NOVELTY - Gas quality determination involves measuring optical absorption of methane and carbon dioxide, and thermal conductivity (lambda) of the sample gas. The optical absorption of liquefied petroleum gas (LPG) is measured from the absorption of the mole fraction of methane and carbon dioxide by addition of liquefied petroleum gas. The mole fraction of LPG is determined using mole fraction of methane and carbon dioxide and thermal conductivity by the addition of liquefied petroleum gas.    USE - Method for determining the quality of gas, particularly biogas or processed biogas sample having methane, carbon dioxide, nitrogen, oxygen and hydrogen by using infrared spectroscopic measurement.    ADVANTAGE - The gas quality determination method enables to determine the quality of gas, particularly biogas or processed biogas sample without adding other existing gas such as hydrogen or other admixtures such as oxygen quickly in a simple manner.    DETAILED DESCRIPTION - Gas quality determination involves measuring optical absorption of methane and carbon dioxide, and thermal conductivity (lambda) of the sample gas. The optical absorption of liquefied petroleum gas (LPG) is measured from the absorption of the mole fraction of methane and carbon dioxide by addition of liquefied petroleum gas. The mole fraction of LPG is determined using mole fraction of methane and carbon dioxide and thermal conductivity by the addition of liquefied petroleum gas. The optically non-detected mole fractions of nitrogen, oxygen and hydrogen are also determined by using lambda by the addition of liquefied petroleum gas mole fraction. The characteristic parameters of the sample gas are calculated from the obtained mole fractions.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart depicting a method for solution by numerical iteration using non-linear approach. (Drawing includes non-English language text).
NOVELTY - Stirrer includes multiple rotary shafts (19a,19b,19c), multiple rotating blade assemblies, two driving sources (13,31) and two power transmission units (35,37,39), which are connected to the latter rotary shaft. The latter power transmission unit has a driving source and multiple hollow shafts. The multiple rotating blade assemblies are connected to a hollow shaft. Latter rotary shaft is arranged inside the former rotary shaft. The latter power transmission unit is arranged in the former power transmission unit.    USE - Stirrer for sludge drying facility.    ADVANTAGE - The stirrer increases microorganism activities and ensures improved productivity.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross sectional view of the stirrer.    Driving sources (13,31)    Rotary shafts (19a,19b,19c)    Power transmission units (35,37,39)    Power transmission gear (51)    Air discharge pipe (93)
NOVELTY - Proposed method relates to processing of loose wastes formed in wood processing and can be used for producing ecologically pure buofuels for industrial and communal services. Proposed method comprises grinding the material, processing it by superheated steam at 300 degrees C in filtration conditions, and subsequent pressing. Proposed method comprises measuring the finished product temperature and moisture content at the press unit outlet, comparing measurement results with rated magnitudes preset at microcontroller. Control signals from the latter are sent to actuating mechanisms to vary the rate of material feed in press die temperature control circuit, and to actuating mechanism that allows feeding superheated steam into the mixer included into moisture content control circuit.    USE - Process engineering.    ADVANTAGE - Reduced inflammability, optimum moisture content of finished products. 1 ex, 1 dwg
NOVELTY - Biodiesel production involves utilizing triglyceride and fatty acid, which are derived from animal fat, vegetable oil or their mixture. Three reaction steps are performed. Mixture of triglycerides and homogeneous acids is preserved. The preserved mixture is neutralized with acid catalyst. The obtained mixture is transesterified with an alkaline homogeneous catalyst.    USE - Method for producing biodiesel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an apparatus for producing biodiesel, which comprises a hermetic and improvable industrial reactor, an electronic control panel, an engine, a pair of submergible electric resistances, an outlet lower valve located at base portion of a tank, an alcohol condenser with a refrigerating liquid and a pressure regulator.
NOVELTY - Composition comprises Bacillus firmusCNCM I-1582 spore and one insect control agent or a fungicide.    USE - The composition is useful: for treating a plant; in seed treatment formulation; and as spray formulation for drench or in-furrow application (all claimed). The composition is useful for reducing crop losses caused by either plant parasitic nematodes or fungi. The composition shows insecticidal and acaricidal activity. The nematicidal activity of the composition was tested in soybeans. The result showed that the biological nematicide exhibited nematode control having less than half the percent difference at 23%.    ADVANTAGE - The composition is eco-friendly and exhibits synergistic effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of treating a plant comprising providing at least one composition comprising at least one spore-forming bacterium (0.0001-20 wt./wt.%) and at least one insect control agent (0.001-20 wt./wt.%) or at least one fungicide, and applying the composition to the plant.
NOVELTY - Coconut shell charcoal manufacturing involves obtaining coconut shell powder by pulverizing coconut shell containing lignin components and fiber. The obtained coconut shell powder is mixed with water. The obtained mixture is molded into desired shape. The molded product is dried and carbonized to obtain charcoal.    USE - Method for manufacturing coconut shell charcoal.    ADVANTAGE - The coconut shell charcoal manufacturing method provides high class microporous, eco-friendly and cost-effective charcoal having various shapes and high carbon content by utilizing only natural material including food waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a photograph of the coconut shell charcoal in perspective top view.
NOVELTY - The system includes utilizing hot gases for predrying wood to be carbonized, where heat radiation is provided to wood by using radiators.    USE - System for reduction of wood consumption and time duration of vegetal coal production process.    ADVANTAGE - The wood consumption and time duration reduction system decreases 40% of total time required for producing vegetal coal, optimizes the wood consumption in vegetal coal production process, increases 8% of production of vegetal coal in each cycle, reduces heat losses, and ensures automated and software-specific management and control of vegetal coal production process, and also ensures that less number of components are required in the wood consumption and time duration reduction system, hence enables an economical production of vegetal coal.
NOVELTY - A spherical polymer is synthesized and added to mixed solution. The mixed solution is mixed with titanium sulfate, and the obtained spherical titanium dioxide supporter is dipped into platinum, to obtain electrode catalyst.    USE - Manufacture of electrode catalyst for fuel cell (claimed). Uses include but are not limited to capacitor, phosphoric acid fuel cell, alkaline fuel cell, molten carbonate fuel cell, polymer electrolyte fuel cell, direct methanol fuel cell, ion exchange film fuel cell, solid oxide fuel cell and proton exchange membrane fuel cell.    ADVANTAGE - The method economically provides electrode catalyst having favorable performance, electrochemical characteristics, oxidation resistance and electric current density by simple process.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating the manufacture of electrode catalyst. (Drawing includes non-English language text).
NOVELTY - A fire log comprises a log made from wood, where the log having a length, a diameter, an upper surface and a base, the base having a top, the log having several cuts formed in the upper surface, the cuts extending downwardly along the length of the log and terminating at the top of the base.    USE - As a fire log selected from flammable campfire device (claimed).    ADVANTAGE - The device is easily ignitable, self-contained campfire can be produced from a single log. The log includes removable segment that enables the control of air flow to increase or decrease flame intensity. The log provides for improved elements in an arrangement for the purposes described that are inexpensive, dependable and fully effective in accomplishing their intended purposes.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for following:    (1) flammable campfire device comprising a wood log having a length, a diameter of at least nine inches, an upper surface and a base, the base having a top, the wood log having several diametrical cuts formed in the upper surface, the cuts extending downwardly along the length of the log and terminating at the top of the base, the cuts forming pie-shaped segments in the wood log; and    (2) making the flammable campfire device involving securing a wood log having a length between twenty-four and seventy-two inches, a top surface and a base, the base having a top; making diametrical cuts through the top surface downwardly along the length to the top of the base, to form pie-shaped segments in the log; making a horizontal cut to a lower end of one of the pie-shaped segments adjacent the top of the base; removing the horizontally cut pie-shaped segment, to expose an area at the top of the base; and adding a chemical to the log in the area at the top of the base.
NOVELTY - An apparatus (10) comprises a water vapor source for outputting water vapor; a plasma source (14) for outputting a plasma which impacts the water vapor and causes hydrogen within the water vapor to disassociate from oxygen; and a collection device collecting the hydrogen disassociate from the water vapor.    USE - Apparatus for the disassociation of hydrogen from water vapor (claimed).    ADVANTAGE - The apparatus is capable of dissociating water molecules into their constituent species.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of an apparatus for the disassociation of hydrogen from water vapor.    Apparatus (10)    Vacuum chamber (12)    Plasma source (14)    Mechanical pump (18)    Differential pump system (20)
NOVELTY - Producing a compound comprises incubating a culture medium with a Clostridium phytofermentans cell, where the cell has altered activity of at least one gene associated with sporulation as compared to the activity of the gene in a wild-type Clostridium phytofermentans strain, and where the altered activity enhances production of the compound; and isolating the compound from the culture medium.    USE - The methods are useful for producing compound; and for reducing sporulation in Clostridium phytofermentans cell (all claimed). Preferably, the methods are useful for producing fuel utilizing various strains of Clostridium phytofermentans with reduced sporulation activity; and for regulating sporulation.    ADVANTAGE - In the method above, the cell has altered activity of at least one gene associated with sporulation as compared to the activity of the gene in wild-type Clostridium phytofermentans strain, where the altered activity enhances production of the compound (claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are: (1) an isolated Clostridium phytofermentans cell comprising altered sporulation activity in comparison to a wild-type strain of Clostridium phytofermentans; (2) a method for reducing sporulation in Clostridium phytofermentans cell, comprising reducing the activity of a gene associated with sporulation; and (3) a fuel producing mixture comprising: an isolated Clostridium phytofermentans microorganism comprising an alteration of at least one gene associated with sporulation; and biomass.
NOVELTY - Device for the optimization during an aerobic fermentation process in a collecting tank for manure substrates, which are produced in agricultural livestock breeding, and/or in sedimentation tank for the treatment of sewage sludge, preferably industrial and domestic sewage sludge, by influencing the molecular structure using electric fields and electromagnetic fields for the generation of vibrational patterns, is claimed.    USE - The device is useful for preventing premature fermentation, putrefaction and/or fungal growth. The device is useful in food industries, preferably during the preparation of juices, spirituous beverages (e.g. beer, wine) and dairy products, chocolates, cheeses, yogurts and pastries.    ADVANTAGE - The device: produces an adjustable and controllable vibratory patterns; reduces gas emission; reduces odor; produces desired water quality in settling tanks.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of a collecting tank having plastic tube which acts as wire spool receiving tube for the wire spool system.    Powder cables (60)    Plastic cap (70)    Collecting tank fixture (80)    Wire spool receiving tube (110)    Tapped hole (130)
NOVELTY - The device (10) has a snail reactor (11) for drying and pyrolizing materials under air exclusion, and a reactor (15) in which partial oxidation is carried out for fragmentation of long-chained tar molecules by under-stoichiometric addition of air. The reactor is filled with pyrolysis coke, pyrolysis gas and water vapor under formation of pyrolysis coke pouring. The reactor is fillable with the coke developed in the snail reactor on the basis of a hauling device (16). A reactor wall has inlet openings for protecting against blockage of gas and/or outlet openings for passing gaseous fuel.    USE - Device for thermochemical transformation of biomass e.g. wood, sewage sludge, domestic waste and industrial waste (all claimed), into gaseous fuel.    ADVANTAGE - The inlet openings and the outlet openings are arranged in the reactor wall and protected from blockage, so that completely troublefree operation of the reactor is guaranteed, interference susceptibility of the biomass is reduced and the tar content in the gaseous fuel is reduced. The device is designed in such a manner that the mechanical defect and disturbances are avoided.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a device for thermochemical transformation of biomass.    Thermochemical transformation device (10)    Snail reactor (11)    Engine (12)    Reactor (15)    Hauling device (16)    Gas filter (17)
NOVELTY - Method for treating lake substrate sludge, involves (a) testing contamination index of the lake substrate sludge, (b) proportioning microbial inoculum in variety and quantity, (c) pouring the microbial inoculum complex into water at a ratio of 10-40 ppm, (d) transferring and transforming the complex microbial inoculum, and degrading the pollutants in the lake water, and (e) testing the contamination index of the substrate sludge, where the inoculum comprises photosynthetic bacterium, Bacillus subtilis, nitro-bacterium, Lactobacillus and microzyme.    USE - The method is useful for treating lake substrate sludge by reducing the pollutants in the sludge (claimed) and for converting organic substance into inorganic substance.
NOVELTY - A communication port (Q) extending from a gasket and the gasket are molded by injection molding to the membrane electrode assembly (MEA). The cell unit (CU) including the gasket is formed at the intermediate portion, and a separator (SP) is inserted between the cell units at the folding region of the communication port. The cell units inserted with the separator is stacked to from a cell stack (ST).    USE - Manufacturing method of fuel cell for electric vehicle. Can also be used in hybrid vehicle and domestic applications.    ADVANTAGE - The positioning of the separator can be performed simultaneously while folding the cell units, and the insulation of the fuel cell stack can be collateralized so that the lamination position of the cell units can be determined accurately with high precision and the manufacturing efficiency of the fuel cell can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of the laminated structure of the cell unit.    String material supply structure (60)    Cell unit (CU)    Expanded metal (EM)    Communication port (Q)    Separator (SP)    Cell stack (ST)
NOVELTY - A fuel cell system comprises modifier (12) which produces fuel gas containing hydrogen that modifies raw material fuel, combustor which burns combustion fuel and heats modifier, fuel cell (11) which produces electric power using fuel gas and oxidizing agent gas, residual fuel gas supply path which is connected to combustor from fuel gas exit of fuel cell, fuel supply path which supplies raw material fuel to modifier, and combustion fuel supply path connected to combustor which branches from fuel supply path.    USE - Fuel cell system.    ADVANTAGE - The fuel cell system implements supply of briefer and efficient raw material and combustion gas, achieves lifetime improvement of desulfurizer by preventing performance degradation of desulfurizer, and improves electric power generation efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the fuel cell system. (Drawing includes non-English language text).    Fuel cell (11)    Modifier (12)    Carbon monoxide removal device (13)    Fuel gas generator (14)    Burner (15)
NOVELTY - The transfer sheet has a liquid permeation layer (2) that is formed on the surface of a base material sheet (1). Catalyst layer (5) containing platinum is formed on the permeation layer. The permeation layer formed with hydrophilic and hydrophobic regions (3,4) is provided with a specific material with which hydrophobic property of the permeation layer changes to hydrophilic property due to the energy irradiation.    USE - Catalyst layer transfer sheet for solid electrolytic membrane used in manufacture of fuel cell (claimed).    ADVANTAGE - The hydrophilic and hydrophobic properties of the electrolytic membrane can be improved reliably and the efficiency of the catalyst layer transfer sheet can be improved while attaining favorable characteristics.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing method of fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the transfer sheet.    Base material sheet (1)    Liquid permeation layer (2)    Hydrophilic region (3)    Hydrophobic region (4)    Catalyst layer (5)
NOVELTY - A biomass pulverization apparatus (1) comprises pulverization table (3) which is rotationally driven within cylindrical shape housing (2) and where biomass solid substance is supplied, roller which operates by cooperating with rotation of table, blowing up air flow which is formed by primary air supplied from lower part of housing, biomass ground material which is conveyed upwards and is classified to coarse powder and fine powder, and squeeze part which air flow path expands in upper direction in housing and cross sectional area passes in predetermined superficial velocity.    USE - Biomass pulverization apparatus for combustion apparatuses e.g. powdered coal burning boiler.    ADVANTAGE - The pulverization apparatus runs stably and maintains classification performance and stable combustion without reducing combustion performance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a control process of biomass pulverization apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional side view of the biomass pulverization apparatus. (Drawing includes non-English language text).    Biomass pulverization apparatus (1)    Housing (2)    Pulverization table (3)    Grinding roller (5)    Dividing supply device (6)
NOVELTY - Method for decoloring melanoidin containing wastewater, involves using Geotrichum candidum Dec 1 (FERM BP-7033).    USE - The method is useful for decoloring melanoidin containing wastewater (claimed) produced from treacle manufacturing plant.
NOVELTY - Biological waste water treatment equipment has biological treatment tank with triple layer of aerobic region, facultative anaerobic region and anaerobic region in the bottom of the tank and organic waste water introducing part which introduces organic waste water from the bottom part of biological treatment tank.    USE - Biological waste water treatment equipment for processing organic waste water with microorganisms.    ADVANTAGE - Volume reduction of surplus sludge is possible and quality of treated water is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of biological waste water treatment apparatus. (Drawing includes non-English language text).    Biological treatment tank (1)    Impeller (3)    Organic waste water introducing part (6)    Introductory pipe (7)    Biological waste water treatment equipment (100)
NOVELTY - An ortho para-hydrogen (deuterium) separation method involves cooling separation cell (16) by controlling temperature to adsorbable temperature of hydrogen gas using mechanical refrigerator (10), introducing hydrogen gas which consists of ortho hydrogen and para-hydrogen to separation cell and adsorbing in adsorption part (18) of separation cell, raising temperature of separation cell from adsorbable temperature, and disconnecting hydrogen gas from adsorption part and discharging.    USE - An ortho para-hydrogen (deuterium) separation method for manufacturing alloys for hydrogen accumulation and fuel cell.    ADVANTAGE - The method increases ratio of ortho hydrogen ratio from hydrogen gas which consists of ortho hydrogen and para-hydrogen simply and stably.    DETAILED DESCRIPTION - An ortho para-hydrogen (deuterium) separation method involves cooling separation cell (16) by controlling temperature to adsorbable temperature of hydrogen gas using mechanical refrigerator (10), introducing hydrogen gas which consists of ortho hydrogen and para-hydrogen to separation cell and adsorbing in adsorption part (18) of separation cell, raising temperature of separation cell from adsorbable temperature, and disconnecting hydrogen gas from adsorption part and discharging. The ratio of hydrogen gas with para-hydrogen which is disconnected is higher than ratio of hydrogen gas with para-hydrogen before absorption. The ratio of hydrogen gas with ortho hydrogen which is disconnected is higher than ratio of hydrogen gas with ortho hydrogen before absorption. An INDEPENDENT CLAIM is included for an ortho para-hydrogen (deuterium) separation apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of ortho para-hydrogen (deuterium) separation apparatus.    Mechanical refrigerator (10)    Pressure gauge (14)    Cooling separation cell (16)    Adsorption part (18)    Highly purified ortho para-hydrogen separation apparatus (20)
NOVELTY - Reducing (M1) the volume of municipal waste and extracting materials involves reducing biomass to liquid form; chemically reducing the biomass substances using enzyme mix to maximize output from the waste material; fermenting the reduces liquid biomass mix to produce specific outputs from waste material; extracting specific output material from liquid for purification and processing; and separating water and remaining solids so that the water may recycle or flush and the solids compost, compressed for fuel use or put to landfill.    USE - For use in vehicles including submarines, aircraft and passenger ferries and cruise ships; use in the disposal or conversion of food waste from food service outlets and food processing sites thus reducing odors and rodent infestations. The process selected controlled feedstock including cardboard and paper; fiberboard and particle board; crop processing waste; grass cuttings; food waste; and human and animal waste (claimed).    ADVANTAGE - The method accelerates and controls the degradation of waste without the intervention of microorganisms or corrosive chemicals and has predictability in the constitution the output by virtue of the specificity of the enzyme mix which is selected or adjusted so that a wide variety of waste can be accommodated.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an apparatus (A1) for reducing waste and extracting materials comprising macerator for breaking solid matter down into smaller pieces for accommodating in an enzyme digestion bath; heat processor and circulating pump to ensure adequate mixing of material within the bath and warming to accelerate the enzyme reaction; filter meals to extract solids from the reaction liquid; and means for extracting material for further processing.
NOVELTY - Edible oil or edible waste oil (O), a synthetic resin and organic refuse (P) are supplied to a heating container (W). The synthetic resin and organic refuse are mixed with edible oil, heated, dissolved and solidified by cooling to form pellet as fuel. The pellet is a crushed material having cylindrical shape, cubical shape or fixed shape.    USE - Manufacture of fuel from synthetic resin e.g. crushed drink container, cap and label, and organic refuse e.g. waste bread crumb, mandarin orange, fruits, cabbage, etc.    ADVANTAGE - The fuel is easily manufactured without contaminating environment and damaging wall material of furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view illustrating manufacture of fuel. (Drawing includes non-English language text)    Blower (B)    Exhaust port (E)    Edible oil (O)    Synthetic resin and organic refuse (P)    Heating container (W)
NOVELTY - The method involves conveying lime mud to a lime kiln (1) in which fuel gas circulating in fluidized bed gasifier (2) is used as fuel and calcium compound is used as bed material for the gasifier. The fuel gas is produced from a bio-based material such as bark, wood chips, sawdust, straw, logging waste, peat, waste paper. The bed material is selected from calcium carbonate, calcium oxide or calcium hydroxide.    USE - Method for treating lime mud formed in pulp manufacturing process and white liquor manufacturing process.    ADVANTAGE - The lime mud is calcinated partly or entirely and is conveyed with product gas to the lime kiln so that fouling of burnt calcium is reduced and the capacity of the lime kiln is increased by calcinating a portion of the lime mud already in the gasifier. The thermal value of product gas is increased so that less amount of gas is required for producing necessary power.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for lime mud treatment plant.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the lime mud treatment plant.    Lime kiln (1)    Fluidized bed gasifier (2)    Process chamber (3)    Separating unit (4)    Drying unit (5)
NOVELTY - A green energy furnace comprises an ash tank, a catalyst, a refractory cover, a water jacket, a hearth set in the refractory cover, and a range combined structure. The ash tank and the catalyst are set at a lower part. The refractory cover and the water jacket are set at a middle part. The range combined structure is set at an upper part. The water jacket is outside of the refractory cover.    USE - A green energy furnace.    ADVANTAGE - The furnace ensures rapid and adequate combustion, increases heat efficiency and environment-friendly performance, is low cost, and has good performance, safety and reliability.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a green energy furnace.
NOVELTY - Water from a mixture comprising a fermentation product and water is removed by distilling the mixture to produce a distillate with a lower concentration of water than the mixture; and permeating water from the distillate through a gas separation membrane to produce a retentate having a lower concentration of water than the distillate.    USE - Process for removing water from a mixture comprising a fermentation product and water (claimed) to produce hydrous ethanol used as an engine fuel or anhydrous ethanol for mixing with gasoline for fuel.    ADVANTAGE - The process can increase production capacity or decreased energy usage per unit of hydrous and/or anhydrous ethanol produced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an apparatus for removing water from a mixture comprising a fermentation product and water, comprising a distillation section; a molecular sieve unit connected to receive distillate from the distillation section, where the distillate having a lower concentration of water than the mixture; and a membrane separation unit located to intercept distillate flowing between the distillation section and the molecular sieve unit or to process a regeneration stream from the molecular sieve unit.
NOVELTY - Biofuel additive is used for diesel engines.    USE - Biofuel additive for diesel engines (claimed).    ADVANTAGE - The biofuel additive reduces fuel consumption, improves diesel engine efficiency and reduces pollution levels compared to heat petroleum diesel. It converts waste into a valuable resource.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (A) composition comprising diesel and 10-30 wt.% of the biofuel additive; and (B) process for preparing the biofuel additive comprising obtaining a crude oil from the weed Argemone mexicana, subjecting the crude oil to a degumming treatment to obtain the degummed oil, washing and neutralizing the degummed oil, removing alkaloids from the degummed oil followed by clarification of the oil to obtain the clarified oil, heating and treating the clarified oil with charcoal followed by filtration to obtain the treated oil, subjecting the treated oil to a step of transesterification in the presence of a catalyst of an alkali or a biocatalyst to obtain the biofuel additive.
NOVELTY - A portable proton exchange membrane fuel cell integrated system comprises air-breathing proton exchange membrane fuel cell, hydrogen generating system providing hydrogen to air-breathing proton exchange membrane fuel cell, and energy storage system. An electric energy output end of the air-breathing proton exchange membrane fuel cell is connected with the energy storage system. Electric energy generated by the air-breathing proton exchange membrane fuel cell is stored by the energy storage system or outputs after the voltage stabilization through the energy storage system.    USE - A portable proton exchange membrane fuel cell integrated system.    ADVANTAGE - The system has simple structure, high credibility, and convenient use.
NOVELTY - A biomass pyrogenation production device comprises a biomass thermal wind furnace; a fire distribution passage; a thermal wind distributor chamber (7) intercommunicated with the biomass thermal wind furnace; lined up pyrogenation reactors comprising a heating chamber (8) having independent wind inlet passage (9), wind discharge passage (10) and exhaust flue gas; and a quick-acting switching-off gates (12).    USE - A biomass pyrogenation production device.    ADVANTAGE - The device achieves continuous production, improves heat operating factor of fuel, and reduces operation cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a biomass pyrogenation production method.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a biomass pyrogenation production device.    Thermal wind distributor chamber (7)    Heating chamber (8)    Wind inlet passage (9)    Wind discharge passage (10)    Quick-acting switching-off gates (12)
NOVELTY - Preparing glycerol alkyl ethers with low amount of mono-ether involves glycerol etherification by recycle of glycerol and/or mono-ether, where glycerol and olefinic hydrocarbon, and/or corresponding 2-10C aldehydes, 2-10C ketones and 2-10C alcohols is reacted in presence of homogeneous acid catalyst with hindered formation of olefin oligomers by reaction step (S1), and neutralization and salt removal step (S2).    USE - For preparing glycerol alkyl ether (claimed) particularly glyceroltert-butyl ether useful as diesel and biodiesel fuel additive.    ADVANTAGE - The process provides glycerol alkyl ethers that are free from by-products, and has low amount of mono-ether.
NOVELTY - A biological degradation unit (1) and aerobic unit (2) are divided into front and rear portions by a baffle. A degradable bacteria packing layer (6) and an aerobic bacteria packing layer (7) formed on a plastic screen comprising polyethylene balls, are provided in middle of biological degradation unit and aerobic unit, respectively. A purification unit (3) is connected to aerobic unit and recycling unit (4) which is connected to water pump (18).    USE - Biological treatment device of fecal sewage.    ADVANTAGE - Simple, compact, durable and convenient biological treatment device can be provided. Degradation, aerobic process, purification and recycling process can be performed continuously.    DETAILED DESCRIPTION - The biological treatment device has an air compressor (19) installed in mechanical auxiliary unit (5) and connected with aeration pipes (16,17) which are in fluid communication with aerobic and purification units. The optimal combination ratio of unit volume in whole volume of treatment device is 35-39% for biological degradation unit, 30-34% for aerobic unit, 14-18% for purification unit, 13-17% for recycling unit. Volume of aerobic bacteria packing layer is 19-25%. Volume of purification packing layer is 4-8%.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biological treatment device.    Biological degradation unit (1)    Aerobic unit (2)    Purification unit (3)    Recycling unit (4)    Mechanical auxiliary unit (5)    Degradable bacteria packing layer (6)    Aerobic bacteria packing layer (7)    Aeration pipes (16,17)    Water pump (18)    Air compressor (19)
NOVELTY - The gasification furnace has a burning furnace (5), which has a double-layer material barrel; and an external barrel (1) equipped with an air inlet (13) and an exhaust port (12). The exhaust port communicates with a first filter (6) by a pipe. The outlet of the first filter is connected with the air inlet of a draft fan (8), of which the exhaust port communicates with the inlet of a second filter (9).    USE - Biomaterial gasification furnace.    ADVANTAGE - The barrel cover can be opened and fed directly without closing the air inlet of the blower and stopping the flame. The fuel gas has high quality; the gas output is quick; and the fire is strong. The gasification furnace is environmentally friendly; and it can save energy, time and labor.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of the biomaterial gasification furnace.    External barrel (1)    Burning furnace (5)    First filter (6)    Draft fan (8)    Second filter (9)    Exhaust port (12)    Air inlet (13)
NOVELTY - The multifunctional biomass gas furnace includes a feed inlet formed in the center of the upper portion of a furnace body. A sealing cover is arranged on the feed inlet . An ash outlet port and a wind inlet port are provided at the lower portion of the furnace body. A vent port, provided at the upper portion of the furnace body, is connected with a separation purifier.    USE - Multifunctional biomass gas furnace used for domestic cooking and heating.    ADVANTAGE - Enables repeated purification of gas, thus ensuring high purity of gas. Facilitates electronic ignition, and ensures stable burning. Achieves high thermal value, and ensures convenient processing.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of multifunctional biomass gas furnace.
NOVELTY - Use of an algal biomass as an activator of a methanization process of a substrate, is claimed.    USE - The algal biomass is useful as an activator of a methanization process of a substrate, where the substrate comprises organic products or by-products of animal or plant origin, preferably animal or plant waste, most preferably manure, agro- food waste, sludge from treatment plant, floating grease or green wastes (claimed). The methanization process is useful for forming biogas.    ADVANTAGE - The process increases the reaction rate and provides very significant achievement in terms of volume of biogas produced per unit of organic matter processed, while maintaining a good level of quality of biogas in terms of rate of methane in the gas mixture. The process is economical by using the algal biomass.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a process-1 of methanization of a substrate constituted of organic products or by-products of animal or plant, preferably animal or plant waste, comprising co-digestion of the substrate with the algal biomass;    (2) a process-2 for preparing the algal biomass comprising washing and grinding raw algal material to obtain a ground algal product; diluting in water of the ground product to obtain a diluted ground product preferably having dry material of 1-20 (preferably 4-6) wt.%; maturating the diluted ground product for 1-48 hours, preferably for 2-24 hours, at 70-100 degrees C, preferably 85-95 degrees C, to obtain a mixture; and separating into two phases of the mixture, preferably by centrifuging/settling, and recovering of the solid phase, followed by pressing of the solid phase, to obtain the algal biomass; and    (3) the algal biomass obtained by the process-2.
NOVELTY - A dry carbon-containing agricultural waste derived from plant is subjected to pyrolysis, which involves heating the waste at 400-500 degrees C for 1-3 hours in the absence of oxygen. The pyrolyzed waste is soaked in an alkaline solution, and pyrolyzed at 800-900 degrees C for 2-4 hours the absence of oxygen to obtain porous carbon material.    USE - Preparation of porous carbon material used for adsorbing substance (claimed) such as methylene blue and iodine. Can also be used for water purification, waste water treatment, gas purification, and manufacture of medicine and filters.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) porous carbon material; and    (2) method of adsorbing substance.    DESCRIPTION OF DRAWING(S) - The drawing shows the flowchart illustrating preparation of porous carbon material from rice straw.    Carbonation process for making carbon-type material using rice straw (1,2)    Activation process for making carbon-type material porous (3,6)
NOVELTY - Manufacturing fuel cell (100) involves forming a channel (112) on one surface of a first wafer (110) and one surface of a second wafer (120), respectively; stacking membrane electrode assembly (140) on one surface of the first wafer; and coupling the second wafer to the first wafer to allow one surface of the second wafer to cover the membrane electrode assembly.    USE - For manufacturing fuel cell.    ADVANTAGE - The method enables manufacture of a fuel cell by preventing the damage of a precisely formed membrane electrode assembly and in a small size at low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell comprising a first wafer, having one surface is formed with a first channel; a membrane electrode assembly, is stacked on one surface of the first wafer; a second wafer, coupled to the first wafer such that one surface of the second wafer on which a second channel is to be formed covers the membrane electrode assembly; and sealing layer (130) (preferably photosensitive material), is interposed between the membrane electrode assembly and at least one of the first wafer and second wafer in order to prevent leak of fluids flowed to the first channel and the second channel.    DESCRIPTION OF DRAWING(S) - The figure shows a cross-sectional view of a method for manufacturing fuel cell.    Fuel cell (100)    Channels (112, 122)    First wafer (110)    Second wafer (120)    Sealing layer (130)    Membrane electrode assembly (140)
NOVELTY - Producing fermentable sugars and acetic acid derivative by treating extract produced by steam cooking of biomass through a staged treatment of clarification, fractionation, and hydrolysis.    USE - For producing fermentable sugars and acetic acid derivative; and for producing ethanol (claimed).    ADVANTAGE - The process is integrated with the host plant process to minimize the effect of loss of heat value from the extracted hemicelluloses and eliminate the need for the waste water treatment plant. Treating the hemicelluloses extracted through a series of membranes, hydrolysis, fermentation and distillation recovers saleable products. The process is integrated with the host plant to reuse water and minimize process energy consumption. In this process, activated sludge is not burned, causing a decrease in the steam produced in the existing plant biomass boiler. However, this steam loss is mitigated by the reduction in energy required by the waste water plant and the host plant where less water heating is required due to the recycle of hot water from the reverse osmosis step.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing ethanol and acetate derivatives by treating extract from a host plant lignocellulosic material, where i) extract is fractionated and concentrated in multiple steps consisting of ultra-, nano- and reverse osmosis membranes with lignin separated from the extract and filtered back as boiler fuel, ii) hemicelluloses are hydrolyzed with sulfuric acid or enzymes into fermentable sugars, iii) fermentable sugars are fermented to cellulosic ethanol, iv) hot clean water from the membranes is recycled back to the host plant, and v) distillation bottoms are evaporated to create a zero liquid effluent plant.
NOVELTY - A switchgrass cultivar Cimarron, comprising all the morphological and physiological properties of the cultivar grown from a seed deposited under ATCC PTA-10116, is new.    USE - The switchgrass cultivar Cimarron is useful in lignocellulosic feedstock for producing biofuel ethanol (all claimed), as fuel pellets, substitute for coal in power generation, boiler fuel and solid biofuel, for monoculture plantings for soil conservation, and for wildlife and livestock grazing and haying.    ADVANTAGE - The switchgrass cultivar Cimarron has increased biomass yield.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) seed of switchgrass cultivar Cimarron;    (2) progeny of switchgrass cultivar Cimarron;    (3) vegetative sprig or clone of the switchgrass cultivar;    (4) part of the switchgrass cultivar plant, where the part is chosen from roots, stems, leaves, pollen and seeds;    (5) lignocellulosic feedstock for use in production of biofuel ethanol, comprising harvested switchgrass plants of cultivar Cimarron; and    (6) method of producing biofuel ethanol, involves providing the above-cited lignocellulosic feedstock, and converting the lignocellulosic feedstock to biofuel.
NOVELTY - Producing fatty acids comprises: (a) inoculating a mixture of cellulose, hemicellulose, and lignin; (b) inhibiting growth of microorganism strain; and (c) inoculating mixture with algae strain.    USE - The method is useful for producing fatty acids (claimed).    ADVANTAGE - The cellulose is the most abundant and renewable carbon source on earth and its efficient transformation into a useable fuel could solve the world's energy problem.    DETAILED DESCRIPTION - Producing fatty acids comprises: (a) inoculating a mixture of at least one of cellulose, hemicellulose, and lignin with at least one microorganism strain that produces one or more cellulase, hemicellulase and laccase, that hydrolyze at least one of cellulose, hemicellulose and lignin, under conditions to produce at least one of glucose, cellobiose, xylose, mannose, galactose, rhamnose, arabinose or other hemicellulose sugars; (b) inhibiting growth of the at least one microorganism strain; and (c) inoculating the mixture of step (b) with at least one algae strain that metabolizes the at least one of glucose, cellobiose, xylose, mannose, galactose, rhamnose, arabinose or other hemicellulose sugars, under conditions so that the at least one algae strain produces one or more fatty acids.
NOVELTY - An isolated cellulase variant, where the variant is a mature form having cellulase activity and comprising a substitution at one or more positions selected from 63, 77, 129, 147, 153, 157, 161, 194, 197, 203, 237, 239, 247, 254, 281, 285, 288, 289, 294, 327, 339, 344, 356, 378, and 382, where the positions are numbered by correspondence with the amino acid sequence of a reference cellobiohydrolase II (CBH2) set forth as fully defined 447 amino acids (SEQ ID NO: 3), given in the specification, is new.    USE - The isolated cellulase variant and methods are useful for converting biomass to sugars; and for producing a fuel (all claimed).    ADVANTAGE - The methods are highly efficient and effective.    DETAILED DESCRIPTION - An isolated cellulase variant, where the variant is a mature form having cellulase activity and comprising a substitution at one or more positions selected from 63, 77, 129, 147, 153, 157, 161, 194, 197, 203, 237, 239, 247, 254, 281, 285, 288, 289, 294, 327, 339, 344, 356, 378, and 382, where the positions are numbered by correspondence with the amino acid sequence of a reference cellobiohydrolase II (CBH2) set forth as fully defined 447 amino acids (SEQ ID NO: 3), given in the specification, and where the substitution at one or more positions causes the cellulase variant to have a more negative net charge in comparison to the reference CBH2, is new.
NOVELTY - A waste gases are contacted with an absorbent composition (54), and the waste gases are absorbed using the absorbent composition (56) to eliminate the carbon dioxide from the waste gases.    USE - Method of eliminating carbon dioxide useful for producing biomass including photoautotrophs e.g. algae in open-pond systems (claimed) used for production of biofuel such as biodiesel.    ADVANTAGE - The method increases the growth rate and fat content of algae by increasing the concentration and solubility carbon dioxide, maintains the steady state saturation level of carbon dioxide surrounding the algae, and enhances recyclability of perfluorodecalin solution from the container.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) absorbent composition for increasing growth rate of photoautotrophs;    (2) absorbent apparatus for eliminating carbon dioxide from waste gases;    (3) system for eliminating carbon dioxide from waste gases to use in production of biomass;    (4) method for operating photobioreactor using carbon dioxide absorbed from waste gases; and    (5) method for operating open-pond system using carbon dioxide absorbed from waste gases.    DESCRIPTION OF DRAWING(S) - The drawing shows block diagram of elimination method of carbon dioxide from the waste gases.    Elimination of carbon dioxide from waste gas (50)    Waste gas is provided (52)    Waste gas is contacted with absorbent composition (54)    Waste gas is absorbed using absorbent composition (56)    Absorbent composition absorbs waste gases to eliminate carbon dioxide (58)
NOVELTY - A cylindrical discharge vessel (1) has an opening (2) to a high pressure region at the top. The nozzles (3) are arranged on the sides of discharge vessel at a distance corresponding to the 0.5-2 times the diameter of the vessel, from the bottom of the vessel, and the nozzles are inclined at 20-60 degrees with respect to vessel center portion. An outlet orifice (5) is arranged at bottom of the vessel for ejecting pretreated biomass into pipeline (6). The vessel is filled with water for 1/2 or 4/5 of its total internal volume equal to 500 liters.    USE - Device for discharging pretreated biomass from higher to lower pressure regions.    ADVANTAGE - The outlet orifice secures a drop in pressure as the biomass mixture is ejected at high speed and the mixture of biomass and water are ejected through the pipeline without blockage by the temperature gradient produced by the liquid at the top and bottom portion of the vessel. Hence the temperature gradient reduces heat loss from the reactor and reduces the energy consumption in production scale biomass processing.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for discharging pretreated biomass from higher to lower pressure regions that involves ejecting pretreated biomass into a pipeline and driving the biomass by pressure drop. The biomass is ejected as slurry that is subsequently pressed to recover water which is subsequently recycled. The water or liquid is added through nozzles or jets at a temperature of 95 degrees C.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of device for discharging pretreated biomass from higher to lower pressure regions.    Discharge vessel (1)    Opening (2)    Nozzle (3)    Outlet orifice (5)    Pipeline (6)
NOVELTY - Producing layered rigid fuel pellets comprises mixing one of biomass material and particulate carbon-based material with a silicate-based binder; agglomerating the mixture by tumbling at ambient temperature to form core pellets; mixing the other of the biomass material and the particulate carbon-based material with the binder; and agglomerating the mixture around the core pellets by tumbling at ambient temperature to form the pellets.    USE - Process of producing layered rigid fuel pellets (claimed).    ADVANTAGE - The fuel pellet leaves little or no combustible fuel in the ash. It has sufficient rigidity after tumbling to allow handling, stacking and/or transportation without any significant breakage.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of a process including material handling and production stages in an industrial plant.
NOVELTY - A raw material supply unit supplies raw material containing hydrocarbon and odorant. An adsorption removal unit containing zeolite absorbs odorant component in the raw material. A reformer generates hydrogen-containing gas by reaction between the raw material from the removal unit and water. A fuel cell generates electric power from the generated gas. An operation control unit controls supply of raw material to the adsorption removal unit, based on the electric power generated by the fuel cell, with increase of flow rate of raw material to adsorption removal unit.    USE - Fuel cell electric power generation system for domestic applications.    ADVANTAGE - Since the supply of raw material to the adsorption removal unit is controlled by the operation control unit, based on the generated electric power, with increase in flow rate of raw material, the energy consumed by the system can be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for operating method of fuel cell generating system.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow chart explaining the process of controlling the operation-control unit. (Drawing includes non-English language text)
NOVELTY - A renewable feedstock is hydrotreated to produce hydrocarbon fraction. Then, the hydrocarbon fraction is hydrocracked, to produce distribution of cracked hydrocarbon, and naphtha fraction is separated from the distribution of cracked hydrocarbon.    USE - Method for producing naphtha boiling-range hydrocarbon for naphtha composition used as fuel for industrial burners and boilers, feedstock for steam cracker and catalytic reforming, industrial solvent, alternative gasoline for combustion engine, and turbine fuel, and for producing hydrogen, and gasoline bend stock, and fuel cell application (all claimed).    ADVANTAGE - The method provides naphtha boiling-range hydrocarbon having high hydrogen-to-carbon ratio economically, using renewable feedstock.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for naphtha composition produced from renewable feedstock. The naphtha has boiling point of 70-400 degrees F and specific gravity of 0.680-0.740 at 20 degrees C.
NOVELTY - Producing oxide based metal-organic framework materials using inverse synthesis, comprises reacting zinc compounds (I) with an acid having at least four donor atoms or an acid derivative of the acid having four donor atoms as a linker in the presence of non-aqueous solvent or dispersion medium, where A is the anion of the acid residue of an acid with two or three donor atoms per molecule.    USE - The oxide based metal organic framework material is useful: as potential gas storage materials in the utilization of alternative energy sources; as natural gas storage materials; in the field of chemical and industrial catalysts; as an analytical separation material in the form of the stationary phase for gas and liquid chromatography; and as sensitive layer in sensor application.    ADVANTAGE - The process produces oxide based metal organic framework material with reproducibility in large quantities with constant maximum specific surface in an economical manner.    DETAILED DESCRIPTION - Producing oxide based metal-organic framework materials using inverse synthesis, comprises reacting zinc compounds of the type of formula (Zn4OA6) (I) with an acid having at least four donor atoms or an acid derivative of the acid having four donor atoms as a linker in the presence of non-aqueous solvent or dispersion medium.    A = anion of the acid residue of an acid with two or three donor atoms per molecule.
NOVELTY - In a process to manufacture a fuel cell stack unit incorporating a soldered element, the element has a ring-shaped enclosed solder stopper bead. When the building element is soldered is contact with the soldering metal in a second interface.    USE - Process to manufacture a fuel cell stack.    ADVANTAGE - The process is more reliable and eliminates the prior art risk of an electrical short circuit due to failure of the join.    DETAILED DESCRIPTION - The solder stopper extends along the outer edge of the component and encircles an aperture for the passage of gas which forms part of the fuel cell system. The height of the solder stopper bead is essentially the same as that of the solder trade at the interface.    DESCRIPTION OF DRAWING(S) - The drawing shows an exploded view of the fuel cell component parts ready for assembly.    Fuel cell (100)    housing upper cell (106)    cathode electrolyte-anode unit (108)    substrate (109)    anode contact material (110)    housing lower section (112)    intermediate element (114)
NOVELTY - An outer periphery edge of hydrocarbon type polymer electrolyte membrane (21), and outer periphery edges of separators (29,30) are made to mutually oppose with each other. The sealing portions (33,34) are adhered between outer periphery edge of polymer electrolyte membrane and outer periphery edges of separators using thermosetting sealing material. The polymer electrolyte membrane is dried and shrunken before integrating the polymer electrolyte membrane in a laminated constitution (200).    USE - Fuel cell manufacturing method.    ADVANTAGE - The shrinkage of polymer electrolyte membrane at the time of adhesion and fuel cell stop can be prevented effectively. Therefore, the stress concerning the polymer electrolyte membrane can be reduced and the durability of the polymer electrolyte membrane can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the laminated constitution of the fuel cell.    Hydrocarbon type polymer electrolyte membrane (21)    Membrane electrode assembly (28)    Separators (29,30)    Sealing portions (33,34)    Laminated constitution (200)
NOVELTY - Microorganism support for denitrifying apparatus, comprises granule of autotrophic denitrifying bacteria movably accommodated in a storage device having several through-holes on the surface. The autotrophic denitrifying bacteria are filled in the denitrifying tank and ammonia nitrogen in natural water supplied in upward flow is continuously removed as nitrogen gas.    USE - Microorganism support used in biological denitrification apparatus (claimed) for reducing ammonia nitrogen and nitrite nitrogen to nitrogen gas and treating wastewater.    ADVANTAGE - The support can be maintained in high concentration and the handling of microorganism is easy. The support has excellent working efficiency and the outflow of the microorganism from the apparatus is prevented. The denitrifying apparatus using the support is space saving and enables rapid and efficient denitrification as the culture period within tank is not required and residence tine is reduced. Replenishment and reclosing are easy and do not require the acclimatization period within the tank.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biological denitrification apparatus.
NOVELTY - An incineration system (10) performs incineration process of waste material and supplies waste material to methane fermentation equipment (20). A mixing apparatus (21) mixes the organic substance in organic waste and dilution water and distributes in the dilution water. A methane fermentation tank (23) to which liquid discharged from water removal device (22) is introduced and methane fermentation is performed with the dilution water. The waste water discharged from the incineration system is used for dilution water.    USE - Refuse treatment facility for performing incineration process of waste material such as municipal solid waste and industrial waste.    ADVANTAGE - The quantity of organic substance introduced into methane fermentation equipment is increased so that more methane gas is manufactured and the merit in environmental view and economic view is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for waste material processing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the refuse treatment facility.    Incineration system (10)    Methane fermentation equipment (20)    Mixing apparatus (21)    Water removal device (22)    Methane fermentation tank (23)
NOVELTY - A waste gas is processed by introducing waste gas containing odor component into absorption tower (13), exhausting waste gas after purification from absorption tower, blowing in gas containing oxygen and oxidatively decomposing odor component in liquid by microorganisms by biologic reactor (12), making liquid of biologic reactor into absorption liquid and circulating through absorption tower, and stirring inside of biologic reactor by stirring apparatus (17) other than aeration.    USE - Processing of waste gas.    ADVANTAGE - The method carries out hydrogen sulfide removal in biologic reactor with high efficiency. The hydrogen sulfide does not vaporize from biologic reactor to air.    DETAILED DESCRIPTION - A waste gas is processed by introducing waste gas containing odor component into absorption tower (13), exhausting waste gas after purification from absorption tower after making waste gas and absorption liquid contact in absorption layer of absorption tower and making absorption liquid absorb odor component, introducing absorption liquid which absorbed odor component in absorption tower into biologic reactor (12), blowing in gas containing oxygen and oxidatively decomposing odor component in liquid by microorganisms by biologic reactor, making liquid of biologic reactor into absorption liquid and circulating through absorption tower, and stirring inside of biologic reactor by stirring apparatus (17) other than aeration. The biologic reactor blows in gas containing oxygen so that dissolved oxygen concentration of liquid may become 0.1-1 mg/L.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the waste gas processing apparatus.    Biologic reactor (12)    Absorption tower (13)    Stirring apparatus (17)    Absorption layer (34)    Absorption liquid circulation line (40)
NOVELTY - A polymer electrolyte membrane is manufactured by synthesizing polyelectrolyte precursor which exhibits proton conductivity by alkaline hydrolysis and acid treatment, forming polyelectrolyte precursor into film, and making radical-proof agent exist in polymerization processes of isolating polyelectrolyte precursor which is polymerized and synthesized from the time of polymerizable raw material preparation.    USE - Manufacture of polymer electrolyte membrane for polymer electrolyte fuel cell (claimed).    ADVANTAGE - The method is simple, and obtains polymer electrolyte membrane which is excellent in radical character-proof and improves durability of polymer electrolyte fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of the electrolytic membrane manufacturing process. (Drawing includes non-English language text).
NOVELTY - The gasifier (1) has a gasifying agent supply pipe (40) for guiding an oxidation gasifying agent e.g. air, towards a fall flow path of a raw material biomass in a reaction container (10), where the biomass is made to react with the agent to produce production gas. A steam supply pipe (15) in another reaction container (20) supplies steam to the production gas to obtain synthesis gas e.g. hydrogen. Modification catalyst (25) is loaded in a space in the container (10) and a reaction space in the container (20) by heat-transfer partition, where the reaction space is positioned in the flow path.    USE - Biomass gasifier for obtaining synthesis gas e.g. carbon monoxide and hydrogen, by performing steam reformation of production gas obtained by partially oxidizing raw material biomass.    ADVANTAGE - The biomass gasifier stably transfers heat produced by partial-oxidation reaction in one of the reaction containers to the steam modification reaction occurring in the other container, thus obtaining the synthesis gas from the raw material biomass with high yield. The gasifier avoids the need of using a shift reaction apparatus, so that the gasifier is compact.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biomass gasification method.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a biomass gasifier.'(Drawing includes non-English language text)'    Biomass gasifier (1)    Reaction containers (10, 20)    Steam supply pipe (15)    Modification catalyst (25)    Gasifying agent supply pipe (40)
NOVELTY - Biodiesel is prepared by filtering hogwash oil in food waste, dehydrating, filtering finely, esterifying and exchanging ester of oil, separating glycerin and decolorizing oil.    USE - Method for preparing biodiesel (claimed).    ADVANTAGE - The method is simple without secondary pollution, utilizes easily obtained raw materials, forms hogwash oil recycled from food waste into valuable product and improves food safety.
NOVELTY - The liquefier has a cold box for storing methane refrigerant and nitrogen refrigerant. Methane heat exchangers (42, 44) perform heat exchange process between the nitrogen refrigerant and the methane refrigerant. A methane expander cycle (40) cools methane, and supplies the methane to the cold box. A swelling unit distends methane of the methane heat exchangers that is installed at a downstream side portion of methane compressors (41, 43). The swelling unit cools mixed-refrigerant, and is installed at a downstream side portion of mixed-refrigerant compressors (22).    USE - Natural gas liquefier for use in a liquefied natural gas (LNG) transportation line.    ADVANTAGE - The liquefier has simple structure by utilizing a nitrogen expander cycle, efficiently performs liquefaction process and refrigerant swelling process, and has stable driving performance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a natural gas liquefaction method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a natural gas liquefier.    Mixed-refrigerant compressors (22)    Nitrogen expander cycle (30)    Methane expander cycle (40)    Methane compressors (41, 43)    Methane heat exchangers (42, 44)
NOVELTY - A light hydrocarbon is recycled from exhaust gas of polyolefin plant by removing impurity from the exhaust gas, and subjecting exhaust gas to an oil-absorption tower having oil absorbent to separate light hydrocarbon. The oil-absorption tower has an inlet or outlet pressure of 0.1-5 MPa, and inlet or outlet temperature of - 200 to 0 degrees C.    USE - Method of recycling light hydrocarbon (preferably 2-5C) from exhaust gas of polyolefin plant (claimed).    ADVANTAGE - The method is simple and convenient, has small energy consumption and low operation cost, has high removal rate of nitrogen and recovery rate of light hydrocarbon, and obtains light hydrocarbon that can be directly sent in olefin separating device.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a method of recycling light hydrocarbon from exhaust gas of polyolefin plant. Drawing includes non-English language text.
NOVELTY - A fuel composition comprises 1-7 vol.% of cyclohexylamine, and 6 vol.% of moisture. 95-40 vol.% of naphtha and 5-60 vol.% of hydrated ethanol are also provided in the fuel composition. The cyclohexylamine is used as an additive for prevention of phase separation.    USE - Fuel composition for internal-combustion engine.    ADVANTAGE - The fuel composition ensures improved octane number by using containing alcoholic ingredient, phase separation protecting effect by using cyclohexylamine, and does not generate harmful emission, thus the composition is eco-friendly.
NOVELTY - A pretreatment liquid comprises water, a metal salt, a fluorescent brightener and at least one butane derivative selected from 3-methoxy-3-methyl-1-butanol, 1,3-butylene glycol and isoprene glycol.    USE - As pretreatment liquid for inkjet recording by attaching an ink composition onto plain paper by an inkjet printer before forming an image on the plain paper (claimed).    ADVANTAGE - The pretreatment liquid appropriately penetrates into plain paper, thereby suppressing deterioration of paper and enabling high-quality printing. Since the pretreatment liquid does not cause deterioration of paper, it can be used in a sufficient amount. Since the pretreatment liquid containing a specified butane derivative and a fluorescent brightener is used, an image with high quality can be formed on plain paper without causing deterioration of paper by the method. In particular, in the case of adopting multi-drop printing, since the concentration of the metal salt per unit area can be controlled, it is easy to regulate the image quality. As a result, a clear image is obtainable.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for inkjet printing involves attaching the colorless pretreatment liquid onto plain paper; and injecting at least one ink composition which react with the pretreatment liquid onto the plain paper after the pretreatment, thereby forming an image, the ink composition containing a coloring material and water.
NOVELTY - Producing clean fuel with solid fermented 2,3-butanediol of wheat straw source comprises: (a) preparation of the raw material; (b) enzymolysis; (c) solid fermenting; and (d) distilling.    USE - The method is useful for producing clean fuel with solid fermented 2,3-butanediol of wheat straw source (claimed).    ADVANTAGE - The method reduces producing cost of 2,3-butanediol and environmental pollution; and the effect of exploiting the natural resources and environmental protection is realized.    DETAILED DESCRIPTION - Producing clean fuel with solid fermented 2,3-butanediol of wheat straw source comprises: (a) prepare of the raw material: the cellulose raw material gained from the wheat straw basified in the paper manufacturing industry, and the cellulose raw material gained from the wheat straw by liquefying, and the cellulose raw material gained from the wheat straw by basifying and stewing, where the cellulose is 60-71% which is smashed for further use; (b) enzymolysis: the raw material is added with 2-5% of cellulose complex enzyme dose (Cellulose Multi-enzyme); the added water is 60-75% of the weight of the raw material; and then the raw material is in enzymolysis for three to five days under the condition that the pH value is 5.5-7.0, and the temperature is 35-45 degrees C; (c) solid fermenting; and (d) distilling: the 2,3-butanediol is gained after decompression and distilling.
NOVELTY - Producing clean fuel from liquid state fermentation of 2,3-butanediol of straw stalk comprises: (a) raw material preparation; (b) zymohydrolysis; (c) liquid state fermentation; and (d) distillation.    USE - The method is useful for producing clean fuel from liquid state fermentation of 2,3-butanediol of straw stalk (claimed).    ADVANTAGE - The production of the 2, 3-butanediol fuel has low cost and has double effects of developing renounce and protecting environment.    DETAILED DESCRIPTION - Producing clean fuel from liquid state fermentation of 2,3-butanediol of straw stalk comprises: (a) raw material preparation: preparing cellulose raw material in straw obtained by basification in paper-making industry and cellulose raw material in straw obtained by liquefaction process or cellulose raw material in straw obtained by basified stewing, where cellulose is 60-70%, which is smashed for future use; (b) zymohydrolysis: adding cellulose multi-enzyme preparation based on the 2-5% of enzyme adding quantity; performing zymohydrolysis for 3-5 days under the condition that the water adding quantity is 5-7 times of the weight of the raw material, pH is 5.5-7.0 and the temperature is 35-45 degrees C; (c) liquid state fermentation; and (d) distillation: distilling and decompressing to obtain 2,3-butanediol.
NOVELTY - The furnace has a fuel drum whose top is installed with a drum cover. An upper part of the fuel drum is installed with a fuel gas output pipe and a waste gas discharging valve. A fuel gas output pipe is connected with a gas inlet pipe on an upper part of a purifier through a hose. A lower part of the fuel drum is installed with an ignition pipe, an air inlet pipe and a dust outlet. The purifier and a 12 watts power-failure double-purpose blower are fixed on a steel frame on a lower part of a furnace platform. An infrared furnace end is installed on table top on an upper part of the platform.    USE - Biomass gasification furnace.    ADVANTAGE - The blower supplies air to the fuel drum to burn the fuel in the fuel drum for gasification, and the gasified fuel can be conveyed to the purifier through a pipeline. The blower is simple in structure, convenient and safe to utilize, environment-friendly and inexpensive, and has broad fuel source.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a biomass gasification furnace.
NOVELTY - The reactor has a slag discharging device (6) and a fluid discharging device (7) that are respectively placed at upper and lower sides of a corresponded mesh screen (3) in a hydrolyzing pool (1). A top cover (2) is provided in an internal-external double-layer structure. An oil-collecting device (9) and an air exhausting device (10) are placed between internal and external layers. A showering device (5) is mounted at a bottom part of the top cover. A water charging device (11) is placed at a lower part of the hydrolyzing pool.    USE - Hydrolyzing acidifying reactor for hydrolyzing restaurant kitchen waste for producing methane.    ADVANTAGE - The reactor effectively hydrolyzes the restaurant kitchen waste without correct sorting, so as to get the acidification liquid for producing methane through anaerobic digestion treatment, thus simplifying the pretreatment process of the restaurant kitchen waste and reducing energy consumption and investment cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial sectional view of a hydrolyzing acidifying reactor.    Hydrolyzing pool (1)    Top cover (2)    Mesh screen (3)    Showering device (5)    Slag discharging device (6)    Fluid discharging device (7)    Oil-collecting device (9)    Air exhausting device (10)    Water charging device (11)
NOVELTY - The method involves fixing screen-shaped drain gratings on river beds at the front circumferences and the two sides of sewage drain hole, and suspending 10-20 layers of polymer membranes with dense cilia, on upper portions of the drain gratings. The discharge of sewage flow is made through the polymer membrane with dense cilia. The distance between the polymer membranes with dense cilia is set in the range of 10-15 cm. The drain gratings are comprised of several baffle plates fixed and connected by connection pin with variable angle.    USE - Method for treating point source pollution.    ADVANTAGE - The treated object is changed into point source pollutant opening from river channel, and the power consumption caused by conveying sewage can be reduced reliably. The sewage is discharged from the drain gratings after being treated biologically through the polymer membrane with dense cilia, so it reaches the discharge standard.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view explaining the treatment method of point source pollution.
NOVELTY - Boiler biomass fuel comprises hypha and/or fungus dreg, and greater than or equal to 25 wt.% water content.    USE - Boiler biomass fuel.    ADVANTAGE - The boiler biomass fuel avoids polluting environment, and effectively uses heat value in the hypha and fungus dreg.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing the boiler biomass fuel comprising dehydrating and drying the hypha and/or fungus dreg.
NOVELTY - A recycle method of carbon dioxide involves separating liquefaction carbon dioxide and water to be concentrated from coal, coke, plant biomass or polymeric material waste material and exhaust gas that consist of carbon, hydrogen and oxygen to react at a high temperature. The synthesis gas which consists of carbon monoxide and hydrogen is manufactured. A compound is synthesized by hydrogenation reaction to be made into a raw material.    USE - Recycle method of carbon dioxide.    ADVANTAGE - Suppresses generation of carbon monoxide to save energy. Can be directly useful for global warming prevention. Suppresses production of the biofuel which uses food as raw material.
NOVELTY - Reducing the sulfur content of a petroleum fluid involves providing a bed of particulates of transition metal or rare earth metal oxide catalyst material, the particulates have a surface area of at least 15 m2/gm, and passing the petroleum fluid through the bed of catalyst material at less than or equal to 650 degrees C.    USE - For reducing the sulfur content of a petroleum fluid (claimed), to obtain hydrogen gas that is used, for e.g. in fuel cells.    ADVANTAGE - The process is capable of reforming both natural gas and jet fuel at below 650 degrees C, and further to the reduction and removal of sulfur-bearing compounds in petroleum fluids. The catalysts produce hydrogen from methane at lower temperatures.    DETAILED DESCRIPTION - Reducing the sulfur content of a petroleum fluid involves providing a bed of particulates of transition metal or rare earth metal oxide catalyst material of formula (M1)x(M2)1-x(O)2-z, the particulates have a surface area of at least 15 m2/gm, and passing the petroleum fluid through the bed of catalyst material at less than or equal to 650 degrees C.    M1=transition metal or a rare earth metal;    M2=rare earth metal;    x=0-0.9;    z=degree of oxygen deficiency in the catalyst relative to M1+M2.    M1 and M2 are two different rare earth metals.
NOVELTY - Apparatus comprises a reaction solution tank (20), a reaction tank (30), a mixer (31), a heater (33), a condenser (40) and a methanol collection tank (50). The mixer is provided for agitating raw material supplied from reaction tank. The condenser is provided for cooling methanol gas. Liquid methanol condensed gas is stored in the methanol collection tank. Methanol and caustic soda are mixed and stored in the reaction solution tank. The heater is provided for heating raw material in the reaction tank.    USE - Apparatus for manufacturing biodiesel.    ADVANTAGE - The apparatus is cost-effective, improves productivity of biodiesel, reduces mixing time in the reaction tank and shortens reaction time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for manufacturing biodiesel, which involves:    (A) heating disposable edible oil at 55-65 degrees C;    (B) agitating reaction solution;    (C) mixing methanol and caustic soda in the disposable edible oil;    (D) heating the obtained mixture for 1-40 hours; and    (E) precipitating the mixture for 40 minutes to separate glycerin from biodiesel.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biodiesel manufacturing device.    Reaction solution tank (20)    Reaction tank (30)    Mixer (31)    Heater (33)    Condenser (40)    Methanol collection tank (50)
NOVELTY - A fuel is produced by introducing effluent stream into first vessel, where effluent stream contains solids and at least one of vegetable oil and petroleum oil; heating effluent to lower its viscosity in first vessel; separating at least some of solids from heated effluent to form a reactant stream; introducing reactant stream to a bioreactor; introducing at least one remediation agent into the bioreactor; heating reactor contents to reaction temperature; and allowing sufficient time to pass such that the reactant stream yields fuel product.    USE - Method for producing fuel (claimed) including biodiesel and renewable fuel for diesel engine.    ADVANTAGE - The fuel does not need for mechanical alterations, and is compatible with existing petroleum distribution infrastructure; and can provide source of on-site fuel generation for remote turbine or engine operation, thus generating power with minimal transportation costs associated with power generation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a process for powering an engine comprising the preparation of fuel; and passing the fuel product to an on-site engine.    DESCRIPTION OF DRAWING(S) - The drawing is a general process flow diagram showing production of fuel.    Stream (510)    Bio-growth tank (600)
NOVELTY - Ultra-pure inert gas production involves dissolving certain amount of active metal salts including nickel in water at 70 degrees C to obtain porous solid substrates. A certain amount of carrier, alkali and alkaline earth metals are also mixed in the obtained porous solid substrates. The resultant is aged for 20 hours in air atmosphere to obtain metal precipitate. The obtained metal precipitate is filtered, washed, dried and plasticized.    USE - Method for producing ultra-pure inert gas by using adsorbent for use in semiconductor manufacturing industry.    ADVANTAGE - The ultra-pure inert gas production method enables to produce the ultra-pure inert gas having fast adsorption performance of oxygen, hydrogen, carbon monoxide, carbon dioxide, methane, steam, nitrogen or inert gases including argon or helium.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow-chart of ultra-pure inert gas production method.    Oxygen gas cylinder (1)    Carbon dioxide cylinder (2)    Mass flow controller (3)    Hydrogen gas cylinder (4)    Fixed bed reactor (5)
NOVELTY - The method involves treating zymotic liquid waste gas by a gas-liquid separator so as to remove the flue gas with high chemical oxygen demand (COD) content. The condensed liquid obtained by treating process, is poured into a sewage disposal system. The temperature of the flue gas is reduced to 35 degrees, and temperature reduced flue gas is discharged to a biological filter. The VOC in the flue gas is resolved under the action of the micro-organisms. The temperature and pH values of the biological filter are 33-38 degrees and 6-8 respectively.    USE - Method for removing zymotic waste gas of amino acid by biological filter.    ADVANTAGE - Since the VOC in the flue gas is resolved under the action of the micro-organisms, the zymotic waste gas can be removed effectively. The living environment of the residents can be improved reliably. The prominent and social environmental benefits can be provided efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the apparatus for removing zymotic waste gas of amino acid. (Drawing includes non-English language text)
NOVELTY - The method involves conveying waste gas to gas-liquid separator. The chemical oxygen demand (COD) rich waste water after separation is sent to mash pool for recycling. The gas and water are supplied from lower and upper sides of spraying tower respectively. The processed gas is sent out from upper side of tower. The solid particles during spraying process are filtered in water box. The spraying water temperature is lowered, and condensed water produced in temperature lowering process is mixed with spraying water and discharged to waste water treating factory.    USE - Method for treating waste gas produced by amino acid fermentation.    ADVANTAGE - The waste gas treating process is simplified, treating operation can be conveniently performed and condensed water is recycled without causing secondary pollution. The steam content and load of subsequent process can be reduced.
NOVELTY - Crude propane and/or crude propylene having 4C hydrocarbon is fractionated by distillation to a fraction (1) having propane and/or propylene as main component, and fraction (2) having 4C or more hydrocarbon as main component. The obtained fraction (2) is fractionated by evaporation to a fraction (3) having 4C hydrocarbon as main component, and fraction (4) having substance with high boiling point than 4C hydrocarbon as main component. Thus, crude propane and/or crude propylene is purified.    USE - Purification of crude propane and/or crude propylene used for manufacturing acrylonitrile used for synthetic resin, acrylic fiber, acryl amide and acrylonitrile-butadiene-styrene resin.    ADVANTAGE - The crude propane and/or crude propylene are continuously and stably purified.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus for purifying crude propane and/or propylene, which has a distilling column (1) for fractionating crude compound to fraction (1) having propane and/or propylene as main component, and fraction (2) having 4C or more hydrocarbon as main component, and an evaporator (2) for fractionating obtained fraction (2) to a fraction (3) having 4C hydrocarbon as main component, and fraction (4) having substance with high boiling point than 4C hydrocarbon as main component.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of flow of refinery processing installation.    Distilling column (1)    Evaporator (2)    Evaporated residue drum (3)    Lines (4-11)
NOVELTY - The method involves introducing chelating agent(s) into an area, and allowing the chelating agent(s) to diffuse through the area. Stabilizing agent(s) and aqueous solution comprising peroxide(s) are introduced.    USE - Method for in situ reclamation of an area contaminated by organic compounds. Uses include but are not limited to gasoline, diesel oil, olefinic hydrocarbons, chlorinated or polychlorinated hydrocarbons, industrial solvents and dry-cleaning solvents, agents for the treatment of wood, herbicides, pesticides, polychlorinated biphenyls and aromatic or polycyclic aromatic hydrocarbons.    ADVANTAGE - The method allows stabilizing and prolonging the lifetimes of the peroxide, thus enabling greater diffusion through the contaminated area and greater reclaiming capacity i.e. greater capacity of transforming the organic compounds into compounds, which are safe and non-toxic for the environment. The method avoids the usage of large amount of aqueous solutions of peroxide at high concentrations and the stripping of the volatile contaminating organic compounds, and allows the oxidation rate to be controlled by avoiding violent reactions and an uncontrolled increase in the temperature. The method can be implemented in an efficient manner without controlling the reaction pH. The greater stabilization of the hydrogen peroxide allows greater capacity of eliminating the contaminating organic compounds.
NOVELTY - Aerobic Rothia sp. strain ZHT4-13 (CGMCC 2684) exopolysaccharide metabolite is new.    USE - Aerobic Rothia sp. strain ZHT4-13 (CGMCC 2684) exopolysaccharide metabolite used for flocculating agent MBF4-13 for wastewater treatment, removal of solid suspension, removal of heavy metals, decoloring dye, and improving performance of active sludge (all claimed).    ADVANTAGE - The exopolysaccharide MBF4-13 has high flocculating activity, in which flocculating rate of kaolin is up to more than 80% and removal rate of hexavalent chrome ions is up to 69.3%; and high decoloring activity for high-concentration wastewater, in which decoloring rates of methylene blue, ink blue, malachite green, and crystallized purple are up to 86.11%, 99.49%, and 97.84%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a preparation method of exopolysaccharide metabolite of aerobic Rothia sp. ZHT4-13 culture liquid.
NOVELTY - Synthetic fuel replacing gasoline and diesel oil comprises 10-70% of benzene, tar, solvent oil or mixture, 10-50% of methanol, ethanol, propanol, butanol extracted from agricultural and forest waste or mixture, 10-15% of normal butanol, isopropanol, ditertiary butyl-p-hydroxytoluene or mixture, 10-25% of bis(cyclopentadienyl) iron, kerosene, solvent oil, mineral oil, lubricating oil, vegetable oil or mixture.    USE - The synthetic fuel replacing gasoline and diesel oil is useful for replacing petrochemical gasoline.    ADVANTAGE - The invention can completely replace the petrochemical gasoline, diesel oil after applied to motor vehicle, and it has fine power effect, and can used without modifying motor vehicle, it also can be mixed with the gasoline and diesel oil according to any proportion, the materials has wide application, low production cost and fine feature of environmental protection, saving petroleum resources.
NOVELTY - Clean production of 2,3-butanediol fuel based on the resource of wheat straw comprises: (a) crushing the cellulose material comprising 61-65% of cellulose for standby; (b) adding a cellulose complex enzyme preparation; (c) adding an acid producing bacterial solution of Klebsiella based on an inoculation amount of 1-5%, and then preserving temperature and fermenting for 3-5 days at 30-40 degrees C; and (d) decompressing and distilling to obtain 2,3-butanediol fuel, where yield is 18-22% of said material by weight.    USE - The method is useful for clean production of 2,3-butanediol fuel based on the resource of wheat straw (claimed).    ADVANTAGE - Production of the 2,3-butanediol fuel is featured with low cost, and the double effects for developing the natural resources and protecting environment.    DETAILED DESCRIPTION - Clean production of 2,3-butanediol fuel based on the resource of wheat straw comprises: (a) crushing the cellulose material comprising 61-65% of cellulose for standby; (b) adding a cellulose complex enzyme preparation, based on an enzyme addition of 2-5% into the material, and then subjecting to enzymolysis for 3-5 days under the condition that pH value is 5.5-7, water addition ratio is 5-7 and temperature is 35-45 degrees C; (c) adding an acid producing bacterial solution of Klebsiella based on an inoculation amount of 1-5%, and then preserving temperature and fermenting for 3-5 days at 30-40 degrees C; and (d) decompressing and distilling to obtain 2,3-butanediol fuel, where yield is 18-22% of said material by weight.
NOVELTY - Preparation of biofuel from microalgae comprises processing wet collected microalgae into algae block/algae powder; mixing catalyst into low-carbon alcohol; directly adding algae block/algae powder; carrying out ester exchange reaction to prepare biodiesel; after finishing reaction, adding organic solvent to extract the reaction liquid, which is divided into organic solvent phase, low-carbon alcohol aqueous phase, and algae slurry; after extracting, collecting organic solvent; and removing organic solvent by distilling to obtain oil liquid, i.e. crude biodiesel.    USE - Process of preparing biofuel i.e. crude biodiesel from microalgae (claimed).    ADVANTAGE - The method extracts microalgae oil and produces biodiesel by one-step; has simplified steps and device; saves cost; and lightens downstream treatment pressure. The sulfuric acid and low-carbon alcohol can be recovered and repeatedly used after being dried, thus, reducing cost. The final product is neutral and needs no washing. The chlorophyll concentrates in low-carbon alcohol, so that interference of chlorophyll to product color is reduced, thus, there is no need to carry out decoloring step.
NOVELTY - A biofuel production apparatus comprises a chamber (110), which includes a tank (111), where the tank is formed in a conical shape having a bottom vent (112). A heater (120) for heating liquid, which is admitted to the tank, is also provided, where the heater directly heats the tank or the liquid admitted to the tank. A regulating valve (132) for controlling opening and closing of liquid, a pump (131) and a pipe (133) are also provided. The pipe is directly connected to the pump.    USE - Biofuel production apparatus.    ADVANTAGE - The biofuel production apparatus produces the biodiesel having improved efficiency and stability in a simple and cost-effective manner by using the heater, and also separates biofuel and waste discharge at same time.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biofuel production apparatus.    Chamber (110)    Tank (111)    Bottom vent (112)    Heater (120)    Pump (131)    Regulating valve (132)    Pipe (133)
NOVELTY - Helical barriers comprise millimeter-sized crystals obtained by crushing eggshells.    USE - Helical barriers for use in exterminating terrestrial mollusks. The helical barriers are arranged in lines or concentric circles or are scattered in crops alone or with natural attractants, which act by obstruct the digestive tract of terrestrial mollusks and causing starvation and preventing them to take any food.    ADVANTAGE - The helical barriers are eco-friendly.
NOVELTY - A biogas tank comprises a sealed fermenting tank (1) and a pre-decomposing tank (2), where the pre-decomposing tank (2) is provided with a material liquid outlet (3) that is connected with the fermenting tank (1).    USE - The biogas tank is useful in the industrial field.    ADVANTAGE - The biogas tank works normally even at low temperature without any heating device.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a biogas production method comprising dividing the biogas into a pre-decomposing tank and a fermenting tank comprising: (a) pre-decomposing the materials for biogas production in the pre-decomposing tank to obtain liquid and solid residue; and (b) concentrating the liquid in the fermenting tank, fermenting it to generate biogas.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of the biogas tank.    Sealed fermenting tank (1)    Pre-decomposing tank (2)    Material liquid outlet (3)
NOVELTY - An optical anode comprises a conductive glass (1), a sputtering layer (2) having bumps (3) on the conductive glass, and a nickel-iron oxide membrane layer (4) on the sputtering layer.    USE - An optical anode useful for production of hydrogen by photoelectrolysis of water (claimed).    ADVANTAGE - The anode has high optical catalysis activity and electric catalysis activity, and has low energy consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing the optical anode comprising sputtering and coating conductive glass for 1-4 hours, attaching silk screen on sputtered conductive glass, further sputtering for 1-3 hours, dipping treated conductive glass in extracting solution containing nickel salt and iron salt to form film, drying at 60-150 degrees C for 10-30 minutes, and thermally treating at 300-600 degrees C for 2-3 hours to form nickel-iron oxide membrane layer.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of an optical anode.    Conductive glass (1)    Sputtering layer (2)    Bumps (3)    Nickel-iron oxide membrane layer (4)
NOVELTY - The continuous hydrogen-production power-generation device has an anode plate and cathode plate that are arranged inside an electrolyte in the cabinet with metal particles in between. The upper and lower ends of the metal particles are respectively arranged with a screen and a diaphragm is set between the cathode plate and the metal particles. A liquid storage tank is connected to the bottom of the cabinet via a pipeline. A filter is connected with the liquid storage tank via the pipeline and is connected to the upper part of the cabinet via pump.    USE - Continuous hydrogen-production power-generation device with metalloid as material used in field of power supply and hydrogen production for supplying hydrogen to hydrogen-oxygen fuel battery, internal engine. Can also be used in connecting with family fuel gas system in parallel for supplying gas and electricity for the kitchen.    ADVANTAGE - Realizes the goals of generating power and producing hydrogen at the same time while avoiding hydrogen storage danger.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the continuous hydrogen-production power-generation device with metalloid.
NOVELTY - A weedicide synergist comprises plant steroids and solvent. The plant steroids are methylsterol, beta -sitosterol, campesterol, ergosterol and/or brassicasterol. The solvent is 10-24C fatty acid, cotton seed oil, palm oil and/or soybean oil.    USE - Weedicide synergist for weedicide composition (claimed).    ADVANTAGE - The synergist improves activity of weedicide, reduces dosage, decreases damage of weedicide to crop and surrounding sensitive crop, increases yield of crop, reduces pollution of weedicide to environment and promotes crop to grow.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a weedicide composition comprising weedicide synergist and weedicide drug.
NOVELTY - A water agent is prepared by drying and crushing Albizia julibrissin leaves into 10-50-mesh powder, adding ethanol (25-95 vol.%) in the powder, and leaching the mixture to obtain a leaching liquid; carrying out a water bath in the leaching liquid to obtain a pasty condensing liquid; and adding distilled water into the pasty condensing liquid, extracting the mixture with n-butanol, decompressing and condensing the n-butanol obtained from the extraction to obtain an Albizia julibrissin extract, and dissolving the extract in the distilled water to obtain the water agent.    USE - Method for preparing a water agent used for treating sclerotinia rot of rape (claimed).    ADVANTAGE - The prepared water agent reduces pollution of agrochemical used for preventing and treating sclerotinia rot of rape; and is harmless without residue.    DETAILED DESCRIPTION - Preparation of a water agent includes (A) taking Albizia julibrissin leaves, drying and crushing the leaves into 10-50-mesh powder, adding ethanol (25-95 vol.%) in the powder in which the weight ratio of powder to ethanol is 1:10-1:20, and leaching the mixture at 10-35 degrees C for 12-24 hours to obtain a leaching liquid; (B) carrying out a water bath in the leaching liquid at - 0.1 MPa and 40-50 degrees C to obtain a pasty condensing liquid; and (C) adding distilled water with the same weight as that of the powder into the pasty condensing liquid, then extracting the mixture with n-butanol with the same volume as that of the suspension liquid, decompressing and condensing the n-butanol obtained from the extraction to obtain an Albizia julibrissin extract, and dissolving the extract in the distilled water to obtain the water agent.
NOVELTY - The device has a liquid rubber paint device (30) that coats a fixed separator with a liquid rubber. A welding machine (40) welds the fixed separator with a phase separation plate such that the phase separation plate is laminated on the fixed separator. A mounting plate (80) places the welding machine on the liquid rubber paint device, and a mounting bracket (36) connects a cylinder device (32) and a coating valve (34). A cylinder main body (32a) is arranged in the mounting plate, and a slider (32b) is combined with the cylinder main body.    USE - Device for manufacturing a unit cell of a fuel cell.    ADVANTAGE - The device saves facility investment cost, precisely controls application of the liquid rubber, and prevents damage of an application height control device.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a unit cell manufacturing device.    Liquid rubber paint device (30)    Cylinder device (32)    Cylinder main body (32a)    Slider (32b)    Coating valve (34)    Mounting bracket (36)    Welding machine (40)    Mounting plate (80)
NOVELTY - Organic composition comprises carboxylic acid.    USE - Organic composition for renewable fuels.    ADVANTAGE - The method eliminates protein-protein interaction.    DETAILED DESCRIPTION - Organic composition comprises carboxylic acid of formula R1-CH2-CH2-CH(R2)-CH2-CH(R3)-C(O)-OH (I).    R1=H or -CH3;    R2, R3=R1 or -CH2CH3;and    n=1-6.    Provided that R2 and R3 is H, and R1 is H, -CH3, or -(CH2)nCH3. INDEPENDENT CLAIMS are included for:    (1) a polyketide synthase (PKS) capable of synthesizing carboxylic acid or lactone;    (2) a recombinant nucleic acid encoding PKS;    (3) a vector comprising recombinant nucleic acid;    (4) a host cell comprising vector, and host cell when cultured under a condition, capable of producing carboxylic acid or lactone;and    (5) a method of producing carboxylic acid and lactone comprising providing host cell, and culturing host cell in culture medium.
NOVELTY - Pollutants and disposal of vinasse by-product treatment and reduction, involves contacting vinasse with symbiotic colonies of microorganism such as fungi and bacteria. An organic reducing agent such as kefir is added to the colonies of microorganism, where solution of vinasse is dispersed on a fixed bed. The solution of vinasse is fermented from hours to multiple days, where the grains of kefir are separated from the solution of vinasse.    USE - Method for treatment and reduction of pollutants of vinasse, and for treatment of disposal of by-products produced from vinasse.
NOVELTY - Solid fuel manufacturing involves performing granule mixing process (10) of organic waste (1a) with carbides to obtain a mixture, which is dried by using drying process (20). Surface passivation process (60), charring process (30) and product evaluation process (50) are also performed. Volatile gases having carbides and hydrocarbons are generated from the dried mixture by charring process and removed by cooling adsorption process (40). The product evaluation process includes measurement of calorific value, self-inflammability and odor of the final product.    USE - Method for manufacturing solid fuel from organic waste including organic sludge and livestock excretions.    ADVANTAGE - The solid fuel manufacturing method provides solid fuel with high calorific value, low self-inflammability and bad odor, and maximizes preservation of renewable energy sources and helps in reducing global warming, thus eco-friendly in nature.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for manufacturing solid fuel from organic waste, which comprises a biaxial equation mixer for recycling water and a drying furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow chart depicting solid fuel manufacturing method. (Drawing includes non-English language text).    Organic waste (1a)    Granule mixing process (10)    Drying process (20)    Charring process (30)    Cooling adsorption process (40)    Product evaluation process (50)    Surface passivation process (60)
NOVELTY - Bioethanol high pressure liquefied extract is obtained by extracting marine algae at 500-1000 megapascal (MPa) and 60-80 degrees C in the presence of pressure medium selected from water or oil. The marine algae is fucoxanthin, rhodophyta, algae, Ulva pertusa, Ecklonia cava or Gelidium amansii.    USE - Method for obtaining bioethanol high pressure liquefied extract for producing glucose.    ADVANTAGE - The bioethanol high pressure liquefied extract obtaining method is cost-effective, effectively elevates the yield of glucose, shortens the fermentation time, and enhances the productivity of bioethanol.
NOVELTY - Sludge treatment involves preparing (S10) the sludge. An anaerobic organism reaction process is performed (S20), which includes decomposing the sludge with anaerobic microorganisms biologically. High temperature anaerobic organism reaction is performed (S30), which includes decomposing the sludge biologically with anaerobic microorganisms. A chemical process of acid is performed (S40), which includes processing the decomposed sludge with acid.    USE - Method for treating sludge discharged from sewage treatment equipment.    ADVANTAGE - The sludge treating method is cost-effective, prevents environmental contamination according to the sludge disuse, and minimizes generation of bad smell and also the generation of the final sludge through decomposition of the sludge.    DETAILED DESCRIPTION - Sludge treatment is carried out by preparing (S10) the sludge. An anaerobic organism reaction process (S20) is performed, which includes decomposing the sludge with anaerobic microorganisms biologically. High temperature anaerobic organism reaction (S30) is performed, which includes decomposing the sludge biologically with anaerobic microorganisms. A chemical process of acid is performed (S40), which includes processing the decomposed sludge with acid. A solid-liquid separation process is performed, which includes separating the sludge. Another chemical processing of acid (S60) is performed by processing the separated sludge with acid. The sludge is discharged after the latter chemical process of acid. The discharged sludge is recirculated multiple times.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of the sludge treatment process. (Drawing includes non-English language text).    Preparing sludge (S10)    Performing anaerobic organism reaction process (S20)    Performing high temperature anaerobic organism reaction process (S30)    Performing chemical processes of acid (S40,S60)    Solid-liquid separation process (S50)
NOVELTY - A coal tar which is chemical by-product of coal is mixed with caustic soda, preheated, and injected into slurry reactor (2) to gasify coal tar mixture. The obtained gasified coal tar mixture is passed through steam reforming reactor (4) and pressure swing adsorption tower (5) to obtain hydrogen.    USE - Method for producing hydrogen gas used as raw material for chemical products.    ADVANTAGE - The method provides highly pure hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows block diagram illustrating the production of hydrogen. (Drawing includes non-English language text)    Mixing reactor (1)    Slurry reactor (2)    Separator (3)    Steam reforming reactor (4)    Pressure swing adsorption tower (5)
NOVELTY - Hydrogen production with solar concentrators and feedstock recycled through carbon dioxide (CO_2), is disclosed. The use of solar energy for production of clean and economical hydrogen gas, by avoiding the costly furnace oil for heating the reformer of hydrocabons such as methanol and avoiding the pollution, is also disclosed. The unwanted reformation byproduct CO_2 is gainfully used by electrochemically combining it with water to synthesize methanol and recycle it to the reformer, and the cost of CO_2 sequestration is avoided. The electrical energy required for the electrochemical reaction to convert CO_2 to methanol is also derived from solar energy, through more efficient photovoltaic concentrator. Hydrogen fed fuel cell for power generation would also provide electrical energy for this reaction. By using CO_2 from the atmosphere and adequate solar/fuel cells energy, full requirement of the reformer would be made up by this synthesis, and this system can be made self-sustaining. Image 0/0
NOVELTY - An improved biomass gasifier essentially comprises a main cylindrical body and an inner cylindrical compartment, the outer main body is provided with a top cover or lid which is preferably hinged at one end. The top cover is provided with two tubes, one for injecting steam and the other being an outlet. The inner compartment is housed within the main body and the space between the two sealed compartments is filled with biomass; the outer wall of the inner compartment is provided with multiple fins. A source of heat is adapted and located at the bottom of the inner compartment for supplying a temperature between 6000?oC and 8000?oC to the biomass, thus producing biogas by the processes of bio-methanation and bio-gasification. Image 1/1
NOVELTY - Synthesis of biodiesel using a novel super turbulent intense mixing reactor, is disclosed. More particularly, a versatile system for continuous production of biodiesel, is disclosed. Image 0/0
NOVELTY - Invention related to fuel energy production field. Particularly to heat producing element - device for energy production by burning down sawdust, characterised that chipped pulp distributed with even layer on a base - paper tape and created sandwich rolled into multi layered roll with a central canal along the longitude axes.    USE - Oil-and-gas production.    ADVANTAGE - Production of easily manufactured, ecologically clean and convenient in use fuel, which can be used as independently as in heating devices for every day use, also in field work conditions. 2 dwg
NOVELTY - Method involves placing a filter in the contamination zone, where the filter is filled with sorbing medium, populated with oil oxidising microorganisms. The sorbing medium used is floating agal plantation, the base of which is a system of joined synthetic ropes, planted with laminaria and focus algae. Laminaria is placed deep in the water on vertical ropes of length 5 m, and focus algae are placed on horizontal ropes in the surface layer.    USE - Chemistry.    ADVANTAGE - Invention increases rate of converting oil contaminates dispersed on the sea surface to products which are safe for marine biota, increases service life of the proposed protective structure due to processes of natural development and restoration of association of algae and oil oxidising bacteria. 8 tbl
NOVELTY - The portion of combustible fuel is converted into electrical energy using fuel cell (104). The unutilized portion fuel is combusted to generate heated gas. The power recovery turbines (168,170) connected to drive shaft (144) are driven using the heated gas. The source of input oxidizing gas is compressed using compressor (140). The combustible fuel is converted into electrical energy using the compressed oxidizing gas. The exhaust energy (132) is recovered during conversion of combustible fuel into mechanical power to provide pressurized source of conditioned air.    USE - Method for generating electric power in aircraft system.    ADVANTAGE - The electrical and pneumatic powers are supplied efficiently to the aircraft system. The weight and the cost of the aircraft are reduced by using heated gas to mechanically drive the power recovery turbine.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the auxiliary power unit (APU) and environment control system.    Fuel cell (104)    Exhaust energy (132)    Compressor (140)    Drive shaft (144)    Power recovery turbines (168,170)
NOVELTY - Process for removing haze from a biofuel or biofuel intermediate, comprises: mixing the biofuel or biofuel intermediate with a clarifier comprising a copolymer at a concentration sufficient to clarify the biofuel or biofuel intermediate, where the copolymer is prepared using a formulation comprising an alpha olefin and maleic anhydride.    USE - The process is useful for clarifying the biofuel or biofuel intermediate (biodiesel), by removing the haze from the biofuel or biofuel intermediate to produce biofuel (all claimed).    ADVANTAGE - The process reduces the haze and/or contaminants to a predetermined level i.e. the process reduces or removes water soluble and water dispersible contaminants e.g. metal salts or oxides and process catalysts and the process provides decreased water concentration in biofuels and biofuel intermediates and, feedstocks.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) the clarifier; and    (2) the biofuel prepared according to the process.
NOVELTY - A body-worn type fuel cell system (10) comprises fuel cell main body (12) which supplies hydrogen gas by introducing water vapor emitted from body into hydrogen producing material (14) and decomposing water molecule.    USE - A body-worn type fuel cell system for microdevice e.g. cardiac pacemaker.    ADVANTAGE - The small-sized body-worn type fuel cell system has larger electric generating capacity than button battery, improves performance of integrated circuit (IC) card, and lengthens validity period of fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the body-worn type fuel cell system.    Body-worn type fuel cell system (10)    Fuel cell main body (12)    Hydrogen producing material (14)    Container (16)    Gasket (18)
NOVELTY - A dry distillation liquid manufacturing apparatus (1) comprises pyrolysis furnace (2) which carries out radiation heating of vegetable carbohydrate which is raw material by coal fire and produces smoking, water storage tank (3) which stores water for carrying out water solubility of smoking, flue (4) which smoke-induces smoking into water storage tank from upper part of pyrolysis furnace, and suction mixing pump (5) which makes smoking microbubble and discharges it in water in water storage tank while installing in tip part of flue in water in water storage tank and sucking smoking from flue.    USE - A dry distillation liquid manufacturing apparatus.    ADVANTAGE - The apparatus extracts and collects dry distillation component contained in raw material of vegetable carbohydrate efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of dry distillation liquid manufacturing apparatus.    Dry distillation liquid manufacturing apparatus (1)    Pyrolysis furnace (2)    Water storage tank (3)    Flue (4)    Suction mixing pump (5)
NOVELTY - The method involves storing communal waste in quarter. A ditch having 3-5 m deep is hollowed and filled with sewage sludge up to the level of 1m below the surface. The sewage sludge is covered with the layer of communal waste which is dug out during ditch hollowing.    USE - Method for sewage sludge utilization for intensification of biogas production in refuse collection depot.    ADVANTAGE - The biogas can be utilized efficiently for energy purposes when the content of methane exceeds 30%. Since the effect of methane is stronger than the greenhouse effect, the biofilters are employed for methane oxidation such that the influence of methane on greenhouse effect is eliminated effectively.
NOVELTY - The fuel processing apparatus has suction portions (33a,33b) that suck the evaporative emission containing two or more fuel components of different properties. A pair of purge valves (38,39) is provided in the purge pipes (35,36) respectively connected to the suction portions, for adjusting the amount of gas emission from the suction portions. An electronic control unit (ECU) (50) is set to control opening degree of purge valves respectively so that the amount of purge of every suction portion is adjusted.    USE - Evaporative fuel processing apparatus of internal combustion engine.    ADVANTAGE - The amount of gas emission in the evaporative fuel can be adjusted optionally by purge valves respectively connected to the suction portions. The component ratio in the purge gas can be suitably changed according to the driving state of the engine. The component ratio of the emitted gas can be changed suitably since the amount of gas emission is changed according to air fuel ratio of the engine. The engine output can be increased efficiently at the time of high load of engine so that performance of engine is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the evaporative fuel processing system. (Drawing includes non-English language text)    Surge tank (16)    Suction portions (33a,33b)    Purge pipes (35,36)    Purge valves (38,39)    ECU (50)
NOVELTY - An aerobic tank (20) processes the to-be-processed water with an activated sludge, flowing in aerobically. An aeration unit (22) supplies micro-bubbles in the aeration tank. An aerobic tank (30) is set with a membrane unit (34) which carries out membrane separation of activated sludge. Based on detected value of ammoniacal nitrogen (NH4-N) concentration in to-be-processed water, the air flow of aerobic tank (20) is adjusted and the concentration of the ammoniacal nitrogen in the tanks is controlled to a processible concentration.    USE - Membrane separation activated sludge processing equipment.    ADVANTAGE - The driving motive power required for the whole apparatus and the aeration unit can be reduced, and the repair of the equipment or the maintenance works of the aeration tanks can be performed efficiently, while improving the scale of the facility. The concentration of ammoniacal nitrogen can be adjusted rapidly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for membrane separation activated sludge processing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the membrane separation activated sludge process equipment.    Aerobic tanks (20,30)    Aeration unit (22)    Membrane unit (34)    Piping (35)    Suction pump (36)
NOVELTY - Manufacture of synthesis gas from a compound which contains carbon and hydrogen or carbon, hydrogen and oxygen involves separating oxygen by supplying oxygen containing gas to oxygen permeating unit, combustion processing by burning a part of synthesis gas using the separated oxygen, supplying compound consists of hydrogen and carbon or hydrogen, carbon and oxygen and mixing with the combustion product, modification reaction processing to produce synthesis gas, recycle processing by supplying part of synthesis gas to the combustion processing and collecting remaining synthesis gas.    USE - Manufacture of synthesis gas from a compound which contains carbon and hydrogen or carbon, hydrogen and oxygen for fuel cell system (claimed), hydrogen station, petroleum refinery, factory, methanol synthesis reaction and Fischer-Tropsch reaction.    ADVANTAGE - Carbonization during material input is prevented and has high reaction efficiency.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) manufacturing apparatus of synthesis gas; and    (2) fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of synthesis gas manufacturing apparatus.    Manufacturing apparatus (100)    Combustion apparatus (200)    Oxygen-permeating film (210)    Combustion part (220)    Supply apparatus (300)    Connecting device (350)    Product measurement part (352)    Modifier (400)    Modification reaction part (410)    Partition plate (420)    Recycle apparatus (500)    Second connection part (510)    Recycle part (511)    Collection part (512)    Recycle control part (520)
NOVELTY - Producing coal, preferably coal slurry from wet biomass, preferably sewage slurry by hydrothermal carbonization, comprises concentrating the biomass by dewatering to a value of above 10% dry substance portion, prior to the hydrothermal carbonization; adjusting the pH of the biomass to less than 4, prior to the hydrothermal carbonization; and subsequently drying the resulting product by process-waste heat originated from the hydrothermal carbonization, where the carbon structures of the biomass are broken preferably at 180-200 degrees C under airtight.    USE - The method is useful for producing coal, preferably coal slurry.    ADVANTAGE - The method reduces chemical costs and high operating costs. The method provides coal with high quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an apparatus for carrying out the above method.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of a system for the production of coal.    Hydrocyclone (1)    Collection container (2)    Decanter (3)    Dosing equipment (4)    Pump. (5)
NOVELTY - A water-preserving organic fertilizer comprises (wt.%) pig excrement (85-99) and water-preserving materials polyacrylamide (0.5-10) and modified starch (0.5-10). The pig excrement is a powdered pig excrement which is thoroughly decomposed and crushed.    USE - A water-preserving organic fertilizer for protecting seedling, resisting drought and accelerating growth.    ADVANTAGE - The method removes the bad smell of raw pig excrement and kill the ovum of pathogenic bacteria. The organic fertilizer is convenient to transport. The polyacrylamide and modified starch enable the fertilizer to preserve water.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of water-preserving organic fertilizer comprising:    (A) adding effective microorganisms microbial inoculum (0.1-0.2% of weight of pig excrement) and water into pig excrement, uniformly mixing to obtain a water content of less than 35-45%, stacking the mixture into a bar-shaped taper which is 2 m wide and 0.5 m high and has no length limit, sealing with a plastic film for 10-15 days, and controlling temperature at 60-70 degrees C to thoroughly decompose the pig excrement; and    (B) drying pig excrement which is thoroughly decomposed and crushing, adding water-preserving material polyacrylamide and modified starch into pig excrement powder, uniformly mixing, and pressing the mixture into grains with diameters of 1-5 mm to obtain the finished product.
NOVELTY - The low-tar biomass gasification furnace has furnace body, internal furnace, gasifying agent inlet pipe, collecting pipe, catalytic cracking chamber and gas-liquid separating chamber. There gasified fuel discharged out from top of gasification furnace flows into catalytic cracking chamber in an interlayer shape outside the furnace heath. The catalytic cracking chamber clings to the furnace hearth, and is equipped with catalyst. The gasifying agent inlet tube is a telescopic thrust jet shaped pipe section, in which gasifying agent is air.    USE - Gasification furnace for residential use to produce low-tar biomass.    ADVANTAGE - Enables to satisfy low-tar content requirement for fuel produced by small resident biomass gasification furnace without generating secondary contamination, and enhances gas production efficiency of low-tar biomass gasification furnace. Provides low-tar biomass gasification furnace with simple structure and easy application.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of low-tar biomass gasification furnace.
NOVELTY - The generation device has electrolytic tank which includes negative electrode plates, positive electrode plates and neutral electrode plates. The neutral electrode plates are located on outermost side of electrolytic electrode plate. An input terminal of electronic driving apparatus preferably as adjustable pulse width modulator is connected to direct current power source, while the output terminal is respectively attached to negative electrode plates and positive electrode plates of electrolytic tank.    USE - Generation device for producing combustion-supporting gas e.g. hydrogen and oxygen used in internal combustion engine or motor of automobile.    ADVANTAGE - Provides generation device with safe and convenient installation, and good energy efficiency. Effectively and noticeably improves efficiency of internal combustion engine since hydrogen and oxygen can be produced, thus saving fuel, reducing discharge of toxic waste gas, and protecting environment.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of generation device.
NOVELTY - The pressure bearing water tank has internally placed cage type electrode provided in stainless steel liner to be used as electrode for producing hydrogen, and made from conducting silica gel. The water tank increases the oxygen content of water near the inner wall of stainless steel liner to increase oxidization restoration capability of stainless steel inner wall suffered from chlorine corrosion. The water electrolyzing loop includes stainless steel liner, internally placed cage type electrode and power supply e.g. photovoltaic power supply or photovoltaic charge power supply.    USE - Pressure bearing water tank used for producing oxygen through electrolysis of water to resist chlorine corrosion of inner wall.    ADVANTAGE - Prolongs lifespan of pressure bearing water tank by 10 years by using internally placed cage type electrode and power supply with low power.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of pressure bearing water tank.
NOVELTY - A water purifying filter (30) contains mineral component for purifying natural water. A water tank (40) receives the clean water and a water intake cock (12) is used for providing the clean water to the outside. An ion exchange resin filter (90) is provided between the water purifying filter and a water tank (50) to provide the distilled water to the water tank (50). The hydrogen is produced from an electrolyzer (60) to the water tank (40) through a hydrogen supply pipe (70).    USE - Water purifier for purifying natural water into clean water for drinking purpose.    ADVANTAGE - The quality of the recycled water is improved by transmitting the dissolved mineral component to the water tank, so that the damage of the electrolyzer is prevented. The blockage and damage of the separation portion, anode plate and cathode plate are prevented. The residual time for purifying the water is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the water purifier.    Water intake cock (12)    Water purifying filter (30)    Water tanks (40,50)    Electrolyzer (60)    Hydrogen supply pipe (70)    Ion exchange resin filter (90)
NOVELTY - A photoelectrochemical hydrogen production reactor has gas storing device formed in a connected state with reaction chamber. A fixing device, located in the first reaction chamber is provided to attached the anode with respect to the cathode. The reaction chamber is provided to perform mix production of the oxygen and hydrogen.    USE - Photoelectrochemical hydrogen production reactor.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for    (1) measuring method of the optical-electric energy conversion efficiency; and    (2) a photoelectrochemical hydrogen production system    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic perspective view of the reactor.
NOVELTY - A sewage treatment system comprises a grill, a water-collecting sedimentation tank, an overhead flood relief channel, and a constructed wetland. The grill is in front of the water-collecting sedimentation tank. The water yielded from the water-collecting sedimentation tank is pumped to the overhead flood relief channel through a sewage pump. The flood relief opening of the overhead flood relief channel is above the water inlet end of the constructed wetland, over 500 mm higher than the water surface of the constructed wetland.    USE - Sewage treatment system for constructed wetland.    ADVANTAGE - The system is simple in structure and can effectively increase the treatment effect of the constructed wetland and increase the degree of purification of the water yielded from the constructed wetland.    DETAILED DESCRIPTION - A sewage treatment system comprises a grill, a water-collecting sedimentation tank, an overhead flood relief channel, and a constructed wetland. The grill is in front of the water-collecting sedimentation tank. The water yielded from the water-collecting sedimentation tank is pumped to the overhead flood relief channel through a sewage pump. The flood relief opening of the overhead flood relief channel is above the water inlet end of the constructed wetland, over 500 mm higher than the water surface of the constructed wetland. The flood relief weir of the overhead flood relief channel is horizontal and extends with a width smaller than or equal to the width of the water inlet end of the constructed wetland under it. The constructed wetland is of a horizontal deflection structure, and the water discharging end is provided with a water storage tank. A horizontal baffle partition board or partition wall can be installed in the constructed wetland.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic flow diagram of the sewage treatment system for constructed wetland.
NOVELTY - Sewage treatment system comprises a grill placed in front of a water-collecting sedimentation tank, an aeration tank, and a constructed wetland. The water yielded from sedimentation tank is connected to aeration tank through a sewage pump. Several horizontal baffle plates that are parallel to each other are placed in constructed wetland to divide the wetland into several water flow passages which are parallel to each other and connected in series. Aerators separated from one another are distributed at the bottom of water flow passages.    USE - A high-efficiency sewage treatment system for constructed wetland.    ADVANTAGE - The system is simple in structure and can effectively increase the treatment effect of the constructed wetland and increase the degree of purification of the water yielded from the constructed wetland.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic flow diagram of the high-efficiency sewage treatment system for constructed wetland.
NOVELTY - A sewage treatment system comprises an anaerobic hydrolytic tank, and a constructed wetland. The water yielded from anaerobic hydrolytic tank enters a water inlet end of the constructed wetland through a water pump and a pipeline. The water inlet end of the constructed wetland is provided with an overhead flood relief channel, in which the yielded water flows from the water pump. A mechanical grill is installed in front of the anaerobic hydrolytic tank. Bottom of anaerobic hydrolytic tank is provided with a sludge scraping device.    USE - A sewage treatment system for constructed wetland using hydrolytic pre-treatment.    ADVANTAGE - The land space occupied by the sewage treatment system is small and the system can treat sewage with comparatively high concentration at low cost.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic flow diagram of a sewage treatment system for constructed wetland using hydrolytic pre-treatment.
NOVELTY - A combined sewage treatment system comprises a mechanical grill, an aeration water-collecting tank, a sedimentation tank, and a constructed wetland connected one by one. The bottom of aeration water-collecting tank is provided with an aeration device that aerates to the tank, and the bottom of the sedimentation tank can be connected with a sludge pump. A discharging pipe of the sludge pump is connected with a sludge concentrating tank. The constructed wetland is of a horizontal deflection structure.    USE - Combined sewage treatment system for constructed wetland.    ADVANTAGE - As the aeration device is added to the water-collection tank to form an aeration water-collecting tank, aeration and aerobic treatment are realized at the same time while collecting water and consequently the pollutants in the sewage are reduced, which is conducive to the subsequent sludge sedimentation in the sedimentation tank, effectively separates the sludge from the sewage, saves the space and device, as well as avoids the fermentation and peculiar smell during the water-collecting process. The horizontal deflection structure of the constructed wetland increases the treatment effect. This system can treat sewage with comparatively high concentration and the expense for the preliminary treatment is low.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic flow diagram of the combined sewage treatment system for constructed wetland.
NOVELTY - A high-concentration sewage treatment system comprises artificial wetland as main treatment object. The matrix of artificial wetland is sand-soil mixture, crushed stone, zeolite, limestone, slack, steel slag, blast furnace slag, porcelain granule, melon-seed sheet and/or cobble, where mussels are cultivated in the artificial wetland.    USE - High-concentration sewage treatment system.    ADVANTAGE - The system has simple structure, decomposes macromolecular organic substance to small molecular organic substance; reduces contaminations in water through active mud tank and secondary sedimentation tank; increases oxygen content in water; improves biochemical process in artificial wetland; and can effectively treat high-concentration sewage and obtains good purification effect.
NOVELTY - A high effective aerobic biochemical and artificial wetland sewage treatment system comprises barrier, first precipitate pool, venturi pipe, splash board, aeration pool and second precipitate pool connected by turns. The barrier is before first precipitate pool, where inlet of tapered part of the venturi pipe is connected with upper part of the first precipitate pool by high-pressure pump, throat part is connected with atmosphere by gas inlet pipe, and outlet of increasing part is equipped with jet current pipeline extending forwards.    USE - High effective aerobic biochemical and artificial wetland sewage treatment system for treating domestic sewage.    ADVANTAGE - The system decomposes organic substances by aeration pool, reduces concentrations of pollutants in water, and has simple structure, convenient operation, good suitability, high content of oxygen in sewage, and good clean-up effect.    DETAILED DESCRIPTION - The high effective aerobic biochemical and artificial wetland sewage treatment system comprises barrier, first precipitate pool, venturi pipe, splash board, aeration pool and second precipitate pool connected by turns. The barrier is before first precipitate pool, where inlet of tapered part of the venturi pipe is connected with upper part of the first precipitate pool by high-pressure pump, throat part is connected with atmosphere by gas inlet pipe, and outlet of increasing part is equipped with jet current pipeline extending forwards. The splash board is before jet current pipe and above aeration pool. The aeration pool is equipped with fixed packed bed. The second precipitate pool is behind aeration pool and is connected with water outlet of aeration pool.
NOVELTY - A sewage treatment system comprises first sedimentation tank, venturi pipe, active vortex slurry tank, second sedimentation tank and artificial wetland. The inlet in decreasing part of venturi pipe is connected with upper part of first sedimentation tank by high pressure pump, where throat is connected with atmosphere by air inflow pipe, and outlet in increasing part is equipped with ejecting pipe extending toward front part. The ejecting pipe is connected with lower part of active vertex slurry tank in tangent direction.    USE - Sewage treatment system for treating domestic sewage.    ADVANTAGE - The system has simple structure, convenient operation, good application, high oxygen content in sewage, and good purification effect.    DETAILED DESCRIPTION - The sewage treatment system comprises first sedimentation tank, venturi pipe, active vortex slurry tank, second sedimentation tank and artificial wetland. The inlet in decreasing part of venturi pipe is connected with upper part of first sedimentation tank by high pressure pump, where throat is connected with atmosphere by air inflow pipe, and outlet in increasing part is equipped with ejecting pipe extending toward front part. The ejecting pipe is connected with lower part of active vertex slurry tank in tangent direction. The second sedimentation tank is behind active vertex slurry tank and connected with its water outlet. The water outlet of second sedimentation tank is connected with the artificial wetland.
NOVELTY - An artificial wetland sewage treatment system comprises first sedimentation tank, venturi tube, contacting oxidization tank, secondary sedimentation tank and artificial wetland, where tapered portion inlet of venturi tube is connected with upper portion of first sedimentation tank by high-pressure pump, throat portion of venturi tube is connected with air by intake pipe, and jet pipe extending upwards is arranged at outlet of expanding portion. The jet pipe is connected with lower portion of contacting oxidization tank along radial direction.    USE - Artificial wetland sewage treatment system for treatment of living sewage.    ADVANTAGE - The system has simple structure, convenient operation, good adaptability, good purification effect and stable technique, and does not cause major fluctuation of treating effect because of change of water yield. The content of oxygen in sewage is high.    DETAILED DESCRIPTION - The artificial wetland sewage treatment system comprises first sedimentation tank, venturi tube, contacting oxidization tank, secondary sedimentation tank and artificial wetland, where tapered portion inlet of venturi tube is connected with upper portion of first sedimentation tank by high-pressure pump, throat portion of venturi tube is connected with air by intake pipe, and jet pipe extending upwards is arranged at outlet of expanding portion. The jet pipe is connected with lower portion of contacting oxidization tank along radial direction, where fixed filling material bed is arranged at middle of contacting oxidization tank, water distributing hole board is arranged under fixed filling material bed and is placed above connection position of jet pipes, and discharged water of secondary sedimentation tank flows in artificial wetland.
