydrocarbonaceous and non-hydrocarbonaceous fuel having a non-hydrocarbonaceous fuel content of greater than or equal to 50 wt.%; and an alcohol fuel additive component comprising alkoxylate detergent or a fatty acid or its derivative. The additive component is soluble in the fuel blend.    USE - Fuel composition for fueling an internal combustion engine and reducing deposition of hydrocarbonaceous-fuel-soluble additives or their derivatives in a fuel system (claimed).    ADVANTAGE - The composition containing alcohol fuels which are additized with an alkoxylate detergent and/or a fatty acid or its derivative can change the composition of the deposits caused by the presence of polyisobutylene (PIB)-based additives in alcohol fuels and alcohol blended fuels, such that the deposits are more easily removed. This enables optimal engine operation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for reducing the deposition of hydrocarbonaceous-fuel-soluble additives or their derivatives from a fuel blend of hydrocarbonaceous and non-hydrocarbonaceous in a fuel system, comprising adding to the fuel blend, which is a liquid at room temperature and comprising a blend of hydrocarbonaceous and non-hydrocarbonaceous fuel, an additive component; and supplying the fuel blend to a fuel system.
NOVELTY - The desulfurization tower has sprinkling device which is arranged on filling layer. The filling layer is equipped with filling material e.g. polypropylene or polyvinyl chloride, while gas distributing device is positioned in inner side of gas distributing layer.    USE - Desulfurization tower for biogas.    ADVANTAGE - Provides a simple and reliable desulfurization tower with favorable purifying effect, has high removing rate of hydrogen sulfide, strong interference between gas and liquid, reduces absorbing resistance, has stable and flexible operation, simple structure, low cost, does not generate scale and block, wearable, corrosion resistant, low energy consumption, and small volume.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of desulfurization tower.
NOVELTY - Waterproof methanol gasoline comprises: constituents in terms of mass percent: 40-68% of gasoline, 10-50% of methanol, 2-10% of light oil and 5-15% of additive.    USE - The waterproof methanol gasoline is useful for industrial and commercial applications.    ADVANTAGE - The gasoline has good water resistance and great power performance.    DETAILED DESCRIPTION - Waterproof methanol gasoline comprises: constituents in terms of mass percent: 40-68% of gasoline, 10-50% of methanol, 2-10% of light oil and 5-15% of additive; the sum of the mass percent of all the constituents is 100%; where the gasoline is one of national standard number 90, number 93, number 95 and number 97; the methanol is the industrial methanol with the liquid water content less than 0.1%; the density of the light oil is between 0.65 and 0.68; the mass percent of each constituent of additive in the complete mass of the methanol gasoline is as following: fatty acid of 2-8%, naphthenic acid of 2-4%, ethanolamine of 0.5-5.0% and solubilizer of 0.05-0.5%; the emulsifier is the mixture of normal butanol, normal hexyl alcohol and polyethylene glycol, the mass percent of each constituent is as following: normal butanol of 40-60%, normal hexyl alcohol of 20-50%, polyethylene glycol of 20-40%; the sum of the mass percent of all the constituents is 100%; the solubilizer is polyether, with the hydrophilic-lipophilic balance (HLB) value between 11 and 14, and molecular weight of 2000 and 5000; the ethanol comprises monoethanol amine, diethanol amine, trithanolamine and the mixture of any two or all of monoethanol amine, diethanol amine, trithanolamine in any proportion.
NOVELTY - Preparing (P1) a treated metal organic framework (MOF) having increased capacity for gas storage as compared to an untreated metal organic framework, involves selecting metal organic framework having pore openings with a diameter and coordinately unsaturated metal sites, and exposing the metal organic framework to a metal site titrant for a sufficient period of time to reach equilibrium state.    USE - For preparing a treated metal organic framework useful in the storage of gas selected from carbon dioxide, nitrogen, carbon monoxide, hydrogen, methane, oxygen, ethane, propane, propylene, ethylene, acetylene, hydrogen cyanide, and oxides of nitrogen and sulfur (claimed).    ADVANTAGE - The treated MOF has increased capacity of 60-100 wt.% for gas storage as compared to an untreated MOF.
NOVELTY - The device has a non-catalytic transforming furnace (2) whose upper part is provided with a rough coal gas nozzle (4). A back transforming gas shock chamber (3) is orderly provided with a venturi scrubber (6) and a scrubbing tower (7). An oxygen distributor i.e. ring-shaped pipe, is installed in a furnace head fire proof layer, and is provided with a cooling water sleeve. A cooling water inlet opening and a cooling water outlet opening are provided on the cooling water sleeve. The rough coal gas nozzle is provided with a nitrogen inlet opening, a vapor joint and an ammonia joint.    USE - Coal gas non-catalytic transformation device for moving a bed slag gasifier.    ADVANTAGE - The device recycles tar, phenol, ammonia and methane in the rough coal gas by a catalytic transforming method in a simple and inexpensive manner. The rough coal gas enters into the furnace from the transforming furnace at top in a high-speed tangent manner and the oxygen in the small nozzle rapidly enters into the top part of the transforming furnace, so that the oxygen is completely mixed and burned with rough coal gas in the head part of the furnace, thus partly transforming methane, tar, phenol, ammonia, fatty acid and carbon in coal-dust into carbon monoxide, hydrogen, carbon dioxide, water, nitrogen and hydrogen sulfide. The device can reduce 20-25 percent of the coal gas non-catalytic transformation technique investment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a coal gas non-catalytic transformation technique.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial sectional view of a coal gas non-catalytic transformation device. '(Drawing includes non-English language text)'    Non-catalytic transforming furnace (2)    Back transforming gas shock chamber (3)    Rough coal gas nozzle (4)    Venturi scrubber (6)    Scrubbing tower (7)
NOVELTY - The method involves installing a heat collecting tank at the upper portion of base of biogas tank. The surface of heat collecting tank is equipped with a light transmitting shade. The hot water inside the heat collecting tank is discharged to the biogas tank by the pipe.    USE - Biogas generation method using solar-heat collection equipment.    ADVANTAGE - The biogas tanks can be prevented from being frozen to crack. Thus the method is implemented at low cost, low energy consumption, simple maintenance etc, in rural areas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biogas generation device.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of biogas generation device.
NOVELTY - Crystallized arabinose powder preparation involves stewing wood fiber with pure water. The stewed wood fiber is hydrolyzed by dilute acid and detoxicated. The detoxicated wood fiber is biofermented. The obtained biofermented wood fiber is purified and pre-concentrated. The obtained pre-concentrated fermentation solution is dried by a belt vacuum dryer to vaporize moisture and to obtain crystals of arabinose. The chromatographic separation is preformed on arabinose crystal to obtain pure arabinose solution.    USE - Method for preparing crystallized arabinose powder for use in grinding mills and starch factories, for use as poultry food and fuel.    ADVANTAGE - The crystallized arabinose powder preparation method is simple and cost effective, requires less labor and has high production efficiency.    DETAILED DESCRIPTION - Crystallized arabinose powder preparation involves stewing wood fiber with pure water. The stewed wood fiber is hydrolyzed by dilute acid and detoxicated. The detoxicated wood fiber is biofermented. The obtained biofermented wood fiber is purified and pre-concentrated. The obtained pre-concentrated fermentation solution is dried by a belt vacuum dryer to vaporize moisture and to obtain crystals of arabinose. The chromatographic separation is preformed on arabinose crystal to obtain pure arabinose solution. The pure arabinose solution is pre-concentrated and dried by a belt vacuum dryer to vaporize moisture and obtain arabinose crystal having less than 8% moisture content. The obtained crystallized arabinose cake is crushed and pelletized to obtain crystallized arabinose having particle size of 3-5mm.
NOVELTY - The system has compost unit having motor (11) and garbage ferment roller (7) which are fixed on bottom frame (3). The gear belts (6) are positioned around the ferment roller. The blocking gears (12) are matched with respective gear belts. A gear (8) is set at the end of ferment roller and output axis of motor is set with small gear engaged with gear (8). The inner wall of ferment roller is evenly set with several material boards. An air exhausting unit and deodorizing unit are connected with compost unit.    USE - Kitchen garbage processing system.    ADVANTAGE - The processing efficiency can be improved and operation cost can be reduced. The energy consumption can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of kitchen garbage processing system.    Bottom frame (3)    Gear belts (6)    Ferment roller (7)    Gear (8)    Motor (11)    Blocking gears (12)
NOVELTY - Rice straw is pulverized into 0.5-5 mm, rice straw is added to hydrofluoric acid solution, heated at 25-100 degrees C for 1-24 hours and agitated at speed of 50-300 rpm and dried to obtain solid fuel. The amount of rice straw is 5-30 times with respect to acid solution. The acid solution has chlorine and nitrogen content of 0.1-10 wt.%.    USE - Manufacture of solid fuel.    ADVANTAGE - The solid fuel is manufactured with high quality and yield.
NOVELTY - Zinc oxide nanoparticles are manufactured by applying discharge between metal zinc electrodes in an aqueous medium.    USE - Manufacture of zinc oxide nanoparticles. Uses include but are not limited to optoelectronic material, photosensitive agent, photocatalyst for transparent conductive thin film, electronic-ceramic material, display device, fluorescent substance, electrode material for dye-sensitized solar cell, pigment for coating material, pharmaceutical and cosmetics.    ADVANTAGE - The method enables manufacture of zinc oxide nanoparticles having uniform particle size and high yield stably and environmental-friendly, using low voltage.
NOVELTY - The fillet manufacturing device has a pressure device (B) having a presser (5) provided with pressure groove (502) in inner side of rotary shaft (2). The spinning portion (501) is descended according to the inner surface of fluid pressure groove with the top of rotary shaft. The roller apparatus (C) having multiple rollers (301) is rotated according to the rotary shaft. A saw blade (402) is placed at lower portion of supporting plate (7), when the rollers are stuck to upper side of discharge bar (403).    USE - Fillet manufacturing device used for processing organic waste such as food waste and livestock excretion.    ADVANTAGE - The overload of the fillet manufacturing device can be prevented according to the dryness of organic waste by controlling the supporting plate and roller.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the fillet manufacturing device.    Rotary shaft (2)    Presser (5)    Supporting plate (7)    Roller (301)    Saw blade (402)    Discharge bar (403)    Spinning portion (501)    Pressure groove (502)    Pressure device (B)    Roller apparatus (C)
NOVELTY - A reactant processing tank (300) stores the treatment water, and a stabilization reactor (200) makes the liquid organic waste to react with predetermined amounts of chemicals like zeolite, vermiculite, and quicklime, during processing. The treated water is extracted from the reactor and is dehydrated, such that a percentage of the water content is dehydrated. The pH of a lysate tank (800) is controlled automatically for addition of an oxidizing agent to the filtrate supplied to the lysate tank. The deposited processed liquid is then discharged out.    USE - Liquid processing system of organic waste matter. Uses include but are not limited to processing of liquid contained in organic waste matter of livestock excretions, sewage sludge, sewage of food effluent, activated sludge, etc.    ADVANTAGE - The liquid of the organic waste matter can be processed efficiently, reliably, and continuously, at very high speed, and the polluting of marine environment and ocean dumping problems can be reduced, while preventing the growth of harmful microorganisms and generation of bad smell from the organic waste matter. The processing can be performed in environmental-friendly manner, at low cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the liquid processing system. (Drawing includes non-English language text)    Storage tank (100)    Stabilization reactor (200)    Reactant processing tank (300)    Extractor (400)    Lysate tank (800)
NOVELTY - A terpolymer is obtained using a mixture containing ester group-containing compounds (1 and 2) and maleic anhydride as comonomer.    USE - Terpolymer is used for cold-flow improving agent used for fuel oil composition containing biodiesel (both claimed).    ADVANTAGE - The cold-flow improving agent containing terpolymer has excellent mobility, and improves cold-filter plugging point of fuel oil. The fuel oil composition including cold-flow improving agent has excellent permeability with respect to filter.    DETAILED DESCRIPTION - A terpolymer is obtained using a mixture containing ester group-containing compounds (1 and 2) and maleic anhydride as comonomer. The ester group-containing compounds are of formula: CH2=CR1-COOR2 (1) and CH2=CR1-COOR3 (2).    R1=H or methyl;    R2=1-30C alkyl;and    R3=6-30C alkyl.    INDEPENDENT CLAIMS are included for the following:    (1) manufacture of terpolymer;    (2) manufacture of copolymer; and    (3) cold-flow improving agent, which contains terpolymer and copolymer.
NOVELTY - A magnesium group hydride is manufactured by creating condensate by stacking and compressing thin pieces with magnesium as main component and thickness of less than or equal to 150 mu m, and reacting magnesium in condensate and hydrogen gas in hydrogen gas atmosphere.    USE - Manufacture of magnesium group hydride used as hydrogen-producing source of fuel cell.    ADVANTAGE - The method is safe, obtains magnesium group hydride efficiently, and improves yield of magnesium group hydride.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of manufacturing method of magnesium group hydride. (Drawing includes non-English language text).
NOVELTY - A refrigeration agent comprises (pts.wt.) propylene (35-50), propane (30-40), tetrafluoroethane (5-16), trifluoroethane (5-10) and liquid carbon dioxide (5-16).    USE - A refrigeration agent for replacing R22 refrigerant.    ADVANTAGE - The agent can replace refrigeration agent R22 for a long time, is soluble in mineral oil and alkylbenzene lubricant, can be directly fed, is non-azeotropic multi-member mixing refrigeration agent, has good thermodynamic performance, is harmless to ozone layer, has little greenhouse effect, and has lower exhaust temperature of compressor than that of R22 system when the refrigeration agent is working at high temperature.
NOVELTY - An enzyme for degrading carbendazim of pesticide comprising an amino acid sequence comprising a fully defined 404 amino acid sequence (SEQ ID NO. 1) given in the specification, is new.    USE - The enzyme and the engineered strain are useful for the treatment of wastewater produced by preparing carbendazim and degradation of the carbendazim (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a gene encoding the enzyme for degrading carbendazim of pesticide, where the nucleotide sequence comprises a fully defined 1215 bp sequence (SEQ ID NO. 2) given in the specification;    (2) an expression vector containing the gene; and    (3) an engineered strain containing the expression vector.
NOVELTY - Production of biodiesel comprises cultivating alga including Chlorella, Haematococcus pluvialis and Dunaliella, extracting fat from alga, performing ester exchange reaction, setting aside and delaminating, and distilling to obtain biodiesel.    USE - Production of biodiesel (claimed).    ADVANTAGE - The method is simple and suitable for mass production; has short reaction, high efficiency, no contamination to biodiesel and great economic and social effects; and can reduce environmental pollution and greenhouse effect. The raw material is abundant.
NOVELTY - Sugar cane bagasse drying involves using thermal and electrical energy of sugar mills or alcohol. A tube heat exchanger (1) is installed in boiler exhaust air, which is blown by a fan (2), where the tube heat exchanger and the fan have a specific size for drying bagasse.    USE - Method for drying sugar cane bagasse for producing briquettes or pellets.    ADVANTAGE - The sugar cane bagasse drying method enables to dry the sugar cane bagasse with increased efficiency in a simple manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the sugar cane bagasse drying method.    Tube heat exchanger (1)    Fan (2)    Dry bagasse (3)    Drying piping (4)    Conveyor belt (8)
NOVELTY - Process for utilizing oil yielding plants, comprises at least partially extracting the proteins from the residues of the plant ingredients used for oil extraction (9) and partially processing the deproteinized plant ingredients for the production of current and heat.    USE - The proteins extracted from the plant ingredients are useful in food, preferably in animal feed. The oil is useful for the production of biofuel and/or edible oil. The plant ingredients are useful for producing energy, which is useful in a thermal power generation system (all claimed).    ADVANTAGE - The by-products of the oil extraction process can be effectively utilized for the production of proteins, current and heat.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a complete system, comprising a system for oil extraction from the oil plants preferably from the oil seed, a system for separating seed bodies and seed shells, a system for protein extraction from the residues of plant ingredients used for oil extraction, a system for processing the deproteinized plant ingredients, preferably a system for compressing the deproteinized plant ingredients to press bodies and a system for energetically utilizing the processed plant ingredients.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the mass or energy flow of the method, in the form of a Sankey-diagram.    Esterification step (6)    Combustion and thermal utilization of crude glycerol (7a, 7b)    Deproteinizing step (9)    Pressing step (10)    Pelleting step (11)
NOVELTY - A chemical product providing system comprises electrolyzer (2) and gasification unit (5) fed with oxygen (B), resulted from the electrolyzer, to produce a synthesis gas (J) by gasification unit. The synthesis gas is a source material for chemical product (M). The chemical product is a synthesized fuel.    USE - Chemical product providing system.    ADVANTAGE - The system provides chemical product which will be processed in a power generator, thus needing less energy for creating such a chemical product or synthesized fuel will be consumed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for providing a chemical product (M) particularly to generate electrical power, comprising feeding oxygen (B), resulted from electrolyzer (2), to gasification unit (5); and producing synthesis gas (J) by gasification unit (5).    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram showing a chemical product providing system.    Electrolyzer (2)    Gasification unit (5)    Oxygen (B)    Synthesis gas (J)    Chemical product (M)
NOVELTY - A modified photosynthetic microorganism comprising one or more exogenous polynucleotide(s) encoding one or more enzyme(s) associated with triglyceride or lipid biosynthesis, is new.    USE - The modified photosynthetic microorganism, preferably Cyanobacterium is useful for producing triglyceride or fatty acid (claimed) useful as feedstock in the production of biofuels and/or various chemical compounds.    ADVANTAGE - The modified photosynthetic microorganism produces an increased amount of triglyceride or fatty acid when compared to the wild-type photosynthetic microorganism.
NOVELTY - Gaseous contaminants in methane-containing feed gas stream are removed by cooling feed gas stream to first temperature to form liquid phase contaminant and methane enriched gaseous phase, separating through first gas/liquid separator (4), cooling methane enriched gaseous phase to second temperature through external refrigerant to form liquid phase contaminant and methane enriched gaseous phase, and separating through second gas/liquid separator (10).    USE - Method of removing gaseous contaminants in methane-containing feed gas stream to produce purified gas stream (claimed) used as liquefied natural gas or heating gas.    ADVANTAGE - The method allows excellent separation of gaseous contaminants, and avoids use of expander between first and second gas/liquid separation.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of gaseous contaminants removal from feed gas stream.    Conduits (1, 3, 5, 6, 9, 11, 12)    Expansion unit (2)    Gas/liquid separators (4, 10)    Heat exchanger (7)    Ethane/propane cascade (8)
NOVELTY - Process (P1) for removing gaseous contaminants from feed gas stream comprising methane/gaseous contaminants involves: (A) providing feed gas stream; (B) cooling feed gas stream to temperature at which liquid phase contaminant is formed as well as methane enriched gaseous phase; (C) separating the two phases by gas/liquid separator; and (D) subjecting methane enriched gaseous phase in step (C) to distillation treatment in distillation device thereby obtaining bottom stream rich in liquid phase contaminant and lean in methane and top stream rich in methane and lean in gaseous contaminant.    USE - For removing gaseous contaminants such as carbon dioxide and hydrogen sulfide from feed gas stream (i.e. natural gas steam) comprising methane and gaseous contaminants (all claimed).    ADVANTAGE - The method is an integrated process for removing improved levels of gaseous contaminants and achieves improved hydrocarbon efficiency when after a gas/liquid separation the contaminants-depleted gaseous phase is subjected to a distillation treatment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for carrying out the process (P1).
NOVELTY - The conversion involves providing an amount of coal slurry, and adding a mixture of biomass and water containing up to 60 % solids to the coal slurry. A resulting mixture is heated under a non-oxidative gas to obtain a stable slurry which contains 20 to 40 % by weight of carbon. Preferably, the non-oxidative gas is selected from a group consisting of argon, helium, nitrogen, hydrogen, carbon dioxide, gaseous hydrocarbons, or corresponding mixtures.    USE - Conversion of biomass into higher carbon content, high energy density slurry for synthesis of transportation fuel from carbonaceous feed stocks.    ADVANTAGE - Enables energy-efficient conversion of biomass into higher carbon content, high energy density slurry. Enables efficient steam hydrogasification process of coal and/or biomass feedstocks. Enables formation of viscous slurry with a high carbon to water ratio to allow ease of handling during preparation, storage and transfer to a reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a photograph of a 50 % by weight biomass water mixture before treatment.