NOVELTY - An aerobic biochemical sewage treatment system comprises grid, first sedimentation tank, venturi pipe, splash board and artificial wetland connected in series. The grid is in front of first sedimentation tank. The inlet in decreasing part of the venturi pipe is connected with upper part of first sedimentation tank by high pressure pump, where throat is connected with atmosphere by air inflow pipe, and outlet in increasing part is equipped with ejecting pipe extending toward front part, and splash board is above artificial wetland in front of ejecting pipe and above aerobic tank.    USE - Artificial wetland aerobic biochemical sewage treatment system for treating domestic sewage.    ADVANTAGE - The system exhibits efficient aeration, improves ambient environment and cleaning degree of water, has simple structure, convenient operation, and good application, and allows large variation of sewage amount.
NOVELTY - A sewage treatment system comprises grid, water tank, flocculating mixing tank, sedimentation tank, aeration tank and artificial wetland which are connected in order.    USE - Sewage treatment system for treating living sewage and other similar organic sewages.    ADVANTAGE - The high-concentration contaminations entering into sewage of artificial wetland and some contaminations not easily treated by biochemical method can be taken out via the way of flocculating precipitation, thus reducing content of contamination entering into sewage of the artificial wetland, reducing area of artificial wetland and sedimentation of contamination in artificial wetland, and avoiding blocking.
NOVELTY - An artificial wetland treatment system comprises anoxic hydrolysis tank, venturi tube, splash board and artificial wetland, which are connected to each other in order, where inlet of gradually shrinking part of venturi tube is connected to upper part of anoxic hydrolysis tank through high pressure pump, and throat part is connected to atmosphere through inlet pipe. The outlet of gradually expanding part is equipped with jetting pipeline extended forwards. The splash board is provided over artificial wetland in front of jetting pipeline.    USE - An artificial wetland treatment system for high concentrated wastewater (claimed).    ADVANTAGE - The artificial wetland treatment system has simple structure, has easily obtained aerobic biochemical micromolecular organic material, and has improved operation condition and purification effect.
NOVELTY - A mushroom compost is prepared by weighing, mixing, crushing, agitating and fermenting mixture containing 35-55 wt.% of wheat straw hood, 25-45 wt.% of straw, 10-16 wt.% of bean cake, 1.5-2 wt.% of dry dairy manure, 0.5-1 wt.% of rice chaff, 0.5-1 wt.% of urea, 0.5-1 wt.% of plaster, 1.5-2 wt.% of chicken manure, 0.1-0.3 wt.% of ammonium sulfate, 0.1-0.3 wt.% of nitrogen-phosphorus-potassium composite fertilizer, 0.1-0.3 wt.% of calcium carbonate and 0.5-0.8 wt.% of calcium superphosphate.    USE - Preparation of mushroom compost.
NOVELTY - A maitake compost is prepared by using (wt.%) cotton seed hull (45-55), bean cake (4-12), corn powder (3-9), corn cob (4-12), rice bran powder (3-9), beanstalk powder (8-12), dry human excrement (3-11), compound fertilizer of phosphorus and potassium (1-3), plaster (0.5-1), lime (0.5-1), kemeling liquid (0.5-1) and oxygenated powder (0.5-1).    USE - Preparation of maitake compost.
NOVELTY - The gas furnace has blower (14) which is connected to bottom of furnace body (5). An exhaust tube (9) communicates to filter barrel (8) set outside the furnace body. A gas conveying tube (7) is connected to filter barrel, and conveys gas to outside. A furnace core (12) communicates to air outlet of blower, and is set at furnace bottom middle in furnace body. The furnace core is a tube provided with through holes (11) in surface. A closing plate (10) is fixed on top end of furnace core.    USE - Gas furnace.    ADVANTAGE - Avoids flameout phenomenon in gas furnace, and simplifies structure of gas furnace with low energy consumption.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of gas furnace.    Furnace body (5)    Gas conveying tube (7)    Filter barrel (8)    Exhaust tube (9)    Closing plate (10)    Through holes (11)    Furnace core (12)    Blower (14)
NOVELTY - The solar greenery gasifier has double layer vacuum glass plate, rectangular container made of iron, asbestos insulated board, and bracket. The double layer vacuum glass plate is installed on surface of rectangular container. Other surfaces of rectangular container are provided with asbestos insulated board, and fixed on the bracket together.    USE - Solar greenery gasifier.    ADVANTAGE - Provides solar greenery gasifier with integrated structure since rectangular container and double layer vacuum glass plate are supported by bracket to make the side of rectangular container face to the sun.    DESCRIPTION OF DRAWING(S) - The drawing shows the perspective view of solar greenery gasifier.
NOVELTY - The oxygen-hydrogen generator is composed of electrolytic power supply and electrolytic tank. The electrolytic tank is composed of the first electrolytic tank and the second electrolytic tank which are closed and connected in series and communicates with each other. The tank bodies of the first electrolytic tank and second electrolytic tank are composed of tank outer layer and tank inner layer in the form of double-layer homocentric column. The outlet joint is connected with inlet tube of cylinder of internal-combustion engine, and is set on second electrolytic tank.    USE - Oxygen-hydrogen generator for internal-combustion engine.    ADVANTAGE - Improves the power and the combustion efficiency of internal-combustion engine. Reduces the combustion consumption, the waste gas discharge, and the carbon deposit in internal-combustion engine. Prolongs the service life of the internal-combustion engine.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of the oxygen-hydrogen generator.
NOVELTY - An electromagnetic dissociation of water involves heating by irradiating with radio frequency (RF) energy or with photons.    USE - For electromagnetic dissociation of water (claimed) to combust salt water, to produce hydrogen from salt water or solutions containing salt water, to volatilize a secondary fuel present in solutions containing salt water, to produce and combust hydrogen obtained from salt water or solutions containing salt water, to volatilize and combust secondary fuel sources present in solutions containing salt water, to desalinate seawater, and/or to carry out the electrolysis of water.    ADVANTAGE - The RF generator is capable of generating an RF signal absorbable by the salt water solution or the salt water mixture having a frequency for transmission via the transmission head and an RF receiver. The method may be performed once or repeatedly, or continuously, or periodically, or intermittently. A frequency for operation of the RF signal may be selected such that the frequency (or its harmonic) is the same as or overlaps with (either partially or completely) specific RF frequencies capable of stimulating or exciting any of the various energy levels of any of the various metal species comprising metal salts or metal compounds that are dissolved or distributed within the soils. Since soils often contain moisture or the metal species present in the soils and clays have water molecules coordinated to them, it is therefore believed that the method could be used to heat and process such metal-containing soils. The soils of contaminated commercial residential and industrial sites, hazardous waste dump sites, gas stations, could be remediated using the method. The method could be coupled with known extraction and remediation processes and methods for in-situ treatment of contaminated soils.
NOVELTY - A steam reformer comprises combustion chamber (118) having an inlet and outlet, combustion catalyst is disposed in the combustion chamber; and reformation chamber having inlet and outlet, reformation catalyst (136) is disposed in reformation chamber, where the combustion catalyst and reformation catalyst are disposed on opposite faces of separation plate disposed between combustion chamber and reformation chamber (132); and where combustion chamber has a volume of less than or equal to 0.05 ml.    USE - As steam reformer useful in a fuel cell (claimed).    ADVANTAGE - The steam reformer provides microcombustors and microreformers which can be made with a very small size and which can operate at low temperature. The steam reformer also provides devices utilizing the microcombustors and/or microreformers instead of more conventional devices such as batteries. The low temperature operation and manufacturing made possible by the reformer allows greater choice of insulating materials, enables greater use of materials with dissimilar thermal expansion coefficients, and enables manufacture on semiconductor chips. The combustors and reformers can be made from plastic including low weight and less required insulation. The additional advantages include more design options, cheap high volume manufacturing, eliminating the need for expensive manufacturing machines (compared to the equipment used in silicon processing), and inexpensive materials.    DESCRIPTION OF DRAWING(S) - The figure shows a cross-sectional view of microreformer.    Combustion chamber (118)    Exhaust channel (120)    Opening (122)    Combustion catalyst (124)    Reforming catalyst (128)    Fuel supply channel (130)    Reformation chamber (132)    Reformation catalyst (136)
NOVELTY - The method involves separating two sides of an end plate with a cell, and laminating the end plate, where two sides of the end plate are pressurized. The end plate is connected with the cell.    USE - Method for manufacturing a fuel cell (claimed).    ADVANTAGE - The method enables reducing the thickness of the end plate so as to reduce the size of the cell.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a fuel cell comprising an end plate.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of a fuel cell manufacturing method.'(Drawing includes non-English language text)'
NOVELTY - A hydroxy fatty acid derivative (I) is used as a fuel or a fuel additive.    USE - Use of hydroxy fatty acid derivative as fuel, and additive for fuel such as gasoline, diesel oil, and alcohol fuel such as ethanol, normal propyl alcohol and normal butyl alcohol (all claimed).    DETAILED DESCRIPTION - A hydroxy fatty acid derivative of formula: HO-C(-H)(-R2)-(CH2)m-C(=O)-OR1 (I) is used as a fuel.    m = 0-3;    R1 = 1-5C alkyl or alkali metal ions:and    R2 = H and 1-17C alkyl.    An INDEPENDENT CLAIM is also included for a fuel composition containing fuel(s) and a hydroxy fatty acid derivative (I).
NOVELTY - Preparing nanocrystalline nickel oxide materials (I), comprises: (a) introducing a nickel starting compound into a reaction chamber using a carrier fluid, where the nickel starting compound is an inorganic nickel salt and is in the form of a solution, slurry, suspension or in the solid state of aggregation; (b) thermally treating the nickel compound in a treatment zone by a pulsating flow at 200-550 degrees C; (c) making nanocrystalline nickel oxide materials; and (d) introducing the obtained nanocrystalline nickel oxide materials into the reactor.    USE - (I) is useful as a catalyst or catalyst precursor for chemical reactions comprising hydrogenation, methanation, alkylation of amines, amination of alcohols, polymerization reaction or Kumada's coupling (all claimed).    ADVANTAGE - The process provides (I) with large BET surface area and high catalytic activity (after reduction to nickel-metal). The process is easy to perform and inexpensive. (I) is suitable for industrial use. The process can be carried out at relatively low temperatures (i.e. 200-550 degrees C, preferably 250-480 degrees C).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) the nanocrystalline nickel oxide materials, characterized by a Brunauer-Emmer-Teller (BET) surface area of more than 100 m2/g; and    (2) a catalyst obtained by reduction of nanocrystalline nickel oxide material.
NOVELTY - Preparing nanocrystalline nickel oxide materials (I), comprises: (a) introducing a nickel starting compound into a reaction chamber using a carrier fluid, where the nickel starting compound is an inorganic nickel salt and is in the form of a solution, slurry, suspension or in the solid state of aggregation; (b) thermally treating the nickel compound in a treatment zone by a pulsating flow at 200-550 degrees C; (c) making nanocrystalline nickel oxide materials; and (d) introducing the obtained nanocrystalline nickel oxide materials into the reactor.    USE - (I) is useful as a catalyst or catalyst precursor for chemical reactions comprising hydrogenation, methanation, alkylation of amines, amination of alcohols, polymerization reaction or Kumada's coupling (all claimed).    ADVANTAGE - The process provides (I) with large BET surface area and high catalytic activity (after reduction to nickel-metal). The process is easy to perform and inexpensive. (I) is suitable for industrial use. The process can be carried out at relatively low temperatures (i.e. 200-550 degrees C, preferably 250-480 degrees C).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) the nanocrystalline nickel oxide materials, characterized by a Brunauer-Emmer-Teller (BET) surface area of more than 100 m2/g; and    (2) a catalyst obtained by reduction of nanocrystalline nickel oxide material.
NOVELTY - The housing (100) comprises a box (170), a hollow chamber formed in the box, a cartridge inserted into the hollow chamber and producing hydrogen, a moisture removing layer (174), which is formed at the wall of the hollow chamber, comprises a chemical hydride and is structured to a form that is similar to a web, a sealing material, and a control element, which is electrically connected to the cartridge and controls the quantity of the produced hydrogen. The box comprises a container (176) having the hollow chamber whose side is open, and a lid (178), which covers the opened hollow chamber.    USE - Housing useful in a device for producing hydrogen in fuel cell power generation system (all claimed).    ADVANTAGE - The housing increases the efficiency of the device for generating hydrogen in an environmental-friendly manner, and improves water efficiency and stability and the yield of the hydrogen.    DETAILED DESCRIPTION - The housing (100) comprises a box (170), a hollow chamber formed in the box, a cartridge inserted into the hollow chamber and producing hydrogen, a moisture removing layer (174), which is formed at the wall of the hollow chamber, comprises a chemical hydride and is structured to a form that is similar to a web, a sealing material, and a control element, which is electrically connected to the cartridge and controls the quantity of the produced hydrogen. The box comprises a container (176) having the hollow chamber whose side is open, and a lid (178), which covers the opened hollow chamber. The sealing material is introduced between the container and the lid, so that the leakage of hydrogen is prevented. INDEPENDENT CLAIMS are included for:    (1) a device for producing hydrogen; and    (2) a fuel cell power generation system.    DESCRIPTION OF DRAWING(S) - The diagram shows a perspective view of a housing.    Housing (100)    Box (170)    Moisture removing layer (174)    Container (176)    Lid. (178)
NOVELTY - The bottom valve of buffering zone branch pipe is opened and the bacterial suspension is flown into accessory pipe. The process of hanging circulation biomembrane is initiated. The middle valve is opened after 2 hours. The flow rate at middle and bottom is adjusted. The top valve is opened after 2 hours. The rate at top, middle and bottom is adjusted. Pressurizing pump and air compressor connected to accessory and branch pipes are stopped after 48 hours. The suspension is discharged. The pump is operated to input water continuously and hanging process is completed.    USE - Circulation biomembrane hanging method for sludge inner circulation type biofiltration pool.    ADVANTAGE - The sludge deposition on the circulation biomembrane is prevented and the adhesive attraction of micro organism is improved. The circulation biomembrane hanging efficiency is increased and the impact-resistant loading capacity is ensured.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the sludge inner circulation type biofiltration pool with circulation biomembrane.
NOVELTY - The method involves heating the thermal gasification medium at 110-500 degrees C in a pre-heater (3) coated with heat insulating material. The pre-heated thermal gasification medium is fed in stages into sodium hydrogen gasification furnace (19) via a host blast distributing header box (7), so that favorable reaction conditions are established within the furnace.    USE - Preheated multistage air-distributing fixed bed straw gasification method.    ADVANTAGE - The straw gasification efficiency can be improved and thermal value of fuel gas can be raised. Also, the amount of clinker and green house gas emission can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the fixed bed straw gasification system.    Pre-heater (3)    Heat exchange element (4)    Header box (7)    Guide pipe (14)    Gasification furnace (19)
NOVELTY - Fuel composition satisfying motor vehicle pollutant emission limit, whose components and volume percentages are as follows: 70-99.5% of gasoline, 0.5-30% of component B, where the proportions of component B with following components to volume percentage are as follows: 75-99% of mixture of lower alcohol, 0.01-0.5% of nitrocompound, 0.8-23.9% of auxiliary solvent, 0.18-0.55% of gasoline cleaning agent, 0.05-0.1% of antioxidant and 0.005-0.2% of antirusting agent.    USE - The fuel composition is useful for automobile fuels.    ADVANTAGE - The composition reduces using amount of the auxiliary solvent with high cost under condition of similar with the common ethanol gasoline; the using amount of the auxiliary solvent is reduced more than 65% compared with common methanol gasoline.
NOVELTY - Processing organic waste comprises contacting the organic waste with the decomposed organic nitrogen compound which makes the enterobacterium culture produce protease; and decomposing the organic nitrogen compound in these organic waste in an anaerobic environment.    USE - The method is useful for processing organic waste (claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a biogas production method comprising an ammonia separation process which isolates the ammonia component produced by the organic nitrogen compound decomposition process; and methane-fermentation process comprising performing a methane fermentation by using the low nitrogen containing organic waste after the ammonia separation process as a raw material; and    (2) an organic-waste processing agent for decomposing the organic nitrogen compound in organic waste containing the enterobacterium which produces protease.
NOVELTY - Low-temperature aerobic composting of organic solid waste includes blending organic solid waste having moisture content of 55-65 mass% and composting conditioner, piling the mixture, and performing circular batch-type ventilation every 30 minutes at 0.05-2 m3 air/(m3 pile/h) each time lasted for 10 minutes. When the composting temperature reaches 40 degrees C, the compost is turned. When the composting temperature reaches above 50 degrees C, the compost is turned every 48 hours until the composting temperature is reduced to 40 degrees C. The compost is turned again until the pile is thoroughly decomposed.    USE - Method for low-temperature aerobic composting of organic solid waste such as urban sewage slurry, urban trash, fowl and livestock manure, and/or food trash (claimed).    ADVANTAGE - The method can be performed at 8 degrees C for 15-20 days until the composting product is thoroughly decomposed. The method has low energy consumption, improved composting temperature, low equipment requirements, low cost, and no secondary contamination.    DETAILED DESCRIPTION - Low-temperature aerobic composting of organic solid waste includes blending organic solid waste having moisture content of 55-65 mass% and composting conditioner; and piling the obtained composting material to a height of 0.8-2 m and having an initial temperature of 5-10 degrees C, and performing circular batch-type ventilation every 30 minutes at 0.05-2 m3 air/(m3 pile/h) each time lasted for 10 minutes. When the composting temperature reaches 40 degrees C, the compost is turned. When the composting temperature reaches above 50 degrees C, the compost is turned every 48 hours until the composting temperature is reduced to 40 degrees C. The compost is turned again until the pile is thoroughly decomposed, and the material is discharged.
NOVELTY - The technique involves removing dust in high-temperature combustible gas with temperature of 500-1500 degrees centigrade by utilizing a filter collector (3), where the dust is discharged from a gasification furnace (1). Tar in the combustible gas is gathered by a combined method of inertia and cooling in a tar drip catcher (6). The tar gathered is made to reflow into a high-temperature oxygen rich combustion area of the gasification furnace by gas flowing power from a jet exhauster (13) and gravity for burning and schizolysis under temperature of 100 degrees centigrade.    USE - Straw gasification technique for a fixed bed.    ADVANTAGE - The technique largely reduces the tar content in the in the combustible gas and realizes that the tar automatically reflows and burns, so that the gasification efficiency, thermal value of combustible gas and gas quality are improved, and the secondary pollution problem caused by tar is resolved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic illustration of a straw gasification technique for a fixed bed.    Gasification furnace (1)    Filter collector (3)    Tar drip catcher (6)    Cooler (7)    Jet exhauster (13)
NOVELTY - A system comprises a heating unit (23) for heating liquefied natural gas. A liquid gas separating unit (24) for separating liquefied natural gas is also provided. A heat exchanger (22) is arranged on upper side of the heating unit, where high caloric component is separated from miniature distillation tower (25). A vaporizer (27) and a liquefied natural gas storage tank (20) for storing liquefied natural gas are additionally provided.    USE - System for reducing heating value of natural gas for floating marine structure, particularly liquefied natural gas regasification vessel (LNG RV) or liquefied natural gas floating storage and regasification units (LNG FSRU) (all claimed).    ADVANTAGE - The system enables to reduce heating value of the natural gas with high purity and high heating value in simple and cost-effective manner without using expensive distillation tower or nitrogen production equipment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for reducing heating value of natural gas, which involves heating the natural gas by using heating unit.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the system for reducing heating value of natural gas.    Liquefied natural gas storage tank (20)    Heat exchanger (22)    Heating unit (23)    Separating unit (24)    Miniature distillation tower (25)    Vaporizer (27)
NOVELTY - The device has charging machine, charging tank, fermentation cylinder, front purifying separator, fuel gas storage cabinet, rear purifier, fuel gas compressor, tubular heat exchangers, devulcanizer and regeneration tank, which are connected sequentially through pipes. The fuel gas inlet and outlets of regeneration tank are connected respectively to uplink pipe connected to devulcanizer and downlink pipe connected to compressor. The inlets and outlets of exchangers are connected respectively to cold and hot water pipes.    USE - Integrated process device for preparing flammable methane gas.    ADVANTAGE - The flammable methane gas can be produced by purifying the gas with desulfurization, decarbonization and dehydration processes using integrated process device.    DESCRIPTION OF DRAWING(S) - The drawing shows a structural view of the integrated process device for preparing flammable methane gas.
NOVELTY - Mixed fuel manufacturing involves storing organic waste containing domestic animals excrements in a waste reservoir (100). Solid material and food effluent leachate are stored in a sedimentation tank (200). Cation is supplied to waste from solid material by using an ion reactor (300). The liquid waste is electrolyzed to obtain mixed fuel gas. The mixed fuel gas is supplied into a gas synthesis tub (500), where gas is obtained.    USE - Device for manufacturing mixed fuel by using gas obtained from waste.    ADVANTAGE - The device enables to manufacture mixed fuel without producing bad smell.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for manufacturing mixed fuel, which involves utilizing organic waste containing domestic animals excrements, solid material and food effluent leachate.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device.    Waste reservoir (100)    Sedimentation tank (200)    Ion reactor (300)    Gas exhaust port (420)    Gas synthesis tub (500)
NOVELTY - Preparation of high yield apple culturing fertilizer comprises crushing dry human excrement, bean cake, rapeseed cake, compound fertilizer, urea, potassium dihydrogen phosphate and pot ale powder; adding carbendazol, Panaplate(RTM: 2,2-dichlorovinyl dimethyl phosphate), paclobutrazol, fruit tree speckle removing agent, calcium carbonate and zuoguoling liquid; and agitating, adding water, storing mixture, covering and compressing using plastic cloth and fermenting to obtain synthetic fruit tree culturing fertilizer.    USE - Method for preparation of high yield apple culturing fertilizer (claimed).    DETAILED DESCRIPTION - Preparation of high yield apple culturing fertilizer comprises crushing materials comprising (wt.%) dry human excrement (32-45), bean cake (25-30), rapeseed cake (12-19), compound fertilizer (3.6-3.7), urea (3.5-4), potassium dihydrogen phosphate (1-1.8) and pot ale powder (1.7-2); adding materials comprising (wt.%) carbendazol (1-2), Panaplate(RTM: 2,2-dichlorovinyl dimethyl phosphate) (0.5-1), paclobutrazol (0.5-1), fruit tree speckle removing agent (0.5-1), calcium carbonate (1-2) and zuoguoling liquid (0.7-1.5); and agitating for 40 minutes, adding water at ratio of 1:1.5-1:1.8, storing mixture, covering and compressing using plastic cloth and fermenting for 7 days to obtain synthetic fruit tree culturing fertilizer.
NOVELTY - Disposing biological chain of animal manure involves mixing of raw materials, converting animal manure into biogas and slag, converting slag to feeding soil to breed earthworms and breeding the earthworms by feeding 8000-12000 earthworms in every square of feeding soil.    USE - Disposing biological chain of animal manure for multi-level conversion (claimed) used in processing manure in large and medium sized farms in an intensive and scaled way.    ADVANTAGE - The process has high efficiency.    DETAILED DESCRIPTION - Disposing biological chain of animal manure involves mixing of raw materials, converting animal manure into biogas and slag, converting slag to feeding soil to breed earthworms and breeding the earthworms by feeding 8000-12000 earthworms in every square of feeding soil. Conversion of animal manure to biogas and slag is performed by uniformly stirring 65-75 parts animal manure, 15-25 parts crushed straw and 5-15 parts water, exposing in sunlight for 3-3.5 hours, stacking for 5 days to obtain a fermented material, letting the temperature reach 45-55 degrees C, adding 0.3-0.8 parts urea, 3-8 parts plant ash and 8-12 parts water to every 1000 parts fermented material, stirring until uniform, pouring to biogas tank, adding 30 degrees C water until the water level is 20-30 cm away from the top of the discharging passage of hydraulic pressure chamber, fermenting at 20-25 degrees C and sealing the movable cover using a mortar to produce biogas and slag after fermentation. Converting slag into feeding soil to breed earthworms is performed by uniformly mixing 65-75 parts slag, 15-25 parts oxidized coal and 8-12 parts dry soil. The diameter of feeding soil is 2-5 cm.
NOVELTY - A methane absorbent comprises liquid organic composite solution formed by mixing 1-6 wt.% castor oil, 8-19 wt.% surface activating agent and water (balance).    USE - Methane absorbent for lowering methane concentration (claimed) in mining wells.    ADVANTAGE - The methane absorbent provides an organic micro environment which can improve dissolution of methane by wrapping methane into the organic micro environment, thus preventing the danger of explosion.
NOVELTY - A methane absorbing agent comprises liquid micelle solution formed by mixing ionic surfactant, nonionic surfactant and water. The total weight of surfactants is 10-20% of the total weight of absorbing agent.    USE - Methane absorbing agent for reducing concentration of methane (claimed) in coal mine wells.    ADVANTAGE - The absorbing agent provides a non-polar micro environment which greatly improves solubility of organic compound containing methane. Hence, explosion of methane gas in mine working surface is prevented and coal mine safety is improved.
NOVELTY - Mixing circulator has hydraulic seal and vertical towers, which are moved up and down by horizontal arms. The vertical towers are moved up and down for movement of shovels. The hydraulic seal stops discharge of biogas from biodigester.    USE - Mixing circulator for biodigester for increasing production of biogas.    ADVANTAGE - The mixing circulator ensures that no biogas particles are left at surface of the mixing circulator.
NOVELTY - Electrolytic generator has solar panel, electrolytic molecular disassociator with molybdenum cathode and stainless steel anode, and deoxidant filter.    USE - Electrolytic generator for molecular dissociation of water molecule at low voltage for producing hydrogen from electrolysis of water.    ADVANTAGE - The electrolytic generator ensures easy storage and transport of hydrogen, and also ensures to produce hydrogen by using minimum amount of energy.
NOVELTY - Hydrogen is produced and power generation and conversion of organic wastes is carried out by using biofuel cell (BFC) reactor as a two-section type solid fermenting coupling ion film biological cell system; directly sending organic wastewater to BFC reactor; and sending organic solid to a fermentation reaction unit through feed inlet to be liquefied by fermenting strain after solid organic substance is crushed. The obtained liquid enters BFC filtering device to be taken as fertilizer after removing residue. The system temperature is controlled at 30-60 degrees C.    USE - Method for producing hydrogen and carrying out power generation conversion of organic wastes (claimed).    ADVANTAGE - The method can integrally couple electrode of anaerobic BFC reaction and microorganism, and carry out anaerobic fermentation of organic substance according to demand. Further, the method achieves clean biological energy source system of power generation by conversion in electrode process of BFC reaction biologically and by direct fermentation.    DETAILED DESCRIPTION - Production of hydrogen and power generation and conversion of organic wastes comprise using BFC reactor as a two-section type solid fermenting coupling ion film biological cell system; directly sending organic wastewater to BFC reactor; and sending organic solid to a fermentation reaction unit through feed inlet to be liquefied by fermenting strain after solid organic substance is crushed. The obtained liquid enters BFC filtering device to be taken as fertilizer after removing residue. The system temperature is controlled at 30-60 degrees C. The BFC reactor produces hydrogen and monitors power generation conversion electrode. The biological cell system comprises upper and lower sections or they independently form two reaction units to separate solid from liquid to produce hydrogen with high added value or generate electric energy.
NOVELTY - Raw materials preparation involves supplying raw materials by pump into a mixing tank, where flow rate of raw material is monitored electronically by a flow controller. A heat exchanger is arranged in raw material area, and raw material is supplied to a storage tank after filtering and processing it.    USE - Method for continuous preparation of raw materials for biodiesel production by using electrical and mechanical equipment.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of raw materials continuous preparation method.
NOVELTY - The direct manufactured fuel cell plug (50) has a sealing material such as polysulfone adhesive fuel sealant that is arranged in a fuel seal boundary of a fuel tank. A lip portion (58) is fixed to an opening formed in a fuel seal boundary of the fuel tank for closing opening provided in the fuel tank. Several pocket elements (60) are arranged to fit with the fasteners provided on the fuel tank.    USE - Direct manufactured fuel cell plug for fuel tank or fuel bay of aircraft (claimed).    ADVANTAGE - The opening provided in the fuel tank can be closed reliably by lip portion of fuel cell plug. Hence, leakage of fuel from fuel tank of aircraft can be avoided. The structure of fuel cell plug can be simplified at low cost and installation process of fuel cell plug with respect to the fuel tank can be performed reliably and effectively. The integrity of aircraft structure can be maintained by avoiding leakage of fuel and damage to the aircraft structure can be minimized.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for system for forming fuel seal boundary in aircraft fuel bay.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the direct manufactured fuel cell plug.    Fuel cell plug (50)    Angled portion (56)    Lip portion (58)    Pocket element (60)
NOVELTY - A pretilachlor containing aqueous emulsion comprises (mass%) pretilachlor crude drug (5-50), pretilachlor (5-60), cosolvent (0-10), surfactant (2-15), anti-freezing agent (4-8), thickening agent (0.5-2), and water (balance).    USE - A pretilachlor containing aqueous emulsion.    ADVANTAGE - The emulsion saves raw material resources, reduces environment pollution, is easy to prepare, and can be used and stored conveniently.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of preparing a pretilachlor containing aqueous emulsion comprising mixing water and anti-freezing agent and thickening agent to obtain water phase; stirring and mixing pretilachlor, surfactant, cosolvent and stabilizing agent to obtain oil phase; adding slowly the prepared water phase to the oil phase or vice versa while stirring to obtain crude emulsion; and subjecting crude emulsion to a high pressure homogenizer.
NOVELTY - A zinc oxide adsorber is supplied into in de-sulfurizer (20), and supplied with exhaust gas containing hydrogen at high temperature discharged from fuel cell stack (50), to remove sulfur compounds from natural gas fuel (10). The sulfur compounds are removed by reducing mercaptan (RSH) in natural gas to form ethyl mercaptan intermediate compound (RH) and hydrogen sulfide, and zinc oxide reacts with hydrogen (2H2) to form zinc sulfide and water molecule.    USE - Desulfurization of natural gas used as molten carbonate fuel for fuel cell for generating electricity.    ADVANTAGE - The method efficiently removes sulfur compounds from natural gas, and saves energy by heat of exhausted gas discharged from fuel cell stack.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic block diagram of desulfurization of natural gas. (Drawing includes non-English language text)    Natural gas fuel (10)    De-sulfurizer (20)    Humidifier (30)    Reformer (40)    Fuel cell stack (50)
NOVELTY - Non-polluted food waste processing involves mixing food waste leachate and slag containing calcium oxide in a ratio of 1:1.5-1:3 to obtain a mixture. 8-10 pts.wt. of fowl droppings and 4-5 pts.wt. of nitrogenous fertilizer are added to the mixture. The mixture is stirred for 140-180 minutes per ton of the mixture to substitute calcium ion of the slag and sodium chloride of the food waste leachate into calcium chloride. The stirred mixture is crushed and dried to obtain fertilizer.    USE - Method for processing non-polluted food waste for obtaining fertilizer as by-product (claimed).    ADVANTAGE - The non-polluted food waste processing method enables to reduce the salt content of food waste leachate effectively in a cost-effective manner.
NOVELTY - Waste toilet paper, sanitary napkin, diaper, and cosmetic cotton (4.2 g) are separated as a raw material from domestic waste. The raw material is dried at 150 degrees C, crushed to a size of 5 mm, pulverized to a size of 2 mm, and extrusion-molded to obtain pulp coal.    USE - Manufacture of pulp coal for use as alternative of bituminous coal used for keeping house warm.    ADVANTAGE - The method enables manufacture of pulp coal having high calorific value by efficiently using domestic waste, thus preventing environmental pollution. The obtained pulp coal functions as fuel, which does not emit carbon dioxide, dioxins, sulfur, and phosphorus.
NOVELTY - A process for the production of methane-containing fuel gas and nitrogenous fertilizer by biomethanation of pelt/chromed leather solid wastes is disclosed, which involves (i) digesting the wastes with an aqueous alkali in concentration of 1-10% w/w at 70-95?oC followed by cooling at ambient temperature; (ii) filtering the reaction mass; (iii) neutralizing the filtrate to pH of 7.0-8 with an acid; and (iv) biomethanating the filtrate with the help of a mixture of acidogenic and methanogenic bacteria. Image 0/0
NOVELTY - A process for the preparation of a gaseous mixture containing hydrogen and carbon monoxide by autothermal reforming, involves (i) performing partial oxidation of a gaseous hydrocarbon feed in a partial oxidation zone, (ii) passing the effluent of the partial oxidation zone to a reforming zone, and (iii) reforming in the presence of a reforming catalyst in the reforming zone to form a reformed product stream comprising mainly synthesis gas, carbon dioxide, methane and inert components such that the reformed product stream has a temperature of 1100-1300?oC and recovering the reformed product stream. Image 0/0
NOVELTY - A sewage sludge and steel generator by combusting fuel containing brown grease are contactor, under conditions effective to dewater the sewage sludge, to obtain fertilizer material.    USE - Method for separating fertilizer material from sewage sludge of building piping, municipal collection system and wastewater treatment plant.    ADVANTAGE - The method economically separates fertilizer material, and is environmental friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus for separating fertilizer material, which contains solid fuel forming apparatus (8) including dewatering unit (20), solid fuel boiler for combusting solid fuel, and steam dryer for dewatering sewage sludge.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of solid fuel forming apparatus.    Solid fuel forming apparatus (8)    Base treatment supply system (16)    Dewatering unit (20)    Mixing unit (24)    Combustible material supply system (26)
NOVELTY - Petroleum alternative fuel is manufactured by transesterifying oil with alcohol and alkali catalyst, vacuum distilling at less than or equal to 5 mmHg and 150-300 degrees C liquid temperature, stirring to separate produced petroleum alternative fuel and glycerin by-product and extracting by distillation of petroleum alternative fuel.    USE - Manufacturing process of petroleum alternative fuel for e.g. biodiesel made from oils and/or waste edible oils.    ADVANTAGE - Washing process is unnecessary, wash water is not emitted, obtained fuel has high purity and transparency and manufacturing process is stable.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing apparatus of petroleum alternative fuel.
NOVELTY - System for culturing algae by domestic sewage, has a sewage treating-filtering subassembly for producing algal nutrient liquid, a culturing subassembly for culturing algae using algal nutrient liquid from the sewage treating-filtering subassembly, and an algae harvesting-processing subassembly for separating and collecting algae from the culturing subassembly and for supplying algae to relative algae processing equipment. The algae harvesting-processing subassembly is further connected with the sewage treating subassembly through a return pipe.    USE - The system is useful for culturing algae (claimed) and for chemical purification.    ADVANTAGE - The carbon elements in domestic sewage and biologic waste can be transformed into oil and other organic molecules. The valuable chemical and biologic products can be produced in process of purifying domestic sewage. The cost of culturing algae in a large scale is reduced and the system is suitable for industrial production of biodiesel from algae.
NOVELTY - The apparatus has electrically driven trolley (2) positioned on top of fermentation tank (100), which drives electrically driven stirring apparatus to stir processing material fermented within fermentation tank. A control panel (26) controls the trolley so as to drive the stirring apparatus. A fixing portion (14) fixes the control panel to trolley so that control panel is positioned in outer space (66) beside the outer surface of the tank.    USE - Fermentation treatment apparatus of manure manufacturing plant for processing e.g. human waste, organic refuse, urine, ammonia and methane.    ADVANTAGE - Since the control panel used to control drive of processing material stirring apparatus is set in outer space beside outer surface of fermentation tank, control panel is not exposed with respect to processed gas raised above from fermentation tank. Hence the durability of the electric system of the control panel can be improved.    DETAILED DESCRIPTION - The fermentation treatment apparatus has fixing portion for fixing the control panel, which includes outrigger (61) projected diagonally upward of the fermentation tank from trolley. A suspending-down section (62) hangs down from outrigger, and a suspension section (63) protrudes towards fermentation tank so as to suspend the control panel.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the fermentation treatment apparatus.    Electrically driven trolley (2)    Fixing portion (14)    Control panel (26)    Outer space (66)    Fermentation tank (100)
NOVELTY - Isolating methyl eugenol from Cymbopogon flexuosus var. sikkimensis, comprises hydrodistilling the grass of Cymbopogon flexuosus var. sikkimensis in a cleavenger type apparatus and isolating the essential oil by conventional methods such as layer separation and solvent extraction, subjecting to fractional distillation the isolated essential oil at reduced pressure of 0.1-0.5 mm (Hg) using a fractionating column at a temperature of 70-215 degrees C and a vapor temperature of 45-315 degrees C, and isolating the pure methyl eugenol by distillation under reduced pressure of 0.1-0.5 mm(Hg).    USE - The method is useful for isolating methyl eugenol from Cymbopogon flexuosus var. sikkimensis (claimed)for synthesis of methyl dopa for preparing anti-hypertensive drug. No biological data given.    ADVANTAGE - The method isolates methyl eugenol from Cymbopogon flexuosus var. sikkimensis without changing the property using an expensive equipment in simple and environment friendly manner. The methyl eugenol does not contain impurity and chemicals, and has high yield of greater than 87%.
NOVELTY - The microblower comprises lamination of top plate, flow-path formation board (20), separator and blower frame in order. The flow-path formation board has a center hole (21) with diameter larger than diameter of discharge outlet in the top plate. The restrictions (23) having channel width narrowing gradually towards the center hole, are formed in inflow path (22) extending towards corners from the center hole.    USE - Piezoelectric microblower for air cooling of electronic device e.g. notebook personal computer, and for fuel transport in fuel cell.    ADVANTAGE - The compressible fluid can be conveyed efficiently without using a check valve, hence flow rate can be increased. The restrictions reduce the loss of pressure energy, thereby allowing the increase in the flow rate.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the piezoelectric microblower.    Inflow port (8)    Flow-path formation board (20)    Center hole (21)    Inflow path (22)    Restrictions (23)
NOVELTY - The system (102) has an interface with a cement-making component for channeling waste heat (106) i.e. waste heat gas, generated during manufacturing of cement. A dryer (114) receives wet bio-solids, and utilizes heated dryer air in direct contact with the bio-solids to produce a dried product, where the dryer air has oxygen content below a level that allows occurrence of combustion in the dryer. A heat exchanger (116) receives the waste heat from the interface, and utilizes the waste heat to heat the dryer air in the dryer, where the waste heat and the dryer air are not mixed.    USE - System for drying bio-solids e.g. municipal sewage, pulp and paper sludge, and industrial sludge, utilizing waste heat generated from a cement-making system during cement-making process to produce dried bio-solids that are utilized as agricultural organic fertilizer and fuel for the cement-making system.    ADVANTAGE - The system avoids clogging within the dryer by mixing of the dried bio-solids with wet bio-solids before sending the wet bio-solids to the dryer, so that the wet bio-solids can be effectively dried. The system decreases the downtime for the drying process by utilizing the waste heat from the cement making process.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a method for drying bio-solids utilizing heat from a cement-making process    (2) a method for generating fuel for a cement-making process.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a drying system that utilizes waste heat from a cement-making system for drying wet bio-solids.    Bio-solids drying system (102)    Waste heat (106)    Dryer (114)    Heat exchanger (116)    Recycling bin (122)
NOVELTY - An additive comprises saccharide ester(s) and polymer having comb structure. If only one saccharide ester is present, the saccharide ester comprises saturated ester group(s) and unsaturated ester group(s). If more than one saccharide ester is present, these saccharide esters comprise a first saccharide ester containing saturated ester group(s) and a second saccharide ester containing unsaturated ester group(s).    USE - Additive for lowering minimum usable temperature of biodiesel fuel or diesel/biodiesel blend (claimed).    ADVANTAGE - The additive provides biodiesel that exhibits efficacy in suppression of nucleation and crystal growth mechanisms observed in biodiesels containing high levels of saturated fatty acid methyl esters. The additive provides improved synthesis of comb polymers in cost and yield.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) biodiesel or diesel/biodiesel blend comprising additive;    (2) use of saccharide(s) in manufacture of additive for use in lowering the minimum usable temperature of biodiesel fuel or diesel/biodiesel blend;    (3) reducing minimum usable temperature of biodiesel fuel or diesel/biodiesel blend comprising combining the biodiesel fuel or diesel/biodiesel blend with additive; and    (4) preparing additive for lowering the minimum usable temperature a biodiesel fuel or diesel/biodiesel blend comprising combining the polymer having comb structure and saccharide ester(s).
NOVELTY - Device comprises many chambers arranged one above the other, where the first chamber is a feeding chamber and equipped with a cutter and the other chambers are real composting areas and kept at a constant temperature by heating modules and equipped respectively with filter fans for filtered air supply and air removal and the final chamber is opened to remove the end product.    USE - The device is useful for producing compost from biodegradable packaging and easily compostable leftovers.    ADVANTAGE - The device is produced in an artistic and constructive manner suitable for setting up in enclosed spaces preferably for easily composting the biodegradable plastics and easily compostable food and garden waste.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a procedure for composting biodegradable packaging and easily compostable leftovers, comprising providing and chopping the material to be compostable in a first feeding chamber.
NOVELTY - The system (10) has a cleaning device e.g. high temperature proton pump (20), arranged upstream to a fuel gas inlet of a fuel cell (30) and provided for purifying hydrogen content in the fuel gas. The purified hydrogen is producible in the pump under consumption of an electric power from the hydrogen content fuel gas at a temperature over 150 degree celcius. The purified hydrogen is applied to a hydrogen outlet of the pump, where the outlet is attached to the inlet. A power electronics (40) regulates an electrical power supply to the pump based on a gaseous fuel requirement of the fuel cell.    USE - Low temperature-polymer electrolyte membrane-fuel cell system.    ADVANTAGE - The system can be constructed in a, a simple, efficient and economical manner, and exhibits higher flexibility. The power electronics regulates the electrical power supply to the pump based on the gaseous fuel requirement of the fuel cell, thus avoiding a need of a large storage tank for storing purified hydrogen, and hence achieving an increased security of the system with mobile applications.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a fuel cell system.    Fuel cell system (10)    High temperature proton pump (20)    Fuel cell (30)    Power electronics (40)    Fuel tank (52)    Accumulator (54)
NOVELTY - A sewage water denitrification treatment method comprises adding methane into to-be-treated water and conducting aerobic or an oxygen-poor denitrification method.    USE - Treatment method for sewage water denitrification.    ADVANTAGE - The solubility of methane gas in water is low, and no large fluctuation of bio-oxygen-need amount is caused in the outlet water. As the methane is in a relatively low price and convenient for transportation, it has relatively high engineering application value.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a sewage water denitrification treatment system comprising a water inlet unit, a water outlet unit, a sewage water denitrification treatment unit and a methane-adding operation unit. The denitrification treatment unit is a reaction tank where a first membrane module, a second membrane module and a recycle pump are mounted.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of sewage water de-nitrification treatment method.
NOVELTY - The device for producing hydrogen comprises a hydrolysis chamber having a metal hydride separated by a thin membrane, which is overlaid with a rigid grid of a reservoir containing a liquid solution for the reaction, with nano-based materials, metal hydrides, nanotubes or nanometals from 1-50 nm. The flow of gas generated is controlled by a pair of rigid walls and membranes.    USE - The hydrogen producing device is useful in an apparatus equipped with a fuel cell for generating electricity (claimed), where the fuel cell is useful in cell phones, laptops, camera, digital cameras, compact disc (CD) players and portable DVD players, music players and portable radios, games, global positioning system and medical devices.    ADVANTAGE - The device is capable of uniformly and constantly producing hydrogen with less consumption of energy thus ensuring effective and controlled generation of electricity for long period of time, and is compact, cost-effective, movable, portable and easy to use.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an apparatus equipped with a fuel cell for generating electricity.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of an assembly of elements of a disposable or rechargeable battery.    Holes (4-41)    Collection tank (4-42)    Treated surface (4-43)    Micro-reservoir (4-44)    Channel. (4-46)
NOVELTY - Method of introducing microorganisms into activated sludge, involves treating activated sludge with enzyme, adding the microorganisms to the obtained sludge, and treating sludge with ultrasonic waves.    USE - The method is useful for introducing microorganism into activated sludge for waste-water treatment (all claimed), e.g. sewage treatment.    ADVANTAGE - The microorganisms are introduced artificially into activated sludge and can be fixed and maintained steadily.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of treating waste-water, which involves introducing microorganism into activated sludge by the above method, and performing waste-water treatment using the activated sludge.
NOVELTY - Preparation of anthropogenic soil, which is terra preta, comprises: mixing charcoal, sugar and phosphoric acid; and adding 10-100 volumes of peat or compost to the mixture by maintaining a constant humidity.    USE - The process is useful for the preparation of the anthropogenic soil, which is terra preta, to provide a fertile soil.    ADVANTAGE - The process ensures high throughput of anthropogenic soil in an economical manner.
NOVELTY - The apparatus has a high pressure pump (26), an upper heating unit e.g. heater (23), for heating liquefied natural gas, and a gas-liquid separation unit (24) heated by the heating unit to separate the liquefied natural gas. A part of a gas component and a liquid component is separated by the gas-liquid separation unit, and a miniature distillation tower (25) separates high caloric component. The high caloric component separated from the miniature distillation tower is stored in a separate storage tank.    USE - Liquefied natural gas calorific value reduction apparatus for use in a floating marine structure e.g. liquefied natural gas regasification vessel (LNG RV) and liquefied natural gas floating storage and regasification unit (LNG FSRU) (all claimed).    ADVANTAGE - The apparatus reduces the calorific value of the liquefied natural gas and separates high caloric component easily. The apparatus has small volume, and is inexpensive. The apparatus eliminates the necessity of a nitrogen production equipment, so as to save the operating cost of the apparatus. The apparatus reduces the usage amount of nitrogen, so as to reduce the running cost of the apparatus.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a floating marine structure comprising a liquefied natural gas re-evaporating apparatus    (2) a liquefied natural gas calorific value reduction method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a liquefied natural gas calorific value reduction apparatus.    Feed pump (21)    Heater (23)    Gas-liquid separation unit (24)    Miniature distillation tower (25)    High pressure pump (26)    Vaporizer (27)
NOVELTY - Sewage denitriding-denitrifying treatment comprises conveying gas carbon source to membrane, supplying gas carbon source through membrane cavity, and denitriding and denitrifying sewage by membrane aeration, where gas partial pressure is kept at lower than bubble point.    USE - Method for sewage denitriding-denitrifying treatment (claimed).    ADVANTAGE - The method and system can increase transmission efficiency of additional gas carbon source in water, reduce bubble diameter, prolong retention time of bubbles in water, and greatly improve utilization rate of gas, thus providing high engineering application value.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a sewage denitriding-denitrifying treatment system.
NOVELTY - Composting bioorganic fertilizer includes mixing raw materials comprising straw powder, rice bran and dregs of beans, adding microorganism, composting, and inspecting to obtain finished product.    USE - Method for composting bioorganic fertilizer (claimed).    ADVANTAGE - The method is simple, and easy and convenient to operate. Raw materials are easy to obtain.
NOVELTY - A disposal apparatus of food wastes comprises a reactor (110) for permitting the food wastes (112) and microbes comprising Bacillus smithii for decomposing the food wastes to be contained; an agitator (130) mounted inside the reactor for mixing the food wastes and the microbes; an air inlet (140) connected with the reactor for permitting air to flow into the reactor; and an air heater (150) connected with the air inlet for heating the air flowing into the reactor.    USE - A disposal apparatus of food wastes generated when processing foods in houses, restaurants and industrial facilities or wastes required to be processed after eating the foods.    ADVANTAGE - The apparatus decomposes food wastes in a nature-friendly manner. It effectively decomposes the food wastes without reducing a moisture content of the food wastes.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of a disposal apparatus of food wastes.    Reactor (110)    Food wastes (112)    Water supplying pipe (114)    Water spraying nozzles (116)    Leachate draining unit (118)    Discharging unit (120)    Agitator (130)    Shaft (132)    Stirring wings (134)    Stirring arms (136)    Motor (138)    Air inlet (140)    Air heater (150)    Pulverizer (160)    Gas outlet (170)    Gas processing unit (180)    Reactor heating unit (190)
NOVELTY - Plant growth inhibitor comprises Solidago extract, Cryptomeria japonica leaf extract, and Chamaecyparis obtusa leaf extract.    USE - The plant growth inhibitor is useful for suppressing growth and germination of weeds.    ADVANTAGE - The plant growth inhibitor is safe, eco-friendly, and suppresses the prolonged reproduction of weeds, and has allelopathy and synergistic effects with respect to weeds.
NOVELTY - Disclosed herein is a process for the anaerobic production of hydrogen and/or ethanol, comprising: preparing a seeding culture from the feces of a herbivorous animal, the seeding culture comprising microorganisms capable of anaerobically digesting cellulose and/or hemicellulose and/or monosaccharide component(s) contained therein to produce hydrogen and/or ethanol; admixing the seeding culture with a substrate to form a mixture, the substrate containing monosaccharide component(s) of at least glucose and/or xylose; and cultivating the mixture under an anaerobic condition, such that hydrogen and/or ethanol is/are produced via the anaerobic digestion of the monosaccharide component(s) contained in the substrate by the microorganisms of the seeding culture.
NOVELTY - Pyrazole compounds (I) and their salts are new.    USE - (I) is useful: for controlling undesired plants or inhibiting their growth; and as herbicides, which is useful in agricultural fields such as paddy fields, crop plant fields, orchards and mulberry fields and non-agricultural fields such as forest land, farm roads, play grounds and factory sites. Tests details are described but no results given.    ADVANTAGE - (I) exhibits excellent herbicidal activities against weeds as compared with conventional compounds of similar types and have a high safety to crop plants. (I) are not adversely affect the environment, and highly safe to animals.    DETAILED DESCRIPTION - Pyrazole compounds of formula (I) and their salts are new.    R1, R3, R4 = alkyl;    R2 = H or alkyl;    R5 = alkyl substituted by one alkoxy, alkoxy substituted by one alkoxy or alkoxycarbonyl;    R6 = alkylsulfonyl; and    A = alkylene substituted by at least one alkyl.    INDEPENDENT CLAIMs are included for:    (1) a pyrazole compound of formula (II); and    (2) the preparation of (I).
NOVELTY - Lithium hydride activation method comprises: performing a nitrification treatment (S1) of reacting lithium hydride with a nitride and forming a chemical compound layer stable to the nitride, on a surface of the lithium hydride; and reducing a particle size (S2) of the lithium hydride provided with the chemical compound layer by a mechanical pulverization treatment after the nitrification treatment is performed.    USE - The lithium hydride activation method is useful: for generating hydrogen; and in solid polymer type fuel cell (all claimed).    ADVANTAGE - The lithium hydride activation method is possible to activate lithium hydride into a form that improves the utilization rate of lithium hydride in the hydrogen generation reaction, and in the solid polymer type fuel cell, thus the solid polymer type fuel cell can be reduced in size. The lithium hydride activated method improves the efficiency in the generation of hydrogen. The particle size reduction process is performed in an atmosphere, which is able to restrain the formation of an oxide layer on a lithium hydride surface.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a hydrogen generation method comprising generating hydrogen by reacting ammonia and the lithium hydride that has been activated by the lithium hydride activation method; and    (2) a solid polymer type fuel cell comprising a lithium hydride treated by using the lithium hydride activation method.    DESCRIPTION OF DRAWING(S) - The figure shows a flowchart of the activation method for lithium hydride.    Nitrification treatment process (S1)    Particle size reduction process. (S2)
NOVELTY - The system (100) has supply units (31,32) that supply combustion gas to cathode (11) and anode (12) of fuel cell (10) from a combustor (30) respectively. The rich combustion gas is supplied to the fuel cell and modifier, until the temperature of the fuel cell and modifier reaches a predefined value. The anode gas and cathode gas are supplied to the modifier, after the temperature of the fuel cell and modifier reaches the predefined value.    USE - Fuel cell system comprising fuel cell e.g. solid oxide fuel cell (claimed) used as power supply for vehicle.    ADVANTAGE - The rise in the temperature of the fuel cell can be reduced by supplying combustion gas to the cathode and anode, using a simple arrangement, so that startability of the fuel cell system can be improved. The exhaustion performance of the fuel cell system can be improved, since the discharge amount of unburned hydrocarbon can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the fuel cell system. (Drawing includes non-English language text)    Fuel cell (10)    Cathode (11)    Anode (12)    Combustor (30)    Combustion gas supply units (31,32)    Fuel cell system (100)
NOVELTY - Glycerin is dehydrated in the presence of a catalyst to obtain acrolein. The catalyst contains rare-earth-metal salt crystal of phosphoric acid. The crystal is obtained by baking the solid content of phosphate ion in the liquid containing hydroxide of rare-earth metal and/or dehydration product of the hydroxide, and water.    USE - Manufacture of acrolein used for manufacture of acrolein derivative (claimed) and manufacture biodiesel.    ADVANTAGE - The method provides acrolein with high yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for catalyst.
NOVELTY - Equipment for handling organic wastewater comprises active membrane bioreactor and organic wastewater degrading bacteria starter can. The organic wastewater degrading bacteria is solidified on the active carrier; and connecting passage is installed between the membrane bioreactor and organic wastewater degrading bacteria starter can.    USE - Equipment for handling organic wastewater, especially organic wastewater that has high concentration and is difficult to degrade (claimed).    ADVANTAGE - The active carrier can absorb the biological floc and pectin to improve the function of activated sludge, slow down the process of membrane fouling, and decrease the products of excess sludge.
NOVELTY - A tea-seed cake bioorganic fertilizer comprises tea-seed cake (2-5 wt.%), and barnyard manure (3-7 wt.%).    USE - A tea-seed cake bioorganic fertilizer (claimed).    ADVANTAGE - The fertilizer has combined effect of control release and quick result. It has good synergistic effect. It has also the effect of killing pest.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing the tea-seed cake bioorganic fertilizer comprising mixing tea-seed cake and barnyard manure, infusing microbial inoculum (0.2 wt.%) and supplementary material, and performing aerobic fermentation; and introducing microbial inoculum (0.1 wt.%) to treated material, fermenting, drying fermented material, crushing, granulating, and filtering.
NOVELTY - Organic fertilizer is produced from sludge by press filtering and dehydrating additive (25-35 wt.%) containing 10-20% water content and sludge (65-75 wt.%) containing 75-85% water content, mixing, stacking and fermenting for 2-4 times for 24-42 days, and processing into particles or powder.    USE - Method of producing organic fertilizer from sludge (claimed).    ADVANTAGE - The method has less investment, utilizes small land, has short treatment period and low circulation cost. The production process does not produce wastes.
NOVELTY - A shrimp feed comprises (mass%): dry brine shrimp meal (20-30), chick embryo protein (5-15), flour (5-15), soybean lecithin (5-10), peanut meal (5-10), fish oil (1.5-5), mineral substance (0.1-0.3), vitamin (0.1-0.3), Bacillus licheniformis agent (0.1-0.3), and fish meal (balance).    USE - Shrimp feed.    ADVANTAGE - The feed is free from antibiotic, and can effectively avoid medicinal residue; reduces discharges of nitrogen, phosphorus and trace element; and realizes environment-friendly cultivation, and generates small damage and influence on water environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing the shrimp feed comprising mixing and grinding dry brine shrimp meal, chick embryo protein, flour, soybean lecithin, peanut meal, fish oil, mineral substance, vitamin, B. licheniformis agent and fish meal to obtain mixed powder; fermenting inoculated yeast strain with mixed powder and water in fermentation pot to obtain fermented feed; tableting, sterilizing and drying the feed; grinding dried feed, classifying and respectively sieving feed to obtain feed with different granularities; and respectively packaging feed, and packaging.
NOVELTY - The furnace has an air-distribution pipe infusing air from multiple directions and lying above the furnace grate inside the furnace body; and an air supplying device outside the furnace body and connected with the air-distribution pipe through the connecting pipe passing through the furnace wall. The air supplying device provides forced wind source for the furnace.    USE - Multi-air distribution fixed bed biomass gasification furnace.    ADVANTAGE - Improves the power of the gasification furnace, reduces tar content in combustible gas as well as sewage by utilizing forced air intake mode through the combination of the air supplying device and air-distribution device, which is in favor of environmental protection. The furnace has no special requirements on size, degree of dryness and feeding way; therefore, it enlarges the application range of biomass raw material.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic cross-sectional of the multi-air distribution fixed bed biomass gasification furnace.
NOVELTY - Composting reaction additive comprises wheat straw, calcium superphosphate and zeolite at weight ratio of 100:9-16:30-20.    USE - Composting reaction additive.    ADVANTAGE - The composting additive can obviously improve effect of composting, improve rotten degree of composting, reduce loss of nitrogen fertilizer, increase enriched accumulation of nutrition (e.g. enriched accumulation of total phosphorus and total potassium), and reduce release of pollution gas as ammonia gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a composting method comprising mixing additive and organic fertilizer and composting, with weight ratio of additive to organic fertilizer at 139-126:500.
NOVELTY - Nickel-aluminum reforming catalyst production involves mixing aqueous solution of nickel nitrate of 0.18-0.36 M, aqueous solution of aluminum nitrate of 0.18-0.36 M and urea solution of 1-6 M to obtain a mixed solution. The obtained mixed solution is aged for 12-48 at 95-100 degrees C. The aged solution is plasticized at 300-500 degrees C under oxygen atmosphere after accomplishing washing and filtering processes.    USE - Method for producing nickel-aluminum reforming catalyst for direct internal reforming of molten carbonate fuel cell.    ADVANTAGE - The nickel-aluminum reforming catalyst production method enables to produce the nickel-aluminum reforming catalyst having high resistivity for poisoning of potassium hydroxide.
NOVELTY - A biomass liquid fuel is indirectly produced by taking gasoline, diesel oil or other fuel oil as an extractant to extract an organic product in a hydrolyte liquid.    USE - Method for indirectly producing a biomass liquid fuel (claimed).    ADVANTAGE - The produced biomass liquid fuel takes the characteristic of the furfural that is easily soluble in aromatic hydrocarbon.
NOVELTY - Vacuum stirrer comprises a methanol evaporator, tank, rotary shaft (49), rotating stirring wings, motor (33), vacuum pump (26) and a discharge conduit (44). The rotary shaft is installed inside the tank and the rotating stirring wings are mounted on the rotary shaft to stir the solution inside the tank. The motor is provided to rotate the rotary shaft. The vacuum pump is connected to the tank through a conduit line (29,30) to vacuumize the tank.    USE - Vacuum stirrer for producing biodiesel.    ADVANTAGE - The vacuum stirrer is simple, ensures excellent stirring efficiency, reduces agitation time, increases the productivity of the biodiesel, and provides biodiesel with a superior quality.    DETAILED DESCRIPTION - Vacuum stirrer comprises a methanol evaporator, tank, rotary shaft, rotating stirring wings, motor, vacuum pump and a discharge conduit. The rotary shaft is installed inside the tank and the rotating stirring wings are mounted on the rotary shaft to stir the solution inside the tank. The motor is provided to rotate the shaft. The vacuum pump is connected to the tank through a conduit line to vacuumize the tank. Caustic soda and methanol are mixed to provide methoxide, where obtained methoxide is reacted with cooking oil, which is used as raw material, in a tank to produce biodiesel. The discharge conduit is used for ejecting glycerin and soap component present in the lower part of the tank.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the vacuum stirrer.    Vacuum pump (26)    Conduit lines (29,30)    Motor (33)    Discharge conduit (44)    Rotary shaft (49)
NOVELTY - A ChlorellaYJ1 that is separated from the secondary urban sewage from urban sewage treatment plant, deposited under CGMCC NO. 3037, is new.    USE - The strain is useful for biodiesel production (claimed).    ADVANTAGE - The strain grows with the secondary urban sewage as the culture medium without extra nutrition elements such as nitrogen and phosphorus, thus reducing the cost of biodiesel production and the consumption of water resource. The urban sewage deep treatment technique constructed with the strain can obtain biodiesel during sewage treatment, which is environment-friendly, low-cost sewage regeneration and recycle technique for biodiesel production.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are: (1) a method for culturing Chlorellacomprising taking the secondary discharged water from urban sewage treatment plant as the culture medium and inoculating the ChlorellaYJ1 with initial inoculating density at 1x10 4-1x10 5ml/10, then culturing it in a place with light-dark ratio of 12 hours:12-14 hours:10 hours and lighting intensity of 800-1300 lux at 22-27 degrees C and relative humidity at 70-80% for 10-22 days, centrifuging the Chlorellaliquid to obtain the Chlorella; and (2) use of the Chlorellafor biodiesel production, where the ChlorellaYJ1 is taken as material for producing biodiesel and is cultured with the secondary discharged water from urban sewage treatment plant as the culture medium, and oil is accumulated by the growth of the Chlorella.
NOVELTY - Producing marsh gas by organic solid waste material through two-phase multilevel anaerobic fermentation comprises: (a) hydrolyzing and acidifying the organic solid waste material; (b) collecting the percolate; (c) preparing methane; and (d) pumping the output water of the methanation reactor in (c) into the acidified reactors.    USE - The method is useful for producing marsh gas by organic solid waste material through two-phase multilevel anaerobic fermentation (claimed).    ADVANTAGE - The method provides high yield of generating gas, short cycle, realization of stably continuous gas generation and no waste water.    DETAILED DESCRIPTION - Producing marsh gas by organic solid waste material through two-phase multilevel anaerobic fermentation comprises: (a) hydrolyzing and acidifying the organic solid waste material is to add the organic solid waste material in to n (n is more than or equal to 2) acidified reactors in parallel; the capacity load of the single acidified reactor is 200 gas volume score (gVS)/L the pH value is controlled at 5.8-6.5 and the temperature is 50-55 degrees C; processing the hydrolyzing acidified reaction to collect the generated gas; (b) collecting the percolate is to pump the percolate generated in n (n is more than or equal to 2) acidified reactors in (a) into the percolate collecting box to be mixed; adjusting the pH value of the percolate to be 7.0-8.0; (c) preparing methane is to pump the percolate whose physiochemical performance is adjusted by (b) into the methanation reactor which is filled with the inoculated material; the pH value is kept at 7.0-8.0 and the temperature is 50-55 degrees C; collecting the generated gas; and (d) pumping the output water of the methanation reactor in (c) into the acidified reactors.
NOVELTY - An olefin diesel oil is produced by mixing black oil type with an organic solvent, and subjecting mixture to functionalization treatment. The black oil type comprises olefin petrol or diesel oil as base oil. The organic solvent comprises methanol or petroleum ether.    USE - Method of producing an olefin diesel oil (claimed).    ADVANTAGE - The method reduces production cost of petrol and diesel oil consumption, and provides an improved management of forest chemical engineering.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a method of producing an olefin diesel oil. Drawing includes non-English language text.
NOVELTY - Bioethanol obtaining involves washing seagrass and obtaining ethanol by compressing it. The obtained ethanol is saccharified and fermented by using a microorganism at a temperature of 20-40 degrees C at a pH of 3-9 in anaerobic conditions. The fermented ethanol is distilled after fracturing.    USE - Method for obtaining bioethanol.    ADVANTAGE - The bioethanol obtaining method is eco-friendly and ensures mass production of high quality bioethanol.
NOVELTY - This invention discloses a method of processing and reusing dead bird bodies and bird decrements, and the method processes and reuses dead bird (such as chicken) bodies and bird decrements together with a waste (such as saw dust, rice grain, corn stem or wheat stem) and an aerobic microorganism to produce a high-grade biological organic fertilizer. This method is superior to the traditional processing method in many aspects including safety, sanitation, quantity reduction, ultimate disposability, disposal timeliness, resource reusability, spatial requirement and cost analysis.
NOVELTY - Treatment for ensuring the exploitability of agricultural liquid manure involves decreasing the pH value of the liquid manure; then adding nutritive materials selected from nitrogen, phosphorus and potassium for plant cultivation, where the pH value is increased during or/and after this operation; and mixing the biologically active material and obtained product applicable for increasing the plant nutriment content of arable lands. The value of the nutriment content of liquid manure is stabilized by keeping the pH below 6 as it is produced.    USE - For ensuring the exploitability of agricultural liquid manure useful for increasing the plant nutriment content of arable lands.    DETAILED DESCRIPTION - Treatment for ensuring the exploitability of agricultural liquid manure involves decreasing the pH value of the liquid manure; then adding nutritive materials selected from nitrogen, phosphorus and potassium for plant cultivation, where the pH value is increased during or/and after this operation; and mixing the biologically active material and obtained product applicable for increasing the plant nutriment content of arable lands. The value of the nutriment content of liquid manure is stabilized by keeping the pH below 6 as it is produced. The stabilized and stored liquid manure is further acidified below pH 3 to eliminate its virulence. The nutritive materials necessary for the plant culture to be grown on a defined arable land are admixed in the adequate quantities to the liquid manure of pH value below 3; and the liquid manure diluted to nutritive solution is inoculated with a microbial inoculating agent.
NOVELTY - Additive has aromatic odor, 5 to 25% camphor, 0.1 to 10% mentol, 5 to 25% ethyl acetate, 10 to 35% naphthalene, 0 to 40% toluole, 0 to 40% xylene, 0 to 35% methanol, 0 to 35% ethanol, 5 to 25% diethyl ether, 0.1 to 10% mineral oil and fuels such as gasoline, ethanol or diesel.    USE - Additive for saving fuel.    ADVANTAGE - The additive is stable, burns easily, insoluble in water, soluble in alcohol, gasoline, benzene, fatty oils, fuels and essential oils, and increases 0.3% octane, reduces saves fuel burn by 33%, releases more energy, decreases carbon monoxide, increases power of fuel burner, gives complete combustion, and also ensures that the additive is good solvent with resins, oils, asphalt, grease, glues, lacquers, plastics, paints and varnishes.
NOVELTY - Biofuel transesterification involves transesterifying biofuel for fifteen minutes at high temperature in presence of catalyst salts.    USE - Method for transesterification of biofuel based on combined catalysis of metal-supported solid catalyst salts in mesoporous materials, and homogeneous catalyst solution.    ADVANTAGE - The biofuel transesterification method improves synthesis of biodiesel, yield and conversion of reactants, and is economical with reduced reaction time.
NOVELTY - The system is provided with high dynamic aerobic process to restore depleted dissolved oxygen in the water by the effect of chemical and biological elements to oxidize organic matter, and provides large amount of oxygen directly.    USE - System for aerobic ecological floating.
NOVELTY - Cultivation of hybrid semilate rice comprises sowing and fertilizing rice seedling bed with less nitrogen fertilizer and more phosphate and potash fertilizers; increasing disease and pest resistance of semilate rice tender seedling using an organic fertilizer; transplanting seedlings after 20-40 days at 7 x 7 inches distance and at 1-2 seedlings; fertilizing with less nitrogen fertilizer and more phosphate fertilizer and potash fertilizer; irrigating paddy field with sufficient water at water level of not greater than 5 (preferably not greater than 8) cm; drying the field; and weeding using a medicine with river sand.    USE - Cultivation of hybrid semilate rice (claimed).    ADVANTAGE - The method is environmentally friendly; increases yield; reduces and eliminates a third tilling for semilate rice through scientific fertilization, irrigation and planting measurement; increases light and ventilation of paddy field to increase disease and pest resistance of tender seedlings with small amount of or without pesticide; and can shorten nutritional stage and prolong reproductive stage of semilate rice.
NOVELTY - The technique involves filtering and de-oiling oil-water to be separated by a stage filter that is filled with surface accumulated filter materials e.g. gel resin. An effluent is filtered from a liquid outlet of the stage filter by another stage filter filled with inner pore deep absorption type filter materials e.g. activated carbon grains. The former stage filter is provided with a shell whose inside is orderly installed with liquid inlet area, filter material layer, an oil-water converging pipe and oil-water separating area from bottom to top.    USE - Technique for de-oiling steam condensed liquid of petrifaction industry, industrial waste water and biochemical disposed water (all claimed) by filtering process.    ADVANTAGE - The technique can separate the oil-water of the extracted liquid of the metallurgical engineering by wet process.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a steam condensed liquid de-oiling technique.
NOVELTY - A straw carbonization stove comprises a stove body; a stove door provided in front of stove body; a chimney provided on upper part of stove body; and an oxygen controlling device comprising flue, sealing cover, lead screw, shaft liner, transmission shaft, driving gear, driven gear and handle. The stove body and stove door are provided with cavities which are connected with a water tank. An interior of the chimney is provided with a fire-controlling adjusting plate connected with an operation handle assembled on stove body through a coupling rod.    USE - Straw carbonization stove.    ADVANTAGE - The straw carbonization stove is easy to manufacture, and has high carbonization quality, high product yield and short production time. Little smoke is discharged.    DETAILED DESCRIPTION - A straw carbonization stove comprises a stove body; a stove door provided in front of stove body; a chimney provided on upper part of stove body; and an oxygen controlling device comprising flue, sealing cover, lead screw, shaft liner, transmission shaft, driving gear, driven gear and handle. The stove body and stove door are provided with cavities which are connected with a water tank. An interior of the chimney is provided with a fire-controlling adjusting plate connected with an operation handle assembled on stove body through a coupling rod. The flue has an air outlet connected with a lower end of the chimney, and an air inlet connected with the inner cavity of stove body and provided with a sealing cover. The sealing cover is assembled at lower end of the lead screw which is interlocked with an inner screw thread of shaft liner by upper end. An outer screw thread of shaft liner is interlocked with an inner screw thread of fixed base. The driven gear is assembled on the shaft liner and connected with the driving gear through chains. The driving gear is assembled on the transmission shaft with the handle.
NOVELTY - A catalyst is obtained by impregnating 10-50 weight% of copper, 5-20 weight% of ceria and 30-60 weight% of zinc.    USE - Catalyst is used for water gas shift reaction for polymer electrolyte fuel cell, hydrogen power plant, ammonia synthesis process and petrochemistry (all claimed).    ADVANTAGE - The catalyst has high conversion effect, durability and high activity even at high and low temperature. The carbon monoxide is converted into highly pure hydrogen using the catalyst.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of catalyst. Copper, zinc and ceria precursor are dissolved in ultra-pure water at 20-60 degrees C, to obtain active metal salt aqueous solution. Ceria is dipped in active metal salt aqueous solution at 30-60 degrees C. The catalyst precursor is filtered, dried in oven at 80-120 degrees C for 2-24 hours, plasticized after raising temperature of the dried catalyst precursor from room temperature to 400-600 degrees C and speed rate of 3-10 degrees C/minute for 2-8 hours under air atmosphere, and molded into tablet or pellet shape by mixing the catalyst and 1~5 weight% of graphite; and    (2) water gas shift reaction which involves converting carbon monoxide into hydrogen using the catalyst at 108-400 degrees C and speed of 3000-10000 hr-1.
NOVELTY - Method for synthesizing biodiesel by reusing distillation by-product, involves esterifying alcohol and oil, separating crude biodiesel and glycerine, and distilling crude biodiesel, where the biodiesel yield productivity and reaction speed are increased by adding remaining reactant after refluxing the remaining by-product (1-10 weight%) based on the weight of oil.    USE - The method for synthesizing biodiesel by reusing distillation by-product (claimed).    ADVANTAGE - The biodiesel is synthesized economically by reusing distillation by-product, increases biodiesel yield productivity, and increases reaction efficiency simultaneously.
NOVELTY - A main catalyst metal precursor, a reaction promoter metal precursor and a diol compound are mixed, and resulting compound is reduced using reducing agent having boron-containing compound (1), and reduced material is refined and dried to obtain fuel cell catalyst.    USE - Manufacture of fuel cell catalyst used for fuel cell electrode for membrane electrode assembly used in fuel cell (all claimed).    ADVANTAGE - The fuel cell catalyst provides fuel capacitor having excellent activity, and fuel cell having excellent power density.    DETAILED DESCRIPTION - A main catalyst metal precursor, a reaction promoter metal precursor and a diol compound are mixed, and resulting compound is reduced using reducing agent having boron-containing compound of formula: MB(OR1OH)4 (1), and reduced material is refined and dried to obtain fuel cell catalyst.    M=sodium, and lithium or potassium;and    R1=2-10C optionally substituted alkyl.
NOVELTY - Two-component mixed refrigerant comprises (in weight%): R170(ethane) (1-6) and R1270(propylene) (94-99).    USE - Two-component mixed refrigerant.    ADVANTAGE - The mixed-refrigerant has excellent refrigeration capacity and does not cause environmental pollution. The mixed-refrigerant improves the durability of system due to low discharge temperature of a compressor.
NOVELTY - A heat exchange apparatus (640) heats supplied water with heating apparatus to produce water vapor. A source gas feed route is connected to a source gas supply pipe (622S) to supply hydrocarbon source gas by which desulphurization is performed in a modifier (620). A water vapor mixing unit merges hydrocarbon source gas and produced water vapor and supplies it to the modifier.    USE - Reformation unit for use as hydrogen gas production apparatus in fuel cell system (claimed) used for apartment houses and stores.    ADVANTAGE - The utilization amount of raw material of reformed gas such as hydrogen gas can be controlled easily.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the reformation unit in fuel cell system.    Modifier (620)    Source gas supply pipe (622S)    Heat exchange apparatus (640)    CO modifying device (820)    CO selective-oxidation device (830)
NOVELTY - A combustion deodorizing apparatus (12) burns and deodorizes anaerobic gas (G) from a storage unit (11). A concentrator (14) concentrates the anaerobic gas into concentration anaerobic gas (G1) before introducing the gas into the combustion deodorizing apparatus.    USE - For processing organic substance e.g. livestock excrement.    ADVANTAGE - A large amount of organic substances are processed without increasing the apparatus cost.    DETAILED DESCRIPTION - The storage unit is equipped with compost, which fragments the organic substance before introducing into the deodorizing apparatus. A condenser (13) and dehumidifier (21) separate moisture content from anaerobic gas. An air introducing apparatus (16) introduces cooling air (A4) into the concentrator and a return path (17) that introduces the cooling air repeatedly into the concentrator.    DESCRIPTION OF DRAWING(S) - The figure shows a block diagram of the organic substance processing system.    Storage unit (11)    Combustion deodorizing apparatus (12)    Condenser (13)    Concentrator (14)    Air introducing apparatus (16)    Return path (17)    Dehumidifier (21)    Cooling air (A4)    Anaerobic gas (G)    Concentration anaerobic gas (G1)
NOVELTY - The combustion apparatus (10) has a temperature detector (18) for detecting the temperature of the flame produced during the burning of hydrogen containing gas and hydrocarbon type fuel supplied by a hydrogen containing gas supply pipe (11) and a fuel feeding pipe (12). A controller (19) stops the supply of hydrogen containing gas and hydrocarbon type fuel from the gas supply pipe and the fuel feeding pipe based on the detected temperature.    USE - For modifier (claimed) of fuel cell electric power generation system (claimed).    ADVANTAGE - The combustion operation is performed safely by enabling detection of ignition failure and accidental fire based on the detected temperature of the flame.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for modifier operation method.    DESCRIPTION OF DRAWING(S) - The figure shows the top and longitudinal cross-sectional views of the combustion apparatus and the fragmentary longitudinal cross-sectional views of the combustion apparatus in the state of burning the hydrocarbon type fuel and in the state of burning the hydrogen containing gas. (Drawing includes non-English language text)    Combustion apparatus (10)    Hydrogen containing gas supply pipe (11)    Fuel feeding pipe (12)    Temperature detector (18)    Controller (19)
NOVELTY - Preparing renewable fuel involves obtaining carbon dioxide from natural or chemical source that would be present in or discharged into the atmosphere; and producing energy storage and transportation material or fuel sufficient to generate energy by hydrogenatively converting the carbon dioxide thus obtained to produce methanol as the material or fuel.    USE - For preparing renewable fuel (claimed), used in internal combustion engines or fuel cells.    ADVANTAGE - The method is environmentally beneficial; utilizing the convenient energy storage and transportation materials, the methanol or dimethyl ether in order to minimizes or eliminates the disadvantages or dangers inherent in the use and transportation of hydrogen, liquefied natural gas (LNG) or liquefied petroleum gas (LPG); provides efficient and economical process; reduces carbon dioxide, major greenhouse gas in the atmosphere thus mitigating global warming; provides effective environmental recycling of carbon dioxide and methanol.
NOVELTY - Converting (M1) a carbonaceous material to a desired product comprising at least one hydrocarbon or alcohol, involves: (A) gasifying the carbonaceous material at least at 700 degrees C to form synthesis gas; and (B) flowing the synthesis gas in a microchannel reactor in contact with a catalyst to convert the synthesis gas to the desired product.    USE - For converting a carbonaceous material selected from coal, oil, biomass, and/or solid-waste, preferably municipal solid waste, hazardous waste, refuse derived fuel, tires, trash, sewage sludge, animal waste, petroleum coke, trash, garbage, agricultural waste, corn stover, switch grass, wood cuttings, timber, grass clippings, construction demolition materials, plastic material, cotton gin waste, landfill gas, biogas, and/or natural gas to a desired product comprising at least one hydrocarbon or alcohol, such as low boiling hydrocarbons, or paraffins, useful as fuels or lubricating oils; or alcohols selected from e.g. methanol, ethanol, 1-propanol, 2-propanol, 1-butanol, or 2-butanol (all claimed) useful as synthetic fuels.    ADVANTAGE - The process is cost effective for producing fuels from cheaper sources.
NOVELTY - The jig has recess that is formed on a metal mold arranged around a membrane electrode assembly. A plate-shaped fuel-cell structural object is mounted on the recess along lamination direction such that the end surface of the structural object contacts with the recess of the metal mold.    USE - Jig for manufacture of fuel cell (claimed) such as polymer electrolyte fuel cell and solid-oxide electrolyte fuel cell.    ADVANTAGE - Since the fuel-cell structural object contacts with the recess of the metal mold, the lamination offset generated with respect to structural object can be suppressed, and the fuel cell can be manufactured easily.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacturing method of fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart explaining the manufacturing process of cell unit of the fuel cell. (Drawing includes non-English language text)
NOVELTY - A gas diffusion layer (22) and a gas flow path (24) containing metal porous block integrated with carbon fibers are prepared separately. The gas diffusion layer and the gas flow path are accumulated and compressed in the lamination direction. The accumulated and compressed gas diffusion layer and gas flow path are subjected to baking operation for forming a gas flow path formation block (16).    USE - Gas flow path formation block for fuel cell.    ADVANTAGE - The performance decrement of the fuel cell is suppressed effectively by increasing the contact area of the gas diffusion layer and the gas flow path.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for gas flow path formation block.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of the gas flow path formation block manufacturing process.(Drawing includes non-English language text)    Gas flow path formation block (16)    Gas diffusion layer (22)    Gas flow path (24)
NOVELTY - The fuel cell apparatus (130) has a reaction apparatus (110) for generating fuel supplied to a fuel cell (140), and a control unit (133) for controlling the operation of the reaction apparatus. The control unit stops the operation of the reaction apparatus, when an improper signal is received from a signal reception section (134).    USE - Fuel cell apparatus for portable electronic device (claimed) such as notebook type personal computer, personal digital assistant, electronic notebook, digital camera, mobile telephone, wristwatch and game machine device.    ADVANTAGE - Since the fuel cell system is stopped in the drag-in prohibition area and its vicinity of high temperature, the reaction apparatus is not overheated.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for control system of fuel cell apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the portable electronic device. (Drawing includes non-English language text)    Reaction apparatus (110)    Fuel cell apparatus (130)    Control unit (133)    Signal reception section (134)    Fuel cell (140)
NOVELTY - The system has an air compressor (10) that supplies compressed air to fuel cell (14). A heat exchange element performs heat exchange between water generated from fuel cell and compressed air supplied to fuel cell. The heat exchange element is operated when correlation value of temperature of air compressor is larger than a predetermined setting value. The air compressor is a root type compressor.    USE - Air compressor system.    ADVANTAGE - Cooling of air compressor can be performed efficiently by the heat exchange between water and compressed air, without requiring complicated control.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the air compressor system. (Drawing includes non-English language text)    Compressor (10)    Fuel cell (14)    Hydrogen tank (18)    Supply line (20)    Flow path (24)
NOVELTY - A hydrogen generating apparatus has a gas supply unit (6) to supply high concentration nitrogen gas with respect to permeation unit (4C) in which separation-extraction of hydrogen gas is carried out by hydrogen separation membrane (4B) and a modification unit (4A) in which the fuel is reformed by hydrogen separation membrane, and the reformed gas flows.    USE - Hydrogen generating apparatus is used as supply source for fuel cell and internal combustion engine (both claimed).    ADVANTAGE - The hydrogen generating apparatus is of reduced size, improves the rate of hydrogen extraction, and the modification reaction in the modification unit is carried out at favorable temperature.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of block diagram of hydrogen generating apparatus. (Drawing includes non-English language text)    Modification unit (4A)    Hydrogen separation membrane (4B)    Permeation unit (4C)    Gas supply unit (6)    Nitrogen content separation membrane (6A)
NOVELTY - A fuel reformer (11) has a heating unit (13) for heating fuel with pressurized steam, a pressure reduction unit (15) for accommodating fuel processed by heating unit and carrying out pressure reduction, and a fuel drying unit for drying pressure-reduced fuel. The drying unit has a steam pressurizing portion (15b) for pressurizing steam generated in pressure reduction unit, and a heat exchange portion (15c) for carrying out heat exchange between pressurized steam and to-be-dried fuel.    USE - Fuel reformer is used in power generating plant.    ADVANTAGE - The fuel reformer consumes reduced amount of energy for modifying fuel, and provides power generating plant having improved electric power generation efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for modification for fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows the flow sheet of power generating plant. (Drawing includes non-English language text)    Fuel reformer (11)    Heating unit (13)    Pressure reduction process unit (15)    Steam pressurizing unit (15b)    Heat exchange portion (15c)
NOVELTY - A fuel cell system (1) contains tank (2) for storing water or alkaline aqueous solution, reactor (4), pump (6), hydrogen gas flow path (8) and supply control unit (10,11). The reactor is accommodated with hydrogen-producing substance which reacts with water or alkaline aqueous solution and generates hydrogen. A pump supplies water or alkaline aqueous solution into tank. The hydrogen gas flow path supplies hydrogen gas produced within reactor to fuel cell (5). The supply control unit controls discharge amount of water or alkaline aqueous solution from pump.    USE - Fuel cell system (claimed) is used as power supply for notebook personal computer, mobile telephone and motor vehicles.    ADVANTAGE - The fuel cell system has simple structure and controlled generation of hydrogen.    DETAILED DESCRIPTION - A fuel cell system contains tank for storing water or alkaline aqueous solution, reactor, pump, hydrogen gas flow path and supply control unit. The reactor is accommodated with hydrogen-producing substance which reacts with water or alkaline aqueous solution and generates hydrogen. A pump supplies water or alkaline aqueous solution into tank. The hydrogen gas flow path supplies hydrogen gas produced within reactor to fuel cell. The supply control unit controls discharge amount of water or alkaline aqueous solution from pump with respect to hydrogen gas flow which in interposed by hydrogen gas flow path. An INDEPENDENT CLAIM is included for method for controlling amount of hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of fuel cell system.    Fuel cell system (1)    Water tank (2)    Reactor (4)    Fuel cell (5)    Pump (6)    Hydrogen gas flow path (8)    Supply control units (10,11)
NOVELTY - The apparatus (1) has a desulfurization tower (3) de-sulfurizing sewage gas i.e. biogas, emitted with a fermenter (2). A compressor (4) compresses desulfurization gas. A cooler (5) cools the compressed gas. A dehumidifier (6) dehumidifies the cooled gas. A storage container (7) stores the dehumidified gas temporarily. A supply line (L6) supplies storage gas to a consumption apparatus (8). A direct delivery line (L7) directly guides the sewage gas that passes through the fermenter or the desulfurization tower to the supply line.    USE - Sewage gas i.e. biogas, storage supply apparatus for use in sewage treatment and livestock farming waste treatment installations.    ADVANTAGE - The direct delivery line directly guides the sewage gas that passes through the fermenter or the desulfurization tower to the supply line, thus reducing the compressor and cooler motive power and the cost of the apparatus, suppressing the exhaustion/degradation of the dehumidification agent or the adsorbent, and simplifying the structure of the apparatus.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a sewage gas storage supply apparatus operating method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of a sewage gas storage supply apparatus.    Supply line (L6)    Direct delivery line (L7)    Sewage gas storage supply apparatus (1)    Fermenter (2)    Desulfurization tower (3)    Compressor (4)    Cooler (5)    Dehumidifier (6)    Storage container (7)    Consumption apparatus (8)
NOVELTY - Combinatorial method for producing low sulfur diesel and high-octane rating naphtha comprises: (a) making distillate hydrocarbon feeding; (b) making high-balmy and basically alkylate-removing hydrocarbon feeding react in hydrocracking reaction zone; (c) mixing drainage flow of hydrodesulfurization reaction zone and drainage flow of hydrocracking reaction zone and obtaining mixed drainage flow; and (d) separating mixture to produce hydrogen enriched air flow, low sulfur diesel flow and high-octane rating naphtha flow.    USE - The method is useful for producing low sulfur diesel and high-octane rating naphtha (claimed).    ADVANTAGE - The invention produces hydrogen enriched air flow, low sulfur diesel and high-octane rating naphtha.    DETAILED DESCRIPTION - Combinatorial method for producing low sulfur diesel and high-octane rating naphtha comprises: (a) making distillate hydrocarbon feeding whose boiling range is greater than 149 degrees C (300 degrees C) and hydrogen enriched supplementary air flow react in hydrodesulfurization reaction zone containing desulfurization catalyst to produce drainage flow of hydrodesulfurization reaction zone containing hydrocarbon whose concentration of sulfur has been reduced; (b) making high-balmy and basically alkylate-removing hydrocarbon feeding react in hydrocracking reaction zone containing hydrocracking catalyst to produce drainage flow of hydrocracking reaction zone of monocyclic aromatic compound boiling at range of naphtha; (c) mixing drainage flow of hydrodesulfurization reaction zone and drainage flow of hydrocracking reaction zone and obtaining mixed drainage flow; and (d) separating mixture coming from the step (c) to produce hydrogen enriched air flow, low sulfur diesel flow and high-octane rating naphtha flow.
NOVELTY - The sludge recycling system includes a slurry pump, a sludge solid-liquid separator, a dosing machine, a kneading homogenizer, a forming machine, and a drying machine which are all connected to and controlled by a PLC system to form an automatic control system. The slurry pump is a sludge screw rod pump. The sludge solid-liquid separator is a screw extruding solid-liquid separator. The kneading homogenizer is a double-screw kneading mixer. The forming machine is a high-pressure screw forming machine. The drying device is a panel turnover dryer.    USE - Sludge recycling system for recycling clean fuel from municipal sludge. Can be used in large, intermediate, or small municipal sewage processing plant for recycling sludge.    ADVANTAGE - Provides a fuel recycling system that has reduced cost, small land space, fast effect, and high conversion rate.    DESCRIPTION OF DRAWING(S) - The drawing shows the flow diagram of the sludge recycling system. (Drawing includes non-English language text).
NOVELTY - A wastewater is treated by flocculating, and carrying out acidic analysis; separating out wood fiber from wastewater under acid condition, and carrying out electrolytic catalysis oxidization; exerting direct current voltage, and filling oxygen to carry out electrolytic catalysis oxidization; carrying out methanation reaction under the action of anaerobic fermentation bacterium; and recycling methane gas, and discharging treated water.    USE - Method of treating wastewater (claimed) for producing ethanol from wood fiber as corn straws and broom corn straws.    ADVANTAGE - The method provides high concentration sewage, effectively recovers and recycles waste material from wastewater, converts organic pollutant at high concentration into reusable methane, and has clean production.    DETAILED DESCRIPTION - Wastewater treatment involves flocculating wastewater, and carrying out acidic analysis; separating out wood fiber from wastewater under acid condition, and carrying out electrolytic catalysis oxidization; conveying into electrolytic catalysis oxidization reactor with three-dimensional particle electrode comprising anode, cathode and solid catalyst particles; exerting direct current voltage, and filling oxygen to carry out electrolytic catalysis oxidization; carrying out methanation reaction under the action of anaerobic fermentation bacterium; and recycling methane gas, and discharging treated water.
NOVELTY - A synthetic charcoal comprises wood chip or rice hull with 10% water content.    USE - A synthetic charcoal.    ADVANTAGE - The synthetic charcoal does not easily break; and has simple manufacturing process, easy to obtain raw material, high heat value that is equal to heat amount obtained by burning normal charcoal, and compact density. The shape of the product can be regulated.
NOVELTY - The stove has a furnace cover (2) installed on a furnace body (1). A heating filtering device (3) is installed on the furnace body. A gas pipe (4) is installed on an upper part of the furnace body. The gas pipe is connected with a hearth (6) of the furnace body through the heating filtering device. A blast pipe (7) is connected with the hearth through a blower (8). The blower is mounted on bottom of the hearth. The blast pipe is connected with the hearth through air inlets uniformly distributed on wall of the blower.    USE - Energy-saving firewood gas stove for a rural domestic gas. Can also be used for tea-making industry.    ADVANTAGE - The stove is simple in structure. The stove reduces consumption of space and makes installation and maintenance convenient, thus uniformly enhancing air-blowing and enabling the generated fuel gas to have high quality without influencing filtering effect. The water in the filtering device can cool and filter the fuel gas, and can be heated by the heat generated during combustion of the firewood in the hearth so as to be directly used as hot water, thus improving the fuel utilization rate, and hence reducing the energy and protecting the environment.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of an energy-saving firewood gas stove.    Furnace body (1)    Furnace cover (2)    Heating filtering device (3)    Gas pipe (4)    Hearth (6)    Blast pipe (7)    Blower (8)
NOVELTY - Preparing high-temperature clean industrial fuel by using pine-stump light oil comprises fully mixing pine-stump light oil with three kinds of organic solvents in a mixing tank according to a certain proportion to obtain the fuel, where the pine-stump light oil is mixed with methanol, ethanol and petroleum ether according to a certain proportion to from the clean industrial fuel.    USE - The method is useful for preparing high-temperature clean industrial fuel (claimed).    ADVANTAGE - The invention not only reduces the cost, but also lessens the pollution of the exhaust gas. The temperature and heat are suitable for firing high-grade ceramic and handiwork and high-temperature clean melting industry.
NOVELTY - Preparing medium-temperature clean industrial fuel by using pine-stump light oil comprises fully mixing pine-stump light oil with three kinds of organic solvents in a mixing tank according to a certain proportion to obtain the fuel, where the pine-stump light oil is mixed with methanol, ethanol and petroleum ether according to a certain proportion to from the medium-temperature clean industrial fuel.    USE - The method is useful for preparing medium-temperature clean industrial fuel (claimed).    ADVANTAGE - The invention not only lowers the cost, but also lessens the pollution of the tail gas. The temperature and heat are suitable for painting automobiles and small clean melting enterprises.
NOVELTY - Operating a compression ignition engine, comprises supplying an aqueous ethanol fuel comprising ethanol, water and ignition improver to the engine and lubricating the engine with a lubricating oil composition, which comprises a base oil of lubricating viscosity and additives comprising one or more nitrogen-containing dispersant additives and one or more neutral or over-based, metal salt-containing detergent additives.    USE - The method is useful for operating a compression ignition engine (claimed), which is compression ignition internal combustion engine.    ADVANTAGE - The method mitigates problems of interaction between the oil composition and the fuel in the compression ignition engine and internal combustion engine. The lubricating oil composition: has a reduced tendency to form deposits when in contact with aqueous ethanol fuel; and has low sulfur concentration, which reduces the impact of the exhaust emissions from the engine on any after treatment devices.    DETAILED DESCRIPTION - Method of operating a compression ignition engine, comprises supplying an aqueous ethanol fuel comprising ethanol (70-96 wt.%), water (10-2 wt.%) and ignition improver (up to 20 wt.%) to the engine and lubricating the engine with a lubricating oil composition, which comprises a major amount of a base oil of lubricating viscosity and a minor amount of additives comprising one or more nitrogen-containing dispersant additives and one or more neutral or over-based, metal salt-containing detergent additives, where the metal salt-containing detergent additives is present at greater than 0 to 1 wt.% and the weight ratio of the total amount of nitrogen in the dispersant additives and the total amount of metal salt in the detergent additives is at least 0.1:1.
NOVELTY - Excited active hydrogen containing water generated by performing magnetic process with respect to water, is electrolyzed to produce hydrogen gas and oxygen gas.    USE - Production of hydrogen gas and oxygen gas for fuel.    ADVANTAGE - The hydrogen gas and oxygen gas are efficiently and rapidly produced with low electric power, and without generating carbon dioxide gas.    DESCRIPTION OF DRAWING(S) - The drawing shows the structure of a magnetic processing system for generating excited active hydrogen containing water. (Drawing includes non-English language text)    Water tank (2)    Magnetic processing apparatus (4a,4b)    Pump (6)    Valves (8b,8r)    Circulatory system (R)
NOVELTY - A gold-containing catalyst is formed by producing starting alloy and dealloying. The production of starting alloy involves melting together gold and at least one less noble metal consisting of silver, copper, rhodium, palladium, and platinum. The dealloying process involves at least partial removal of the at least one less noble metal by dissolving the at least one less noble metal out of starting alloy.    USE - Method for forming gold-containing catalyst (claimed) for oxidation of carbon monoxide to carbon dioxide used in fuel cell preferably polymer electrolyte membrane fuel cell; and for protection of anode catalyst against blocking by carbon monoxide.    ADVANTAGE - The formed catalyst has porous structure, and accelerates and/or influences product selectivity of oxidation and reduction reactions.
NOVELTY - The method involves supplying hydrogen gas to a fuel cell stack (10) in a fuel system, and exhausting current generation in the fuel cell stack using a current generating unit. Atmosphere air is reduced to diffuse to an air electrode (14), and an electrolyte film is formed on the air electrode. An oxide film is formed in the air electrode catalyst layer. An external lead (22) is connected with a switch (18), and a metallic catalyst reaction point of the air electrode catalyst layer is determined to activate accelerate of the fuel cell.    USE - Method for accelerating activation of a fuel cell.    ADVANTAGE - The method easily activates a platinum catalyst in the fuel cell and avoids high load and long time load cycle. The method reduces the need of hydrogen gas amount during activating process of the fuel cell stack and provides efficient activation procedure.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a fuel cell activation accelerating method.'(Drawing includes non-English language text)'    Fuel cell stack (10)    Fuel anode (12)    Air electrode (14)    Transmitted film (16)    Switch (18)    External lead (22)
NOVELTY - Invention relates to liquid fuel compositions for diesel engines based on biofuel and can be used for producing liquid fuel from organic material, mainly of plant origin, with physical and chemical characteristics equivalent to those of petroleum diesel fuel, but with better environmental characteristics. The fuel is a mixture of 50 vol % biofuel, 10 vol % butyric acid octyl ester, 10 vol % pentanoic acid heptyl ester, 10 vol % pentanoic acid nonyl ester, 10 vol % caproic acid nonyl ester, 10 vol % butyric acid isoamyl ester.    USE - Chemistry.    ADVANTAGE - Invention reduces adverse effect of power generation on the environment, widens the raw material base by using renewable material. 2 tbl
NOVELTY - A solar temperature-increasing square or rectangular methane tank comprises a feed tank, a discharge tank, a square or rectangular fermenting tank, and a tank cover matching with the fermenting tank; where the tank cover is a light-absorbing/light-passing shell with curved surface, or tapered light-absorbing/light-passing shell; and a solar warm chamber or solar heat insulating shield is mounted above the fermenting tank and the tank cover with curved surface.    USE - The solar temperature-increasing square or rectangular methane tank is useful for multiple kinds of fermenting raw materials, especially a great amount of agricultural straws.    ADVANTAGE - The solar temperature-increasing square or rectangular methane tank can generate methane normally at lower temperature; and it has simple structure and low construction cost. Moreover, it can save time and labor, with high utilization of solar energy, low domination and healthy. Additionally, it is convenient for use and maintenance, and is very beneficial for rural fertilizer stacking and environmental protection.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the solar temperature-increasing square or rectangular methane tank.
NOVELTY - The biomass gasification furnace has feeding opening (1), gas generation chamber (2), furnace body (3), slag outlet (6), circular chassis (8), fan (12), purifier (13), infrared stove (14) and furnace frame (15). A rotary air distributor (4) is arranged on top of guide air chamber at the middle of circular chassis. An ash outlet is arranged at the bottom center of guide air chamber. The air inlet and guide baffle are arranged at side of guide air chamber.    USE - Biomass gasification furnace.    ADVANTAGE - Eliminates the need of pressurizing gas generation chamber, and prolongs burning time in which the gas generation chamber can be used for 4 hours continuously after being full. Enables to use biomass gasification furnace at any time without secondary light, and simplifies operation. Enables to automatically feed flammable substance, performs complete conversion, and obtains high gas generation rate of flammable substance.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of biomass gasification furnace.    Feeding opening (1)    Gas generation chamber (2)    Furnace body (3)    Rotary air distributor (4)    Slag outlet (6)    Circular chassis (8)    Fan (12)    Purifier (13)    Infrared stove (14)    Furnace frame (15)
NOVELTY - Utilizing CO2 waste involves recovering carbon dioxide from an industrial process that produces a waste stream comprising carbon dioxide in an amount greater than an amount of carbon dioxide present in starting materials for the industrial process; producing hydrogen using a renewable energy resource; and producing a hydrocarbon material utilizing the produced hydrogen and the recovered carbon dioxide.    USE - For utilization of CO2 waste (claimed) which is useful for producing fuel materials e.g. methane, methanol carbon monoxide, syngas, gasoline products, and/or other fuel materials from carbon dioxide recovered from a waste stream of an industrial process and hydrogen produced using renewable energy resources.    ADVANTAGE - The method provides carbon dioxide in chemical forms which is more suitable for storage and transport costs in the production of the valuable fuels; and provides a relatively inexpensive and optimized system.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a system (S1) for utilizing waste CO2 comprising an industrial element for producing waste CO2, a second element powered by a renewable energy resource for producing hydrogen, and a third element utilizing the waste CO2 and the hydrogen for producing a hydrocarbon material; and    (2) a system (S2) for recycling carbon dioxide comprising a first plant configured to operate a process that produces a waste stream having carbon dioxide in an amount greater than an amount of carbon dioxide present in starting materials for the process, a second plant that generates power from a renewable energy resource, device for recovering the carbon dioxide from the waste stream, device for producing hydrogen using the power from the renewable energy resource, and device for producing a hydrocarbon material utilizing the produced hydrogen and recovered carbon dioxide.
NOVELTY - Anaerobic treatment device for treating wastewater containing sulfate and organic material comprises anaerobic bioreactor provided with water distributor for distributing wastewater; filler acid production stage for contacting wastewater to acidify the organic material and reduce sulfate; filler gas production stage for contacting the discharged water of filler acid production stage to produce biogas; and water discharging stage. The top part of the anaerobic bioreactor is connected with biogas devulcanizer through a biogas collection pipe.    USE - Anaerobic treatment device for treating wastewater containing sulfate and organic material at high concentration.    DETAILED DESCRIPTION - Anaerobic treatment device for treating wastewater containing sulfate and organic material comprises anaerobic bioreactor provided with water distributor for distributing wastewater; filler acid production stage for contacting wastewater to acidify the organic material and reduce sulfate; filler gas production stage for contacting the discharged water of filler acid production stage to produce biogas; and water discharging stage. The top part of the anaerobic bioreactor is connected with biogas devulcanizer through a biogas collection pipe. The biogas devulcanizer is connected with filler gas production stage through gas collection tank and biogas reflux pump. The water discharging stage is provided with water outlet, and is connected with water reflux opening of water distributor through water reflux pump.
NOVELTY - High salt-content organic wastewater treatment device comprises electric flocculating unit and membrane biological treatment unit. It carries out electric flocculating of wastewater in flocculating unit and then membrane separation and biological treatment in the membrane biological treatment unit. The electric flocculating unit comprises flocculating tank, flocculating area provided in the flocculating tank, parallel anode plate and cathode plate, deposition area provided on lower part of flocculating tank, and slag-removing machine provided on upper part of the flocculating tank.    USE - High salt-content organic wastewater treatment device.    ADVANTAGE - The device has simple treatment process, stable treatment effect, good quality of discharged water, and low operation cost.
NOVELTY - The device has a light path system producing two groups of optical interference fringes by using a light source (1), and an analogue to digital conversion circuit converting an image signal into a data signal. A microprocessor calculates a concentration value of detecting gas by comparing a level offset of two digital waveforms, and compensates precision of a concentration value calculation automatically by comparing distance value of a lowest power level centre point and a standard value corresponding to groups of interference fringe and two beams of quite dark interference fringes.    USE - Methane/carbon dioxide detecting device.    ADVANTAGE - The device has capability of zero automatic trace and precision auto-compensation for detecting the concentration of the methane or carbon dioxide in gas. The two groups of optical interference fringes in a light path are utilized to realize the differencing process of optical image, so that the device processes the data in differencing way, so as to improve the anti-interference capacity. The device solves the problem of the severe unbalance of the precision and severe drift caused by the aberration of the optical system for the optical interference methane detection instrument based on the auto-compensation principle of the apparatus precision. The device can be identified intelligently by the instrument, and the instrument can be calibrated in an effective manner when the device precision is severely unbalanced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a methane/carbon dioxide detecting device.    Light source (1)    Optical collector (2)    Diaphragm (3)    Image sensor (6)    Gas chamber (8)
NOVELTY - Method for producing ethanol using rhizome of Pueraria plant as a raw material, involves adding heat resistant liquefaction enzyme to rhizome of Pueraria plant, heating at 60-80 degrees C for 0.5-3 hours, adding heat resistant saccharogenic amylase, heating at 40-60 degrees C for 0.5-3 hours, and performing alcoholic fermentation.    USE - The method is useful for producing ethanol (claimed) which is used as fuel for motor vehicle.    ADVANTAGE - The ethanol can be mass produced cost-effectively by simple process.
NOVELTY - A hydrogen permselective membrane (1) comprises metal support body (2) which has greater than or equal to 2 through-holes (3), and palladium (Pd) alloy film (4) arranged so that through-hole might be covered to one surface of metal support body which has base layer (5) with thickness of 0.1-2 mu m and surface layer with thickness of 0.1-20 mu m that are laminated from metal support body side. The measurement surface area (S)/measurement region area (A) ratio of surface layer is greater than or equal to 2.    USE - A hydrogen permselective membrane for modifier used for carrying out steam reforming of hydrocarbon fuels and producing hydrogen rich gas.    ADVANTAGE - The hydrogen permselective membrane has outstanding hydrogen permeation efficiency in hydrogen purification.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of manufacturing hydrogen permselective membrane.    DESCRIPTION OF DRAWING(S) - The drawing shows a fragmentary sectional view of the hydrogen permselective membrane.    Hydrogen permselective membrane (1)    Metal support body (2)    Through-hole (3)    Palladium alloy film (4)    Base layer (5)
NOVELTY - Synthesizing nitramines involves nitrosylating an amine moiety to a nitrosamine by adding sodium nitrate into a solution of a strong acid and then adding the amine moiety to form the corresponding nitrosamine; and oxidizing the nitrosamine to its corresponding nitramine.    USE - For synthesizing nitramines (claimed) used in fuel cells and other portable power devices.    ADVANTAGE - The method enables to synthesize nitramines on a large scale. The process is a two-step process.
NOVELTY - Fuel based on vine shoots, with the content of energy crops, comprises a mixture containing basic energy crop in the form of vine shoots, with water content of up to 20 (preferably 29.99-90) wt.%, combustible additives (4.99-70 wt.%), and containing non-combustible additives (0.01-20 wt.%). The combustible additives are other energy crops, wood and tree bark, coal, vegetal waste and/or other secondary raw materials of vegetal origin. Each of the combustible additives has water content of up to 50 wt.%.    USE - As a vine shoots fuel (claimed) used in the area of acquiring renewable energy resources, particularly for heating and generation of hot service water; and in a steam engine or turbine to generate electric power or in a co-generation unit based on steam engine or turbine.    ADVANTAGE - The composition provides a technologically and economically effective fuel with favorable storage as well as combustive characteristics which is created by a fuel based on vine shoots.
NOVELTY - The device has an air-distribution plate (2) installed in an inner side of a furnace body, where the plate divides the furnace body into an upper cavity i.e. hearth (7), and a lower cavity i.e. air room (8). A feed inlet (6) is installed in a side of the hearth, and an air inlet pipe (5) is connected to a side of the air room. A slag emission pipe (4) is installed in an inner side of the air room. The slag emission pipe is connected with the hearth through the plate. Multiple windshields (1) are provided with windshield holes i.e. one-way opened holes, in the plate.    USE - Biomass fluidized bed spiral-flow air-distribution device for use in a biomass fuel generation field and an industry boiler.    ADVANTAGE - The device can apparently increase adaptability to a material and stability of an operation. The device performs fluidization direction combustion or gasification for the materials such as rice hull, wheat straw, corn straw, cotton straw, wood powder, branch and bark.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass fluidized bed spiral-flow air-distribution device.    Windshields (1)    Air-distribution plate (2)    Slag emission pipe (4)    Air inlet pipe (5)    Feed inlet (6)    Hearth (7)    Air room (8)
NOVELTY - The harmless treating process involves combining the tail fume and gas discharged from gas-solid separation with tail gas produced by the dried sludge belt delivery system and feeding them into a wet desulfurization system; and discharging tail gas by a fume discharge chimney after being sprayed by desulfurizing slurry. The fume is formed with the fume extracted from the front part of an air pre-heater of the coal powder boiler and the fume extracted from the back part of an ash separator. The mixed fume is fed into a sludge dryer to dry the sludge.    USE - Harmless treating process for changing municipal sludge into resource using coal powder boiler and coal delivering and tail gas exhausting system of existing power plant.    ADVANTAGE - The coal and dried sludge are burnt in the boiler, the exhausted fume enters the ash separator and a wet desulfurization system, and the tail gas generated during the conveying is exhausted to the desulfurization system, thus, the discharge of pollutant meets requirements and secondary pollution is avoided. Effectively makes use of the boiler and devices for coal delivery, de-dusting and de-sulfurizing, so the whole process is featured with simple device, it requires little investment, its building period is short, and its operation cost is low.    DESCRIPTION OF DRAWING(S) - The drawing shows the flowchart of the harmless treating process for changing municipal sludge into resource. (Drawing also includes non-English language text).