NOVELTY - The apparatus has a heat pressurization reactor (13) for accommodating organic sludge and a mixer (22) for agitating organic sludge contained in the reactor, so that solid-liquid slurry is produced from organic sludge and discharged from the reactor. A temperature sensor (24) measures temperature inside the reactor and a manometer (25) measures pressure inside the reactor. A temperature controller (23) and pressure controller (27) are arranged in the reactor, for maintaining the temperature and pressure inside the reactor at constant levels.    USE - Apparatus for continuously manufacturing solid-liquid slurry from organic sludge such as food waste, livestock wastewater, biomass, etc., used for producing methane gas.    ADVANTAGE - The organic sludge can be processed efficiently, while reducing the energy consumption of the manufacturing apparatus. The cost required for treatment of organic sludge can be reduced and effective recycling of solid material and liquid supernatant can be enabled by using a simple arrangement, without causing environmental pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for continuous solid-liquid slurry manufacturing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the organic sludge processing device.    Heat pressurization reactor (13)    Mixer (22)    Temperature controller (23)    Temperature sensor (24)    Manometer (25)    Pressure controller (27)
NOVELTY - The engine (10) has a fuel injector (28), an oxidizing agent injector (26), and a water injector (30) respectively injecting fuel, oxidizing agent, and water (24) into a combustion chamber (13) defined by a piston (14) located in a cylinder (12). An exhaust valve (16) selectively opens and allows exhaust gases to be expelled from the chamber. The engine is configured such that water is injected by the injector after combustion of the fuel has commenced. A catalytic converter (50) is placed after an exhaust port (17) to allow the exhaust gases to flow directly to the catalytic converter.    USE - Internal combustion engine i.e. two-stroke engine (claimed), for a land vehicle i.e. passenger car, and a sea vehicle. Can also be used for inline six and boxer four cylinder engines.    ADVANTAGE - The engine utilizes the catalytic converter that allows more and direct heat transfer from the exhaust gas to a catalyst of the catalytic converter, so that the catalyst is quickly heated to ensure better emission level. The catalytic converter is placed closest possible to the exhaust port so as to optimally utilize the heat of the exhaust gases, which immediately come out from the combustion chamber, so that heat loss to the surrounding can be minimized.    DETAILED DESCRIPTION - The oxidizing agent is a gas mixture comprising 90 percentage oxygen. The engine operates using liquid fuels such as diesel, gasoline, biodiesel, bioethanol and methanol, or gaseous fuel such as compressed natural gas. An INDEPENDENT CLAIM is also included for a method for operating an internal combustion engine.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of an internal combustion engine.    Internal combustion engine (10)    Cylinder (12)    Combustion chamber (13)    Piston (14)    Exhaust valve (16)    Exhaust port (17)    Crankshaft (18)    Water (24)    Oxidizing agent injector (26)    Fuel injector (28)    Water injector (30)    Catalytic converter (50)
NOVELTY - The air conditioning system has a desiccant wheel (20) including desiccant material to which moisture from ambient air is transferred. An evaporative cooler set in communication with an air flow divider has dry channel that receives dry fraction of dehumidified air and transfers heat from dry fraction to produce conditioned air stream. A fuel cell in communication with the air flow divider receives the fuel cell fraction of dehumidified air and produces electric current and hot exhaust air that removes moisture from the wheel for regenerating the wheel.    USE - Air conditioning system for use in commercial and residential buildings.    ADVANTAGE - The energy efficiency of the system is improved by using waste heat generated by the fuel system. The durability of the system can be enhanced by supplying dry air to fuel cell and providing appropriate level of humidity during summer time comfort cooling and winter time comfort heating.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the desiccant wheel.    Desiccant wheel (20)    Desiccant tube (30)    Axle (40)    Inlet hole (50)    Dehumidified air flow divider (56)
NOVELTY - Fractionating hemicellulose from lignocellulosic matter, comprises treating the lignocellulosic matter with a solvent at a reaction temperature of 100-250 degrees C, a reaction pressure of 5-2 and 50 atmosphere.    USE - The method is useful for fractionating hemicellulose from lignocellulosic matter, and for producing an alkylated lignin product (ethylated lignin) from lignocellulosic matter (all claimed). The lignin product is useful in wood-related materials (e.g. sawmill, paper mill discards and offcuts, saw dust, particle board and leaves) and industrial products such as pulp, paper, papermaking sludge, textiles and cloths, dextran, and rayon. The lignin product is useful for transport fuel for applications in the manufacture of fragrances, resins and/or polymers.    ADVANTAGE - The method fractionates the lignocellulosic biomass under mild conditions, thus prevents dehydration and undesirable formation of tar-like molecules to increase the yield of sugars obtained during the process.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) fractionating lignocellulosic matter, comprising: (a) solvating hemicellulose from the lignocellulosic matter using the method; (b) removing solvated hemicellulose from solid matter remaining after step (a); (c) solvating lignin from the solid matter remaining after step (b) by using a supercritical solvent;    (2) producing an alkylated lignin product from lignocellulosic matter, comprising fractionating lignocellulosic matter, where an alkylating agent is used as the supercritical solvent, and the agent alkylates the lignin of step (c); and    (3) a product obtained by the method.
NOVELTY - Methane fermentation apparatus comprises slurry adjustment tank (11) which slurries organic waste, methane fermentation tank (12) which carries out methane fermentation of the slurry, pH meter (23) which measures pH of the fermented liquor, electric conductivity meter (21, 22) which measures electric conductivity of the fermented liquor, calculation machine (30) which calculates the alkalinity, ammonia nitrogen concentration and total organic acid concentration of the fermented liquor.    USE - Methane fermentation apparatus for decomposing organic refuse and sludge.    ADVANTAGE - The alkalinity, ammonia nitrogen concentration and total organic acid concentration of the fermented liquor are automatically measured, thus the methane fermentation can be adjusted accordingly.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the methane fermentation apparatus. (Drawing includes non-English language texts).    Slurry adjustment tank (11)    Methane fermentation tank (12)    Electric conductivity meter (21, 22)    pH meter (23)    Calculation machine (30)
NOVELTY - A metal complex consists of 2,5-dihydroxybenzoic acid, bi-dentate ligand (1) and metal chosen from chromium, molybdenum, tungsten, manganese, iron, ruthenium, cobalt, rhodium, nickel, palladium, copper, zinc and cadmium.    USE - Metal complex is used in adsorbent, occlusion material and separation material for adsorbing, occluding and separating carbon dioxide, hydrogen, carbon monoxide, oxygen, nitrogen, 1-4C hydrocarbon, noble gas, hydrogen sulfide, ammonia, sulfur oxide, nitrogen oxide, siloxane, steam, organic steam, methane and in-air carbon dioxide (all claimed).    ADVANTAGE - The metal complex provides material having excellent gas-separation performance and gas-adsorbent characteristics.    DETAILED DESCRIPTION - A metal complex consists of 2,5-dihydroxybenzoic acid, bi-dentate ligand of formula (1), and metal chosen from chromium, molybdenum, tungsten, manganese, iron, ruthenium, cobalt, rhodium, nickel, palladium, copper, zinc and cadmium.    R1-R8=H, optionally substituted alkyl or halo;and    or R1+R2,R3+R4,R5+R6,R7+R8=alkylene, oxyalkylene or optionally substituted alkenylene.    An INDEPENDENT CLAIM is included for manufacture of the metal complex, which involves reacting 2,5-dihydroxybenzoic acid, bi-dentate ligand (1) and metal salt chosen from chromium salt, molybdenum salt, tungsten salt, manganese salt, iron salt, ruthenium salt, cobalt salt, rhodium salt, nickel salt, palladium salt, copper salt, zinc salt and cadmium salt, in solvent.
NOVELTY - A gasification reactor thermally decomposes and gasifies the gasification raw material. A filter main unit (5) acquires and removes the removal target object such as tar and ash content from the generation gas. A heat exchanger cools the gas generated by the gasification reactor. A heating apparatus (6) heats the filter main unit so that the removal target object adhered to the surface of a filter material (5a) made of metal fiber and acquired by the filter main unit is thermally decomposed.    USE - Filter apparatus for use in biomass gasifier for gasifying the biomass of wood chip and paper garbage and generating clean high calorie gas used as fuel of gas engine for electric power generation.    ADVANTAGE - The removal target object e.g. tar and ash content is removed from the generation gas by using the filter main unit before the generated gas is introduced into the heat exchanger, hence the need for preventing the adhesion of the removal target object to the surface of the heat exchanger is eliminated. The removal target object adhered to the surface of the filter material and acquired by the filter main unit is thermally decomposed by heating the filter main unit using the heating apparatus, hence the pressure loss produced by acquired removal target object is recovered without removing the filter main portion and the maintenance property of the filter main unit is improved. The gas generation efficiency is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the filter apparatus. (Drawing includes non-English language text)    Filter main unit (5)    Filter material (5a)    Heating apparatus (6)    Compressed air spraying apparatus (7)    Filter apparatus (A)
NOVELTY - Producing hydrogen from a hydrocarbon charge and steam, comprises: producing synthesis gas in a unit of steam reforming of the hydrocarbon feedstock in the presence of water vapor, where a fuel provides the heat for the reaction; converting the obtained steam of synthesis gas into a hydrogen stream containing methane and carbon dioxide; collecting carbon dioxide present in the stream to separate the carbon dioxide from hydrogen stream; and collecting and recycling for steam reforming of impurities present in the hydrogen stream.    USE - The process is useful for producing hydrogen from a hydrocarbon charge and steam.    ADVANTAGE - The process: allows almost complete capture of carbon dioxide; recycling of methane pressure towards the entrance of steam reforming without using a compressor and without loss of energy; and relaxes the constraint on the specification of the rate of carbon dioxide capture, thus reducing the energy consumption.
NOVELTY - Production of biogas by fermentation of biomass in a biogas plant, comprises: fermenting biomass in at least two steps, which are a hydrolysis- and a first methanizing step; separating gas mixture produced in the first methanizing step in two gas portions, where a first- and second portion mainly consists of methane and carbon dioxide, respectively; introducing the carbon dioxide and hydrogen containing hydrolysis gases derived from the hydrolysis step, in the reactor of a second methanizing step; and reacting hydrogen and carbon dioxide to methane in the presence of methanogenic bacteria.    USE - The process is useful for the production of biogas.    ADVANTAGE - The process produces biogas with improved yield (300-500 m3 biogas/hour) and higher concentration of methane (more than 60 vol.%).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a biogas plant for carrying out the above process, comprising at least one hydrolysis reactor, at least two methanation reactors, which are a first methanation reactor and a second methanation reactor, at least a separation device for separating two gas-portions of the gas mixture resulted from the first methanation step, at least a transporting device for transporting the carbon dioxide from the first methanation step to the second methanation reactor, at least a transporting device to transport hydrogen-containing hydrolysis gases derived from the hydrolysis reactor to the second methanation reactor, at least a feeding device to introduce gases in the second methanation reactor, at least a feeding device for feeding a bacterial culture in the second methanation reactor, where the bacterial culture includes methanogenic bacteria; and    (2) an immobilized bacterial culture used in the above process or in the biogas plant, where the bacterial culture comprises methanogenic bacteria.
NOVELTY - The method involves making available a porous metal foil (1), and pressing a porous volume with a corresponding triangular profile from the foil by a press unit (5) with given profile. The profiled volume is applied on another porous metal foil (2) and connected with the foil by thermal treatment. A soldering foil (3) is provided on an upper side of the latter porous metal foil, where the material of the soldering foil penetrates into the porous material of the porous metal foil by thermal treatment.    USE - Method for manufacturing a tubular metallic solid electrolyte fuel cell (claimed).    ADVANTAGE - The method applies the profiled volume on the porous metal foil, and connects the profiled volume with the foil by thermal treatment, so that the tubular fuel cell can be manufactured industrially in a simple manner with reduced time and expenditure.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a tubular fuel cell comprising two porous metal foils.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view explaining the steps in a manufacturing process of a tubular metallic solid electrolyte fuel cell. '(Drawing includes non-English language text)'    Porous metal foils (1, 2)    Soldering foil (3)    Press unit (5)    Metal-based fuel cell supporting structure (20)    Interconnector (25)
NOVELTY - A process using microorganisms for the treatment of effluents discharged by the process industries, for obtaining decolorized effluents with reduced pollution level, involves selecting microorganisms of the fungus group belonging to the family Ascomycetes, isolated from marine sources, capable of producing several lignin degrading enzymes; inoculating a growth medium composed of carbon/nitrogen sources with the microorganism; and incubating the resulting culture in the effluents at pH 2-12 at ambient temperature, over a period of less than 72 hours, to obtain the effluents in a decolorized state with reduced pollution level. Image 0/0
NOVELTY - Bio fatty acid ethylester and bio glycerin are produced by uniformly adding a vegetable oil (sunflower, rape or linseed oil) kept at 20-60 degrees C to ethanol (96-100% (v/v)) containing potassium hydroxide (KOH) (0.25-2.5 g), sodium hydroxide (NaOH) (0.12-2 g) or sulfuric acid (0.25-2.5 ml) as catalyst for 100 ml oil, then mixing the mixture for greater than or equal to 0.5 hour after the addition, settling the mixture, and then separating glycerin and ester phases. The molar proportion of vegetable oil to ethanol is 1:3-6.    USE - Process for producing bio fatty acid ethylester and bio glycerin. The bio fatty acid ethylester is used as biodiesel. The bio glycerin is used in cosmetic industry.    ADVANTAGE - The process uses only natural materials, is energy-effective, and does not produce environment contaminating by-products.
NOVELTY - Hydrogen generator has a sealed case 1, inside of which a cylindrical partition 2 is vertically and coaxially fitted and divides the case into a central reaction zone containing solid metallic and liquid reagents and a peripheral zone containing a liquid reagent. The cover of the case is fitted with connecting pipes for inlet of reagents 10 and 15, outlet of hydrogen 17 and a pressure sensor 18. The partition is tightly attached to the bottom of the case and to the cover with a gap. The generator is fitted with micropumps 11 and 12 on pipes connecting the central and peripheral zones, and an electronic control unit 19 connected to the pressure sensor 18 and micropumps 11 and 12.    USE - Chemistry.    ADVANTAGE - Invention enables efficient control of hydrogen output for various consumption rates. 4 cl, 1 dwg
NOVELTY - The furnace has a gasification furnace body (1) whose upper part is equipped with a furnace cover (3) and an exhaust pipe (5). A lower part of the gasification furnace body is equipped with an air inlet (4), a dust discharge port (6) and a slag removing port (11). A middle lower part of a gas purifier (2) is equipped with an inner purifier dust removing screen (9). Top of the gas purifier is equipped with a fuel gas outlet pipe (8). Bottom of the gas purifier is equipped with a purifier deslagging pipe (10). The furnace cover is equipped with an asbestos sealing ring and a clamping fastener.    USE - Biomass gasification furnace.    ADVANTAGE - The furnace has simple structure, safe sealing effect, heat preservation effect, energy conservation function, environmental friendly function and high practicability, and is convenient to use.    DESCRIPTION OF DRAWING(S) - The drawing shows a side perspective view of a biomass gasification furnace in partial section.    Gasification furnace body (1)    Gas purifier (2)    Furnace cover (3)    Air inlet (4)    Exhaust pipe (5)    Dust discharge port (6)    Fuel gas outlet pipe (8)    Inner purifier dust removing screen (9)    Purifier deslagging pipe (10)    Slag removing port (11)
NOVELTY - Membrane comprises a hollow support (5) having many pores (6), and an active phase comprising a gas-selective capting material (17) embedded into the pores.    USE - The membrane is useful: for separation of carbon dioxide or butane from other gas e.g. nitrogen; and in automotive vehicle (all claimed).    ADVANTAGE - The membrane: is highly resistant to thermal shocks; is environmentally friendly; and offers high fluxes and promising carbon dioxide separation factors. The membrane exhibits higher permeance together with better mechanical stability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a gas separation apparatus comprising at least one membrane, a gas intake fluidly connected to one end of the support, and adapted to receive a gas mixture of at least N gases, N not greater than 1, where the gas-selective capting material is selective to at least one to at most N-1 gases of the gas mixture;    (2) a method of manufacturing a membrane comprising embedding an active phase comprising gas-selective capting material into pores of a hollow support; and    (3) a device adapted to be fixed onto an automotive vehicle having a combustion engine, comprising a separating unit adapted to receive an exhaust gas from the engine, and to separate carbon dioxide from the exhaust gas, where the separating unit comprises the membrane.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic cross-section of view inside the membrane.    Inner surface of a fiber (1a)    Support (5)    Pores (6)    Gas-selective capting material (17)
NOVELTY - Fuel composition (I) comprises a major amount of a middle distillate fuel comprising fatty acid methyl esters (0.5-30 wt.% relative to the total amount of (I)); and a minor amount of an additive composition comprising an antioxidant system comprising at least one cyclic amine antioxidant and at least one phenolic antioxidant, and at least one ashless dispersant.    USE - The composition deals about the fuel composition such as diesel and/or biodiesel fuel compositions for home heating applications.    ADVANTAGE - (I) demonstrates reduced sediment formation as compared to a fuel composition devoid of the additive composition. The additive in (I) improves heating power in home heating applications. The fuel in (I), is derived from biological sources.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of reducing sediment formation in (I), comprising providing a major amount of the middle distillate fuel; and mixing with the fuel a minor amount of the additive composition.
NOVELTY - A foam control agent is new.    USE - A foam control agent used for controlling foam in a fermentation process including biofuel, e.g. ethanol production, or sugar cane based bioethanol production (claimed).    ADVANTAGE - The foam control agent controls foam formation for a longer time than currently known agents, and is biodegradable.    DETAILED DESCRIPTION - A foam control agent of formula R2-C(H)(R1)-O-(CH2CH2O)n-(CHR3CHR4)y-H or (II), is new.    R1, R2=H, or 1-18C linear or branched alkyl group;    R3, R4=H, or 2-6C alkyl radical;    n=3-40; and    y=0.5-5.    With the proviso that R1R2 contain 8-18C. Less than 10 mol % R1 or R2=H. Provided that R3R4 together contain 2-6C.
NOVELTY - A hydrocarbon fuel oil with paraffins as the main constituent, comprises (mass%): paraffins of less than 13 carbons ( not less than 60); isoparaffins of greater than or equal to 15 carbons (0.01-9); and normal paraffins of greater than or equal to 13 carbons ( not greater than 2).    USE - As hydrocarbon fuel oil useful in fuel cell systems (Claimed).    ADVANTAGE - The hydrocarbon fuel oil for use in fuel cell systems which has as its main constituent paraffins where the proportion of hydrocarbons with a large number of carbons is high, and it is possible to reduce the inlet temperature of the reforming apparatus in fuel cell systems where hydrogen is obtained by reforming a hydrocarbon fuel oil. The incorporation of isoparaffins of greater than or equal to 15 carbons, normal paraffins of greater than or equal to 13 carbons and isoparaffins of greater than or equal to 17 carbons up to specified ratios, produces a heavier hydrocarbon fuel oil for use in fuel cell systems, whilst enabling superior safety during handling with higher flash points and a reduction of the inlet temperature of the reforming apparatus to 310 degrees C.
NOVELTY - The device (100) has a heater (140) for a heating slope part, and a reactor (110) equipped in the slope part. A biomass feeder (120) is equipped in one side of an upper part of the reactor for supplying biomass to the slope part. A fluid yarn feeder (130) is equipped in other side of the upper part of the reactor for supplying high temperature fluid yarn to the upper side of the biomass. A gas exhaust port discharges gas generated on a top part of the reactor during rapid thermal degradation process. A transparent window is arranged to face with the slope part.    USE - Device for manufacturing bio stock i.e. liquid fuel.    ADVANTAGE - The device decomposes the heat rapidly, and manufactures the bio stock with high yield and high efficiency. The device improves the quality of the bio stock and combustion efficiency. The device can steadily secure the rapid thermal degradability of the biomass. The device facilitates the bio stock manufacturing operation, and saves the product unit cost and running cost. The device can maintain the biomass at the preset temperature. The device can remove the harmful material within the gas by a treatment tool, and can control the bio stock manufacturing process by analyzing data in a gas analyzer.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a bio stock manufacturing system comprising a cyclone tool and a condenser    (2) a method for manufacturing bio stock.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a bio stock manufacturing device.    Bio stock manufacturing device (100)    Reactor (110)    Biomass feeder (120)    Fluid yarn feeder (130)    Heater (140)
NOVELTY - The device has a lower cylinder cover (3) provided with a drain pipe interface (8). An end of a backflow sleeve (5) is fixed on an upper cylinder cover (2), and another end of the backflow sleeve is inserted into filtering liquid in a cylinder (1). The backflow sleeve is provided with an opening (6), and an end face of a gas outlet pipe (7) is inserted into the backflow sleeve through the upper cylinder cover. The end face of the gas outlet pipe is higher than liquid surface of the filtering liquid. An overflow device is mounted in the cylinder.    USE - Filtering device for a biomass gasification furnace.    ADVANTAGE - The device secondarily filters the fuel gas, and improves filtering effects. The overflow device has draining function for ensuring safety of a gas supply system of a biomass gasification system work for a long time. The device utilizes an isolation cover for effectively avoiding the fuel gas flowing out from the cylinder through an overflow pipe. The isolation cover has gas and water separating function. The device is simple in structure and convenient to operate, and can be widely popularized.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a filtering device.    Cylinder (1)    Upper cylinder cover (2)    Lower cylinder cover (3)    Backflow sleeve (5)    Opening (6)    Gas outlet pipe (7)    Drain pipe interface (8)
NOVELTY - The gasifier has an ash outlet (8) and a waste discharge port (7) fixed outside a stove body (1) whose side face is fixed with a filter (11) and a gas discharge valve (17). A waste discharge valve (10) is fixed at a bottom part of the filter that is fixed with a gas stove (14). An interface of a secondary oxygen supply valve (15) is fixed with a vent tube (9) whose end is fixed with an air inlet (12) of a blower fan. Two outlets are provided in another end of the tube, where one of the outlets is fixed with a fuel chamber (2) and a T-shaped blowing nozzle that are provided with multiple vents.    USE - Broken corn straw gasifier for use in a rural area.    ADVANTAGE - The outlet of the vent tube is connected with the fuel chamber, thus filtering oxygen-deficiency gas generated in the fuel chamber by a filter interlayer, and mixing the oxygen-deficiency gas with air sent by the secondary oxygen supply tube through the secondary oxygen supply valve to form inflammable gas. The gasifier utilizes broken corn straws, broken corn cores and saw dust as fuel, and saves energy, and improves environment protecting effect, and is convenient to assemble.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a broken corn straw gasifier.    Stove body (1)    Fuel chamber (2)    Waste discharge port (7)    Ash outlet (8)    Vent tube (9)    Waste discharge valve (10)    Filter (11)    Air inlet (12)    Gas stove (14)    Secondary oxygen supply valve (15)    Gas discharge valve (17)
NOVELTY - Solid fuel contains biomass, and glycerin, fats and oils, and/or fatty acid alkylester.    USE - Solid fuel is used as biodiesel fuel for thermal power generation.    ADVANTAGE - The solid fuel is manufactured with high calorie, high combustibility and high quality. The solid fuel has favorable handling property and transportation property.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of solid fuel, which involves mixing (S1) biomass, and glycerin, fats and oils, and/or fatty acid alkylester, and compression-molding (S2) mixture.    DESCRIPTION OF DRAWING(S) - The drawing shows the flowchart illustrating manufacture of solid fuel. (Drawing includes non-English language text)    Mixing process (S1)    Compression molding process (S2)
NOVELTY - Methanol emulsified diesel production involves adding hydrophilic emulsifier to methanol to obtain water phase while stirring methanol. Oleophylic emulsifier is added to diesel to obtain oil phase. The oil phase and water phase are emulsified by super gravity effect. Primary emulsion and precise emulsion are performed continuously to generate water-in-oil type methanol emulsified diesel.    USE - Method for producing methanol emulsified diesel (claimed).    ADVANTAGE - The methanol emulsified diesel production method enables to produce methanol emulsified diesel, which has good stability, uniform distribution of grain diameter and high quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for methanol emulsified diesel production method, which comprises an emulsifier, water phase delivery pump, storage groove, oil phase delivery pump and a flow meter.