NOVELTY - The system (10) has a combustion chamber (31) with a distal end such that directed heated gas stream flows in a direction opposite to another direction along length of an inner pyrolysis chamber (35) between ends of a single-chambered pyrolysis unit (30). A rotary air lock (70) introduces biomass into the pyrolysis unit for capturing and channeling exhaust gases containing entrained matter resulting from pyrolytic reaction within the pyrolysis unit. A separating and collecting unit separates and collects bio-fuel entrained in the exhaust gases from the pyrolysis unit.    USE - Concentric-chambered pyrolysis system for subjecting biomass to pyrolysis to extract bio-fuel from the biomass.    ADVANTAGE - The system reduces the amount of heat loss to the surrounding environment through an outer wall of the single-chambered pyrolysis unit. The wall of the combustion chamber provides significant radiant heat transfer to the biomass flowing through the pyrolysis chamber at the designed temperature of the combustion exhaust, thus increasing the rate of heat transfer to the biomass, and hence subjecting biomass to pyrolysis to extract bio-fuel from the biomass in efficient manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for subjecting biomass to pyrolysis to extract bio-fuel from the biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a concentric-chambered pyrolysis system.    Concentric-chambered pyrolysis system (10)    Single-chambered pyrolysis unit (30)    Combustion chamber (31)    Inner pyrolysis chamber (35)    Outer pyrolysis chamber (39)    Bio-oil condensing system (62)    Rotary air lock (70)    Cyclone separator (80)
NOVELTY - The method involves placing excrement in a reaction kettle for thermolysis to obtain biomass liquefied oil, where the excrement is obtained from chickens, ducks, geese, pigs, and/or human. Solid content in the excrement is obtained from 10 to 30 percentages by mass. The reaction kettle is utilized for a protecting and reducing gas or inert gas obtained by introducing a carrier gas e.g. reducing gas, hydrogen or carbon monoxide, into the reaction kettle. A catalyst is utilized to perform the thermolysis reaction.    USE - Method for preparing biomass liquefied oil i.e. biomass fuel oil (claimed), which is utilized to prepare diesel oil, gasoline, and kerosene.    ADVANTAGE - The method reaches the energy input and output ratio of 1:3. The average thermal value of the biomass liquefied oil is enhanced as high as 34.65 mega joules/kilogram (MJ/kg), and provides stable thermal value of the biomass liquefied oil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biomass liquefied oil to prepare diesel oil, gasoline, and kerosene.
NOVELTY - The carbonization device comprises of a loading car (1), a loading rail (2), a tractor (3), fuel gas pipes (27,29,32,37), an explosion proof dust remover (28), a fuel gas distributor (36), and a wind distribution case (42). A carbonization furnace (5) has an upper section equipped with a spiral feeding machine (20), a middle section equipped with rotary grates (8-10), and a lower section equipped with a fuel gas combustion nozzle (11), a cooling case (6), and a spiral carbon discharging machine (7).    USE - Carbonization device for producing carbon and wood tar from agricultural and forest wastes.    ADVANTAGE - Provides device that is capable of using small granular wastes such as wood processing residue, furfural residue, shell and kernel as raw materials, and using volatile matter in the raw materials as heat source to produce carbon and wood tar. Provides device with simple structure, and convenient operation. Enables producing carbon with stable quality. Enables converting agricultural and forest wastes in large scale.    DESCRIPTION OF DRAWING(S) - The drawing shows the cross sectional view of the carbonization device.    Loading car (1)    Loading rail (2)    Tractor (3)    Carbonization furnace (5)    Cooling case (6)    Spiral carbon discharging machine (7)    Rotary grates (8-10)    Fuel gas combustion nozzle (11)    Spiral feeding machine (20)    Fuel gas pipes (27,29,32,37)    Explosion proof dust remover (28)    Fuel gas distributor (36)    Wind distribution case (42)
NOVELTY - The generating method involves applying an electric field to a liquid-phase working medium (50), and applying elastic vibrations to the working medium to actuate excitation of an electrical discharge and produce sonoplasma. Preferably, the electric field is created through the application of DC or AC voltage to discharge electrodes (46,47), or through the introduction of electromagnetic waves into the working medium.    USE - Generating method for volumetric abnormal glow sonoplasma discharge within liquid-phase working medium contained in reactor for performing a chemical process. Uses include but are not limited to decomposing water, producing hydrogen, producing stable organic compounds, production of gases, wastewater treatment and disinfection, stimulation of oxidation-reduction reactions, reduction of oxide and sulfide compounds to their metals, production of pure metals and alloys in the form of nanosized powders, or metal coatings.    ADVANTAGE - Enables initiating and maintaining an abnormal glow volumetric sonoplasma discharge using a lower amount of electric power.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a volumetric abnormal glow sonoplasma discharge excitation apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic sectional view of a reactor for the initiation of volumetric abnormal glow sonoplasma discharge within non-conducting liquids fitted with an electro-acoustic transducer as a source of elastic vibrations.    Electro-acoustic transducer (41)    Water-cooled reaction chamber (43)    Rod electrodes (44)    Discharge electrodes (46,47)    Liquid-phase working medium (50)
NOVELTY - The device has a shell (1) with an upper end face welded with an upper top shell (2) and an upper connecting plate (4) of a water inlet pipe (6). A lower end face of the shell (1) is welded with a lower bottom shell (3) and a lower connecting plate (5) of a water outlet pipe (7). The shell wall is welded with a cold water pipe (8) and a hot water pipe (9). A gas inlet pipe (10) is inserted into a hole of the upper top shell.    USE - Circuitous separating device for a biomass gasification furnace.    ADVANTAGE - The device is simple and compact in structure, convenient to manufacture and installation and better in separating effect of the fuel gas, water gas and coke oil, which are circuitously cooled.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a circuitous separating device.    Shell (1)    Upper top shell (2)    Lower bottom shell (3)    Upper connecting plate (4)    Lower connecting plate (5)    Water inlet pipe (6)    Water outlet pipe (7)    Cold water pipe (8)    Hot water pipe (9)    Gas inlet pipe (10)
NOVELTY - The straw gasification furnace has an aero-genesis furnace (1) with an air-producing assembly (2) joined to a rolling furnace grate (3). The aero-genesis furnace is joined to an induced draft fan (5), which is joined to a filtering box (8) equipped with a clapboard. The filtering box is joined to an air-water separating box (13), which is joined to a kitchen range (18). The coaxial direct direction of the kitchen range is suspended and displaced with respect to a boiler furnace (19), which is separately joined to a heat supplying pipe (20), a fume drain pipe (17) and a water return pipe (22).    USE - Energy-saving type multi-functional straw gasification furnace used in heating and cooking.    ADVANTAGE - Provides gasification furnace with improved fuel gas quality and increased heat utility ratio.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of the energy-saving type multi-functional straw gasification furnace.    Aero-genesis furnace (1)    Air-producing assembly (2)    Rolling furnace grate (3)    Induced draft fan (5)    Filtering box (8)    Fume drain pipe (17)    Kitchen range (18)    Boiler furnace (19)    Heat supplying pipe (20)    Water return pipe (22)
NOVELTY - The tar water processor has a secondary purifying cylinder that is joined to primary and third purifying cylinders via a U-shaped pipe and a pipeline, respectively. The primary purifying cylinder has a top that is led out from a three-way inlet pipe towards the top of a biomass gasification furnace. All purifying cylinders are joined to a tar discharging valve, and communicated by a tar water discharge pipe. A purified fuel gas outlet is formed at both sides of the third purifying cylinder, while a tar water separation sleeve and a pipeline cleaning port are formed at inner and top sections.    USE - Tar water processor for biomass gasification furnace.    ADVANTAGE - Ensures automatic separation of tar, water, and combustible gas, while improving gasification combustion value. Suppresses degradation in biogas gasification quality due to loss of tar treatment.    DESCRIPTION OF DRAWING(S) - The drawing shows the cross sectional view of the tar water processor.
NOVELTY - The bio-mass molding system and a fuel energy-saving recycling device has a crusher cutter holder (21) mounted on the power shaft of a crusher. A material-crush cutter (14) is mounted on the crusher cutter holder. A housing case (13) stores the crusher cutter holder and is connected with a loading tank (12). The loading tank is equipped with a material-inlet roller (9). The power box is equipped with a power shaft, which in turn is equipped with symmetrical rod-stock formers and lump-stock former, matching the molding-material fuel device.    USE - Bio-mass molding system and fuel energy-saving recycling device.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of a bio-mass molding system and fuel energy-saving recycling device.    Material inlet roller (9)    Loading tank (12)    Housing case (13)    Material-crush cutter (14)    Crusher cutter holder (21)
NOVELTY - The environment friendly faggot fuel gas stove has a combustion stove (1) and a wind pipe (9) that are connected to a draft fan, which is accessed from a lower section. A fuel gas pipe (3) extends from the upper region of the fuel gas stove, and inserted into a fuel gas filter (5). The pure fuel gas pipe is connected to the fuel gas filter, and to a fuel gas stove (6) or a gas storage bucket (7).    USE - Environment friendly faggot fuel gas stove.    ADVANTAGE - Provides wide and easy to obtain fuel source for fuel gas stove. Ensures fuel gas purifying and automatic separation of production material, while improving quality of the produced fuel gas. Enhances safety due to stove with nearly no pressure, thus providing environmental protection, clean, and convenient use.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of the environment friendly faggot fuel gas stove.    Combustion stove (1)    Fuel gas pipe (3)    Fuel gas filter (5)    Fuel gas stove (6)    Gas storage bucket (7)    Wind pipe (9)
NOVELTY - The biomass gasification gas stove has a furnace (1) and a separator (2) that are set in parallel in a water tank (3). A gas stove (5) is set on a water tank cover (6), which is the hearth of the gas stove. A blower (4) is set outside of the water tank. A tube valve system (7) connects the associated components to form an integral structure.    USE - Biomass gasification gas stove.    ADVANTAGE - Provides gas stove that efficiently combusts the combustible gas to generate heat..    DESCRIPTION OF DRAWING(S) - The drawing shows the cross sectional view of the biomass gasification gas stove.    Furnace (1)    Separator (2)    Water tank (3)    Blower (4)    Gas stove (5)    Water tank cover (6)    Tube valve system (7)
NOVELTY - The botanical gasification furnace has a taper multi-tube heating furnace with a cleaning door (9) set at top of a taper multi-tube heating furnace (26). Heating holes are formed in the middle of the taper multi-tube heating furnace. An inlet tube (24) is set the bottom of a taper multi-tube heating furnace water layer (27), and joined to the outlet pipe (17) of a botanical gasification furnace water layer. An outlet tube is set at the top side of the heating furnace water layer, and joined to the inlet pipe (18) of the botanical gasification furnace water layer via a radiator.    USE - Botanical gasification furnace for converting organic plant into combustible gas.    ADVANTAGE - Provides furnace with energy saving, reduce emission, environmental protection, and long service life, thus ensuring safety and reliability.    DESCRIPTION OF DRAWING(S) - The drawing shows the cross sectional view of the botanical gasification furnace.    Cleaning door (9)    Outlet pipe (17)    Inlet pipe (18)    Inlet tube (24)    Taper multi-tube heating furnace (26)    Taper multi-tube heating furnace water layer (27)
NOVELTY - Treatment system (S1) comprises several of zero-valent metal particles, a weak acid, and an organic hydrogen donating solvent.    USE - For treating contaminated natural media or an ex-situ structure for the remediation of poly chlorinated biphenyls (PCBs) (claimed), chlorinated pesticides and other halogenated compounds found in natural media including groundwater, surface water, sediment and soil, and painted structures, or within the binding or caulking material on ex-situ structures.    ADVANTAGE - The treatment system does not require the addition of noble metal coating to the metal particles; does not negatively alter the natural media, allowing the contaminant to be treated in situ without costly dredging, thus decreases the impact of cleanup; and does not provides hazardous by-products, which eliminates long-term environmental liabilities, minimizes the potential of leaching or spreading hazardous waste into the environment, and eliminates costly hazardous waste disposal costs.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for treating (M1) a contaminated natural media or an ex-situ structure involving applying the treatment system (S1) to the contaminated natural media or to the ex situ structure.
NOVELTY - Neutralizing or reducing carbon dioxide emissions due to human activities related to the combustion or use of carbon containing fuels comprises capturing carbon dioxide and chemically recycling it to form carbon containing compounds or products which can be combusted or used without increasing the carbon dioxide content of the atmosphere.    USE - For neutralizing or reducing carbon dioxide emissions due to human activities related to the combustion or use of carbon containing fuels (claimed) e.g. dimethyl ether used as substitute for diesel fuel, natural gas or LPG for heating purposes for households or industrial use (claimed); used as convenient energy storage and transportation materials, fuels (including for internal combustion or fuel cells), household and industrial gases (for heating, cooking) as well as renewable raw materials for producing synthetic hydrocarbons and their products.    ADVANTAGE - The method achieves mitigation of the harmful generation of carbon dioxide that adds to the carbon footprint of human activities through the initial capture of the equivalent. By mitigating the harmful excessive carbon footprint of human activities, no excessive carbon dioxide is released into the atmosphere allowing the continued environmentally friendly renewable use of carbon containing fuels and materials while also diminishing or neutralizing the harmful environmental effect of excessive carbon dioxide discharge into the atmosphere causing global warming.
NOVELTY - Processing biogas, comprises compressing the biogas and separating the carbon dioxide from the biogas, so that biomethane remains with a high methane portion, where the biomethane and/or carbon dioxide are expanded to ambient pressure and thus mechanical output is obtained.    USE - The method is useful for processing biogas.    ADVANTAGE - The biomethane and/or carbon dioxide are expanded thus obtaining mechanical output, which is again positively supplied into the energy balance of biogas processing. The method provides a significant cost saving in the operation of biogas treatment plants. The method also ensures the production of biomethane in an economical manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device (1) for the processing of gases, preferably of biogas, comprising compressor (4) and a gas processing device (7), in which carbon dioxide is separated from the biogas and biomethane remains with a high methane portion, additionally at least one expansion device (11) for obtaining mechanical output from the expansion of at least one gas.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of a device for biogas treatment.    Biogas processing device (1)    Compressor (4)    Motor (5)    Gas processing device (7)    Expansion device (11)
NOVELTY - Method for introducing target auxotrophy gene into yeast cell, involves transforming yeast cell with an expression cassette for gene expression, deleting target auxotrophy-controlling gene from yeast cell, introducing the expressed gene into yeast cell and removing yeast selection marker from the transformed yeast cell, where cassette for yeast selection marker and fragment contains two homologous recombined fragments which are homologous to regions located on both sides of a target auxotrophy-controlling gene in a predetermined array.    USE - The method is useful for introducing target auxotrophy gene into yeast cell for producing ethanol (all claimed) which is used as fuel and for producing various chemical substances. The yeast includes sake yeast, wine yeast, beer yeast or bread yeast.    ADVANTAGE - The cellulolytic yeast has excellent alcoholic-fermentation capability, alcoholic tolerance, acid resistance and high heat resistance. The auxotrophic genes can be introduced simultaneously into yeast cell by simple process. The ethanol improves energy conversion efficiency and is easy to transport.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) vector for introducing target auxotrophy gene into yeast cell by the above described process; and    (2) cellulolytic yeast, capable of expressing the enzyme which cleaves ( beta ) 1,4-glycosidic linkage.
NOVELTY - A reaction zone(s) is provided and maintained at sufficient time, temperature, pressure and wave length of UV-light. An ozone and atomic oxygen are synthesized from oxygen in a reaction zone by subjecting humidified air to UV-light. A hydroxide is synthesized by subjecting ozone and water to UV-light to obtain a mixture containing atomic oxygen and hydroxide. The plant material is impregnated with the obtained mixture. Thus the production of hydrolyzed plant material is carried out.    USE - Production of hydrolyzed plant material e.g. lignocellulosic material is used in fermentation process of biomass fuel, ethanol and biogas, and production of animal and human food (all claimed).    ADVANTAGE - The method economically provides hydrolyzed plant material without hazardous material, and environmental friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of degraded plant material by frost burst(s).
NOVELTY - An acidulated oil is refined by contacting oil to ultra-filtration membrane at 30-70 (preferably 40-60) degrees C under 0.2-0.5 MPa, pressurizing to refine saponifiable material, and intercepting non-saponifiable material with diameter at greater than 1 mu m. The ultra-filtration membrane is organic ultra-filtration membrane.    USE - Method of refining acidulated oil (claimed) for producing biological diesel fuel.    ADVANTAGE - The method improves quality of oil, where content of saponifiable material is improved to more than 95 wt.%, and moisture content is reduced to 1.5 wt.%; and has simple operation, low production cost, and no pollution.
NOVELTY - The method involves sending a part of biogas to the biogas generator to generate the electricity and complement with the wind-electricity to provide the daily electricity for the farmer and sending other part of biogas to the residents for providing gas used in daily life for farmer, after the biogas generated by the biogas generator is processed by the water condenser and biogas purification regulator. The biogas generated by the biogas generator is processed by the water condenser and biogas purification regulator, and sent to the home of the farmer for providing the gas used in daily life.    USE - Method for integrated wind-biogas-electricity power generation and air supply by wind-electricity.    ADVANTAGE - Improves and stabilizes the reaction temperature of biogas reactor, so as to keep the stability of produced gas, improve the biogas output, clean the conversion efficiency of biomass, realize various and scaled utilization of biogas, save the energy and reduce the consumption. Realizes harmless treatment of waste and reduces the waste, making the method environment-friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram illustrating the method for integrated wind-biogas-electricity power generation and air supply by wind-electricity. (Drawing also includes non-English language text).
NOVELTY - Movable dual-drum fuel forming machine through curing of straws comprises matching set of crushing machine and extruder having shell, provided with pair of material extruding opposite rollers placed in sequence and provided with extruding through holes.    USE - Movable dual-drum fuel forming machine through curing of straws.    ADVANTAGE - The machine has longer service life and good forming effect; and can be optionally moved to adapt to the extrusion forming of various biomasses.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the movable dual-drum fuel forming machine through curing of straws.
NOVELTY - A compound liquid agent comprises carrier, nucleic acid and organic acid.    USE - A compound liquid agent used in biotreating unit for sewage control and treatment, e.g. by active sludge method (claimed).    ADVANTAGE - The product is convenient to use, has high and quick biotreatment strengthening ability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of preparing compound liquid agent by mixing aqueous solution of nucleic acid with organic acid solution of carrier, and storing at 0-4 degrees C.
NOVELTY - A clean high-grade industrial fuel in a solvent type and low temperature state is prepared by mixing petroleum ether, ethanol and methanol as solvents according to a certain proportion; and carrying out functionalization to the organic solvents.    USE - Method for preparing a clean high-grade industrial fuel in a solvent type and low temperature state (claimed).    ADVANTAGE - The method reduces the cost of fuel and tail gas. After burning, the prepared industrial fuel has no carbon, thus making it almost clean. Temperature and heat of the prepared fuel are suitable for ironing of high-grade garment factory and tea furnace of large or medium enterprises.
NOVELTY - An organic fertilizer is prepared from poultry manure by mixing and uniformly agitating (mass%) wood powder (40-50), rice bran (40-50), glucose (3-8) and microbial fermenter (3-8), adding equal amount of water to ferment the mixture, adding the fermenting substance into the poultry manure at ratio of 1:10, uniformly agitating, fermenting the poultry manure, granulating and drying the poultry manure after fermenting.    USE - Method for preparing organic fertilizer from poultry manure (claimed).    ADVANTAGE - The method can greatly accelerate fermentation speed of poultry manure, improve nitrogen content after the poultry manure is fermented, and strengthen the effect of organic fertilizer.
NOVELTY - A low temperature clean industrial fuel is prepared by mixing pine-stump light oil with methanol, ethanol and petroleum ether.    USE - Method of preparing a low temperature clean industrial fuel (claimed) for use in ironing cloth, or tea furnace of large or medium-sized enterprise.    ADVANTAGE - The method reduces cost of industrial clean fuel oil, and reduces exhaust gas pollution.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a method of low temperature clean industrial fuel prepared by pine-stump light oil.    Close blending pot (1)    Fuel oil tank (2)    Pine-stump light oil (3)    Methanol, ethanol and petroleum ether (4)
NOVELTY - A clean high-grade industrial fuel in solvent type and medium temperature state is prepared by mixing petroleum ether, ethanol and methanol, and reacting obtained mixture.    USE - Method of preparing a clean high-grade industrial fuel in solvent type and medium temperature state (claimed) for use in cleaning sintered high-grade ceramic or handicraft article, or cleaning painting of high-grade car.    ADVANTAGE - The method reduces fuel cost, produces a carbon-free exhaust gas, and does not produce dust.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a method of preparing a clean high-grade industrial fuel in solvent type and medium temperature state.    Sealed mixer (1)    Centrifuge (2)    Fuel storage tank (4)    Methanol (5)    Flash reducing agent and alcohol-soluble lubricant (6)
NOVELTY - A carbon monoxide (CO) integral catalyst comprises ruthenium (Ru) (0.1-2 wt.%) as active component, auxiliary agent including alkali metal oxide and/or alkali earth metal oxide, and alumina gel coated cordierite carrier, where content of alumina gel is 2-10 wt.% of the catalyst. The mol ratio of Ru and alkali metal oxide and/or metal element in alkali metal oxide is 1-20:1.    USE - Carbon monoxide integral catalyst for selective oxidation hydrogen-rich reformed gas (claimed) used as fuel in fuel cell.    ADVANTAGE - The catalyst has high activity, high selectivity, low noble metal content, low ignition temperature, wide temperature range, and convenient application in fuel cell system; and can deeply eliminate CO in reformed gas, thus providing clean fuel to fuel cell.
NOVELTY - The catcher has an upper tank body (1) connected to a coal gas inlet (4), and a lower tank body (5) connected to a coal gas outlet (8). Equilateral hexagonal electrode tubes are exposed between the upper tank body and lower tank body, and electrode wires (3) are located at centre part of each electrode tube. Ends of the electrode wires are fixed on metal plates (10) in the tank bodies. The metal plates are electrically connected with electrodes (2), and two output electrodes of a high-voltage direct current power supply (9) are respectively connected to the electrodes and the electrode tubes.    USE - Coal gas tar catcher.    ADVANTAGE - The electrode tubes are arranged in equilateral hexagonal honeycomb shape, and any side except the external side of the electrode tubes is shared by two electrode tubes to save the materials and effectively increase the circulation area of the coal gas, thus improving the treatment capacity of the coal gas. The external electrode tube is directly exposed in the air so as to cool the coal gas while collecting the tar.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a coal gas tar catcher.    Upper tank body (1)    Electrodes (2)    Electrode wires (3)    Coal gas inlet (4)    Lower tank body (5)    Coal gas outlet (8)    High-voltage direct current power supply (9)    Metal plates (10)
NOVELTY - The fluid separation fluoropolymer coated membrane, comprises a thin coating of a fluoropolymer on a porous asymmetric membrane layer. The porous asymmetric membrane layer comprises a mixture of polymer and a type of molecular sieve.    USE - The fluoropolymer coated membrane is useful: for separating a liquid or gas from mixtures of liquids or gases such as nitrogen and oxygen, carbon dioxide and methane, carbon dioxide and nitrogen, hydrogen and methane or carbon monoxide, helium and methane, ethylacetate and ethanol, diethylether and ethanol, acetic acid and ethanol, benzene and ethanol, chloroform and ethanol, chloroform and methanol, acetone and isopropylether, allylalcohol and allylether, allylalcohol and cyclohexane, butanol and butylacetate, butanol and 1-butylether, ethanol and ethylbutylether, propylacetate and propanol, isopropylether and isopropanol, methanol and ethanol and isopropanol, and ethylacetate and ethanol and acetic acid; or for desalination of water by reverse osmosis, organic/aqueous liquid separation, organic/organic separation or pervaporation (all claimed) in chemical, petrochemical, pharmaceutical and allied industries.    ADVANTAGE - The fluoropolymer coated membrane has low capital cost, high gas selectivity and permeability, improved performance durability, high thermal, mechanical, chemical and electrical stability and high resistance to hydrocarbon contaminants, solvent swelling and carbon dioxide plasticization, and achieves efficient, rapid, economical and desired separation of the liquid/gas from its mixtures.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a method for making the fluid separation fluoropolymer coated membrane; and    (2) a process for separating a liquid or gas from mixtures of liquids or gases using the fluoropolymer coated membranes.
NOVELTY - Biodiesel production involves obtaining intermediate product by using raw material made of vegetable oil, animal fat or their mixture. The obtained intermediate product is processed with methanol or ethanol through esterification reaction, where impurities are discharged through high speed centrifugal separation. Molecules are separated by using methyl ester and ethyl ester at 50-150 degrees C through element distillation technology.    USE - Method for producing biodiesel for internal combustion engines by using centrifugal separation.    ADVANTAGE - The biodiesel production method is simple and cost-effective, which produces the biodiesel having improved production efficiency and high purity in an eco-friendly manner.
NOVELTY - A functionalized carbohydrate material comprises saccharide units arranged in a molecular chain, where one out of every 2-250 saccharide units comprises a carboxylic acid group or its ester or salt. The number of carboxylic acid groups is determined by titration.    USE - Functionalized carbohydrate material including biomass or biomass-derived materials such as starchy materials, cellulosic materials or lignocellulosic materials in fibrous form, for use in fermentation to produce fuel including hydrogen, alcohol (e.g. ethanol or butanol), or hydrocarbon.    ADVANTAGE - The functionalized carbohydrate material is more soluble, easier to utilize by various microorganisms during fermentation or can be more stable over the long term. Further, the carbohydrate material is less prone to oxidation and can have enhanced long-term stability (e.g. to oxidation in air under ambient conditions).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of preparing a functionalized carbohydrate, comprising treating a base material comprising a carbohydrate containing saccharide units, with accelerated particles in an oxidizing environment to prepare a functionalized carbohydrate in which one out of every 2-250 saccharide units comprises a carboxylic acid group, and/or to prepare a functionalized carbohydrate in which one out of every 5-1500 saccharide units comprises a nitroso, nitro, or nitrile group.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of biomass being ionized, and then oxidized or quenched.
NOVELTY - A pesticide suspension contains 5-50 wt.% of 2,6-dichloro-n-(((4-chlorophenyl)amino)carbonyl)benzamide, and additives.    USE - Pesticide suspension for preventing pests.    ADVANTAGE - The pesticide suspension is safe for human body, animal, natural enemies of pests and other beneficial organisms; avoids environment pollution caused by a great amount of organic solvent; and has simple preparation and low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing pesticide comprising:    (A) completely mixing 2,6-dichloro-n-(((4-chlorophenyl)amino)carbonyl)benzamide with wetting dispersant;    (B) sequentially adding thickening agent, stabilizing agent, antifoaming agent, penetration enhancer, anti-freezing agent and deionized water in the mixture while uniformly stirring; and    (C) processing mixed materials in a ball mill for 2-5 hours until particle size of the 2,6-dichloro-n-(((4-chlorophenyl)amino)carbonyl)benzamide is less than 4 mu m.
NOVELTY - A fomesafen micro-emulsion comprises fomesafen (1-20%), surfactant (5-25%), cosolvent (5-15%), stabilizer (0.01-5%), synergistic agent (0.5-5%), penetrating agent (0.1-5%), and water (to 100%).    USE - A fomesafen micro-emulsion, i.e. an agricultural weedicide.    ADVANTAGE - The fomesafen micro-emulsion has low toxicity, is pollution-free dose which is safe to humans and animals, is hard to generate weed drug fastness, and has high raw material utilization rate, simple process, and low production cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of preparing the fomesafen micro-emulsion, comprising uniformly stirring the fomesafen as a raw material with the cosolvent; adding the surfactant, the stabilizer, the synergistic agent, the antifreeze agent and the penetrating agent by proportion; mixing them uniformly; adding deionized water; stirring them uniformly; and standing and obtaining the micro-emulsion.
NOVELTY - A pesticide composition, i.e. water dispersible granules, comprises (wt.%) chlorantraniliprole (1-45), active ingredient B (5-40), auxiliary agents (1-20), and a filler (balance); or, i.e. a suspending agent, comprises (wt.%) chlorantraniliprole (1-40), active ingredient B (5-50), auxiliary agents (2-30), and water (balance). The active ingredient B is buprofezin and/or nitenpyram.    USE - A pesticide composition for preventing pests in crops (claimed).    ADVANTAGE - The pesticide composition can prevent pests effectively in one dosage; utilizes components having remarkable synergy between each other; has strong contact and stomach function and systemic action with high activity to the pests, and quick and long effects; can inhibit and defer the generation of resistance of the pests to single reagent; and can reduce the pollution to environment, which protects the ecological environment and human health.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of preparing the pesticide composition, comprising (A) mixing naphthalenesulfonic, a raw drug of the active ingredient B, the auxiliary agents and the filling material uniformly, crushing them until the fineness is more than 800 meshes, pelleting through a wet method or ebullition, drying the pelletized products in a drying oven, sieving the dried products with a vibration sieve, and extracting the granules with a fineness of 10-60 meshes as the finished products, thus obtaining the pesticide composition which is water dispersible granules; or (B) adding a raw drug of the chlorantraniliprole, the auxiliary agents, the active ingredient B and the ionized water in a sand cylinder and stirring them uniformly, then adding sand grinding media glass beads after the high-speed stirring and pre-dispersing for 30 minutes, grinding for 2 hours and then removing the glass beads, and keeping all grain diameters under 5 mu m, thus obtaining the pesticide composition which is a suspending agent.
NOVELTY - Solid biomass fuel is prepared by transforming biomass raw materials comprising forestry residue and crop straws including maize and wheat into feeding shed, crushing into thin and short fibers, sending into material cabin while further crushing raw materials needing secondary crushing, storing temporarily in material cabin, adjusting and mixing powdered materials in cabin or adding water to adjust moisture content and removing dust, sending continuously to solid forming machine, extruding into shapes without additives and having lignin as binder, cutting, cooling, weighing and packing.    USE - Method for producing solid biomass fuel including blocky and granular fuels (claimed).    ADVANTAGE - The method provides continuous and stable industrial production of solid fuel, and solves problem on large energy consumption and low production efficiency, thus solving rural energy problem and improving rural environment.    DETAILED DESCRIPTION - Solid biomass fuel is prepared by:    (A) transforming biomass raw materials comprising forestry residue and crop straws including maize and wheat into feeding shed and stacking along direction of feeding conveyor belt;    (B) crushing into thin and short fibers, sending into material cabin while further crushing raw materials needing secondary crushing to grain size of smaller than 5 mm and storing temporarily in material cabin with lifter and shoveling plates to stir and mix;    (C) adjusting and mixing powdered materials in cabin or adding water to adjust moisture content and removing dust, and sending continuously to solid forming machine;    (D) extruding into shapes without additives and having lignin as binder, cutting and cooling formed high-temperature solid fuel discharged at 75-85 degrees C; and    (E) weighing and packing.
NOVELTY - Post-treatment of high temperature and high flow rate mixture of gas and solid from plasma coal cracking process comprises separating product from the plasma coal cracking process by the rapid gas-solid separation structure, which forms semi-finished gas product and semi-finished solid product; cooling the semi-finished gas product using quenching medium which forms pyrolysis gas; reacting the solid product with pure water and steam, or filling the reactor with hydrogen to form methane; and using generated heat for providing part of electricity for the plasma generator.    USE - Method for post-treatment of high temperature and high flow rate mixture of gas and solid from plasma coal cracking process (claimed).    ADVANTAGE - The method increases acetylene content in the pyrolysis gas, total conversion rate of coal and comprehensive value of the process.    DETAILED DESCRIPTION - Post-treatment of high temperature and high flow rate mixture of gas and solid in plasma coal cracking process comprises:    (A) separating product at 1200-1500 K and 150-200 m/s from the plasma coal cracking process by the rapid gas-solid separation structure, which forms semi-finished gas product and semi-finished solid product;    (B) cooling the semi-finished gas product using quenching medium at room temperature, which forms pyrolysis gas containing ethyne, methane, carbon monoxide, hydrogen, and carbon dioxide;    (C) sending the semi-finished solid product which is coal powder and has 1100-1400 K to a reactor, reacting it with pure water and steam to form carbon monoxide and hydrogen, or filling the reactor with hydrogen to form methane; and    (D) using heat generated by the reaction of the semi-finished solid product for providing part of electricity for the plasma generator.
NOVELTY - Binder additive has glycerin from processes of production of biodiesel, from renewable energy sources, derived from vegetable oils such as sunflower, rapeseed, soybeans and other oilseeds or animal fats and produced through chemical process. The binder additive also has monoalkyl fatty acid long chain.    USE - Binder additive for use in process of pelletizing iron ore.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for obtaining pellets of iron ore.
NOVELTY - Low temperature resistant alcohol clean fuel oil comprises (in weight%): ethanol (10-30), 4-12C petrol component oil (65-86), glycerol and/or 1,3-dioxolane-4-methanol (0.01-5).    USE - Low temperature resistant alcohol clean fuel oil.    ADVANTAGE - The alcohol clean fuel oil has excellent low temperature resistance and can be used at a temperature of -20 degrees C. The low temperature resistant alcohol clean fuel oil can be produced cost-effectively by a simple process. The intersolubility of the alcohol and oil is excellent.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing the low temperature resistant alcohol clean fuel oil, which involves adding petrol component oil, ethanol and glycerol and/or 1,3-dioxolane-4-methanol to the reaction kettle at room temperature according to the ratio, and then agitating uniformly.
NOVELTY - Biodiesel comprises (in weight%): biodiesel (70-95) and 18-54C fatty acid alkylester (5-30) having one or more carboxy groups.    USE - As biodiesel.    ADVANTAGE - The biodiesel has enhanced pour point and filter plugging point without reduction of ester value.
NOVELTY - A refrigerant mixture composition comprises (in weight%) propane (20-30), propylene (35-45) and trifluoromethyl iodide (20-30) as hydrocarbon-based coolant gas, and difluoromethane (5-10) as hydrofluorocarbon-based refrigerant gas.    USE - The mixture composition is used for refrigerator.    ADVANTAGE - A refrigerant mixture composition minimize design change of refrigerator system using freon-based refrigerant. The refrigerator system has excellent volume refrigerating capacity, performance coefficient, and good steam pressure property.
NOVELTY - A hydrogen-production apparatus (1) comprises reaction liquid supply part (5) and reaction supply unit which supply reaction liquid to cartridge which accommodates hydrogen-producing agent in container.    USE - Hydrogen production apparatus for fuel cell apparatus (claimed) used for domestic electrical appliance, personal computer and portable electronic device.    ADVANTAGE - The apparatus can safely and efficiently remove hydrogen gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a hydrogen production process.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the hydrogen production apparatus.    Hydrogen-production apparatus (1)    Reaction liquid supply part (5)    Reaction liquid accommodating part (6)    Reaction liquid supply structure (7)    Reaction liquid feed route (8)
NOVELTY - The apparatus has electrodes that are spaced apart by a distance of 0.125-0.2 inch in an electrolyte chamber. The electrodes are supplied with voltage in response to adjustment of engine throttle according to spark plug signal of engine. Amount of hydrogen and oxygen produced is controlled to prevent stoichiometric excess associated with amount of fuel and gas combination required by engine. Fresh air is supplied to the electrolytic chamber to dislodge hydrogen and oxygen clinging to electrodes.    USE - Hydrogen generator apparatus for internal combustion engine of vehicle. Can also be used in engine of marine vessel and stationary engine.    ADVANTAGE - The structure enables reduction in fuel consumption, resulting in doubling of vehicle's fuel mileage. Hazardous situation due to over production of hydrogen and oxygen can be avoided reliably. Hydrogen generator apparatus of compact structure which is easy to install and assemble, can be obtained.    DESCRIPTION OF DRAWING(S) - The drawing shows the perspective view of the hydrogen generator assembly without chamber.
NOVELTY - The electrolytic cell (100) has an assembling type insulation member for maintaining the interval of the electrode plates; a gas sump tank (160) on which the emitted hydrogen oxygen mixed gas accumulates; and insulation boards (170a,170b) for insulating electrolytic cell, arranged between the joint contact parts (111b, 121a,121b) of the left and right paired plate-shaped electrolytic cell covers (110a,110b) and electrolytic cell main body (120).    USE - Electrolytic cell for hydrogen oxygen mixed gas generator used as heat source. Uses include but are not limited to hydrogen oxygen mixed gas warm air furnace, a hydrogen oxygen mixing gas boiler, hydrogen oxygen mixed gas carbonization apparatus, and an incinerator.    ADVANTAGE - The electrolytic cell can generate hydrogen oxygen mixed gas efficiently. Decreases electric power loss by insulating two places, the electrolytic cell cover of an anode side, and the electrolytic cell cover at the side of a cathode. Stability of each electrode plate in electrolysis room interior is securable. The pressure of electrolysis room interior can be distributed by providing the cylindrical gas sump tank on which the emitted hydrogen oxygen mixed gas accumulates.    DESCRIPTION OF DRAWING(S) - The drawing shows the assembly perspective view of the electrolytic cell of the hydrogen oxygen mixed gas generator.    Electrolytic cell (100)    Left and right paired plate-shaped electrolytic cell covers (110a,110b)    Joint contact parts (111b, 121a,121b)    Electrolytic cell main body (120)    Gas sump tank (160)    Insulation boards (170a,170b)
NOVELTY - A fuel reformer comprises reaction container (21) where nitridation hydrogen type gas fuel containing ammonia and hydrazine is supplied, and microwave exposure part (22) which irradiates and heats microwave to modification catalyst (23) containing transition metal and its oxide. The modification catalyst and nitridation hydrogen type gas fuel contact while accommodating modification catalyst. The fuel reformer decomposes nitridation hydrogen type gas fuel according to catalytic reaction, and produces hydrogen and nitrogen.    USE - A fuel reformer e.g. optimal fuel reformer for modifying fuel used for fuel cell system (claimed). Can also be used for manufacturing hydrogen.    ADVANTAGE - The fuel reformer can be efficiently modified by relatively low temperature even if ammonia cannot absorb microwave easily.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the fuel reformer.    Fuel supply part (10)    Reaction container (21)    Microwave exposure part (22)    Modification catalyst (23)    Cavity resonator (30)
NOVELTY - A water evaporation unit (7) has a cylinder (9) and a spiral pipe (8) connected to the cylinder. The supply units (5,6) supply source gas and water respectively to the spiral pipe. A modification catalyst layer (10) having modification catalyst generates reformed gas by performing modification reaction with respect to mixed gas obtained by mixing source gas and water vapor. A denaturation catalyst layer (11) arranged in the outer side of water evaporation unit reduces the carbon monoxide in the reformed gas by shift reaction.    USE - Hydrogen producing apparatus mounted in fuel cell power generating device (claimed) for supplying gas containing hydrogen to fuel cell system used for domestic application.    ADVANTAGE - Since the water evaporation unit and flow path of source gas can be formed, the water and source gas can be reliably guided to the water evaporation unit and evaporation of water can be enabled, while simultaneously stimulating the mixing of water vapor and source gas. The change in catalyst temperature by heat exchange with the catalyst in unexpected location can be prevented and stable operation can be achieved without restricting the flow within water evaporation unit.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the hydrogen producing apparatus. (Drawing includes non-English language text)    Source gas supply unit (5)    Water supply unit (6)    Water evaporation unit (7)    Spiral pipe (8)    Cylinder (9)    Modification catalyst layer (10)    Denaturation catalyst layer (11)
NOVELTY - A semiconductor oxide film (2) contains semiconducting oxide which absorbs light and produces an electron and a hole. The semiconducting oxide is tungsten containing ferric oxide. The atomic ratio of iron with respect to tungsten is 0.02-0.08.    USE - Semiconductor oxide film is used as photocatalyst film for hydrogen-producing apparatus (claimed).    ADVANTAGE - The semiconductor oxide film has excellent photoelectric conversion efficiency.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of semiconductor oxide film, which involves forming a film by sputtering ( alpha )-ferric oxide and tungsten oxide as a target material and heat-processing the film at 550-600 degrees C; and    (2) hydrogen-producing apparatus (1), which has semiconductor oxide film, a transparent conductive film (3), a transparent substrate (4) and a solar cell provided from the light-receiving surface side, and an electroconductive component which electrically connects transparent conductive film and solar cell, and penetrates to the transparent substrate along the thickness direction.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of the hydrogen-producing apparatus.    Hydrogen-producing apparatus (1)    Semiconductor oxide film (2)    Transparent conductive film (3)    Transparent substrate (4)    Electrolytic aqueous solution (8)
NOVELTY - The apparatus has an annular shift reaction section whose one end is connected to downstream of a modification-reaction section (2), while providing a preliminary modification section in the upstream of the modification-reaction section. A source gas inflow tube (6) is connected to upstream of the preliminary modification section, and the downstream of shift reaction section is connected to a reformed-gas discharge pipe (25) through a carbon monoxide selective oxidation section.    USE - External heating-type hydrogen production apparatus for fuel cell electric power generation system (claimed).    ADVANTAGE - Since the preliminary modification section is provided in the upstream of modification-reaction section, a portion of catalyst can be modified efficiency while improving the performance and reducing the reaction burden and size of the modification-reaction section.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell electric power generation system.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of external heating-type hydrogen production apparatus.    Modification-reaction section (2)    Outer cylinder (3)    Source gas inflow chamber (5)    Source gas inflow tube (6)    Reformed-gas discharge pipe (25)
NOVELTY - The electrolyzer (10) has an electrolytic cell (12) that includes an anode (22) and a cathode (24). The cathode has a brush-shaped electrolyte unit with several electroconductive wires (64) positioned opposing the anode surface at predetermined intervals. The tip portions and the peripheral surface of the electroconductive wires function as electrode surface, when electrolysis is carried out in the presence of an electrolytic solution.    USE - Electrolyzer for combustion simulation system for internal combustion engine (both claimed) e.g. diesel engine.    ADVANTAGE - Since the peripheral surface along with the tip portion of the electroconductive wires function as electrode surface, the efficiency of generated hydrogen can be increased greatly. By mixing hydroxyacetic acid and citric acid with respect to the electrolyzed water, the electroconductive wires can be maintained in clean state irrespective of long working hours of the electrolyzer, improving the efficiency of the gas generated. Since the standard fuel is combusted completely, the generation of hazardous ingredients is suppressed.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial cross-sectional view of the electrolyzer.    Electrolyzer (10)    Electrolytic cell (12)    Anode (22)    Cathode (24)    Electroconductive wires (64)
NOVELTY - The hydrogen production system comprises a system for regeneration of oxide material consumed by the production of hydrogen, and a unit for removing hydrogen product and introducing in the regeneration system. The oxide material comprises two forms of different valence oxides, and is mesophorous with a porosity of 2-50 nm. The surface of the oxide material is covered of nanoparticles of noble metal such as rhodium. The couple of oxides are doped with low valence cations. The oxide material has a specific surface of higher than 50 m2/g.    USE - The system for the production of hydrogen is useful in an on-board device such as vehicle propulsion system, and as an energy source for fuel cell.    ADVANTAGE - The system is capable of easily, economically and energy efficiently producing the hydrogen in large scale.    DETAILED DESCRIPTION - The hydrogen production system comprises a system for regeneration of oxide material consumed by the production of hydrogen, and a unit for removing hydrogen product and introducing in the regeneration system. The oxide material comprises two forms of different valence oxides, and is mesophorous with a porosity of 2-50 nm. The surface of the oxide material is covered of nanoparticles of noble metal such as rhodium. The couple of oxides are doped with low valence cations. The oxide material has a specific surface of higher than 50 m2/g. The regeneration system is a heat exchanger, and has a pressure of lower than 0.01 mbar.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a hydrogen production system (Drawing includes non-English language text).
NOVELTY - The gasification plant (1) has fluid path extending between a tank (3a) containing liquid methane and gas holder (4a) of storage station (4). A gasification unit (6) is arranged along the fluid path. The gasification unit has Stirling engine (9) with respective cold cylinder (16) and hot cylinder (21). The heat exchanger (37) arranged along the fluid path, is in heat exchange relationship with cold cylinder, to maintain the cold cylinder at a temperature much lower than the ambient temperature, with recovery and transformation of latent heat into mechanical energy.    USE - Gasification plant e.g. gasifier for gasification of methane from liquid state to gas state.    ADVANTAGE - The gasifier of unusually compact size, with impeccable ecological behavior, and improved energy balance, can be provided.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for transforming latent heat of combustible gas in liquid state in general and of liquid methane in particular into useful mechanical energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the gasifier.    Gasification plant (1)    Tank containing liquid methane (3a)    Storage station (4)    Gas holder (4a)    Gasification unit (6)    Stirling engine (9)    Cold cylinder (16)    Hot cylinder (21)    Heat exchanger (37)
NOVELTY - An Agrobacterium strain LAD9 with heterotrophic nitrification-aerobic denitrification performance, for the strain LAD9, where 16S rRNA gene has nucleotide sequence expressed by sequence comprising 1418 bp (SEQ ID NO. not defined) and where the accession number in Genbank is FJ63330 and preservation number is CGMCC No.2962, is new.    USE - The strain is useful for treating nitrogen-containing waste water, where the Agrobacterium sp. strain LAD9 is added in the nitrogen-containing waste water; the nitrogen in the waste water is removed by carrying out aeration and maintaining dissolved oxygen at 2-6 mg/L (claimed).    ADVANTAGE - The invention has high denitrifying effect, convenient operation; compared with the traditional biological denitrifying process, it has big economic benefit.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a microorganism microbial inoculum prepared by taking the Agrobacterium strain LAD9 as active component.
NOVELTY - The system has a septic tank containing a source of anaerobic or fermentation activity e.g. fermentation chamber, for producing air/methane gas mixture. An irrigation disposal line leads to a sub surface irrigation dispersal system positioned in the soil in sub surface disposal area. An air/methane gas supply line (66) draws the air/methane gas from the tank, and injects the gas into the disposal line for passing the gas into the soil via the dispersal system. The area comprises crops or vegetation irrigated by sub surface drip lines (72) and irrigation emitters (76).    USE - System for disposing methane gas from a septic tank and an anaerobic digestion system to waste water drainage field or leach field.    ADVANTAGE - The system rapidly removes septic gas including hydrogen sulfide, from a septic tank, thus avoiding the environmental problems of venting the gas into the atmosphere, and preventing deterioration of the tank and damage of cover plates of the tank.    DETAILED DESCRIPTION - The source of anaerobic or fermentation activity comprises animal waste lagoon, landfill or sewage treatment plant. An INDEPENDENT CLAIM is also included for a method for disposing methane gas from a septic tank.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a methane gas disposing system illustrating drawing of waste-water effluent and air/methane gas from a septic tank and dispersing the gas in the soil by pressure-dosing via a subsurface irrigation dispersal system.    Venturi-type differential pressure injector (60)    Air/methane gas supply line (66)    Suction inlet (68)    Subsurface drip line (72)    Irrigation emitter (76)
NOVELTY - Electricity is generated by mixing and combusting marsh gas generated from sludge with garbage in marsh gas tank, where the mixture ratio of marsh gas to garbage is 50-500 m3 marsh gas/ton garbage, and combustion temperature in combustion furnace is 850-1300 degrees C; dehydrating; and drying the generated biogas residue and mixing with ash slag to produce brick and ceramic to change wastes into resource.    USE - Method for generating electricity.    ADVANTAGE - The marsh gas is fully combusted, and the combusted product meets the discharge standards. The biogas residue and the ash slag are comprehensively utilized. The two wastes are converted into resources.    DETAILED DESCRIPTION - The combustion temperature in the combustion furnace is 900-1200 degrees C. The method uses an energy conversion system, a flue gas purifying system, and a resource comprehensive utilization system. The marsh gas and the domestic garbage are sent to the combustion furnace to be combusted, the and generated heat is converted into electricity by the energy conversion system. The generated harmful flue gas is sent to a purifying device to be absorbed, and the dried biogas residue and the generated ash slag are comprehensively used in the resource comprehensive utilization system after being collected.    DESCRIPTION OF DRAWING(S) - The drawing is a block diagram of a method for generating electricity (Drawing includes non-English language text).
NOVELTY - A two-step fermenting biogas tank comprises a one-step fermenting tank, a two-step fermenting tank, a feed pipe and a discharge pipe, where the one-step fermenting tank and the two-step fermenting tank are connected by the feed pipe; a filter grate is provided at the opening of the feed pipe in the one-step fermenting tank; the discharge pipe is connected with the two-step fermenting tank by the one-step fermenting tank; a single-way valve is provided at the part of discharge pipe extending into the one-step fermenting tank.    USE - The two-step fermenting biogas tank is useful for households in the rural area.    ADVANTAGE - The biogas tank has scientific design and low cost; after starting up by adding dairy manure once, it can normally run only by adding straws.
NOVELTY - Fertilizer is prepared by taking (wt.%) soybean cake (5-10), dry human excrement (10-15), chicken manure (20-23), wood ash (8-11), composite fertilizer (10-15), potassium chloride (3-7), urea (14-22), calcium-magnesia phosphate fertilizer (5-8), potassium sulfate (3-5), heavy calcium (1-2) and paclobutrazol (1-2) as ingredients.    USE - Method of preparing fertilizer used for yielding peanuts (claimed).
NOVELTY - Preparing biosorbent for processing phthalocyanine dye wastewater comprises: (a) adding sterile water to the activated Aspergillus niger and obtaining Aspergillus niger mycelium pellet; (b) sterilizing the Aspergillus niger mycelium pellet, filtering it, and obtaining the deactivated Aspergillus niger mycelium pellet; (c) drying, crushing, and obtaining Aspergillus niger killed germ powder; and (d) moving 2.00 g of Aspergillus niger killed germ powder to the conic bottle filled with hydrochloric acid, and drying and crushing.    USE - The process is useful for preparing biosorbent for processing phthalocyanine dye wastewater (claimed).    DETAILED DESCRIPTION - Preparing biosorbent for processing phthalocyanine dye wastewater comprises: (a) adding sterile water to the activated Aspergillus niger, scrabing the spore, filtering it, pouring the obtained lysate to a conic bottle filled with the sterile water and glass balls, shaking it until it is dispersed monospore through the microscopical study, counting it, adjusting the concentration of the spore suspension by using the sterile water, inoculating it to the sterilized liquid culture medium, culturing it, and obtaining Aspergillus niger mycelium pellet; (b) sterilizing the Aspergillus niger mycelium pellet, filtering it, and obtaining the deactivated Aspergillus niger mycelium pellet; (c) drying it to the balanced weight, crushing it, and obtaining Aspergillus niger killed germ powder; and (d) moving 2.00 g of Aspergillus niger killed germ powder to the conic bottle filled with hydrochloric acid (HCl), separating the solid and liquid of the shaked mixture, cleaning the modified adsorbent by using the deionized water until the pH value of the cleaning solution is neutral; drying it to the balanced weight, crushing it, and obtaining the biosorbent for processing phthalocyanine dye wastewater.
NOVELTY - The self-control voltage regulation type tank includes an electrification contact point pressure gauge (16), a hydrogen-conveying valve (18), and a fast connector (19) which are connected with a hydrogen-conveying pipe (17). The lower end of a water injection pipe (10) is connected with a liquid storage chamber (8). The upper end of the water injection pipe is connected with a three-way valve (11). The side end of the three-way valve is connected with a water-adding pipe (14). The upper end of the three-way valve is connected with a water injection port (13).    USE - Self-control voltage regulation type tank for producing hydrogen from brine electrolysis aluminum and delivering the hydrogen to a hydrogen-consuming device. Uses include but are not limited to transport tool, hydrogen fuel battery, or hydrogen-fired appliance.    ADVANTAGE - Enables safe and reliable production of hydrogen which is non-toxic, tasteless, and harmless. Enables production of clean and green secondary energy. Allows recycling of aluminum and addition agent.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of self-control voltage regulation type tank.    Liquid storage chamber (8)    Water injection pipe (10)    Three-way valve (11)    Water injection port (13)    Water-adding pipe (14)    Electrification contact point pressure gauge (16)    Hydrogen-conveying pipe (17)    Hydrogen-conveying valve (18)    Fast connector (19)
NOVELTY - A water jacket type composite fertilizer cooler comprises a cooling machine roller (1) having an external wall that is provided with a water jacket (2); where the water jacket is provided with a water inlet pipe (3) and a water outlet pipe (4).    USE - The water jacket type composite fertilizer cooler is useful for industrial and commercial applications.    ADVANTAGE - The water jacket type composite fertilizer cooler has high fertilizer cooling effect, reduced length of cooler, and lowered equipment cost. Moreover, it recycles hot water, saves energy, reduces discharge of hot air, and protects the environment.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the water jacket type composite fertilizer cooler.    Cooling machine roller (1)    Water jacket (2)    Water inlet pipe (3)    Water outlet pipe (4)
NOVELTY - The generator includes a sealed container fixed to the mobile device and formed with a hydrogen outlet and a water inlet. A water electrolysis device is installed at the bottom of the container, and is connected by a hydrogen output pipe to the gas inlet pipe of the internal combustion engine. A water pipe is connected to the electro-bath of the water electrolysis device to selectively add water to the water electrolysis device. The water electrolysis device includes anode and cathode that extend tot he outside of the sealed container.    USE - Hydrogen generator for feeding auxiliary fuel to e.g. internal combustion engine of mobile device.    ADVANTAGE - Simple structure. Reduces manufacturing and assembling cost. Increases energy utilization rate. Ensures reliable operation of hydrogen generator.    DESCRIPTION OF DRAWING(S) - The drawing shows the cut-isometric view of the hydrogen generator.
NOVELTY - Blend comprises: a hydrocarbonaceous composition; and a corrosion inhibitory amount of amino-alcohol compounds of formula (I) or their salts.    USE - Used as fuel and petroleum based blend.    ADVANTAGE - The amino-alcohol additives: improve the corrosion properties and microbial resistance of hydrocarbonaceous compositions (gasoline, diesel, biodiesel and diesel/biodiesel blends); inhibit the corrosion of systems in contact with the hydrocarbonaceous compositions, e.g. storage tanks, pipelines and engines; and synergistically enhance the activity of biocides in hydrocarbonaceous compositions, thus provides more effective and longer-lasting microbial control at reduced biocide concentrations.    DETAILED DESCRIPTION - Blend comprises: a hydrocarbonaceous composition; and a corrosion inhibitory amount of substituted amino-alcohol compounds of formula (R1-C(OH)(R3)-R5-C(NH2)(R4)-R2) (I) or their salts.    Either R1, R3 = H, (cyclo)alkyl, alkenyl, alkynyl or aryl; or    CR1R3 = cycloalkyl; either    R2, R4 = H, (cyclo)alkyl, cycloalkyl-alkyl or aryl, aryl-alkyl; or    CR2R4 = cycloalkyl; and    R5 = absent or 1-10C alkylene, arylene, arylene-alkylene- or -alkylene-arylene, where the alkyl, cycloalkyl, alkylene, aryl and arylene are optionally substituted with alkyl or phenyl.    Provided R2 and R4 together contain 3 or more C atoms. An INDEPENDENT CLAIM is included for a method for providing microbial resistance to a biodiesel fuel, comprising including the biodiesel fuel to (I).
NOVELTY - Identification of stimulant that increases biogenic production of methane in hydrocarbon-bearing formation, comprises obtaining a nucleic acid sequence from microorganism(s) derived from hydrocarbon-bearing formation environment; determining presence of gene product(s) of nucleic acid sequence, where gene product is an enzyme in a pathway involved in conversion of hydrocarbon to methane; and identifying a substrate, reactant or cofactor of enzyme that increases methane production when provided to microorganism(s) in hydrocarbon-bearing formation.    USE - Identification of stimulant useful for enhancing biogenic production of methane in hydrocarbon-bearing formation (claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a process for enhancing biogenic production of methane in hydrocarbon-bearing formation, comprising introducing a stimulant into hydrocarbon-bearing formation, or comprising modulating an enzyme, or comprising introducing defined microbial assemblage into a coalbed optionally together with substrate, reactant or cofactor;    (2) a method of identifying a defined microbial assemblage for conversion of coal to methane; and    (3) a defined microbial assemblage for conversion of coal to methane.
NOVELTY - A silicon carbide ceramics comprises silicon carbide particles and binding material containing silicon carbide having crystal phase different from silicon carbide particles. The silicon carbide particles contain silicon carbide having crystal phase measured based on JCPDS card number 049-1428, and have different particle size.    USE - Silicon carbide ceramics used for honeycomb structure (claimed) used as filter for collecting waste gas from internal combustion engine, boiler, chemical reaction apparatus and modifier of fuel cell.    ADVANTAGE - The silicon carbide ceramics has excellent microparticles-collecting property.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of silicon carbide ceramics, which involves mixing silicon carbide powder containing fine silicon carbide powder, coarse silicon carbide powder having average particle diameter more than fine silicon carbide powder, silicon nitride powder and carbon powder, molding the mixture to a defined shape, heat processing the molded product at 1500-1850 degrees C. The fine silicon-carbide powder has average particle diameter of less than 15 microns based on JCPDS card number 029-1127.
NOVELTY - A fuel (1,2) having non-uniform particle size is filled in fuel container (3).    USE - Method for filling fuel such as methanol and hydrogen for particulate fuel cell in fuel container used as power supply for portable electronic device (all claimed). Uses include but are not limited to polymer electrolyte fuel cell, direct methanol-type fuel cell and solid oxide fuel cell for secondary battery for notebook personal computer, digital camera and mobile telephone.    ADVANTAGE - The method improves filling rate and stabilizes the supply amount of the fuel to the container.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the filling state of the fuel.    Fuels (1,2)    Fuel container (3)
NOVELTY - Method for producing ethanol, involves obtaining organic compound and extracting ethanol from organic compound by performing ethanol fermentation under aerobic or anaerobic conditions using microorganism chosen from fungi having alcohol productivity, Zymomonas and lactic acid bacteria, obtaining fertilizer precursor component, decomposing fertilizer precursor component using microorganism under aerobic or anaerobic conditions, and extracting ethanol while obtaining organic compound from inorganic substance based on assimilation of microorganism.    USE - The method is useful for producing ethanol (claimed).    ADVANTAGE - The method uses carbon dioxide and industrial waste as raw material for the preparation of ethanol and prevents water contamination and air pollution. Hence the method is eco-friendly.
NOVELTY - Bank-filtered water denitrification involves setting biofilter (110), stirrer (150) and aerator (300) in water well (100). Hydrogen gas is supplied to settling pond (800) and dissolved, and autotrophic denitrification bacteria are cultivated. Denitrification of nitrate nitrogen is carried out in anaerobic condition and residual sludge is removed. Air or nitrogen gas is provisionally supplied to the aerator.    USE - Method for denitrifying bank-filtered water.    ADVANTAGE - The bank-filtered water denitrification method is safe as there is no danger of explosion, and enables to denitrify bank-filtered water by using hydrogen gas, which is harmless to human body.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for denitrifying bank filtered water, which includes water well, intake pump, settling pond and hydrogen gas supply apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device. (Drawing includes non-English language text).    Water well (100)    Biofilter (110)    Stirrer (150)    Aerator (300)    Settling pond (800)
NOVELTY - Bank-filtered water denitrification involves installing horizontal collector (20) at lower part of water well (10). A porous pipe (30) is set up inside the horizontal collector and connected to hydrogen gas supply pipe (40). The hydrogen gas supply pipe is connected to hydrogen gas supply apparatus (50). Hydrogen gas is supplied from hydrogen gas supply apparatus to the porous pipe through hydrogen gas supply pipe, and is dissolved in bank-filtered water of aquifer (200). Nitrate nitrogen present in bank-filtered water is denitrified by using autotrophic denitrification bacteria.    USE - Method for denitrifying bank-filtered water.    ADVANTAGE - The bank-filtered water denitrification method is cost-effective and safe as there is no danger of explosion, and enables to denitrify bank-filtered water by using hydrogen gas, which is harmless to human body.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for denitrifying bank-filtered water, which includes water well, horizontal collector, hydrogen gas supply pipe and hydrogen gas supply apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the device. (Drawing includes non-English language text).    Water well (10)    Horizontal collector (20)    Porous pipe (30)    Hydrogen gas supply pipe (40)    Hydrogen gas supply apparatus (50)    Aquifer (200)
NOVELTY - The method of remediating a subsurface contaminant plume, comprises introducing a mixed culture of Dehalococcoides strain consisting of ATCC Deposit PTA-8259 into a subsurface region contaminated with a chlorinated ethene or halogenated ethane, and maintaining anaerobic conditions in association with the Dehalococcoides strain.    USE - The method is useful for remediating a subsurface contaminant plume for converting toxic organic contaminants into nontoxic end products and for microbial based chlorinated ethene destruction.    ADVANTAGE - The method achieves economical and non-invasive dechlorination even in the presence of high source concentrations of chlorinated ethenes, desirable end products, greater tolerance to high levels of contaminants and reduction in chlorinated hydrocarbon levels, addresses various forms of chlorinated hydrocarbons, and ensures complete reduction of halogenated compounds under anaerobic conditions.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a mixed culture of Dehalococcoides microorganisms; and    (2) a process for biodegradation of a material.    DESCRIPTION OF DRAWING(S) - The diagram shows a cross sectional view of an in situ product and support for removal of chlorinated ethenes.    Injection wells (10)    Water table (12)    Impermeable section (13)    Screens (14)    Contaminated zone. (20)
NOVELTY - An oxidation self-heat type reformer contains modification portion and oxidation heat-emitting portion. A gas containing hydrogen and/or carbon monoxide is introduced into oxidation heat-emitting part and substance which heat-generates by oxidation reaction, and oxidizing gas containing oxygen. The modification portion is heated to more than temperature whose modification reaction of reforming raw material and water vapor are carried out by oxidation heat emission of partial-oxidation reaction.    USE - Method for starting oxidation self-heat type reformer for solid oxide fuel cell.    ADVANTAGE - The method easily starts oxidation self-heat type reformer without using heater and damaging catalyst.    DETAILED DESCRIPTION - An oxidation self-heat type reformer contains modification portion and oxidation heat-emitting portion. The modification portion produces reformed gas containing hydrogen as main component, by modification of mixture of reforming raw material containing hydrocarbon, aliphatic alcohol and/or water vapor. The oxidation heat-emitting portion generates heat by filling a portion with oxidation catalyst, and oxidizing a portion reforming raw material or reformed gas. A gas containing hydrogen and/or carbon monoxide is introduced into oxidation heat-emitting part and substance which heat-generates by oxidation reaction, and oxidizing gas containing oxygen. The modification portion is heated to more than temperature whose modification reaction of reforming raw material and water vapor are carried out by oxidation heat emission of partial-oxidation reaction.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of solid oxide fuel cell containing oxidation self-heat type reformer. (Drawing includes non-English language text)    Oxidation self-heat type reformer (1)    Solid oxide fuel cell (2)    Raw material introducing line (3)    Anode waste gas exit (7)    Cathode waste gas exit (8)
NOVELTY - A benzene sulfonyl urea is new.    USE - Benzene sulfonyl urea for use as medical lead compound.    ADVANTAGE - The method uses raw materials that are easy to obtain, does not use virulent raw materials thus avoids the serious environmental pollution thus is environment friendly, and has good industrial application prospect.    DETAILED DESCRIPTION - A benzene sulfonyl urea of formula (I) is new.    R=H, halo, 1-10C alkyl, OH, NO 2, trifluoromethyl or aldehyde group.    An INDEPENDENT CLAIM is included for preparation of benzene sulfonyl urea.
NOVELTY - Treatment of sludge comprises treating a sewage collected from a sewage disposal plant through grate-grit chamber-biological treatment-secondary precipitating pool treatment to generate sludge water; during the sludge precipitating stage, adding 250-350 g fly ash to every 1L sludge water, and uniformly mixing to precipitate the sludge; and pumping the precipitated sludge water to a sludge dehydrated workshop with a pump to dehydrate such that water content of the sludge water dehydrated through a press filter reaches 40-50%.    USE - Method for the treatment of sludge used for sintering and building material brick, and as an agricultural fertilizer (claimed).    ADVANTAGE - The fly ash improves dehydrating property of the sludge without adding other materials.
NOVELTY - A low-nutrient Scenedesmus sp. LX1 that is separated from the tap water stored for one month, deposited under CGMCC NO. 3036, is new.    USE - The strain is useful for sewage advanced treatment, where the sewage is the secondary discharged water of deposition tank in normal city sewage secondary treatment process (all claimed).    ADVANTAGE - Because the Scenedesmus can grow in the low-nutrient environment, the nitrogen and phosphorus in the secondary discharged water can be removed to a low level; thus it reduces algal bloom to a maximum extent; the method using Scenedesmus to remove nitrogen and phosphorus in the secondary discharged water is featured with environment-friendly performance, low cost, good economical benefit, good nitrogen and phosphorus removing effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is use low-nutrient Scenedesmus in sewage advanced treatment comprising following steps: inoculating the Scenedesmus in sewage; carrying out advanced treatment for sewage by photosynthesis of the Scenedesmus cell in order to remove nitrogen and phosphorus in sewage, where the specific step is as follows: (a) inoculating the Scenedesmus in sewage; the primary inoculating density is 1x10-3x105/ml; (b) putting inoculated Scenedesmus in the condition that the light-darkness ratio is 14 hours:10 hours; the temperature is 25 degrees C; the relative humidity is 75%; the illumination strength is 800-1300 lux; carrying out culturing; using Scenedesmus cell to carry out photosynthesis in order to absorb nitrogen and phosphorus; after 3-13 hours, the maximum removing rate of the nitrogen and phosphorus in sewage can reach more than 95% and 99%; and (c) using high-speed centrifugal machine to centrifuge Scenedesmus liquid; and collecting Scenedesmus.
NOVELTY - A waste gas is treated by inletting air into waste gas containing nitrogen oxide using air compressor to adjust concentration and degree of oxidation; washing, and entering waste gas from the bottom of solid fermentation organism reaction pillar; discharging purified gas from top of the reaction pillar; transporting cleaning solution; and showering into the reaction pillar.    USE - Method of treating waste gas containing nitrogen oxide (claimed).    ADVANTAGE - The method has low equipment cost, and high conversion rate of nitrogen oxide.
NOVELTY - A bio-control bacteria reagent for preventing and treating Ephestia elutella, where the bio-control bacteria reagent is prepared by culturing test tube seeds.    USE - The bio-control bacteria reagent is useful for preventing and treating E. elutella (claimed) stored in the tobacco.    ADVANTAGE - The biological preparation can be used safely; it has low pollution for tobacco and environment and it can be used for biological preventing E. elutella stored in the tobacco.    DETAILED DESCRIPTION - A bio-control bacteria reagent for preventing and treating E. elutella, where the bio-control bacteria reagent is prepared by culturing test tube seeds, fermenting liquid, and preparing bio-control bacteria reagent as follows: (a) producing strain which is Bacillus thuringiensis subsp. colmer strain 5, CGMCC NO. 2895; (b) culturing test tube seeds: inoculating strain 5 to test tube bevel culture medium with 5% of beef extract, 1.0% of peptone, 2.0% of agar and 0.5% of sodium chloride, where its pH value is 8.0, culturing them for 2 days at 30 degrees C, obtaining test tube seeds; (c) fermenting liquid: inoculating seeds to fermenting pot with 0.5% of corn powder, 2.0% of soybean powder, 0.15% of yeast powder, 0.25% of fish powder, 0.05% of peptone, 0.25% of potassium dihydrophospate, 0.05% of calcium carbonate, 0.035% of magnesium sulfate, 0.025% of de-foaming agent and surplus water, where its pH value is 7.5, fermenting them at 30 degrees C with 15% of throughput, fermenting for 36 hours under condition of 150 revolution per minute (rpm) agitating speed; (d) preparing bio-control bacteria reagent: centrifuging 5000 g of culture liquid for 20 minutes at 5 degrees C by use of centrifuging machine, freeze-drying deposit at room temperature, crushing and obtaining bio-control bacteria reagent.
NOVELTY - S-(+)-(o-chlorophenyl) glycine is prepared by reacting o-chlorobenzaldehyde, potassium cyanide, ammonium bicarbonate to synthesize (+/-) o-chlorobenzene hydantoin; dissolving the (+/-) o-chlorobenzene hydantoin with water; regulating pH of aqueous solution to 8-10; then adding Agrobacterium as enzyme (10-20 mass% of (+/-) o-chlorobenzene hydantoin) to react for 1-3 days under protection of nitrogen at 35-45 degrees C in shaking condition.    USE - Method for preparing S-(+)-(o-chlorophenyl) glycine (claimed).    ADVANTAGE - The method does not use any chiral compound and directly obtains chiral product by enzyme catalysis; and has high yield, low cost and simple process. Further, because of enzyme catalysis technology, the whole production process uses less organic solvent, has less waste material and is environment-friendly.
NOVELTY - This invention is regarding a kind of microorganism organic fertilizer of high-speed fermentation enzyme. During the process of its growing up, activiting, reproducing by using the microorganism, the concerning function character is that it can carry on fermenting and decomposing the organic waste material, biological remnant body, animal excreta etc. In addition, crushing the organic waste material and adjusting the appropriate C/N ratio, the water content, the quantity of the air supply. Furthermore, to increase microorganism organic fertilizer of high-speed ferment enzyme on condition that the microorganism ferment temperature in the reactor groove is between 40 degree and 95 degree, it can promote the responding of microorganism, shorten the time of well-rotted compost, it also can kill and extinguish the germ of the raw material, parasite, harmful microorganism which are live in the organic waste material, biological remnant body and animal excreta. Meanwhile, it can step up the fermentation enzyme activity to accelerate the fermentation, the well-rotted compost organic material, and then forms the organic fertilizer.
NOVELTY - A biological refining of wood fiber raw material comprises crushing and sieving wood fiber raw material, obtaining long fiber, short fiber and powder; using 2-step method of alkali treatment and oxidation treatment to treat obtained long fiber, and making into paper pulp; and synchronously processing diastatic fermentation to short fiber and powder to obtain ethanol.    USE - Method for biological refining of wood fiber raw material (claimed).    ADVANTAGE - The method can comprehensively utilize raw material for producing paper pulp, ethanol and lignin; and does not need sulfur element and chlorine element, reduces wastewater discharge, and has good environment-friendly property. Compared with sulfate pulp made from same raw material, obtained paper pulp has higher obtaining rate and better paper pulp property. The paper pulp can obtain relatively high enzymolysis rate under function of relative low use amount of cellulase.
NOVELTY - Producing ethanol in macroalgae saccharification liquid containing mannitol comprises: (a) manufacturing macroalgae saccharification liquid; (b) pre-processing the macroalgae with fucoxanthin; and (c) cultivating recombinant Escherichia coli comprising pyruvate decarboxylase (pdc) and alcohol dehydrogenase (adh) genes in the macroalgae saccharification liquid.    USE - The method is useful for producing ethanol from macroalgae saccharification containing mannitol (claimed).    ADVANTAGE - Ethanol can be produced from any kind of macroalgae, thus improving biomass fuel production.
NOVELTY - Generating hydrogen on a vehicle involves passing urea over a catalyst selected from nickel-containing catalyst.    USE - For generating hydrogen used as a fuel for fuel cell, and as a reductant for NOx in combustion exhausts; and in an exhaust gas after treatment system (claimed).    ADVANTAGE - The method generates 50% addition hydrogen gas, which is derived from water vapor. The urea is better hydrogen source for fuel cell than toxic methanol. The NOx control system is improved system and useful during cold start and during low temperature sections of the engine operating cycle. The system reduces catalyst size and associated weight penalty, thus reduces overall system cost.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for following:    (1) in the catalytic production of hydrogen, urea and water vapor as a feedstock, is used;    (2) improved NOx control system for combustion exhausts of vehicles i.e. light duty diesel vehicles, comprising a urea storage tank, urea dosing unit and a control unit associated in it, and a selective catalyst reduction (SCR) catalyst unit, and/or a NOx absorber unit, where the urea tank is connected to a catalytic unit capable of converting urea into hydrogen, and unit for supplying the hydrogen formed to the SCR catalyst unit and/or the NOx absorber unit; and    (3) catalytic reactor comprising a flow-through monolith having several cells, where each of at least a proportion of the cells has a resistance heating wire located in it, and the resistance heating wire has a catalytic surface.
NOVELTY - Filters (15) are provided in water inlet of centrifugal water pump (10). A water pressure gauge (7) is provided on a spray pipe (5). A drain pipe (16) is connected to inlet of high pressure centrifugal exhauster (8). The outlet of exhauster is connected to air inlet pipe (17) provided at the lower side of bio-trickling filter (1). An air outlet pipe (18) is provided at upper side of bio-trickling filter. A water regulating pool is connected to outlet of filtrate pipeline system. A time relay controls the metering pump arranged between pool and pipeline system.    USE - Device for deodorizing and nitrogen-protection of aerobic compost of solid organic waste.    ADVANTAGE - The deodorizing and recycling of aerobic compost of solid organic waste can be controlled effectively. The device can be operated easily. The volatilization of ammonia and nitrogen in the aerobic compost of solid organic waste can be performed efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the deodorizing and nitrogen-protection device.    Bio-trickling filter (1)    Spray pipe (5)    Water pressure gauge (7)    High pressure centrifugal exhauster (8)    Centrifugal water pump (10)    Filters (15)    Primary drain pipe (16)    Air inlet pipe (17)    Air outlet pipe (18)
NOVELTY - Lawn fertilizer preparation involves collecting and washing cypridina and crustaceans selected from food residues, crab shell, starfish, and by-products of chicken slaughterhouse and fishes and pulverizing them into a size of 5-30 mm to prepare organic waste. The organic waste is heated by water in a heating device. Loess, germanium, pyrophyllite, 10-30 wt.% of quicklime and dolomite are added to hydrolyze the mixture at a temperature of 100-200 degrees C for 60-180 minutes.    USE - Method for preparing lawn fertilizer.    ADVANTAGE - The lawn fertilizer preparation method is eco-friendly, provides lawn fertilizer, which regenerates tissues, promotes the rearing of plants roots and prevents the plants from being stressed.    DETAILED DESCRIPTION - Lawn fertilizer preparation involves collecting and washing cypridina and crustaceans selected from food residues, crab shell, starfish and by-products of chicken slaughterhouse and fishes, and pulverizing them into a size of 5-30 mm to prepare organic waste. An additive is prepared by collecting Artemisia capillaris Thunb, Cnidii Rhizoma and lawn grass, and cutting them into a size of 5-30 mm. 40 wt.% of bean-curd dregs, 10 wt.% of bean and 30 wt.% of corn are mixed with the cut plant mixture. The plant mixture is steamed and cooled to 30 degrees C. 10-20 wt.% of rice bran is mixed and is allowed to ferment at 30-40 degrees C for 5-7 days. Quicklime and dolomite are added to the organic waste in a heat processing device. The steam liquidized product is mixed with finely crushed bamboo, arrowroot, reed, ascidian, cornstalk, vegetables and pine needles, which are pulverized into 80-100 meshes and is allowed to stabilize for 2-3 days.
NOVELTY - A to-be-processed food wastewater is collected and filtered, and contaminants are removed. A neutralizer is added to wastewater, and mixed. Flocculant and flocculation aid are added, and wastewater is passed through separation films. Biological treatment is carried out using microorganisms, and wastewater is filtered by a filter medium. Thus, food wastewater treatment is enabled.    USE - Treatment of food wastewater.    ADVANTAGE - The food wastewater is quickly purified in small-scale installation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for food wastewater treatment apparatus, which has a collection tank for collecting wastewater, a filtration tank having filtration mesh for filtering contaminants of wastewater, a balancing tank, a reaction tank, solid-liquid separation tank, primary and secondary aeration tank and settling tanks, and a decoloring and deodorizing tank. The balancing tank carries out injection of neutralizer into the wastewater, and has a balancing agitator for agitating wastewater and the neutralizer. The reaction tank injects flocculant and flocculation aid into the wastewater and has reaction agitator for agitating wastewater. The solid-liquid separation tank discharges contaminants by separating flocculated contaminants in reaction tank from the wastewater. The primary aeration tank and settling tank have carriers for degrading wastewater separated from solid-liquid separation tank by microorganisms. The secondary aeration tank and settling tank carry out degradation of wastewater by microorganisms, and have membranes installed such that the wastewater passes through the membranes. The decoloring and deodorizing tank has a filtering material.
NOVELTY - Treatment of a biological film and a granular sludge in an organic wastewater comprises mixing an organism reinforced bacterium fluid and a padding, adding a nutrient fluid and sodium bicarbonate, and exchanging the mixed liquid every 3-4 days till the biological film is formed on the padding; placing the padding in a padding area (4) of a composite device, and directly inoculating the granular sludge; and controlling water-inlet chemical oxygen demand (COD) and sulfate (SO42-) density.    USE - Method for the treatment of a biological film and a granular sludge in an organic wastewater (claimed).    ADVANTAGE - The method enables the sulfate reducing bacteria hanging film on the used padding to achieve fixation, which increases the organism holding quantity of the reactor. High-efficient reduction of the sulfate is achieved while removing the organic matter.    DETAILED DESCRIPTION - Treatment of a biological film and a granular sludge in an organic wastewater comprises:    (A) mixing an organism reinforced bacterium fluid and a padding at a volume ratio of 1:10, adding a nutrient fluid, adding sodium bicarbonate having a density of 500 mg/L to adjust the alkalinity of the mixed liquid, where the pH of the mixed liquid is 7.5, and exchanging the mixed liquid every 3-4 days till the biological film is formed on the padding, where the temperature of the mixed liquid is 25-30 degrees C during the film hanging;    (B) placing the padding in a padding area (4) of a composite device of the anaerobic biological film and the granular sludge, and directly inoculating the granular sludge in a sludge bed area (3) producing the activity of methane; and    (C) controlling water-inlet COD density at 2000-3000 mg/L, and SO42- density at 500-600 mg/L.    DESCRIPTION OF DRAWING(S) - The drawing is a sectional view of the composite device.    Sludge bed area (3)    Padding area (4)    Pump (12)
NOVELTY - Improvement of sludge disruption effect and strengthening subsequent anaerobic digestion comprises after carrying out gravity precipitation and condensation of residual sludge from secondary sedimentation tank of city life sewage treatment factory, sending the residual sludge in an ultrasonic reactor for ultrasonic wave irradiation and adding sodium hydroxide (NaOH), where cavitation effect of ultrasonic wave in water produces extreme physical condition, the cell wall structure of the sludge is damaged, and easily degraded organic material is dissolved.    USE - Method of improving sludge disruption effect and strengthening subsequent anaerobic digestion (claimed), useful in treating residual sludge of sewage treatment factory.    ADVANTAGE - The method improves the chemical oxygen demand concentration in sludge liquid phase by 52 times; and improves methane yield by 40.6%. It overcomes the problem of the limitation in the application of ultrasonic wave due to high energy consumption.    DETAILED DESCRIPTION - Improvement of sludge disruption effect and strengthening subsequent anaerobic digestion comprises after carrying out gravity precipitation and condensation of the residual sludge from secondary sedimentation tank of city life sewage treatment factory, sending the residual sludge in an ultrasonic reactor for ultrasonic wave irradiation and adding NaOH, where cavitation effect of ultrasonic wave in water produces extreme physical condition, the cell wall structure of the sludge is damaged, and easily degraded organic material is dissolved, such that the content of soluble organic substance in sludge liquid phase is increased; putting the sludge after common action of ultrasonic wave and NaOH in a shaker to react for 24 hours; sending the sludge in an anaerobic digestion reactor to carry out subsequent anaerobic digestion at moderate temperature; and collecting biogas produced by digestion through a gas collector and measuring yield of methane.
NOVELTY - A polymeric biological liquid fuel comprises (wt.%) alkylol amide (1-2), potassium hydroxide (0.5-1.5), fatty alcohol (2-5), methanol (60-80), ethanol (7-15), and additives such as ferrocene (0.5-1.5), hydrogen peroxide (6-10) and toluene (8.5-16.5).    USE - A polymeric biological liquid fuel.    ADVANTAGE - The fuel is non-toxic and harmless; has no fume, no odor, no pressure, no explosion and no residual solution; does not discharge wastes; provides adequate ignition, clean and sanitary, and high efficiency; and saves energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of preparing polymeric biological liquid fuel by reacting raw materials, heating at 35 degrees C, agitating for 20 minutes, setting aside for greater than or equal to 2 hours at normal temperature, and filtering.
NOVELTY - Organic material compost manufacturing involves storing food wastes and injecting stored food wastes into preprocessing chamber furnace. The injected food waste is crushed and fermented by inoculating microorganism and mixing sawdust or wood chip. Fermentation is carried out in three fermentation rooms to obtain a fermentation product. The microorganism is provided from microorganism culture jar.    USE - Method for manufacturing organic material compost.    ADVANTAGE - The organic material compost manufacturing method enables to manufacture the organic material compost with high productivity by reducing generation of effluent and bad smell, where generated effluent or waste water is used to culture the microorganism.
NOVELTY - A biomass is pretreated by cutting biomass into short pieces of 3-40 mm; dipping short pieces for 15-90 minutes into water at 15-80 degrees C; tearing up short pieces after dipping; subjecting pieces obtained by tearing to hydrothermal reaction in condition of heating or heating and pressurizing; and pressing straw after subjecting to hydrothermal reaction to obtain saccharification solution and saccharification residues.    USE - Method for pretreating biomass for production of biogas (claimed).    ADVANTAGE - The method improves biodegradability of straw, accelerates fermentation speed, can be operated with high efficiency, and converts biomass in large scale.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for production of biogas through anaerobic fermentation of biomass comprising subjecting saccharification solution obtained by pressing after pretreatment to methane fermentation, and returning fermentation solution to pretreatment or to step for ultrasonic treatment for decomposing.
NOVELTY - Cultivating biologic strain for purifying mixed organic waste gas having volatility and low concentration comprises: (a) cultivating strain; (b) mixing strains and inoculating, and preparing sludge concentration of the mixed strain with tap water; and (c) taking mixed organic substance in the waste gas as substrate.    USE - The method is useful for cultivating biologic strain for purifying mixed organic waste gas having volatility and low concentration (claimed).    ADVANTAGE - The invention can degrade several target component compounds high efficiently and simultaneously.    DETAILED DESCRIPTION - Cultivating biologic strain for purifying mixed organic waste gas having volatility and low concentration comprises: (a) cultivating strain one; (b) mixing strain one with strain two and inoculating, and preparing sludge concentration of the mixed strain with tap water; and (c) taking mixed organic substance in the waste gas as substrate, throwing into an inoculated culture medium, cultivating and acclimatizing the inoculums; where the strain one is obtained by cultivating and acclimatizing the active sludge from dyeing wastewater treatment plant, which is mixed strain of Flavobacterium and waxy Bacillus; the strain two is obtained by collecting active sludge in secondary settlement tank of petrochemical sewage treatment plant, which is mixed strain containing Flavobacterium, waxy Bacillus, Achromobacter xylosoxidans and Pseudomonas stutzeri.
NOVELTY - In-situ remediation of groundwater nitrate pollution, involves using cornstalk and/or cornstalk hydrolyzate fluid as denitrification carbon source, adding denitrifying bacteria flora-enriched fluid to nitrate-polluted groundwater, and removing nitrate nitrogen by biological denitrification.    USE - In-situ remediation of groundwater nitrate pollution with cornstalk.    ADVANTAGE - The method efficiently uses cornstalk biomass, while efficiently eliminating nitride pollution of groundwater.
NOVELTY - Biodiesel fuel is obtained by a modification process, which involves reacting a raw material, oil, and fatty acid, or a mixture of the oil with alcohol in the presence of an acid catalyst. The acid catalyst is a hydrophobic zeolite having a warped surface of 100-1200 m2/g and a silicon/aluminum molar ratio of 20-450.    USE - Manufacture of biodiesel fuel for domestic and industrial applications.    ADVANTAGE - The method uses a specific zeolite having proper acid strength, and enables simple manufacture of biodiesel fuel with high conversion ratio (80% or more) by using a raw material having high free-fatty-acid content.
NOVELTY - The solar heating system is provided with anaerobic fermentation cylinder (2), solar heat collector (1), heat storage water tank (8), three-way conversion valves (14), recycle-water pumps, detection control system and connecting pipes. The heat storage water tank is divided by a separation plate for heat storage and heat supply. A heater (3) is laid inside fermentation cylinder, and is connected with regulating water tank (17). A feeding pipe (24) and discharge pipe (23) passes through sludge waste heat reclaiming heat exchanger (4) to fermentation cylinder.    USE - Constant temperature solar heating system for medium/high temperature anaerobic fermentation cylinder.    ADVANTAGE - The high solar energy utilizing rate is achieved by storing the heat reliably.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the constant temperature solar heating system.    Solar heat collector (1)    Anaerobic fermentation cylinder (2)    Heater (3)    Sludge waste heat reclaiming heat exchanger (4)    Heat storage water tank (8)    Three-way conversion valves (14)    Regulating water tank (17)    Discharge pipe (23)    Feeding pipe (24)
NOVELTY - A fuel producing system has a preprocessing portion (104) to generate biogas (b) by preprocessing the collected biogas (a), a consolidation portion (108) to generate methane gas by consolidating the biogas (b) and a compression portion (I) (112) to generate compressed methane gas by compressing the methane gas.    USE - System is used for producing fuel (claimed) for car. Can also be used in boiler and fuel cell.    ADVANTAGE - The system produces fuel using biogas, by increasing concentration of methane gas in the biogas and removing carbon dioxide from biogas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of fuel, which involves generating biogas (b) by preprocessing the collected biogas (a), generating methane gas by consolidating the biogas (b) and generating compressed methane gas by compressing the obtained methane gas.    DESCRIPTION OF DRAWING(S) - The drawing shows the flowchart of the fuel manufacturing system. (Drawing includes non-English language text)    Capture sites (102,106,110)    Preprocessing portion (104)    Consolidation portion (108)    Compression portion (112)    Charge unit (116)
NOVELTY - The apparatus has a pair of laser light sources (14,15) to generate pump light and signal light. A difference frequency light generating unit (16) generates difference frequency light from pump light and signal light. An optical detection unit (18) sets pump light, signal light and difference frequency light to optical absorption wavelength having high molar absorption coefficient and detects irradiation of laser beam to gas measurement region (2). A control unit (11) measures concentration of gas based on the detection output of optical detection unit.    USE - Apparatus for measuring concentration of gas such as carbon dioxide, methane and carbon monoxide.    ADVANTAGE - The concentration of the gas can be measured with high accuracy using the laser beam irradiated to gas measurement region.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the gas measurement apparatus. (Drawing include non-English language text)    Gas measurement region (2)    Control unit (11)    Laser light sources (14,15)    Difference frequency light generating unit (16)    Optical detection unit (18)
NOVELTY - The apparatus (100) has a potentiostat (4) which connects electroconductive elements (2) supporting laminated portion (1). A primary layer (7) is formed in one surface and secondary layer (8) is formed in other surface of electroconductive element. A catalyst metal-ion containing solution (10) is supplied to contact location of electroconductive element and laminated portion. The catalyst metal is deposited in primary or secondary layer to which catalyst metal-ion containing solution is supplied, when electrical potential difference is produced between the layers.    USE - Apparatus for manufacturing electrode for fuel cell used in motor vehicle such as electric vehicle, and domestic co-generation system.    ADVANTAGE - Since the catalyst metal-ion containing solution is supplied by electrical potential difference condition, the productivity of electrode is improved so that utilization factor of catalyst metal is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing method of electrode for fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the manufacturing apparatus of electrode for fuel cell.    Laminated portion (1)    Electroconductive element (2)    Potentiostat (4)    Primary layer (7)    Secondary layer (8)    Catalyst metal-ion containing solution (10)    Manufacturing apparatus (100)
NOVELTY - The electrode has anode (4) and cathode (6) arranged between carbon boards or nickel boards (11,12), so that carbonate powder is dispersed on the surface of the anode and cathode. The amount of carbonate (10) with respect to the total volume of pores in the anode and cathode reaches 80 %, by heating the anode and cathode to about 60 minutes, at a temperature greater than or equal to 650 degrees C, in nitrogen atmosphere. The difference between porosities of cathode and anode before oxidation is in the range of 0-13 %.    USE - Electrode of molten carbonate fuel cell (MCFC) (claimed) used in manufacture of power equipment.    ADVANTAGE - The start-up of the fuel cell can be made favorable by impregnating carbonate into the electrode. The output voltage of the fuel cell can be increased, by adjusting the porosity of the anode and cathode.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing method of electrode of molten carbonate fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the electrode of the molten carbonate fuel cell. (Drawing includes non-English language text)    Cathode (4)    Anode (6)    Carbonate (10)    Nickel boards (11,12)
NOVELTY - The biomass gasification regeneration energy source system has a pre-treatment device (4), a pyrolytic decomposition gasification unit (13), a carbon-transforming unit (15), a melting unit (17), and a synthesis gas-reforming unit (27) that are joined to each other. The pre-treatment device and pyrolytic decomposition gasification unit are independent irrespective of absence of oxygen. A poly-radical accelerated reaction unit (23) is between the pyrolytic decomposition gasification unit and synthesis gas-reforming unit.    USE - Multi-level controlling poly-radical biomass gasification regeneration energy source system for transforming wide biomass, carbon-containing raw materials, such as energy source crops, side products of agriculture and forestry, organic wastes, industrial and dangerous wastes into high-grade energy source.    ADVANTAGE - Cost effective by eliminating auxiliary fuel, while maximizing gasification efficiency. Enables cracking tar and removing pollutant. Offers energy-saving and environmentally friendly technology with non-burning and innoxious treatment.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of the multi-level controlling poly-radical biomass gasification regeneration energy source system.    Pre-treatment device (4)    Pyrolytic decomposition gasification unit (13)    Carbon-transforming unit (15)    Melting unit (17)    Poly-radical accelerated reaction unit (23)    Synthesis gas-reforming unit (27)
NOVELTY - An improved process for the purification of water by removing phenol from water containing 5000 mg/l or less of phenol using a mutated Pseudomonas strain, involves contacting by passing a mixture of water containing phenol and domestic waste water in the ratio of 1:0.5 to 1:2 volume/volume with a novel mutated strain of Pseudomonas, immobilized on rice bran based activated carbon, and packed in a reactor for 24-44 hours and collecting the purified water coming out of the reactor. Image 0/0
NOVELTY - A solid wood fuel body contains 0.1-3 wt.% of flour content including anti-slagging additives selected from calcium (Ca) and aluminum (Al) salts.    USE - As an energy source for power stations or central heating boilers (claimed).    ADVANTAGE - The wood fuel is an improved wood fuel based on saw dust and/or chips, exhibiting improved fuel ash properties, upon combustion in the high temperature regions resulting in smaller, less tenacious fireside deposits, reduced slagging and less fouling, and is easy-to-remove using conventional cleaning methods. The wood-based fuel, particularly wood pellet, which provides more friable ash deposit in the fireside sections of combustion systems, and solves the prior art disadvantages. The additive improves wood fuels in terms of reduced slagging and fouling tendencies, more friable ash or combustions residues, and wood flour processing, in particular pelletizing. The additive should not be troubled by caking and have excellent flowability. The flour-based wood fuel additive essentially comprises high amounts of flour and an optimized content of calcium and/or aluminum salts.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing a solid wood fuel body involving providing non-pyrolyzed wood, preferably ground and/or milled wood, with 0.1-3 wt.% of flour content to obtain the body containing flour content including anti-slagging additives selected from calcium and aluminum salts, where the mixture is processed to obtain solid wood fuel body.
NOVELTY - Method for producing hen dropping fertilizer, involves adding (in weight parts): discarded unfermented and alkaline hen droppings (100) having moisture content of 25-40 weight% to acidic waste microbial bed containing eryngii mushroom (Pleurotus eryngii), maitake mushroom (Grifola frondosa), shimeji mushroom or shiitake mushroom (10), and fermenting to produce hen dropping fertilizer.    USE - The method is useful for producing hen dropping fertilizer (claimed).    ADVANTAGE - The fertilizer can be produced rapidly, and production of offensive odor during fermentation is prevented.
NOVELTY - A fuel cell system (100) is provided with fuel cell (20), hydrogen production unit (26) and amino acid storage unit which supplies amino compound to hydrogen production unit which radicalizes the amino compound having amino group and decomposes according to catalytic reaction and produces hydrogen which is supplied to the fuel cell.    USE - Fuel cell system is used for vehicle (claimed).    ADVANTAGE - The fuel cell system is compact and economical.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of fuel-cell vehicle. (Drawing includes non-English language text)    Fuel cell (20)    Ammonia feed pump (24)    Hydrogen production unit (26)    Fuel cell system (100)    Fuel-cell vehicle (1000)
NOVELTY - A soluble granule comprises (wt.%) glyphosate ammonium (50-95), glyphosate synergist (0.5-25), phosphate (0.5-40), filler (0-10), xanthan gum (0.1-0.5), and water.    USE - A soluble granule for controlling weed (claimed).    ADVANTAGE - The granule has stable property, requires simple and smooth production, has no environment pollution, and does not easily absorb moisture.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing a soluble granule, comprising mixing glyphosate ammonium, glyphosate synergist, phosphate, filler, and xanthan gum; granulating; and drying.
NOVELTY - A hydrogen is produced and purified by covering hydrogen generator with heat insulating coating, cooling hydrogen gas, removing condensate with water absorbing material, and removing alkali mist with alkali remover.    USE - Method of producing and purifying hydrogen (claimed).    ADVANTAGE - The method reduces temperature on external wall of hydrogen generator, and effectively removes condensate and alkali mist, which is safe and simple for operation.
NOVELTY - A potato alcohol wastewater is treated by separating solid and liquid of alcohol waste slurry liquid produced in potato production, introducing alcohol waste slurry liquid into anaerobic tank to carry out anaerobic digest, and recycling produced biogas in anaerobic digestion. The solid and liquid of alcohol wastewater are separated before anaerobic digestion is carried out to alcohol wastewater.    USE - Method for treatment of potato alcohol wastewater (claimed).    ADVANTAGE - The method is environment-friendly, has less solid waste slurry, and less mud and high biogas yield.
NOVELTY - A Tricholoma giganteum compost comprises (wt.%) pure straw powder (32-45), bran (25-40),dry dairy manure ( 12-19), corn powder (3.6-6.7), rice bran powder (3.5-4), bean cake powder (0.5-1), rape seed cake (1.7-2), white sugar (0.58-1), plaster (0.1-0.3), calcium carbonate (0.1-0.3), carbendazol (0.1-0.3), and monopotassium phosphate (0.5-0.8).    USE - A T. giganteum compost.
NOVELTY - The system has a reforming module connected with a fuel cell stack, and a heat exchange device located adjacent to the reforming module. A pipe is connected between the heat exchange device, fuel cell stack and a heat/cooling medium, where the heat medium supplies heat of the heat exchange device to the fuel cell stack. The reforming module comprises an auto-heat reforming unit, a high temperature water-gas shift reaction unit and a regenerative thermal oxidation unit. The water-gas shift reaction unit is connected between the auto-heat reforming unit and the thermal oxidation unit.    USE - Fuel cell generating system.    ADVANTAGE - The system can transfer heat of the heat medium to the fuel cell stack by cycling the heat medium between the heat exchange device and the fuel cell stack, so that heat of the reforming module can be utilized to pre-heat the fuel cell stack. The system can increase temperature of fuel cell stack to operating temperature without consuming extra electric energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a heat regulating system for regulating temperature of a fuel cell stack.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a fuel cell generating system.'(Drawing includes non-English language text)'
NOVELTY - The oxygen or hydrogen dissolving apparatus has a conductor (5) that is provided in outer side of electrode (2) contacting to polymer electrolyte membrane (1). The water electrolyzer having raw material incorporated in stationary plate is provided in outer side of conductor for pressing the electrodes with respect to polymer electrolyte membrane. The hydrogen and oxygen gas emitted as microbubble from the electrodes is collected through gas discharge hole (7) provided in fixed plate.    USE - Oxygen or hydrogen dissolving apparatus. Uses include but are not limited to educational applications, recycled water supply apparatus for medical field, sterilizer for fishing culture applications and hydroponic applications.    ADVANTAGE - The hydrogen or oxygen gas can be dissolved in the water rapidly. The hydrogen or oxygen gas can be emitted effectively, even if the gas emitted from lower side of electrodes is higher than the atmospheric pressure.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the oxygen or hydrogen dissolving apparatus. (Drawing includes non-English language text)    Polymer electrolyte membrane (1)    Electrode (2)    Conductor (5)    Gas discharge hole (7)
NOVELTY - The process involves liquefying natural gas liquids at elevated pressures for increasing required condensation temperature. The temperatures and pressures are compared to a transportable liquid carbon-dioxide. Transportation of liquefied carbon-dioxide at pressures ranging from 400 to 600 pound per square inch gauge (psig) and temperatures ranging from minus 10 degree Fahrenheit to 40 degree Fahrenheit are handled by pressurized liquefied natural gas (PLNG) vessels.    USE - Process for backhauling carbon-dioxide on liquefied petroleum gas (LPG) or pressurized liquefied natural gas (PLNG) ships in a PLNG technology.    ADVANTAGE - The process allows applying elements of pressurized liquefied natural gas (PLNG) technology to a transportation of liquefied carbon-dioxide. The method allows conditions for PLNG transport range from 150 to 1100 pound per square inch gauge (psig) and minus 190 degree Fahrenheit to minus 80 degree Fahrenheit, thus minimizing weight of the overall transport vessel.
NOVELTY - The sensor (1) has a diaphragm-like heat-insulation support layer (12) spread in an opening part of a through-hole formed on a silicon substrate (11). A heater layer (13) is provided on the support layer. An electric-insulation layer (14) is provided such that the support layer and the heater layer are covered. An intermediate buffer layer (16) is provided on the electric-insulation layer. A tin oxide sense layer (15b) is provided on the buffer layer. The buffer layer stacks silicon di-oxide and tin oxide thin films. The electric-insulation layer contains silicon di-oxide.    USE - Thin film gas sensor i.e. low-power-consumption-type thin film gas sensor, for use in a gas-leakage alarm unit to detect leakage of gas in a house. Uses include but are not limited to carbon monoxide, methane gas, propane gas, and ethanol vapor.    ADVANTAGE - The intermediate buffer layer stacks the silicon di-oxide and tin oxide thin films, thus avoiding influence of stress change in the electric-insulation layer and the sense layer, and hence suppressing generation of micro-crack.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of a thin film gas sensor.'(Drawing includes non-English language text)'    Thin film gas sensor (1)    Silicon substrate (11)    Diaphragm-like heat-insulation support layer (12)    Heater layer (13)    Electric-insulation layer (14)    Tin oxide sense layer (15b)    Intermediate buffer layer (16)
NOVELTY - A modifier containing ozonized vegetable oil and having pour point fall effect, is added into biodiesel fuel to obtain solid-phase and liquid-phase of biodiesel fuel. The obtained solid-phase contains precipitated saturated fatty acid alkylester, and liquid-phase contains unsaturated fatty acid alkylester.    USE - Separation of biodiesel fuel such as methyl-esterification fuel used for engines.    ADVANTAGE - The method provides diesel fuel having excellent low-temperature fluidity and combustibility, and high cetane number. The engines containing obtained diesel fuel has favorable engine starting property without noise and reduced fuel consumption.
NOVELTY - Synthesizing oxidized fuel from soybean oil methyl ester, comprises aging the fuel to a low level of oxidation stability as measured by a Rancimat induction period of less than 1 hour.    USE - The process is useful for synthesizing oxidized fuels, which is useful for engines with biodiesel fuels.    ADVANTAGE - The process: yields consistent quality of oxidized fuel; and is cheaper and quicker than the alternate option of aging the fuel by purging of air through the barrel of fuel.
NOVELTY - Potassium methylate in form of dry substance or anhydrous solution in methyl alcohol is used as a catalyst when splitting oils and fats, in etherification reactions during production of biodiesel, surface active substances, pharmaceutical and cosmetic preparations. The method involves reacting potassium hydroxide and methanol at high temperature with removal of the formed water using dry methyl alcohol. Synthesis is done in a reaction-separation process in a film type counterflow column reactor at 92-130C, uniform on the entire height of the reactor, while feeding the initial solution from the top, made by dissolving potassium hydroxide in methyl alcohol, and dry methyl alcohol vapour from the bottom.    USE - Chemistry.    ADVANTAGE - More efficient desorption of the formed water and output of the process and reduced energy consumption of the process. 1 tbl, 1 dwg, 5 ex
NOVELTY - The method involves transferring electrolyte solution (26) e.g. sodium chloride brine solution from an electrolyte source to an electrolyte cell (10). The electrolytes present the solution are electrolyzed to form one or more oxidants (16) and hydrogen gas (14). The oxidants are transferred to a container (24) by using hydrogen gas. The concentration of the oxidant is increased relative to that of the electrolytes in the container, by circulating the oxidants back into the electrolytic cell such that it is maintained between approximately 3 to 15 grams per liter of free available chlorine.    USE - Method for increasing oxidant concentration in disinfecting solution for water treatment system for home-use and consumer market. Can also be used in spray bottle applications for surface cleaning, waste water treatment system, cooling tower treatment system, etc.    ADVANTAGE - By re-circulating the electrolytes and circulating the oxidants back into the electrolytic cell from the container, the concentration of the oxidant in the container can be increased effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for system for increasing oxidant concentration.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the electrolyte cell.    Electrolyte cell (10)    Hydrogen gas (14)    Oxidant (16)    Container (24)    Electrolyte solution (26)    Controller (28)
NOVELTY - A hydrogen producing method involves spontaneously producing anode reaction including oxidation reaction of hydride ion and cathode reaction including hydrogen producing reaction in solution containing ionic hydride and hydroxide through cation interchangeable electrolytic membrane.    USE - A hydrogen producing method.    ADVANTAGE - The method is efficient, simple, safe and easy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a hydrogen producing apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of hydrogen producing apparatus.    Hydrogen producing apparatus (1)    Anode side electrode (2)    Cathode side electrode (3)    Cation interchangeable electrolytic membrane (4)    External circuit (5)
NOVELTY - The vertical rotary biomass gasification furnace has furnace chamber (2) whose lower portion is provided with thick fuel gas temperature raising channel inlet (5A) and thick fuel gas temperature raising channel outlet (5B). A grate is provided at the bottom of furnace chamber, and set in V-shaped residue hopper. The upper portion of grate is connected to inner wall of furnace chamber, while the bottom is connected to residue scraping device (10). A motor (15) is connected to gear of residue scraping device to be used as power input source.    USE - Vertical rotary biomass gasification furnace.    ADVANTAGE - Performs continuous feeding and removal of residue of upper absorbing fixed bed gasification furnace. Enables to continuously and stably run with controllable parameters of frequency, speed and temperature, and obtains uniform distribution of materials. Improves heat efficiency since temperature of furnace is constant. Reduces energy consumption and material consumption. Reduces labor intensity of operators and eliminates bad effect to environment.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of vertical rotary biomass gasification furnace.    Furnace chamber (2)    Thick fuel gas temperature raising channel inlet (5A)    Thick fuel gas temperature raising channel outlet (5B)    Residue scraping device (10)    Motor (15)
NOVELTY - An alternative fuel of coal is manufactured by pumping sludge to filter press using pumping apparatus, deaerating gas component contained in sludge, dehydrating sludge sent from pumping apparatus by applying pressure in filter press, carrying out pressurization destruction of microorganisms cell wall contained in sludge, making sludge to contain less than or equal to 40% of moisture, mixing 70% of organic sludge and 30% of pulverized coal containing microorganisms, molding mixture into pellet form using molding machine, and obtaining alternative fuel of coal.    USE - Manufacture of alternative fuel of coal.    ADVANTAGE - The method uses landfill and incineration disposal effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a dehydrating system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of manufacturing method of alternative fuel of coal. (Drawing includes non-English language text).
NOVELTY - An alcohol wastewater anaerobic-digestion treatment comprises pretreating high-concentration organic wastewater generated in the production process of product with biomass as raw material, then continuously processing anaerobic digestion at two grade of high temperature and middle temperature.    USE - Method of anaerobic-digestion treatment of alcohol wastewater (claimed).    ADVANTAGE - The method has high chemical oxygen demand (COD) removing rate, and high biogas yield.
NOVELTY - The fuel cell has a stack (5) comprising an electrolytic membrane (6) placed between two electrodes (15a, 15b) perpendicular to a support substrate (1) that is made of electrically insulating material. The electrodes respectively have catalytic layers (7a, 7b) that are in contact with the membrane, and electrically conductive porous diffusion layers (16). The stack is inserted between electrically conductive support partitions (17a, 17b) perpendicular to the support substrate. The partitions constitute current collectors of the stack, and are electrically isolated from one another.    USE - Fuel cell for producing electricity.    ADVANTAGE - The structure of the porous diffusion layers assures effective diffusion of combustible fluid and oxidizing fluid towards the catalytic layers of the stack. The arrangement of the stack allows an increase in the power density with respect to the surface of the fuel cell, while limiting the heat losses when the stack is electrically connected with another stack.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for forming a fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a stack of a fuel cell.    Support substrate (1)    Stack (5)    Electrolytic membrane (6)    Catalytic layers (7a, 7b)    Electrodes (15a, 15b)    Porous diffusion layers (16)    Support partitions (17a, 17b)
NOVELTY - The magneto hydrodynamic fuel cell uses fuel and oxidant stream to generate an AC current in an external circuit. Hydrogen is injected into an electrolyte (2) through an electrically non-conductive fuel pipe (5). The electrolyte is made to rotate in a circular direction by a turbine (4) with blades.    USE - Magneto hydrodynamic fuel cell for generating AC voltage for e.g. transport applications.    ADVANTAGE - Can operate without electrodes and membranes. Enables generation of AC voltage which is useful for further transformation and convenient for transport applications.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of magneto hydrodynamic fuel cell.    Electrolyte (2)    Turbine (4)    Fuel pipe (5)    Secondary coil (15)    Electrical load (24)
NOVELTY - The water electrolysis device positive and negative electrode plates which are alternatively arranged and are connected by positive and negative electrode rods. The positive and negative electrode rods are connected to an electrolysis supply. One of the positive and negative electrode plates is of a mesh structure, and the other electrode plates are in the shape of flat plate. The electrical conductor is stainless steel, and the insulator is made from a high temperature resistant nylon material.    USE - Water electrolysis device using low current to produce hydrogen as auxiliary fuel of engine.    ADVANTAGE - Energy consumption is low and energy conversion rate is high. The water electrolysis device has simple structure, reasonable design and low production cost.    DESCRIPTION OF DRAWING(S) - The drawing shows the perspective view of the water electrolysis device.
NOVELTY - A biomass carbonization and vaporization device comprises a furnace with control valve, where furnace is sequentially connected to a condensing tower, screening tower, centrifugal tower and purification tower. A variable-frequency ventilator is arranged between centrifugal tower and purification tower. The condensing tower, screening tower and centrifugal tower are connected to a separation tank and cooling tower with temperature control circulating pump. The furnace is connected to a gas separation device for quickly putting out a fire.    USE - A biomass carbonization and vaporization device.    ADVANTAGE - The device has safe performance and good quality, and enables fast carbonization and large extraction. The whole process generates no pollution and waste, saves energy, and protects the environment. All materials are converted into products.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biomass carbonization and vaporization technique comprising using crop straw.