NOVELTY - Cobalt-indium/hydrogen- beta -catalyst comprises cobalt and indium as active components supported on H- beta -molecular sieve with the silicon and aluminum ratio of 10-50. The cobalt and indium supported on the H- beta -molecular sieve is 1-5 wt.%.    USE - Cobalt-indium/hydrogen- beta -catalyst comprises cobalt and indium as active components supported on H- beta -molecular    ADVANTAGE - The catalyst improves the nitrogen oxides removing rate by selectively catalytic reducing nitrogen oxides through the low hydrocarbon induced by the barrier discharge plasma, and further lowers the active temperature; and has improved water-resistance and sulfur resistance.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparation of cobalt (Co)-indium (In)/hydrogen (H)- beta -catalyst comprising co-dipping the Co nitrate (0.05-0.2 mol/L) and In nitrate solution at the H- beta -molecular sieve, standing with the room temperature for 20-26 hours, drying at 100-120 degrees C for 3-6 hours; further roasting at 400-600 degrees C for 2-6 hours, finally pressing, crushing and sieving with 40-60 meshes to obtain the Co-In/H-beta catalyst; and    (2) a method for catalytic purifying the nitrogen oxides of the coal-fired flue gas through the impulse plasma, comprising taking low hydrocarbon as the reducing agent with the air speed of 10000 hour-1, and reducing the nitrogen oxides of the coal-fired flue gas by taking the Co-In/H- beta as the catalyst, where the volume ratio of the low hydrocarbon and nitrogen oxides of the coal-fired flue gas is 0.5-3, the reaction is carried out at 200-500 degrees C, the volume concentration of the oxygen is 2.0-8.0 vol.%, the carbon dioxide is 8-15 vol.%, the steam humidity is 3-10% and the volume concentration of the sulfur dioxide is 100-4000 ppm.
NOVELTY - The method involves compressing (200) certain amount of the waste gas stored in a storage tank to low pressure and compressing (400) certain amount of gas to high pressure. The waste gas compressed to low and high pressures are purified (100) to obtain a predetermined amount of methane gas from the compressed waste gas. The methane gas is selectively supplied to the vehicle (1) to be used as fuel for recharging (500) the vehicle.    USE - Method of converting waste gas generated from sewage disposal plant and landfill into fuel.    ADVANTAGE - The fuel gas for vehicle is obtained at low cost by using waste gas generated from sewage disposal plant and landfill as raw material and by using inexpensive equipments. The burden of the user of the vehicle for charging the vehicle is reduced.    DETAILED DESCRIPTION - The methane gas is stored in buffer containers and the methane gas is ejected from the buffer containers for charging the vehicle. The waste gas is compressed to low pressure of 5-15kgf/cm3 and the waste gas is compressed to high pressure of 240-260kgf/cm3.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the system for converting waste gas generated from sewage disposal plant and landfill into fuel. (Drawing includes non-English language text)    Vehicle (1)    Compressed waste gas purification step (100)    Waste gas compression steps (200,400)    Compressed gas storage step (300)    Vehicle recharging step (500)
NOVELTY - An enteromorpha is dried, crushed and cracked in a cracking reactor at 500-600 degrees C and maintained for 1 second. The cracked product is cooled, and biological oil is pyrolyzed in gas and converted into liquid phase. Then, the gas and solid phases are recycled, and one portion of non-condensable gas in the pyrolyzing gas is recycled to a thermal pyrolyzing furnace as secondary wind and another portion of the non-condensable gas is recycled to a combusting furnace as fuel. The amount of raw material added is 100 kg/hour.    USE - Preparation of biological oil.    ADVANTAGE - The method provides biological oil having productivity of 53%. The conversion rate of biomass is 90%.
NOVELTY - The meter has a fine filter whose outlet is divided into two routes, where one of the routes is connected with a checking valve i.e. three-way valve, for transmitting gas to a gas survey sensor and other route is connected with a side valve. An output of a steady flow valve is connected with a gas flow meter whose output is connected with a gas inlet of a gas sensor. An output interface is connected with an external equipment to provide a signal and a power supply unit receives external power to provide electric power to internal electric parts.    USE - Integrative gas on-line survey meter. Uses include but are not limited to on-line measuring of component content of gas e.g. carbon monoxide, carbon di-oxide, silicon di-oxide, nitric oxide, nitrogen dioxide, nitrous oxide, methane, hydrochloric acid, hydrogen sulfide, hydrogen fluoride, oxygen, hydrogen and chloride and polycomponent at electrical department, environmental protection department, oil field, chemical engineering department, fertilizer department, gas manufacturing department, metallurgy department, coal mining field, refuse incineration field, medical treatment and scientific experiment field.    ADVANTAGE - The survey meter realizes measurement of polycomponent.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an integrative gas on-line survey meter.'(Drawing includes non-English language text)'
NOVELTY - The burner has a furnace body (2) supported on a bracket, where an insulating layer is formed at a side wall and a top wall of the furnace body whose bottom part is fixedly connected to a base. A circular fire grate is assembled at an upper part of the base. A lower end of a vertical worm wheel shaft (10) is supported on the bracket through a bearing and an upper end is fixedly connected to a fire grate rotating shaft. An upper part of the body is connected to a cylindrical nozzle (3), where a material feeding opening is assembled on a furnace at an opposite side of the nozzle.    USE - Biomass molded fuel gasification direct combustion burner.    ADVANTAGE - The burner is compact in structure and small in volume. The manufacturing cost and the energy consumption of the burner are reduced. The environment is protected in an efficient manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass molded fuel gasification direct combustion burner.    Furnace body (2)    Cylindrical nozzle (3)    Fan (7)    Vertical worm wheel shaft (10)    Air inlet pipe (13)
NOVELTY - The device has a closed ash cleaning port (2.2) provided at a side of a combustion heating device body (2), and an ignition chamber (2.1) i.e. chamber body, provided at a lower part of a joint of the combustion heating device body and a gasification heating device body (1). A grate is installed at a lower part of the ignition chamber, and an oblique grate is installed at an upper part of the ignition chamber. Fire-resistant insulating layers are respectively provided at inner walls of the gasification heating device body and the combustion heating device body.    USE - Biomass burning gasification heating device for a biomass fuel stove.    ADVANTAGE - The device is provided with the gasification heating device body and the combustion heating device body for gasifying and burning simultaneously. The device avoids tar accumulating problem, and improves the combustion. The device has high heat utilization rate.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass burning gasification heating device.    Gasification heating device body (1)    Handle (1.1)    Combustion heating device body (2)    Ignition chamber (2.1)    Closed ash cleaning port (2.2)
NOVELTY - The method involves providing a switch (6) at an oxygen conveying pipe (7) of a straw gasification furnace (1). Total oxygen supply amount is controlled by the switch, and oxygen is supplied through a gap to enable a stove (4) to burn continuously in a non-working state of the straw gasification furnace. Flame and the oxygen supply amount are jointly controlled by the switch to control combustion quality of the straw gasification furnace.    USE - Oxygen supply control method for a straw gasification furnace.    ADVANTAGE - The oxygen supply amount and the combustion quality of the straw gasification furnace are controlled by the switch, so that the fire banking time is prolonged.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a straw gasification furnace.    Straw gasification furnace (1)    Stove (4)    Switch (6)    Oxygen conveying pipes (7, 8)
NOVELTY - The device has a reaction pot comprising a pre-concerted mixing pot and a finished product pot. A strengthen churning circling pipeline of an outer side pot is provided between the pre-concerted mixing pot and the finished product pot. The strengthen churning circling pipeline assembles an impulse device e.g. mothball device, ultrasonic machine and a magnetization machine. A junior mixing pot is connected to the impulse device through an exit valve. The magnetization machine is connected to the finished product pot. A magnetization pipe is made of stainless steel material.    USE - Bio-diesel producing device.    ADVANTAGE - The device enables mixing raw material in the junior mixing port and passing through surge cavitation for ultrasonic and magnetization disposal reducing viscosity, clearing the impurity with better mixing reaction effect. The device improves the product rate from 85.2 percentage to about the 96 percentage, and increases the quality index    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a bio-diesel producing device.
NOVELTY - The mixer has speed reducer whose ends are connected to one end of motor and coupled respectively. The other end of the speed reducer is connected to one end of rotation shaft supported by housing. A spiral blade is set at upper surface of rotation shaft and bending cutter is fixed to the shaft. A bump cutter group is provided between inner wall of housing and lower portion of bending cutter. The charging hoppers are provided on the upper surface of the housing and a filtering mesh is set in the inner cavity of the one charging hopper.    USE - Crushing mixer for organic solid waste.    ADVANTAGE - The structure of the mixer can be simplified reliably, the mixer can be operated conveniently, the working efficiency of the mixer can be improved, the good mixing and crushing effects can be ensured and the improved fermenting effect can be ensured.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the crushing mixer.
NOVELTY - The device has reaction container (1) comprising double-layer tank main portion (2) and heat preservation layer (3). The heat preservation layer is arranged covering the periphery of tank main portion except the bottom portion. A hollow portion (6) is arranged between the inner and outer layers (4,5) of tank main portion. The upper portion of the reaction container is comprised with upper vent hole (13) that is arranged for providing communication of the tank main portion with external environment. An ammonia absorption device (8) is positioned in the vent hole.    USE - Compost device.    ADVANTAGE - The composting effect of the device is improved and the device can be operated conveniently. The composting treatment time is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the compost device.    Reaction container (1)    Tank main portion (2)    Heat preservation layer (3)    Inner layer (4)    Outer layer (5)    Hollow portion (6)    Ammonia absorption device (8)    Upper vent hole (13)
NOVELTY - The method involves processing liquid in domestic garbage, after separating the solid and liquid from garbage. The solid material such as battery, bricks, broken tiles, soil and clinker are sorted, cleaned with water and dried. The sorted solid material is stored in warehouse, and conveyed to processing plant. The aluminum, tin and stibium stainless steel substance in the sorted battery are conveyed through a belt conveyor.    USE - Method for recycling domestic garbage in city and town.    ADVANTAGE - The recycling of domestic garbage is performed efficiently without spoiling environment.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view illustrating the process for recycling domestic garbage. (Drawing includes non-English language text)
NOVELTY - A catalyst comprises transition metal and phosphorus.    USE - Catalyst used for generating hydrogen by hydrolysis of ammonia-borane.    ADVANTAGE - The catalyst has high catalytic activity and enables to generate hydrogen at a higher speed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of catalyst, which involves using transition metal source and galvano solution containing phosphorus source, and anode and cathode.
NOVELTY - The apparatus has a blast pipe that is connected to one side of a drain hole formed in lower portion of an exhaust frame installed at surface of composting facility. A drain pipe is connected to other side of drain hole, while connecting end portion of drain pipe to a manhole (2) and a large diameter pipeline (11). Several exhaust holes (13) are formed in the bottom of pipeline for draining the water through the drain pipe. A fan is installed in main portion of composting facility for supplying air through the exhaust hole formed in the bottom of pipeline.    USE - Apparatus for preventing air leakage in drain pipe used in compositing facility.    ADVANTAGE - The leakage of air supplied from the fan through the manhole is prevented by supplying air through the exhaust hole formed in bottom of large diameter pipeline.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the air leakage prevention apparatus.    Manhole (2)    Air leakage prevention apparatus (10)    Large diameter pipeline (11)    Exhaust hole (13)    Connection slope (14)
NOVELTY - The furnace main portion comprises an activation chamber (A3) located under a pyrolyzing furnace chamber (A1), such that the inner space of furnace main portion is segmented by a sealing partition. A slide sealing cover plate (6) on the top portion of pyrolyzing furnace chamber is equipped with an inverted-V type groove track made of mosaic sealing materials and slide sealing friction element (3) positioned matching with the groove track.    USE - Microwave heating type cracking furnace.    ADVANTAGE - The structure of cracking furnace is simplified and reliability of cracking furnace is improved efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the microwave heating type cracking furnace.    Slide sealing friction element (3)    Slide sealing cover plate (6)    Material compression plate (8)    Gas outlet (17)    Pyrolyzing furnace chamber (A1)    Activation chamber (A3)
NOVELTY - The air inlets (50,50a,50b) supplies air to inner portion of reaction bath comprising denitrification tank (12), activation bath (14) and nitrification tank (16). The air pumps (121,141,161) at reactor bottom portion, are connected to respective air input hoses (123,143,163). The air from air inlets is discharged through outlets of each air pump. A rotary current formation structure (200) is provided with curved blades to generate vortex flow, so that effluent collides with microorganism in clockwise or counter clockwise direction.    USE - High-rate microbial mixer for purification of high concentration organic wastewater such as livestock wastewater.    ADVANTAGE - Since the vortex flow is generated with the rotary current formation structure, the mixing of air with the effluent and microorganism can be made smoothly. The deposition of high concentration suspended particles or microorganism in the floor of reaction bath can be prevented by the vortex flow. The efficiency of the mixer can be improved and the maintenance can be facilitated.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of the high-rate microbial mixer.    Denitrification tank (12)    Activation bath (14)    Nitrification tank (16)    Air inlets (50,50a,50b)    Air pumps (121,141,161)    Air input hoses (123,143,163)    Rotary current formation structure (200)
NOVELTY - The system has a pair of electrolyte separators (30,30') installed between an electrode unit and the walls of an electrolytic cell (20) to separate an electrolyte electrolyzed with hydrogen-oxygen mixed gas generated in electrode unit. A cooling section cools the electrolyte, and an air supply pipe (60) installed at bottom of electrode unit supplies compressed air to electrode unit, from a compressed air supply section. A mixed gas separation filter (40) is provided on top side of electrode unit to separate and collect the mixed gas from the electrolyte.    USE - Hydrogen-oxygen mixed gas generation system.    ADVANTAGE - An increased amount of hydrogen-oxygen mixed gas can be produced efficiently, and the electrolysis efficiency is enhanced. The generation of unpleasant smell during the generation of hydrogen-oxygen mixed gas is suppressed.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the hydrogen-oxygen mixed gas generation system.    Electrolytic cell (20)    Electrolyte separators (30,30')    Mixed gas separation filter (40)    Air supply pipe (60)    Cooling water supply pipe (81)
NOVELTY - The apparatus has a fermentation tank (D) to which a water pipe (A) connected to gas boiler (B1) is connected. The kitchen waste accommodated into the fermentation tank is heated, after tightly closing the fermentation tank, so that methane gas is generated in the fermentation tank. Air is periodically sent into the fermentation tank.    USE - Apparatus for generating methane gas by heating kitchen waste. Can also be used in heating livestock excretion waste, human excretion waste, food waste, rice hull, sawdust, and other agricultural and fishing wastes.    ADVANTAGE - Environmental pollution can be effectively suppressed, as methane gas is generated by heating kitchen waste, livestock excretion waste, human excretion waste, food waste, rice hull, sawdust, and other agricultural and fishing wastes, without the influence of seasonal changes.    DESCRIPTION OF DRAWING(S) - The drawings show the schematic views of the principal portions of apparatus used for generating methane gas. (Drawing includes non-English language text)    Water pipe (A)    Gas hose (B)    Gas boiler (B1)    Gas oven (B2)    Gas stabilizer (B8)
NOVELTY - The cathode (110) has a backing layer (120) with Nafion (RTM: sulfonated tetrafluoroethylene based fluoropolymer-copolymer) is mounted on an aperture in a fuel chamber of a microbial fuel cell (100). A catalyst layer (125) made of cobalt or platinum is mounted on the backing layer in the face that opposes the aperture so that the catalyst layer is in fluid communication with atmospheric oxygen. The backing layer communicates protons from the chamber to the catalyst layer and prevents contamination of the catalyst layer by fuel within the chamber.    USE - Cathode for microbial fuel cell such as single chambered microbial fuel cell and two-chambered fuel cell used for generating electricity and microbial electrolysis cell used for generating hydrogen (both claimed).    ADVANTAGE - The backing layer communicates protons from the fuel chamber of the microbial fuel cell to the catalyst layer and prevents contamination of the catalyst layer by the fuel within the chamber and hence the performance and durability of the microbial fuel cell is increased effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the microbial fuel cell.    Microbial fuel cell (100)    Cathode (110)    Teflonized carbon cloth (115)    Backing layer (120)    Catalyst layer (125)
NOVELTY - The method involves feeding a cooled gas mixture (206) to a gas separation membrane (208) to provide methane enriched permeate stream (210) and nitrogen enriched residue stream (211). The residue stream is cooled and reduced in pressure to provide methane-rich liquid and nitrogen-enriched vapor that is condensed and mixed with the liquid, and fed to a distillation column. A liquid methane withdrawn from a bottom of column is pressurized and vaporized to provide a vaporized methane stream that is warmed and combined with the permeate stream to provide a gaseous methane stream (294).    USE - Method for purifying a gas mixture including methane and nitrogen.    ADVANTAGE - The method enables operating efficiently over a narrow range of feed nitrogen or a membrane-only solution and separating the nitrogen from methane by utilizing the single distillation column, thus reducing energy input and lowering capital costs required for separating nitrogen from methane.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a system for purifying a gas mixture including methane and nitrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a hybrid membrane/cryogenic distillation system for removing nitrogen from methane.    Cooled gas mixture (206)    Gas separation membrane (208)    Methane enriched permeate stream (210)    Nitrogen enriched residue stream (211)    Gaseous methane stream (294)
NOVELTY - A fuel cell assembly includes a cell, a fuel supply apparatus and a heater for warming fuel. The fuel supply apparatus, the heater and the cell are connected together with a number of pipes in turn. The heater is a radiator for an electronic device. A liquid fuel coming from the fuel supply apparatus flows to the cell via the heater and is warmed up by the heater.
NOVELTY - Method of implanting water-permeable tube in contaminated soil, involves collecting organic substance of the water-soluble heavy metal which exists in contaminated soil, adding liquid to water-permeable tube, and removing the collected heavy metal aqueous solution and a liquid organic substance using a well-known unit.    USE - The method is useful for implanting water-permeable tube (claimed) for processing contaminated soil.    ADVANTAGE - The method enables to reproduce the contaminated soil.
NOVELTY - A modification system comprises source gas supply system which is provided with closed type humidification tank in cooling system (9) that circulates through fuel cell (8) and blows in and supplies source gas for reformed gas generation in reservoir water of humidification tank, and raw material gas-steam mixture supply system which supplies mixture of source gas that retains in upper space of humidification tank and steam to modifier (1). The system supplies hydrogen rich reformed gas produced with modifier of heating type of autooxidation to fuel cell.    USE - A modification system for fuel cell.    ADVANTAGE - The installation of combustion type steam generator and blower for air supply for oxidation are omitted. The system assembly is simplified. The cost reduction is performed.    DESCRIPTION OF DRAWING(S) - The drawing shows a process flow chart of the modification system.    Modifier (1)    Desulfurizer (2)    Carbon monoxide reduction device (7)    Fuel cell (8)    Cooling system (9)
NOVELTY - Process for production of biogas from briquettes of fruit and vegetable processing waste is disclosed, which involves dissolving the briquette of fruit and vegetable processing waste in water to make a homogenized slurry, feeding the slurry into an anaerobic digester at a loading rate of 6-18%, feeding the slurry to the digester at hydraulic retention time (HRT) of 35-60 days, and recovering the biogas from the digester. Image 0/0
NOVELTY - Use of a single- or multi-layer film with at least one layer made of thermoplastic polyurethanes (TPU), as a separating film between a gas mixture of different compositions, is claimed.    USE - The single- or multi-layer film is useful as separating film between a gas mixture of different compositions and as membrane film in biogas device (claimed).    ADVANTAGE - The single- or multi-layer film is flexible at low temperatures and exhibits high mechanical properties, abrasion resistance, weldability, resistance to microbial attack, elasticity, low permeability for methane, and good resistance against media influences in the gas chamber.
NOVELTY - A thermo-chemical reactor has a reactor body that rotates about an axis (5) and a press (18) that forces a pyrolysis fuel against the reactor contact surface. The contact surface forms a part of the reactor body. The reactor operates an ablative flash pyrolysis process creating uniform conditions over the entire contact surface between the raw material and contact surface, and maximises the use of the available contact surface area.    USE - Thermo-chemical reactor producing fuel for an agricultural harvesting machine diesel engine.    ADVANTAGE - The reactor converts biomass residual liquids into a diesel fuel for the harvesting vehicle more efficiently than prior art.    DESCRIPTION OF DRAWING(S) - The drawing is shows the processing of harvested pyrolysis fuel on board a self-powered harvesting machine.    axis of rotation (5)    contact surface (14)    feed drum (18)    channel (19)    feed pipe (25)    drain pipe (26)    rake (27)
NOVELTY - Use of Amorpha fruticosa, hazel, elder, bullace and oleaster as energy plants, is disclosed.    USE - The plants Amorpha fruticosa, hazel, elder, bullace and oleaster are useful: as energy plants; and to produce electricity and to heat homes.    ADVANTAGE - The plants Amorpha fruticosa, hazel, elder, bullace and oleaster do not need industrially produced fertilizer, do not exhaust the soil and could be reproduced by seed, resulting in advantageous plantation costs.