NOVELTY - A tertiary treatment and diffluent-irrigation-drainage device has a sludge pump (6) set at the outlet at bottom of a first purifying pond (1) and connected to dry land (7); a clarified water canal (8) that irrigates and discharges the clarified water and is arranged with three purifying ponds in parallel and is connected with the outlet at the bottom of third purifying pond (3); and clapboards (9) set in each purifying pond.    USE - Tertiary treatment and diffluent-irrigation-drainage device for biogas liquid.    ADVANTAGE - Prevents polluting the environment and atmosphere and reduces plague risk of pig in the biosphere while eliminating problem in which production reduction of paddy rice for biogas liquid is mixed into irrigation water for farmland by making biogas liquid and clarified water be distributed to discharge and irrigate.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a tertiary treatment and diffluent-irrigation-drainage device.    First purifying pond (1)    Third purifying pond (3)    Sludge pump (6)    Dry land (7)    Clarified water canal (8)    Clapboards (9)
NOVELTY - The water-saving environment-friendly device on job site, comprises a water collection settlement device, which is connected with a high-level water tank of a toilet sewage recycling device, a sewage chamber of biogas tank, an agitation station water tank and a cleaning water tank respectively through a water supply pipe. The recycling tank of the toilet sewage recycling device is connected with a septic tank of the biogas tank through a chute.    USE - Water-saving environment-friendly device on job site.    ADVANTAGE - Can collect, settle and use water discharged from the foundation ditch, the rain water and washing wastewater through the water collecting settlement device, and can ferment and purify the sewage by recycling in the recycling tank by the setting of biogas.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of the water-saving environment-friendly device on job site.
NOVELTY - A natural gas stream is cooled in upstream closed-loop refrigeration cycles (13,14) and open-loop methane refrigeration cycle (15) respectively, to form cooled methane stream. A multistage separation vessel (25) is arranged downstream of cooling pass, and upstream of warming pass of heat exchanger in open-loop methane refrigeration cycle. The cooled methane stream is separated into vapor stream and liquid stream, in separation vessel. The nitrogen mole fraction of vapor stream is set 1.25 times greater than nitrogen mole fraction of cooled methane stream supplied to vessel.    USE - Method for liquefying natural gas stream in cascade-type liquefied natural gas (LNG) facility.    ADVANTAGE - The nitrogen can be efficiently removed from the liquefied natural gas. The capital, maintenance and operating costs can be minimized, and the profit can be maximized.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the cascade-type LNG facility.    Upstream closed-loop refrigeration cycles (13,14)    Open-loop methane refrigeration cycle (15)    Refrigerant chillers (18,21)    Refrigerant economizer (24)    Multistage separation vessel (25)
NOVELTY - A natural gas is purified by contacting mixture of unpretreated gases with polybenzoxazole membrane at 50-200 degrees C to produce permeate gas stream comprising higher concentration of carbon dioxide than mixture of unpretreated gases, and product gas stream comprising lower concentration of carbon dioxide than unpretreated gases.    USE - Process of purifying natural gas (claimed).    ADVANTAGE - The process uses high gas permeability polybenzoxazole membranes which can be operated at high temperature to provide sufficient dew point margin for product gas; thus significantly saving capital cost, and reducing existing membrane footprint at greater than 50%.
NOVELTY - A treating unit (10) comprises a microbial cell (12) comprising conditioned activated sludge, and a supporting device (14) constructed by at least two rings (142, 144, 146) located on different planes and having a defined interior space. The microbial cell is contained in the interior space.    USE - A treating unit for a biological or wastewater treatment, or treating apparatus for simultaneously removing organics and nitrogen compounds from wastewater (claimed).    ADVANTAGE - The unit has a sludge design that does not require sludge to be returned; can be stabilized in a short period; is capable of removing organics, nitrogen compounds and suspended solids from wastewater under a controlled aeration mode; has enhanced efficiency thus reducing expenses; and is capable of eliminating the peeling of microbial aggregations.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a biological treatment apparatus;    (2) a wastewater treatment apparatus;    (3) a wastewater treatment system; and    (4) a treating apparatus.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a treating unit for wastewater.    Treating unit (10)    Microbial cell (12)    Supporting device (14)    Rings (142, 144, 146)
NOVELTY - Forming a microreactor (2) comprising a reaction chamber including a catalyst for producing gaseous hydrogen to be supplied to at least one micro fuel cell, comprises providing at least one first silicon die defining an active surface of the reaction chamber; anisotropically etching the at least one first silicon die to form many notches and ridges to define an increased active surface; and depositing a layer of the catalyst on at least one portion of the increased active surface.    USE - The microreactor is useful in device for the production of energy for portable applications (claimed).    ADVANTAGE - The microreactor allows the reduction of the overall size of the energy production system. The method: provides the microreactor economically; and reduces non-polluting by-products. The device increases the production of gaseous hydrogen produced in the reaction chamber, hence more efficient for the production of energy. The microreactor is versatile.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) the microreactor comprising the reaction chamber; at least one first silicon die having a face to define an active surface for the reaction chamber; the active surface comprising many notches and ridges to define an increased active surface; and a catalyst layer on at least a portion of the increased active surface; and    (2) a device for the production of energy for portable applications comprising at least one micro fuel cell (1); and the microreactor.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic block diagram of the device for the production of energy.    Micro fuel cell (2) Microreactor (1)    First tank (3)    Second tank. (4)
NOVELTY - A steam-reforming catalyst layer (2) is arranged in upstream of hydrocarbon and steam inlet section (1). A non-catalyst layer (3) is arranged in downstream of steam-reforming catalyst layer. A shift catalyst layer (4) is arranged in downstream of non-catalyst layer. The shift catalyst layer has shift catalyst that performs shift reaction of reformed gas. A hydrogen separation membrane (5) penetrates the shift catalyst layer. An exit portion (6) is provided in the downstream of shift catalyst layer.    USE - Membrane separation-type hydrogen production apparatus for use in hydrogen station.    ADVANTAGE - The hydrogen production efficiency of the apparatus is improved. The structure of the hydrogen production apparatus is simplified.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for hydrogen production method.    DESCRIPTION OF DRAWING(S) - The drawing shows a model of hydrogen production apparatus. (Drawing includes non-English language text)    Hydrocarbon and steam inlet section (1)    Steam-reforming catalyst layer (2)    Non-catalyst layer (3)    Shift catalyst layer (4)    Hydrogen separation membrane (5)    Exit portion (6)
NOVELTY - A carbon monoxide removal apparatus (2) removes carbon monoxide from hydrogen rich reformed gas (B) produced from source gas (A) by using carbon monoxide adsorption agent such as activated alumina and silica gel so as to obtain hydrogen gas (C) to be supplied to fuel cell (3). The removal apparatus has several carbon monoxide adsorption columns (2a,2b) filled with adsorption agents so that adsorption removal operation is performed in one column and stack off gas (D) of fuel cell is circulated under reduced pressure in other columns to reproduce adsorption agent.    USE - Fuel cell system for domestic applications.    ADVANTAGE - The need of using heating and cooling operation for carbon monoxide adsorption columns is prevented while switching the operation of carbon monoxide removal apparatus between carbon monoxide adsorption and carbon monoxide adsorption agent reproduction. Hence the adsorption and reproduction operations can be performed within short cycle time without increasing size of the carbon monoxide removal apparatus and the installation area of the fuel cell system can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a structural view of the fuel cell system.    Carbon monoxide removal apparatus (2)    Carbon monoxide adsorption columns (2a,2b)    Fuel cell (3)    Source gas (A)    Hydrogen rich reformed gas (B)    Hydrogen gas (C)    Stack off gas (D)
NOVELTY - An aliphatic alcohol, fats and oils, fatty-acid alkylester, glycerin and calcium compound are transesterificated in presence of calcium-containing solid catalyst, to obtain a reaction mixture, and the fatty-acid alkylester is removed from the reaction mixture. When the fatty-acid alkylester is contacted with hydroxy-containing property activated carbon, the calcium compound mixed in fatty-acid alkylester is absorbed to hydroxy-containing property activated carbon, and the fatty-acid alkylester is removed. The moisture content of the fatty-acid alkylester is 20-60 mass%.    USE - Manufacture of fatty-acid alkylester for biodiesel fuel.    ADVANTAGE - The fatty-acid alkylester is efficiently manufactured.    DETAILED DESCRIPTION - An aliphatic alcohol, fats and oils, fatty-acid alkylester, glycerin and calcium compound are transesterificated in presence of calcium-containing solid catalyst, to obtain a reaction mixture, and the fatty-acid alkylester is removed from the reaction mixture. When the fatty-acid alkylester is contacted with hydroxy-containing property activated carbon, the calcium compound mixed in fatty-acid alkylester is absorbed to hydroxy-containing property activated carbon, and the fatty-acid alkylester is removed. The moisture content of the fatty-acid alkylester is 20-60 mass%. The hydroxy-containing property activated carbon has pH of 3-7. An INDEPENDENT CLAIM is included for purification of fatty-acid alkylester.
NOVELTY - A solid catalyst comprises charcoal which is made to support alkaline-earth metal oxide.    USE - A solid catalyst for manufacture of biodiesel fuel, and transesterification between oil and fat and alcohol.    ADVANTAGE - The solid catalyst has sufficient catalyst activity, is excellent in recyclability, and has no load to environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a manufacturing method of solid catalyst.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph of amount of base points of catalysts and relationship of biodiesel fuel yield. (Drawing includes non-English language text).
NOVELTY - A gasification catalyst is obtained by slurring a composite material and inorganic binder. The composite material is supported by carrier surface in shape of high dispersion, and contains tungsten salt, cobalt salt and/or molybdenum salt, two or more types of nickel salt, nickel acetate and nickel carbonate, magnesium raw material and calcium raw material.    USE - Catalyst is used for gasifying biomass and sewage sludge using gasification processing system (claimed).    ADVANTAGE - The gasification catalyst has high catalyst activity, and sulfur poisoning-proof property, and is economically manufactured even at low temperature without using noble metal.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of gasification catalyst, which involves mixing magnesium oxide (2) in aqueous solution containing tungsten salt, cobalt salt and/or molybdenum salt and two or more types of nickel salt, nickel acetate and nickel carbonate, reacting, producing composite material (1), drying, dehydrating (3,4), washing, mixing with calcium raw material, obtaining catalyst precursor (5), slurring the obtained catalyst precursor, obtaining catalyst slurry (6), adding inorganic binder or organic binder to the obtained catalyst slurry, producing catalyst slurry containing binder, supporting the catalyst slurry containing binder to the carrier surface, drying and baking; and    (2) gasification processing system, consists of gasification catalyst provided in gasifier which heats and burns organic-type gasifying material.    .    DESCRIPTION OF DRAWING(S) - The drawing shows flowchart of manufacturing process of gasification catalyst. (Drawing includes non-English language text)    Preparation of composite material (1)    Addition of magnesium oxide powder or suspension liquid (2)    Dehydration (3,4)    Preparation of catalyst precursor (5)    Preparation of catalyst slurry (6)
NOVELTY - A catalyst comprises platinum, niobium, tungsten and/or antimony which are supported by tin oxide carrier.    USE - A catalyst for oxidation removal of methane in combustion exhaust gas containing methane, sulfur oxide and excess oxygen (claimed).    ADVANTAGE - The catalyst exhibits high methane degradation ability at low temperature, reduces usage amount of expensive noble metal, has very outstanding resistance, and is excellent in economical efficiency.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) method of manufacturing catalyst involving carrying out impregnation support of aqueous solution of niobium compound, tungsten compound and antimony compound by tin oxide carrier, carrying out impregnation support of aqueous solution of platinum compound after drying and baking; and    (2) method of carrying out oxidation removal of methane in combustion exhaust gas containing methane, sulfur oxide and excess oxygen involving making waste gas contact catalyst at 300-500 degrees C.
NOVELTY - A catalyst is formed by supporting titanium oxide carrier into components chosen from platinum, niobium, tungsten, iridium and antimony. The catalyst removes methane from waste gas containing sulfur oxide and excess oxygen, by oxidation.    USE - Catalyst is used for purification of combustion exhaust gas (claimed) such as methane-fermentation gas and natural gas-type town gas.    ADVANTAGE - The catalyst has high methane oxidation ability at low temperature for long period of time, and economically purifies combustion exhaust gas using reduced amount of noble metals.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of catalyst, which involves impregnating titanium oxide carrier in aqueous solution containing components chosen from platinum, niobium, tungsten, iridium and antimony, drying and baking; and    (2) method for purifying exhaust gas, which involves contacting waste gas and catalyst, and removing methane from exhaust gas.
NOVELTY - The alarm has a detection unit provided in a box body (1). The box body is provided with a function button, a display screen and an alarm lamp connected with a signal processing circuit. An infrared light source (18) and an infrared detector (19) i.e. twin-channel pyroelectric detector, are fixed with internal surfaces of two end closures (6, 7) via supporting bodies (8, 9) and located in a focus position of concave mirror faces of the internal surfaces of the end closures. A dust-proof and water-proof venting cover has a filtering net.    USE - Portable infrared methane gas alarm.    ADVANTAGE - The detection unit is simple, rational and compact in structure, and convenient to process and carry. The alarm has high sensitivity, fast response speed, better stability, high measuring accuracy and wide application range.    DETAILED DESCRIPTION - The filtering net utilizes a polyfluortetraethylene film.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a portable infrared methane gas alarm.    Box body (1)    End closures (6, 7)    Supporting bodies (8, 9)    Infrared light source (18)    Infrared detector (19)
NOVELTY - Biological organic fertilizer is produced by adjusting carbon-nitrogen ratio of pig manure with sawdust as carbon source and fermenting to compost.    USE - Method for producing biological organic fertilizer (claimed).    ADVANTAGE - The method obtains fertilizer having nutrient content of 7% and organic matter content of more than 50%.
NOVELTY - An aerobic composting system comprises temperature-time controlling and recording meter, perforation plate dividing container into upper and lower parts, wind chamber at lower part, composting reactor at upper part having exhaust opening at top, temperature controller at interior of composting reactor having internal temperature sensor and humidity sensor connected to temperature-time controlling and recording meter through lead wires, centrifugal fan, rotor flow meter, ventilation pipe mounted at 1 side of wind chamber, and percolate discharging pipe at bottom of wind chamber.    USE - An aerobic composting system for storing nitrogen-phosphorus and reducing discharge of ammonia in composting of livestock manure (claimed) and producing fertilizer.    ADVANTAGE - The system obtains treated livestock manure being harmless and stabilized, and with improved fertilizing efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of storing nitrogen-phosphorus and reducing discharge of ammonia in composting of livestock manure comprising:    (A) mixing uniformly livestock manure with crushed adjusting agent and packing in composting reactor of aerobic composting system;    (B) feeding magnesium salt solution during mixing of livestock manure with crushed adjusting agent or after packing in composting reactor and mixing uniformly with livestock manure and adjusting agent;    (C) composting at high temperature through produced heat energy;    (D) controlling centrifugal fan to have continuous or intermittent ventilation, and allowing air entering into wind chamber to uniformly pass through stock pile formed by livestock manure, adjusting agent and magnesium salt solution through perforation plate with temperature preset at 60 degrees C by temperature controller; and    (E) monitoring change of humidity.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of aerobic composting system.
NOVELTY - A biological organic fertilizer comprises animal manure, humic acid, straw powder and biological bacteria, prepared by mixing at Kg-weight ratio of 130:30:260:1, sealing in closed container at more than 15 degrees C, fermenting anaerobically for 7 days, taking out mixture, mixing obtained semi-finished product (180 Kg), straw powder (360 Kg) and small quantity of biological bacteria, stirring uniformly, drying at 60 degrees C, packing and storing.    USE - A biological organic fertilizer used for improving crumb structure of soil, decomposing phosphorus and potassium, solidifying nitrogen and shortening growth period of crops.    ADVANTAGE - The fertilizer has simple preparation and increases quality and yield of agricultural products.
NOVELTY - A corrosion-inhibition anti-sludging agent comprises (mg/L) hydroxyethylidene-1,1-diphosphonic acid (0.2-1.2); 2-phosphonobutane-1,2,4-tricarboxylic acid (0.125-1); sulfonic acid polymer (0.14-1.2); maleic acid-acrylic acid copolymer (0.625-5); polyacrylic acid (0-1.6); and copper corrosion inhibitor (0-0.4).    USE - Corrosion-inhibition anti-sludging agent used in circulating cooling water system.    ADVANTAGE - The antisludging agent has good performance in preventing calcium carbonate sediment, can be used at a reduced dosage, and lessens damage to the environment caused by phosphorus emission. The added antisludging agent is not greater than 20 mg/L at normal situation. The total phosphorus content in the circulating water is not greater than 0.5 mg/L.
NOVELTY - A biodiesel is produced by igniting the biomass at the bottom of the furnace and paving a layer of sawdust or chaff; transferring the biomass to a vertical thermal decomposition furnace without prior drying when the biomass temperature reaches 200-300 degrees C; and heating further at above 400 degrees C to obtain biodiesel, wood gas and carbon.    USE - Method of producing a biodiesel (claimed).    ADVANTAGE - The method is low cost.
NOVELTY - Pre-treatment method involves exhausting heavy inorganic substance from an outlet at the bottom of an air current suspension wind selector; sending low-moisture light organic substance separated from air current suspension wind selector into an air dryer to be aired to form garbage fuel; sending high-moisture medium organic substance separated from the air current suspension wind selector into an extruding-desiccation machine; sending organic garbage material after dehydration into the air dryer for further treatment of removing water, and forming garbage fuel.    USE - Pre-treatment method for household garbage used as fuel of e.g. gasification furnace, burning furnace or industrial boiler.    ADVANTAGE - Ensures harmless, reduction and recycling treatment of household garbage by performing environment-friendly treatment of the household garbage.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a household garbage pre-treatment device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a household garbage pre-treatment device.    Light organic outlet (2)    Medium organic outlet (11)    Blowing interface (16)    Medium material suspension region (20)    Light material suspension region (22)
NOVELTY - The hydrogen production system has a water electrolytic cell (3) with electrolytic cell units (7) having same or different hydrogen producing capability. Each electrolytic cell unit is joined to a solar battery (1) through switches within a switch block (2). The solar battery, switch block, water electrolytic cell, water path sub-system (4), and gas path sub-system (5) are joined to a control device (6) through an analogue signal line and a control signal line. The control device drives the electrolytic cell units in different combinations to work according to the power input by solar battery.    USE - System for producing hydrogen by electrolyzing water with solar battery in energy resource fields such as solar energy and hydrogen production.    ADVANTAGE - Ensures automatic control of the capacity of the water electrolytic cell according to power change under the different solar radiation condition to achieve direct matching between the solar battery and water electrolytic cell, and to produce hydrogen by electrolyzing water.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the hydrogen production system.    Solar battery (1)    Switch block (2)    Water electrolytic cell (3)    Water path sub-system (4)    Gas path sub-system (5)    Control device (6)    Electrolytic cell units (7)
NOVELTY - A waste distilled grain of great flavor wine is used by cleaning and preparing the waste distilled grain of great flavor wine; drying the prepared waste distilled grain and controlling water content to 6-15%; grinding obtained product to separate attachment and rice hull; and sieving ground waste distilled grain using sieve with 20-80 meshes of pore diameter.    USE - Method for using waste distilled grain of great flavor wine used as fuel or burnt to make into white carbon black, and for producing animal feed (claimed).    ADVANTAGE - The method makes use of device with less investment. Production cost is low, and quality of the obtained feed is good. Combustion rate of rice hull is high, and quality of rice hull ash is stable.
NOVELTY - Methane gas from biomass resources and compost are manufactured by using airtight fermentation reaction installation (1) where the interior space has flexible gas impermeable sheet material (31) and is filled with coarsely crushed biomass feedstock material, spreading water which contains methane fermentation microbe using a spray nozzle (4) from the upper part of raw material filler (2), extracting sprayed water, advancing methane fermentation reaction by circulating repeatedly, extracting and collecting methane gas and collecting fillers as fermented compost.    USE - Manufacture of methane gas from biomass resources, and compost for large-scale methane production and organic fertilizer.    ADVANTAGE - The reaction installation is low cost, has a simple structure, can be installed easily, utilizes biomass resources effectively and is economically advantageous.    DETAILED DESCRIPTION - Methane gas from biomass resources and compost are manufactured by using airtight fermentation reaction installation (1) where the interior space has flexible gas impermeable sheet material (31) and is filled with coarsely crushed biomass feedstock material, spreading water which contains methane fermentation microbe using a spray nozzle (4) from the upper part of raw material filler (2), extracting sprayed water from the bottom part of fermentation reaction installation, advancing methane fermentation reaction by circulating repeatedly through an external circulatory system and spreading to the upper part of raw material filler, extracting and collecting methane gas from the upper space of fermentation reaction installation and collecting fillers as fermented compost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic explanatory diagram of the manufacture of methane gas and compost.    Fermentation reaction installation (1)    Raw material filler (2)    Waste water (3)    Spray nozzle (4)    Primary crusher (5)
NOVELTY - A reforming system comprises a combustion and reforming reaction unit, a water-gas shift reaction unit and a ceramic board. Each reaction unit includes two plates, a respective channel plate arranged between two plates and the ceramic board. A catalyst layer is formed on the surface of ceramic board. The reformed gas is generated in the combustion and reforming reaction unit using reforming raw material. The generated reformate gas reacts water and carbon monoxide is produced in water-gas shift reaction. A selective oxidation unit is also provided.    USE - Reforming system.    ADVANTAGE - The reforming system improves stability of catalyst by preparing ceramic of small thermal expansion, improves conversion ratio of catalyst and remarkably reduces weight whole system.    DESCRIPTION OF DRAWING(S) - The drawing shows a configuration diagram of the reforming system.
NOVELTY - A water-gas shift reactor comprises a channel plate arranged between two plates, a ceramic board and a fluid inflow port or fluid exhaust port. A catalyst layer is formed on the surface of ceramic board. The high temperature water and reformate gas react in the channel plate.    USE - Water-gas shift reactor.    ADVANTAGE - The water-gas shift reactor improves stability of catalyst by preparing ceramic of small thermal expansion, improves conversion ratio of catalyst and remarkably reduces weight of whole reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows an exploded perspective view of the water gas shift reactor. (Drawing includes non-English language text).
NOVELTY - The electrode array method involves connecting an anode made of stainless steel plate to a cathode made of titanium plate. The water is electrolyzed by supplying power to the electrode. The surface of the electrode is boisterously processed for increasing the generation of brown gas, which comprises hydrogen and oxygen.    USE - Electrode array method for water electrolysis.    ADVANTAGE - The water is electrolyzed by supplying power to the electrode, and the surface of the electrode is boisterously processed for increasing the generation of brown gas, which comprises hydrogen and oxygen, and thus enables increasing the combustion efficiency of the fuel with low heat generation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of an electrode plate surface processing method.
NOVELTY - A stable suspending biomembrane band, composed of a loose layer (2) and a tight layer, is made by first connecting a sleeve (1) to the loose layer made from composite material, woolen material or textile material, connecting the lower part of the loose layer to the compact layer (3) made from composite material, woolen material or textile material, cutting the compact layer into wide bands with a width of 300 to 800 millimeters, arranging a falling sleeve (5) in the gap on the lower end of the compact layer, and arranging a flow curtain (4) in the compact layer.    USE - Stable suspending biomembrane band for ecological water purification. Can also be used for culturing diversified propagation of species as well as treating nitrogen and phosphorus.    ADVANTAGE - When water velocity is accelerated, water can flow through the flow curtain so as to maintain the stability of the compact layer; enabling the biomembrane band to be stabilized in water, which is good for culturing diversified propagation of species. The device also offers a reasonable and scientific structure, which can be simply operated at low cost and offers high efficiency of treating nitrogen and phosphorus and good quality of purified water.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of a stable suspending biomembrane band.    Sleeve (1)    Loose layer (2)    Compact layer (3)    Flow curtain (4)    Falling sleeve (5)
NOVELTY - A fertilizer fuel gas equipment being a fully hermetic equipment comprises a fermenting chamber, a control chamber, and a separating chamber, which are connected to each other in turn.    USE - The fertilizer fuel gas equipment is useful as dustbin for the organic substances, where the excrement from human and animal, straws and proper organic substances are added into it.    ADVANTAGE - The fertilizer fuel gas equipment can export fertilizer according to the requirements and can achieve continuous output of fertilizer. Moreover, it can meet the large and middle excrement treatment factories, slaughter houses and breeding factories; and it can also meet the need of single household in rural areas in organic fertilizer and fuel gas. Additionally, it has strong applicability, high efficiency, and low cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the fertilizer fuel gas equipment.    Feeding hole (1)    Outlet pipe (3)    Filter plate (4)    Duplex control valve (7)    Slope (8)
NOVELTY - Increasing the efficiency of cellulose hydrolysis using a cellulase comprises: (a) combining a cellulosic substrate, a cellulase composition, and recombinant swollenin; and (b) incubating the cellulosic substrate, cellulase composition, and swollenin under conditions conducive to hydrolysis of cellulose, where the presence of recombinant swollenin increases the efficiency of cellulase hydrolysis by the cellulase composition compared to that obtained using a the cellulase composition in the absence of swollenin.    USE - The method is useful for increasing the efficiency of cellulose hydrolysis using a cellulase (claimed).    ADVANTAGE - The method enhances the efficiency of a cellulase n producing sugars from cellulosic biomass using the polypeptide swollenin.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is an enzyme composition comprising: (a) a mixed cellulase composition comprising an endoglucanase, a cellobiohydrolases, and a beta -glucosidase; and (b) recombinant swollenin.
NOVELTY - The device has a screen distributor (6) on the lower part of the shell (1). A gas inlet pipe (4) within the shell has an outlet extending out of the upper part of the shell and penetrating deeply under the distributor. A gas outlet (2) and a water-replenishing hole (3) are on upper part of the shell. The upper part of the distributor is filled with a filler (5) of metal or ceramics. An emptying hole (7) and a liquid level meter (8) are set at the bottom and lower side face of the shell. Level of water in the shell is higher than the distributor to submerge more than half of filler height.    USE - Decoking device for biomass schizolysis.    ADVANTAGE - The device is simple in structure, providing convenience in operation and good decoking effect without danger of air pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of a decoking device.    Shell (1)    Gas outlet (2)    Water-replenishing hole (3)    Gas inlet pipe (4)    Filler (5)    Screen distributor (6)    Emptying hole (7)    Liquid level meter (8)
NOVELTY - A suspending agent comprises (wt.%) avilamycin (0.5-3) and azocyclotin (5-30) as active ingredients, wet dispersing agent (0.5-10), stabilizer (0.05-3), anti-freezing agent (1-5), antifoaming agent (0.2-1) and deionized water (balance).    USE - Suspending agent for preventing insect pests and mites in fruits and vegetables.    ADVANTAGE - The suspending agent is safe to use and has high adhesion rate in the using process with less environment pollution and no medical harm to crops.
NOVELTY - A biological compound fertilizer comprises liquid manure sustained release agent with millipores, biological bacterial fertilizer, high-efficiency organic matter, inorganic nitrogen, phosphorus, potassium, and trace elements.    USE - A biological compound fertilizer.    ADVANTAGE - The fertilizer is rich in nutrient, has good water retention function, and increases survival rate and breeding rate of bacteria, thus balancing growth of crops.
NOVELTY - A copper-containing sewage is biologically repaired by adding probiotics to the sewage containing copper pollutant, growing dayflower, using grown dayflowers as manure when the dayflowers have seeds, moving parts of the dayflower from polluted water, and harvesting the dayflowers to be used as raw materials for distilling deoxynojirimycin.    USE - Method of biologically repairing a copper-containing sewage (claimed).    ADVANTAGE - The method reduces pollution, beautifies the environment, and produces product that can be used as raw materials.
NOVELTY - Methane is prepared by using high-efficiency synthetic gas and controlling the reaction temperature in the first stage reactor to recycle the heat energy released by reaction.    USE - Method of preparing methane (claimed).    ADVANTAGE - The method ensures high conversion rate of the raw materials.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a method of preparing methane. Drawing includes non-English language text.
NOVELTY - Methane is synthesized by taking carbon dioxide as inert gas during synthesis.    USE - Method of synthesizing methane (claimed).    ADVANTAGE - The method obtains methane having carbon monoxide having a concentration of less than 0.2 wt.%; ensures high concentration of the product; produces high-grade steam and hot water; and reduces power consumption.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a method of synthesizing methane. Drawing includes non-English language text.    High-temperature reactors (5, 10)    Middle-temperature reactor (14)
NOVELTY - Composite methanol fuel comprises methanol (60-90 vol.%) and petroleum solvent (balance).    USE - Composite methanol fuel for automobile (claimed).    ADVANTAGE - The composite methanol fuel is inexpensive; and has simple preparation method, low cost, and lower consumption compared with prior art methanol fuel consumption. The automobile can easily be started at low temperature.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a preparation method of composite methanol fuel comprising mixing methanol and petroleum solvent in a container; and stirring uniformly to obtain composite methanol fuel.
NOVELTY - An absorbing agent is prepared by taking attapulgite clay as a raw material, crushing and adding in an acid solution, modifying at constant temperature of 60-90 degrees C for a proper time, washing until pH value is 7, and then drying and baking to obtain the absorbing agent.    USE - An absorbing agent for absorbing and separating carbon dioxide from a gas containing methane and/or nitrogen gas (claimed).    ADVANTAGE - The absorbing agent can be simply and easily prepared; and has big absorbing capacity to carbon dioxide, and obvious absorbing and separating effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of preparing the absorbing agent.
NOVELTY - The test device has a hydrogen absorbing bottle connected with a comb tube beam. A heating electrical stove is arranged outside of the hydrogen absorbing bottle, and the heating electrical stove is provided with a temperature holding outer housing, a sensor and a temperature control part. The hydrogen absorbing bottle is provided with a sample air inlet/outlet, an absorbing response bottle, an oxidizing and reducing agent and a heating electric stove. The heating electric stove is in contact with the hydrogen absorbing bottle.    USE - Test device for measuring hydrogen and methane amount in fuel gas.    ADVANTAGE - The test device has better air tightness, achieves improvement in measuring precision, separately measures the hydrogen and the methane amount, and eliminates system error.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a test device.
NOVELTY - Invention may be used in chemical instrument making. On foundation of reactor body 1 they install rod 9 with reservoir 12, which comprises initial catalyst. Reactor is tightly closed with cover 5, and reactor body 1 is heated up to temperature of reaction execution, afterwards it is filled with carbonic acid gas. Then reactor is opened and cover 5 is installed, which contains in cavity 7 ampoule 6 with water sample retained in cavity by plug-fixator 8 with openings for water outlet and fixed additional second rod 10 with reservoirs 11 on it filled with zinc dust. Methane produced as a result of synthesis is supplied to gas proportional counter.    USE - Instrument making.    ADVANTAGE - Simplified operation of reactor, reduced power and process costs, improved efficiency and accuracy of executed measurements.
NOVELTY - Lignocellulosic biomass pretreatment involves preparing a hydrolysate from lignocellulosic biomass and injecting 1-10 mu per ml of enzymes into the hydrolysate to polymerize fermentation inhibitory compounds, which are precipitated from the hydrolysates. The precipitates are removed and hydrolysate is fermented. The enzyme reacts with a phenolic compound and hydrolysate, where the phenolic compound is polymerized.    USE - Method for pretreating lignocellulosic biomass for preparing biofuel (claimed).    ADVANTAGE - The lignocellulosic biomass pretreatment method is eco-friendly, halogen free, effectively removes the microorganisms, and ensures high productivity of biofuel.
NOVELTY - Active carbon granules containing non-woven shoe material comprise non-woven shoe material, where active carbon granules are uniformly and firmly absorbed between fibers of non-woven shoe material.    USE - Active carbon granules containing non-woven shoe material.    ADVANTAGE - The non-woven shoe material has good ventilation, strong ability of absorbing and inhibiting bacterial, and ability of absorbing and decomposing harmful substances; releases anions, prevents dermatophytosis and moisture bidirectional regulation; and is capable of removing undesirable and abnormal odor.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a manufacturing method of the active carbon granules containing non-woven shoe material comprising:    (A) dipping active carbon powder with clean water, adding resin glue, mixing and pouring resin glue containing active carbon into mixed serous fluid with calcium carbonate powder, water and environment-friendly auxiliary agent, and uniformly agitating;    (B) pouring mixed serous fluid into serous groove, dipping prefabricated non-woven fabrics into serous groove, mixing with serous fluid, and removing auxiliary agent serous fluid on surface via a dual-roller; and    (C) drying slurry-removed non-woven fabrics into drying tunnel, rolling via hot pressing roller and cold pressing roller, and cutting from machine.
NOVELTY - Purification of an organic matter and gases comprises carrying out vaporization by adding an absorbing agent; passing the gas flow through series of devices for removing acid or alkali, removing specific impurities, and removing high-boiling impurities; and condensing.    USE - Method for the purification of an organic matter, e.g. chloroethylene, methyl chloride, narcotine, curafume, fluorotrichloromethane, monochlorodifluoromethane, epoxy ethane, butane, isobutene, methylamine, dimethylamine, trimethylamine, ethylamine, ketene, vinyl ether, methyl mercaptan, propylene, butylenes-(1), or butylenes-(2); and gases including nitrogen, hydrogen, oxygen, chlorine, or inert gases (claimed).    ADVANTAGE - The method achieves liquid organic matter with high purity, and convenient for the organic matters whose boiling points are a bit lower than the room temperature.    DESCRIPTION OF DRAWING(S) - The drawing is a flow diagram of the method for the purification of the organic matter and gases.    Heater (6, 15)    Cooler (12)    Cold trap (13)    Thermograph (16)    Condenser (20)
NOVELTY - The present invention relates to a production system for hydrogen-rich gaseous fuel and its production process. The production system for hydrogen-rich gaseous fuel comprises a water vapor feeding device for transporting water vapor; an air feeding device for transporting air; an alcohol vapor feeding device for transporting alcohol vapor; and a heat insulation reactor of which the exterior has a heat insulation wall. Moreover, a reformer is disposed in the heat insulation wall and a catalyst bed is disposed in the reformer. The mixture gas formed by water vapor, air and alcohol vapor is transported to the catalyst bed in the heat insulation reactor to generate hydrogen after reaction. The production process transports the mixture gas formed by water vapor, air and alcohol vapor to the catalyst bed of the heat insulation reactor, and outputs hydrogen from the heat insulation reactor after reaction. The present invention can reduce the volume and the catalyst cost of the conventional hydrogen generation reactor.
NOVELTY - The invention provides a DC steam plasma torch device and its electrode etching suppression method, which can use any kind of gas as the working gas, wherein the use of steam can greatly reduce the generation of nitrogen oxide and produce clean heat source of high temperature, high-plasma density, high-energy density and high chemical activity, so as to effectively process harmful wastes or convert the harmful wastes into organic substance for producing synthesize gas and stable the recyclable lava, thereby to fully broaden the recycling efforts. The present invention provides the torch which can be operated for a long time periods, and reduce the thermal load of the electrode and alleviate its melting and etching rate, and further increase the effective mass of the electrode for being melted and etched by controlling the working gas field when an arc root performs a large-area cyclic movement on the inner wall surface of the electrode, so as to prolong the electrode service life for increasing its maintenance cycle, thereby effectively reduce the operating cost of torque related to the manufacturing operations and increase the reliability and usability of the plasma processing system.
NOVELTY - The system has a zinc electrode provided with a current collector, where a gas-releasing electrode and the current collector are separately arranged in a zinc compound-containing aqueous electrolyte. A liquid input passage and a liquid output passage are connected with a bump and an electrolyte container. A water replenishing passage is arranged in the electrolyte container, and a gas-liquid separator is connected to the electrolyte container, where the range of the distance between the current collector of the zinc electrode and the gas-releasing electrode is 1 millimeters-30 millimeters.    USE - Electrochemical system for use in a gas engine for producing and storing hydrogen. Can also be used for energy storage and burning promotion.    ADVANTAGE - The system can be used to largely and periodically produce hydrogen in a lower cost, and has a long lifetime. The system can be conveniently scaled up and used in a gas engine for saving petrol and decreasing the discharge.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of an electrochemical system.
NOVELTY - Converting a carbonaceous material to a desired product comprising methane, methanol and/or dimethyl ether involves gasifying the carbonaceous material at temperature of at least 700 degrees C to form synthesis gas; and flowing the synthesis gas through two reaction zones in a microchannel reactor in contact with catalysts to form the desired product.    USE - For converting carbonaceous material comprising non-food carbonaceous material and food resource, such as coal, oil, biomass, and solid-waste, to desired product comprising methane, methanol and/or dimethyl ether (claimed).    ADVANTAGE - The process is in expensive, converts waste products (e.g. trash and garbage) into methane, methanol and/or dimethyl ether on a relatively small scale of 50-500 cubic meters of gas or liters of liquid per day; converts carbonaceous materials such as municipal solid waste to methane, methanol and/or dimethyl ether on a scale of thousands or tens of thousands of cubic meters of gas or liters of liquid per day, thus it is adapted for use with small and larger scale operations.    DETAILED DESCRIPTION - Converting a carbonaceous material to a desired product comprising methane, methanol and/or dimethyl ether, involves: (a) gasifying the carbonaceous material at temperature of at least 700 degrees C to form synthesis gas; (b) flowing the synthesis gas through a first reaction zone in a microchannel reactor at a first reaction temperature in contact with a first catalyst to form an intermediate product composition comprising synthesis gas and the desired product; and (c) flowing the intermediate product composition through second reaction zone in the microchannel reactor at second reaction temperature in contact with second catalyst to form the desired product; where the approach to equilibrium for conversion of the synthesis gas in the first and second reaction zones is at least 5%, and exchanging heat between the reaction zones and heat exchangers.
NOVELTY - The biomass gasifier (B) has a gasification reaction apparatus (10) equipped with an observation port (16a) for watching throwing-in part (7), in which biomass is thrown, from the outside. A biomass remover (20) removes the biomass (S) blocked in the throwing-in part.    USE - Biomass gasifier for gasifying biomass and producing clean high-calorie gas used as fuel of engine for electric power generation.    ADVANTAGE - Enables steady supply of biomass for efficient production of gas since clogging of biomass in the throwing-in part can be confirmed through the observation port and biomass blocked in the throwing-in part can be removed.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the biomass gasifier.    Throwing-in part (7)    Gasification reaction apparatus (10)    Observation port (16a)    Biomass remover (20)    Biomass gasifier (B)    Biomass (S)
NOVELTY - Preparation of pre-sulfurized natural latex radical slow release fertilizer involves using polysaccharide chitosan and sodium alginate as package material for shaping the fertilizer by packaging, and using pre-sulfurizing natural latex as package material with different slow release speed in a certain range by controlling the crosslink density of the pre-sulfurized natural latex radical.    USE - Preparation of pre-sulfurized natural latex radical slow release fertilizer used for saline lake area.    ADVANTAGE - The method efficiently and safely provides pre-sulfurized natural latex radical slow release fertilizer. The pre-sulfurized natural latex radical slow release fertilizer is environmental-friendly.
NOVELTY - An aqueous emulsion comprises (wt.%) flusilazole (2-30); a solvent (5-20); a surfactant (5-15); an antifreezing agent (1-6); and water (balance).    USE - An aqueous emulsion, i.e. a bactericide, for treating apple scab and powdery mildew.    ADVANTAGE - The aqueous emulsion is environmentally friendly.
NOVELTY - The cell has a fuel storage unit for storing fuel supplied to an anode, boil-off part, and an actuator. A temperature sensor measures temperature of a membrane electrode assembly, and a controller controls opening and closing operation of the actuator according to a signal delivered from the temperature sensor. The anode, electrolyte film and a cathode are laminated in the membrane electrode assembly. The actuator opens and closes fuel flow between the boil-off part and the fuel storage unit.    USE - Vapor such as methanol vapor and ethanol vapor, fuel feeding type fuel cell for use in an electricity generating set.    ADVANTAGE - The inner temperature of the cell is maintained in an optimal range, thus improving the electrogenesis efficiency of the cell, and hence improving the performance of the cell.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for controlling temperature of a vapor fuel feeding type fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a vapor fuel feeding type fuel cell.'(Drawing includes non-English language text)'
NOVELTY - A catalyst for thermal decomposition of water comprises sodium-yttrium type zeolite by which ion exchange was carried out with monovalent alkali metal ion in one part is adhered or coated on surface of fiber inactive at heat resistance.    USE - A catalyst for thermal decomposition of water.    ADVANTAGE - The catalyst continuously obtains hydrogen as fuel such as fuel cell directly by thermal decomposition by using water as raw material inexpensively and stably, and has high yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a thermal decomposition method of water involving filling reaction tube with catalyst for thermal decomposition of water, making inside of a reaction tube into high temperature and pressure reduction atmosphere, inducing water vapor to reaction tube, and decomposing water vapor into hydrogen gas and oxygen gas.
NOVELTY - The biomass gasification furnace has ash leading-out port (38) connected with the bottom of a furnace main body (1). Stirring gears (30) are provided on a stirring shaft (26) and arranged inside the furnace main body. A motor (14) for driving the stirring shaft is provided outside the furnace main body. A material loading cabin (3) is connected at the front part of a feed port (11) and controls entry of materials. An ash leading-out cabin (39) is connected between the ash leading-out port and the bottom of the furnace main body (1), and used for controlling the exit of ashes.    USE - Biomass gasification furnace.    ADVANTAGE - Enables continuous supply of gas when adding material in the furnace and leading out ashes from the furnace. Increases burning efficiency and fixes the location of the gasification layer in the furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows the cross-sectional view of the biomass gasification furnace.    Furnace main body (1)    Material loading cabin (3)    Feed port (11)    Motor (14)    Stirring shaft (26)    Stirring gears (30)    Ash leading-out port (38)    Ash leading-out cabin (39)
NOVELTY - The straw gasification furnace includes spiral air holes (4) that are opened on the pipe wall at the inner end of an air intake pipe (2). A screw (5) is in bolt connection with the upper end of a furnace main body (1). A rotating handle (6) is provided at the upper end of the screw. An agitating rod (7) is provided at the middle of the screw. A spiral blade (8) is provided at the lower part of the screw.    USE - Straw gasification furnace.    ADVANTAGE - Enables convenient operation of the straw gasification furnace, which performs continuous and uniform combustion of straw to produce gas.    DESCRIPTION OF DRAWING(S) - The drawing shows the partial cross-section explanatory view of the straw gasification furnace.    Furnace main body (1)    Air intake pipe (2)    Spiral air holes (4)    Screw (5)    Rotating handle (6)    Agitating rod (7)    Spiral blade (8)
NOVELTY - The environment-friendly dry distillation device has a condenser (3) with an air outlet end connected to the air inlet end of a pump (4) and a pyroligneous storage tank (9). The air outlet end of the pump is connected to the air inlet end of a liquid drop separator (5). The air outlet end of liquid drop separator is connected to an air cabinet (7) via pipe (6), and to the pyroligneous storage tank. The air cabinet is connected to the bottom of a combustion chamber (10) by pipe. The bottom of the combustion chamber is connected to a liquefying air tank (8).    USE - Environment-friendly dry distillation device for earth kiln biomass.    ADVANTAGE - Provides environment-friendly dry distillation device having a compact structure and rational design. Provides an energy-saving, environment-friendly and efficient dry distillation device for earth kiln biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows the explanatory drawing of the environment-friendly dry distillation device for earth kiln biomass.    Condenser (3)    Pump (4)    Liquid drop separator (5)    Pipe (6)    Air cabinet (7)    Liquefying air tank (8)    Pyroligneous storage tank (9)    Combustion chamber (10)
NOVELTY - The biomass gasification furnace has a tar outlet (14) arranged at the bottom of a gas cleaning chamber (13) placed at lowest layer of furnace body (4). A furnace body rack (15) is welded to bottom of furnace body. A gas outlet (16) is set on gas cleaning chamber. A gas guiding pipe (17) communicates with the gas cleaning chamber and an upper gas guiding port (18). A fan interface is welded to the furnace body. The intermediate section of the fan interface communicates with a flame nozzle (8), and its ends are exposed from the furnace body.    USE - Biomass gasification furnace for generating combustible gases, e.g. carbon monoxide, methane and hydrogen gas, which are supplied for daily cooking, heating, warming and bathing.    ADVANTAGE - Produce good quality combustible gas. Provides a biomass gasification furnace having a compact structure and all-around functionality. Enables convenient operation of the biomass gasification furnace, which can be operated year-round without any pollution to the environment.    DESCRIPTION OF DRAWING(S) - The drawing shows the explanatory view of the biomass gasification furnace.    Furnace body (4)    Flame nozzle (8)    Gas cleaning chamber (13)    Tar outlet (14)    Furnace body rack (15)    Gas outlet (16)    Gas guiding pipe (17)    Upper gas guiding port (18)
NOVELTY - A heating stove for straw gasification furnace comprises a lower part of combustion chamber that is a hollow cavity for placing the gas cooker head, and an upper part that is a flue. The hot water pipes arranged in criss-cross with two ends interconnected with the water sleeve are installed in the inner cavity of the combustion chamber. A valve is installed in the upper port of the flue. A fire pipe is installed at one side of the flue.    USE - Heating stove for straw gasification furnace.    ADVANTAGE - Solves the problem that the straw gasified gas in the countryside is simplex in utilization for taking the straw gasified gas as energy source for heating. Provides heating stove which is simple in structure, convenient in installation and high in thermal efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows the front view of the heating stove for straw gasification furnace.
NOVELTY - A straw furnace comprises a material feeding hopper (2) that is welded at the top of a furnace (1) while having a viewing window (4) and a sealing cover (3). A material discharge hole (5) is lower than a discharge pipeline hole (8). An ash hole (6) is in the lower position of the furnace. The air holes (7) are formed at the bottom of the furnace.    USE - Straw furnace for providing fuel gas to family, factory and mine in community and rural area.    ADVANTAGE - Solves the problem that the fuel cannot be fully supplied and the supplement effect is not good for the lack of pressure in the power-down condition by the working principle of air pressure pump to save energy and be environmentally friendly. Saves investment of small units and improves life condition, quality and level.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of the straw furnace.    Furnace (1)    Material feeding hopper (2)    Sealing cover (3)    Viewing window (4)    Material discharge hole (5)    Ash hole (6)    Air holes (7)    Discharge pipeline hole (8)
NOVELTY - A movable soft biogas generator comprises a gas bag (1) and a material port (2); where the bottom of the end head of the air bag and the material port are connected by a soft tube (3); the upper hole of the material port is provided with a sealing cover (4) capable of opening; and a safety valve (5), a pressure gauge (6), and a biogas outlet pipe (7) are provided at the top of the air bag.    USE - The movable soft biogas generator is useful for treating waste and producing biogas and organic fertilizer.    ADVANTAGE - The movable soft biogas generator has light weight, is mobile, and appropriate for any environment. Moreover, it is efficient, continuous, integrative, and low in cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the movable soft biogas generator.    Gas bag (1)    Material port (2)    Soft tube (3)    Sealing cover (4)    Safety valve (5)    Pressure gauge (6)    Biogas outlet pipe (7)
NOVELTY - A single cell is manufactured. A gas is flown through the gas flow path of the single cell and the characteristic value reflecting pressure loss is calculated. The single cell is mounted on a to-be-stacked single cell to form a stacked structure. The characteristic value of single cell is determined and compared with a tolerance range. When the characteristic value is within the tolerance range, the stacked structure is used for further stacking of single cells.    USE - Method for manufacturing fuel cell e.g. polymer electrolyte fuel cell. Can also be used in solid oxide fuel cell.    ADVANTAGE - The pressure loss difference between the adjacent fuel cells is suppressed and the shortage of gas supply to the cells is prevented. The fall in voltage of single cell by the lack in gas flow volume is prevented and the fall in performance is suppressed. By stacking the single cells based on the characteristic value and irrespective of the number, the manufacturing efficiency is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows the flowchart illustrating the fuel cell manufacturing process. (Drawing includes non-English language text)
NOVELTY - Cement is produced by pretreating organic garbage into granular fuel; sending granular organic garbage fuel to fuel decomposing furnace of cement production device to decompose; and volatilizing organic component as gas phase, oxidizing and firing in cement kiln.    USE - Method for producing cement (claimed).    ADVANTAGE - The method uses organic garbage in replaced of fire coal, thus reducing cost of the cement.
NOVELTY - A fuel composition comprises (wt.%) methanol (90-95), hydrogen peroxide solution (2-5), and carburetor cleaning agent (3-5).    USE - A fuel composition for use in internal-combustion engine, preferably motorcycle or automobile.    ADVANTAGE - The composition reduces fuel cost, saves energy, has lower sulfide compound content thus reducing sulfur oxide in the smoke, and is environment-friendly.
NOVELTY - An alcohol raw material (1) which contains abundant moisture content is subjected to extraction process using an ether-type solvent (3), so that the solvent in alcohol is removed, to obtain absolute alcohol.    USE - Purification of alcohol used for manufacture of gasohol (claimed).    ADVANTAGE - The purification method of alcohol is carried out with reduced steam consumption and energy, and gasohol in high yield is produced economically using the alcohol.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of process flow of absolute alcohol and manufacture of gasohol. (Drawing includes non-English language text)    Alcohol raw material (1)    Ether-type solvent (2)    Extract (3)    Stripper alcohol recycle (4)    Drain (5)    Gasoline (6)    Gasohol (7)
NOVELTY - A solid alkali catalyst is new.    USE - Solid alkali catalyst for synthesizing biodiesel (claimed).    ADVANTAGE - The catalyst has high catalytic activity and good reuse property; and has mild reaction condition without environment pollution.    DETAILED DESCRIPTION - The solid alkali catalyst of formula N'y/M 2+1-x(M 3+) xO 2+x-y/2is new.    N'=halogen anion;    M 2+=bivalent metal cation;    M 3+=trivalent metal cation;    x=0.25-0.45; and    y=0.05-0.3.    INDEPENDENT CLAIMS are included for:    (1) a preparation method of the biodiesel synthesizing catalyst; and    (2) use of solid alkali catalyst for synthesizing biodiesel comprising (A) putting oil and low-carbon alcohol at ratio of 3-6:1 and the catalyst (0.3-3 wt.% of reactant) into 3-mouth flask, increasing temperature to 30-120 degrees C under stirring condition and reacting for 1-6 hours; (B) separating solid alkali catalyst, dividing layers so that upper layer is provided with biodiesel and unreacted alcohol while lower layer is provided with glycerin; and (C) decreasing pressure at upper layer to separate and recover the alcohol and obtain biodiesel, where low-carbon alcohol comprises methanol, alcohol, glycol, propanol alcohol, isopropyl alcohol, n-butylalcohol and/or tert-butyl alcohol, and oil comprises plant oil, animal oil, waste oil and hogwash oil.
NOVELTY - Making methanol via synthesis gas from organic wastes involves transforming wastes into gas mixture (M1) containing carbon dioxide and monoxide and hydrogen by blowing oxygen, water vapor, tar and polluted water in fixed bed gasifying generator. Combustion of purified M1 in gas engine provides electric energy for producing oxygen by decomposing water, which is then blown in generator and together with hydrogen produced ensures required carbon monoxide to hydrogen proportion in reactor. Carbon dioxide is extracted from synthesis gas and transformed to methanol by mixing with hydrogen.    USE - For producing methanol via synthesis gas from organic wastes consisting of solid municipal waste, waste water sludge and biomass.    ADVANTAGE - The process produces methanol via synthesis gas from organic wastes consisting of solid municipal waste, waste water sludge and biomass.    DETAILED DESCRIPTION - Producing methanol via synthesis gas from organic wastes involves transforming wastes consisting mainly of solid municipal waste, waste water sludge and biomass into a gas mixture containing carbon dioxide, carbon monoxide and hydrogen by blowing oxygen, water vapor and tar produced in the process, as well as polluted water in a fixed bed gasifying generator. Combustion of the purified gas mixture in a gas engine provides the electric energy required for producing oxygen by the decomposition of water, which is then blown in the generator and together with the hydrogen produced ensures the required carbon monoxide to hydrogen proportion in the methanol reactor. Carbon dioxide is extracted from the synthesis gas by water scrubbing, stored and then transformed to methanol after mixing with hydrogen gained using electric energy produced by cyclically available renewable energy.
NOVELTY - A biomass is liquefied by physically mixing 30-95 wt.% of methanol (80-99 v/v%), 0.1-3 wt.% of catalyst, and biomass pulverized into 20-100 meshes; conveying them into reaction device; stirring them uniformly; heating them up to 250-350 degrees C and pressing them to 8-18 MPa, and keeping this state for 0.5-6 hours; cooling them; and separating solid and liquid to obtain liquid fuel oil of biomass.    USE - Method for biomass liquefaction used to prepare fuel oil (claimed) for spark-ignition engine.
NOVELTY - A synthetic ammonia gas production briquette comprises 85-90 pts. fine anthracite and 10-15 pts. organic composite adhesive. The organic composite adhesive comprises straw, humic acid and sodium hydroxide solution at a weight ratio of 2.5-5.5:6.5-15.5:82.0-88.0.    USE - A synthetic ammonia gas production briquette.    ADVANTAGE - The synthetic ammonia gas production briquette has widely available materials, low production cost, high activity and cold strength and heat intensity. The addition of biomass reduces burning point and discharge of smoke and dust. Burn-off rate is improved. Consumption of coal per ton ammonia is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of synthetic ammonia gas production briquette comprising    (A) air drying straw, cutting and milling to 2-3 cm and crushing anthracite to less than 3 mm;    (B) adding sodium hydroxide solution to reactor, then adding straw, stirring and raising temperature, adding humic acid when temperature reaches 90-95 degrees C, and reacting for 40-60 minutes at 90-95 degrees C to obtain organic composite adhesive; and    (C) mixing organic composite adhesive with anthracite, uniformly mixing, forming and drying.
NOVELTY - Coal-based clean methane is synthesized by complementing synthetic gas obtained through gasification with hydrogen (H2) to adjust ratio of H2 and carbon monoxide (CO).    USE - Method for synthesizing clean methane (claimed) including generating butyl octanol.    ADVANTAGE - The method recycles materials, saves energy, lowers material consumption and reduces emission.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic flow diagram of coal-based clean methane synthesis. (Drawing includes non-English language text).    Methane gasifying-tower preheater (6)    Steam generator (7)    Cooler (8)    Moisture separator (9)    Circulating machine (11)
NOVELTY - This invention relates to a method of preparing health-care raw material containing syringin extracted from Siberian ginseng by the extraction of syringin from Siberian ginseng, comprising extracting syringin by semi-continuous pressurized fluid for 45 minutes, with the use of a pressurized water extraction process. This invention improves the time-consuming conventional extraction methods in which organic solvent is used. Therefore, this invention characterizes in that it can prevent doing harms to the human body and the environment pollution.
NOVELTY - Grasses can be properly planted on a mountain, a riverside, lakes, seas, cliff side, in a pond, a reservoir, a rill and a river of national land with an area of 9.6 million km2. The grasses planted on an obscure wasteland have higher yield than any other prairie; and can enrich the living condition and relieve pressure of every Chinese in 1.3 billion people by 1.3 mu m by planting the grass for feeding the cattle on the wasteland.    USE - Grasses for feeding ten million of cattle, where beef and milk are delicious foods for people (claimed). The grasses can also be used for feeding a rabbit, a fish, a pig and a goose.    ADVANTAGE - The grasses are good green feed; can grow to be tender grasses with a 50-cm height in 24 hours under guaranteeing condition of warm climate and enough water; have high yield; are environmental source for human from nature; can bring large material well-being for human by using these resources.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a methane that can be used in an industry. A rural methane tank of China has gone through the course of development for more than 50 years. It is constructed by taking a single family as a main body, uses much construction materials and has less methane tank efficiency, so that the methane must be used in an industry like a size of a river area and a natural administrative village. A cattle breeding field scale can be decided based on grass production quantity. The methane tank can be constructed in a suburb of urban and natural village to produce methane. The methane tank construction in the village can solve employment problem, can greatly improve efficiency of the methane tank, and can use waste in methane well.
NOVELTY - An equivalent methane concentration (EMC) of gas stream is increased by providing membrane having feed side and permeate side; passing raw gas stream comprising methane and carbon dioxide; passing oxygen-containing stream across the permeate side; withdrawing from feed side a residue stream having second EMC that is higher than the first EMC; and withdrawing from permeate side a permeate stream that is enriched in carbon dioxide compared with oxygen-containing stream.    USE - Method of increasing equivalent methane concentration (EMC) of gas stream for fuel.    ADVANTAGE - The process provides residue stream with enriched methane and oxygen, and EMC value that enables to be flared or combusted by mixing with ordinary air; and is completely passive, and operated purely in sweep mode, i.e. with total gas pressure on both sides of membrane is the same. Thus, having membrane permeation that is driven solely by concentration gradients, and does not need compressors or vacuum pumps.    DETAILED DESCRIPTION - Increasing EMC of gas stream involves providing membrane having feed side and permeate side, which is selectively permeable to carbon dioxide over methane and to oxygen over nitrogen; passing raw gas stream comprising methane and carbon dioxide, and having first EMC, across feed side; passing oxygen-containing stream across the permeate side; withdrawing from feed side a residue stream having second EMC that is higher than the first EMC; and withdrawing from permeate side a permeate stream that is enriched in carbon dioxide compared with oxygen-containing stream.
NOVELTY - The method involves measuring pressure drop across a recirculation pump (30) and temperature of anode recirculation gas. Pressure drop across an anode side of a fuel cell stack (12) is calculated. Volume flow of gas flowing through the anode side is calculated as a function of calculated pressure drop, temperature and the measured pressure drop. Density of gas flowing through recirculation loop is calculated based on the volume flow, measured pressure drop and speed of pump. Percentage of hydrogen in the gas is calculated based on the density, temperature and the measured pressure drop.    USE - Method for determining concentration of hydrogen in anode recirculation loop of a fuel cell stack in a fuel cell system (claimed) that is utilized in a vehicle.    ADVANTAGE - The method enables accurate determination of the hydrogen concentration in the anode recirculation loop, thus enabling the fuel cell stack to be operated under optimized conditions, and hence maximizing the performance of the fuel system.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a fuel cell system, comprising a fresh hydrogen source.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a anode recirculation in a fuel cell system.    Fuel cell system (10)    Fuel cell stack (12)    Hydrogen source (14)    Mixing junction (16)    Recirculation pump (30)
NOVELTY - Development of biological pretreatment of waste organic solids comprises mixing solid organic waste to be treated, with the remainder serving as a source of microorganisms for the anaerobic digestion; and adding a new biological agent constituted for mature compost for 24 hours at atmospheric pressure and room temperature.    USE - The method is useful for development of biological pretreatment of waste organic solids; and for biogas production in industrial plants (all claimed).    ADVANTAGE - The method can operate withy higher organic loading rates fed into the system to increase the capability of processing and/or facilities management; improves the net production of methane and the speed of digestion; and it does not require huge financial investments as it only requires recirculation using an aerobic composting unit pre-mixed with anaerobic digesters.
NOVELTY - The gasifier (1), for biomass material, has a grid (29) in the lower section (7) of a housing (3) to support the biomass. A vertical shaft (17) rotates the grid on a horizontal plane.    USE - The gasifier is for converting the biomass into a liquid fuel.    ADVANTAGE - The grid rotation allows residue to drop through without stoppages and allows an unimpeded gas flow through the biomass.    DESCRIPTION OF DRAWING(S) - The drawings show a schematic view of the gasifier and schematic sections of it.    gasifier (1)    housing (3)    fireproof lining (5)    lower housing section (7)    shaft drive flange (15)    shaft (17)    grid (29)
NOVELTY - The fixed-bed gasification reactor (1), to produce a pyrolysis gas from biomass and other organic materials, has a vertical screw (2) within the cylindrical interior (13) to give an even distribution and mixing action to the biomass. The screw rotates around an axis (21) between the cover (141) and the base (142) through a drive motor (22). The screw is composed of perforated or grid plates. The vertical screw also passes through the upper biomass drying section (4).    USE - The fixed-bed gasification reactor is for the production of a pyrolysis gas from biomass and other organic materials, especially wood, using steam and air as the gasification agents.    ADVANTAGE - The reactor is particularly suitable for flexible and/or soft materials.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fixed-bed gasification reactor.    reactor (1)    vertical screw (2)    drying zone (4)    burner (5)    steel mantle (11)    cylindrical interior (13)    vertical axis (21)    drive motor (22)    combustion chamber (51)    cover (141)    base (142)
NOVELTY - Method for treating a gas stream containing 80-99 vol.% of nitrogen and 1-10 vol.% of methane, comprises subjecting the gas stream to regenerative thermal oxidation process, which makes the methane depletion.    USE - The method is useful for treating a gas stream containing nitrogen and methane.    ADVANTAGE - The method meets the current or future applicable environmental regulations.
NOVELTY - The method involves forming hydrogen pump (1) that is provided with anode and cathode chambers (13,14) which are provided in anode and cathode electrode side of electrolyte substrate (10), and are arranged confronting anode and cathode electrodes (11,12). The object gas containing hydrogen is introduced into anode chamber and hydrogen in the gas is decomposed at anode electrode. The hydrogen produced at cathode electrode is emitted so that emitted hydrogen is sucked by vacuum pump (7) so as to promote the separability of hydrogen from cathode electrode.    USE - Gaseous-phase recycled-waste-water matter separation method.    ADVANTAGE - The performance of hydrogen pump is improved by separating hydrogen from cathode electrode such that generation amount of hydrogen can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for gaseous-phase recycled-waste-water matter separation apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen separator. (Drawing includes non-English language text)    Hydrogen pump (1)    Vacuum pump (7)    Electrolyte substrate (10)    Anode electrode (11)    Cathode electrode (12)    Anode chamber (13)    Cathode chamber (14)
NOVELTY - High temperature steam electrolysis cell (100) comprises hydrogen electrode which electrolyzes steam and generates hydrogen and oxide ion, oxygen electrode (130) which generates oxygen and consists of catalyst layer (132) and current collection layer (134) of electronic conductive mixed oxide and cerium complex oxide, and oxygen ion permeable substrate (120) which consists of electrolyte between the hydrogen and oxygen electrode.    USE - High temperature steam electrolysis cell for producing hydrogen and oxygen gas.    ADVANTAGE - Has excellent coating film peeling resistance due to thermal expansion, low electrolytic voltage and inexpensive.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the oxygen electrode. (Drawing includes non-English language text).    High temperature steam electrolysis cell (100)    Substrate (120)    Oxygen electrode (130)    Catalyst layer (132)    Current collection layer (134)    Separator (170)
NOVELTY - The hydrogen gas discharge/occlusion unit (10) has latent heat storage material provided in the circumference of hydrogen storage alloy (14). A closed circulatory system is provided in which hydrogen storage alloy is heated using heat of solidification generated by latent heat storage material (16), so that latent heat storage material is dissolved using heat generated by hydrogen storage alloy.    USE - Hydrogen gas discharge/occlusion unit for fuel cell electric power generation system. Can also be used in temporary storage of hydrogen.    ADVANTAGE - Discharge/occlusion of specific quantity of hydrogen gas can be performed at high efficiency by hydrogen gas discharge/occlusion unit of simpler structure, by effective utilization of heat generated by hydrogen storage alloy, by providing closed circulatory system in which hydrogen storage alloy is heated using heat of solidification generated by latent heat storage material, so that latent heat storage material is dissolved using heat generated by hydrogen storage alloy, while improving overcooling prevention characteristics, without the need of supply of energy from external apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the hydrogen gas discharge/occlusion unit. (Drawing includes non-English language text)    Hydrogen gas discharge/occlusion unit (10)    Airtight container (11)    Hydrogen storage alloy chamber (12)    Hydrogen storage alloy (14)    Latent heat storage material chamber (15)    Latent heat storage material (16)
NOVELTY - The apparatus (1000) has the support stands (200,300) that are formed on the base portions (104,106) so as to support a rotating mechanism (500) and a cell lamination mounting portion (400). The fuel cell laminated structure (10) positioned on the mounting portion is pressed by a press mechanism (430) when rotating the cell lamination mounting portion with respect to rotating shaft of rotating mechanism along the direction perpendicular to positioning direction of fuel cell laminated structure upon manually turning the rotating handle (520) of rotating mechanism.    USE - Fuel cell manufacturing apparatus.    ADVANTAGE - The cell lamination mounting portion can be rotated easily so that the manufacturing efficiency of the fuel cell manufacturing apparatus is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing method of fuel cell.    DESCRIPTION OF DRAWING(S) - The drawings show the perspective views of fuel cell manufacturing apparatus. (Drawing includes non-English language text)    Fuel cell laminated structure (10)    Base portions (104,106)    Support stands (200,300)    Cell lamination mounting portion (400)    Press mechanism (430)    Rotating mechanism (500)    Rotating handle (520)    Fuel cell manufacturing apparatus (1000)
NOVELTY - Transesterification of animal and vegetable oil used as raw material is carried out using a catalyst and alcohol to produce biodiesel fuel. Glycerin by-product produced during manufacture of biodiesel fuel is supplied to ground or ground water contaminated with organic halogen compound. Anaerobic microbe capable of decomposing organic halogen compound and contained in contaminated ground or ground water is activated, and contaminated ground or ground water is purified. Thus, recycling of glycerin by-product is enabled.    USE - Method for recycling glycerin by-product produced during manufacture of biodiesel fuel.    ADVANTAGE - The glycerin by-product produced during manufacture of biodiesel fuel is easily and economically recycled.    DESCRIPTION OF DRAWING(S) - The drawing shows the graph illustrating time dependent change of organic halogen compound concentration by glycerin by-product. (Drawing includes non-English language text)
NOVELTY - Purification of biodiesel, comprises: providing a crude biodiesel containing at least a glycoside; reacting the crude biodiesel with an adsorbent containing at least a smectite-silica gel mixed phase exhibiting a specific surface area of greater than 120 m2/g, a total pore volume of greater than 0.35 ml/g, a silicon content, calculated as silicon dioxide, of at least 60 wt.%; and separating a purified biodiesel from the adsorbent.    USE - The method is useful for the purification of biodiesel, preferably for removing steryl glycoside from the biodiesel.    ADVANTAGE - In the method, even very small amounts of glycosides, preferably steryl glycosides can be removed from the biodiesel. The method is simple and inexpensive, so that the method can be used even for fine purification of biodiesel, which already has a very high quality.
NOVELTY - Urban sewage treatment device comprises insulating tank, dirt collector, biogas generating tank, and gas collector. A gap is provided between the insulating tank and the biogas generating tank. The dirt collector comprises sewage separating device and water outlet. Detachable active carbon filter plate and microporous film are arranged on the sewage separating device.    USE - Urban sewage treatment device.    ADVANTAGE - Compared with the prior art, the urban sewage treatment device effectively removes pollutants from domestic sewage; avoids pipeline plugging; and turns product that causes secondary pollution into useful material.
NOVELTY - The furnace has a flue outlet hole opened on a water sealing tank (2.3) of the lower furnace body (2) upper edge; roller wheels (2.5) and dynamic motor (2.1) externally equipped in the outside edge (2.2) of water sealing tank. The outside lower edge of the water sealing tank cover (1.2) of the upper furnace body (1) is set on the roller wheel. The flue outlet hole is linked to the flue outlet pipe (2.6). The bottom of the lower furnace body is equipped with an air inlet port (2.8) linked to a fan (2.0). An oxygen distributing pipe (3) is set between the flue outlet pipe and the fan.    USE - Biomass combined gasification furnace for the gasification combustion for varieties of straws and biomass fuels.    ADVANTAGE - The furnace is featured with original structure, simplicity, practicality, convenient use and excellent effect in environment protection and energy saving.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic perspective view of the biological environmental-friendly high-efficiency energy-saving biomass combined gasification furnace. (Drawing also includes non-English language text).    Upper furnace body (1)    Water sealing tank cover (1.2)    Lower furnace body (2)    Fan (2.0)    Dynamic motor (2.1)    Outside edge (2.2)    Water sealing tank (2.3)    Roller wheels (2.5)    Flue outlet pipe (2.6)    Air inlet port (2.8)    Oxygen distributing pipe (3)
NOVELTY - The furnace has a water jacket (2.3) provided between the inner furnace wall (2.2) and the outer furnace wall of the stove; and a water outlet pipe (2.4) and a water return pipe (2.5) connected with the water jacket and provided on the outer wall of the water jacket. The water outlet pipe and the water return pipe are connected with the radiator (3). The kitchen range is provided at the upper opening of the stove.    USE - Multifunctional straw gasification furnace for cooking stove.    ADVANTAGE - The furnace is multifunctional, energy-saving and environmentally-friendly, and uses waste. The furnace is used conveniently.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of the structure of the ecological environmentally-friendly efficient energy-saving multifunctional straw gasification furnace.    Inner furnace wall (2.2)    Water jacket (2.3)    Water outlet pipe (2.4)    Water return pipe (2.5)    Radiator (3)
NOVELTY - Compound fertilizer comprises urea, ammonium phosphate, potassium chloride, organic material and bentonite as the main materials to be processed into granular fertilizer. It comprises (mass%) organic material (15), nitrogen (10-12), phosphorus oxide (4-5) and potassium oxide (10-12). The nitrogen/phosphorus oxide/potassium oxide ratio is 2-3:1:2-3. The total nutrient content is 25-28%. The organic material is lees, turf, waste bamboo, and/or treated paper mill sludge. The organic fertilizer is formed by fermenting and maturing the organic material.    USE - Compound fertilizer for bamboo (claimed) useful in papermaking.    ADVANTAGE - The compound fertilizer increases bamboo yield by 15-20%, where the yield per acre is increased by more than 210 kg. It supplies needed nutrient elements according to the growth feature of the bamboo. It provides safety, high efficiency, and low investment. It meets the needs of rapid growth and stable yield of the bamboo.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing the fertilizer comprising:    (A) pre-treating organic materials by cultivating flies on the lees to let the fly maggot stay in the lees to increase the content of organic nitrogen in the lees, and treating the paper mill sludge by cultivating earthworm or by composting;    (B) weighing the materials based on mixture ratio: urea (99-22 pts. wt.), ammonium phosphate (9-11 pts. wt.), potassium chloride (18-21 pts. wt.), lees (23 pts. wt.) or turf (26 pts. wt.) and bentonite (2-14 pts. wt.);    (C) drying and crushing the ingredients;    (D) mixing the ingredients in a high-speed mixer, granulating the mixture, drying, cooling and separating the granules; and    (E) packing the granules after inspection, and then inspecting to obtain the finished product.
NOVELTY - The furnace has a fuel gas outlet (7), a porous medium (13), a fuel gas pipe (11) and a fuel gas outlet (12) form a fuel gas conveying pipe i.e. U-shaped pipe or spiral coil pipe, in a material cabin (8), where the material cabin is internally equipped with the fuel gas outlet (7). The porous medium is selected from heat insulating ceramic, dolomite, olivine, clay mine, charcoal, carbon metal compound and nickel-based tar catalyst.    USE - Cracking biomass gasification furnace inside tar furnace.    ADVANTAGE - The furnace enhances heat storing, filtering and catalyzing functions of the porous medium to reduce tar content in the fuel gas, so that the tar content in biomass is reduced, and conversion rate and thermal value of the gas are improved. The fuel gas passing through the fuel gas pipe and burning area do not burn with the air in the burning area, thus avoiding technical difficulty of lower absorption type that the flue gas is easy to be burned. The burning area can heat the fuel gas through the fuel pipe.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a cracking biomass gasification furnace inside tar furnace.    Fuel gas outlets (7, 12)    Material cabin (8)    Fuel gas pipe (11)    Porous medium (13)    Secondary air inlet (14)
NOVELTY - The furnace has two flue gas outlets (7, 10) fixed on side faces of a hopper (6) and a reducing chamber (11). Spiral flow and heat guiding blades (9) are welded on side face of a burning chamber (3) and fixed in a flue gas collecting chamber (8). Side faces of a hopper (5), the reducing chamber and a furnace wall (13) form the flue gas collecting chamber. A side wall surface of the hopper (6) is equipped with the flue gas outlet (7). A side wall surface of the reducing chamber is equipped with the flue gas outlet (10).    USE - Counter-flow biomass gasification furnace for use in a rural area.    ADVANTAGE - The furnace avoids the technical difficulty of lower absorption type. The tar in the fuel gas passing through the reducing area is converted, so that the tar content in biomass is reduced and the conversion rate and thermal value of the gas are improved. The furnace has small resistance, high conversion rate, easy operation and low tar content. The furnace can utilize different kinds of biomass such as straw, chaff, sawdust and peanut shells to make flue gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a counter-flow biomass gasification furnace.    Burning chamber (3)    Hoppers (5, 6)    Flue gas outlets (7, 10)    Flue gas collecting chamber (8)    Spiral flow and heat guiding blades (9)    Reducing chamber (11)    Furnace wall (13)
NOVELTY - The device has a carbonization chamber (1) provided in an upper-segment, and a main gasification chamber (2) formed in a middle-segment. An ash chamber (3) is placed at a lower-segment. The upper, middle and lower segments are separated by grids (9) and heat-storing grates (18). A radiation cylinder (13) surrounds a periphery of the gasification chamber that is composed of a heat conductive cylinder (14), lower-segment heat-preserving layer (22) and an outer wall (4). An air hole (11) is formed at a side wall of a furnace body on an upper portion of the gasification chamber.    USE - Vertical cylindrical structured upper-absorption-type household biomass gasification device.    ADVANTAGE - The device does not use external igniting heat source, and has high igniting speed. The device provides high temperature in gasification central zone, reduces the content of tar and reduces the heat loss of the furnace body. The device has high gasification efficiency. The flame sealing time of the gasification furnace is long. The device has simple and compact structure, simple operation and low running cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of an upper-absorption-type household biomass gasification device.    Carbonization chamber (1)    Main gasification chamber (2)    Ash chamber (3)    Outer wall (4)    Grids (9)    Air hole (11)    Radiation cylinder (13)    Heat conductive cylinder (14)    Heat-storing grates (18)    Lower-segment heat-preserving layer (22)
NOVELTY - The furnace has a biomass material feeding port is connected with a gasification chamber by a material changer. Multiple material distributors (10) are installed in a middle part of a rectangular gasification reaction chamber (11), where the reaction chamber is placed in a middle part of the furnace. A chain type grate (12) is placed at a bottom part of the reaction chamber, where the chain type grate is equipped on a delivering belt of a driving roller and a driven roller. Multiple material distributors are uniformly distributed and placed above the chain type grate.    USE - Grate type gasification furnace for gasifying agriculture and forestry biomass material.    ADVANTAGE - The furnace has scientific and rational structure. The furnace replaces a screen plate that fixes gap movement of the gasification furnace by the chain type grate that runs continuously, so that the furnace is convenient to use and maintain. The furnace can cut the agriculture and forestry biomass material into rod-shaped or sheet material, thus avoiding crashing of the material into grain, and enabling smooth gasification to generate combustive gas, so that the furnace can feed, prepare carbon and supply gas in a continuous and steady manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a grate type gasification furnace.    Material distributors (10)    Rectangular gasification reaction chamber (11)    Chain type grate (12)    High-temperature carbon outlet (13)
NOVELTY - An electric power supply mechanism has an iron core (2), primary and secondary coils (3,4) that are installed on the outer side of a hydrolyzing device main structure (1). The primary and secondary coils are wound around the iron core. The alternating current (AC) power is converted into direct current (DC) power by a rectifier (13).    USE - Apparatus for supplying electric current to electrode of hydrolyzing apparatus (claimed) for fuel cell.    ADVANTAGE - The hydrolyzing effect can be increased reliably and electric power generation efficiency can be improved effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for hydrolyzing apparatus has a hydrogen electrode (5) made of nickel, that is provided in an oxygen retention chamber. An oxygen electrode (6) installed in an electrode apparatus, is filled with the particulate manganese.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the electric current supply apparatus.    Hydrolyzing device main structure (1)    Iron core (2)    Primary coil (3)    Secondary coil (4)    Hydrogen electrode (5)    Oxygen electrode (6)    Rectifier (13)
NOVELTY - A biomass is conveyed to an entrained-bed-gasification furnace (130) by an air flow conveyance process and gasified in the furnace, to generate gas which is then cooled. A portion(s) of generated gas after performing cooling process is used as carrier gas. The temperature of gas used as carrier gas is more than temperature of gas obtained after carrying out cooling process.    USE - Gasification method.    ADVANTAGE - The gasifier produces large amount of heat emission using a portion of gas as carrier gas without generating the problem of piping by tar.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for gasifier (100), which has a material supply apparatus (110) for supplying the biomass as raw material to entrained-bed-gasification furnace, carrier-gas supply apparatus (120) for supplying carrier gas, cooling device (140) for cooling the gas, temperature control apparatus (160) for heat-retaining or heating the cooled gas. Using temperature control apparatus, portion(s) of generated gas cooled using the cooling device is maintained at a temperature higher than the temperature of generated gas after cooling. Portion(s) of gas is used as carrier gas for carrier-gas supply apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of gasifier. (Drawing includes non-English language text).    Gasifier (100)    Material supply apparatus (110)    Carrier-gas supply apparatus (120)    Entrained-bed-gasification furnace (130)    Cooling device (140)    Temperature control apparatus (160)
NOVELTY - The apparatus (100) has a filtration part (3) connected to a combustion chamber (1) for collecting combustion gas i.e. methane, and a ventilation fan (2) that supplies combustion air to the chamber via an air supply pipe (P1) and an exhaust gas pipe (P2). The filtration part is filled with a down space part, where the combustion gas is flowed out via a repower piping (P3) by opening a lower pressure valve according to inner pressure of the down space part. A freight air line (P4) communicates with the air supply and exhaust gas pipes, and an open valve (V) is fixed in the exhaust gas pipe.    USE - Combustion gas gathering apparatus for use in an indoor residential area.    ADVANTAGE - The apparatus utilizes combustible rubbish to generate heat energy, thus increasing energy recycling modulus of the combustible rubbish. The combustible gas is reused as exhaust gas to generate fuel gas, thus increasing energy recovery rate. The exhaust gas is passed through aqueous solution of the filtration part, thus reducing harmful components and lightening environmental contamination by the exhaust gas. The concentration of oxygen contained in the combustion gas is increased through the freight air line, and the filtration part efficiently performs separate collection of the combustion gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a combustion gas gathering apparatus.    Air supply pipe (P1)    Exhaust gas pipe (P2)    Repower piping (P3)    Freight air line (P4)    Open valve (V)    Combustion chamber (1)    Ventilation fan (2)    Filtration part (3)    Combustion gas gathering apparatus (100)
NOVELTY - The multi-functional movable device has a condenser (N1) and a vacuum device (10) which are connected to valves by pipelines. A mixing device has a biofuel tank (13), a base oil tank (14), a finished oil tank (15) and a shock tube mixer (18) connected with each other by pipelines, valves, pipeline pumps and mounted on the movable device.    USE - Multi-functional movable device for producing biofuel.    ADVANTAGE - Offers simple, inexpensive and convenient to use multi-functional movable device.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of a multi-functional movable device.    Vacuum device (10)    Biofuel tank (13)    Base oil tank (14)    Finished oil tank (15)    Shock tube mixer (18)    Condenser (N1)
NOVELTY - The hydrogen delivery pipe network has a hydrogen delivery pipe that projects upwards, and connected to an inverse U-pipe. A regulation valve is set on the high-level horizontal pipe of the inverse U-pipe. The hydrogen delivery pipe is connected to the hydrogen escape pipe and valve. The height of the hydrogen escape pipe is less than the height of the regulation valve.    USE - Hydrogen delivery pipe network for electrolysis bath.    ADVANTAGE - Ensures accumulation of water in the hydrogen regulation valve. Ensures stable chlorine and hydrogen pressure difference. Enhances protection of ion membrane of the subsequent device, while reducing accidental stop caused by the chlorine and hydrogen pressure difference undulation.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of the hydrogen delivery pipe network.
NOVELTY - A hydrogen gas generator comprises a reaction chamber (26) for receiving a solid reactant, and having a reaction product separator impermeable to the solid reactant and a spring for biasing reactant products against the separator; a liquid reactant dispenser for storing a liquid reactant such that dispensed liquid reactant reacts with the solid reactant in the reaction chamber to produce hydrogen gas and a waste product that are permeable through the separator; and a product collector for collecting hydrogen gas and waste product that have passed through the separator.    USE - Hydrogen gas generator, i.e. fuel cartridge for supplying hydrogen gas to fuel cell system used in portable electronic devices, e.g. personal digital assistants, mobile phones or entertainment devices. The fuel cell system can also be used for providing heat and electrical power to personal apparel, such as jacket.    ADVANTAGE - The hydrogen gas generator can contain the caustic fuel solution and prevent leakage, especially when the portable fuel cell system will be used in close proximity to humans.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram of fluid flow inside the fuel cartridge.    Connector sub-assembly (22)    Outer and inner bags (25, 27)    Reactor chamber (26)    Hydrogen collection membrane (32)    Acid solution pump (52)
NOVELTY - Preparing a mixture of biofuels comprising fatty acid esters and a glycerol ether mixture from fatty substance and ethanol, comprises: (a) transesterifying of vegetable or animal oil by alcohol, in the presence of a catalyst made of strong solid Bronsted acid characterized by a differential heat ( greater than or equal to 150 KJ/mol) of ammonia absorption, to obtain esters of fatty acid and glycerol; and (b) etherifying the obtained glycerol by alcohol in the presence of the catalyst to obtain glycerol ether, where the steps of (a) and (b) take place simultaneously.    USE - The process is useful for preparing the mixture of biofuels.    ADVANTAGE - The process can be simply and easily carried out without any expensive steps, hence cost effective.
NOVELTY - A deposit containing hydroxide, oxide and/or carbonate of nickel, magnesium and aluminum compounds is added into surface of carrier and baked, to obtain catalyst.    USE - Manufacture of catalyst used for modification of hydrocarbon such as liquefied petroleum gas, light naphtha, heavy naphtha, naphtha, gasoline, kerosene, light oil, heavy oil, alcohol, ether, biodiesel fuel and vegetable oil for manufacture of hydrogen for fuel cell (all claimed) for motor vehicle.    ADVANTAGE - The method efficiently provides catalyst.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for modification of hydrocarbon which involves using the catalyst.
NOVELTY - Device for processing starch manufacture waste water produced from starch factory, has storage tank (3) which holds only the low concentration protein waste water produced in the purification process of a secondary decanter juice (X2) and/or starch which is the starch manufacture waste water, anaerobic-treatment tank (4) which uses the storage completion waste water discharged from storage tank and carries out methane fermentation, and aerobic-treatment tank (5) which carries out the aerobic treatment of the fermentation processed liquid of the anaerobic-treatment tank.    USE - The device is useful for processing starch manufacture waste water produced from starch factory (claimed), and producing methane.    ADVANTAGE - The methane fermentation is carried out stably. The stabilization of starch manufacture waste water is facilitated.    DETAILED DESCRIPTION - Device for processing starch manufacture waste water produced from starch factory, has storage tank (3) which holds only the low concentration protein waste water produced in the purification process of a secondary decanter juice (X2) and/or starch which is the starch manufacture waste water for a predetermined retention temperature and holding time, anaerobic-treatment tank (4) which uses the storage completion waste water discharged from storage tank as a fermentation stock solution and carries out methane fermentation, and aerobic-treatment tank (5) which carries out the aerobic treatment of the fermentation processed liquid of the anaerobic-treatment tank. An INDEPENDENT CLAIM is included for a method for processing starch manufacture waste water produced from starch factory.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the device for processing starch manufacture waste water. (Drawing includes non-English language text)    Storage tank (3)    Anaerobic-treatment tank (4)    Aerobic-treatment tank (5)    Secondary decanter juice (X2)
NOVELTY - A water vapor modification catalyst contains noble metal component consists of ruthenium, rhodium or platinum in alumina support, and rare earth metal. The product of the noble metal quantitative formula in mass% contained in the catalyst and noble metal component dispersion degree in % is greater than or equal to 100, and the noble metal component dispersion degree is less than or equal to 70%.    USE - Water vapor modification catalyst for hydrogen production (claimed).    ADVANTAGE - Fall of catalyst performance by carbon deposition is suppressed, modification reaction start at low temperature is attained, obstruction of modifier by active deterioration of modification catalyst or caulking is suppressed, long-term hydrogen production becomes possible, performance decrement by thermal deterioration of modification catalyst is reduced, hydrogen production is economical, durability of modifier is improved, modifier structure is simplified and cost reduction is attained.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) manufacture of water vapor modification catalyst for hydrogen production involving introducing rare earth metal on alumina support by impregnating, baking in 600-800 degrees C in the presence of oxygen and reduction processing in liquid phase at 65-100 degrees C; and    (2) hydrogen production method involving using fuel oil for hydrogen production and water vapor modification catalyst for hydrogen production and starting water vapor modification reaction in the modification part at less than or equal to 500 degrees C to obtain product containing hydrogen.
NOVELTY - Solid fine granule components (12) containing carbon and having size of millimeter range are pre-mixed to an organic sludge (10). The organic sludge comprising dispersed solid fine granule components is injected to a dryer (3), dry-processed, and the sludge is stirred with a stirring paddle in a heating space.    USE - Dry treatment of organic sludge such as activated sludge and surplus sludge discharged from waste treatment plant and foodstuff factory, used as fuel in combustion installation of thermal-power-generation boiler.    ADVANTAGE - The method enables dry treatment of organic sludge economically, and suppresses adhesion of the organic sludge to dryer by mixing uniformly solid fine granule components and organic sludge.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for dry processing system of organic sludge, which has dryer with an injection portion of organic sludge, heating space to dry the organic sludge and stirring paddle to stir the organic sludge in the heating space, and a pre-mixer (2) to mix solid fine granule components and organic sludge, and the discharged mixture from the pre-mixer is injected to the injection portion of the dryer.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the organic sludge drying processing system. (Drawing includes non-English language text)    Pre-mixer (2)    Dryer (3)    Boiler (4)    Organic sludge (10)    Solid fine granule component (12)
NOVELTY - An introduction unit (24) introduces breathe-out air into collection box (12). A detection unit is coupled to the carbon nano-tube (CNT) air sensors (40a-40c) provided in the collection box for detecting the change of electrical resistance of CNT air sensors. The exhaustion units (28,29) are provided in the collection box for discharging the air inside the collection box. The surface modification of CNT structure is performed by chemical substance such as acetone, pentane and nitrogen monoxide in breathe-out air.    USE - Breathe-out air sensing apparatus for use in treatment of diseases such as diabetes, and health care.    ADVANTAGE - The specified chemical substance in the breathe-out air can be measured by simple operation with high accuracy and high sensitivity. The user can able to judge the health condition daily by sensing the breathe-out air.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the breathe-out air sensing apparatus.    Breathe-out air sensing apparatus (10)    Breathe-out air collection box (12)    External-air introduction unit (24)    Exhaustion units (28,29)    CNT air sensors (40a-40c)
NOVELTY - Rapidly composting organic waste comprises adding regulator to organic waste to adjust water content to 30-65%, putting pretreated material in ventilated fermentation tank, adjusting carbon and nitrogen content by adding nitrogen containing compound, fermenting, adding nitrogen and oxygen, and fermenting for 1-60 days.    USE - Method of rapidly composting organic waste (claimed).    ADVANTAGE - The method is suitable for large scale composting.
NOVELTY - Landfill gas is deep purified by removing nitrogen gas and oxygen through pressure swing adsorption.    USE - Method of deep purifying landfill gas for preparing methane (claimed).    ADVANTAGE - The method is simple with compact equipment and low operation cost, does not utilize catalyst to hydrogenate and deoxidate which avoids mixing of hydrogen gas in purified methane, removes organic impurities and obtains methane having purity of greater than or equal to 99%.
NOVELTY - The methanol recovery device for producing biodiesel oil from waste vegetable oil and animal oil is comprised of an enamel reactor (1) connected above the condenser (2). The condenser is connected below a buffer pot (3) which is connected below enamel reactor and above a spiral cooler. The condenser is connected with the spiral cooler (4) and the spiral cooler is connected above the refrigerator (5).    USE - Methanol recovery device for producing biodiesel oil from waste vegetable oil and animal oil.    ADVANTAGE - Provides device which sends uncooled methanol to the spiral cooler to form methanol liquid which can be recycled. Improves utilization factor of methanol.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a methanol recovery device.    Enamel reactor (1)    Condenser (2)    Buffer pot (3)    Spiral cooler (4)    Refrigerator (5)
NOVELTY - Sewage sludge is dried by accelerating the activity of photosynthesis microbe, Actinomyces or yeast, Bacillus natto, by mixing a greater than or equal to 20% volume ratio wood chips to sewage sludge with 80-90% moisture content and heat fermentation.    USE - Drying of sewage sludge for fuel e.g. boiler fuel (claimed).    ADVANTAGE - The process is efficient, economical and sewage sludge is reduced, easy to handle and can be utilized as fuel.
NOVELTY - Pig manure compost is prepared by mixing pig manure (1 ton) having water content of 70-75% produced from large-scale pig farm, filler (70-150 Kg) consisting of sawdust and/or straw, rotten pig manure compost (40-70 Kg) and bamboo charcoal particles (30-90 Kg) having grain diameter of 1-3 mm in compost groove, treating in static forced draft ventilation at 20-30 m3/(hour.ton), and rotting for 30-36 days.    USE - Method for preparing pig manure compost (claimed).    ADVANTAGE - The method has fast heating up and dehydration, reduced composting time, reduces nutrient loss in compost, is convenient to use without secondary pollution and low in cost.
NOVELTY - A degradable controlled release fertilizer is made by drying, crushing, screening, mixing and extruding fermented waste slag and fertilizer at a weight ratio of 45-65:35-64 to obtain columned fertilizer particle having 6-12 mm diameter and 10-20 mm length.    USE - A degradable controlled release fertilizer (claimed).    ADVANTAGE - The fertilizer has compact coating on its surface, and is environmentally friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing degradable controlled release fertilizer comprising drying fermented waste slag until water content is not greater than 20%, crushing and screening obtained powder to not greater than 2 mm grain size, screening fertilizer using 2-mm pore size sieve, taking the powder with not greater than 2 mm grain size, uniformly mixing obtained fermented waste slag with the fertilizer powder, and extruding.
NOVELTY - A phycomycetes mixed microorganism preparation, where the microorganism preparation is prepared by sterile pure Scenedesmus, Burkholderia cepacia GS3C, Sphingomonas GY2B, pyrene degrading bacteria GP3, Pseudomonas GP3A, and Pandoraea ponmenusa GP3B; the sterile pure Scenedesmus is sterilized and purified; the preserving number of GS3C is CCTCC M 207169; the preserving number of GY2B CCTCC M 206019; the preserving number of GP3B CCTCC NO: M 207166; and the preserving number of GP3 CCTCC NO: M 207166, is new.    USE - The phycomycetes mixed microorganism preparation is useful for repairing the water petroleum pollutant and processing waste water organism (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is the preparation method of phycomycetes mixed microorganism preparation above.
NOVELTY - A catalyst comprises metal oxide chosen from titanium oxide, zirconium oxide, magnesium oxide, vanadium oxide, niobium oxide, molybdenum oxide, tungsten oxide, manganese oxide, iron oxide, aluminum oxide, cobalt oxide and/or nickel oxide, and metal hydroxide chosen from potassium hydroxide, sodium hydroxide, lithium hydroxide, magnesium hydroxide, beryllium hydroxide and/or calcium hydroxide.    USE - Catalyst for hydrogen producing apparatus, hydrogen fueled engine system and hydrogen burner system (claimed).    ADVANTAGE - The catalyst is inexpensive and efficiently collects hydrogen.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) catalyst manufacturing apparatus comprising mixing kettle for melt mixing metal oxide and metal hydroxide, adhesion board where melted mixture is adhered, and heat treatment furnace which accommodates adhesion board and heat processes mixture;    (2) hydrogen-producing apparatus (40) comprising steam generation apparatus (41) which generates superheated steam, catalyst storage apparatus (42) which accommodates catalyst, water vapor circulation system for returning water vapor, hydrogen or oxygen in steam generation apparatus or catalyst storage apparatus;    (3) hydrogen fueled engine system which generates and sends hydrogen gas to hydrogen fueled engine; and    (4) hydrogen burner system comprising catalyst storage apparatus which accommodates catalyst and discharges high temperature steam which is exhaust gas from hydrogen burner which burns hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the systems of hydrogen-producing apparatus.    Hydrogen-producing apparatus (40)    Steam generation apparatus (41)    Catalyst storage apparatus (42)    Water tank (44)    Sealing casing (45)
NOVELTY - An automatic transfer-storehouse device for compost comprises a storehouse orbit, a machine orbit, a travel switch, a frame, a driving device, a road wheel, a ground orbit, and a stop pin; where the machine orbit can be adjusted; and the stop pin is set on the ground orbit.    USE - The automatic transfer-storehouse device is useful for compost (claimed).    ADVANTAGE - The automatic transfer-storehouse device precisely achieves abutting joint with orbit by special design compared with current technology; where it can carry out automatic transfer-storehouse for compost turner without controlling by human beings at site. Moreover, in utlizing the automatic transfer-storehouse device, the phenomenon that the compost turner can not get in transfer-storehouse machine normally or the accidents of side turning and creeping down due to insufficient abutting joint degree of accuracy of orbit will not occur.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the automatic transfer-storehouse device for compost.
NOVELTY - The purifier has a mixed fuel gas input tube introduced from a top part of a cooling water box and communicated to a mixed gas chamber by perforating the water box. A water mist purifying box is internally equipped with a fume input tube whose upper end is connected to a fume output tube of a straw gasification furnace. An upper part of the mist purifying box is equipped with a mixed fuel gas outlet connected to the mixed fuel gas input tube within a water cooling tar purifying box. A lower part of the mist purifying box is equipped with a purified water overflow pipe.    USE - Purifier for a straw gasification furnace.    ADVANTAGE - The purifier carries out the secondary purification of the straw gasification fuel gas for treatment of the tar and harmful gas within the fuel gas, and improves the burning effect of the fuel gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a purifier.
NOVELTY - The generator has an electrode core (8) with an anode electrode (8a) and cathode electrode (8b) electrically connected to power supply (B) through lead wire (9). The connection portion (C) formed by connecting the anode electrode and cathode electrode with lead wire is arranged below a cylindrical embedding structure (10) made of non-electroconductive synthetic resin.    USE - Active hydrogen water generator installed in bathtub and water tank.    ADVANTAGE - Since the connection portion of the electrodes is not exposed in water, the electrical connection failure between the electrodes is avoided and earth-leakage can be prevented. Also, the generative capacity of hydrogenous water can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of the active hydrogen water generator. (Drawing includes non-English language text)    Electrode core (8)    Anode electrode (8a)    Cathode electrode (8b)    Lead wire (9)    Cylindrical embedding structure (10)    Power supply (B)    Connection portion (C)
NOVELTY - Tar content reduction involves contacting gas obtained from gasification process with a catalyst containing noble metals. The noble metal is selected from platinum, palladium, rhodium, iridium, osmium, ruthenium or rhenium. The tar includes a mixture of cyclic and polycyclic aromatic hydrocarbons.    USE - Method for reducing tar content in gases resulting from a biomass gasification process of carbon-containing starting material.    ADVANTAGE - The tar content reduction method enables to reduce the tar content in gases from biomass gasification process having improved efficiency in simple manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for producing synthetic gas, which involves using catalyst containing noble metals.
NOVELTY - Tar content reduction involves contacting gas obtained from gasification process with a catalyst containing noble metals. The noble metal is selected from platinum, palladium, rhodium, iridium, osmium, ruthenium or rhenium. An element is used in combination with another noble metal or nickel in case of platinum. The gas is not brought into contact with a catalyst on zirconium basis prior to the contact with the catalyst containing noble metals.    USE - Method for reducing tar content in gases resulting from a biomass gasification process of carbon-containing starting material.    ADVANTAGE - The tar content reduction method enables to reduce the tar content in gases from biomass gasification process in simple manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for producing synthetic gas, which involves using catalyst containing noble metals.
NOVELTY - The bigmass gasification stove has flame collecting shades (13,14) which are set on the stove head (9). The air inlet holes and the heat-preserving ring (11) are set on the flame collecting shades. The heat separating layer (10) and the heat-preserving layer (15) are set on the periphery of the stove head. The upper and lower outer shades (12,16) are set on the exterior of the stove head.    USE - Bigmass gasification stove for use in warming and cooking in northern area.    ADVANTAGE - Provides the bigmass gasification stove, in which the biomass fuel gas enters directly the gas inlet pipe without filtering and reflowing to combust, and liquid such as tar is combusted fully without generating residue and bad odor and pollution. Simplifies the structure of the gasification stove, thus making the gasification stove more convenient to use.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the bigmass gasification stove.    Stove head (9)    Heat separating layer (10)    Heat-preserving ring (11)    Outer shades (12,16)    Flame collecting shades (13,14)    Heat-preserving layer (15)
NOVELTY - The pyrolysis method involves performing each load of the reactions of biomass pyrolysis and gasification in the same place and same time, so that part of the heat required for pyrolysis is obtained by a gasification of the other.    USE - Pyrolysis method for biomass and gasification of coal obtained by pyrolysis reactor.    ADVANTAGE - The pyrolysis method ensures power-efficient procedure, that requires no previous grinding and is performed in a reactor in a simple manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of a pyrolysis method.
NOVELTY - A solid fuel comprises minute particle mixture of coconut charcoal powder and palm charcoal dust having particle size of 0.1 mm, interparticle mixture of coconut charcoal powder and palm charcoal dust having particle size of 5-0.15 mm, and igniting composition containing mixture of adhesive comprising corn starch and tapioca starch and yellow soil powder comprising barium, sodium nitrate and alum.    USE - A solid fuel.    ADVANTAGE - The solid fuel is excellent in quality and mean temperature, and can maintain high temperature from initial.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing method of solid fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of processing method of solid fuel using palm charcoal and coconut charcoal. (Drawing includes non-English language text).
NOVELTY - Apparatus comprises a mixer (52) equipped with a mixture tub (40), an organic waste inlet tube (42), and a pivot axis (52-1). A screw type agitating vane (52-2) is formed in the boundary surface of pivot axis. A vertical type dry anaerobic digester (50), a sludge culture medium (60) for cultivating anaerobe and a sludge inlet tube (62) connected to sludge culture medium are provided. A biogas reservoir (70) for storing biogas generated in vertical type dry anaerobic digester is also provided. The organic solid industrial waste and organic liquid waste are mixed in mixture tub.    USE - Apparatus for producing biogas.    ADVANTAGE - The apparatus requires less establishment area as vertical type dry anaerobic digester is used, and ensures smooth production of biogas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the apparatus. (Drawing includes non-English language text).    Mixture tub (40)    Organic waste inlet tube (42)    Vertical type dry anaerobic digester (50)    Mixer (52)    Pivot axis (52-1)    Screw type agitating vane (52-2)    Sludge culture medium (60)    Sludge inlet tube (62)    Biogas reservoir (70)
NOVELTY - Apparatus (100) for generating hydrogen involves electrolytic bath (130) into which an electrolyte solution (135) is injected, anode (110) placed inside the electrolytic bath to generate an electron, cathode (120) to generate hydrogen by receiving the electron from anode, gelling agent (170) to gel the electrolyte solution such that fluidity of the electrolyte solution is reduced.    USE - For generating hydrogen useful in a fuel cell (claimed) in small portable electronic devices include the Polymer Electrolyte Membrane Fuel Cell (PEMFC), Direct Methanol Fuel Cell (DMFC).    ADVANTAGE - The apparatus prevents an electrolyte solution from reversely flowing when hydrogen is generated so that the humidity of the hydrogen can be decreased, and prevent the electrolyte solution from leaking to the outside when an electrolytic bath moves. Simultaneously, hydrogen can be additionally generated from the electrolyte solution which has been preserved without being released. Consequently, the entire amount of the generated hydrogen can be increased. The fluidity of the electrolyte solution is reduced, so that when hydrogen is generated, it is possible to prevent the electrolyte solution from reversely flowing in company with the hydrogen, thus the fuel cell power generation system is capable of generating electrical energy more effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell power generation system comprising the apparatus and fuel cell to generate electrical energy by converting the chemical energy of the hydrogen generated from the cathode.    DESCRIPTION OF DRAWING(S) - The figure shows schematic view of an apparatus for generating hydrogen.    Apparatus (100)    Anode (110)    Cathode (120)    Electrolytic bath (130)    Electrolyte solution (135)    Gelling agent (170)
NOVELTY - An alcohol-based gasoline cosolvent comprises (pts.wt.) fatty alcohol (20-28), acetamide (5-10), alkylphenol polyether (3-5), methyl tertiary butyl ether (30-35), fatty acid methyl ester (25-30), acetone (10-15), tert-butyl alcohol (1-3), antioxidant (0.05-0.08), and antiswelling agent (0.05-0.08).    USE - An alcohol-based gasoline cosolvent.    ADVANTAGE - The cosolvent is safe, does not produce pollutants and peculiar smell, requires less dosage to be effective, has excellent fluxing effect, does not have metal component and mechanical impurities, and increases octane content of gasoline from number 90 to number 95-99.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of preparing an alcohol-based gasoline cosolvent comprising reacting fatty alcohol and tert-butyl alcohol at 50-60 plus minus 1 degrees C and vacuum pressure of 0.4 mPa; adding acetamide; stirring the mixture for 30-40 minutes; adding alkylphenol polyether; mixing the mixture for 30-40 minutes; cooling to 23-28 degrees C; adding methyl tertiary butyl ether, fatty acid methyl ester, acetone, antioxidant and antiswelling agent; and stirring the mixture for 15-25 minutes.
NOVELTY - A carbonization equipment of bamboo comprises of an external-heating biomass gasifier/combustor furnace and a earth kiln. The external-heating biomass gasifier/combustor connects with the kiln forming the carbonization equipment of bamboo. In one embodiment, the heating rate and the temperature uniformity conditions in the kiln are both greatly improved since the high temperature flue gas from the gasifier/combustor are uniformly brought to contact with and directly heat the bamboo charge in the kiln. Therefore, the carbonization equipment of bamboo significantly shortens the carbonizing time when compares with the conventional bamboo-carbonizing equipment. Moreover, the yield of the bamboo charcoal and the carbon content of the charcoal are also increased.
NOVELTY - Production of biodiesel comprises treating animal and plant oil, waste cooking oil, and oil plants; and acidifying, removing water, methylesterifying, reacting with methanol at supercritical condition, transesterifying, filtering, reclaiming methanol and separating phases.    USE - Method for production of biodiesel (claimed).    ADVANTAGE - The method shortens the time for transforming biological oils into biodiesel, improves yield of biodiesel, greatly reduces production cost, and produces products that are free from alkali or acidic catalyst and waste alkali discharge; has esterification rate of more than 95%, reproducible material, wide application and simple post treatment, with no environmental pollution.
NOVELTY - A novel solar biogas tank, comprising a tank body, a feeding opening, a discharging opening and a gas outlet pipe, where the tank body is formed as a sphere shape by connecting upper and lower two semi spheres (3, 6) through a flange (5); two sides outside central point of lower semi sphere of the tank bogy are provided with a bearing flange (7) movably matched with a pushing-pulling bearing (10) set on a bearing seat (8).    USE - A novel solar biogas tank (claimed).    ADVANTAGE - The novel solar biogas tank has good sealing performance, quick fermentation, large yield, simple structure and convenient operation and use. Also, it does not leak water, leak gas, and can resist corrosion and aging.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the solar biogas tank.    Upper and lower two semi spheres (3, 6)    Flange (5)    Bearing flange (7)    Bearing seat (8)    Pushing-pulling bearing (10)
NOVELTY - A portable hydrogen producer primarily comprises a body containing a hollow reaction chamber. The reaction chamber has a material inlet and an air outlet, wherein the material inlet allows reaction solution and metal material to be fed into the reaction chamber so as to perform chemical reaction therebetween. The hydrogen producer further comprises an air-pressure detecting unit for detecting the status of the chemical solution in the reaction chamber and an air dispatching unit for exporting hydrogen in the reaction chamber to an external device that consumes hydrogen for operation, such as fuel cell.
NOVELTY - A method for biodegrading oil material during the process of food waste composting. The method includes forming a food waste-compost mixture, and mixing the food waste-compost mixture with an oil containing material to form a compost co-metabolic mixture. The compost co-metabolic mixture degrades the oil material during the composting process until a great part of the oil material is degraded.
NOVELTY - A method for preparing nutrient liquid without sterilizes process is provided. The method includes providing a suspension culture of Trichoderma (TCT301), and mixing a raw material with the suspension culture to make compost tea by performing an aerobic-like fermentation. The raw material is selected from one of food waste mixture, leachate and mature compost mixture.
NOVELTY - The VOCs waste gas treatment system has a waste gas collection system and a gas outlet pipe. The VOCs waste gas is fed into the biochemical treatment device through the waste gas collection system, and the waste gas is discharged through the gas outlet pipe after treatment of the biochemical treatment device.    USE - Volatile organic compounds waste gas treatment system.    ADVANTAGE - Solves the problem of wastewater generated in general biological base pool with simple structure, saves the cost of nutrient fluid and reduces the running cost of the system.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic cross-sectional view of the VOCs waste gas treatment system. (Drawing also includes non-English language text).
NOVELTY - The generator has the micropore jet current clapboard which is provided with jet current micropore. The micropore hydrosphere outflow clapboard is provided with the overflow micropore. The jet current micropore and the overflow micropore are at the concentric position. The positive and negative plating and painting polar plates are provided between the micropore hydrosphere outflow clapboard and the micropore jet current clapboard. The power supply connector in connection with anode of external power supply is provided in the positive and negative plating and painting polar plates.    USE - Generator of hydrogen and oxygen mixed air by electrolysizing water.    ADVANTAGE - Reduces temperature of generator, reduces difficulties of hydrosphere separation and refrigeration, and reduces drain current since the generator has evenly liquid exchange and discharges the hydrosphere timely.    DESCRIPTION OF DRAWING(S) - The drawing shows a front schematic view of the generator of hydrogen and oxygen mixed air by electrolyzing water.
NOVELTY - Accelerant composition comprises 25-55 wt.% of sodium oxide, 5-15 wt.% of calcium oxide, 10-20 wt.% of calcium nitrate, 10-20 wt.% of sodium nitrate, 5-15 wt.% of potassium nitrate, 5-15 wt.% of barium nitrate and 0.5-2 wt.% of aluminum powder. 5-14 wt.% of paraffin, 5-14 wt.% of phosphoric acid, 5-14 wt.% of hexamine, 2-7 wt.% of soda, 15-60 wt.% of charcoal and 25-35 wt.% of activated charcoal are also included. The sludge is selected from waste sludge, wastewater sludge or night soil sludge.    USE - Accelerant composition for producing fuel from sludge.    ADVANTAGE - The accelerant composition has maximum caloric value.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for manufacturing accelerant composition, which involves:    (A) mixing sodium oxide, calcium oxide, calcium nitrate, sodium nitrate, potassium nitrate, barium nitrate and aluminum powder in a mixer to obtain a composition; and    (B) mixing paraffin, phosphoric acid, hexamine, soda, charcoal and activated charcoal to the composition.    DESCRIPTION OF DRAWING(S) - The drawing shows a photograph of the sludge.
NOVELTY - An automatic compost discharging machine comprises falling material bucket, sliding surface layer, paddle, transmission mechanism, and driving mechanism; where the surface contacting with the material is provided with sliding surface layer and anti-cambering mechanism.    USE - The automatic compost discharging machine is useful for compost comprising sludge, garbage, and livestock manure in fermentation chamber.    ADVANTAGE - Compared with the existing technology, the automatic compost discharging machine can replace loading machine; where the transporting vehicle does not need to enter the fermentation tank that reduces damages on vehicle and human body. Moreover, the surface contacting with the material is provided with sliding surface layer and anti-cambering mechanism, which ensure the materials to fluently enter the next process.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the automatic compost discharging machine.
NOVELTY - Hydraulic extrusion machine comprises a driving unit (100), a main body (10), pairs of compression screws (20), a heater, a scrap hole (12) and a drive transfer gear (110), which is inserted inside of the main body of the hydraulic extrusion machine. The scrap hole is equipped at upper side of the main body. The heater is equipped inner side of the main body. The pairs of compression screws are equipped at regular interval in the main body of the hydraulic extrusion machine.    USE - Hydraulic extrusion machine for refuse-derived fuel.    ADVANTAGE - The hydraulic extrusion machine refuses fuel in a cost-effective manner and automatically maintains the temperature and pressure of the machine.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross sectional view of the hydraulic extrusion machine.    Main body (10)    Scrap hole (12)    Pairs of compression screws (20)    Driving unit (100)    Drive transfer gear (110)
NOVELTY - A composite catalyst is obtained loading oxides and/or phosphides and/or silicides and/or borides of chromium, tungsten, molybdenum, cobalt, nickel, zinc, cadmium, copper, platinum, tin, antimony, zirconium and/or strontium (element A) as active element, on porous carriers. The content of active element is 0.5-3% of the catalyst carrier by element.    USE - Composite catalyst is used for catalyzing and modifying low-proportion M15 and M30 methanol gasoline containing 5%-50% methanol (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of composite catalyst, which involves putting the catalyst carrier into a muffle furnace and roasted it at 400-800 degrees C for 4-7 hours, dissolving water-soluble compound(s) containing elements (A) in distilled water, carrying out bulk immersion of carrier in the solution, roasting carrier, utilizing distilled water to wash and filter the solution, drying the filtered product at room temperature to 130 degrees C for 0.5-8 hours, roasting it at 300-800 degrees C for 2-6 hours to obtain a catalyst precursor, and at 500-1000 degrees C, deoxidizing the catalyst precursor using a deoxidizing gas.
NOVELTY - Organic waste gas is collected by a gas skirt, and particles with grain size more than 2.5 mu m are removed by using a bag-type duster. The dust-removed organic waste gas is introduced into a photocatalysis reactor, and volatile organic matter is decomposed into micromolecular organic matter or converted into carbon dioxide and water by a photocatalyst loaded on active carbon cellosilk. The catalytically-oxidized organic waste gas is introduced into a bio-trickling filter tower to remove the remaining organic matter in the waste gas microbiologically.    USE - Combined photocatalysis-microbiological treatment of industrial organic waste gas (claimed).    ADVANTAGE - The method enables efficient removal of suspended particles and volatile organic matter contained in organic waste gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for equipment used for combined photocatalysis-microbiological treatment of organic waste gas, equipped with a gas skirt, a bag-type duster, a photocatalysis reactor, and a bio-trickling filter tower which are connected by pipes in sequence. A gas speed pressure gauge and a blower are connected between the bag-type duster and photocatalysis reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the combined photocatalysis-microbiological treatment method of organic waste gas.
NOVELTY - The sewage treatment system has a primary precipitating pool (1) connected to a sewage bio-treatment system (2) and a pre-regulating pool (4). The sewage bio-treatment system is connected to another precipitating pool (3), and the pre-regulating pool is connected to an alkaline fermenting pool (5). The alkaline fermenting pool is connected to the regulating pool that is connected to a dehydration equipment (33). A carbon source storing pool (7) is connected to pipes connecting primary precipitating pool and the sewage bio-treatment system.    USE - Sewage treatment system.    ADVANTAGE - The water sludge stabilization can be achieved. The high-quality carbon source can be obtained conveniently, and the by-product can be used as fertilizer with low investment and low operation cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the sewage treatment system. (Drawing includes non-English language text)    Primary precipitating pool (1)    Sewage bio-treatment system (2)    Precipitating pool (3)    Pre-regulating pool (4)    Alkaline fermenting pool (5)    Carbon source storing pool (7)    Dehydration equipment (33)
NOVELTY - The solar marsh gas fermentor has a hot water exchanger and solar heat collection tube, which are vertically fixed on a metal bracket. A water output pipe and a water inlet pipe are arranged on back portion of hot water exchanger and connected with a water path switching switch. Several water circulation pipelines are made of stainless steel material and arranged below a reaction tank, whose inlet and outlet holes are connected with switch. The water outlet pipe is connected with a spray head provided in a water tank arranged on top of reaction tank.    USE - Solar marsh gas fermentor installed in home.    ADVANTAGE - The space for installing solar marsh gas fermentor can be utilized effectively. The material feeding and discharging processes can be performed effectively so that the operability of solar marsh gas fermentor can be improved. The gasification and acidification reactions can be performed effectively and respectively in the marsh gas fermenting process. The raw materials to the reaction chambers can be supplied alternately so that the marsh gas can be generated synchronously and quality of the marsh gas can be improved. The concentration of marsh gas can be improved.
NOVELTY - The method involves locating magnetic poles (1) on upper and lower surfaces of container (4) and installing armature channel (3) at inner lower end of container. The channel is stored with strong electrolytic solution (8). The channel has sides set with electrodes (2) and top portion set with concave clapboard (5). Air clapboard (6) divides the container into air chambers (7). An electrolysis circuit is formed by electrodes in solution so as to produce hydrogen energy when electric conductor is passed through the channel.    USE - Method for electrolyzing hydrogen of strong electrolyte solution.    ADVANTAGE - The electrolysis of hydrogen in strong electrolyte solution can be performed at low cost by applying relatively low voltage to electrolysis circuit.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the electrolysis apparatus.    Magnetic pole (1)    Electrode (2)    Armature channel (3)    Container (4)    Concave clapboard (5)    Air clapboard (6)    Air chamber (7)    Strong electrolytic solution (8)
NOVELTY - The reaction device has a cylindrical reactor (1) comprising a pre-heating section (3) and catalytic reactor (5). A sealing structure (4) is arranged between the pre-heating section and catalytic reactor. An air inlet channel is formed between the outer wall (51) of catalytic reactor and inner wall of cylindrical reactor. Several air pores with diameter less than that of the catalyst in catalytic reactor are formed between the outer wall and inner wall (52) of catalytic reactor.    USE - Reaction device for gas phase catalytic hydrogenation/dechlorination of carbon tetrachloride.    ADVANTAGE - The structure of reaction device is simplified and simple and convenient operation of the reaction device is achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the reaction device.    Cylindrical reactor (1)    Pre-heating section (3)    Sealing structure (4)    Catalytic reactor (5)    Outer wall of catalytic reactor (51)    Inner wall of catalytic reactor (52)
NOVELTY - A water-adding excrement-turning demister of biogas tank comprises a bobber and an externally connected hose; where a central pipe passes through the bobber; the water inlet of the central pipe is connected to the externally connected hose; the water outlet is sealed; and the pipe wall of the central pipe is provided with jetting mesh.    USE - The water-adding excrement-turning demister of biogas tank is useful for industrial applications.    ADVANTAGE - The water-adding excrement-turning demister floats at the central of water level of biogas tank to make the pressurized water jet from the jetting mesh to crush foams on the liquid level of tank and blend tank. Moreover, it has simple structure, is strongly practical, and can uniformly blend biogas tank crush foams. Additionally, it can be set permanently in the tank; it does not need people to blend tank; and it is safe.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the water-adding excrement-turning demister of biogas tank.
NOVELTY - An automatic decomposing garbage bin comprises a bin cover and a bin body; where a turnover plate, a microorganism layer, a liquid accumulating layer, a water exhaust opening, and a liquid gathering basin are set in the bin body from upside to downside; a rotating shaft crossly penetrates the bin body and runs through the turnover plate; and the bin body is set with a door.    USE - The automatic decomposing garbage bin is useful for industrial applications.    ADVANTAGE - The automatic decomposing garbage bin is energy-saving, has no black smoke, has no open flame, and has relatively low temperature. Moreover, it avoids pollution to the environment and reduces the transporting amount of the urban garbage.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the automatic decomposing garbage bin.
NOVELTY - Gas mixing anaerobic digester comprises a digestion tank (10), a wastewater inlet pipe (12), a well unit (20) and a diffuser (30). A separator (40), a decant pipe (50), a release space (42), a guide portion (46) and a baffle (44) are also included. A gas exhaust tube (14), a blower (17) and a circulation discharge hole (21a) are also included. The effluent is flown and circulated in the digestion tank, where the diffuser provides the lifting power for circulating effluent. The generated gas is injected within the well unit and the separator controls the solid-liquid separation of the sludge.    USE - Gas mixing anaerobic digester.    ADVANTAGE - The gas mixing anaerobic digester is cost-effective, enhances the contact efficiency of the sludge and inflow wastewater by using the lifting phenomenon of the biogas, maximizes the process efficiency of the organic compound, regularly maintains the concentration of solids and liquids inside the digestion tank, increases the organic treatment efficiency of the effluent, reduces the breakdown of the generated sludge floc, maximizes the removal of the microorganism from the sludge, and improves the cloudiness of the processing water in gas stirring mode.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a gas mixing anaerobic digester.    Digestion tank (10)    Wastewater inlet pipe (12)    Gas exhaust tube (14)    Blower (17)    Well unit (20)    Circulation discharge hole (21a)    Diffuser (30)    Separator (40)    Release space (42)    Baffle (44)    Guide portion (46)    Decant pipe (50)
NOVELTY - The waste heat generated by fuel cell (110) during power generation is absorbed by cooling water. The waste heat water is made to flow through waste-heat recovery piping (130) and is collected in thermal storage tank (140). The heating feed back is installed inside the tank so that the waste heat water is provided to supplementary heat source feeding mechanism (180) and bifurcated portion (171) through redemption outlet line (170) so as to provide waste heat water to operating heat source of absorption refrigerating machine.    USE - Fuel cell waste heat recovery system for fuel cell such as proton exchange membrane fuel cell (PEMFC), direct methanol fuel cell (DMFC), molten carbonate fuel cell (MCFC), and solid oxide fuel cell (SOFC).    ADVANTAGE - The waste heat recovery rate of the fuel cell can be enhanced. The waste heat water stored in the thermal storage tank can be recycled efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fuel cell waste heat recovery system. (Drawing includes non-English language text)    Fuel cell (110)    Waste-heat recovery piping (130)    Thermal storage tank (140)    Redemption outlet line (170)    Bifurcated portion (171)    Supplementary heat source feeding mechanism (180)
NOVELTY - Carbonizing machine comprises a cooling device (6), a coil-type cooling pipe (8) and a chimney (7), which is connected to the coil-type cooling pipe. The coil-type cooling pipe cools water running out of the chimney. A sticking apparatus (30), a projection device and a discharge reactor (16) are also included, where the discharge reactor is installed at top of the chimney. The discharge reactor discharges combustion gas. The projection device is connected to cooling device.    USE - Carbonizing machine for manufacturing seaweed liquid by using seaweed resources.    ADVANTAGE - The seaweed manufacturing liquid carbonizing machine is eco-friendly and enables to prepare seaweed liquid easily.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic perspective view of the seaweed manufacturing liquid carbonizing machine. (Drawing includes non-English language text).    Cooling device (6)    Chimney (7)    Coil-type cooling pipe (8)    Discharge reactor (16)    Sticking apparatus (30)
NOVELTY - The system has housing (140) accommodating porous layers and a membrane electrode assembly (130). Pore is formed in one of the porous layers, and absorbs liquid fuel using the capillary force. The membrane electrode assembly surrounds the peripheral part of the porous layers, and produces power by utilizing the liquid fuel. A vent is formed in other porous layer for ejecting gas, where the vent is greater than the pore. An inlet port (142) is formed in the housing so that the liquid fuel is injected in the former porous layer.    USE - Fuel cell generation system for use in hand phone. Uses include but are not limited to hydrogen injection type fuel cell, methanol implantation type fuel cell, molten carbonate fuel cell and solid oxide fuel cell.    ADVANTAGE - The system eliminates the need of a separate pump for supplying the liquid fuel, thus achieving reduction in size and weight. The service life of the system is increased. The system enables the generated gas to be easily exhausted when producing the power, thus increasing the power production efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a fuel cell generation system.    Fuel cell (100)    Membrane electrode assembly (130)    Housing (140)    Inlet port (142)    Opening (144)
NOVELTY - The device has a roof which is set with a feeder with upper, middle and lower sections which are a pre-heating drying section, a pre-reducing section and a reducing section. The combustion chamber is arranged inside the reducing section above a grate. The grate is a heat exchange grate with bottom being provided with a slag discharging outlet. A rare-earth fireproof mud layer is arranged on the furnace wall and the catalyzing and cracking device is set inside the combustion chamber. A furnace wall inside the combustion chamber is installed with a wave frequency emitter.    USE - Biomass ion catalyzing, cracking and gasifying device.    ADVANTAGE - Exhibits low heat loss and high gasifying effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross sectional perspective view of the biomass ion catalyzing, cracking and gasifying device.
NOVELTY - The rotary straw gasification furnace has a furnace, a furnace cover, and an oil water draining valve. A burning chamber is mounted in the furnace and connected with a blower. The furnace comprises two furnace bodies whose upper end cover is a whole one furnace cover. The lower ends are on a whole holder (14). The two furnace bodies communicate with each other by an exhaust pipe. The two furnace bodies comprise a two-layer sealing burning furnace body (4) and a secondary filter furnace body (5).    USE - Rotary straw gasification furnace.    ADVANTAGE - Provides a device with low cost and accessories, simple operation, convenient use, high yield, low flue gas and clean combustible gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross sectional perspective view of the rotary straw gasification furnace.    Two-layer sealing burning furnace body (4)    Secondary filter furnace body (5)    Screen-shaped filter separation plate (6)    Water outlet (8)    Holder (14)
NOVELTY - The biomass energy straw gasification furnace has a dust chamber which is provided under the grate. A combustible gas outlet is provided above the outer part of the furnace. The combustible gas that is discharged from the combustible gas outlet is returned to the hollow throat area in the furnace through a gas tube. A combustible gas outlet of dust stopping screen device and dust cleaning hole are provided at the lower section of the furnace. A sealing gasification device is provided at the bottom of the furnace.    USE - Biomass energy straw gasification furnace for combustible gas purifier (claimed).    DESCRIPTION OF DRAWING(S) - The drawing shows a cross sectional perspective view of the biomass energy straw gasification furnace.
NOVELTY - The rotor type machine has a bracket, a hopper, a discharging port, a transmission device matched to motor and installed in gear box. A rotor is set in the rotor box below the hopper. The rotor is connected to the transmission device. The rotor is a cone-shaped rotor and that has a taper ratio of 1 is to 15. The rotor is equipped with a forward spinning spiral groove.    USE - Rotor type machine for producing charcoal from straw.    ADVANTAGE - Enables to obtain a straw charcoal that is even. Enables the straw which to be burned and stacked in an appropriate position.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory perspective view of the rotor type machine.
NOVELTY - The pyrolyzing furnace has a flue, a chimney base, a wood tar tank and a recycling tower. The outlet of the flue is connected with the recycling tower. The recycling tower is a metallic cylinder. The upper section and the lower section of the metallic cylinder are sealed while the middle section is welded with a predetermined number of metallic hollow tubes. The upper head of the metallic cylinder is welded with a cold water pipe. The lower head of the metallic cylinder is welded with a hot water pipe.    USE - Pyrolyzing furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the pyrolyzing furnace.
NOVELTY - Zirconium-metal organic framework (Zr-MOF) (A1) having a surface area of at least 1020 m2/g is new.    USE - As zirconium-metal organic framework (Zr-MOF) useful as electrode material in a lithium battery; in a hydrogen fuel cell having a hydrogen reservoir for retaining gas, preferably hydrogen, methane or acetylene; as physiologically tolerable Zr-MOFs for use in medicine for the manufacture of a sustained release medicament for treatment of a human or non-human animal; as catalyst or catalyst support (claimed).    ADVANTAGE - The zirconium-metal organic framework material made using cornerstones based on zirconium has catalytic activity; and it exhibits excellent stability, porosity and surface area. The compound has ability to adsorb large volumes of gas, and has both high thermal and chemical stability, especially water stability. Because of the nature of Group 4 metals, the Zr metal can be in more than one oxidation state. This makes the Zr-MOFs ideal candidates for use as catalysts (e.g. in olefin polymerization), or more especially as electrodes in lithium batteries. The Zr-MOF is water and acid-stable. The Zr-MOFs have a strong and stable 3D structure and a wide range of possible oxidation states for Zr making them especially suitable for use in place of graphite as the electrode material.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) new functionalized Zr-MOF compound having a surface area of at least 500 m2/g;    (2) a gas container comprising a sealable vessel containing a Zr-MOF, optionally containing a gas;    (3) a sustained release pharmaceutical composition comprising a physiologically tolerable Zr-MOF containing a drug substance, e.g. a substance with therapeutic or prophylactic effect or with utility in diagnosis; and    (4) a catalyzed process for reacting a reagent to produce a product involving using Zr-MOF as the catalyst or catalyst carrier.
NOVELTY - Producing fuel from pressed biomass, comprises subjecting the biomass to a drying process, before the compression molding process; a mechanical dewatering process to reduce the moisture content, before the drying process; and a first crushing process, before the mechanical dewatering process, where the biomass is finely reduced in the first crushing process or the biomass is washed before or after the first crushing process.    USE - The process and the apparatus are useful for producing fuel from the pressed biomass (claimed) such as agriculture, forestry and horticulture products including waste e.g. garden or kitchen waste, and waste from the industrial processing of biomass such as food processing and paper.    ADVANTAGE - The process provides fuel with better calorific value, improved fuel properties and lowest possible burden of production facilities, and at lower energy expenditure. The fuel does not have any harmful substances.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an apparatus for producing fuel from biomass, comprising: a device (1) for molding the biomass, which is present upstream to the device (2) for drying the biomass, which is present upstream to the device (3) for mechanical dewatering of the biomass to reduce its moisture content; and a device (4) for crushing the biomass, which is present upstream or downstream to a device (5) for washing the biomass.    DESCRIPTION OF DRAWING(S) - The figure shows the apparatus for the production of fuel from pressed biomass.    Press-molded equipment (1)    Drying equipment (2)    Dehumidifying equipment (3)    Initial crushing equipment (4)    Washing equipment. (5)
NOVELTY - The apparatus has a rotary cylindrical retort enclosed within a static refractory insulated outer vessel that is heated by introduced hot gases with a feed mechanism. The retort is provided with internal longitudinal parallel vanes (9, 11) for distributing fuel and maintaining a vane position adjacent to a heated shell of the retort. A shape of the vanes forms a longitudinal cavity when a circumference of the retort is longitudinally cut away between the vanes to provide an access for the hot gases to penetrate towards an axis of the vessel for providing an increased heated surface area.    USE - Apparatus i.e. gasifier, for gasification of a material e.g. carbonaceous, wood and plastic material, to produce a high quality gas to fuel a reciprocating gas engine for generation of electricity.    ADVANTAGE - The apparatus facilitates gasification of any carbonaceous or other material with the significant calorific value to produce a high quality gas preferably to fuel a reciprocating gas engine for generation of electricity. The feeding mechanism is designed for ensuring a positive seal between a gasifier and atmosphere, removing the entrained air from the fuel, and positively feeding the fuel to the gasifier. The apparatus has robust design. The apparatus is designed to heat up the fuel as rapidly as possible to the pyrolysis temperature in order to ensure maximum efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of a gasifier.    Vessel circumference (3)    Refractory lining (6)    Longitudinal space (8)    Internal longitudinal parallel vanes (9, 11)    Restricted passage (10)
NOVELTY - A fractionating tower has a tower top condenser (3) provided with gas outlet (4) and communicated with the tower joint (1) via flange (2). The tower joint is communicated with the tower bottom kettle (9) via the flange. The tower bottom kettle has a discharging orifice (8) and a feeding orifice (10) on one side. The tower joint inner bottom has tower internal component (7) put with filling (6) of particle, ring, or silk-like shape. The filling, made of metal or ceramics, is provided with liquid distributing machine.    USE - Fractionating tower for biomass cracking gas.    ADVANTAGE - Provides good fractionating effect since the fractionating tower is simple to operate.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of a fractionating tower.    Tower joint (1)    Flange (2)    Tower top condenser (3)    Gas outlet (4)    Filling (6)    Tower internal component (7)    Discharging orifice (8)    Tower bottom kettle (9)    Feeding orifice (10)
NOVELTY - The reactor has a solid material storage tank (2), with a discharge opening (1) at the lower part, communicating with a gas-solid separation settling chamber (3) at the upper part. A cracking reaction tube (7) with an ash damper (10) at the bottom and a spiral propelling feeder (8) on one side extends out from the settling chamber. A heating furnace (6) is mounted above the settling chamber and passed by the cracking reaction tube. An overflow weir (9) on the upper end of the settling chamber is passed by the ash damper. A cyclone separator (4) with an outlet (5) is at the chamber upper part.    USE - Fast biomass cracking reactor.    ADVANTAGE - The reactor has a simplified structure, offering convenient operation and fine service performance.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of a fast biomass cracking reactor.    Discharge opening (1)    Solid material storage tank (2)    Gas-solid separation settling chamber (3)    Cyclone separator (4)    Outlet (5)    Heating furnace (6)    Cracking reaction tube (7)    Spiral propelling feeder (8)    Overflow weir (9)    Ash damper (10)
NOVELTY - The condenser has a gas inlet tube (3) with an inlet extending within and out of a condenser shell (2) and a lower end provided with gas distributing machine (6). A gas outlet (4) and a condensing tube (5) are on the upper part and inner part of the condenser shell, respectively. The inlet and outlet of the condensing tube extend out of the condenser shell. The bottom of the condenser shell is provided with blow-down tube (7) and overflowing tube (1).    USE - Condenser for biomass cracking gas.    ADVANTAGE - The condenser is easy to operate and provides high efficiency, since issues relating to tar condensing and high costs are solved.    DETAILED DESCRIPTION - The condenser has a gas inlet tube (3) with an inlet extending within and out of a condenser shell (2) and a lower end provided with gas distributing machine (6). A gas outlet (4) and a condensing tube (5) are on the upper part and inner part of the condenser shell, respectively. The inlet and outlet of the condensing tube extend out of the condenser shell. The bottom of the condenser shell is provided with blow-down tube (7) and overflowing tube (1). The blow-down tube is provided with valve. The position of the overflowing tube outlet is higher than the position of the gas distributing machine. The upper part of the condenser shell is provided with water-supplementing orifice (8), which is higher than the overflowing tube outlet. The inner part of the condenser shell is filled with water up to a water level higher than part of the condensing tube.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of a condenser.    Overflowing tube (1)    Condenser shell (2)    Gas inlet tube (3)    Gas outlet (4)    Condensing tube (5)    Gas distributing machine (6)    Blow-down tube (7)    Water-supplementing orifice (8)
NOVELTY - The system has isolation unit (33) to isolate ammonia (GN) from waste water obtained from wet gas-purification installation (A). A supply unit supplies ammonia isolated from waster water to gasification installation (11).    USE - Gas-purification system for performing purification process of ammonia in gasifying gas produced from organic waste, biomass fuel, solid fuel and industrial waste.    ADVANTAGE - The purification process of ammonia in gasifying gas can be performed effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for processing method of ammonia.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the gas-purification system. (Drawing includes non-English language text)    Gasification installation (11)    Isolation unit (33)    Pushing-in fan (41)    Wet gas-purification installation (A)    Ammonia (GN)
NOVELTY - The device has an air tangential inlet (3) and a fuel gas tangential outlet (9) that are welded in an outermost layer of an anti-dromic heat exchanger (2). An internal furnace (1) is located at center of the anti-dromic heat exchanger. A heat conducting rod (11) is located in an inner part of an internal furnace (4). The anti-dromic heat exchanger is installed in an outer side of the internal furnace, where an inner side of the internal furnace is equipped with the heat conducting rod.    USE - Biomass such as corn straw, wheat straw, rice hull and peanut shell, high temperature gasification device.    ADVANTAGE - The heat conducting rod equipped in the internal furnace transfers heat from oxidation zone of the furnace to heat decomposition zone, thus improving temperature of biomass gasification reaction and reducing tar content in biomass fuel gas, and hence improving transformation ratio and heat value of fuel gas. The device has self-pre-heating, self-keeping temperature, self-cooling, low energy consumption, high transformation ratio, high heat value of produced fuel gas and low tar content. The device can be utilized for producing fuel gas by utilizing multiple biomasses of corn straw, wheat straw, rice hull and peanut shell.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a biomass e.g. wheat straw, high temperature gasification device.    Internal furnace (1)    Anti-dromic heat exchanger (2)    Air tangential inlet (3)    Internal furnace (4)    Fuel gas tangential outlet (9)    Heat conducting rod (11)
NOVELTY - The vehicular movable integrated device has coagulating sedimentation device, high-grade catalytic oxidation device, MBR reactor, and lifting pump. The coagulating sedimentation device having drug charging device, mixer, and sludge discharging device, is connected with lifting pump and high-grade catalytic oxidation device by communicating pipe. The high-grade catalytic oxidation device having drug charging device, mixer, sludge discharging device, and pH on-line testing device, is connected with the MBR reactor by communicating pipe.    USE - Vehicular movable integrated device.    ADVANTAGE - Achieves small discharge amount of fracturing fluid, high concentration of organic substance, great chroma and viscosity, simple operation, high degree of automation at low running cost.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the vehicular movable integrated device. (Drawing includes non-English language text).
NOVELTY - The method comprises discharging a purified water (2) over parallel flow-through membrane modules (4) by a pump from a mixture (3) of reactor contents during cleaning the membrane module in which the purified water is flowed through a second pump to purified water discharge in opposite direction of a cleaning fluid and entered into bio reactor (1).    USE - Method for continuous discharge of purified water from a bio-reactor using porous membranes, useful in anaerobic sewage plant.    ADVANTAGE - The method ensures economical, effective and continuous discharge of the purified water from the bio reactor with less energy consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for continuous discharge of purified water from a bioreactor.    DESCRIPTION OF DRAWING(S) - The figure shows an external integration of membranes.    Bioreactor (1)    Purified water (2)    Mixture (3)    Membrane module (4)    Vacuum pump. (5)
NOVELTY - The method comprises mixing fiber-containing raw materials with water, steam and further additives under heating of the raw- and additional materials and conditioning the mixture at 200 degrees C in pressure free manner or in over-pressure. The mixture is held before pressing over long time at 150 degrees C in an intermediate container (4). The raw material is added to fat and lignin.    USE - Method for the production of pressed products from fiber containing raw materials such as wood, straw or peat in a pressing- or expander plant.    ADVANTAGE - The method ensures cost-effective, rapid and simple production of pressed product with high throughput and less consumption of energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for the production of pressed product.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of a device for the production of pressed product.    Pelleting press (1)    Mixer (2)    Detention element (2)    Intermediate container (4)    Double screw. (9)
NOVELTY - The method involves arranging an electrolytic membrane (210) with glass transition temperature. A catalyst layer (220) containing electrolyte is formed with glass transition temperature lower than that of electrolytic membrane. The electrolytic membrane and catalyst layer are joined by thermo-compression at temperature of range of +/- 5 degrees C with respect to glass transition temperature of catalyst layer.    USE - Manufacturing method of fuel cell.    ADVANTAGE - Since the electrolytic membrane and catalyst layer are joined by thermo-compression at temperature with respect to glass transition temperature of catalyst layer, the fuel cell is manufactured efficiently, without damaging the pore structure of catalyst layer.    DESCRIPTION OF DRAWING(S) - The drawings show the sectional views explaining the manufacturing process of fuel cell.    Electrolytic membrane (210)    Catalyst layer (220)    Membrane electrode assembly (250)    Base material (400)    Sheet for catalysts (410)
NOVELTY - Module preparation involves providing housing, in which a layer of a porous support material having hydrophilic characteristics is arranged, where the layer has two surfaces. A liquid containing a compound is introduced into the porous support material. The porous substrate material is overflowed with a fluid containing another compound, which is able to react with the former compound. The former compound is reacted with the latter compound to form polymer.    USE - Method for preparing module for water purification for electronic industry, boiler water purification, drinking water production from brackish water and sea water, sewage cleaning, fluid sterilization, recuperation of coloring materials, latex or polyvinyl alcohol, oil water separation in pharmaceutical and biotechnical separations, gas and vapor permeation, moist exchange and electrolytic processes, and extraction or absorption processes, for oxygenation or inert gas including nitrogen production by separation of carbon dioxide and nitrogen, hydrogen recuperation in refineries by separation of hydrogen and hydrocarbons, adaptation of synthesis gas concentration by separation of hydrogen and carbon monoxide, separation of hydrogen and nitrogen in ammonia exhaust gas, acidic gas treatment and production of fermentation gas by separation of carbon dioxide and hydrocarbons, drying natural gas by separation of water and hydrocarbons, treating acidic gas by separating hydrogen sulfide and hydrocarbons, helium separation from hydrocarbons and nitrogen to hydrocarbon recovery or exhaust air purification by separation of hydrocarbons from air (all claimed).    ADVANTAGE - The module preparation method enables to produce the module having high mechanical stability, high transmembrane fluxes and improved mass transfer in flow channels in a cost-effective manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the module.    Inlets (26,27)    Outlets (28,29)
NOVELTY - Method, in which triglyceride is transesterified with an alcohol in the presence of a solid catalyst comprising zeolite X with silicon/aluminum atomic ratio of less than 1.2, is claimed.    USE - The method is useful for the production of biodiesel.    ADVANTAGE - The method is carried out at moderate temperature and pressure, with good yield and high reaction rate.
NOVELTY - A drying and vertical pyrolysis unit is a vertical metal cylinder fitted with fixed or removable decks, variously slotted, perforated and/or screened, and with a rotating central shaft which carries arms from which hang rakes of varied type.    USE - Drying and vertical pyrolysis unit for continuous feed and transport of lignocellulosic materials.    ADVANTAGE - The drying and vertical pyrolysis unit is sufficiently compact, lightweight and robust which allows its transport on a vehicle or trailer and its operation while in motion; has a controllable temperature profile and a short residence time for feed materials; and not only provides for extraction of solid, liquid and gaseous products of pyrolysis but uses some of its own lignocellulosic feed and derived pyrolysis gas as a main or sole fuel for continued pyrolysis.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic elevation view of a drying and vertical pyrolysis unit.
NOVELTY - The method involves supplying food rubbish stored in a storing tank based on a treating quantity, and crushing a particle of the supplied food rubbish to certain size. Moisture content of the food rubbish in a treatment process is reduced through squeezing and de-watering processes about 70 percentage. A treating substance dried by a drying process is compressed and transported. An oil substance i.e. steamed-shaped gas, is generated in an oiling process, where the oil substance is condensed by a heat exchanger. The oil and the gas generated are stored.    USE - Method for producing biomass energy by re-using food rubbish to perform manure collecting or forming fodder in an oil import.    ADVANTAGE - The method easily enables use of the food rubbish to perform manure collecting or forming fodder. The method produces the energy by using the food rubbish, and increases an oil import substituting effect during high oil price times.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for producing biomass energy by re-using food rubbish.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic side view of a biomass energy producing device.'(Drawing includes non-English language text)'
NOVELTY - A straw gasification furnace comprises an external shell (4), an internal shell (1), an upper separation plate (2) welded between upper ends of the shells, a lower separation plate (6) welded between lower ends of the shells, a water pipe welded with an upper part of the external shell, a water inflow pipe (5) welded with a lower middle part of the external shell, a superconductive heating pipe communicating with a reducing layer in the furnace, and an exhaust pipe (7) welded with the upper parts of the external and internal shells.    USE - A straw gasification furnace for pyrolyzing excess straws, rice straws, and plants.    DESCRIPTION OF DRAWING(S) - The drawing is a sectional view of the straw gasification furnace.    Internal shell (1)    Upper separation plate (2)    External shell (4)    Water inflow pipe (5)    Lower separation plate (6)    Exhaust pipe (7)
NOVELTY - The method involves conveying biomass e.g. organic waste, into a spiral conveyer, and conveying the biomass into a microwave pyrolysis reactor to absorb microwave. Carbon residue is discharged via a discharge port of the reactor after heating, and pyrolysis is carried out in microwave pyrolysis reaction to generate organic vapor at high temperature. The vapor is conveyed to a cyclone separator to remove carbon particles and sands, and conveyed into a condenser from the separator for cooling, where condensable part is changed into bio-oil and dropped into an oil tank to obtain the bio-oil.    USE - Method for preparing bio-oil through microwave pyrolysis.    ADVANTAGE - The method avoids the need for heat conduction, meets best process requirements of extracting bio-oil, and is implemented at low temperature and controllable pyrolysis temperature without thermal inertia.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram illustrating a method for preparing bio-oil through microwave pyrolysis.'(Drawing includes non-English language text)'
NOVELTY - The method involves feeding a material to a fluidized bed reactor (2) through a combined feeder (1). The material dried in a raw material drying chamber (17) is collected in a storage hopper (16). Cooling medium is atomized by a nozzle of a spraying tower (7). Cracking gas sent to the spraying tower is fully condensed in bio-oil. Bio-oil granules are captured and fallen in an oil-liquid separator (8). Upper spraying medium in a spraying medium cooler (10) is recycled by a pump. Residual gas is conveyed to a gas storage tank (18) to be treated and utilized as fuel gas.    USE - Method for pyrolytically self-heating self-circulating and cracking cellulose biomass to prepare liquid fuel.    ADVANTAGE - The volatile gas and coke generated in the pyrolysis process are recovered and effectively utilized, which realizes self-heating of the pyrolysis system and saves the cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a pyrolytic biomass self-heating, self-circulating and cracking system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a pyrolytic biomass self-heating self-circulating cracking device.    Combined feeder (1)    Fluidized bed reactor (2)    Spraying tower (7)    Oil-liquid separator (8)    Spraying medium cooler (10)    Storage hopper (16)    Raw material drying chamber (17)    Gas storage tank (18)
NOVELTY - The system has a drier (1) provided with a rubbish hopper (102) and an supply-air outlet (103) in front, a suction opening (105) on back, and a discharge port (106) at tail end. A synthesis gas outlet (203) of a gasification furnace (2) is connected to a synthesis gas inlet (1101) of a whirlwind dust collector (11). A synthesis gas inlet (1204) of a wetting purifier (12) is connected to a synthesis gas outlet (1102) of the collector. A purified synthesis gas outlet (1201) is connected to a suction port of a compressor (14). An exhaust port of the compressor is connected to a gas cabinet (15).    USE - System for gasifying domestic waste and organic waste.    ADVANTAGE - The system improves the gasifying rate and quality of waste. The system breaks down the virulent substance such as dioxin, and removes the tar. The system converts the domestic waste and organic waste into the secondary clean energy, and produces the coal gas in hydrogen, methanol and dimethyl ether liquid gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a domestic waste and organic waste gasifying system.    Drier (1)    Gasification furnace (2)    Whirlwind dust collector (11)    Wetting purifier (12)    Compressor (14)    Gas cabinet (15)    Rubbish hopper (102)    Supply-air outlet (103)    Suction opening (105)    Discharge port (106)    Synthesis gas outlets (203, 1102)    Synthesis gas inlets (1101, 1204)    Purified synthesis gas outlet (1201)
NOVELTY - A solid alkali catalyst comprises (wt.%) zirconium dioxide (81-83), calcium oxide (15-17), and potassium hydroxide (1-3).    USE - A solid alkali catalyst for preparing a biological diesel oil (claimed).    ADVANTAGE - The catalyst obtains high stability and activity, and can be easily separated and repeatedly used.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing a solid alkali catalyst, comprising:    (A) uniformly mixing zirconium oxychloride and calcium chloride in a reactor to obtain 0.1-0.3 mol/L solution;    (B) adding ammonia water, continuously heating, and stirring, where the mole ratio of the mixed solution and ammonia water is 1:1;    (C) controlling pH of the solution at 8-10, to generate a deposition completely;    (D) aging the deposition for 1-5 hours, filtering, and washing with deionized water until there is no chloride ion detected;    (E) drying it for 12 hours at 110 degrees C, roasting for 4-8 hours at 600-850 degrees C;    (F) grinding, screening, and dipping in 0.01-0.05 mol/L potassium hydroxide solution overnight; and    (G) dipping and mixing for 12 hours in deionized water, roasting for 4-8 hours at 600-850 degrees C.
NOVELTY - Sheet-like hydrogen producing agent, comprises a hydrogen producing layer formed on water-absorptive sheet. The hydrogen producing layer contains hydrogen producing agent and resin.    USE - Sheet-like agent is used for producing hydrogen gas for fuel cell.    ADVANTAGE - The agent has favorable handleability and enables to produce hydrogen at constant rate.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) pleated-type hydrogen producing agent formed by alternatively folding the sheet-like hydrogen producing agent; and    (2) method for producing the sheet-like hydrogen producing agent.
NOVELTY - Preparing a biofertilizer using palm oil mill waste, comprises: collecting kernel shell, empty fruit bunch (EFB), palm oil mill effluent (POME) and fiber (a fibrous residue of palm oil milling operation) from palm oil mill waste; carbonizing the kernel shell to obtain carbon; incinerating the EFB to obtain ash; treating the POME with micro air bubbles and filtering the treated POME to obtain decanter cake of POME sludge; mixing the fiber, the kernel shell carbon, the EFB ash and the decanter cake; and maturing the mixture to produce a biofertilizer.    USE - The method is useful for preparing biofertilizer using palm oil mill waste. The biofertilizer is useful to prevent or slowly treat soil diseases such as ganoderma disease. Tests details are described but no results given.    ADVANTAGE - The method is an environmental friendly and economical process of completely treating palm oil mill wastes. The biofertilizer: can maximize the physiological growth of plants; and employs solid state fermentation to promote the proliferation of microorganisms and improves soil conditions resulting in producing healthy plants.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a biofertilizer prepared by maturing a mixture of carbon obtained by carbonizing kernel shell, ash obtained by incinerating EFB, decanter cake of POME sludge obtained from POME, and fiber.
NOVELTY - The method involves applying active pressure to a resin base material (24) in a mold (26) at an ambient temperature, such that a pre-form (32) having desired shape and a selected pore structure of a fuel cell component (22), is formed. The pre-from is heated at a higher temperature to fully cure the resin base material, and lock the selected pore structure in place, without applying active pressure to the pre-form.    USE - Manufacturing method of fuel cell component e.g. water transport plate (claimed).    ADVANTAGE - Since active pressure is not applied while heating the pre-form, simplifies manufacturing process and allows use of simpler equipment, hence reduces manufacturing cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the arrangement for manufacturing fuel cell component.    Fuel cell component (22)    Resin base material (24)    Mold (26)    Pre-form (32)    Heater (36)
NOVELTY - The furnace has a furnace body (1), and a hearth (2) provided in the furnace body. The lower part of the hearth is provided with a fire grate (3). The bottom of the hearth is provided with an ash bucket (5) sealed with the hearth. The upper part of the hearth is opened with an air inlet (4). A gap is formed between the hearth and inner wall of the furnace body to form gasification air channel (6). The lower part of the furnace body is opened with gasification air inlet (7). The upper part of the hearth is opened with gasification air hole (8).    USE - Biomass direct-fired gasification furnace for burning biomass materials.    ADVANTAGE - Provides a biomass direct-fired gasification furnace that has reasonable and simple structure, and convenient operation. Ensures that the biomass direct-fired gasification furnace has dual function of direct firing and gasification-firing under effect of direct firing. Ensures that no tar is generated during gasification. Ensures saved energy and reduced discharge since the biomass furnace material can be directly fired and fired by gasification-firing without generating gasification carbon residue.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the biomass firing gasification device.    Furnace body (1)    Hearth (2)    Fire grate (3)    Air inlet (4)    Ash bucket (5)    Gasification air channel (6)    Gasification air inlet (7)    Gasification air hole (8)
NOVELTY - The furnace has a furnace body (1) formed with an ash discharge port (14) at its bottom. A nozzle (2) is arranged at the bottom of the furnace body, and is formed with an air hole for down spraying. A ventilating pipe (3) is connected to the nozzle. The side of the furnace body is provided with a buffer gas cabinet (6). The upper part of the furnace body is connected to the buffer gas cabinet. The top end of the buffer gas cabinet is arranged with a stove (7). A gas supply valve (8) and an air supply valve (9) are arranged between the stove and buffer gas cabinet.    USE - Down-spraying biomass gasification furnace for burning biomass material.    ADVANTAGE - Provides a down-spraying biomass gasification furnace that burns and consumes the charcoal at the bottom of the furnace because a nozzle that sprays gas downward is arranged at the bottom of the furnace thus improving the material utilization ratio with a quick starting speed. Ensures that the down-spraying biomass gasification furnace has simple structure and convenient operation, prevents tar leakage from the pipeline, and improves heat utilization ratio.    DETAILED DESCRIPTION - The other end of the ventilating pipe is connected to an air fan (4) outside the furnace body. The top end of the furnace body is provided with a feeding cover (5).    DESCRIPTION OF DRAWING(S) - The drawing shows the cross-sectional view of the down-spraying biomass gasification furnace.    Furnace body (1)    Nozzle (2)    Ventilating pipe (3)    Air fan (4)    Feeding cover (5)    Buffer gas cabinet (6)    Stove (7)    Gas supply valve (8)    Air supply valve (9)    Ash discharge port (14)
NOVELTY - Production device has reaction kettle (6) with outlet linked to methanol recycler (10), while the other outlet is linked to second butterfly type centrifuge (7). The outlet of second butterfly type centrifuge is attached to crude glycerin tank (9), while other outlet is respectively attached to crude bio-diesel tank (8) and methanol recycler. The outlet of methanol recycler is linked to inlet of reaction kettle by methanol tank (5), while the other outlet is respectively linked to water washing kettle (11), third butterfly type centrifuge (12), film evaporator (13) and rectifying tower (14).    USE - Production device used for providing refined bio-diesel by using high acid value oil.    ADVANTAGE - Provides production device with continuous production process and low production cost, and safe and pollution free production process. Obtains refined bio-diesel with high quality that meets the requirement of national bio-diesel standard.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic block diagram of production device.    Methanol tank (5)    Reaction kettle (6)    Second butterfly type centrifuge (7)    Crude bio-diesel tank (8)    Crude glycerin tank (9)    Methanol recycler (10)    Water washing kettle (11)    Third butterfly type centrifuge (12)    Film evaporator (13)    Rectifying tower (14)
NOVELTY - The manufacturing device has primary disc type centrifuge (6) connected to outlet of reacting kettle (1). The inlets of methanol recycling device (9) are respectively linked to outlets of reacting kettle and biological diesel oil storage tank (7). The outlet of biological diesel oil storage tank is attached to water washing kettle (10) used for removing impurity and catalyst in biological diesel oil. A secondary disc type centrifuge (11) is linked to outlet of water washing kettle. A film evaporator (12) is linked to outlet of secondary disc type centrifuge, and used for removing water.    USE - Manufacturing device for producing refined biological diesel oil.    ADVANTAGE - Enables to continuously manufacture and produce biological diesel oil with high property, without causing pollution during manufacturing process.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic block diagram of manufacturing device.    Reacting kettle (1)    Primary disc type centrifuge (6)    Biological diesel oil storage tank (7)    Methanol recycling device (9)    Water washing kettle (10)    Secondary disc type centrifuge (11)    Film evaporator (12)
NOVELTY - The furnace has a cabin cavity surrounding an external wall of a dust deposit chamber at a bottom of a furnace body. The cavity is equipped with porous filter sheets that are arranged in form of a mazy radiation. A top of the cavity corresponding to a side of a cabin cavity air inlet holes is equipped with air through holes linked to a purification baking cabin. Internal and external walls of an interlayer are equipped with the sheets that are arranged in crossing manner. An external wall of the body corresponding to the side of the inlet holes is equipped with a purified fuel gas outlet.    USE - Biomass gasification-purification integrated furnace.    ADVANTAGE - The furnace comprises double functions of gas generation and gas purification, and effectively removes the coal tar, moisture and dust.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass gasification-purification integrated furnace.
NOVELTY - The combustion apparatus has sealing furnace, furnace grate, furnace cover, and ash outlet at the bottom of furnace. Ignition device is set on one side at bottom of furnace, while air inlet channel is formed on other side. The outer part of furnace is connected to draught fan, while its inner end is connected to spiral blower. The furnace cover has a closed feed pipe. A combustible gas output pipe is set on top of furnace. A fume purification device is connected to top of furnace. The outlet of fume purification device is connected to purified combustible gas output channel and gas cooker.    USE - Combustion apparatus for converting plants into combustible gas.    ADVANTAGE - Provides a combustion apparatus that has high heat efficiency, does not damage human body, does not pollute the environment, and is convenient to use.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of the combustion apparatus.
NOVELTY - The device has a catalyzing component for detecting methane, and an acousto-optic warning circuit, a display circuit, an oxygen sensor, an oxygen signal amplifying circuit and a key circuit connected with corresponding ports of a single chip computer. Four switches of the key circuit are connected in parallel. Output ends of the oxygen signal amplifying circuit and an amplifying circuit are connected with an analog-to-digital (A/D) converter port of the single chip computer.    USE - Methane and oxygen measuring device.    ADVANTAGE - The device can simultaneously detect methane and oxygen, and is inexpensive.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a methane and oxygen measuring device.'(Drawing includes non-English language text)'
NOVELTY - Invention pertains to agriculture, namely to production of fertilisers, and may be used for rapid preparation of biocompost from organic wastes of cattle breeding and poultry husbandry. Processing line contains a node of preliminary preparation of mixture, made as capacities of two spreader-trailers, unloading conveyors whereof are set along the entire bottom surface area of the capacities and are coupled by means of guiding cover with unloading device of the mixer, located under these unloading conveyors, with crushing beaters set there above; they are covered from above with reflecting cover made as an arch, whereat mixture decontamination device is made as fermenting boxes with capability of aeration, connected with unloading device of the mixer, with additionally installed therein second screw - cutter with the same pitch, but with an opposite coiling, with a drive gear securing rotation away from it, with their centers arranged horizontally at a distance less than two radiuses of coils, enabling getting partial mutual overlapping.    USE - Agriculture.    ADVANTAGE - Increased evenness of input in received mass for composting. 2 dwg
NOVELTY - As preventive means for protection of plants it is suggested to use natural nutritive fumitory aromatiser"Plus Liquid Smoke". 0.15-2.5%-aqueous solution of the aromatiser is used.    USE - Agriculture.    ADVANTAGE - High efficiency, ecologically safe preventive protection of plants against destructive insects.
NOVELTY - A method (M1) for recovering tallow from meat processing wastewater involves: adding a coagulant composition to the wastewater to agglomerate suspended fats, oil and grease particles in the wastewater, separating solid waste materials from the wastewater and isolating tallow from the solid waste materials, where the coagulant composition comprises tannin.    USE - For recovering tallow from meat processing wastewater (claimed) for producing biofuels such as biodiesel.    ADVANTAGE - The method enhances removal of fats, oil and grease from meat processing waste-waters without the addition of heavy metals.
NOVELTY - The system has a raw fuel inlet tube (1) that is divided into two branch pipes (2,4) for connecting with a normal temperature desulfurizer and a hydrodesulfurization device, respectively. The temperature of hydrogenation catalyst of the hydrodesulfurization device which supplies raw fuel to the desulfurizer, is lower than the operating temperature during operation start time. The raw fuel is supplied to the hydrodesulfurization device for de-sulfurizing the fuel when temperature of catalyst of hydrodesulfurization device reaches specific operating temperature.    USE - Desulfurization system of raw fuel for fuel hydrogen production of polymer electrolyte fuel cell (PEFC). Can also be used in solid oxide fuel cell.    ADVANTAGE - The replacement of de-sulfurizing agent in the normal temperature desulfurizer is not required and increase in capacity of adsorption agent of desulfurization system is suppressed. Hence, desorption and leak of sulfur content from adsorption agent by temperature variation are eliminated efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the desulfurization system of raw fuel. (Drawing includes non-English language text)    Raw fuel inlet tube (1)    Branch pipes (2,4)    Raw fuel outlet tubes (3,5)    Hydrogen supply pipe (7)    Shut-off valves (a-c)
NOVELTY - Fertilizer, contains combination of urea and component obtained by processing hen dropping combustion ash with sulfuric acid.    USE - The fertilizer is useful for growing and producing edible plant having reduced nitrate content (claimed), which is useful for preventing methemoglobin blood disease caused by excessive intake of nitrate. Uses include but not limited to vegetable e.g. spinach, lettuce, cabbage, carrot, potato, onion, yam, tomato and pumpkin, grain plants e.g. rice, wheat and millet, bean plants e.g. soybean and adzuki bean plant, and fruit trees e.g. citrus fruit, apple and kiwi trees.    ADVANTAGE - The fertilizer enables production of vegetable and other edible plants having high safety, as the nitrate content of the plant is reduced. The fertilizer is produced using industrial waste.
NOVELTY - A fluidity improver contains component (a) containing aromatic carboxylic acid compound (1) and amino compound or substituted benzene compound (2).    USE - Fluidity improver is used for biodiesel fuel composition (claimed).    ADVANTAGE - The fluidity improver efficiently improves low-temperature fluidity of biodiesel fuel.    DETAILED DESCRIPTION - A fluidity improver contains component (a) containing aromatic carboxylic acid compound of formula (1) and amino compound or substituted benzene compound of formula (2). The amino compound is of formula: HN(-R5)(-R6).    R1,R3,R21,R23=H or hydrocarbyl optionally having sulfur, oxygen and/or nitrogen;    R2,R4=R1 or carboxy;    R5,R6=H or 8-22C hydrocarbyl optionally having oxygen and/or nitrogen;    R22,R24=R2 or group of formula: -C(=O)-N(-R25)-R26;    R25,R26=R5;and    R27,R28=group of formula: HN(-R5)(-R6).    R2 and R3, R3 and R4 optionally combine together, to form a ring. R2 and R4, and R22 and R24 are not carboxyl group simultaneously. R5 and R6, and R25 and R26 are not H simultaneously. R22 and R23, R23 and R24 optionally combine together, to form a ring. An INDEPENDENT CLAIM is included for biodiesel fuel composition, which contains the fluidity improver and biodiesel fuel.
NOVELTY - Increasing production level of isoprenoids in an algal cell comprises increasing expression of a polynucleotide sequence that encodes 4-hydroxy-3-methylbut-2-enyl diphosphate reductase (IDS) in the cell.    USE - The methods are useful for increasing production level of isoprenoids in algal cell; and for increasing production level of carotenoids in algal cell (all claimed). Isoprenoids are useful as biofuels, nutraceuticals, commercial flavor and fragrance compounds as well as antimalarial and anticancer drugs. Carotenoids are useful for pharmaceuticals, food supplements, electro-optic applications, animal feed additives, and colorants.    ADVANTAGE - The invention provides improved host cells that provide for increased production of isoprenoids or carotenoids.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a method for increasing production level of carotenoids in an algal cell comprising increasing expression of a polynucleotide sequence that encodes phytoene desaturases (PDS) in the cell; and    (2) an algal cell comprising a polynucleotide sequence that is genetically engineered to express a higher level of IDS than a corresponding wild type algal cell, where the cell produces an increased level of isoprenoids than a corresponding wild type algal cell; or an algal cell comprising a polynucleotide sequence that is genetically engineered to express a higher level of PDS than a corresponding wild type algal cell, where the cell produces an increased level of carotenoids than a corresponding wild type algal cell.
NOVELTY - The method involves sintering metal powder on the surface (2) of a metal sintering porous substrate (3). A hydrogen separation film is formed integrated on the surface of the metal sintering porous substrate sintered with metal powder to smooth the surface. A thin film is formed on the smoothed surface of the metal sintering porous substrate.    USE - Method for manufacturing metal porous substrate used in polymer electrolyte fuel cell. Can also be used in hydrogen gas purification installation and hydrogen gas manufacturing equipment.    ADVANTAGE - Since the thin film is formed on the smoothed surface of the metal sintering porous substrate, the generation of crack or pinhole while forming the thin film is prevented. The function of the fuel cell is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for metal sintering porous substrate.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the barrier property testing apparatus.    Pressure tank (1)    Surface (2)    Metal sintering porous substrate (3)    Air exit portion (4)    Pressure gauge (5)
NOVELTY - The method involves providing a separator (600) having anode and cathode plates (300,400) and an intermediate plate (500). A lamination resin (777) is arranged to peripheral portion of cathode and anode plates, and is heated so that resin is attached to the peripheral portion. The peripheral portion of anode and cathode plates is dragged in.    USE - Manufacturing method of fuel cell.    ADVANTAGE - The generation of short circuit is suppressed since the lamination resin is contacted with separator. The attachability and assemblability of fuel cell are improved and fuel cell can be manufactured at low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for separator.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the fuel cell.(Drawing includes non-English language text)    Anode plate (300)    Cathode plate (400)    Intermediate plate (500)    Separator (600)    Lamination resin (777)
NOVELTY - The method involves providing a raw material (10) of a continuous carbon-fiber composite in a semi-cured state. The raw material is formed corresponding to the length and shape of a fuel cell separator. The raw material is stacked and adhered according to the length of the separator. The raw material is provided on a high temperature hot-press (22) that is heated and pressed. Unnecessary portions are removed from the separator, and the obtained separator is post-cured. A carbon black conductive powder for improving electrical conductivity is mixed with a polymer binder.    USE - Method for manufacturing a fuel cell separator (claimed) that is utilized for producing electricity through an electrochemical reaction of hydrogen and oxygen.    ADVANTAGE - The method reduces the processing time of the fuel cell separator and increases the work safety, and offers good electrical conductivity across fibers.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a method for manufacturing a fuel cell separator.'(Drawing includes non-English language text)'    Raw material (10)    Roller (12)    Milling roller (18)    Pile/compression roller (20)    High temperature hot-press (22)
NOVELTY - Methane fermentation treatment of organic waste involves heating organic waste in adjustment tank (2) and carrying out solubilization processing, carrying out methane fermentation treatment of liquid waste from adjustment tank in methane fermentation tank (5), carrying out heat sterilization processing of digested sludge from methane fermentation tank by sterilization tank, returning part of liquid fertilizer discharged from sterilization tank to adjustment tank, and using liquid fertilizer as dilution water of organic waste.    USE - Methane fermentation treatment of organic waste.    ADVANTAGE - The method reduces heat consumption, and stably and efficiently performs methane fermentation treatment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a methane fermentation treatment system of organic waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the processing system. (Drawing includes non-English language text).    Preprocessor (1)    Adjustment tank (2)    Circulation pump (3)    Pumping pump (4,6)    Methane fermentation tank (5)
NOVELTY - A culture medium formulation comprises carbon source and organic nitrogen source comprising edible fungus husk, wheat bran, and maize flour; urea as inorganic nitrogen source; inorganic salt comprising dipotassium hydrogen phosphate, potassium dihydrogen phosphate, magnesium sulfate, carbendazol, sea salt, and calcium superphosphate; and vitamin B1.    USE - Culture medium formulation for producing fuel alcohol (claimed).    ADVANTAGE - The formulation can reuse the edible fungus husk, saves grain consumption, reduces production cost of fuel alcohol, and recycles agriculture resource effectively.
NOVELTY - A binder comprises (pts.wt.) asphalt powder (10-15), coal tar (10-16), tar residue (14-17), MF4 (0.1), nitric oxide (0.1), sodium corrosive acid (1.2-2.5), dodecylbenzene sulfonic acid (0.3), polyethylene-acid amide (0.5), astringing first grade cellulose (1-1.5), sodium hydroxide (2) and dextrin (1).    USE - A binder for producing coke used in metallurgy, chemical fertilizer or calcium carbide industries.    ADVANTAGE - The binder can easily produce coke having cool intensity after drying of 70-90 kg/single ball; cannot be dispersed or powderized at high temperature (1300 degrees C); has good chemical activity and small weight reduction of stable carbon; and uses additive which does not comprise chemical composition of magnesium, phosphorus, aluminum and iron.
NOVELTY - The boiler has a reinforcing combustion chamber made of fire-resistant insulating material, and an ash collecting chamber and a thermolysis combustion chamber provided with a water jacket. A water cooling grate is fixed at a lower end of the thermolysis combustion chamber. A gas distribution chamber is connected with a heat exchange chamber, and a flue is connected at a top end of the heat exchange chamber. The water jacket and the water cooling grate are connected with a water tank of the heat exchange chamber at a side of the thermolysis combustion chamber.    USE - Firewood straw direct combustion type boiler.    ADVANTAGE - The boiler realizes the direct combustion of the firewood straw, ensures high thermal value of the firewood straw, high thermal intensity, provides a workable way for processing the firewood straw, completely utilizes the firewood straw, and reduces the environment pollution caused by incinerating the firewood straw.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a firewood straw direct combustion type boiler combustion technique.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial sectional view of a firewood straw direct combustion type boiler.
NOVELTY - A water-based insect aerosol comprises (wt.%) insecticide including tetramethrin (0.1-0.2), D-cyphenothrin (0.1-0.2) and R-d-trans-prallethrin (0.05-0.1); solvent including n-alkane (4-5) and deionized water (49-52); emulsifier including sorbitan monooleate (0.8-1.4) and polyoxyethylene sorbitan monooleate (0.2-0.6); and propellant including dimethyl ether (41-44.5).    USE - A water-based insect aerosol.    ADVANTAGE - The insect aerosol is environmentally friendly. The solvent does not include kerosene, so that after spraying, the room does not have a kerosene smell, and surface of object does not have an oil mark.
NOVELTY - Anaerobic co-metabolism treatment of coal chemical engineering wastewater comprises taking anaerobic grain sludge as primary mud source and methanol as co-metabolism matrix; controlling ratio of chemical oxygen demand (COD) added in methanol and in the wastewater each day to 0.1-0.5 and hydraulic retention time of water of 24 hours; and controlling the stable working condition.    USE - Method of anaerobic co-metabolism treatment of coal chemical engineering wastewater (claimed).    ADVANTAGE - The method improves anaerobic biodegradability of the wastewater, shortens start-up time of the reactor and solves the problem of difficult anaerobic treatment of coal chemical engineering wastewater. After stable operation, the COD removal can reach to more than 50% and the removal of total phenol reaches 70-80%.    DETAILED DESCRIPTION - Anaerobic co-metabolism treatment of coal chemical engineering wastewater comprises selecting phenols as main pollutant, coal chemical engineering wastewater with 3000-4000 mg/L COD and total phenol concentration of 600-800 mg/L as wastewater for treatment; placing anaerobic grain sludge as primary mud source in a middle temperature anaerobic reactor which can preserve temperature at 32-35 degrees C and allowing to stand for 12-24 hours; adding methanol as co-metabolism matrix to wastewater such that the amount of COD in the methanol and in the wastewater each day is controlled at 0.1-0.5; introducing the wastewater with methanol to the anaerobic reactor and allowing hydraulic retention time of 24 hours; and controlling the stable working conditions and operating for three months to reach the stable working condition based on ratio of methanol batching.
NOVELTY - A wood wax oil comprises (pts. wt.) vegetable oil (75-85), vegetable or animal wax (0.1-1), rosin resin (11-22), siccative (1-2), and co-solvent (0.1-1).    USE - Wood wax oil for insect prevention.    ADVANTAGE - The oil is environment-friendly and can completely permeate into wood. It can keep fine performances of the wood in long time and can prevent cracking of wood. The wood has excellent performance, is flame retardant, and has improved use quality.
NOVELTY - Manufacture of anti-acarid nonwoven fabric comprises mixing and stirring low melting index polypropylene with anti-acarid masterbatch in vacuum, squeezing and melting in screw extruder to form hot melt mass, filtering, measuring, distributing and spinning in spinning box, cooling spun filaments by side blowing, drawing primary filaments in drawing device, forming fiber net in net forming machine, thermally pressing in thermal pressing machine, and rolling the obtained nonwoven material using a rolling machine. The method uses an automatic three-component measuring, mixing and feeding system.    USE - Manufacture of anti-acarid nonwoven fabric (claimed).    ADVANTAGE - The nonwoven fabric is comfortable to use; and has abundant raw material source, low manufacturing cost, high strength, washing resistance, anti-acarid effect and durability. The method is short, fast and environmentally friendly.
NOVELTY - A magnetic nanometer material is used as oxidation reduction catalysts for catalyzing hydrogen peroxide to generate into hydroxy free radical.    USE - Magnetic nanometer material used as oxidation reduction catalysts, preferably for catalyzing hydrogen peroxide to generate into hydroxy free radical, useful in treatment of organic pollutants, treatment of organic wastewater, decoloration of dye wastewater, sterilization and algae removal, degeneration of toxic composition, or oxidation of organic agricultural chemicals (claimed).    ADVANTAGE - The material has low cost, easy preparation, and high stability. It can be reclaimed and repeatedly used, and has no secondary pollution.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a method of using magnetic nanometer materials for treating organic pollutants;    (2) a method for reclaiming magnetic nanometer material using magnet or centrifugal effect; and    (3) a method for regenerating magnetic nanometer material.
NOVELTY - Imidazole derivatives (I), and their agrochemically usable salts, are new.    USE - In fungicidal composition for controlling or protecting against phytopathogenic microorganisms, preferably fungal organisms; controlling or preventing an infestation of crop plants, harvested food crops or non-living materials by phytopathogenic or spoilage microorganisms or organisms potentially harmful to man; and in the manufacture of a medicament for treatment of cancer (claimed). The phytopathogenic microorganisms are selected from, e.g. Alternaria sp., Ustilago spp..    ADVANTAGE - The compound (I) has excellent activity at low rates of application, well tolerated by plants, and environmentally safe. Also the compound (I) has curative, preventive and systemic properties, and used for protecting numerous cultivated plants.    DETAILED DESCRIPTION - Imidazole derivatives of formula (I), and their agrochemically usable salts, are new.    R 1=halo or 1-4C (halo)alkyl;    R 2=optionally substituted aryl;    R 3=halo or OR 7;    R 4and R 5=H, halo or OR 7;    R 6=halo or 1-4C alkyl;    R 7=H, 1-6C (halo)alkyl, 3-7C cycloalkyl, 3-10C cycloalkylalkyl, 2-6C (halo)alkenyl, 3-7C cycloalkenyl, 2-6C (halo)alkynyl, 2-6C alkyloxyalkyl, 3-8C dialkylaminoalkyl, 4-10C cycloalkylaminoalkyl or 4-10C heterocyclylalkyl.    Provided that when R 3is halo, at least one of R 4or R 5is OR 7; and when R 3is OR 7, at least one of R 4or R 5is OR 7or halo. INDEPENDENT CLAIMS are included for the following:    (1) preparation of the imidazole derivatives (I); and    (2) fungicidal composition for controlling or protecting against phytopathogenic microorganisms, comprising the compound (I) as active ingredient, in free form or in agrochemically usable salt form, and at least one adjuvant.
NOVELTY - A biodiesel composition comprises a biodiesel fuel component; an alcohol component; a water component; an anhydrous emulsifier component, comprising glyceryl monooleate or ammonium oleate, present in an amount enough for the biodiesel fuel, alcohol, water, and emulsifier components to form an emulsion; and a cetane-enhancer component.    USE - Biodiesel composition for use in internal-combustion engines.    ADVANTAGE - The biodiesel composition uses high purity glyceryl monooleate providing the composition thermal stability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a diesel composition for use in internal-combustion engines, comprising a diesel fuel component; an alcohol component; a water component; an anhydrous emulsifier component as above; and a cetane-enhancer component.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram that shows a new method for synthesizing monoglycerides.
NOVELTY - An isolated microorganism designated as bacterial isolate S. putrefaciens LH4:18 (ATCC No. PTA-8822), is new.    USE - The isolate is useful for improving oil recovery from an oil reservoir, for promoting hydrocarbon bioremediation, and for promoting oil pipeline maintenance (all claimed).    ADVANTAGE - The present invention provides Shewanella species utilized in enhanced oil recovery.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are: (1) an oil recovery enhancing composition comprising S. putrefaciens LH4:18 (ATCC No. PTA-8822), one or more electron acceptors, and at least one carbon source; (2) a method for improving oil recovery from an oil reservoir by (i) providing a composition comprising as bacterial isolate S. putrefaciens LH4:18 (ATCC No. PTA-8822), and minimal medium comprising simple nitrates capable of promoting the growth of the isolate, and (ii) inoculating the reservoir with the composition of (i), where growth of the isolate, under denitrifying conditions, in the oil reservoir promotes improved oil recovery; (3) a method for promoting hydrocarbon bioremediation by applying bacterial isolate S. putrefaciens LH4:18 (ATCC No. PTA-8822) to an area contaminated with hydrocarbons; and (4) a method for promoting oil pipeline maintenance by applying bacterial isolate S. putrefaciens LH4:18 (ATCC No. PTA-8822) to an oil pipeline.
NOVELTY - A pyrazol-4-yl-carboxylic acid amide compound or its salts, isomers, structural isomers, stereoisomers, diastereoisomers, enantiomers, tautomers or N-oxides, is new.    USE - As active ingredient in the composition for controlling and protecting against phytopathogenic microorganisms (claimed); also useful for protecting plants e.g. barley, rye, oat, rice against diseases caused by phytopathogenic microorganisms e.g. fungi, bacteria or viruses.    ADVANTAGE - The compounds has excellent activity at low rates of application; is well tolerated by plants; and is environmentally safe.    DETAILED DESCRIPTION - A pyrazol-4-yl-carboxylic acid amide compound of formula (I) or its salts, isomers, structural isomers, stereoisomers, diastereoisomers, enantiomers, tautomers or N-oxides, is new.    R1=H or 1-4C alkyl;    R2=H or 1-4C alkyl;    R3=H or 3-7C cycloalkyl;    B'=group of formula (i);    R4=H, halo or 1-6C alkyl;    R5=H or halo;    R6=H, halo, 1-6C alkyl, 2-6C alkenyl, 3-6C alkinyl, 3-6C cycloalkyl-3-6C alkinyl, halophenoxy, halophenyl-3-6C alkinyl, C(1-4C alkyl)=NO-1-4C alkyl, 1-6C haloalkyl, 1-6C haloalkoxy, 2-6C haloalkenyl or 2-6C haloalkenyloxy;    R7=H or halo;    R8=H, halo, 1-6C alkyl, 1-6C alkoxy;    G'=(CH2)2, (CH2)3, (CH2)2O or CH2OCH2;    A'=group of formula (ii);    R9=H or 1-4C alkyl;    R10=1-4C alkyl, 1-4C haloalkyl or halo;    R11=H or halo.    An INDEPENDENT CLAIM is included for new intermediates of N-(2-hydroxy ethyl)pyraszol-4-yl carboxylic acid amides of formula (II), N-(3-hydroxy propyl)pyraszol-4-yl carboxylic acid amides of formula (III), oxazole compound of formula (IV), and amine compounds of formula (V) and (VI).    X1=-S(O)- or -S(O)2-.
NOVELTY - A composition comprises (wt.%): pentafluoroethane (17-22), 1,1,1,2-tetrafluoroethane (77-81) and n-butane (1-2); and optionally at least additive.    USE - As heat transfer compositions used in air-conditioners, freezers, refrigerators, heat pumps, water chillers, flooded evaporator chillers, direct expansion chillers, walk-in coolers, heat pumps, mobile refrigerators, and/or mobile air conditioning units; and also as aerosol propellant, foaming agents, blowing agents, solvents, cleaning agents, carrier fluids, displacement drying agents, buffing abrasion agents, polymerization media, expansion agents for polyolefins and polyurethane, gaseous dielectrics, extinguishing agents, and fire suppression agents in liquid or gaseous form.    ADVANTAGE - The compositions are used as heat transfer compositions that achieve a balance of properties and performance characteristics including non-flammability, heat transfer capacity, environmental goals, effects in equipment, and system energy efficiency; and also have improved lubricant viscosity, improved oil-return in use in vapor compression heat transfer system, superior solubility with mineral oil while remaining below industry acceptable flammability performance.
NOVELTY - Additive comprises a (meth)acrylic polymer obtained by polymerization of at least one (meth)acrylic monomer, where at least 20%, preferably at least 50% of carbon of the monomer is originated from renewable sources according to ASTM D6866.    USE - The polymer is useful as additive to improve cold resistance of biofuels with distillate oil (claimed).    ADVANTAGE - The additive improves the flow properties of oil, prevents the agglomeration of crystals and delays or modifies the crystallization of paraffins.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a process for preparing the (meth)acrylic monomer of formula (R1-C(=O)-Z1-R3-Z2-C(=O)-C(R4)=CH2) (I), comprising reacting ester compound of plant or animal oil of formula (R1-COO-R2) with a bifunctional compound of formula (X-R3-Y1) followed by the reaction with (meth)acrylic ester compound of formula (CH2=C(R4)-C(=O)-OR5); and    (2) the (meth)acrylic polymer obtained by radical polymerization of (meth)acrylic monomer.    R1 = 8-30C alkyl;    R4 = H or methyl;    Z1, Z2 = O, NH or NR1a;    R1a = 1-8C alkyl; and    R3 = 2-20C alkylene and optionally comprising at least unsaturation or heteroatoms such as N or O.
NOVELTY - Acinetobacter sp. PSGB03 strain is separated from intestine of Plutella xylostella larva, and is new. The Acinetobacter sp. PSGB03 strain has deposition number (KACC 91364P).    USE - Acinetobacter sp. PSGB03 strain for use as biofertilizer for promoting plant growth (claimed).    ADVANTAGE - The Acinetobacter sp. PSGB03 strain promotes growth of plant in a cost-effective manner and is eco-friendly.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a recombinant microbe for promoting plant growth;    (2) a method for manufacturing the biofertilizer; and    (3) a method for promoting growth of plant, which involves dipping Acinetobacter species PSGB03 strain, Acinetobacter species PSGB04 strain, Pseudomonas species PRGB06 strain or Pseudomonas species PRGB11 strain with indole 3-acetic acid and salicylic acid for azofication.
NOVELTY - Manufacturing of culturing algae and refining oil coupled by processing organic sewage water and residue comprises: (a) process of organic sewage water and residue; (b) marsh gas power generation and heat supply; (c) using carbon dioxide flue and organic sewage, cultivating marsh gas and collecting micro-alga; (d) comprehensive utilization of the oily micro-algae; and (e) pre-treatment of the micro-algae oil and ester exchange reaction.    USE - The method is useful for manufacturing of culturing algae and refining oil (claimed).    ADVANTAGE - The invention couples the organic sewage water and residue process, micro-algae culturing and machining and biologic diesel refining, which does not only reduces manufacturing cost, but also realizes clean production of biologic diesel and treats three wastes.
NOVELTY - A Bacillus subtilis 203, where it is stored in CGCC in Wuhan University, Luojiashan, Wuchang, Wuhan, Hunan on July 2nd, 2007 with preservation number CCTCC No: M207094.    USE - The B. subtilis is useful in plate antagonism effect for No. 4 Fusarium oxysporum f.sp.cubens; for preventing the browning or rotting of main root and vascular bundle of banana plant; and in antagonism effect for cotton fusarium wilt, Verticillium dahliae, Fusarium oxysporum f.sp.niveum, tomato Fusarium wilt, Curvularia lunata or Gloeosporium musarum (all claimed).    ADVANTAGE - The B. subtilis 203 is environment-friendly and safe, and it has high prospect in development and application.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for preparing the B. subtilis 203, where it is obtained via plate facing and screening.
NOVELTY - Preparing fuel ethanol by using alocasia as raw material, comprises: (a) smashing and pulping the collected alocasia; (b) steaming or boiling the alocasia slurry; (c) fermenting the alocasia raw material; and (d) crude distilling, rectifying and dewatering the fermented product.    USE - The method is useful for preparing fuel ethanol by using alocasia as raw material (claimed).    ADVANTAGE - The method reduces the production cost of the fuel ethanol in torrid-subtropical regions, and improves the production efficiency; the method can bring some fine social and economic benefits.    DETAILED DESCRIPTION - Preparing fuel ethanol by using alocasia as raw material, comprises: (a) smashing pulping the collected alocasia; (b) steaming or boiling the alocasia slurry prepared by (a) for 1 hour at 80-100 degrees C; and cooling to 60 degrees C; adjusting the pH value as 4.0-4.5; adding diastatic enzyme according to raw material proportion of 80-200 units/g; and hydrolyzing for 1 hour at constant temperature to carry out detoxification and saccharification; (c) fermenting the alocasia raw material processed by (b) to transform sugar into ethanol; and (d) crude distilling, rectifying and dewatering the fermented product of (c) to obtain the fuel ethanol.
NOVELTY - Repellent composition comprises 0.1-55.5% of lambda-cyhalothrin, 0.2-9% of vermin flavor, 0.5-7.5% of insecticidal plant extract, 0.4-21.5% of emulsifier, 0.1-6.5% of antioxidant and 33-96.8% of solvent containing essential ingredient.    USE - Repellent composition for killing insects and for use as paint sealant for coating on fabric, garment, military uniform, tile, wallpaper, mosquito net, door, window frame, anti-glare, bimetal, curtain, carpet, laminated paper, kitchen appliance, and plastic molding product (claimed).    ADVANTAGE - The repellent composition is eco-friendly, has excellent insecticidal and repellent effects, and prevents from disaster of chigger.
NOVELTY - Method for decomposing keratin containing material, involves decomposing keratin containing material in presence of microorganisms belonging to Meiothermus that can decompose organic waste and can be used as an acidic manure.    USE - The method is useful for decomposing keratin containing material, which can be used as acidic manure (claimed). The keratin containing material includes feather and hair.    ADVANTAGE - The keratin containing material can be decomposed easily.
NOVELTY - Apparatus for manufacturing water soluble saccharides from paper sludge involves hydrolysis processing unit which adds water-soluble gas catalyst at normal temperature and atmospheric pressure in a pressurized water while heating to 120-250 degrees C and hydrolyze paper sludge, and catalyst recovering unit which recovers the catalysts from the product.    USE - Apparatus for manufacturing water soluble saccharides from paper sludge (claimed).    ADVANTAGE - Has a simple structure, improves utilization of the paper sludge and has high yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a manufacture of water soluble saccharides.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the apparatus for manufacturing water soluble saccharides. (Drawing includes non-English language text).    Storage tank (11)    Inlet tube (12)    High-pressure pump (13)    Reactor (20)    Solid-liquid-separation device (21)
NOVELTY - Organic sewage is purified by settling and separating sand, big particles and impurities; settling and separating mud by biological flocculation; purifying sewage using plant, animal and microorganism; allowing the mud to enter a marsh gas tank for fermentation, and feeding earthworm on the mud of the marsh gas tank and the sand of a sand settling tank.    USE - Method for purifying organic sewage including non-toxic organic sewage, farm sewage, domestic sewage and municipal sewage.    ADVANTAGE - The dung left by the earthworm is used as organic fertilizer with good quality. The sewage is converted into clean water without noise from a machine and without odor. The settling and purifying system works without any human monitoring. Fishes and hydrophytic vegetable can be fed in the system for additional income. The marsh gas is taken as the energy while the earthworm is the feed or traditional Chinese medicinal material. The method has small investment and easy operation, uses system with simple structure, and saves electricity and labor. The purified water can be recycled and reaches first-grade state discharge standard.
NOVELTY - Apparatus (20) comprises a main body (10), an evaporation pad (1), a feed port (5), an exhaust blower (7), a vibration damping shell (8), an inlet port (11), and an outlet port (12), which is connected to the exhaust blower. The evaporation pad is inserted inside of the main body. The feed port is equipped at upper side of the main body. The inlet port is equipped at rear part of the main body.    USE - Apparatus for vaporizing pyroligneous liquor composition.    ADVANTAGE - The pyroligneous liquor composition vaporizing apparatus is eco-friendly and cost-effective.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic front view of the pyroligneous liquor composition vaporizing apparatus.    Evaporation pad (1)    Feed port (5)    Exhaust blower (7)    Vibration damping shell (8)    Main body (10)    Inlet port (11)    Outlet port (12)    Apparatus (20)
NOVELTY - An apparatus comprises a reaction bath (1), and an organic waste reservoir (2) connected to the reaction bath. A microorganism activity inhibitor reservoir (3) is connected to a gas reservoir (11). A reaction container and hydrogen gas separation apparatus (8) are connected to the bio hydrogen gas production reactor. A gas conveying line (10) is also connected to hydrogen gas separation apparatus and reaction container.    USE - Apparatus for producing bio-hydrogen gas from organic waste.    ADVANTAGE - The apparatus enables to produce the bio-hydrogen gas with high efficiency in a cost-effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for producing bio-hydrogen gas from organic waste, which involves injecting organic waste into reaction bath, injecting methane producing microorganisms in the reaction bath, injecting inert gas inside the reaction bath and organic waste, where generated bio-hydrogen gas is collected.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the apparatus for producing bio-hydrogen gas from organic waste.    Reaction bath (1)    Organic waste reservoir (2)    Microorganism activity inhibitor reservoir (3)    Hydrogen gas separation apparatus (8)    Gas conveying line (10)    Gas reservoir (11)
NOVELTY - Biogas generator using organic waste comprises dry anaerobic digester, gas holder, sludge undercurrent, and gas inside bin.    USE - The generator is useful for producing biogas.    ADVANTAGE - The invention has improved recovery rate and low cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biogas generator.
NOVELTY - An environment friendly composition with excellent cleaning, sterilizing power, and fungicide activity; where it exhibits the powerful sterilizing power, and the fungicide power in the chelate resin in the addition of the organic antibacterial agent nano silver that dips while having the nature surfactant in which the material extracts from the excellent non-ionic surfactant is manufactured with the material as the cleansing source liquid expecting the extirpates vermin effect, is new.    USE - The environment friendly composition is useful for cleaning, and sterilizing power, where it has excellent fungicide activity (claimed).    ADVANTAGE - The materials, and the natural material heater sterilization and cleaning composition are harmless in the human body.    DETAILED DESCRIPTION - An environment friendly composition with excellent cleaning, sterilizing power, and fungicide activity; where it exhibits the powerful sterilizing power, and the fungicide power in the chelate resin in the addition of the organic antibacterial agent nano silver that dips while having the nature surfactant in which the material which extracts from the excellent non-ionic surfactant is manufactured with the material as the cleansing source liquid expecting the extirpates vermin effect, and heater sterilization and cleaning; and can maximize the extirpates vermin effect with the addition of the mixture of fir and the natural material extracted from the cypress timber, is new.
NOVELTY - Bamboo charcoal manufacturing involves heating deep deep-ocean water, where the heated deep-ocean water is concentrated. The concentrated deep-ocean water is carbonized by adding mineral content, where bamboo cuts pieces are added to the treated deep sea water including mineral content.    USE - Method for manufacturing bamboo charcoal having high mineral content by using deep-ocean water.    ADVANTAGE - The bamboo charcoal manufacturing method enables to produce the bamboo charcoal having high mineral content by using deep-ocean water in a convenient and cost-effective manner.
NOVELTY - A coking gas is introduced into a hydration reactor and made to counter-contact with hydrate working fluid from top portion of the hydration reactor. Methane contained in the coking gas is hydrated with water in the hydrate working fluid to form hydrate, and hydrogen in the coking gas is simultaneously concentrated to obtain hydrogen of high concentration. The operation pressure and operation temperature of the hydration reactor is 0.20-1 MPa and 3-15 degrees C, respectively. Thus, low-pressure treatment of coal coking gas is enabled.    USE - Treatment of coal coking gas for production of methane and hydrogen.    ADVANTAGE - The method enables efficient and economical low-pressure treatment of coal coking gas and manufacture of methane and hydrogen of high concentration, with suppressed energy consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus for low-pressure treatment of coal coking gas.
NOVELTY - Method for reacting, extracting and upgrading biomass pyrolysis oil, by adding biomass pyrolysis oil, low-carbon alcohol and catalyst to reaction kettle, adding hydrogen peroxide water solution to the oxidant, reacting, lowering temperature after total reflux reaction, concentrating and layering, separating black oil phase at upper layer after distilling, gathering cut fraction and distilling to obtain black thick liquid as the product, diluting the solution using methanol to obtain modified biomass oil having pH of 4-6 and water content of 0.5-2.0%.    USE - The method is useful for reacting, extracting and upgrading biomass pyrolysis oil (claimed).    DETAILED DESCRIPTION - Method for reacting, extracting and upgrading biomass pyrolysis oil, involves (a) adding biomass pyrolysis oil, low-carbon alcohol and catalyst in the ratio of 100:40-100:2-10 to a reaction kettle, adding hydrogen peroxide water solution (30%) in the ratio of 100:20-60 of the biomass pyrolysis oil to the oxidant, and heating and reacting for 5-8 hours at 80-100 degrees C, (b) lowering the temperature after completing the total reflux reaction, concentrating and layering, where the lower layer has clear transparent water solution, (c) separating the black oil phase at the upper layer after distilling at 80 degrees C and at 10 KPa, gathering the cut fraction and completing distilling to obtain black thick liquid as the product, and (d) diluting the solution whose ratio of product to methanol is 4:1, using methanol to obtain modified biomass oil having pH of 4-6, density of 1.0-1.1 g/cm3, water content of 0.5-2.0%, thermal value of 25.0-30.0 kJ/g, and viscosity of 36-40 mm2/s at 30 degrees C.
NOVELTY - Alcohol-based fuel comprises (in weight%) petrochemical fuel (50-64), methanol (30-42), acetone (1.5-2), isobutyl alcohol (3-5), zinc peroxide (0.5-1), isoamylene (0.05-0.1), barium salt of phosphosulfurized polyisobutylene (0.05-0.1), phenol (0.05-0.1), polyalkenyl succinimide (0.05-0.1), isopropyl alcohol (0.01) at lower than -10 degrees C in winter, ferrocene (0.3) when sulfur content of material is higher than 0.08, and phytate (0.3) during storing or transporting mass of fuel.    USE - The alcohol-based fuel is useful in diesel engines.    ADVANTAGE - The alcohol-based fuel exhibit high stability, saves energy, has corrosion resistance, is cost-effective, and does not cause environmental pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing alcohol-based fuel, which involves initially mixing all crude materials except petrochemical fuel and maintaining for more than 3 hours to obtain modified mixture, then mixing the petrochemical fuel with the modified mixture, uniformly stirring the obtained mixture, maintaining for more than 3 hours, and then obtaining the alcohol-based fuel.
NOVELTY - Clean and energy-saving methanol diesel oil comprises (in weight%) methanol (10-40), diesel oil (40-70) and auxiliary agent (5-20).    USE - Clean and energy-saving methanol diesel oil.    ADVANTAGE - The methanol diesel oil is inexpensive, nonvolatile, highly pure, saves energy and non-corrosive, has high flash point and hexadecane number of methanol, exhibits complete combustion, excellent compatibility and stability, and does not cause environmental pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing clean and energy-saving methanol diesel oil, which involves mixing methanol, auxiliary agent and diesel oil for 5-30 minutes, after the color is bright to obtain clean and energy-saving methanol diesel oil.
NOVELTY - Combustible gas containing solid fuel, comprises (in weight parts) sludge (150-330), animal feces (370-450) and plant powder (300-400). The odor removing agent (0.1-0.3) is added during winter. The odor removing agent (0.5-0.7) is added during summer. The composition further comprises fermenting agent. The fermenting agent (0.2-0.5) is added during winter. The fermenting agent (0.1-0.2) is added during summer.    USE - As combustible gas containing solid fuel (claimed).    ADVANTAGE - The composition saves energy and reduces the discharge of harmful substance, thus eco-friendly. The composition improves 10-20% of heat value and saves 25-30% of efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of producing combustible gas containing solid fuel, which involves adding odor removing agent into sludge, mixing the components with plant powder, adding fermenting agent into animal feces and stirring the obtained mixture using stirrer and piling the mixture using molding machine.
NOVELTY - A coal-bed methane is supplied to a hydration reactor from bottom to contact with a hydrate working fluid. The hydration reaction is carried out between the coal-bed methane and hydrate working fluid to generate hydrate which is removed from the coal-bed methane. The hydration reactor is operated at 3-18 degrees C and pressure of 0.11-0.85 MPa.    USE - Method used for low-pressure treating coal-bed methane.    ADVANTAGE - The method treats coal-bed methane with oxygen at low pressure, and lowers the exhaust amount of methane, and is eco-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus for low pressure treating coal-bed methane, which has a hydration reactor with combined structure of a sprayer and a sieve plate, a spraying zone with a nozzle for spraying hydrate working fluid at the upper portion of the reactor, a sieve zone with sieve plates at lower portion of the reactor and a cooling coil for removing heat during reaction and provided inside the reactor, a coal-bed methane inlet and a hydrate slurry outlet provided at the bottom of the reactor, a hydrate working fluid inlet and a purified gas outlet provided at top of the reactor and a porous filter plate for concentrating the hydrate concentration of hydrate slurry and arranged inside the reactor close to the hydrate slurry outlet. The hydrate slurry outlet is arranged at lateral bottom of the hydrate reactor. The filter plate inclines to the hydrate slurry outlet. The angle between the filter plate and the horizontal surface is 5-15 degrees . The projection area of filter plate at the hydration reactor plane is 60-75% of the inner section area of the reactor. The hole diameter of hole in the filter plate is 3-8 mm. The total hole opening area is 5-20% of the filter plate area.
NOVELTY - An automatic production apparatus comprises a reactor, an ion exchange filter (5), and a control system (4) for controlling solenoid valve (11) and motor. The solenoid valve, and a heater (7) are connected to a temperature controller, and the solenoid valve is controlled with a timer. The heater is connected to the temperature controller, which is connected to a mixer (6).    USE - Automatic production apparatus for producing biodiesel.    ADVANTAGE - The automatic production apparatus produces the biodiesel from vegetable waste in an eco-friendly manner by recycling environmental contamination including oil resources.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the automatic production apparatus for producing biodiesel.    Control system (4)    Ion exchange filter (5)    Mixer (6)    Heater (7)    Solenoid valve (11)
NOVELTY - Apparatus (A) comprises a dryer unit (D), a burner (3), four transport units (51,52,53,54), a rotation unit (4), a selection unit (6), and a packing machine (8), which includes a hopper (1) and a drum (2). Raw material is transferred into the latter transport unit from the former transport unit. The raw material is kept into the hopper for drying. The rotation unit is connected to the burner.    USE - Apparatus for manufacturing compost.    ADVANTAGE - The apparatus enables to mass production of the compost with proper particle size.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the apparatus.    Hopper (1)    Drum (2)    Burner (3)    Rotation unit (4)    Selection unit (6)    Packing machine (8)    Transport units (51,52,53,54)    Apparatus (A)    Dryer unit (D)
NOVELTY - Fertilizer composition comprises 50-90 wt.% of natural plant vinegar and microorganism.    USE - Fertilizer composition for pyroligneous liquor.    ADVANTAGE - The fertilizer composition is eco-friendly and improves the resistivity of seed and disease with the organic acid.
NOVELTY - Device contains a biofermenter in form of a hollow closed container, in the bottom part of which there are pipes with air inlet openings, connected by a ventilator. The air supply system comprises an additional forced-draught fan, connected to wind pipes. The surface area of air delivery holes increases moving away from the ventilators. Air is supplied into the ventilator through a cone-shaped funnel, in which there is an electric heater. An ozoniser is fitted for concentrating air with oxygen.    USE - Agriculture.    ADVANTAGE - Shorter composting time and improved quality of the end product. 3 cl, 2 dwg
NOVELTY - Sewage disposal involves flowing sewage through a sewage drain system. Suspended solid particles are removed from the sewage, and dirty materials are also removed from the sewage in a disposal plant by filtration. Suspended solid particles are precipitated in a settling tank. The remaining sewage is transferred to an aeration tank, where sludge mass is formed which is precipitated. Silicon dioxide and methane are also generated from the sewage.    USE - Method for disposing sewage.    ADVANTAGE - The sewage disposal method is economical, eco-friendly and enables to dispose sewage efficiently in short duration.
NOVELTY - Invention refers to the field of waste flow decontamination and utilisation of the solid carbon-nitrogen containing waste with generating of biomethane for domestic needs in detached houses removed from lines of heat and power supply. Biogas generator with regulated capacity consists of lower tank, loading and deloading chutes and upper open tank. Reactor and gasholder are coincided in the lower tank. For capacity control and mixing the upper tank is connected with a lower tank with a tube.    USE - Chemistry.    ADVANTAGE - Simplifying of device construction and cost decreasing. 5 dwg
NOVELTY - Soil MALAKHIT is related to soils based on peat and biocompost obtained by utilisation of solid municipal waste used in'green'construction for cultivation of flowers and turfgrass (version 1) and coniferous scrub (version 2). Soil includes underdecomposed upper-moor peat with acidity of 2.5 pH or more and biocompost at respective weight ratio of 30:70 (version 1) and 50:50 (version 2), mineral fertilisers represented by nitrogen, phosphor and/or potassium fertilisers depending on volatile nitrogen, phosphor and potassium form content in the biocompost (versions 1 and 2), and dolomite powder (version 1). Biocompost includes aerobic fermentation products of solid municipal waste and OMUT microbe fertiliser (10 wt %) containing association of active microbes Clavibacter michiganese, Bacillus amylognefaciens, Micrococcus various, cultivated in bird droppings.    USE - Agriculture.    ADVANTAGE - Extended application sphere of solid municipal waste, improved soil quality, maintenance of active microbiological process course, improved development of plants. 4 cl, 1 dwg, 3 tbl, 5 ex
NOVELTY - Treatment of organic sewage and production of enzyme from biomass carrier comprises air-drying bagasse for 48 hours, pulverizing, and sterilizing; putting powder in enzyme producing vessel (3) sterilized by soaking in benzalkonium bromide for 24 hours, controlling temperature and dissolved oxygen content, and supplementing nitrogen-controlled culture medium every 15-30 days; and flowing organic sewage and fresh enzyme liquid in organic sewage treatment vessel (4), solidifying zymoprotein on the surface of elastic stuffing, and degrading sewage.    USE - Method of treating organic sewage and producing enzyme from biomass carrier (claimed).    ADVANTAGE - The method combines enzyme production and sewage treatment, thus reducing the cost.    DETAILED DESCRIPTION - Treatment of organic sewage and production of enzyme from biomass carrier comprises air-drying bagasse for 48 hours, pulverizing, and sterilizing at 121 degrees C under 101.3 kPa for 20 minutes; putting powder in enzyme producing vessel (3) sterilized by soaking in benzalkonium bromide for 24 hours, controlling temperature at 30 degrees C and dissolved oxygen content at 5 mg/L, and supplementing nitrogen-controlled culture medium every 15-30 days; and flowing organic sewage and fresh enzyme liquid in organic sewage treatment vessel (4), solidifying zymoprotein on the surface of elastic stuffing, and degrading pollutant in the sewage. An INDEPENDENT CLAIM is included for a device used for treating organic sewage and producing enzyme comprising temperature controlling chamber (1), heating device (2), enzyme producing vessel and organic sewage treatment vessel.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a device used for treating organic sewage and producing enzyme.    Temperature controlling chamber (1)    Heating device (2)    Enzyme producing vessel (3)    Organic sewage treatment vessel (4)
NOVELTY - The device has a material inlet and a methane outlet arranged on top of fermentation cylinder respectively. A juice outlet and a biogas outlet are arranged at mid-portion of the cylinder. The material outlet of material pre-treatment tank is connected to liquor inoculation distributing unit which is arranged on the cylinder by the juice outlet.    USE - Dry anaerobic fermentation device for diphase inoculation of liquor.    ADVANTAGE - The uniform inoculation of liquor can be performed, fermentation speed of liquor is increased, efficiency of biogas is increased and the generation of waste liquor is prevented effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of the dry anaerobic fermentation device.
NOVELTY - Treating device for organic waste comprises a vacuum sealing tank and a stirrer, where a reaction chamber and a heating chamber are provided in the vacuum sealing tank, a mixture consisting of material prescription, micro-organism ferment and slurry degraded by organic wastes is stored in the reaction chamber; the stirrer is provided in the reaction chamber, a circulating heat conducting liquid is provided in the heating chamber, the vacuum sealing tank is provided with a feed hole and a discharge hole; and a stirrer, provided in the reaction and used for stirring the mixture.    USE - The device is useful for treating organic waste (claimed).    ADVANTAGE - The treating device effectively shortens the treatment time of organic wastes and decreases working space.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device.
NOVELTY - Organic inorganic fertilizer manufacturing involves preparing mud as a main raw material. The prepared mud is mixed with polysaccharide plants including corn stalk and cane stem to obtain a mixture. Livestock excretions, triple salt, yeast and a heavy metal remover are also added to the mixture. The mixture is fermented in a fermentor, where fermented mixture is dried and pulverized to obtain a dried mixture.    USE - Method for manufacturing an organic inorganic fertilizer.    ADVANTAGE - The organic inorganic fertilizer manufacturing method is cost-effective and enables to prepare organic inorganic fertilizer, which neutralizes acidified soil with a light alkali component of the mineral component and increases the production of crops.
NOVELTY - Compost comprises 90-110 pts. of residue of herb medicine, 30-50 pts. of rice water, 5-15 pts. of sawdust, 5-7 pts. of muscovado sugar water, 25-45 pts. of enterolith silica, 50-60 pts.wt. of peat moss, 1-3 pts.wt. of sawdust and 1-3 pts.wt. of anion emission crushed material. The enterolith silica comprises 45-55wt.% of silica, 25-35wt.% of alumina, 7-13wt.% of calcium oxide, 3-5wt.% of sodium oxide, 0.1-1wt.% of magnesium oxide, 0.1-1wt% of ferric oxide, 0.1-1wt.% of potassium oxide and 0.1-1wt.% of titanium dioxide.    USE - Compost for cultivating plants.    ADVANTAGE - The compost is eco-friendly and prevents environmental pollution caused by the residue of herb medicine.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for producing compost, which involves:    (A) utilizing residue of herb medicine;    (B) mixing 90-110 pts. of residue of herb medicine and 30-50 pts. of rice water and fermenting the mixture at 45 degrees C;    (C) adding 5-15 pts. of sawdust and 5-7 pts. of muscovado sugar water and fermenting mixture at 70 degrees C;    (D) drying fermented residue of herb medicine; and    (E) adding 25-45 pts. of enterolith silica, 50-60 pts.wt. of peat moss, 1-3 pts.wt. of sawdust and 1-3 pts.wt. of anion emission crushed material to 3-5 pts.wt. of prepared residue of herb medicine to obtain the compost.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of the compost production method. (Drawing includes non-English language text).    Mixing residue of herb medicine and rice water (S10)    adding sawdust and muscovado sugar water (S20)    drying fermented residue of herb medicine (S30)    Adding enterolith silica, peat moss, sawdust and anion emission crushed material (S40)
NOVELTY - Granular fertilizer or soil improvement substance, comprises ashes of hen-droppings containing phosphoric acid and potash, calcium superphosphate, rice bran and fermentation microorganism.    USE - The agent is useful as granular fertilizer for improving soil (claimed), thus used in agriculture.    ADVANTAGE - The granular fertilizer or soil improvement substance disperses easily and produces fertilizer effect at an early stage. The pH is adjusted effectively such that the composition prevents problem associated with high pH. The ashes of hen-droppings can be recycled.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of producing granular fertilizer or soil improvement substance, which involves mixing rice bran, fermentation microorganism, ashes of hen-droppings and calcium superphosphate, adjusting pH by adding calcium superphosphate, fermenting the obtained mixture subjected to hydrolysis, drying the fermented mixture and adjusting grain size after drying.
NOVELTY - Clay mineral system antimicrobial substance capable of suppressing fungi, comprises inorganic laminar compound derived from clay mineral having cation exchange ability in interlayer as main raw material, where one or more portion of cation in an interlayer and interlayer water is substituted by metal cation or organic compound complex. The organic ligand of the organic complex contains caffeine or caffeine ingredient.    USE - The clay mineral system antimicrobial substance is useful in agent for suppressing function of microorganisms including fungi (claimed) and bacteria, e.g. Legionella spp.. Can also be used for promoting plant growth, controlling insect pest and preventing plant diseases, e.g. strawberry blight.    ADVANTAGE - The clay mineral system antimicrobial substance is highly stable and has excellent sustained release property and synergistic effect. The clay mineral system antimicrobial substance retains antimicrobial effect for a long period of time and is eco-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing clay mineral system antimicrobial substance, which involves using the above inorganic laminar compound derived from clay mineral having cation exchange ability in interlayer as main raw material.
NOVELTY - A completely-dissolved fishery fertilizer comprises (wt.%) monoammonium phosphate (15-45), sodium humate (12-20), sodium silicate (5-12), premix compound (8-13), and urea (30-40).    USE - Completely-dissolved fishery fertilizer used in aquaculture, preferably for fish, Margaritana, mussel and shellfish, sea cucumber, or prawn; and in production of plankton (zooplankton or phytoplankton), preferably protozoan, rotifer, Cladocera, nauplius, Calanus, or sword algae, the algae comprising blue algae, Chlorella, Cryptomonadales, diatom, or euglena (claimed).    ADVANTAGE - The fertilizer has comprehensive nutrition and balance proportion, dissolves faster and has high utilization rate, can be simply prepared, has less dosage, long lasting effect, and low cost. It can accelerate propagation of food organism, and can directionally culture beneficial algae, improve water quality, increase dissolved oxygen, avoids pond from flooding, and reduce disease. It has stable quality, is green and harmless for man and animals, and will not pollute the environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing the fishery fertilizer comprising weighing monoammonium phosphate, sodium humate, sodium silicate, premix compound, and urea, crushing to 40-60 meshes, and uniformly mixing.
NOVELTY - A solid molded fuel additive comprises (wt.%) aluminum oxide (Al2O3, 20-30), ferric oxide (Fe2O3, 15-30) and kaolin (40-65).    USE - A solid molded fuel additive for biomass (claimed) including straw.    ADVANTAGE - The fuel additive improves dust melting point of straw, does not easily bind slag and deposit dust during combustion, improves utility ratio of fuel and is combusted.
NOVELTY - Biomass is gasified by heating with a gasifying agent consisting of carbon dioxide and oxygen, to obtain syngas containing hydrogen and carbon monoxide. Tar, sulfur oxide, and/or nitrogen compound contained in syngas are removed, followed by removal of carbon dioxide and water vapor. Dimethylether is then obtained by reacting the processed syngas on a dimethylether-synthesis catalyst. All the processes are carried out under pressure conditions exceeding atmospheric pressure.    USE - Manufacture of dimethylether from biomass, for use as fuel in electric-power generation and heat supply.    ADVANTAGE - The method eliminates the need for compressing syngas produced by biomass gasification. Heat loss in gasification process is reduced by utilizing the heat of combustion. Since pressurized gasification is carried out, generation amount of tar is reduced. Since purification is carried out by a dry process, temperature reduction of syngas is prevented and syngas reheating process is eliminated. Yield of dimethylether is increased.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for dimethylether manufacturing apparatus (100) equipped with a gasifying portion (1) for thermochemically decomposing biomass, gas-purification portion (2) connected with the gasification portion and filled with gas-purification agent (A) which adsorbs tar, sulfur oxide, and nitrogen compound, gas-purification portion (3) connected with portion (2) and filled with gas-purification agent (B) which adsorbs carbon dioxide and water vapor, and dimethylether-synthesis portion (4) connected with portion (3).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the dimethylether manufacturing apparatus. (Drawing includes non-English language text)    Gasification portion (1)    Gas-purification portions (2,3)    Dimethylether-synthesis portion (4)    Dimethylether recovery portion (6)    Dimethylether manufacturing apparatus (100)
NOVELTY - An anti-bacterial mildew-proof environment friendly spray-coating liquid comprises (wt.%) modified absorbent (0.5-20) comprising mixed soluble salt of anti-bacterial mildew-proof ion (1-30); nano photocatalyst (0.1-10); adhesive film forming agent (0.1-10); dispersant (0.1-5); and deionized water (balance).    USE - An anti-bacterial mildew-proof environment friendly spray-coating liquid for purifying air of buildings or other structure (claimed).    ADVANTAGE - The coating liquid has simple preparation method, and is environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of preparing an anti-bacterial mildew-proof environment friendly spray-coating liquid comprising:    (A) mixing photocatalyst with an inorganic acid solution having a pH value of 1-4 to obtain a photocatalyst solution;    (B) mixing an absorbent and mixed soluble salt solution at a ratio of 100:1-30, and setting aside the mixture for 1-3 hours to obtain a modified absorbent;    (C) mixing with the adhesive film forming agent and dispersant to form suspension;    (D) mixing the prepared photocatalyst solution and the prepared suspension at a weight ratio of 1:0.1-10 to obtain a precursor of the spray coating liquid; and    (E) grinding and ball milling the precursor, and filtering using 200-mesh filter screen or filter cloth.
NOVELTY - Solid compound (I) comprising a polyaminoborane, and at least one inorganic oxidant, is new.    USE - (I) is useful for generating hydrogen by self-sustaining combustion reaction (claimed), where the hydrogen is useful as fuel or reducing agent in many industrial processes and devices.    ADVANTAGE - (I) provides the hydrogen with good yield, and does not cause any toxic effects to user.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a powdery solid composition, which is precursor of (I), comprising polyaminoborane and inorganic oxidant, preferably ammonium nitrate, alkaline nitrates, alkaline-earth nitrates, metal nitrates, metal oxides, and/or oxidants of the dinitramine family; and    (2) a process for hydrogen generation by self-sustained combustion of (I).
NOVELTY - An interlayer water in an interlayer containing clay mineral having cation exchange ability as main raw material is exchanged with organic compound having bioactive function, the interlayer water is removed by heat-processing the clay mineral, to obtain clay mineral-type composite material. A hydrophobic group is provided to the surface of clay mineral before performing condensation of clay mineral in interlayer. Then, the organic compound is introduced into the interlayer of clay mineral. Thus, sustained-release control method of clay mineral-type composite material is carried out.    USE - Sustained-release control method of clay mineral-type composite material.    ADVANTAGE - The method is environment-friendly, and provides clay mineral-type composite material having excellent stability and bioactive function such as insect repelling property, anti-microorganism property, freshness maintaining property and aroma property.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for clay mineral-type composite material, which is used as functional raw material.
NOVELTY - The compost aerator comprises a tube-like construction with round or angular cross-section on a wire mesh (4) or a tube (3) equipped with holes or boards or metal-/plastic rods that are constructed so that air passages are existed on the entire height without fell through the compost materials to be filled, and a fastening strut (7, 10) or base for the composter or mouse grid (8), on corresponding holding device (9, 11) in order to guarantee the durability of central arrangement of the ventilation.    USE - Used as compost aerator.    ADVANTAGE - The compost aerator has good flexibility, ensures long term aeration and prevents extensively an anaerobic material condensation through suitable additional ventilation.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of compost aerator.    Tube (3)    Wire mesh (4)    Fastening strut (7, 10)    Mouse grid (8)    Holding device. (9, 11)
NOVELTY - Ethanol is manufactured by performing enzyme saccharification of cellulose, producing saccharide and obtaining saccharide solution by adding saccharogenic amylase to saccharification tank which accommodated biomass consists of cellulose, filtering using a filter to remove biomass residue, filtering using ultrafiltration membrane to remove saccharogenic amylase, introducing the saccharide solution in fermentation tank and performing ethanol fermentation to obtain ethanol aqueous solution by adding ethanol fermentation microbe to the fermentation tank.    USE - Manufacture of ethanol for motor fuel.    ADVANTAGE - Clogging of ultrafiltration membrane by biomass residue is prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of the manufacture of ethanol. (Drawing includes non-English language text).
NOVELTY - Foamy composition for capturing insect pest, contains undiluted solution which consists of water, surfactant and propellant. The foamy state exhibits initial stage adhesiveness temporarily after injection and then becomes non-adhesive. The viscosity of foamy composition reduces during the transfer of initial stage adhesiveness to non-adhesive state. The liquid state or mixture of liquid and bubble state are exhibited in the non-adhesive state.    USE - The foamy composition is useful for capturing insect pest (all claimed) including ant, cockroach, millipede, centipede, stink bug, spider, caterpillar, moth aphid, wood louse (Porcellio scaber), scutiger (Thereuonema tuberculata) or ground beetle. The foamy composition includes aerosol.    ADVANTAGE - The insects can be captured reliably. The composition is highly safe with respect to humans and is eco-friendly. The composition adheres to an injection surface and thus can be wiped off safely and easily. The foamy state can be maintained for a long time on wall surface, and thus the dripped liquid can be suppressed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for insect capture tool, which is obtained by accommodating the foamy composition for capturing insect pest in the pressure-resistant container provided with injection valve apparatus.
NOVELTY - A pressure varying adsorption method of condensed coal-bed methane containing carbon dioxide displacement, comprises raw material gas absorption, working gas replacement, bend layer regeneration, side product gas pressurization and working gas reclaiming. The working gas replacement uses replacement with pressure or normal pressure displacement operation mode. The methane is replaced and absorbed by carbon dioxide under an absorption pressure, or under a normal pressure.    USE - A pressure varying adsorption method for condensed coal-bed methane containing carbon dioxide displacement (claimed).    ADVANTAGE - The pressure varying adsorption method uses the methane as top product to increase the concentration and yield of the methane gas product; is suitable for coal-bed gases with different methane contents; and is capable of changing the coal-bed gas with low methane concentration to a natural gas fuel with good quality and a lower cost. The methane concentration of the gas product obtained from the coal-bed gas with methane concentration of 20% can reach over 90%. The reclaiming rate is high, which is up to 90%. The gas product can be conveyed by a pipe, and can also be stored in tanks.