NOVELTY - A supplied waste is collected and separated (3) into non-combustible and combustible fractions. Then, non-combustible fraction is discharged and the combustible fraction is converted to hard and brittle fuel agglomerates at high temperature and pressure.    USE - Method of converting waste into fuel used in fluidized bed plant and grate-fired installation.    ADVANTAGE - The method provides fuel having improved combustion efficiency.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) installation for converting waste into fuel, which comprises a device for supplying waste, a device placed in series with the supply device for separating the collected waste into combustible and non-combustible fraction, a device placed in series with the separating device for discharging the non-combustible fraction, and a device placed in series with the separating device for converting the combustible fraction at high temperature and pressure to hard and brittle fuel agglomerates; and    (2) fuel agglomerate.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram explaining the method of converting waste into fuel.    Intake and storage of municipal waste (1)    Size reducing (2)    Separation of non-combustible (3)    Drying (4)    Separation of organics and plastics (5)
NOVELTY - Invention is related to complex processing of shipboard waste waters and organic garbage and may be used for certain enterprises, organisations, municipal entities, military camps, recreation centers, small towns and northern territories. Domestic waste and dry garbage is separated into organic substrate, which is supplied into installation of anaerobic fermentation with generation of fuel biogas and assist products: disinfected sludge and liquid phase. Dry waste may be burned without preparation in solid-fueled furnace of steam generating unit. Unreclaimable dry waste is pressed, stored and forwarded for further processing. Oil-containing waters are separated into watered oil product, which is burned in steam generating unit, and slightly contaminated water, which after polishing treatment and disinfection is supplied into reservoir or to consumers. Dry burnable waste and watered oil products are burned in steam generating unit, smoke gases are purified, and water vapour of high parametres is used for heat supply, in power and propulsion devices. Station is arranged in the form of self-propelled or non-self-propelled vessel, motor transport facility or in block-container version in the form of easily transportable separate functional modules.    USE - Technological processes.    ADVANTAGE - Complete processing of waste with production of thermal, electric and mechanical energy. 1 dwg
NOVELTY - The method involves applying pressure to a support medium (12A) and to a polymer electrolyte membrane (3) in a thickness direction by utilizing a roll press (7) such that a catalyst electrode (11A) is transferred to a surface of the electrolyte membrane. Pressure is applied to another support medium (12B) and the polymer electrolyte membrane in the thickness direction by utilizing another roll press (8) such that another catalyst electrode (11B) is transferred to an opposite surface of the electrolyte membrane, where the roll press are provided with a set of rollers (7A, 7B, 8A, 8B).    USE - Method for manufacturing a membrane electrode assembly utilized in a fuel cell (all claimed) i.e. polymer electrolyte fuel cell.    ADVANTAGE - The method allows quickly joining the catalyst electrodes to the polymer electrolyte membrane, and enables controlling microstructures in the catalyst electrodes, thus improving performance and production efficiency of the membrane electrode assembly, and reducing manufacturing cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a structure for joining a catalyst electrode and a polymer electrolyte membrane.    Polymer electrolyte membrane (3)    Roll presses (7, 8)    Rollers (7A, 7B, 8A, 8B)    Catalyst electrodes (11A, 11B)    Support media (12A, 12B)
NOVELTY - Microbial cell comprising genes encoding enzymes that catalyze the reactions: (a) pyruvate to acetolactate; (b) acetolactate to 2,3-dihydroxyisovalerate; (c) 2,3-dihydroxyisovalerate to 2-ketoisovalerate; (d) 2-ketoisovalerate to isobutyryl-coenzyme A (CoA); (e) isobutyryl-CoA to butyryl-CoA; (f) butyryl-CoA to butyraldehyde; and (g) butyraldehyde to butanol, where the cell produces butanol, is new.    USE - The microbial cell is useful for producing butanol which is useful as a chemical and/or a bio-fuel (all claimed), or as an additive to fuels e.g. gasoline.    ADVANTAGE - The process of producing butanol is carried out only in 6-7 reaction steps starting from pyruvate to give butanol.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for: (a1) a process of producing butanol comprising fermenting the microbial cell in a suitable fermentation medium under conditions where butanol is produced; (b1) an enzyme having acetolactate synthase activity which is an amino acid sequence of SEQ ID NOs: 32 (derived from Penicillium chrysogenum), 33 or 34 (Sequences not defined here may be found at ftp://ftp.wipo.int/pub/published_pct_sequences/publication); (c1) an enzyme having ketol-acid reductoisomerase activity which is an amino acid sequence of SEQ ID NO: 35 (derived from Penicillium chrysogenum) (Sequences not defined here may be found at ftp://ftp.wipo.int/pub/published_pct_sequences/publication); and (d1) an enzyme having branched-chain ketoacid dehydrogenase activity comprising subunits of amino acid sequences of SEQ ID NOs: 38, 39, 40 or 41 (all derived from Penicillium chrysogenum) (Sequences not defined here may be found at ftp://ftp.wipo.int/pub/published_pct_sequences/publication).
NOVELTY - A thermophilic bacterial strain capable of producing butanol and/or hydrogen from glycerol is new.    USE - In a starter culture; in the fermentation to produce a biofuel and/or a biochemical (preferably at least one biomass, bio-fuel, bio-gas, biochemical, methanol, ethanol, propanol, isopropanol, propanediol, butanol, hydrogen, acetate, and/or lactate); and for producing hydrogen and/or butanol from glycerol (claimed).    ADVANTAGE - The strain is adaptable to, or adapted to e.g. an environmentally friendly, CO2-neutral, and/or economically feasible solution for bio-fuel and/or bio-chemical production. The method for the production of strain adapts a current energy system into a more sustainable one; reduces dependency on imported fuels; develops an energy production based on renewable resources; increases energy efficiency; contributes substantial reductions in greenhouse gas emissions; and improves the competitiveness of e.g. national and/or European industries.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a method (M1) of producing at least one biomass, bio-fuel(s), bio-gas(es), and/or biochemical(s) involving providing a fermentable substrate comprising a carbohydrate and/or glycerol, and subjecting the fermentable substrate to a fermentation, where the fermentation involves a bacterial strain or a starter culture; and    (2) a method (M2) for isolating a thermophilic bacterial strain capable of producing hydrogen and/or butanol from glycerol.
NOVELTY - An ammonia decomposition catalyst contains a catalytically active component containing molybdenum, tungsten, vanadium, chromium, manganese, iron, cobalt, and/or nickel. The ammonia decomposition catalyst is capable of decomposing ammonia into nitrogen and hydrogen.    USE - Ammonia decomposition catalyst is used for ammonia processing method (claimed) for producing hydrogen used for fuel cell.    ADVANTAGE - The economical catalyst is capable of decomposing ammonia efficiently, and highly purified hydrogen is obtained at low temperature and high velocity. The environmental-friendly ammonia processing method is performed with reduced consumption of energy.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of ammonia decomposition catalyst, which involves preparing oxide of component (A) or mixture of oxide of component (A) and component (B), and processing with ammonia gas or nitrogen-hydrogen mixed gas at 300-800 degrees C; and    (2) ammonia processing method, which involves processing ammonia-containing gas using ammonia decomposition catalyst, decomposing ammonia into nitrogen and hydrogen, and acquiring hydrogen.
NOVELTY - A method of improving oxidation stability of biodiesel fuel(s) or mixtures of biodiesel fuel(s) and conventional diesel fuel(s), involves addition to such biodiesel fuel(s) or the mixtures a stability additive selected from one or a mixture of N,N-di(1-5C-alkyl)cyclohexylamine(s) in an amount of at least 250 mg per liter of the biodiesel fuel or per liter of the biodiesel fuel components in the mixture of biodiesel fuel and conventional diesel fuel.    USE - For improving the oxidation stability of biodiesel fuel (claimed) used for combustion in diesel engines or as blending stock.    ADVANTAGE - The method improves the oxidation stability of biodiesel fuel. The oxidation stability is increased by at least 65% (preferably greater than or equal to 100%) compared to the oxidation stability of the fuel without the stability additive as measured by the Rancimat Test.
NOVELTY - Anaerobic digestion treatment of sewage sludge comprises bacterial process that is carried out in absence of oxygen. The bacterial process comprises treating sewage sludge resulting from treatment of municipal or industrial wastewater with composition comprising fermentation supernatant comprising active enzymes from Saccharomyces cerevisiae culture and nonionic surfactant. The bacterial process includes thermophilic digestion, in which sludge is fermented in tanks at 55 degrees C, or mesophilic digestion, at 36 degrees C.    USE - Method for anaerobic digestion treatment of sewage sludge for production of biogas used in generators for electricity production and/or in boilers for heating purposes (claimed).    ADVANTAGE - The method occurs in the absence of urea or saponins.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for generating electricity from organic waste materials comprising converting biogas generated from organic waste to hydrogen in a fuel cell, and converting hydrogen to electricity.
NOVELTY - An isolated photosynthetic microorganism comprising a nucleic acid encoding (a) a fatty acid of length less than 16C, (b) heterologous thioesterase enzyme, or (c) a heterologous thioesterase, wax synthase, pyruvate decarboxylase, and alcohol dehydrogenase, is new.    USE - The isolated photosynthetic microorganism, Cyanobacterium, preferably Synechococcus sp. is useful for producing biodiesel fuel (all claimed).    ADVANTAGE - The produced combustible fuel has improved cloud or gel point.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for producing biodiesel fuel, involves (i) culturing the above-cited microorganism comprising a nucleic acid encoding a fatty acid of length less than 16C, extracting a medium chain fatty acid from the bacteria, and esterifying the fatty acid to yield medium chain hydrocarbon biodiesel fuel composition, or (ii) culturing the microorganism comprising a nucleic acid encoding a heterologous thioesterase, wax synthase, pyruvate decarboxylase and alcohol dehydrogenase, and extracting a medium chain hydrocarbon biodiesel fuel composition from the bacteria; and    (2) combustible fuel produced by the method.
NOVELTY - The water distribution device has U-shaped water distribution branch pipe units (1) which are provided at the bottom of intermediate-temperature UASB reactor. The branch pipes (7) are connected with a water feeding main pipe (8), and are provided with gate valve (6).    USE - Water distribution device for intermediate-temperature UASB reactor.    ADVANTAGE - Ensures that water may quickly form hydraulic rotating currents to mix with each other and the homogenizing effect of the whole tank is excellent. Ensures that blocked water distributing branch pipes can be easily cleared up. Provides the large-volume columnar intermediate-temperature UASB reactor with stable chemical oxygen demand (COD) removal rate of more than 70 percent and predetermined biogas production index of COD during the normal operation.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of the water distribution device for intermediate-temperature UASB reactor.    U-shaped water distribution branch pipe units (1)    Blind flanges (5)    Gate valve (6)    Branch pipes (7)    Water feeding main pipe (8)    Arc connecting pipe (9)
NOVELTY - Straw methane station comprises a raw material tank, a feeding tank and a fermenting tank which are connected in turn.    USE - The device is useful for fermenting straw.    ADVANTAGE - The device is environment-friendly, highly-efficient, and solves the problems of low rate of heat transmission and fermentation of straw.    DETAILED DESCRIPTION - Straw methane station comprises a raw material tank, a feeding tank, and a fermenting tank which are connected in turn; the feeding tank is respectively connected with a lifting material storage tank and a discharging material storage tank; the lifting material storage tank is provided with a vacuum pump and the discharging material storage tank is provided with a booster pump; the top of the fermenting tank is connected with a separating purifying device through a gas generating pipe; and a methane pipe mounted in a compressor is respectively connected with the separating purifying device and the methane storage tank.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the straw methane station.
NOVELTY - A water channel (2) is mounted on the outer wall of the electrolytic cell (1). The electrolytic cell comprises multiple electrolytic chambers that are connected in series. Each electrolytic chamber is divided into multiple small electrolytic chambers by polar plates. The lower part of the electrolytic cell is provided with a connected residual slag pot (5).    USE - Integrative water box electrolytic cell.    ADVANTAGE - A water cooling circulating device outside electrolytic cell brings residual heat away, thus providing thermal dispersion effect. Improves quality of mixed gas of hydrogen and oxygen. Guarantees stability of working liquid level and guarantees use effect of device for long time. Reduces noise, thus enabling use in various environments.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the integrative water box electrolytic cell.    Electrolytic cell (1)    Water channel (2)    Residual slag pot (5)
NOVELTY - Process for fixation of carbon and for energy production, comprises: production of aquatic biomass using carbon dioxide and sunlight; and combustion of aquatic biomass.    USE - The process is useful for fixation of carbon and energy production.    ADVANTAGE - The process is simple, time-consuming and eco-friendly for fixation of carbon and for energy production.
NOVELTY - The method involves heating heavy oil (SOE1) i.e. vacuum gas oil, up to a point of pyrolysis of hydrocarbonaceous biomass (BM1) at a temperature between 320 and 400 degree Celsius, such that fuels or propellants are formed in the heated heavy oil. The fuels or propellants are separated from the heated heavy oil and are condensed. The biomass contained in the heavy oil is between 5 weight percentage and 30 weight percentage based on the total volume, where the biomass includes moisture content (FBM) of maximum 1.0 weight percentage based on the biomass.    USE - Method for extracting a fuel or propellant through thermal cracking of a heavy oil in the presence of moist hydrocarbonaceous biomass.    ADVANTAGE - The biomass contained in the heavy oil is between 5 weight percentage and 30 weight percentage based on the total volume, such that increased proportion of short-chained hydrocarbon is achieved in a by-product. The method extracts the fuel or the propellant through thermal cracking of the heavy oil in the presence of hydrocarbonaceous biomass, using mineral or silicate catalysts, thus improving product quality and product yield.    DESCRIPTION OF DRAWING(S) - The drawing shows a simplified flow diagram of a method for extracting a fuel or propellant through thermal cracking of a heavy oil.    Hydrocarbonaceous biomass (BM1)    Moisture content (FBM)    Condenser (K)    Reactor (R1)    Heavy oil (SOE1)
NOVELTY - A polymer electrolyte fuel cell is manufactured by a forming a thin-film protective layer in a picture frame shape by applying a resin material to a peripheral edge portion (20P) of an electrolyte membrane (1) of the fuel cell by an ink jet method. The fuel cell includes electrolyte membrane, a catalyst layer, and a protective layer.    USE - Method of manufacturing a polymer electrolyte fuel cell (claimed).    ADVANTAGE - The method manufactures fuel cell that prevents occurrence of a buckled site in a peripheral end portion of a catalyst layer and creep deformation of an electrolyte membrane thus having improved reliability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a half-cell structural body (60) of a polymer electrolyte fuel cell; and    (2) a polymer electrolyte fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic sectional view of a polymer electrolyte fuel cell.    Electrolyte membrane (1)    Carrier membrane (4)    Picture frame-shape protective layer (20)    Peripheral edge portion (20P)    Catalyst layer (30)    Half-cell structural body (60)
NOVELTY - A fuel cell system comprises a fuel cell (2) which generates electric power by electrochemical reaction of a fuel (AA) containing liquefied ammonia and an oxidizing agent, a fuel-supply unit for supplying fuel to the fuel cell, an oxidizing agent-supply unit for supplying oxidizing agent to the fuel cell, a temperature measuring unit which measures the temperature of fuel cell, and a control unit. The control unit of fuel cell system controls the pressure of fuel supplied to the fuel cell from fuel-supply unit according to the temperature of fuel cell.    USE - System is used for fuel cell stack.    ADVANTAGE - The fuel cell system economically provides improved electric power generation performance. The concentration overvoltage of anode in the fuel cell system is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of fuel cell stack. (Drawing includes non-English language text)    Fuel cell (2)    Anode internal channel (3)    Anode catalyst electrode layer (4)    Anion exchange membrane (5)    Cathode internal channel (7)    Fuel (AA)
NOVELTY - A crude alcohol containing sulfur compound is desulfurized by contacting the crude alcohol with separation membrane based on pervaporation method, to reduce the content of sulfur compound in crude alcohol.    USE - Manufacture of alcohol used for manufacturing hydrogen or synthesis gas (claimed). Can also be used for manufacturing automotive fuel for motor vehicle.    ADVANTAGE - The alcohol having low sulfur content, is manufactured using simple method. The hydrogen or synthesis gas is efficiently manufactured using the alcohol.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of hydrogen or synthesis gas, which involves carrying out catalytic-reforming reaction of alcohol.
NOVELTY - The method involves converting alternating current (AC) from nuclear power plant to DC electric current by converter (6) such as rectifier or transformer on conditioner. A radiation excited water from spent fuel pool (12) is delivered to electrolyzer (7) comprising an alkaline electrolyzer, proton exchange membrane electrolyzer and an alkaline ionomer based electrolyzer solid onside electrolyzer. The DC electric current is applied to at least one pair of electrode of each electrolyzer to produce hydrogen.    USE - Method for electrolyte production of hydrogen using spent fuel pool of nuclear power plant.    ADVANTAGE - The enhanced efficiency in running the nuclear power plant decreases the cost of hydrogen production in addition to reduction in electrical energy required to form hydrogen, since water is excited by radiation from stored spent fuel rods. The production of hydrogen permits the electrical power to be more efficiently produced by a grid energy storage system.    DESCRIPTION OF DRAWING(S) - The drawing shows a grid energy storage system for nuclear power plant.    Converter (6)    Electrolyzer (7)    Cathode (8)    Membrane (9)    Anode (10)    Spent fuel pool (12)
NOVELTY - Manure is prepared by mixing incinerated ash of hen droppings and shochu liquor, adding soil microorganism, and fermenting to increase the concentration of soluble phosphorus.    USE - The manure is useful as fertilizer.    ADVANTAGE - The manure contains high concentration of soluble phosphorus that can be absorbed by the plants.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the manure, which involves performing the above-mentioned process.
NOVELTY - A pig feces conveying system has excrement conveying apparatus which conveys excrement through excrement conveying piping to fermenter of fermentation apparatus which ferment the excrement from the excrement collection site where pig droppings are temporarily brought together.    USE - Pig feces conveying system for agricultural use.    ADVANTAGE - Pig feces are automatically collected.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the downstream part of pig feces conveying apparatus. (Drawing includes non-English language text).    Accumulation pit (3)    Piping (4)    Branch pipe (5)    Pump (6)    Fermentation apparatus (7)
NOVELTY - The agent comprises zinc particles coated with a noble metal, and thermoplast or polytetrafluoroethylene as compression aids, where the zinc powder after contamination with 0.1-10 atom%, relative to the total zinc quantity, of metals of group 11 in the periodic table on its surface and mixing with untreated zinc powder is compressed into tablets. The contamination- and/or coating metal are copper. The solution contains copper sulfate.    USE - The agent useful as corrosion element or as anode in gas production cell for producing hydrogen for conveying flowable substances in mechanical spraying.    ADVANTAGE - The agent ensures efficient and economical production of hydrogen with less consumption of material.    DETAILED DESCRIPTION - (1) a method for producing an agent; and    (2) a method for production of hydrogen by using an agent.
NOVELTY - An achromatization or detoxification process for waste dyeing water involves azo dye decoloring treatment process by decomposition in anaerobic condition using azo reductase microorganism and decomposing aromatic amines produced in aerobic condition.    USE - Achromatization or detoxification process for waste dyeing water (claimed).    ADVANTAGE - Waste dyeing water is detoxified and decolored which makes it non-harmful to the environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for achromatization or detoxification apparatus for waste dyeing water.    DESCRIPTION OF DRAWING(S) - The drawing shows a waste dyeing water processing apparatus. (Drawing includes non-English language text).    Achromatization or detoxification processing apparatus (1)    pH control tank (11)    Culture tank (12)    Aerator (13,14, 15, 16)    Sedimentation tank (17)
NOVELTY - An electric power generation system comprises modifier (100) which modifies fuel which flows downstream from upstream into hydrogen, fuel supply part which supplies fuel to modifier, fuel cell generated by hydrogen produced with modifier, electrothermal heaters (31-34) arranged between upstream and downstream of modifier, temperature detecting parts which detect temperature of corresponding electrothermal heater, and control part which maintains temperature of electrothermal heaters to each fixed temperature.    USE - An electric power generation system.    ADVANTAGE - The electric power generation system can suppress raise of carbon monoxide concentration.    DETAILED DESCRIPTION - An electric power generation system comprises modifier (100) which modifies fuel which flows downstream from upstream into hydrogen, fuel supply part which supplies fuel to modifier, fuel cell generated by hydrogen produced with modifier, electrothermal heaters (31-34) arranged between upstream and downstream of modifier, temperature detecting parts which detect temperature of corresponding electrothermal heater, and control part which maintains temperature of electrothermal heaters to each fixed temperature. The electrothermal heaters are feedback-controlled based on detection temperature by corresponding temperature detecting part. The upstream order is made to reduce fixed temperature of electrothermal heaters from downstream while control part reduces supply flow rate by fuel supply part.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of modifier.    First passage substrate (1)    Second passage substrate (2)    Electrothermal heaters (31-34)    Supply pipe (41)    Modifier (100)
NOVELTY - The apparatus has a container to accommodate a reaction apparatus main section, and a temperature sensor to detect the temperature of the reaction apparatus main section. A movement apparatus moves a radiation reflector to the exterior of the container, to a position in which the radiation reflector overlaps with a radiation transmission region provided in the container to radiate the heat of the apparatus main section. The overlapping area of the radiation reflector and the radiation transmission region is changed according to the temperature detected by sensor.    USE - Reaction apparatus of fuel cell apparatus mounted in electronic device (claimed) such as notebook type personal computer. Can also be used in personal digital assistant, electronic notebook, digital camera, mobile telephone, wristwatch, game machine device and motor vehicle.    ADVANTAGE - The quantity of the radiation discharged from the reaction apparatus main section is changed according to the condition at the time of operation of the fuel cell apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating the operation of the fuel cell apparatus. (Drawing includes non-English language text)
NOVELTY - A fuel cell system has fuel cell generated by electrochemical reaction of reactive gas, cartridge type ion exchanger (47) positioned in a piping (46) connected to the fuel cell, and valve (48) which blocks the piping in connection part when the ion exchanger is removed from the piping.    USE - A fuel cell system.    ADVANTAGE - The management of fuel cell system is easy and simple.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of ion exchanger of cooling pipe line. (Drawing includes non-English language text).    Cooling piping (46)    Ion exchanger (47)    Valve (48, 49)    Inlet port (50)
NOVELTY - A fuel cell installation comprises humidification unit (3) which humidifies fuel, modification unit (5) which modifies humidified fuel and obtains hydrogen rich anode gas and fuel cell (1) which produces electric power according to electrochemical reaction of cathode gas containing anode gas and oxygen which are obtained by modification unit.    USE - Fuel cell installation for combined cycle power generation installation and fuel transformation apparatus (claimed).    ADVANTAGE - The fuel cell installation suppresses electric power generation loss and can attain increase in efficiency in high power origin.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) combined cycle power generation installation; and    (2) fuel transformation apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic systematic view of the fuel cell installation. (Drawing includes non-English language text).    Fuel cell (1)    Combustor (2)    Humidification unit (3)    Heating water (4)    Modification unit (5)
NOVELTY - A wound care device comprises first material and second material, which materials individually do not gel when exposed to fluid but do gel when brought together and exposed to a fluid.    USE - Wound care device for fibrous wound dressing and hemostatic material useful for absorbing fluid discharged from physiological target site (claimed).    ADVANTAGE - The device removes the need for using volatile solvents, reduced pollution and risk of exposure to hazardous materials for workers; provides less expensive and easier process to carry out; and is easy to apply in a water base, so new and different materials can be easily incorporated. The waste materials which are produced are cheaper to process and are more environment- friendly.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) manufacturing the wound care device comprising providing first material and second material; and bringing first material and second material together; and    (2) a method for absorbing fluid discharged from physiological target site comprising applying to physiological target site the wound care device.
NOVELTY - An oxidation catalyst of water consists of mononuclear ruthenium mono-aquo-complex formed using 2,2':6',2"-terpyridine derivative and diimine coordinating ruthenium(II).    USE - Oxidation catalyst of water is used as anode catalyst for energy conversion and hydrogen generation.    ADVANTAGE - The oxidation catalyst of water has excellent catalyst activity, and is manufactured using simple method.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for mononuclear ruthenium mono-aquo-complex.