NOVELTY - A bacteria-containing fertilizer is manufactured by mixing fertilizer, straw fiber powder (1-25 wt.%, 60-80 meshes) porous laminated silicate powder (3-20 wt.%, 80-200 meshes) and livestock excretion (3-50 wt.%), drying and shaping to obtain particle fertilizer having not greater than 3% water content, spraying bacteria and nutrient liquid, and fermenting at controlled temperature, humidity and pH.    USE - Method of manufacturing bacteria-containing fertilizer (claimed).    ADVANTAGE - The method has low energy consumption, and the obtained fertilizer has good quality.
NOVELTY - An organic waste in which oxygen does not permeate inside easily, and biochemical reaction by microorganisms is not carried out easily is maintained still. The oxygen is forcedly supplied to the inside of the organic waste. The inside temperature of the organic waste in which oxygen is supplied is raised by the biochemical reaction. The raised temperature is maintained, biochemical reaction is continued and the organic waste is composted.    USE - Processing of organic waste such as livestock excretion, agricultural waste material, foodstuff waste material (all claimed), sewage sludge and organic refuse.    ADVANTAGE - The method enables processing of organic waste with high moisture content and reducing the amount of organic waste efficiently and economically, without mixing agricultural byproduct such as sawdust. The heat energy produced by enforcing the processing of organic waste is efficiently utilized as heat source.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) processing apparatus of organic waste, which has a sealable container (2) to accommodate organic waste insertably, and a pressure-control apparatus to control the pressure in the container between atmospheric pressure to 15 atmosphere; and    (2) heat energy utilization method, which involves utilizing heat generated by processing organic waste in presence of oxygen and carbon monoxide as a heat source.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of processing apparatus of the organic waste.    High pressure gas cylinder (1)    Container (2)    Intake pipe (3)    Exhaust pipe (5)    Heat insulation chamber (7)
NOVELTY - The ecological green area system includes a filling material bed (1) which is covered with a pebble layer (2), a rough sand layer (3), a silver sand layer (4) and a microorganism layer (5) from the bottom upwards. The top part of the microorganism layer is covered with a crisscross pipe net (6). The top part of the microorganism layer is planted with a layer of plants (7) whose roots are flourishing. The side of the filling material bed is provided with a water outlet (8). A water-resistant layer (9) is formed between the filling material bed and each filling material layer.    USE - Ecological green area system for treating feces from toilet.    ADVANTAGE - Ensures that running cost of the ecological green area system is low, and its treatment efficiency is high. Ensures that the treated feces water is discharged while meeting a standard, which is clear and can be recycled, thus saving water resource. Ensures that the ecological green area system beautifies environment while treating toilet feces.    DESCRIPTION OF DRAWING(S) - The drawing shows the cross-sectional view of the ecological green area system.    Filling material bed (1)    Pebble layer (2)    Rough sand layer (3)    Silver sand layer (4)    Microorganism layer (5)    Crisscross pipe net (6)    Layer of plants (7)    Water outlet (8)    Water-resistant layer (9)
NOVELTY - A process for producing a glyceride product which is enriched in monounsaturated fatty acids relative to the starting glyceride involves alcoholysis of triglycerides employing lipolytic enzymes selective for saturated fatty acids and/or lipolytic enzymes selective for the 1-position and/or the 3-position in a glyceride; and separation of saturated fatty acid esters (fraction A) from a monounsaturated glycerides (fraction B).    USE - For producing a glyceride product which is enriched in monounsaturated fatty acids relative to the starting glyceride; for producing biodiesel, surfactant, or high purity grade chemicals; and for producing consumer products and/or fried food products (preferably edible oil, consumer oil, margarine, shortenings, frying oil, battered fried products, baked products like bread, cake, cookies, biscuits or snack foods such as e.g. chips and french fries) (all claimed).    ADVANTAGE - The process is a high efficient process and generates high purity products such as fatty acid esters; and provides a high purity chemical grade or high purity food grade.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a glyceride product comprising monounsaturated fatty acids (at least 70-100 mole%).
NOVELTY - Gas fuel is produced from biomass containing lignocellulose by adding sterilized biomass containing lignocellulose in a fermentation container, inoculating cellulase-producing microorganisms, anaerobically culturing, extracting hydrolyzed and fermented substance from the fermentation container, passing in digestion container, inoculating methane-producing microorganism, hydrogen-producing microorganism and acetic acid bacteria, and anaerobically culturing.    USE - Method of producing gas fuel from biomass containing lignocellulose (claimed).    ADVANTAGE - The method produces organic substances including acetic acid, glycerol and alcohol, and has 90% conversion rate of biomass into methane. The method has low energy consumption.
NOVELTY - A bio-organic fertilizer comprises (pts.wt.) composite amino acid (0.1-0.3), and biochemical yellow humic acid (0.7-0.9).    USE - A bio-organic fertilizer for crops.    ADVANTAGE - The fertilizer can improve physicochemical property and fertility of the soil, increases crop yield, and does not pollute environment.
NOVELTY - Tar wastewater treatment comprises performing filtration and absorption of wastewater out of a washing tower with biomass ash; introducing air into the treated wastewater for 10-24 hours; sending aerated wastewater into a precipitation pool to remove the impurities; and introducing aerobic bacteria into the treated wastewater.    USE - Method for treating tar wastewater.    ADVANTAGE - The treated wastewater meets the national discharging standards and generates no secondary contamination to the environment.    DESCRIPTION OF DRAWING(S) - The drawing is a block diagram of a method for treating tar wastewater (Drawing includes non-English language text).
NOVELTY - Composite probiotics comprise photosynthetic bacteria strain, lactic acid bacteria strain, Bacillus, actinomycetes strain, microzyme, and filamentous fungi strain having a weight ratio of 1-5:1-3:0.5-1.5:1-1.4:0.6-1:1-5 (preferably 3:2:1:1.2:0.8:3). The strains have alive-bacterium content of 180000000-260000000 (preferably 220000000)/ml.    USE - Composite probiotics for environmental restoration of eutrophication aquaculture water, treatment of household garbage (claimed), deodorization of toilet, utilization of household garbage, treatment of water of smelly lake, or purification of tap water or swimming pool.    ADVANTAGE - The composite probiotics are cheap, and convert poisonous and harmful substance to nontoxic and harmless substance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of preparing composite probiotics comprising mixing photosynthetic bacteria, lactic acid bacteria, Bacillus, actinomycetes, microzyme and filamentous fungi; placing obtained mixture in a culture medium comprising (wt.%) corn flour (8-16), peptone (1-5), glucose (6-14) and pure water (balance); and fermenting at 20-26 degrees C for 10-14 days.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a method of preparing a composite probiotics. Drawing includes non-English language text.
NOVELTY - Directionally building and controlling function of an aerobic particle sludge comprises: (a) providing microorganism; (b) making the microorganism in the aerobic particle sludge produce special degradation function for receipting movable functional gene segment; and (c) obtaining aerobic particle sludge with stable structure and special degradation function by enrichment culture of the hybridized aerobic particle sludge.    USE - The method is useful for directionally building and controlling function of aerobic particle sludge (claimed).    ADVANTAGE - The method is simple, quick, and efficient compared with traditional methods.    DETAILED DESCRIPTION - Directionally building and controlling function of an aerobic particle sludge comprises: (a) providing microorganism: taking functional gene segment as donor bacterium, mature or half-mature aerobic particle sludge as receptor bacterium, directly hybridizing donor bacterium/receptor bacterium outside the system (ectopic hybridizing) or in the system (in situ hybridizing); (b) making the microorganism in the aerobic particle sludge produce special degradation function for receipting movable functional gene segment; and (c) obtaining aerobic particle sludge with stable structure and special degradation function by enrichment culture of the hybridized aerobic particle sludge.
NOVELTY - A biological denitrification apparatus has a denitrifying reaction tank (4), unit for adding calcium compound to natural water, and control unit. Natural water containing nitrate nitrogen and/or nitrite nitrogen is introduced from lower portion of reaction tank, and denitrifying processing of water is carried out by contacting with granule having aggregate of denitrifying bacteria. The treated water is removed from reaction tank upper portion. The control unit controls calcium compound addition unit such that calcium level of natural water is set to predetermined value.    USE - Biological denitrification apparatus.    ADVANTAGE - The apparatus efficiently enables denitrification processing. The amount of calcium compound added to natural water is controlled effectively. The floating of sludge is prevented.    DETAILED DESCRIPTION - A biological denitrification apparatus has a denitrifying reaction tank, unit for adding calcium compound to natural water, and control unit. Natural water containing nitrate nitrogen and/or nitrite nitrogen is introduced from lower portion of reaction tank, and denitrifying processing of water is carried out by contacting with granule having aggregate of denitrifying bacteria at high concentration in presence of organic substance. The treated water is removed from reaction tank upper portion. The control unit controls calcium compound addition unit such that calcium level of natural water is set to predetermined value, based on amount of nitrate nitrogen and/or nitrite nitrogen in water introduced and discharged from tank.    DESCRIPTION OF DRAWING(S) - The drawing shows the systematic diagram of biological denitrification apparatus. (Drawing includes non-English language text)    Natural water tank (1)    Equalizing tank (2)    Treated water tank (3)    Denitrification reaction tank (4)    Separation unit (6)
NOVELTY - Method of composting organic waste, involves primary treatment processing of organic waste by accommodating organic waste in sealable processing tank equipped inside with stirring unit, adjusting pH of organic waste to 7.5-9.5 and heating at 85-120 degrees C for 20 minutes-3 hours, where the nitrogen content contained in the organic waste is separated as ammonia, removing ammonia with predetermined amount of air or water vapor supplied from the processing tank, and secondary treatment processing of organic waste by composting the primary treatment processed product using microorganism.    USE - The method is useful for composting organic waste (claimed) such as livestock farm waste material and sewage sludge, thus useful for preparing fertilizer or soil improvement material.    ADVANTAGE - The organic waste can be composted efficiently by a simple process, as the processing tank is not occupied for a long period of time and the composting conditions can be controlled easily. The generation of offensive odor due to production of ammonia is prevented efficiently. The compost has high quality and humification.    DETAILED DESCRIPTION - Method of composting organic waste, involves primary treatment processing of organic waste by accommodating organic waste in sealable processing tank equipped inside with stirring unit, adjusting pH of organic waste to 7.5-9.5 and heating at 85-120 degrees C for 20 minutes-3 hours, where the nitrogen content contained in the organic waste is separated as ammonia, removing the nitrogen content contained in the organic waste by stripping the produced ammonia with predetermined amount of air or water vapor supplied from the processing tank, and secondary treatment processing of organic waste by composting the primary treatment processed product using microorganism.
NOVELTY - A small-sized animal excrement fermenting device comprises a normal pressure boiler, a water box, and a fermenting box; where the normal pressure boiler is connected to the fermenting box through a hot water pipe; a blender, a decelerated starting drive system, and a temperature monitoring system are set in the fermenting box; the main shaft of the blender is connected to the decelerated starting drive system; the water box is respectively connected to the normal pressure boiler and the fermenting box; and the connection positions are equipped with a pipe pump and a water gate.    USE - The small-sized animal excrement fermenting device is useful for producing organic fertilizer by animal excrement.    ADVANTAGE - The small-sized animal excrement fermenting device is simple, has convenient operation and installation, and it takes up small area.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the small-sized animal excrement fermenting device.
NOVELTY - A compound microbial viable bacteria preparation comprising Pediococcus, microzyme, and Bacillus, the total quantity of which is 1 billion/g, is new.    USE - The compound is useful for preparing organic waste water purifying agent; aquaculture water purifying agent; deodorant, oil stain removing agent, or pipeline blockage removing agent for garbage fields, public occasions, farm product markets, and kitchens; feed additives in the livestock industry or pet breeding; as well as disease preventing preparation for agricultural microbes.    ADVANTAGE - The compound microbial viable bacteria preparation in this invention may effectively decompose large quantities of putrescent organic matters, inhibit the growth of harmful organisms, and remove the odor characterized by high ammonia nitrogen removal rate, free from remainder sludge, effective deodorization, and low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for preparing the compound microbial viable bacteria preparation.
NOVELTY - A molten carbonate fuel cell reforming catalyst is protected by covering zeolite membrane layer on surface of reforming catalyst to prepare core shell catalyst.    USE - Protection of molten carbonate fuel cell reforming catalyst for catalytic reaction (claimed) and interior of cell.    ADVANTAGE - The method prolongs service life of catalyst and improves operation time of cell.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an application of protection method of molten carbonate fuel cell reforming catalyst.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the method of protecting molten carbonate fuel cell reforming catalyst. (Drawing includes non-English language text).
NOVELTY - Liquid fuel comprises (in weight%) methanol (70-75), water (10-15), turpentine (13-16) and additive (1-4), where the additive is prepared by using 30% of hydrogen peroxide, cyclohexane, ferrocene, liquid paraffin and ethanol.    USE - Liquid fuel.    ADVANTAGE - The liquid fuel is economical and environmental-friendly, has high thermal value, and exhibits high safety. The liquid fuel is easily, economically and efficiently manufactured, has no harmful gases, and has excellent workability and practicability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing liquid fuel, which involves dissolving ferrocene using ethanol, adding 30% of hydrogen peroxide, cyclohexane and liquid paraffin to obtain the additive, then adding methanol, water and turpentine into a mixer, and then adding additive to the mixture and stirring to obtain the liquid fuel.
NOVELTY - Production of a combined microbe bacteria fertilizer comprises adding molasses as a culture medium to an active slurry in a sewage treatment after fermentation; adding water, and adding a mixed strain; adding grass peat; and drying, where the mass ratio of active slurry, molasses, water, mixed strain, and grass peat is 70-80:7-12:10-20:3-8:10-15. The compound strain comprises Paenibacillus macerans, Bacillus megatherium, B. cereus, B. mucilaginosus, ray fungi, microzyme, and Lactobacillus at a mass ratio of 25-35:5-15:5-15:15-25:5-15:5-15:5-15.    USE - Method for the production of a combined microbe bacteria fertilizer (claimed).    ADVANTAGE - The method reutilizes sewage slurry, and is inexpensive.
NOVELTY - Preparing bioorganic fertilizer containing bacteria, involves fermenting organic manure under aerobic condition for 10 days and adjusting water content of material to 25-30%, granulating fermented material, rapidly drying granules in barrel at high temperature such that water content of dried granules is less than or equal to 5%, cooling and adding microbial inoculum to granules by spraying bacteria to granules under high pressure using special bacteria adding device such that number of viable bacteria is 2 billion/g and maintaining water content of material at 12-14% before packing.    USE - The method is useful for preparing bioorganic fertilizer containing bacteria (claimed).    ADVANTAGE - The method provides bioorganic fertilizer rich in beneficial viable bacteria.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for special bacteria adding device, which has power assembly, high pressure bacteria adding unit, antiblocking unit and dosing unit that are connected in turn, where the power assembly is set above the high pressure bacteria adding unit, and the left and right sides of the antiblocking unit are connected with the high pressure bacteria adding unit and the dosing unit, where the height of the dosing device is higher than the right side of the power assembly.
NOVELTY - Producing biodiesel using oil grains as raw material and sulfuric acid as catalyst, involves mixing oil grains, solvent and catalyst at 40-90 degrees C, stirring and refluxing for 1-4 hours, obtaining monoester phase of rich fatty acid alkyl and rich glycerin after reaction and static separation, where the monoester phase of rich fatty acid alkyl comprises fatty acid alkyl and small quantity of extender dissolved in solvent, obtaining glycerin and solvent (20-60 weight%) by distillation from glycerin, where the solvent includes lower alcohol solvent with low boiling point.    USE - The method is useful for producing biodiesel (claimed).    ADVANTAGE - The biodiesel can be mass produced simply and efficiently at low cost.
NOVELTY - A 3-hydroxycephem compound is prepared by mixing thiazoline derivative, paratoluenesulfonyl chloride and solvent; stirring obtained mixture for sulfonylation reaction at - 10 to 25 degrees C; adding morpholine and base solution; subjecting mixture to enamine reaction at - 30 to 50 degrees C to obtain a phenyl derivative; cooling phenyl derivative to - 60 to 10 degrees C; adding an acidic binder and liquid bromine; reacting for 0.5-5 hours; adding hydrochloric acid and methanol; reacting at 0-30 degrees C for 5-10 hours; extracting; crystallizing; and drying obtained crystals.    USE - Method of preparing a 3-hydroxycephem compound (claimed)    ADVANTAGE - The method is safe, simple, cheap, and environment friendly; does not generate by-products; utilizes efficiently the raw materials thus reducing production cost; has improved yield; and prepares product having a high purity.    DETAILED DESCRIPTION - A 3-hydroxycephem compound of formula (I) is prepared by mixing thiazoline derivative of formula (II), p-toluenesulfonyl chloride and solvent; stirring obtained mixture for sulfonylation reaction at - 10 to 25 (preferably 0-10) degrees C; adding morpholine and base solution; subjecting mixture to enamine reaction at - 30 to 50 (preferably - 25 to 0) degrees C to obtain a phenyl of formula (III); cooling (III) to - 60 to 10 (preferably - 55 to - 15) degrees C; adding an acidic binder and liquid bromine; reacting for 0.5-5 (preferably 0.5-1.5) hours; adding hydrochloric acid having a concentration of 5-15 mass% and methanol; reacting at 0-30 (preferably 5-25) degrees C for 5-10 (preferably 6-8) hours; extracting; crystallizing; and drying obtained crystals.    R1-R2=not defined.
NOVELTY - An inertial electrostatic confinement (IEC) anaerobic reaction equipment comprises a water wheel-distributing device, anaerobic reactor, reinforced inner-outer circulation mass transfer system, intersected plate deposition unit, three-phase separator and marsh gas collecting unit. The water wheel-distributing device is located on a bottom of reactor. The mass transfer system is set on a middle portion of reactor. The intersected plate deposition unit is located on upper portion of anaerobic reactor. The three-phase separator and marsh gas collecting unit are located on anaerobic reactor.    USE - An IEC anaerobic reaction equipment for anaerobic biological treatment of high-concentration organic wastewater and for generation of methane.    ADVANTAGE - The anaerobic reaction equipment has improved water distribution and combination of inner circulation and outer circulation. By the synergistic action of inner circulation and outer circulation, the equipment can form large particles of anaerobic sludge having high methane-generating activity. The equipment has high-efficiency water inlet. The volume load can reach 25 kg chemical oxygen demand/m3.day during treatment of high-concentration organic wastewater.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an IEC anaerobic reaction technique.
NOVELTY - Product comprises a protective paint containing a compound comprising chlorothalonil, N'-dimethyl-N-phenylsulfamide, 4,5-dichloro-2-n-octyl-3(2H)-isothiazolone, 2-methylthio-4-tert-butylamino-6-cyclopropylamino-s-triziane, 3-(3,4-dichlorophenyl)-1,1-dimethylurea, N-(dichlorofluoromethylthio)- N',N'-dimethyl-N-p-tolylsulfamide and 2-(p-chlorophenyl)-3-cyano-4-bromo-5-trifluoromethyl pyrrole bound to metal oxide nanoparticles.    USE - The product is useful for preventing marine biofouling of a substrate by a marine biofouling organism (claimed), and in antifouling products such as paints. No biological data given.    ADVANTAGE - The product is ecologically safer than many existing antifouling compounds.
NOVELTY - Process for breaking down ethanol into one carbon unit in a prereformer, comprises reacting ethanol and water vapor on a catalyst comprising platinum on a carrier containing a mixture of zirconium oxide and cerium oxide at 300-550 degrees C.    USE - The process is useful for breaking down ethanol into one carbon units, which are methane, carbon monoxide and carbon dioxide.    ADVANTAGE - The use of platinum as an active metal reduces the amount of the catalyst used so that the risk potential is reduced and allows the method to be carried out in a simple manner. The catalyst is prepared by using less amount of platinum. The process avoids direct dehydration of ethanol into ethene and water. The catalyst functions at a temperature below 450 degrees C and allows a maximum overall efficiency of the prereformer.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) the catalyst used in the above process; and    (2) a process for producing the catalyst, comprising kneading cerium oxide, zirconium oxide, optionally rare earth metal oxide and optionally aluminum oxide under the addition of water followed by shaping, drying and calcining, where an aqueous platinum solution is added before the kneading or carrying after the drying.
NOVELTY - A hydrocarbon removing device (13) located upstream or downstream of a desulfurizer (4) partially removes hydrocarbon constituents in the raw material. A switching device (9) switches flow of raw material between a supply path (23) through which raw material passes only to the desulfurizer and not to hydrocarbon removing device, and a supply path (24) through which the raw material passes through desulfurizer and hydrocarbon removing device. A control apparatus (20) controls operation of the switching device.    USE - Hydrogen generating apparatus for fuel cell system.    ADVANTAGE - The deterioration of modification catalyst is reduced by supplying the raw material only to the desulfurizer and not to hydrocarbon removing device by switching to respective supply path.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for operation method of hydrogen generating apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the fuel cell system comprising hydrogen generating apparatus. (Drawing includes non-English language text)    Desulfurizer (4)    Flow path switching device (9)    Hydrocarbon removing device (13)    Control apparatus (20)    Raw material supply paths (23,24)
NOVELTY - A biogas is contacted with a silicon adsorption agent having a pore with pore diameter of 1 plus minus 0.5 nm to remove hydrogen sulfide in biogas.    USE - Removal of hydrogen sulfide in biogas used for fermenting organic waste and excrement of livestock.    ADVANTAGE - The method enables removal of hydrogen sulfide in biogas completely, by pressure-fluctuation adsorption method.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the pressure-fluctuation adsorption apparatus.    Adsorption columns (A,B)    Gas-compression machine (11)    Buffer tank (12)    Product tank (13)    Flow regulating valve (22)
NOVELTY - A proton conductor containing tin-phosphorus-containing electrolyte is formed into film by physical vapor deposition, to manufacture proton conductor (30).    USE - Manufacture of proton conductor used for manufacture of fuel cell (claimed).    ADVANTAGE - The deliquescence of proton conductor is suppressed effectively during manufacture of proton conductor. The reduction in electric power generation performance of full cell is suppressed.    DETAILED DESCRIPTION - A proton conductor comprising tin-phosphorus-containing electrolyte (AB2O7-type electrolyte) is formed into film by physical vapor deposition, to manufacture proton conductor. The A-site of electrolyte contains tin and B-site includes phosphorus. An INDEPENDENT CLAIM is included for manufacture of fuel cell, involves forming film using proton conductor containing AB2O7-type electrolyte by physical vapor deposition on primary electrode, and positioning secondary electrode at side opposite to primary electrode.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating manufacture of proton conductor. (Drawing includes non-English language text)    Electrolyte material (10)    Substrate (20)    Proton conductor (30)
NOVELTY - Cosmetic composition conditioned in aerosol, comprises an exothermic metal salt and a propellant, in an anhydrous medium.    USE - The composition is useful for shaving of keratin materials, preferably skin (claimed).    ADVANTAGE - The composition provides good warming effect to the skin.
NOVELTY - An Acinetobacter microorganism comprising decomposability with respect to the polycyclic aromatic compound which a hydroxyl group produces on an aromatic ring by cleavage reaction of a monocyclic aromatic compound or an aromatic ring which has a hydroxyl group, is new.    USE - The microorganism is useful for decomposing polycyclic aromatic compound (claimed).    ADVANTAGE - The invention is harmless and inexpensive.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are: (1) a biological product for decomposing polycyclic aromatic compound which a hydroxyl group produces on an aromatic ring by cleavage reaction of a monocyclic aromatic compound or an aromatic ring containing the Acinetobacter microorganisms which has a hydroxyl group; and (2) a method to decompose the polycyclic aromatic compound which a hydroxyl group produces on an aromatic ring by cleavage reaction of a monocyclic aromatic compound or an aromatic ring which has a hydroxyl group contained in the contaminated said water or soil comprising process which the water or soil contaminated with the polycyclic aromatic compound which a hydroxyl group produces on an aromatic ring by cleavage reaction of the monocyclic aromatic compound or aromatic ring which has the Acinetobacter microorganisms and the hydroxyl group is made to contact.
NOVELTY - The immersion type membrane separator (10) includes an aeration unit (15) arranged below a separation-membrane module (11). A baffle plate (18) is arranged on the bottom face (30a) of a reaction tank (30) without contacting the side of a separation-membrane unit (13), so that the separation-membrane unit can be raised independently with respect to the baffle plate.    USE - Immersion type membrane separator used with reaction tank of membrane bioreactor for wastewater treatment in e.g. factory, commercial establishment.    ADVANTAGE - Can be easily installed and raised with respect to reaction tank. Allows easy and fast exchanging of separation-membrane module, thus ensuring favorable maintenance property. Reduces installation cost of immersion type membrane separator with multiple separation-membrane units. Allows a membrane bioreactor to efficiently obtain clear filtrate water and efficiently decompose organic matter contained in processed water by microbial treatment using an activated sludge.    DESCRIPTION OF DRAWING(S) - The drawing shows the side view of immersion type membrane separator.    Immersion type membrane separator (10)    Separation-membrane module (11)    Separation-membrane unit (13)    Aeration unit (15)    Baffle plate (18)    Reaction tank (30)    Bottom face (30a)
NOVELTY - Eliminating scum of activated sludge comprises suppressing generation of scum and injecting Bacillus licheniformis in the processor of an activated sludge.    USE - The method is useful for eliminating scum of activated sludge (claimed).    ADVANTAGE - The invention solves the problem easily.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a microorganism of B. licheniformis which suppresses bacterial growth.
NOVELTY - Planting crop comprises using mixture of biogas residue and/or biogas liquid as base fertilizer, and applying biogas liquid to crop after planting the crop.    USE - Method of planting crop (claimed).    ADVANTAGE - The method scientifically enhances utilization of biogas residue and biogas liquid, thus reducing environmental pollutant.
NOVELTY - A biological feed comprises (kg) yacon residue (60-65); immature tangerine (8-10); albumen powder (20-25); China root (5-10); and herba centipedae (10-20). It is prepared by respectively drying the yacon residue, the immature tangerine, the China root and the herba centipedae; crushing the dried materials into powder; mixing the powder with the albumen powder; and then granulating the mixture to obtain the feed.    USE - A biological feed for use solely or together with other feeds, and for livestock breeding industry or aquaculture.    ADVANTAGE - The biological feed uses the yacon residue together with the albumen powder so that nutrition of the raw materials can be used to the maximum extent; reduces environment pollution; saves resources, since the immature tangerine, the China root and the herba centipedae are added; and can improve the resistance of an animal and reduce the probability of becoming ill.
NOVELTY - Methane synthesis reactor comprises concurrent flow heat exchanging pipes (18) and counter flow heat exchanging pipes (17). The reactor includes a quench gas distributor (14), raw material gas inlet (9), quench gas inlet (10), shell (11), buffer cavity (12), upper carrier plate (13), packing layer (15), catalyst bed (16), lower carrier plate (19), connecting gas cavity (20), buffer cavity (21), produced gas outlet (22), and thermocouple installing port (23). The packing layer is a ceramic ball or catalyst carrier.    USE - Reactor for synthesizing methane.    ADVANTAGE - The reactor is made of convenient manufacturing method, and has homogenous bed temperature and little circulating airflow.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of the reactor.    Raw material gas inlet (9)    Quench gas inlet (10)    Shell (11)    Buffer cavity (12)    Upper carrier plate (13)    Quench gas distributor (14)    Packing layer (15)    Catalyst bed (16)    Counter flow heat exchanging pipes (17)    Concurrent flow heat exchanging pipes (18)    Lower carrier plate (19)    Connecting gas cavity (20)    Buffer cavity (21)    Produced gas outlet (22)    Thermocouple installing port (23)
NOVELTY - A fertilizer is prepared by concentrating a mother liquor after fermenting extraction to obtain fermentation mother liquor having a concentration of 25 Be; concentrating further the obtained concentrated fermentation mother liquor to 45-50 Be; adding powdery substance to the concentrated mother liquor at a ratio of 3-5:1 (preferably 4:1); mixing; granulating the mixture at high pressure; and drying. The powdery substance is fiber or quarry powder, or grass-planting ash or clay.    USE - Method of preparing a fertilizer (claimed).    ADVANTAGE - The method does not pollute the environment; can be done at lower temperature; does not produce smoky flavor; and does not cause harm to human body.
NOVELTY - Device useful for making methane sensor which has in combination of a platinum wire coil, which has diameter of 1-2 mm, is claimed. The coil is encapsulated in alumina. The platinum wire has diameter of 46-50 SWG. The platinum wire encapsulation coil of alumina surface has a coating of catalyst of platinum and palladium in the ratio 1:1-1:5 and rare-earth metal. Image 0/1
NOVELTY - Production of methanol involves treating sugar alcohol with hydrogen in the presence of a hydrogenolysis catalyst comprising a transition metal, and thus producing methanol by hydrogenolysis of the sugar alcohol.    USE - For the production of methanol (claimed) which is used as a fuel, typically an automotive fuel, or as a building block, reactant or feedstock in the production of other chemicals. The methanol also used to esterify unwanted free fatty acids present in the production of biodiesel.    ADVANTAGE - The method provides methanol for esterification of unwanted free fatty acids present in the production of biodiesel, thus the process used to convert the glycerol by-product of a biodiesel production process into methanol, and that methanol is used to esterify free fatty acids present in the biodiesel production process in order to produce further biodiesel. The methanol is formed selectively by direct catalytic hydrogenolysis of glycerol and other poly-alcohols, where the selectivity of the hydrogenolysis for methanol is 20-100 (preferably 60-100)%. The selectivity of the hydrogenolysis reaction for methanol is at least 30 (preferably at least 50)%.    DETAILED DESCRIPTION - Production of methanol involves: treating sugar alcohol of formula HO-CH2-(CH(OH))n-CH2-OH (I) or HO-CH2-(CH(OH))m-CH=O (II), with hydrogen in the presence of a hydrogenolysis catalyst comprising a transition metal, and thus producing methanol by hydrogenolysis of the sugar alcohol.    n=0 or greater than or equal to 1;    m= greater than or equal to 1.
NOVELTY - The gasifier has a gasifier main body (13) which heats biomass feedstock and generates pyrolysis gas. A normally-closed solenoid valve (36) is provided in an air supply tube (35) which supplies air to a thermal decomposition chamber (33) of the gasifier main body.    USE - Gasifier for biomass gasification system (claimed) for producing electric power.    ADVANTAGE - Avoids that the residual gas in gasifier leaks outside through the air supply pipe, when driving of the gasifier is stopped.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a biomass gasification system; and    (2) a shutdown method of a gasifier in a biomass gasification system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a biomass gasification system. (Drawing includes non-English language text).    Gasifier main body (13)    Air blower (22)    Thermal decomposition chamber (33)    Air supply tube (35)    Solenoid valve (36)
NOVELTY - The method involves forming pellet by compression molding of gas-hydrate and conveying gas-hydrate using belt conveyor. The water dissolved with electrolyte, is sprayed on gas-hydrate pellet conveyed through belt conveyor. The water film layer is formed on gas-hydrate pellet.    USE - Method for forming water film layer on surface of gas-hydrate pellet.    ADVANTAGE - The water film layer is uniformly formed on whole surface of gas-hydrate pellet without increasing the consumption amount of water.    DETAILED DESCRIPTION - The electrolyte is selected from group consisting of sodium chloride, calcium chloride, magnesium chloride and silver iodide. The gas hydrate pellet is reversed and conveyed through belt conveyor so as to form water film layer on the other surface of gas-hydrate pellet. An INDEPENDENT CLAIM is included for water film layer formation apparatus has pellet inversion unit that reverses gas-hydrate pellet to form water film layer on other surface of gas-hydrate pellet.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart explaining the manufacturing method of gas-hydrate pellet. (Drawing includes non-English language text)
NOVELTY - The assembly to prepare lignocellulose for pyrolysis has a hermetically sealed zone (14) with a pyrolysis unit (18). A conveyor screw compressor (5-9) acts as the inflow opening into the zone with a hermetic seal for the opening provided by a biomass strand of the compressed lignocellulose. The sealing prevents a convective gas exchange at the opening. A cutter or chopper (16), between the compressor and the pyrolysis unit, reduces the biomass strand into particles (19).    USE - The assembly is for the pyrolysis of biomass materials e.g. wood, straw, hay, paper, etc., to be used for base chemical materials or fuel. (Both claimed).    ADVANTAGE - The system handles inhomogeneous lignocellulose materials efficiently, with a simplified chain between delivery and pyrolysis.    DESCRIPTION OF DRAWING(S) - The drawings show schematic views of the pyrolysis assembly.    conveyor screw compressor (5-9)    hermetically sealed zone (14)    cutter/chopper (16)    pyrolysis unit (18)    biomass particles (19)
NOVELTY - The method involves expanding the nitrogen refrigerant streams (121,122) to intermediate and lower pressures. The differentially pressure expanded nitrogen refrigerant streams and the nitrogen refrigerant streams before pressure expansion are in heat exchanging relationship with natural gas, while heating operations is performed in several heat exchangers (116,117,118a,118b). The nitrogen streams are compressed in three-stage compressors (113,114,115a,115b). Hydrocarbons are removed from the natural gas after pre-cooling process. Complete cooling of natural gas is then performed.    USE - Natural gas liquefaction method for large-scale or offshore environment used for production of liquefied natural gas (LNG).    ADVANTAGE - Processes of natural gas liquefaction apparatus can be independently and efficiently performed, without the need of providing additional pre-cooling or liquefaction circuit, and without the need of performing complex procedures, while ensuring maximum heat exchange amount, and achieving complete liquefaction of LNG. A simple natural gas liquefaction apparatus or reduced size can be easily provided as only one refrigeration circuit is required, while reducing power consumption. Power requirements of the nitrogen refrigeration circuit can be reduced, as the natural gas is pre-cooled before reaching the nitrogen refrigeration circuit.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for natural gas liquefaction apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the natural gas liquefaction system.    Heat exchangers (101,103,116,117,118a,118b,202a,202b)    Compressors (113,114,115a,115b)    Nitrogen refrigerant streams (121,122)    Natural gas liquefaction system (200)    Heavy hydrogen column (219)
NOVELTY - Preparing hydrocarbon fuels comprises: removing carbon dioxide from the air; electrolyzing water to produce hydrogen; and hydrogenating the carbon dioxide with the hydrogen to form hydrocarbons, where the process primarily uses a renewable energy source comprising concentrated solar power, photovoltaic solar power, wind, hydro, and tidal energy, where the hydrocarbons produced would be suitable for fuel for air, road or sea transport and would, from an environmental perspective, be carbon neutral.    USE - The process is useful for preparing hydrocarbon fuels, which are useful for air, road or sea transport, from an environmental perspective, as carbon neutral.    ADVANTAGE - The hydrocarbons are excellent energy carriers. The process is cost-effective and disrupts less area in the earth.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an apparatus for the generation of the hydrocarbon fuel comprising means for harnessing renewable energy, means for removing carbon dioxide from air, means for the electrolysis of water, and means for the hydrogenation of the carbon dioxide with the hydrogen.
NOVELTY - In a waste pyrolysis furnace, having a pyrolysis tube (12) (with an externally accessible loading opening and material delivery opening), a combustion tube (26, 30) (receiving material from the pyrolysis tube and having an outlet opening) and an annular space (at least partially enclosing the pyrolysis tube and communicating with a flue gas outlet (40) and the combustion tube, so that flue gas flows into the space), the annular space is supplied with flue gas radially from the exterior.    USE - For pyrolysis of waste material, such as (preferably dried) clarified sludge from a municipal clarification plant.    ADVANTAGE - The arrangement eliminates the risk of destructive combustion processes at the transition between the pyrolysis and combustion tubes, which could cause damage to the furnace or even explosions. Maintenance costs are thus reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for operating a waste pyrolysis furnace, in which flue gas generated in a combustion tube (26, 30) is supplied to a space enclosing a pyrolysis tube (12) so that the pyrolysis tube is indirectly heated by the flue gas, where the pyrolysis gas flow path into the space runs outside the combustion and pyrolysis tubes.    DESCRIPTION OF DRAWING(S) - The figure shows a side view of a rotating tube furnace for pyrolysis of waste material.    Furnace (10)    Pyrolysis tube (12)    First section of furnace tube (24)    Furnace tube (26)    Combustion tube section of furnace tube (30)    Flue gas outlet (40)    Ash particle collector (42)    Flue gas channel (54)    Vertical sections of flue gas channel (54a, 54c)    Horizontal section of flue gas channel (54b)    Housing (56)    Burner (60)    Guiding rings (66, 68)    Driving ring (70)    Motor (72)    Partially burned gas tube (74)    External connection (78)
NOVELTY - A solid-liquid separator (1) separates the portion of liquid from the excrement of livestock. A vacuum valve unit (2) sucks out the separated liquid stored temporarily by a vacuum pressure. A vacuum tube (3) conveys a portion of sucked-out liquid by a vacuum pressure generated by a vacuum station (4) to biogas plant (B).    USE - Livestock excrement transit system for use in animal waste treatment plant.    ADVANTAGE - Excrement of livestock can be conveyed efficiently. Vacuum tube passage can be cleaned reliably using appropriate amount of wash water supplied by wash water supply unit. Excrement of livestock is conveyed to biogas plant for producing organic fertilizer.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the livestock excrement transit system. (Drawing includes non-English language text)    Solid-liquid separator (1)    Vacuum valve unit (2)    Vacuum tube (3)    Vacuum station (4)    Biogas plant (B)    Dairy facility (R)
NOVELTY - A clean fuel comprises (pts.wt.) methanol (5-90), light oil (10-80), methyl tert-butyl ether (3-20), light hydrocarbons (5-20), mixed octane (2-6), coal chemical light oil (6-20) and hydrogenation pentene (2-10).    USE - A clean fuel for vehicle (claimed).    ADVANTAGE - The clean fuel is energy-saving.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of preparing clean fuel comprising:    (A) adding raw materials into mixing tank, melting at normal temperature and under pressure for 30 minutes, and conveying to reactor through anti-explosion liquid pressure pump;    (B) opening anti-explosion impacting pump at output pressure of 10 MPa to form high-pressure liquid flow in reactor;    (C) forming strong collision from 2 high-pressure liquid flow to crush micropowder in liquid raw materials into particles of 10-30 nm and mix uniformly for 50 minutes; and    (D) conveying into storing tank through anti-explosion liquid pressure pump and stabilizing naturally at normal temperature and under pressure for 30 minutes.
NOVELTY - A mixed fuel comprises (wt.%) methanol (90-98) and hydrogen peroxide (2-10).    USE - A mixed fuel used for internal combustion engine of motorcycle or car.    ADVANTAGE - The mixed fuel reduces fuel cost of motorcycle and car, saves energy, improves combustion quality and does not contain sulfide, thus reducing sulfur dioxide content in smoke and protecting environment.
NOVELTY - The pyrolytic reaction purifying furnace is comprised of fixed bed down-draft gasification furnace, fire grate, feeding orifice arranged on the furnace wall, winding distributing mouth, slag discharging orifice and fuel outlet. The lower side of fire grate is provided with a fuel gas flow periphrastic flow way. The cracking catalyzing reaction bed can be arranged on the furnace bottom which is formed by particle catalyst and cover plate.    USE - Pyrolytic reaction purifying gas furnace for crop waste treatment.    ADVANTAGE - Provides pyrolytic reaction purifying gas furnace which forces fuel gas flow to slowly move in flow way, prolongs stopping time of fuel at high temperature environment. Improves tar cracking rate, gasification efficiency and fuel thermal value.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross sectional view of pyrolytic reaction purifying gas furnace.
NOVELTY - The device has an ash flue whose upper end is connected with an ash outlet of a gasification furnace. A lower end of the ash flue is provided with a rotary ash basin, and a rotary helical blade is provided in the ash flue. An ash scraper is provided on an outer surface of an ash pipe. A top end of the ash scraper is larger than an edge of the ash basin. Horizontal length of the upper end of the ash scraper surpasses the edge of the ash basin. A lower end of the ash scraper is lower than that of the ash flue.    USE - Wet ash discharging device for a biomass gasification furnace.    ADVANTAGE - The device has high automatic degree and protects environment.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial sectional view of a wet ash discharging device.
NOVELTY - Treatment of alkaline wastewater, which involves adding 10% solution of composition of alkalophilic bacteria comprising 2 strains of Bacillus alkalophilus mixed in equal proportion, to alkaline wastewater or effluents, adding starch/carbohydrates to the alkaline wastewater, and incubating for 2-7 days, is claimed. Image 0/0
NOVELTY - The business module comprises a meter (230), a bundled tube (170), a high level oxygen gas (150), a low level heating apparatus, a high level hydrogen gas (160), a low level utilization device, a low level heat absorption equipment (250) and a low level supply device. The high level oxygen gas is generated for an optical catalyst analysis (130) during the electrolysis of a water (100) and an air (110). A commercial transaction (410) is done between a producer (380) and a supplier (390). The commercial transaction is also done between the supplier and a user (400).    USE - Business module for high level oxygen hydrogen energy manufacturing.    ADVANTAGE - The business module comprises a meter, a bundled tube, and high level oxygen gas, where the high level oxygen gas is generated for an optical catalyst analysis during the electrolysis of the water and an air, thus ensures to prevent the pollution of water, and hence provides an economical business module.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic graphical representation of a business module.    Water (100)    Air (110)    Optical catalyst analysis (130)    High level oxygen gas (150)    High level hydrogen gas (160)    Bundled tube (170)    Meter (230)    Low level heat absorption equipment (250)    Producer (380)    Supplier (390)    User (400)    Commercial transaction (410)
NOVELTY - A liquid fertilizer contains (pts. wt.) biogas concentrated solution (50-80), urea (20-30), potassium dihydrogen phosphate (15-25), calcium chloride (1-3), magnesium sulfate heptahydrate (2-4), ferric chloride hexahydrate (1-1.5), zinc sulfate heptahydrate (0.8-1), boric acid (0.5-1), molybdic acid ammonium salt tetrahydrate (0.4-0.7), cupric sulfate pentahydrate (0.2-0.3), manganese chloride tetrahydrate (0.1-0.2), citric acid monohydrate (3-5), ascorbic acid (1-5), and Tween 80(RTM: polyoxyethylene (20) sorbitan monooleate) (1-5).    USE - Liquid fertilizer for use as soilless culture nutrient liquid for vegetable and/or as foliar fertilizer (claimed).    ADVANTAGE - The liquid fertilizer is environment-friendly and convenient to transport; and has stable fertilizer effect, sufficient nutrient ingredients, abundant material source, low cost and large usage area.    DETAILED DESCRIPTION - A liquid fertilizer contains (pts. wt.) biogas concentrated solution (50-80), urea (20-30), potassium dihydrogen phosphate (15-25), calcium chloride (1-3), magnesium sulfate heptahydrate (2-4), ferric chloride hexahydrate (1-1.5), zinc sulfate heptahydrate (0.8-1), boric acid (0.5-1), molybdic acid ammonium salt tetrahydrate (0.4-0.7), cupric sulfate pentahydrate (0.2-0.3), manganese chloride tetrahydrate (0.1-0.2), citric acid monohydrate (3-5), ascorbic acid (1-5), and Tween 80(RTM: polyoxyethylene (20) sorbitan monooleate) (1-5). The liquid fertilizer has a pH of 7-8.5. When the liquid fertilizer is applied, water is added for diluting 500-2000 times. Acid is used for regulating pH to 6-7.
NOVELTY - Production of granular calcareous material includes agglomerating shell powder and weathered coal, pelletizing, and processing into material for preventing blighted grain peanut.    USE - Method for producing granular calcareous material for preventing blighted grain peanut (claimed).    ADVANTAGE - The method is simple and convenient to implement; and not only reduces environment pollution, but also drives recycling utilization of resource. Raw material such as oyster shell has low cost. The granular material is convenient to use and promotes high-efficiency production of peanut.
NOVELTY - Production of methanol with co-production of methane comprises applying methane-containing synthesis gas to synthesize methanol; and utilizing residual components of hydrogen (H2), carbon monoxide (CO), and carbon dioxide (CO2) in the resultant methanol vent gas to synthesize methane.    USE - Method of producing methanol with co-production of methane useful as material for producing compressed natural gas and liquefied natural gas, and for recycling to ease temperature rise in the methanation reaction (claimed).
NOVELTY - Methane is produced by taking purge gas from methanol or coal-derived synthesis gas as raw material.    USE - Method of producing methane used as raw material for producing CNG or LNG (claimed).    ADVANTAGE - The method recycles heat from methanation products through multiple stages of heat exchange.
NOVELTY - A methanol gasoline fuel comprises (pts.wt.) gasoline (20-80), methanol (20-90), petroleum ether (2-10), 2-methyl pentane (1-5), octane (0-5), isooctane (0-5), diethyl carbonate (0-5), styrene (0-4), trimethylborate (0.2-4), di-n-butyl phosphate (0-5), dimethyl carbonate (0.5-5), methyl tert-butyl ether (0-5), ether (0-4), isopropyl ether (0-4), acetone (0-6), isopropyl alcohol (0-4), isobutyl alcohol (0-5), and antioxidant (0-4). The fuel is produced by mixing auxiliary agents with infusing gasoline and methanol, and sampling to detect and obtain the product.    USE - A methanol gasoline fuel.    ADVANTAGE - The fuel has increased octane number, and maintains stability of vehicle.
NOVELTY - A block-shaped industrial biomass fuel is prepared by airing straws until water ratio is lower than 35%, crushing, stacking, heating, decomposing, and drying until water ratio is lower than 30%; drying, heating, delaying and blowing air to dry straws until water ratio is lower than 25% at 30-60 degrees C; and doping block-shaped industrial biomass fuel additive (3-8 mass%), uniformly agitating, extruding, and molding. The straw is corn straw, cotton straw, kaoliang straw or wheat straw.    USE - Method of preparing block-shaped industrial biomass fuel (claimed).    ADVANTAGE - The method provides biomass fuel with 0.8-1.2 g/cm3 molding intensity, 95-97% molding rate, increased yield to 1-1.2 ton/hour, less than 75 kW/ton comprehensive energy consumption, increased ash fusion point to more than 250 degrees C, and more than 98% combustion efficiency.
NOVELTY - The toxic substance removal material includes a fiber assembly consists of fibers having diameters greater than or equal to 10 micrometers and made from non-polar polymeric material. The fabric weight of a fine fiber assembly of 1 micrometer or less of fiber diameters is 0.5 grams per square meter or less. The fine fiber assembly of 1 micrometer or less of fiber diameters is laminated on the fiber assembly of 10 micrometers or more of fiber diameters.    USE - Toxic substance removal material for countering viruses. Can also be used in producing air cleaners and liquid purifiers.    ADVANTAGE - Increases collection efficiency and eliminates raise of pressure loss in microfiber. Enables reliable removal of toxic substances.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a toxic substance removal method.
NOVELTY - A polymer electrolyte fuel cell system has a fuel cell main component (10) having two or more porous carbon electrodes arranged in parallel on both surfaces of a solid polymer electrolyte membrane, and a hydrogen producing material (30) for supplying hydrogen gas to fuel cell main component by decomposing water molecule. The main component has a printed wiring board comprising an opening for permeating hydrogen gas and oxygen at both surfaces.    USE - Polymer electrolyte fuel cell system is used as power supply in electronic device, such as integrated circuit tag.    ADVANTAGE - The polymer electrolyte fuel cell system is economical and has simple structure.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of polymer electrolyte fuel cell system. (Drawing includes non-English language text)    Fuel cell main component (10)    Hydrogen producing material (30)    Water vapor coagulator (32)    Aluminum lamination pack (34)    Spacer (36)
NOVELTY - The electron emission apparatus (X) has a transformer with primary coil and secondary coil that is connected to cathode of diode whose anode is connected to current limiting resistor. The current limiting resistor is connected to an emission end (EB) discharging electrons to a radiator. An emission circuit is provided with an input terminal connecting the trigger diode and one end of primary coil whose other end is connected to another input terminal.    USE - Electron emission apparatus for use in improvement of fuel consumption (claimed) of motor vehicle, ship and aircraft, and in purification of polluted water (claimed) drained from factory.    ADVANTAGE - The electrons discharged from the electron emission apparatus can be used to improve the fuel consumption and to purify the polluted water so that the environment pollution can be prevented and fuel consumption can be improved efficiently.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) fuel consumption improvement method; and    (2) purification method of polluted water.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the electron emission apparatus. (Drawing includes non-English language text)    Device main portion (1)    Power cord (2)    Electron emission unit (3)    Emission end (EB)    Electron emission apparatus (X)
NOVELTY - The composition has a base formulation of one or more alkyl esters of a C2-C12 carboxylic acid or mixtures, one or more alkyl esters of a vegetable oil, methyl hexate, methyl octanate, or mixtures and optionally butanol.    USE - Vegetable fuel composition for preparation of a lamp fuel, heating fuel, fuel for cooking and/or cooling fuel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for producing the vegetable fuel composition.
NOVELTY - The method involves generating reformed gas to modify hydrocarbon type fuel supplied by a modification burner (17). The water vapor for performing modification process is generated and supplied with combustion exhaust gas after heating a modification unit (3). The generated water vapor is heated by an electric heater (24). The modification burner is burned when the modification and the fuel supply starting conditions are satisfied and the water vapor generation process is started, to heat the water vapor generation unit (J) and hydrogen containing gas forming unit.    USE - Starting method of hydrogen containing gas production apparatus used in fuel cell power generating device.    ADVANTAGE - The modification burner is burned when the modification and the fuel supply starting conditions are satisfied and the water vapor generation process is started, to heat the water vapor and the hydrogen containing gas generators and hence the generation of damage to the water vapor generator is suppressed easily.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the fuel cell power generating device provided with hydrogen containing gas production apparatus. (Drawing includes non-English language text)    Modification unit (3)    Conduction chamber (8)    Modification burner (17)    Electric heater (24)    Water vapor generation unit (J)
NOVELTY - A raw material containing animal and vegetable fats is trans-esterified (A) with lower-alkyl alcohol using alkali catalyst, to obtain oil phase. The obtained oil phase is purified (B) by pouring the oil phase on ion-exchange resin, and reducing the soap. Then, purified oil phase is subjected to vacuum distillation (C), to obtain fatty acid lower alkyl ester. The degree of cross-linking is 8-16%. The ion-exchange resin is chosen from gel-type strongly acidic cation exchange resin or porous-type strongly acidic cation exchange resin.    USE - Manufacture of fatty-acid lower alkyl ester used for biomass fuel.    ADVANTAGE - The method provides highly purified fatty-acid lower alkyl ester in high yield and excellent stability.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of manufacture of fatty-acid lower alkyl ester (Drawing includes non-English language text).    Transesterification process (A)    Purification process (B)    Vacuum distillation process (C)
NOVELTY - The analyzer has a difference type photodetector (66) detecting absorption spectrum of a laser beam absorbed in waste gas. An absorption spectrum adjustment unit (71) adjusts the absorption spectrum, such that the absorption spectrum becomes high-limit-setting value by which the maximum value of the difference signal calculated by the photodetector is preset. A component density calculation unit (72) calculates the component density in waste gas using the absorption spectrum adjusted by the absorption spectrum adjustment unit.    USE - Analyzer for analyzing waste gas of an internal combustion engine of a vehicle. Uses include but are not limited to waste gas such as carbon monoxide, carbon dioxide, ammonia, methane and water.    ADVANTAGE - The component density calculation unit calculates the component density in the waste gas using the absorption spectrum adjusted by the absorption spectrum adjustment unit, thus improving detection accuracy of the spectral intensity of the absorption spectrum while increasing measurement precision of the component density in waste gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a waste gas analysis method.    DESCRIPTION OF DRAWING(S) - The drawing shows a functional block diagram of a computer apparatus.'(Drawing includes non-English language text)'    Controller (6)    Computer apparatus (7)    Difference type photodetector (66)    Absorption spectrum adjustment unit (71)    Component density calculation unit (72)
NOVELTY - A modifier (63) has inlet tube (62) which introduces fuel gas with water vapor connected to one end portion, and discharge pipe (64) which discharges reformed gas connected to other end portion. The inlet tube contains modified catalyst. The generated reformed gas is supplied to fuel electrode layer. The modified catalyst is ruthenium catalyst (83) and/or rhodium catalyst. The discharge pipe contains nickel catalyst (84). The content of ruthenium catalyst and/or rhodium catalyst is 3-10 volume% with respect to total content of modified catalyst.    USE - Modifier is used for flat-type solid oxide fuel cell (claimed) for household electric power generating apparatus, industry and thermal power station.    ADVANTAGE - The inactivation of catalyst in the modifier by carbon precipitation is prevented.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for flat-type solid oxide fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows sectional view of modifier.    Inlet tube (62)    Modifier (63)    Discharge pipe (64)    Ruthenium modified catalyst (83)    Nickel modified catalyst (84)
NOVELTY - Production of hydrogen comprises providing permeable vessel(s), causing an acid to permeate the permeable vessel, and collecting propagated hydrogen. The permeable vessel contains entrapped metal particles. The entrapped metal particles react with the acid to propagate hydrogen. The metal particles are exposed to reducing atmosphere.    USE - Method for production of hydrogen for use as renewable fuel for transportation and fuel cells (claimed).    ADVANTAGE - The method provides hydrogen without consumption of metal but with consumption of acid, and provides reduction of ionic metal products. The method allows metal to be regenerated, reused, and renewed.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) permeable vessel; and    (2) hydrogen gas production system.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross sectional diagram of the reactor system.    Hydrogen gas generator (100)    Reactor (101)    Jacket (102)    Gel beads (103)    Sintered discs (104)    Fluid inlet unit (105)
NOVELTY - Method for producing ethanol, involves adding saccharogenic amylase into reaction tank comprising biomass containing cellulose, performing enzymatic saccharification of the cellulose and producing saccharide; removing biomass residue produced by enzymatic saccharification of cellulose; removing saccharogenic amylase; adding ethanol fermenting microorganisms into the reaction tank, performing ethanol fermentation of the saccharide, and obtaining ethanol; and removing the ethanol fermenting microorganism.    USE - The method is useful for producing ethanol used as motor fuel.    ADVANTAGE - The increase in concentration of saccharide in the reaction tank can be suppressed and the saccharification activity of saccharogenic amylase can be maintained.    DETAILED DESCRIPTION - Method for producing ethanol, involves (a) adding saccharogenic amylase into reaction tank comprising biomass containing cellulose, performing enzymatic saccharification of the cellulose and producing saccharide; removing biomass residue produced by enzymatic saccharification of cellulose; removing saccharogenic amylase; adding ethanol fermenting microorganisms into the reaction tank, performing ethanol fermentation of the saccharide, and obtaining ethanol; and removing the ethanol fermenting microorganism; or (b) adding saccharogenic amylase and ethanol fermenting microorganism, and simultaneously performing enzymatic saccharification of cellulose and ethanol fermentation of the produced saccharide; and removing biomass residue, ethanol fermenting microorganism and saccharogenic amylase.
NOVELTY - A hydrogen production catalyst comprises metal supported by regular-mesoporous porous component. The metal is chosen from platinum, palladium, rhodium, rhenium, iridium, ruthenium and osmium. The catalyst modifies 2C or more oxygen-containing hydrocarbon, to generate hydrogen.    USE - Catalyst is used for producing hydrogen used for fuel cell system (both claimed).    ADVANTAGE - The hydrogen production catalyst efficiently and easily generates hydrogen in high yield. The generation of intermediate product such as ethylene, methane and acetaldehyde are suppressed by using oxygen-containing hydrocarbon.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) hydrogen production method, which involves contacting 2C or more oxygen-containing hydrocarbon with hydrogen production catalyst, and modifying oxygen-containing hydrocarbon; and    (2) fuel cell system, which comprises an oxygen-containing gas supply unit, a modifier filled with hydrogen production catalyst, and a fuel cell which generates hydrogen by modifying oxygen-containing gas supplied from oxygen-containing gas supply unit using the catalyst in modifier.
NOVELTY - The furnace has an ash gathering chamber assembled between an upper hearth and a lower hearth. An ash hole is opened at a middle part of the upper hearth. A radiating shade is provided in a dust hole. A lower end of the radiating shade and the lower hearth are welded together. A right end of an air inlet pipe enters a furnace body from bottom and extends upward to an upper end in the radiating shade. A left end of the air inlet pipe is connected in series to an air control valve, and an air outlet of a blower.    USE - Dual-purpose straw coal gasification furnace.    ADVANTAGE - The furnace has high energy-saving effect, sanitary and environment friendly usage and high efficiency. The furnace is inexpensive.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial sectional view of a dual-purpose straw coal gasification furnace.
NOVELTY - The use of marine yeast using a Rhodosporidium paludigenum to directly generating a microbiological fuel cell. An anode electrode (5) is placed in an open anode chamber (2). A cathode electrode (4) is placed in a open cathode chamber (1). A proton exchange membrane (3) is arranged between the anode and the cathode chambers. The anode chamber is filled with organic fuel liquid containing bacterium fluid and Sodium phosphate. A surface of the membrane is made of Nafion (RTM: sulfonated tetrafluoroethylene). The anode electrode is made of iron. The cathode electrode is made of graphite.    USE - Use of marine yeast.    ADVANTAGE - The microbiological fuel cell is environment friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a microbiological fuel cell preparation method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a use of a marine yeast.    Cathode chamber (1)    Anode chamber (2)    Proton exchange membrane (3)    Cathode electrode (4)    Anode electrode (5)
NOVELTY - A multifunctional concentrated liquid fertilizer comprises (pts.wt.) urea (10-33), monoammonium phosphate (10-30), potassium salt (10-60), sodium tetraborate (0.2-5), manganese sulfate (0.1-1), copper sulfate (0.1-1), zinc sulfate (0.1-1), ammonium molybdate (0.1-1.5), and hydroxyl cellulose (0.01-0.5).    USE - A multifunctional concentrated liquid fertilizer.    ADVANTAGE - The fertilizer has low cost, is rich in nutrients, and is environment-friendly.
NOVELTY - A long-acting self-polishing antifouling paint used for aluminum, steel substrate surface and waterline portion, comprises zinc acrylate, compound antifouling agent, pigment, filling material, anti-settling agent, and solvent; where the paint is dark red and acts as antifouling paint for seawater engineering or ship bottom; it can effectively prevent seawater creatures from damaging the ship bottom in 3-5 years; it is environment-friendly and convenient to construct; and it can keep the speed of the ship not to be affected and saves fuel.    USE - The long-acting self-polishing antifouling paint is useful for aluminum, steel substrate surface and waterline portion (claimed).    ADVANTAGE - The long-acting self-polishing antifouling paint can effectively prevent seawater creatures from damaging the ship bottom in 3-5 years. Moreover, it is environment-friendly and convenient to construct. Additionally, it can keep the speed of the ship not to be affected and saves fuel; and it has excellent overcoatability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for preparing the long-acting self-polishing antifouling paint.
NOVELTY - Catalyzing synthesis of biogasoline from sorbitol comprises preparing platinum-loaded catalyst comprising carrier that is molecular sieve HZSM-5 with particle size of 20-200 mesh, and platinum (0.5-2% of the quantity of carrier); mixing reduced catalyst with aqueous solution of sorbitol, and adding mixture into micro high pressure slurry bed of reactor; and introducing hydrogen to start the reaction. The high pressure hydrogen is introduced into reactor with core that is micro high pressure slurry bed through an inlet.    USE - Method of catalyzing synthesis of biogasoline from sorbitol (claimed), for use as vehicle gasoline.    ADVANTAGE - The method increases total octane number of product. The biogasoline has high octane number, conversion rate of greater than or equal to 80%, C5+ selectivity, and high isoparaffin content.    DETAILED DESCRIPTION - Catalyzing synthesis of biogasoline from sorbitol comprises preparing platinum-loaded catalyst comprising carrier that is molecular sieve HZSM-5 with particle size of 20-200 mesh, and platinum (0.5-2% of the quantity of carrier); mixing reduced catalyst with aqueous solution of sorbitol, and adding mixture into micro high pressure slurry bed of reactor; and introducing hydrogen to start the reaction. The high pressure hydrogen is introduced into reactor with core that is micro high pressure slurry bed through an inlet. The pressure of system is stabilized by using pressure maintaining valve and regulating value. The flow rate of hydrogen is regulated by using electromagnetic flow meter. The volume of tail gas is measured by using wet flow meter. The tail gas after the reaction is discharged from reactor.
NOVELTY - The treating method involves adopting chemical grade lead to perform lead lining treatment with contacting material of esterification reaction device. The esterification reaction device is made of common straight carbon steel.    USE - Treating method for esterification reaction device used for producing bio-diesel by taking different animals and plants ester or oil as raw material by inert metal lead used in anti-corrosive engineering processing.    ADVANTAGE - Improves service life of chemical engineering device and pipe and reduces corrosive rate of filled medium. Provides an inexpensive and simple method for treating esterification reaction device that takes different animals and plants ester or oil as raw material, and has strong anti-corrosive performance.
NOVELTY - A mobile soft methane tank comprises a tank body (1) having two sides that are provided with a feeding port (2) and a discharging port (3); where the top is provided with a gas conveying pipe (4); and the tank body is formed by connecting anti-acid and anti-alkali polyvinyl chloride material high in terylene strength.    USE - The mobile soft methane tank is useful for industrial and commercial applications.    ADVANTAGE - The mobile soft methane tank adopts anti-acid anti-alkali polyvinyl chloride cloth high in terylene strength as tank body; thus, it is bending-resistant, has fine flexibility, and high tensile strength; it insulates heat and temperature and resists moisture resistance and flame; the construction is simple; the tank body is firm; the cleaned tank body is convenient for storage when it does not produce methane; it is has no permeability; the bonding and sealing performance are fine; and it does not leak gas or water. Moreover, it is safe and practical; there is no need to embed the tank in stratum; the tank body can be separated from the ground; the conveying, moving, maintaining and cleaning of the tank body are easy; and it is appropriate for large scale industrial production.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the mobile soft methane tank.    Tank body (1)    Feeding port (2)    Discharging port (3)    Gas conveying pipe (4)
NOVELTY - The environment-friendly water-adding engine system comprises a system turbine, a hydrogen storage bottle, a hydrogen engine, a hydrogen generator for generating hydrogen by electrolyzing water through electric power provided by a battery, and a cooling exhaust system. The hydrogen produced by the hydrogen generator is injected into the hydrogen storage bottle, which is connected to the hydrogen engine through an air pipeline. The hydrogen engine is connected to the system turbine and the cooling exhaust system through a system electric generator.    USE - Environment-friendly water-adding engine system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the environment-friendly water-adding engine system.
NOVELTY - Converting a carbonaceous material to a product (H1) comprising at least one hydrocarbon or at least one alcohol, involves: (A) gasifying the carbonaceous material at a temperature of at least 700 degrees C to form synthesis gas; and (B) flowing the synthesis gas in a microchannel reactor (200) in contact with a catalyst to convert the synthesis gas to the product (H1).    USE - For converting a carbonaceous material (e.g. coal, oil, biomass, solid-waste, refuse derived fuel) to a product comprising at least one hydrocarbon or at least one alcohol useful as fuel (claimed) (e.g. automotive fuel, diesel fuel and aviation fuel).    ADVANTAGE - The process converts carbonaceous materials such as biomass, solid-waste to hydrocarbons and alcohols that can be used as synthetic fuel (e.g. automotive fuel, diesel fuel, aviation fuel); employs the use of microchannel reactors which are compact and readily transportable; can be adapted for use in apparatus that can be readily transported to remote locations, such as military bases; converts waste products generated at such military bases into fuels such as automotive fuel, diesel fuel, aviation fuel; can be adapted to produce 50-500 barrels per day of synthetic fuel at such a base; and can also be adaptable for use with larger scale operations where carbonaceous material sources such as municipal solid waste are converted to useful products such as synthetic fuel.    DESCRIPTION OF DRAWING(S) - The figure shows a flowsheet of the process for converting carbonaceous material to at least one hydrocarbon or at least one alcohol.    Gasifier (110)    Line for entering carbonaceous material to gasifier (112)    Line for flowing synthesis gas from gasifier into microchannel reactor; (116)    Microchannel reactor (200)    Line for flowing product out of microchannel reactor (202)
NOVELTY - Production of biofuels comprises: (a) production of bioethanol or bioethanol and sugar from beet or other raw materials; (b) production of other biocombustible materials and/or chemicals from bio-ethanol obtained in (a) or by-products obtained in (a).    USE - The method is useful for production of biofuels (claimed). The biofuel is useful for reducing energy costs.
NOVELTY - A multifunctional type control valve (510) provided in water inlet pipe (51) controls opening and closing of atrial siphon. A pressure emission pipe (52) discharges pressure in filtration pipe (1) and a pressure emission valve (520) is provided in pressure emission pipe. A soil pipe (53) outputs waste water after backwashing the filtration pipe to exterior through a tank filter (10). A backwashing pipe (54) is provided between each filtration pipe for performing backwashing operation and a flow volume valve (540) is provided in the backwashing pipe.    USE - Water treatment filter.    ADVANTAGE - The impurity, heavy metal or agrochemical compound in the water are removed and clean water is maintained.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the water treatment filter.    Filtration pipe (1)    Tank filter (10)    Water inlet pipe (51)    Pressure emission pipe (52)    Soil pipe (53)    Backwashing pipe (54)    Multifunctional type control valve (510)    Pressure emission valve (520)    Flow volume valve (540)
NOVELTY - A refrigerating machine oil comprises monoester with moving viscosity of not greater than 7 mm2/second at 40 degrees C.    USE - Refrigerating machine oil for refrigerant.    ADVANTAGE - The machine oil has low viscosity, and good safety and stability with chlorine-free nitrogen containing Freon refrigerant or halogen atom free hydrocarbon refrigerant with smaller greenhouse effect.    DETAILED DESCRIPTION - Refrigerating machine oil comprises monoester of formula (R1-C(O)-O-R2) with moving viscosity of not greater than 7 mm2/second at 40 degrees C.    R1=5-9C branched or straight chain alkyl; and    R2=8-10C branched or straight chain alkyl.    INDEPENDENT CLAIMS are included for:    (1) a a working fluid comprising refrigerating machine oil and hydrocarbon refrigerant selected from ethane, propane, butane and isobutene; and    (2) a refrigerator.
NOVELTY - Improved process for preparing stable immobilized biocatalyst, comprises (a) preparing 0.5-5% chitosan solution in acetic acid, (b) suspending biocatalyst in potassium phosphate buffer solution at 0.01M to 0.05M, (c) adding obtained biocatalyst suspension in chitosan solution as obtained in step (a), and (d) preparing membrane from chitosan-biocatalyst suspension of step (c) by conventional spreading and drying to get desired stable immobilized biocatalyst. The process utilizes acetic acid and potassium buffer solution for preparing chitosan solution and biocatalyst suspension respectively.    USE - The process is useful for preparing stable immobilized biocatalyst (claimed) which is useful in food, diary and pharmaceutical industries.    ADVANTAGE - The process: utilizes chitosan as the immobilization matrix which is biodegradable, inexpensive, non-toxic and environmentally friendly; is simple, economical and safer; and provides biocatalyst that are quite stable and does not leak out of the membrane.
NOVELTY - Electric power system comprises a cartridge (200), which is filled with cooling water, and a casing (100) having multiple base apertures. A hydrogen supply line (130) with multiple connectors (133) and a body (210) are also provided, where the inner side is coated with metal powder containing alkali catalyst for hydrogen generation. The cartridge is connected by a variable location unit to the inner side of the body. A pack assembling structure, a hinge and a cover are also provided. The casing is equipped with an inlet port and a vent to allow exchange of cooling water at the inner side.    USE - Electric power system for generating hydrogen.    ADVANTAGE - The electric power system produces hydrogen in desired amount.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of electric power system.    Casing (100)    Hydrogen supply line (130)    Connectors (133)    Cartridge (200)    Body (210)
NOVELTY - A biomass containing polyphenol group substance or phenol group substance, a solvent having hydrogen supply ability, a hydrogen activation catalyst, and a metal capable of dissolving in solvent and generating atomic hydrogen are mixed. Hydrogen is supplied from the solvent, added to aromatic ring of polyphenol group substance or phenol group, and substance is reduced and liquefied. Thus, polyphenol group substance or phenol group substance is processed.    USE - Processing of polyphenol group substance or phenol group substance, such as lignin for producing liquid fuel.    ADVANTAGE - The polyphenol group substance or phenol group substance is stably and efficiently reduced and processed at mild conditions. The generation amount of atomic hydrogen is increased.
NOVELTY - Cooking oil purification involves segregating impurities at reduced pressure by using supercritical fluid. The obtained cooking oil is extracted by using extractor at 32-100 degrees C. The extracted oil is refined for 1-10 hours. The supercritical fluid is selected from propane, butane, dimethyl ether or carbon dioxide.    USE - Method for purifying cooking oil for use as raw material for producing biodiesel fuel.    ADVANTAGE - The cooking oil purification method enables to remove impurities with high efficiency in an economic and eco-friendly manner, where the purified oil provides biodiesel fuel having high quality at low production cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the cooking oil purification method by using an apparatus.    Extractor (10)    Separators (20,21,22)    High pressure pump (40)    Cooking oil (50)    Carbon dioxide storage tank (60)
NOVELTY - Producing biodiesel, by mixing oil and absolute methanol in cold condition, adding catalyst of thionyl chloride and stirring to perform esterification reaction, cooling the liquid after the esterification reaction, when the temperature is lowered to 5-30 degrees C, adding water slowly, centrifuging the mixture liquid, adding alkaline solution into the upper layer of mixture liquid with biodiesel to modify the pH, water rinsing the upper layer of mixture liquid to be neutral, and then decompressing and distilling to obtain the biodiesel.    USE - The method is useful for producing biodiesel (claimed).    ADVANTAGE - The energy consumption is low, reaction time is short, and percent conversion of the biodiesel is high.    DETAILED DESCRIPTION - Method of producing biodiesel, involves (i) adding oil and absolute methanol into a reaction kettle in the ratio of 1:3-6, stirring the mixture of oil and absolute methanol in cold condition, when the temperature is lowered to 5-15 degrees C, adding catalyst of thionyl chloride slowly and stirring to perform esterification reaction, and stirring for 0.5-1 hour, where the content of thionyl chloride is 1-1.5 times of oil, and the temperature of the esterification reaction is 5-15 degrees C, (ii) cooling the liquid after the esterification reaction, when the temperature is lowered to 5-30 degrees C, adding water slowly, where the content of the water is 1.2-2 times of the thionyl chloride, (iii) centrifuging the mixture liquid, discarding the glycerin of the lower layer of mixture liquid, and adding alkaline solution into the upper layer of mixture liquid with biodiesel to modify the pH, where the pH of the upper layer of mixture liquid is 7-8, and water rinsing the upper layer of mixture liquid to be neutral, and then decompressing and distilling to obtain the biodiesel.
NOVELTY - A microemulsified biomass fuel comprises (wt.%) biomass fuel (4-45), diesel fuel (46-95), emulsifier (0.4-8), cosurfactant (0.05-0.2), oxidation and corrosion inhibitor (0.01-0.06), and heat value improving agent (0.01-1).    USE - A microemulsified biomass fuel (claimed) for use as biomass energy and for use in automobile.    ADVANTAGE - The microemulsified biomass fuel is stable for more than 1 year, has excellent antioxidation stability, is resistant to corrosion, produces less ash, and has high heat combustion heat value. Its preparation is simple and reliable, and has low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing the microemulsified biomass fuel comprising filtering impurities of biomass fuel, centrifuging to remove heavy components, reducing pressure, and distilling light component to obtain clear and transparent biomass fuel; adding lipophilic emulsifier to diesel fuel, stirring, adding hydrophilic emulsifier, uniformly stirring, homogenizing at 55-65 degrees C for 30-180 minutes at 6000-10000 rpm, adding oxidation and corrosion inhibitor, heat value improving agent and cosurfactant, homogenizing, and emulsifying.
NOVELTY - Extracting methane from oxygen-containing coal bed gas by liquefying and separating at low temperature comprises cooling raw gas of oxygen-containing coal bed gas, then rectifying the oxygen-containing coal bed gas so as to obtain separated and purified methane.    USE - The method is useful for extracting methane from oxygen-containing coal bed gas (claimed).    ADVANTAGE - The process and device for pre-treatment of raw gas are reduced, so that cost is reduced greatly.
NOVELTY - Biosynthetic diesel oil, comprises (in %) methanol (70-85), dimethylbutane (10-20), benzene (4-6), and amber (1-4). The biosynthetic diesel oil is prepared by adding methanol to reaction tank, and then adding dimethylbutane to the reaction tank within 15 minutes, stirring the mixture for 10 minutes, adding benzene to the mixture and stirring the mixture for 5 minutes, adding amber to the obtained mixture and stirring the mixture for 20 minutes and then filtering the mixture to obtain biosynthetic diesel oil.    USE - The biosynthetic diesel oil is useful as fuel for power machine and large and small size vehicles.    ADVANTAGE - The biosynthetic diesel oil can be prepared easily by a cost-effective process. The biosynthetic diesel oil has no residues, do not discharge waste liquid and does not cause environmental pollution.
NOVELTY - Blue flame compound is prepared using an additive and a basic fuel in a mass ratio of 0.5-1:1000. The basic fuel can be propane, liquefied petroleum gas, or light oil. The additive is composed of (in mass%) trimellitate (3-6), urotropine (5-12), cobalt naphthenate (0.2-4), methyl tert-butyl ether (10-40), n-octyl alcohol (2-8), methanol (1-10), 2,6-di-tert-butyl-p-cresol (501) (6-12), ferrocene (2-15), dimethylsiloxane (2-5), solvent naphtha 200 (20-50), nanoparticles of nickel/magnesium oxide supported on silica (5Ni/5MgO-SiO2) (0.5-1), and conditioner (1-10).    USE - The blue flame compound is useful as industrial fuel gas of nanometer (claimed) which is useful as energy source.    ADVANTAGE - The blue flame compound has high thermal value, and high working efficiency.
NOVELTY - A composition for use as a silage inoculant for enhancing biogas production comprising a biogas production enhancing amount of a biologically pure culture of Lactobacillus buchneri, strain LN4888 or LN4017, deposited under NRRL B-30866 or PTA-6138, respectively, or its functional mutant; and a suitable carrier, is new.    USE - The composition is useful as a silage inoculant for enhancing biogas production (claimed). Specifically, the composition is used as silage inoculant for improving degradation of plant biomass for enhanced production of biogas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for enhancing biogas production from plant silage comprising: adding an amount of a ferulate esterase containing composition to the silage, where the ferulate esterase is derived from a biologically pure culture of a ferulate esterase producing Lactobacillus strain or its functional mutant; adding the silage to a biogas generator; and producing an increased amount of biogas in comparison to silage not treated with a ferulate esterase containing composition.
NOVELTY - Disintegrated wood is loaded through a loading unit 2 to a horizontal reactor 1 with continuous counterflow supply of heat carrier from a fire chamber 8 by a screw 3 set at the beginning of the reactor 1 horizontal channel; separate dense but gas permeable layers of wood particles are produced continuously by prepressing. Pyrolysis is carried out sequentially in each prepressed layer with simultaneous withdrawal and condensation of steam and gases and their filtration in the prepressed layer.    USE - Woodworking industry.    ADVANTAGE - Invention allows for the increase of the disintegrated wood continuous thermal processing efficiency, increase the level of the wood waste utilisation, provide for meeting of the environment safety requirements due to the absence of toxic emissions into the environment. 2 cl, 1 tbl, 1 dwg
NOVELTY - The piezoelectric cell includes a thin piezoelectric crystal plate located in a structure comprising of three stacked plates. The stacked plates are coated with a material that can retain atomic oxygen. The piezoelectric cell generates the electric power required for dissociation from the pressure in the container housing the water vapor.    USE - Piezoelectric cell for water vapor dissociation. Can be used for performing water vapor dissociation of two water components, namely hydrogen and oxygen.    ADVANTAGE - Provides a piezoelectric cell that separates the components of water by polarizing the hydrogen atoms and oxygen atoms of water. Combines the piezoelectric properties of certain crystals with a dissociation cell system in a single device. Alters the composition typology of the fuel cell as well as the typical operation of the fuel cell in order to generate electrical power inside the actual dissociation cell.    DESCRIPTION OF DRAWING(S) - The drawing is a perspective view showing the layer structure of the piezoelectric cell for water dissociation.
NOVELTY - The rotary hydrogen generator includes a rotor and a stator, in addition to auxiliary mechanical components. Piezoelectric cells are housed in the side notches in the rotor. The rotary hydrogen generator also has a device which can cyclically subject the piezoelectric cells to different pressure states to break down the water molecule and other compounds containing into their respective components. The cycle takes place during the time required for the side notches of the rotor to complete a full turn.    USE - Rotating hydrogen generator used in production of hydrogen. Can be used for separating hydrogen from compounds like water vapor or other compounds containing hydrogen such as alcohols and hydrocarbons.    ADVANTAGE - Provides a rotary generator that provides a satisfactory way of performing physical separation of hydrogen content in compounds like water vapor, or other compounds containing hydrogen such as alcohols and hydrocarbons. Prevents formation of cracks in the rotor to prevent water vapor from leaking through the cracks on the external wall of the rotor. Ensures easy and simple alignment and assembly of the rotor and stator to form the rotary hydrogen generator.    DESCRIPTION OF DRAWING(S) - The drawing is a sectional view showing how a rotor fits inside the stator of the rotary hydrogen generator.
NOVELTY - Preparation of coal-like material from biomass, comprises: (i) heating a reaction mixture comprising water and biomass to obtain a reaction mixture comprising activated biomass; and (ii) adding a polymerization initiator to the reaction mixture to polymerize the activated biomass and to obtain a reaction mixture comprising coal-like material.    USE - The process is useful in the preparation of coal-like material from biomass (claimed), where the biomass is crop, agricultural food and waste, feed crop residues, wood (such as wood flour, wood waste, scrap wood, sawdust, chips and discards), straw (including rice straw), grass, leaves, chaff and bagasse.    ADVANTAGE - The coal-like material has, in terms of its dry mass: a carbon content of greater than 50 wt.% and/or a calorific value of greater than 23 (preferably 24)MJ/kg. The process: provides an improved and quicker yield of the coal-like material in enhanced space-time yield, and allows for enhanced quality control of the final product, as well as improved reproducibility; is cheaper in terms of the necessary equipment (less elaborate and less expensive equipment (e.g. a simple autoclave)) and it is a very safe process; avoids the energy-consuming drying of the biomass; does not contain any contaminants such as metals; and minimizes formation of side products. The residual liquid phase obtained in the separation subsequent to step (ii) is reused in the hydrothermal carbonization process.
NOVELTY - A plasma sheet is used as a unit (A) for manufacturing gas by pyrolytic heating, gasifying and dissociation of large volumes of starting materials (10).    USE - Plasma sheet for manufacturing gas from hydrogen-bearing starting materials such as carbonaceous materials for e.g. coal, petroleum and natural gas, and waste including municipal solid waste, industrial waste and biomass. Can also be used for manufacturing ceramic tiles, carbon black, carbon nanotube, pyrolytic graphite for insulation, and road paving materials.    ADVANTAGE - The process enables high-volume and high mass-flow rate manufacture of gas at low cost, and is environment-friendly.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a plasma array (45) is used as a unit (B) for manufacturing gas by pyrolytic heating, gasification and dissociation of large volumes of starting materials    (2) a process for high-volume and high mass-flow rate manufacture of gas by pyrolytic heating, gasification and dissociation of large volumes of starting materials using the plasma sheet or the plasma array.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a plasma reactor comprising plasma sheets in an array.    Starting materials (10)    Hopper (15)    Control system (30)    Plasma array (45)    Slag pool (55)
NOVELTY - An apparatus (100) for generating hydrogen comprises electrolytic bath (130) to contain electrolyte solution (135); anode (110) placed inside the electrolytic bath to generate an electron; a cathode (120) placed inside the electrolytic bath to generate hydrogen by receiving electron from anode; controller (140) electrically connected to the anode and cathode, to control flow of electricity between anode and cathode; and hydrogen generating material (170) to generate hydrogen through the reaction with electrolyte solution to start the controller.    USE - As apparatus for generating hydrogen useful in fuel cell power generation system (claimed).    ADVANTAGE - The auxiliary power source can be removed by electrically connecting the mechanical switch to the controller in parallel. The fuel cell power generation system is manufactured with reduced cost in smaller size and is capable of more stably generating the electrical energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell power generation system comprising the apparatus for generating hydrogen; and a fuel cell configured to generate electrical energy by converting chemical energy of the hydrogen generated from the cathode and hydrogen generating material.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of an apparatus for generating hydrogen.    Apparatus (100)    Anode (110)    Cathode (120)    Electrolytic bath (130)    Electrolyte solution (135)    Controller (140)    Hydrogen generating material (170)
NOVELTY - An apparatus (100) for generating hydrogen comprises an electrolytic bath, to contain electrolyte solution; anode (110) placed inside electrolytic bath (130), to generate electron; cathode (120) placed inside the electrolytic bath, to generate hydrogen by receiving electron from anode; controller (140) electrically connected to the anode and cathode, to control flow of electricity between the anode and cathode; and mechanical switch (170) electrically connected to the controller in parallel, to flow electricity between the anode and cathode to start the controller.    USE - As apparatus for generating hydrogen useful in fuel cell power generation system (claimed).    ADVANTAGE - The auxiliary power source can be removed by electrically connecting the mechanical switch to the controller in parallel. The fuel cell power generation system is manufactured with reduced cost in smaller size and is capable of more stably generating the electrical energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a fuel cell power generation system comprising the apparatus for generating hydrogen; and a fuel cell configured to generate electrical energy by converting chemical energy of the hydrogen generated from the cathode.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of an apparatus for generating hydrogen.    Apparatus (100)    Anode (110)    Cathode (120)    Electrolytic bath (130)    Controller (140)    Mechanical switch (170)
NOVELTY - An M15-M85 alcohol ether fuel comprises (wt.%) gasoline (10-85), methanol (10-85), cosolvent (0.1-1.5), preservative, and modified compounding agent (1.5-30).    USE - M15-M85 alcohol ether fuel for vehicle, e.g. engine.    ADVANTAGE - The fuel has strong dynamical property, good energy-saving effect, excellent acceleration property, high octane number and strong power; thus providing engine with high compression ratio, improved efficiency, and increased rate of economizing gasoline which is more than 15-21%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of preparing M15-M85 alcohol ether fuel by mixing cosolvent, infusing gasoline, synthesizing methanol and mixed cosolvent, sampling, and detecting sample.
NOVELTY - A high-water-content organic waste containing livestock excretion and/or foodstuff waste material is dehydrated, and chlorine and/or chloride compound contained in the organic waste are removed. The obtained dechlorinated organic waste is dried or heat-dried using combustion exhaust gas produced during incineration of low-moisture content organic waste. The dry dechlorinated organic waste has chlorine concentration of 3000 ppm or less and moisture content (W) of 30 mass% or less. Thus, fuel-formation method of high-water-content organic waste is carried out.    USE - Fuel-formation method used for producing biomass fuel (claimed). Can also be used for electric power generation and cement manufacturing process.    ADVANTAGE - The biomass fuel having high combustion efficiency is manufactured eco-friendly and economically using high-water-content organic waste containing livestock excretion and/or foodstuff waste material. The obstruction of corrosion piping in the combustion apparatus during burning of biomass fuel is prevented.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biomass fuel, which is obtained by drying or heat-drying dechlorinated organic waste using combustion exhaust gas.    DESCRIPTION OF DRAWING(S) - The drawing shows the flowsheet of fuel-formation installation used for fuel-formation method. (Drawing includes non-English language text)    Dehydrator (2)    Incinerator (3)    Heat exchanger (4)    Drying machine (5)    Moisture content (W)
NOVELTY - The pre-processor processes the biomass hydrothermally in specific temperature and pressure within range of 0.1-4Mpa. The obtained slurry of biomass containing nonmetallic type catalyst is introduced into heater and is heated. The heated slurry of biomass is introduced into pre-heater and is pre-heated. The slurry of pre-heated biomass is introduced into reactor and is hydrothermally treated in pressure of 22.1MPa or more. The slurry of biomass adhered on inner surface of heater, reactor and piping which connects heater and pre-heater, is peeled by peeling apparatus.    USE - Biomass gasification system with biomass adhesion prevention function.    ADVANTAGE - The occlusion of interior of piping due to adhesion of slurry of biomass on the inner surface of piping which connects heater and pre-heater, can be prevented. The energy can be efficiently exploited by using biomass gasification system with biomass adhesion prevention function. The amount of heating fuel, and waste gas generation amount can be reduced reliably.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biomass adhesion prevention method involves peeling slurry of biomass adhered on inner surface by giving vibration or by spraying gas to at-least one or more inner surface among inner surface of piping which connects the heater and pre-heater, inner surface of reactor. The slurry of biomass adhered on inner surface is peeled when the temperature of the heater is set to 26.0 or more.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical view representing the pressure near exit of heat exchanger of pre-processor with respect to starting time of the biomass gasification system. (Drawing includes non-English language text)
NOVELTY - The biomass gasification system has a preheater with a second heat exchanger (131) that pre-heats gas containing oxygen using the exhaust heat of an electric power generating apparatus. A jam prevention apparatus (260) has a heat resistant wire (261) that penetrates an exit from the inlet port of one pipe of the second heat exchanger. A drive device (262) performs driving of the wire.    USE - Biomass gasification system with biomass adhesion prevention function for processing livestock excretion. Uses include but are not limited to organic refuse, foodstuff waste material, and sewage sludge.    ADVANTAGE - Prevents obstruction in the reactor by peeling the slurry of biomass from the inner surface of the reactor. Prevents flow back of the slurry body through the valve.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biomass processing method.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of the second heat exchanger. (Drawing includes non-English language text).    Second heat exchanger (131)    Peeling apparatus (250)    Jam prevention apparatus (260)    Heat resistant wire (261)    Drive device (262)
NOVELTY - The system has a gasifier that thermally decomposes waste material and generates pyrolysis gas. A reformer (5) reforms the pyrolysis gas emitted from the gasifier to generate fuel gas. A desulfurizing agent injection unit injects desulfurizing agent of a granular material into the duct of fuel gas to remove sulfur compound in fuel gas. A bag filter (23) is positioned at the downstream side of the desulfurizing agent injection unit.    USE - Waste material gasification processing system for generating fuel for gas turbine. Uses include but are not limited to gasification process of municipal solid waste, wood type biomass, car shredder dust and industrial waste.    ADVANTAGE - The desulfurization rate can be improved and the pressure loss of fuel gas can be reduced. The reaction products collected in the bag filter can be recovered and the desulfurizing agent can be recycled.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the waste material gasification processing system. (Drawing includes non-English language text)    Reformer (5)    Heat recovery boiler (9)    Hopper (13,27)    Bag filters (19,23)    Electric power generation unit (26)
NOVELTY - The electrode (2) has electroconductive flat springs (8,9) that connect working electrodes (6,7) and multipole boards (3,4). An ionic permeability diaphragm (5) is arranged between the working electrodes. The working electrodes, multipole boards and flat springs are made of iron, iron alloy, nickel and nickel alloy. The nickel plating, nickel sulfur plating, platinum plating or platinum type alloy plating is formed on the electrode.    USE - Electrode for alkaline water electrolysis apparatus used for manufacturing hydrogen by performing gasification of coke or petroleum.    ADVANTAGE - The deformation of the working electrode can be prevented, since the load acting on the working electrode can be reduced due to the elastic deformation of the flat springs. The mechanical strength and dimensional accuracy of the electrode can be improved, since the gap formed between the diaphragm and working electrodes can be prevented. The hydrogen overvoltage of the electrode can be reduced, so that the electrolysis efficiency can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows an expanded sectional view of the electrolysis unit of the alkaline water electrolysis apparatus comprising electrode.    Electrode (2)    Multipole boards (3,4)    Ionic permeability diaphragm (5)    Working electrodes (6,7)    Flat springs (8,9)
NOVELTY - Preparing environmentally friendly fertilizers using peat and liquid manure, is claimed.    USE - The process is useful for preparing fertilizers. No biological data given.    ADVANTAGE - The process provides environmentally friendly fertilizers. The process is cost-effective for preparing the fertilizer.
NOVELTY - Gas quality determination involves measuring optical absorption and thermal conductivity of carbon monoxide, carbon dioxide and methane in gas sample. The optical absorption of the gas sample is measured by infrared spectroscopic measurement. Determined parameters of the gas sample are calorific value, density, Wobbe Index and methane number.    USE - Method for determining quality of a gas sample including hydrogen, carbon monoxide, carbon dioxide, nitrogen and methane as main components.    ADVANTAGE - The gas quality determination method enables to determine the quality of the gas sample in an eco-friendly manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the gas quality determination method. (Drawing includes non-English language text).
NOVELTY - A gasifier (5) generates thermal decomposition residue. A reformer (13) reforms the pyrolysis gas to generate the reformed gas. A heat recovery boiler (17) recovers the heat of reformed gas discharged from reformer. A bag filter (23) collects the dust contained in reformed gas discharged from heat recovery boiler. Supply units supply the dust collected by heat recovery boiler and bag filter to gasifier. Water vapor is injected into reformer to convert the carbon in pyrolysis gas into water gas.    USE - Waste-material gasification processing system used for decomposition of waste-material such as municipal solid waste, biomass, car shredder dust and industrial waste.    ADVANTAGE - The tar contained in the pyrolysis gas can be decomposed thermally, so that the concentration of tar in the pyrolysis gas can be reduced efficiently.    DETAILED DESCRIPTION - A fractionation unit fractionates thermal decomposition carbon from the thermal decomposition residue. A combustion furnace burns the thermal decomposition carbon. A cooling unit cools the waste gas discharged from combustion furnace. A supply unit supplies fly-ash collected by cooling unit to gasifier.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic block diagram of the waste-material gasification processing system. (Drawing includes non-English language text)    Drier (1)    Gasifier (5)    Reformer (13)    Heat recovery boiler (17)    Bag filter (23)
NOVELTY - The method involves performing a thermal decomposition process to thermally decompose a waste material (a) e.g. municipal solid waste, and to generate pyrolysis gas (b) and residue (c). A gas reforming process is performed for reforming altitude-advantage hydrocarbon by adding and heating an oxidizing agent. A heat recovery process is performed to collect heat energies from a reformed gas (f) that is produced during the reforming process. Carbonized materials (g) are supplied to an entrance side whose temperature is maintained at specific degrees.    USE - Refuse-disposal method for carrying out reforming of pyrolysis gas from waste material such as industrial waste containing general wastes and flammables, and municipal solid waste, where the pyrolysis gas is recycled into a fuel gas such as gas-engine fuel and fuel cell fuel.    ADVANTAGE - The method effectively supplies carbonized materials to the entrance side, thus resulting in adhesion of tar to the carbonized material, reliably collecting the carbonized material and soot by a dust removal bag filter, achieving improvement in energy-recovery efficiency, and preventing trouble of the gas cleanup process.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a garbage disposal equipment.'(Drawing includes non-English language text)'    Waste material (a)    Pyrolysis gas (b)    Residue (c)    Reformed gas (f)    Carbonized material (g)
NOVELTY - A sludge aerobic compost device comprises a fermenting chamber (1) and a draining device (8); where the fermenting chamber is equipped with an exhaust port (5) and a vent (2), which are communicated to its interior; the exhaust port is formed at the upper part of the fermenting chamber, and lower part of the fermenting chamber is equipped with a water treatment device (3) in a demountable way; and the lower part of the fermenting chamber is communicated to the draining device in a detachable way.    USE - The sludge aerobic compost device is useful for industrial and commercial applications.    ADVANTAGE - The sludge aerobic compost device discharges material conveniently and can be conveniently cleaned.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the sludge aerobic compost device.    Fermenting chamber (1)    Vent (2)    Water treatment device (3)    Exhaust port (5)    Draining device (8)
NOVELTY - The complete equipment comprises a material tank with outlet connected to a first oil pump (2-1), a plate-frame filter (3), a temporary storage tank (4), and a vacuum drying kettle (5) in series. A second oil pump (2-2) is connected to a first esterification kettle (6), which is connected to a second esterification kettle (9) by a third oil pump (2-3). The second esterification kettle is connected to a vacuum drying boiler (12), which is connected to a distilling kettle (13) by a fourth oil pump. The distilling kettle is connected to a finished-product oil-storage tank by a condenser (14).    USE - Complete equipment for producing biodiesel.    ADVANTAGE - Can effectively solves the production of the biodiesel and satisfies need of the fuel. Achieves a simple structure, low cost, easy operation, high extract effect, energy-saving and environment-friendly performance.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic illustration of the complete equipment for producing biodiesel.    First oil pump (2-1)    Second oil pump (2-2)    Third oil pump (2-3)    Plate-frame filter (3)    Temporary storage tank (4)    Vacuum drying kettle (5)    First esterification kettle (6)    Second esterification kettle (9)    Vacuum drying boiler (12)    Distilling kettle (13)    Condenser (14)
NOVELTY - The system has a feed port (10) for supplying biomass. A heat transfer member (22) is installed in a side wall of furnace according to drop direction of the biomass. A pyrolysis mat (24) is installed in a lower part of the heat transfer member. A gas exhaust port (30) for ejecting gas is connected with the feed port. A carrier (50) supports a lower part of the furnace.    USE - Biomass gasification system.    ADVANTAGE - The system occupies less space and facilitates installation and movement, and can efficiently change the biomass to combustible fuel. The system has better operating efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of a biomass gasification system.    Feed port (10)    Heat transfer member (22)    Pyrolysis mat (24)    Gas exhaust port (30)    Carrier (50)
NOVELTY - The system has a central control panel (60), and an electric power converting section (20) for measuring reactive power values. A distributor distributes the reactive power values, and a linear control part performs linear control of the system. An anti-accumulation prevents accumulation saturation of the linear control part, and a linear distributor (70) is equipped with a driven comparator producing an error signal. A control signal is transmitted to the electric power converting section.    USE - Electric power generating system for use in a light power generation facility, wind-driven electric plant and a fuel cell generation facility.    ADVANTAGE - The system avoids voltage drop and voltage rise by using the reactive power of the electric power converting section, and prevents the generator from being intercepted. The system has high efficiency and stable power quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for driving an electric power generating system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of an electric power generating system.'(Drawing includes non-English language text)'    Generator (10)    Electric power converting section (20)    Voltage comparator (40)    Central control panel (60)    Linear distributor (70)
NOVELTY - Modification system for woody biomass gas has thermal decomposition furnace (1) for thermally decomposing woody biomass, modification-reaction device (2) where carbonized material particles from gas produced in thermal decomposition furnace is supplied and tar vapors are modified to hydrogen, carbon monoxide and carbon dioxide, and engine (3) which uses the modified gas as fuel.    USE - Modification system for woody biomass gas.    ADVANTAGE - Thermochemical regeneration of tar is achieved, contained tar is reduced and removed, heat energy of tar is used effectively as fuel, reaction is performed at low temperature, is cost-efficient, tar adhesion, staining and trouble due to caulking is not produced, engine durability is improved and installation, wastewater treatment and maintenance costs are reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of modification system for woody biomass gas.    Thermal decomposition furnace (1)    Modification reaction device (2)    Engine (3)    Pipe line (4)    Raw material hopper (5)
NOVELTY - A biological harmless efficient dynamic fermenting equipment for cow dung comprises an embedded cement fermenting tank set in shed; where a walking orbit is set on the upper edge of tank wall of the fermenting tank; a walking type turning and throwing machine capable of moving forward and backward is mounted on the walking orbit; and a turning and throwing endless track capable of moving leftward and rightward is set on the walking type turning and throwing machine.    USE - The biological harmless efficient dynamic fermenting equipment is useful for cow dung (claimed).    ADVANTAGE - The biological harmless efficient dynamic fermenting equipment can effectively reduce the fermenting pollution; where the fermenting period is short; and it solves the problems comprising harmful treatment of cow dung and resource utilization. Moreover, the cow dung is treated through the device to shorten the fermentation period to 7-8 days and reduce the polluting time; where in the shed, the abuse that cow dung and outer air are contacted directly is reduced; and the space for spreading pollution is cut off.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the biological harmless efficient dynamic fermenting equipment for cow dung.
NOVELTY - The concrete nutritious flowerpot comprises 20-40 mass percent magnesium oxide, 3-8 mass percent urea, 3-8 mass percent potassium fertilizer, 6-15 mass percent calcium superphosphate, 15-30 mass percent clay, 5-15 mass percent paper pulp or wooden meal and 15-20 mass percent magnesium chloride.    USE - Concrete nutritious flowerpot for use in gardening and furnishing.    ADVANTAGE - Grows well without artificial fertilizer application. Enables environmentally-friendly degradation of waste flowerpot. Ensures cost-effective production of flower pot which is convenient and practical to use.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a concrete nutritious flowerpot preparation method.
NOVELTY - The technique involves mixing and stirring biomass particles and biomass oil according to appropriate proportion and forming pulp biomass, and sending pulp biomass into a thermal cranking reactor and gasifying at a high temperature. The gasified pulp biomass is separated in carbon particles and gas by a whirlwind separator. A carbon collector collects the carbon particles. Gas is condensed with biomass to form bio-fuel by a gas-water heat exchanger and an oil collector. The biomass is provided with crop straw, plant straw, tree branches and wood dregs.    USE - Technique for atomizing and thermal cranking a pulp biomass.    ADVANTAGE - The pulp biomass has atomizing effect and stable temperature range. The pulp atomizing realizes uniform mixing of the gas and the material, thus guaranteeing the thermal crank and increasing thermal crank effect and material use ratio. The technique enhances compact structure, continuous and circular operation, high manufacturing efficiency and high oil production yield. The method is inexpensive.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a pulp biomass atomizing and thermal-cracking device comprising an on-line grinder connected between a screw-rod pulp transmitting pump.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow chart of a pulp biomass thermal cranking and atomizing technique.'(Drawing includes non-English language text)'
NOVELTY - Preparation of biodiesel oil and its side product comprises pretreating plant oil, animal oil or waste edible oil; adding alcohol solution of catalyst for ester-exchange reaction, and roughly separating ester-exchanged product to obtain crude methyl ester or crude ethyl ester; and carrying out multilevel molecular distillation by degassing, purifying and decoloring crude product to prepare biodiesel oil and side products including fatty acid monoglyceride and its derivatives.    USE - Method for preparation of biodiesel oil and its side product including fatty acid monoglyceride and its derivatives (claimed).    ADVANTAGE - The method is environment-friendly and easy to industrialize; and completes purification and refinement of biodiesel oil, and reduces cost of biodiesel oil. The purified biodiesel oil has higher purity and meets international standard.
NOVELTY - Biodiesel is prepared by mixing methanol and oil having not less than 3 mg potassium hydroxide (KOH)/g acid value, standing to obtain methanol phase and oil phase, decompressing methanol phase, distilling to reclaim methanol, and acid catalyzing obtained distillate in methanol; and performing alkaline catalysis to reclaimed methanol and oil phase. The oil phase has not less than 0.1-3 mg KOH/g acid value.    USE - Method of preparing biodiesel (claimed).    ADVANTAGE - The method neutralizes acidity of the oil by physical process thus loses is reduced, and has low energy consumption and short reaction period. The de-acidified product of high acid value oil is directly catalyzed to prepare the biodiesel. The method has low cost, and reduces hazard in acid catalyzing the oil.
NOVELTY - An electrolytic tank (2) is formed by connecting electrolytic chambers (1) each split into small electrolytic chambers by polar plates with rhombic convex-concave grooves. The positive and negative electrodes of tank are connected with corresponding electrodes of electrolytic power (3). At top part of each electrolytic chamber is gas discharging tube (101) connected to gas cylinder manifold (4) whose gas discharging end is connected to internal water seal (5) connected to external water seal (6) via gas guide tube. The outer side of electrolytic chambers has cooling circulation device.    USE - Hydrogen-oxygen mixed gas generator.    ADVANTAGE - Uses multi-chamber electrolysis, enables adequate utilization of electric energy efficiency, and water cooling circulation device set outside electrolytic tank has evident radiating effect, thus improving quality of hydrogen-oxygen mixed gas, and ensuring stability of working liquid level and usage effect of opening machine for a long time. Electrolytic tank uses bubbles that are easy to break and electrode plates of convex-concave groove capable of increasing electrolytic effective area, thus gas yield is enlarged.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the hydrogen-oxygen mixed gas generator.    Electrolytic chambers (1)    Electrolytic tank (2)    Electrolytic power (3)    Gas cylinder manifold (4)    Internal water seal (5)    External water seal (6)    Gas discharging tube (101)
NOVELTY - A holder (10) has polymeric absorber (14) which absorbs and maintains volatile organic material from soil or underground water, and active promoter (12) of volatile organic compound decomposing microbe.    USE - Holder for volatile organic material decomposition microbes such as Dehalococcoides genus, Desulfitobactrium genus, Desulfomonile genus, Dehalobacter genus, Dehalospirillum genus, Desulfomicrobium genus, Clostridium genus, Acetobacterium genus, Rhodococcus genus, Xanthobacter genus and/or Mycobacterium genus, used in purification of contaminated soil (all claimed) and underground water.    ADVANTAGE - The holder enables to decompose the volatile organic material in contaminated soil with high efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for purification method of contaminated soil, which involves injecting the holder in soil contaminated by volatile organic material.    DESCRIPTION OF DRAWING(S) - The drawing shows the perspective view of the holder.    Holder (10)    Active promoter (12)    Polymeric absorber (14)
NOVELTY - The trapping machine has bait air inlet which is connected with air outlet of butane-carbon dioxide generator that is used as air source of trapping machine. The butane-carbon dioxide generator is provided with butane tank and generator which is provided with mixing and burning chambers.    USE - Trapping machine for mosquito.    ADVANTAGE - Provides a trapping machine that can conveniently generate a carbon dioxide by using a butane tank, and is convenient to use.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of trapping machine for mosquito.
NOVELTY - The power-generating mosquito trapper has inlet end of power supply which is connected with butane-carbon dioxide-sterling thermo-electric generating device through storage batteries. The butane-carbon dioxide-sterling thermo-electric generating device is provided with combustor, sterling machine and power generator.    USE - Butane-carbon dioxide-sterling thermo-electric power-generating mosquito trapper.    ADVANTAGE - Provides a mosquito trapper that can be used conveniently since butane pot is used to burn the butane so electric power needed by the mosquito trapper with the sterling machine can be supplied with one step.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic sectional view of butane-carbon dioxide-sterling thermo-electric power-generating mosquito trapper.
NOVELTY - The butane-carbon dioxide generator has gas nozzle which is arranged on mixing chamber. The outer side end of gas nozzle is connected with butane gas tank, while inner nozzle is located in mixing chamber. An air perforation is set on mixing chamber. A generator shell arranged at front end of filter body is provided with gas outlet, while front end of burning chamber is provided with filter body that is made from loose cordierite.    USE - Butane-carbon dioxide generator.    ADVANTAGE - Provides a butane-carbon dioxide generator that uses a butane gas tank as production source of carbon dioxide, and conveniently reduces usage amount of carbon dioxide gas.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of butane-carbon dioxide generator.
NOVELTY - A gasification furnace has gas-separating chamber (2) and superheating chamber (4) set in the fire-proof furnace chamber (5) of second gasification furnace chamber. Gas-separating chamber is connected to superheating chamber. The bottom plate of furnace (24) is arranged at the bottom of first and second gasification furnace chambers. The furnace wall of first gasification furnace is formed by the fire-proof furnace liner (35), heat insulating layer (6) and shell (7). The furnace wall of second gasification furnace is formed by fire-proof furnace liner, heat insulating layer and shell.    USE - Gasification furnace used for treating biomass and trash to convert into valuable synthetic gas, such as coal gas for city use and other gas materials used for producing hydrogen, methanol and dimethyl ether.    ADVANTAGE - Improves efficiency of gasification furnace and quality of synthetic gas by treating trash and biomass by gasification process. Provides gasification furnace that is good for purification process by removing tar and poisonous dioxin and reducing pollutant in synthetic gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of the gasification furnace.    Gas-separating chamber (2)    Superheating chamber (4)    Fire-proof furnace chamber (5)    Heat insulating layer (6)    Shell (7)    Furnace (24)    Fire-proof furnace liner (35)
NOVELTY - The device has a heating furnace comprising a burning furnace (1) and a cracking furnace (2) that are communicated with each other. The burning furnace is equipped with a shell (1.0), a gasification chamber (1.1) and a burning chamber (1.2). An upper part of a cracking furnace is equipped with a cracking cylinder (2.1) that is filled with a kitchen wastage e.g. waste rubber, as cracking materials. An end of the cracking cylinder is equipped with a rotating driving part (2.4) and an oil outflow pipe (2.7), and a chimney (2.3) is provided on an upper part of the cracking furnace.    USE - Energy-saving and environmentally friendly device for producing bio-diesel from kitchen wastage such as waste rubber, wood scrap, firewood and waste plastic (all claimed).    ADVANTAGE - The device is suitable for making bio-diesel from waste material, and has high energy saving and environment protecting effect. The device can change waste into useful material, and production process can be continuous.    DETAILED DESCRIPTION - The kitchen wastage includes, wood scrap, firewood and waste plastic.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a kitchen wastage utilization type energy-saving and environmentally friendly device for producing bio-diesel in partial sectional.    Burning furnace (1)    Shell (1.0)    Gasification chamber (1.1)    Burning chamber (1.2)    Cracking furnace (2)    Cracking cylinder (2.1)    Chimney (2.3)    Rotating driving part (2.4)    Oil outflow pipe (2.7)
NOVELTY - The hydrogen-oxygen generating device has drain holes (61), exhaust holes (62), a rear cover (60), and a connecting part (70). Multiple frames (10,10') are provided, where each frame consists of a combining aperture (10b). The connecting part cross-couples the rear cover and the frame through the combining aperture. The water is drained through the drain holes and the hydrogen-oxygen gas mixture is exhausted through the exhaust holes.    USE - Hydrogen-oxygen generating device.    ADVANTAGE - The water is drained through the drain holes and the hydrogen-oxygen gas mixture is exhausted through the exhaust holes, and hence increases the electrolysis efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective exploded view of a hydrogen-oxygen generating device.    Frames (10,10')    Combining aperture (10b)    Rear cover (60)    Drain holes (61)    Exhaust holes (62)    Connecting part (70)
NOVELTY - The apparatus has a membrane electrode assembly comprising interior frames with liquid inlets forming holes between sides of frames. The assembly has ripstop nylon membrane, and a gasket fixed to border of respective sides of a membrane. Two end frames comprise a channel formed on one side between aperture and liquid inlet. An insulator plate has two sides among which one side faces one side of electrode. A compression plate has two sides among which one side faces and contact insulator plate.    USE - Electrochemical apparatus for performing electrolysis of water to produce hydrogen used for powering motor vehicle, cooking, space heating, heating hot water, and air conditioning and refrigeration units.    ADVANTAGE - The utilization of electricity to generate hydrogen is performed effectively. The weight of the electrochemical apparatus is reduced, while improving durability of the apparatus.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for hydrogen gas production method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the hydrogen system.    Hydrogen system (10)    Power selection and conditioning module (14)    Solar panels (22)    Wind turbines (24)    Vehicle (42)
NOVELTY - The apparatus has a combustion catalyst (134) for hydrogen formed in a flow path (131), and combustion catalyst (135) for fuel formed in a flow path (133). A fuel intake port (120) and hydrogen intake port (121) are formed in the respective flow paths (133,131) formed in upper substrate (111) and integrated to a reactor. The air intake ports (119,122) are formed in the upper substrate and inner substrate, for supplying air to the flow paths.    USE - Reaction apparatus used in electric power generating apparatus. Uses include but are not limited to digital camera, mobile phone, notebook personal computer (PC), wristwatch, personal digital assistant (PDA), computer, etc.    ADVANTAGE - The hydrogen and fuel can be burned separately and efficiently by using a simple arrangement.    DESCRIPTION OF DRAWING(S) - The drawing shows the top view of the upper substrate.    Upper substrate (111)    Air intake ports (119,122)    Fuel intake port (120)    Hydrogen intake port (121)    Flow paths (131,133)    Combustion catalysts (134,135)
NOVELTY - Methanol-based clean fuel comprises (pts.wt.) additive (0.5-3) and gasoline component oil (84.5-7). The methanol-based clean fuel is prepared by adding additive into gasoline component oil, adding obtained mixture into methanol (15-90 pts.wt.) of 15% methanol-90% methanol (M15-M90) methanol clean fuel.    USE - Methanol-based clean fuel for vehicle (claimed).    ADVANTAGE - The method produces fuel having high octane number and low heat value of methanol.