NOVELTY - A waste-water-treatment apparatus has a processing tank (3) and a natural water line (2) which supplies nitrogenous waste water containing ammonia to processing tank. The processing tank has nitrifying bacteria (4) and anaerobic ammonium oxidizing bacteria (5).    USE - Apparatus is used for waste-water-treatment method (claimed).    ADVANTAGE - The waste-water-treatment method using the apparatus is carried out with reduced residual nitrogen concentration in waste water.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for waste-water-treatment method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of waste-water-treatment apparatus.    Natural water tank (1)    Natural water line (2)    Processing tank (3)    Nitrifying bacteria (4)    Anaerobic ammonium oxidizing bacteria (5)
NOVELTY - A modified catalyst contains catalytic active component supported by carrier having specific area of 310 m2/g. The carrier is inorganic complex oxide carrier containing titania.    USE - Modified catalyst is used for producing hydrogen (both claimed) in fuel cell system and hydrogen plants in petroleum refinery.    ADVANTAGE - The modified catalyst has high catalytic activity. The modified catalyst economically produces hydrogen without occlusion and caulking of modifier by active deterioration of catalyst at low temperature, for long period of time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing hydrogen, which involves performing water vapor reforming reaction in modification portion containing fuel oil and modification catalyst, with inlet temperature of catalyst layer at 520 degrees C or less.
NOVELTY - A modification catalyst is manufactured by uniformly dissolving complex oxide precursor compound containing metals other than titanium with organic multidentate ligand, hydrolyzing, bake-processing at 400-800 degrees C under oxygen environment, obtaining titania containing complex oxide with specific surface area of greater than or equal to 310 m2/g, and using titania containing complex oxide used as support.    USE - Manufacture of modification catalyst for hydrogen production for fuel cells.    ADVANTAGE - The method obtains modification catalyst which shortens time of producing hydrogen, and can manufacture hydrogen effectively. The water vapor reforming reaction at low temperature is effectively advanced with small noble metal usage-amount, and fall of catalyst activity is suppressed.
NOVELTY - 3C or more olefin is obtained by using ethanol in presence of catalyst containing iron, zirconium and zeolite.    USE - Manufacture of 3C or more olefin used as fuel.    ADVANTAGE - The method provides propylene with high selectivity and conversion ratio.
NOVELTY - The electric power supplying structure (25) has an electroconductive porous structure (26) comprising several holes along thickness direction. A wave-like electroconductivity porous board (27) comprising several peaks and troughs, is arranged on the electroconductive porous structure.    USE - Electric power supplying structure for water electrolysis stack of water electrolysis apparatus (both claimed) e.g. solid polymer film water electrolysis apparatus used for generating fuel for solid electrolyte fuel cell.    ADVANTAGE - The distribution of pure water and generation of gas are performed efficiently. The contact resistance of electric power supplying structure is reduced and electrolysis efficiency is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of the electrolysis apparatus. (Drawing includes non-English language text)    Electric power supplying structure (25)    Electroconductive porous structure (26)    Electroconductivity porous board (27)
NOVELTY - A catalyst-layer paste composition comprises catalyst powder, solvent, water and binder containing anion-conductive polyelectrolyte.    USE - Paste composition used for catalyst layer for manufacturing electrode and film catalyst layer-joined component of electrolysis cell used for producing hydrogen (all claimed).    ADVANTAGE - The paste composition has excellent stability and provides catalyst layer with excellent crack-proof property and suppressed generation of pinhole.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) catalyst layer (2,3) with transfer base material;    (2) electrode;    (3) film catalyst layer-joined component;    (4) electrolysis cell;    (5) manufacture of electrode; and    (6) manufacture of electrolysis cell (10).    DESCRIPTION OF DRAWING(S) - The drawing shows sectional view of electrolysis cell.    Anion-conductive polymer electrolyte membrane (1)    Catalyst layers (2,3)    Metal porous components (4,5)    Electrolysis cell (10)
NOVELTY - A portion(s) of stainless steel-type material is etched using electrolyte solution (105) containing liquid mixture, and lithium chloride as solute. The liquid mixture contains water and alcohol as solvent.    USE - Method for processing stainless steel-type material used in reactor for fuel cell apparatus (all claimed) used as power supply for motor vehicle and portable apparatus.    ADVANTAGE - The method provides stainless steel-type material having improved surface area.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) reactor which has substrate forming flow path for reaction material, and processed stainless steel-type material; and    (2) fuel cell apparatus, which has modifier for producing hydrogen by reacting fuel and water in reactor, and fuel cell for generating electric power by reacting hydrogen and oxygen.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of etching apparatus. (Drawing includes non-English language text)    Etching apparatus (100)    Container (101)    Substrate (103)    Metal plate (104)    Electrolyte solution (105)
NOVELTY - Glycerin monoether production involves reacting glycerol and tert.-butanol to obtain a condensation product. Glycerol and tert.-butanol are taken in wt. ratio of 1:1-1:10, and reacted together in a closed reactor by heating at 150-170 degrees C, and agitating the reaction mixture, in presence of 4-50wt.% of highly selective heterogeneous catalyst, to obtain glycerin monoether.    USE - Method for producing glycerin monoether for use as additive for biodiesel (claimed).    ADVANTAGE - The glycerin monoether production method enables to produce glycerin monoether which can be used to improve the fuel quality.
NOVELTY - Catigua fuel comprises oil extract of varieties of catigua.    USE - Catigua fuel for use as alternative fuel in manufacturing of edible oils, biofuels, biodiesel and lubricants for machinery and engines, and for use in pharmaceuticals.    ADVANTAGE - The catigua fuel enables to replace conventional oils.
NOVELTY - The device has an organic solid waste distributing unit fixed on a lower part of a waste-gas collecting unit. A delivery unit is fixed on a top part of a vertical column on a left side in an inner chamber of housing, and an oscillating chute is fixed under a right port of the delivery unit. A fermenting unit is fixed on a lower part of the chute, and a gas supply device is fixed on a lower part of the fermenting unit. A screw discharging unit is fixed on a lower part of the gas supply device, and extrudes a fermented material from an outlet on right side of the fermenting unit.    USE - Continuous dynamic quick composting device.    ADVANTAGE - The device has high automatic operation degree and simple process, and stability of the device can be improved. The device improves harmless effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a continuous dynamic quick composting device.
NOVELTY - The car has a submersible sewage pump installed on a hand two-wheel trolley, and a water hose connected with a drainage opening of the submersible sewage pump. A hand capstan (9) is fixed on the trolley, where top end of the trolley is articulated with a supporting rod (8). An articulation position is provided with pulleys, and a wire of the hand capstan passes through the pulleys, and is fixed on the submersible sewage pump. A trolley frame (4) and the supporting rod are made of telescopic sleeves.    USE - Deslagging car for fermented waste biogas residue exhausted from methane tank in a rural area.    ADVANTAGE - The car is designed such that the car can be operated outside the well head to avoid absorption of toxic gases into a human body, so that toxic gases exhausted from the methane tank do not produce any impact on the working group. The car reduces labor intensity during operation and performs deslagging work in a convenient, simple and easy manner. The car is convenient to descend the submersible sewage pump or lift position of the sewage pump and observe depth by bridging the trolley on the well head of the methane tank, thus improving working efficiency of the car.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a deslagging car.    Trolley frame (4)    Supporting rod (8)    Hand capstan (9)
NOVELTY - The gasifier has a small wok stand installed in an inner ring of a wok stand, and a fuel switch knob installed above a furnace cover. A gas transmitting pipe of a fuel switch is connected with an inlet manifold, and a horn connected with a bottom face of a gas stove head is installed in the inlet manifold. An inlet gas filter cover is installed below the fuel switch, and a filter provided with multiple holes is installed inside a furnace body. A hanging ring is fixed in the filter, and multiple straw honeycomb cakes are fixed inside the furnace body.    USE - Environment-friendly and energy-saving straw gasifier.    ADVANTAGE - The gasifier smolders a straw inside a furnace to be gasified and converted into hydrogen, methanol, ethane and butane flammable gas, thus effectively increasing quality of generated gas, and saving energy. The gasifier effectively filters smoke, dust and tar discharged by the straw combustion. The gasifier heats water, and can heat crop in a large vinyl house during winter. The furnace body is sealed, so that fire does not extinguish for 24 hours.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of an environment-friendly and energy-saving straw gasifier.
NOVELTY - The system has a straw case whose upper end is connected with a fuel gas stove through a pipeline, where the fuel gas stove is connected with a fuel gas furnace through the pipeline. The upper end of the straw case is connected to a heating unit through the pipeline, and a thrust rod is fixed on a top part of the straw case. A lower end of the straw case is formed with an ignition hole and a tapping hole, where a side of a lower end of the straw case is connected to a fan. A side of the straw case is provided with a waste discharging chimney.    USE - Straw fuel gas generation system.    ADVANTAGE - The system can fire the straw in an environment-friendly way, and generates clean fuel by pyrolyzing through the gasification furnace, thus improving the utilization rate of the reproducible straw resource, avoiding the need for directly stacking the straw, and avoiding energy wastage and air pollution caused by firing the straw. The system can completely obtain the organic substances such as nitrogen, phosphorus and potassium from the straw.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a straw fuel gas generation system.
NOVELTY - A sensor (38) is coupled to a hydrogen conversion device (12). A hydrogen cooled electrical generator (30) is coupled to the hydrogen conversion device. The hydrogen gas flowing through a vent formed in the electrical generator is controlled and the quantity of hydrogen gas is determined by a controller based on the operating state. The precursor material (14) made of oxygenated hydrocarbon, metal hydride material and sodium borohydroxide is coupled to hydrogen conversion device. The electro-chemical cell stack comprises electrodes made of platinum.    USE - System for reporting hydrogen gas emission from hydrogen cooled electrical generator.    ADVANTAGE - The reporting of the hydrogen gas emission from the hydrogen cooled electrical generator is performed efficiently at low cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the system for reporting hydrogen gas emission from the hydrogen cooled electrical generator.    System for reporting hydrogen gas emission from hydrogen cooled electrical generator (10)    Hydrogen conversion device (12)    Precursor material (14)    Electrical generator (30)    Sensor (38)
NOVELTY - The apparatus has an insertion opening that is formed in the outer peripheral surface of the rotating drums (1,2). A cover portion for insertion opening is provided in a spindle (3) of each rotating drum. The rotating drums are rotated by handle portion (7). A support frame is arranged in rotating drums in left-right direction to support spindles of rotating drums. A bearing bar (11) which is provided at spindle in axial direction, is extended to internal peripheral surface of rotating drum from spindle. The bearing bar is rotated uniquely with respect to spindle.    USE - Apparatus for processing organic refuse produced at home and store.    ADVANTAGE - The large-sized organic refuse such as bone of fish can be segmented and processed effectively, and the rotating drums can be cleaned reliably. The organic refuse adhered to the bearing bar and the stirring board can be removed easily.    DETAILED DESCRIPTION - A stirring board (12) is fixed to the internal peripheral surface of the bearing bar. A stopper (14) which is protrudingly provided at the inner surface of the rotating drum, is contacted with the bearing bar or stirring board. A tie rod (13) which is fixed to the spindle, is passed through the bearing bars.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the organic refuse processing apparatus.    Rotating drums (1,2)    Spindle (3)    Handle portion (7)    Bearing bar (11)    Stirring board (12)    Tie rod (13)    Stopper (14)
NOVELTY - Producing an algal biomass i.e. readily separable from water, comprises heating an aqueous slurry comprising an algal biomass, a suitable separation agent comprising a metal oxide/hydroxide, and water in a pressure vessel at 150-250 degrees C and at a pressure that maintains the water in the liquid phase.    USE - The algal biomass is useful: as a fertilizer and stock food; and to produce a biofuel, a biofuel precursor or one or more organic chemical products (all claimed). No biological data given.    ADVANTAGE - The method is cost effective. The algal biomass is readily separable from water.
NOVELTY - An elastomeric composition (C1) comprises a hydrogenated nitrile rubber (HNBR) and filler, (greater than 200 parts per rubber).    USE - For producing injection molding articles and shaped articles, such as seals, hoses, bearing pads, stators, well head seals, valve plates, cable sheathing, wheels, rollers, pipe seals, couplings, as well as for alternative fuels such as flex-fuels (gasoline-alcohol blends) and biodiesels.    ADVANTAGE - The hydrogenated nitrile rubber has a Mooney viscosity below 55 (preferably 30, especially 10) (ML(1+4) at 100 degrees C). The use of these high acrylonitrile content polymers and ultra-high acrylonitrile low Mooney viscosity polymers with high filler levels yields very good mechanical and processing properties as well very good performance and minimal swelling in biodiesel and flex-fuel. The compositions have high filler levels, excellent processability, scorch safety and very good resistance to aggressive fluids and fuels.
NOVELTY - The method comprises separating biogas originating from fermentation into a usable biogas stream consisting of methane gas and an exhaust gas stream (13) containing undesired substances, and thermally or catalytically oxidizing the exhaust gas stream, where the exhaust gas stream is guided prior to oxidation through closed storage containers (15) and/or fermentation residue containers (16, 17, 18). The exhaust gas flows successively to the storage container and/or fermentation residue container or is separated into partial quantities.    USE - The method is useful for treating biogas.    ADVANTAGE - The method provides adequate protection against explosions and ensures economical and optimal treatment of biogas with high quality and quantity.    DETAILED DESCRIPTION - The method comprises separating biogas originating from fermentation into a usable biogas stream consisting of methane gas and an exhaust gas stream (13) containing undesired substances, and thermally or catalytically oxidizing the exhaust gas stream, where the exhaust gas stream is guided prior to oxidation through closed storage containers (15) and/or fermentation residue containers (16, 17, 18). The exhaust gas flows successively to the storage container and/or fermentation residue container or is separated into partial quantities, which are separately fed respectively to the storage container and/or fermentation residue container. The exhaust gas is combusted and the combustion heat is used for covering the heat requirement of the biogas plant and optionally the external heat consumer. An INDEPENDENT CLAIM is included for a biogas plant (11).    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of a biogas plant.    Biogas treatment plant (11)    Product gas stream (12)    Exhaust gas stream (13)    Storage container (15)    Fermentation residue container. (16, 17, 18)
NOVELTY - A transforming device comprises air supply header pipe, air exhaust header pipe, air supply branch pipes and air exhaust branch pipes. One end of air supply branch pipe is connected with air supply header pipe, and the other end is connected with fermentation duct for supplying air. One end of air exhaust branch pipe is connected with air exhaust header pipe, and the other end is connected with fermentation tunnel for exhaust air. The system further comprises afterheat utilization air pipes.    USE - A transforming device used for utilizing fermentation process afterheat for tunnel aerobic composting.    ADVANTAGE - The afterheat utilization air pipe can directly lead exhaust air with afterheat from air exhaust header pipe, thus well utilizing afterheat and shortening fermentation period.    DETAILED DESCRIPTION - A transforming device comprises air supply header pipe, air exhaust header pipe, air supply branch pipes and air exhaust branch pipes. One end of air supply branch pipe is connected with air supply header pipe, and the other end is connected with fermentation duct for supplying air. One end of air exhaust branch pipe is connected with air exhaust header pipe, and the other end is connected with fermentation tunnel for exhaust air. The system further comprises afterheat utilization air pipes. One end of afterheat utilization air pipe is connected with air exhaust header pipe, and the other end is connected with air supply branch pipe. The afterheat utilization air pipe is provided with afterheat utilization air valve.
NOVELTY - The straw gasification burner has a furnace (13) that is integrally provided with a combustion chamber (12) whose bottom is provided with a baffle (2). An air channel is arranged between a wall (14) of combustion chamber and housing (15) of furnace. The outlet of combustion chamber is provided with a rotational flow jet (17) that is provided with several spiral blades. An inlet of combustion chamber is provided with an electric heater (9) that is connected with a material conveying pipe (7) using a screw (5).    USE - Straw gasification burner.    ADVANTAGE - The straw can be burnt easily while improving the combustion efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of the straw gasification burner. (Drawing includes non-English language text)    Baffle (2)    Screw (5)    Material conveying pipe (7)    Electric heater (9)    Combustion chamber (12)    Furnace (13)    Wall (14)    Housing (15)    Rotational flow jet (17)
NOVELTY - A biological membrane pipeline comprises major pipeline and air conduit, where side face of major pipeline is formed with at least one opening. Each opening is provided with air conduit whose lower side is inserted in the major pipeline. The air conduit is formed with ventilation holes on side face of upper side of major pipeline and on side face of lower side inserted into the major pipeline. The top end of air conduit is sealed. The major pipeline is filled with gravels or crushed concretes; and two ends of major pipeline have a porous plate, respectively.    USE - Biological membrane pipeline for wastewater treatment (claimed).    ADVANTAGE - By placing the major pipeline under the ground, the aboveground space is not occupied; and the generated mature microorganism membrane has comparatively strong adaptability to the variation of the quality and quantity of the wastewater. The pipeline has good operation stability, and it can stably remove the pollutant.    DESCRIPTION OF DRAWING(S) - The drawing is a perspective view of a biological membrane pipeline for wastewater treatment.
NOVELTY - The device has a fuel gasification furnace (1) whose upper end is provided with a gland bush (3) and lower end is opened with a dust outlet (4). A furnace surface (5) is installed above a furnace body and a discharge flue (6). A fuel gas conveying pipeline (7) is connected with the fuel gasification furnace. An air blocking bucket (8) is fixed above an inside of the fuel gasification furnace. An air blocking plate is placed in enclosed water gas separating boxes (11). The adjacent water gas separating boxes are connected with each other through a pipeline (16).    USE - Environment-friendly and energy-saving straw gasification device.    ADVANTAGE - The device is reasonable in structure, utilizes and treats tar and waste water, recovers the tar, and achieves full and strong combustion, stronger flame and high popularization value.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of an environment-friendly and energy-saving straw gasification device.    Fuel gasification furnace (1)    Gland bush (3)    Dust outlet (4)    Furnace surface (5)    Discharge flue (6)    Fuel gas conveying pipeline (7)    Air blocking bucket (8)    Enclosed water gas separating boxes (11)    Pipeline (16)
NOVELTY - The gasifier has a dry-distilling chamber (1), a main gasifying chamber (2) and an ash chamber (3) provided on its respective upper, middle and lower sections. The sections are separated by a heat-accumulating grid (9) and a heat-accumulating grate (18). Four sides of the main gasifying chamber are enclosed by a radiation cylinder (13). Gas holes (10) are formed on a side wall in an upper part of the radiating cylinder. The ash chamber is formed by enclosing an outer wall (4) and a lower insulating layer (22). A cone air rising hole (20) is arranged at the center of the grate.    USE - Vertical cylindrical household straw gasifier.    ADVANTAGE - The gasifier does not require external firing heat source, and can perform firing operation in a rapid manner and reduce tar content. The gasifier has high gasifying center temperature. The gasifier has reduced radiating loss and high gasifying efficiency and long fire-sealing time. The gasifier has simple structure, and is compact and convenient and inexpensive to operate.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a vertical cylindrical household straw gasifier.    Dry-distilling chamber (1)    Main gasifying chamber (2)    Ash chamber (3)    Outer wall (4)    Heat-accumulating grid (9)    Gas holes (10)    Radiation cylinder (13)    Heat-accumulating grate (18)    Cone air rising hole (20)    Lower insulating layer (22)
NOVELTY - Organic compound modifier comprises 50-60% of furfural residue, 5-12% of stove ash, 30-35% of livestock manure and 3-7% of lignite.    USE - Organic compound modifier for paddy field.    ADVANTAGE - The organic compound modifier is manufactured easily and cost effectively, and is convenient to use and apply.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing organic compound modifier.
NOVELTY - Pre-treatment system of an organic raw material in a marsh gas comprises a high speed dispersion crusher technique added before conveying an organic fermentation substance to a fermentation tank or a fermentation pool, in which the high speed dispersion crushing method comprises the continuous high speed dispersion crushing and the interval high speed dispersion crushing methods.    USE - The pre-treatment system of an organic raw material in a marsh gas is useful for performing ultra-thin homogeneous treatment on the marsh gas organism and plant raw material.    ADVANTAGE - The system effectively improves the yield of the marsh gas.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are: (1) a high speed dispersion crusher structure composed of a stator and a rotor with cogs (or a fixed disk and a rotary disk with cogs), the gap between the stator and the rotor is adjustable; in the high speed centrifugal rotation process of the rotor (or the rotary disk), strong impact, cutting, dispersing and turbulence effects are produced between the stator and the rotor (or the fixed disk and the rotary disk); and (2) an organic organism and plant raw material for producing the marsh gas comprising: the first-grade treated mud and the second-grade treated mud in a sewage treatment plant; the waste in an abattoir and a food processing plant; the city waste including the organic garbage in homes, restaurants, food markets and plant garbage in the gardens; the waste in a swine farm, including pig manure, cow manure and chicken manure; the agricultural by product including the dregs of corns and sugar canes, rotted vegetables and fruits; the forestry by product including the dregs produced in a lumber mill and forest work; the blue algae, algae, duckweeds, water plants in the lakes and rivers; the Enteromorpha prolifera, blue algae, algae, and ocean water plants in oceans; and the waste in fish industry including the organic wastes of the sea fish and fresh water fish.
NOVELTY - A heating unit has xenon lamp (1) provided at focus of reflecting mirror (2) such that light emitted from lamp is reflected to cellulose sample through diaphragm, shutter and quartz glass tube (5). A control unit has programmable logic controller (10) connected to valves (V1-V5). The input and output ends of valves (V1,V2) are connected to nitrogen and liquid nitrogen tanks (7,8) and valves (V3,V4), respectively. The output end of valve (V4) is connected with glass tube which is connected to output end of valve (V5) in connection with gas chromatograph (11).    USE - Device for making intermediate product of cellulose pyrolysis.    ADVANTAGE - The heating of cellulose sample can be controlled efficiently by using the shutter.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for making intermediate product of cellulose pyrolysis.    Xenon lamp (1)    Reflecting mirror (2)    Quartz glass tube (5)    Nitrogen tank (7)    Liquid nitrogen tank (8)    Programmable logic controller (10)    Gas chromatograph (11)    Valves (V1-V5)
NOVELTY - The stove has gas supplier (6) at the bottom of stove casing (3), around which several nozzles (7) are uniformly distributed. The dust storage baffle (10) and dust cleaning port (13) are provided at the bottom of the stove casing connected with multi-level filter purifier (15). An oil removing cover (5) surrounded by baffle, is provided at the bottom of the stove casing. The gas supplier is fixed with the oil removing cover by steel rings (9). A gas outlet pipe (12) in the cover, is connected with multi-level purifier and helical pipe (14).    USE - Straw gasification stove for family with 3-5 people, school or business with 300-500 people.    ADVANTAGE - The straw gasification stove can be operated simply and safely at low cost. The removal rate of the tar can be made more than 99.9%. The blockage of the pipe of the stove is avoided and the cooker cannot be eroded so that the service life can be increased. The efficiency of the stove can be improved and the energy can be saved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the straw gasification stove.    Stove casing (3)    Oil removing cover (5)    Gas supplier (6)    Nozzle (7)    Steel ring (9)    Dust storage baffle (10)    Gas outlet pipe (12)    Dust cleaning port (13)    Helical pipe (14)    Multi-level filter purifier (15)
NOVELTY - The hydrogen and faux substitute natural gas combining device has a purifying agent (3) interconnected to a level-one transformation adsorption tank (4) through a pipeline (9). A substitute natural gas outlet (11) is provided on the level-one transformation adsorption tank interconnected with a level-two transformation adsorption tank (5) through the pipeline. A hydrogen outlet (13) and a level-two transformation adsorption desorption air outlet (12) are provided on the level-two transformation adsorption tank.    USE - Hydrogen and faux substitute natural gas combining device.    ADVANTAGE - Refines faux substitute natural gas and hydrogen from the coke-oven gas at the same time.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of a hydrogen and faux substitute natural gas combining device.    Purifying agent (3)    Level-one transformation adsorption tank (4)    Level-two transformation adsorption tank (5)    Pipeline (9)    Substitute natural gas outlet (11)    Level-two transformation adsorption desorption air outlet (12)    Hydrogen outlet (13)
NOVELTY - Initial biomass with humidity of 15-25% is supplied to first device 2 where it is heated up to temperature of 350-450 degrees C. Then coal residue is supplied from first device 2 to second device 3, where it is heated up to temperature of 850-1000 degrees C and then it is supplied from it to third device 4. Steam-gas is supplied from first device 2 to third device 4, where they are filtered through coal residue, and after that, they are supplied to cooler-condenser 7. Steam-gases are supplied from second device 3 to cooler 6, where they are cooled to 350-400 degrees C, after that they are supplied to cooler-condenser 7.    USE - Oil and gas production.    ADVANTAGE - Decreasing power consumption of the process and reducing hydrocarbon fuel being used, possibility of supplying high-caloric gaseous fuel to distant consumers. 1 dwg
NOVELTY - Treating gas field wastewater by new composite flocculant, where the new composite flocculant is capable of treating the wastewater drained from oil-gas field.    USE - The method is useful for treating gas field wastewater by new composite flocculant (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a composite flocculant comprising: selecting an efficient flocculant-generating bacterium multiprotein bridging factor (MBF)-28 from the soil polluted by the gas field wastewater, culturing the flocculant-generating bacterium MBF-28 in a fermentation medium for 3 days at 30-35 degrees C at a speed of 120-200 rpm; centrifuging at a high speed of 8000-10000 rpm; taking 1-3 ml of supernatant fermentation liquid and formulating 1-3 ml of the inorganic flocculant 0.1% ferric chloride (FeCl3); a separation method of the flocculant-generating bacterium MBF-28 comprises: separating the culture medium: dissolving 2-4 g of beef extract, 0.5-1.0 g of yeast extract, 0.2-0.4 g of ammonium nitrate (NH4NO3), 0.5-1.0 g of potassium dihydrogen phosphate (KH2PO4), 1.0-2.0 g of K2HPO4, 0.2-0.5 g of magnesium sulfate heptahydrate (MgSO4.7H2O) and 0.01-0.05 g of ferrous sulfate (FeSO4) into 1-5 times of the gas field wastewater to 1000 ml; the separation method of the flocculant-generating bacterium MBF-28 comprises: fermenting the culture medium: applying 20 g of glucose, 0.5-1.0 g of the yeast extract, 0.5-1.0 g of the KH2PO4, 1.0-2.0 of the K2HPO4, 0.2-0.5 g of ammonium sulfate ((NH4)2SO4), 0.1-0.5 g of sodium chloride (NaCl), 0.5-1 of calcium chloride (CaCl2), 0.2-0.5 of the MgSO4.7H2O, 0.01-0.02 g of the FeSO4 and 1000 ml of water, where the pH is 7.0-8.0.
NOVELTY - Organic fertilizer is produced by crushing carpopodium of oil palm, dipping in water, inoculating with microorganism VT (0.1-0.5 wt.% of fresh carpopodium), mixing and fermenting.    USE - Method for producing organic fertilizer (claimed).    ADVANTAGE - The method controls composting period to 25 days and achieves organic content of 50%, saves 15-20% of fermentation area and improves quantity of composted product.
NOVELTY - A water fertilizer composition comprises (pts.wt.) photosynthetic bacteria (0.5-1.5), ammonium sulfate (1-2), calcium superphosphate (0.5-1.5) and organic fertilizer (5-7).    USE - A water fertilizer composition used for culturing phytoplankton and zooplankton.    ADVANTAGE - The composition has fast and lasting manurial effect, and simple preparation suitable for large-scale industrial production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of water fertilizer composition comprising stirring uniformly photosynthetic bacteria, ammonium sulfate, calcium superphosphate and organic fertilizer.
NOVELTY - A hydrogen is produced by mixing bamboo charcoal which fixes microorganisms group for hydrogen producing containing new microorganism which belong to Klebsiella oxytoca (NITE P-638) with raw material organic matter, and decomposing raw material organic matter.    USE - Production of hydrogen.    ADVANTAGE - The method is excellent in hydrogen production efficiency.
NOVELTY - Inner jacked spherical biogas tank comprises charging hole, manure-stored barrel, and manure-pumping device.    USE - The inner jacked spherical biogas tank is useful for industrial and commercial applications.    ADVANTAGE - The utility model has good insulating performance; the liquid rises and descends continuously during the gas-producing and gas-using process, so it stirs and breaks the fermenting materials; the culvert pipe is not blocked during the gas-using and gas-producing process; it drastically improves yield and utilization rate of the biogas tank; the hydraulic chamber divides the biogas tank into upper and lower layers, so it is convenient to charge material, clean slag; and it is convenient for the maintenance man to come in and out; it avoids potential safety hazard of maintenance work.    DETAILED DESCRIPTION - Inner jacked spherical biogas tank, where the biogas tank is spherical; a charging hole is set on one side of the middle part; a manure-stored barrel is set on the other side of the middle part by a manure-pumping device; a mouth is set at the top of the biogas tank; a hopper-shaped hydraulic chamber is set under the mouth; the bottom of the hopper-shaped hydraulic chamber is connected to a connecting pipe; through holes are symmetrically set on the connecting pipe; a movable cover is set in the pipe under the through holes; a fermenting chamber is set outside the hopper-shaped hydraulic chamber.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the inner jacked spherical biogas tank.
NOVELTY - The low-temperature generator has a hydrogen inlet (1) and a positive electrode (2) connected with a hydroxyl ion (3). An oxygen inlet (5), a discharged hot water (6) and a carbon dioxide working medium pipeline (7) are connected with a heat exchanger (8). A carbon dioxide pressurizer (9) is inserted into a steam turbine (10) to drive a carbon dioxide cooler (12) of a generator (11) to connect with a carbon dioxide cycling pump (13). Heat energy generated by an alkaline hydrogen-oxygen fuel cell is heated in a cogeneration structural device for generating power with carbon dioxide.    USE - Carbon dioxide working medium cogeneration carbonate heat-energy and low-temperature generator.    ADVANTAGE - The carbon dioxide working medium is heated by excess heat to be supercritical at higher than 50 degrees centigrade, so that the carbon dioxide working medium is expanded to drive the steam turbine to generate the power. The generator is utilized for the working medium in high pressure, low vaporization temperature, better vaporization potential, and low volume flow conditions, and when the working medium is non-corrosive, non-inflammable, non-toxic and tasteless. The generator has environment-friendly and energy-saving effects.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a carbon dioxide working medium cogeneration carbonate heat-energy and low-temperature generator.    Hydrogen inlet (1)    Positive electrode (2)    Hydroxyl ion (3)    Oxygen inlet (5)    Discharged hot water (6)    Carbon dioxide working medium pipeline (7)    Heat exchanger (8)    Carbon dioxide pressurizer (9)    Steam turbine (10)    Generator (11)    Carbon dioxide cooler (12)    Carbon dioxide cycling pump (13)
NOVELTY - The device has a loading cabin (1) equipped on a primary furnace, and a cone spiral feeding device (14) equipped under the loading cabin. A primary cabin (2) is connected with a discharging port of the cone spiral feeding device. A charging port of the cone spiral feeding device is connected with a discharging port of the loading cabin in a sealing manner. A cooler (5) is filled with cooling water in a tangent direction by a water inlet tube, where cooling water forms a continuous circulation by an overflow tube in a refluxing manner.    USE - Biomass gasifying device.    ADVANTAGE - The device can crack tar oil and separate tar and cooling water. The device filers the smoke dust, avoids polluting water and environment and suits for supplying gas to biomass.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a preparation method for a biomass gasifying device.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass gasifying device.    Loading cabin (1)    Primary cabin (2)    Cooler (5)    Cone spiral feeding device (14)    High temperature cracking device (15)
NOVELTY - Deep treating sewage and reducing carbon dioxide (CO2) comprise pre-treating sewage and flue gas via higher oxidization; and adjusting pH of the pre-treated sewage to 6.5-8.5 via sodium carbonate (Na2CO3) or calcium oxide (CaO), conveying the sewage and flue gas after adjustment into a bioreactor, and using engineered microalgae to deep treat to finish the treatment of sewage and emission reduction of CO2.    USE - Method of deep treating sewage and reducing carbon dioxide emission (claimed).    ADVANTAGE - The method solves the problems of existing technology that the algae are difficult to be treated in sewage because the organic pollutant with large molecules in water cannot be absorbed. It reuses the CO2 from the flue gas. Functional products can be extracted from the engineered microalgae. The method has low cost and investment, high efficiency and treating effect; and is capable of reutilizing flue gas, increasing the source of biomaterial energy, reducing the difficulty in deep treatment of sewage, decreasing the engineering cost, and changing the traditional sewage treatment concept.
NOVELTY - A dye wastewater treatment method comprises a materializing pre-treatment, an anaerobic treatment, and an aerobic treatment carried out in sequence. The materializing pre-treatment is conducted to remove a part of chromaticity and chemical oxygen demand. The treated water is discharged or recycled after further treatment. An advanced oxidation treatment is conducted to the water discharged from the aerobic treatment to finally remove degradation-refractory pollutant at the end of the wastewater treatment and the intermediate metabolized substances produced in the biological treatment.    USE - A dye wastewater treatment method (claimed).    ADVANTAGE - The method can have an effective treatment on the degradation-refractory dye wastewater to lower the operation cost and standardize the indexes like COD and chromaticity of the discharged water to the national norm so as to address the domestic current situation of difficulties in tackling the dye wastewater and to meet the requirement of upgrading and restructuring the sewage treatment plant according to the increased standard of environment protection in the future.    DESCRIPTION OF DRAWING(S) - The drawing is a block diagram illustrating a dye wastewater treatment method (Drawing includes non-English language text).
NOVELTY - An electrolyte level monitoring sensor has a tube (82) equipped with circuit including a switch positioned adjacent to selected level of aqueous solution. A float (88) which floats on aqueous solution, slidably engages with tube and moves along the tube by the changes in surface level of solution. A controller controls system operation in response to the monitoring conditions. The controller indicates the period when level of aqueous solution reaches the selected level indicated by float actuating the switch.    USE - Hydrogen generating system for use in internal combustion engine of vehicle e.g. petrol fueled motor vehicle such as passenger car, and light duty truck, and diesel fueled motor vehicle such as heavy duty truck and heavy equipment.    ADVANTAGE - The properties of the fuel are improved and combustion efficiency is improved resulting in a cleaner burn and better fuel economy. The reliability, and durability of the engine are improved, and exhaust pollutant amount is reduced. The hydrogen generating system can be installed easily.    DESCRIPTION OF DRAWING(S) - The drawing shows a partially cut-away perspective view of the electrolysis cell of electrolyte level monitoring apparatus.    Cap (74)    Outlet (75)    Fill plug (76)    Tube (82)    Float (88)
NOVELTY - The device includes a hydrogen-oxygen generator for generating oxygen and hydrogen by the electrolytic water. Power of the hydrogen-oxygen generator is a provided by a solar battery. The oxygen and the hydrogen separately flow into a coal-burning or oil-burning combustor via a pipeline.    USE - Device for generating hydrogen and oxygen using solar energy, electrolytic water and combustion.    ADVANTAGE - Saves energy and reduces emission by using solar energy to produce direct current and using electrolyzing water to generate oxygen and hydrogen. Improves burning rate of combustor by utilizing oxygen and hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic block diagram showing the device for generating hydrogen and oxygen. (Drawing includes non-English language text)
NOVELTY - A methanol gasoline metal corrosion inhibitor comprises (wt.%): fatty alcohol (40-60), anti-rust agent (10-30), alkenyl ester or ether (15-35) and surfactant (3-8).    USE - Methanol gasoline metal corrosion inhibitor.    ADVANTAGE - The corrosion inhibitor exhibits anti-rust effect to metal by car contrast experiment of 20000 km, where overhauling shows that air cylinder pressure of engine is normal. The erosion consumption of air cylinder is equivalent to that of used commercial gasoline. The oil supply system and vaporizer do not have obvious corrosion phenomenon.
NOVELTY - A reed biomass is integrally applied by performing extraction separation to bioactive substances in reed stalks and leaves, performing reduced pressure concentration to extracting solution, employing concentrated solution as antioxidant for greasy fat and bacteriostat for microorganism and performing corresponding pretreatment to reed stem leaf residues abundant in cellulose biomass after taking bioactive substances, performing saccharification fermentation to produce biofuel ethanol, and applying residues as cow feed to form integrated application system for reed biomass.    USE - Integrated application of reed biomass.    DETAILED DESCRIPTION - A reed biomass is integrally applied by performing extraction separation to bioactive substances in reed stalks and leaves, performing reduced pressure concentration to extracting solution, employing concentrated solution as antioxidant for greasy fat and bacteriostat for microorganism and performing corresponding pretreatment to reed stem leaf residues abundant in cellulose biomass after taking bioactive substances, performing saccharification fermentation to produce biofuel ethanol, and applying residues as cow feed to form integrated application system for reed biomass. The reed residues after fermentation by Saccharomycetes is abundant in single cell protein (SCP).
NOVELTY - Biodiesel is produced by washing, soaking, mixing and crushing raw material to obtain pasty pretreated liquor, performing acid hydrolysis to obtain hydrolysate; detoxifying the hydrolysate using macroporous resin, and preparing fermentation medium; adding oil-producing thallus, fermenting, and centrifuging fermentation liquid to collect oil containing microorganism; extracting oil by Soxhlet method, reducing pressure, and recycling extraction agent by distillation to obtain microbiological oil; and performing catalysis reaction and ester exchange reaction with short-chain alcohol.    USE - Method of producing biodiesel (claimed).    ADVANTAGE - The method is simple and has low cost.    DETAILED DESCRIPTION - Biodiesel is produced by washing, soaking, mixing and crushing litchi slag, litchi seed and litchi rind obtained during producing litchi juice or litchi wine to obtain pasty pretreated liquor, performing acid hydrolysis at high temperature and pressure to obtain hydrolysate; detoxifying the hydrolysate using macroporous resin, and preparing fermentation medium; adding oil-producing thallus, fermenting, and centrifuging fermentation liquid to collect oil containing microorganism; extracting oil by Soxhlet method, reducing pressure, and recycling extraction agent by distillation to obtain microbiological oil; and performing catalysis reaction and ester exchange reaction with short-chain alcohol.
NOVELTY - The apparatus (200) has a purging station (230) for jetting water on bad smell containing gas generated in a bad smell generation facility (100). Another purging station (220) has filters purifying the bad smell containing gas emitted from a gas receiver (210) by using pine needle microorganism that is diluted in water. The pine needle microorganism ferments mixed rice for a predetermined period. The fermented rice is mixed with muscovado sugar corresponding to season or temperature.    USE - Apparatus for reducing odor of livestock waste such as pig ordure, fowl urine and cow dung urine in stockbreeding field and agricultural field.    ADVANTAGE - The apparatus effectively reduces the bad smell of the livestock waste by using the pine needle microorganism, thus providing clean environment with less maintenance and production costs and less labor intensity.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of an apparatus for reducing odor using pine needle microorganism.'(Drawing includes non-English language text)'    Bad small generation facility (100)    Odor reduction facility (200)    Gas receiver (210)    Purging stations (220, 230)
NOVELTY - The system has several fluid collecting containers and fluid collecting pipes. The fluid collection containers are provided for conveying fluids to fluid collecting pipes. The sleeves for storage bag, are provided for preventing the amount of waste entered into the fluid collecting containers and the fluid collecting pipes.    USE - System for collecting and recycling methane from organic waste.    ADVANTAGE - The methane can be collected and recycled easily and accurately, and the permeation of waste into the fluid collecting pipe and fluid collecting container can be suppressed reliably.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for collecting and recycling methane from burying site.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the methane collecting and recycling system.
NOVELTY - The integrated type electric stove has a gas supplying pipeline (2) and wind inlet pipeline (16) are respectively connected with the high temperature generator (1) and smoke exhausting pipeline (5). The end portion of gas supply pipeline is connected with the gas inlet of mixture-type catalyst (8) connected to pressure meter (13) and marsh gas fermenting pool (9) made of unplasticized PVC sealing material and plastic product. The gas outlet of mixture-type catalyst is connected with the gas inlet of the stove (12) by pipeline.    USE - Hybrid stove using power and biomass fuel.    ADVANTAGE - The integrated type electric stove is featured with high heat, less cost, adequate gas source, convenient usage and health/environment protection.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the integrated type electric stove of marsh gas biomass fuel.    High temperature generator (1)    Gas supplying pipeline (2)    Smoke exhausting pipeline (5)    Mixture-type catalyst (8)    Marsh gas fermenting pool (9)    Stove (12)    Pressure meter (13)    Wind inlet pipeline (16)
NOVELTY - A gas flue ring is provided at upper portion of furnace structure. A U-shaped water storage tank is provided at upper portion of furnace structure. An air exhausting and stirring device is provided at center portion of furnace structure. A fuel gas input pipe is provided on upper end of coke filtering device. A valve is provided on fuel gas output pipe. A taper cover is provided to cover center portion of tank. A smoke channel has two ends among which one end is connected with furnace structure upper portion, and other end is connected with smoke and dust filter.    USE - Straw gasifier for gasification of rice straw, wheat straw, weed and melon vine.    ADVANTAGE - The main components of the furnace are assembled easily, while improving safety during operation of furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the straw gasifier.
NOVELTY - A wastewater ecotoxicity reduction system consists of a flow control bath (110), an electrolyzer (130), a chemical bath (140), an adsorption tower (150), and a biological treatment unit (160). The electrolyzer electrochemically decomposes the harmful chemical substances contained in wastewater flowing in from the flow control bath. The chemical bath aggregates heavy metals and suspended solids as hydroxides, from wastewater flowing in from the electrolyzer. The biological treatment unit removes organic material from wastewater by using microorganisms.    USE - System is used for reducing ecotoxicity of wastewater (claimed) discharged from chemical industries.    ADVANTAGE - The system enables economical and efficient reduction of ecotoxicity of wastewater, without using an ion-exchange resin, and provides treated water having required discharge standards. Formaldehyde is completely removed.    DETAILED DESCRIPTION - A wastewater ecotoxicity reduction system consists of a flow control bath which controls the load of wastewater and homogenizes the water quality, an electrolyzer, a chemical bath, an adsorption tower, and a biological treatment unit. The electrolyzer electrochemically decomposes the harmful chemical substances contained in wastewater flowing in from the flow control bath. The chemical bath aggregates heavy metals and suspended solids as hydroxides, from wastewater flowing in from the electrolyzer. The adsorption tower processes wastewater flowing in from the chemical bath by adsorption process. The biological treatment unit removes organic material from wastewater by using microorganisms. An INDEPENDENT CLAIM is included for wastewater ecotoxicity reduction method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the ecotoxicity reduction system. (Drawing includes non-English language text)    Flow control bath (110)    Electrolyzer (130)    Chemical bath (140)    Adsorption tower (150)    Biological treatment unit (160)
NOVELTY - Processing organic wastes, involves introducing liquid or solid organic wastes into different material storage tanks, crushing organic wastes, introducing the crushed material into retting pool, blending the organic wastes with water, adding inoculum and subjecting pre-treated material to anaerobic fermentation at high temperature, preparing the biogas residue into efficient composite organic biofertilizer, refluxing produced biogas slurry, introducing biogas into thermoelectricity linkage device and supplying electrical energy and thermal energy.    USE - The method is useful for processing organic wastes to produce organic eco-fertilizer (claimed).    ADVANTAGE - The method cost-effectively produces stable fertilizer without causing environmental pollution, and the fertilizer is suitable for various crops.    DETAILED DESCRIPTION - Method for processing organic wastes, involves (a) introducing liquid or solid organic wastes into different material storage tanks, crushing the organic wastes until the granularity is not greater than 30 mm, (b) introducing the crushed material into retting pool for retting, blending the organic wastes with water, adjusting carbon nitrogen ratio to 20-30:1, and total sulfide concentration to 30-35%, (c) adding inoculum and subjecting pre-treated material to anaerobic fermentation at high temperature, and (d) preparing the biogas residue produced in step (c) into efficient composite organic biofertilizer, refluxing the produced biogas slurry or subjecting to aerobic composite process, and introducing the biogas into thermoelectricity linkage device and supplying electrical energy and thermal energy.