NOVELTY - A composite material in granular or powder form is prepared by mixing raw materials rich in sulfate and ferric oxide or hydroxide. The mol ratio of sulfur to iron in composite material is 20:1-1:3.    USE - Composite material in granular or powder form for reducing greenhouse gas emission in environment rich in organic material and anaerobe, including water pond, city sight water body, river, ditch, paddy field, artificial wetland, marsh, lake, sea and garbage burying square (claimed).    ADVANTAGE - The composite material can efficiently inhibit activity of methane bacteria, and convert unstable organic carbon to be inorganic carbonate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of using composite material for reducing greenhouse gas emission comprising pouring composite material granule or powder into environment rich in organic material and anaerobe comprising water pond, city sight water body, river, ditch, paddy field, artificial wetland, marsh, lake, sea and garbage burying square.
NOVELTY - The method comprises adding 2 ml of alcohol such as ethanol or methanol as carbon substrate to 100 liter of seawater for increasing the metabolic activities of an anaerobic bacterial strain, and removing the developing reaction products by a skimmer. The added solution has 40% of alcohol content. The addition of alcohol slowly takes place in the free seawater volume of a basin and not directly to the occupants of a seawater basin or corals. The nitrate content is measured for 24 hours after adding the alcohol and a renewed addition of alcohol is carried out during exceeding desired values.    USE - Method for cleaning seawater in a seawater aquarium, seawater basin for pisciculture and seawater plant by removing nitrates, protein compounds and other contaminants using anaerobic bacterial strain.    ADVANTAGE - The method is capable of simply, continuously and economically cleaning the seawater by effectively removing the nitrates and protein compounds thus preventing the reduction of the growth and the living conditions of the corals and the fish and its life span.
NOVELTY - The energy storing device has solar photovoltaic cell assembly, pure water electrolytic bath, pure water tank, hydrogen storage tank, oxygen storage tank and hydrogen-oxygen fuel cell. The hydrogen outlet of pure water electrolytic bath is connected to hydrogen inlet of hydrogen storage tank. The oxygen outlet of pure water electrolytic bath is connected to oxygen inlet of oxygen storage tank. The hydrogen outlet of hydrogen storage tank is connected to hydrogen inlet of hydrogen-oxygen fuel cell. A hydrogen control valve is provided between hydrogen storage tank and hydrogen-oxygen fuel cell.    USE - Solar-photovoltaic-water energy storing device for industrial use.    ADVANTAGE - Provides a solar-photovoltaic-water energy storing device that is free of pollution in use, and is environment-friendly. Ensures that the solar-photovoltaic-water energy storing device can be repeatedly use, has long service life, has simple structure, is reliable, and is easy to industrialize.    DETAILED DESCRIPTION - The positive and negative power lines of the solar photovoltaic cell assembly are correspondingly connected to the positive and negative power lines of the pure water electrolytic bath. The pure water inlet of the pure water electrolytic bath is connected to the pure water outlet of the pure water tank. The pure water inlet of the pure water tank is connected to the pure water outlet of the hydrogen-oxygen fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic block diagram of the solar-photovoltaic-water energy storing device.
NOVELTY - A catalyst comprises particles containing copper oxide supported by carrier containing zirconium oxide, and carrier containing zinc oxide. The ratio of copper in copper oxide is 8-48 mass%. The copper oxide in the catalyst is reduced at 240 degrees C for 30 minutes in an atmosphere containing nitrogen and 11 volume% of hydrogen gas, to obtain zerovalent copper and monovalent copper. The ratio of zerovalent copper and monovalent copper with respect to 100 mol% of copper is 45-75 mol% and 25-55 mol%, respectively.    USE - Catalyst used for modifier (claimed) and producing hydrogen used as fuel for fuel cell used in portable device.    ADVANTAGE - The catalyst has high methanol conversion ratio which suppresses aggregation of reduced copper particles.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for modifier, which comprises the catalyst positioned in the flow path for circulating reformed gas.
NOVELTY - A carbon monoxide oxidation catalyst contains platinum, and copper (5-25 atomic%). The carbon monoxide oxidation catalyst oxidizes carbon monoxide in mixture of gas containing carbon monoxide and oxygen to carbon dioxide.    USE - Carbon monoxide oxidation catalyst is used for fuel for polymer electrolyte fuel cell for electric vehicle.    ADVANTAGE - The carbon monoxide oxidation catalyst has high catalyst activity at low temperature, and efficiently oxidizes carbon monoxide in hydrocarbon modification system at low temperature.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of the carbon monoxide oxidation catalyst, which involves dispersing a support in aqueous solution, adding a platinum precursor, a copper precursor and a reduction adjuvant in the aqueous solution and irradiating electron beam in the aqueous solution; and    (2) carbon monoxide oxidation apparatus, which oxidizes carbon monoxide generated when modifying hydrocarbon and generating hydrogen gas, using carbon monoxide oxidation catalyst. The carbon monoxide oxidation apparatus is hydrocarbon modification system which modifies hydrocarbon and generates hydrogen gas.
NOVELTY - A fine groove portion (5) is formed at one surface of metal substrate(s) (4,6). A catalyst carrying layer (9) is formed in groove portion. Substrates are joined, and joined component (2) is formed. Fine groove portion has tunnel-like flow path (3), and joined component is connected to flow path. A copper-zinc group catalyst (C) is supported to catalyst carrying layer. A precursor solution containing copper precursor, zinc precursor and reducing agent is filled in flow path. Solution is heat-processed, and precursor solution is removed to manufacture micro-reactor (1).    USE - Manufacture of micro-reactor for modifying hydrocarbon and producing hydrogen.    ADVANTAGE - The micro-reactor having high reaction efficiency is manufactured. The aggregation of catalyst is prevented. The load of catalyst is increased in tunnel-like flow path.    DETAILED DESCRIPTION - A fine groove portion is formed at one surface of metal substrate(s). A catalyst carrying layer is formed in fine groove portion. The substrates are joined, and joined component having raw material inlet and gas exhaust port is formed. The fine groove portion has tunnel-like flow path, and joined component is connected to flow path. A copper-zinc group catalyst is supported to catalyst carrying layer. A precursor solution is filled in the flow path. The precursor solution contains copper precursor (10-200 mmol/L), zinc precursor (5-100 mmol/L) and reducing agent (20-400 mmol/L). The solution is heat-processed, and precursor solution is removed to manufacture micro-reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows the process diagram explaining manufacture of micro-reactor.    Micro-reactor (1)    Joined component (2)    Tunnel-like flow path (3)    Metal substrates (4,6)    Fine groove portions (5,7)    Catalyst carrying layer (9)    Insulating layer (10)    Heat generating material (11)    Catalyst (C)
NOVELTY - The catalytic cracking method involves heating flour-like solid acid catalyst in an autoclave (1), to a temperature ranging from 350 to 450 degrees Celsius. Liquid fats and oils are made to contact the solid acid catalyst, removing the oxygen-containing component from the fats and oils. A hydrocarbon mixture containing C9-C24 olefin and paraffin as main component, is combined.    USE - Catalytic cracking method of waste edible oil. e.g. animal oil such as lard, vegetable oil such as palm oil, rapeseed oil, corn oil, soybean oil.    ADVANTAGE - Obtains high yield of fuel for diesel engines with excellent liquidity and whose freezing point is 20 degree Celsius or less, at low-cost by combining hydrocarbon mixture containing olefin and paraffin to waste edible oil.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the reaction apparatus which implements the catalytic cracking method.    Autoclave (1)    Stirrer (2)    Heater (3)    Pump (5)    Receptor (9)
NOVELTY - The apparatus (1) has a purification unit (10) that uses chemicals for purifying the filtration containing bacteria, and a biotic purification unit (20) that filters the filtration containing bacteria. A physical purification unit (30) uses a pressure filter to filter the filtration.    USE - Polluted water purification apparatus for removing various pollutant materials such as sludge from polluted water or wastewater from industries, commercial establishment, construction site, etc.    ADVANTAGE - The purification process can be performed efficiently within a short period, and the amount of waste material can be reduced, by arranging the purification apparatuses as specified. The effluent-standard value can be satisfied, and the polluted water can be cleaned completely. The cleaning performance can be stabilized. The size and assembly of the apparatus can be reduced, and it can be efficiently used in a broad field, accordingly.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the polluted water purification apparatus.    Polluted water purification apparatus (1)    Chemical purification unit (10)    Water neutralization adjustment tank (11)    Biotic purification unit (20)    Physical purification unit (30)
NOVELTY - The apparatus has a cooler (17) arranged in the downstream of a catalytic reaction device (14) to cool process gas required for reduction of catalyst and to separate liquid and gas. A liquid level indicator (20) determines whether the liquid level reaches a predetermined level. When the predetermined level is reached, a control unit (24) opens a cut-off valve (21) to discharge liquid from the cooler to a water storage tank (22). A balance (23) measures the amount of water in tank and accordingly determines the completion of reduction reaction.    USE - Catalytic reduction apparatus for fuel modifier used in phosphoric acid type fuel cell system.    ADVANTAGE - The completion of reduction of catalyst is determined in short time, from the amount of water. The precision in estimating the completion of reduction is improved, as the concentration of hydrogen in entrance and exit of the reactor is not analyzed. Hence the cost of determining completion is reduced. By controlling the temperature of catalytic reaction device within predetermined range, complicated temperature management can be reduced and schedule for controlling reduction can be made easily.    DETAILED DESCRIPTION - The control unit increases the concentration of reducing gas in the catalytic reaction device based on the amount of water, so that the temperature does not exceed a predetermined value. A temperature sensor measures the temperature of catalytic reaction device to confirm that abnormal exothermic reaction is not generated. The reduction reaction is completed.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the reduction apparatus. (Drawing includes non-English language text)    Catalytic reaction device (14)    Cooler (17)    Liquid level indicator (20)    Cut-off valve (21)    Water storage tank (22)    Balance (23)    Control unit (24)
NOVELTY - Carbon ball is prepared by stirring using blade type stirring drier of heat-conducting oil furnace with oil temperature of less than 320 degrees C, drying, carbonizing and treating on-line sludge of sewage treatment plant at 270 degrees C; splitting produced carbon to improve drying efficiency, returning one part to feed port to mix with sludge, increasing permeability and drying sludge quickly; and producing carbon ball at the other part for oil furnace burning, discharging fume from opening of feed position after water spray treatment, and recycling deposition.    USE - Method for preparing carbon ball (claimed).    ADVANTAGE - The method mixes produced gas reflux and water, increases space heat quantity of device, improves drying efficiency of sludge and reduces production cost when purifying fume; and produces furnace ash after burning charcoal ball used as fertilizer or for manufacturing brick.
NOVELTY - A corrosion- and swelling-reducing methanol comprises (wt.%) petrol (33-90), industrial methanol (5-50), lacquer solvent (5-17) and additive composition (1000 ppm).    USE - A corrosion- and swelling-reducing methanol fuel for vehicle (claimed).
NOVELTY - Preparing ethanol fuel through utilization of plant straws comprises: (a) preparing hydrolysis liquid through acid hydrolysis of plant straws; (b) preparing acetic acid mixed liquid through anaerobic fermentation of the hydrolysis liquid; (c) carrying out an esterification reaction to the acetic acid mixed liquid and methanol in the presence of a first catalyst to obtain a mixed ester; and (d) carrying out hydrogenation reaction to the mixed ester in the presence of a second catalyst to obtain the ethanol fuel.    USE - The process is useful for preparing ethanol fuel through utilization of plant straws (claimed).    ADVANTAGE - In the process, the prepared mixed alcohol uses biomass like the wasted straws from agriculture and forestry as the raw material to change the waste into valuable compound, which saves the production cost and reduces the environment pollution. Moreover, the yield of the fuel ethanol is high; the oxygen content is high; the octane number is large; the combustion performance is good; and the pollutants that are discharged during the combustion is little.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of the process for preparing ethanol fuel through utilization of plant straws (Drawing includes non-English language text).
NOVELTY - Industrially producing organic compound fertilizer by using L-tryptophan fermentation waste liquid, comprises: adding base fertilizer to fermentation waste liquid containing 80-90% of water to obtain slurry containing 50-60% of water; pressurizing the slurry, granulating, drying it in granulating and drying machine through slurry pump to obtain organic compound fertilizer particle; at last sieving the compound fertilizer particle and cooling to obtain finished product; packing the finished product and sending to storehouse.    USE - The method is useful for producing organic compound fertilizer by using L-tryptophan fermentation waste liquid (claimed).    ADVANTAGE - The method industrially treats the fermentation waste liquid to realize zero discharge of sewage and protect biological environment; the fermentation waste liquid is used for producing organic compound fertilizer which changes waste into valuables, the production cost is low, the economic and social benefits are great; and the production process is simple and stable, the operation is convenient, the yield is high, and the grade is high.
NOVELTY - A biogas generator of country poultry house comprises a biogas tank (1) and a biogas chamber (2); where the biogas tank and biogas chamber are set in a manure pit under the poultry house (3); the inlet of biogas tank is communicated with outlet of the poultry house; and a slag discharge (4) is set on the biogas tank.    USE - The biogas generator is useful for country poultry house (claimed).    ADVANTAGE - The biogas generator of country poultry house can be built in original poultry manure pit to reduce the floor area by using original poultry manure pit; where there is no need to dig biogas pit; the input is reduced; and there is no need to cast concrete. Moreover, it is compact to seal; the temperature in the generator is adjustable; and the material in the biogas tank is cycled and agitated by biogas internal circulation. Additionally, it makes the material to fully generate biogas and improves the yield of biogas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the biogas generator of country poultry house.    Biogas tank (1)    Biogas chamber (2)    Poultry house (3)    Slag discharge (4)
NOVELTY - Excrements fuel manufacturing involves providing 80-90 wt.% of excrements in a dryer at 100-150 degrees C. 10-20 wt.% of gunpowder is also added into the dryer to obtain a mixture. The obtained mixture is molded to a specified formation. The produced material is dried at 80-100 degrees C.    USE - Method for manufacturing excrements fuel.    ADVANTAGE - The excrements fuel manufacturing method enables to produce the excrements fuel having high energy efficiency in an eco-friendly and cost-effective manner.
NOVELTY - Method for producing ethanol, involves fermenting raw materials such as banana and plantain.    USE - The method is useful for producing ethanol (claimed).    ADVANTAGE - The ethanol can be produced in large scale by a cost-effective process.
NOVELTY - Production of microalgae by domestic sewage and industrial wastewater comprises: early-stage culture: adding domestic sewage which is treated primarily and filtered in a bioreactor, adding algae in the reactor, culturing with oxygen and carbon dioxide (CO2) during stirring until under the microalgae cells reach stabilization period; oil reduction: adding industrial waste liquid which is from sugar cane bagasse fermentation in the reactor and 200-1000 times the volume of the culture, inducing accumulation of oil in the cells, and extracting the cells when oil accumulation is stable.    USE - The method is useful for production of microalgae by domestic sewage and industrial wastewater (claimed).    ADVANTAGE - The method continuously produces microalgae with high oil content, and lowers culture cost of microalgae greatly, making it favorable for industrializing microalgae culture.
NOVELTY - Milk waste anaerobic digestion involves injecting food waste and seeding anaerobe in an anaerobic digester. The milk waste is injected into the anaerobic digester. The obtained mixture is anaerobically treated at 50-60 degrees C and 12 days of hydraulic retention time (HRT). The generated methane gas is collected. The acid is added to saturated salt water.    USE - Method for anaerobically digesting milk waste.    ADVANTAGE - The milk waste anaerobic digestion method is eco-friendly, efficiently reduces organic compound component in milk waste and generates large amount of methane gas, which is utilized as alternative energy source.
NOVELTY - Device comprises an infrared lamp (20) and a reactor (1). The infrared lamp is set up around the reactor. The reactor is provided to convert methanol into a supercritical fluid. The reaction temperature inside the reactor is maintained at 250 degrees C.    USE - Device for producing biodiesel.    ADVANTAGE - The device rapidly increases the alternative energy or bio-energy, solves the problem of environment contamination and fuel, and oil supply, and improves the production yield of biodiesel.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biodiesel production device.    Reactor (1)    Evaporator (3)    Nitrogen gas inlet (4)    Condenser (5)    Feed pump (6)    Infrared lamp (20)
NOVELTY - Solid fuel manufacturing involves mixing 55-75 wt.% of bamboo charcoal powder, 4-10 wt.% of corn starch and 17-25 wt.% of barium to obtain a mixture. The obtained mixture is transferred into a mold for forming solid fuel by using 0.6-0.8 kilogram-force per square centimeter (kgf/cm2) water vapor pressure.    USE - Method for manufacturing solid fuel by using charcoal powder.    ADVANTAGE - The solid fuel manufacturing method produces the solid fuel with improved yield, excellent combustion efficiency, and good thermal power without producing smoke and toxic gases in a very simple and cost-effective manner, and also provides meat with excellent taste and softness without fishy smell.
NOVELTY - Charcoal manufacturing involves cutting oak including mangrove, pine, bamboo in 1m size. The cut pieces are closed or covered by using brick or soil, where fire is provided through a small fuel hole on entrance bottom. The fire burns continuously for 5-7 days, where white smoke is ejected through chimney.    USE - Method for manufacturing charcoal.    ADVANTAGE - The charcoal manufacturing method enables to produce the charcoal with high calorific value and long burning time in a convenient manner in any season.
NOVELTY - Preparing biogas comprises crushing wood fiber straw and placing in steam explosion device; obtaining powder and filamentous steam exploded straw materials; and subjecting to anaerobic fermentation in anaerobic biogas reactor.    USE - Method of preparing biogas (claimed).    ADVANTAGE - Content of methane in biogas is up to 65-75%. The method improves structure limitation problem of anaerobic fermentation of wood fiber straw, obtains clean energy and treats wood fiber straw waste material in countryside.
NOVELTY - Producing biogas comprises crushing Pennisetum hydridum as raw material; placing in anaerobic reactor, adding inoculum at an amount of 5-30% of the dry weight of the fermenting substance; and adding water, adjusting total solids load to 2.0-8.0%, sealing the reactor, connecting to a gas storage device, and fermenting. The temperature of the reaction is 25-55 degrees C. The fermentation period is 25-30 days.    USE - Method of producing biogas (claimed).    ADVANTAGE - The method transforms P. hydridum with extremely strong life and reproductive performance to an energy crop.
NOVELTY - The method involves drying cellulose/plastic waste by performing treatment with a drying medium i.e. gaseous medium (13), with a temperature in a range of 50 to 150 degrees centigrade, where exit temperature of the drying medium is 115 degrees centigrade or lower. The dried cellulose/plastic waste is fed to a purification stage, and the dried cellulose/plastic waste is subjected to the effect of a treatment phase, where the treatment phase includes a wind separator (2), sieve (21), and metal separator.    USE - Method for processing a mixture of waste particles including cellulose/plastic waste e.g. municipal and urban waste, household waste and industrial waste, to produce a cellulose/plastic product such as fuel and fuel pellets.    ADVANTAGE - The method facilitates obtaining of the cellulose/plastic product with a good calorific value, low ash and low chlorine content. The method allows a part of heat generated in a combustion unit to be used for heating and drying of the cellulose/plastic waste or the drying medium, so that the heat can be effectively utilized.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view representing steps involved in a waste treatment to obtain a fluff material.    Wind separator (2)    Gaseous medium (13)    Eddy-current system (20)    Sieve (21)    Dried well (25)
NOVELTY - A planar bioreactor comprises an inlet device for introducing a flow of fluid into the bioreactor; a main reactor bed for receiving the flow of fluid from the inlet device; and an outlet for discharging the flow of fluid from the main reactor bed. The main reactor bed has a surface area greater than the depth of fluid in the bioreactor to allow light to penetrate through the depth of fluid in the main reactor bed as the fluid flows through the main reactor bed; and has a flow distribution device to promote uniform or plug flow of fluid through the main reactor bed.    USE - Planar bioreactor for conducting light induced bioreactions of fluids to produce oil (claimed).    ADVANTAGE - The bioreactor is cost effective and permits mass energy balancing to maximize efficiency in multiple bed reactor systems, and permits multiple returns to derive maximum output from algal suspension and solar energy. As a result, more efficient production of oil within the algal cells is achieved. Further, the inlet device introduces turbulence into the flow, and the formation of turbulence within the fluid promotes surface renewal of the algae to expose more of the algae to sunlight, thus increasing the efficiency of the bioreactor.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of conducting a light induced bioreaction of a fluid in a bioreactor, comprising:    (A) introducing flow of fluid into the bioreactor using an inlet device;    (B) passing the flow of fluid from the inlet device into and through the main reactor bed;    (C) producing a uniform or plug flow of fluid in the reactor bed by passing the flow in the reactor bed through the flow distributor device;    (D) allowing light to penetrate through the depth of the fluid flow through the reactor bed in uniform or plug flow to initiate the light induced bioreaction within the fluid; and    (E) discharging the fluid from the main reactor bed through an outlet device.
NOVELTY - A consistency of methane is increased by concentrating methane through multilevel pressure varying adsorption technology, where pressure of feed gas is 0.02-0.04 MPa; reducing methane concentrations of absorbed exit gas to 20-70% for first level, and feed gas below 1% for second level; using evacuated gas in first level as feed gas of third level through which methane concentration is increased by greater than or equal to 95-100%; using evacuated gas of second level as feed gas of first level; and taking absorbed exit gas of third level as feed gas of first level. The gas mixture has methane consistency of 26-85%.    USE - Method of increasing consistency of methane (claimed).    ADVANTAGE - The method provides product with low cost.
NOVELTY - Pyrolysis of a larch wood comprises preparing a larch bark; spiral feeding the larch bark particle with particle diameter of 0.3-0.45 mm to a spouted circulating fluidized bed reactor at a 20 rpm; mixing with 25 m3/hour fluidized gas in the reactor; carrying out rapid pyrolysis reaction at 825 K; carrying out gas-solid separation by passing the pyrolyzed gas and solid carbon through a gas solid separation system; and condensing in a four-level condensing system.    USE - Method for the pyrolysis of a larch wood (claimed).
NOVELTY - The jig has coating layer (2) that covers the upper surface of a rectangular shaped base (1) which is made of alumina, zirconia, mullite or cordierite. A green sheet is arranged on the surface of the coating layer that is made of an electrolytic material similar to electrolytic material comprised in green sheet. The surface roughness and porosity of the coating layer is 0.1-1.0 psi m and 30-70% respectively.    USE - Jig for solid oxide fuel cell manufacture.    ADVANTAGE - Since green sheet and coating layer are made of same material, the scattering of ingredient of green sheet can be prevented, the fall of mechanical strength and power density can be prevented, the running cost and material cost can be reduced significantly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing method of jig for solid oxide fuel cell manufacture.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of the jig.    Rectangular shaped base (1)    Coating layer (2)
NOVELTY - A device for biomass gasification comprises a biomass gasification furnace, a gas dust collector, a gas frozen purifier, a gas filter purifier connected with each other by a gas pipeline; the gas filter purifier is orderly connected with a booster pump, a storage cabinet, and a voltage measuring device.    USE - The device is useful for biomass gasification (claimed).    ADVANTAGE - It makes full use of the waste resource of biomass and converts the waste resource into effective energy; and it has rational device structure and simple technique; the tar remained in the gas can be removed effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a technique for preparing gas by using biomass gasification device comprising: (a) burning the biomass raw material by sending it to the biomass gasification device, removing the impurity from the generated gas by the dust blocking plate, discharging the gas from the gas outlet; (b) introducing the gas into the gas dust collector, removing the dust and the impurity from the gas by the dust collector; (c) purifying the gas by secondary frozen purifier so as to remove the tar in the gas; (d) filtering the gas by the gas filter purifier, then purifying and filtering the gas again to obtain the gas capable of meeting the requirement; and (e) performing flow rate adjusting to the gas by the booster pump, the storage cabinet and the voltage measuring device and then sending it to the determined user.
NOVELTY - Olefinic diesel fuel is prepared from pine root oil by mixing pine root oil with methanol and petroleum ether to obtain homogeneous liquid, adding antiknock agent, stabilizer and lubricant, and filtering.    USE - Method of preparing olefinic diesel fuel from pine root oil (claimed).    ADVANTAGE - The method has low cost.
NOVELTY - A multifunctional straw gasification furnace has water sealed tank (3) set on upper opening of furnace body (2) to correspond to water sealing cover (4); a wind inlet box (5) set on lower part of furnace body to correspond to a fire grate (6) inside the furnace body and connected with a fan (8) by a pipeline (7); a wind distributing chamber (11) set at the upper part of furnace body and connected with a movable cooking range (12). Wind distributing chamber is connected with the fan by pipelines; Furnace body with ash outlet (15) is connected with flue (13) connected to air outlet pipe (14).    USE - Multi-functional straw gasification furnace for warming and cooking in countryside.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a multifunctional straw gasification furnace.    Furnace body (2)    Water sealed tank (3)    Water sealing cover (4)    Wind inlet box (5)    Fire grate (6)    Pipeline (7)    Fan (8)    Wind distributing chamber (11)    Movable cooking range (12)    Flue (13)    Air outlet pipe (14)    Ash outlet (15)
NOVELTY - A universal gasifying device has an air inlet pipe connected with a jetting device; and multiple step-shaped nozzles mounted in the jetting device uniformly by refractory bricks. Nozzles have shrunk openings in which the outer ends are large and inner ends are small. The end of nozzle with large diameter is communicated with air inlet pipe. The end of nozzle with small diameter is set as inward air outlet end. The air outlet ends of nozzles surround a combustion cavity.    USE - Universal gasifying device for biomass, coal oven or boiler.    ADVANTAGE - Provides universal gasifying device that ensures fuel fully contacts with the oxygen to improve combustion conditions of fuel, to make the fuel burn fully, and to reduce the pollution of fuel in combustion process.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the universal gasifying device.
NOVELTY - A biomass gasifying furnace has a furnace body; a gasifying stove; and a purifier. Communicated transmission pipelines are set between the gasifying stove and purifier. Furnace body is communicated with the transmission pipeline by a fire-supplying flexible pipe and a pressure-regulating air duct. Furnace body is communicated with the pressure-regulating air duct and fan. One or more ash outlet communicated with the inner part of furnace body is set on the surface of furnace body. Valves are set on pipe walls of the transmission pipeline and pressure-regulating air duct.    USE - Biomass gasifying furnace.    ADVANTAGE - Provides highly efficient and environment-friendly biomass gasifying furnace since biomass is fully burnt as the gasifying reaction chamber pre-heats the combustion air in the process of gasifying the biomass and generation of environmental pollution is prevented. Reduces labor intensity and ensures saving energy resources since biomass gasifying furnace is operated continuously for long period of time without adding biomass during the process.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass gasifying furnace.
NOVELTY - A vapor purifying drain device has a side tank wall welded with a water inlet pipe having a valve. The upper part of other side tank wall is welded with a reversed L-shaped sewage outlet pipe (5). The lower part of side tank wall is welded with a drain pipe (6) whose internal bore thread is engaged with a choke plug (7). The side wall of middle upper tank and top tank wall in a vapor purifying drain tank (1) are welded with at least one baffle plate. The opposite tank side wall and top tank wall are welded with at least one baffle plate.    USE - Vapor purifying drain device for biomass gasification furnace.    ADVANTAGE - Provides vapor purifying drain device with simple and compact structure, low production cost, convenient use and long efficient circulation, thus guarantees normal use of gasification furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of the vapor purifying drain device of biomass gasification furnace.    Vapor purifying drain tank (1)    Gas outlet pipe (3)    Sewage outlet pipe (5)    Drain pipe (6)    Choke plug (7)
NOVELTY - A charring device has a stirring device (3) provided at interior of cavity of shell (1) of a charring furnace. The main shaft (4) of stirring device is transversely installed on middle part of cavity through bearings arranged on two ends of shell. One end of main shaft is extended to exterior of shell and connected to the output shaft of a speed reducer (8) through a coupling (10). The input shaft of speed reducer is connected to output shaft of main motor (9). The lower part of shell is transversely provided with mesh-shaped carbide powder outlet matched to a discharging device (14).    USE - Charring device for converting waste biomass straw into biomass fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the charring device of biomass fuel.    Shell (1)    Stirring device (3)    Main shaft (4)    Speed reducer (8)    Main motor (9)    Coupling (10)    Discharging device (14)
NOVELTY - A cooling and purifying device has a gas inlet chamber (1) and a gas transition chamber (4) set above a cooling chamber; a drain chamber set under the cooling chamber; a filter chamber (5) and a gas outlet chamber set on one side of gas transition chamber, cooling chamber and drain chamber; and gas outlet chamber set under the filter chamber. Gas inlet chamber is connected to drain chamber by a cooling pipe (7) set in the cooling chamber.    USE - Cooling and purifying device for straw gasification furnace.    ADVANTAGE - Ensures combustible gas produced when burning the straw in straw gasification furnace is purified effectively by adopting the structure in which gas inlet chamber and gas transition chamber are set above the cooling chamber, drain chamber is set under the cooling chamber, filter chamber and gas outlet chamber are set on one side of gas transition chamber, cooling chamber and drain chamber, and gas outlet chamber is set under the filter chamber. Ensures purified gas meets the standard of high quality and clean gas since cooling and purifying device performs de-tarring, de-dusting, and de-water-vapor operations.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the cooling and purifying device of a straw gasification furnace.    Gas inlet chamber (1)    Gas transition chamber (4)    Filter chamber (5)    Cooling pipe (7)    Exhaust hole (8)
NOVELTY - A biomass gasification type energy-saving gas furnace has a gas discharge pipe (7) connected with a gas feed pipe (5) and connected inside a combustion furnace (10); a gas feed pipe (9) and air feed pipe (2) connected through a combustion-supporting pipe (8); a water discharge pipe (11) set on lower part of combustion furnace (10); a cover (12) set on top of combustion furnace and includes an inner gas cap (13); an outer gas cap (14) provided on the periphery of inner gas cap; an outer cooking disk (15) set on the periphery of outer gas cap. Each pipeline has a valve respectively.    USE - Biomass gasification type energy-saving gas furnace.    ADVANTAGE - Provides biomass gasification type energy-saving gas furnace in which pressure stabilization and constant temperature control is automatic, quick three loop rotational flow gas generation is realized, and is featured with ionic decoking, purification, blue flame combustion, low cost and convenient popularization since dead grass, straws, wheat husks, rice hulls, firewood, sawdust, corncob, dry animal manure, faulty coal are used as fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a biomass gasification type energy-saving gas furnace.    Air feed pipe (2)    Gas feed pipe (5)    Gas discharge pipe (7)    Combustion-supporting pipe (8)    Gas feed pipe (9)    Combustion furnace (10)    Water discharge pipe (11)    Cover (12)    Inner gas cap (13)    Outer gas cap (14)    Outer cooking disk (15)
NOVELTY - The device has a gasification furnace provided with a furnace hearth (2), a high-temperature cracking chamber (4) and an ash chamber (7) in turn from top to bottom. An upper end of the furnace hearth is provided with a feeding hole (1). The high-temperature cracking chamber is provided with an igniting hole (5), and a lower end of the cracking chamber is connected with the ash chamber through a furnace bridge (6). A lower opening of a pipeline chimney (9) is connected with the cracking chamber. A chimney valve (10) and a gas guiding valve (11) are provided on the pipeline chimney.    USE - Biomass gasification device.    ADVANTAGE - The device has simple structure and reliable operation, and requires low manufacturing cost and eliminates the need of a power unit.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass gasification device.    Feeding hole (1)    Furnace hearth (2)    High-temperature cracking chamber (4)    Igniting hole (5)    Furnace bridge (6)    Ash chamber (7)    Pipeline chimney (9)    Chimney valve (10)    Gas guiding valve (11)
NOVELTY - The method involves opening a valve between a closed preparation hopper (2) and a feeding hopper (3), and slowly adding treated biomass powder into the feeding hopper from the preparation hopper. The biomass powder is mixed into a fluidized bed reactor (5) via a feed device (4). A separated thermal cracking gas is passed into two grade condensers (10, 11). Uncondensable gas is collected in a gas storage tank (15) via a gas pump (14), and the gas is filled to a lower layer (8) of a heat carrier heater as a combustible gas.    USE - Method for preparing biological oil via biomass thermal cracking.    ADVANTAGE - The method can be implemented in an inexpensive manner without secondary pollution, and reduces consumption of energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for preparation of biological oil via biomass thermal cracking.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biological oil preparing method.    Closed preparation hopper (2)    Feeding hopper (3)    Feed device (4)    Fluidized bed reactor (5)    Lower layer (8)    Grade condensers (10, 11)    Gas pump (14)    Gas storage tank (15)
NOVELTY - A waste motor-vehicle shredder dust which is sieved to 5 mm is introduced into cement pyroprocess. The mass ratio of waste motor-vehicle shredder dust is 30% or less.    USE - Formation of fuel of waste motor-vehicle shredder dust used for cement firing.    ADVANTAGE - The method provides fuel of waste motor-vehicle shredder dust efficiently. The cement of high quality is manufactured using the fuel of waste motor-vehicle shredder dust.
NOVELTY - The method involves sieving a crushed wood type or agricultural type biomass feedstock by a sieve (3), gasifying a plus sieve (4) i.e. large particle, at an entrained-bed-gasification furnace, and producing combustible gas and a char, which is gasified by an entrained-bed type gasifier (7). Sieving (5) i.e. small particle, is gasified at a temperature lower than that of entrained bed gasification at another entrained-bed-gasification furnace, where a breadth of an opening-of-sieve size used during sieving ranges from 1 to 3 millimeters.    USE - Method for gasification of a crushed wood type biomass or an agricultural type biomass e.g. sugarcane and straw, for converting the biomass into combustible gas i.e. raw fuel gas, for electric power generation and hydrogen production. Can also be used for gasification of forestry type biomass e.g. paper manufacture waste material, lumber waste material, thinning lumber, fuel-wood, rice bran and plant, a livestock farming type biomass e.g. livestock waste material, a fishery type biomass e.g. fish processing dreg, and a waste material type biomass e.g. organic refuse, refused derived fuel, garden tree, construction waste, and sewage sludge.    ADVANTAGE - The combustible gas and the char, which is gasified by the entrained-bed type gasifier, are produced, where the sieving is gasified at the temperature lower than that of the entrained bed gasification at the entrained-bed-gasification furnace, thus increasing efficiency of the gasification of the wood type or agricultural type biomass, and enabling the gasification of the wood type or agricultural type biomass in an economical manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow representation illustrating a gasification method of a wood type or agricultural type biomass.    Wood type or agricultural type biomass (1)    Crusher (2)    Sieve (3)    Plus sieve (4)    Sieving (5)    Gasification material supply device (6)    Entrained-bed type gasifier (7)
NOVELTY - The furnace has a furnace body (1) whose inner wall is equipped with a heat insulated layer (2). A conical grate (3) is transversely fixed in a side wall of the furnace body. An upper operation opening (4) is provided on an upper part of the grate, and a lower operation opening (5) and a ventilated hole (6) are formed on a lower part of the grate on the side wall of the furnace body. A heat preserving protection layer (7) is fixed on an exterior of the side wall of the furnace body. A bottom part of the furnace body is equipped with a cooling medium (8).    USE - Biomass gasification furnace.    ADVANTAGE - The furnace can be easily operated. The furnace body has good heat preserving effect. The furnace has stable gasification efficiency and heat value of fuel gas during the gasification process of the biomass. The furnace can decompose ash generated by the furnace body in work, and achieves cracking of tar and auxiliary purifying target.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a biomass gasification furnace.    Furnace body (1)    Heat insulated layer (2)    Conical grate (3)    Upper operation opening (4)    Lower operation opening (5)    Ventilated hole (6)    Heat preserving protection layer (7)    Cooling medium (8)
NOVELTY - The device has a cooling chamber internally equipped with two aeration pipes that are communicated to each other through a communication pipe. An inlet pipe is sleeved within one aeration pipe, and outlet pipe is sleeved within another aeration pipe. Bottom part of the cooling chamber is equipped with a water collecting tank having drain holes. Top end of the cooling chamber is equipped with a filtering chamber having vent holes. The filtering chamber is internally equipped with a filter. Bottom end of the filtering chamber is equipped with a filtering screen.    USE - Gas purifying device for a straw gasification furnace.    ADVANTAGE - The device purifies tar, dust and moisture within the fume discharged from the straw gasification furnace, thus providing clean, dry and burned enough discharged fume.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a gas purifying device in partial section.
NOVELTY - The device has an insulating layer arranged between a water-bath spray thrower and a dry filter. The water-bath spray thrower is provided with an inlet/outlet pipeline and a gas transmission pipeline. A heat exchanger is provided with an inlet chamber, an outlet chamber and a heat exchange area. An inlet chamber and an outlet chamber are separated from each other by a heat exchange area. Outlet of the device is arranged on an upper part of the dry filter, and a drain valve is placed at a bottom part of the heat exchanger.    USE - Composite filter device for gasification and canalization of biomass fuel gas.    ADVANTAGE - The device is compact in structure, small in space and simple and easy to assemble. The device has combined multiple-filtration and multiple-cooling structure and highly efficient technical process, so that a pure, clear fuel gas with little pollution can be obtained. The device has a 99 percent tar removal rate, and supplies clean and convenient fuel gas to rural areas.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a composite filter device.
NOVELTY - The device has a heat exchange area equipped with cooling circulation water, a water pipe and a heat exchange pipe. The heat exchange area isolates a gas inlet chamber and a gas outlet chamber by two isolation plates. Two ends of the heat exchange pipe are connected with the gas inlet chamber and the gas outlet chamber. Four filter meshes are installed in a filter layer. A gas channel is passed in another filter layer by a gas transfer pipe after passing through one of the filter meshes. The gas outlet of a composite filter is located on an upper part of a dry filter.    USE - Device for purifying biomass gas.    ADVANTAGE - The device uses the rural biomass waste to form gas. The device enhances cleaning of rural area, and conveniently provides gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass gas purification device.
NOVELTY - Alcoholic fermentation waste liquor is treated by putting alcohol waste liquor, coal with granularity of less than 10 mm, water and additive in globe mill for blending and grinding to obtain alcohol waste liquor coal pulp with solid particle granularity of less than 0.5 mm and 58-70% solid content; and sending alcohol waste liquor coal pulp (58-70%) and gasification agent into gasification furnace through different passages of entrained flow gasification nozzle for reaction under 0.01-8.7 MPa at 1200-1700 degrees C.    USE - Method for treating alcoholic fermentation waste liquor used for producing coal gas (claimed).    ADVANTAGE - The method has high gasification efficiency and high performance, is advanced in simple operation, low energy consumption and almost no pollution, with reduces alcohol waste liquor treating period, and realizes minimization, stabilization, decontamination and large-scale utilization of waste as resource of alcohol waste liquor.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for treating alcoholic fermentation waste liquor comprising globe mill (1), shaking screen (2), coal pulp tank (3), coal pulp pump (4) and entrained flow gasification furnace (5), interconnected one by one through pipelines.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the device for treating alcoholic fermentation waste liquor. (Drawing includes non-English language text).    Globe mill (1)    Shaking screen (2)    Coal pulp tank (3)    Coal pulp pump (4)    Entrained flow gasification furnace (5)
NOVELTY - An aeration treatment fluidized bed device comprises a diesel engine or electric motor, air compressor, drainage aerator, biological contamination-proof filter material, and chamber for microbial agent and medicine. The device uses a pontoon to compose a floating support, and produces a compressed air using the diesel engine or electric motor. The compressed air is conveyed through a pipe into drainage aerator having gaps, pipes on its top and bottom or ditches. A lower part is provided with a drainage pipe frame.    USE - An aeration treatment fluidized bed device for upgrading and draining deep water.    ADVANTAGE - The device is easy to install; and has simple structure, good mobility, long service life, high purification efficiency, high energy-saving effect and low cost.    DETAILED DESCRIPTION - An aeration treatment fluidized bed device comprises a diesel engine or electric motor, air compressor, drainage aerator, biological contamination-proof filter material, and chamber for microbial agent and medicine. The device uses a pontoon to compose a floating support, and produces a compressed air using the diesel engine or electric motor. The compressed air is conveyed through a pipe into drainage aerator having gaps, pipes on its top and bottom or ditches. A lower part is provided with a drainage pipe frame. The drainage pipe (frame) or ditches selectively upgrade the deep water. Upper pipe or ditches upgrade all the deep water. The microbial agent is added to sewage at position near the sewage surface. An oxygen-rich sewage is completely mixed with microbial agent to biologically purify. A biological filter material and a plant root support are arranged on position near the sewage surface to further process the contamination in sewage. The device is provided with a drainage frame. The drainage pipe can selectively supply oxygen to deep water during working to reduce energy consumption.
NOVELTY - The biomass gasification machine an auxiliary furnace (7) that is joined to a main furnace (4) by an aeration pipe (6), and having a water sleeve that communicates with a main water tank (1) by a temperature reducing pipe (8). A furnace core water tank (3) is mounted in the middle of the main furnace, and communicates with the main water tank. A high pressure hydrosphere mixing device (10) and an atomization separating device (11) are connected between a washing desulphurization device (9) and a dehydration device (12).    USE - Biomass gasification machine for producing gas by biomass.    ADVANTAGE - Reduces the temperature of the gasification furnace, while enabling heating of water by required heat quantity. Enables providing large amount of hot water energy resource through uninterrupted continuous work for warming and swimming by user.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of the biomass gasification machine.    Main water tank (1)    Furnace core water tank (3)    Main furnace (4)    Aeration pipe (6)    Auxiliary furnace (7)    Temperature reducing pipe (8)    Washing desulphurization device (9)    High pressure hydrosphere mixing device (10)    Atomization separating device (11)    Dehydration device (12)
NOVELTY - The cotton-stalk carbonizing device has an induced air device (3) is provided at a connection position of a carbonizing chamber (5) and a cooling chamber (2). A vent (6) is provided on the carbonizing chamber, which has inner cavities that are connected to the cooling chamber of a sintering kiln.    USE - Carbonizing device for cotton-stalk used as barbecue material or internal combustion material of fire brick. Can also be used for carbonizations of other crop straws.    ADVANTAGE - Enables use of cotton-stalk as barbecue material or internal combustion material of fire brick after carbonizing using the afterheat produced in the producing process of the kiln.    DESCRIPTION OF DRAWING(S) - The drawing shows the cross sectional view of the cotton-stalk carbonizing device.    Cooling chamber (2)    Induced air device (3)    Carbonizing chamber (5)    Vent (6)    Blast volume adjustment baffle (7)
NOVELTY - The multifunctional gasification furnace has a combustor connected to an air outlet at the top end of a purifier. A blast fan is connected to an air inlet at the bottom of the purifier to communicate with a connecting pipeline at the bottom end.    USE - Multifunctional gasification furnace for use in country side.    ADVANTAGE - Offers simple, reliable, convenient to use and safe multifunctional gas furnace that provides environmental protection. Ensures fast gas generating speed and high heat efficiency. Prevents leakage of harmful gas. Reduces requirement and use of coal to decrease environmental pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of a multifunctional gasification furnace.
NOVELTY - A biogas generation tank comprises a tank body (1), a feeding hole (2) on the tank body, a ventilated hole (3), and a hydraulic chamber (4) connected to the interior and exterior of the tank body; where the tank body is the reinforced concrete structure comprising an upper body and a lower body locked with each other.    USE - The biogas generation tank is useful for industrial and commercial applications.    ADVANTAGE - The biogas generation tank has high strength, long service life, low cost, convenient manufacture, transport and installation, and high yield.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the biogas generation tank.    Tank body (1)    Feeding hole (2)    Ventilated hole (3)    Hydraulic chamber (4)
NOVELTY - An organic waste is processed by throwing in organic waste in gasifier (3) maintained at reducing environment of oxygen ratio of less than or equal to 1, thermally decomposing to pyrolysis gas, tar and thermal decomposition residue, controlling water/carbon rate (H2O/C ratio) in gasifier, and adjusting compounding ratio of carbon content contained in thermal decomposition residue and carbon content contained in reformed gas.    USE - Processing of organic waste e.g. woody biomass, sewage sludge and municipal solid waste.    ADVANTAGE - The method achieves acceleration of effective usage of recovered thermal decomposition residue (carbonized material) and carries out maximum recycling of energy of organic waste.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) gasifier;    (2) reformer; and    (3) organic waste processing apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the organic waste processing apparatus. (Drawing includes non-English language text).    Hopper (1)    Feeder (2)    Gasifier (3)    Blower (4)    Cyclone apparatus (5)
NOVELTY - System (I) for producing hydrogen comprises a reactor including a reaction channel adapted to receive a reaction stream including a mixture of supercritical water and a hydrocarbon fuel and a catalyst positioned in the reaction channel so that a product stream containing hydrogen is produced by a reaction in the reaction channel when the mixture is exposed to the catalyst, where the catalyst contains a catalytically active metal and a promoter in a metal format, which is potassium, sodium, rubidium, lithium, cesium, beryllium, magnesium, calcium, strontium or barium.    USE - The system is useful for producing hydrogen, which is useful as a fuel and energy source in powering automobiles and is also useful in hydrogenation, ammonia synthesis and fuel cells.    ADVANTAGE - The hydrogen generation system is simple, lightweight and compact and gives increased hydrogen production, which is due to: the increase of the inlet pressure of the reaction stream that will increase the driving force for the hydrogen separation, as a result the reactors are compact and capable of sustaining higher pressures and favor more hydrogen production; an equilibrium shift in the reaction stream, preferably as the hydrogen concentration decreases in the reaction stream, the reaction shifts to produce more hydrogen. The removal of the reaction product, hydrogen lowers the necessary reaction temperature that increases the range of materials acceptable for the reactor, thus resulting in lower cost, better performance and increased ease of manufacture for the reactor. The hydrogen production process may be used either on-board a vehicle or in a stationary facility.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic illustration of the interior of a compact reactor.    Reaction channels (12a, 12b, 12c, 12d)    Hydrogen channels (14a, 14b)    Heating stream channels (16a, 16b)    Heat transfer walls (20a, 20b, 20c, 20d)    Housing (30)
NOVELTY - The fuel cell stack is equipped with a fuel cell that produces electric power at predetermined temperature range. Another fuel cell produces electric power at a different temperature range higher than predetermined temperature range.    USE - Fuel cell stack for fuel cell system for supplying power to electric vehicle.    ADVANTAGE - The electric power generation performance is improved efficiently at wide temperature range, without increasing the size of fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph illustrating the relationship between the output performance and temperature range of fuel cell. (Drawing includes non-English language text)
NOVELTY - The method involves forming insulator films (16,22) at outer periphery of the separator (14). Several membrane electrode assemblies are laminated at surfaces of separator coated with insulator film. The fuel cell main structure is formed and the fuel cell monitoring cable terminal (20), is attached to fuel cell main structure by removing the portion of insulator film formed at separator.    USE - Manufacturing method of fuel cell (claimed).    ADVANTAGE - Since the terminal is attached to fuel cell main structure by removing the portion of insulator film formed at separator, the generation of short-circuit and earth-leakage are eliminated. The attachment of terminal is synchronized with removal of insulator film so that the terminal installation process is simplified.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows the cross-sectional views of separator and fuel cell monitor cable terminal.    Separator (14)    Insulator films (16,22)    Fuel cell monitoring cable terminal (20)    Clip portion (24)
NOVELTY - The fuel cell system has a processing tank (11) that stores liquid fuel containing hydrazine discharged from a fuel cell (2). A processing agent provision unit (21) provides processing agent for carrying out exothermic reaction of hydrazine and detoxifying liquid fuel. A processing side supply pipe (22) supplies processing agent from the processing agent provision unit to the processing tank. A fuel cell side supply pipe (23) supplies processing agent to the fuel cell when temperature rise of the fuel cell is required.    USE - Fuel cell system mounted in electric vehicle e.g. electric car.    ADVANTAGE - The detoxification of the liquid fuel and the raise of the electric power generation efficiency of the fuel cell are achieved simultaneously using simple structure. The size reduction and cost reduction of the fuel cell system are achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the fuel cell system.    Fuel cell (2)    Processing tank (11)    Processing agent provision unit (21)    Processing side supply pipe (22)    Fuel cell side supply pipe (23)
NOVELTY - The fuel cell system has a control apparatus (20) that controls the driving of circulation pump (12) according to the load condition of fuel cell (2). The control apparatus drives the circulation pump when the electric current value generated by the fuel cell is more than predetermined reference value or stops the circulation pump when the electric current value is less than the reference value.    USE - Fuel cell system.    ADVANTAGE - As the control apparatus drives the circulation pump when electric current value generated by fuel cell is more than reference value otherwise stops the circulation pump, deterioration of fuel consumption by motive power loss is prevented hence eliminating accumulation of impurity in anode gas flow path with respect to the loaded condition of fuel cell. As the electric current value generated by the fuel cell is compared with the predetermined reference values, performance of electric power generation and fuel consumption are improved by reducing motive power loss.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of fuel cell system.    Fuel cell (2)    Pressure regulation valve (8)    Circulation pump (12)    Control apparatus (20)    Ammeter (22)
NOVELTY - The apparatus (3) has heat sources (351,352) that heat the water and fuel suction units (311,312). A temperature sensor (37) measures the temperature of suction units. A heat regulation device (371) controls and maintains the heat source to preset temperature based on measured temperature. The suction units have introducing portions (311a,312a) into which the water and alcohol supplied to suction units are introduced. The pressure loss in introducing portion supplied with alcohol, is large compared with pressure loss in introducing portion supplied with water.    USE - Vaporization apparatus for vaporizing liquid such as mixture of water and alcohol used in electric power generating apparatus (both claimed) mounted in portable apparatus such as notebook personal computer and mobile telephone.    ADVANTAGE - The generation of bubble in introducing portions of the suction units, can be suppressed and pulsation during operation of vaporization apparatus can be prevented such that liquid can be vaporized stably and simply and hence the electric power generation performance of electric power generation cell can be stabilized.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for electric power generating apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the vaporization apparatus.(Drawing includes non-English language text)    Vaporization apparatus (3)    Temperature sensor (37)    Water suction unit (311)    Introducing portions (311a,312a)    Fuel suction unit (312)    Heat sources (351,352)    Heat regulation device (371)
NOVELTY - The processing apparatus has a dilution container (6) that mixes and dilutes the hydrogen gas purged from a fuel cell so as to discharge the hydrogen gas. The inner side of dilution container is provided with expansion chambers (25,26) to which cathode-off gas pipe (14) is connected. The pure hydrogen pipe (8) is connected to a dilution chamber (24) that is formed in a closed space at inner side of dilution container. The dilution chamber is arranged between the expansion chambers, and is maintained as resonance chamber.    USE - Exhaust gas processing apparatus of fuel cell (claimed) used in electric vehicle.    ADVANTAGE - The purge sound generated during purge hydrogen discharge can be attenuated by arranging the dilution chamber between the expansion chambers such that size of the processing apparatus can be reduced. The muffling and dilution capabilities of dilution container can be improved with reduced weight at low cost.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of the exhaust gas processing apparatus.(Drawing includes non-English language text)    Dilution container (6)    Pure hydrogen pipe (8)    Cathode-off gas pipe (14)    Dilution chamber (24)    Expansion chambers (25,26)
NOVELTY - A hydrogen selective gas separation membrane comprises silicon-oxygen bond, element (M), silicon and oxygen in hydrogen gas at 400 degrees C or more. The molar ratio of element (M) with respect to silicon is 0.06-0.19.    USE - Hydrogen selective gas separation membrane is used for fuel cell.    ADVANTAGE - The hydrogen selective gas separation membrane selectively and efficiently separates hydrogen gas, and has stable gas-separation performance for long period of time, and excellent durability.
NOVELTY - The apparatus has a combustion pipe that guides flame from burner, towards cylinder (31b). The projection (43) guides the waste gas (E) smoothly into waste gas flow path (33) through lower opening (33a), so that the gas does not accumulate at the bottom portion (38). The waste gas flow path of reformer, allows the waste gas to pass through modification section (32) that generates reformed gas by carrying out steam reforming of the raw material for hydrogen production.    USE - Hydrogen production apparatus for fuel cell system (claimed).    ADVANTAGE - The gas is guided smoothly along the waste gas flow path without accumulating at the lower portion below which of the carbon monoxide removal apparatus is arranged. The temperature of the carbon monoxide removal apparatus is maintained and the fall of efficiency of the monoxide removal apparatus can be prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows an enlarged view of a section of the hydrogen production apparatus.    Cylinder (31b)    Modification section (32)    Waste gas flow path (33)    Lower opening of waste gas flow path (33a)    Bottom portion (38)    Projection (43)    Waste gas (E)
NOVELTY - The supply apparatus (3) has a liquid fuel supply system (20) that supplies the liquid fuel to a modifier (5) such that the sulfur content is removed by a desulfurizer (22) using the reformed gas generated by the modifier. A water supply system (30) supplies the hot water that supplies heat to a desulfurization catalyst (23) of the desulfurizer, such the water receives from a burner (6) that heats the modification catalyst of the modifier.    USE - Reforming raw material supply apparatus of fuel cell system (claimed) used as domestic electric power supply source.    ADVANTAGE - The reforming raw material supply apparatus can heat the desulphurization catalyst of the desulfurizer efficiently and the structure of the reforming raw material supply apparatus is simplified.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the fuel cell system. (Drawing includes non-English language text)    Reforming raw material supply apparatus (3)    Modifier (5)    Burner (6)    Liquid fuel supply system (20)    Desulfurizer (22)    Desulfurization catalyst (23)    Water supply system (30)
NOVELTY - The apparatus (3) has a hydrogen permeable membrane (15) that separates hydrogen from the source gas. A hydrogen separation tube (8) has a support tube (11) that supports the hydrogen permeable membrane, when the modification catalyst modifies the source gas. A heater pattern (25) arranged in the surface or inside the hydrogen separation tube heats the hydrogen separation tube.    USE - Apparatus for producing hydrogen gas for fuel cell.    ADVANTAGE - The external heater is not required for the hydrogen production apparatus. The generation of the heat shock can be suppressed and hence the generation of the crack of the hydrogen separation tube can be prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows the side and cross-sectional views of the hydrogen production apparatus.    Apparatus for producing hydrogen gas (3)    Hydrogen separation tube (8)    Support tube (11)    Hydrogen permeable membrane (15)    Heater pattern (25)
NOVELTY - The apparatus (3) has heat source (35) which heats the porous structure (31) comprising liquid introducing section (31a) and liquid vaporization section (31b). The average diameter of air hole of porous structure is set larger than the gas saturation solubility of liquid in introducing section, when the heat is not applied to porous structure.    USE - Vaporization apparatus of electric power generation apparatus (claimed) used in mobile phone and notebook personal computer (PC).    ADVANTAGE - The generation of bubble in liquid introducing section of porous structure can be suppressed by setting the average diameter of air hole of porous structure larger than the gas saturation solubility of liquid in introducing section, when the heat is not applied to porous structure. The electric power generation can be made stable.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for electric power generation apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the vaporization apparatus. (Drawing includes non-English language text)    Vaporization apparatus (3)    Porous structure (31)    Liquid introducing section (31a)    Liquid vaporization section (31b)    Heat source (35)
NOVELTY - The firewood gas-generating cooking device has air inlet pipe (5) and air inlet cover (6) which are connected while the outlet joint pipe (7), wound disk return-gas pipe (8), return-gas pipe (9), gas inlet joint (10) are connected in turn. The gas supply joint pipe is connected to the gas inlet pipe (14), and then connected to the fuel hole (16) via the gas inlet pipe. The other gas inlet pipe (15) is connected to the gas inlet pipe.    USE - Firewood gas-generating stove.    ADVANTAGE - Provides a firewood gas-generating cooking device that saves on firewood and does not pollute environment.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the firewood gas-generating cooking device.    Air inlet pipe (5)    Air inlet cover (6)    Outlet joint pipe (7)    Wound disk return-gas pipe (8)    Return-gas pipe (9)    Gas inlet joint (10)    Gas inlet pipe (14)    Gas inlet pipe (15)    Fuel hole (16)
NOVELTY - The production device has power supply source which is respectively connected with the electrolytic tank and controller to supply electricity. The electrolytic tank is connected with electrical quantity recycling device. The cathode and anode plates are equipped in the electrical quantity recycling device. A controller is connected with the electrical quantity recycling device to regulate the time and quality of electrical quantity recycling, and is provided with programmable logical controller and control switch.    USE - Production device for generating hydrogen by electrolyzing water.    ADVANTAGE - Provides a device that recycles the electrical quantity consumed in producing hydrogen and uses the recycled electrical quantity to make the electrolytic tank generate a voltage for electrolyzing, and repeats the process to reduce the consumption of electricity in electrolyzing.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic block diagram of production device.
NOVELTY - A process for preparing an improved catalyst suitable for producing methane rich gases, is disclosed. An aqueous solution of metal nitrates is reacted with aqueous alkali solution containing silica and alumina to form mixed precipitated slurry. The precipitate is calcined, washed and dried to obtain the catalyst. Image 0/0
NOVELTY - The fuel cell (1) has fuel gas generation chamber (B) with accommodation portion (B1) to accommodate water reacted with fuel in accommodation portion (B2). The electric power is generated when hydrogen gas is supplied to electric power generation cell (C). The fuel gas chamber is in latching state with fuel gas main structure by securing structure (48) when fuel gas main structure is mutually connected with fuel gas generation chamber through pipe. The latching state is released by providing external force to press-structure (49) contacting with securing structure.    USE - Fuel cell used as main power supply of mobile telephone, digital camera and notebook personal computer. Can also be used in charging of lithium ion secondary battery.    ADVANTAGE - The fuel gas generation chamber is detachable easily with respect to fuel-cell main structure, and disposition of pipe connected between fuel cell main structure and fuel gas generation chamber is avoided reliably.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view illustrating the internal structure of the fuel cell.    Fuel cell (1)    Securing structure (48)    Press-structure (49)    Fuel gas generation chamber (B)    Water accommodation portion (B1)    Fuel accommodation portion (B2)    Electric power generation cell (C)
NOVELTY - Process for regenerating acidic ionic liquid catalyst (I) comprises contacting the ionic liquid catalyst with at least one regeneration metal in a regeneration zone in the presence of added hydrogen under regeneration conditions for a time to increase the activity of the ionic liquid catalyst.    USE - (I) is used to catalyze a Friedel-Crafts reaction (preferably alkylation) (all claimed). (I) is useful for isoparaffin alkylation.    ADVANTAGE - The process reduces the requirement to replace the ionic liquid catalyst in alkylation reactions, thus reducing the operating expenses. The process provides the way for the practical, commercial use of these environmental friendly catalysts. The process provides (I) in a non-destructive manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the ionic liquid catalyst, which has been regenerated by the above process.
NOVELTY - A gas-hydrate pellet (h3) is accommodated inside an acceptance chamber (15) and the cooling depressurization process is performed, so that the pressure of pellet is reduced. The liquid refrigerant (r) is filled inside the chamber and the pellet is immersed, so that the pellet is cooled by contacting with the liquid refrigerant.    USE - Method of manufacturing gas-hydrate by mixing methane gas and propane gas to raw-water.    ADVANTAGE - The pellet is cooled efficiently without supplying lot of refrigerant, since the thermal capacity of liquid refrigerant is high and the specific heat of refrigerant is larger than the coolant gas, so that the acceptance chamber is made compact and the size of production apparatus is reduced. The pellet and liquid refrigerant are separated and the refrigerant adhered to the pellet is volatized, so that the compression motive power of coolant gas is made unnecessary and the cooling motive power of liquid refrigerant is reduced.    DETAILED DESCRIPTION - The liquid refrigerant adhered to the gas-hydrate pellet is vaporized, while separating the gas-hydrate pellet and liquid refrigerant. An INDEPENDENT CLAIM is included for gas-hydrate production apparatus, which includes a cooling depressurization apparatus (4) with liquid refrigerant supply port, refrigerant discharge port, insertion opening for gas-hydrate pellet. A solid-liquid separator (5) is provided for separating the refrigerant and gas-hydrate pellet. The support port, discharge port and the insertion opening together forms the acceptance chamber.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the gas-hydrate production apparatus.    Cooling depressurization apparatus (4)    Solid-liquid separator (5)    Acceptance chamber (15)    Gas-hydrate pellet (h3)    Liquid refrigerant (r)
NOVELTY - A source gas (g1) and raw water (w1) are subjected to hydration reaction to generate gas-hydrate, dehydrated to discharge moisture content, and molded. When discharging wastewater (w2) in dehydration process, pure water is added to hydration reaction, and ion concentration in raw water is adjusted to decomposition suppression concentration of gas-hydrate.    USE - Manufacture of gas-hydrate.    ADVANTAGE - The method provides high-quality gas-hydrate having reduced degradability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus for producing gas-hydrate. The apparatus contains generating apparatus, water-removal device, molding apparatus, exhaust passage discharged to system outside, measurement unit to measure electrolyte ion concentration contained in moisture content, and regulating valves (v1-v3). The regulating valves are opened and closed by signal of electrolytic ion concentration and supply path which supplies pure water to generating apparatus. The water-removal devices are a reflux path which returns moisture content drained from gas-hydrate to generating apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of apparatus for producing gas-hydrate.    Source gas (g1)    Gas-hydrate slurry (h1)    Valve (v1-v3)    Raw water (w1)    Wastewater (w2)
NOVELTY - Composition comprises refrigerant agents of pentafluoroethane (R-125) (60-75 wt.%); 1,1-difluoroethane (R-152a) (15-30 wt.%); a refrigerant agent (2-15 wt.%) selected from a first group of 1,1,1,2,3,3,3-heptafluoropropane (R-227ea) and/or 1,1,1,2-tetrafluoroethane (R-134a); and another refrigerant agent (0-4 wt.%) selected from a second group of dimethyl ether (DME) and/or propane (R-290).    USE - As a monochlorodifluoromethane (R-22) substitute refrigerant fluid in a heat transfer system particularly in air conditioning system (claimed).    ADVANTAGE - The composition reduces the GWP (Global Warming Potential) factor, a factor representing one of the most desired parameters in the new products. This factor is intrinsically linked to the energy efficiency depending on the electric power generation source, so the efficiency of the mixture is also a desirable and indispensable factor. The proposed mixtures have efficiencies similar to R-22 in all the fields, high, medium and low temperature.
NOVELTY - A composition for preventing two-spotted spider mite infection or disease, comprises essential oils selected from basil, bergamot, laue seed, cardamon Silon (Cardamone Ceylon), citronella java, clary sage, clove bud, coriander, eucalyptus, geranium, lavender, lemon eucalyptus, lemongrass, marjoram, oregano, pennyroyal, peppermint, sage, spearmint, thyme red, thyme white and wormwood, is new.    USE - The compositions are useful for preventing two-spotted spider mite, Myzus persicae, Plutella xylostella, mulberry thrips, and Rhizoctonia solani infections (all claimed).    ADVANTAGE - The composition can be used to develop a more environment-friendly nature killing insects, fungicide. Therefore, it can be used as a disinfectant.
NOVELTY - A polyoxin aqueous solution comprises (wt.%) polyoxin (1-10), surfactant (0.2-10), preservative (0.1-2.0) and water.    USE - A polyoxin aqueous solution for use as biological pesticide.    ADVANTAGE - The aqueous solution is safe and environment friendly, and has low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of polyoxin aqueous solution, comprising uniformly stirring polyoxin and aqueous solution auxiliary material and packaging when quality meets the requirement by mass detecting technology, to obtain product.
NOVELTY - The apparatus (1) has planar composite discharge plates (7) formed by stacking dielectric material (11) on bottom surfaces of metallic discharge electrodes (10). The discharge plates are arranged in multiple levels, and plasma discharge spaces which serve as operating gas passages are provided between the plates. Ceramic rolling elements (12) are packed in holes (9) of the discharge electrodes.    USE - Apparatus for removal of particulate matter in exhaust gas from diesel engine.    ADVANTAGE - Since the rolling elements are freely moveable within the holes of discharge electrodes, the contamination of the surface of the rolling element by adherence of particulate matter can be avoided and stable plasma production can be ensured.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the particulate matter apparatus.    Particulate removal apparatus (1)    Discharge plate (7)    Hole (9)    Discharge electrode (10)    Dielectric material (11)    Rolling element (12)
NOVELTY - A manure comprises 0.1-0.2 part of Clostridium thermocellum, 0.1-0.2 part of powder of Actinomyces melanocyles, 0.1-0.2 part of powder of A. roseus, 0.1-0.2 part of powder of A. cellulosae, 0.1-0.2 part of powder of Aspergillus oryzae, 0.1-0.2 part of powder of Rhizopus and 0.1-0.2 part of powder of Trichoderma.    USE - A manure for aquiculture.    ADVANTAGE - The manure is capable of effectively inhibiting reproduction of pathogenic bacteria of aquatic livestock, solving problem of culture pollution, enhancing animal disease resistance and maintaining water ecologic balance. The manure special can effectively improve yield, quality and feed return rate of aquatic product.    DETAILED DESCRIPTION - A manure comprises 0.1-0.2 part of Clostridium thermocellum, 0.1-0.2 part of powder of Actinomyces melanocyles, 0.1-0.2 part of powder of A. roseus, 0.1-0.2 part of powder of A. cellulosae, 0.1-0.2 part of powder of Aspergillus oryzae, 0.1-0.2 part of powder of Rhizopus and 0.1-0.2 part of powder of Trichoderma, 18-20 parts of wheat-bran mixture comprising wheat-bran with sterile water in weight ratio of 1 to 1, 0.1-0.2 part of powder of Saccharomyces, 0.1-0.2 part of powder of deotnichum candium, 0.5-0.6 part of liquid of lactic acid bacteria, 0.5-0.6 part of liquid of Enterococcus leuconostoc, 0.5-0.6 part of liquid of sulfur-oxidizing bacteria, 0.5-0.6 part of liquid of aerobic anoxynic phototrophic bacteria, and 16-26 parts of fungi nutrient solution comprising 1-3 part(s) of monopotassium phosphate liquid, 1-1.5 part(s) of calcium chloride, 1-1.5 part(s) of urea and 5-7 parts of saccharide. The mixture and sterile water is added to sterile water solution for reserving in accordance with weight ratio of 1 to 2. An INDEPENDENT CLAIM is included for a preparation method of manure.
NOVELTY - Synthesis of biodiesel comprises reacting fatty acid with thionyl chloride at 20-40 degrees C for 1-3 hours, adding 1-4C alcohol, and reacting for 0.5-1.5 hours to prepare fatty acid ester. The charging mole ratio of fatty acid to thionyl chloride to alcohol is 1:1-1.3:1-1.3.    USE - Method for synthesis of biodiesel (claimed) used as biological energy source.    ADVANTAGE - The method is safe and environment friendly; and has low energy consumption, simple technique and post-treatment, low production cost, high yield and no pollution.
NOVELTY - A briquette composition comprises biomass fuel, blind coal and water glass adhesive.    USE - A briquette composition.    ADVANTAGE - The briquette is safe and easy to burn, and difficult to crush during transportation and use; has long combustion time and good air permeability; and contains no volatile components, thus avoiding a black smoke during combustion. The water glass has high adhesive intensity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of briquette composition comprising crushing biomass fuel, blind coal and water glass adhesive, agitating and uniformly mixing, pressing using a pressing machine to obtain a briquette, and carbonizing in a carbonization stove.
NOVELTY - Producing a fermentation product from lignocellulose-containing material comprises: (a) pretreating lignocellulose-containing material; (b) preparing a slurry of pretreated lignocellulose-containing material and thermo treated distiller's grain; (c) hydrolyzing the slurry with one or more cellulolytic enzymes; and (d) fermenting with a fermenting organism.    USE - The method is useful for producing a fermentation product from lignocellulose-containing material (claimed).    ADVANTAGE - The invention provides low cost renewable energy sources.
NOVELTY - The complex hydraulic-concreting ready-package biogas generator has gas outlet pedestal (2) which is positioned on top portion of biogas generator shell (1), while gas outlet pipe (3) is arranged on gas outlet pedestal. A feed inlet (4) is arranged at one side of top portion of biogas generator shell. A pedestal (6) is arranged at bottom portion of biogas generator shell, while hydraulic tank (5) is arranged at other side of to portion of biogas generator shell.    USE - Complex hydraulic-concreting ready-package biogas generator.    ADVANTAGE - Provides a generator with ellipsoid space, shallow bearing depth, large fermentation area, no fermentation blind area, good sealing for pool body, has no moveable cover, easy to operate, can be massly produced, convenient to install, and is provided with inexpensive pool.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for manufacturing complex hydraulic-concreting ready-package biogas generator.    DESCRIPTION OF DRAWING(S) - The drawing shows the side view of complex hydraulic-concreting ready-package biogas generator.    Biogas generator shell (1)    Gas outlet pedestal (2)    Gas outlet pipe (3)    Feed inlet (4)    Hydraulic tank (5)    Pedestal (6)
NOVELTY - Rain-processing technique-road biological treatment comprises using rain-processing filter material having substrate in certain graduation and microbiocenose as special roadbed under penetrable road and moisture-preserving layer; and equipping space below roadbed with porous pipes to collect purified rain and sending to well or pool for storage.    USE - Method of rain-processing technique-road biological treatment for rain collection, rain reutilization and rain quality purification and for biological environment for microorganisms to treat organic-pollution water quality and part of the sewage in the rain (claimed).    ADVANTAGE - The method treats pollutants in rain through biochemical reaction of microorganisms when rain flows by penetrable road, thus purifying water and realizing purification treatment, collection and reutilization of rain on road surface like city road, square and parking lot on the basis of not influencing the use function of the road; and the method is environment protection water treating field.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a biological environment for microorganisms comprising microorganisms-contained filter material laid under in moist environment under penetrable road and moisture-preserving layer.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the rain-processing filter material (Drawing includes non-English language text).
NOVELTY - Glyphosate is prepared by adding (pts.wt.) N-(phosphonomethyl) iminodiacetic acid (100) and active catalyst (5-20) in aqueous-phase medium (100-400) into reaction tank with 0.5-1.2 MPa, introducing oxygen (20-100 wt.%) for catalytic oxidization reaction at 55-110 degrees C, adding filter cake into saturated glyphosate solution (800-1500 pts.wt.), increasing temperature, separating active carbon and glyphosate solution, cooling glyphosate solution, crystallizing, separating, and passing through membrane separating device.    USE - Method for preparing glyphosate (claimed).    ADVANTAGE - The method recycles catalyzed, oxidized and high-concentration N-(phosphonomethyl) iminodiacetic acid of mother liquor to prepare glyphosate, has low cost, enhances yield of solid glyphosate, and avoids environmental pollution caused by side product formaldehyde.    DETAILED DESCRIPTION - Preparation of glyphosate comprises:    (A) adding (pts.wt.) N-(phosphonomethyl) iminodiacetic acid (100) and active catalyst (5-20) in aqueous-phase medium (100-400) into reaction tank with 0.5-1.2 Mpa, introducing oxygen (20-100 wt.%) to perform catalytic oxidization reaction at 55-110 degrees C, and separating solid and liquid to obtain filter cake having glyphosate crystals and active carbon;    (B) adding filter cake into saturated glyphosate solution (800-1500 pts.wt.), increasing temperature to dissolve, separating active carbon and glyphosate solution, and collecting active carbon catalyst to recycle; cooling glyphosate solution, crystallizing, separating to obtain solid glyphosate product and filtrate used as saturated glyphosate solution;and    (C) passing reaction mother liquor through membrane separating device to separate glyphosate and side product formaldehyde in mother liquor, recovering formaldehyde solution, returning glyphosate mother liquor as aqueous-phase medium to recycle for 2-50 times or used as saturated glyphosate solution.
NOVELTY - A microbiological fertilizer comprises blood wastewater as raw material; where it is obtained by carrying out microbiological fermentation using the blood wastewater.    USE - The microbiological fertilizer is useful for crop farming (claimed).    ADVANTAGE - The microbiological fertilizer reduces pesticide residue.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for preparing the microbiological fertilizer.
NOVELTY - Preparation of tebuconazole aqueous emulsion comprises dissolving tebuconazole in little solvent and surfactant, and uniformly stirring to obtain uniform oil phase; mixing and stirring water, antifoaming agent, antifreezing agent and thickening agent to form uniform aqueous phase; and adding oil phase into aqueous phase at normal temperature and 200-1700 rpm for 30-60 minutes, or adding aqueous phase into oil phase to form finely dispersed aqueous emulsion, where average particle diameter of product is less than 20.00 ~mm.    USE - Method for preparation of tebuconazole aqueous emulsion (claimed) for use as pesticide for preventing common diseases on fruit trees and vegetables.    ADVANTAGE - The product is safely produced, stored and transported; is safely and conveniently used; and is environment friendly.    DETAILED DESCRIPTION - Preparation of tebuconazole aqueous emulsion comprises:    (A) preparing materials comprising (wt.%) tebuconazole (1-25), emulsifier (1-20), antifreezing agent (1-5), antifoaming agent (0-2), solvent (1-45), thickening agent (0.1-3) and water;    (B) dissolving tebuconazole in little solvent and surfactant, and uniformly stirring to obtain uniform oil phase;    (C) mixing and stirring water, antifoaming agent, antifreezing agent and thickening agent to form uniform aqueous phase; and    (D) adding oil phase into aqueous phase at normal temperature and 200-1700 rpm for 30-60 minutes, or adding aqueous phase into oil phase to form finely dispersed aqueous emulsion, where average particle diameter of product is less than 20.00 ~mm.
NOVELTY - Herbicide composition comprises sulfonylurea, pyridines and acetochlor at weight ratio of 0.1-5:0.1-10:0.1-40.    USE - Herbicide composition used for treating annual perennial graminaceous and broad leaved weed of rice field (claimed).    ADVANTAGE - The composition improves weeding effect, decreases using amount, reduces cost on agrochemical and side effect to environment, and simultaneously expands weeding spectrum.
NOVELTY - A microecological preparation for animals comprises blood wastewater as raw material; where it is prepared by microorganism fermentation by using the blood wastewater.    USE - The microecological preparation is useful in animal breeding (claimed).    ADVANTAGE - The microecological preparation resolves the pollution problem of blood wastewater to the environment. Moreover, it changes waste into valuable compound to carry out clean production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for preparing the microecological preparation for animals.
NOVELTY - Producing marsh gas by wastewater from production of dextran comprises fermenting the wastewater in anaerobic condition by a marsh gas fermentation cylinder, and adding nitrogen and phosphorus in the wastewater.    USE - The process is useful for producing marsh gas by wastewater from production of dextran (claimed).    ADVANTAGE - In utilizing the process, the chemical oxygen demand (COD) removal rate of the wastewater is more than 90%, one cubic meter of the wastewater can form 40-70 m3 of marsh gases, and methane content of the marsh gas is 50-60 vol.%. Moreover, the process makes use of the wastewater from production of dextran, changes the waste into valuable compound, reduces pollution, and brings good economical benefit.
NOVELTY - Treating penicillin waste water residue, comprises: taking penicillin waste water residue as raw material; fermenting by inoculating Bacillus to remove penicillin remaining charge; treating fermentation liquor by using acid and alkali and then separating solid and liquid to separate the remaining charge-removed penicillin fungus dreg.    USE - The method is useful for treating penicillin waste water residue (claimed).    ADVANTAGE - The method is good for further waste water treatment; the waste residue of which the penicillin remaining charge is removed and can be used in feedstuff and manure safely. The method solves the problem of separating waste water residue produced by the technology of extracting penicillin from decantor, and the problem of using penicillin waste residue safely.
NOVELTY - The up-flow compound ecological bed includes a main body and a water distributing channel. A porous filter plate is provided in the main body while a dielectric material is provided on the porous filter plate. The upside of the dielectric material is provided with artificial soil. A sewage inlet is connected with the water distributing channel while the sewage outlet is placed on the side wall of the main body at the upper part of the dielectric material.    USE - Up flow compound ecological bed.    ADVANTAGE - Low cost, free from redundant maintenance, energy saving, approximately free from any operation cost, and needs no human interference such that it is particularly suitable to be used in the rural areas.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the up flow compound ecological bed.
NOVELTY - The ecological bed has a sewage inlet arranged at one end of the host body and which opens in the distributing channel whose rear part is connected with immersion flow tube. The immersion flow tube includes a capillary immersion flow tube with both the immersion flow tube and the capillary immersion flow tube provided with holes. The immersion flow tube and the capillary immersion flow tube are evenly distributed in the medium material layer. The sewage outlet is arranged at another end of the host body.    USE - Radial flow compound ecological bed.    ADVANTAGE - Low in investment and has a self-renewing performance after being built. Minimal maintenance and does not consume too much energy. Basically free from any running cost, and all the treatment flows are automatically processed. Needs no manual intervention, therefore, is very fit for use in rural areas.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the radial flow compound ecological bed.
NOVELTY - Refinery exhaust gas and coke oven gas are utilized by performing purification treatment and a cascade separation process to refinery exhaust gas and/or coke oven gas as material gas to obtain hydrogen. All by-product gases of separation process are sent to a mixture preparation device to mix with liquefied natural gas or liquefied petroleum gas, and the heat value is regulated to obtain substitute natural gas product which is then transported to a natural gas pipe.    USE - Method for utilizing refinery exhaust gas and coke oven gas (claimed).    ADVANTAGE - The method is economical and can utilize refinery exhaust gas and the coke oven gas to the largest degree.
NOVELTY - Compensating organic carbon source for constructed wetland comprises adding crushed branches, wood powder and/or plant straws as organic carbon source to a constructed wetland. When inlet water quality is stable, the organic carbon source is directly added to the filler of the constructed wetland. When the inlet water quality is unstable, the organic carbon source is added to an organic carbon releasing pool, and decomposition liquor in the releasing pool is placed to the constructed wetland.    USE - Compensating organic carbon source for constructed wetland.    ADVANTAGE - The plant material has low cost and readily available. The operation and the post maintenance management are simple, and plenty of manpower and physical resources can be saved. The denitrification efficiency of the constructed wetland can be improved by compensating plant material when sewage with low carbon nitrogen ratio of the constructed wetland is treated by a simple method. The removing ratio of total N can be improved to more than 70%.
NOVELTY - Organic pollutant wastewater treatment comprises preparing a phase transfer carrier by fermenting an agricultural waste residue with basidiomycetes; adding the phase transfer carrier to the organic pollutant wastewater, and transferring the pollutant from liquid phase to solid phase; carrying out regeneration of the phase transfer carrier by degrading the pollutants using basidiomycetes through solid continuous fermentation way, and regenerating phase transfer capability of the phase transfer carrier; and carrying out continuous treatment using the regenerated phase transfer carrier.    USE - Method for the organic pollutant wastewater treatment (claimed).    ADVANTAGE - The method is inexpensive.
NOVELTY - Production of fertilizer composition from urban sludge comprises dehydrating sludge, drying, crushing, screening using 70-120 mesh sieve, assaying, adding additive (1-15 wt.% of sludge), adding nitrogen-phosphorus-potassium (NPK) materials and microelement as soluble materials, mixing, fermenting, granulating, drying and packing. Sludge assay data are used as reference for adding proper amounts of substances to meet standard content of fertilizer composition.    USE - Production of fertilizer composition from urban sludge (claimed) for use in agriculture.    ADVANTAGE - The method and the addition of additive enable the NPK components, which are not absorbed easily by plants, to be converted into easily-absorbed quick-acting fertilizer. The NPK materials and microelement have low amount used and low cost. The fertilizer composition has quick effect and long lasting effect.
NOVELTY - Green asymmetric synthesis of chiral bicyclic compound involves reacting cyclonene derivatives and nitroolefin derivatives for 3-72 hours at - 20-40 degrees C in the presence of chiral secondary amine catalyst, protonic acid and water; and separating the reaction solution to obtain chiral bicyclic compound. The mol ratio of the nitroolefin derivatives to the cyclonene derivatives is 1:1-3. The mol ratio of the nitroolefin derivatives/chiral secondary amine catalyst/protonic acid/water is 1:0.05-0.3:0.05-0.3:30-40.    USE - Method for symmetric synthesizing chiral bicyclic compound (I) (claimed).    ADVANTAGE - The method is capable of producing compound having good response characteristics.    DETAILED DESCRIPTION - Green asymmetric synthesis of chiral bicyclic compound of formula (I) involves:    (A) using cyclonene derivatives of formula (II) and nitroolefin derivatives of formula R4-CH-CH-NO2 as raw materials;    (B) reacting for 3-72 hours at - 20-40 degrees C in the presence of chiral secondary amine catalyst, protonic acid and water; and    (C) separating the reaction solution to obtain chiral bicyclic compound (I).    The chiral secondary amine catalyst is proline derivatives of formula (IV). The mol ratio of the nitroolefin derivatives to the cyclonene derivatives (II) is 1:1-3. The mol ratio of the nitroolefin derivatives/chiral secondary amine catalyst/protonic acid/water is 1:0.05-0.3:0.05-0.3:30-40.    R1-R3=H or 1-20C alkyl;    R4=H or 1-20C alkyl, 2-methoxyphenyl, 3-methoxyphenyl, 4-methoxyphenyl, 2-methylphenyl, 3-methylphenyl, 4-methylphenyl, phenyl, 2-fluorophenyl, 3-fluorophenyl, 4-fluorophenyl, 2-chlorophenyl, 3-chlorophenyl, 4-chlorophenyl, 2-bromophenyl, 3-bromophenyl, 4-bromophenyl, 2-nitrophenyl, 3-nitrophenyl, 4-nitrophenyl, 2-trifluoromethylphenyl, 3-trifluoromethylphenyl, 4-trifluoromethylphenyl, furyl or thienyl;and    R5=sulfur-containing compound of formulae (1-3).
NOVELTY - An isolated Bacillus subtilis dcy-1 strain deposited under CCTCC NO: M 208122 for biofermentation bed and producing pig manure compost, is new.    USE - The strain is useful for biofermentation bed and producing pig manure compost (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a microbial agent comprising the strain above.
NOVELTY - Preparing biogas, where it is invented according to principles of bi-phase anaerobic fermentation and adsorbent biological releasing regeneration, where the adsorbent is regarded as carrier; and then the fatty acid and other fermentation products in acidification reactor in the bi-phase anaerobic fermentation are adsorbed by the adsorbent.    USE - The method is useful for preparing biogas (claimed).    DETAILED DESCRIPTION - Preparing biogas, where it is invented according to principles of bi-phase anaerobic fermentation and adsorbent biological releasing regeneration, where the adsorbent is regarded as carrier; and then the fatty acid and other fermentation products in acidification reactor in the bi-phase anaerobic fermentation are adsorbed by the adsorbent; and then the adsorbent adsorbed with fatty acid and other fermentation products is disposed in methane-phase reactor; the fatty acid and other fermentation products adsorbed on the adsorbent are decomposed by microorganism in the methane-phase reactor, to generate methane; the process for generating methane is biological releasing regeneration process to the adsorbent; the adsorbent after releasing and regenerating is washed to reuse.
NOVELTY - Device comprises a dryer (30), a stirring unit (40), a slack hopper (50), a mold (60) and a storage tank (70), which is connected to a packing machine (80) and a transfer unit (90). The dryer includes a drying furnace (31), a multistage non-combustible conveyor (32) and a heat combustion unit (33). A high speed vapor discharge device (34) is also included, which is installed at upper part of the drying furnace. The mold is connected to the stirring unit and the transfer unit.    USE - Device for treating waste and sewage sludge.    ADVANTAGE - The device is eco-friendly and cost-effective, and enables to improve the calorific value of the waste and sewage sludge.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for manufacturing device, which involves utilizing dryer, the stirring unit, the slack hopper, the mold, the storage tank, the packing machine and the transfer unit.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device.    Dryer (30)    Drying furnace (31)    Multistage non-combustible conveyor (32)    Heat combustion unit (33)    High speed vapor discharge device (34)    Stirring unit (40)    Slack hopper (50)    Mold (60)    Storage tank (70)    Packing machine (80)    Transfer unit (90)
NOVELTY - Comprehensive treatment of livestock manure comprises: (a) separating dry and wet livestock manures; and (b) separating rain and sewage; then dividing it into three parts: part of dry manures enters organic fertilizer factory to prepare organic fertilizer by the scientific process; part of dry manures are prepared to livestock manure organic fertilizer by windrow composting method; the residual part of dry manures and liquid manure enters biogas tank for anaerobic fermenting to produce biogas and biogas fertilizer; and the building and operation of the biogas is property management mode.    USE - The method is useful for comprehensive treatment of livestock manure (claimed).    ADVANTAGE - The advantages of the method are as follows: adopting comprehensive treatment method of the livestock manure, it makes full use of the livestock manure, achieves zero discharge of the pollution of the livestock manure and protects ecological environment; the application of the livestock manure organic fertilizer improves quality of the soil, improves quality of the grain and vegetable, reduces amount of the chemical fertilizer and increases income of the farmer. The invention is easy to be promoted, has low operation cost, good economical benefit, ecological benefit and social benefit.
NOVELTY - A combined treatment for organic wastewater with high concentration is performed by eliminating organic substances with high concentration based on biodegradability differences of the organic substances at different stages; eliminating biodegradable organic substances using micro aerobic bacteria treatment method; improving biodegradability of wastewater using chemical oxidation method; and carrying out post-treatment to ensure water quality of discharged water using active sludge method.    USE - Method for combined treatment of organic wastewater with high concentration (claimed).    ADVANTAGE - The method has high eliminating efficiency, and generates less sludge.
NOVELTY - Production of hydrogen includes feeding a mixture of alcohol and water into an anode chamber of a reforming channel via a circulating pump, applying direct current (DC) voltage between anode and cathode of reforming channel to electrochemically reform alcohol and water in the anode, and reducing water in cathode to separate hydrogen. The anode and cathode chambers are separated from each other by a solid anion conductive polymer film as electrolyte.    USE - Method for producing hydrogen (claimed).    ADVANTAGE - The method produces hydrogen with low voltage and has low cost and low energy consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a hydrogen production device comprising a DC power supply, a vessel for storing mixture of alcohol and water, an anode chamber for circulation and in/out of the mixture of alcohol and water, a cathode chamber for storing water, and a hydrogen collector connected with the cathode chamber. Anode and cathode are respectively arranged on two side surfaces of a solid anion conductive polymer film. The anode chamber, cathode chamber, cathode, anode and solid anion conductive polymer film are formed into a reforming channel. The anode and cathode are connected with the DC power supply.
NOVELTY - A copper-2-mercaptobenzothiazole comprising specific crystal form, where X-powder diffraction diagram of copper-2-mercaptobenzothiazole appears interplanar spacing d which equals to 13.360, 8.455, 7.650 and 3.822 and belongs to characteristic peak of copper-2-mercaptobenzothiazole, is new.    USE - The copper-2-mercaptobenzothiazole with specific crystal form is useful for preventing and treating agricultural plant disease, where the copper-2-mercaptobenzothiazole with specific crystal form is used for preventing and treating bacteroidal and fungal diseases of crops, fruit trees and vegetables (claimed).    ADVANTAGE - The invention is simple, low cost and environment-friendly; and the prepared copper-2-mercaptobenzothiazole with specific crystal form has stable property and wide anti-fungal spectrum.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a preparation method of the copper-2-mercaptobenzothiazole with specific crystal form.
NOVELTY - A waste gas processing apparatus (25) has a catalyst storage case (30) for accommodating the combustion catalyst (32). The catalyst storage case has an accommodating portion (33) for accommodating the combustion catalyst in upper portion side, and a condensed water collecting portion (34) for collecting specific condensed water produced in the catalyst storage case with the temperature fall of the waste gas, at lower portion side during the shutdown processing of the fuel cell apparatus.    USE - Fuel cell apparatus.    ADVANTAGE - The specific condensed water can be produced in the catalyst storage case effectively during the shutdown processing of the fuel cell apparatus. The spoiling of the combustion catalyst is suppressed at the time of restarting of the fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the fuel cell apparatus.    Waste gas processing apparatus (25)    Catalyst storage case (30)    Combustion catalyst (32)    Accommodating portion (33)    Condensed water collecting portion (34)
NOVELTY - A biomass gasification furnace comprises a biomass cycle flowing system, a biomass fuel gas turbo-generator set, and a biomass fuel gas boiler system. The biomass fuel gas turbo-generator set and the biomass fuel gas boiler system are connected with fuel gas transfer passages of the biomass cycle flowing system.    USE - A biomass gasification furnace.    ADVANTAGE - The biomass gasification furnace is inexpensive.
NOVELTY - A coal burning boiler comprises a biomass fuel gasification and combustion system having a biomass gas burner, a biomass gas pipeline, and a biomass fuel gasification system. The biomass gas burner is inside a furnace of a coal burning boiler.    USE - A coal burning boiler.    ADVANTAGE - The coal burning boiler is inexpensive, has simple structure, and allows coal to be replaced by inexpensive bio-raw materials.
NOVELTY - A reaction apparatus has base (2) with reaction medium flow path (1), supply path (3) for supplying reaction medium to supply port (3a), discharge port (4a) downstream from flow path, exhaust passage for emitting the reaction medium and circuit (5) on base where reaction medium returns.    USE - A reaction apparatus for fuel cell systems used in mobile telephone or notebook personal computer.    ADVANTAGE - The reaction rate of reaction medium is increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross section (a) and planar perspective drawing (b) of reaction apparatus.    Flow path (1)    Base (2)    Supply path (3)    Supply port (3a)    Exhaust passage (4)    Discharge port (4a)    Circuit (5)
NOVELTY - The straw biomass gasification cooking device has a charging basket (1), a combustion furnace (10), a cooking stove (9) and a machine body (4). A purifier (5) that is under the machine body is provided and is connected with a cooking stove through the gas conduit (3). The cooking stove is provided at the top end of the machine body while a combustion furnace is at the bottom of the charging basket. The charging basket is connected with a purifier through the gas conduit.    USE - Gasification cooking device for straw biomass.    ADVANTAGE - Provides a worry free and safe usage since there is no pressure and no poison in the gas. Enables convenient installation and economical and practical without the need of professional tool to install. Saves on energy and has high efficiency since the fuel can be obtained locally. Provides convenient usage and simple operation. Enables adding of material to burn to generate gas even in midcourse without burning out which ensures clean, no tar, and no smoke operation. Performs double purification which makes the gas more pure and generate more working heat without using power and fuel gas which contributes to environment protection.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic of the straw biomass gasification cooking device.    Charging basket (1)    Gas conduit (3)    Machine body (4)    Purifier (5)    Cooking stove (9)    Combustion furnace (10)
NOVELTY - The biomass gasification furnace has a fuel gas processing cylinder (5) installed on outer lateral wall of furnace body (1) and over an oxygen sender. The lacing blades (8) are staggered on the outer and inner side inner walls of the fuel gas processing cylinder. The lower end of the air conducting tube (2) is in connection with the inner cavity of the fuel gas processing cylinder while an air transmission tube (6) is installed on its outer lateral wall. A hanged plate typed separator (4) is installed in the air conducting tube.    USE - High efficiency low-exhausting biomass gasification furnace for biomass gasification oxygen supply.    ADVANTAGE - Provides a high efficiency low-exhausting biomass gasification furnace which has uniform oxygen supply, stable thermal decomposition, rational air purification, duration burning and no odor with simple to structure that is small to cover, convenient to install in set, operate and maintain.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the high efficiency low-exhausting biomass gasification furnace.    Furnace body (1)    Air conducting tube (2)    Hanged plate typed separator (4)    Fuel gas processing cylinder (5)    Air transmission tube (6)    Lacing blades (8)
NOVELTY - The fully automatic straw gasification furnace has gasification furnace with bottom that is set with a lighting port. An automatic igniter is installed through the lighting port and the furnace body is connected with a condensation purifier through a gas pipe. The condensation purifier is set with the gas outlet pipeline and is internally set with a partition board. The partition board has two sides which are respectively set with condensing boards.    USE - Fully automatic straw gasification furnace.    ADVANTAGE - Provides a straw gasification furnace that uses biomass as the fuel and adopts the electronic ignition way for combustion. Uses a multi-separation-and-condensation purifier so the separation and purification effects of gas are better than the normal gasification furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the fully automatic straw gasification furnace.
NOVELTY - The straw gasification set has a gas barrel (8) which is provided with a purified gas outlet (10) in the top. The gas-fluid separator (3) consists of a water tank (11) and a gas-fluid separation tower (12) which is provided on the water tank and connected with an inner cavity. The purified gas outlet is connected with a gas inlet (15) of the gas-fluid separation tower through a pipe (14). The gas-fluid separation tower has a lower part which is provided with a gas outlet (16).    USE - Straw gasification set for biological gasification device.    ADVANTAGE - Provides convenient maintenance, high gas-fluid separation efficiency, fine integral purification effect and high gas production amount.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the straw gasification set.    Gas-fluid separator (3)    Gas barrel (8)    Purified gas outlet (10)    Water tank (11)    Gas-fluid separation tower (12)    Pipe (14)    Gas inlet (15)    Gas outlet (16)
NOVELTY - The tar-less anti-overhead continuously charged straw gasification cooking device has gasification burner which includes a burner body (1) having a housing (2) and an inside core (4). The vent holes (6) are evenly distributed in a lower peripheral wall of the inside core. An air intake system includes an annular aeration pipe (8) and air inlet (10) provided on bottom of gas pipe (9).    USE - Tar-less anti-overhead continuously charged straw gasification cooking device.    ADVANTAGE - Enables material to be evenly burned and in which the material integrally falls down after burning. Provides a straw gasification cooking device with no deviant combustion and overhead phenomenon in use while ensuring that the continuous batch charge will not cause flame-out and the charging orifice does not smoke. Enables the tar and water vapor generated by the burning of the material to be completely cracked into the combustible gas into the stove and not to be exhausted to the outside. Provides very convenient use and is in accordance with the environment protection requirement.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the tar-less anti-overhead continuously charged straw gasification cooking device.    Burner body (1)    Housing (2)    Inside core (4)    Vent holes (6)    Annular aeration pipe (8)    Gas pipe (9)    Air inlet (10)
NOVELTY - The efficient energy-saving biomass gasification cooking device has a furnace body which is equipped with ash fetching opening (8). A purifier has a bottom which is equipped with sewage draining pipe (24) with ball valve (9). Another combustion cooling range (10) connected with gas pipe is set inside the warming furnace (11) which is equipped with water inlet pipe (14) and water outlet pipe (15) that are connected with heating radiator. A superconducting heat pipe (13) is equipped above the combustion cooling range.    USE - Efficient energy-saving biomass gasification cooking device.    ADVANTAGE - Prevents deformation of furnace body due to too high temperature in the furnace as the fire-resistant layer is made from fire-resistant cement, sand and grain material. Slows down raise speed of water vapor and tar in combustible gas since the baffle places are set inside the purifier, thus, water vapor and tar can be separated from combustible gas in collision progress with the baffle plate by cooling and then they are discharged from sewage draining exit, which guarantees relative high purity of combustible gas to be used.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic structure of the efficient energy-saving biomass gasification cooking device.    Ash fetching opening (8)    Ball valve (9)    Combustion cooling range (10)    Warming furnace (11)    Superconducting heat pipe (13)    Water inlet pipe (14)    Water outlet pipe (15)    Sewage draining pipe (24)
NOVELTY - The biomaterial gasification device has a gas generator, cyclone separator, compound filtration device, liquid ring compressor, gas water separator and pressure vessel that are connected in sequence by gas delivery pipes. The pressure vessel is connected to a user gas delivery pipe network by reducing valves. The pressure balance pipe has ends connected with the gas delivery pipe on the gas inflow end of liquid ring compressor and gas delivery pipe on gas outflow end of gas water separator. The gas water separator is equipped with a water draining valve and liquid level meter.    USE - Biomaterial gasification device for converting biological wastes in rural areas into fuel gas.    ADVANTAGE - Enables to convert biomaterial fuels and wastes with low thermal value into the environmentally friendly biofuel gas with high thermal value. Provides a simple technique and scientific design and can save energy and reduce emission providing wide application range. Converts the biological wastes in rural areas into fuel gas quickly and deliver them by pipes such that people in rural areas can use clean and convenient gas as people in urban areas.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of the biomaterial gasification device.
NOVELTY - The biomass gasification equipment has gas generator, gas buffer tank, filtering system, water ring compressor, gas-water separator and pressure container connected in turn to each other via gas transferring pipes. The pressure container is connected to user-terminal pipes via pressure reducing valve. The ends of pressure balance pipe are connected to the gas transferring pipe on gas inlet end of water ring compressor and to the gas transferring pipe on gas outlet end of gas-water separator. The gas-water separator is equipped with water discharging valve and water-level gauge.    USE - Biomass gasification equipment for converting wastes into fuel gas to transfer by pipes in e.g. rural areas.    ADVANTAGE - Enables to convert biomass raw material with low heat value and waste into clean environment-friendly biomass fuel gas with high heat value. Provides a more reasonable, simpler and compact structure while taking up small area and is highly efficient and safe. Obtains high-purity, clean and pollution-free fuel gas and solves the separating problem of wood tar. Effectively prevents the corrosion of pipe, blockage and environment pollution. Prevents conversion of wastes in countries into fuel gas to be transferred by pipes so as to provide clean and convenient fuel gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass gasification equipment.
NOVELTY - The thin film type gas sensor has an insulating film (12) that is formed on the surface of a substrate (11). A thin film heat sensing structure (5), metal thin film resistor (6) and the electrode pads (7) are arranged on the surface of the insulating film. A beam structure (2) is positioned at the surface of the heat sensing structure such that a circular or polygonal shaped groove (3a) is formed at the back surface side (2a) of the beam structure. The soft flexible material is embedded in the groove.    USE - Thin film type gas sensor used for detecting combustible gas such as hydrogen gas and methane gas on surface of detecting element, and for use in portable apparatus and household application.    ADVANTAGE - Since the groove is formed at back surface of beam structure, the heat deformation of the beam structure due to the thermal stress can be prevented. Thus, the destruction of the beam structure is prevented so that the durability of the thin film type gas sensor is improved.    DESCRIPTION OF DRAWING(S) - The drawings show the top view and end elevation views of thin film type gas sensor.    Beam structure (2)    Back surface side of beam structure (2a)    Circular or polygonal shaped groove (3a)    Thin film heat sensing structure (5)    Metal thin film resistor (6)    Electrode pad (7)    Substrate (11)    Insulating film (12)
NOVELTY - New method of improving soil fertility with microorganism isolated from earthworms, is disclosed. Image 0/0
NOVELTY - An environment friendly process for making losartan potassium is disclosed. Aqueous potassium hydroxide solution is added to losartan free acid. The mixture is stirred, and the filtrate is added to the water immiscible solvent. The water was removed azeotropically to form losartan potassium. Image 0/0
NOVELTY - Process of neutralizing beverage industrial wastewater by a bacterial strain Exiguobacterium sp. isolated in India, where the strain is capable of bringing down the pH of wastewater from 12.00-7.00 units within 1-1.5 hours. Image 0/0
NOVELTY - Preparing fatty acid alkyl ester for bio-diesel fuels involves carrying out an esterification reaction of fatty acid raw material with alcohol in the presence of metal catalyst.    USE - For preparing fatty acid alkyl ester for bio-diesel fuels (claimed).    ADVANTAGE - The method does not require the glycerine purification process, and has the superior conversion ratio of fatty acid; and is applicable to the manufacturing apparatus of an industrial scale as well as of a small scale. The method provides fatty acid alkyl ester of high purity and high conversion ratio which is obtained by two-step distillation processes. Thus the total process for producing fatty acid alkyl ester is simplified and cost for process facilities and reduces the operation. The method is economically favorable since worthless fatty acid distillate and/or cheap fatty acid are used as the raw material.
NOVELTY - The fuel cell (1) has several cells (C1,C2) that are fed with fuel gas from one surface and oxygen from the other surface for generating electric power. A cell holder (6) holding the cells forms an internal space together with cells. A fuel generating unit (B) arranged in the internal space generates the fuel gas. The ammonia removal agent removes ammonia from the generated fuel gas.    USE - Fuel cell for charging lithium ion secondary battery used in portable electronic device such as mobile telephone. Can also be used in digital camera and notebook computer.    ADVANTAGE - The size of the fuel cell can be made smaller since the piping space is minimized by arranging fuel generating unit in the internal space and the unnecessary portion of the fuel cell can be sealed using the resin.    DESCRIPTION OF DRAWING(S) - The drawing shows an exploded perspective view of the fuel cell.    Fuel cell (1)    Substrate (2)    Cell holder (6)    Fuel generating unit (B)    Cells (C1,C2)
NOVELTY - The plant has a compensated vacuum/pressure system which controls pressure throughout a circuit through which fuel gas flows. An air conditioning system cools the air discharged from fluidized bed reactor used for conversion of waste into fuel gas at extremely high temperature. A filtration system provided for dry filtration of the obtained gas includes a bag filter, a filter cleaning device, an ash extraction device and a thermal ash cleaner.    USE - Plant for converting solid waste such as biomass into fuel gas.
NOVELTY - A lactic acid bacteria having excellent acid resistance and capable of fermenting lactic acid, specifically a Lactobacillus plantarum ST2 strain (NITE P-509) or ST11 (NITE P-510), is new.    USE - The bacteria is useful for fermenting lactic acid; and for preparing microorganism composition for producing silage and fertilizer (all claimed). It is also useful as a livestock feed.    ADVANTAGE - The invention provides a lactic acid bacteria having excellent acid resistance (claimed). The fodder formation is easy and it has high assimilation efficiency.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a microorganism composition comprising the lactic acid bacteria above;    (2) a production method of silage comprising adding the microorganism composition to silage material; and    (3) a production method of fertilizer comprising adding the microorganism composition to a manure material.
NOVELTY - Producing liquid fuel from a biogas comprises passing the biogas through a liquid petroleum fraction at greater than or equal to 100 degrees C but below boiling, while contacting the biogas and the liquid petroleum fraction with a transition metal to produce a gaseous effluent; and condensing the effluent to liquid form.    USE - Method for producing liquid fuel from a biogas including hydrogen, carbon monoxide and/or methane, or natural gas (claimed), used in driving engine or other machinery or appliance that is run by a petroleum-based fuel.    ADVANTAGE - The method can provide gaseous product that results from the contact containing a vapor that can be condensed to achieve the liquid fuel. The condensed product is chemically distinct from the liquid petroleum fraction, and when the process is operated on a continuous basis without adding further liquid petroleum fraction to the reaction medium, the product is produced in a volume that far exceeds the starting volume of the reaction medium
NOVELTY - Sewage disposal method of stud farm, involves deodorizing and purifying livestock farm waste water discharged from stud farm by mixing with lactic acid bacteria mixture containing Lactobacillus fermentum and Enterococcus faecium, flowing the treated water into transpiration water tank in which wood chips such as wood chip and saw dust are stored, and performing transpiration processing of the treated water by which the treated water is subjected to evaporation and radiation.    USE - The method is useful for sewage disposal of stud farm (claimed).    ADVANTAGE - The livestock farm waste water discharged from stud farm can be deodorized and purified without using pharmaceutical or sterilization agent containing large quantities of chemical substances. The sewage disposal method can be carried out without exerting bad influence on environment or without stocking surroundings.    DETAILED DESCRIPTION - Sewage disposal method of stud farm, involves deodorizing and purifying livestock farm waste water discharged from stud farm by mixing with lactic acid bacteria mixture containing Lactobacillus fermentum and Enterococcus faecium, where the biochemical oxygen demand (BOD) of the treated water is 50-200 part per million (ppm), flowing the treated water into transpiration water tank in which wood chips such as wood chip and saw dust are stored, and performing transpiration processing of the treated water by which the treated water is subjected to evaporation into air and radiation.
NOVELTY - A compost manufactured by fermentation comprising an isolated or extracted microbe group from a cultured Shirakamisanchi, i.e. Shirakami bacterium, is new.    USE - The compost is useful as organic fertilizer for agricultural applications.    ADVANTAGE - The compost can minimize pollution and it does not contribute to global warming.
NOVELTY - Producing liquid fuel from a biogas comprises passing the biogas through a liquid petroleum fraction at greater than or equal to 100 degrees C but below boiling, while contacting the biogas and the liquid petroleum fraction with a transition metal to produce a gaseous effluent; and condensing the effluent to liquid form.    USE - Method for producing liquid fuel from a biogas including hydrogen, carbon monoxide, and/or 90-100 mol% methane or natural gas (claimed), used in driving engine or other machinery or appliance that is run by a petroleum-based fuel.    ADVANTAGE - The method can provide gaseous product that results from the contact contains a vapor that can be condensed to achieve the liquid fuel. The condensed product is chemically distinct from the liquid petroleum fraction, and when the process is operated on a continuous basis without adding further liquid petroleum fraction to the reaction medium, the product is produced in a volume that far exceeds the starting volume of the reaction medium.