NOVELTY - A ferment drying chamber (6) has a material feeding hole (11) at upper end, and a material discharging hole (7) at lower end. A hollow blending shaft (21) fixed with a hollow blending blade (30), is penetrated through both sides of ferment drying chamber. A decelerating motor (1) is connected with the right end of blending shaft. An air inlet of an air distributing pipe (34) of ferment drying chamber, is connected with an air outlet of a heat exchanger. A moisture discharging hole of ferment drying chamber, is connected with an inlet of dust collector.    USE - Biochemical organic trash treating machine.    ADVANTAGE - The organic trash can be oxidized, fermented and dried efficiently, with less pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biochemical organic trash treating machine.    Decelerating motor (1)    Ferment drying chamber (6)    Material discharging hole (7)    Material feeding hole (11)    Hollow blending shaft (21)    Hollow blending blade (30)    Air distributing pipe (34)
NOVELTY - The method involves subjecting sewage to organic degrading, reverse nitrating, and denitriding processes by conveying sewage into a biological treatment pool provided with suspension filling material and millipore aeration device. The treated sewage from the biological treatment pool is let into an ecological treatment pool containing iron and calcium substrate and water plants for removal of organic material and phosphorus. The ecological treated sewage is then sterilized in a sterilization pool and is finally let into an adjacent water channel.    USE - Integrative biological-ecological sewage processing method.    ADVANTAGE - The sewage can be treated biologically and ecologically at low energy consumption. The reactor used for treating the sewage has simple structure, good impact resistance, occupies less installation space, and is convenient to manage.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for integrative biological-ecological sewage processing reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the integrative biological-ecological sewage processing reactor.
NOVELTY - The system has a cracking unit (D) into which gaseous product is injected. The garbage is crushed into crushing chamber (D2). The solid carbide is injected to the crushing chamber for treating the garbage. The sorted garbage is injected into pyrolyzing chamber (D1) into which nitrogen gas is injected.    USE - System for producing coal gas and active carbon using garbage.    ADVANTAGE - The utilization efficiency of the garbage can be improved so that environmental pollution can be reduced without consumption of energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing coal gas and active carbon using garbage.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the system for producing coal gas and active carbon using garbage. (Drawing includes non-English language text)    Gas collection unit (A)    Recycling unit (B)    Cracking unit (D)    Pyrolyzing chamber (D1)    Crushing chamber (D2)
NOVELTY - The biodiesel production reactor has a curved portion (12) that is provided in upper region (10) along a reference line (13). The biodiesel fuel filled in reactor portion is sealed by providing the curved portion.    USE - Biodiesel production reactor.    ADVANTAGE - The moisture content contained in the biodiesel fuel can be removed efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of the biodiesel production reactor.    Upper region (10)    Curved portion (12)    Reference line (13)
NOVELTY - The apparatus has a pre-processing unit (100) including multiple sections (110-130), and post-processing unit (200) connected to the pre-processing unit via flow paths (220,230). The pre-processing unit has a dirty water inlet pipe (140), and delivery tubes (142,144) formed in intermediate portion of adjacent sections. A slab panel (152) with multiple slots (154) is installed covering the sections (110,120). The flow paths (220,230) are formed through lattice type frame and porous concrete frame of the post-processing unit.    USE - Sewage purification apparatus.    ADVANTAGE - The purification degree of sewage can be improved by the pre-processing and post-processing treatments.    DESCRIPTION OF DRAWING(S) - The drawing shows the cross-sectional view of the sewage purification apparatus.    Pre-processing unit (100)    Sections of pre-processing unit (110-130)    Dirty water inlet pipe (140)    Delivery tubes (142,144)    Slab panel (152)    Slot (154)    Post-processing unit (200)    Flow paths (220,230)
NOVELTY - The device has a big tooth (9) embedded on lower end face of furnace cover (17) and fixedly connected to bracket (5) which is fixedly connected to bottom of furnace (26). One end of ventilation pipe (96) is connected to a blower (39) and the other end is entered into ash house formed by bracket. A small tooth (8) is arranged under big tooth and supported by a pulley (32) arranged on bracket. One end side of small tooth is connected to pull rope (34) which is wound around the pulley and the other end side of small tooth is connected to reset spring (7) fixed on bracket.    USE - Household straw gasifying device for cooking agricultural product.    ADVANTAGE - The gas producing time can be prolonged, the gas producing speed can be accelerated and the gas yield can be increased such that the produced gas can be used repeatedly for long period of time. The secondary pollution resulting from the tar produced by household gasifier can be prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the household straw gasifying device.    Bracket (5)    Reset spring (7)    Small tooth (8)    Big tooth (9)    Furnace cover (17)    Furnace (26)    Pulley (32)    Pull rope (34)    Blower (39)    Ventilation pipe (96)
NOVELTY - Metal precursor containing solution is used for producing metal nanoparticle dispersed solution. The dispersed solution and an ionomer solution are mixed and a carbon support is immersed in the mixed solution to obtain metal-ionomer impregnated carbon complex as polyelectrolyte complex catalyst.    USE - Manufacture of polyelectrolyte complex catalyst used in catalyst ink and membrane electrode assembly for fuel cells (all claimed) e.g. polymer electrolyte fuel cell, phosphoric acid fuel cell, molten carbonate fuel cell and solid oxide fuel cell used as power supply for mobile devices and domestic applications.    ADVANTAGE - The polyelectrolyte complex catalyst enables to manufacture membrane electrode assembly having improved ion conductivity moisture resistance and durability.    DESCRIPTION OF DRAWING(S) - The drawing shows the flowchart of the manufacture of the polyelectrolyte complex catalyst. (Drawing includes non-English language text)
NOVELTY - The generator has an electrode unit arranged in electrolytic cell, to which current is supplied to electrolyze water for producing hydrogen/oxygen gas. The electrodes (110,120) arranged alternately are fixed to fixing unit. The rod-shaped portions (112,122) are formed in the electrodes. The hydrogen/oxygen gas filtered by filter, is collected by collection unit.    USE - Hydrogen/oxygen gas generator.    ADVANTAGE - The electrolysis efficiency can be improved and the hydrogen/oxygen gas can be generated reliably.    DESCRIPTION OF DRAWING(S) - The drawing shows an exploded perspective view of the electrode unit.    Electrodes (110,120)    Terminals of electrodes (110a,120a)    Edges of rod-shaped elements (111,121)    Rod-shaped portions (112,122)
NOVELTY - The gas generator has electrode unit that is provided with electrode boards (110,120) in which concave and convex portions (111,121) are formed. The spacers (130) are arranged between the electrode boards. The water is electrolyzed by applying current to the terminals (110a,120a) of the electrode boards, to generate hydrogen/oxygen gas. The generated gas is collected by a collection unit.    USE - Hydrogen/oxygen gas generator.    ADVANTAGE - The hydrogen/oxygen gas can be generated easily without mixing the propane gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the electrode unit.    Electrode boards (110,120)    Terminals (110a,120a)    Concave and convex portions (111,121)    Fitting hole (123)    Spacers (130)
NOVELTY - The generator has an electrode unit arranged in electrolytic cell, to which current is supplied to electrolyze water for producing hydrogen/oxygen gas. The electrode boards (110,120) are arranged alternately in the electrode unit. The spacers are arranged at equal intervals between the electrode boards. The hydrogen/oxygen gas filtered by filter, is collected by collection unit.    USE - Hydrogen/oxygen gas generator.    ADVANTAGE - The electrolysis efficiency can be improved and the hydrogen/oxygen gas can be generated reliably without mixing propane gas.    DESCRIPTION OF DRAWING(S) - The drawing shows an exploded perspective view of the electrode unit.    Electrode boards (110,120)    Terminals of electrode boards (110a,120a)    Fixing rod (135)
NOVELTY - The generator has electrolytic cell with electrode unit to which direct current is supplied for electrolyzing water and producing hydrogen and oxygen gases. A frame (130) includes several grooves for accommodating the terminals (110a,120a) of first and second electrodes (110,120). A mixed gas separation filter arranged above the frame, separates the produced hydrogen and oxygen gases. A collecting unit arranged above the mixed gas separation filter, collects the hydrogen and oxygen gases from the mixed gas separation filter.    USE - Hydrogen-oxygen mixed gas generator.    ADVANTAGE - The hydrogen and oxygen gases can be classified easily, and electrolysis efficiency of electrode unit can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the frame with electrodes.    Electrodes (110,120)    Terminals (110a,120a)    Frame (130)
NOVELTY - Identifier composition contains fluorane compound (1).    USE - Composition is used for identifying oil products for e.g. gasoline, light oil, heavy oil, kerosene, biodiesel, bioethanol, organic solvent, toluene and benzene (all claimed).    ADVANTAGE - The composition visually identifies oil products conveniently and easily.    DETAILED DESCRIPTION - Identifier composition contains fluorane compound of formula (1).    R1-R4=H or 1-6C linear alkyl.
NOVELTY - A pipeline diverter comprises pipe arrangement (31) including inlet (32), and at least first and second outlets (34, 36) with axes; and selection sleeve (64) moveable between at least first and second sleeve positions. The outlet axes diverge degrees from inlet axis and from each other. The outlets have upstream end portions with gaps in adjacent sides that are closest to the inlet axis. The selection sleeve has pipe part directing flow between inlet and first outlet, and blocker part (84) blocking flow between inlet and second outlet.    USE - Pipeline diverter for diverting pig and/or fluid.    ADVANTAGE - The diverter has minimal weight and size (while still being constructed of a given high strength material such as steel). The passage formed by flow part of selection sleeve, has a bulge on a side opposite axis of curvature of flow part. The bulge allows elongated pig to more easily move along curved path between inlet and one of the outlets.    DESCRIPTION OF DRAWING(S) - The drawing is a sectional view showing a diverter.    Pipe arrangement (31)    Inlet (32)    Outlets (34, 36)    Selection sleeve (64)    Blocker part (84)
NOVELTY - A light source (7) positioned at one end portion (6b) of measurement cell (6) emits the infrared rays to the infrared sensor positioned at other end portion (6c) of measurement cell. The internal peripheral surface (6d) of the cell is polished with pure aluminum.    USE - Gas cell for gas sample chamber in gas concentration measuring apparatus (both claimed). Uses include but are not limited to measurement of concentration of gases such as carbon monoxide, carbon dioxide, water vapor, nitrogen oxide gas, sulfur oxide gas, hydrogen sulfide gas, ozone gas, methane gas and nitric oxide gas.    ADVANTAGE - The deterioration of gas concentration measurement accuracy is prevented efficiently, as the irregular infrared reflection in the internal peripheral surface of gas cell is prevented.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) gas sample chamber; and    (2) gas concentration measuring apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the structure of gas sample chamber. (Drawing includes non-English language text)    Gas concentration measuring apparatus (1)    Gas sample chamber (2)    Gas cell (6)    End portions of gas cell (6b,6c)    Internal peripheral surface of gas cell (6d)    Light source (7)
NOVELTY - A biofuel comprises dried combustible materials comprising crop straws, ruderal, tree barks, branches, and sawdust; where it is prepared by crushing the dried combustible materials into granules with grain diameter of 1-5 cm; adding water having weight that is 15-25% of that of the dried combustible materials, and cured adhesive powder having weight that is 0-0.5% of that of the dried combustible materials, and uniformly mixing; keeping still for 48-72 hours under coverage condition; and pressing the obtained product as a cake block at 130-160 degrees C and under 8 tons of pressure.    USE - The biofuel is useful for industrial and commercial applications.    ADVANTAGE - The biofuel effectively improves the combustion rate of the combustible materials; where the combustion utilization ratio can be more than 40%. Moreover, the discharging concentrations of components comprising carbon monoxide, carbon dioxide, and sulfur dioxide in smoke gas meet the requirement of the national environment protection.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a preparation method of the biofuel.
NOVELTY - A container (7) is filled with an adsorption agent consisting of silver support zeolite. The raw fuel is supplied to the container containing the adsorption agent consisting of silver support zeolite for adsorbing the odorization agent.    USE - Apparatus for removing odorization agent containing mercaptans, sulfido, thiophenes and cyclohexene in raw fuel for production of hydrogen fuel of fuel cell e.g. polymer electrolyte fuel cell and solid oxide fuel cell (both claimed).    ADVANTAGE - The odorization agent is removed effectively, so that the deposition of carbon on the surface of modification catalyst of water vapor modifier is prevented. The decline in the hydrogen production efficiency can be prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the test apparatus for removing odorization agent in raw fuel. (Drawing includes non-English language text)    Town-gas pipe (1)    Cyclohexene standard gas pipe (2)    Container (7)    Exit-side pipe (8)    Shut-off valves (V1-V7)
NOVELTY - Process for the preparation of a composition of alcoholic ester of 6-26C linear monocarboxylic acid and glycerin comprises reacting vegetable or animal fatty body with 1-8C aliphatic monoalcohol in the presence of at least one heterogeneous catalyst based on solid mesostructured silica containing zinc.    USE - The process is useful for the preparation of the composition of the alcoholic ester of 6-26C linear monocarboxylic acid, and glycerin, where the fatty ester is useful in many application including diesel fuel, household fuels, ecological solvents, a base compound for the fabrication of sulfonates of fatty alcohol, amides, and dimers of ester.    ADVANTAGE - The process is simple and economical to produce the composition of 6-26C linear monocarboxylic acid alcoholic ester and glycerin with high purity and high yield. The process is carried out without environmental pollution, hence the process is eco-friendly. The catalyst used in the process is stable and recyclable.
NOVELTY - Isolated or purified polypeptide having an improved beta-glucosidase activity compared to the beta-glucosidase activity of wild BGL1 protein (SEQ ID NO: 2), comprising amino acids sequence in which at least one amino acid is altered compared to the amino acid sequence having SEQ ID NO: 2, where the altered amino acid is present in the positions of 225, 238, 240 and 241 of the amino acid sequence of SEQ ID NO: 2, is new, (where SEQ ID NO. 2 is not defined).    USE - The polypeptide is useful for the hydrolysis of cellobiose into glucose; and for the production of biofuel (all claimed), where the biofuel includes ethanol, butanol or isopropanol.    ADVANTAGE - The polypeptide has improved beta-glucosidase activity compared to the beta-glucosidase activity of wild BGL1 protein (SEQ ID NO: 2). The polypeptide is obtained from the natural raw material, and cost-effective for the production of the biofuel.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) an isolated or purified nucleic acid, which encodes the polypeptide;    (2) a vector comprising the nucleic acid;    (3) an isolated host cell comprising the polypeptide, the nucleic acids or the vector;    (4) an enzymatic composition acting on lignocellulosic biomass, where the enzymatic composition is produced by filamentous fungi including the polypeptide; and    (5) a process for the production of biofuel from the biomass, comprising placing the biomass in suspension in aqueous phase to hydrolyze, adding the enzymatic composition acting on the lignocellulosic biomass to start the hydrolysis, determining the released sugars, separating the sugar solution from the non-hydrolyzed solid fraction, fermenting the sugar solution, and separating the biofuel from fermentation wort.
NOVELTY - Carbon fiber electrode is immersed in an electrolyte solution as anode (17) or cathode (21), direct flow voltage is applied to two poles and electrolysis is carried out. The carbon fiber electrode is made of aggregate of fine and long carbon fibers. The carbon fiber is polyacrylonitrile type carbon fiber or pitch-based carbon fiber. The carbon fiber electrode has flexibility.    USE - Electrolysis for manufacturing sodium hydroxide, hydrogen and chlorine from sodium chloride aqueous solution and water, and manufacturing hydrogen from seawater or water (all claimed).    ADVANTAGE - Sodium hydroxide is manufactured with high productivity using carbon fiber electrode having excellent flexibility.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) electrolysis apparatus; and    (2) manufacture of hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of apparatus used for manufacturing sodium hydroxide.    Anode chamber (16)    Anode (17)    Cathode chamber (18)    Cation exchange membrane (19)    Cathode (21)
NOVELTY - A stirring mechanism (40) stirs the excretion with the micro-organism growth promoting base material accommodated in the digester (20). A heater heats the micro-organism growth promoting base material. A moisture sensor detects moisture content of micro-organism growth promoting base material. A controller (60) controls heating mechanism to maintain the moisture content of micro-organism growth promoting base material in reserve operation mode, and to reduce the moisture content in dehumidification operation mode, based on the detected moisture content.    USE - Toilet provided with digester.    ADVANTAGE - Moisture content of the micro-organism growth promoting base material can be controlled exactly and digester performance can be improved. Hence, easier-to-use toilet can be provided with digester.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the toilet provided with digester.    Door (14)    Digester (20)    Feed water tank (32)    Stirring mechanism (40)    Controller (60)
NOVELTY - To-be-processed water is processed in methane fermentation tank using acid producing microbe, methane producer and denitrifying bacteria by upward flow anaerobic sludge processing system. Ammonia nitrogen in to-be-processed water flowing in methane fermentation tank is nitrified to nitrite nitrogen using nitrifying bacteria. A portion of to-be-processed water of nitrification tank is circulated, returned to methane fermentation tank and reacted under condition at which nitrification is suppressed.    USE - Processing of nitrogen-containing organic wastewater e.g. foodstuff-processed wastewater, industrial wastewater and livestock farming wastewater.    ADVANTAGE - The nitrogen-containing organic wastewater is efficiently and stably processed at high chemical oxygen demand removal rate and nitrogen removal rate.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view illustrating wastewater treatment method. (Drawing includes non-English language text)
NOVELTY - A characteristic change switching material consists of polymer metal complex having structural unit (i) containing bivalent cation and 1,4-bis(4-pyridyl)benzene.    USE - Characteristic change type switching material used as recording material and adsorbing material. Can also be used as magnetic material, gas occlusion material, sensor and catalyst.    ADVANTAGE - The characteristic of the switching material changed after applying predetermined gas does not return to the original characteristic before the application of gas, even if the application of gas is stopped.    DETAILED DESCRIPTION - A characteristic change switching material consists of polymer metal complex having structural unit of formula: (XY'2L2)n (i).    X=bivalent cation chosen from cobalt, nickel and copper;    Y'=counter ion containing 1 or more fluoro;and    L=1,4-bis(4-pyridyl)benzene.    An INDEPENDENT CLAIM is included for switching method of characteristics change type switching material, which involves changing from gate type polymer complex to I-type polymer complex using switching gas and converting the I-type complex to gate type complex by contact with hydroxyl-containing low molecular substance.
NOVELTY - To-be-processed water is subjected to ozone treatment by supplying ozone, and ozone injection ratio is controlled to predetermined range. The ozone-treated to-be-processed water is subjected to biological treatment, and organic material is decomposed using microorganism with respect to to-be-processed water. A circulation process is carried out between ozone treatment and biological treatment, during which the biological-treated water is circulated to ozone treatment. Thus, water-treatment method is carried out.    USE - Method for treating wastewater e.g. sewage secondary-treatment water, final disposal-site leachate, river water, underground water, lakes, marshes, industrial wastewater, agricultural effluent and refuse disposal wastewater.    ADVANTAGE - The method safely and economically provides stable and high-quality treated water having improved transparency, and effectively suppresses generation of hypochlorous acid.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for water treatment system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of water treatment system. (Drawing includes non-English language text)    Ozone treatment tank (1a)    Biological treatment tank (2)    Sand filter (3)    Dissolved ozone concentration measurement portion (4a1,4b1)    Waste ozone gas concentration measurement portion (4a2,4b2)
NOVELTY - The experimental device has a gas collecting unit that collects gas produced in an anode chamber (1) and a cathode chamber (2) via draining and gas-collecting method. The cathode chamber and anode chamber are made of organic glass and a feeding and are connected with sampling pipe (9) and a gas outlet (15) via a rubber stopper (8). An electro-chemical working station unit (7) provides an electrolytic power to the anode chamber and cathode chamber via the electrode wire.    USE - Experimental device for producing hydrogen by fermentation with help of electrolysis.    ADVANTAGE - Provides a material of the device that is convenient to obtain and low cost. Enables convenient regulation and recording of the parameter regulation and reaction effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a diagram of an experimental device for producing hydrogen by fermentation with help of electrolysis.    Anode chamber (1)    Cathode chamber (2)    Electro-chemical working station unit (7)    Rubber stopper (8)    Sampling pipe (9)    Gas outlet (15)
NOVELTY - A biomass gasification furnace has upper furnace grid (11) comprising of more than two stirring rods (5), evenly distributed on top face surface, with stirring rod having length ranging from 4 to 15 centimeters. The upper furnace grid has longitudinal driving shaft (14) in middle part which extends to lower part of lower furnace grid (12), with the outer extending end connected to bevel gear (13) which is joggled to shaft end of level driving shaft (18) receiving rotational force from speed motor (1).    USE - Biomass gasification furnace.    ADVANTAGE - Provides a furnace having simple structure, low maintenance and convenient to use.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the furnace.    Speed motor (1)    Stirring rods (5)    Upper furnace grid (11)    Lower furnace grid (12)    Bevel gear (13)    Longitudinal driving shaft (14)    Level driving shaft (18)
NOVELTY - Constant temperature fostering slot for earthworm dung fermented feed comprises slot body, slot cap, the inside of the slot body downside set the filter net, the slot bottom set the insulated electric heat wire, the insulated electric heat wire is connected with the temperature control meter through the lead.    USE - The constant temperature fostering slot is useful for earthworm dung fermented feed (claimed).    ADVANTAGE - The device has cheap cost, equal heat temperature, automatic temperature control, and safe.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the constant temperature fostering slot.
NOVELTY - The liquid is filled in a container. A drain port is provided at lower portion of the container. An admitting port is provided in the middle portion of the container. A vent is formed in the upper portion of the container and is connected with a furnace head through an air scoop. A tar purifying device is provided in the container.    USE - Inflamer for straw gasification stove used in domestic field.    ADVANTAGE - The tar is removed from the gas using the tar purifying device. The structure of the inflamer is simplified. The cost of the inflamer is reduced. The purification effect of the tar purifying device is improved. The gas burning effect is improved. The time required for cleaning the furnace head is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the inflamer.
NOVELTY - Biological fuel oil preparation involves adding 30-95 wt.% of methanol or ethanol, 0-3 wt.% of catalyst, biomass mixture and plastic into a reaction device. The biomass mixture is crushed to 20-100 meshes. The raw materials in the reaction device are agitated uniformly, and temperature is maintained at 250-350 degrees C, and pressure is maintained at 8-18 megapascal, for 0.5-6 hour. The reaction device is cooled to room temperature and normal pressure is attained, on completion of the reaction. The obtained fuel is filtered using solid-liquid separation to obtain liquid biological fuel oil.    USE - Method for preparing biological fuel oil for use as fuel in car engine.
NOVELTY - A hearth (12) is provided with a combustion supporting system. Several reaction chambers are provided in furnace (1). The hearth has a grate groove and oxygen amount controlling fan (10). The grate is mounted in the grate groove. The grate comprises fixed grate portion and movable grate portion. A scraping plate (13) is provided in upper portion of grate and connected to movable grate. A push rod (4) is arranged under the hearth. The push rod has ends that are connected to push device (23) and furnace respectively.    USE - High-temperature dry distiller for processing tobacco wastes.    ADVANTAGE - The energy consumption of dry distiller is improved. The tobacco wastes can be processed and reused efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the high-temperature dry distiller.    Furnace (1)    Push rod (4)    Oxygen amount controlling fan (10)    Hearth (12)    Scraping plate (13)    Push device (23)
NOVELTY - Methanol gasoline is prepared by using 70-88 vol.% of gasoline, 5-15 vol.% of methanol, 2-5 vol.% of diethylamine, 2-5 vol.% of toluene, 1-5 vol.% of polysorbate 80 and 2-5 vol.% of sodium dodecyl sulfate. Polysobate 80 and sodium dodecyl sulfate are mixed to obtain mixed solution. Methanol, diethylamine and toluene are put into a high-frequency electromagnetic processor for 1-2 hours for magnetization. The magnetized solution and mixed solution are mixed and stirred uniformly to obtain the desired product.    USE - Methanol gasoline.    ADVANTAGE - The methanol gasoline ensures high and long term stability without formation of layers.
NOVELTY - Methane purification involves collecting produced methane. Methane is treated with water to remove solid impurity and is washed with calcium hydroxide for neutralizing and removing the acidic material such as sulfuretted hydrogen and carbon dioxide. Neutralized waste liquid is discharged through liquid discharging pipe. The obtained methane is dried by using a drier and is drained into a gas storing cylinder by using a compressor. The liquid discharging pipe is connected to a carbonization tower to create waste liquid flow into the inner part of carbonization tower.    USE - Method for purifying methane (claimed).    ADVANTAGE - The methane purification method enables to purify methane completely and improve overall efficiency, and ensures recovery of washed waste caustic liquid material, and is easily promoted and applied for beneficial economy.    DETAILED DESCRIPTION - Methane purification involves collecting produced methane. Methane is treated with water to remove solid impurity and is washed with calcium hydroxide for neutralizing and removing the acidic material such as sulfuretted hydrogen and carbon dioxide. Neutralized waste liquid is discharged through liquid discharging pipe. The obtained methane is dried by using a drier and is drained into a gas storing cylinder by using a compressor. The liquid discharging pipe is connected to a carbonization tower to create waste liquid flow into the inner part of carbonization tower. The waste liquid inside the carbonization tower is able to access carbon dioxide into it for making redundant calcium hydroxide. The deposited mixture fluid is pumped into a dehydration pool for dehydrating the mixture. The dehydrated and dried mixture is packed as prepared chemical or industrial chemical.
NOVELTY - Improving oxidation stability of Jatropha curcas oil and mixed fuel diesel comprises adding n-propyl gallate or coking gallic acid to Jatropha curcas oil or fuel diesel obtained by mixing Jatropha curcas oil and petroleum diesel; where the total addition amount is 100-2000 mg/kg; the fuel diesel is prepared by mixing Jatropha curcas oil and petroleum diesel; and the volume concentration of Jatropha curcas oil to petroleum diesel is 5-9.9%.    USE - The process is useful for improving oxidation stability of Jatropha curcas oil and mixed fuel diesel (claimed).    ADVANTAGE - In the process of improving oxidation stability of Jatropha curcas oil and mixed fuel diesel, the additive has antioxidant function; where it cannot product free radical and deposit; and it is good for popularizing biodiesel.
NOVELTY - The boiler has water storage sleeve (17) set between an inner furnace structure (19) and an outer furnace structure (16). A water inlet pipe base and a steam outlet are provided in the water storage sleeve. A chain stoker (20) set in a lower portion of the inner furnace structure, is provided with a ventilating pipe (9) at a bottom portion. The steam outlet of the water storage sleeve is connected with the ventilating pipe. A ventilating equipment is respectively connected with a ring venting ring and the ventilating pipe.    USE - Biomass gas-producing boiler.    ADVANTAGE - The burnable gas can be burned directly while decreasing emission of heat, and the gas production can be enabled in a secure manner without the need for anti-explosion door. The boiler can be operated conveniently, and can be assembled at low cost. The boiler configuration can be modified suitably, and an effective utilization of heat can be realized.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the biomass gas-producing boiler.    Ventilating pipe (9)    Outer furnace structure (16)    Water storage sleeve (17)    Inner furnace structure (19)    Chain stoker (20)
NOVELTY - A fuel gas outlet pipe (3) is connected to upper outer wall. The middle lower furnace wall on the outer enclosure of furnace (1) is welded with wind inlet sleeve tube (10), and the corresponding furnace wall is welded with bulkhead sleeve tube (6). An air nozzle (8) is inserted in the wind inlet sleeve tube and the bulkhead sleeve tube. A screw (9) is meshed in wind inlet sleeve tube outside the furnace. The narrow gap of air nozzle tube wall stretched out of wind inlet sleeve tube is inserted with wind adjusting plate (5).    USE - Movable air nozzle structure of biomass gasifier.    ADVANTAGE - The generated product blocking the air inlet pipe can be prevented, thus the structure can be maintained efficiently. The gasifier can be operated efficiently, using a simple structure.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of movable air nozzle structure.    Furnace (1)    Fuel gas outlet pipe (3)    Wind adjusting plate (5)    Bulkhead sleeve tube (6)    Air nozzle (8)    Screw (9)    Wind inlet sleeve tube (10)
NOVELTY - The stove has stove core (5) that is provided with stove sleeve (1) which is filled with milling straw. A lower stove chamber is provided with ring slot, and is connected with wind sending port. A material feeding machine (2) is hinged and fixed at lower stove chamber through central axis. An inner chamber provided at upper side of stove is connected with filter inlet, and inner chamber provided at lower side of stove is installed with stove filter (6).    USE - Gasification stove e.g. straw gasification stove.    ADVANTAGE - The tar block produced in stove can be eliminated since the inner chamber provided at lower side of stove is installed with stove filter.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the gasification stove.    Stove sleeve (1)    Material feeding machine (2)    Stove core (5)    Stove filter (6)    Wind supplying port (7)
NOVELTY - The device has a group of open circle field yoke (6) installed on a frame (5). A permanent magnet (7) is provided in a jaw opening of the field yoke. The frame is provided with an oblate post supporting part and a coaxial round pipe. A screw hole is formed in the oblate post supporting part. An oxygen rich channel is provided at two ends of the frame. Axes (13) of the field yoke is connected with an oxygen rich channel that is connected with an oxidant inlet of a battery in a generating system of a fuel cell.    USE - Oxygen collecting device for a solid oxide fuel cell in a high gradient magnetic field.    ADVANTAGE - The device has simple structure and low cost, and increases generating efficiency of the fuel cell. The device saves energy, and reduces noise.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of an oxygen collecting device.    Frame (5)    Open circle field yoke (6)    Permanent magnet (7)    Axes (13)    Oxygen rich inlet (17)
NOVELTY - A ring-shaped sink portion (5) is provided on top of outer cylinder (2). A cover (6) is covered on the sink portion. An air outlet (7) is provided on upper portion of outer cylinder. A three-way pipeline (10) is connected to air outlet of outer cylinder. The ends of pipeline are connected to adjusting valve (11) and gas circulation chamber provided in outer wall of outer cylinder. A fuel gas outlet (12) is provided on top of gas circulation chamber.    USE - Vegetation powder gasification furnace.    ADVANTAGE - The gasification rate and operability of furnace are improved. The structure of gasification furnace is simplified. The energy consumption of furnace can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of the gasification furnace.    Outer cylinder (2)    Sink portion (5)    Cover (6)    Air outlet (7)    Three-way pipeline (10)    Adjusting valve (11)    Fuel gas outlet (12)
NOVELTY - The advanced treatment and recycling device has a lift pump (11) that is provided in a water collection tank (1). An air blower (12) is connected to an auxiliary tank (6). A back washing pump (14) has an inlet joined to a water storage tank (8), and an outlet joined to the auxiliary tank. A booster pump (13) is provided in a pipeline between the water storage tank and a filter (9). A settling tank (4) has an outlet joined to a sludge tank (10).    USE - Advanced treatment and recycling device for pulping and papermaking wastewater.    ADVANTAGE - Provides device that is featured with scientific design, high automation, advanced technical process, excellent effect, and low treatment cost. Eliminates increase the salt content of wastewater.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic block diagram of the advanced treatment and recycling device.    Water collection tank (1)    Settling tank (4)    Auxiliary tank (6)    Water storage tank (8)    Filter (9)    Sludge tank (10)    Lift pump (11)    Air blower (12)    Booster pump (13)    Back washing pump (14)
NOVELTY - The furnace has a gas taking pipe (4) fixed in a furnace body (9), where lower end of the gas taking pipe is passed through a grate (11) and an upper end is connected with a furnace cover (3). A secondary gas taking pipe (1) is mounted on an upper part of the furnace body. An upper end of an air inlet pipe (15) is equipped with an air outlet cover (10), which is equipped with multiple air outlets. An upper part of a furnace shell (6) is equipped with a sealing water chute (5). An ash baffle plate (2) is mounted in the furnace body fixed close to the secondary gas taking pipe.    USE - Straw gasification furnace.    ADVANTAGE - The furnace design ensures that fuel gas is entered through the lower end of the gas taking pipe and the tar in the fuel is gasified in the pipe in a convenient manner. The furnace has simple structure, low cost and easy washing.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a straw gasification furnace.    Secondary gas taking pipe (1)    Ash baffle plate (2)    Furnace cover (3)    Gas taking pipe (4)    Sealing water chute (5)    Furnace shell (6)    Furnace body (9)    Air outlet cover (10)    Grate (11)    Air inlet pipe (15)
NOVELTY - The furnace has an air inlet pipe (1) fixed in a lower part while an upper part is provided with an air outlet pipe (7). A liner (4) is installed in a shell drum (3), and a lower part of the liner is provided with a round hole. The shell drum is set in a range of 2-6 cm from the liner, where the liner is made of iron sheet, copper and refractory material (2).    USE - Environment-friendly and energy-saving biomass gasification furnace.    ADVANTAGE - The furnace reduces the pollution, increases the quality and speed of the gas production, activates the gas flow without blocking the pipeline, increases the heat efficiency and prolongs the service life so as to meet the requirements of production and living.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of an environment-friendly and energy-saving biomass gasification furnace.    Air inlet pipe (1)    Refractory material (2)    Shell drum (3)    Liner (4)    Air outlet pipe (7)
NOVELTY - The pipe has a tube body (1) whose upper part is provided with a porous pipe (2), where four sides of the porous pipe are provided with air blowing openings (5). The porous pipe is welded with an upper opening (6), where length of the porous pipe is set in a range of 12-28 centimeters. An end of the tube body is provided with a buckle cover (3) and other end is connected with an air blower (4), where the inlet pipe is made of ferric, copper and refractory materials.    USE - Air inlet pipe for an environment-friendly and energy-saving biomass gasification furnace.    ADVANTAGE - The pipe seals the oxygen air to manage through a hole blowing pipe of the air blower, and supplies oxygen rationally. The pipe can forcibly supply oxygen directly, so that the pipe can improve the produced gas quality, and has better stability. The pipe saves fuel, prevents empty cavity, and has less scale residue or no scale residue. The pipe does not block the circular hole, can be produced in mass and has large service life.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of an air inlet pipe for an environment-friendly and energy-saving biomass gasification furnace.    Tube body (1)    Porous pipe (2)    Buckle cover (3)    Air blower (4)    Air blowing openings (5)    Upper opening (6)
NOVELTY - The pipe has a pipe body (1) whose upper part is equipped with a blowing hole (2). An end of the pipe body is equipped with a buckle cover (3) and other end is equipped with a blast blower (4), where the pipe is made of iron, copper and flameproof materials.    USE - Air inlet pipe for an environment-friendly and energy-saving biomass gasification furnace.    ADVANTAGE - The blast blower blows the porous pipe to make oxygen to be sealed and rationally provided, so that the pipe forcibly and directly blows oxygen, enhances the quality of generated gas and has improved stability. The pipe saves fuel and prevents the generation of empty cavity. The pipe prevents residues, and does not block round holes. The pipe can be produced in mass, and has large service life.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of an air inlet pipe for an environment-friendly and energy-saving biomass gasification furnace .    Pipe body (1)    Blowing hole (2)    Buckle cover (3)    Blast blower (4)
NOVELTY - A biomass gas filtering tank (2) is connected between a double-layer combustion furnace section (5) and a double-layer gasification furnace section (3). An interlayer straw combustion tank (1) is mounted outside the combustion furnace section. The double-layer gasification furnace section is arranged with a combustible gas storage chamber (12). The biomass gas filtrating tank is connected to a fuel gas conduit (14) connected with a warming operation chamber (4) through the combustible gas storage chamber to connect with a flame nozzle (13) of a heater.    USE - Dual-purpose straw gasification furnace.    ADVANTAGE - The straw gasification furnace can be simply operated and conveniently utilized. The external appearance of the furnace can be enhanced at low cost, while achieving energy saving and environmental protection functions, and maximizing the smoke exhaust.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the straw gasification furnace.    Interlayer straw combustion tank (1)    Biomass gas filtering tank (2)    Double-layer gasification furnace section (3)    Warming operation chamber (4)    Double-layer combustion furnace section (5)    Combustible gas storage chamber (12)    Flame nozzle (13)    Fuel gas conduit (14)
NOVELTY - The boiler has a boiler body provided with a feed port (4) correspondingly to a cavity, and a dust outlet (5) connected with the cavity and opened below the boiler body. One side of the boiler body is provided with a fire outlet (6) connected with the cavity. A hot air connection port (7) and a hot air water return port (8) are arranged on the boiler body. The boiler body is installed with a ventilation pipe connected with the cavity, and an air cap is installed on the ventilation pipe. The fire outlet is installed with a baffle plate.    USE - Biomass gasification boiler for use in an indoor area of a house in a rural area.    ADVANTAGE - The boiler has less smell, high cleanness and sanitation.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a biomass gasification boiler.    Feed port (4)    Dust outlet (5)    Fire outlet (6)    Hot air connection port (7)    Hot air water return port (8)
NOVELTY - The gasifier has a furnace cover water seal (2) fixed at a furnace cover (1). A gas distributor (7) with an air hole located above an air outlet of a blasting device (9) is fixed at middle of a furnace bottom (6). An ignition hole (4) close to the gas distributor is arranged in a furnace body. A connection pipeline is composed of a gas output tube (14) and an emptying tube (13), a water-gas separator (17) and an oxygenation tube (10) that communicates with the gas output tube. A section of water seal elbow (15) is set on the water-gas separator.    USE - Energy-saving gasifier for use in an underdeveloped village and a mountain area.    ADVANTAGE - The gasifier is simple in structure, easy to ignite, high in thermal efficiency and low in production cost, and can use firewood, grass, sawdust, crop wastes for generating combustible gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an energy-saving gasifier.    Furnace cover (1)    Furnace cover water seal (2)    Ignition hole (4)    Furnace bottom (6)    Gas distributor (7)    Blasting device (9)    Oxygenation tube (10)    Emptying tube (13)    Gas output tube (14)    Water seal elbow (15)    Water-gas separator (17)
NOVELTY - A nitrogen-containing heterocyclic compound (1) is new.    USE - Novel nitrogen-containing heterocyclic compound is used as germicide in agriculture and horticulture (claimed) for preventing or controlling various plant diseases caused by fungi. Uses include but not limited to brown leaf spot, sclerotic disease, seedling damping off, powdery mildew, leaf mildew, early blight, red spot disease, club root, scab, grey rot disease, canker, disease caused by Botrytis cinerea and downy mildew in sugar beet peanut, cucumber, onion, cabbage, kidney bean, apple and wheat.    ADVANTAGE - The nitrogen-containing heterocyclic compound is highly safe as it causes no toxicity, and environment-friendly, and enables reliable control of plant diseases without causing drug induced damage.    DETAILED DESCRIPTION - A nitrogen-containing heterocyclic compound of formula (1) or its salt is new.    X=1-12C alkyl, 2-12C alkenyl, 2-12C alkynyl, 3-12C cycloalkyl, 4-12C cycloalkenyl, 8-12C cycloalkynyl, heterocyclic group, 1-12C acyl, (1-imino)1-12C alkyl, hydroxyl, amino, mercapto or sulfonyl (all optionally substituted), halo, cyano or nitro;    X on adjacent carbon atoms=optionally substituted 5-8 membered ring;    m=0-6;    R=1-12C alkyl, 2-12C alkenyl, 2-12C alkynyl, 3-12C cycloalkyl, 4-12C cycloalkenyl, 8-12C cycloalkynyl, 2-12C aryl, heterocyclic group, 1-12C acyl or sulfonyl (all optionally substituted);    Q=6-12C aryl or heterocyclic group (both optionally substituted);    A=carbon, nitrogen, oxygen, or sulfur;    n=1 or 2;and    doublet of continuous line and dotted line=single bond or double bond.
NOVELTY - Biodiesel purification involves obtaining glycerin by transesterification reaction of rapeseed oil from castor seeds and using ethanol and an alkaline catalyst for separating the obtained glycerin. Excess ethanol is removed from the ester mixture by evaporation, which contains 60-80% of alkyl esters, 5-15% of glycerin and 15-30% of ethanol. 2-5% of n-hexane is added to the mixture and is stirred. The mixture is transferred to a homogeneous glass vessel fitted with electrodes and is contacted with an inventory of the glycerin settling vessel in a ratio of 10:1-5:1 by volume.    USE - Method for purifying biodiesel.    ADVANTAGE - The biodiesel purification effectively separates the glycerin fraction formed during transesterification of a mixture of long-chain triglycerides from castor oil in short time.    DETAILED DESCRIPTION - Biodiesel purification involves obtaining glycerin by transesterification reaction of rapeseed oil from castor seeds and using ethanol and an alkaline catalyst for separating the obtained glycerin. Excess ethanol is removed from the ester mixture by evaporation, which contains 60-80% of alkyl esters, 5-15% of glycerin and 15-30% of ethanol. 2-5% of n-hexane is added to the mixture and is stirred. The mixture is transferred to a homogeneous glass vessel fitted with electrodes and is contacted with an inventory of the glycerin settling vessel in a ratio of 10:1-5:1 by volume. An electrical current is alternately applied to the solution by applying an electric field of high voltage by using voltage converters in a range of 1-5 kilovolts by electroseparation technique. 5-15 vol.% of ethanol mixed esters are also removed and a temperature of 90 degrees C is maintained by using a heating bath for the mixture.
NOVELTY - The furnace has a furnace bar arranged in a furnace body, and ash chamber placed below the body. An ash discharging pore is arranged along connection edge part of the furnace bar and an inner wall of the body. The furnace bar is equipped with an ash poking mechanism that is utilized for poking lime-ash in the furnace bar into the ash discharging pore. The ash poking mechanism is linked with an ash poking driving mechanism that is arranged in a cylinder-shaped shield below the furnace bar, and a surface of the furnace bar is coated with a heat insulating material.    USE - Biomass gasification furnace.    ADVANTAGE - The furnace utilizes the ash poking driving mechanism to drive the ash poking mechanism, so that the lime-ash in the furnace bar is continuously discharged. The furnace is better for chemical reaction of biomass raw material, so that the working efficiency of the furnace is improved. The furnace avoids the leakage of materials of the furnace bar. The shield below the furnace bar protects the ash poking driving mechanism.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass gasification furnace in partial section.
NOVELTY - Composted manure preparing apparatus has ventilation floor (1) equipped with channel (3) formed in the floor surface (2), drain tank, through-holes formed in the floor surface, cover (4) which covers the channel and is equipped with the through-hole, and cavity portion (5) formed from the channel and cover, where the drain tank connects with the channel, the through-hole is a vent-hole and waste-water port, and the cavity portion formed from the channel and cover is an air flow passage and drainage channel.    USE - The composted manure preparing apparatus is useful for preparing composted manure (claimed) from livestock excretion. The prepared composted manure is useful as fertilizer.    ADVANTAGE - The composted manure preparing apparatus is convenient to use.    DETAILED DESCRIPTION - Composted manure preparing apparatus has (a) ventilation floor equipped with channel formed in the floor surface, drain tank, through-holes formed in the floor surface, cover which covers the channel and is equipped with the through-hole, and cavity portion formed from the channel and cover, where the drain tank connects with the channel, the through-hole is a vent-hole and waste-water port, and the cavity portion formed from the channel and cover is an air flow passage and drainage channel, or (b) the ventilation floor provided with the pipe in which ventilation and drainage are possible, the drain tank, the pipe which is formed from the groove formed in the floor surface of the ventilation floor, the cover which covers the channel and is equipped with a through-hole, and the channel connected with the drain tank.    DESCRIPTION OF DRAWING(S) - The drawing shows sectional view of composted manure preparing apparatus.    Ventilation floor (1)    Floor surface (2)    Channel (3)    Cover (4)    Cavity portion (5)
NOVELTY - The modular trickling filter bioreactor includes unit modules (1) which are mutually superposed in a longitudinal direction to form an integral reactor main body. Each unit module is filled with fillers and includes at least one tank. Openings are formed in the side wall and bottom wall of each unit module. A water distribution device is arranged above the uppermost unit module of the reactor main body.    USE - Modular trickling filter bioreactor for treating sewage.    ADVANTAGE - Can be flexibly assembled and expanded according to the amount of sewage to be treated by using a unit module combining structure. Reduces cost, improves treatment capability, and ensures convenient construction and maintenance.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of modular trickling filter bioreactor.    Unit modules (1)
NOVELTY - Zinc nitrate hexahydrate and terephthalic acid are dissolved in solvent (I), and ultrasonic wave is irradiated to the solution and agitated to obtain metal organic source structure (MOF-5) particles. Then, particles are cooled to room temperature, further dissolved in solvent (I), and ultrasonic wave is irradiated to the solution. Then, resulting particles are re-washed using solvent (II) and dried to obtain metal organic source structure (MCF-5).    USE - Manufacture of metal organic source structure used for preservation or adsorption of micromolecules such as carbon dioxide, methane and hydrogen (claimed).    ADVANTAGE - The metal organic source structure is manufactured economically.
NOVELTY - Bioethanol production involves using Agavaceas family plants as raw materials. The Agavaceas family plants contain carbohydrates, which are processed by fermentation, distillation and dehydration to obtain ethanol. Dehydrating membranes are added to the process to balance the energy.    USE - Method for producing bioethanol for use as biofuel or gasoline additive.