NOVELTY - The apparatus has a reformer (24) that reforms the pyrolysis gas (b) obtained from a gasifier (22). A gas purification apparatus (25) purifies the reformed gas output from reformer, and supplies the purified gas to the gas engine (27), to drive apparatus. A recuperator (3) burns flammable component in the pyrolysis gas which is branched before reformer, and recovers burning heat.    USE - Apparatus for generating electric power using pyrolysis gas obtained from biomass of e.g. municipal solid waste, sewage sludge, wooden waste material, etc.    ADVANTAGE - The removal of hazardous component in reformed gas using caustic soda is prevented efficiently. The amount of oxygen supply in the reformer is reduced efficiently, while reducing the size of the reformed-gas processing apparatus of the reformer.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the electric power generation apparatus.    Recuperator (3)    Gasifier (22)    Reformer (24)    Gas-purification apparatus (25)    Gas engine (27)    Pyrolysis gas (b)
NOVELTY - A reforming portion (15) has tubular catalytic converter (15a) comprising substrate supporting catalytic component. The catalytic converter is arranged such that the center axis extends along the supply direction of the fuel and oxidizer. A communication passage (15b) is arranged along inner wall of the catalytic converter so as to communicate with supply portion. The fuel and oxidizer supplied from the supply portion to the communication passage is passed from the inner wall of the catalytic converter to outer wall for reforming the fuel.    USE - Fuel reformer for reforming fuel e.g. hydrocarbon fuel and light oil (both claimed) to produce hydrogen-rich gas, for fuel cell in internal combustion engine.    ADVANTAGE - The reforming efficiency of the fuel reformer can be improved without affecting the startability. The size of the fuel reformer can be reduced and fuel reformer can be manufactured at low cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a longitudinal sectional view of the fuel reformer.    Fuel reformer (10)    Fuel inlet portion (11)    Oxidizer inlet portion (12)    Reforming portion (15)    Catalytic converter (15a)    Communication passage (15b)
NOVELTY - Enhancing (M1) the production rate of at least one metabolite involves: a) oxidizing a carbon source with at least one microbe capable of fermentation in at least one compartment with at least one portal; and b) adding at least one electron acceptor to accept electrons from the at least one microbe after oxidation of the carbon source.    USE - For enhancing the production rate of at least one metabolite (comprising biofuel, brewed beverage, hydrogen, acetic acid, citric acid, lactic acid and alcohol) (claimed).    ADVANTAGE - The method improves the rate of removing excess electrons generated by microbial fermentation processes; and enhances the production rate of at least one metabolite by using a bacterial culture and further generates electricity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) generating (M2) current in a system that enhances the production rate of at least one metabolite involving: oxidizing a carbon source with at least one microbe capable of fermentation in at least one compartment with at least one portal; and adding at least one electrode to accept electrons from the at least one microbe after oxidation of the carbon source, where the at least one electrode comprises at least one anode connected to at least one cathode; and    (2) a system for enhancing the production rate of at least one metabolite having at least one compartment with at least one portal, comprising at least one microbe capable of fermentation, a carbon source, and at least one electron acceptor in the at least one compartment where the electron acceptor accepts electrons from the microbe capable of fermentation after the carbon source is oxidized.
NOVELTY - A hydrogen production apparatus (10) has a modifier (2) which modifies the hydrogen raw material to generate gas containing hydrogen, shift reaction device (3) which reduces the carbon monoxide concentration in the gas from the modifier by shift reaction, cooler (4) which cools the gas obtained from the shift reaction device, heating unit (5) which heats the gas cooled by the cooler, and selective oxidation reactor (6) which has selective oxidation catalyst layer filled with catalyst.    USE - Apparatus for production of hydrogen for fuel cell system (both claimed) used for motor vehicle, fixed electric power generation system and co-generation system.    ADVANTAGE - The hydrogen production apparatus enables easy control of moderate temperature of gas supplied to selective oxidation catalyst layer, without controlling flow of cooling medium. The fuel cell system is inexpensive and enables stable operation.    DETAILED DESCRIPTION - A hydrogen production apparatus has a modifier which modifies the hydrogen raw material to generate gas containing hydrogen, shift reaction device which reduces the carbon monoxide concentration in the gas from the modifier by shift reaction, cooler which cools the gas obtained from the shift reaction device, heating unit which heats the gas cooled by the cooler, and selective oxidation reactor which has selective oxidation catalyst layer filled with catalyst capable of accelerating selective oxidation reaction by which carbon monoxide is selectively oxidized for reducing carbon monoxide concentration in the gas heated by the heating unit. An INDEPENDENT CLAIM is included for fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows the flowchart of fuel cell system. (Drawing includes non-English language text)    Desulfurizer (1)    Modifier (2)    Shift reaction device (3)    Cooler (4)    Heating unit (5)    Selective oxidation reactor (6)    Hydrogen production apparatus (10)    Fuel cell (20)
NOVELTY - A fuel cell cabinet (900) liquid cooling system comprises a fuel cell, a liquid cooling system for dissipating heat generated by the fuel cell; and a controller that controls the liquid cooling system for maintaining a predetermined temperature range of a first cooling liquid of the fuel cell.    USE - A fuel cell cabinet liquid cooling system.    ADVANTAGE - The cooling system does not require timely service to prevent overflowing of the container or bucket used to capture the water thus reducing complexity of operating and managing the system.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a fuel cell cabinet (900) air feed system;    (2) fuel cell cabinet;    (3) a fuel cell cabinet heat management and thermal control system;    (4) a method of managing and controlling an internal air temperature of a fuel cell cabinet; and    (5) a fuel cell cabinet wastewater management system.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic partial view of a cabinet.    Fuel cell cabinet (900)    Pump assembly (904A)    Plenum (928)    Redundant pump (1102A)    Manifold (1110A)
NOVELTY - A supply pipe is connected to a high pressure air supply unit. A groove-shaped joint (11) accommodates the supply pipe between the surface layer materials (2). The surface layer materials are made of olefin rubber. The rear side of surface layer material is fixed on the floor surface using adhesive agent. A guard element is arranged between the surface layer materials.    USE - Apparatus for processing fermentation of to-be processed material such as livestock dung and organic refuse.    ADVANTAGE - The damage to the supply pipe can be prevented. The fermentation processing of to-be processed material can be performed stably over long period of time.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of the fermentation processing apparatus.    Surface layer materials (2)    Nozzle portion (4)    Nozzle hole (7)    Counter-bore hole (8)    Groove-shaped joint (11)
NOVELTY - Fuel cell (30) is manufactured by hydrogen treatment process which performs hydrogen processing before electric power generation of hydrogen separation membrane electrolytic membrane joined body (10) having proton conductivity provided on hydrogen separation membrane (12) which permeates hydrogen as a proton and/or a hydrogen atom.    USE - A manufacturing process for fuel cell (claimed).    ADVANTAGE - The interfacial removal of the hydrogen separation membrane and electrolytic membrane during electric power generation is suppressed.    DESCRIPTION OF DRAWING(S) - The drawing shows a process diagram of the manufacturing process of fuel cell. (Drawing includes non-English language text).    Hydrogen separation membrane electrolytic membrane joined body (10)    Hydrogen separation membrane (12)    Electrolytic membrane (14)    Cathode (20)    Fuel cell (30)
NOVELTY - The method involves filling conductive resin ink (22) in recess portion formed in metal substrate (21). The conductive resin ink filled in the recess portion is transferred to intaglio plate made of silicone resin.    USE - Method of manufacturing separator for fuel cell e.g. polymer type fuel cell, phosphoric acid type fuel cell, molten carbonate type fuel cell, solid oxide type fuel cell and alkali type fuel cell.    ADVANTAGE - The electroconductivity, corrosion resistance, mechanical strength and size reduction of the separator can be obtained easily and cheaply. The formation of recess portion can be performed easily.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the separator for fuel cell.    Metal substrate (21)    Conductive resin ink (22)    Concave groove A (23)    Concave groove B (24)
NOVELTY - Esterification of free fatty acid contained in a fatty substance, comprises (a) providing a fatty substance comprising 1-100 wt.% of fatty acid; (b) adding at least one alcohol and methane sulfonic acid; (c) conducting the esterification reaction at a temperature of 45-70 degrees C at a pressure of 1-5 atmospheres, preferably 1-2 atmospheres; (d) recovering the fatty substance containing less than 0.5 wt.% of free fatty acids, after separation of the esterification of alcohol and water.    USE - The process is useful for the esterification of free fatty acid to prepare the bio-diesel (claimed).    ADVANTAGE - The process is simple, efficient and easy to industrialize esterification.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a process for preparing bio-diesel, comprising: providing fatty substance comprising 1-100 wt.% of free fatty acids; adding alcohol and methane sulfonic acid; conducting esterification at 45-70 degrees C, at a pressure of 1-5 atmospheres, preferably 1-2 atmosphere; recovering the fatty substance comprising 0.5 wt.% of free fatty acids, after separating esterification alcohol and water; optionally filtering the product; adding basic catalyst and alcohol; conducting transesterification at 30-300 degrees C, at a pressure of 1-100 bars; and recovering, optional drying and filtrating of transesterified free fatty acid ester.
NOVELTY - An ethanol-containing raw material is passed through reaction temperature of 400 degrees C or more to noble metal supported catalyst having rhodium and/or ruthenium to the surface of inorganic oxide which is support to obtain methane-containing gas. The noble metal has dispersion degree of 25% or more. The ethanol-containing raw material contains ethanol and water vapor.    USE - Manufacture of methane-containing gas.    ADVANTAGE - The methane-containing gas is manufactured efficiently and economically using noble metal supported catalyst.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for catalyst for manufacturing methane-containing gas.
NOVELTY - The biomass gasification furnace has a top of sleeve type heat exchanger (3-1) which is set with a hot air or hot water outlet pipe (3-6). One side of the sleeve type heat exchanger is provided with an exhaust pipe for smoke (3-7). A super-conducting pipe is fixed on the bottom of vertical pipe of air or water passage and is situated inside and outside the air or water passage. A heat exchanging water jacket of flue is connected with a water jacket of gasification furnace (1-8) through the connecting pipe of water jacket.    USE - Biomass gasification furnace for generating hot air and hot water.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic perspective view of the biomass gasification furnace.    Furnace body (1-1)    Gasification furnace (1-8)    Sleeve type heat exchanger (3-1)    Hot air or hot water outlet pipe (3-6)    Exhaust pipe for smoke (3-7)
NOVELTY - Producing biodiesel comprises: (a) transesterifying triglycerides with methanol; (b) separating the obtained biodiesel and glycerin; (c) reacting a portion of the glycerin to 1-hydroxyacetone or acetone; (d) reacting a portion of the glycerin with the 1-hydroxyacetone or acetone to obtain (2-methyl-(1,3)dioxolan-4-yl)-methanol compound (I); and adding the obtained (I) to the biodiesel.    USE - The process is useful for producing the biodiesel and (I), which is useful as an additive for the biodiesel (all claimed).    ADVANTAGE - The process produces the biodiesel with reduced cost.    DETAILED DESCRIPTION - Producing biodiesel comprises: (a) transesterifying triglycerides with methanol; (b) separating the obtained biodiesel and glycerin; (c) reacting a portion of the glycerin to 1-hydroxyacetone or acetone; (d) reacting a portion of the glycerin with the 1-hydroxyacetone or acetone to obtain (2-methyl-(1,3)dioxolan-4-yl)-methanol compound of the formula (I); and adding the obtained (I) to the biodiesel.    R1 = H or OH.    INDEPENDENT CLAIMS are included for:    (1) the biodiesel produced by the above process; and    (2) producing (I) comprising reacting glycerin with acetone or 1-hydroxyacetone in a heterogeneous catalyzed reaction, where the catalyst is an inorganic-organic composite material.
NOVELTY - The reforming device (10) has a modification section (12) that generates reformed gas from the raw fuel. A steam supply unit (100) supplies steam into modification section. A heat exchanger (108) having cross sectional area larger than pipe vaporizes the water by exchanging heat with the hydrogen rich reformed gas that is generated when the raw fuel is burned.    USE - Reforming device for polymer electrode fuel cell.    ADVANTAGE - The water can be efficiently supplied to the modification section and water can be vaporized effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the reforming device. (Drawing includes non-English language text)    Reforming device (10)    Modification section (12)    Oxidation portion (16)    Steam supply unit (100)    Heat exchanger (108)
NOVELTY - A high pressure continuous reaction tower for biodiesel comprises a reaction tower main body, a heating inlet/outlet, and a raw material inlet/outlet; where the reaction tower main body is of sealed cylinder structure, where the bottom is provided with a heating inlet, and the top part is provided with a heating outlet; one side of the heating outlet of the top part is arranged with an expansion tank connected with the reaction tower via a safe valve; and the thick ascending tubes are arranged in the reaction tower, and the thin descending tubes are arranged correspondingly.    USE - The high pressure continuous reaction tower is useful for biodiesel (claimed).    ADVANTAGE - The high pressure continuous reaction tower has a pressure in the pipe that can reach to 35 MPa; thus, it obviously improves leak tightness and safety of the reaction tower, and provides high temperature resistance and low manufacture cost.    DETAILED DESCRIPTION - A high pressure continuous reaction tower for biodiesel comprises a reaction tower main body, a heating inlet/outlet, and a raw material inlet/outlet; where the reaction tower main body is of sealed cylinder structure, where the bottom is provided with a heating inlet, and the top part is provided with a heating outlet; one side of the heating outlet of the top part is arranged with an expansion tank connected with the reaction tower via a safe valve; the thick ascending tubes are arranged in the reaction tower, and the thin descending tubes are arranged correspondingly; a filler material is filled in the ascending tubes; one side of the heating inlet of the bottom of the reaction tower is provided with a raw material inlet connected with the ascending tubes of the reaction tower; and the raw material outlet at one side of the lower part of the reaction tower is connected with the descending tubes of the reaction tower.
NOVELTY - The furnace has a rotary taper (34) whose top part is connected with a lower section feed column (3). Top of a fixed taper (33) is connected with a fume pipeline (38). A combustion supporting air inlet is equipped at top of a furnace body (4). A fuel gas outlet (31) is located at an upper part of a fuel gas channel (9). A gas delivery pipeline (30) is connected with a gas storage cabinet through a draft fan (27). An upper section feed column (2) is screwed with the lower section feed column and fastened by locking screws.    USE - Internal combustion heating rotary tapered biomass gasification furnace.    ADVANTAGE - The furnace improves biomass gasification rate and heat value of fuel gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an internal combustion heating rotary tapered biomass gasification furnace.    Upper section feed column (2)    Lower section feed column (3)    Furnace body (4)    Fuel gas channel (9)    Draft fan (27)    Gas delivery pipeline (30)    Fuel gas outlet (31)    Fixed taper (33)    Rotary taper (34)    Fume pipeline (38)
NOVELTY - The device has a inlet pipe (4) inserted in filter liquid in a cylinder (1) after passing through a upper cylinder cover (2). A drain pipe interface (8) is placed on a lower cylinder cover (3). An end of a reflux sleeve (5) is fixed to the upper cylinder cover. Another end of the reflux sleeve is inserted in the filter liquid. An opening (6) is formed on the reflux sleeve, and an air outlet pipe (7) is inserted in the reflux sleeve by passing through the upper cylinder cover. An overflow device is mounted in the cylinder, and a shielding cap (10) is sleeved outside of an overflow pipe (9).    USE - Filter device for a biomass gasifier.    ADVANTAGE - The device processes a secondary filter to fuel gas to improve the filtering effect obviously. The overflow device provides good drainage effect to ensure the gas supply system of the gasifier to operate safely for long time. The shielding cap cuts off the fuel gas effectively to flow out of the cylinder by passing through the overflow pipe to perform gas water separating function. The device is simple in structure and convenient to operate, and has wide range of application.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a filter device for a biomass gasifier.    Cylinder (1)    Upper cylinder cover (2)    Lower cylinder cover (3)    Inlet pipe (4)    Reflux sleeve (5)    Opening (6)    Air outlet pipe (7)    Drain pipe interface (8)    Overflow pipe (9)    Shielding cap (10)
NOVELTY - Low-temperature industrial fuel is prepared from pine heavy oil by mixing pine heavy oil with organic solvents comprising methanol, ethanol and petroleum ether.    USE - Method of preparing low-temperature industrial fuel from pine heavy oil (claimed).    ADVANTAGE - The method reduces cost of industrial fuel oil, and enhances solidifying point of fuel oil so that it can be used at low temperature. The method has low energy consumption and is carried out at temperature and needs heat quantity that small boiler and water boiler are suitable to be used.
NOVELTY - High-temperature industrial fuel is prepared from pine heavy oil by blending pine heavy with organic solvents comprising methanol, ethanol and petroleum ether.    USE - Method of preparing high-temperature industrial fuel from pine heavy oil (claimed).    ADVANTAGE - The method reduces the cost of industrial fuel oil, and enhances solidification point of fuel oil so that it can be used at high temperature. The method requires temperature and heat quantity that sintering and smelting devices in small industries are suitable to be used.
NOVELTY - Medium-temperature industrial fuel is prepared from pine heavy oil by blending pine heavy oil with organic solvents comprising methanol, ethanol and petroleum ether.    USE - Method of preparing medium-temperature industrial fuel from pine heavy oil (claimed).    ADVANTAGE - The method reduces the cost of the industrial fuel oil and enhances solidification point of the fuel so that it can be used at medium temperature.
NOVELTY - A fuel pellet comprises a natural particulate cellulosic material; and a biosolid material made from a dried bioslurry effluent derived from fats, oils, and grease found in non-edible food residuals from sanitary sewer drainage (SSD); where the biosolid material and the cellulosic material are homogenous and particlized mixture and having 5-15 wt.% moisture and a particle size of a maximum of - 5 mesh before being pelletized.    USE - A fuel pellet.    ADVANTAGE - The fuel pellet resists crumbling, is easily ignitable, burns fast and completely, has a heating value approaching that of coal, and does not require high pelletizing temperature.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing a fuel pellet, comprising:    (A) providing particulate natural cellulosic material having greater than or equal to 5 wt.% moisture; providing a biosolid material made from a dried bioslurry effluent derived from fats, oils, and grease found in non-edible food residuals from SSD;    (B) preparing a homogenous mixture including the particulate cellulosic material and the biosolid material; and    (C) pelletizing the mixture by compressing and extruding.    DESCRIPTION OF DRAWING(S) - The drawing is a flow diagram of the method for manufacturing the fuel pellet.    Wash-up macerator (104)    Effluent discharge (106)    Sewer (112)    Recycle (114)    Plastic particulate (160)
NOVELTY - The straw carbonizing furnace has a furnace door that is installed at the front surface of a furnace body, while a chimney is set at the top of the furnace body. Both furnace body and furnace door are equipped with hollow cavities, which are linked to a water tank. The chimney is equipped with a fire-control regulating plate, which is connected to an operation handgrip installed on the furnace body through a connecting bar.    USE - Straw carbonizing furnace.    ADVANTAGE - Provides straw carbonizing furnace characterized by advanced rational structure, easy manufacturing, short producing period, high carbonizing quality, high product yield, and small amount of discharge flue gases.    DESCRIPTION OF DRAWING(S) - The drawing shows the cross sectional view of the straw carbonizing furnace.
NOVELTY - The straw gas making furnace has water grooves (3) that are formed at the circumference of a furnace body (6). A spherical gas vapor separation cover (2) occludes the upper surface of the furnace body, and having edges arranged in the water grooves. Gas collecting pipes (12) are provided at the bottom of the water grooves. A gas storage chamber (5) is formed under the water grooves.    USE - Straw gas making furnace used in house.    ADVANTAGE - Provides straw gas making furnace with simple structure, reasonable design, and high gas making efficiency. Enables producing gas with high purity. Ensures fast discharge of gas, thus shortening the gas production period.    DESCRIPTION OF DRAWING(S) - The drawing shows the cross sectional view of the straw gas making furnace.    Water grooves (3)    Gas storage chamber (5)    Furnace body (6)    Gas collecting pipes (12)
NOVELTY - A bio-crude has a total acid number (TAN) of less than 10, preferably less than 5, and a pH of greater than 3.5.    USE - Bio-crude for processing in conventional refinery equipment, stainless steel equipment (claimed) or carbon steel equipment.    ADVANTAGE - The bio-crude can be processed in conventional refinery equipment by themselves or blended with mineral crudes.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a process for preparing the bio-crude, comprising pyrolyzing a biomass material in the presence of a catalyst to form a bio-crude, and optionally reducing the TAN of the bio-crude by adding a base.
NOVELTY - Process for reducing the particle size of a biomass material, comprises: (a) providing a biomass material; (b) reducing the particle size of the biomass material; (c) mixing the biomass material with a fluidizable inorganic particulate material; and (d) subjecting the mixture to fluidization and/or flow conditions, where the particle size of the biomass material is reduced further.    USE - The process is useful for reducing the particle size of a biomass material. The process is useful for subsequent conversion of the biomass to liquid products, such as bio-oil.    ADVANTAGE - The process avoids the formation of catalyst fines, and allows for the capture of biomass fines. The process minimizes or avoids catalyst plugging and pressure drop build-up.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a composition comprising solid biomass particles/ligno-cellulosic particles coated onto inorganic particulate material.
NOVELTY - An integrated waste usage and energy, food and/or feed production system comprises anaerobic digester unit, liquid-solid separation unit, refinery unit, algae bioreactor unit, electricity generating unit (i.e. power plant), oil extraction unit, and optionally gasification unit connected to separator unit.    USE - An integrated waste usage and energy, food and/or feed production system for process where food or feed supplements from algae oil are made and for energy production.    ADVANTAGE - The system allows carrying out gasification instead of combustion, thus provides higher efficiency of conversion from biomass, and does not require elucidation. The system allows minimization of damage caused to the eco- and food chain systems.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for converting biomass particularly manure into useful end products comprising obtaining manure; subjecting manure to anaerobic digestion; obtaining gas output from anaerobic digestion; using the gas output for energy production; obtaining non-gas output (i.e. digestate) from anaerobic digestion; subjecting the non-gas output to separation of solids and liquid; optionally subjecting the obtained solids to gasification to obtain syngas and using gas for energy production; subjecting obtained liquid to refining step to obtain refined liquid; using the liquid to feed algae to obtain food and/or feed grade output from algae bioreactor; obtaining oxygen output from algae bioreactor; using oxygen output for energy production; obtaining algae output from algae bioreactor; subjecting the algae output to food grade oil extraction; obtaining algae oil as extract from oil extraction; using algae oil, e.g. in biodiesel, in feed supplement, or in food supplement; obtaining algae cake as residue from oil extraction, using the residue, e.g. in food and/or feed applications or in generation of bioethanol via carbohydrate fermentation.
NOVELTY - Method for preparing fertilizer, involves adding water in the prepared raw materials, uniformly agitating, passing the mixture in extrusion molding machine, and granulating to obtain fertilizer.    USE - The method is useful for preparing fertilizer (claimed).    ADVANTAGE - The fertilizer is prepared by a simple and cost-effective process. The method does not discharge harmful gas during granulation process and thus does not cause environmental pollution.
NOVELTY - A green project for intensively processing and recycling sewage and trash in village and town comprises fermentation vat as aerobic environment, warming dish, and large-scale greenhouse shed under a sealed environment. The sewage is discharged into the fermentation vat after being heated to 30 degrees C in the warming dish. The sewage after being heated is anaerobically fermented with the trash in the fermentation vat to produce methane. The fermentation vat has spiral machine for discharge. Straws and other plants can be also used as material besides the trash and mud.    USE - The green project is for intensively processing and recycling sewage and trash in village and town to produce methane through anaerobic fermentation. The methane is applicable for civilian use, industry or treatment process.    ADVANTAGE - The green project does not use mineral or electrical energy, and chemical agent; fully uses the organic material; has low investment for a time and long-term return; has little labor force, low operating cost, simple management, and no secondary pollution; and can be used for all geographical conditions and climate. The project can obtain clean methane with high heat productivity, which is suitable for industrial scale production and for biofuel factory. The sewage after processing can be discharged or it reaches the standard for agricultural use. The remaining trash can be reused again after ferment. The semi-clean water after fermentation by the anaerobic microbe is then discharged into the environment and further purified by the plant to reach the mark for exhaust and agricultural use.    DESCRIPTION OF DRAWING(S) - The drawing is a perspective view of the fermentation vat, warming dish and large-scale greenhouse shed used in green project for intensively processing and recycling sewage and trash in village and town.
NOVELTY - Biofuel is prepared from flue gas by cooling massive flue gas discharged from power plant and iron and steel factory, taking continuous carbon dioxide discharge source, performing photosynthesis with algae in water in a specially designed closed lighting bioreactor, absorbing carbon dioxide in algae and culture liquid, collecting and extracting material to obtain algal biofuel, and absorbing carbon dioxide from flue gas in bioreactor.    USE - Method of preparing biofuel from flue gas (claimed).    ADVANTAGE - The method reduces carbon dioxide in flue gas, thus reducing discharge of greenhouse gas to more than 40%. The method has low cost.
NOVELTY - A chemical mixture comprises chemicals for inhibiting production of methane gas and for concurrently inhibiting the production of hydrogen sulfide gas.    USE - Chemical mixture for controlling emission of biogases generated by biodegradable matter subject to undergoing anaerobic decomposition (claimed).    ADVANTAGE - The method reduces generation of selected environmentally undesirable and potentially harmful gases such as hydrogen sulfide.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for controlling emission of biogases generated by biodegradable matter undergoing anaerobic decomposition comprising applying a chemical mixture to the biodegradable matter.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross sectional view of the paper product.
NOVELTY - A module type trickling filter bioreactor comprises unit module(s) with box structure and a water distributing device. The sidewall and bottom of the unit module are opened with holes; and the unit module is filled with filler. The unit modules are superposed on one another to form an integral reactor body. The water distributing device is provided above the unit module located in the uppermost layer of the reactor body.    USE - Module type trickling filter bioreactor for sewage disposal.    ADVANTAGE - Because the module type trickling filter bioreactor uses the structure of combined unit modules, the processing unit can be assembled and enlarged flexibly according to the quantity of sewage to be treated, thus the cost of the bioreactor is reduced and the handling capacity is improved. The bioreactor is simple and convenient to construct and maintain.
NOVELTY - A biochemical multiple-purpose industrial production line comprises livestock feces and straw tanks (1, 2), bacterial fermentation tanks (3, 4, 5, 6), material separator (7, 8), and product deep processor (9, 10). The livestock feces and straw are processed by mixing feces and straw, then passing to bacterial fermentation tanks for fermentation, then passing through material separator, and deeply processing the separated products to obtain methane, biofertilizer and feed.    USE - A biochemical multiple-purpose industrial production line for livestock feces and straw for preparing methane, biofertilizer and feed.    ADVANTAGE - The industrial production line is advanced, fully automated, has high efficiency, and does not produce environmental pollutant.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a biochemical multiple-purpose industrial production line.    Livestock feces and straw tanks (1, 2)    Bacterial fermentation tanks (3, 4, 5, 6)    Material separator (7, 8)    Product deep processor (9, 10)
NOVELTY - An organic fertilizer is produced by mixing rice hull and fowl manure, adjusting water content of the mixture, adjusting pH value, and fermenting; diluting an acidic cellulose with water, spraying the solution to rice hull and fowl manure mixture, and fermenting; inoculating biological leavened food, fermenting, and adding trace element fertilizer and urea; and increasing fermentation temperature and drying.    USE - Method of producing an organic fertilizer (claimed) for promoting plant growth, improving photosynthetic efficiency of plant, or reducing incidence rate of plant diseases and insect pests.    ADVANTAGE - The method activates soil thus improving quality and output, reduces usage of agricultural chemical and chemical fertilizer, and decreases environmental pollution.    DETAILED DESCRIPTION - An organic fertilizer is produced by:    (A) mixing (wt.%) rice hull (50-59) and fowl manure (35-40), adjusting water content of the mixture to 40-45%, adjusting pH to 5.5-6.5, and fermenting;    (B) diluting an acidic cellulose with water to obtain a solution having a concentration 0.03 g/l, spraying the solution (10 l) to rice hull and fowl manure mixture, and fermenting at higher than 20 degrees C for 3-5 days;    (C) inoculating biological leavened food (0.1 wt.% of mixture), fermenting for 20-30 days, turning the fermented materials for 8-10 times, and adding (wt.%) trace element fertilizer (0.8-1) and urea (0.1-0.2); and    (D) increasing fermentation temperature to 72 degrees C, and drying to adjust water content to below 20%.    The fowl manure is chicken of duck manure. The trace element is zinc sulfate, borax or copper sulfate. An INDEPENDENT CLAIM is included for organic fertilizer comprising (wt.%) chicken manure (35-40), rice hull (50-59), aerobic zymogen-thermophilic Bacillus (0.08-0.1), trace element fertilizer (0.8-1), urea (0.1-0.2), and acidic cellulose (0.08-0.1).
NOVELTY - A multifunctional soil conditioner comprises fermented organic waste, water, nitrogen fertilizer, modified chitosan solution and polyacrylamide.    USE - A multifunctional soil conditioner for Chinese medicinal plant and vegetable.    ADVANTAGE - The conditioner increases the use of parent bagasse and polyacrylamide which has effective water and fertilizer retention; and provides short growth period, increased yield, reduced fertilizer dosage and improved crop quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of preparing multifunctional soil conditioner by pre-drying bagasse and waste bacteria bag, controlling nitrogen fertilizer of 0.5-5% and water of 50-70%, and performing natural pile fermentation to obtain carbon/nitrogen (C/N) at ratio of 20-50; and mixing fermented organic waste with 0.1-1% modified chitosan and polyacrylamide to mass ratio of 1:0.5-5:0.01-0.05.
NOVELTY - Urban household ecological energy pot comprises ecological flushing-free toilet, throwing port for kitchen domestic garbage, ferment gas storing pot, pressure limiting gas leading device and waste discharging device.    USE - Urban household ecological energy pot used for handling urban domestic garbage and feces, generating clean combustive energy gas by fermenting of microorganism and providing fuel gas for urban households (claimed).    ADVANTAGE - The urban household ecological energy pot can reduce discharging of the pollution by urban households and uses pollutant and living waste as resources, thus saving energy and expenditure of household consumption and reducing discharging and pollution. The bulk and shape can be selected according to situation in the washroom, the size of population and the usage condition of the fuel gas. There is no pollution and the energy pot is safe and reliable.    DETAILED DESCRIPTION - Urban household ecological energy pot comprises ecological flushing-free toilet, throwing port for kitchen domestic garbage, ferment gas storing pot, pressure limiting gas leading device and waste discharging device. The energy pot is produced by plastic steel integrative molding with intellectualized operation, toilet connected to ferment gas storing pot in air-proof way; setting ferment gas storing pot at lower part of the pot and setting gas storing room on upper part of the pot; discharging waste residue and liquid periodically by control valve to sewer directly; leading combustive gas in gas storing pot by top gas-guide tube; and providing top with manometer and pressure limiting valve, observing pressure in pot and discharging gas when pressure beyond the limited value.
NOVELTY - An organic fertilizer composition comprises (wt.%) organic fertilizer (45-60), urea (15-20) containing 46% of nitrogen, potassium sulfate (10-15) containing 52% of potassium oxide, and calcium-magnesium phosphate fertilizer (13-20) containing 12% of phosphorus pentoxide.    USE - An organic fertilizer composition for tea oil Camellia (claimed).    ADVANTAGE - The organic fertilizer composition is environmentally friendly, has simple ingredients, can balance nutrition and promote growth of tea oil Camellia, and can reduce soil hardening.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of organic fertilizer composition comprising:    (A) adding poultry manure to a fermentation strain, sufficiently mixing and fermenting for 30-40 days while turning fermentation material every 6-8 days to obtain a completely fermented organic fertilizer; and    (B) uniformly mixing completely fermented organic fertilizer with urea, potassium sulfate and calcium-magnesium phosphate fertilizer to obtain organic fertilizer composition.
NOVELTY - A fuel ethanol is prepared by cutting, drying, crushing, and passing bamboo processing waste through a sieve of 80 meshes, in which the powder that passes through the sieve is taken as fine bamboo powder and other powder that does not pass through the sieve is taken as coarse bamboo powder; cooking coarse bamboo powder to hydrolyze hemicellulose, to remove lignin, and to separate out cellulose; hydrolyzing separated cellulose using an organic acid; hydrolyzing fine bamboo powder using organic acid; and fermenting reducing monosaccharide obtained by hydrolyzing after subjecting to detoxication.    USE - Method for preparing fuel ethanol for producing reducing sugar (claimed).    ADVANTAGE - The method provides high yield of ethanol fuel and reduced energy consumption of hydrolysis. Inorganic acid for hydrolyzing can be recycled. Dosage of water is less, such that environmental pollution is reduced, and cost is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a reducing sugar obtained by the method of preparing ethanol fuel in which detoxication is carried out by using excessive calcium hydroxide whose pH is regulated to 9-10, and then regulated back to 5.5 by using sulfuric acid.
NOVELTY - This invention provides processes for making organic fertilizer by excrement of pig, which comprises: a) supplying gem stone treated water to feed pigs activate microbes in pig's intestines so that pigs release odorless excrement; b) manufacturing compost through a blending of pig excrement and wood, sugar can dregs and rice bran; c) agitating homogeneously; d) adding water in compost to reach 70% water content; e) speeding up fermentation and anti-odor by adding anaerobic bacteria; f) adjusting pH value to 7; g) packing in bag for the purpose of stacking fermentation; h) after completing fully fermentation, removing impurities and making pellet to produce organic compost. The invented process can prepare high quality organic compost without odor and poison from pig excrement.
NOVELTY - Bacillus pumilus strain BI-10 has an accession number KCTC 11149BP, and is new.    USE - Bacillus pumilus strain BI-10 for use in promoting initial proteolysis of organic compound in soil.    ADVANTAGE - The Bacillus pumilus strain increases the productivity of nitrates, and shortens the stabilization or mineralization period of the organic compound.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for processing Bacillus pumilus strain BI-10, which involves reducing the mineralization period of the organic compound in the soil.
NOVELTY - A biological straw material is pre-treated by physical and biological method, mixed with fermenting strain, provided into anaerobic fermenting reactor and subjected anaerobic reaction to obtain marsh gas. The obtained marsh gas is subjected decarbolizing treatment, introduced into marsh storing device and conveyed to users through conveying pipe net. The marsh dreg and marsh liquid are discharged from anaerobic reactor through physical separation. The obtained marsh liquid is used in backflow of anaerobic fermenting reactor.    USE - Method for preparing marsh gas.    ADVANTAGE - The method easily provides marsh gas in short time. The marsh dreg obtained by the method is used as solid organic fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for device for preparing marsh gas, which contains transversely anaerobic fermenting reactor including stirring device in which turbine-shaped vane stirring device is fixed to rotating shaft.
NOVELTY - Biogas tank comprises a biogas generation tank and a gas storage tank and is designed in the form of cylinder. The middle upper part of the biogas tank is provided with an automatic liquid drain pipe device, while the bottom part is provided with 45 degrees angle taper. A feed hole and discharge hole are provided, which oppositely form slope of 15 degrees . A central rolling shaft of the drain blockage device is located on the discharge hole, and is a reversing concave channel.    USE - Biogas tank for producing biogas in urban areas by using human excrements and vegetable leaf residues.    ADVANTAGE - The biogas tank is automated and suitable for the urban areas.
NOVELTY - An improved bottom dry seal type carbonizer cum gasifier for converting the solid biomass to gaseous fuel through thermochemical conversions biomass is held in the gasifier by means of a flat grate and during pyrolisis, a self-sustained high temperature zone is maintained inside the reduction zone. Image 0/0
NOVELTY - A bio film support, which is a specially designed carrier material for supporting microbial growth useful in the biological treatment of wastewater. The carrier material has an inner twisted double helical structure which is enclosed in a spherical enclosure with flow through passages, designed to allow good flow of wastewater through the microbial film having been established on the surfaces. The carrier material permits formation of bio film on its surface and thus enhances the growth of biomass in the reactor and also increases the treatment efficiency. Each support is made of synthetic material, preferably polyvinyl chloride and polyethylene having a dimension of 25 mm in diameter and bulk density of 1.0-1.3 g/cm^3. The total surface area of each carrier material is larger than 0.4 m^2, preferably 0.6 m^2. The biofilm support having higher surface area helps in the colonization of heterotrophic bacterial population in the bioreactor for the removal of organics and nutrients in the wastewater. Image 0/0
NOVELTY - An eco-friendly system for generating thermal energy from waste biomass, comprising- (i) a furnace (2) capable of generating and withstanding high temperature, round or tetragonal at the bottom and tapering at the top assuming a conical shape and fitted at the top with a pipe (2A); (ii) a set of boiler tube(s) (1) placed on the top of the furnace; (iii) a rectangular or tubular structure (1A) housing the boiler tube and the furnace, the structure having insulated wall (13) to prevent dissipation of heat; (iv) an outlet (18) for the flue gases leading to a cyclone (3) equipped with means for spraying water or wet steam (12), the cyclone carrying a tubular body (3A) for leading away a part of flue gases and fitted with a butterfly control valve (5) for regulating flow of effluent gases; (v) a tubular body connecting the body to the suction blower (4) with a connection at the bottom of the furnace for blowing air/hot gases inside the burner zone of the furnace; (vi) a water tank (6) in which the downpipe of the cyclone is kept submerged in water for trapping particulate matter carried by the effluent gases from the furnace; (vii) a hopper (8) for waste biomass used as fuel fitted with a fuel flow control device (7), from which the fuel is released onto an endless conveyor belt (9) for being led to the furnace gate (15) with the help of suction point of blower and (viii) a fuel injection blower (10) for introducing fuel inside the furnace by means of pressurized air jet blown through the pipe (11). The present invention also deals with a process for generating thermal energy and the accompanying illustrates the invention. Image 1/1
NOVELTY - The degumming of decorticated ramie fibers by biochemical method, is disclosed. The Ramie occupies prime position due to its fiber high strength, luster durability and resistance to microbial attack. The fibers consist of long thick walled cells cemented together with non-cellulosic material is termed as gummy materials. The degumming involves cooking the decorticated fiber bundles in water containing sodium hydroxide at 160?oC for 4 hours or with sodium hydroxide, sodium sulfite, ethylene diamine tetraacetic acid at 120?oC for 2 hours. The process is an energy intensive process and discharges effluents. The process describes a biochemical method of treating the decorticated fibers bundles at room temperature under anaerobic condition for 48 hours followed by boiling in dilute alkaline water 100?oC for 30 minutes. The wash water containing gummy materials is processed for the production of biogas such that fiber having softer feel with higher strength elongation is obtained efficiently. Image 0/0
NOVELTY - The stove is provided to gasify and combust solid biomass such as biomass briquettes and further combust the charcoal thus only ash remains and leaves to water filled ash pot. The stove is provided for thermal energy application for various usages like cooking food, making sweets, making namkeen, generating steam for thermal use or generating electricity. The stove is used for economical replacement of fossil fuel like coal, coke, liquefied petroleum gas (LPG), diesel and natural fuels like charcoal and wood, etc. The biomass is combusted in to double jacketed combustion chamber made of stainless steel or mild steel and having numbers of holes to provide secondary and primary air thus to attain maximum retention time and combustion of volatiles and char of biomass. The ash is taken out without the disturbance in cooking with the help of ash drawer to ash pot from ash draw gate. Image 0/0
NOVELTY - A novel supported composite membrane for gas separation is disclosed. The gas separation membrane is formed on a porous ceramic support. The membrane layer comprises polymer matrix with mesoporous silica dispersed in the matrix. The alumina containing mesoporous material of MCM41 family is uniformly dispersed in hydroxyethylcellulose membrane layer, and increased the selective permeation of carbon dioxide through the composite membrane. The membrane layer formed on silicon carbide supports showed carbon dioxide/nitrogen selectivity of 50 and carbon dioxide/methane selectivity of 46. Image 0/0
NOVELTY - A processing method of organic sludge involves additive addition process (2) which adds additive with calcium oxide as main component to organic dewatered sludge and mixing, viscous adjustment process (3) which carries out predetermined time leaving-to-stand of organic dewatered sludge after addition of additive and adjusting viscosity of organic dewatered sludge, and formation process (4) which molds organic dewatered sludge that became predetermined viscosity through viscous adjustment process to defined shape.    USE - A processing method of organic sludge.    ADVANTAGE - The method suppresses increase of the amount of ash content when burning part and solid fuel manufactured from organic dewatered sludge.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of processing method of organic sludge. (Drawing includes non-English language text).    Dehydration process (1)    Additive addition process (2)    Viscous adjustment process (3)    Formation process (4)    Drying process (5)
NOVELTY - The de-sulfuring apparatus has a heat exchanger (122) that performs heat-exchange between de-sulfurized liquid fuel which flows out of a desulfurizer (121), and liquid fuel such as kerosene supplied to the desulfurizer by a liquid fuel supply unit (110). A heater (122B4) is provided in a distribution channel (122B), and heats the de-sulfurized liquid fuel that is heat-exchanged and flows into a buffer tank (123).    USE - De-sulfuring apparatus for fuel gas production apparatus of fuel cell system (all claimed) used for producing electric power.    ADVANTAGE - Ensures stable supply of liquid fuel, while ensuring efficient desulfurization process. Prevents generation of pulsating current during liquid fuel supply process without enlarging the capacity of the buffer tank. Ensures favorable and efficient generation of electric power by stabilizing the ratio of fuel gas and oxygen containing gas.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a desulfurization method;    (2) a production apparatus of fuel gas for fuel cells; and    (3) a fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of the de-sulfuring apparatus. (Drawing includes non-English language text).    Liquid fuel supply unit (110)    Desulfurizer (121)    Heat exchanger (122)    Distribution channel (122B)    Heater (122B4)    Buffer tank (123)
NOVELTY - A waste oil emulsion fuel generating apparatus has a fuel mixing apparatus (51) mixing together the waste edible oil, fuel oil, water, and emulsifier transferred from a fuel transfer installation (3) to produce emulsion fuel to be transferred to a diesel engine electric power generating apparatus (1). The diesel engine driving state of the electric power generating apparatus is monitored. Based on the monitoring result, a mixing control apparatus (6) computes and controls the fuel volume allocation of the waste edible oil, fuel oil, water, and emulsifier.    USE - Waste oil emulsion fuel generating apparatus e.g. for use in diesel engine electric power generation system, as well as in waste edible oil emulsion fuel utilization power generating plant system.    ADVANTAGE - Allocation of flow volume of waste edible oil, fuel oil, water, and emulsifier to be supplied to mixing apparatus can be computed and controlled based on diesel engine operating state, improving combustion efficiency and exhaust gas property.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of a waste edible oil emulsion fuel utilization power generating plant system. (Drawing includes non-English language text).    Diesel engine electric power generating apparatus (1)    Fuel supply installation (2)    Fuel transfer installation (3)    Mixing control apparatus (6)    Fuel mixing apparatus (51)
NOVELTY - The method involves providing fuel electrode side catalyst layer (4a) on the surface of a polymer electrolyte membrane (1). A catalyst layer (4b) provided with an oxidizing agent electrode side catalyst layer precursor (4b'), is arranged on the other surface of the polymer electrolyte membrane. The oxidizing agent electrode side catalyst layer precursor is made of carbonaceous material and polyelectrolyte resin. The electric potential of more than 1.0 volts is applied to the oxidizing agent electrode side catalyst layer precursor.    USE - Manufacturing method of fuel cell (claimed) such as solid polymer electrolyte type fuel cell.    ADVANTAGE - The drying of the electrode and polymer electrolyte membrane can be suppressed effectively. The fuel cell with high electric power generation performance and reduced weight can be manufactured reliably.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view illustrating the manufacturing process of fuel cell.    Polymer electrolyte membrane (1)    Fuel electrode side catalyst layer (4a)    Oxidizing agent electrode side catalyst layer (4b)    Oxidizing agent electrode side catalyst layer precursor (4b')    External power supply units (9,9')
NOVELTY - A low molecular weight electrolyte layer containing a polyelectrolyte is formed on the surface of an electrolytic membrane containing a polyelectrolyte. The equivalent weight (EW) values of polyelectrolytes in the low molecular weight electrolyte layer and the electrolytic membrane are made to differ within 10%. The hot pressing operation is performed for a laminated structure containing the electrolytic membrane, low molecular weight electrolyte layer and an electrode.    USE - Membrane electrode assembly (MEA) manufacturing method for fuel cell e.g. polymer electrolyte fuel cell.    ADVANTAGE - The adhesiveness of the electrolytic membrane and the electrode is improved by suppressing the generation of stress and increase of contact resistance between the electrolytic membrane and the low molecular weight electrolyte layer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell membrane electrode assembly.    DESCRIPTION OF DRAWING(S) - The drawing shows the flowchart explaining the MEA manufacturing method.(Drawing includes non-English language text)
NOVELTY - The system has fuel cell (7) driven in the temperature that evaporates the cooling water circulating in a cooling water system (9). A vapor splitter (30) isolates the produced water vapor from the cooling water. The water vapor supply system (35) is arranged to mix the isolated water vapor with the source gas. The mixture of isolated water vapor and supply gas is supplied to an internal heating type modifier (1) that generates reformed gas containing hydrogen. The anode waste gas is supplied to thermal load installation such as biomass ethanol production facility.    USE - Solid polymer electrolyte fuel cell system for thermal load installation such as gas heat pump type air conditioning equipment, absorption-type gas air conditioning equipment and biomass ethanol production facility (all claimed) and for household application.    ADVANTAGE - The thermal efficiency of the fuel cell system is improved by the efficient arrangement of modifier and fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of fuel cell system.(Drawing includes non-English language text)    Internal heating type modifier (1)    Fuel cell (7)    Cooling water system (9)    Vapor splitter (30)    Water vapor supply system (35)
NOVELTY - The gas tester (10) has a solid light-emitting device (1) for irradiating light to the detection object gas, and a gas introducing unit (2c) for introducing the detection object gas between the primary and secondary elements (2a,2b). A pair of fiber Bragg lattices (FGB) (2,3) radiates a portion of reflected light from the secondary element while selectively performing continuous reflection of the light corresponding to the absorption wavelength of detection object gas between the primary and secondary elements.    USE - Gas tester e.g. infrared absorption type gas tester for detecting concentration of compound gas such as methane gas and carbon monoxide gas, and for use in fire alarm system.    ADVANTAGE - The detection object gas can be detected with high precision, and the size and weight of the tester can be reduced. The lifetime of the gas tester can be extended and the reliability of the tester can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the gas tester.(Drawing includes non-English language text)    Solid light-emitting device (1)    FGB (2,3)    Primary element (2a)    Secondary element (2b)    Gas introducing unit (2c)    Gas tester (10)
NOVELTY - The method involves arranging electrode (20) on surface of a metal support structure (10) having high gas permeability property. An oxide electrolyte (30) is arranged on the other surface of the metal support structure. The metal support structure is planarized by sintering the oxide electrolyte.    USE - Manufacturing method of fuel cell e.g. polymer electrolyte fuel cell and solid oxide fuel cell.    ADVANTAGE - The crack initiation of the oxide electrolyte can be suppressed reliably. The volumetric shrinkage at the time of sintering the oxide electrolyte is absorbed effectively by the contraction of the convex surface of the metal support structure. The electronic conductivity fall of the cathode electrode resulting from the crack generation can be suppressed efficiently.    DESCRIPTION OF DRAWING(S) - The drawings show the cross-sectional views illustrating the manufacturing process of fuel cell. (Drawing includes non-English language text)    Metal support structure (10)    Electrode (20)    Oxide electrolyte (30)    Cathode electrode (40)    Fuel cell (100)
NOVELTY - The method involves producing a micropassage between two main surfaces in an impermeable support (2) e.g. substrate, that is traversed by the micropassage. A main surface (2a) is brought in contact with an aqueous solution comprising suspension particles. Application of pressure (P) is applied between a fabric (4) and the surface (2a) of the support and a relative movement of the fabric and of the surface are simultaneously performed for introducing spherical particles (5) forming porous material in each micropassage. Permeable proton conducting layer is formed on one of the surfaces.    USE - Method for producing a porous membrane (claimed) that is used in a fuel cell.    ADVANTAGE - The method produces the porous membrane in an easy manner, and increases contact surface to slow down the flow of particles around the micro passages to increase efficiency of the membrane. The pressure applied on the particles causes sintering of the particles to improve mechanical resistance of the micropassage assembly. The micropassage contains particle and 50 percentage porosity if the particles have diameters equal to that of the micropassage, thus adjusting porosity by controlling the size of particles in the micropassage.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional schematic view illustrating steps of a method for producing a porous membrane.    Pressure (P)    Support (2)    Main surface (2a)    Maintain layer (3)    Fabric (4)    Particles (5)
NOVELTY - The method comprises mixing a fiber containing raw materials such as mixed fodder, wood, straw, bituminous peat or like with water, steam and further additives in a press- or expander plant under heating of the raw materials and additives. The mixture is held in an intermediate container (4) before pressing over long time at 150 degrees C and defined humidity and is uniformly dosed in the press. The raw material is added to additional fat and/or lignin. The conditioning is carried out in pressure free manner or in over pressure.    USE - Method for the production of pressed products from fiber containing raw materials in a press- or expander plant.    ADVANTAGE - The method ensures economical and rapid production of pressed products from fiber containing raw materials with high throughput and less energy consumption per ton of pellets.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for producing pressed products from fiber containing raw materials.    DESCRIPTION OF DRAWING(S) - The figure shows a principle representation of a device for the production of pressed products from fiber containing raw materials.    Mixer (2)    Intermediate container (4)    Canal (6)    Product supply opening (7)    Product discharge opening. (8)
NOVELTY - A catalyst (C1) used in transesterification of short chain alcohols with vegetable and animal oils, crude or refined oil, waste vegetable oils comprises as base: alkali hydroxides or alkali methoxides, soil alkali hydroxides or soil alkali metoxides; as alcohol: short chain alcohols like methanol, ethanol, isopropyl alcohol, n-propyl alcohol, butanol; as polyelectrolyte gel: nonionic, anionic and cationic polyelectrolyte gel.    USE - In transesterification of short chain alcohols with vegetable and animal oils, crude or refined oil, and waste vegetable oils (claimed); in fatty acid methyl ester production; in biodiesel production technologies.    ADVANTAGE - The homogeneous alkali polymeric gel catalyst (HAPJEK) is simple; provides shorter transesterification time, rapid transterification reaction, rapid precipitation of glycerine after transestrification and does not require neutralization and washing; low cost product and comprises utilization of polyelectrolyte gel in fatty acid alkyl ester production with heterogeneous catalyst.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) producing homogenous catalyst (C1) involving mixing sodium hydroxide (NaOH) or potassium hydroxide (KOH), alcohol and polyelectrolyte gel in reactor (5a); and    (2) producing heterogeneous catalyst involving providing rapid precipitation of glycerine, neutralization of heterogeneous catalyst released into the reaction media and utilization of polyelectrolyte gels together with heterogeneous catalysts to remove from the reaction media.    DESCRIPTION OF DRAWING(S) - The figure shows two stages HAPJEK production.    Potassium hydroxide tank (1)    Alcohol tank (2)    Gel tank (3)    , (5b) Reactors (5a)    Stirred reactor (6) Storage tank (5c)
NOVELTY - The processing apparatus has a waste food electrolytic cell (100). An automatically operated recycling thickener (200) and a water level control sensor (231) are connected to a heater (233). Ferric chloride solution paths (21,22) and water separation spaces (18,19) are formed in the electrolytic cell. Upper side of the electrolytic cell is closed hermetically for preventing out flow of vacuum pressure. A mixing gas chamber (3) is provided for collecting methane and ammonia gases generated by electrolysis process of oxygen and hydrogen in the electrolytic cell.    USE - Processing apparatus.    ADVANTAGE - The upper side of the electrolytic cell is closed hermetically for preventing out flow of vacuum pressure, and hence produces pollution-free clean energy, and ensures complete recycling of the waste food.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a waste food processing apparatus.    Mixing gas chamber (3)    Water separation spaces (18,19)    Ferric chloride solution paths (21,22)    Electrolytic cell (100)    Recycling thickener (200)    Water level control sensor (231)    Heater (233)
NOVELTY - Upward flow anaerobic sludge blanket (UASB) reactor has porous carrier useful for immobilizing microorganisms, is fixed to a reactor main body (25).    USE - The UASB reactor is useful in biological nitrification denitrifying apparatus (claimed) for removing nitrogen from waste water using microorganisms.    ADVANTAGE - The microorganisms can be immobilized easily and nitrogen from the sludge can be removed efficiently. The carrier does not interfere with fluidization of granule sludge after the formation of granule sludge, as carrier is attached to the intermediate portion of the reactor main body. As biological nitrification denitrifying apparatus is equipped with UASB reactor, the apparatus is driven steadily and rapidly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biological nitrification denitrifying apparatus, which consists of UASB reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of upward flow anaerobic sludge blanket (UASB) reactor.    UASB denitrifying column (20)    Granule sludge (21)    Sponge carrier (22)    Reactor main body (25)    Sponge (29)
NOVELTY - A growth promotion agent contains trivalent ferric iron.    USE - Growth promotion agent of denitrifying bacteria is used for device for treating wastewater (both claimed).    ADVANTAGE - The growth promotion agent improves denitrifying activity of denitrifying bacteria efficiently, and denitrifying bacteria denitrify wastewater efficiently. The discharge amount of nitrous oxide on wastewater treatment is reduced, using the growth promotion agent.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) wastewater treatment equipment (100), which has a denitrifying tank (10) which reduces nitrate ion and/or nitrite ion to nitrous oxide and/or nitrogen by introducing denitrifying bacteria to wastewater containing nitrate ion and/or nitrite ion and a growth promotion agent supply unit (20) to supply growth promotion agent of denitrifying bacteria containing trivalent ferric iron to the denitrifying tank;    (2) wastewater treatment, which involves reducing nitrate ion and/or nitrite ion to nitrous oxide and/or nitrogen by introducing denitrifying bacteria to wastewater containing nitrate ion and/or nitrite ion in denitrifying tank and proliferating denitrifying bacteria in denitrifying tank in presence of growth promotion agent; and    (3) anti-microbial agent, which contains chelating agent of trivalent ferric iron.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the wastewater treatment equipment. (Drawing includes non-English language text)    Denitrifying tank (10)    Growth promotion agent supply unit (20)    Wastewater treatment equipment (100)
NOVELTY - The method involves removing ammonia nitrogen so that ammonia-nitrogen concentration in waste water of methane fermentation treatment completed in methane fermentation facility (1) is set to equal to or less than 0.1kg. The dissolved substance contained in waste water is solidified to solid substance for filter process while decreasing temperature of exhaust gas, after removal of ammonia nitrogen.    USE - Processing method of general waste e.g. domestic wastes such as human waste, livestock excrements, food-processing waste material and industrial wastes such as organic refuse, wood, processing-of-marine products waste material and plastics.    ADVANTAGE - The waste material can be processed without generation of odor and smoke, and the quantity of water to-be-sprayed is reduced. Thus the effective usage of biomass is stimulated.    DESCRIPTION OF DRAWING(S) - The drawing shows a block flow diagram illustrating the processing method of general waste. (Drawing includes non-English language text)    Methane fermentation facility (1)    Ammonia nitrogen removal facility (2)    Apparatus for decreasing temperature (5)    Incineration facility (6)    Melting facility (8)
NOVELTY - A hydrogen-containing gas utilization system has a hydrogenation apparatus (1) and an electric power generating apparatus (3). An aromatic hydrocarbon is hydrogenated using a hydrogen-containing gas, and a portion of the gas in the hydrogenation reaction product is supplied to the electric power generating apparatus.    USE - Utilization system of hydrogen-containing gas discharged from petroleum refinery, iron mill and biomass-waste gasifier, used in home, building, office and electrical vehicle.    ADVANTAGE - The utilization system utilizes other gas with high energy efficiency. The hydrogen which utilizes heat generated by electric power generation in modification of hydrocarbon is reduced, and hence the electric power generation efficiency is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the hydrogen-containing-gas utilization system. (Drawing includes non-English language text)    Hydrogenation apparatus (1)    Gas-liquid separation apparatus (2)    Electric power generating apparatus (3)
NOVELTY - A multi-functional direct combustion biomass superconductive gasification furnace comprises smoke baffle, ondol connecting hole, smoke cylinder opening, water outlet, thermal tube, gasifier in furnace door, fire cover, gasifier in furnace girder, gasifier in hearth, front ventilation regulating door, two lateral ventilation regulating holes, ash outlet, reversing grate, furnace body and pedestal.    USE - A multi-functional direct combustion biomass superconductive gasification furnace for cooking, heating, heat supply and washing.    ADVANTAGE - The multi-functional direct combustion biomass superconductive gasification furnace saves energy and half of fuel relative to general furnace, and has no smoke, high efficiency, very high thermal value, fast heat conduction, high heat conduction speed and good heat supply effect.
NOVELTY - A cellulose ethanol based clean fuel comprises (in weight parts) additive (0.5-3) and gas part oil (84.5-7), ethanol (15-90) where ethanol contains M15-M90 methanol. The additive comprises latent solvent (20-40), distillation range regulator (40-60), power performance energizer (5-10), combustion improver (0.01-0.2), low temperature promoter (1-5), corrosion prevention anti-swelling agent (0.4-1), chemical inhibitor (0.05-0.1) and inhibitor (5-19).    USE - Cellulose ethanol based clean fuel for automobile i.e. car.    ADVANTAGE - The fuel has low calorific value, and improves the dynamic performance of the engine, and saves energy. The fuel is cost-effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing cellulose ethanol based clean fuel.
NOVELTY - A platinum carrying carbon comprises platinum particles or its alloy particles supported on a surface modified carbon material. The surface modified carbon material comprises carbon material surface modified using organic group and has peak half value width, derived from (002) plane of 6 degrees or less in terms of angle 2 theta between an incident X-ray and reflective X-ray, measured by powder X-ray diffractometry.    USE - Platinum carrying carbon is used for catalyst for electrode film assembly for fuel cell (all claimed).    ADVANTAGE - The platinum carrying carbon has high dispersion, and provides the catalyst having high catalyst utilization factor, fuel cell having excellent battery characteristics and durability and electrode film assembly having excellent oxidation corrosion resistance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for electrode film assembly (10), which has solid polymer electrolyte membrane and catalyst layer provided in contact with film of solid polymer electric charge. The catalyst layer contains catalyst containing platinum carrying carbon.    DESCRIPTION OF DRAWING(S) - The drawing shows sectional view of structure of electrode film assembly.    Electrode film assembly (10)    Polymer electrolyte membrane (11)    Anode electrode (12)    Cathode electrode (13)    Cathode pole catalyst layer (13b)
NOVELTY - Microbial fuel cell, contains external circuit and pair of electrode. The circuit is connected to the electrode pair. The cathode contains agglomerate that has a three-dimensional structure in solution containing electroconductive fine particles and microorganisms having extracellular electron transport potential. The electroconductive fine particle transmits electron to the cathode from the microorganisms.    USE - The microbial fuel cell is useful for producing electrical energy.    ADVANTAGE - The microbial fuel cell increases the electric current density without using a mediator, and hence the fuel cell is inexpensive and highly safe. The microorganism enables reliable transport of electron to the electrode, and forms 3-dimensional structure that enhances the efficiency of the fuel cell, and the electric current production by 50 times or more.
NOVELTY - Process for producing triptane and/or triptene from a feed comprising dimethyl ether and/or methanol, comprises contacting the feed with an acidic zeolite catalyst having a structure that comprises at least one connecting channel that contains a 12 or 14 membered ring at 125-275 degrees C.    USE - The process is useful for producing triptane and/or triptene from a feed comprising dimethyl ether and/or methanol.    ADVANTAGE - The process selectively (preferably over 80%) produces triptane and/or triptene at lower temperature. The process produces the product with relatively low content of aromatics such as polymethylbenzenes.
NOVELTY - The system has a solar cell which transforms solar energy and wind energy into electrical energy. The electrical energy is used to electrolyse water in an electrolysis collecting and storing device to generate combustible hydrogen. The electrolysis collecting and storing device collects and stores hydrogen by a predefined pressure so that the solar and wind energy which cannot be stored is directly transformed into chemical energy which can be stored directly. The system generates the combustion-supporting oxygen when generating the combustible hydrogen.    USE - Solar energy and wind energy system for manufacturing combustible gas.    ADVANTAGE - Exhibits a wide application area, simple structure, convenience for using, stable operation, safety and reliability, long service time, non-toxicity, harmlessness, no pollution, low manufacturing cost and operating cost, strong adaptability to the environment and generating combustible hydrogen and widely used oxygen.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic perspective view of the solar energy and wind energy system.    Hydrogen gas-collecting channel (C2)    Oxygen gas-collecting channel (C3)    Hydrogen transferring pipe (C4)    Oxygen transferring pipe (C5)    Hydrogen overflow pipe (C6)
NOVELTY - A closed generator is filled with water. Electrolytic strips are provided inside the generator and outside a battery of the electrolytic strips. The generator has a pipeline where hydrogen-oxygen mixed gas is generated after electrolysis of water. The pipeline is connected to a valve of an engine. The generator is provided with a main control device and a vacuum switch.    USE - Automobile hydrogen production fuel oil energy saving device.    ADVANTAGE - Generated hydrogen-oxygen mixed gas is transmitted to valve of engine after electrolysis of water such that ideal oil-gas mixture is generated in combustion system of engine, thus fuel oil consumption is lowered, efficiency of engine is increased, service time of engine is prolonged and harmful gas generated due to incomplete combustion is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the automobile hydrogen production fuel oil energy saving device.
NOVELTY - The infrared straw gasification furnace has a blasting gas inlet pipe (2.2) that is provided at the bottom of a furnace body (1), and connected to the inner chamber of the furnace body. A fuel gas outlet pipe (2.1), provided at the upper section of the furnace body, is connected to the inner chamber of the furnace body, and to a filter. The outlet of the filter is connected with the gas supply pipe (2.6) of an infrared burner (3). An oxygen supplementing pipe (2.3) is provided between the gas supply pipe and blasting gas inlet pipe.    USE - Infrared straw gasification furnace for providing heat source using combustible waste such as straw and firewood as fuel.    ADVANTAGE - Provides infrared straw gasification furnace that is ecological, environment-friendly, efficient, convenient to use, and energy-saving.    DESCRIPTION OF DRAWING(S) - The drawing shows the isometric view of the infrared straw gasification furnace.    Furnace body (1)    Fuel gas outlet pipe (2.1)    Blasting gas inlet pipe (2.2)    Oxygen supplementing pipe (2.3)    Gas supply pipe (2.6)    Infrared burner (3)
NOVELTY - The up-draft type biological particle gasification furnace has an air outlet that is formed at the upper section of a gasification furnace body, which has an upper hearth, a grate and an ash cabin. An air feed mechanism has an outlet that communicates with the ash cabin by an air pipe. The lower wall of the hearth is internally equipped with a water jacket, which has a top that communicates with the air pipe of the air feed mechanism by a vapor pipe.    USE - Up-draft type biological particle gasification furnace for producing biogas in gas or oil boiler.    ADVANTAGE - Provides furnace that can feed material, produce gas, and operate consecutively. Provides furnace that is economical. Suppresses energy shortage by using biological energy. Increases utilization efficiency of biological resource which is converted into biogas.    DESCRIPTION OF DRAWING(S) - The drawing shows the cross sectional view of the up-draft type biological particle gasification furnace.
NOVELTY - The biomass heating gasification furnace has a water outlet and a water inlet that are formed at the upper and lower surfaces of a heat-conducting water tank (4), which is mounted on an infrared kitchen range (3). The water inlet communicates with a hot water outlet pipe at one side of a furnace body (1) via a pipeline, while the water outlet communicates with a radiator main pipeline. The tank has a middle space formed between inner and outer water jackets. Heat-conducting tubes are uniformly welded on the inner wall of the inner water jacket.    USE - Biomass heating gasification furnace for boiler.    ADVANTAGE - Ensures more adequate and more environment-friendly biomass material combustion via biomass gasification technology. Increases the heat conversion efficiency of the boiler through the water layer formed by the double-layered barrel-shaped structure of the furnace body. Enables performing multiple functions such as heating and bathing through the aid of the set water inlet and water outlet.    DESCRIPTION OF DRAWING(S) - The drawing shows the isometric view of the biomass heating gasification furnace.    Furnace body (1)    Converter (2)    Infrared kitchen range (3)    Heat-conducting water tank (4)
NOVELTY - The gasification furnace has a water groove (4) that is formed above a charging basket (1). A blow pipe (5) is set at the bottom of the basket, and joined to a fan (7) via an air supply outlet (6). A gas inlet pipe is set at the upper side of the basket, and joined to a converter via a pipeline. A tar exhaust outlet is set in the bottom of the converter. A gas outlet pipe is set on the top of the converter, and joined to an infrared kitchen range. Three layers of filter chips are set below the gas inlet pipe in the converter. Condensing pipes are set on the inner wall of the converter.    USE - Gasification furnace used in dining hall and restaurant.    ADVANTAGE - Eliminates potential safety hazard by connecting the kitchen range installation via pipeline. Reduces chemical heat loss due to efficient mixing of gas with air for combustion. Provides furnace that is smokeless, odorless, no carbon deposit, no waste gas, safe, and environment-friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows the isometric view of the gasification furnace.    Charging basket (1)    Water groove (4)    Blow pipe (5)    Air supply outlet (6)    Fan (7)
NOVELTY - The infrared biomass gasification furnace has a water sink (4) and a blasting pipe (5) that are set at the upper and lower surfaces of a material drum (1), respectively. The blasting pipe is joined to a fan (7) via an air inlet (6). An air intake is set at the upper side of the material drum, and joined to the interior of a purifier (2) via a pipeline. A tar outlet and an air outlet are formed at the bottom and top of the purifier. The air outlet communicates with an infrared furnace head via the pipeline.    USE - Infrared biomass gasification furnace for performing flameless combustion.    ADVANTAGE - Eliminates potential safety hazards by implementing furnace mounting by pipeline connection. Reduces chemical heat loss due to complete mixing of gas with air for combustion. Eliminates separation of free carbons when performing flameless combustion. Eliminates soot at pot bottom after long period of use. Provides furnace that does not produce smoke, odor, carbon deposit, and waste gas.    DESCRIPTION OF DRAWING(S) - The drawing shows the isometric view of the infrared biomass gasification furnace.    Material drum (1)    Purifier (2)    Water sink (4)    Blasting pipe (5)    Air inlet (6)    Fan (7)
NOVELTY - A high-energy biomass heating gasification furnace has gasification furnace body comprising of combustion plant and heating plant. The heating plant has heating plate and pipeline connecting the heating plate with the combustion plant so to transmit the cooled heat media after heat emission to the combustion plant for thermal cycle.    USE - High-energy heating gasification furnace.    ADVANTAGE - Provides a high-energy biomass heating gasification furnace with simple structure at low production and operation cost. Promotes energy conservation and environmental protection. Ensures safety and reliability of the furnace that is convenient to operate and maintain.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the high-energy biomass heating gasification furnace.
NOVELTY - A high-energy biomass gasification boiler comprises a biomass gasification generator and a gas-fired boiler. The biomass gasification generator comprises a closed shell and a lining in the shell. A hollow gasification chamber is in the lining. An air-collecting chamber is installed on the upper part of the gasification chamber and interconnected with the gasification boiler via pipeline. The gas-fired boiler takes the combustible gas generated by biomass gasification generator as the fuel.    USE - High-energy biomass gasification boiler.    ADVANTAGE - Provides a high-energy biomass gasification boiler that with simple and rational structure and high overall efficiency at low production and operation cost.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic of the high-energy biomass gasification boiler.
NOVELTY - A combustor has water-jacketing shell equipped with water supplying pipe and water returning pipe. A gas cooker is arranged inside of the water-jacketing shell. A secondary heating pipe is installed at the inner wall of the water-jacketing shell. The ventilation holes are formed at the lower part of the water-jacketing shell.    USE - Combustor for straw gasification furnace.    ADVANTAGE - Enables reliable combustion of combustible gas by the formation of ventilation holes on the lower part of the water-jacketing shell. Increases combustion efficiency of combustible gas generated by the straw gasification furnace. Improves heat energy utilization ratio. Achieves energy-saving and environment protection effect.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional drawing of the combustor.
NOVELTY - The furnace comprises main furnace (1), basin-shaped grate (10) and working hole (15). The main furnace contains secondary heating sleeve which serves as hollow column with sleeve (7), baffle plate and connecting pipe (8). The sleeve is provided with holes at both sides of baffle plate which communicates with second aeration pipe (3) and third aeration pipe (4). One end of second aeration pipe communicates with first secondary furnace (5) while one end of third aeration pipe is connected with second secondary furnace (6). The connecting pipe is connected with running water pipe by valve.    USE - Bi-circulating secondary-cracking straw gasification furnace.    ADVANTAGE - Adds secondary heating sleeve and first secondary furnace to the straw gasification furnace based on downdraft main and secondary straw gasification furnace, so that the furnace gas can be cracked twice circularly, and the tar in the furnace is cracked sufficiently. Increases yield and quality of fuel gas by the good and simple structured bi-circulating secondary-cracking straw gasification furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows the longitudinal cross sectional view of the bi-circulating secondary-cracking straw gasification furnace.    Main furnace (1)    Second aeration pipe (3)    Third aeration pipe (4)    First secondary furnace (5)    Second secondary furnace (6)    Sleeve (7)    Connecting pipe (8)    Basin-shaped grate (10)    Working hole (15)
NOVELTY - Composition comprises hydroxystearic acid, oil and fat, which are cooled and solidified.    USE - Composition for preparing biodiesel, candles and soaps from industrial waste.    ADVANTAGE - The composition ensures easy recycling of industrial waste.
NOVELTY - The method involves connecting an internal combustion engine and an electrolytic cell (3). A direct current power supply and a cathode (2) are provided, where hydrogen and oxygen are generated and transferred to an anode (1) at the upper part of the electrolytic cell in the form of a mixed gas (4). An air inlet port and a water removal unit (6) are provided with the internal combustion engine, where the mixed gas is injected into the combustion chamber of the internal combustion engine.    USE - Method for electrolyzing water.    ADVANTAGE - The air inlet port and a water removal unit are provided with the internal combustion engine, where the mixed gas is injected into the combustion chamber of the internal combustion engine, and ensures to increase the explosion power of the existing fuel and also enables to save the fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of a method for connecting internal combustion engine and electrolytic cell. (Drawing includes non-English language text).    Anode (1)    Cathode (2)    Electrolytic cell (3)    Mixed gas (4)    Water removal unit (6)
NOVELTY - A soil phosphorus activator comprises (pts.wt.) vitamin C fermented residue (35-45), lignite (35-45), sawdust (3-5), natural zeolite powder (3-5), and clinker (10-14).    USE - The soil phosphorus activator is useful for farmland after mixing with the fertilizer.    ADVANTAGE - The soil phosphorus activator is environment-friendly and has simple process and low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a preparation method of the soil phosphorus activator.
NOVELTY - The furnace has furnace body that is sleeved with sealed inlet chamber on the lower part periphery. The interior of furnace body communicates to inlet chamber through air inlets. A sealed hot water tank is arranged on upper part periphery of the furnace body where mixed fuel gas outlet pipe communicating with purification filter is arranged. An air inlet pipe communicates with inlet chamber and to the purification filter, respectively. An exhaust gas discharging port is arranged on the mixed fuel gas outlet pipe.    USE - Hot air type straw gasification furnace for crops. Can be used for continuously supplying gas by burning after lightening and adding straw fuel, until the straw fuel within the furnace body is exhausted.    ADVANTAGE - Provides hot air type straw gasification furnace with simple and reasonable design, and can be used conveniently. Improves yield of the hot air type straw gasification furnace by 15 to 20 percent compared with common gas manufacturing furnace. Prevents step of the spark out since it is free from fuel gas.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic of the hot air type straw gasification furnace.
NOVELTY - The cracking device has thermal cracking kettles (1) that are arranged in a batch. Each batch of the thermal cracking kettles is arrayed and located in the thermal cracking furnace (2). A rolling pulley is set below the supporting leg at the bottom of thermal cracking kettle.    USE - High-efficiency thermal cracking device for scale use of biomass.    ADVANTAGE - Increases volume of thermal cracking kettle so to perform a scale and continuous production. Promotes overall heat utilization rate of the high-efficiency thermal cracking. Saves energy, improves structures of the gasifying chamber, combustion chamber and heat storage chamber, thus making flow of the gas inside the combustion chamber smoother. Makes temperature in each part of the device in ideal balanced state so as to promote the quality of the product.    DESCRIPTION OF DRAWING(S) - The drawing illustrates the high-efficiency thermal cracking device.    Thermal cracking kettles (1)    Thermal cracking furnace (2)
NOVELTY - A biomass gasification boiler has gas outlet (13) provided over the filter screens. A hot water outlet (4) is set at one side of upper part of furnace body (1) with water tank (5) on which heat-conducting pipes (6) are symmetrically arranged at the middle. A circular air disc (8) is set on ash hole (9) formed at lower part of furnace body. A cold water inlet (7) is set at right side while air supplying outlet (10) is set at left side of ash hole.    USE - Biomass gasification boiler.    ADVANTAGE - Converses generated material to gaseous fuel, so the fuel level and energy utilization rate can be improved, and energy sources can be saved. Provides small and economic biomass gasification boiler that is free of coal, and has high burning rate at low cost. Can replace the existing coal burning boiler. Reduces discharge of carbon monoxide, sulfur dioxide and soot so that air environment can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic of the biomass gasification boiler.    Furnace body (1)    Hot water outlet (4)    Water tank (5)    Heat-conducting pipes (6)    Cold water inlet (7)    Circular air disc (8)    Ash hole (9)    Air supplying outlet (10)    Gas outlet (13)
NOVELTY - The furnace has taper canopy on upper part of a soot filter. A valve in space between the fuel gas outlet pipe and gas cooker is set on the spot of flue pipe located near the smoke-and-dust elimination filter. One end of flue pipe is connected to soot filter while other end is connected to upper part of smoke-and-dust elimination filter on top end of taper cover. The taper cover is used to cover the centre of the U-shaped water storing tank on upper part of the furnace. A smoke-discharge pipe is mounted at the center of the taper cover.    USE - High-new straw gasification furnace.    ADVANTAGE - Exhibits sufficient smoldering effect. Effectively enhances quality of generated gas, saves energy. Effectively filter and remove the soot and the tar set out from the straw. Adopts electronic automatic lighting in the gas-cooker. Provides furnace body with acid-corrosion resistant and high-temperature resistant dope. Prolongs service life of the gasification furnace. Provides convenience for the soot and as well as to the tar elimination and maintenance. Ensures safe operation when supplying heat for the scouring bath. Saves a lot of coal, gasoline and natural gas for the country and the construction of the socialistic new village. Enables improvement in the social benefits and economic benefits of the high-new straw gasification furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the high-new straw gasification furnace.
NOVELTY - The straw gasification furnace has air inflow pipe (12) having top end in furnace body (1) that is higher than the grate (8). An air outflow plate (7) formed with multiple exhaust holes is provided on top end of furnace body. The inner sidewall of furnace body is firmly connected with first air supply pipe (4) whose lower part can passes through the grate. An inlet under the grate is connected with secondary air supply pipe (11) installed on the furnace body wall.    USE - Straw gasification furnace for gasifying un-pulverized straws.    ADVANTAGE - Provides straw gasification furnace with strong fire and no tar that can completely gasify the un-pulverized straws.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic of the straw gasification furnace.    Furnace body (1)    First air supply pipe (4)    Air outflow plate (7)    Grate (8)    Secondary air supply pipe (11)    Air inflow pipe (12)
NOVELTY - The trolley has trolley body (1) having wheels (11) at the bottom, and storage cabinet (12) on upper part. Outer cover of furnace body (13) of gasification furnace is set on upper surface of trolley body. A water tank set on upper part of furnace body has gas conveying port on left side and hot water outlet on right side. A heat conducting tube is set at the center of furnace body with ash outlet at the lower part. An air supply port is set at the left side of ash outlet with circular wind disk on its upper part and cold water inlet at the right side.    USE - Multifunctional biomass gasification snack trolley. Can be used in barbecuing.    ADVANTAGE - Provides a snack trolley that is green, smokeless, environment-friendly and sanitary, and can be operated conveniently. Produces no greasy smoke and ash when used in barbecuing. Provides furnace with uniform heat and has strong penetrating power so to make golden, crispy, tender, fragrant and delicious barbecued food.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of the multifunctional biomass gasification snack trolley.    Trolley body (1)    Wheels (11)    Storage cabinet (12)    Furnace body (13)
NOVELTY - An equipment for treating pollution-free fertilizer and generating biogas, comprises multiple collection tanks containing organic wastes; where the collection tanks are connected to the front fermenting tank through a transfer feeding pump; the fermenting tank is connected to the back fermenting tank; and the biogas liquid of front and back fermenting tanks is transferred to the dewatering machine to dewater through the material liquid pump.    USE - The equipment is useful for treating pollution-free fertilizer and generating biogas (claimed).    ADVANTAGE - The equipment does not need to stop in the process of removing sewage and maintaining to ensure continuous generation of biogas and compost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the equipment for treating pollution-free fertilizer and generating biogas.
NOVELTY - A vegetable waste organic fertilizer comprises (wt.%) vegetable waste (73-84), organic material (10-20), calcium cyanamide (2-4), and natural zeolite (3-5).    USE - A vegetable waste organic fertilizer for green vegetables.    ADVANTAGE - The fertilizer has good protection effect, and is easy to prepare.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of producing a vegetable waste organic fertilizer comprising stacking organic matters, vegetable wastes, calcium cyanamide and natural zeolite into layers, coating the organic matters on the outer layer, sealing with plastic cloth, fermenting for 7-10 days, mechanically or manually turning the fermented material, sealing using plastic cloth, fermenting for 7-10 days, and drying to obtain organic fertilizer.
NOVELTY - Carbon dioxide purification involves purifying waste gas generated in only mono-ethylene glycol advanced (OMEGA) process by using pure oxygen combustion process. The waste gas includes more than 90% of carbon dioxide, 10000-20000 parts per million of volatile organic compounds and 1.2-2% of oxygen.    USE - Method for purifying carbon dioxide.    ADVANTAGE - The carbon dioxide purification method is cost-effective and eco-friendly, removes harmful material, and ensures efficient collection of carbon dioxide and safe OMEGA process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for purifying carbon dioxide, which includes depressurization valve, fuel delivery system for supplying auxiliary fuel to inlet gas, oxygen measuring device and lower explosive limit detector.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the carbon dioxide purification device.    Emergency vent (110)    Process gas inflow auto valve (111)    Depressurization valve (112)    Lower explosive limit detector (131)    Outlet (143)
NOVELTY - A slow release compound fertilizer comprises (wt.%) powdered rock phosphate (10-40), potassium feldspar (10-40), coal refuse (15-40), magnesite powder (10-20), nitrogenous fertilizer (10-30), bentonite (8-18), diatomite (1-3), and microelement (0.3-1). The powdered rock phosphate, potassium feldspar, coal refuse and coke are combusted at 500-800 degrees C for 8-16 hours to obtain combusted mixture.    USE - Slow release compound fertilizer for every kind of soil and for growing every kind of plants.    ADVANTAGE - The slow release compound fertilizer is environment-friendly, energy-saving and soil-improving; releases slowly; and has high using efficiency and low production cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of slow release compound fertilizer by:    (A) combusting powdered rock phosphate, potassium feldspar, coal refuse and coke at 500-800 degrees C for 8-16 hours, cooling, crushing, and sieving through 60 meshes;    (B) respectively crushing magnesite powder, bentonite and diatomite, and sieving through 60 meshes;    (C) mixing the components, drying, and sieving; and    (D) quality checking and packaging.
NOVELTY - Use of a trace element solution comprising at least one trace element and at least two complexing agents for metal ions, for the supplementation of nutrients for an anaerobic biogas fermentation, is claimed.    USE - The trace element solution is useful for the supplementation of nutrients for anaerobic biogas fermentation, preferably for the extraction of biogas.    ADVANTAGE - The complexing agents can transport trace elements in complexed form over the cell membrane and release the trace elements into the cell. The biogas improves the availability of trace elements for the microorganisms.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) the trace element solution; and    (2) a process for the extraction of biogas in a biogas plant, comprising adding the trace element solution containing at least one trace element and at least one complexing agent to the biogas plant.
NOVELTY - A turner comprises an elevated track, a loading stage and a mixing unit, where the elevated track is set with a couple of longitudinal tracks that are fixed on posts at two sides of the compost plant and a transverse track crossing the longitudinal elevated tracks.    USE - The turner is useful in the industrial field.    DETAILED DESCRIPTION - A turner comprising an elevated track, a loading stage and a mixing unit, where the elevated track is set with a couple of longitudinal tracks that are fixed on posts at two sides of the compost plant and a transverse track crossing the longitudinal elevated tracks; further, a sliding base is set on the transverse track; the sliding base runs to make the transverse track move reciprocally along the longitudinal tracks; the loading stage is set on the transverse track and arranged with a sliding pulley wheel, so the loading stage can move reciprocally along the transverse track; a mixing bench and a chain belt are arranged inside the mixing unit; the mixing bench is connected to the loading stage via shaft and swings up and down; a set of elevating device is set on the mixing bench for controlling swinging angle of the mixing bench; the chain belt is engaged with the driving gear on the mixing bench and the driven gear at two end edges of the mixing bench; the driving gear is driven by a main motor to make the chain belt and auxiliary harrow rotate around peripheral edge of the mixing bench.
NOVELTY - A ball is provided between inner ring and outer ring of braking ring. An intake sieve portion is horizontally fixed to material storehouse to divide the storehouse into upper and lower chambers. An air compressor is connected to lower chamber. A material inlet is provided at the upper side of storehouse. A motor is provided on a supporting seat. A friction wheel is mounted on rotating shaft of motor. The friction wheel is connected to bottom portion of storehouse. A lifter is provided under the supporting seat. Wheels are mounted under the bottom board.    USE - Screw drum-type compost reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the compost reactor.
NOVELTY - The module has insulation boards (16a,16b) that are positioned among fuel cell stacks (21a,21b), and a heat conduction board (15) that is arranged between insulation boards. The heat conduction board is formed of material having heat conduction larger than that of insulation boards. The insulation boards are divided into several segments (161a-166a,161b-166b) such that the each divided segment mutually isolates from each other.    USE - Fuel cell module for fuel cell (claimed) e.g. solid oxide fuel cell, used as apparatus for generating fuel gas and oxidizing agent gas.    ADVANTAGE - The weight reduction of fuel cell module can be achieved while being able to attain equalization of temperature distribution along longitudinal direction of fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the fuel cell module.    Heat conduction board (15)    Insulation boards (16a,16b)    Fuel cell stacks (21a,21b)    Segments (161a-166a,161b-166b)    Flow direction (L)
NOVELTY - The system has a temperature sensor (55) that measures temperature of hazardous component reduction unit (5A) that reduces the hazardous component of anode gas generated by a modification unit (34) at anode of fuel cell (1). A temperature control unit adjusts the measured temperature of hazardous component reduction unit according to cooling capacity of water flowing through channel (4a) of heat-exchanging unit (4), by outputting the command for setting the target temperature of reduction unit within constant temperature.    USE - Fuel cell system for vehicle, electric machine and electronic device.    ADVANTAGE - The stability of operation of hazardous component reduction unit during supply start of anode gas generated at anode of fuel cell is improved efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the modifier in fuel cell system. (Drawing includes non-English language text)    Fuel cell (1)    Heat-exchanging unit (4)    Channels (4a,4b)    Hazardous component reduction unit (5A)    Modification unit (34)    Temperature sensor (55)
NOVELTY - The fuel cell module (FC) has a combustion chamber (27) which combusts the fuel gas and oxidizing agent gas reacted in several fuel cells (2) formed in a module container (8). The exhaust gas discharged from the combustion chamber is guided to the exterior of module container through a flow path (50). The modifiers (41,42) are arranged upstream side of the fuel cell and thermal capacity of modifier (41) is smaller than that of the modifier (42).    USE - Fuel cell module e.g. solid oxide fuel cell module.    ADVANTAGE - The consumption of fuel gas can be reduced at the time of temperature rising and lowering of fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a longitudinal cross-sectional view of the fuel cell module.    Fuel cell (2)    Module container (8)    Combustion chamber (27)    Modifiers (41,42)    Fuel cell module (FC)
NOVELTY - The low voltage electrical circuits (2a,2b) with renewable energy sources (1) are utilized to systematically charge and discharge several wet electrolytic type batteries (3) to generate gases. The gases are drawn into a system of mechanisms and the containers (4) within a central module where hydrogen is separated from oxygen and other impurities. The hot exhaust gases discharged from a turbine powered booster generator used as a heat source are used for a combinational central heating and cooking unit. A gas supply system is set with a hydraulic pump and a ram.    USE - Production method of hydrogen used as fuel for vehicle such as cars, and as household fuel for cooking and heating applications.    ADVANTAGE - The production amount of hydrogen can be increased, and carbon dioxide emission and toxic emissions into the atmosphere can be reduced so that the global warming problems can be solved effectively, while reducing the production time of hydrogen. The usage of mains electricity, mains gas, or heating oil for cooking and heating applications can be reduced, accordingly.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow block diagram of the hydrogen production process.    Energy source (1)    Low voltage electrical circuits (2a,2b)    Electrolytic type battery (3)    Partial vacuum draw-off container (4)    High pressure hydrogen fill container (5)
NOVELTY - A plant for obtaining methane gas from organic waste, with a fermentation chamber (3), a gas collection space (7) and a post fermentation chamber (4), in which the gas collection space lying directly above the fermentation chamber, is not separated structurally from the fermentation chamber, and also with at least one feed duct (6) and one discharge duct (18) for the excess fermented liquid from the post fermentation chamber, is disclosed. The chambers are heat insulated and the fermentation chamber and the post fermentation chamber situated above the former, are connected in such a way of communicating vessels and are combined into a unit (1). The upper part of the post fermentation chamber, is connected through a connecting duct (10) closable by a valve (11) to the gas collection space and is further connected to at least one gas duct (12) leading to a surge tank and the discharge duct is communicated with the post fermentation chamber and the connecting duct (10) can be opened or closed by the valve time dependently and/or dependent on the level of filling in the fermentation chamber (13) and/or gas pressure prevailing in the gas collection space. Image 0/4
NOVELTY - A water purification process system (1) comprises flow path (10) which supplies and distributes wastewater, enrichment part which enriches dissolved oxygen of wastewater that is arranged in flow path so that plant may be planted within flow path and wastewater may be purified, and liquid feeding part which liquid feeds in position inside flow path. The water where dissolved oxygen is enriched is collected in collection position inside flow path.    USE - Water purification process system.    ADVANTAGE - The water purification process system performs water purification process of plant which is maintained and stabilized even when water of high pollutional load is supplied, and has high water purification process capability.    DESCRIPTION OF DRAWING(S) - The drawing shows a top view of the water purification process system.    Water purification process system (1)    Flow path (10)    Liquid feeding pump (41)    Liquid feeding path (42)    Discharge pipe (70)
NOVELTY - Producing anhydrous fermentation product involves treating at least one plant (10) derived material to produce a broth having less than or equal to 5 wt.% of the fermentation product (12); extracting a vapor mixture (24) having less than or equal to 45 wt.% of the fermentation product from the broth; removing water vapor from the vapor mixture through a vapor separation membrane to produce a product vapor; and extracting heat energy from at least one of the removed water (17) or product vapor (40).    USE - For producing anhydrous fermentation product (claimed) useful as fuel grade ethanol or acetone, butanol or ethanol (ABE) mixtures from sugarcane, corn kernels, wheat or other starch feedstock.    ADVANTAGE - The process of removing water from a mixture comprising low amount of alcohol e.g. less than 8% or less than 5%, reduces product inhibition for low sugar concentration in the feed, and reduces enzyme inhibition or limits the concentration of suspended solids in the fermenter.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an apparatus for producing anhydrous fermentation product comprising cellulosic or ligno-cellulosic processing system, broth vaporization unit and membrane vapor separation unit, where the components are connected sequentially in a once-through feed to product flow path.    DESCRIPTION OF DRAWING(S) - The figure shows a simplified schematic flow sheet of an ethanol processing plant.    Plant (10)    Product (12)    Water (17)    Vapor mixture (24)    Product vapor (40)
NOVELTY - Equipment comprises waste, which is formed during the production of charcoal.    USE - Equipment for carbonizing biomass and for condensation of gas and vapor.    ADVANTAGE - The equipment is eco-friendly.
NOVELTY - System comprises biomass.    USE - System for obtaining biofuel, bio-oil, charcoal powder, acid extract and pyrolytic gases.    ADVANTAGE - The system is eco-friendly and ensures development and generation of renewable energy alternative to fossil fuel and material derived from petroleum by accelerated thermal degradation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for obtaining biofuel, bio-oil, charcoal powder, acid extract and pyrolytic gases.
NOVELTY - A wastewater treatment apparatus has an equalizing tank (1) for adjusting to-be-processed water (14), an aerator (2) for aerating to-be-processed water, a membrane separator (3) provided in aerator and carrying out membrane separation of activated sludge, a dehydrator (6) for dehydrating surplus sludge from aerator, and a processing tank for performing predetermined processing without returning supernatant liquid produced by dehydration in equalizing tank or aerator.    USE - Apparatus is used for treating wastewater, such as industrial wastewater and domestic wastewater.    ADVANTAGE - The dehydrating performance of wastewater is effectively improved, and water is economically treated. The obstruction of separation membrane is prevented.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for operation method of wastewater treatment apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows the flowchart of membrane separation activated sludge apparatus.    Equalizing tank (1)    Aerator (2)    Membrane separator (3)    Dehydrator (6)    To-be-processed water (14)
NOVELTY - Microorganisms immobilization support (10) comprises porous body (14) which fixes microorganisms, frame (12) which has same size as cross section of wastewater treatment reactor, and space part in which porous body is hold and positioned regularly. The porous body consists of porous bodies of same size as space part of frame. The support has strength which does not deform even if frame stacks up frames.    USE - Microorganisms immobilization support for fixing microorganisms in wastewater-treatment reactor using biologically-treating method.    ADVANTAGE - The support is inexpensive, has reduced size, and is excellent in nitrification performance.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a biological nitrification denitrifying apparatus; and    (2) a usage method of the biological nitrification denitrifying apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of microorganisms immobilization support.    Microorganisms immobilization support (10)    Frame (12)    Porous body (14)    Projection part (17a, 17b, 17c)    Space part (19)
NOVELTY - A sewage disposal method involves inducing scum that contains oil component from grease trap or wastewater decomposition process tank to decomposition tank, draining water content while making scum contact and adhere to carrier, and decomposing oil component that ventilates to decomposition tank and is contained in oil component decomposition microorganisms at aerobic environment in scum.    USE - A sewage disposal method.    ADVANTAGE - The method decreases outflow of microorganisms in grease trap or wastewater decomposition process tank, accelerates proliferation of microorganisms, and efficiently performs lipolysis by microorganisms.    DETAILED DESCRIPTION - A sewage disposal method involves inducing scum that contains oil component from grease trap or wastewater decomposition process tank to decomposition tank, draining water content while making scum contact and adhere to carrier, and decomposing oil component that ventilates to decomposition tank and is contained in oil component decomposition microorganisms at aerobic environment in scum. The grease trap or wastewater decomposition process tank, decomposition tank that accommodates carrier consisting of porous material which carries oil component decomposition microorganisms, and ventilation unit that ventilates decomposition tank are provided in a sewage treatment unit. An INDEPENDENT CLAIM is included for a sewage treatment unit.    DESCRIPTION OF DRAWING(S) - The drawing shows a conceptual diagram of the sewage treatment unit. (Drawing includes non-English language text).
NOVELTY - A useful carbonized material manufacture facility comprises carbonization furnace (1) of waste material, carbonized material reclaimer (2) that recovers carbonized material that comes out from carbonization furnace, carbonized material manufacturing equipment (8) that manufactures useful carbonized material from recovered carbonized material, and measurement/conveyance installation (13) of dust with low combustible content rate attached to carbonized material manufacturing equipment.    USE - Useful carbonized material manufacture facility.    ADVANTAGE - The facility can manufacture useful carbonized materials with different combustible content concentrations without producing variation and yield defect of product property.    DETAILED DESCRIPTION - A useful carbonized material manufacture facility comprises carbonization furnace (1) of waste material, carbonized material reclaimer (2) that recovers carbonized material that comes out from carbonization furnace, carbonized material manufacturing equipment (8) that manufactures useful carbonized material from recovered carbonized material, and measurement/conveyance installation (13) of dust with low combustible content rate attached to carbonized material manufacturing equipment. The flammable concentration of useful carbonized material is made adjustable by changing mixing ratio of dust conveyed from installation and recovered carbonized material.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the useful carbonized material manufacture facility. (Drawing includes non-English language text).    Carbonization furnace (1)    Carbonized material reclaimer (2)    Heat recovery installation (4)    Carbonized material manufacturing equipment (8)    Measurement/conveyance installation (13)
NOVELTY - Biologically active substrate comprises a material, which provides colonization room for contaminants degrading microbacteria, other material, which exhibits contaminants retention properties, and an oil retention support material, which is permeable to water.    USE - The substrate is useful: for degradation and retention of contaminants in surface water; in infiltration basin; and in shaft insert of a drainage shaft (all claimed).    ADVANTAGE - The substrate readily provides a mechanical filtering effect, and reduces or decomposes organic contaminants into harmless individual items or recombines with other substances, so that hazardous products are no longer present as contaminants existing substances.
NOVELTY - Powdered or granular care product, is claimed, which is packed as capsules portioned into water-soluble foil, so that a simplified application is enabled.    USE - The care product is useful: for garden and other ponds (claimed); and as fertilizer for aquatic plants. No biological data given.    ADVANTAGE - The care product is user-friendly. The outer shell of capsules is made of a special foil, which can dissolve in water.
NOVELTY - Extracting products from biomass involves destructively distilling the biomass using solar power as an energy source; and collecting the resulting products.    USE - For extracting energy products comprising methane, methanol, acetone, acetic acid, creosotes, various tars, celluloses, pyroligneous acid, carbon or acetone, from biomass comprising sisal, sugar cane including waste sugar cane, wood, maize or maize stems, coffee husks, cashew nuts, coconuts, and thick-stemmed plant material (claimed).    ADVANTAGE - The energy needed for the process is derived from solar power. Suitably more than 50%, more suitably greater than or equal to 70%, particularly greater than or equal to 80% of the total energy requirement of the process is provided by solar power. Thus, the process can be operated very efficiently, without the need for conventional fuels with their attendant environmental and other problems. The process also has the advantage of employing a renewable energy resource (i.e. biomass) as the raw starting material. The products recovered from the process can be used locally to meet local needs. This is potentially of great benefit to countries of the developing world, where energy products are often in short supply or are too expensive to import.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an apparatus for extracting products from biomass, comprising: unit for destructive distillation of the biomass; unit for converting solar power into heat energy in a form suitable for driving the distillation; and unit for collecting the extracted products.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of an apparatus used for extracting products from biomass.
NOVELTY - The method involves setting projection length of oxygen supply nozzle extending into the reformer about 200 mm or more, so that the oxygen gas blown from oxygen supply nozzle into reformer collides with fuel gas. The oxygen gas blowing direction is about 7 degrees or less from furnace central direction.    USE - Modification method of fuel gas emitted during gasification process of solid-fuel substance such as municipal solid waste, industrial waste, coal and coke.    ADVANTAGE - The fuel gas is modified with high thermal efficiency, without damaging the refractory structure.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view illustrating the waste treatment by gasification modification system. (Drawing includes non-English language text)
NOVELTY - A ferrite type stainless steel material comprises (in mass%) carbon (0-0.030), silicon (0-1.00), manganese (0-1.50), chromium (15.0-25.0), molybdenum (0.50-3.00), cobalt (0.50-4.00), copper (0.50-2.00), nitrogen (0-0.030) and remaining iron and unavoidable impurity. The amount of chromium, molybdenum, cobalt and copper satisfy preset relations.    USE - Ferrite type stainless steel material for automobile exhaust component such as exhaust manifold, catalytic converter case, front pipe, two-wheeled vehicle waste gas passage, duct of liquefied nitrogen gas electric power generation, micro gas turbine, fuel cell modifier and gas heat pump.    ADVANTAGE - The ferrite type stainless steel material has excellent thermal fatigue characteristics and is manufactured without using expensive raw material and special installation.    DETAILED DESCRIPTION - A ferrite type stainless steel material comprises (in mass%) carbon (0-0.030), silicon (0-1.00), manganese (0-1.50), chromium (15.0-25.0), molybdenum (0.50-3.00), cobalt (0.50-4.00), copper (0.50-2.00), nitrogen (0-0.030) and remaining iron and unavoidable impurity. The amount of chromium (W1), amount of molybdenum (W2), amount of cobalt (W3) and amount of copper (W4) satisfy the relations: 0.25x W1+0.30x W2+0.60x W3-0.40x W4 greater than or equal to 5.7, where W1 is 20 mass% or less and W3 is 3.0 mass% or less, 0.25x W1+0.30x W2-0.10x W3-0.40x W4 greater than or equal to 3.6, where W1 is 20 mass% or less and W3 is more than 3.0 mass%, 0.15x W1-0.30x W2+0.10x W3+0.40x W4 less than or equal to 4.4, where W1 is more than 20 mass% and W3 is more than 3.0 mass%, 0.15x W1-0.30x W2-0.60x W3+0.40x W4 less than or equal to 2.3, where W1 is more than 20 mass% and W3 is 3.0 mass% or less, and 25x W1+3.0x W3+50x W4 greater than or equal to 70.
NOVELTY - The waste treatment plant (1) has a gasifier oven with an upper (18), middle (26) and lower section (12) in connection with a gas condenser (42), in connection with a turbine module (44). The treatment plant comprises a combustion chamber, a turbine and a generator (58) in connection with the turbine module.    USE - Waste treatment plant for generating electric energy from combustion gases.    ADVANTAGE - The waste treatment plant has a gasifier oven with an upper, middle and lower section in connection with a gas condenser, in connection with a turbine module, and hence ensures ecologically harmless operation with satisfying energy balance.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a waste treatment plant module; and    (2) a method for generating electric energy from waste under utilization of a treatment plant.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an assembly of a waste treatment plant.    Waste treatment plant (1)    Gasifier oven lower section (12)    Gasifier oven upper section (18)    Gasifier oven middle section (26)    Gas condenser (42)    Turbine module (44)    Generator (58)
NOVELTY - The chamber (1) has a double structure including chambers (2, 4), where outer side i.e. flow path (5) and inner side i.e. interior space, of the double structure are connected with each other in a partition surface. Dry cleaning air is supplied between the outer side and the inner side. A piping is connected to an upper part of the inner side for suctioning exhaust gas from the inner side. An opening part is equipped with a door, and the partition surface surrounds a circumference three ways of the opening part for opening the upper side.    USE - Dry cleaning chamber for drying paste of an electrode and a semiconductor substrate during manufacturing a fuel cell in a dry work room.    ADVANTAGE - The double structure cannot be sealed inside, thus maintaining inside humidity, and avoiding supply of dry cleaning air to an exterior of the chamber for maintaining external humidity of the chamber. The usage amount of the dry cleaning air is reduced, and energy required for production of the dry cleaning air is reduced. The chamber eliminates carbon-dioxide emissions and environmental impacts. The dry cleaning air has specific gravity greater than air, so that the dry cleaning air flows without using pressurization apparatus. The opening part is shielded, thus preventing penetration of external air into the chamber.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a dry cleaning chamber.    Dry cleaning chamber (1)    Chambers (2, 4)    Flow path (5)    Conveyor part (10)    Dry work room (50)
NOVELTY - The apparatus (25) has a cylindrical off-gas nozzle (25c) provided inside the combustion pipe (25b) along the axial direction of combustion pipe. Several primary jet nozzles (25c1) are provided in the front-end side of nozzle. A partition plate (25b1) is fixed by the base end side position between nozzle and combustion pipe from primary jet nozzle. The secondary jet nozzles (25b2) are provided around the off-gas nozzle. The anode-off gas or fuel gas ejected from primary jet nozzle, is mixed with oxidizing agent gas to eject combustion air from secondary jet nozzle.    USE - Combustion apparatus of reformer used in fuel cell system (both claimed).    ADVANTAGE - An appropriate shaped flame is produced without suppressing the expansion of flame, and the reduction of nitrogen oxide concentration and carbon monoxide concentration is ensured.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) reformer; and    (2) fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the combustion apparatus.    Combustion apparatus (25)    Combustion pipe (25b)    Partition plate (25b1)    Secondary jet nozzle (25b2)    Cylindrical off-gas nozzle (25c)    Primary jet nozzle (25c1)    Combustion air supply pipe (64)
NOVELTY - The system has anode and cathode electrodes arranged at surfaces of electrolytic membrane. The reactive gas is supplied from reactive-gas supply structure to separator which supplies the gas to electrodes. The positive and negative electric potentials are respectively supplied to cathode and anode electrodes by using power supply. The electric load is connected to power supply path after reactive-gas supply is stopped to consume oxygen for hydrogen generation at cathode electrode side. The water content is supplied to anode electrode through electrolytic membrane.    USE - Fuel cell system for electric power generation used in driving of motor vehicle.    ADVANTAGE - The deterioration of catalyst after stopping the supply of reactive gas such as cathode gas, is suppressed by connecting electric load at power supply path to consume oxygen for generation of hydrogen obtained by connection of electric load with cathode electrode. The water content in cathode electrode is removed effectively through anode electrode.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart explaining the start-stop time control for supply of reactive gas to cathode electrode. (Drawing includes non-English language text)
NOVELTY - The system has a main heat exchanger comprising a circulation nitrogen heat return passage. The circulation nitrogen heat return passage of the main heat exchanger, a circulation pressure nitrogen heat release passage of a liquefied natural gas (LNG)-nitrogen heat exchanger, a circulation intermediate pressure nitrogen heat release passage, a circulation high-pressure nitrogen heat release passage and a compressor pipeline form a circulation nitrogen system. The LNG is reheated via a natural gas heat return passage of the LNG-nitrogen heat exchanger to output at a constant temperature.    USE - Space division system.    ADVANTAGE - The system utilizes liquefied natural gas (LNG) cold energy efficiently, and avoids danger when natural gas enters into the space division device while the space division fails to contact directly with a cyclic part. The high-pressure liquid nitrogen throttled with intermediate pressure is partly entered into LNG-nitrogen heat exchanger for deep overcooling to recover energy and compensate for shortage of LNG high-grade cold energy. The circulation nitrogen utilizes LNG cold energy to cool, to reduce compressed power consumption and obtain super-critical pressure nitrogen. The system has small amount of heat exchanger passages, concise process organization and wide application range, and is safe, reliable, convenient to operate and control and low in cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a circuit diagram of a space division system.'(Drawing includes non-English language text)'
NOVELTY - A peat is produced by cutting mechanically peat blocks (15) having a high moisture content from a bog selected from a lifting groove, placing the cut peat blocks to dry on self-supporting bases (14), and collecting peat blocks from the bases when the moisture content is at a chosen level. The peat blocks are placed on the bases mechanically and the bases are handled mechanically at least when placing the peat blocks on the bases.    USE - Method of producing a peat.    ADVANTAGE - The method has accelerated drying step, is simple, and has improved handling and storing of peat blocks.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a base for use in peat production; and    (2) an equipment for producing peat.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of placing the peat blocks on a base.    Self-supporting bases (14)    Peat blocks (15)    Drying blocks (16)
NOVELTY - The method involves heating cryogenic liquid i.e. liquefied natural gas, in a series of separated passages at pressure of 60 bars abs, and cooling calorigenic fluid e.g. inert gas such as gaseous nitrogen, in another series of separated passages. Each passage of the former series is separated from the passage closer to the latter series by an auxiliary passage containing fin tubes in which the inert gas is circulated.    USE - Method for reheating cryogenic liquid i.e. liquefied natural gas, by exchanging heat with calorigenic fluid e.g. inert gas such as gaseous nitrogen, in a plate and fin tube exchanger for starting the plate and fin tube exchanger (claimed).    ADVANTAGE - The passage of one series is separated from the other passage closer to the other series by the auxiliary passage containing fin tubes in which the inert gas is circulated, thus avoiding the pollution of the nitrogen by the liquefied natural gas, while preventing the damage of the exchanger. The passages can be used for cooling the exchanger in a progressive and controlled manner, during starting of the exchanger.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for starting a plate and fin tube exchanger.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of parallel passages of a plate and fin tube exchanger in an exchanger width direction.
NOVELTY - A two-stage catalytic process (P1) for converting biomass feedstock involves (A) establishing intimate contact of biomass feedstock in particulate form with inorganic catalyst material; (B) subjecting mixture of biomass feedstock and catalyst material to biocatalytic cracking (BCC) reaction in first biocatalytic cracking unit to form condensable product and solid biomass material; (C) separating condensable product from solid biomass material; and (D) subjecting solid biomass material from step C) to second biocatalytic cracking reaction in second biocatalytic cracking unit.    USE - As two-stage catalytic process for converting biomass feedstock (claimed). The bio-oil is produced in the first stage BCC comprising significant amount of triglycerides and fatty acid esters and may be converted to diesel fuel by e.g. hydrocracking.    ADVANTAGE - The conversion products of the first stage are not subjected to the more severe conditions of the second stage, so that less coke or char is formed. The more severe conditions of the second stage increases the overall yield of the process. The two-stage process can be conducted continuously. The two-stage BCC process provides the operator with a high level of operating flexibility.
NOVELTY - Methane fermentation system has (a) fermenter (1) for performing methane fermentation of organic waste by maintaining the temperature at 60 degrees C or more, and (b) ammonia collecting equipment for collecting ammonia from the fermented liquor after methane fermentation.    USE - The methane fermentation system is useful in feed production apparatus for fermenting organic waste to produce fermented liquor and by-product ammonia, where ammonia produced is useful for producing feed (all claimed) and the fermented liquor is useful as fertilizer.    ADVANTAGE - The amount of ammonia generated is increased. The high value added feed can be obtained. The feed is compact and economical. The nitrogen amount in fermented liquor is reduced. The nitrogen contamination of underground water is reduced.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) feed production apparatus has (a) fermenter for performing methane fermentation of organic waste by maintaining the temperature at 60 degrees C or more, (b) ammonia collecting equipment for collecting ammonia from the fermented liquor after methane fermentation, and (c) ammonia processing tank (6) into which the diffused ammonia is brought into contact with the feed raw material; and    (2) method for producing feed using ammonia obtained after collecting fermented liquid, involves performing methane fermentation of organic waste by maintaining the temperature at 60 degrees C or more, collecting ammonia from the fermented liquid after methane fermentation using ammonia collecting equipment, and contacting the ammonia with feed raw material in ammonia processing tank.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic representation of feed production apparatus.    Fermenter (1)    Ammonia collecting column (2)    Shower (3)    Recycle tank (5)    Ammonia processing tank (6)